Enhanced production of aromatics from propane with a temperature-shifting two-stage fluidized bed reactor

A temperature-shifting two-stage fluidized bed reactor technology was used to convert propane and its intermediate products into aromatics. The first stage served for the aromatization of propane with a Ga/ZSM-5 catalyst at 570 °C. The second stage served for the alkylation of the intermediates of o...

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Autores principales: Yang, Yifeng, Hou, Yilin, Chen, Zhaohui, Wang, Huiqiu, Wang, Yu, Liu, Boyang, Dong, Zhuoya, Gao, Jun, Wei, Ran, Qian, Weizhong
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2019
Materias:
Chemistry
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9070441/
https://www.ncbi.nlm.nih.gov/pubmed/35531041
http://dx.doi.org/10.1039/c9ra05420k
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author Yang, Yifeng
Hou, Yilin
Chen, Zhaohui
Wang, Huiqiu
Wang, Yu
Liu, Boyang
Dong, Zhuoya
Gao, Jun
Wei, Ran
Qian, Weizhong
author_facet Yang, Yifeng
Hou, Yilin
Chen, Zhaohui
Wang, Huiqiu
Wang, Yu
Liu, Boyang
Dong, Zhuoya
Gao, Jun
Wei, Ran
Qian, Weizhong
author_sort Yang, Yifeng
collection PubMed
description A temperature-shifting two-stage fluidized bed reactor technology was used to convert propane and its intermediate products into aromatics. The first stage served for the aromatization of propane with a Ga/ZSM-5 catalyst at 570 °C. The second stage served for the alkylation of the intermediates of olefins at 300 °C. The increased yield of aromatics was attributed to the effective transformation of C(2)–C(3) olefins as well as due to the suppression of the hydrogen transfer effect of the olefins.
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spelling pubmed-90704412022-05-05 Enhanced production of aromatics from propane with a temperature-shifting two-stage fluidized bed reactor Yang, Yifeng Hou, Yilin Chen, Zhaohui Wang, Huiqiu Wang, Yu Liu, Boyang Dong, Zhuoya Gao, Jun Wei, Ran Qian, Weizhong RSC Adv Chemistry A temperature-shifting two-stage fluidized bed reactor technology was used to convert propane and its intermediate products into aromatics. The first stage served for the aromatization of propane with a Ga/ZSM-5 catalyst at 570 °C. The second stage served for the alkylation of the intermediates of olefins at 300 °C. The increased yield of aromatics was attributed to the effective transformation of C(2)–C(3) olefins as well as due to the suppression of the hydrogen transfer effect of the olefins. The Royal Society of Chemistry 2019-08-23 /pmc/articles/PMC9070441/ /pubmed/35531041 http://dx.doi.org/10.1039/c9ra05420k Text en This journal is © The Royal Society of Chemistry https://creativecommons.org/licenses/by-nc/3.0/
spellingShingle Chemistry
Yang, Yifeng
Hou, Yilin
Chen, Zhaohui
Wang, Huiqiu
Wang, Yu
Liu, Boyang
Dong, Zhuoya
Gao, Jun
Wei, Ran
Qian, Weizhong
Enhanced production of aromatics from propane with a temperature-shifting two-stage fluidized bed reactor
title Enhanced production of aromatics from propane with a temperature-shifting two-stage fluidized bed reactor
title_full Enhanced production of aromatics from propane with a temperature-shifting two-stage fluidized bed reactor
title_fullStr Enhanced production of aromatics from propane with a temperature-shifting two-stage fluidized bed reactor
title_full_unstemmed Enhanced production of aromatics from propane with a temperature-shifting two-stage fluidized bed reactor
title_short Enhanced production of aromatics from propane with a temperature-shifting two-stage fluidized bed reactor
title_sort enhanced production of aromatics from propane with a temperature-shifting two-stage fluidized bed reactor
topic Chemistry
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9070441/
https://www.ncbi.nlm.nih.gov/pubmed/35531041
http://dx.doi.org/10.1039/c9ra05420k
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