E. LAIST, F. F. FRICK & R. S. OLIVER. PROCESS 0F PREPARING ALUMINA. APPLICATION FILED APR. l0, i918. Patented Apr. 15, 1919. LSOOAL?. www? wim mm e, d, .M i „â M .ï l. M MW? „y ,5î mßw , .m M „m .W , „Wm „.„f .w.m„ .w.c;.Wwfï«To.,w...E dma.._. œ w „ï“ w@ _ I aftoz #w114 sTATíEs PATE " oEEIoE. FREDERICK LAIsT, FREDERICK E. EEICK, AND ROBERT s. oLIvEn, 0E ANAcoNDA, _ MCNTANA, AssIGNoEs To ANACCNDA COPPER MINING COMPANY, or ANACoNDA, , MONTANA, A CoaronATIoN or MONTANA - - - _ PROCESS Í02E' PREPABING ALUMINA. Speciñcation of lLetters Patent. 1,300,417. Patented Apr. >15,191.9.> Application ñled April 10, 1918. Serial No. 227,722. To all 'whom it may concern: ‘ This is however merely a preferable Imode’ 55 Be it known that we, (1) FREDERICK LAIsT, of procedure: For example, the solution (2) FREDERICK _F. FRIox, and (3) ROBERTS. may be run into ponds or other- crystallizing OLIVER, citizens of the United States, resid system where the cooling will take place ing at Anaconda, in the county of Deerlodge slowly', in which case the crystals` will be and State of Montana,_have invented cer large in size. The crystals obtained by 'the 60 tain new and useful Improvements in Proc method first described are somewhat purer y esses of Preparing Alumina, of which the than (those obtained by the latter method." following is a specification. 10 This invention is a process applicable to If the iron in the original solution has been completely reduced to the ferrous state the preparation of commercially pure alu before the addition of‘potassium sulfate, the, mina, particularly from ’clays or equivalent resulting alum will be remarkably free from silicates of aluminum. Clay- is essentially a iron. This is highly important, especially ' in case the aluminum oxid eventually pro erally mixed with some quartz. Clay to be duced is to be used for the manufacturefof treated in accordance with this process metallic aluminum. By proceeding in the 70 more or less impure aluminum silicate, gen 15 should preferably be reasonably low in iron, manner first above described, we have suc calcium and magnesium. Potassium may or may not be present. 20 ` ' The process in its preferred embodiment does not exceed 0.10 per cent. The alum is now dried and ignited to'a 75 is cyclical in character, and is indicated in the accompanying drawing, which is a dia temperature approximating 1000° C. The gram in the form of a flow sheet >of the 25 ceeded in preparing L from@ ordinary clay aluminum oxid of which the iron content ignition is preferably carried on in a fur- ` process. The operation thus indicated is as nace similar to' a by-product coke oven, or follows : in an electric furnace; that is to say in suchThe clay is first mixed with concentrated type of furnace that fire gases do not become 80 sulfuric acid, and the mixture is heated to mixed with the gaseous products from the 30W-400o centigrade in order to decompose the aluminum silicate, as well as potassium 30 silicate, if present. This reaction results in the formation of aluminum and potassium sulfates, more or less sulfate of iron being likewise produced. The soluble sulfates are dioxid and oxygen, into sulfuric acid; and the production of sulfuric acid is much sim now extracted by means of hot water, or- a plerwhen the gases are relatively pure. ' Tt decomposition ofthe alum. This is forthe reason that the process contemplates the con version of such gaseous products of decom position, comprising sulfur trioxid, sulfur 85 solution of potassium sulfate, and any ferric is understood, however, that the ignition iron in ‘the resulting solution is reduced to may be carried on in oil >or gas-fired fur the ferrous state by means of metallic alu naces of any type. minum, metallic iron,‘sulfur dioxid, or fother We have found that under the preferred 'operating conditions approximately 2O per The solution which now contains essen cent. of the sulfuric acid combined with the appropriate reducing agent. 40 ‘ -È tially aluminum sulfate, ferrous sulfate, and aluminum is expelled in the form of sulfur 95 possibly potassium sulfate, is filtered from trioxid (S03) . This may be separated from ’ the residue which consists chiefly of silica. the mixture of sulfur dioxid and oxygen’ by The clear solution is mixed hot with suffi any appropriate method, such Aas electro cient potassium sulfate (unless this has been static precipitation, or absorption in con added to the leaching solution) to form centrated sulfuric acid. The sulfur dioxid potassium alum by reaction with all of the may likewise be converted into sulfuric acid aluminum sulfate contained in the solution. in accordance with _the well known methods. Preferably the solution is then cooled as The