Morrison & Foerster LLP
Catalytic cracking process for increasing simultaneously the yields of diesel oil and liquefied gas
This discloses a process for catalytically cracking hydrocarbon stocks in a riser or fluidized bed reactor simultaneously to increase yields of diesel and liquefied gas. The process includes the steps of: first, charging a gasoline stock and a catalytic cracking catalyst into a lower zone of the reactor to permit contact between the catalyst and the gasoline stock and to produce a liquefied gas-rich oil-gas mixture containing reacted catalyst. The resulting liquefied gas-rich oil-gas mixture (still containing reacted catalyst) is then introduced into a reaction zone above the lower zone of the reactor. Simultaneously, at least one conventional catalytic cracking hydrocarbon feed is also fed independently into at least two sites is situated at a different height above the lower zone of the reactor. The resulting mixture is then separated in a conventional fashion.
Research Institute of Petroleum Processing, Sinopec China Petrochemical Corporation
C
C10G
inventional
Hua Zeyu Xiaoxiang Anguo Shuxin Ruichi Jiushun Yamin Zhigang Zubi Wei
Cui Wang Zhong Mao Cui Zhang Zhang Wang Zhang Chen Wang