Catalytic Upgrading of Vacuum Residue-Derived Cracking Gas-Oil for Maximum Light Olefin Production in a Combination of a Fluidized Bed and Fixed Bed Reactor-Reference-Cited by-同舟云学术

Catalytic Upgrading of Vacuum Residue-Derived Cracking Gas-Oil for Maximum Light Olefin Production in a Combination of a Fluidized Bed and Fixed Bed Reactor

Published:2019-07-26 Issue:8 Volume:33 Page:7297-7304
ISSN:0887-0624
Container-title:Energy & Fuels
language:en
Short-container-title:Energy Fuels

Author:

Tian Yuanyu¹²^ORCID,Che Yuanjun¹^ORCID,Chen Minshen¹,Feng Wen¹,Zhang Jinhong¹^ORCID,Qiao Yingyun¹

Affiliation:

1. State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Qingdao 266580, China

2. Key Laboratory of Low Carbon Energy and Chemical Engineering, Shandong University of Science and Technology, Qingdao, Shandong 266590, China

Funder

Ministry of Education of the People's Republic of China

National Natural Science Foundation of China

Natural Science Foundation of Shandong Province

Publisher

American Chemical Society (ACS)

Subject

Energy Engineering and Power Technology,Fuel Technology,General Chemical Engineering

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.energyfuels.9b01949

Reference35 articles.

1. Enhancing the production of light olefins from heavy crude oils: Turning challenges into opportunities

2. Downer Catalytic Pyrolysis (DCP): A Novel Process for Light Olefins Production

3. Enhancing propylene production from catalytic cracking of Arabian Light VGO over novel zeolites as FCC catalyst additives

4. Catalytic cracking of Arabian Light VGO over novel zeolites as FCC catalyst additives for maximizing propylene yield

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