Document 216830

006 AG
Membrane Systems
“Membranes, Modules
and how to select them”
Wolfgang Thalhammer
006 AG – Membrane Systems
Presentation Overview
• Short membrane science
• Selection of membrane cut off
• Selection of module configuration
• Selection of membrane material
• Membrane screening trials, examples
• New modules and membranes on the market
006 AG – Membrane Systems
006 AG – Membrane Systems
Filtrate flow
Filter cake thickness
time
Tangential Flow Filtration
• Increases flux levels
• Reduced fouling rate
• Tangential flow creates shear on membrane surface
006 AG – Membrane Systems
time
Filter cake thickness
Filtrate flow
A membrane can separate
phases, macro and micromolecules in liquid or gas
solution. Selectivity is primarily
based on size difference and
secondarily on charge &
hydrophobic characteristics.
- Semi permeable barriers, they are selective
Size based separation
Membrane
Definition of a Membrane
MF
UF
NF
RO
But!!!
Advantage of physical barrier seperation!!!
• Operating parameters effect MWCO
(diffusion VS convection)
• MWCO changes also with charge
and polarity of feed and membrane
• MWCO is a relative figure.
006 AG – Membrane Systems
Polymer
Selectivity needed for the process
Selection for Trials
Cost Capital investment, running cost
Ceramic
Process parameters Capacity, yield, temperature, pH...
• Definition of MWCO differs for
different manufacturer
006 AG – Membrane Systems
Stainless steel
Membrane Material
Feed parameters TS, viscosity, composition, particles, ...
Membrane configuration
Plate & Frame
Cassette
Flat sheet
Tubular
Hollow fibre
Spiral wound
>0.6micron
Membrane cut off
Selectivity Cut Off, seperation quality
Selection of Membranes
%
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006 AG – Membrane Systems
006 AG – Membrane Systems
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Selectivity of different membrane types
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Membrane types
MF
UF
NF
RO
006 AG – Membrane Systems
Flat sheets
-plate distance
-air flow
-backflushable
Plate & Frame
-plate distance
-flow distributors
-construction material
-glue type
-backflushable
006 AG – Membrane Systems
Stainless steel
Membrane Material
Polymer
Tubular
-channel diameter
-nr of channels
-module length
Cassette
-channel height
-flow Distributors
-seal material
-construction material
Spiral Wound
-feed spacer hight
-feed spacer type
-sanitary design
-construction material
-glue type
Hollow fibre
-channel diameter
-nr of channels
-module length
-construction material
backflushable
Membrane configurations
Selection for Trials
Cost Capital investment, running cost
Ceramic
Process parameters Capacity, yield, temperature, pH...
Feed parameters TS, viscosity, composition, particles, ...
Membrane configuration
Plate & Frame
Cassette
Tubular
Hollow fibre
Spiral wound
>0.6micron
Membrane cut off
Selectivity Cut Off, seperation quality
Selection of Membranes
+
+
0
Tubular
Hollow fibre
Spiral wound
Flat sheet
(submerged)
MF
006 AG – Membrane Systems
Stainless steel
Membrane Material
0
+
++
+++
++
++
UF
+++
+
+
+++
+
++
+
+
Backflushability
NF
RO
Selection of Membranes
-1 –
0.5bar
40bar or
higher
5bar
60bar
10bar
60bar or
higher
Cleanabiltiy
Hollow fibre
Spiral wound
Selection for Trials
Cost Capital investment, running cost
Ceramic
Polymer
Process parameters Capacity, yield, temperature, pH...
Tubular
Feed parameters TS, viscosity, composition, particles, ...
Membrane configuration
Plate & Frame
Cassette
>0.6micron
Membrane cut off
+++
-
+
++
+
+
Max
Energy
pressure demand
Selectivity Cut Off, seperation quality
++
Cassette
006 AG – Membrane Systems
++
Viscosity Solids
Plate & Frame
Configuration
Membrane configurations
-2 – 13
0-14
2-11.5
Stainless steel
Ceramic *
Polymer
50°C
350°C
350°C
Temperature
Chlorine
Limited
Ok
Ok
006 AG – Membrane Systems
Ceramics
(Al2O3,
ZrO2,
TiO2)
•...
• Porosity
• Charge or IEP
• Carrier
• Thickness
• Hydrophobicity
Material effects
Membrane materials
Polymer
(PS, PES,
PP, PAN, ...)
