Choice of catalysts for FCC pretreatment
Conference
·
· Natl. Pet. Refiners Assoc., (Tech. Pap.); (United States)
OSTI ID:6163688
Catalysts for FCC pretreatment are facing increasingly tougher feedstocks. This is partly the result of the general reduced availability of sweet crudes, and partly due to inclusion of larger amounts of unsaturated fractions such as coker gas oils. At the same time, process conditions are often limited by equipment designed for easier feedstocks. The result is that the requirements to the pretreating catalyst are today far more exacting. In this paper the authors demonstrate that the conversion of sulfur, nitrogen and polynuclear aromatics can be maximised by varying catalyst pore dimensions and/or particle size. Furthermore, it is shown that the optimum pore size depends on the reactivity of the feedstock and its diffusional properties. Whether or not it is advantageous to use smaller particles also depends on the properties of the feed.
- Research Organization:
- Haldor Topsoe Inc., Pasadena, TX
- OSTI ID:
- 6163688
- Report Number(s):
- CONF-8403125-
- Conference Information:
- Journal Name: Natl. Pet. Refiners Assoc., (Tech. Pap.); (United States) Journal Volume: AM-84-59
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
02 PETROLEUM
020400* -- Petroleum-- Processing
AROMATICS
CATALYSTS
CATALYTIC CRACKING
CATALYTIC EFFECTS
CHEMICAL FEEDSTOCKS
CHEMICAL REACTIONS
CRACKING
CRYSTAL STRUCTURE
DECOMPOSITION
DENITRIFICATION
DESULFURIZATION
DIFFUSION
HYDROCARBONS
MICROSTRUCTURE
ORGANIC COMPOUNDS
PARTICLE SIZE
POLYCYCLIC AROMATIC HYDROCARBONS
POROSITY
PYROLYSIS
REMOVAL
SIZE
THERMOCHEMICAL PROCESSES
020400* -- Petroleum-- Processing
AROMATICS
CATALYSTS
CATALYTIC CRACKING
CATALYTIC EFFECTS
CHEMICAL FEEDSTOCKS
CHEMICAL REACTIONS
CRACKING
CRYSTAL STRUCTURE
DECOMPOSITION
DENITRIFICATION
DESULFURIZATION
DIFFUSION
HYDROCARBONS
MICROSTRUCTURE
ORGANIC COMPOUNDS
PARTICLE SIZE
POLYCYCLIC AROMATIC HYDROCARBONS
POROSITY
PYROLYSIS
REMOVAL
SIZE
THERMOCHEMICAL PROCESSES