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MembraneMembrane
SeparationSeparation
ByBy
Nitish GuptaNitish Gupta
Chemical Engineering 3Chemical Engineering 3rdrd
yearyear
Meerut Institute of Engineering and TechnologyMeerut Institute of Engineering and Technology
2
1. Overview1. Overview
• Membrane separation process is a feed
consisting of a mixture of two or more
components are partially separated by
means of semi permeable barrier (the
membrane) through which one or more
species move faster than another or
other species.
3
• Part of the feed that does not pass
through membrane, i.e. retained is
called Retentate.
• Part of the feed that passes through
the membrane is called permeate.
4
2. Why Membrane Separation2. Why Membrane Separation
• Saves large amount of energy.
• Long life membrane.
• Defect free.
• More compact
• More easily operated, controlled and
maintained.
5
3.Desirable attributes3.Desirable attributes
• Good permeability.
• High selectivity.
• Chemical and Mechanical compatibility with
the processing environment.
• Ability to withstand large pressure
differences across the membrane thickness.
4. Membrane materials4. Membrane materials
• All the membrane materials are made
from synthetic and natural polymer.
• These polymers can be formed by
addition, condensation or by the
copolymerization processes.
• Thermoplastic polymer membranes can
be used for the temperature upto glass
transition temperature.
• Thermosetting polymers never melts.
6
• Membranes made of glassy polymers can
operate below or above the glass
transition temperature.
• Aromatic polyamides (also called aramids)
are high melting crystalline polymers that
have better long term thermal stability
and higher resistance to solvents than do
aliphatic polyamide, such as nylon.
• Polycarbonate differs from most other
polymers because they can be extruded
into various shape,films and sheets. 8
9
4. Permeance factor4. Permeance factor
To be effective for separating a mixture
of chemical component a polymer
membrane should have high permeance
and a high permeance ratio.
The permeance of the given species
diffusing through membrane of given
thickness is analogous to mass transfer
coefficient. i.e. flow rate of that
species per unit cross sectional area of
membrane per unit driving force
( pressure, concentration etc.)
10
The membrane which consist of thin
dense skin about .1 to 1 micrometer in
thick is called perm selective layer.
Ni = Pm / lm (driving force)
where, Pm is Permeability
lm is Membrane thickness.
11
5. Transport in membranes5. Transport in membranes
It is important to understand the nature
of transport phenomenon in membranes
because both the permeance and driving
force depends on the mechanism of
transport.
Membranes can be macro porous, micro
porous and dense ( non-porous).
12
5 (a) Porous Membranes5 (a) Porous Membranes
• If the pore diameter is larger as
compared to the molecular diameter and
a pressure differences exists across
the membrane, bulk or convective flow
through the pores occurs. Such a flow is
generally undesirable because it is not
perm selective and therefore no
separation between component and feed
occurs.
Contd.
13
• If fugacity, activity, concentration
differences exists across the
membrane but the pressure is same on
the both side, perm selective diffusion
of the component through the pores will
takes place.
Contd.
14
5 (b) Non porous Membranes5 (b) Non porous Membranes
In this gas or liquid components absorbs
into the membrane at the upstream
face diffusion through the solid
membrane and desorbs at the face.
Diffusivities of solid is less than gas as
well as liquid.
water vapor in air is .25
water in ethanol liquid is 1.2*10-5
water in cellulose acetate is 1.0*10-8
15
6. Some Industrial Application6. Some Industrial Application
of Membrane Separationof Membrane Separation
• Dialysis
• Gas permeation
• Reverse osmosis
• Pervaporation
16
DIALYSISDIALYSIS
• Dialysis is membrane processes that
use pressure difference as the driving
force.
• It is of great importance in
hemodialysis, in which urea, creatine,
uric acid, phosphate and chlorides are
removed from blood without removing
essential higher molecular weight
compounds and blood cells. This dialysis
is called as artificial kidney. 17
18
REVERSE OSMOSISREVERSE OSMOSIS
• It refers to the passage of solvent such
as water, through a dense membrane
i.e. permeable to the solvent, but not
the solute.
• It was first experimented by Nollet
with water, an alcohol and an animal
bladder.
• Reverse osmosis is applied to the
desalination and purification of sea
water, brackish water and waste water. 19
20
PERVAPORATIONPERVAPORATION
• pervaporation is the combination of
two words perm selective and
evaporation.
• Here vaporization may occur near the
downstream face of the membrane,
such that the membrane can considered
to operate with two zones, a liquid
phase zone and a vapor phase zone as
shown in the figure.
21
22
Contd.
• It is used for the removal of volatile
organic compounds ( VOCs).
• Dehydration of ethanol.
• Removal of organics from water.
