Characterization of Pore Structure: Foundation

Name: Characterization of Pore Structure: Foundation
Uploaded: 2017-07-05T07:57:07+00:00
Duration: PTM28S7
Channel: Aliyah Curlin
Description: Characterization of Pore Structure: Foundation

Characterization of Pore Structure: Foundation
Dr. Akshaya Jena Director of Research Porous Materials, Inc., USA

Topics Pore structure Characteristics of pore structure
Characterization techniques Extrusion Flow Porometry Liquid Extrusion Porosimetry Mercury Intrusion Porosimetry

Topics Conclusions Nonmercury Intrusion Porosimetry Vapor Adsorption
Vapor Condensation Conclusions

Typical Pore Structure

Three Different Kinds of Pores
Pore Structure Three Different Kinds of Pores

Characteristics of Pore Structure

Characteristics of Pore Structure
Effects of application environment on pore structure characteristics

Characterization Techniques

Extrusion Flow Porometry (Capillary Flow Porometry)
Principle Displacement of a wetting liquid from a pore Wetting liquid: Flows spontaneously into pores

Principle Displacement of a wetting liquid from a pore For displacement of wetting (gs/l<gs/g) liquid from a pore by a gas Work done by gas = Increase in interfacial free energy

For all small displacement of liquid

p d V = gs/g dSs/g+ gs/l dSs/l + gl/g dSl/g p = differential pressure dV = infinitesimal increase in volume of the gas in the pore dSs/g = infinitesimal increase in interfacial area For a wetting liquid: p = gl/g cos q (dSs/g/dV) (dSs/g/dV) = measure of pore size

For most pores size not defined Types of pore cross-section

Definition of pore diameter, D [dS/dV](pore) = [dS/dV](cylindrical opening of diameter, D) = 4/D D = [4gl/g cos q]/p

Test Method Dry Curve Flow rate, F versus p for a dry sample

Test Method For viscous flow F = [/(256m l ps)]iNiDi4][pi + po]p  = a constant m = viscosity of gas l = thickness ps = standard pressure Ni = number of pores of diameter Di p = differential pressure, inlet pressure, pi minus outlet pressure, po

Dry curve normally concave upward Membranes showing three different ways in which flow rate may vary with differential pressure

Others possible shape of dry curve because of: High pressure Nonviscous flow Tortuous paths for flow High flow rate Pore diameter Interaction of sample with liquid

Wet Curve F versus p for a wet sample Initially there is no gas flow The largest pore is emptied first and gas flow begins With increase in differential pressure smaller pores are emptied and gas flow increases When all pores are empty wet curve converges with the dry curve with the dry curve

Equipment The PMI Capillary Flow Porometer

Measurable Characteristics Through pore Throat Diameter The technique measured only the throat diameter Variation of pore size along pore path and the measured pore diameter

The largest pore diameter (Bubble Point Pore Diameter) Bubble point pressure in F vs p plot.

Mean flow pore diameter Dry, wet and half-dry curves for a filter and the mean flow pressure

Pore diameter range Largest - Bubble point pressure Lowest - pressure at which wet and dry curves meet

Distribution: F = [/ (256 l ps)] [iNiDi4][pi+po]p (F w,j / Fd,j) = [g(D,N, …)]w,j/[g(D,N,…)]d,j Cumulative filter flow [(F w,j / Fd,j)x100]

Cumulative filter flow

Flow distribution over pore diameter fF = - d[Fw/Fd)x100]/dD Flow distribution over pore diameter [(Fw/Fd)x100] = D1D2[-fFdD] Area in a pore size range = % flow in that size range

Fractional pore number distribution Fractional pore number = Ni/iNi Fractional pore number distribution

Liquid permeability Computed from flow rate at average pressure using Darcy’s law F = k (A/ml)(pi-po) Change of flow rate of water through paper as a function of differential pressure

Gas permeability Computed from flow rate at STP F = k (A/2mlps)(pi+po)[pi-po] Can be expressed in any unit: Darcy Gurley Frazier Rayls Flow of air through a filter

Envelope Surface Area Based on Kozeny-Carman relation [F l/p A] = {P3/[K(1-P)2S2m]} + [ZP2p]/[(1-P) S (2ppr)1/2 F = gas flow rate in volume at average pressure, p per unit time p = average pressure, [(pi+po)/2], where pi is the inlet pressure and po is the outlet pressure

Envelope Surface Area F = gas flow rate in volume at average pressure, p per unit time p = average pressure, [(pi+po)/2], where pi is the inlet pressure and po is the outlet pressure l = thickness of sample p = pressure drop, (pi - po) A = cross-sectional area of sample P = porosity (pore volume / total volume) = [1-(rb/ra)]

Envelope Surface Area rb = bulk density of sample ra = true density of sample S = through pore surface area per unit volume of solid in the sample m = viscosity of gas r = density of the gas at the average pressure, p K = a constant dependent on the geometry of the pores in the porous media. It has a value close to 5 for random pored media Z = a constant. It is shown to be (48/13p).

