Abstract

Multiple Hydrodynamic States in Trickle Bed Reactors Have Been the Subject of Numerous Hydrodynamic Investigations. the Extent of Variation in the Hydrodynamic Parameters (Like Holdup and Pressure Drop) is Large and This Variation Can Be Expected to Have a Significant Impact on the Conversion in a Reaction System. This Study Presents Reaction Data for Α-Methyl Styrene Hydrogenation in a Trickle Bed Reactor over a Range of Conditions that Include Gas and Liquid Limitations. It is Seen that Liquid Flow Rate Variation Induced Hysteresis Has a Large Impact on the Conversion. for Gas-Limited Reactions, the Upper Branch of the Pressure Drop Hysteresis Loop Has a Higher Conversion Than the Lower Branch at the Same Linear Fluid Velocities and Catalyst Weight, While for Liquid-Limited Reactions the Lower Branch Has a Higher Conversion Than the Upper Branch (The Difference in Productivity Being Up to 20%). These Trends Cannot Be Explained by Differences in Wetting Efficiency. Instead, It is Proposed that for This System the Gas-Liquid Mass Transfer Rate is the Limiting Step in Gas-Limited Reactions, While the Liquid-Solid Mass Transfer Rate is the Limiting Step in Liquid-Limited Reactions. © 2007 American Institute of Chemical Engineers.

Department(s)

Chemical and Biochemical Engineering

Keywords and Phrases

Mass transfer; Multi-phase flow; Trickle bed reactors

International Standard Serial Number (ISSN)

1547-5905; 0001-1541

Document Type

Article - Journal

Document Version

Citation

File Type

text

Language(s)

English

Rights

© 2023 Wiley; American Institute of Chemical Engineers (AIChE), All rights reserved.

Publication Date

01 Jan 2008

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