A modified FCC process for maximizing isoparaffins (MIP) in cracked naphtha

Acta Petrolei Sinica (Petroleum Processing Section)

Volumn 19, Issue 1, 2003, Pages 43-47

  Xu, You hao ^a   Zhang, Jiu shun ^a   Long, Jun ^a   He, Ming yuan ^a   Xu, Hui ^b  

^a RESEARCH INSTITUTE OF PETROLEUM PROCESSING   (China)

^b SINOPEC   (China)

Author keywords

Catalytic cracking; Gasoline stock; Olefin; Reaction mechanism; Riser reactor

Indexed keywords

EID: 0037310638     PISSN: 10018719     EISSN: None     Source Type: Journal    
DOI: None     Document Type: Article

References (5)

1. Xu Y H, et al. A catalytic conversion method for production of isobutane and gasoline rich in isoparaffins[P]. CN: 1232069A. 1999.
2. Julius Scherzer. Octane-enhancing zeolitic FCC catalysts: scientific and technical aspects[J]. Catal Rev-Sci Eng, 1989, 3(31): 215-354.
3. Venuto P B, Habib E T. Fluid Catalytic Cracking with Zeolite Catalysts[M]. US: Marcel Dekker Inc. 1979.
4. Xu Y H, et al. A riser reactor applied in fluidized catalytic conversion[P]. CN: 1237477A. 1999.
5. Xu Y H, et al. A catalytic conversion method for reduction of olefin content in LPG and gasoline[P]. CN: 1245202A. 1999.