Biotechnology Letters Volume 27, Number 17 Laboratory Scale Bioremediation of Acid Mine Water Drainage from a Disused Tin Mine Lawrence Darkwah, Neil A. Rowson, Christopher J. Hewitt DOI: 10.1007/s10529-005-3201-z (1251 - 1257) Inhibition of Platelet Aggregation of a Mutant Proinsulin Chimera Engineered by Introduction of a Native Lys-Gly-Asp-containing Sequence Jian Jing and Shan Lu DOI: 10.1007/s10529-005-3202-y (1259 - 1265) Construction of an Effective Protein Expression System Using the tpl Promoter in Escherichia coli Takashi Koyanagi, Takane Katayama, Ai Hirao, Hideyuki Suzuki, Hidehiko Kumagai DOI: 10.1007/s10529-005-0216-4 (1267 - 1271) Purification and Properties of an N-acetylglucosaminidase from Streptomyces (1273 - 1276) cerradoensis Iderval da Silva Junior Sobrinho, Luiz Artur Mendes Bataus, Valéria Ribeiro Maitan, Cirano José Ulhoa DOI: 10.1007/s10529-005-0218-2 A Modified PCR System for Amplifying β-ketoacyl-ACP Synthase Gene Fragments with DNA from Streptomyces luteogriseus Feng-Ming Yu, Xin Jiang, Jin-Chuan Wu, Ying-Jin Yuan DOI: 10.1007/s10529-005-3219-2 (1277 - 1282) Molecular Cloning and Tissue Distribution of SF-1-related Orphan Receptors During Sexual Maturation in Female Goldfish Cheol Young Choi and Hamid R. Habibi DOI: 10.1007/s10529-005-0220-8 (1283 - 1290) Enhancement of Isoflavone Synthase Activity by Co-expression of P450 Reductase (1291 - 1294) from Rice Dae Hwan Kim, Bong Gyu Kim, Hyo Jung Lee, Yoongho Lim, Hor Gil Hur, Joong-Hoon Ahn DOI: 10.1007/s10529-005-0221-7 Structural Characterization of β-glucans of Agaricus brasiliensis in Different Stages (1295 - 1299) of Fruiting Body Maturity and their Use in Nutraceutical Products Carla Maísa Camelini, Marcelo Maraschin, Margarida Matos Mendonça, Cezar Zucco, Antonio Gilberto Ferreira, Leila Aley Tavares DOI: 10.1007/s10529-005-0222-6 Taxane Production in Suspension Culture of Taxus × Media var. Hicksii Carried Out in Flasks and Bioreactor Katarzyna Syklowska-Baranek and Miroslawa Furmanowa DOI: 10.1007/s10529-005-0223-5 (1301 - 1304) Regio- and Stereo-selective Hydroxylation of Abietic Acid Derivatives by Mucor circinelloides and Mortierella isabellina Koichi Mitsukura, Takeshi Imoto, Hirokazu Nagaoka, Toyokazu Yoshida, Toru Nagasawa DOI: 10.1007/s10529-005-3224-5 (1305 - 1310) Increased Conformational and Thermal Stability Properties for Phenylalanine Dehydrogenase by Chemical Glycosidation with End-group Activated Dextran Reynaldo Villalonga, Shinjiro Tachibana, Yunel Pérez, Yasuhisa Asano DOI: 10.1007/s10529-005-3225-4 (1311 - 1317) Production of Fungal Biomass Immobilized Loofa Sponge (FBILS)-discs for the Removal of Heavy Metal Ions and Chlorinated Compounds from Aqueous Solution M. Iqbal, A. Saeed, R.G.J. Edyvean, B. O’Sullivan, P. Styring DOI: 10.1007/s10529-005-0477-y (1319 - 1323) A Metal Ion as a Cofactor Attenuates Substrate Inhibition in the Enzymatic Production of a High Concentration of Kazuaki Yoshimune, Ai Hirayama, Mitsuaki Moriguchi DOI: 10.1007/s10529-005-0480-3 (1325 - 1328) Characterization of an Extracellular Serine Protease Gene from the Nematophagous (1329 - 1334) Fungus Lecanicillium psalliotae Jinkui Yang, Xiaowei Huang, Baoyu Tian, Hui Sun, Junxin Duan, Wenping Wu, Keqin Zhang DOI: 10.1007/s10529-005-0482-1 Author’s Quick Check Checklist for Preparing Manuscripts for Submission DOI: 10.1007/s10529-005-1074-9 (1335 - 1335) Ó Springer 2005 Biotechnology Letters (2005) 27: 1251–1257 DOI 10.1007/s10529-005-3201-z Laboratory scale bioremediation of acid mine water drainage from a disused tin mine Lawrence Darkwah, Neil A. Rowson & Christopher J. Hewitt* Centre for Formulation Engineering, Biochemical Engineering, School of Engineering (Chemical Engineering), The University of Birmingham, Edgbaston, B15 2TT, UK *Author for correspondence (Fax: +44-121-414-5324; E-mail: [email protected].) Received 6 May 2005; Revisions requested 2 June 2005; Revisions received 13 June 2005; Accepted 14 June 2005 Key words: acid mine drainage, Acidithiobacillus ferrooxidans, bioremediation, laboratory scale, microbial catalysis Abstract Real acidic mine-water drainage was seeded with Acidithiobacillus ferrooxidans to catalyse the removal of iron contained therein. The addition of At. ferrooxidans increased metal precipitation kinetics and decreased the water iron content by 70%. Supplementing non-sterile mine water with a bacterial growth medium accelerated metal removal by indigenous micro-organisms both at the 500 ml shake-flask and 5 l bioreactor scale. Introduction Both alkaline and acid mine water drainage (ADM) is a growing world-wide problem for both working and abandoned mines as well as colliery spoil heaps due to the highly toxic products generated in both underground and surface mining (Johnson 2003). In particular, acidic drainages originate from the exposure of sulphidic mineral surfaces to O2, which results in the formation of soluble sulphates. On contact with water, these minerals (mostly with a high ferrous iron content) become oxidised, usually with microbial catalytic enhancement, producing ferric ions and H2. These ions when leached into streams cause the water to become more acidic, normally reaching pH values <3. Additionally, other metal ions, such as Cd, Cu, Mn, Al and As, also leach into the AMD, at final concentrations far above permissible legal levels. Wheal Jane, an important cassiterite (the main mineral ore for tin) mine within the Carnon Valley (Cornwall, UK) provided the AMD for use in this study. The workings that make up this disused mine (work finished finally in c. 1991) extend to a depth of 450 m below ground being partially flooded and very wet. This is probably due to water seeping from interconnected workings that historically produced pyrite and arsenopyrite. During the mines working life such water, partially treated, was actively pumped and discharged into the River Carnon (UK) but, when government funding was withdrawn, all treatment ceased so the rising mine water, with a pH of 2.8 and a high metal content, was passively discharged into the River Carnon (UK). Further attempts to treat the water with CaCO3 (lime) before it was pumped into the existing Wheal Jane tailings dam were made but, when this stopped for technical reasons in January 1992, 50 million litres of acidic metal laden water were accidentally released into the river. Since this water contained iron hydroxides at high levels, a very visual contamination of the local river caused significant public pressure for a long-term solution to the problem of AMD in the UK (Banks et al. 1997, Somerfield et al. 1994). Many methods have been investigated, designed and used in remediating AMD. Most 1252 common, are the passive (wetland) methods, conventional active methods of adding limestone, quicklime or NaOH (caustic soda) or soda ash to promote metal precipitation and other biological routes such as biosorbents and rotating biological contactors (Wildeman 1993, Groudev et al. 1999, Shutes 2001, Brown et al. 2002). The bioremediation approach to AMD remediation, which incorporates both biological and passive chemical processes, is a proven alternative to conventional environmental cleanup technologies (Macaskie et al. 1995, Boswell et al. 1998, Bonthrone et al. 2000). The naturally occurring, acidophilic bacterium Acidithiobacillus ferrooxidans has long been used for the bioleaching of copper from chalcopyrite (CuFeS2) because it can oxidise ferrous iron at a high rate, exhibits rapid growth and is able to tolerate high iron concentrations (Kelly & Wood 2000). For these reasons, it has also been studied extensively for use in solving environmental problems involving iron rich AMD. Therefore in this work we seek to investigate and enhance the capability of the indigenous mostly acidophilic iron and sulphur-oxidising bacteria (Hallberg & Johnson 2005, Johnson 2003) in the mine water to oxidise the ferrous iron in solution to ferric iron. The latter quickly precipitates at the low pH of the AMD used here and is easily removed using conventional technologies such as sedimentation (enhanced by flocculation or the use of hydro-cyclones), froth flotation or filtration. This was done firstly, by supplementing the water with a bacterial growth medium and secondly by seeding the water with a culture of the bacterium At. ferrooxidans at both the shake flask and laboratory scale. (average 1.7107 cells/ml) was produced on ATCC medium 64 (GM) and maintained at 4 °C. GM is made up from two solutions. Solution A, 0.4 g (NH4)2SO4, 0.2 g KH2PO4 and 0.08 g MgSO4Æ7H2O made up in 400 ml distilled water. Solution B, 10.0 g FeSO4Æ7H2O made up in 100 ml distilled water and acidified with 1 ml 0.5 M H2SO4. Solution A was autoclaved at 121 °C for 20 min whilst Solution B was filtersterilised (0.2 lm) and the two combined aseptically. The pH of the GM was 2.8. AMD experiments Aliquots of AMD were either heat-sterilised (121 °C for 20 min) or not. These are referred to as heat-sterilised mine water (HSMW) and nonsterilised mine water (NSMW), respectively. Both of these (NSMW and HSMW) were supplemented with 50%, 80% and 90% (v/v) GM or distilled water where appropriate. A total volume of 50 ml of each of the above solutions was put into duplicate 500 ml shake flasks and shaken on an orbital shaker at 100 rpm and 30 °C. Similar flasks were inoculated with 10% (v/v) At. ferrooxidans where appropriate and also incubated at 30 °C and 100 rpm. In a similar way, laboratory scale bioreactor studies were carried out in a 5 l cylindrical glass vessel, (157 mm diameter 260 mm total height), with a working volume of 4 l. The vessel was fitted with one 76 mm diameter, four bladed Rushton turbine which was situated 30 mm above the bottom of the vessel. The vessel also had four equally spaced vertical baffles, width 17 mm. The vessel was equipped for the measurement of pH and temperature. Cultures were run at 30 °C with an impeller speed of 100 rpm. Materials and methods Analytical methods Acid mine water (AMD) AMD was obtained from the Wheal Jane mine (Cornwall, UK). Fresh AMD was collected in pre-sterilized plastic bottles. This water was then stored at 4 °C and used for experiments less than 5 days from the date of collection. Bacterial strain and growth medium At. ferrooxidans (ATCC 19859) was used to inoculate the AMD where appropriate. Inoculum For all experiments, 10 ml samples were taken and filtered through a 0.45 lm cellulose acetate membrane filter to remove precipitates (mostly insoluble ferric iron species) and then acidified with 1.5 ll conc. HNO3 per 1 ml sample and kept at 4 °C for total soluble iron (mostly ferrous iron species) content analysis using an atomic absorption spectrophotometer (Model 751, Instrumentation Laboratory, USA) (Greenberg et al. 1992). For shake flask experiments, the remainder of the sample was used to measure 1253 temperature, pH and in all cases reduction–oxidation (redox) potential using a Water Test Meter calibrated as per the manufacturers instructions (Hannah Instruments, UK). Results and discussion A series of experiments was carried out in 500 ml shake-flasks and a 5 l bioreactor where the AMD was sterilised or not, supplemented with various proportions of GM (50%, 80%, 90% v/v) or distilled water or not and inoculated with a laboratory strain of At. ferrooxidans or not. Since conventional techniques for following microbial activity were not suitable for use in this case, because of the very complex particulate nature of the GM and mine water mixture used, metabolic activity can be inferred from changes in redox potential (mV) (Nemati & Harrison 2000, Bhatti et al. 2001, Medrano-Roldan et al. 2001) changes in pH and a decreases in total (ferrous) iron in solution. Also, because AMD is an environmental sample, its composition varies with the time 3.2 550 500 3.0 4000 450 2.8 3000 pH 400 2.6 350 2000 2.4 300 1000 0 2.2 Redox potential (mV) 5000 Total iron in solution mg/l of year but, even with these different starting concentrations of iron (also due to the differing proportions of GM used), reproducible measurements of pH, redox potential (mV), total iron in solution mg/l were made for duplicate experiments (not all data shown, Figures 1–5). Initial studies showed that the At. ferrooxidans strain used here could not grow in undiluted AMD or AMD diluted with sterile distilled water (50% v/ v) but exhibited a typical growth profile on the GM. This confirmed the work of others (Dennison et al. 2001) that showed that the AMD needs to be supplemented with a phosphate source for At. ferrooxidans to grow. The effect of both heat-sterilisation and supplementing the AMD with 90% (v/v) of GM can be seen in Figure 1. In the case of the HSMW, the total iron in solution remained high (3300–4500 mg/l), the redox potential was always below 355 mV and the pH remained above 2.3 indicating little microbial activity and ferrous iron removed from solution throughout. However, in the case of the NSMW, the increase in redox potential to a maximum of 250 2.0 200 0 2 4 6 8 Time (days) pH HSMW pH NSMW Redox potential (mV) HSMW Redox potential (mV) NSMW Total iron in solution mg/l HSMW Total iron in solution mg/l NSMW Fig. 1. pH, redox potential (mV) and total iron in solution mg/l shake flask profiles for HSMW and NSMW both supplemented with 90% GM. 1254 2.6 4500 650 4000 600 550 3000 2500 2000 2.2 500 450 2.0 400 1500 Redox potential (mV) 3500 pH Total iron in solution mg/l 2.4 1.8 350 1000 500 1.6 300 0 2 4 6 8 Time (days) pH HSMW pH NSMW Redox potential (mV) HSMW Redox potential (mV) NSMW Tot al iron in solution mg/l HSMW Tot al iron in solution mg/l NSMW Fig. 2. pH, redox potential (mV) and total iron in solution mg/l shake flask profiles for HSMW and NSMW both inoculated with At. ferrooxidans and supplemented with 90% GM. 520 mV with a concomitant decrease in pH to 2.2 indicated indigenous microbial activity (Nemati & Harrison 2000, Bhatti et al. 2001, Medrano-Roldan et al. 2001), which was capable of oxidising ferrous iron to ferric iron hence lowering the total iron in solution by 70% after 6 days’ incubation. The effect of inoculating the HSMW and NSMW supplemented with 90% (v/v) GM with At. ferrooxidans is illustrated in Figure 2. In both cases the redox potential had risen above 550 mV and the pH had dropped to <1.8 by the end of day 2. This indicated sufficient microbial activity to reduce the total iron in solution to below 1300 mg/l (>70% reduction) in both cases during the same time period. Essentially identical experiments were carried out in a 5 l stirred (100 rpm) tank bioreactor and similar results were obtained. The effect of inoculating the NSMW supplemented with 80% (v/v) GM with At. ferrooxidans is illustrated in Figure 3. In the case of the NSMW supplemented with 80% (v/v) GM without inoculation, the total iron in solution decreased only slightly (5% by day 5), the redox potential rose steadily from 200 to 320 mV and the pH fell from 2.9 to 2.4 indicating diminished microbial activity and ferrous iron oxidtion throughout. However, in the case of the inoculated NSMW supplemented with 80% (v/v) GM, the redox potential increased to a maximum of 600 mV by day 2 and a steady decrease in pH to 1.7 throughout. This indicated microbial activity which was capable of lowering the total iron in solution by 45% after 2 days’ incubation increasing to 56% by day 5. Essentially, identical experiments were carried out in a 5 l stirred (100 rpm) tank bioreactor and similar results were obtained. The effect of adding 50% (v/v) GM to both NSMW and NSMW inoculated with At. ferrooxidans in a 5 l stirred (100 rpm) tank bioreactor is shown in Figure 4. In the case of the NSMW supplemented with 50% (v/v) GM without inoculation, the total iron in solution decreased only slightly initially but there was a greater secondary decrease starting on day 6 resulting in a 50% drop in total iron in solution by day 8. A similar 3.0 4000 2.8 3500 700 600 2.6 500 3000 2.4 2500 400 2.2 2000 300 1500 2.0 1000 1.8 500 1.6 Redox potential (mV) 4500 pH Total iron in solution mg/l 1255 200 100 0 2 4 6 8 Time (days) pH NSMW not inoculated pH NSMW inoculated Redox potential (mV) NSMW not inoculated Redox potential (mV) NSMW inoculated Total iron in solution mg/l NSMW not inoculated Total iron in solution mg/l NSMW inoculated Fig. 3. pH, redox potential (mV) and total iron in solution mg/l shake flask profiles for NSMW and NSMW inoculated with At. ferrooxidans, where both were supplemented with 80% GM. trend was observed for pH but the redox potential increased gradually throughout. In the case of the NSMW supplemented with 50% (v/v) GM with inoculation, the total iron in solution had decreased by 80% by day 2. This was followed by a concomitant decrease in pH and increase in redox potential. Essentially identical experiments were carried out in 500 ml Erlenmeyer shake flasks and similar results were obtained. The effect of adding 10% (v/v) GM to both NSMW and NSMW inoculated with At. ferrooxidans in a 5 l stirred (100 rpm) tank bioreactor is shown in Figure 5. In the case of the NSMW supplemented with 10% (v/v) GM without inoculation, the total iron in solution gradually declined with an 80% drop by day 6. A similar trend was observed for pH but redox potential increased gradually, throughout. In the case of the NSMW supplemented with 10% (v/v) GM with inoculation, similar results were obtained and the total iron in solution had decreased by 80% by day 6. This was followed by a concomitant decrease in pH and increase in redox potential. Essentially identical experiments were carried out in 500 ml Erlenmeyer shake flasks and similar results were obtained. Conclusions Supplementing non-sterile mine water (NSMW) with growth medium (GM) at varying proportions, enhances natural microbial activity and facilitates the removal of total iron from solution from real acidic mine water such as that obtained from the Wheal Jane mine even when its composition varies according to the time of year and, not unsurprisingly, that this effect increases with increasing proportions of the GM. Further that the addition of a pure culture of At. ferrooxidans to either heat-sterilized mine water or NSMW further enhances the ferrous iron oxidation kinetics. The subsequent hydrolysis of the resultant ferric iron causes it to precipitate very rapidly and it can then be removed from suspension by conventional techniques, in this case, filtration. Process performance seems to be independent of the scale of operation examined here (shake-flask 1256 2.8 700 1200 600 1000 500 2.4 800 pH Total iron in solution mg/l 2.6 600 400 2.2 300 400 2.0 200 200 0 Redox potential (mV) 1400 1.8 100 0 2 4 6 8 Time (days) pH NSMW not inoculated pH NSMW inoculated Redox potential (mV) NSMW not inoculated Redox potential (mV) NSMW inoculated Total iron in solution mg/l NSMW not inoclulated Total iron in solution mg/l NSMW inoculated Fig. 4. pH, redox potential (mV) and total iron in solution mg/l 5 l laboratory scale bioreactor profiles for NSMW and NSMW inoculated with At. ferrooxidans where both were supplemented with 50% GM. 600 3.2 550 500 3.0 400 450 2.8 300 pH Total iron in solution mg/l 500 3.4 400 2.6 350 200 2.4 100 0 Redox potential (mV) 600 300 2.2 250 2.0 200 0 2 4 6 8 Time (days) pH NSMW not inoculated pH NSMW inoculated Redox potential (mV) NSMW not inoculated Redox potential (mV) NSMW inoculated Tot al iron in solution mg/l NSMW not inoculated Tot al iron in solution mg/l NSMW inoculated Fig. 5. pH, redox potential (mV) and total iron in solution mg/l 5 l laboratory scale bioreactor profiles for NSMW and NSMW inoculated with At. ferrooxidans where both were supplemented with 10% GM. 1257 and 5 l laboratory scale) and demonstrates the potential of using such a system for treating real acid mine water drainage containing a high ferrous iron content. Acknowledgements The authors are grateful to United Utilities (Cornwall, UK) for allowing samples to be taken from the Wheal Jane mining facility. This work was funded by the Ghana Scholarship Agency through the Commonwealth Scholarship Commission. References Banks D, Younger PL, Arnesen RT, Iversen ER, Banks SB (1997) Mine-water chemistry: the good, the bad and the ugly. Environ. Geol. 32: 157–174. Bhatti TM, Bigham JM, Tuovinen OH (2001) Bacterial and chemical oxidation of marcasite and pyrite. In: Ciminelli VST & Garcia JR, eds. International Biohydrometallurgy Symposium Proceedings, Process Metallurgy, Part A, Amsterdam: Elsevier, pp. 617–625. Bonthrone KM, Quarmby J, Hewitt CJ, Allan VJM, PatersonBeedle M, Kennedy JF, Macaskie LE (2000) The effect of the growth medium on the composition and metal binding behaviour of the extracellular polymeric material of a metalaccumulating Citrobacter sp. Environ. Technol. 21: 123–134. Boswell CD, Hewitt CJ, Macaskie LE (1998) An application of bacterial flow cytometry: Evaluation of the toxic effects of four heavy metals on Acinetobacter sp. with potential for bioremediation of contaminated wastewaters. Biotechnol. Lett. 20: 857–863. Brown M, Barley B, Wood H (2002) Minewater Treatment: Technology, Application and Policy, Dorchester, UK:IWA Publishing. Dennison FD, Sen AM, Hallberg KB, Johnson DB (2001) Biological versus abiotic oxidation of iron in acid mine drainage waters: An important role for moderately acidophilic, iron-oxidising bacteria. In: Ciminelli VST & Garcia JR, eds. International Biohydrometallurgy Symposium Proceedings, Process Metallurgy, Part A, Amsterdam: Elsevier, pp. 493–501. Greenberg AE, Clesceri LS, Eaton AD (1992) Standard methods for the examination of water and wastewater, 18USA:American Public Health Association. Groudev SN, Bratcova SG, Komnitsas K (1999) Treatment of waters polluted with radioactive elements and heavy metals by means of a laboratory passive system. Miner. Eng. 12: 261–270. Hallberg KB, Johnson DB (2005) Microbiology of a wetland ecosystem constructed to remediate mine drainage from a heavy metal mine. Sci. Total Environ. 338: 53–66. Johnson DB (2003) Chemical and microbiological characteristics of mineral spoils and drainage waters at abandoned coal and metal mines. Water Air Soil Poll. 3: 47–66. Kelly DP, Wood AP (2000) Reclassification of some species of Thiobacillus ferrooxidans to the newly designated genera Acidithiobacillus, Halothiobacillus and Thermithiobacillus. Int. J. Syst. Bacterial. 50: 511–516. Macaskie LE, Hewitt CJ, Shearer JA, Kent CA (1995) Biomass production for the removal of heavy metals from aqueous solutions at low pH using growth-decoupled cells of a Citrobacter spp. Int. Biodeter. Biodegr. 73–92. Medrano-Roldan H, Chavez-Gonzalez BP, Solis-Soto A, Morales-Castro J, Ochoa-Martinez LA, Rocha-Fuentes M, Pereyra-Alferez B, Gala-Wong JL, Ramirez-Rodriguez GD, Davila-Flores RT (2001) Growth of a native Thiobacillus ferrooxidans strain in mine tailings. In: Ciminelli VST & Garcia JR, eds. International Biohydrometallurgy Symposium Proceedings, Process Metallurgy, Part A, Amsterdam: Elsevier, pp. 587–593. Nemati M, Harrison STL (2000) A comparative study on thermophilic and mesophilic biooxidation of ferrous iron. Min. Eng. 13: 19–24. Shutes RBE (2001) Artificial wetlands and water quality improvement. Environ. Int. 26: 441–447. Somerfield PJ, Gee MJ, Warwrick RM (1994) Benthic community structure in relation to an instantaneous discharge of waste water from a tin mine. Mar. Pollut. Bull. 28: 363–369. Wildeman TR (1993) Passive bioremediation of metals from water using reactors or constructed wetlands. In: Means J & Hinchee R, eds. Emerging Technology for Bioremediation of Metals, Boca Raton: Interpharm/CRC, pp. 13 –25. Biotechnology Letters (2005) 27: 1259–1265 DOI 10.1007/s10529-005-3202-y Springer 2005 Inhibition of platelet aggregation of a mutant proinsulin chimera engineered by introduction of a native Lys-Gly-Asp-containing sequence Jian Jing* & Shan Lu Department of Biochemistry and Biotechnology, Laboratory of Biotechnology and Protein Engineering, Beijing Normal University, 100875, Beijing, China *Author for correspondence (Fax: +86-10-58807365; E-mail: [email protected]) Received 13 January 2005; Revisions requested 2 February 2005; Revisions received 14 June 2005; Accepted 14 June 2005 Key words: glycoprotein IIb/IIIa receptor, inhibition of platelet aggregation, KGD (Lys-Gly-Asp) motif, proinsulin mutant Abstract An eight amino acid sequence, CAKGDWNC, from disintegrin barbourin, was introduced into an inactive human proinsulin molecule between the B28 and A2 sites to construct a chimeric, anti-thrombosis recombinant protein. The constructed Lys-Gly-Asp (KGD)-proinsulin gene was expressed in Escherichia coli and then purified. The KGD-proinsulin chimera protein inhibits human platelet aggregation, induced by ADP, with an IC50 value (molar concentration causing 50% inhibition of platelet aggregation) of 830 nM and demonstrates also specific affinity to glycoprotein IIb/IIIa receptor. Its insulin receptor binding activity remaines as low as 0.04% with native insulin as a control. Introduction The functional motif of Arg-Gly-Asp/Lys-GlyAsp (RGD/KGD) exists in many adhesion proteins, such as fibrinogen, fibronectin and von Willebrand factor. Platelet aggregation is an important step in thrombotic events and requires the binding of fibrinogen to glycoprotein IIb/IIIa receptor on activated platelets. Most proteins or peptides from snake and leech venom (Musial & Niewiarowski 1990, Scarborough et al. 1991), known as the disintegrin family, containing RGD motifs or KGD motifs, are potential antagonists of platelet aggregation. The RGD motif occurs in many disintegrins, but the KGD motif has only been found in the disintegrins barbourin (Scarborough et al. 1991) and ussuristatin-2 (Kiyotaka & Shigeyuki 1999). RGD and KGD motifs have almost the same biological activity to inhibit platelet aggregation but the KGD motif is glycoprotein IIb/IIIa receptor-specific as compared with the RGD motif. If KGD-containing proteins or peptides can simulate the conformation of native functional KGD motif, they may be also glycoprotein IIb/IIIa receptor-specific and have high potency to inhibit platelet aggregation by interacting specificially with glycoprotein IIb/ IIIa receptor on the platelet surface (Wittig et al. 1998). Minoux et al. (2000) have revealed that functional KGD motif is usually located at the top of solvent-accessible, highly flexible loop structure and always tends to assume a b-turn conformation (Minoux et al. 2000). Insulin is produced by cleavage of the C-peptide of proinsulin, the precursor of insulin hormone. The C-peptide, exposed on the surface of proinsulin, is a loose loop structure (Weiss et al. 1990) which is similar to the KGD motif of native KGD-containing disintegrins. To obtain a novel platelet aggregation inhibitor, an eight amino acid peptide, CAKGDWNC, originated from the functional motif of the disintegrin, barbourin (Scarborough et al. 1991), was selected to replace the C-peptide of human proinsulin to 1260 construct a chimeric anti-thrombosis peptide. The structure of chimeric KGD-proinsulin molecule was simulated, inhibitory activity of platelet aggregation, glycoprotein IIb/IIIa receptor binding specificity and insulin hormone activity were determined. Materials and methods Simulation of the KGD-proinsulin structure The structure of the KGD-proinsulin was simulated with sgi workstation using Insight II software. Structural simulation was carried out with the data of NMR structure of native human insulin (Protein Data Bank, Brookheaven, CA). The Biopolymer module in Insight II was employed to add the CAKGDWNC sequence between the B28 and A2 sites of insulin structure. At the same time, the A6Cys and A11Cys of proinsulin were replaced by Ser to delete the intra-A chain disulfide bond. The Builder module was employed to carry out structural optimization (iterations: 1000; derivative: 0.01). Construction of the KGD-proinsulin mutant gene The standard polymerase chain reaction method was employed to construct mutant KGD-containing proinsulin gene. The proinsulin gene with A6 and A11 Cys to Ala mutations was used as the template (Dai & Tang 1996). The sequences of the primers were as follows: AGAAAGACGTTGGAG (primer l, 5¢ primer); GACTAATATTACGTCGACTCCCAAATAACCAA TATTCCCCCAGCACTGAAGCTGCTACGGTGGTAGAA (primer 2, mutant primer); ATTAGCTAGGTGGCC (primer 3, complementary to the mutant primer); GTCTGATCCCCGGCA (primer 4, 3¢ primer). Primer 1 and 2 were used to obtain upstream DNA fragment, and primer 3 and 4 were used to obtain downstream DNA fragment. Then, the above two DNA fragments were mixed and annealed with the primer 1 and 4 to obtain full-length KGD-proinsulin gene. The recombinant gene was confirmed by DNA sequencing and cloned into an expression vector pET21a at BamHI and HindIII sites under the control of a T7 promoter. The constructed recombinant expression vector was named as pEK214 and used to transform Escherichia coli BL21(DE3)pLysS for further expression and purification of the KGD-proinsulin protein. Expression and purification of the KGD-proinsulin The procedures for expression and refolding of the KGD-proinsulin were as described previously with some modifications (Jing & Tang 2000). After Sephacryl S200 separation, the pH of the KGD-proinsulin fraction was adjusted to 3.5 with 2 M HCl, and solid NaCl to 12.5% (w/v) to salt-out the KGD-proinsulin. The pellet was collected by centrifugation and dissolved in 0.05 M Tris–HCl and 40% (v/v) 2-propanol, pH 7.0, and was further purified by DEAE Sephadex ionexchange chromatography. Characterization of the KGD-proinsulin Amino acid composition and circular dichroism (CD) analysis were done as described (Dai & Tang 1996). The molecular weight of the KGDproinsulin was determined