Demonstration plant for new FCC technology yields increased propylene

Yuichiro Fujiyama*, Halim H. Redhwi, Abdullah M. Aitani, M. Rahat Saeed, Christopher F. Dean

*Corresponding author for this work

Research output: Contribution to specialist publicationArticle

20 Scopus citations

Abstract

A novel FCC process that boosts propylene production has been proven in a 30-b/d demonstration plant in Saudi Arabia (Fig. 1). Suitable for an integrated refinery-petrochemical complex, the high-severity process combines mechanical modications to conventional FCC with changes in process variables and catalyst formulations. The process' main operating features are a downflow reactor system, high reaction temperature, short contact time, and high catalyst: oil ratio. Similar to most reactor designs involving competing reactions and secondary product degradation, there are concerns about catalyst-feed contacting, back mixing, and control of the reaction time and temperature.

Original languageEnglish
Pages54-58
Number of pages5
Volume103
No36
Specialist publicationOil and Gas Journal
StatePublished - 26 Sep 2005

ASJC Scopus subject areas

  • Fuel Technology
  • Energy Engineering and Power Technology

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