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Reverse Osmosis Ultrafiltration Microfiltration

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Presentation on theme: "Reverse Osmosis Ultrafiltration Microfiltration"— Presentation transcript:

1 Reverse Osmosis Ultrafiltration Microfiltration
MEMBRANE PROCESSES Reverse Osmosis Ultrafiltration Microfiltration

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.

3 Microfiltration Dead-end Filtration Feed Filter Cake Membrane Permeate

4 Microfiltration Crossflow Microfiltration Feed Retentate Membrane
Permeate 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 Concentrate 100% 50% ! Membrane Permeate 50% !
Suspended Solids Colloids Dissolved Solids Concentrate Suspended Solids Colloids Dissolved Solids 100% 50% ! Membrane Permeate Low molecular weight dissolved solids Liquid 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 Aerobic Biological Treatment with Membrane Separation
Final Effluent BOD <2 SS Aerobic Biological Process Sed Tank Pretreatment MF Influent BOD 300 SS TKN 50 PO Primary Sludge Secondary Sludge

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 micro-molecular coarse particles Ionic range macro-molecular microorganisms Reverse Osmosis Ultrafiltration Nanofiltration Microfiltration MWCO microns

11 APPLIED PRESSURES Reverse Osmosis: 100-800 psi 1000-5500 kPa
Ultrafiltration: psi 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 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 Polyarcylonitrile Cellulose Acetate Polyethersulfone Fluoropolymer Polyvinylidene fluoride Poly vinyl chloride


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