by mass spectrometry. Inhibition of platelet aggregation was determined as follows. Fresh human blood was anticoagulated with 0.01 M sodium citrate (10% v/v), pH 7.4, and centrufuged at 150 g at 25 C for 10 min. The supernatant was collected as platelet-rich plasma. The protein samples were dissolved in 0.9% NaCl. Platelet-rich plasma, 300 ll, was incubated with 25 ll of various concentrations of protein samples at 37 C for 2 min before addition of 25 ll of 100 lM adenosine 5¢-diphosphate. The inhibition of platelet aggregation was determined by light transmission measurement. The IC50 value was calculated by linear regression. Cell attachment assay was carried out to determine glycoprotein IIb/IIIa receptor binding specificity. The human melanoma cell line K2 was cultured in modified RPM1640 medium containing 12% fetal calf serum and harvested at subconfluency with 0.4% trypsin and 1 mM EDTA. Wells (2 cm2) of six-well dishes were treated with 50 ll of fibrinogen (50 lg ml)1) or fibronectin (50 lg ml)1) in PBS overnight at 4 C. A 500 ll aliquot of cells (1.5 105 cells ml)1) was added to each well. The cells were incubated for 1.5 h at 37 C, then non-adherent cells were removed by aspiration, and adherent cells were fixed and stained with 2% Giemsa solution for 60 min. The 1261 total number of cells in each well was counted microscopically. Insulin receptor binding assay was done as following. Insulin receptor was partially isolated as crude membranes from human placenta. The proteins were diluted into a series of concentrations in KRB buffer (0.114 M NaCl, 1.2 mM MgSO4, 0.03 M HEPES, 0.05 M KCl, 1.2 mM KH2PO4, 1.3 mM CaCl2, 0.01 M NaHCO3, pH 7.4). To 50 ll of protein samples, an equal volume of properly diluted 125I-insulin in KRB buffer and 6-fold diluted insulin receptor in KRB buffer in 2% of bovine serum albumin were added and the samples were mixed. The mixtures were incubated overnight at 4 C and centrifuged at 10,000 g for 5 min. The radioactvitiy of the pellets was determined by gamma ray detection. The concentration of native insulin producing 50% inhibition of 125I-insulin binding to receptor was set as 100%, and the activity of the KGDproinsulin was compared. deleted. A1Gly and B30Thr were replaced by two Cys residues on the two ends of the eight amino acid KGD-containing peptide. The two Cys introduced with the KGD-containing peptide may form a disulfide-bond to improve platelet aggregation inhibitory activity of the KGD-proinsulin protein. The structural simulation and homology modeling of the KGD-proinsulin chimera was carried out with the sgi-workstation using Insight II-software based on detailed structural information of mutant proinsulin (Hua et al. 1996) and the disintegrin barbourin (Minoux et al. 2000). The simulated structure (Figure 1) of the KGD-proinsulin chimera protein demonstrates that the CAKGDWNC-peptide introduced between the B28 site and A2 site of the mutant proinsulin with intra-A chain disulfide-bond deletion exhibits its functional motif to interact with the glycoprotein IIb/IIIa receptor, know as fibrinogen receptor. The structural property of the KGD-proinsulin provides necessary requirements of recognition and interaction with Results and discussion Design of the KGD-proinsulin molecule Intra-A chain disulfide bond-deleted proinsulin and insulin mutant shows almost no insulin receptor binding activity, but whole immune activity is retained (Dai & Tang 1996). The structure of the intra-A chain disulfide bond-deleted proinsulin mutant is quite similar to that of native proinsulin (Hua et al. 1996). That suggests that the intra-A chain disulfide bond-deleted proinsulin can be adopted as a promising scaffold for foreign functional motif to exhibit its active conformation. The mutant proinsulin with intraA chain disulfide bond deletion is human origin and inactive in vivo, it can also be prepared easily as recombinant protein. Spatial distance between B28 site of the B-chain and A2 site of the A chain is about 5–10 Å which is suitable for inserting a small peptide. Also, the proinsulin and native KGD-containing platelet antagonists are all small proteins rich in disulfide bonds. The chimeric KGD-proinsulin has the possibility to specifically inhibit platelet aggregation and shows no insulin hormone activity as a mutant proinsulin scaffold. To reduce further the possibility of degradation of proinsulin to insulin, B29Lys, a possible protease digestion site was Fig. 1. Simulation of three-dimensional structure of the KGD-proinsulin. The structure was simulated with an sgi workstation using Insight II software. Peptide backbone is shown as a long slender coil shaded in black, with the KGD sequence (including the side-chains) highlighted. The KGDmotif lies on the surface of mutant proinsulin molecule and the side-chains of the KGD sequence are extended to the outside of loop structure. The KGD-motif is far away from the core of mutant proinsulin and exhibit a native-like conformation. Replacement of the C-peptide with KGD-containing sequence has little influence on the proinsulin structure. 1262 the glycoprotein IIb/IIIa receptor on platelet cell surface. So there is great possibility to obtain a novel potent anti-thrombosis protein with the specificity of the glycoprotein IIb/IIIa receptor. Expression, purification, and characterization of the KGD-proinsulin Routine recombinant DNA techniques were used to construct the chimeric gene and the gene was over-expressed in Escherichia coli BL21(DE3)pLyS with constructed expression vector pEK214. The expression and purification of the KGD-proinsulin is mainly processed according to the method described previously (Jing & Tang 2000). The expressed protein was analyzed, as shown in Figure 2a. The expression level was about 17% of total cellular proteins based on the spectrophotometric analysis. After isolation of the inclusion bodies, unfolding and refolding of the KGD-proinsulin protein, Sephacryl S200 chromatography was used to separate the refolded KGD-proinsulin chiemra protein, as shown in Figure 2b. (Peak 2 stands for the KGD-proinsulin chimera protein fraction.) The KGD-proinsulin was further purified by a DEAE-Sephadex ion-exchange chromatography (Figure 2c). High homogeneity of purified KGDproinsulin recombinant protein can be determined by both SDS-PAGE (Figure 2a) and Fig. 2. Purification of the KGD-proinsulin chimera protein. (a) Analysis of expression of recombinant clones by 15% SDS-PAGE. Lane 1, protein molecular weight marker; lane 2, total cellular proteins of cells transformed by pET21a vector; lanes 3 and 4, total cellular proteins of cells transformed by recombinant expression plasmid pEK214; lane 5, purified KGD-proinsulin after DEAESephadex chromatography. (b) Sephacryl S200 chromatography separation. The column (1 50 cm) was eluted with 0.05 M Gly–NaOH buffer (pH 10.8). Peak 2 represents the KGD-proinsulin. (c) DEAE-Sephadex ion-exchange chromatography to further purify the KGD-proinsulin. The column (1 5 cm) was equilibrated with 0.05 M Tris–HC1 and 40% 2-isopropanol at pH 7.0. The KGD-proinsulin was eluted out with a linear NaCl gradient from 0 to 0.30 M in a total volume of 75 ml. Peak 2 represents the KGD-proinsulin. (d) Electrophoretic analysis of purified KGD-proinsulin on 12% (v/v) polyacrylamide gel. Lane 1, human proinsulin; lane 2, purified KGD-proinsulin after DEAE-Sephadex ion-exchange chromatography. The gels were stained with Coomassie Brilliant Blue R-250. 1263 native PAGE (Figure 2d) analyses. The predicted pI of the KGD-proinsulin chimera is about 5.3, so our previous procedure for the purification of recombinant human mutant proinsulin (Jing & Tang 2000) can be adopted to purify the mutant KGD-proinsulin chimeric protein. The final results were shown by Figure 2 which is in agreement with our expectation. Amino acid composition analysis of the KGD-proinsulin chimera was carried out also with native human proinsulin peptide as a control and the data agrees well with the amino acid residues numbers calculated by its primary structure (data not shown). CD spectra analysis indicated the KGD-proinsulin contains very close secondary-structure contents compared with human insulin (Table 1). This determination suggests that our structural simulation of the KGD-proinsulin is very similar to its actual stereo-structure. The inhibitory activity of adenosine 5¢-diphosphate-induced human platelet aggregation by the Table 1. Secondary structure content (%) of the KGD-proinsulin chimera with CD spectra analysis. a-Helix b-Sheet Random structure KGD-proinsulin Insulin 15.1 22.6 63.3 22.8 17.1 60.1 KGD-proinsulin was tested, as shown in Figure 3. Light transmission of ADP-induced platelet aggregation is illustrated in Figure 3a. The KGD-proinsulin shows high platelet aggregation inhibitory activity. The IC50 value calculated is about 830 nM as shown in Figure 3b, which is high compared with that of native disintegrins (Gan 1988, Musial & Niewiarowski 1990, Scarborough et al. 1991). Under the same conditions, both human proinsulin and insulin peptides showed no inhibitory activity of the platelet aggregation (data not shown). The result suggests that the CAKGDWNC-sequence inserted between the B28 site and the A2 site of the mutant proinsulin with intra-A chain disulfide-bond deletion exhibits its functional conformation and can interact directly with corresponding glycoprotein IIb/IIIa receptor on the platelet cell surface. The potent inhibitory activity of the KGD-proinsulin agrees well with our expectation based on the result of structural simulation of the KGD-proinsulin chimera protein. Insulin receptor binding assay showed that the insulin receptor binding activity of the KGDproinsulin is only 0.04% of native human insulin, as shown in Figure 4. This agrees with our expectation that the KGD-proinsulin would not exhibit insulin hormone activity, so the KGDproinsulin chimera is a safe and specific antithrombosis agent and the mutant proinsulin with intra-A chain disulfide bond deletion only acts as Fig. 3. Inhibitory activity analysis of adenosine 5¢-diphosphate-induced platelet aggregation by the KGD-proinsulin. (a) Light transmission measurement of platelet aggregation. Three hundred microliters of platelet-rich plasma were incubated with 25 ll of various concentrations of the KGD-proinsulin at 37 C for 2 min before addition of 25 ll 100 l M ADP. Samples 1–5 represent control buffer, 0.1, 0.5, 1.0 and 10 lm KGD-proinsulin, respectively. (b) Inhibition curve of adenosine 5¢-diphosphate-induced platelet aggregation of the KGD-proinsulin. 1264 Adhesi on % of K2 melanoma cells( 103) 100 × Binding of 125I-insulin(%) 80 60 40 20 0 0 1 2 3 4 5 6 Log concentration(ng ml-1) of KGD-proinsulin 120 100 80 60 40 20 0 0 1 10 100 1000 Concentration (nM) of KGD-proinsulin Fig. 4. Insulin receptor binding assays of the KGD-proinsulin. Vertical axis indicates the binding of 125I-insulin to insulin receptor, and horizontal axis is logarithm of the native insulins or KGD-proinsulin concentrations. The binding of the 125 I-insulin in the absence of native insulin was set at 100%. (n): native insulin, (d): KGD-proinsulin. Fig. 5. Effects of the KGD-proinsulin on adhesion of K2 melanoma cell to (n) fibrinogen and (d) fibronectin. The KGD-proinsulin inhibits the attachment of K2 cell to fibrinogen-coated wells, while it does not block cell attachment to fibronectin-coated wells. All determinations were made in quadruplicate and each sample was examined a minimum of three times. a molecular scaffold. The cell attachment assay showed that the KGD-proinsulin could inhibit the attachment of K2 human melanoma cells to fibrinogen-coated wells but not block the cells’ attachment to fibronetin-coated wells. This phenomena suggests that the KGD-proinsulin exhibited high binding activity with glycoprotein IIb/ IIIa receptor known as the fribrinogen receptor and low activity with alpha5beta1 receptor known as the fibronectin receptor (Figure 5). This receptor specificity indicated that the KGDcontaining sequence introduced into the mutant proinsulin scaffold exhibited its full activity and the KGD-proinsulin not only inhibits platelet aggregation, but also recognizes and interacts specificially with the glycoprotein IIb/IIIa receptor. The detailed structure determination of the KGD-proinsulin chimera is carried out currently. Proinsulin molecule is human origin and has almost no immunogenicity to humans. The constructed KGD-proinsulin with the scaffold of human proinsulin molecule should also not demonstrate immunogenicity when adopted as a therapeutic agent in vivo. In this respect, the KGDproinsulin has a considerable advantage over some naturally occurring antagonists of platelet aggregation purified from snake and leech venom (Gan 1988, Musial & Niewiarowski 1990, Scarborough et al. 1991). The KGD-proinsulin chimera is a first reported KGD-containing recombinant mutant proinsulin with glycoprotein IIb/IIIa receptor specificity. The KGD-proinsulin is easy to obtain through large-scale fermentation as compared with other large recombinant anti-thrombosis proteins (Lee et al. 1993, Nie & Tang 1998). We conclude from the above result that the replacement of the C-peptide with the CAKGDWNC-peptide in mutant proinsulin yields a novel anti-thrombosis agent with potent anti-platelet aggregation activity and the glycoprotein IIb/IIIa receptor binding specificity, but no insulin hormone activity and immunogenicity to human body. This advantage enables the KGD-proinsulin chimera possibility to be adopted as a novel therapeutic agent during the treatment of thrombosis disease. Acknowledgments We thank especially Prof Qun Wei, for helpful discussion about this work; Dr Yin-Ye Wang, for the cell attachment assay; Prof Jian-Xing Ma, from Oklahoma University Health Science Center U.S.A., for suggestion about this manuscript. This work was supported by a grant from Nature Science Foundation of China (30171100, 1265 2001) and a grant from Funds of Distinguished Young Scholars of Beijing Normal University to Dr Jian Jing (104977, 2003). References Dai Y, Tang JG (1996) Characteristic, activity and conformational studies of [A6-Ser, A11-Ser]-insulin. Biochim. Biophys. Acta 1296: 63–68. Gan ZR (1988) A potent platelet aggregation inhibitor from the venom of viper, Echis carinatus. J. Biol. Chem. 263: 19827– 19832. Hua QX, Hu SQ, Frank BH, Jia W, Chu YC, Wang SH, Burke GT, Katsoyannis PG, Weiss MA (1996) Mapping the functional surface of insulin by design: structure and function of a novel A-chain analogue. J. Mol. Biol. 264: 390–403. Jing J, Tang JG (2000) Platelet aggregation inhibitory activity of mutant proinsulin with C-peptide replaced by CRGDSC sequence. Biotechnol. Lett. 22: 47–52. Kiyotaka O, Shigeyuki T (1999) Ussuristatin 2, a novel KGDcontaining disintegrin from Agkistrodon ussuriensis venom. J. Biochem. 125: 31–35. Lee G, Chan W, Hurle MR, Desjarlais RL, Waston F, Sathe GM, Wetzel R (1993) Strong inhibition of fibrinogen binding to platelet receptor alpha IIb beta 3 by RGD sequences installed into a presentation scaffold. Protein Eng. 6: 745–754. Minoux H, Chipot C, Brown D, Maigret B (2000) Structural analysis of the KGD sequence loop of barbourin an alphaIIbbeta3-specific disintegrin. J. Comput. Aided Mol. Des. 14: 317–327. Musial J, Niewiarowski S (1990) Inhibition of platelet adhesion to surfaces of extra-corporeal circuits by disintegrins: RGDcontaining peptide from viper venoms. Circulation 82: 261– 273. Nie X, Tang JG (1998) RGD-containing trypsin with both platelet aggregation inhibitory activity and proteolytic activity. Biochem. Mol. Biol. Int. 45: 1149–1154. Scarborough R, Rose JW, Hsu MA, Phillips DR, Fried VA, Campbell AM, Nannizzi L, Charo IF (1991) Barbourin. A GPIIb/IIIa-specific integrin antagonist from the venom of Sistrurus m barbouri. J. Biol. Chem. 566: 9359–9362. Weiss MA, Frank BH, Khait I, Pekar A, Heine R, Shoelson SE, Neuringer LJ (1990) NMR and photo-CIDNP studies of human proinsulin and prohormone processing intermediates with application to endopeptidase recognition. Biochemistry 29: 8389–8401. Wittig K, Rothe G, Schmitz G (1998) Inhibition of fibrinogen binding and surface recruitment of GPIIb/IIIa as dosedependent effects of the RGD-mimetic MK-852. Thromb. Haemost. 79: 625–630. Springer 2005 Biotechnology Letters (2005) 27: 1267–1271 DOI 10.1007/s10529-005-0216-4 Construction of an effective protein expression system using the tpl promoter in Escherichia coli Takashi Koyanagi1, Takane Katayama2, Ai Hirao1, Hideyuki Suzuki1 & Hidehiko Kumagai22,* 1 Division of Integrated Life Science, Graduate School of Biostudies, Kyoto University, Sakyo-ku Kyoto, 606-8502, Japan 2 Research Institute for Bioresources and Biotechnology, Ishikawa Prefectural University, Nonoichi-machi Ishikawa, 921-8836, Japan *Author for correspondence (Fax: +81-76-227-7557; E-mail: [email protected]) Received after revision 14 June 2005; Accepted 14 June 2005 Key words: Escherichia coli, protein expression system, the tpl promoter, transcriptional regulator TyrR, tyrosine transporter TutB Abstract An effective protein expression system was constructed in Escherichia coli using the promoter of the tyrosine phenol-lyase (tpl) gene of Erwinia herbicola. This system involves a mutant form of the TyrR protein with an enhanced ability to activate tpl and the TutB protein with an ability to transport L -tyrosine (an inducer of Tpl). The highest expression level obtained for this system was more than twice that obtained for the tac system, although it was lower than the level obtained for the T7 system, as revealed with the lacreporter assay and SDS-polyacrylamide gel electrophoresis. Introduction Expression of the tyrosine phenol-lyase (tpl) gene is tyrosine-inducible (Kumagai et al. 1970, Antson et al. 1993, Suzuki et al. 1993), the basis of which is the TyrR-mediated transcriptional activation in the presence of L -tyrosine (Suzuki et al. 1995, Bai & Somerville 1998, Katayama et al. 1999, Pittard et al. 2005). In the previous study on TyrR of Erwinia herbicola, we obtained the mutant tyrR5 allele (tyrRV67A Y72C E201G), the product of which activated tpl expression even without the addition of L-tyrosine to the medium (Katayama et al. 2000). Since the ability of this mutant TyrRV67A Y72C E201G to activate the tpl promoter was significant (Koyanagi et al. 2005), we considered that it could be applied to creating a heterologous protein expression system in Escherichia coli. The construction of the tpl-expression system and evaluation of the system using the lac-reporter assay and SDS-PAGE analysis are described in this paper. Materials and methods Bacterial strains The bacterial strains used in this study were derivatives of E. coli K-12. HMS174 (kDE3) (Campbell et al. 1978), JM101 (Yanisch-Perron et al. 1985), TK743 [F) ara D(lac-pro) thi DtyrR::cat+] (Katayama et al. 2000), and derivatives of TK743 were used as host strains. Media LB broth (Miller 1992) was used as the growth medium. Ampicillin, chloramphenicol, kanamycin, and tetracycline were used at 100, 30, 30, and 15 lg/ml, respectively. 1268 Genetic techniques Standard genetic techniques were used essentially as described by Sambrook & Russell (2001). The lac-reporter gene (lacZ) was amplified by highfidelity PCR using KOD-Plus polymerase (Toyobo). Site-directed mutagenesis was carried out by the method of Kunkel et al. (1987). The entire fragment to be used for manipulation was sequenced to ensure that no base change other than those planned had occurred. The lysogenization of phage kDE3 was performed according to the protocol supplied by Novagen. b-Galactosidase assay An overnight culture was added to fresh LB medium at 1%(v/v). The culture was incubated at 37 C with shaking at 120 rpm. Samples were withdrawn at specific time points and subjected to a b-galactosidase assay according to the method of Miller (1992). For each strain, assays were performed for separate cultures of five independently isolated transformants. SDS-PAGE analysis The cells grown in LB medium were harvested, suspended in 10 mM sodium phosphate buffer (pH 7.2), disrupted by sonication, and then centrifuged at 10,000 g for 10 min to separate the soluble fraction from the insoluble fraction. Ten micrograms of protein from the soluble fraction were loaded on a 12% SDS-PAGE. The concentration of protein was determined by the Lowry method. The insoluble fraction was washed once with 10 mM sodium phosphate buffer (pH 7.2), suspended and boiled in cracking buffer (60 mM Tris/HCl (pH 6.8), 140 mM 2-mercaptoethanol, 35 mM SDS, 1 M glycerol, and 150 lM Bromophenol Blue), and then centrifuged at 10,000 g for 10 min. The supernatant, equivalent to 0.7 lg (wet wt) of cells, was loaded on the same gel. After the electrophoresis, the gel was stained with Coomassie Brilliant Blue R-250. Results and discussion Construction of the vector First, we made a suitable expression vector with multiple cloning sites as shown in Figure 1. Step 1: Fig. 1. Scheme of the vector’s construction. The numbering of pAH423 starts at the first T in the sequence GAATTC (EcoRI), and the unique restriction sites are indicated. The multiple cloning sites are shown below the map. An NdeI site was introduced at the initiation codon of the tpl gene on pTK304 (Katayama et al. 1999) by site-directed mutagenesis. Step 2: The 1269 1.5-kb NdeI-PstI fragment containing the coding region of tpl was replaced with a similarly digested short fragment that was made by annealing two complementary oligonucleotides containing multiple cloning sites, 5¢-CCATATGGATCCGCGGCCGCCATGGCTGCAGG-3¢ and 5¢-CCTGCA GCCATGGCGGCCGCGGATCCATATGG -3¢. Step 3: The resulting plasmid was digested with SphI, blunt-ended, and ligated with the 0.7-kb XmnI fragment containing a strong transcription terminator (rrnBT1T2) excised from pTrc99A (Amersham). Step 4: Next, the region containing the TyrR binding sites, the tpl promoter, the ribosome-binding site, the multiple cloning sites, and the transcription terminator in this order was excised by digestion with SmaI and HindIII (blunt-ended), and inserted into a blunt-ended NdeI site of pBR322. Step 5: Finally, the tetracycline resistance gene was deleted by removing the 0.8-kb EcoRV-NruI fragment to generate pAH423. Evaluation of the tpl-expression system using the lac-reporter gene The efficiency of the tpl-expression system was evaluated using the lac-reporter assay. The b-galactosidase (lacZ) gene was inserted into the NdeI-NotI sites of pAH423, and the resulting reporter plasmid (pAH444) was introduced into TK743 [F) ara D(lac-pro) thi DtyrR::cat+] carrying either the wild-type tyrR gene or the mutant tyrR5 gene on a pSC101-derived plasmid. The strain was grown in LB medium and then subjected to the b-galactosidase assay. As shown in Figure 2, the strain carrying the tyrR5 allele had significantly increased reporter activity as compared to the strain carrying the wild-type allele. The level of expression was further elevated on introduction of the tyrosine transporter tutB gene (Katayama et al. 2002). In the presence of a pACYC-derived plasmid carrying tutB, approximately 1.3-fold more activity was obtained, due to the increased intracellular concentration of L-tyrosine (an inducer of Tpl). However, no significant effect was observed on the expression level even when 0.1% L-tyrosine was added to the medium, maybe because LB broth originally contains a considerable amount of L-tyrosine (data not shown). Thus, the level of Fig. 2. Evaluation of the tpl-expression system using the lacreporter assay. The plasmid pAH423 carrying the lac-reporter gene under the control of the tpl promoter (pAH444) was introduced into strain TK743 [F) ara D(lac-pro) thi DtyrR::cat+] carrying either the wild-type tyrR gene (pSC101 replicon tet+tyrRE. herbicola+) ()) or the tyrR5 gene (pSC101 replicon tet+ tyrRE. herbicolaV67A Y72C E201G) (s) on the plasmid, or strain TK743 carrying an empty vector (pSC101 replicon tet+) (h). The strain carrying the tyrR5 allele was further transformed with a plasmid carrying tutB (p15A replicon kan+ tutB+) (n). These strains were grown in LB medium. Samples were withdrawn at the indicated time, and subjected to a b-galactosidase assay. The values are averages of at least two independent experiments. expression is maximized when the strain carrying tyrR5 and tutB is used as a host and incubated in LB medium for 32 h. The highest value obtained for the tpl-expression system was compared to that obtained for the tac- and T7-expression systems. The lacreporter gene was inserted into the NdeI-PstI (blunt-ended) sites of pMAL-c2E (for the tac system; New England BioLabs) to generate pAH349, and the NdeI-BamHI (blunt-ended) sites of pET-3a (for the T7 system; Novagen) to generate pAH471. The resulting reporter plasmids pAH349 (tac system) and pAH471 (T7 system) were introduced into strain AH359 [F’ traD36 lacIq D (lacZ)M15 proA+B+/ara D(lacpro) thi DtyrR::cat+] and kDE3-lysogenized AH359, respectively. The reporter plasmid for the tpl system, pAH444, was introduced into strain AH359 carrying the tyrR5 and tutB genes on separate plasmids. These strains were grown in LB medium and, as for the tac and T7 1270 systems, 0.5 mM IPTG was added at the midgrowth phase to induce expression. Samples were withdrawn at different times, and subjected to a b-galactosidase assay. The inhibitory effect of IPTG (the substrate analogue) on b-galactosidase activity was negligible (3.6% of total Miller U). As a result, the highest expression level obtained for the tpl system (20,000 ± 3,000 Miller U) was found to be 2.5-fold higher than that for the tac system (7,900 ± 800 Miller U, 2 h after induction). This was also the case when a different E. coli strain, JM101, was used as a host (21,000 ± 2,000 Miller U for the tpl system vs. 8,600 ± 500 Miller U for the tac system). Although JM101 possesses the wild-type tyrR allele on its chromosome, it did not affect the action of TyrRV67A Y72C E201G on the tpl promoter, indicating that the tyrR) genotype is not necessary for the host genetic background. Compared to the T7 system, the tpl system exhibited a comparatively low level of efficiency of expression. The highest value obtained for the T7 system using AH359 (kDE3) as a host was 33,000 ± 2,000 Miller U, about 1.7-fold higher than that obtained for the tpl system. When HMS174 (kDE3) (Novagen) was used as a host cell, a maximum of 28,000 ± 4,000 Miller U was obtained. As for strain HMS174 (kDE3) harboring the reporter plasmid pAH471, the net reporter activity was calculated by subtracting the b-galactosidase activity of the host (Lac+) (9,000 ± 1,000 Miller U) from the total activity of the strain carrying pAH471 (37,000 ± 4,000 Miller U). Next, the solubility and functionality of the synthesized LacZ protein were evaluated by SDSPAGE analysis. The cells harvested when the reporter activity was at a maximum were disrupted by sonication, and then centrifuged at 10,000 g for 10 min to separate the soluble fraction from the remaining insoluble fraction. Each fraction was subjected to electrophoresis, and the gel was stained with Coomassie Brilliant Blue R-250. The LacZ protein was detected with a molecular size of approximately 120 kDa as shown in Figure 3 (indicated by an arrow). Consequently, it was revealed that the differences among the three systems as to the amounts of soluble forms of LacZ well reflected the results of the reporter assay. The tpl system (lanes 4 and 5) produced a soluble b-galactosidase at two- to three-fold higher level of the tac system (lanes 2 and 3), but at about a two-fold Fig. 3. Comparison of the amounts of soluble and insoluble forms of the LacZ protein expressed by the tac-, tpl-, and T7expression systems. The cells grown in LB medium were harvested, suspended in 10 mM sodium phosphate buffer (pH 7.2), disrupted by sonication, and then centrifuged. The soluble fractions (equivalent to 10 lg of protein; lanes 2–7) and insoluble fractions (equivalent to 0.7 lg of wet weight of cells; lanes 9–11) were loaded on a 12% SDS-polyacrylamide gel, and the gel was stained with Coomassie Brilliant Blue R-250. b-Galactosidase is indicated by an arrow (approximately 120 kDa). Lanes 1 and 8, Prestained Protein Marker, Broad Range (New England BioLabs); lanes 2 and 3, the tac system using AH359 and JM101 as hosts, respectively; lanes 4 and 5, the tpl system using AH359 and JM101 as hosts, respectively; lanes 6 and 7, the T7 system using AH359 (kDE3) and HMS174 (kDE3) as hosts, respectively; lanes 9–11, the tac-, tpl-, and T7-expression systems using AH359 (for tac and tpl) and AH359 (kDE3) (for T7) as hosts. lower level than the T7 system (lane 6 and 7). The results suggested that all soluble protein molecules expressed by the tpl system should be functional. Apparently all LacZ molecules were expressed in a soluble form when its gene was placed under the control of the tpl promoter (lane 10), while a significant amount of LacZ was synthesized in an insoluble form when the T7 system was employed (lane 11). The results presented here indicate that we succeeded in constructing an effective protein expression system by using the tpl promoter, the mutant TyrR protein, and the tyrosine transporter TutB. One important advantage of this system is that, essentially, any strain is available as the host, in contrast to the T7 system which requires a certain genetic background for the infection and/or lysogenization of phage kDE3 when one wants to use a specific E. coli strain as 1271 an expression host. Thus, although the tplexpression system is not applicable to proteins toxic to E. coli, it could serve as a good alternative to commonly used protein expression systems. Acknowledgements This work was partly supported by a Grant-inAid for Scientific Research (B), No. 14360056, from the Ministry of Education, Culture, Sports, Science, and Technology, Japan. T. Koyanagi was supported by the 21st Century COE Program of the Ministry of Education, Culture, Sports, Science and Technology. References Antson AA, Demidkina TV, Gollnick P, Dauter Z, von Tersch RL, Long J, Berezhnoy SN, Phillips RS, Harutyunyan EH, Wilson KS (1993) Three-dimensional structure of tyrosine phenol-lyase. Biochemistry 32: 4195–4206. Bai Q, Somerville RL (1998) Integration host factor and cyclic AMP receptor protein are required for TyrR-mediated activation of tpl in Citrobacter freundii. J. Bacteriol. 