Model-Based Optimization of an Acetylene Hydrogenation Reactor To Improve Overall Ethylene Plant Economics-Reference-Cited by-同舟云学术

Model-Based Optimization of an Acetylene Hydrogenation Reactor To Improve Overall Ethylene Plant Economics

Published:2018-07-24 Issue:30 Volume:57 Page:9943-9951
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Aeowjaroenlap Hattachai¹^ORCID,Chotiwiriyakun Kritsada¹,Tiensai Nattawat¹,Tanthapanichakoon Wiwut¹,Spatenka Stepan²,Cano Alejandro²

Affiliation:

1. SCG Chemicals Co., Ltd., 271 Sukhumvit Rd., Map Ta Phut, Muang Rayong, Thailand 21150

2. Process Systems Enterprise, Ltd., 26-28 Hammersmith Grove, London, W6 7HA, United Kingdom

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.7b05234

Reference30 articles.

1. Kaiser, V.; Laugier, J. P.; DiCinto, R.; Picciotti, M. Acetylene Removal from Cracked Gas: A Technology Overview. Presented at the AIChE Ethylene Producers Conference, 1999; Paper No. 68c.

2. Kinetics and reactor modeling of a Pd-Ag/Al2O3 catalyst during selective hydrogenation of ethyne

3. Evaluating the Risk of C–C Bond Formation during Selective Hydrogenation of Acetylene on Palladium

4. C–C Coupling on Single-Atom-Based Heterogeneous Catalyst

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