发明名称 Fluid catalytic cracking process for heavy oil
摘要 A heavy fraction oil is catalytically cracked by contacting the oil with a catalyst mixture consisting of 60 to 95 wt % of a base cracking catalyst containing an ultra stable Y-type zeolite and less than 0.5 wt % of rare-earth metal oxide, and 5 to 40 wt % of an additive containing a shape-selective zeolite, in a fluid catalytic cracking apparatus having a regeneration zone, a down flow-type reaction zone, a separation zone, and a stripping zone, and under conditions that a reaction zone outlet temperature is in the range of 580 to 630° C., the catalyst/oil ratio is in the range of 15 to 40 wt/wt, and the contact time of hydrocarbons in the reaction zone is in the range of 0.1 to 1.0 seconds. According to the fluid catalytic cracking process, the yield of light-fraction olefins can be enhanced.
申请公布号 US2003006168(A1) 申请公布日期 2003.01.09
申请号 US20010883464 申请日期 2001.06.07
申请人 INO TAKASHI;OKUHARA TOSHIAKI;ABUL-HAMAYEL MOHAMMAD;AITANI ABDULLAH;MAGHRABI ABDULGADER 发明人 INO TAKASHI;OKUHARA TOSHIAKI;ABUL-HAMAYEL MOHAMMAD;AITANI ABDULLAH;MAGHRABI ABDULGADER
分类号 C10G11/05;C10G11/18;(IPC1-7):C10G11/05;C10G11/00;C10G11/02 主分类号 C10G11/05
代理机构 代理人
主权项
地址