180: 6173–6186. Campbell JL, Richardson CC, Studier FW (1978) Genetic recombination and complementation between bacteriophage T7 and cloned fragments of T7 DNA. Proc. Natl. Acad. Sci. USA 75: 2276–2280. Katayama T, Suzuki H, Koyanagi T, Kumagai H (2000) Cloning and random mutagenesis of the Erwinia herbicola tyrR gene for high-level expression of tyrosine phenol-lyase. Appl. Environ. Microbiol. 66: 4764–4771. Katayama T, Suzuki H, Koyanagi T, Kumagai H (2002) Functional analysis of the Erwinia herbicola tutB gene and its product. J. Bacteriol. 184: 3135–3141. Katayama T, Suzuki H, Yamamoto K, Kumagai H (1999) Transcriptional regulation of tyrosine phenol-lyase gene mediated through TyrR and cAMP receptor protein. Biosci. Biotechnol. Biochem. 63: 1823–1827. Koyanagi T, Katayama T, Suzuki H, Nakazawa H, Yokozeki K, Kumagai H (2005) Effective production of 3,4-dihydroxyphenyl-L -alanine (L -DOPA) with Erwinia herbicola cells carrying a mutant transcriptional regulator TyrR. J. Biotechnol. 115: 303–306. Kumagai H, Yamada H, Matsui H, Ohkishi H, Ogata K (1970) Tyrosine phenol lyase. I. Purification, crystallization, and properties. J. Biol. Chem. 245: 1767–1772. Kunkel TA, Roberts JD, Zakour RA (1987) Rapid and efficient site-specific mutagenesis without phenotypic selection. Methods in Enzymology 154: 367–382. Miller JH (1992) A Short Course in Bacterial Genetics. A Laboratory Manual and Handbook for Escherichia coli and Related Bacteria. Cold Spring, Harbor, NY:Cold Spring Harbor Laboratory. Pittard J, Camakaris H, Yang J (2005) The TyrR regulon. Mol. Microbiol. 55: 16–26. Sambrook J, Russell DW (2001) Moleculer Cloning: A Laboratory Manual, 3rd edn. Cold Spring Harbor, NY:Cold Spring Harbor Laboratory. Suzuki H, Katayama T, Yamamoto K, Kumagai H (1995) Transcriptional regulation of tyrosine phenol-lyase gene of Erwinia herbicola AJ2985. Biosci. Biotechnol. Biochem. 59: 2339–2341. Suzuki H, Nishihara K, Usui N, Matsui H, Kumagai H (1993) Cloning and nucleotide sequence of Erwinia herbicola AJ2982 tyrosine phenol-lyase gene. J. Ferment. Bioeng. 75: 145–148. Yanisch-Perron C, Vieira J, Messing J (1985) Improved M13 phage cloning vectors and host strains: nucleotide sequences of the M13mp18 and pUC19 vectors. Gene 33: 103–119. Springer 2005 Biotechnology Letters (2005) 27: 1273–1276 DOI 10.1007/s10529-005-0218-2 Purification and properties of an N-acetylglucosaminidase from Streptomyces cerradoensis Iderval da Silva Junior Sobrinho1, Luiz Artur Mendes Bataus2, Valéria Ribeiro Maitan2 & Cirano José Ulhoa1,* 1 Laboratório de Enzimologia, Universidade Federal de Goiás, 74001-970, Goiânia, GO, Brazil Laboratório de Bioquı´mica e Engenharia Gene´tica, Universidade Federal de Goiás, 74001-970, Goiânia, GO, Brazil *Author for correspondence (E-mail: [email protected]) 2 Received 22 March 2005; Revisions requested 19 April 2005; Revisions received 14 June 2005; Accepted 15 June 2005 Key words: N-acetylglucosaminidase, characterization, production, Streptomyces cerradoensis Abstract An N-acetylglucosaminidase produced by Streptomyces cerradoensis was partially purified giving, by SDSPAGE analysis, two main protein bands with Mr of 58.9 and 56.4 kDa. The Km and Vmax values for the enzyme using p-nitrophenyl-b-N-acetylglucosaminide as substrate were of 0.13 mM and 1.95 U mg)1 protein, respectively. The enzyme was optimally activity at pH 5.5 and at 50 C when assayed over 10 min. Enzyme activity was strongly inhibited by Cu2+ and Hg2+ at 10 mM, and was specific to substrates containing acetamide groups such as p-nitrophenyl-b-N-acetylglucosaminide and p-nitrophenyl-b-D-N,N¢diacetylchitobiose. Introduction Chitin, a b)1, 4-linked polymer of N-acetylglucosamine, is a structural component of the arthropod exoskeleton and is a common constituent of fungal cell walls. The complete degradation of chitin is performed by the chitinolytic system composed of chitinases (EC 3.2.1.14) and N-acetylglucosaminidases (E.C. 3.2.1.30) (Sahai & Manocha 1993). Chitinases can hydrolase the substrate by two possible mechanisms, identified by the products of hydrolysis: (a) endochitinases cleave internal bonds within chitin releasing chitotetraose, chitotriose and chitobiose; (b) exochitinases catalyses the release of chitobiose without the formation of oligo or monosaccharides. The N-acetylglucosaminidases cleave chitobiose, chitotriose and chitotetraose releasing N-acetylglucosamine. Among bacteria, the actinomycetes are an important chitinase-producing group, especially those belonging to the genus Streptomyces (Broadway et al. 1995, El Sayed et al. 2000, Gomes et al. 2000, Ueno & Miyashita 2000). There is less work about N-acetylglucosaminidase from other organisms and few researches have been done to characterize this type of enzyme from Streptomyces. In this article we describe the partial purification and characterization of a Nacetylglucosaminidase produced by Streptomyces cerradoensis, isolated from Brazilian cerrado soils. Materials and methods Microorganism and enzyme production Streptomyces cerradoensis obtained from solid culture media (ISP-2) were inoculated in Erlenmeyer flasks containing 50 ml YEME liquid media (Hopwood et al. 1985). 1274 Samples of 50 ll of cells suspension from YEME media were added to Erlenmeyer flasks (250 ml) containing 50 ml media: 0.2% (w/v) K2HPO4, 0.3% (w/v) NaCl, 0.3% (w/v) KNO3, 0.05% (w/v) MgSO4 Æ 7H2O, 0.04% (w/v) CaCl2 Æ 2H2O, 0.002% (w/v) FeSO4, 0.001% (w/v) MnSO4, 1% (w/v) chitin, pH 7.0. The flasks were incubated at 30 C with shaking (150 rpm) for 9 days. N-Acetylglucosaminidase assay (NAGase) Enzyme activity was assayed using p-nitrophenyl-b-N-acetylglucosaminide (pNP-GlcNAc) as substrate. The reaction mixture consisted of 50 ll enzyme solution, 350 ll 50 mM sodium acetate buffer (pH 5.5) and 100 ll 5 mM pNPGlcNAc as described by Ulhoa and Peberdy (1993). One unit (U) of enzyme was defined as the amount of enzyme that released 1 lM p-nitrophenol per min. Partial enzyme purification Samples of the supernatant (150 ml) were applied to a SP-Sepharose chromatography column (2.2 15 cm), equilibrated with 50 mM sodium acetate buffer (pH 5.5), at 1 ml min)1. The column was washed with the same buffer and the proteins eluted with a linear gradient of 0–1 M NaCl. Fractions containing NAGase activity were pooled, dialyzed against 50 mM sodium acetate buffer (pH 5.0), and applied to methylSepharose column (1 5 cm). The adsorbed proteins were eluted at 4 C with a decreasing linear gradient of (NH4)2SO4 (1.2 M to 0). Fractions containing NAGase activity were pooled and stored at )10 C. SDS-PAGE with 10 % (w/v) polyacrylamide was by the standard method of by Laemmli. The proteins were silver stained by the method of Blum et al. (1987). Results and discussion Production of N-acetylglucosaminidase Recently, we isolated a chitin-degrading actinomycete from soil sample, which was identified as belonging to Streptomyces genus. Sequence analysis of the gene encoding 16S rDNA (GeneBank Accession No. AY627277) showed that this actinomycete is a new species, named by us as Streptomyces cerradoensis. This strain showed in preliminary tests, high chitinase and N-acetylglucosaminidase (NAGase) activity when grown in chitin-containing medium. A main peaks of NAGase activity (0.061 U) was found after 120 h growth at 30 C. Partial purification of N-acetylglucosaminidase The enzyme was partially purified from a culture supernatant by ion exchange chromatography and gel filtration. The fractions obtained after the procedure were free of chitinase activity. At the final steps, two main bands of protein were detected by SDS-PAGE with apparent molecular mass of 58.9 and 56.4 kDa (Figure 1). This Thin-layer chromatography The end products of the enzymatic hydrolysis of N,N¢-diacetylchitobiose (5 mM), N,N¢,N¢¢-triacetylchitotriose (5 mM) and colloidal chitin (0.2%, w/v) were analyzed by TLC according to Chung et al. (1995). Fig. 1. Protein profile on SDS-PAGE at a concentration of 10% polyacrylamide. Lane M indicates the molecular mass markers and N shows the N-acetylglucosaminidase partially. Phosphorylase b (99.4 kDa), serum albumin (66.0 kDa), ovalbumin (45.0 kDa) and carbonic anhydrase (29.0 kDa) were used as molecular mass standards. 1275 Table 1. Biochemical properties of the NAGase from Streptomyces cerradoensis. pH Optimum Temperature optimum (C) Temperature stability pH 5.5 over 30 min 40 C 55 C Km (mM) Vmax (U mg)1 protein) Inhibition by Hg2+ (10 mM) Inhibition by Cu2+ (10 mM) 5.0 50 30% 12% 0.13 1.95 100% 78% The effect of pH on the enzyme activity was determined by varying the pH of the reaction mixtures using sodium acetate (pH 3.5–5.5) and potassium phosphate buffer (pH 6.0–7.5). The effect of temperature on the enzymatic activity was determined at the pH optimum, in the range of 30–75 C. The effect of temperature on the enzyme stability was analyzed by previously incubating the enzyme at 40 and 55 C for 30 min. Michaelis– Menten constant (Km) was determined by non-linear-regression analysis of data obtained by measuring the rate of qNP-GlcNAc hydrolysis (from 0.02 to 0.6 mM). The inhibition of the NAGase activity by metal ions was determined through previous incubation of the enzyme samples with 10 mM ZnSO4, KCl, MgSO4, CaCl2, CuSO4 and HgCl2 for 2 min. Results are means values of three replicates. molecular weight was in a similar range to that produced by S. thermoviolaceus (Tsujibo et al. 1998) although, smaller NAGases (27 and 49.5 kDa) also have been isolated and characterized from Streptomyces plicatus (Tarentino et al. 1978, Trimble et al. 1982). Enzyme characterization The lower Km (0.13 mM) indicates that the enzyme has high affinity for the substrate when it is compared with those reported for S. thermoviolaceus (0.43 mM) and for S. hygroscopicus (NA1: 0.12 mM and NA2: 0.76 mM) (Irhuma et al. 1991, Tsujibo et al. 1998). Most bacterial NAGases are optimally active in the range of pH 4–5 and between 50 and 60 C (Trimble et al. 1982, Irhuma et al. 1991, Saito et al. 1998, Tsujibo et al. 1998). Concurring with this, the NAGase of S. cerradoensis displayed maximal activity at pH 5 and at 50 C (Table 1). The enzyme, though, rapidly lost activity either at 40 or 55 C (Table 1). Activity was not affected by Ca2+, Mg2+ and Zn2+ but was inhibited by Cu2+ and Hg2+ at 10 mM. Almost all of the NAGases from Streptomyces are inhibited by Hg2+ indicating the importance of indole amino acid residues in the enzyme function (Irhuma et al. 1991, Trimble et al. 1982, Tsujibo et al. 1998). Substrate specificity The activity of the enzyme was observed only over substrates containing acetamide groups (Table 2). Similar results were observed for NAGase from other Streptomyces species, suggesting that acetamide groups are important to the recognition of chitin and its oligomers by these enzymes (Tsujibo et al. 1998). N-Acetylglucosaminide was released from N,N¢-diacetylchitobiose and N,N¢,N¢¢-triacetylchitotriose after 24 h incubation, while this monomer was released from colloidal chitin only after 48 h incubation. Such a profile indicates that this enzyme acts at the extremity of the substrates releasing N-acetylglucosaminide and accords with the definition of NGAse as proposed by Sahai and Manocha (1993). Acknowledgements This work was supported by a biotechnology research grant to C.J. Ulhoa from CNPq and FUNAPE/UFG. I.S. Jr. Sobrinho was supported by CAPES/MEC Brazil. Table 2. Specificity of N-acetylglucosaminidase to different substrates. Substrate (5 mM) Enzyme activity (U) Relative activity (%) p-Nitrophenyl-b-N-acetylglucosaminide p-Nitrophenyl-b-D-N,N’-diacetylchitobiose p-Nitrophenyl-b-D-glucopyranoside p-Nitrophenyl-b-D-galactopyranoside 27 ± 4 6.5 ± 0.04 0.07 ± 0.01 0 100 25 0.3 0 The reaction mixture consisted of 50 ll of enzyme solution, 350 ll 50 mM sodium acetate buffer (pH 5.5) and 100 ll of specific pnitrophenyl substrate (5 mM). One unit (U) of enzyme was defined as the amount of enzyme that released 1 lM p-nitrophenol per min. 1276 References Blum H, Beier H, Gross H (1987) Improved silver staining of plants proteins, RNA and DNA in polyacrilamide gels. Eletrophoresis 8: 93–99. Broadway RM, Williams DL, Kain WC, Harman GE, Lorito M, Labeda DP (1995) Partial characterization of chitinolytic enzymes from Streptomyces albidoflavus. Lett. Appl. Microbiol. 20: 271–276. Chung YC, Kobayashi T, Kanai H, Akiba T, Kudo T (1995) Purification and properties of extracellular amylase from the hyperthermophilic archeon Thermococcus profundus DT 5432. Appl. Environ. Microbiol. 1: 1502–1506. El Sayed EISA, Ezzat SM, Ghaly MF, Mansour M, El Bohey MA (2000) Purification and characterization of two chitinases from Streptomyces albovinaceus S-22. World J. Microbiol. Biotechnol. 16: 87–89. Gomes RC, Semêdo LTAS, Soares RMA, Alviano CS, Linhares LF, Coelho RRR (2000) Chitinolytic activity of actinomycetes from a cerrado soil and their potential in biocontrol. Lett. Appl. Microbiol. 30: 146–150. Hopwood DA, Bibb MJ, Chater KF, Kieser T, Bruton CJ, Kieser HM, Lydiate DJ, Smith CP, Ward JM, Schrempf H (1985) Genetic Manipulation of Streptomyces: A Laboratory Manual, New York:The John Innes Foundation. Irhuma A, Gallagher J, Hackett TJ, McHale AP (1991) Studies on N-acetylglucosaminidase activity produced by Streptomyces hygroscopicus. Biochim. Biophys. Acta 1074: 1–5. Sahai AS, Manocha MS (1993) Chitinases of fungi and plants: their involvement in morphogenesis and host–parasite interaction. FEMS Microbiol. Rev. 4: 317–338. Saito A, Fujii T, Yoneyama T, Miyashita K (1998) glk is involved in glucose repression of chitinase production in Streptomyces lividans. J. Bacteriol. 180: 2911–2914. Tarentino AL, Trimble RB, Maley F (1978) Endo-b-N-acetylglucosaminidase from Streptomyces plicatus. Methods in Enzymology 1: 574–580. Trimble RB, Tarentino AL, Aumick GE, Maley F (1982) Endob-N-acetylglucosaminidase L from Streptomyces plicatus. Methods in Enzymology 83: 603–610. Tsujibo H, Hatano N, Mikami T, Hirasawa A, Miyamoto K, Inamori Y (1998) A novel b-N-acetylglucosaminidase from Streptomyces thermoviolaceus OPC-520: gene cloning, expression, and assignment to family 3 of the glycosyl hydrolases. Appl. Environ. Microbiol. 64: 2920–2924. Ulhoa CJ, Peberdy JF (1993) Effect of carbon sources on chitobiose production by Trichoderma harzianum. Mycology Res. 97: 45–48. Ueno H, Miyashita K (2000) Inductive production of chitinolytic enzymes in soil microcosms using chitin, other carbonsources, and chitinase-producing Streptomyces. Soil Sci. Plant Nut. 46: 863–871. Springer 2005 Biotechnology Letters (2005) 27: 1277–1282 DOI 10.1007/s10529-005-3219-2 A modified PCR system for amplifying b-ketoacyl-ACP synthase gene fragments with DNA from Streptomyces luteogriseus Feng-Ming Yu, Xin Jiang, Jin-Chuan Wu & Ying-Jin Yuan* Department of Pharmaceutical Engineering, Tianjin University, P.O. Box 6888, 300072, Tianjin, P. R. China *Author for correspondence (Fax: 86-22-27403888; E-mail: [email protected], [email protected]) Received 27 April 2005; Revisions requested 18 May 2005; Revisions received 15 June 2005; Accepted 15 June 2005 Key words: b-ketoacyl-ACP luteogriseus synthase, gene amplification, modified PCR system, Streptomyces Abstract Streptomyces luteogriseus strain 099, producing a new type of macrolide antibiotic with anti-coxB6 virus and anti-HIV protease activities, was isolated from soil. PCR was optimized to amplify b-ketoacyl-ACP synthase (KS) genes. The system was optimized around the use of higher concentrations of DMSO (15% vs. 10% v/v) and dNTP (500 lM vs. 50–200 lM) and a lower annealing temperature (55 C vs. 60–70 C) than the normal PCR method used to amplify high GC content DNA. Introduction Actinomycetes, especially streptomyces, are major producers of antibiotics and other secondary metabolites and are industrially important. The research on the functional genome is becoming deeper and wider. The total sequence of Streptomyces coelicolor and S. averimitilis genomes and partial gene sequence of some other important strains producing antibiotics have been reported. This has resulted in a call for genetic reconstruction of strains for producing industrially useful metabolites and the synthesis of new type of antibiotics using combinatorial biosynthesis (Rodrigue et al. 2003, Weber et al. 2003). The study of relative genes for antibiotic synthesis is therefore essential. Genes of streptomyces are usually obtained by a shot-gun method which is time-consuming. According to the homology among genes, fragments could be obtained by PCR (Izumikawa et al. 2003). For GC-rich template DNA from streptomyces PCR is often frustrated by inadequate yield of the target DNA sequence and undesired non-specific bonds (Chakrabarti & Schutt 2001). So normal PCR is not suitable for amplifying gene fragments of streptomyces and different corrective actions have different results under different conditions. It is essential that the PCR system and reaction conditions for streptomyces be optimized. Streptomyces luteogriseus 099 was isolated from soil by our group. It can produce a secondary metabolite having good anti-coxB6 virus and anti-HIV protease properties with the IC50 of 230 lg/ml and 40 lg/ml, respectively, showing a broad application spectrum (Wang 2004). By means of precursors and specific inhibitors added during experiments, together with NMR, UV and IR spectrum analyses, the screened substance was speculated to be a macrolide antibiotic synthesized through the polyketide pathway. However, we found that a KS (b-ketoacyl-ACP synthase) fragment of its genome could not be amplified perfectly by normal PCR. We have therefore attempted the to optimize the PCR system and reaction conditions and report the results below. 1278 Materials and methods Strains and culture medium Streptomyces luteogriseus 099 was isolated and preserved in our laboratory. E. coli DH5a was obtained from Prof. Lai-Jun Xing of Nankai University, China. The medium for S. luteogriseus contained 5 g glucose, 30 g soluble starch, 4 g peptone, 1.5 g K2HPO4, 0.25 g NaCl, 0.5 g MgSO4 in 1 liter water, pH 7.0. Luria–Bertani (LB) medium was used for showing E.coli. Reagents and materials A PCR reagent kit, restriction enzyme EcoRI, HindIII, DNA Marker DL2000 and pMD-18T vector were obtained from Takara Biotechnology Corporation. The Ultra-sep Gel Extraction kit was obtained from Omega Bio-Tek, USA. The Hybaid PCR express thermal cycler was obtained from Hybaid, UK. The GDS-8000 System and UVP Bioimaging Systems were obtained from UVP, Inc., USA. Other chemicals were of reagent grade and obtained commercially. Genome DNA extraction A modified method of Hopwood et al. (1985) was used. After culturing S. luteogriseus for 24 h, the mycelium was collected, washed with 150 mM NaCl/100 mM EDTA and treated with lysozyme at 37 C. After addition of SDS followed by heating to 65 C, the viscosity of the mycelium solution declined. Equal volumes of phenol/chloroform/isoamyl alcohol (25:24:1, by vol.) were added to remove protein. After extracting twice with chloroform, 0.9 vol. cold 2-propanol was added into the aqueous phase to precipitate DNA. DNA was washed twice with 70% (v/v) ethanol, dried at room temperature and then dissolved in TE buffer (pH 8.0). RNA was degraded in the same manner by RNase. The purity and content of DNA were measured by absorbancies. designed according to the homology of KS gene sequences in S. avermitilis, S. coelicolor and other strains published in the GeneBank. Primers were provided by Shanghai Sangon Biological Engineering Technology and Services Co., Ltd, China. PCR system PCR was carried out under the following conditions. The original reaction system was determined by the preliminary experiment with the PCR solution containing 5 ll 10 buffer, 2.5 mM MgCl2, 500 lM dNTP, 500 ng DNA template, 1 lM each primer, certain organic additives at different concentrations and 0.5 ll Taq polymerase (5 U/ll) with the volume made to 50 ll with sterilize water. The reaction was conducted at 95 C for 10 min, 94 C for 30 s, 55 C for 30 s, 72 C for 1 min (40 cycles) and 72 C for 10 min, respectively. Electrophoresis Electrophoresis of amplification products was done on 1% agarose gels in which 5 ll reaction products were loaded with 0.5 ll 10 loading buffer. Gels were run at 80 V for 40 min, stained with ethidium bromide, visualized on a UV transilluminator and documented by UVP Bioimaging System. Amplification product purified from gel The Ultra-Sep Gel Extraction Kit was used to purify the amplification product according to manufacturer’s recommendation. Techniques for DNA manipulation DNA manipulation techniques were carried out according to standard protocols and instruction kits, which include linkage of the amplification product with the vector, transformation into E. coli, screening of the positive clone and plasmid preparation, etc. Primer designing DNA sequencing Forward primer (5¢-GCTCGTACTCGTCGCT CCCGGCCAG-3¢) and reversed primer (5¢-CGACATGGTCGCGACGGTCTCCTCG-3¢) were Amplification product was sequenced by Shanghai Sangon Biological Engineering Technology and Services Co., Ltd, China. 1279 Fig. 1. Effect of additive types on amplification. (a), DMSO; (b), methanamide; (c), glycerol (Lane M, DL2000 DNA marker; lane 1, PCR with no additive; lanes 2–6, PCR with additives at 1, 5, 10, 15 and 20% (v/v), respectively); (d), PCR at different pre-denaturation times (Lane M, DL2000 DNA marker; lane 1, 10 min; lane 2, 5 min). Results and discussion PCR enhancement by additives GC content in the Streptomyces genome is over 70%. Higher energy is needed to melt DNA chains otherwise primers cannot be coupled with the template DNA for two chains combined together (Chenchik et al. 1996) and there will be no amplification product. To lower the annealing temperature to make it suitable for the annealing between primers and template and favorable for 1280 DNA polymerase to go through the secondary structure region, as well as to avoid the nonspecific amplification and the formation of primer dimer at the same time, some measures have been taken, such as improving the denaturing temperature, adding organic solvents including formamide (Sarkar et al. 1990) dimethylsulfoxide (DMSO) (Baskaran et al. 1996), glycerol (Pomp and Medrano 1991) and betaine (Hengen 1997). However, these methods are not always effective for reasons that are still unclear. In our experiments, the pre-denaturation time was prolonged to 10 min and the annealing temperature was increased from 55 to 70 C but there was no target fragment amplified. When glycerol and formamide were added into the reaction system, no target fragment was amplified (Figure 1a–c). Formamide slightly suppressed the dimer formation and non-specific amplification. Glycerol only inhibited non-specific amplification. Amplification was evident with DMSO at 5% (v/v) and was maximal at 15% (v/v). Above 15% or under 5% (v/v), amplification was not observed. It is characteristic that the amount of the added DMSO was higher in our system than in the normal reaction system, and 15% (v/v) DMSO was used in the subsequent experiments. Although 10% (v/v) DMSO is the commonly used concentration for amplifying high GC content DNA (Pomp and Medrano 1991, Carmody et al. 2004) it is changeable and adjustable according to the practical conditions. When the pre-denaturation time was shortened to 5 min, the amplified product was detected and its quantity changed little (Figure 1d). Therefore the pre-denaturation time was set at 5 min. Effect of primer concentration on PCR The optimal primer concentration is between 0.1 and 1.0 lM. If the primer concentration is too high, it would lead to a mismatch between primer and template, non-specific amplification and an increased chance of dimer formation. In our experiments, a better yield and specificity of amplified product were detected with each primer at 1 lM, but there was dimer formation (Figure 2). When a pair of primers was used at 0.2 lM, no dimer formation was observed but the amount of amplified product became less. The Fig. 2. Effect of primer concentration on amplification reaction. Lane M, DL2000 DNA marker; lanes 1–5, PCR with primers at 0.2, 1, 2, 3 and 4 lM, respectively. suitable primer concentration was between 0.2 and 1 lM so 1 lM was used in the subsequent experiments. Effect of dNTP amount on PCR In the amplification reaction, increased precision of the reaction was obtained with a lower concentration of dNTP. When its concentration was below 400 lM, the target amplification product was not detected but reached its maximum at 500 lM (Figure 3). A higher concentration of dNTP was unfavorable for PCR due to its combination with Mg2+ resulting in the shortage of free Mg2+. In the normal PCR system, the dNTP concentration ranged from 50 to 200 lM but, in our system, the dNTP concentration was as high as 500 lM, dramatically exceeding that conventionally used. Influence of Mg2+ on amplification Mg2+ can alter the amount of amplification product by changing DNA polymerase activity and affect the reaction specificity by virtue of changing the primer annealing temperature. The optimal concentration of Mg2+ changes when 1281 Fig. 3. Effect of dNTP concentration on amplification. Lane M, DL2000 DNA marker; lanes 1–5, PCR with dNTP at 100, 200, 300, 400 and 500 lM, respectively. Fig. 4. Effect of Mg2+ on amplification. Lane M, DL2000 DNA marker; lanes 1–6, PCR with Mg2+ at 0.5, 1, 1.5, 2, 2.5 and 3 mM, respectively. different primers, templates and different amounts of dNTP are used. A high concentration of Mg2+ would increase the output and non-specificity and decrease the fidelity. But the yield may be reduced at low concentrations. In our experiments, the best result was obtained at 2 mM Mg2+ (Figure 4). reduce the possibility of mutant and ensure plentiful amplification product, 30–35 cycles are recommended in this PCR system. Effect of template DNA concentration on PCR In order to reduce the probability of mistakes produced by Taq polymerase and achieve a higher quantity of amplified product, a higher concentration of DNA was used. If DNA content is too high, it will increase contamination and reduce the amplification efficiency. With the template concentration increased, the amount of amplification product increased and peaked at 400 ng (Figure 5). So 400 ng was selected as the optimized DNA concentration in the subsequent tests. Influence of cycles on amplification Figure 6 shows that amplification was evident when the cycles reached 25 and the yield was maximal at 35 cycles. In order to save energy, Fig. 5. Effect of DNA amount on amplification reaction. Lane M, DL2000 DNA marker, lanes 1–5: PCR with DNA at 100, 200, 300, 400 and 500 ng, respectively. 1282 concentrations of DMSO and dNTP and lower annealing temperature. Acknowledgement We wish to thank the ‘‘863’’ Hi-Tech Research and Development Program of China (Grant No. 2001AA214081) and the National Natural Science Foundation of China (Grant No. 20425620) for financial support. References Fig. 6. Effect of cycles on amplification. Lane M, DL2000 DNA marker; lanes 1–4, PCR with 25, 30, 35 and 40 cycles, respectively. In addition to the conditions discussed above, the annealing temperature also influenced PCR. The annealing temperature must be low enough to ensure efficient annealing and high enough to reduce non-specific combination between primer and template. The reasonable annealing temperature should be between 55 and 70 C in the normal PCR and should be higher in GC-rich template DNA system. In this study, there was no necessity for PCR to be carried out at a higher annealing temperature because no specific bonds were amplified at lower annealing temperature when DMSO was added. In summary: the reaction system and conditions for amplification of this fragment in S. luteogriseus were set up as follows: the PCR solution contained 5 ll 10 buffer, 2 mM MgCl2, 500 lM dNTP, 400 ng DNA template, each primer 1 lM, 2.5 U Taq polymerase and 7.5 ll DMSO, with the volume brought to 50 ll with sterilize water. The reaction was conducted at 95 C for 5 min, 94 C for 30 s, 55 C for 30 s, 72 C for 1 min (35 cycles) and 72 C for 10 min. This protocol is unique in terms of the higher Baskaran N, Kandpal RP, Bhargava AK, Glynn MW, Bale A, Weissman SM (1996) Uniform amplification of a mixture of deoxyribonucleic acids with varying GC content. Genome Res. 6: 633–638. Carmody M, Byrne B, Murphy B, Breen C, Lynch S, Flood E, Finnan S, Caffrey P (2004) Analysis and manipulation of amphotericin biosynthetic genes by means of modified phage KC515 transduction techniques. Gene 343: 107–155. Chakrabarti R, Schutt CE (2001) The enhancement of PCR amplification by low molecular-weight sulfones. Gene 274: 293–298. Chenchik A, Diachenko L, Moqadam F, Tarabykin V, Lukyanov S, Siebert PD (1996) Full-length cDNA cloning and determination of mRNA 5¢ and 3¢ ends by amplification of adaptor-ligated cDNA. Biotechniques 21: 526–534. Hengen PN (1997) Optimizing multiplex and LA-PCR with betaine. Trends Biochem. Sci. 22: 225–226. Hopwood DA, Bibb MJ, Chater KF, Kieser T, Bruton CJ, Kieser HM, Lydiate DJ, Smith CP, Ward JM, Shrempf H (1985) Genetic Manipulation of Streptomyces: A Laboratory Manual. Norwich: John Innes Foundation. Izumikawa M, Murata M, Tachibana K, Ebizuka Y, Fujii I (2003) Cloning of modular type I polyketide synthase genes from salinomycin producing strain of Streptomyces albus. Bioorg. Med. Chem. 11: 3401–3405. Pomp D, Medrano JF (1991) Organic solvents as facilitators of polymerase chain- reaction. Biotechniques 10: 58–59. Rodrigue E, Hu Z, Ou S, Volchegursky Y, Hutchinson CR, McDaniel R (2003) Rapid engineering of polyketide overproduction by gene transfer to industrially optimized strains. J. Ind. Microbiol. Biotechnol. 