Trickle‐bed reactors: A review

AIChE Journal

Volumn 29, Issue 1, 1983, Pages 1-18

  Herskowitz, Mordechay ^a   Smith, J M ^b  

^a BEN GURION UNIVERSITY OF THE NEGEV   (Israel)

^b UNIVERSITY OF CALIFORNIA   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

EID: 84984102155     PISSN: 00011541     EISSN: 15475905     Source Type: Journal    
DOI: 10.1002/aic.690290102     Document Type: Review

References (110)

1. Effectiveness Factors for General Reaction Rate Forms
2. The Influence of Viscosity on Axial Mixing in Trickle Flow in Packed Beds
3. Effect of Liquid Wetting on Catalyst Effectiveness in Trickle‐Bed Reactors
4. Recent Progress in Two‐Phase Gas‐Liquid Mass Transfer in Packed Beds
5. Transition to Pulsed Flow in Mixed‐Phase Cocurrent Downflow through a Fixed Bed
6. Local Particle‐Liquid Mass Transfer Fluctuations in Mixed Phase Cocurrent Downflow Through a Fixed Bed in the Pulsing Regime
7. Two‐Phase Pressure Drop in Cocurrent Downflow in Packed Beds: Air‐Silicon Oil Systems
8. Dynamic Liquid Holdup in Two‐Phase Downflow in Packed Beds: Air‐Silicone Oil System
9. Liquid‐Solid Contacting Efficiency in Trickle‐Bed Reactors
10. A Computational Model for Predicting and Corelating the Behavior of Fixed‐Bed Reactors
11. Catalyst Effectiveness Factor and Contacting Efficiency in Trickle‐Bed Reactors
12. Interfacial Area and Boundary of Hydrodynamic Flow Region in Packed Column with Cocurrent Downward Flow
13. Liquid‐Phase Volumetric and Mass Transfer Coefficient, and Boundary of Hydrodynamic Flow Region in Packed Column with Cocurrent Downward Flow
14. Absorption in Packed Towers with Cocurrent Downward High‐Velocity Flows
15. Hydrodynamics and Solid‐Liquid Contacting Effectiveness in Trickle‐Bed Reactors
16. Trickle‐Bed Reactor Performance, Part I. Holdup and Mass Transfer Effects
17. Analysis of Three‐Phase Reactors
18. Performance of Trickle‐Bed and Slurry Reactors
19. Trickle‐Bed Oxidation Reactors
20. th Order Kinetics in Trickle‐Bed Reactors
21. Qualitative Observations of Heat and Mass Transfer Effects on the Behavior of a Trickle‐Bed Reactor
22. Measurement of Axial Temperature Profiles in an Adiabatic Trickle Bed Reactor
23. A Cell Model of the Osothermal Trickle‐Bed Reactor
24. Effective Radial Thermal Conductivity in Cocurrent Flow of a Gas and Liquid through a Packed Bed
25. Liquid Distribution in Trickle‐Bed Reactors, Part I: Flow Measurements
26. Liquid Distribution in Trickle‐Bed Reactors, Part II: Tracer Studies
27. Effectiveness Factors and Mass Transfer in Trickle‐Bed Reactors
28. Wetting Efficiency in Trickle‐Bed Reactors. The Overall Effectiveness Factor of Partially Wetted Catalyst Particles
29. Effect of Wetting Efficiency on Selectivity in a Trickle‐Bed Reactor
30. Wetting Efficiency in Trickle‐Bed Reactors: It's Effect on the Reactor Performance
31. Two‐Phase Cocurrent Downflow in Packed Beds
32. Multiphase Catalytic Packed‐Bed Reactions
33. Concurrent Gas‐Liquid Flow in Packed Columns
34. A Model for Liquid Distribution in Packed Columns and Trickle‐Bed Reactors
35. Multiple Hydrodynamic States in Cocurrent Two‐Phase Downflow through Packed Beds
36. Pressure Drop and Holdup in Two‐Phase Cocurrent Trickle Flows through Beds of Small Particles
37. Flow Characteristics and Axial Dispersion in Two‐Phase Downflow in Packed Columns
38. Experimental Determination of the Spreading Factor
39. Trickle‐Bed Reactors: Criteria of Negligible Transport Effects and of Partial Wetting
40. Packed Bed Liquid Phase Dispersion in Pulsed Gas‐Liquid Downflow
41. Effective Interfacial Area and Liquid Side Mass Transfer Coefficient in Trickle‐Bed Reactors
42. Effectiveness Factor of a Catalyst Pellet in a Trickle Bed Reactor
43. Oxidation of Sulfur Dioxide in a Trickle‐Bed Reactor
44. Flow Pattern of Cocurrent Gas‐Liquid Downflow in Packed Beds
45. Correlation of Dynamic Holdup in Packed Beds with Cocurrent Gas‐Liquid Downflow
46. Effective Radial Thermal Conductivity in Packed Beds with Gas‐Liquid Downflow
47. Apparent Wall Heat Transfer Coefficient in Packed Beds with Downward Cocurrent Gas‐Liquid Flow
48. The Role of Liquid Holdup and Effective Wetting in the Performance of Trickle‐Bed Reactors
49. Mixing in Trickle Flow through Packed Beds
