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Characterization of filtration
membranes
Course of Bioreactors and Downstream Processes M
cristiana.boi@unibo.it
CONFIDENTIAL: NOT FOR DISTRIBUTION
Membrane characterization
Cristiana Boi
 The characterization of membrane properties helps not only
to choose the right membrane for a given application, but
also to gain a better understanding of their preparation
methods and on the selectivity and fouling mechanisms.
 The methods used give access to macroscopic or
microscopic quantities, characteristic of the membrane
structure and the chemistry of the material.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Membrane choice
Cristiana Boi
Structural and transfer characteristics (hydraulic permeability
and selectivity curve) provide information on how the
membrane will perform in the intended separation process:
the permeate flow that can be expected and the size of
molecules likely to be rejected by the membrane.
Surface physicochemical and chemical properties (charge,
hydrophilic–hydrophobic nature, and chemical composition),
which allow fouling and interactions among the different types
of molecules at the membrane surface to be predicted to
some extent.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Characterization methods
Cristiana Boi
Membrane characterization methods can be divided in two
categories:
 for the chemical and structural properties of the membrane;
 for the functional properties, such as selectivity or
permeability.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Structural Characteristics
Cristiana Boi
The characterization methods developed for obtaining
information on the membrane structure can be divided into
three types:
 microscopy techniques;
 liquid intrusion or displacement techniques;
 techniques that measure tracer molecule retention.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Microscopy Techniques
Cristiana Boi
These techniques provide information on surface topology,
roughness, and pore size.
Several microscopic observation methods are used, which
differ by their implementation and their resolution.
 Electron microscopy (SEM, TEM);
 Near Field Microscopy (STM, AFM);
 X-ray synchrotron microtomography.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Principles of Electron Microscopes
Cristiana Boi CONFIDENTIAL: NOT FOR DISTRIBUTION
Applications of SEM
Cristiana Boi
SEM is be an effective method for:
1. characterizing flat membranes;
2. assessing the effect of preparation conditions on the
structure of hollow fiber membranes;
3. observing the evolution of membrane morphology after
contact with washing solutions;
4. measuring the thickness of deposits (0.2–0.4 µm) formed
during membrane fouling.
CONFIDENTIAL: NOT FOR DISTRIBUTION
SEM image of a polysulfone hollow fiber
membrane (MWCO: 40 kDa)
Cristiana Boi
C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Schematic description of a (STM)
Cristiana Boi
C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Example of STM of a membrane
Cristiana Boi
Image of a 100 kDa polysulfone membrane obtained by scanning
tunneling microscopy (STM); (b) Cross sections corresponding to the
lines drawn in the picture 5 (middle-bottom).
Bessieres, A., Meireles, M., Coratger, R., Beauvillain, J., Sanchez, V. J. Membr. Sci. 1996, 109, 271–284.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Example of an AFM of a membrane
Cristiana Boi
(a) Example of an image of a tracked etched polycarbonate membrane
(Nuclepore) – nominal pore size : 0.2 µm; (b) same sample – blow-up
(1000x1000)nm2; and (c) cross section along the line drawn in picture (a).
C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Comparison STM and AFM
Cristiana Boi CONFIDENTIAL: NOT FOR DISTRIBUTION
X-ray synchrotron
microtomography
Cristiana Boi
3D reconstruction volume of a part of
a PVDF hollow fiber microfiltration
membrane from SRµCT.
Dimensions of the observed volume
are 420 µm x 320 µm x 190 µm.
Remigy, J.C., Meireles, M., Thibault, X. J. Membr. Sci. 2007, 305, 27–35.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Displacement Techniques
Cristiana Boi
These methods consist of wetting the membrane with a wetting
agent (phase 1) of known surface tension and contact angle
with the membrane, then expelling it from the membrane pores
by displacing it with a second phase (phase 2), which is
generally air or an immiscible liquid.
 bubble point;
 liquid/gas displacement;
 liquid–liquid porometry.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Bubble point
Cristiana Boi
In the bubble point method, the pores of the membrane are
completely wet with a liquid (phase 1) which is then displaced
with air (phase 2). The Young–Laplace equation allows the
maximum pore radius to be calculated from the value of the
transmembrane pressure measured when the first bubbles
are detected in the permeate compartment:
where γL is the surface tension of the liquid (N m-1) and ϑ the
contact angle between the liquid and the membrane surface.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Mercury intrusion
Cristiana Boi
Variant of the bubble point method in which phase 1 is air and
phase 2 is mercury that is gradually forced into the membrane
pores.