30: 480–488. Sarkar G, Kapelner S, Sommer SS (1990) Formamide can dramatically improve the specificity of PCR. Nucleic Acids Res. 18: 7465. Wang ZP, (2004) Study on isolation, identification, bioactivity and biosynthesis of Maituolaimycin inhibiting HIV PR and CVB6. PhD Thesis. Tianjin, China: Tianjin University. Weber T, Welzel K, Pelzer S, Vente A, Wohlleben W (2003) Exploiting the genetic potential of polyketide producing streptomycetes. J. Biotechnol. 106: 221–232. Springer 2005 Biotechnology Letters (2005) 27: 1283–1290 DOI 10.1007/s10529-005-0220-8 Molecular cloning and tissue distribution of SF-1-related orphan receptors during sexual maturation in female goldfish Cheol Young Choi1,* & Hamid R. Habibi2 1 Division of Marine Environment & Bioscience, Korea Maritime University, 606-791, Busan, Korea Department of Biological Sciences, University of Calgary, T2N 1N4, Calgary, Alberta, Canada *Author for correspondence (Fax: +82-51-404-3988; E-mail: [email protected]) 2 Received 18 April 2005; Revisions requested 2 May 2005; Revisions received 15 June 2005; Accepted 16 June 2005 Key words: cDNA cloning, goldfish, RT-PCR, SF-1, tissue distribution Abstract The steroidogenic factor (SF)-1 gene is one of a number of orphan nuclear receptors, which is a key transcriptional regulator in vertebrate reproduction. We have isolated the SF-1 homologue cDNA from the goldfish pituitary and designed primers for SF-1 on the basis of the highly conserved regions of various known SF-1 superfamily genes. SF-1 cDNA contained 1,948 nucleotides including an open reading frame predicted to encode a protein of 503 amino acids. The distribution pattern of SF-1 in a variety of tissues during sexual maturation in female goldfish was also examined by RT-PCR. Significant variations in the relative expression of SF-1 were observed in different tissues in immature and mature female goldfish. SF-1 transcript in pituitary was significantly higher than other tissues tested in immature and mature female goldfish. Lower expression of SF-1 was observed in the liver but was not detected in brain and ovary of the immature female goldfish. Presence of SF-1 was the predominant expression in the pituitary and brain of mature female goldfish. Also, in the mature female goldfish, a weak transcript was detected in liver and ovary. Interestingly, RT-PCR analysis revealed that the expression of SF-1 became higher in the brain and weaker in the liver in maturing female goldfish. Thus, SF-1 may be regulated in goldfish brain and/or liver. Thus is also tissue-specific distribution of SF-1 during sexual maturation in female goldfish. Introduction Many transcriptional factors in the orphan nuclear receptor superfamily have recently been cloned. Fushi tarazu transcription factor-1 (FTZF1), a member of an orphan nuclear receptor is important transcriptional regulator of the fushi tarazu home box gene in Drosophila (Yu et al. 1997). After the isolation of Drosophila FTZ-F1 cDNA, many FTZ-1 homologues such as bovine (Honda et al. 1993), rat (Galarneau et al. 1996), chicken (Kudo & Sutou 1997), frog (Kawano et al. 1998) and human (Galarneau et al. 1998) were reported. Recent sequence alignments also support the existence of the orphan nuclear receptors in teleost fish (Liu et al. 1997, Watanabe et al. 1999, Chai & Chan 2000). Vertebrate FTZF1 homologues were mainly classified into two subgroups by phylogenetic tree analysis (Nakajima et al. 2000) and/or based on function, tissue distribution (Galarneau et al. 1996, Hofsten et al. 2001). One is a subgroup of SF-1/Ad4BP (Steroidogenic factor-1/adrenal 4-binding protein), and the other is that of LRH/FTF (Liver receptor homologue protein/a1-fetoprotein transcription factor). The SF-1 is expressed in the adrenal cortex and gonads (Honda et al. 1993) in which steroid hormones are synthesized. SF-1 is essential for development of the steroidogenic organs, a role that has been extended to all levels of the hypothalamic-pituitary-gonadal axis (Ingraham et al. 1284 1994, Manglesdorf et al. 1995). Moreover, the expression is maintained in male embryos during testis differentiation, but declines in female embryos just after the onset of ovarian differentiation, although it increases in females in late embryogenesis (Ikeda et al. 1994). In chicken, SF1 expression during ovarian differentiation increases, which is opposite to the pattern seen in mammals, where it decreases in females (Smith et al. 1999). Mammalian LRH receptors regulate a1-fetoprotein expression and are located in endodermal cells in pancreas and liver (Galarneau et al. 1996). Nuclear receptors are composed of several homologous modular domains. The members of this superfamily have a number of common features and their proteins can be divided into distinct domains: an amino-terminal activation domain, a central to the function of these proteins is the highly conserved DNA-binding domain (DBD). The second most conserved region is referred to as the ligand-binding domain (LBD) which mediates ligand-induced transactivation and participates in receptor dimerization (Mangelsdorf et al. 1995). Moreover, the region I functions as the DBD contains the two zinc finger motifs and has the activity of binding to hormone response elements, and the regions II and III as the LBD/dimerization domain (Honda et al. 1993). RT-PCR analysis of various zebrafish tissues indicated preferential expression of the SF-1 mRNA in liver, followed by brain, testis and lower expression in ovary (Liu et al. 1997). Studies by Hofsten et al. (2001) demonstrated the presence of the Medaka SF-1 and its predominant expression in the ovary. However, no information is available on the sequence and RT-PCR analysis of various tissues indicated preferential expression of SF-1 homologues mRNA in goldfish. The objectives of this study were to characterize the SF-1 homologues cDNA and investigate its tissue distribution in goldfish as a step to towards understanding the molecular mechanisms of SF-1 homologues action. The results also provide for the first time a comparison of the tissue distribution of SF-1 homologues mRNA during sexual maturation in female goldfish. Materials and methods Animals Goldfish (Carassius auratus) ranged from 10 to 13 cm in length were purchased from Aquatic Imports (Calgary, Alberta, Canada), and kept at 17–18 C in a semi-recirculating tank. The light regime was 16 h light, 8 h dark photoperiod. Goldfish were anesthetized with 3-aminobenzoic acid ethyl ester (Sigma) and killed in accordance with the principles and guidelines of the Canadian Council of Animal Care. The gonads were removed and weighted for calculated of the gonadosomatic index (GSI = gonad weight/body weight 100). Tissue samples from female goldfish at sexually immature (GSI: 4.5–6.0) and mature stages (GSI: 18.5–22.0) which were removed, and stored at )80 C until used. Isolation of the SF-1 homologues cDNA Two highly conserved regions of the chicken (Gallus gallus) FTZ-F1 (Kudo & Sutou 1997), frog (Rana rugosa) SF-1 (Kawano et al. 1998) and medaka (Oryzias latipes) FTZ-F1 (Watanabe et al. 1999) were design mixed primers for the polymerase chain reaction (PCR). One of the regions is located at the DBD domain [primer 1: 5¢-ACAAGTTTGG(G/C)CCC ATGTAC-3¢], and the other at the LBL domain [primer 2: 5¢-AGGTGCTTGTGGTA(C/G)AGGTA-3¢] (Figure 1). Total RNA was extracted from each tissue using an RNAgents Total RNA Isolation System (Promega, Madison, WI), according to manufacturer’s instructions. One lg of total RNA was used for cDNA synthesis as described by Choi and Habibi (2003). Amplification was performed as previously described (Choi & Habibi 2003) using Taq DNA polymerase (Promega) and PCR for 38 cycles of 45 s at 94 C, 45 s at 54 C, and 1 min at 72 C, except that the first denaturation was carried out for 3 min and the last elongation reaction for 5 min. After electrophoresis on 1% TAE-agarose gels, the DNA fragment was excised and ligated into the pGEM-T Easy Vector (Promega) according to the manufacture’s instructions, and sequenced. 1285 Fig. 1. Cloning and sequencing strategy for the goldfish (Carassius auratus) orphan nuclear receptor steroidogenic factor (SF)-1 cDNA using the 5¢/3¢ RACE and RT-PCR. The open bar indicates the open reading frame (ORF). Arrows indicate the relative location and direction of primers. Rapid amplication of cDNA 3¢ ends (3¢ RACE) The 3¢ RACE technique was used to obtain sequences downstream of the PCR product using 3¢ RACE System (Version 2.0 kit, Gibco/BRL). First-strand cDNA synthesis was initiated at the poly (A)+ RNA using the oligo (dT) anchor primer [5¢-TGGAAGAATTCGCGGCCGCAGGA AT18-3¢]. The 3¢ RACE-PCR product was amplified by PCR using gene specific primers [primer 3: 5¢-TTACGTGGAGAGCGTGTACG-3¢] and [3¢ RACE adaptor primer: 5¢-TGGAAGAATTC GCGGCCGCAG-3¢] (Figure 1) under the following conditions; 0.2 lg cDNA as template, 10 lM primer 3 and 3¢ RACE adaptor primer, 10 mM of each dNTP, and Taq DNA polymerase (5 U/ll, Promega) in 50 ll buffer. Nested PCR was performed using 35 cycles of 94 C for 45 s for denaturing, 57 C for 45 s for primer annealing, and 72 C for 1 min for extension, followed by final 1 cycle of 5 min at 72 C for extension. The final PCR product was amplified and T-A cloned into pGEM-T Easy Vector, and sequenced. Rapid amplication of cDNA 5¢ end (5¢ RACE) The 5¢ RACE System (Version 2.0 kit, Gibco/ BRL) was employed to obtain transcript sequences upstream of the PCR product. Five micrograms of total RNA was reverse transcribed according to the kit protocol using a gene specific primer [primer 4; 5¢-GTCGACGTATGTGTA-3¢] located within the coding sequence (Figure 1). For the 5¢ RACE-PCR, two gene specific primers, [primer 5; 5¢-CTGGTGTAGTGCTCTCAGCTT-3¢] and [primer 6; 5¢-ACGCCGGGTACTGTG CTGGCA-3¢], were designed (Figure 1). The 5¢ RACE-PCR was carried out using primer 5 and the oligo(dG) anchor primer [5¢-GGCCACG CGTCGACTAGTACGGGIIGGGIIGGGIIG-3¢] included in the kit. Second amplication was conducted using primer 6 and 5¢ RACE adaptor primer [5¢-GGCCACGCGTCGACTAGTAC-3¢] under the same conditions as 3¢ RACE nested amplication (Figure 1). Additional controls that amplify dC-tailed cDNA using each primer individually (either primer 6 or 5¢ RACE adaptor primer) were used to identify nonspecific products. The final nested PCR product was amplified and cloned, and the DNA sequence was analyzed using the GENETYX-WIN (Software Develop. Co., Japan) software package. Reverse transcriptase-polymerase chain reaction (RT-PCR) For the RT-PCR, two specific primers were used to amplify SF-1 cDNA as follows: [primer 7; 5¢-ACTACAGCTATGGCACGGAC-3¢] and [primer 8; 5¢-AGATGCAGGTTCTCTTGGCA3¢] (Figure 1). First, cDNA was synthesized from 1 lg total RNA from brain, pituitary, ovary and liver of goldfish. RT reactions were done with reverse transcribed with an oligo(dT) primer and M-MLV reverse transcriptase (Gibco/BRL). The reaction mixture was activated at 94 C for 3 min, 38 reaction cycles were conducted as follows: 45 s denaturing at 94 C, 45 s annealing at 54 C, and 1 min extension at 72 C, followed by 1 cycle of 5 min extension at 72 C. Fifteen lg of each PCR products were electrophoresed on 1% TAE-agarose gels, with a 1 kb plus DNA ladder 1286 (Gibco/BRL) used as a reference to estimate the molecular weights of the amplified fragments. High-resolution scanner carried out quantification of PCR amplified fragment and the band densities were estimated using NIH image software (NIH, Bethesda, MD). As a control for loading, in each case the loading was controlled by amplification of goldfish b-actin. The densitometry process from ethidium bromide stained gel was optimized for linearity as described in a previous study (Choi & Habibi 2003). Statistical analysis The results were presented as the mean ± the standard deviations (SD), and were analyzed by a one-way ANOVA followed by the Duncan’s multiple range tests were applied for statistical analysis. The means were considered statistically different if p < 0.01. Results Cloning and characterization of the goldfish SF-1 cDNA We designed a set of nucleotide primers based on the nucleotide sequence, which is highly conserved regions of known various species, as described in Materials and methods. One major PCR fragment (1169 base pair) was amplified from the goldfish pituitary and was separated by electrophoresis. Goldfish SF-1 cDNA generated by the 3¢ and 5¢ RACE procedures were subsequently combined to generate a full-length cDNA sequence. The 1,948 bp cDNA had an open reading frame (ORF) of 1,509 bp that began with the first ATG codon at position 22 bp and ended with a TGA stop codon at position 1,531 bp (accession number AF526537). A putative polyadenylation signal AATAAA (Proudfoot & Brownlee 1976) occurred at position 1,908 bp (accession number AF526537). SF-1 cDNA has a related high homology with the other species as follow: medaka (O. latipes) FTZ-F1 (66.9% identity and 82.3% similarity) (Watanabe et al. 1999), frog (R. rugosa) FTZF1b (63.2% identity and 81.4% similarity) (Nakajima et al. 2000), chicken (G. gallus) FTZ-F1 (62.9% identity and 82.1% similarity) (Kudo & Sutou 1997) and zebrafish (D. rerio) FTZ-F1b (61.6% identity and 78.4% similarity) (Chai & Chan 2000) are shown in Figure 2. The zinc fingers which are in region I (DBD domain); regions II and III are located in the LBD domain. When amino acid sequences of these domains are aligned with those of FTZ-F1 homologues cDNA of other species, regions I and II are appeared to high similarity. Goldfish SF-1 contains a high degree of conservation in the region I (90.9–97.0% identity), region II (92.9–100% identity) and region III (56.5–73.9% identity) when compared to medaka FTZ-F1, zebrafish FTZ-F1, zebrafish FTZ-F1b, chicken FTZ-F1 and frog FTZ-F1b (Figure 2). Apart from the regions I–III, this receptor subclass has a characteristic conserved amino acid sequence, called the FTZ-F1 box (Figure 2). It lies adjacent to the zinc fingers are required for high affinity and sequence-specific binding. The FTZ-F1 box is 30 amino acids and is 100% identical among medaka FTZ-F1, zebrafish FTZ-F1, chicken FTZ-F1 and frog FTZ-F1b, except for zebrafish FTZ-F1b (Figure 2) Tissue distribution of the goldfish SF-1 Using RT-PCR, we investigated the expression of SF-1 mRNA in various tissues in female goldfish at sexually immature and mature stage. The expression of b-actin was monitored in all tissues and used as control to normalize for loading. Lower expression of SF-1 was observed in the liver, but extremely low expression was detected in brain and ovary of the immature female goldfish. SF-1 mRNA was very highly expressed in mature female goldfish pituitary and brain, followed by liver which, was lower expressed in ovary (Figure 3). Homologies of goldfish SF-1 with other species of nuclear hormone receptor subfamily Discussion Homological analyses using the GenBank and the EMBL general database searches indicated that the amino acid sequence of the goldfish Mammalian reproductive function is regulated by the hypothalamic-pituitary-gonadal axis. SF-1 is 1287 Fig. 2. Deduced amino acid comparisons of the goldfish (Carassius auratus) SF-1. Goldfish amino acid sequences are compared with the deduced amino acid sequences of the medaka (Oryzias latipes) FTZ-F1, zebrafish (Danio rerio) FTZ-F1, zebrafish (D. rerio) FTZ-F1b, chicken (Gallus gallus) FTZ-F1 and frog (Rana rugosa) FTZ-F1b. The sequences were taken from the GenBank/ EMBL/DDBJ sequence databases. SF-1 homologues sequences used for alignment are goldfish SF-1 (gfSF-1, AF526537), medaka FTZ-F1 (mFTZF1, AB026834), zebrafish FTZ-F1 (zFTZF1, AF014926), zebrafish FTZ-F1b (zFTZFb, AF198086), chicken FTZF1 (cFTZF1, AB002404) and frog FTZ-F1b (fFTZF1, AB035499). To aid comparisons, functional motifs as described by Wong et al. (1996) are indicated; regions I-III, P box, D box, FTZ-F1 box and the activation function (AF)-2 motif. Gaps in the sequences are indicated as dashes. Dots indicate residues identical to those of gfSF-1. 1288 essential for gonadal development and function, implicates SF-1 as important regulatory role in the reproductive system (Ingraham et al. 1994). This study provides the complete coding sequence of the SF-1 cDNA in the goldfish pituitary. The goldfish SF-1 cDNA was found to contain an open reading frame of 1509 nucleotides encoding a protein of 503 amino acids. SF-1 proteins have three conserved regions. The region I functions as the DBD contains the zinc finger motifs and has the activity of binding to hormone response elements, and the regions II and III as the LBD (Honda et al. 1993). The zinc finger motifs of the steroid hormone receptor superfamily have two functional domains; the socalled P and D boxes. Region I recognizes and binds the specific sequences of target genes, the expression of which is regulated by the nuclear receptor. The P box in the first zinc finger distinguishes between the sequences of hormone response elements. Goldfish SF-1 was found to be a P box, which is positioned at the base of the zinc finger, and is ESCKG in all FTZ-F1 boxcontaining receptors. The D box in the second zinc finger recognizes the spacing of those elements. Furthermore, the two sequences in the putative LBD, called region II and III, have been used to classify nuclear hormone receptor (Wang et al. 1989). Region II is highly conserved and region III is less conserved (Figure 2). Some studies revealed that transcriptionally active FTZ-F1 homolog in vertebrate showed conserved activation function (AF)-2 motif sequence, LLIEML, is located in LBD at amino acid 491–496 (Figure 2), indicating that transcriptional activation is dependent on ligand binding as reported previously (Tora et al. 1989). Galarneau et al. (1996) reported that complete removal of the AF-2 motif from the LBD of rat LRH-1 also caused the loss of its trans-activation function. This result suggests that the transcriptional activities of the members of the FTZ-F1 Fig. 3. One microgram of total RNA prepared from brain (B), pituitary (P), ovary (O), liver (L) and control as a no tissue (N) were reverse transcribed and amplified in immature and mature male goldfish using SF-1 specific primer. Tissue distribution of goldfish SF-1 was analyzed by RT-PCR. The expression of b-actin mRNA was evaluated in each RT reaction product as a loading control. The expression level of each tissue was normalized with respect to the b-actin signal, and expressed as relative expression level. An asterisk indicates a significant difference compared between immature and mature goldfish (p < 0.01). Values are mean ± the standard deviations of these four experiments, each using separate female goldfish. 1289 subfamily are mainly due to their C-terminal regions. SF-1 is apparently able to stimulate the synthesis of not only corticosteroids, such as glucocorticoids, in the adrenal cortex but also the production of estrogens and androgens in the ovary and testis by activating the expression of the enzymes that synthesize precursors to these hormones and by increasing the expression of aromatase (Lynch et al. 1993), which conducts bioconversion of androgens to estrogens. Additionally, it is also able to indirectly control the synthesis of primary steroid sex hormones by acting at the pituitary level to influence the expression of the gonadotropin hormone genes (Barnhart & Mellon 1994). In this study, we also compared the expression pattern of SF-1 in a variety of tissues in female goldfish at immature and mature stage by RT-PCR. Lower expression of SF-1 was observed in the liver, but not detected in brain and ovary of the immature female goldfish. Presence of SF-1 was the predominant expression in the pituitary and brain of mature female goldfish. Also, in the mature female goldfish, weak transcript was detected in brain and ovary. Interestingly, RT-PCR analysis revealed that the expression of goldfish SF-1 became higher in the brain and weaker in the liver during maturing female, respectively (Figure 3). This agrees with a previous report (Kawano et al. 1998) that high expression of mature frog FTZ-F1 mRNA was detected in the brain, but not ovary. Interestingly, mature female goldfish liver SF-1 mRNA levels were decreased significantly compared to immature female goldfish. Taken together, these data indicate a global role for FTZ-F1 at each stages of liver and gonadal function. On the other hand, the FTZ-F1 gene family constitutes a subgroup of orphan nuclear receptors, which can be divided into two groups, LRH/FTF (liver receptor homologue protein/afetoprotein transcription factor) and SF-1, based on function, tissue distribution (Galarneau et al. 1996, Hofsten et al. 2001) and phylogenetic tree analysis (Nakajima et al. 2000). In zebrafish, however, Hofsten et al. (2001) demonstrated that while the expression in liver is indicative of a LRH/FTF function, the expression in other tissues, such as the pituitary, brain and gonad is indicative of SF-1 function. Moreover, amino acid sequences in the regions I and II of goldfish SF-1 showed high similarity to not only LRH but also SF-1, suggesting the importance of each region for the function of these proteins. In these observations, coupled with obtained expression patterns, indicate that goldfish FTZ-F1 homologues exhibit characteristics that are indicative of both LRH/FTF- and SF-1-like genes, may have other developmental roles in goldfish. SF-1 mRNA was strongly expressed in immature and mature goldfish pituitary. SF-1 regulates the activity of steroidogenic enzyme in bovine adrenal cells and luteal cells (Liu & Simpson 1997). Therefore, SF-1 may also control steroidogenesis in goldfish pituitary. Interestingly, RT-PCR analysis revealed that the expression of goldfish SF-1 was found in the goldfish liver but it became weaker in the liver of mature female goldfish. The findings suggest that SF-1 homologues may plays an important roles in the regulation of liver function since it is particularly less expression in developing female goldfish liver. Moreover, at present, little information is available on the relative importance of SF-1 homologues in the regulation of vitellogenesis and reproduction in goldfish and other teleosts species. The present results are in accord with findings in mammals and other vertebrates concerning tissue specific expression of SF-1 homologues. Information obtained in this study on tissue distribution of SF-1 homologues provides a framework for better understanding of physiological significance of these groups of the orphan nuclear receptor in goldfish. The significance of these findings remains to be investigated as more information on regulation of brain and liver, and seasonal variation of SF-1 homologues because available in goldfish and other vertebrates. Acknowledgement This work was supported by a grant from the Natural Sciences and Engineering Research Council of Canada. 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Ó Springer 2005 Biotechnology Letters (2005) 27: 1291–1294 DOI 10.1007/s10529-005-0221-7 Enhancement of isoflavone synthase activity by co-expression of P450 reductase from rice Dae Hwan Kim1, Bong Gyu Kim1, Hyo Jung Lee1, Yoongho Lim1, Hor Gil Hur2 & Joong-Hoon Ahn1,* 1 Bio/Molecular Informatics Center, Department of Molecular Biotechnology, Konkuk University, 143-701, Seoul, Korea 2 Department of Environmental Science and Engineering and International Environmental Research Center, Kwangju Institute of Science and Technology, Gwangju, Korea *Author for correspondence (Fax: +82-2-3437-6106; E-mail: [email protected]) Received after revisions 20 June 2005; Accepted 20 June 2005 Key words: cytochrome P450, cytochrome P450 reductase, Saccharomyces cerevisiae, secondary metabolism Abstract Plant cytochrome P450s interact with a flavoprotein, NADPH-cytochrome P450 reductase (CPR), to transfer electrons from NADPH. The gene for rice P450 reductase (RCPR) was cloned and expressed in Saccaromyces cerevisiae, where the specific activity of the expressed RPCR was 0.91 U/mg protein. When isoflavone synthase gene (IFS) from red clover, used as a model system of plant cytochrome P450, was co-expressed with RCPR in yeast, the production of genistein from naringein increased about 4.3-fold, indicating that the RCPR efficiently interacts with cytochrome P450 to transfer electrons from NADPH. Introduction Cytochrome P450 monooxygenases (P450s) play a critical role in many biosynthetic pathways, including the detoxification of exogenous compounds. For example, in animals, P450s are involved in drug, steroid and fatty acid metabolism. In plants, their activity mediates the synthesis of lignins, UV protectants, pigments, defense compounds, fatty acids, hormones, and signaling molecules, as well as the catabolism of herbicides, insecticides, and pollutants (Schuler & WerckReichhart 2003). The biological functions of P450s rely on an electron donor, NADPH-cytrochrome P450 reductase (CPR). CPR transfers two electrons from NADPH to P450s (Porter et al. 1987). From the genome sequences, Arabidopsis has 273 P450s and rice more than 300, though the function of most of these is unknown. The development of an in vitro assay would be a critical step an in analyzing the function of individual P450s. Our group has been interested in the functional characterization of P450s from rice and we have now developed an in vitro assay system in which CPR from rice was cloned and expressed in Saccharomyces cerevisiae. Then, isoflavone synthase, a plant P450, was expressed together with CPR in the yeast to enhance the P450 activity. Materials and methods Cloning of rice CPR gene and CPR assay A reverse-transcriptase polymerase chain reaction (RT-PCR) was carried out to clone the CPR gene from rice with primers of the following sequences: CAACCAAACCCTCGCTTC as forward primer and GCTAGAGCGAGCTATTTC 1292 TGAAS as reverse primer. The resulting PCR product was subcloned into pGMET vector (Promega, Madison, WI, USA) and sequenced. For the in vitro rice CPR enzyme assay, a cytochrome c reductase [NADPH] assay kit (Sigma) was used. The rate of reduction was calculated by differential absorption at 550 nm (Ro et al. 2002). One unit of activity was defined as the amount of CPR produced for the reduction of 1 lmol cytochrome c per min. Functional expression of rice CPR in Saccharomyces cerevisiae To subclone the rice CPR gene into the pESCHis vector (Stratagene, La Jolla, CA, USA), two new primers were synthesized: a forward primer, containing the initiation codon ATGGCGC TGGCGCTGGA, a reverse primer, contained a restriction enzyme site SpeI (ACTAGT), and a stop codon ATACTAGTTCACCATACGTCAC GGAGCCTGC. PCR was carried out with Pfu Taq polymerase (Stratagene, La Jolla, CA, USA) and the resulting PCR product was digested with SpeI. The pESC-His vector was cut with EcoRI, blunted with Klenow enzyme, digested with SpeI, and then used for the ligation. Expression of RCPR was followed according to manufacture’s instructions. Microsomes from the transformant were isolated by the method of Stansfield & Kelly (1996). Microsomal protein (1 mg), containing either isoflavone synthase (IFS) or IFS plus RCPR mixed with 1 mM NADPH and 100 lM naringenin, was incubated at 30 °C for 2 h. The reaction mixture was extracted twice with ethyl acetate; the solvent was then evaporated in vacuo and the residue was dissolved in methanol. Analysis of flavonoid was by HPLC as described in Kim et al. (2002). Concentrations of naringenin and geninstein were determined from a standard curve calculated with various known concentrations of both compounds against the peak area detected on HPLC. For both compounds, the standard HPLC detection curve was linear up to 1 lmol. Results and discussion The rice genome database was searched with Arabidopsis CPR gene (GenBank accession number X66016) to find rice CPR. Several rice genes, which showed homology with Arabidopsis CPR, were found and some of them were annotated as cytochrome P450 reductase. Among them, one gene (XP_474161, RCPR) showing the highest homology was cloned by RT-PCR. The RCPR consists of a 2088-bp open reading frame. The predicted protein has domains that are commonly found in other CPR; FMN, FAD, and NADPH binding domains. It showed 82% identity with NADPH-cytochrome P450 reductase (AAG17471) from Triticum aestivum and 72% with that from Populus balsamifera subsp. trichocarpa Populus deltoids (AAK15259). To express the RCPR in yeast, it was cloned into the pESC-His vector under the control of a galactose-inducible promoter and the resulting construct was transformed into S. cerevisiae INVSc1 (his-, leu-, trp-, ura-). Transformants that grew in the absence of histidine were selected. As a control, the pESEC-His vector was transformed into the same yeast strain. From four independent yeast transformants, containing either RCPR or the expression vector, microsomes were isolated and CPR activity measured by reduction of cytochrome c. Specific activity of the crude RCPR from the four dependent transformants ranged from 1.12 to 1.32 lmol min)1 mg)1 with an average of 1.21 lmol min)1 mg)1, while yeast, containing the vector only, showed a specific activity of 0.28–0.35 lmol min)1 mg)1, with an average of 0.31. Thus, specific activity of the expressed RCPR was 0.9 lmol min)1 mg)1. The reduction of cytochrome c by recombinant rice CPR protein was dependent on NADPH, but not on NADH, as shown in other CPRs (Koopmann & Hahlbrock 1997, Mizutani & Ohta 1998). Therefore, based on the in vitro enzyme assays, we can conclude that the RCPR cDNA encodes functional rice CPR enzyme. As endogenous CPR activity is a limiting factor in yeast when foreign P450s are overexpressed (Urban et al. 1994), we determined whether the expressed rice CPR activity enhanced cytochrome P450 activity in yeast. IFS from red clover was used as a model system of plant cytochrome P450. In a previous study (Kim et al. 2003), it was shown that IFS expressed in yeast could convert naringenin into genistein. The yeast strain containing RCPR was retransformed with an IFS construct (Figure 1). pG AL 1 IFS (P450) pYES2 URA 3 pG AL 10 1293 RCPR pESC-HIS HIS 3 S.cerevisiae (His3-, Leu2-, Trp1-, Ura3-) Fig. 1. Co-expression strategy of isoflavone synthase (IFS) and rice cytochrome P450 reductase (RCPR) in Saccharomyces cerevisiae. IFS converts naringenin into genistein. RCPR transfers two electrons from NADPH to IFS. RCPR, with his3 gene as a selection marker, was transformed into S. cerevisiae and then IFS, a plant P450, with ura3 gene as a selection marker, was transformed again into the yeast strain that was originally transformed with RCPR. The resulting transformants were selected on uracil- and histidine-deleted media, since the IFS construct contains the ura3 gene as a selection marker. Several transformants were analyzed for the presence of the constructs, RCPR and IFS. As a control, a yeast transformant, containing only IFS, was generated. Microsomes from three independent transformants, with either IFS or IFS and RCPR, were isolated, respectively and IFS activity was measured. The reaction product was analyzed with HPLC to determined whether a reaction had occurred. Naringenin was eluted at 12.5 min and genistein at 15.5 min (Figure 2 a, b). Reaction products with IFS showed a smaller genistein peak than those with IFS plus RCPR (Figure 2 c, d). To measure the amount of genistein generated by IFS, several concentrations of narigenin and genistein were analyzed by HPLC and the HPLC absorbance was used as the standard for calculating the concentration of the reaction product. HPLC absorbance vs. concentration of each flavonoids showed a linear relationship from 0 to 200 lM. IFS itself produced an average 18 lM genistein from 100 lM naringenin, while IFS co-expressed with RCPR produced 77 lM, equal to about 4.3-fold increase in IFS activity. This indicates that RCPR enhanced the IFS activity in yeast cells. Even though IFS was cloned from red clover, RCPR could effectively transfer electrons to IFS. Therefore, the current CYP expression system could be applicable for the functional studies of CYPs, not only from rice but also from other plants. (a) mAU 120 OH 100 80 HO 60 40 20 O OH O Naringenin 0 0 mAU 120 100 80 60 5 10 15 20 (b) HO O OH 40 20 O OH Genistein 0 0 mAU 120 5 10 15 20 5 10 15 20 5 10 Time(min) 15 20 (c) 100 80 60 40 20 0 0 mAU 120 (d) 100 80 60 40 20 0 0 Fig. 2. HPLC elution profile of reaction product by red clover isoflavone synthase co-expressed with rice P450 reductase. Microsomes from either vector pES-His (a, b), isoflavone synthase gene (c), or isoflavone synthase co-expressed with rice P450 reductase (d) were incubated with 1 mM NADPH and 100 lM naringenin (genistein was used instead of naringenin in b). The reaction products were analyzed by HPLC. 1294 Acknowledgements This work was supported by a grant from the Biogreen 21 Program, Rural Development Administration, Republic of Korea and partially by KRF2004-F00019 (KRF). References Kim BG, Kim SY, Song HS, Lee C, Hur HG, Kim SI, Ahn J-H (2003) Cloning and expression of the isoflavone synthase gene (IFS-Tp) from Trifolium pretense. Mol. Cells 15: 301–306. Koopmann E, Hahlbrock K (1997) Differentially regulated NADPH:cytochrome P450 oxidoreductases in parsley. Proc. Natl. Acad. Sci. U S A. 94: 14954–14559. Mizutani M, Ohta D (1998) Two isoforms of NADPH:Cytochrome P450 reductase in Arabidopsis thaliana. Plant Physiol. 