50. A Dual‐Series Solution for the Effectiveness Factor of Partially Wetted Catalysts in Trickle‐Bed Reactors
51. Analysis of Catalyst Effectiveness in Trickle‐Bed Reactors Processing Volatile or Nonvolatile Reactants
52. Some Comments on Models for Evaluation of Catalyst Effectiveness Factors in Trickle Bed Reactors
53. Evaluation of Liquid‐Solid Contacting in Trickle‐Bed Reactors by Tracer Methods
54. Flow Pattern, Pressure Loss and Liquid Holdup Data in Gas‐Liquid Downflow Packed Beds with Foaming and Nonfoaming Hydrocarbons
55. Effect of Catalyst Particle Size on Performance of a Trickle‐Bed Reactor
56. Mass Transfer and Contacting Efficiency in a Trickle‐Bed Reactor
57. Flow Pattern and Some Holdup Data in Trickle‐Bed Reactors for Foaming, Nonfoaming and Viscous Organic Liquids
58. Hydrodynamics and Interfacial Areas in Downward Cocurrent Gas‐Liquid Flow through Fixed Beds. Influence of the Liquid
59. Interfacial Area in Trickle‐Bed Reactors: Comparison Between Ionic and Organic Liquids and Between Raschig Rings and Small Diameter Particle
60. Heat Transfer from Wall in Gas‐Liquid Cocurrent Packed Bed
61. Liquid Distribution in Reactors with Randomly Porous Beds
62. Wall Flow in Trickle‐Bed Reactors
63. Effect of Physical Properties of the Wetting Liquid on its Distribution in Trickle‐Bed Reactors
64. Effectiveness Factors in Trickle‐Bed Reactors
65. Mixing‐Cell Method for Design of Trickle‐Bed Reactor
66. Particle Mass Transfer during Cocurrent Downward Gas‐Liquid Flow in Packed Beds
67. Direct Solid Catalyzed Reaction of a Vapor in an Apparently Completely Wetted Trickle‐Bed Reactor
68. Trickle‐Bed Reactors
69. Liquid‐Solid Mass Transfer in Packed Beds with Downward Concurrent Gas‐Liquid Flow
70. An Evaluation of Models for Liquid Backmixing in Trickle‐Bed Reactors
71. A New Tracer Method for Determination of Liquid‐Solid Contacting Efficiency in Trickle‐Bed Reactors
72. Liquid Holdup and Dispersion in Trickle‐Bed Reactors
73. Partial Wetting in Trickle‐Bed Reactors: the Reduction of Crotonaldehyde over a Palladium Catalyst
74. Mass Transfer and Adsorption in Liquid Full and Trickle‐Beds
75. Flow Regime Transitions in Trickle‐Bed Reactors
76. Catalyst Area Wetted by Flowing and Semistagnant Liquid in Trickle‐Bed Reactors
77. Influence of Gas Velocity and Packing Geometry on Pulsing Inception in Trickle‐Bed Reactors
78. Hydrodynamic Models for the Interpretation of the Liquid Flow in Trickle‐Bed Reactors
79. Packing Wetting in Trickle‐Bed Reactors, Influence of the Gas Flow Rate
80. Spreading Coefficient in Randomly Packed Porous Beds
81. Distribution and Radial Spread of Liquid in Two‐Phase Concurrent Flows in a Packed Bed
82. Pressure Drop and Liquid Holdup for Two‐Phase Concurrent Flow in Packed Beds
83. Solid‐Liquid Mass Transfer in Concurrent Two‐Phase Flow through Packed Beds
84. Heat Transfer in Trickle‐Bed Reactors
85. Heat Transfer in Packed Bed Reactors with One Phase Flow
86. Distribution of Liquid over a Random Packing
87. Distribution of Liquid over a Random Packing, VII
88. Distribution of Liquid over a Random Packing, VIII
89. The Effect of Liquid Flow Distribution on the Behavior of a Trickle‐Bed Reactor
90. Radial Liquid Distribution in Concurrent Two‐Phase Downflow in Packed Beds
91. Two‐Phase Downflow Through Catalyst Beds
92. Catalyst Particle Effectiveness with Unsymmetrical Boundary Conditions
93. Mass Transfer in Trickle‐Bed Reactors at Low Reynolds Number
94. Catalyst Dilution for Improved Performance of Laboratory Trickle‐Bed Reactors
95. Rate of Dissolution of Solid Substances
96. Multiphase Reactors: Mass Transfer and Modeling
97. Residence Time Distribution in the Liquid Phase of Trickle Flow in Packed Columns
98. Fluid‐Flow Characteristics of Concurrent Gas‐Liquid Flow in Packed Beds
99. Heat Transfer Characteristics of Concurrent Gas‐Liquid Flow in Packed Beds
100. Forced Convection Heat Transfer Correlations for Flow in Pipes, Past Flat Plates, Single Cylinders, Simple Spheres, and for Flow in Packed Beds and Tube Bundles
101. Dynamics of a Trickle‐Bed Hydrocracker with a Quenching System
102. Liquid‐Solid Mass Transfer in Gas‐Liquid Cocurrent Flows Through Beds of Small Particles