Mercury has a very small contact angle with most materials.
Both bubble point and mercury intrusion have the drawback
that they require very high pressures (from 1 to several
kilobars) to analyze pores of the order of 10 nm like those
found in ultrafiltration membranes.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Liquid–liquid porometry
Cristiana Boi
This method consists of wetting the membrane with a wetting
liquid (phase 1) then expelling the liquid from the membrane
pores by displacing it with another liquid (phase 2) that is
immiscible with the former. The pressure that has to be
applied depends directly on the interfacial tension between
the two liquids. Thus, by a appropriate choice of the liquid 1-
liquid 2 pair (based on a water–isobutanol–methanol
combination), the pressures to be applied for the analysis of
small-radius pores need not exceed 10 bar or so.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Liquid–liquid porometry
Cristiana Boi
Example of a bi-modal pore-size distribution obtained on an ultrafiltration membrane by
bi-liquid porometry (liquid mixture: methanol, isobutanol, 1 butanol and water; interfacial
tension between organic phase and aqueous phase: 0.35mN-1m).
C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Water permeability
Cristiana Boi
In the presence of a pure solvent, any increase in
transmembrane pressure leads to a proportional increase in
the permeate volume flux density which allows the membrane
to be considered as an ideal porous medium.
The coefficient of proportionality, Lp (assumed constant), is
called the hydraulic permeability of the membrane and
depends on its intrinsic characteristics: porosity, pore-size
distribution, thickness, and hydrophilic nature. This parameter
(Lp) thus represents the volume of solvent that passes through
the membrane per unit of pressure, filtering area, and time.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Water permeability
Cristiana Boi
From tests with pure water, the permeability of the membrane
can be determined by means of Darcy’s law:
Deviations from linearity may arise from the compressibility of
the membrane, or from the retention of some impurities
remaining in the retentate compartment.
J : flux density (m s-1),
Q : pure solvent filtration rate (m3 s-1),
A : filtering surface area (m2),
Lp : hydraulic permeability of membrane (m),
µ : dynamic viscosity of pure solvent (Pa s),
P : transmembrane pressure (Pa)
Rm: hydraulic resistance of membrane (m-1)
CONFIDENTIAL: NOT FOR DISTRIBUTION
Tracer Retention Techniques
Cristiana Boi
Tracer retention techniques measure the transfer of
macromolecules (ultrafiltration) of calibrated particles called
tracers, and these measurements are then compared with a
transport model.
The principle is to measure the retention of a series of tracers
of different sizes so as to obtain a curve of selectivity versus
molar mass (or size) of the molecules
CONFIDENTIAL: NOT FOR DISTRIBUTION
Choice of Tracers
Cristiana Boi
The tracers used must fulfill several criteria:
 have few specific interactions with the membrane material
or the macromolecules that may be absorbed on to the
membrane to account for its intrinsic characteristics;
 have molar masses (or sizes) that cover the broadest
retention range possible, especially in the region close to
100%;
 be detectable even at very low concentrations in the
collected permeate.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Examples of Tracers
Cristiana Boi
C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Applicability of tracer
retention methods
Cristiana Boi
 Method is suitable for UF membranes: dextrans, PEGs and
proteins are used as tracers;
 NF membranes: the tracer can be small PEGs, sugars or
inorganic salts;
 RO: NaCl as a tracer. Membranes for water desalination
have 99% NaCl rejection, while membranes for brackish
water have 96% rejection.
For MF membranes is very difficult apply since there are only
a few suitable tracers of sufficient size (polyethylene oxide,
high MW dextrans).
CONFIDENTIAL: NOT FOR DISTRIBUTION
Selectivity curve
Cristiana Boi
Selectivity curve for dextran molecules: MWCO (molecular weight of a
molecule rejected at 90% by the membrane) is 85 kDa
C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Microbiological Tracers
Cristiana Boi
Microbiological tracers are used because membranes have
been considered as potential screens against microbiological
contamination of waters or air.
