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Adsorption and Catalysis
Dr. King Lun Yeung Department of Chemical Engineering Hong Kong University of Science and Technology CENG 511 Lecture 3
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Physical Adsorption Texture and morphology
specific surface area of catalyst pore size pore shape pore-size distribution (same size or various sizes?) pore volume
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Pore Size and Shape Pore Diameter Pore Shape micropores (< 2 nm)
mesopores (2 – 50 nm) macropores (> 50 nm) Pore Shape cylinder slit ink-bottle wedge
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Pore Size and Shape Pore Structure Silica Carbon Zeolite
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Pore Size and Shape Why is it important?
it dictates the diffusion process through the material.
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Pore Size and Shape Why is it important?
directly affect the selectivity of the catalytic reaction.
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Pore Size and Shape Measurement Techniques 1 10 100 1000 10000
Pore diameter (nm) Micro Meso Macro N 2 capillary condensation Hg porosimetry
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N2 Physisorption Adsorption and Desorption Isotherms Desorption
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N2 Physisorption Adsorption and Desorption Isotherms III n p / VI V I
VI V I II B IV
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Isotherms Type I Langmuir Adsorption Isotherm Assumptions:
/ Assumptions: homogeneous surface (all adsorption sites energetically identical) monolayer adsorption (so no multilayer adsorption) no interaction between adsorbed molecules
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Isotherms Type II Type IV Multilayer adsorption (starting at B)
/ n ad B Multilayer adsorption (starting at B) Common for pore-free materials Type IV n ad p / B Similar to II at low p Pore condensation at high p
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Isotherms Type III Type IV
n ad p / Strong cohesion force between adsorbed molecules, e.g. when water adsorbs on hydrophobic activated carbon Type IV n ad p / Similar to III at low p Pore condensation at high p
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Physisorption Surface area measurement
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Physisorption Different Adsorbates Used in Physisorption Studies
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N2 Physisorption Adsorption and Desorption Isotherms
Langmuir Adsorption? No: strong adsorption at low p due to condensation in micropores at higher p saturation due to finite (micro)pore volume
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BET Isotherm
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BET Isotherm
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BET Isotherm Nonporous Silica and Alumina Low p/p0:
filling of micropores favoured adsorption at most reactive sites (heterogeneity) High p/p0: capillary condensation BET equation Range 0.05 < p/p0 < 0.3 is used to determine SBET
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Pore Size and Surface Area
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Pore Size Distribution
Kelvin Equation
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Pore Size Distribution
Kelvin Equation Cylindrical pore Ink-bottle pore Pore with shape of interstice between close-packed particles Adsorbed layer t dp dm
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Kelvin Equation
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Kelvin Equation Pore filling Model Cylindrical Pore Channel
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Hysteresis Loop Information on pore shape
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Pore Size Distribution
t-Method nad t Proportional to St Note: nad is experimental result t is calculated from correlation t versus p
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Kelvin Equation t-Method
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Kelvin Equation Shape of t-plots
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Kelvin Equation Interpretation of t-Plot -alumina
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Kelvin Equation Pore Size Distribution -alumina r = t + 2V RTIn P0 P
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Mercury Porosimetry Pore Size Distribution
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Mercury Porosimetry Pore Size Distribution -alumina
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N2 Physisorption versus Hg Porosimetry
Hg cannot penetrate small (micro)pores, N2 can Uncertainty of contact angle and surface tension values Cracking or deforming of samples
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Texture Data on Common Catalysts
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N2 Adsorption Isotherms & Pore Volume Distributions
wide-pore silica -alumina
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N2 Adsorption Isotherms & Pore Volume Distributions
-alumina activated carbon
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N2 Adsorption Isotherms & Pore Volume Distributions
Raney Ni ZSM-5
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Hg Intrusion Curves & Pore Volume Distributions
wide-pore silica -alumina
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Hg Intrusion Curves & Pore Volume Distributions
-alumina activated carbon
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Hg Intrusion Curves & Pore Volume Distributions
Raney Ni ZSM-5
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BET- & t-plots wide-pore silica -alumina
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BET- & t-plots -alumina activated carbon
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BET- & t-plots Raney Ni ZSM-5
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Chemisorption Surface Characterization Specific surface area of phases
Types of active sites Number of active sites Reactivity of active sites Stability of active sites
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Chemisorption Metal Dispersion
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Adsorption Mode
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Adsorption Stoichiometry
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Particle Size and Dispersion
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Supported Metal Particles
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Number of Surface Atoms
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Pulse Chemisorption
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Monolayer capacity: 0.06 mmol / g Pt
Pulse Chemisorption On-line Thermoconductivity Detector Monolayer capacity: mmol / g Pt
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Step Chemisorption On-line Mass Spectrometer
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Temperature Programmed Desorption
Adsorption Site Differentiation NH3 desorption from HZSM-5
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Temperature Programmed Desorption
Adsorption Energetics After ammonia saturation the sample is degassed at 120 °C for 60 minutes Heating Rate of 5, 10, 15 and 20 °C/min
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Temperature Programmed Desorption
Adsorption Energetics 12.49 A factor 24.51 Ed (kJ/mole) 5.4639 Intercept Slope Beta = heating rate [K / min] Tp = maximum desorption peak temperature Ed = Desorption energy [Kj / mole] A = Arrhenius factor R = [J / mol K]
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Temperature Programmed Reduction
characterisation of oxidic catalysts and other reducible catalysts qualitative information on oxidation state quantitative kinetic data optimisation of catalyst pretreatment
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Temperature Programmed Reduction
Fe2O3
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Temperature Programmed Reduction
Fe2O3 Dry H2/Ar
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Temperature Programmed Reduction
Fe2O3 Wet H2/Ar (3% H2O)
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Temperature Programmed Reduction
Fe2O3
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Kinetic Models for Reduction
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Infrared Spectroscopy
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Infrared Spectroscopy
Reactor Cell Transmittance DRIFTS
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Analysis of Catalyst Preparation
Surface Hydroxyl Groups NH4ReO4 Alumina Dry impregnation Drying 383 K, 16 h Calcination 323 K, 2 h Re2O7/ Alumina
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Analysis of Catalyst Preparation
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IR Probe Molecule Acidity Measurement
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IR Probe Molecule Acidity Measurement
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Kelvin Equation Pore Size Distribution
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Kelvin Equation Pore Size Distribution
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In-Situ Reaction Study
TCE Photocatalytic Oxidation
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In-Situ Reaction Study
PCO of Ethylene
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In-Situ Reaction Study
PCO of 1,1-DCE
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In-Situ Reaction Study
PCO of cis-1,2-DCE
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In-Situ Reaction Study
PCO of trans-1,2-DCE
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In-Situ Reaction Study
PCO of TCE
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In-Situ Reaction Study
PCO of Tetrachloroethylene
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