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Adsorption and Catalysis

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Presentation on theme: "Adsorption and Catalysis"— Presentation transcript:

1 Adsorption and Catalysis
Dr. King Lun Yeung Department of Chemical Engineering Hong Kong University of Science and Technology CENG 511 Lecture 3

2 Physical Adsorption Texture and morphology
specific surface area of catalyst pore size pore shape pore-size distribution (same size or various sizes?) pore volume

3 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

4 Pore Size and Shape Pore Structure Silica Carbon Zeolite

5 Pore Size and Shape Why is it important?
it dictates the diffusion process through the material.

6 Pore Size and Shape Why is it important?
directly affect the selectivity of the catalytic reaction.

7 Pore Size and Shape Measurement Techniques 1 10 100 1000 10000
Pore diameter (nm) Micro Meso Macro N 2 capillary condensation Hg porosimetry

8 N2 Physisorption Adsorption and Desorption Isotherms Desorption

9 N2 Physisorption Adsorption and Desorption Isotherms III n p / VI V I
VI V I II B IV

10 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

11 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

12 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

13 Physisorption Surface area measurement

14 Physisorption Different Adsorbates Used in Physisorption Studies

15 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

16 BET Isotherm

17 BET Isotherm

18 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

19 Pore Size and Surface Area

20 Pore Size Distribution
Kelvin Equation

21 Pore Size Distribution
Kelvin Equation Cylindrical pore Ink-bottle pore Pore with shape of interstice between close-packed particles Adsorbed layer t dp dm

22 Kelvin Equation

23 Kelvin Equation Pore filling Model Cylindrical Pore Channel

24 Hysteresis Loop Information on pore shape

25 Pore Size Distribution
t-Method nad t Proportional to St Note: nad is experimental result t is calculated from correlation t versus p

26 Kelvin Equation t-Method

27 Kelvin Equation Shape of t-plots

28 Kelvin Equation Interpretation of t-Plot -alumina

29 Kelvin Equation Pore Size Distribution -alumina r = t + 2V RTIn P0 P

30 Mercury Porosimetry Pore Size Distribution

31 Mercury Porosimetry Pore Size Distribution -alumina

32 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

33 Texture Data on Common Catalysts

34 N2 Adsorption Isotherms & Pore Volume Distributions
wide-pore silica -alumina

35 N2 Adsorption Isotherms & Pore Volume Distributions
-alumina activated carbon

36 N2 Adsorption Isotherms & Pore Volume Distributions
Raney Ni ZSM-5

37 Hg Intrusion Curves & Pore Volume Distributions
wide-pore silica -alumina

38 Hg Intrusion Curves & Pore Volume Distributions
-alumina activated carbon

39 Hg Intrusion Curves & Pore Volume Distributions
Raney Ni ZSM-5

40 BET- & t-plots wide-pore silica -alumina

41 BET- & t-plots -alumina activated carbon

42 BET- & t-plots Raney Ni ZSM-5

43 Chemisorption Surface Characterization Specific surface area of phases
Types of active sites Number of active sites Reactivity of active sites Stability of active sites

44 Chemisorption Metal Dispersion

45 Adsorption Mode

46 Adsorption Stoichiometry

47 Particle Size and Dispersion

48 Supported Metal Particles

49 Number of Surface Atoms

50 Pulse Chemisorption

51 Monolayer capacity: 0.06 mmol / g Pt
Pulse Chemisorption On-line Thermoconductivity Detector Monolayer capacity: mmol / g Pt

52 Step Chemisorption On-line Mass Spectrometer

53 Temperature Programmed Desorption
Adsorption Site Differentiation NH3 desorption from HZSM-5

54 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

55 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]

56 Temperature Programmed Reduction
characterisation of oxidic catalysts and other reducible catalysts qualitative information on oxidation state quantitative kinetic data optimisation of catalyst pretreatment

57 Temperature Programmed Reduction
Fe2O3

58 Temperature Programmed Reduction
Fe2O3 Dry H2/Ar

59 Temperature Programmed Reduction
Fe2O3 Wet H2/Ar (3% H2O)

60 Temperature Programmed Reduction
Fe2O3

61 Kinetic Models for Reduction

62 Infrared Spectroscopy

63 Infrared Spectroscopy
Reactor Cell Transmittance DRIFTS

64 Analysis of Catalyst Preparation
Surface Hydroxyl Groups NH4ReO4 Alumina Dry impregnation Drying 383 K, 16 h Calcination 323 K, 2 h Re2O7/ Alumina

65 Analysis of Catalyst Preparation

66 IR Probe Molecule Acidity Measurement

67 IR Probe Molecule Acidity Measurement

68 Kelvin Equation Pore Size Distribution

69 Kelvin Equation Pore Size Distribution

70 In-Situ Reaction Study
TCE Photocatalytic Oxidation

71 In-Situ Reaction Study
PCO of Ethylene

72 In-Situ Reaction Study
PCO of 1,1-DCE

73 In-Situ Reaction Study
PCO of cis-1,2-DCE

74 In-Situ Reaction Study
PCO of trans-1,2-DCE

75 In-Situ Reaction Study
PCO of TCE

76 In-Situ Reaction Study
PCO of Tetrachloroethylene


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