A numerical investigation of gasoline production from multi-stage FCC systems [electronic resource].
- Washington, D.C. : United States. Dept. of Energy, 2000.
Oak Ridge, Tenn. : Distributed by the Office of Scientific and Technical Information, U.S. Dept. of Energy.
- Physical Description:
- 9 pages : digital, PDF file
- Additional Creators:
- Argonne National Laboratory, United States. Department of Energy, and United States. Department of Energy. Office of Scientific and Technical Information
- Restrictions on Access:
- Free-to-read Unrestricted online access
- Staged, fluid catalytic cracking (FCC) processes are deemed to have the potential to enhance FCC performance in the areas of product selectivity, operating flexibility, throughput, reliability, operating costs, and emissions. Computational fluid dynamic (CFD) codes are used to analyze various staged FCC concepts to help accelerate their development into commercial products. Three conceptual multi-stage FCC systems were evaluated using a validated CFD code. The results indicated potential increases of gasoline production from these conceptual designs.
- Report Numbers:
- E 1.99:anl/es/cp-101839
- Other Subject(s):
- Published through SciTech Connect.
8th International Energy Forum, ENERGEX 2000, Las Vegas, NV (US), 07/23/2000--07/28/2000.
Petrick, M.; Chang, S. L.; Zhou, C. Q.
- Funding Information:
View MARC record | catkey: 14703413