2. Contents
• Introduction
• Working and Principle
• Membrane
• Membrane Fouling
• Methods to remove Membrane Fouling
• Cleaning
• Applications
3. INTRODUCTION
• Ultrafiltration (UF) is a variety of membrane filtration in
which forces like pressure or concentration gradients lead
to a separation through a semipermeable membrane.
5. INTRODUCTION (CONTINUE..)
• This separation process is used in industry and research for
purifying and concentrating macromolecular (103 - 106 Da)
solutions, especially protein solutions.
• Pore diameters in the 10-1000 A range.
6. WORKING
• Suspended solids and solutes of high molecular weight are retained
in the so-called retentate, while water and low molecular weight
solutes pass through the membrane in the permeate(filtrate).
7. PRINCIPLE
• The relationship between the applied pressure on the solution to be separated
and the flux through the membrane is most commonly described by the Darcy
equation:
• Where J is the flux (flow rate per membrane area)
• TMP is the transmembrane pressure (pressure difference between feed and
permeate stream)
• μ is solvent viscosity
• Rt is the total resistance (sum of membrane and fouling resistance).
8. MEMBRANE
• The membrane used for
UF should have :
• High porosity
• Narrow pore size
distribution
10. Factors effecting rentity of membranes
1. Size of molecules
2. Shape of the molecule
3. Membrane material
4. Presence of other solutes
5. Membrane configuration
6. Fouling and absorption effects
11. Pore Size of membranes
• UF membrane have pore sizes larger than Reverse Osmosis Process.
• These membranes are mostly used for fractionating processes (to
separate high molecular weight solutes from low molecular weight).
• The pore size of UF membrane ranges from 0.001 micron – 0.02
micron.
12. Membrane Fouling
• The major challenge faced in UF is membrane fouling.
• Overtime the filtrate will accumulate on the membrane surface and clog the pores.
• Greatly reduces membrane effectiveness and efficieny.
• This reduces the effective TMP of the system, therefore reducing permeation rate. The
increase in concentrated layer at the membrane wall decreases the permeate flux, due
to increase in resistance which reduces the driving force for solvent to transport
through membrane surface.
• Methods have been developed to reduce this effect for continuous operation.
14. Types of Fouling
1. Particulate deposition
• Standard blocking: macromolecules are uniformly deposited on pore
walls
• Complete blocking: membrane pore is completely sealed by a
macromolecule
• Cake formation: accumulated particles or macromolecules form a
fouling layer on the membrane surface, in UF this is also known as a
gel layer
• Intermediate blocking: when macromolecules deposit into pores or
onto already blocked pores, contributing to cake formation
15. Types of Fouling (Continue..)
2. Scaling
As a result of concentration polarization at the membrane surface,
increased ion concentrations may exceed solubility thresholds and
precipitate on the membrane surface. These inorganic salt deposits can
block pores causing flux decline, membrane degradation and loss of
production. The formation of scale is highly dependent on factors
affecting both solubility and concentration polarization including pH,
temperature, flow velocity and permeation rate.
16. Types of Fouling (Continue..)
3. Biofouling
• Microorganisms will adhere to the membrane surface forming a gel
layer – known as biofilm.
• The film increases the resistance to flow, acting as an additional
barrier to permeation.
18. Methods To Reduce Membrane Fouling
• Optimize pH and ionic strength of the feed solution to minimize the
adsorption or deposition of the feed materials.
• Select an appropriate pre-filtration procedure or other means to remove
large molecules.
• Select a membrane with an optimum pore size.
• Optimize the operating conditions. This includes increasing
transmembrane pressure to maximize flux.
19. Cleaning
• Cleaning of the membrane is done regularly to prevent the accumulation of
foulants .
• Regular backwashing is often conducted every 10 min for some processes
to remove cake layers formed on the membrane surface.
• By pressurising the permeate stream and forcing it back through the
membrane, accumulated particles can be dislodged, improving the flux of
the process.
20. Cleaning (Continue..)
• Backwashing is limited in its ability to remove more complex forms of
fouling such as biofouling, scaling or adsorption to pore walls.
• These types of foulants require chemical cleaning to be removed. The
common types of chemicals used for cleaning are:
• Acidic solutions for the control of inorganic scale deposits.
• Alkali solutions for removal of organic compounds.
• Biocides or disinfection such as Chlorine or Peroxide when bio-fouling
is evident.
21. Applications
• Water Treatment
1. Process water (Remove oxides, acids, bases, pathogens, inorganic
salts etc from raw water)
2. Drinking water (viruses and various microorganisms are removed)
3. Waste water (Remove Pollution and reduction of waste from water)
25. Applications (Continue..)
• Other applications include :
• Filtration of effluent from paper pulp mill
• Removal of pathogens from milk
• Fruit juice concentration and clarification
• Dialysis and other blood treatments
• Alcoholic beverage industries
• Vegetable oils
• Sugar industry