116: 357–367. Porter TD, Wilson TE, Kasper CB (1987) Expression of a functional 78,000 dalton mammalian flavoprotein, NADPH–cytochrome P-450 oxidoreductase, in Escherichia coli. Arch. Biochem. Biophys. 254: 353–367. Ro D-K, Ehlting J, Douglas CJ (2002) Cloning, functional expression, and subcellular localization of multiple NADPH-cytochrome P450 reductase from hybrid poplar. Plant Physiol. 130: 1837–1851. Schuler MA, Werck-Reichhart D (2003) Functional genomics of P450s. Annu. Rev. Plant. Biol. 54: 629–667. Stansfield I, Kelly SL (1996) Purification and quantification of Saccharomyces cerevisiae cytochrome P450. In: Evans IV, ed. Yeast Protocols: Methods in Cell and Molecular Biology, New Jersey: Humana Press, pp. 355–366. Urban P, Werck-Reichhart D, Teutsch HG, Durst F, Regnier S, Kazmaier M, Pompon D (1994) Characterization of recombinant plant cinnamate 4-hydroxylase produced in yeast. Kinetic and spectral properties of the major plant P450 of the phenylpropanoid pathway. Eur. J. Biochem. 222: 843–850. Urban P, Mignotte C, Kazmaier M, Delorme F, Pompon D (1997) Cloning, yeast expression, and characterization of the coupling of two distantly related Arabidopsis thaliana NADPH-cytochrome P450 reductase with P450 CYP73A5. J. Biol. Chem. 272: 19176–19186. Springer 2005 Biotechnology Letters (2005) 27: 1295–1299 DOI 10.1007/s10529-005-0222-6 Structural characterization of b-glucans of Agaricus brasiliensis in different stages of fruiting body maturity and their use in nutraceutical products Carla Maı́sa Camelini1, Marcelo Maraschin2, Margarida Matos de Mendonça1,*, Cezar Zucco3, Antonio Gilberto Ferreira4 & Leila Aley Tavares4 1 Departamento de Microbiologia e Parasitologia, Centro de Cieˆncias Biológicas, 88040-900, Santa Catarina, Florianópolis, Brasil 2 Departamento de Fitotecnia, Centro de Cieˆncias Agrárias, 88040-900, Santa Catarina, Florianópolis, Brasil 3 Departamento de Quı´mica, Universidade Federal de Santa Catarina, 88040-900, Santa Catarina, Florianópolis, Brasil 4 Departamento de Quı´mica, Universidade Federal de São Carlos, 13565-905, São Paulo, São Carlos, Brasil *Author for correspondence (Fax: +55-48-331-9258; E-mail: [email protected]) Received 17 February 2005; Revisions requested 22 February 2005; Revisions received 20 June 2005; Accepted 21 June 2005 Key words: Agaricus blazei, Agaricus brasiliensis, b-glucan, nutraceutical, polysaccharide Abstract b-Glucans of Agaricus brasiliensis fruiting bodies in different stages of maturity were isolated and characterized by FTIR and NMR. These fractions had greater amount of (1 fi 6)-b-glucan and the (1 fi 3)-bglucan increased with fruiting bodies maturation. Yields of b-glucans increased from 42 mg b-glucans g)1 fruiting bodies (dry wt) in immature stage to 43 mg g)1 in mature stage with immature spores, and decreased to 40 mg g)1 in mature stage with spore maturation. Mature fruiting bodies, which included these glucans, have potential therapeutical benefits for use in nutraceutical products. Introduction Agaricus brasiliensis Wasser & Didukh (Wasser et al. 2002) (=Agaricus blazei ss. Heinem.), known in Brazil as Cogumelo medicinel, has been widely cultivated in the country because of its medicinal properties such as immunomodulatory and antitumor activities (Kawagishi et al. 1989, Mizuno et al. 1990, Ohno et al. 2001, Dong et al. 2002). The mushroom is commercialized in several countries as a nutraceutical product which is a novel class of dietary supplements including partially refined extract or dried biomass from the mushroom made into a capsule or tablet (Chang & Buswell 1996). Agaricus brasiliensis is harvested in Brazil mostly in the immature stage when the cap is still closed to meet exportation standards. Although immature fruiting bodies have not yet achieved their highest biomass, it is at this stage that they reach the highest market value for exportation. Farmers usually discard the mature fruiting bodies. The quality of a nutraceutical is dependent on the chemical composition of the fruiting body, particularly in relation to the content of b-glucans. However, no studies have been developed to characterize the b-glucans at different stages of fruiting body maturity and on potential use on the preparation of nutraceutical. Kawagishi et al. (1989) characterized the b-glucans with antitumoral properties of A. blazei and detected an alkali soluble (1 fi 6)-b-D-glucan with no (1 fi 3)-b-linkages. Mizuno et al. (1990), using a water extraction method, identified (1 fi 6)–(1 fi 3)-b-D-glucans in the same species. Recently, Ohno et al. (2001) working on an alkali-soluble fraction detected (1 fi 6)-b-D-glucans and a small but significant amount of (1 fi 3)-b-D-glucans in A. blazei. 1296 None of these authors indicated the stage of development of the fruiting bodies selected in their studies. In this study, we examined the structural evolution of water-soluble polysaccharides such as b-glucans of A. brasiliensis in three different stages of fruiting body maturity. Materials and methods Fruiting body selection Commercially cultivated fruiting bodies of Agaricus brasiliensis (strain UFSC-51) were obtained in Biguaçú, Santa Catarina, Southern Brazil, in 2003. The fruiting bodies were harvested and dried in different stages of maturity: immature (cap closed) and mature (cap opened). The mature stage was further characterized into immature spores and mature spores as seen on Figure 1. Extraction of the polysaccharide fraction Cell wall polysaccharides were extracted and purified according to Mizuno et al. (1990). Samples of dried fruiting bodies of A. brasiliensis (20 g) were grounded, washed with 120 ml 85% (v/v) ethanol and filtered. The residue was washed with 350 ml 85% (v/v) ethanol holding at 80 C for 3 h (3 times). The polysaccharides were sequentially extracted with 350 ml water holdings at 100 C for 3 h (3 times). These aqueous fractions were collected by filtration, followed by the addition of 4 vol. 95% (v/v) ethanol. The mixture was then held overnight to obtain the polysaccharide fraction, which was concentrated and dialyzed against distilled water. This fraction was then freeze-dried, weighed and analyzed. Fig. 1. Agaricus brasiliensis fruiting bodies in different stages of maturity: (SI) immature (cap closed), (SII) mature (cap opened) with immature spores, and (SIII) mature with mature spores. Polysaccharide purification Each sample (1 g) was dissolved in distilled water and passed through a DEAE-cellulose column chromatography (2 cm width 35 cm length). The neutral fraction eluted with water (105 ml) was discarded and selected fractions of 0.25, 0.5 and 0.75 M NaCl (105 ml each) were concentrated and then dialyzed extensively. The polysaccharide was fractionated according to the highest molecular weight on a Toyopear HW-65F (Tosoh) column (2 cm width 35 cm length) selecting the first 35 ml eluted. The b-glucans (unadsorbed) was separated using Con A-Sepharose 4B (Fluka Biochemika) column (1.5 cm width 10 cm length), freeze-dried, weighted and analyzed. Polysaccharide analyses The polysaccharide fractions (before and after purification of b-glucans) of A. brasiliensis from each stage of maturity were analyzed. Protein content was determined using the Bradford method with BSA as reference. The FTIR spectra were determined with an ABD Bomem Inc. FTLA 2000 spectrometer and KBr discs. 1H and 13 C NMR spectra of 30 mg and 120 mg polysaccharides fractions, respectively in D2O (600 ll) were recorded at 298 K using a Bruker DRX400 spectrometer operating at 9.4 Tesla and TSPA-d4 like external reference. Results and discussion Polysaccharide analyses The FTIR spectra (Figure 2) suggested the presence of a small amount of protein (band at 1540 cm)l) which was confirmed by the Bradford method (Table 1) and the absence of uronic acids (no carbonyl bands over 1700 cm)l). The characteristic bands of b-glucans occurred in the 1000– 1100 cm)1 region due to O-substituted glucose residues. The band at 1400 cm)l evidenced the presence of a b-glucan. These spectra showed a weak band at 890 cm)l revealing a b configuration on the main glucan. The weak band at 910 cm)l and 850 cm)l indicated the presence of a a-glucan (Gutiérrez et al. 1996). 1297 Fig. 2. FTIR spectra of polysaccharide fractions obtained from Agaricus brasiliensis fruiting bodies in different stages of maturity. (SI-a) aqueous fraction from immature stage isolated at 100 C (before purification of b-glucans) and (SI-b) same fraction after purification of b-glucans; (SII-a) aqueous fraction from mature stage with immature spores isolated at 100 C and (SII-b) same fraction after purification of b-glucans; (SIII-a) aqueous fraction from mature stage with mature spores isolated at 100 C and (SIII-b) same fraction after purification of b-glucans. 13 C NMR spectra from polysaccharide fractions (before and after purification of b-glucans) from A. brasiliensis, in each stage of maturity, are shown in Figure 3. Assignment of each spectrum was made by comparison with previously published spectra (Dong et al. 2002, Mizuno et al. 1990, Ohno et al. 1985, 2001, Saito et al. 1976, York 1995). Agaricus brasiliensis fruiting bodies in different stages of maturity contained b-glucans and also a-glucans. All spectra showed six major signals on the spectra assigned to (1 fi 6)-b-glucosidic linkages (Figure 3). The anomeric C-1 signal around 105.1 ppm with closely located signals at 104.7 ppm and 104.4 ppm were attributed as b configurations. The substituted C-6 signal could be identified at 71.0 ppm from the reverse peak in the DEPT spectrum and non-substituted C-6 signal at 62.9 ppm, suggesting a higher amount of (1 fi 6)-b-glucan than (1 fi 3)-b-glucan. Fractions from all stages before purification of b-glucans showed the signal at 86.5 ppm, attributed to substituted C-3, which was weaker than the non-substituted C-3 signal at 77.8 ppm (Figure 3). This suggested that most C-3 was not substituted, and a small amount of (1 fi 3)-bglucan was present. The signal at 86.5 ppm was not detected in the fraction after purification of b-glucans from immature fruiting bodies (SI-b), suggesting a smaller amount of the (1 fi 3)-bglucans than other fractions. All spectra showed signals at 83.0 ppm, suggesting a (1 fi 2)-b-glucosidic linkage. The signals at 102.0 ppm and 100.2 ppm indicated a-configurations as well as (1 fi 4)-a- and (1 fi 6)-a-linkages at 79.0 ppm and 68.0 ppm, respectively. Fruiting bodies in mature stages showed an increased signal on C-1 (102 ppm) of a (1 fi 4)-a-glucosidic linkage, suggesting an increased amount of this type of glucan with spore matured. The 1H NMR spectra of both fractions showed the anomeric signals around 4.6 and 3.2 ppm and confirmed the b-glucans. Table 1 shows characteristics of glucans in fruiting bodies in different stages of Table 1. Structural characterization, the yield of water soluble glucans at 100 C from A. brasiliensis fruiting bodies in different stages of maturity and the amount of protein detected in the fractions before and after purification of b-glucans. Stages of maturitya SISIISIIIa a b a b a b Glucans Protein (mg g)1 dry wt) (1 fi 6)-b- (1 fi 2)-b- (1 fi 3)-b- (1 fi 4)-a- (1 fi 6)-a- Yield (mg g)1 dry wt) +++b +++ +++ +++ +++ +++ +d + + + + + + )e ++c ++ ++ ++ ) ) ++ ) +++ ) + ) + ) + ) 102 42 106 43 111 40 6.0 5.8 7.2 6.0 9.9 6.7 Maturity stages of fruiting bodies from which glucans were isolated: (SI-a) aqueous fraction from immature stage isolated at 100 C (before purification of b-glucans) and (SI-b) same fraction after purication of b-glucans; (SII-a) aqueous fraction from mature stage with immature spores isolated at 100 C and (SII-b) same fraction after purification of b-glucans; (SIII-a) aqueous fraction from mature stage with mature spores isolated at 100 C and (SIII-b) same fraction after purification of b-glucans. b +++ Highest amount, c++ intermediate amount, d+ smallest amount, e- no/low level of glucans detected in the fractions. 1298 branches on the (1 fi 3)-b-backbone during maturation of fruiting bodies of A. bisporus. It is important to emphasize that linear (1 fi 6)-b-glucan extracted from Penicillium islandicum did not present bioactivity (Ohno et al. 1986). However, (1 fi 3)-b-side branches are structurally important and enhance the immunomodulatory activity at polysaccharides (Dong et al. 2002). As Mizuno et al. (1990) evidenced, important anti-tumor activity is linked to a water-soluble (1 fi 6)– (1 fi 3)-b-D-glucan. As a consequence, mature fruiting bodies of A. brasiliensis should be used for nutraceutical products because they contain these important glucans. Furthermore, a significant increase on another water soluble (1 fi 4)-aglucan with anti-tumor activity also occurred during maturation from SII to SIII (Mizuno et al. 1990). Cap-opened, more fragile mature fruiting bodies of A. brasiliensis should be selected over immature ones for the production of nutraceuticals. Additionally, this strategy will provide the consumer with a higher diversity of glucans, optimizing bioactivities such as the antitumoral one, additionally allowing farmers an efficient and profitable use of the mushroom biomass. Fig. 3. 13C NMR spectra of polysaccharide fractions obtained from Agaricus brasiliensis fruiting bodies, in different stages of maturity, in D2O at 298 K and a number of scans between 30,000 and 35,000. (SI-a) aqueous fraction from immature stage isolated at 100 C (before purification of b-glucans) and (SI-b) same fraction after purification of b-glucans; (SII-a) aqueous fraction from mature stage with immature spores isolated at 100 C and (SII-b) same fraction after purification of b-glucans; (SIII-a) aqueous fraction from mature stage with mature spores isolated at 100 C and (SIII-b) same fraction after purification of b-glucans. maturity and the yield of each polysaccharide fraction before and after purification of b-glucans. Additionally, the small amount of protein detected is shown. The yield and structural diversity of glucans increased as the fruiting bodies matured. In mature stages the amount of (1 fi 3)-b-glucans (SII-b and SIII-b) was higher than in the immature stage. These glucans are possibly side branches of a (1 fi 6)-b-backbone as indicated by Dong et al. (2002) and Ohno et al. (2001) who described that b-glucans of A. blazei fruiting bodies had a (1 fi 6)-b-backbone structure with (1 fi 3)b-side branches. Mol & Wessels (1990) also showed a greater proportion of (1 fi 6)-b-side Acknowledgements This work was partially supported by a grant from the Conselho Nacional de Desenvolvimento Cientı́fico e Tecnológico (CNPq). The senior author would like to thank CNPq for the Biotechnology fellowship and the Mushroom Farmers of Santa Catarina. We thank Dr. Admir Giachini for editorial comments on this manuscript. References Chang ST, Buswell JA (1996) Mushroom nutriceuticals. World J. Microb. Biotech. 12: 473–476. Dong Q, Yao J, Yang X, Fang J (2002) Structural characterization of water-soluble b-D-glucan from fruiting bodies of Agaricus blazei Murr. Carbohyd. Res. 337: 1417–1421. Gutiérrez A, Prieto A, Martlnez AT (1996) Structural characterization of extracellular polysaccharides produced by fungi from the genus Pleurotus. Carbohyd. Res. 281: 143–154. Kawagishi H, Inagaki R, Kanao T, Mizuno T (1989) Fraction and antitumor activity of the water-insoluble residue of Agaricus blazei fruiting bodies. Carbohydr. Res. 186: 267–273. 1299 Mizuno T, Hagiwara T, Nakamura T, Ito H, Shimura K, Sumiya T, Asakura A (1990) Antitumor activity and some properties of water-soluble polysaccharides from ‘‘Himematsutake’’, the fruiting body of Agaricus blazei Murill. Agric. Biol. Chem. 54: 2889–2896. Mol PC, Wessels JGH (1990) Differences in wall structure between substrate hyphae and hyphae of fruit-body stipes in Agaricus bisporus. Mycol. Res. 94: 472–479. Ohno N, Furukawa M, Miura NN, Adachi Y, Motoi M, Yadomae T (2001) Antitumor b-glucan from the cultured fruit body of A. blazei. Biol. Pharm. Bull. 24: 820–828. Ohno N, Iino K, Takeyama T, Suzuki I, Sato K, Oikawa S, Miyazaki T, Yadomae T (1985) Structural characterization and antitumor activity of the extracts from matted mycelium of cultured Grifola frondosa. Chem. Pharm. Bull. 33: 3395–3401. Ohno N, Hayashi M, Iino K, Suzuki I, Oikawa S, Sato K, Yadomae T (1986) Effect of glucans on the antitumor activity of Grifolan. Chem. Pharm. Bull. 34: 2149–2154. Saito H, Ohki T, Yoshioka Y, Fukuoka F (1976) A 13C nuclear magnetic resonance study of a gel-forming branched (1 fi 3)-b-D-glucan from Pleurotus ostreatus (fr.): determination of side-chains and conformation of the polymer-chain in relation to gel-structure. FEBS Lett. 68: 15–18. Wasser SP, Didukh MY, Amazonas MALA, Nevo E, Stamets P, Eira AF (2002) Is a widely cultivated culinary-medicinal royal sun Agaricus (the Himematsutake mushroom) indeed Agaricus blazei Murrill?. Int. J. Med. Mush. 4: 267–290. York WS (1995) A conformational model for cyclic b-(1 fi 2)linked glucans based on NMR analysis of the glucans produced by Xanthomonas campestris. Carbohyd. Res. 278: 205–225. Springer 2005 Biotechnology Letters (2005) 27: 1301--1304 DOI 10.1007/s10529-005-0223-5 Taxane production in suspension culture of Taxus 3 media var. Hicksii carried out in flasks and bioreactor Katarzyna Syklowska-Baranek* & Miroslawa Furmanowa Department of Biology and Pharmaceutical Botany, Medical University of Warsaw, ul. Banacha 1, 02--097, Warsaw, Poland *Author for correspondence (E-mail: [email protected]) Received: 6 April 2005; Revisions requested 14 April 2005; Revisions received 20 June 2005; Accepted 21 June 2005 Key words: bioreactor, 10-deacetylbaccatin III, paclitaxel, L-phenylalanine, Taxus · media var. Hicksii Abstract Paclitaxel and 10-deacetylbaccatin III (10-DAB III) were produced in suspension cultures of Taxus · media var. Hicksii grown in shake-flasks and in a 7-l bioreactor reaching, in the bioreactor, 4.4 mg l)1 (on day 14) and 37.5 mg l)1 (on day 11). In shake-flasks the highest total content of paclitaxel and 10-DAB III was 7.3 mg l)1 (on day 4) and 8.8 mg l)1 (on day 18). Phenylalanine, at 0.05 mM, increased paclitaxel accumulation in cells cultivated in bioreactor and flasks 30-fold and 9-fold (from 0.02 mg l)1 to 0.6 mg l)1 and to 0.2 mg l)1, respectively). The 10-DAB III content in cells from flasks was increased from 0.4 mg l)1 to 1.6 mg l)1. Introduction The structurally complex taxane diterpenoid, paclitaxel, first isolated from the bark of the Taxus brevifolia, is a highly effective anti-cancer drug used widely in the treatment of various carcinomas, melanomas, and sarcomas. The 10-deacetylbaccatin III (10-DAB III) is an intermediate in paclitaxel biosynthesis (Walker & Croteau 2001) and currently paclitaxel and its analogue, docetaxel, are produced semi-synthetically through acylation of 10-DAB III isolated from needles of various Taxus species. Taxus-derived cell cultures may be a useful an alternative source of paclitaxel and its derivatives as the complete chemical synthesis is uneconomic and, moreover, an increasing demand for new taxoids with improved biological activity and possible application against other diseases has been observed. Currently paclitaxel, manufactured by plant cell culture technology, is the active compound of Genexol produced by Samyang Genex (www.genexol.com). Among many applied strategies to enhance paclitaxel accumulation in cell culture the medium supplementation with L-phenylalanine, the precursor of paclitaxel’s side chain, resulted in considerable increase in paclitaxel production in suspension cultures of Taxus species as it was reviewed by Zhong (2002). The aim of this work was to conduct a comparative study of biomass growth and examined the influence of L-phenylalanine on production of paclitaxel and 10-DAB III in suspension culture of Taxus · media var. Hicksii carried out in flasks and 7-l bioreactor. This is the first report describing the 10-DAB III and paclitaxel accumulation in suspension culture performed in shake flasks and bioreactor. Materials and methods Flask cultures Suspension culture of Taxus · media var. Hicksii was initiated from callus of seedling origin differentiating into roots. Shake-flask cultures were carried out in 250-ml Erlenmeyer flasks 1302 containing 30 ml modified DCR medium (Gupta & Durzan 1985). The medium was supplemented with 1 mg NAA l)1, 4.8 mg picloram l)1, 500 mg casein hydrolysate l)1 and 30 g sucrose l)1. Cells were transferred to the fresh medium every four weeks. To perform the comparative studies the culture was continued in the same medium but with addition of 8.25 mg L-phenylalanine l)1 (0.05 mM). To examine the time growth parameters about 2.5 g fresh weight of 28-day old cells was placed onto 25 ml fresh medium in 250-ml Erlenmeyer flasks. Every 3--4 days, samples from 2 flasks were collected. The fresh and dry weight of the cells was recorded. The medium was submitted for detection of the pH, content of sucrose and its conductivity, as well for chemical analysis. Bioreactor cultures The culture was performed in 7-l mixed-type airlift reactor implemented with Rushton-type stirred tank (Biostad Ed, Braun). The working volume was 5 l. The inoculum was 2% (w/v) DCR medium as described above. From day 1--4 of culture stirring was set at 400 rpm, and next till the end of experiment at 200 rpm. The pH value was set at 5.42. To determine growth parameters the procedure mentioned above was used. The cultures were maintained at 25±2 C under fluorescent light (40 lmol m)2 s)1) and 12 h light/dark cycle. Chemical analysis The content of paclitaxel (Sigma) and 10-DAB III (donated by Prof. Jaziri from Free University of Brussels) in cells and samples of medium was determinated using method presented earlier (Furmanowa & Syklowska-Baranek 2000). All these experiments were conducted twice. Statistical analysis was performed using the StatSoft STATISTICA PL software. Results and discussion Paclitaxel and 10-DAB III production during batch culture, carried out in bioreactor and in the Erlenmeyer flasks, were compared. The growth of biomass in Erlenmeyer flasks and bioreactor was similar up to day 14. A lag phase was not observed. In the culture carried out in the bioreactor, starting from day 14, there was a rapid decline of biomass accumulation which could be attributed to cell breakage. Moreover from day 4 until the end of cultivation in the bioreactor sucrose was not taken up from the medium and remained on unchanged. On the other hand, the consumption of sucrose in flasks corresponded well to the cell growth profile, and was 90% exhausted by day 14 -- at the onset of stationary growth phase. Navia-Osorio et al. (2002) also reported the lack of the lag phase after inoculation in experiments conducted in 20l bioreactor. Data recorded during cultivating cells in bioreactor might be contributed to higher cell damage by sharing as the medium stirring was set at 400 rpm. The similar growth pattern of suspension culture performed in flasks and bioreactors was also reported by Pestchanker et al. (1996). The supplementation of medium with L-phenylalanine increased the production of cell-associated paclitaxel both in the bioreactor and flasks (see Tables 1 and 2). The influence of this amino acid was the most pronounced in cultures performed in bioreactor where a 30-fold rise in paclitaxel accumulation in cells was obtained (Table 2). Jha et al. (1998) reported a 3-fold enhance of paclitaxel with addition of 2.5 mg IAAand phenylalanine l)1 to the medium. Fett-Neto et al. (1994) demonstrated 4-fold increase of cell-associated paclitaxel content but that the precursor did not promote the accumulation of paclitaxel in the medium relative to the control. L-Phenylalanine added to the medium along with other precursors and elicitors at optimized doses doubled the paclitaxel content of the cells (Luo & He 2004). A combination of in situ extraction with organic solvents, precursor feeding and additional carbon source introduction gave 5 times higher paclitaxel production in comparison to the control (Yuan et al. 2001). Also a 3-fold rise of paclitaxel accumulation in Taxus · media var. Hicksii transgenic root culture was found after elicitation with methyl jasmonte (Furmanowa & Syklowska-Baranek 2000). In our experiments the highest total paclitaxel production (cell-associated and extracellular) was higher in flasks (Tables 1 and 2). However, 1303 Table 1. Paclitaxel and 10-DAB III content (mg l)1) in cells and medium containing L-phenylalanine from suspension culture of Taxus · media var. Hicksii carried out in flasks (values are means of four samples ±SD). Growth (days) 4 7 11 14 18 21 25 28 Cells Medium Total Dry weight (g l)1) Paclitaxel 10-DAB III Paclitaxel 10-DAB III Paclitaxel 10-DAB III 14.2±0.890 16.1±1.002 18.6±2.001 22.2±2.124 21.5±1.954 20.2±1.025 18.2±1.047 21.8±0.712 0.03±0.002 0.2±0.003 0.04±0.001 0.2±0.003 0.1±0.001 0 0 0 1.0±0.008 0.7±0.007 1.0±0.008 0.8±0.007 0.5±0.004 0.8±0.005 1.6±0.014 0.2±0.002 7.3±0.052 1.1±0.002 0 0 0 0 0 0 6.6±0.027 0.3±0.002 2.6±0.003 4.1±0.012 8.2±0.044 3.7±0.039 4.3±0.081 4.8±0.056 7.3±0.171 1.3±0.024 0.04±0.002 0.2±0.021 0.1±0.002 0 0 0 7.6±0.810 1.0±0.254 3.6±0.436 4.9±0.564 8.8±0.641 4.5±0.123 5.9±0.921 5.0±1.002 Taxane content determined in cells from suspension culture carried out in medium without L-phenylalanine in shake flasks (control): paclitaxel 0.02±0.003 mg l)1, 10-DAB III 0.4±0.004 mg l)1; 0 -- taxanes not detected. Table 2. Paclitaxel and 10-DAB III content (mg l)1) in cells and medium containing L-phenylalanine from suspension culture of Taxus · media var. Hicksii carried out in bioreactor (values are means of four samples ± SD). Growth (days) 1 4 7 11 14 18 21 Cells Medium Total Dry weight (g l)1) Paclitaxel 10-DAB III Paclitaxel 10-DAB III Paclitaxel 10-DAB III 3.5±0.451 5.4±0.612 5.0±0.398 7.9±0.887 18.6±1.014 15.2±2.007 11.9±1.985 0 0.04±0.003 0.3±0.008 0.6±0.007 0.4±0.010 0 0 0 0.05±0.007 0.07±0.006 0.08±0.005 0.04±0.002 0 0 1.2±0.081 2.2±0.064 1.1±0.032 0 4.0±0.076 0 0 4.2±0.065 11.5±1.018 12.9±1.425 37.4±2.523 9.3±0.874 0 0 1.2±0.054 2.3±0.036 1.4±0.014 0.6±0.052 4.4±0.321 0 0 4.2±0.029 11.6±0.764 13.0±0.0214 37.5±2.395 9.9±0.845 0 0 Taxane content determined in cells from suspension culture carried out in medium without L-phenylalanine in shake flasks (control): paclitaxel 0.02±0.003 mg l)1, 10-DAB III 0.4±0.004 mg l)1; 0 -- taxanes not detected. paclitaxel in cells from flasks was produced only up to day 18 and was not detected after day 7 in the medium (Table 1). Higher amounts of 10-DAB III were accumulated by cells cultivated in flasks than in bioreactor. But substantially higher quantities of 10-DAB III were secreted to the medium in bioreactor than in flasks (Tables 1 and 2). In our experiments the highest total concentrations of paclitaxel detected in bioreactor coincided with the lowest 10-DAB III amounts (Table 2). In the bioreactor paclitaxel and 10-DAB III accumulation in cells and their secretion to the medium was continuous, moreover at day 11 four peaks of unidentified paclitaxel analogues but in concentration several times higher than paclitaxel, were observed both in cells and medium. During culturing, the excretion of both taxanes in cells grown in flasks and in the bioreactor exceeded on average 72% of the total compound content which is consistent with results obtained by Navia-Osorio et al. (2002) and Pestchanker et al. (1996) although Wickremesinhe & Arteca (1994) reported only a 10% release of paclitaxel in suspension culture of Taxus · media. It was earlier demonstrated that at low inoculum sizes of 1.5 and 2.0 g dry wt l)1 the extracellular paclitaxel concentration was relatively higher (Wang et al. 1997) which is in accordance with our results. Precursor feeding strategy employed in our experiments seems to be promising for future improving and scale-up of taxane production in suspension culture of Taxus species, when 10DAB III production amounted to 37.5 mg l)1 1304 within 11 days of culture and paclitaxel yielded 4.4 mg l)1 within 14 days of culture. Acknowledgements This research work was supported by the grant from the State Committee for Scientific Research No. 4 P05F 028 12. We are grateful to Professor Mondher Jaziri from the Laboratory of Biotechnology and Plant Morphology, Free University of Brussels for the 10-deacetylbaccatin III standard. References Fett-Neto AG, Melanson SJ, Nicholson SA, Pennington JJ, DiCosmo F (1994) Improved taxol yield by aromatic carboxylic acid and amino acid feeding to cell cultures of Taxus cuspidata. Biotechnol. Bioeng. 