 Bacteria;
 Viruses;
 Surrogates.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Microbiological Tracers
Cristiana Boi
In general, filtration reduces the content in microorganisms,
but does not guarantee their complete elimination. The
reduction in microorganisms is often measured by the log
removal value (LRV), defined as
The maximum LRV that can be claimed depends on the
concentration of bacteria in the challenging suspension. For
example, if the concentration is 106 cfu/ml in the retentate and
zero in the permeate, one counts 1 cfu/ml in the latter and the
LRV is then 6.
P
F
c
c
LRV 10
log

CONFIDENTIAL: NOT FOR DISTRIBUTION
Bacteria
Cristiana Boi
The first discrimination was done between filters rated 0.2 and
0.45 µm, by using Brevundimonas diminuta; several bacteria
are used for membrane characterization, as for example
CONFIDENTIAL: NOT FOR DISTRIBUTION
Virus
Cristiana Boi
Most viruses are two orders of magnitude smaller than
bacteria.
Differences in membrane characterization:
 higher diffusivity;
 surface interactions in their behavior.
In particular, viruses have a strong tendency to adsorb onto
surfaces. For this reason, the apparent retention of viruses by
membranes may be much higher than the actual filter
capacity.
Experiments of virus retention are performed in the worst-
case conditions: this will guarantee that when in operation, the
membrane will show either the same or a better retention of
the viruses.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Surrogates
Cristiana Boi
Surrogates of the microorganisms, which would mimic their
behavior and allow simpler and faster membrane
characterization. Latex or silica particles, and gold sols have
therefore been used. Thus far, two major drawbacks have
been pointed out:
 the much lower sensitivity of the particle detection methods,
which limits the range of LRV that can be explored;
 the difference in surface properties (charge, stiffness,
hydrophilic character, etc..) between such surrogates and
bioparticles, which induces a difference in retention, as, for
example, by charge exclusion, by adsorption on or in the
membrane material.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Determination of Hydrophilic/
Hydrophobic Nature of Membranes
Cristiana Boi
The hydrophilic nature of a material is a very important
parameter as it conditions the solute-membrane and solvent-
membrane interactions.
In many applications, hydrophilic membranes are more
efficient than hydrophobic ones, the latter being confronted
with more serious fouling whenever hydrophobic molecules or
particles (proteins, colloids, etc.) are present in the fluid to be
filtered. The same is true for surfactants, the adsorption of
which is more pronounced on hydrophobic materials.
The hydrophilic/hydrophobic nature of a membrane is
determined by measuring the contact angle or by using the
capillary elevation balance. The liquid normally used for this
purpose is water.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Contact Angle Measurement
Cristiana Boi
Sessile drop method
This method consists of placing a drop of liquid (generally water)
on the surface of the membrane.
The wettability of the surface is then characterized by the contact
angle between the solid surface and the tangent to the liquid
surface at the contact point.
• ϑ=0 solid is perfectly wettable by
the liquid (hydrophilic if the liquid is
water);
• ϑ <π/2 more or less wettable;
• ϑ >π/2 more or less not wettable
(hydrophobic if the liquid is water).
C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Contact Angle Measurement
Cristiana Boi
Captive bubble method
Used when membrane properties do not allow the contact angle
to be measured by placing a drop on the surface.
The membrane is immersed in water with the surface to be
analyzed facing downward. A micro-syringe is then used to trap an
air bubble on the lower surface of the membrane.
C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Contact Angle Measurement
Cristiana Boi
Capillary Elevation Balance
For membranes with nonplanar geometry, such as hollow
fibers, another method can be envisaged. It consists of
measuring the weight gained by a material placed in contact
with a liquid as a function of time. The speed at which a given
liquid spontaneously penetrates a porous solid by capillarity
depends directly on the porous structure of the material and
the affinity of the liquid for the material.
