A NEW CATALYTIC CRACKING PROCESS TO MAXIMIZE REFINERY PROPYLENE

Ali G. Maadhah; Yuuichirou Fujiyama; Halim Redhwi; Mohammed Abul-Hamayel; Abdullah Aitani; Mian Saeed; Christopher Dean

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A NEW CATALYTIC CRACKING PROCESS TO MAXIMIZE REFINERY PROPYLENE

机译：最大化炼油厂丙烯的新催化裂化工艺

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A novel high-severity FCC process that maximizes propylene production is under development by research teams in Saudi Arabia and Japan. The process has been proven in a 30-BPD demonstration plant at Saudi Aramco's refinery, Saudi Arabia, and at a 500-BPD

机译：沙特阿拉伯和日本的研究团队正在开发一种新颖的高强度FCC工艺，该工艺可以最大程度地提高丙烯的产量。该工艺已在沙特阿美炼油厂沙特阿拉伯的30-BPD示范工厂和500-BPD的示范工厂中得到验证。

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来源
《The Arabian Journal for Science and Engineering. Section B, Engineering》 |2008年第1b期|p.17-28|共12页
作者
Ali G. Maadhah; Yuuichirou Fujiyama; Halim Redhwi; Mohammed Abul-Hamayel; Abdullah Aitani; Mian Saeed; Christopher Dean;
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作者单位

Chemical Engineering Department King Fahd University of Petroleum & Minerals Dhahran, Saudi Arabia;

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收录信息美国《科学引文索引》(SCI);
原文格式 PDF
正文语种 eng
中图分类自然科学总论;
关键词
aromatics; cracking; downer; FCC catalysts; gasoline; octane; olefins; propylene; riser;

机译：芳烃;裂化;降碳剂;FCC催化剂;汽油;辛烷;烯烃;丙烯;立管;

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专利

1. Ten-lump kinetic model for the two-stage riser catalytic cracking for maximizing propylene yield (TMP) process [J] . Yupeng Du, Qi Yang, Chengtao Zhang Applied Petrochemical Research . 2015,第4期

机译：两级提升管催化裂化的十集动力学模型，可最大程度地提高丙烯收率（TMP）工艺
2. Ten-lump kinetic model for the two-stage riser catalytic cracking for maximizing propylene yield (TMP) process [J] . Yupeng Du, Qi Yang, Chengtao Zhang, Applied Petrochemical Research . 2015,第4期

机译：两级提升管催化裂化的十集动力学模型，可最大程度地提高丙烯收率（TMP）工艺
3. Advances of two-stage riser catalytic cracking of heavy oil for maximizing propylene yield (TMP) process [J] . Yang Chaohe, Chen Xiaobo, Zhang Jinhong, Applied Petrochemical Research . 2014,第4期

机译：重油两级提升管催化裂化以最大化丙烯产率（TMP）工艺的进展
4. Studies on the Catalytic Cracking of Different Gas Oils for Maximizing Propylene [C] . Xiaobo Chen, Benxian Shen, Chunyi Li International Conference on Energy and Environmental Protection . 2012

机译：不同汽油催化裂化最大化丙烯的研究
5. Maximizing Light Olefins Yield from the Fluid Catalytic Cracking of Whole Crude Oil [D] . Onimisi, Usman Abdulhafiz. 2016

机译：从全原油的流体催化裂化中最大化光烯烃产量
6. Advances of two-stage riser catalytic cracking of heavy oil for maximizing propylene yield (TMP) process [O] . Yang Chaohe, Chen Xiaobo, Zhang Jinhong, -1

机译：重油两段式提升管催化裂化以最大化丙烯产率（TMP）工艺的进展
7. Ten-lump kinetic model for the two-stage riser catalytic cracking for maximizing propylene yield (TMP) process [O] . 2015

机译：两级提升管催化裂化的十集动力学模型，可最大程度地提高丙烯收率（TMP）工艺
8. Petroleum Refineries: Catalytic Cracking Units, Catalytic Reforming Units, and Sulfur Recovery Units. Background Information for Promulgated Standards and Response to Comments. [R] . 2001

机译：炼油厂：催化裂化装置，催化重整装置和硫磺回收装置。颁布标准的背景信息和对评论的回应。

A NEW CATALYTIC CRACKING PROCESS TO MAXIMIZE REFINERY PROPYLENE

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