44: 967--971. Furmanowa M, Syklowska-Baranek K (2000) Hairy root cultures of Taxus · media var. Hicksii Rehd. as a new source of paclitaxel and 10-deacetylbaccatin III. Biotechnol. Lett. 22: 683--686. Gupta PK, Durzan DJ (1985) Shoot multiplication from mature trees of Douglas-fir (Pseudotsuga menziesii) and Sugar pine (Pinus lambertiana). Plant Cell Rep. 4: 177--179. Jha S, Sanyal D, Ghosh B, Jha TB (1998) Improved taxol yield in cell suspension culture of Taxus wallichiana (Himalayan Yew). Planta Med. 64: 270--272. Luo J, He GY (2004) Optimization of elicitors and precursors for paclitaxel production in cell suspension culture of Taxus chinensis in the presence of nutrient feeding. Process Biochem. 39: 1073--1079. Navia-Osorio A, Garden H, Cusidó RM, Palazón J, Alferman AW, Piñol TM (2002) Production of paclitaxel and baccatin III in a 20-L airlift bioreactor by a cell suspension of Taxus wallichiana. Planta Med. 68: 336--340. Pestchanker LJ, Roberts SC, Shuler ML (1996) Kinetics of taxol production and nutrient use in suspension cultures of Taxus cuspidata in shake flasks and a Wilson-type bioreactor. Enzyme Microb. Technol. 19: 256--260. Walker K, Croteau R (2001) Taxol biosynthesis genes. Phytochemistry 58: 1--7. Wang HQ, Zhong JJ, Yu JT (1997) Enhanced production of taxol in suspension cultures of Taxus chinensis by controlling inoculum size. Biotechnol. Lett. 19: 353--355. Wickremesinhe ERM, Arteca RN (1994) Taxus cell suspension cultures: optimizing growth and production of taxol. J. Plant Physiol. 144: 183--188. Yuan YJ, Wei ZJ, Wu ZL, Wu JC (2001) Improved taxol production in suspension cultures of Taxus chinensis var. mairei by in situ extraction combined with precursor feeding and additional carbon source introduction in airlift loop reactor. Biotechnol. Lett. 23: 1659--1662. Zhong JJ (2002) Plant cell culture form production of paclitaxel and other taxanes. J. Biosci. Bioeng. 94: 591--599. Ó Springer 2005 Biotechnology Letters (2005) 27: 1305–1310 DOI 10.1007/s10529-005-3224-5 Regio- and stereo-selective hydroxylation of abietic acid derivatives by Mucor circinelloides and Mortierella isabellina Koichi Mitsukura, Takeshi Imoto, Hirokazu Nagaoka, Toyokazu Yoshida & Toru Nagasawa* Department of Biomolecular Science, Gifu University, 1-1 Yanagido, Gifu, 501-1193, Japan *Author for correspondence (Fax: +81-58-293-2647; E-mail: [email protected]) Received 27 April 2005; Revisions requested 24 May 2005; Revisions received 20 June 2005; Accepted 21 June 2005 Key words: abietic acid derivatives, microbial hydroxylation, regio-selective, stereo-selective Abstract Mucor circinelloides and Mortierella isabellina hydroxylated dehydroabietic acid (DehA). DehA was converted regio- and stereo-selectively by whole cells of Mr. circinelloides to give 2a-hydroxydehydroabietic acid in a 75% molar conversion yield (11 mM from 14.7 mM DehA) after 72 h in the cultivation medium containing 3% (v/v) Tween 80. With cells of Ma. isabellina, under the same conditions, 20.5 mM (6.5 g l)1) 2–hydroxydehydroabietic acid (a/b=81/19) was formed from 26.4 mM DehA. Introduction Rosin, commonly known as resin acid, is an abundant renewable resource obtained from pitch pine. It is comprised of several diterpenoic acid derivatives, such as abietic acid, dehydroabietic acid, dihydroabietic acid, pimaric acid and tetrahydroabietic acid. They are widely used to synthesize sizing agents for paper, emulsifying agents for synthetic rubber, resin for printing inks, resin adhesives, etc. (Sadhra et al. 1994). On the other hand, the leakage of the resin acid into natural world through the production process of paper and pulp has often caused severe environmental pollution problems (Owens 1991). Therefore, the microbial degradation or detoxification of resin acid has been studied (Liss et al. 1997, Martin et al. 1999). Further broad applications of resin acids can be expected in the field of synthetic chemicals due to their unique chemical and physical properties. Several biological activities such as anti-ulcer (Wada et al. 1985), anti-microbial (Savluchinske Feio et al. 1999) and anti-inflammatory (Fernandez et al. 2001) effects of resin derivatives have also been reported. In the present study, we have surveyed microorganisms to catalyze the hydroxylation of abietic acid derivatives and found a strain of Mucor circinelloides IT25 that catalyzes the regio-selective and stereo-selective hydroxylation of both abietic acid and dehydroabietic acid. Materials and methods Chemicals Abietic acid (AbA), dehydroabietic acid (DehA), dihydroabietic acid (DihA) and rosin containing 2% (w/w) AbA, 58% (w/w) DehA and 36% (w/w) DihA were kindly provided by Arakawa Chemical Industries (Japan). Products from the following suppliers were used: polypeptone (Nippon Seiyaku, Japan), meat extract (Mikunikagaku, Japan) and yeast extract (Oriental Yeast, Japan). All other chemicals were of guaranteed reagent grade. 1306 Isolation of microorganisms capable of converting abietic acid derivatives Microorganisms capable of converting AbA, DehA or DihA were isolated in two ways using two types of basal media. To collect fungi from soil, a mixture of soil samples (approximately 2 g) suspended in 5 ml 0.85% (w/v) NaCl was plated onto medium A containing 30 g sucrose l)1, 2 g NaNO l)13, 1 g K2HPO4 l)1, 0.5 g MgSO4Æ7H2O l)1, 0.5 g KCl l)1, 0.01 g FeSO4Æ7H2O l)1 and 20 g agar l)1and incubated at 28 °C. A single colony on each plate was picked, and its AbA or DehA-converting activity was evaluated. Alternatively, a conventional enrichment culture was carried out aerobically at 28 °C for 14 days in a test-tube containing 5 ml medium B (pH 7.3) which consisted of 4 g rosin l)1, 10 g sucrose l)1, 1 g yeast extract l)1, 2 g NH4Cl l)1, 1 g K2HPO4 l)1, 0.5 g MgSO4Æ7H2O l)1, 0.5 g KCl l)1and 0.01 g FeSO4Æ7H2O l)1. Each culture was spread on the plate containing the medium A and 2% (w/v) agar and incubated at 28 °C. The conversion of rosin was checked by thin-layer chromatography (TLC) analysis. 0.2% (w/v) AbA, DehA or DihA were added to the medium. Biotransformation of each substrate was carried out at 28 °C for 7 days. Identification of reaction products The reaction products (see Figure 1) converted from AbA, DehA or DihA were purified using a silica gel column (n-hexane:ethyl acetate=8:1, 4/1, 2:1, 1:1, 0:1, and methanol, v/v) and preparative TLC (n-hexane:ethyl acetate=2:1, v/v). The analyses of products were carried out using a Varian INOVA 400 for NMR, a Jeol Automass SUN300 for GC-MS, and a Horiba SEPA300 for optical rotation. Identification of microorganisms Among 238 isolates, three bacteria (HR1, HR6, and HR34) and two molds (IT 25 and HR32) exhibited abietic acid derivative-converting activity. Based on morphological, physiological and biological aspects, these five strains were identified by the National Collections of Industrial, Food and Marine Bacteria, Japan. Culture conditions and conversion of AbA, DehA and DihA The pre-culture was carried out at 28 °C for 2 days with reciprocal shaking in a test-tube containing 5 ml medium (pH 5.5) comprised of 5 g polypepton l)1, 2 g yeast extract l)1, 1 g K2HPO4 l)1, 0.5 g MgSO4Æ7H2O l)1 and 0.01 g FeSO4Æ7H2O l)1. The pre-culture was added to a 500 ml shaking-flask containing 30 ml of the same medium using pre-culture. Cultivation was carried out at 28 °C for 2 days with reciprocal shaking (115 strokes min)1), and then Fig. 1. Microbial conversion of various abietic acid derivatives. 1307 High performance liquid chromatography (HPLC) analysis Each compound was analyzed by reverse-phase HPLC using an ODS column (Waters Spherisorb, 4.6150 mm) and methanol/water (8:2, v/v) for elution at 1 ml min)1 and monitoring at 230 nm. Optimization of culture medium For the studies on the optimization of culture medium, a mixture comprised of 0.1% (w/v) K2HPO4, 0.05% (w/v) MgSO4Æ7H2O, and 0.001% (w/v) FeSO4Æ7H2O was used as the basal medium. The pre-culture using medium A was carried out at 28 °C for 2 days with reciprocal shaking. Cultivation was carried out at 28 °C for 3 days with reciprocal shaking. Results Microbial conversion of AbA, DehA and DihA Among fungi isolates, Mortierella isabellina HR32 exhibited a powerful hydroxylation activity for DehA. In addition, we found that Mr. circinelloides IT 25 exhibited a novel DehAconverting activity. Mr. circinelloides IT25 catalyzed the regio- and stereo-selective hydroxylation of AbA and DehA to 2a-hydroxyabietic acid and 2a-hydroxydehydroabietic acid, respectively. With AbA as a substrate, the aromatization of AbA to DehA proceeded in the course of cultivation medium due to its AbA instability. Although Mr. javanicus IAM 6087 also exhibited DehA-hydroxylation activity, it was lower than that of Mr. circinelloides IT25. Ma. isabellina HR32 also showed the hydroxylation activity for DehA or DihA. 2-hydroxydehydroabietic acid formed from DehA was a mixture of two isomers, i.e., 81% a-isomer and 19% b-isomer, as revealed in an analysis of NMR after esterification with trimethylsilyldiazomethane in a methanol solution. When using AbA as a substrate, however, 2a-hydroxyabietic acid was not formed at all. If the other isolates were examined, Moraxella sp. HR6 converted DehA and DihA to 3,7-dioxodehydroabietin and 3,7-dioxodihydroabietin, respectively, probably through the oxidation at C3 and C7 followed by decarboxylation at C4 with a low molar conversion yield. Pseudomonas sp. HR34 converted DihA to 7-oxodihydroabietic acid. On the other hand, Sphingomonas sp. HR1 catalyzed the rapid degradation of DehA or DihA, so that their hydroxylated products were not detected. These microbial conversions of abietic acid derivatives we found are summarized in Figure 1. The product obtained from AbA, DehA or DihA by microbial conversion was purified by silica gel column and identified by NMR and MS. 2a-Hydroxydehydroabietic acid: 1H-NMR (CDCl3, 400 MHz) d 7.18 (1H, d, J=8.0 Hz), 7.02 (1H, dd, J=8.0, 1.6 Hz), 6.91 (1H, d, J=1.6 Hz), 4.11 (1H, tt, J=11.4, 4.1 Hz), 2.88–2.96 (2H, m), 2.82 (1H, septet, J=7.0 Hz), 2.67 (1H, m), 2,25 (1H, dd, J=12.6, 2.0 Hz), 2.12(1H, s), 2.07 (1H, m), 1.78–1.90 (1H, m), 1.77 (1H, t, J=11.7 Hz), 1.57–1.65 (1H, m), 1.48 (1H, t, J=11.7 Hz), 1.31 (3H, s), 1.28 (3H, s), 1.22 (6H, d, J=7.0 Hz); 13CNMR (CDCl3, 100 MHz) d182.8, 146.1, 145.8, 134.2, 127.0, 124.1, 123.9, 65.1, 48.2, 47.1, 45.2, 44.3, 38.6, 33.5, 29.8, 26.1, 24.0, 20.9, 17.3; GCMS (methyl ester) (m/z) 330 (M+), 312, 283, 255, 237(100%), 195; [a]24.5D +60.4 (c. 0.16, CHCl3). In the case of Ma. isabellina HR32, the optical rotation is [a]24.5D +44 (c. 0.185, CHCl3). 2a-Hydroxyabietic acid: 1H-NMR (CDCl3, 400 MHz) d 5.78 (1H, s), 5.37 (1H, d, J=4.4 Hz), 3.94 (1H, tt, J=11.6, 4.0 Hz), 2.21 (1H, dd, J=13.6, 6.2 Hz), 2.10 (1H, brs), 1.92–2.08 (3H, m), 1.83 (1H, d, J=11.7 Hz), 1.78 (1H, t, J=11.7 Hz), 1.27 (3H, s), 1.21–1.26 (5H, m), 1.13 (1H, t, J=12.0 Hz), 1.10 (3H, d, J=7.0 Hz), 1.00 (1H, t, J=6.6 Hz), 0.86 (3H s,); 13 C-NMR (CDCl3, 100 MHz) d182.9, 145.4, 135.1, 122.1, 120.3, 64.6, 50.9, 47.5, 45.3, 44.5, 36.3, 34.8, 27.3, 25.1, 22.5, 21.4, 20.8, 17.7, 14.9; GC-MS (methyl ester) (m/z) 332 (M+), 314, 255(100%), 239. 1 2-Hydroxydihydroabietic acid: H-NMR (CDCl3, 400 MHz) d 3.97 (1H, tt, J=11.4, 4.2 Hz), 2.11–2.17 (1H, m), 2.04–2.11 (1H, m), 2.03 (1H, dd, J=13.2, 2.6 Hz), 1.69–1.83 (2H, m), 1.53–1.63 (2H, m), 1.19 (2H, t, J=8.4 Hz), 1.14 (2H, t, J=11.7 Hz), 1.02 (3H, s), 0.95–1.01 (1H, m), 0.88 (3H, d, J=7.0 Hz), 0.87 (3H, d, J=7.0 Hz); 13C-NMR (CDCl3, 100 MHz) d182.6, 136.8, 126.3, 65.1, 48.3, 45.9, 45.3, 44.8, 40.4, 38.6, 34.3, 32.5, 31.8, 27.1, 24.7, 1308 20.8, 20.4, 19.9, 19.5, 17.3; GC-MS (methyl ester) (m/z) 334 (M+), 316, 301, 273, 257, 241(100%). 7-Oxodihydroabietic acid: 13C-NMR (CDCl3, 100 MHz) d200.0, 182.3, 166.5, 130.6, 46.3, 44.6, 39.5, 39.2, 36.7, 36.2, 34.4, 32.3, 26.7, 26.2, 26.0, 19.8, 19.5, 17.8, 17.7, 16.2; GC-MS (methyl ester) (m/z) 332 (M+), 317, 289, 273, 257(100%), 229. 3,7-Dioxodehydroabietin: 13C-NMR (CDCl3, 100 MHz) d210.7, 197.4, 149.8, 147.6, 132.7, 130.8, 125.4, 124.4, 47.8, 44.9, 39.4, 37.7, 37.2, 36.7, 33.6, 23.8, 23.7, 21.2, 11.0; GC-MS (m/z) 284 (M+), 269(100%), 227, 199. 3,7-Dioxodihydroabietin: 13C-NMR (CDCl3, 100 MHz) d210.7, 197.8, 163.5, 131.9, 48.0, 44.7, 39.4, 38.7, 38.3, 37.5, 35.2, 32.3, 27.4, 26.8, 25.9, 19.7, 19.5, 16.0, 10.9. Optimal conditions for accumulation of 2a-hydroxydehydroabietic acid To enhance the hydroxylation activity of Mr. circinelloides IT25 and Ma. isabellina HR32, the culture conditions were optimized. The activity was evaluated by measuring the amount of 2a-hydroxydehydroabietic acid formed in the medium at 28°C after 72 h cultivation. The optimal medium for Mr. circinelloides IT25 consisted of 20 g sodium L-glutamate l)1, 10 g malt extract l)1, 1 g K2HPO4 l)1, 0.5 g MgSO4Æ7H2O l)1, and 0.01 g FeSO4Æ7H2O l)1 at pH 7.5. Under these conditions, it produced 5.4 mM 2ahydroxydehydroabietic acid from 14.7 mM DehA with a 37% molar conversion yield. Culture conditions of Ma. isabellina HR32 were also examined. The optimized medium was comprised of 20 g polypeptone l)1, 20 g yeast extract l)1, 1 g K2HPO4 l)1, 0.5 g MgSO4Æ7H2O l)1 and 0.01 g FeSO4Æ7H2O l)1 at pH 5.0. When the cultivaion was carried out using the medium, 5.6 mM 2-hydroxydehydroabietic acid was formed from 26.4 mM DehA with a 21% molar conversion yield. For further improvement of the productivity of 2a-hydroxydehydroabietic acid, the effect of organic solvents and detergents on DehA hydroxylation was examined (Table 1). The addition of 1% (v/v) methanol or ethanol was effective in slightly extending of the formation of 2a-hydroxydehydroabietic acid by Ma. isabellina HR32. The additon of 3% (v/v) Tween 80 resulted in a significant enhancement of 2a-hydroxydehydroabietic Table 1. Effects of organic solvents and detergents on production of 2-hydroxydehydroabietic acid. Organic solvent or detergent None Methanol Ethanol Acetone Dimethyl sulfoxide Tween 20 Tween 80 Triton X)100 Cone (% v/v) 1 1 1 1 1 1 2 3 4 1 Relative activity (%) Mucor circinelloides Mortierella isabellina 100 92 92 93 55 98 128 166 204 204 96 100 149 145 90 96 124 195 353 365 360 0 DehA (150 mg, 0.50 mmol) and (270 mg, 0.90 mmol), respectively, was added to the cultivation medium of either Mr. circinelloides or Ma. isabellina. Strain IT25 and HR32 cells formed 5.4 mM and 5.6 mM 2-hydroxydehydroabietic acid, respectively, without organic solvents and detergents after 72 h cultivation at 28 °C. These values were taken as 100%. acid production by Mr. circinelloides IT 25 or Ma. isabellina HR32. Mr. circinelloides IT 25 produced 11 mM (3.5 g l)1) 2a-hydroxydehydroabietic acid from 14.7 mM DehA with a 75% molar conversion yield. In the case of Ma. isabellina HR32, 20.5 mM (6.5 g l)1) 2-hydroxydehydroabietic acid (a/b=81/19) was produced from 26.4 mM DehA with a 78% molar conversion yield (Table 1). Effects of P450 inhibitors on DehA hydroxylation The effect of common P450 inhibitors on the hydroxylation of DehA by Mr. circinelloides IT 25 was examined by adding 0.5 mM P450 inhibitors to the cultivation medium (Table 2). The hydroxylation activity of Mr. circinelloides IT 25 was inhibited by all P450 inhibitors tested, with 1-aminobenzotriazole causing the most significant inhibition. Discussion In previous studies of biodegradation of DehA, some bacteria could grow on DehA as a carbon source, and the biodegradation pathways of 1309 Table 2. Effect of P450 inhibitors at 0.5 mM on DhA hydroxylation by Mr. circinelloides IT25. Inhibitor Relative activity (%) None Methoxsalen 1-Aminobenzotriazole Ketoconazole Miconazole Menadione 100 49 36 52 75 76 Hydroxylation of DhA was carried out at 28 °C for 72 h cultivation in the optimum medium containing 3% (v/v) Tween 80. The formation of 10 mM 2a-hydroxydehydroabietic acid in the absence of P450 inhibitors was taken as 100% – see Table 1 for absolute values. DehA have been outlined as shown in Figure 2a based on studies of their metabolic intermediates or molecular genetics. The microbial degradation or conversion of AbA has scarcely been studied due to its chemical lability, causing it to change readily into DehA (Martin & Mohn 2000). In the present study, we found that Moraxella sp. HR6 acted on DehA, and forming a new metabolite, 3,7-dioxodehydroabietin. This result suggested that Moraxella sp. HR6 probably degraded DehA through a pathway similar to pathway A in Figure 2a. A low amount of accumulated of 3,7-dioxodehydroabietin suggested that the activity of the dioxygenase required to catalyze cleavage of the subsequent rings might be high. When DehA was replaced with DihA, the accumulation of a new metabolite, 3,7-dioxodihydroabietin was observed at a higher concentration than that of 3,7-dioxodehydroabietin. Thus, the degradation of 3,7-dioxodihydroabietin proceeded at lower rate than 3,7-dioxodehydroabietin because the cyclohexane ring of DihA is resistant to the meta-cleavage catalyzed by dioxygenase. Pseudomonas sp. HR34 also catabolized DihA rapidly and a new metabolite, 7-oxodihydroabietic acid, was detected. This suggests that the degradation of DehA by Pseudomonas sp. HR34 probably Fig. 2. (a) Possible degradation pathway of DehA by Flavobacterium resinovorum (Biellmann et al. 1973a) (A), Alcaligenes eutrophus and Pseudomonas sp. (Biellmann et al. 1973b) (B), Pseudomonas abietaniphila BKME)9 (Martin and Morn 1999) (b) Conversion of DehA by Fusarium oxysporum or F. moniliforme (Tapia et al. 1997) (C), Mortierella isabellina (Kutney et al. 1981) (D) and Chaetomium cochliodes (Yano et al. 1994) (E). 1310 proceeded through pathway B (see Figure 2). When Sphingomonas sp. HR1 cells were used, DehA was completely degraded. In contrast to bacteria, no mold capable of assimilating DehA as a sole carbon source has been reported. As shown in Figure 2b, two molds convert DehA into the hydroxylated catabolites. In our studies, Ma. isabellina HR32 produced a mixture of 2a- and 2b-hydroxydehydroabietic acid through pathway D. We also found that Ma. isabellina HR32 catalyzed the hydroxylation of DihA at C2 and Mr. circinelloides IT25 catalyzed the hydroxylation of AbA at C2. We isolated these metabolites and identified their chemical structures. The addition of nonionic detergent Tween 20 or Tween 80 enhanced production of 2a-hydroxydehydroabietic acid. We assume that Tween 20 and Tween 80 probably enhanced the solubility of rosin or the permeability of the cell membrane (Baklashova & Koshcheenko 1980). Based on the effect of P450 inhibitors on DehA hydroxylation, we suggested that Mr. circinelloides IT25 might proceed through a system incorporating P450. Conclusion Until now, the production of catabolic intermediates of DehA, a renewable natural resource, has not been undertaken from the viewpoint of their application and development. In the present studies, we have produced, for the first time, a large amount of 2a-hydroxydehydroabietic acid by optimizing the culture conditions and are proceeding to examine its applications as a functional material. Acknowledgements We are grateful to Life Science Research Center in Gifu University for NMR and mass measurements. References Baklashova TG, Koshcheenko KA (1980) Effect of detergents on the hydroxylation of indolyl)3-acetic acid by an Aspergillus niger culture. Mikrobiologiia 49: 546–550. Biellmann JF, Branlant G, Gero-Robert M, Poiret M (1973a) Dégradation bactérienne de l’acide déhydroabiétique par un Flavobacterium resinovorum. Tetrahedron 29: 1227–1236. Biellmann JF, Branlant G, Gero-Robert M, Poiret M (1973b) Dégradation bactérienne de l’acide déhydroabiétique par un Pseudomonas et une Alcaligenes. Tetrahedron 29: 1237–1241. Fernandez MA, Tornos MP, Garcia MD, de las Heras B, Villar AM, Saenz MT (2001) Anti-inflammatory activity of abietic acid, a diterpene isolated from Pimenta racemosa var. grissea. J. Pharm. Pharmacol. 53: 867–872. Kutney JP, Singh M, Hewitt GM, Salisbury PJ, Worth BR, Servizi JA, Martens DW, Gordon RW (1981) Studies related to biological detoxification of kraft pulp mill effluent I. The biodegradation of dehydroabietic acid with Mortierella isabellina. Can. J. Chem. 59: 2334–2341. Liss SN, Bicho PA, Saddler JN (1997) Mini-review: Microbiology and biodegradation of resin acids in pulp mill effluents. Can. J. Microbiol 43: 599–611. Martin VJJ, Mohn WW (1999) A novel aromatic-ring-hydroxylating dioxygenase from the diterpenoid-degrading bacterium, Pseudomonas abietaniphila BKME)9. J. Bacteriol. 181: 2675–2682. Martin VJJ, Yu Z, Mohn WW (1999) Mini review: Recent advances in understanding resin acid biodegradation: microbial diversity and metabolism. Arch. Microbiol. 172: 131–138. Martin VJJ, Mohn WW (2000) Genetic investigation of the catabolic pathway for degradation of abietic diterpenoids by Pseudomonas abietaniphila BKME)9. J. Bacteriol. 182: 3784–3983. Owens JW (1991) The hazard assessment of pulp and paper effluents in the aquatic environment: a review. Environ. Toxicol. Chem. 10: 1511–1540. Sadhra S, Foulds IS, Gray CN, Koh D, Gardiner K (1994) Colophony – uses, health effects, airborne measurements and analysis. Ann. Occup. Hyg. 38: 385–396. Savluchinske Feio S, Gigante B, Roseiro JC, Marcelo-Curto MJ (1999) Antimicrobial activity of diterpene resin acid derivatives. J. Microbiol. Methods 35: 201–206. Tapia AA, Vallejo MD, Gouiric SC, Feresin GE, Rossomando PC, Bustos DA (1997) Hydroxylation of dehydroabietic acid by Fusarium species. Phytochemistry 46: 131–133. Wada H, Kodato S, Kawamori M, Morikawa T, Nakai H, Takeda M, Saito S, Onoda Y, Tamaki H (1985) Antiulcer activity of dehydroabietic acid derivatives. Chem. Pharm. Bull. (Tokyo) 33: 1472–1487. Yano S, Nakamura T, Uehara T, Furuno T, Takahashi A (1994) Biotransformation of terpenoids in conifers by microorganisms I. Hydroxylation of dehydroabietic acid by Chaetomium cochliodes. Mokuzai Gakkaishi 40: 1226–1232. Springer 2005 Biotechnology Letters (2005) 27: 1311–1317 DOI 10.1007/s10529-005-3225-4 Increased conformational and thermal stability properties for phenylalanine dehydrogenase by chemical glycosidation with end-group activated dextran Reynaldo Villalonga1,*, Shinjiro Tachibana2, Yunel Pérez1 & Yasuhisa Asano2 1 Enzyme Technology Group, Center for Biotechnological Studies, University of Matanzas, 44740, Matanzas, C.P, Cuba 2 Biotechnology Research Center, Toyama Prefectural University, 5180 Kurokawa, 939-0398, Kosugi, Toyama, Japan *Author for correspondence (Fax: +53-45-253101; E-mail: [email protected]) Received 20 May 2005; Revisions requested 26 May 2005; Revisions received 20 June 2005; Accepted 21 June 2005 Key words: dextran, enzyme stability, glycosidation, phenylalanine dehydrogenase Abstract A mono-aminated dextran derivative was attached to Bacillus badius phenylalanine dehydrogenase via a carbodiimide-catalyzed reaction. The optimum temperature for the conjugate was 10 C higher than for native enzyme, and its thermostability was improved by 8 C. The activation free energy of thermal inactivation at 45 C was increased by 16.8 kJ/mol. The improved conformational stability of the modified enzyme was confirmed by fluorescence spectroscopy. Introduction Phenylalanine dehydrogenase (PheDH, EC 1.4.1.20) from Bacillus badius is a NAD+-dependent octameric enzyme that catalyzes the reversible oxidation–reduction reactions for Lphenylalanine (Asano 1999). This enzyme has been used in the colorimetric screening of phenylketonuria in neonates in Japan (Asano et al. 1987), and also constitutes a valuable catalyst for the enantioselective synthesis of Phe and related L-amino acids from their keto analogs (Asano et al. 1990). However, the biocatalytic and analytical applications of this enzyme is limited by its rapid inactivation at elevated temperatures (Asano et al. 1987). Cross-linking of enzymes with polyactivated polymers has been widely used for increasing functional stability (Srivastava 1991, Gómez & Villalonga 2000, Darias & Villalonga 2001, Villalonga et al. 2003). Site-specific modification with polyethylenglycols has been also reported as stabilizing method for enzymes (Veronese et al. 2002). We recently described the use of monoactivated cyclodextrin derivatives as glycosidation agents for preparing thermostable neoglycoenzymes (Cao et al. 2003, Villalonga et al. 2003, Fernández et al. 2004). However, chemically activated cyclodextrins are expensive materials, and this fact limits their wide use in the synthesis of neo-glycoenzymes for industrial application. Dextrans are less expensive and non-toxic polysaccharides produced by bacteria from sucrose, and consisting of linear a-1,6-linked D-glucopyranose units with some degree of branching via 1,3-linkages (Mehvar 2000). High stable enzyme derivatives have been prepared by crosslinking the protein surfaces with polyactivated dextrans (Srivastava 1991), but this approach yields to enzyme preparations with low catalytic activity. This problem could be solved by using mono-activated polymer derivatives, but the 1312 preparation of such kind of mono-activated macromolecules requires well specific reaction conditions as well as the adequate selection of the polymer size (Bruneel & Schacht 1995). The present paper reports the preparation of an end-group mono-aminated dextran derivative, and its use as glycosidation agent for B. badius PheDH. The influence of this modification on the catalytic and stability properties of this oxidoreductase is evaluated. Materials and methods Materials Phenylalanine dehydrogenase from Bacillus badius (18.4 U/mg), recombinantly expressed in E. coli, was prepared as previously described (Asano et al. 1987). L-Phenylalanine, NAD+ and 1-ethyl-3-(3-dimethylaminopropyl) carbodiimide hydrochloride (EDAC) were purchased from Wako Pure Chemicals. Dextran 5000 was from Serva. All other chemicals were analytical grade. Synthesis of end-group aminated dextran Dextran (2 g), dissolved in 10 ml distilled water was treated with 1 ml 1,6-hexylenediamine and stirred for 2 h. NaBH3CN, 150 mg, was then added and the reaction mixture was continuously stirring at room temperature overnight. The solution was further extensively dialyzed vs. distilled water using a Spectrapor 6 dialysis tubing (Serva, molecular weight cut-off 1000 Da) and finally lyophilized. The aminated dextran derivative was characterized by 1H-NMR spectrometry using a Bruker AVANTE 400 MHz apparatus. Preparation of PheDH-dextran conjugate EDAC, 10 mg, was added to a reaction mixture containing 4 mg PheDH dissolved in 3 ml 50 mM sodium phosphate buffer, pH 6.0, and 100 mg aminated dextran. The solution was stirred for 1 h at room temperature, then at 4 C for 16 h and finally dialyzed at 4 C against 10 mM potassium phosphate buffer, pH 7.0, containing 1 mM EDTA and 5 mM 2-mercaptoethanol. Analytical determinations The enzymatic activity of native and modified PheDH was determined at 25 C in 100 mM glycine/KCl/KOH buffer, pH 10.4, containing 2.5 mM NAD+ and using 10 mM L-Phe as substrate (Asano et al. 1987). One unit of L-phenylalanine dehydrogenase activity is defined as the amount of enzyme that catalyzes the formation of 1 lmol NADH per min under the described conditions. Michaelis-Menten parameters were calculated from Eadie-Hofstee plots. Protein concentration was estimated from the absorbance at 280 nm using the absorption coefficient A1% 1cm ¼ 6:3 (Asano et al. 1987). Total carbohydrates were determined by the phenol/sulfuric acid method using glucose as standard (Dubois et al. 1956). The molecular weight of the enzyme forms was determined by analytical GPC on TSKGEL G3000SW column (4.560 cm), calibrated with protein standards from Oriental Yeast Co., Ltd. The fluorescence emission spectra of native and modified PheDH before and after thermal denaturation at 55 C were measured with 0.7 nmol enzyme in 10 mM sodium phosphate buffer, pH 7.0, containing 1 mM EDTA and 5 mM 2-mercaptoethanol, using a spectrofluorimeter with excitation at 280 nm and the emission scanned between 300–400 nm. Light scattering measurements of native and dextran-modified PheDH were monitored at 400 nm after excitation at 280 nm. Results and discussion The strategy used for end-group functionalization of dextran involves the treatment with a molar excess of 1,6-hexylenediamine in the presence of NaBH3CN in order to reduce only the new imine bonds formed at the reducing end of the polymer. Through this procedure, a high yield of mono-activated dextran was obtained (about 91%), as determined by 1H-NMR spectra (data not shown). The amino dextran derivative synthesized was further attached to the free carboxylate groups from aspartic and glutamic acid residues located at the protein surface of PheDH, through the 1313 Fig. 1. Preparation of PheDH-dextran conjugate. formation of stable amide links by using a water soluble carbodiimide as coupling agent. Due to the mono-activated nature of the modifying polymer, each mol of polysaccharide was attached to a single amino acid residue. The overall synthetic process employed for preparing this neo-glycoenzyme is illustrated in Figure 1. Table 1. Structural and catalytic properties of dextranmodified PheDH. Parameter PheDH PheDH-dextran Molecular weight (kDa) Dextran content (mol/mol protein) Specific activity (Umg)1) Km (lM) kcat (s)1) kcat/Km (lM)1s)1) 325.6 – 342 3 18.4 215 816 3.8 16.3 164 714 4.4 The structural and catalytic properties of this enzyme-polymer conjugate are reported in Table 1. The molecular weight of PheDH, determined by analytical GPC, was increased in about 16.4 kDa after glycosidation with dextran. This result represents an average of 3 mol polysaccharide attached to each mol octameric protein. On the other hand, the specific dehydrogenase activity retained by the conjugated enzyme was estimated to be about 89%. It was further demonstrated that this reduction was partially mediated by the presence of EDAC as catalyst in the reaction media. Steric hindrance to the diffusion of L-Phe to the active site of the enzyme, caused by the presence of the bulky polysaccharide moieties at the surface of PheDH, could be also considered as a possible cause of this reduction. Glycosidation with dextran enhanced the affinity of the enzyme for L-Phe: Km was decreased by 1.3-fold for Phe- 1314 Relative Activity (%) 100 80 60 40 20 0 30 40 50 60 70 Temperature (°C) Fig. 2. Temperature-activity profile of native (s) and dextran-modified PheDH (d).The enzyme activity of native and modified enzyme preparations (about 10 U/ml, corresponding to 100% in the graphic), was measured at different temperatures in 100 mM glycine/KCl/KOH buffer, pH 10.4. As a control, a physical mixture of PheDH and amino dextran (X) was also evaluated. 