Summary Flow Porometry measures a large variety of important pore structure characteristics. Results particularly relevant for filtration media Toxic materials, high pressures & subzero temperatures not used A highly versatile technique

Extrusion Porosimetry
Principle Prevention of gas from flowing out after displacing wetting liquid in pore Place membrane under the sample Largest pore of membrane <Smallest pore of interest in sample p(to empty sample pores)<p(to empty membrane pores) D = [4 gl/g cos q]/p

Principle of extrusion porosimetry Displaced liquid flows through membrane & measured

Principle of extrusion porosimetry Gas that displaces liquid in sample pores does not pass through membrane

Test method Differential pressure yields pore diameter Extruded liquid (weight or volume) gives pore volume

Equipment PMI Liquid Extrusion Porosimeter

Measurable Characteristics Through pore volume Pore volume plotted against differential pressure

Through pore diameter Measured pore volume plotted against pore diameter

Through pore volume distribution Distribution function fv = -(dV/d logD) Pore Volume distribution function Area in any pore size range = volume of pores in that range

Through pore surface area Integration of Equation: p = gl/g cos q (dSs/g/dV) S = p dV/(gl/g cos q) Not very accurate Sensitive to pore configuration Over estimates volume of pore throat

Liquid permeability From liquid flow rate Liquid flow rate as a function of differential pressure

Summary Only technique that permits measurement of through pore volume Does not use toxic materials, high pressures and subzero temperatures.

Mercury Intrusion Porosimetry
Principle Intrusion of a non-wetting liquid in to pore Non-wetting liquid cannot enter pores spontaneously gs/l >gs/g

Pressurized liquid can enter pores Work done by the liquid = Increase in interfacial free energy (p-pg) dV = (gs/l -gs/g) ds  P = (-gl/g cos q) (dS/dV)

From definition of pore diameter (dS/dV) pore = (dS/dV) circular opening of diameter, D = 4/D p = -4gl/g cos q/D

Test Method Measured intrusion pressure yields pore diameter Measured intrusion volume of mercury yields pore volume

Equipment The PMI Mercury Intrusion Porosimeter

Mercury Intrusion Porosimeter
Measurable Characteristics Through and blind pore volume Intrusion volume with pressure

Through and blind pore diameter Measurable pore diameters

Through and blind pore diameter Cumulative pore volume with pore diameter

Through and blind pore diameter Examples of pore configurations in which some of the diameters are not measurable

Pore Volume distribution fv = -(dV/d log D) Pore size distribution Area in a size range = Pore volume in that range

Through and blind pore surface are S = [1/(-gl/g cos q)] p dV Cumulative surface area

Surface area not very accurate Wide parts of ink-bottle pores measured as pores with neck diameter Inkbottle pore

Surface area not very accurate For very small pores, large pressure increases cause small increases in volume. The integral is less accurate. At high pressures, correction terms in the small volume of small pores is appreciable

Mercury Intrusion Porosiemtry
Extrusion volume and hysteresis Hysteresis in the intrusion-extrusion cycle

Inkbottle pore

Summary Almost any material can be tested - mercury in non-wetting to most materials No flow characteristics are measurable Uses toxic materials and high pressures

Non-Mercury Intrusion Porosimetry
Principle Exactly same as mercury intrusion porosimetry Non-wetting intrusion liquid is NOT MERCURY Water Oil Application liquid

Measurable Characteristics All characteristics measurable by mercury intrusion porosimetry - measurable

Measurable Characteristics Advantages over Mercury Intrusion Porosimetry No toxic material used An order of magnitude low pressures used Smaller pores measurable Can measure one kind of pores in a mixture like the mixture of hydrophobic and hydrophilic pores

Summary Can measure all characteristics measurable by Mercury Intrusion without using any toxic material or high pressures Can detect one kind of pore in a mixture

Adsorbed layers of molecules on a surface
Vapor Adsorption Principle Physical Adsorption Weak van der Waal’s type interaction with surface Multi-layer adsorption Adsorbed layers of molecules on a surface

Vapor Adsorption BET theory of physical adsorption
[p/(po-p)W] = [1/(WmC)] + [(c-1)/WmC](p/po) W = amount of adsorbed gas Wm = amount of gas that can form a monomolecular layer C = a dimensionless constant = (A1v2/A2v1) exp [(E-L)/RT]

Vapor Adsorption [p/po-p)W]versus(p/po)-linear
Wm = 1/[(intercept)+(slope)] Surface area: S = WmNoa No = Avogadro’s number a = cross-sectional area of the adsorbed gas molecule

Vapor Adsorption Chemisorption
Chemical interaction between the gas and the surface Only one layer of molecules gets bonded to the material

Vapor Adsorption Model for chemisorption (Langmuir)
p/W = [1(KWm)]+p[1/Wm] p = pressure of gas W = amount of adsorbed gas K = Ko exp(E/RT) Wm = amount of adsorbed gas for a completed monomolecular layer

Vapor Adsorption Test Method Sample maintained at constant temperature
Volumetric method: A known amount of gas is introduced in to the sample chamber of known volume Amount of gas left in the sample chamber is computed from change in gas pressure

Vapor Adsorption Test Method Gravimetric method
Weight gain of sample in the sample chamber is measured

