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MEMBRANE PROCESSES
Reverse Osmosis
Ultrafiltration
Microfiltration
What Are Membranes?
Membranes are thin films of synthetic organic
or inorganic (ceramic) materials, which can
bring about a very selective separation
between a fluid and its components. The
fluid may be a gas or a liquid but in
Environmental Engineering we are more
concerned with water and wastewater.
Microfiltration
Membrane
Dead-end Filtration
Feed
Filter Cake
Permeate
Microfiltration
Crossflow Microfiltration
Feed
Retentate
Permeate
Membrane
Notes: The retentate may be recirculated to the feed
A “dynamic” membrane may be created by adding Lime or
KMnO4 to the feed, to precipitate MnO2 on membrane
Membrane Operation
Feed
Suspended Solids
Colloids
Dissolved Solids
Concentrate
Suspended Solids
Colloids
Dissolved Solids
Permeate
Low molecular
weight dissolved
solids
Liquid
Membrane
100% 50% !
50% !
To River, Sewer or Re-use
Applications of Membranes in
Wastewater Treatment
• Pressure driven solid liquid separation processes
• Tertiary treatment of wastewaters following
secondary sedimentation
• Production of high quality effluent in re-use
schemes
• Alternative to sedimentation tank for solid/liquid
separation in:
– aerobic biological treatment
– anaerobic biological treatment
Pretreatment Sed
Tank
Aerobic
Biological
Process
Final Effluent
Influent
BOD 300
SS 300
TKN 50
PO4 15
BOD <2
SS 0
Primary
Sludge
Secondary
Sludge
Aerobic Biological Treatment
with Membrane Separation
MF
Membrane Anaerobic Reactor
Influent
Effluent
UF/MF Unit
Anaerobic Reactor
Wastage
Recycle
Gas
Advantages of Membrane Processes
• They are usually continuous
• Comparatively low energy utilisation
• No phase change of contaminants
• Small temperature change
• Modular design
• Minimum of moving parts
• Physical separation of contaminants
Filtration Range
Reverse Osmosis
Nanofiltration
Ultrafiltration
Microfiltration
MWCO 0 100 200 20000 100000 500000
microns 0 0.001 0.01 0.1
Ionic range
micro-molecular
microorganisms
coarse
particles
macro-molecular
APPLIED PRESSURES
Reverse Osmosis: 100-800 psi
1000-5500 kPa
Ultrafiltration: 5-100 psi
35-695 kPa
Microfiltration: Low
Microfiltration Design Considerations
• High flux
• Back-flushable
• High membrane area/volume ratio allowing low pressure
drop whilst maintaining high tangential velocities
• Simple installation and continuous operation with
minimum supervision
• Low operating pressure
• Easy maintenance and simple membrane replacement
• Low energy consumption
• Relatively low capital costs
Microfiltration Applications
Current Future
Wine Drinking Water
Dextrose clarification Hydrocarbon Separation
Haze removal from gelatin Milk-fat Separation
Beer clarification Food and Beverage
Pharmaceutical/biological Industrial Wastewater
Municipal Wastewater Treatment Paint
Biotechnology
Ultrafiltration Applications
Current Future
Juice clarification Domestic wastewater
Increase cheese yield More industrial wastewaters
Gelatin concentration Protein harvesting
Electroplating wastewater Petroleum processing
Protein from cheese whey Wastewater re-use
Concentration of oil emulsions Potable water (THM concern)
Pharmaceutical industry Abattoir (blood recovery)
“Grey” water Pulp and paper industry
Industrial Wastewater etc etc
Reverse Osmosis
Very different process to MF of UF. It is a
solubilisation diffusion technique that makes use
of a semi-permeable membrane which in turn acts
as a barrier to dissolved salts and inorganic
molecules.
It also confines organics with molecular weights
greater than 100
RO membranes do not have identifiable pores as in
MF or UF (i.e. too small - atomic size)
Applications of Reverse Osmosis
Current Future
Desalination for potable water
,, from sea water Chemical process industries
,, from brackish water Metals recovery
,, for effluent re-use Food processing WWT
Ultrapure water for semiconductors Textile wastewater re-use
,, ,, for pharmaceuticals Pulp and paper WWT
,, ,, for medical use Contaminated land
remediation
Boiler feed water Dairy industry WWT
Treatment of hazardous materials
Comparison of Membrane Processes
Ultrafiltration Reverse Osmosis Microfiltration
Operates on difficult Requires extensive pre- Rapidly fouled by colloids
colloidal water treatment of colloids giving high replacement costs
Low pressure (2-6 bar) High pressure (10-30 bar) Low pressure (2-4 bar)
Low energy consumption High energy Low energy
High recovery (up to 95%) Low recovery (50-80%) 100% recovery
Chemical tolerance pH 1-13 pH 2-11 pH 1-13
High temperature up to 80oC 45oC max. High temperatures possible
High resistance to oxidising Limited resistance to High resistance to oxidising
agents oxidising agents agents
Stream sterilisable Stream sterilisation not Stream sterilisation possible
membranes available possible
Hygienic module designs Modules not as hygienic Hygienic designs available
available
Some Properties of Typical Commercial
Ultrafiltration Membranes
Material pH Maximum Pressure Maximum Temp.
