Identification of Mass Transfer Limitations by Kinetic Modeling of a Technical-Scale Trickle Bed Reactor for the Hydrogenation of Viscous Aromatics-Reference-Cited by-同舟云学术

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Identification of Mass Transfer Limitations by Kinetic Modeling of a Technical-Scale Trickle Bed Reactor for the Hydrogenation of Viscous Aromatics

Published:2023-12-18 Issue:1 Volume:63 Page:147-162
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Held Hendrik¹^ORCID,Freund Hannsjörg¹^ORCID

Affiliation:

1. Institute of Reaction Engineering and Catalysis, TU Dortmund University, Emil-Figge-Str. 66, 44227 Dortmund, Germany

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.3c03273

Reference32 articles.

1. Heterogeneous catalytic deuteration of substituted benzenes in acetic acetic acid-d1

2. Kinetics of toluene hydrogenation on Ni/Al2O3 catalyst

3. Kinetics of the Liquid-Phase Hydrogenation of Benzene and Some Monosubstituted Alkylbenzenes over a Nickel Catalyst

4. Kinetics of ethylbenzene hydrogenation on Ni/Al2O3

Cited by 1 articles. 订阅此论文施引文献订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献

1. Conceptual study on the intensification of gas–liquid mass transfer in trickle bed reactors by the application of strut-based and novel sheet-based periodic open cellular structures (POCS);Chemical Engineering and Processing - Process Intensification;2024-10

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