100 Residual Activity (%) DH after modification with dextran. On the contrary, the rate of dehydrogenation of L-Phe was only slightly decreased for the transformed enzyme, as is revealed by the lower value of kcat. The catalytic behaviour of PheDH at high temperatures was noticeably improved after glycosidation with the polymer. In order to evaluate the effect of this modification on the enzyme thermoresistance, different types of experiments were performed. As a, native PheDH was mixed with mono-aminated dextran in order to eliminate any contribution caused by the physical presence of the polysaccharide. Figure 2 shows the temperature-activity profiles of native and dextran-modified PheDH preparations. PheDH showed maximum catalytic activity at 40 C, and this value of optimum temperature was not affected by the physical presence of the aminated dextran. On the contrary, the optimum temperature for dehydrogenation of L-Phe was increased in about 10 C for the enzyme after conjugation with the polysaccharide. This fact could be justified by the improved thermostabilization showed by the conjugated enzyme (see below), avoiding protein denaturation until higher temperatures and then favouring to reach a high catalytic activity of PheDH at elevated temperatures. The effect of 10 min of incubation at different temperatures on the catalytic activity of both PheDH forms is shown in Figure 3. Dextran- 80 60 40 20 0 30 40 50 60 70 Temperature (°C) Fig. 3. Thermal stability profile of native (s) and dextranmodified PheDH (d). Native and modified enzyme preparations (about 50 U/ml, corresponding to 100% in the graphic), were incubated in 10 mM potassium phosphate buffer, pH 7.0, containing 1 mM EDTA and 5 mM 2-mercaptoethanol at the stated temperatures for 10 min. Samples were removed, chilled quickly, and assayed for enzymatic activity. As a control, a physical mixture of PheDH and amino dextran (X) was also evaluated. modified enzyme was more resistant to heat treatment at temperatures higher than 45 C, in comparison with the native counterpart. Consequently, the value of T50, defined as the temperature at which 50% of the initial activity was retained, was increased from 54 to 62 C for PheDH after glycosidation with the polysaccharide. Figure 4 shows the time course of inactivation of PheDH preparations at different temperatures ranging from 45 to 60 C. As can be observed, both enzyme preparations progressively lost activity with time though a second order inactivation mechanism, and then the data obtained were analyzed according to a series-type enzyme inactivation model involving two first-order steps (Sadana & Henley 1987), in which k1 and k2 are the inactivation rate constants. The kinetics constants were calculated by using a non-linear regression procedure based on the MarquardtLevenberg method of iterative convergence included into the Microcal Origin 7.0 software (Microcal Software, Inc., MA, USA). This kind of biphasic thermal inactivation process is characteristic for oligomeric proteins like PheDH (Asano et al. 1987). However, it should be noted that the modified enzyme possessed lower inactivation rate constants and consequently higher values of half life times, 1315 (a) 80 60 40 20 0 0 30 60 90 120 90 120 Time (min) Residual Activity (%) (b) 100 80 60 40 20 0 0 30 60 Time (min) (a) Fig. 4. Kinetics of thermal inactivation of native (a) and dextran-modified PheDH (b) at 45 C (m), 50 C (X), 55 C (s) and 60 C (n). Native and modified enzyme preparations (about 50 U/ml, corresponding to 100% in the graphic), were incubated at different temperatures in 10 mM potassium phosphate buffer, pH 7.0, containing 1 mM EDTA and 5 mM 2mercaptoethanol. Aliquots were removed at scheduled times, chilled quickly, and assayed for enzymatic activity. Relative Intensity Residual Activity (%) 100 at 45 C, temperature at which the activation Gibbs energy of the first phase of thermal inactivation (DGi) (Darias & Villalonga 2001) increased in about 16.8 kJ/mol. The molecular events behind the thermal stabilization showed by modified PheDH may be explained by the combined contribution of several factors, previously demonstrated to be effective in the maintenance of the active conformation of neo-glycoenzymes. Among these, the most important factors could be the conformational stabilization of dextran-modified PheDH molecules due to the formation of new intramolecular hydrogen bonds (Srivastava 1991); and the hydrophilization of the non-polar surface areas of the enzyme, preventing the thermal inactivation mechanisms associated with the formation of intermolecular protein aggregates due to hydrophobic interactions (Venkatesh & Sundaram 1998). 45 t1/2 t1/2 t1/2 t1/2 t1/2 t1/2 t1/2 t1/2 50 55 60 (1) (2) (1) (2) (1) (2) (1) (2) PheDH PheDH-dextran 2.0 19.3 1.0 4.4 0.7 2.6 0.07 0.17 231 n.d. 9.6 116 4.4 23 0.4 3.9 300 325 350 375 400 375 400 λ emission (nm) (b) 900 n.d.: Not determined. Relative Intensity (C)/t1/2 (h) 600 0 300 Table 2. Half-life times of native and dextran-modified PheDH at different temperatures. Temperature 900 600 300 0 300 325 350 λemission (nm) indicating an enhancement in its thermal stability (Table 2). The thermostabilization effect for dextran-modified PheDH was especially noticeable Fig. 5. Fluorescence emission spectra of native (a) and dextran-modified PheDH (b) before (——) and after (ÆÆÆÆÆÆÆÆ) 1 h incubation at 55C. 1316 nIcreased light scattering (%) In order to prove these hypotheses, the fluorescence spectra of native and modified protein were recorded at 25 C and after 1 h incubation at 55 C (Figure 5). The fluorescence spectra of both native and modified PheDH upon excitation at 280 nm showed an identical emission maximum at 313 nm, which is characteristic of tryptophan residues buried into the hydrophobic protein core. However, thermal treatment at 55 C resulted in the unfolding of non-modified enzyme, as evidenced by the decrease in the fluorescence intensity and the appearance of a secondary band, shifted to the red zone of the spectra. On the contrary, dextran-modified enzyme showed smaller decrease in the fluorescence intensity after identical heat treatment, indicating that a more compact protein structure is formed after glycosidation of PheDH with monoactivated dextran. Figure 6 shows the influence of heat treatment at 55 C on the light scattering intensity of native and modified enzymes. Increased light scattering was observed for both enzyme forms after incubation at this temperature, indicating the occurrence of intermolecular aggregation processes in the thermal inactivation mechanism of this protein. However, glycosidation of PheDH with dextran resulted in the reduction of intermolecular associations as evidenced by reduced light scattering. This result suggests that the hydrophilic polysaccharide moieties prevented inactivation of PheDH due to aggregation processes when is incubated at elevated temperatures. In this work PheDH was chemically glycosidated with an end-group aminated dextran. This modification resulted in a noticeable improvement of the conformational and thermal stability properties of this oxido-reductase. The influence of protein aggregation processes on the inactivation mechanism of PheDH at elevated temperature was also determined, as well as the reduction of this phenomenon after attachment of the polysaccharide. Attending to these results, we suggest the covalent glycosidation of PheDH with end-group aminated dextran as a useful method for improving its resistance to heat inactivation. Acknowledgements This research was supported by grants from The Japan Society for the Promotion of Sciences to R. Villalonga and Y. Asano (Grant S-04257), and from Toyama Medical-Bio Cluster (The Ministry of Education, Culture, Sports, Science and Technology, Japan) to Y. Asano and S. Tachibana. Dextran derivative was synthesized in Matanzas University, Cuba, and the modification of PheDH and its properties were investigated in Toyama Prefectural University, Japan. Financial support to R. Villalonga from the International Foundation for Science, Stockholm, Sweden, and the Organisation for the Prohibition of Chemical Weapons, The Hague, The Netherlands (Grant F/3004-1) is also acknowledged. 180 References 135 90 45 0 0 30 60 90 120 Time of incubation at 55°C (min) Fig. 6. Influence of time of incubation at 55 C on light scattering at 400 nm of native (s) and dextran-modified PheDH (d). Asano Y (1999) Phenylalanine dehydrogenase. In: Flickinger MC & Drew SW eds. Encyclopedia of Bioprocess Technology: Fermentation, Biocatalysis and Bioseparation, New York: John Wiley & Sons, Inc, pp. 1955–1963. Asano Y, Yamada A, Kato K, Yamaguchi K, Hibino Y, Hirai K, Kondo K (1990) Enantioselective synthesis of (S)-amino acids by phenylalanine dehydrogenase from Bacillus sphaericus: use of natural and recombinant enzymes. J. Org. Chem. 55: 5567– 5571. Asano Y, Yamada A, Kato Y, Yamaguchi K, Hibino Y, Hirai K, Kondo K (1987) Phenylalanine dehydrogenase of Bacillus badius. Purification, characterization and gene cloning. Eur. J. Biochem. 168: 153–159. Bruneel D, Schacht E (1995) End group modification of pullulan. Polymer 36: 169–172. 1317 Cao R, Fragoso A, Almiral E, Villalonga R (2003) Supramolecular chemistry of cyclodextrins in Cuba. Supramol. Chem. 15: 161–170. Darias R, Villalonga R (2001) Functional stabilization of cellulase by covalent modification with chitosan. J. Chem. Technol. Biotechnol. 76: 489–493. Dubois MK, Gilles A, Hamilton JK, Rebers PA, Smith F (1956) Colorimetric method for determination of sugars and related substances. Anal. Chem. 28: 350–356. Fernández M, Fragoso A, Cao R, Baños M, Ansorge-Schumacher M, Hartmeier W, Villalonga R (2004) Functional properties and application in peptide synthesis of trypsin modified with cyclodextrin-containing dicarboxylic acids. J. Mol. Catalysis B. Enzymatic 31: 47–52. Gómez L, Villalonga R (2000) Functional stabilization of invertase by covalent modification with pectin. Biotechnol. Lett. 22: 1191–1195. Mehvar R (2000) Dextrans for targeted and sustained delivery of therapeutic and imaging agents. J. Control. Release 69: 1–25. Sadana A, Henley JP (1987) Single-step unimolecular non-firstorder enzyme deactivation. Biotechnol. Bioeng. 30: 717–723. Srivastava RAK (1991) Studies on stabilization of amylase by covalent coupling to soluble polysaccharides. Enzyme Microb. Technol. 13: 164–170. Venkatesh R, Sundaram PV (1998) Modulation of stability properties of bovine trypsin after in vitro structural changes with a variety of chemical modifiers. Protein Eng. 11: 691–698. Veronese FM, Caliceti P, Schiavon O, Sergi M (2002) Polyethylene glycol-superoxide dismutase, a conjugate in search of exploitation. Adv. Drug Deliv. Rev. 54: 587–606. Villalonga R, Fernández M, Fragoso A, Cao R, Di Pierro P, Mariniello L, Porta R (2003) Transglutaminase-catalyzed synthesis of trypsin-cyclodextrin conjugates. Kinetics and stability properties. Biotechnol. Bioeng. 81: 732–737. Ó Springer 2005 Biotechnology Letters (2005) 27: 1319–1323 DOI 10.1007/s10529-005-0477-y Production of fungal biomass immobilized loofa sponge (FBILS)-discs for the removal of heavy metal ions and chlorinated compounds from aqueous solution M. Iqbal1, A. Saeed1, R.G.J. Edyvean2, B. O’Sullivan2 & P. Styring2 1 Environment Biotechnology Group, Biotechnology and Food Research Centre, PCSIR Laboratories Complex, 54600, Lahore, Pakistan 2 Department of Chemical and Process Engineering, University of Sheffield, S1 3JD, Sheffield, UK Received 10 June 2005; Revisions requested 10 June 2005; Revisions received 23 June 2005; Accepted 28 June 2005 Key words: cadmium, 4-chloroanisole, fungal immobilization, loofa sponge, metal biosorption Phanerochaete chrysosporium Abstract A white rot basidiomycete, Phanerochaete chrysosporium, was immobilized on loofa sponge (FBILS) discs. It removed ca. 37 and 71 mg Cd (II) g)1 from 50 and 200 mg l)1 aqueous solutions and up to 89% of 4-chloroanisole from a 10 mg l)1 aqueous solution. FBILS are physically strong and chemically recalcitrant, resisting temperature, mechanical agitation, and variations in pH without alteration to shape, structure or texture. Introduction Pollution in water supplies and in waste-water discharge is a cause of increasing legislative and public concern. In many countries, industry is required to meet ever higher quality standards and has a need for improved, and environmentally sound, waste treatment methodologies for the removal of toxic chemicals from effluents. The use of biomass as biosorbents for pollutants offers an environmentally sound and potentially low cost alternative to existing technologies. Fungal biomasses have high affinities for toxic metals (Kratochvil & Volesky 1998) and organic chemicals (Perez et al. 1997, Reddy et al. 1998) in aqueous solution. Commercial application of such biomass has been hindered by problems associated mainly with physical manipulation (McHale & McHale 1994). Low mechanical strength and fragmentation of the biomass can cause difficulties in the contacting and separation of the effluent and biomass and this limits process design. Immobilization technologies have been suggested to overcome these problems (Trujillo et al. 1995, Aloysius et al. 1999). Immobilization of microbial biomass in polymeric gel matrices is the most extensively studied method (Leenen et al. 1996, Arica et al. 2001). However, production of large amounts of gel beads needed for commercial applications is expensive and requires specialist equipment. Furthermore, the use of such polymeric matrices results in closed structures with restrictive diffusion and low mechanical strength (Hu & Reeves 1997). The ideal immobilization matrix is strong and resistant and has an open structure. The plantderived Loofa sponge is an inexpensive and easily available biological, and therefore renewable, matrix produced in most tropical and subtropical countries. The sponge is made up of interconnecting voids with an open network of fibrous support giving the potential for rapid contact of immobilized cells to the surrounding aqueous medium. Merits of the loofa biomatrix system include freedom from materials that might be toxic 1320 to microbial cells, simple application and operation technique, and high stability during longterm repeated use. The white rot basidiomycete, Phanerochaete chrysosporium, was chosen for this study as it has a known affinity for metal ions but this is the first report on the immobilization of P. chrysosporium on a biomatrix for the bioremediation of both inorganic and organic pollutants from aqueous solution. While the mechanisms for inorganic and organic removal are likely to be different, the inclusion of cadmium sorption experiments ensures continuity with previous work on biosorbents and to test the hypothesis that this form of immobilization does not affect metal uptake, and therefore surface reactivity of the fungal hyphae. Materials and methods Microorganism and culture medium The white-rot basidiomycete, Phanerochaete chrysosporium ATTC 24725, was grown on (g l)1 distilled water); D-glucose, 10; KH2PO4, 2; MgSO4 Æ 7H2O, 0.5; NH4Cl, 0.1; CaCl2 Æ H2O, 0.1; thiamine, 0.001; at pH 4.5. Immobilizing materials and production of FBILS-discs Loofa sponge for use as an immobilization matrix was obtained from the ripened dried fruit of Luffa cylindrica. The loofa was cut into discs of approximately 2.5 cm diam. and 2–3 mm thick, soaked in boiling water for 30 min, thoroughly washed under tap water and left for 24 h in distilled water, changed 3–4 times. The discs were then oven dried at 70 °C and stored in a desiccator. A mycelium suspension of P. chrysosporium, 0.5 ml, was inoculated in 100 ml of autoclaved growth medium containing four pre-weighed loofa sponge discs in 250 ml Erlenmeyer flasks. Flasks, with no loofa sponge discs in the medium, were inoculated to provide free fungal biomass controls. The inoculated flasks were shaken at 100 rpm at 34 °C. After 8 days, both free and loofa immobilized biomass of P. chrysosporium (hereafter called FBILS – Fungal biomass immobilized loofa sponge) were harvested from the medium, washed twice with distilled water and stored at 4 °C until use. The dry weight of the fungal biomass was determined by weighing oven dried (70 °C overnight) sponge discs before and after fungal growth. Results and discussion Properties of loofa sponge The successful use of immobilized biosorbents requires that the immobilization matrix provides a high surface contact area and is stable to adverse chemical and physical treatments. Neither autoclaving (10 times for 20 min), nor pH (2.0–12 for 24 days) produced any change in the shape and structure of the sponge. Table 1 shows the lowest and highest values of physical parameters of loofa sponge discs. These results indicate that loofa sponge discs can be repeatedly reused in adverse conditions. Production and properties of FBILS biosorbent Microscopic examination shows hyphal growth in the sponge matrix within 24 h of incubation. Complete coverage of the sponge disc with the hyphae of P. chrysosporium occurs within 5 days (Figure 1a–c) and growth continues until the attainment of stationary phase at day 7. While the immobilized hyphal biomass is packed tightly within the sponge there remain large numbers of micro-channels for free movement of solute during the biosorption process (Figure 1c). In contrast, the free hyphal growth was compact and pelleted. At day 8, immobilized P. chrysosporium had a 21% increase in biomass over the freely growing control with biomass levels reaching 1900 mg l)1. Such an increase is unusual in immobilized systems. Table 1. Some physical characteristics of loofa (Luffa cylindrica) sponge. Physical properties Structural nature Porosity (%) Density (g/cm3) Specific pore volume (cm3/g) Fibrous network 85–95 0.018–0.05 26–34 1321 growth medium containing the inexpensive sponge discs without any prior chemical treatment. Metal removal studies Figure 2 shows the efficiency of the removal of Cd (II) from solution by FBILS, free fungal biomass and loofa sponge control. While other authors have reported reductions in metal ion Fig. 1. Immobilization of Phanerochaete chrysosporium within loofa sponge discs: (a) loofa sponge disc; (b) loofa sponge disc covered with P. chrysosporium hyphal biomass; (c) scanning electron micrographs of immobilized P. chrysosporium showing micro-channel and void volume for free solute movement. White scale bars at bottom of micrograph = 10 lm. No change in the shape, size or weight of FBILS was observed during exposure to various pH in the range 2–12 and were stable when exposed to acid (HCl), alkali (NaOH) and salt (NaCl) solutions for 5 days. FBILS retain 99% of the immobilized biomass within the loofa sponge when shaken for 7 days at 150 rpm in distilled water. In contrast to the results for FBILS, significant cell leakage has been reported to occur during biosorption from systems immobilized using polymer gel systems (Hu & Reeves 1997). These results show that, in contrast to the polymer gel immobilization method which requires more sophisticated equipment involving high costs, the more robust FBILS system can be made simply by adding the microbial cell/hyphal/spore suspensions to a Fig. 2. Biosorption of Cd (II) from (a) 50 mg l)1 and (b) 200 mg l)1 solutions by free or immobilized Phanerochaete chrysosporium. Cd (II) solutions were prepared from Cd(NO3)2 and adjusted to pH 5 using 0.1 M NaOH. Fresh dilutions were used for each experiment. Hundred milligram of free or immobilized (FBILS-discs) fungal biomass was contacted with 100 ml Cd (II) solution in 250 ml flasks shaken at 100 rpm at 20 ± 2 °C. Free fungal biomass was separated by centrifugation at 3500 g for 5 min, whereas FBILS-discs were separated by simple decantation. Residual concentrations of Cd (II) in the supernatant were determined using an atomic absorption spectrophotometer. Metal-free and fungal biomass-free solutions were used as controls. Statistical analysis of the data was carried out according to the Duncan’s new multiple range test (Steel & Torrie 1996). 1322 uptake when biomass is immobilized, these results show that this form of immobilization does not affect metal uptake capacity of the fungal hyphae. Mahan and Holcombe (1992) reported a 40% reduction in the sorption of Pb (II) when Stichococcus bacillaris was immobilized on silica gel and Lopez et al. (2002) report a 60% decrease in metal sorption by Pseudomonas fluorescens cells immobilized in agar beads, both in comparison with free cells. The statistically significant lower uptake of Cd (II) by free hyphal biomass found in this work may be due to a reduction in the surface area available for sorption due to hyphal aggregation and pelletization. Such reductions due to aggregation have been found for yeast cells as well as fungal hyphae (de Rome & Gadd 1987, Plette et al. 1996, Aloysius et al. 1999). The findings presented here indicate no diffusional limitations and demonstrate that FBILS are better suited for biosorption and other reactions than either free hyphal biomass or polymeric gel immobilization. From 50 mg l)1 metal solution uptake reached 36.8 ± 0.7 mg g)1 fungal biomass for FBILS but only 29.7 ± 0.9 mg g)1 free fungal biomass. For 200 mg l)1 metal solution, uptake reached 71.3 ± 1.3 mg g)1 fungal biomass for FBILS but only 59.9 ± 1.5 mg g)1 free fungal biomass. From isotherm studies the maximum uptake levels are 75.9 ± 1.7 mg g)1 for FBILS and 63.7 ± 1.5 mg g)1 for free fungal biomass from Cd (II) concentrations of 250 mg l)1 and above. Chlorinated aromatic organic compound removal studies Chlorinated aromatic organic compounds pose severe environmental and health hazards. In particular, methods for the removal of poly-chlorinated dioxins and dibenzofurans are of widespread interest. Because of the hazardous properties of these materials, 4-chloroanisole in aqueous solution was chosen as a model compound as it can be regarded as being structurally similar to half a dichlorodioxin molecule (Figure 3). After 7 days, contact at 34 °C, FBILS removed 84%, 78% and 69% of 4-chloroanisole from a 5, 10 and 20 mg l)1 aqueous solutions (Table 2). No removal was detected in the 4-chloroanisole control using untreated loofa sponge. Hundred percent of 4-chloroanisole was Fig. 3. Structures of 4-chloroanisole (1) and dichlorodioxin (2). Table 2. Removal of different concentrations of 4-chloroanisole by fungus biomass immobilized in loofa sponge (FBILS) discs after 7 days. 4-chloroanisole, initial concentration (mg l)1) 4-chloroanisole removed (mg g)1 FBILS disc) 5 10 20 14.1 ± 0.9 25.4 ± 1.2 45.8 ± 2.8 Fig. 4. Effect of contact time on the removal of 4-chloroanisole from aqueous solution. FBILS-discs were shaken at 100 rpm for 10 days in an aqueous solution of 10 mg l)1 4 chloroanisole at 35 °C. This concentration (and the others used) is well below the maximum solubility of 4-chloroanisole in water (237 mg l)1, Lun et al. 1995). FBILS were removed after different periods of contact by simple decantation. Hundred millilitre of the decanted culture medium was mixed with an equal volume of diethyl ether in a separating funnel. The organic layer was removed, reduced to 10% volume and analysed for 4-chloroanisole by GC using a WCOT (Wall Coated Open Tubular) fused silica capillary column, 30 m 0.25 mm ID. Concentrations of 4-chloroanisole were determined against calibration standards using accurately obtained solutions of the organic material in diethyl ether. Dry weight of fungal biomass was determined after drying in an oven at 70 °C overnight. removed from 250 ml of 10 mg solution in 8 days (Figure 4). There was no evidence in the chromatograms for the presence of aromatic deg- 1323 radation intermediates such as anisole or phenols, however, the control studies show that this removal does not occur by an adsorption process. It is known that P. chrysosporium will degrade the aromatic ring structure of chlorinated aromatic compounds to carboxylic acids and carbon dioxide (Valli et al. 1992), so this is the likely pathway. Such compounds would not be detected using the current experimental technique. These results clearly demonstrated the ability of FBILS to remove the chlorinated organic compound from aqueous solution. Furthermore, the absence of aromatic degradation products demonstrates added value in the process, as degrading chlorodioxins simply to dioxins would only lead to a small decrease in toxicity. Degradation of the whole structure to carboxylic acids represents a much cleaner overall remediation process. Conclusions Loofa sponge is an effective immobilization matrix for the entrapment of fungal hyphae to produce the fungal biomass immobilized loofa sponge (FBILS). FBILS have a high capacity to remove both the toxic metal and chlorinated organic compounds from aqueous solution. High bioremoval capacity, good mechanical strength, ease of handling, high porosity and low cost availability of the immobilization matrix are features which lend this system to practical applications for the removal of metals and chlorinated aromatic compounds from industrial effluents. References Aloysius R, Karim MIA, Ariff AB (1999) The mechanism of cadmium removal from aqueous solution by nonmetabolizing free and immobilized live biomass of Rhizopus oligosporus. World J. Microbiol. Biotechnol. 15: 571–578. Arica MY, Kacar Y, Gene O (2001) Entrapment of white rot fungus Trametes versicolor in ca-alginate beads: preparation and biosorption kinetic analysis for cadmium removal from aqueous solution. Bioresource Technol. 