It is best applied when the heat solution
is dilute in the permeant because
sensible heat of feed mixture provides
the enthalpy of vaporization to
permeate. 23
Thank youThank you
24

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Membrane Separation Processes

  • 1. 1 MembraneMembrane SeparationSeparation ByBy Nitish GuptaNitish Gupta Chemical Engineering 3Chemical Engineering 3rdrd yearyear Meerut Institute of Engineering and TechnologyMeerut Institute of Engineering and Technology
  • 2. 2 1. Overview1. Overview • Membrane separation process is a feed consisting of a mixture of two or more components are partially separated by means of semi permeable barrier (the membrane) through which one or more species move faster than another or other species.
  • 3. 3 • Part of the feed that does not pass through membrane, i.e. retained is called Retentate. • Part of the feed that passes through the membrane is called permeate.
  • 4. 4 2. Why Membrane Separation2. Why Membrane Separation • Saves large amount of energy. • Long life membrane. • Defect free. • More compact • More easily operated, controlled and maintained.
  • 5. 5 3.Desirable attributes3.Desirable attributes • Good permeability. • High selectivity. • Chemical and Mechanical compatibility with the processing environment. • Ability to withstand large pressure differences across the membrane thickness.
  • 6. 4. Membrane materials4. Membrane materials • All the membrane materials are made from synthetic and natural polymer. • These polymers can be formed by addition, condensation or by the copolymerization processes. • Thermoplastic polymer membranes can be used for the temperature upto glass transition temperature. • Thermosetting polymers never melts. 6
  • 7.
  • 8. • Membranes made of glassy polymers can operate below or above the glass transition temperature. • Aromatic polyamides (also called aramids) are high melting crystalline polymers that have better long term thermal stability and higher resistance to solvents than do aliphatic polyamide, such as nylon. • Polycarbonate differs from most other polymers because they can be extruded into various shape,films and sheets. 8
  • 9. 9 4. Permeance factor4. Permeance factor To be effective for separating a mixture of chemical component a polymer membrane should have high permeance and a high permeance ratio. The permeance of the given species diffusing through membrane of given thickness is analogous to mass transfer coefficient. i.e. flow rate of that species per unit cross sectional area of membrane per unit driving force ( pressure, concentration etc.)
  • 10. 10 The membrane which consist of thin dense skin about .1 to 1 micrometer in thick is called perm selective layer. Ni = Pm / lm (driving force) where, Pm is Permeability lm is Membrane thickness.
  • 11. 11 5. Transport in membranes5. Transport in membranes It is important to understand the nature of transport phenomenon in membranes because both the permeance and driving force depends on the mechanism of transport. Membranes can be macro porous, micro porous and dense ( non-porous).
  • 12. 12 5 (a) Porous Membranes5 (a) Porous Membranes • If the pore diameter is larger as compared to the molecular diameter and a pressure differences exists across the membrane, bulk or convective flow through the pores occurs. Such a flow is generally undesirable because it is not perm selective and therefore no separation between component and feed occurs. Contd.
  • 13. 13 • If fugacity, activity, concentration differences exists across the membrane but the pressure is same on the both side, perm selective diffusion of the component through the pores will takes place. Contd.
  • 14. 14
  • 15. 5 (b) Non porous Membranes5 (b) Non porous Membranes In this gas or liquid components absorbs into the membrane at the upstream face diffusion through the solid membrane and desorbs at the face. Diffusivities of solid is less than gas as well as liquid. water vapor in air is .25 water in ethanol liquid is 1.2*10-5 water in cellulose acetate is 1.0*10-8 15
  • 16. 6. Some Industrial Application6. Some Industrial Application of Membrane Separationof Membrane Separation • Dialysis • Gas permeation • Reverse osmosis • Pervaporation 16
  • 17. DIALYSISDIALYSIS • Dialysis is membrane processes that use pressure difference as the driving force. • It is of great importance in hemodialysis, in which urea, creatine, uric acid, phosphate and chlorides are removed from blood without removing essential higher molecular weight compounds and blood cells. This dialysis is called as artificial kidney. 17
  • 18. 18
  • 19. REVERSE OSMOSISREVERSE OSMOSIS • It refers to the passage of solvent such as water, through a dense membrane i.e. permeable to the solvent, but not the solute. • It was first experimented by Nollet with water, an alcohol and an animal bladder. • Reverse osmosis is applied to the desalination and purification of sea water, brackish water and waste water. 19
  • 20. 20
  • 21. PERVAPORATIONPERVAPORATION • pervaporation is the combination of two words perm selective and evaporation. • Here vaporization may occur near the downstream face of the membrane, such that the membrane can considered to operate with two zones, a liquid phase zone and a vapor phase zone as shown in the figure. 21
  • 23. • It is used for the removal of volatile organic compounds ( VOCs). • Dehydration of ethanol. • Removal of organics from water. It is best applied when the heat solution is dilute in the permeant because sensible heat of feed mixture provides the enthalpy of vaporization to permeate. 23