Patent · US Expired

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
0Family size

Assignee

Inventors

Key dates

Filing dateFeb 16, 2000
Grant dateApr 18, 2006
Priority date
Expiry dateFeb 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.