80: 121–129. de Rome L, Gadd GM (1987) Copper adsorption by Rhizopus arrhizus, Cladosporium resinae and Penicillium italicum. Appl. Microbiol. Biotechnol. 26: 84–90. Hu MZC, Reeves M (1997) Biosorption of uranium by Pseudomonas aeruginosa strain CUS immobilized in a novel matrix. Biotechnol. Prog. 13: 60–70. Kratochvil D, Volesky B (1998) Advances in the biosorption of heavy metals. Trends Biotechnol. 16: 291–302. Leenen EJTM, Dos Santos VAPM, Grolle KCF, Tramper J, Wijffels RH (1996) Characteristics of and selection criteria for cell immobilization in wastewater treatment. Water Res. 30: 2985–2996. Lopez A, Lazaro N, Morales S, Marques AM (2002) Nickel biosorption by free and immobilized cells of Pseudomonas fluorescens 4F39: a comparative study. Water Air Soil Poll. 135: 157–172. Lun R, Shiu WY, Mackay D (1995) Aqueous solubilities and octanol water partition coefficients of chloroveratroles and chloroanisoles. J. Chem. Eng. Data 40: 959–962. Mahan CA, Holcombe JA (1992) Immobilization of algae cells on silica gel and their characterization for trace metal preconcentration. Anal. Chem. 64: 1933–1939. McHale AP, McHale S (1994) Microbial biosorption of metals: potential in the treatment of metal pollution. Biotechnol. Adv. 12: 647–652. Perez RR, Benito GG, Miranda MP (1997) Chlorophenol degradation by Phanerochaete chrysosporium. Bioresource Technol. 60: 207–213. Plette ACC, Benedetti MF, Riemsdjik WH (1996) Competitive binding of protons, calcium, cadmium and zinc to isolated cell walls of a gram-positive soil bacterium. Environ. Sci. Technol. 30: 1902–1910. Reddy GVB, Gelpke MDS, Gold MH (1998) Degradation of 2,4,6-trichlorophenol by Phanerochaete chrysosporium: involvement of reductive dechlorination. J. Bacteriol. 180: 5159–5164. Steel RGD, Torrie JH (1996) Principles and Procedures of Statistics: A Biometrical Approach, 3New York:McGrawHill. Trujillo EM, Sprinti M, Zhuang H (1995) Immobilized biomass: a new class of heavy metal ion exchangers. In: Senguptal AK, ed. Ion Exchange Technology: Advances in Pollution Control, Pennsylvania: Technomic Publishing Company Inc, pp. 225–271. Valli K, Wariishi H, Gold MH (1992) Degradation of 2,7dichlorodibenzo-p-dioxin by the lignin-degrading basidomycete Phanerochaete chrysosporium. J. Bacteriol. 174: 2131–2137. Ó Springer 2005 Biotechnology Letters (2005) 27: 1325–1328 DOI 10.1007/s10529-005-0480-3 A metal ion as a cofactor attenuates substrate inhibition in the enzymatic production of a high concentration of D-glutamate using N-acyl-D-glutamate amidohydrolase Kazuaki Yoshimune, Ai Hirayama & Mitsuaki Moriguchi* Department of Applied Chemistry, Faculty of Engineering, Oita University, Dannoharu 700, 870-1192, Oita, Japan *Author for correspondence (Fax: +81-97-554-7890; E-mail: [email protected]) Received 5 May 2005; Revisions requested 2 June 2005; Revisions received 27 June 2005; Accepted 27 June 2005 Key words: D-aminoacylase, D-aspartate, D-glutamate production, N-acyl-D-aspartate amidohydrolase, Nacyl-D-glutamate amidohydrolase Abstract N-Acyl-D-glutamate amidohydrolase (D-AGase) was inhibited by 94 % when 1 mol/l N-acetyl-DLglutamate was used as a substrate. The addition of 1 mM Co2+ stabilized D-AGase. Moreover, the substrate inhibition was weakened to 88% with the addition of 0.4 mM Co2+ to the reaction mixture. Although 2+ D-AGase is a zinc-metalloenzyme, the addition of Zn from 0.01 to 10 mM did not increase the D-glutamic acid production in the saturated substrate. Under optimal conditions, 0.38 M D-glutamic acid was obtained from N-acyl-DL-glutamate with 100% of the theoretical yield after 48 h. Introduction N-Acyl-D-amino acid amidohydrolases catalyze the hydrolysis of N-acyl derivatives of various Damino acids to D-amino acids and fatty acids and can be used to resolve DL-amino acids. They are divided into three types according to their substrate specificities. D-Aminoacylase (D-ANase) acts on N-acyl derivatives of various neutral Damino acids. D-ANase from Alcaligenes xylosoxydans subsp. xylosoxydans A-6 (Alcaligenes A-6) has been applied as a commercial enzyme (D-aminoacylase ‘‘Amano’’) for the optical resolution production of neutral D-amino acids (Wakayama et al. 2003). N-Acyl-D-glutamate amidohydrolase (D-AGase) and N-acyl-D-aspartate amidohydrolase (D-AAase) are specific for N-acyl-D-glutamate and N-acyl-D-aspartate, respectively (Wakayama & Moriguchi 2001). The D-ANase of Alcaligenes A-6 contains 2.3 g atom Zn2+ per mol (Wakayama et al. 2000). However, the activity is inhibited by 92% by 1 mM Zn2+ (Moriguchi et al. 1993b). Lai et al. (2004) reported that a large excess of Zn2+ strongly inhibits D-ANase of Alcaligenes faecalis DA1 because it changes the conformation of its active center. D-AGase of Pseudomonas sp. strain 5f-1 is zinc-metalloenzyme, and the activity is inhibited by 47% by 2 mM Zn2+ (Wakayama et al. 1995b). The activity of D-AAase from Alcaligenes A-6 is also inhibited by 73% by 2 mM Zn2+ (Moriguchi et al. 1993a). These inhibitions may be of the same manner as that of 2+ D-ANase of Alcaligenes faecalis DA1. Co can 2+ often substitute for Zn to restore the activity of the apo-form of the zinc-metalloenzyme (Vallee & Galdes 1984). Moreover, D-AGase of Pseudomonas sp. strain 5f-1 is stabilized by Co2+ (Wakayama et al. 1995b). Although D-AGase is inhibited by Zn2+, Co2+ has no inhibitory effect on the enzyme at the concentration that stabilizes the enzyme (Wakayama et al. 1995b). Thus, 1326 Co2+ can be a useful additive for stabilizing zinc-metalloenzymes, such as D-AGase. In industrial productions using enzymes, high concentrations of substrate are often reacted for a long time to increase the production yield and recovery of the product. Thus, industrial enzymes are required to have a high activity and stability in the presence of high concentrations of its substrate and product. Previously, we reported that the production levels of D-AGase of Alcaligenes A-6 in Escherichia coli are increased by the coexpression of molecular chaperones (Yoshimune et al. 2004). Despite the increasing activity of DAGase, the enzyme is unable to produce a high concentration of D-glutamic acid in a high yield. This may be due to the substrate inhibition and stability of D-AGase in the presence of high concentrations of its substrate. Here we report how to remove substrate inhibition in an industrial production using an enzyme. Materials and methods Materials Plasmid pKGSD2 encoding D-AGase (Yoshimune et al. 2004) and plasmid pETAD1 encoding D-AAase (Wakayama et al. 1995c) were prepared as described previously. N-AcetylDL-glutamate and N-acetyl-DL-aspartate were purchased from Sigma. All other chemicals were from Wako Pure Chemicals. Enzyme preparation The recombinant D-AGase or D-AAase was overproduced in E. coli using pKGSD2 or pETAD1, respectively, as previously described (Wakayama et al. 1995c; Yoshimune et al. 2004). E. coli in 10 mM potassium phosphate buffer (pH 7.0) was disrupted by sonication, and cell debris was removed by centrifugation. The supernatant obtained was used as the enzyme solution. Assay of enzyme activity The activities of D-AGase and D-AAase were assayed by measuring the D-amino acid formed. The reaction mixture (0.2 ml) contained 100 mM potassium phosphate buffer (pH 7.0), 40 mM Nacetyl-DL-amino acid and enzyme (10 ll). After incubation at 30 °C for 10 min, the reaction was stopped by adding 0.1 ml 0.25 M NaOH. The Damino acid formed was measured by the 2,4,6trinitrobenzenesulfonic acid (TNBS) method (Fields 1972). One unit of the enzyme was defined as the amount of enzyme that catalyzed the formation of 1 lmol D-amino acid per min. Using substrates above 0.1 M, reaction mixtures were adjusted to pH 8.5 with 25% (w/v) NaHCO3. After incubation at 30 °C for 1 h, the reaction was stopped by boiling for 3 min. The insoluble substrate and product were dissolved with the addition of water. The concentration of the D-amino acid in the solution was determined by the TNBS method. Determination of the concentration of product and substrate The D-amino acid concentrations were determined by the TNBS method. For the determination of the concentration of N-acetyl-DL-amino acid, the acid was hydrolyzed by the corresponding N-acyl-D-amino acid amidohydrolase, and the D-amino acid produced was measured with the TNBS method. The concentration of saturated N-acetyl-DL-amino acid was defined as the concentration in the supernatant of a solution containing 1.5 M N-acetyl-DL-amino acid and 25% (w/v) NaHCO3 at 30 °C. The solubility of the N-acetyl-DL-amino acids was increased by neutralization with sodium hydrogencarbonate. The solubility of N-acetyl-DL-glutamate or Nacetyl-DL-aspartate in 25% (w/v) NaHCO3 was about 0.96 or 0.65 M, respectively. Results and discussion Effects of the substrate concentrations on the activities of N-acyl-D-amino acid amidohydrolases The activities of D-AGase and D-AAase were inhibited by 83% and 94 %, respectively, with 1 M N-acetyl-DL-amino acids. On the other hand, the activities of D-AGase and D-AAase were unaffected by their products, 0.4 M D-glutamic 1327 acid and 0.4 M D-aspartic acid, respectively, in the presence of 1 M N-acetyl-DL-amino acids. These results suggest that product inhibition did not take place and the productivities of D-glutamic and D-aspartic acids increase by the attenuation of substrate inhibition. Effect of Co2+ on the production of D-glutamic acid in the saturated substrate Figure 1 shows the effect of Co2+ on the production of D-glutamic acid. Its productivity was increased more than three times by 1 mM Co2+ in 1.25 M N-acetyl-DL-glutamate. In the absence of Co2+, D-glutamate was not produced after 3 h. On the other hand, a small increase of D-glutamate was observed from 3 h through 24 h in the presence of Co2+ (data not shown). The increase of production level were considered probable cause of the stabilization by Co2+. D-AGase was stabilized by Co2+ at 30 °C (Table 1) but not at 40 °C (data not shown). Co2+ might slightly change the conformation of D-AGase to stabilize it at 30 °C. Activity of D-AGase was doubled by 0.4 mM Co2+ with 0.96 M N-acetyl-DL-glutamate (data not shown). However, the D-AGase activity was not affected by 0.4 mM Co2+ when 40 mM N-acetyl-DL-glutamate was used as a substrate concentration (standard assay condition; data not shown). Co2+ might change the conformation of the active center of D-AGase to weaken the inhibition of the substrate. Although D-AGase is considered to be a zinc-metalloenzyme (Wakayama et al. 1995a), Zn2+ did not affect the production of D-glutamic acid in the saturated substrate (data not shown). The production level of D-glutamate was not increased by 1 mM Mg2+, Mn2+, Fe2+, Fe3+, Ni2+, Cu2+ or Ba2+ (data not shown). Zn2+ of zinc-metallo enzyme can be often replaced by Co2+ or Mn2+. Furthermore, L-aminoacylase (Toogood et al. 2002) and thermolysin (Holland et al. 1995) are acti- Fig. 1. Effect of Co2+ on the production of D-glutamic acid. A reaction mixture containing 1.25 M N-acetyl-DL-glutamate, 25% (w/v) NaHCO3, 125 mM potassium phosphate buffer (pH 7.0), and 2 U/ml D-AGase was incubated with various concentrations of Co2+ for 24 h at 30 °C. The reaction was stopped by boiling for 3 min. vated by Co2+. Co2+ can be a useful additive for activating and stabilizing zinc-metallo enzymes. Neither Co2+ nor Zn2+ increased the production level of D-aspartic acid by D-AAase in the saturated substrate. D-Amino acid production by N-acyl-D-amino acid amidohydrolases Figure 2 shows the time course of the production of D-glutamic acid with the use of D-AGase in 1 mM Co2+ and 0.77 M N-acetyl-DL-glutamate. Only 20% of theoretical yield was obtained up to approximately 14 h of the reaction, probably because of the substrate inhibition. After 20 h of the reaction, the amount of D-glutamic acid rapidly increased due to the lower concentration of the substrate. Under the same condition, D- Table 1. Effect of various metal ions on the stability of D-AGase. Metal ion No addition Concentration (mM) Residual activity (%) 46 Mg2+ Mn2+ Fe2+ Fe3+ Co2+ 1 1 1 1 0.2 1 2 49 0 2.4 9.7 42 98 62 Ni2+ Cu2+ Zn2+ Ba2+ 4 1 1 1 1 31 1.4 0 52 43 The enzyme solutions containing 100 mM potassium phosphate buffer (pH 7.0) and 2 U D-AGase/ml in the presence of various metal ions were incubated at 30 °C for 12 h. The residual D-AGase activities were measured. 1328 oretical yield in this condition. Further studies will be required to understand the mechanisms of Co2+ action on D-AGase. References Fig. 2. Time course of D-glutamic acid production. A reaction mixture containing 0.77 M N-acetyl-DL-glutamate, 0.2 g/ml sodium hydrogencarbonate, a 380 mM potassium phosphate buffer (pH 7.0), 1 mM Co2+, and 2 U D-AGase was incubated at 30 °C. Fig. 3. Time course of D-aspartic acid production. A reaction mixture containing 0.77 M N-acetyl-DL-aspartate, 0.2 g/NaHCO3/ml and 380 mM potassium phosphate buffer (pH 7.0), and 2 U D-AAase was incubated at 30 °C. aspartic acid was produced at 70% of the theoretical yield for 48 h (Figure 3). A slight increase in D-aspartic acid was observed after 24 h of the reaction, probably due to the inactivation of the enzyme. D-AAase must be stabilized for the production of D-aspartic acid with 100 % of the the- Fields R (1972) The rapid determination of amino groups with TNBS. Method Enzymol. 25: 464–468. Holland DR, Hausrath AC, Juers D, Matthews BW (1995) Structural analysis of zinc substitutions in the active site of thermolysin. Protein Sci. 4: 1955–1965. Lai WL, Chou LY, Ting CY, Kirby R, Tsai YC, Wang AHJ, Liaw SH (2004) The functional role of the binuclear metal center in D-aminoacylase. J. Biol. Chem. 279: 13962– 13967. Moriguchi M, Sakai K, Katsuno Y, Maki T, Wakayama M (1993a) Purification and characterization of novel N-acyl-Daspartate amidohydrolase from Alcaligenes xylosoxydans subsp. xylosoxydans A-6. Biosci. Biotech. Biochem. 57: 1145– 1148. Moriguchi M, Sakai K, Miyamoto Y, Wakayama M (1993b) Production, purification, and characterization of D-aminoacylase from Alcaligenes xylosoxydans subsp. xylosoxydans A-6. Biosci. Biotech. Biochem. 57: 1149–1152. Toogood HS, Hollingsworth EJ, Brown RC, Taylor IN, Taylor SJC, McCague R, Littlechild JA (2002) A thermostable L-aminoacylase from Thermococcus litoralis: cloning, overexpression, characterization, and applications in biotransformations. Extremophiles 6: 111–122. Vallee BL, Galdes A (1984) The metallobiochemistry of zinc enzymes. Adv. Enzymol. Relat. Areas. Mol. Biol. 56: 283–430. Wakayama M, Ashika T, Miyamoto Y, Yoshikawa T, Sonoda Y, Sakai K, Moriguchi M (1995a) Primary structure of N-acyl-D-glutamate amidohydrolase from Alcaligenes xylosoxydans subsp. xylosoxydans A-6. J. Biochem. 118: 204–209. Wakayama M, Miura Y, Oshima K, Sakai K, Moriguchi M (1995b) Metal-characterization of N-acyl-D-glutamate amidohydrolase from Pseudomonas sp. strain 5f-1. Biosci. Biotech. Biochem. 59: 1489–1492. Wakayama M, Watanabe E, Takenaka Y, Miyamoto Y, Tau Y, Sakai K, Moriguchi M (1995c) Cloning, expression, and nucleotide sequence of the N-acyl-D-aspartate amidohydrolase gene from Alcaligenes xylosoxydans subsp. xylosoxydans A-6. J. Ferment. Bioeng. 80: 311–317. Wakayama M, Moriguchi M (2001) Comparative biochemistry of bacterial N-acyl-D-amino acid amidohydrolase. J. Mol. Catal. B: Enzym. 12: 15–25. Wakayama M, Yada H, Kanda S, Hayashi S, Yatsuda Y, Sakai K, Moriguchi M (2000) Role of conserved histidine residues in D-aminoacylase from Alcaligenes xylosoxydans subsp. xylosoxydans A-6. Biosci. Biotechnol. Biochem. 64: 1–8. Wakayama M, Yoshimune K, Hirose Y, Moriguchi M (2003) Production of D-amino acid amidohydrolase and its structure and function. J. Mol. Catal. B: Enzym. 23: 71–85. Yoshimune K, Ninomiya Y, Wakayama M, Moriguchi M (2004) Molecular chaperones facilitate the soluble expression of N-acyl-D-amino acid amidohydrolases in Escherichia coli. J. Ind. Microbiol. Biotechnol. 31: 421–426. Springer 2005 Biotechnology Letters (2005) 27: 1329--1334 DOI 10.1007/s10529-005-0482-1 Characterization of an extracellular serine protease gene from the nematophagous fungus Lecanicillium psalliotae Jinkui Yang1, Xiaowei Huang1, Baoyu Tian1, Hui Sun1, Junxin Duan2, Wenping Wu2 & Keqin Zhang1,* 1 Laboratory for Conservation and Utilization of Bio-resources, Yunnan University, 650091, Kunming, P. R. China 2 Research and Development Center of Novozymes in China, 100085, Beijing, P. R. China *Author for correspondence (Fax: +86-871-5034878; E-mail: [email protected]) Received 27 April 2005; Revisions requested 24 May 2005; Revisions received 27 June 2005; Accepted 29 June 2005 Key words: gene cloning, Lecanicillium psalliotae, serine protease, similarity comparison Abstract The gene encoding a cuticle-degrading serine protease was cloned from three isolates of Lecanicillium psalliotae (syn. Verticillium psalliotae) by 3¢ and 5¢ RACE (rapid amplification of cDNA ends) method. The gene encodes for 382 amino acids and the protein shares conserved motifs with subtilisin N and peptidase S8. Comparison of translated cDNA sequences of three isolates revealed one amino acid polymorphism at position 230. The deduced protease sequence shared high degree of similarities to other cuticle-degrading proteases from other nematophagous fungi. Introduction Extracellular enzymes are important virulence factors in nematophagous and entomophagous fungi (Segers et al. 1994, Tunlid et al. 1994, Bonants et al. 1995, Joshi et al. 1995). LopezLlorca (1990) isolated a serine protease P32 from Pochonia suchlasporia (syn. Verticillium suchlasporium) and found it was involved in egg penetration of nematode. Subsequently, two proteases, VCP1 and PIP, were isolated from nematophagous fungi Pochonia chlamydosporia (syn. Verticillium chlamydosporium) and Paeciliomyces lilacinus, respectively (Segers et al. 1994, Bonants et al. 1995). Similar extracellular proteases also had been found in entomophagous fungi (St Leger et al. 1992, Joshi et al. 1995). Moreover, collagenase and chitinase have been identified from nematophagous fungi Arthrobot- rys amerospora, Po. chlamydosporia and Po. suchlasporia (Schenck et al. 1980, Tikhonov et al. 2002). Lecanicillium psalliotae is a nematophagus fungus with commercial potential for the biocontrol of root knot and cyst nematodes. It produces an alkaline serine protease, Ver112, during infection of the saprophytic nematode Panagrellus redivivus. Ver112 had been purified from culture filtrates of L. psalliotae. The N-terminal amino acid sequence has been submitted to Swiss-Prot (accession number Q68GV9). In this report, we described the cloning of an alkaline serine protease from L. psalliotae by the 3¢ and 5¢ RACE method, the analysis of the primary amino acid sequence of protease Ver112 from three isolates, and comparison with other cuticledegrading serine proteases isolated from different nematophagous and entomopathogenic fungi. 1330 Materials and methods Microorganisms and culture conditions Three isolates (112, 602 and 608) of nematophagous fungus Lecanicillium psalliotae used in this study were originally isolated from field soil samples in Yunnan Province; strain 112 has been deposited in the China General Microbiological Culture Collection Center. Fungi were cultured in PD (potato/dextrose) medium at 26 C with shaking at 200 rpm for 3 days. Escherichia coli DH 5a was used in all DNA manipulations and grown in Luria--Bertani medium containing (per liter): 10 g tryptone, 10 g NaCl, 5 g yeast extract, and 16 g agar. Genomic DNA and total RNA extraction Mycelium were collected by filtration in a sterilized filter funnel and ground to a fine powder in liquid N2. DNA was extracted according to the method of Zhang et al. (1996). Total RNA extraction was done according to the manual of TRIzol Reagent (Invitrogen, America), and RNA was stored at )70 C. Amplification of 3¢ and 5¢ nucleotide sequence A partial cDNA of Ver112 was obtained by 3¢ RACE kit (Invitrogen, America) using a degenerate primer, SERP3-1 5¢-ACNCARCARCARGG NGCNAC-3¢, which was designed according to the N-terminal amino acid residues of the protease Ver112. The first strand cDNA and target cDNA were synthesized according to the manual of 3¢ RACE system for rapid amplification of cDNA ends. 5¢ RACE was conducted as described in the manual of 5¢ RACE system for rapid amplification of cDNA ends using two gene-specific primers derived from the 3¢ RACE product, R5-1 5¢-AGTCTTGGACTCCGATGGTG-3¢, and R52 5¢-TGGGAGATGCGAGTAAGTC -3¢. RACE, genomic DNA and the first strand of cDNA was used as template, respectively. Target DNA and cDNA were amplified by a touchdown program (Kim et al. 2003). The cDNA and genomic sequences were compared using the DNAman software package (Version 5.2.2, Lynnon Biosoft, Canada). Cloning and sequencing The PCR products were purified from a 1% agarose gel using a DNA fragment purification kit ver 2.0 (Takara, Japan) and subcloned into pGEM-T Vector (Promega, America). White colonies were randomly selected and purified using the plasmid DNA purification kit (Qiagen, German) and the plasmid DNA was sequenced using an ABI 3730 autosequencer (Perkin--Elmer, America) with four fluorescent dyes. The sequencing primers were T7 and SP6 universal primers (Takara, Japan). Sequence data were analyzed using DNAman software package. Sequence identity was compared with other cuticledegrading protease gene using the GenBank database. Sequence analysis Database searches were performed using BlastX (http://www.ncbi.nlm.nih.gov/BLAST). Signal sequence prediction was performed using Signal P (http://www.cbs.dtu.dk/services/ signalP) (Henrik et al. 1997). Multiple sequence alignments were performed using DNAman software package. Proteins were examined for conserved motifs using Pfam (http://pfam. wustl.edu/hmmsearch. shtml) (Garcia-Sanchez et al. 2004). N-linked glycosylation sites were predicted by NetNGlyc (http://www.cbs.dtu.dk/services/NetNGlyc/). Results Amplification of the Ver112 chromosomal gene and full-length cDNA Cloning of the cuticle-degrading serine protease Two gene-specific primers, FP 5¢-CTGATTATCAACAAGATGCGTC-3¢ and RP 5¢-TTACG TGGCGCCGTTGAAGGC-3¢, were designed according to the PCR fragments of 3¢ and 5¢ Under the conditions described above, a 500 bp PCR product (Figure 1) was successfully amplified by 5¢ RACE and sequencing indicated that the PCR fragment contained a putative start co- 1331 Fig. 1. Result of PCR amplification. Lanes 1, 2 and 4 -- result of 5¢ RACE amplification; lanes 3 and 5 -- DNA marker (Ladder 100 bp, Promega, America); lanes 6 and 9 -- PCR fragment amplified with genomic DNA as template; lanes 7, 8 and 10 -- PCR fragment amplified with the first strand of cDNA as template. don (ATG). One thousand one hundred and fifty and 1350 bp fragments (Figure 1) were amplified by using, respectively, the first strand of cDNA and genomic DNA as template from three isolates of L. psalliotae. These fragments were also cloned and sequenced. The combined nucleotide sequence for the partial DNA and cDNA were 1640 and 1440 bp, respectively. Sequence analysis The sequence of Ver112 comprised an ORF, which contained three introns and four exons. It encoded a polypeptide of 382 amino acid residues with a Mr of 39.654, which shared conserved motifs with subtilisin N and peptidase S8. Comparison of Ver112 with other serine proteases from nematophagous fungi revealed that it was typical of fungal serine proteases, which possessed a pre-pro-peptide structure. It has a signal peptide (15 amino acids) consisting of the initial methionine, a core of seven hydrophobic residues, a helix-breaking residue (proline), and four hydrophobic residues before a signal peptidase cleavage site (Ala-Leu-Ala). Comparison of the deduced amino acid sequence with the N-terminal sequence of Ver112 revealed that the mature protein started at residue 103, and the final residue of the pro-peptide was an asparagine (N), position in 102. Each intron began with GT and ended with AG, which was a common feature of fungal introns and had been observed in the serine protease gene from Acremonium chrysogenum (Isogai et al. 1991). The mature protein consisted of 280 amino acids. Comparison of the nucleotide sequences of Ver112 from three isolates of L. psalliotae re- vealed that they were very conservative, the nucleotide sequences from L. psalliotae 112 and 608 were identical, and there were four nucleotide residues different from L. psalliotae 602, two of them located at the second intron, and two other variable nucleotides located at different exons, which resulted in one amino acid polymorphism at position 230, arginine (A) changed to glycine (G). Like VCP1, Ver112 lacks any N-linked glycosylation site (Asn-X-Ser/Thr). These nucleotide sequences have been submitted to GenBank, under accession numbers AY 692148 (112 and 608) and AY870806 (602). Comparison of Ver112 with other serine proteases isolated from nematophagous and entomopathogenic fungi These cuticle-degrading proteases shared some similar biochemical properties of low molecular mass and being inhibited by PMSF (phenylmethylsulfonylfluoride) (Table 1). However, PII and Aozl isolated from nematode-trapping fungi A. oligospora had lower pI and higher molecular masses than other proteases from nematophagous and entomopathogenic fungi. The databank search showed that Ver112 shared extensive similarities to fungal members of the subtilisin family of serine proteases (Figure 2). The deduced amino acid sequence of the Ver112 showed 39.6%, 41.7%, 62.8%, 75.7%, 57.0%, 61% and 58.2% identity, respectively, to Aozl (Arthrobotrys oligospora), PII (A. oligospora), PIP (Pic. lilacinus), Pr1 (Beauveria bassiana), PrA (Metarhizium anisopliae), Prk (Tritirachium album), and VCP1 (Po. chlamydosporia). The signal peptide and pro-region cleav- 1332 Table 1. Partial characterization of cuticle-degrading serine proteases isolated from different nematophagous and entomopathogenic fungi. Protease PII Aozl VCPl P32 Ver112 PIP PrA Pr1 Fungus Arthrobotrys oligospora Arthrobotrys oligospora Pochonia chlamydosporia Pochonia suchlasporia Lecanicillium psalliotae Paecilomyces lilacinus Metarhizium anisopliae Beauveria bassiana Molecular mass (kDa) 35 38 33 32 32 33 25 32 Inhibitor of protease a PMSF PMSF, SSIb PMSF PMSF, pCMBc PMSF PMSF PMSF PMSF pI Reference 4.6 4.9 10.2 --10.2 10.2 10.0 Tunlid et al. (1994) Zhao et al. (2004) Segers et al. (1994) Lopez-Llorca LV (1990) GenBank (AAU01968) Bonants et al. (1995) St Leger et al. (1992) Joshi et al. (1995) a PMSF, phenylmethylsulfonylfluoride. SSI, Streptomyces subtilisin inhibitor. c pCMB, p-chloromercuric benzoic acid. b age sites of them were conserved and the first amino acid of mature proteases was alanine. They shared the conservation of the aspartic acid (Asp143)--histidine (His173)--serine (Ser328) (in Ver112) catalytic triad. The two blocks of sidechains that form the sides of the substrate-binding S1 pocket in subtilisin occur in regions of high similarity and consist of Ser236Leu237Gly238 and Ala262Ala263Gly264, respectively, in Ver112. Furthermore, the highly conserved Asn265 (in Ver112) is important in subtilisin for stabilization of the reaction intermediate formed during proteolysis (Kraut 1977). Discussion Extracellular serine proteases have been isolated, cloned and purified from several nematophagous and entomopathogenic fungi. From Table 1 and Figure 2, these cuticle-degrading serine proteases from different nematophagous and entomopathogenic fungi may be divided into two categories according to the difference of biochemical characterization and primary sequence. Class I is isolated from nematode-trapping fungi and has lower pI, and class II is isolated from nematode- parasitic or egg-parasitic fungi and has higher pI. However, whether the differences of biochemical characterization between classes II and I are important for the ability of the enzymes to degrade components of the nematode cuticle and eggshell, respectively, and whether the differences is connected to their mode of infection are currently not known. The high degree of similarities between extracellular serine proteases from different nematophagous and entomopathogenic fungi suggest that they may derive from a common ancestral subtilisin-like protease gene. Cloning of Ver112 provides a good foundation for future investigation of infection mechanism and improvement the pathogenicity of nematophagous and entomopathogenic fungi. Acknowledgement We are grateful to Dr. Dilantha Fernando in the University of Manitoba, Canada, and Dr. Li Haipeng in the Ludwig-Maximilians-Universität München, Germany, for their invaluable comments and revising the manuscript. The c Fig. 2. Alignment of subtilase amino acid sequences from Arthrobotrys oligospora (PII and Aozl), Paeciliomyces lilacinus (PIP), Beauveria bassiana (Pr1), Metarhizium anisopliae (PrA), Tritirachium album (Prk), Pochonia chlamydosporia (VCP1) and Lecanicillium psalliotae (Ver112). The GenBank accession numbers are CAA63841, AAM93666, AAA91584, AAK70804, CAB64346, P06873, CAD20578 and AAU01968, respectively. Areas shaded in black are conserved regions (100% similarity), areas shaded in gray are high degree similarity (more than 50% similarity) and unshaded areas are regions of variability between the proteases. , indicates Putative signal-sequence cleavage site; . indicates Proregion cleavage site. m indicates the aspartic acid (Asp143)--histidine (His173)-serine (Ser328) (in Ver112) catalytic triad. 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Mycologia 96: 16--22. Biotechnology Letters (2005) 27: 1335 DOI 10.1007/s10529-005-1074-9 Ó Springer 2005
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