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FLASHCARDS - Heterogeneous Catalysis

Sulivan González Catalysis Degree Englisch 36 Karten

FLASHCARDS - Heterogeneous Catalysis

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  1. 1Benefits of Heterogeneous Catalysts (3 P)- Easier recovery (filtration)
    -- Easier to use in continuous (flow) reactors
    - Easier to handle (eg. strong acids)
    - Nearly all are porous: v. important property
  2. 2Surface area formular = radius
    n = no. of pores
    l = length of cube
    Surface area formula
  3. 3IUPAC definition... size for: 1) Micropores 2) Mesopores 3) Macropores1) <2.0 nm
    2) 2 - 50 nm
    3) >50 nm
  4. 4Variable surface chemistryVariable surface chemistry
  5. 52D Materials: - Clays2D Materials: - Clays
  6. 6Clays - neutral, no catalyst activity --> Isomorphous substitution: inserts charge into system: more active catalystClays - neutral, no catalyst activity --&gt; Isomorphous substitution: inserts charge into system: more active catalyst
  7. 7Clays: - Effect of isomorphous substituion- Bronsted acid: Charge polarises OH
    - No direct \(H^{+}\) exchange as it will dissolve the material
    Clays: - Effect of isomorphous substituion
  8. 8Clays: - Effect of isomorphous substituion 2- Hydrated interlayer gaps reduce catalyst activity --> DRY
    - BUT, drying makes interlayers come closer together, so slower catalysis --> COMPROMISE
    Clays: - Effect of isomorphous substituion 2
  9. 9Catalyst activationCatalyst activation
  10. 10Pillaring cations Layer collpase - problem especially w/ high charge density cationsReplace a (eg) \(Na^{+}\) w/ this: Gap maintained even when heated (dried)Pillaring cations Layer collpase - problem especially w/ high charge density cations
  11. 11Reactions of claysReactions of clays
  12. 12Other layered materialsOther layered materials
  13. 133D Catalysts - Microporous systems3D Catalysts - Microporous systems
  14. 14Catalytic sites within zeolitesCatalytic sites within zeolites
  15. 15Acidic ZeolitesAcidic Zeolites
  16. 16Pore size and diffusionAperture diameter used to define narrowest entry point
    - Ring size defined by no. of O atoms present (= no. of Si + heteroatoms)
    - Apreture dimensions between 0.4-0.75 nm
  17. 17Pore size and diffusion 2: (3 P)- Molecular: pores >> molecule
    - Knudsen: pores > molecule
    - Configurational: pores \(\simeq\) molecule
    Pore size and diffusion 2: (3 P)
  18. 18Diffusion in porous materials depend on: (3 P)1) Pore diameter
    2) Connectivity (move & connect between pores: more degrees of freedom --> better catalytic activity)
    3) Tortuosity
    Diffusion in porous materials depend on: (3 P)
  19. 195 stages involved in a liquid phase reaction using a porous solid catalyst - NOTE: for gas phase reactions, thickness of hydrodynamic layer = 0, so 1) and 5) can be omitted1) Diffusion of reactants through hydrodynamic layer
    2) Diffusion of reactants through pore system
    3) Reaction
    4) Diffusion of products through pore system
    5) Diffusion of products through hydrodynamic layer
    - For 1) & 2), parameters influencing the rate are: Thickness of hydrodynamic layer & pore size/geometry respectively
  20. 205 stages involved in a liquid phase reaction using a porous solid catalyst 2 - Optimizing performance:- 1) & 5) --> Heating: viscosity drops, rate increases.
    Stirring: hydrodynamic layer decreases, rate increases
    - 3) If high \(E_a\) --> heating increases rate
    - Low \(E_a\) suggests process is diffusion controlled
    - To distinguish between each: If RDS is 1), 5), 2) & 4), stirring will increase rate for 1) and 5), NOT for 2) and 4)
    NOTE: Increasing temperature does NOT increase rate of 2) and 4)
  21. 21Test for diffusion control- Diffusion dependent on pore size & pore size is not temperature dependent.Test for diffusion control
  22. 22How is pore size measured (2 P):- X-ray diffractions (work for crystalline systems)
    - Porosimetry: Gives pore size of porous solids. Adsrobtion of gas (eg N2) onto a solid over a range of partial pressures at the b.p of the gas
    Stage 1: low partial pressure - monolayer of gas on surface (surface area calc.)
    Stage 2: higher partial pressure - pores fill with liquid N2 to stabilise the meniscus (pore size calc.)
  23. 23How is pore size measured - PorosimetryHow is pore size measured - Porosimetry
  24. 24Measuring acidity of zeolites- Desorption of ammonia: Higher temp of desorp. higher the acidity
    - Acidic strength \(\propto\) 1/Al content
    - Concentration of sites \(\propto\) Al content
    Measuring acidity of zeolites
  25. 25Shape selectivity - Key property of zeolites (eg H-ZSM5)Selectivity based on shape/size rather than electronic propertiesShape selectivity - Key property of zeolites (eg H-ZSM5)
  26. 26Reactant selectivityReactant selectivity
  27. 27Other uses of zeolitesAS a host for catalytic species (reactants can enter the supercage)
  28. 28Titanium silicates (TS-1): Oxidation catalystTitanium silicates (TS-1): Oxidation catalyst
  29. 29Titanium silicates (TS-1): Oxidation catalyst 2Titanium silicates (TS-1): Oxidation catalyst 2
  30. 30Titanium silicates (TS-1) w/ 2 Ti: Oxidation catalystTitanium silicates (TS-1) w/ 2 Ti: Oxidation catalyst
  31. 31Mesoporous systems - Larger templates give unstable materials. Solution...Micelle Templated Silicas (MTS)Mesoporous systems - Larger templates give unstable materials. Solution...
  32. 32Addition of Heteroatoms to MTSAddition of Heteroatoms to MTS
  33. 33ALMA industrial process Catalyst = \((VO)_2P_2O_7\)ALMA industrial process Catalyst = \((VO)_2P_2O_7\)
  34. 34What is meant by isomorphous substitution in context of porous solidsWhat is meant by isomorphous substitution in context of porous solids
  35. 35—
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FLASHCARDS - Heterogeneous Catalysis
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Sulivan González
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