Catalytic hydrogenation reactors for the fine chemicals industries. Their design and operation
- 1 February 1997
- journal article
- Published by Elsevier in Chemical Engineering and Processing - Process Intensification
- Vol. 36 (1) , 17-27
- https://doi.org/10.1016/s0255-2701(96)04168-2
Abstract
No abstract availableKeywords
This publication has 16 references indexed in Scilit:
- A mathematical model for multiple hydrogenation reactions in a continuous stirred three-phase slurry reactor with an evaporating solventChemical Engineering Science, 1992
- The catalytic hydrogenation of 2,4-dinitrotoluene in a continuous stirred three-phase slurry reactor with an evaporating solventChemical Engineering Science, 1992
- Kinetics of the hydrogenation of 2,4-dinitrotoluene over a palladium on alumina catalystChemical Engineering Science, 1992
- Hydrodynamics in a cocurrent gas‐liquid trickle bed at elevated pressuresAIChE Journal, 1991
- Hydrodynamics in a pressurized cocurrent gas-liquid trickle-bed reactorChemical Engineering & Technology, 1991
- The influence of the reactor pressure on the hydrodynamics in a cocurrent gas-liquid trickle-bed reactorChemical Engineering Science, 1990
- Kinetics of the catalytic hydrogenation of 2,4-dinitrotoluene. 2. Modeling of the reaction rates and catalyst activityIndustrial & Engineering Chemistry Research, 1990
- Kinetics of the catalytic hydrogenation of 2,4-dinitrotoluene. 1. Experiments, reaction scheme, and catalyst activityIndustrial & Engineering Chemistry Research, 1990
- The transition between trickle flow and pulse flow in a cocurrent gas—liquid trickle-bed reactor at elevated pressuresChemical Engineering Science, 1990
- Development of catalytic hydrogenation reactors for the fine chemicals industryChemical Engineering Science, 1988