CONFIDENTIAL: NOT FOR DISTRIBUTION
Contact Angle Measurement
Cristiana Boi
 The values obtained for contact angles depend on the
measuring technique used;
 Moreover, they also depend on many factors connected
with how the sample is prepared and the characteristics of
the zone analyzed (local roughness, porosity, heterogeneity
in the surface chemical composition, etc.).
 It has been shown that the more porous a membrane is,
the more hydrophilic it appears to be.
It is preferable to use these methods to establish a
comparative classification of membranes, all other things
being equal.
CONFIDENTIAL: NOT FOR DISTRIBUTION

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Membrane characterization

  • 1. Characterization of filtration membranes Course of Bioreactors and Downstream Processes M cristiana.boi@unibo.it CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 2. Membrane characterization Cristiana Boi  The characterization of membrane properties helps not only to choose the right membrane for a given application, but also to gain a better understanding of their preparation methods and on the selectivity and fouling mechanisms.  The methods used give access to macroscopic or microscopic quantities, characteristic of the membrane structure and the chemistry of the material. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 3. Membrane choice Cristiana Boi Structural and transfer characteristics (hydraulic permeability and selectivity curve) provide information on how the membrane will perform in the intended separation process: the permeate flow that can be expected and the size of molecules likely to be rejected by the membrane. Surface physicochemical and chemical properties (charge, hydrophilic–hydrophobic nature, and chemical composition), which allow fouling and interactions among the different types of molecules at the membrane surface to be predicted to some extent. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 4. Characterization methods Cristiana Boi Membrane characterization methods can be divided in two categories:  for the chemical and structural properties of the membrane;  for the functional properties, such as selectivity or permeability. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 5. Structural Characteristics Cristiana Boi The characterization methods developed for obtaining information on the membrane structure can be divided into three types:  microscopy techniques;  liquid intrusion or displacement techniques;  techniques that measure tracer molecule retention. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 6. Microscopy Techniques Cristiana Boi These techniques provide information on surface topology, roughness, and pore size. Several microscopic observation methods are used, which differ by their implementation and their resolution.  Electron microscopy (SEM, TEM);  Near Field Microscopy (STM, AFM);  X-ray synchrotron microtomography. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 7. Principles of Electron Microscopes Cristiana Boi CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 8. Applications of SEM Cristiana Boi SEM is be an effective method for: 1. characterizing flat membranes; 2. assessing the effect of preparation conditions on the structure of hollow fiber membranes; 3. observing the evolution of membrane morphology after contact with washing solutions; 4. measuring the thickness of deposits (0.2–0.4 µm) formed during membrane fouling. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 9. SEM image of a polysulfone hollow fiber membrane (MWCO: 40 kDa) Cristiana Boi C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 10. Schematic description of a (STM) Cristiana Boi C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 11. Example of STM of a membrane Cristiana Boi Image of a 100 kDa polysulfone membrane obtained by scanning tunneling microscopy (STM); (b) Cross sections corresponding to the lines drawn in the picture 5 (middle-bottom). Bessieres, A., Meireles, M., Coratger, R., Beauvillain, J., Sanchez, V. J. Membr. Sci. 1996, 109, 271–284. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 12. Example of an AFM of a membrane Cristiana Boi (a) Example of an image of a tracked etched polycarbonate membrane (Nuclepore) – nominal pore size : 0.2 µm; (b) same sample – blow-up (1000x1000)nm2; and (c) cross section along the line drawn in picture (a). C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 13. Comparison STM and AFM Cristiana Boi CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 14. X-ray synchrotron microtomography Cristiana Boi 3D reconstruction volume of a part of a PVDF hollow fiber microfiltration membrane from SRµCT. Dimensions of the observed volume are 420 µm x 320 µm x 190 µm. Remigy, J.C., Meireles, M., Thibault, X. J. Membr. Sci. 2007, 305, 27–35. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 15. Displacement Techniques Cristiana Boi These methods consist of wetting the membrane with a wetting agent (phase 1) of known surface tension and contact angle with the membrane, then expelling it from the membrane pores by displacing it with a second phase (phase 2), which is generally air or an immiscible liquid.  bubble point;  liquid/gas displacement;  liquid–liquid porometry. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 16. Bubble point Cristiana Boi In the bubble point method, the pores of the membrane are completely wet with a liquid (phase 1) which is then displaced with air (phase 2). The Young–Laplace equation allows the maximum pore radius to be calculated from the value of the transmembrane pressure measured when the first bubbles are detected in the permeate compartment: where γL is the surface tension of the liquid (N m-1) and ϑ the contact angle between the liquid and the membrane surface. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 17. Mercury intrusion Cristiana Boi Variant of the bubble point method in which phase 1 is air and phase 2 is mercury that is gradually forced into the membrane pores. Mercury has a very small contact angle with most materials. Both bubble point and mercury intrusion have the drawback that they require very high pressures (from 1 to several kilobars) to analyze pores of the order of 10 nm like those found in ultrafiltration membranes. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 18. Liquid–liquid porometry Cristiana Boi This method consists of wetting the membrane with a wetting liquid (phase 1) then expelling the liquid from the membrane pores by displacing it with another liquid (phase 2) that is immiscible with the former. The pressure that has to be applied depends directly on the interfacial tension between the two liquids. Thus, by a appropriate choice of the liquid 1- liquid 2 pair (based on a water–isobutanol–methanol combination), the pressures to be applied for the analysis of small-radius pores need not exceed 10 bar or so. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 19. Liquid–liquid porometry Cristiana Boi Example of a bi-modal pore-size distribution obtained on an ultrafiltration membrane by bi-liquid porometry (liquid mixture: methanol, isobutanol, 1 butanol and water; interfacial tension between organic phase and aqueous phase: 0.35mN-1m). C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 20. Water permeability Cristiana Boi In the presence of a pure solvent, any increase in transmembrane pressure leads to a proportional increase in the permeate volume flux density which allows the membrane to be considered as an ideal porous medium. The coefficient of proportionality, Lp (assumed constant), is called the hydraulic permeability of the membrane and depends on its intrinsic characteristics: porosity, pore-size distribution, thickness, and hydrophilic nature. This parameter (Lp) thus represents the volume of solvent that passes through the membrane per unit of pressure, filtering area, and time. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 21. Water permeability Cristiana Boi From tests with pure water, the permeability of the membrane can be determined by means of Darcy’s law: Deviations from linearity may arise from the compressibility of the membrane, or from the retention of some impurities remaining in the retentate compartment. J : flux density (m s-1), Q : pure solvent filtration rate (m3 s-1), A : filtering surface area (m2), Lp : hydraulic permeability of membrane (m), µ : dynamic viscosity of pure solvent (Pa s), P : transmembrane pressure (Pa) Rm: hydraulic resistance of membrane (m-1) CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 22. Tracer Retention Techniques Cristiana Boi Tracer retention techniques measure the transfer of macromolecules (ultrafiltration) of calibrated particles called tracers, and these measurements are then compared with a transport model. The principle is to measure the retention of a series of tracers of different sizes so as to obtain a curve of selectivity versus molar mass (or size) of the molecules CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 23. Choice of Tracers Cristiana Boi The tracers used must fulfill several criteria:  have few specific interactions with the membrane material or the macromolecules that may be absorbed on to the membrane to account for its intrinsic characteristics;  have molar masses (or sizes) that cover the broadest retention range possible, especially in the region close to 100%;  be detectable even at very low concentrations in the collected permeate. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 24. Examples of Tracers Cristiana Boi C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 25. Applicability of tracer retention methods Cristiana Boi  Method is suitable for UF membranes: dextrans, PEGs and proteins are used as tracers;  NF membranes: the tracer can be small PEGs, sugars or inorganic salts;  RO: NaCl as a tracer. Membranes for water desalination have 99% NaCl rejection, while membranes for brackish water have 96% rejection. For MF membranes is very difficult apply since there are only a few suitable tracers of sufficient size (polyethylene oxide, high MW dextrans). CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 26. Selectivity curve Cristiana Boi Selectivity curve for dextran molecules: MWCO (molecular weight of a molecule rejected at 90% by the membrane) is 85 kDa C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 27. Microbiological Tracers Cristiana Boi Microbiological tracers are used because membranes have been considered as potential screens against microbiological contamination of waters or air.  