(bar) (bar)
Polysulphone 2-12 15 70
Polyarcylonitrile 2-10 10 60
Cellulose Acetate 3-6 25 30
Polyethersulfone 2-12 30 70
Fluoropolymer 2-12 10 60
Polyvinylidene fluoride 2-12 10 70
Poly vinyl chloride 2-12 10 50

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membgka.ppt

  • 2. What Are Membranes? Membranes are thin films of synthetic organic or inorganic (ceramic) materials, which can bring about a very selective separation between a fluid and its components. The fluid may be a gas or a liquid but in Environmental Engineering we are more concerned with water and wastewater.
  • 4. Microfiltration Crossflow Microfiltration Feed Retentate Permeate Membrane Notes: The retentate may be recirculated to the feed A “dynamic” membrane may be created by adding Lime or KMnO4 to the feed, to precipitate MnO2 on membrane
  • 5. Membrane Operation Feed Suspended Solids Colloids Dissolved Solids Concentrate Suspended Solids Colloids Dissolved Solids Permeate Low molecular weight dissolved solids Liquid Membrane 100% 50% ! 50% ! To River, Sewer or Re-use
  • 6. Applications of Membranes in Wastewater Treatment • Pressure driven solid liquid separation processes • Tertiary treatment of wastewaters following secondary sedimentation • Production of high quality effluent in re-use schemes • Alternative to sedimentation tank for solid/liquid separation in: – aerobic biological treatment – anaerobic biological treatment
  • 7. Pretreatment Sed Tank Aerobic Biological Process Final Effluent Influent BOD 300 SS 300 TKN 50 PO4 15 BOD <2 SS 0 Primary Sludge Secondary Sludge Aerobic Biological Treatment with Membrane Separation MF
  • 8. Membrane Anaerobic Reactor Influent Effluent UF/MF Unit Anaerobic Reactor Wastage Recycle Gas
  • 9. Advantages of Membrane Processes • They are usually continuous • Comparatively low energy utilisation • No phase change of contaminants • Small temperature change • Modular design • Minimum of moving parts • Physical separation of contaminants
  • 10. Filtration Range Reverse Osmosis Nanofiltration Ultrafiltration Microfiltration MWCO 0 100 200 20000 100000 500000 microns 0 0.001 0.01 0.1 Ionic range micro-molecular microorganisms coarse particles macro-molecular
  • 11. APPLIED PRESSURES Reverse Osmosis: 100-800 psi 1000-5500 kPa Ultrafiltration: 5-100 psi 35-695 kPa Microfiltration: Low
  • 12. Microfiltration Design Considerations • High flux • Back-flushable • High membrane area/volume ratio allowing low pressure drop whilst maintaining high tangential velocities • Simple installation and continuous operation with minimum supervision • Low operating pressure • Easy maintenance and simple membrane replacement • Low energy consumption • Relatively low capital costs
  • 13. Microfiltration Applications Current Future Wine Drinking Water Dextrose clarification Hydrocarbon Separation Haze removal from gelatin Milk-fat Separation Beer clarification Food and Beverage Pharmaceutical/biological Industrial Wastewater Municipal Wastewater Treatment Paint Biotechnology
  • 14. Ultrafiltration Applications Current Future Juice clarification Domestic wastewater Increase cheese yield More industrial wastewaters Gelatin concentration Protein harvesting Electroplating wastewater Petroleum processing Protein from cheese whey Wastewater re-use Concentration of oil emulsions Potable water (THM concern) Pharmaceutical industry Abattoir (blood recovery) “Grey” water Pulp and paper industry Industrial Wastewater etc etc
  • 15. Reverse Osmosis Very different process to MF of UF. It is a solubilisation diffusion technique that makes use of a semi-permeable membrane which in turn acts as a barrier to dissolved salts and inorganic molecules. It also confines organics with molecular weights greater than 100 RO membranes do not have identifiable pores as in MF or UF (i.e. too small - atomic size)
  • 16. Applications of Reverse Osmosis Current Future Desalination for potable water ,, from sea water Chemical process industries ,, from brackish water Metals recovery ,, for effluent re-use Food processing WWT Ultrapure water for semiconductors Textile wastewater re-use ,, ,, for pharmaceuticals Pulp and paper WWT ,, ,, for medical use Contaminated land remediation Boiler feed water Dairy industry WWT Treatment of hazardous materials
  • 17. Comparison of Membrane Processes Ultrafiltration Reverse Osmosis Microfiltration Operates on difficult Requires extensive pre- Rapidly fouled by colloids colloidal water treatment of colloids giving high replacement costs Low pressure (2-6 bar) High pressure (10-30 bar) Low pressure (2-4 bar) Low energy consumption High energy Low energy High recovery (up to 95%) Low recovery (50-80%) 100% recovery Chemical tolerance pH 1-13 pH 2-11 pH 1-13 High temperature up to 80oC 45oC max. High temperatures possible High resistance to oxidising Limited resistance to High resistance to oxidising agents oxidising agents agents Stream sterilisable Stream sterilisation not Stream sterilisation possible membranes available possible Hygienic module designs Modules not as hygienic Hygienic designs available available
  • 18. Some Properties of Typical Commercial Ultrafiltration Membranes Material pH Maximum Pressure Maximum Temp. (bar) (bar) Polysulphone 2-12 15 70 Polyarcylonitrile 2-10 10 60 Cellulose Acetate 3-6 25 30 Polyethersulfone 2-12 30 70 Fluoropolymer 2-12 10 60 Polyvinylidene fluoride 2-12 10 70 Poly vinyl chloride 2-12 10 50