Maximization production of light olefins from dual-stage catalytic dehydrogenation cracking of crude oil: Catalysis mechanism and pilot trial-Reference-Cited by-同舟云学术

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Maximization production of light olefins from dual-stage catalytic dehydrogenation cracking of crude oil: Catalysis mechanism and pilot trial

Published:2024-11 Issue: Volume:375 Page:132570
ISSN:0016-2361
Container-title:Fuel
language:en
Short-container-title:Fuel

Author:

Zhang Di^ORCID,Zong Peijie,Wang Chengbiao,Shang Yanchao,Xu Wenlong^ORCID,Wen Kai,Qiao Yingyun,Tian Yuanyu

Publisher

Elsevier BV

Reference52 articles.

1. A viewpoint on the refinery of the future: catalyst and process challenges;Alabdullah;ACS Catal,2020

2. Prospects of refinery switching from conventional to integrated: an opportunity for sustainable investment in the petrochemical industry;Al-Samhan;Fuel,2022

3. Fundamental study of hierarchical millisecond gas-phase catalytic cracking process for enhancing the production of light olefins from vacuum residue;Che;Fuel,2019

4. Produce petrochemicals directly from crude oil catalytic cracking, a techno-economic analysis and life cycle society-environment assessment;Zhou;J Clean Prod,2021

5. One-step leap in achieving oil-to-chemicals by using a two-stage riser reactor: molecular-level process model and multi-objective optimization strategy;Zhou;Chem Eng J,2022

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