sulfuric acid thus produced is applied 50 rapidly as possible, and is stirred while cool to the treatment of a fresh batch of clay in .ing in orde-r that the resulting crystals'of a repetition of the process. The solid residue remaining after the ig potassium alum may be of small size, The precipitate formed under these conditions is nition of the alum is essentially a mixture of similar in appearance to granulated sugar. aluminum oxid and'potassium sulfate. This 45 100 105 1,300,417 2 miXture is leached with Water. The residue fates, and dissolving the saine; reducing any ferrie iron to the ferrous state; adding to the solution potassium sulfate in propor 55 tion to conyert the aluminum sulfate into consists of commercially pure aluminum oxid, and after drying is ready- for use in the production of metallic aluminum, or for any other purpose for which commercially pure aluminumI oXid is required. The solu tion of potassium sulfate is either used di potassium alum; crystallizing' the alum and igniting the same >at 'a su?licient tempera ture to produce alumina, potassium sulfate, returning the potassium sulfate to the proc rect for leaching fresh batches of sulfatedv and oxids of sulfur ;'recovering the alumina; clay or is evaporated, and the potassium sul 60 fate is returned to' the cyclical process at ' ess at the appropriate stage for producing. l the appropriate stage for the precipitation with aluminum sulfate additional quantities ' 10 of alum from fresh batches of .aluminum of potassium alum; and converting the oXids of sulfur into sulfuric acid applicable for 65 à ' Inf case the clay contains potassium there use in the treatment of further quantities Will Abe a corresponding accumulation of I¿of the aluminous raw material. 3. In a process of preparing commercially » potassium sulfate, which may of course be marketed or disposed of in any desired man pure alumina from aluminous raw'v mate sulfate. ner. 4 rials, the steps which consist in converting - In so far as 'sulfates of the other alkali the alumina component ofthe raw material into aluminum sulfate; reacting thereon» metals may be capable of replacing potas sium sulfate in this reaction they'are to be with potassium sulfate to produce potassium regarded as equivalent thereto for the pur alum; and recovering potassium'sulfate and commercially pure alumina from the alum poses of this- invention. » ' l It is >obvious that the process above de thus produced.l 4. In a cyclical process of preparing com 25 scribed as applicable to thev preparation of alumina from clay, is equally applicable to > mercially pure alumina from aluminum sul the preparation of alumina from aluminum fate, the steps Which consist in reacting upon sulfate from any source, including alunite aluminum sulfate in aqueous solution Wit'. or the like. We claim :--- - . - - -1. A cyclical process of producing com mercially pure alumina from aluminous raw ._ materials,~ comprising treatin the alumi 35 nous material with sulfuric acid in propor tion sufficient to convert the bases intoy sul 80 potassium sulfate to produce potassium alum; decomposing the alum by heat to pro duce commercially pure alumina and po tassium sulfate; and utilizing the recovered potassium sulfate in a repetitlon ofthe proc-` .85 ess. - - - _ , , 5. In a cyclical process of preparing com fates, and dissolving the same; reducing any mercially pure alumina from aluminum sul- ` ferrie iron to the ferrous state; adding to fate contaminated by ferrie- iron,` the steps the solution potassium sulfate in propor Whlch consist in reducing the ferric iron to 90 tion to convert the aluminum sulfate into the ferrous state; treating the resulting alu 40 potassium alum; crystallizing the alum and minum sulfate in aqueous solution with po-V ‘ tassium sulfate in proportion to produce po ture to produce alumina, potassium sulfate, tassium alum; crystallizing and recoverlng 95 and oXidS of sulfur; recovering the alumina; the alum and decomposing the same by heat and returning the potassium sulfate to the to produce commerclally pure alumina and potassium sulfate; and utilizing the re 45 process at the appropriate stage for produc ing With aluminum sulfate _additional quan covered potassium sulfate in a repetition of ’ the process. vtitles of potassium alum. igniting the same at a sufficient tempera# . 2. AAcyclical 'rocess of producingv com In testimony whereof', we affix our signa mercially pure a umina from aluminous raw tures. 50 materials, comprising treating the alumi FREDERICK LAIST. nous material with sulfuric acid in propor tion suíiicient to convert the bases -into sul ROB-,ERI` -S.» OLIVER. FREDERICK F. FRICK. 100
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