* No phosphoric acid
Allowed cleaning chemicals:
-nitric acid,
-citric/lactic acid
-phosphoric acid
-sodium hyrdoxid
-potassium hydroxid
+ tensides, chelating agents, sequestrants, buffers,...
pH
Material
Metal
006 AG – Membrane Systems
Stain less steal
Metal
Membrane materials
MF
UF
NF
RO
006 AG – Membrane Systems
Polymer
Polymer plate & Frame
Tubular polymer
Hollow fibre ceramics
Polymer cassette
Tubular ceramics
Tubular metal
Cost of membrane solutions
Selection for Trials
Cost Capital investment, running cost
Ceramic
Process parameters Capacity, yield, temperature, pH...
Hollow fibre polymer
Spiral wound
006 AG – Membrane Systems
Stainless steel
Membrane Material
Feed parameters TS, viscosity, composition, particles, ...
Membrane configuration
Plate & Frame
Cassette
Tubular
Hollow fibre
Spiral wound
>0.6micron
Membrane cut off
Selectivity Cut Off, seperation quality
Selection of Membranes
006 AG – Membrane Systems
Cost: spiral wound would be cheapest, possible?
polymer, ceramics, stainless steal
Process parameters: 5 m3 / d, pH 6, Temperature 50°C, VCR 20
Spiral wound, hollow fibre, tubular, plate & frame, cassette,
Feed properties: 10% TS, water like, contains cell debries, proteins, amino acids, salts
MF 0.2 micron
Example 1 for membrane selection
Selectivity of process: Clarification of fermentation broth
Costumer: Yeast factory
006 AG – Membrane Systems
Spiral wound
Tubular ceramics
Tubular metal
Cost of membrane solutions
UF 10-20kDa
Support customers and factories
•
006 AG – Membrane Systems
Optimum CIP procedures
New process developments
•
Process optimization
•
Membrane screening for optimum membrane type
The membrane laboratory is used for:
•
•
We have lots of membranes on stock and hence
can offer rapid membrane screening and process
development.
•
•
The MMS laboratory is specialised in developing
membrane based processes.
•
Membrane trials in process development
006 AG – Membrane Systems
Cost: even hollowfibre to expensive, spiral wound possible, with pretreatment
(dedusting, defating) ?
polymer, ceramics, stainless steal
Processparameters: 200 m3 / d, pH 6, Temperature 50°C, VCR 20
hollow fibre, tubular, plate & frame, cassette,
Feed properties: 6% TS, water like, contains 0.5% Protein, 0.01% fat and 0.01%
solids > 0.1mm (chesse dust)
Selectivity of process: Whey protein recovery
Costumer: Cheese factory
Example 2 for membrane selection
006 AG – Membrane Systems
• Pressure drop
• Regeneration problems
Industrial Systems
1
2
3
Clean membrane water flux
4
5
Membrane screening example 1,
„yeast clarification“
Pilot Systems
• Fouling layer = f(Vs, TMP, temp, backflush)
• Flux vs Concentration
• Max. Concentration level
006 AG – Membrane Systems
Laboratory Systems
Lab-Pilot-Industrial Systems
HpHT
Duratherm
DX-Type
Koch
GE
Microdyn Nadir
80°C
006 AG – Membrane Systems
006 AG – Membrane Systems
3-14
2-11.5
1.8 - 12.5
pH Range
Disadvantage:
-Lower stability
-Expoxy glue is heat and chemical instable
Advantage:
-No resistance in carrier, higher flux
Inocep ceramic hollow fibre
Disadvantage
-25% higher membrane cost
50 (san.: 90°C)
60°C (clean.: 80°C)
Max Temprature
Advantages
-improve cleaning or sanitation possibilities
-reduce cleaning cost
-make high temperature processes possible
Name
Manufacturer
Spiral wound modules with extended pH and/or temperature range
HpHT polymer modules
Further
006 AG – Membrane Systems
Dairy Ultra UF
• Reticulated (void-free) membrane structure, lower protein passage.
• Increased membrane hydrophilicity.
• Reduced Clean Water Flux -.
St gobain ceramics,
-Improved porosity of support, lower resistance
-Maintains stability of ceramics compared to Inocep hollow fibres
Microsieves,
- Pore size distribution narrow, photolithographic methods
- Membrane resistance up to three orders of magnitude lower
006 AG – Membrane Systems
Disadvantages
- Only one MWCO available
- High packing density
Advantages
- Backflushable cassette system
- High packing density
Permeate spacer fused with membrane
Flowcell
006 AG – Membrane Systems
Danke sehr für die Aufmerksamkeit
006 AG – Membrane Systems
to create cost effective, stable and flexible solutions.
- experience,
- feed analysis,
- screening trials ,
- and process simulation,
Membrane selection is a complex issue with multiple
possibilites. We base it on
Summary