Vapor Adsorption Equipment The PMI Sorptometer

Vapor Adsorption Measurable Characteristics
Through and blind pore surface area Multipoint surface area [p/(po-p)W]versus(p/po)linear in the range 0.05< (p/po)<0.35 Plot of [p/(po-p)W]versus (p/po)

Plot of [p/(po-p)W]versus (p/po)
Vapor Adsorption Plot of [p/(po-p)W]versus (p/po)

Vapor Adsorption Single point surface area
Assuming large C, Wm, is computed from a single measurement Good approximation for large C

Vapor Adsorption Chemisorption
Chemisorption of many chemicals measurable Water Carbon monoxide Carbon dioxide Poisonous chemicals Many others Over a wide range of temperature and pressure

Chemisorption of ammonia at 25C plotted after p/W = [1/KWm)]+p[1/Wm]
Vapor Adsorption Chemisorption of ammonia at 25C plotted after p/W = [1/KWm)]+p[1/Wm] /

Vapor Adsorption Summary Technique determines surface area accurately
Both through pore and blind pore surface areas are measured.

Vapor Condensation Principle Condensation of vapor in pore
Condensation in pore

Vapor Condensation  G[v(p)l (pore)]
dV({G[v(p)l(bulk)]}/V) +dSGs[s/vs/l] = 0 dV = volume of condensed liquid V = molar volume of liquid dS = solid/liquid interfacial area

Vapor Condensation dV({G[v(p)l(bulk) = G[v(p)v(po)] = RT ln (po/p)
Gs[s/vs/l] = (gs/l - gs/v) ln(p/po) = -[4Vgl/v cos q/RT]/D

Vapor Condensation Definition of pore diameter (dS/dV) Pore
= (dS/dV)Cyliderical opening of diameter, D = 4/D ln(p/po) = -[4Vgl/v cos q/RT]/D

Vapor Condensation Test method Measures relative vapor pressure (p/po)
Measures amount of condensed vapor At a given pressure

Vapor Condensation Equipment The PMI Sorptometer

Variation of cumulative pore volume with relative pressure
Vapor Condensation Measurable Characteristics Through and blind pore volume Condensation occurs in through & blind pores Variation of cumulative pore volume with relative pressure

Vapor Condensation Through and blind diameter
Diameter of pore from condensation ln(p/po) = -[4V gl/v cos q/RT]D Prior to condensation, pores contain adsorbed films True pore radius, rp rp = (D/2)+t t = thickness of adsorbed layer

Variation of cumulative pore volume with pore diameter
Vapor Condensation Variation of cumulative pore volume with pore diameter

Vapor Condensation Pore Volume Distribution
Distribution function fv: fv = -(dV/dD) Pore size distribution by gas adsorption Area in any pore diameter range = volume of pores in that range

Vapor Condensation Pore structure of materials containing very small pores Type of pores Macropores: >0.05mm Mesopores: mm Micropores: <0.002mm

Vapor Condensation Pore structure of materials containing very small pores Capability Technique: mm Validity of relations:  mm For micropores data need to be analyzed using other models

Adsorption and desorption isotherms
Vapor Condensation Adsorption and desorption isotherms and hystersis Adsorption and desorption isotherms

Adsorption/desorption isotherms for chemisorption of ammonia at 25C
Vapor Condensation Adsorption/desorption isotherms for chemisorption of ammonia at 25C

Vapor Condensation Shape of adsorption curve  many factors
Large number of larger pores  High adsorption at high pressure Large number of small pores  saturation Strong interaction of adsorbate with the adsorbed  increasing adsorption

Examples of a few different type of adsorption curves
Vapor Condensation Examples of a few different type of adsorption curves

Vapor Condensation Summary
Measure volume and diameter of very small through and blind pores No other technique can measure such characteristics

Conclusions Extrusion Techniques
Two recent techniques Extrusion Flow Porometry & Liquid Extrusion Porosimetry have been discussed in detail

Conclusions The techniques are capable of measuring a wide variety of pore structure characteristics of through pores including fluid flow characteristics, which other techniques cannot measure

Conclusion All characteristics particularly relevant for filtration are measurable The techniques do not use toxic materials, high pressures or subzero temperatures

Conclusion Mercury Intrusion Techniques
The widely used mercury intrusion porosimetry has been briefly discussed This technique can measure pore volume and pore diameters of through and blind pores in almost any material

Conclusion Fluid flow characteristics cannot be measured
Uses very high pressures and mercury, which is toxic

Conclusion Non- Mercury Intrusion Techniques
The novel technique non-mercury intrusion porosimetry has been discussed This technique can measure pore volume and diameter of through and blind pores like mercury intrusion porosimetry

Conclusion No toxic material is used and pressure required is almost an order of magnitude less.

Conclusion Gas adsorption & condensation techniques
The widely used gas adsorption and condensation techniques were discussed briefly These techniques can measure surface area, pore diameter and pore volume of through and blind pores Characteristics of very small pores are measurable

Conclusion Flow properties are not measurable
Many require subzero temperatures

Thank You

Characterization of Pore Structure: Foundation

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