Multi stage selective catalytic cracking process and a system for producing high yield of middle distillate products from heavy hydrocarbon feedstocks
US7029571B1 · kind B1 · utility
52Cited by
14References
22Claims
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Key dates
| Filing date | Feb 16, 2000 |
| Grant date | Apr 18, 2006 |
| Priority date | — |
| Expiry date | Feb 16, 2020 |
Classification
- Technology area (CPC C)Chemistry; Metallurgy
- CPC primaryC10G51/026
- WIPO fieldBasic materials chemistry
- WIPO sectorChemistry
Abstract
According to this invention, there is provided a process and apparatus for catalytic cracking of various petroleum based heavy feed stocks in the presence of solid zeolite catalyst and high pore size acidic components for selective bottom cracking and mixtures thereof, in multiple riser type continuously circulating fluidized bed reactors operated at different severities to produce high yield of middle distillates, in the range of 50–65 wt % of fresh feed.
Source: USPTO / EPO open patent data. Objective bibliographic and citation counts.