Bacteria;  Viruses;  Surrogates. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 28. Microbiological Tracers Cristiana Boi In general, filtration reduces the content in microorganisms, but does not guarantee their complete elimination. The reduction in microorganisms is often measured by the log removal value (LRV), defined as The maximum LRV that can be claimed depends on the concentration of bacteria in the challenging suspension. For example, if the concentration is 106 cfu/ml in the retentate and zero in the permeate, one counts 1 cfu/ml in the latter and the LRV is then 6. P F c c LRV 10 log  CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 29. Bacteria Cristiana Boi The first discrimination was done between filters rated 0.2 and 0.45 µm, by using Brevundimonas diminuta; several bacteria are used for membrane characterization, as for example CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 30. Virus Cristiana Boi Most viruses are two orders of magnitude smaller than bacteria. Differences in membrane characterization:  higher diffusivity;  surface interactions in their behavior. In particular, viruses have a strong tendency to adsorb onto surfaces. For this reason, the apparent retention of viruses by membranes may be much higher than the actual filter capacity. Experiments of virus retention are performed in the worst- case conditions: this will guarantee that when in operation, the membrane will show either the same or a better retention of the viruses. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 31. Surrogates Cristiana Boi Surrogates of the microorganisms, which would mimic their behavior and allow simpler and faster membrane characterization. Latex or silica particles, and gold sols have therefore been used. Thus far, two major drawbacks have been pointed out:  the much lower sensitivity of the particle detection methods, which limits the range of LRV that can be explored;  the difference in surface properties (charge, stiffness, hydrophilic character, etc..) between such surrogates and bioparticles, which induces a difference in retention, as, for example, by charge exclusion, by adsorption on or in the membrane material. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 32. Determination of Hydrophilic/ Hydrophobic Nature of Membranes Cristiana Boi The hydrophilic nature of a material is a very important parameter as it conditions the solute-membrane and solvent- membrane interactions. In many applications, hydrophilic membranes are more efficient than hydrophobic ones, the latter being confronted with more serious fouling whenever hydrophobic molecules or particles (proteins, colloids, etc.) are present in the fluid to be filtered. The same is true for surfactants, the adsorption of which is more pronounced on hydrophobic materials. The hydrophilic/hydrophobic nature of a membrane is determined by measuring the contact angle or by using the capillary elevation balance. The liquid normally used for this purpose is water. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 33. Contact Angle Measurement Cristiana Boi Sessile drop method This method consists of placing a drop of liquid (generally water) on the surface of the membrane. The wettability of the surface is then characterized by the contact angle between the solid surface and the tangent to the liquid surface at the contact point. • ϑ=0 solid is perfectly wettable by the liquid (hydrophilic if the liquid is water); • ϑ <π/2 more or less wettable; • ϑ >π/2 more or less not wettable (hydrophobic if the liquid is water). C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 34. Contact Angle Measurement Cristiana Boi Captive bubble method Used when membrane properties do not allow the contact angle to be measured by placing a drop on the surface. The membrane is immersed in water with the surface to be analyzed facing downward. A micro-syringe is then used to trap an air bubble on the lower surface of the membrane. C Causserand and P Aimar in Comprehensive Membrane Science and Engineering, Drioli and Giorno Eds, 2010 Elsevier. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 35. Contact Angle Measurement Cristiana Boi Capillary Elevation Balance For membranes with nonplanar geometry, such as hollow fibers, another method can be envisaged. It consists of measuring the weight gained by a material placed in contact with a liquid as a function of time. The speed at which a given liquid spontaneously penetrates a porous solid by capillarity depends directly on the porous structure of the material and the affinity of the liquid for the material. CONFIDENTIAL: NOT FOR DISTRIBUTION
  • 36. Contact Angle Measurement Cristiana Boi  The values obtained for contact angles depend on the measuring technique used;  Moreover, they also depend on many factors connected with how the sample is prepared and the characteristics of the zone analyzed (local roughness, porosity, heterogeneity in the surface chemical composition, etc.).  It has been shown that the more porous a membrane is, the more hydrophilic it appears to be. It is preferable to use these methods to establish a comparative classification of membranes, all other things being equal. CONFIDENTIAL: NOT FOR DISTRIBUTION