
基本信息:
- 专利标题: CATALYTIC CONVERSION PROCESS
- 专利标题(中):催化转化过程
- 申请号:US12672666 申请日:2008-08-07
- 公开(公告)号:US20100213102A1 公开(公告)日:2010-08-26
- 发明人: Youhao Xu , Lishun Dai , Longsheng Tian , Shouye Cui , Jianhong Gong , Chaogang Xie , Jiushun Zhang , Jun Long , Zhijian Da , Hong Nie , Jinbiao Guo , Zhigang Zhang
- 申请人: Youhao Xu , Lishun Dai , Longsheng Tian , Shouye Cui , Jianhong Gong , Chaogang Xie , Jiushun Zhang , Jun Long , Zhijian Da , Hong Nie , Jinbiao Guo , Zhigang Zhang
- 专利权人: China Petroleum & Chemical Corporation,Research Institute of Petroleum Processing, Sinopec
- 当前专利权人: China Petroleum & Chemical Corporation,Research Institute of Petroleum Processing, Sinopec
- 优先权: CN200710120112.0 20070809; CN200810101853.9 20080313
- 国际申请: PCT/CN2008/001439 WO 20080807
- 主分类号: C10G57/00
- IPC分类号: C10G57/00 ; C10G11/05
摘要:
A catalytic conversion process which comprises catalytic cracking reaction of a hydrocarbon feedstock contacting with a medium pore size zeolite enriched catalyst in a reactor, characterized in that reaction temperature, weight hourly space velocity and catalyst/feedstock ratio by weight are sufficient to achieve a yield of fluid catalytic cracking gas oil between 12% and 60% by weight of said feedstock, wherein said weight hourly space velocity is between 25 h−1 and 100 h−1, said reaction temperature is between 450° C. and 600° C., and said catalyst/feedstock ratio by weight is between 1 and 30. This invention relates to a catalytic conversion process, especially for heavy feedstock oil to produce higher octane gasoline and an enhanced yield of propylene. More particularly, the invention relates to a process to utilize petroleum oil resources efficiently for decreasing the yield of dry gas and coke significantly.
摘要(中):
催化转化方法,其包括在反应器中与中等孔径的沸石富集催化剂接触的烃原料的催化裂化反应,其特征在于反应温度,重量时空速和催化剂/原料重量比足以实现 流化催化裂化瓦斯油在所述原料的12重量%至60重量%之间,其中所述重时空速在25h -1和100h -1之间,所述反应温度在450℃和600℃之间, 并且所述催化剂/原料的重量比在1和30之间。本发明涉及催化转化方法,特别是用于重质原料油生产高辛烷值汽油和提高丙烯收率的方法。 更具体地说,本发明涉及一种利用石油资源有效降低干燥气体和焦炭产率的方法。
公开/授权文献:
- US08696887B2 Catalytic conversion process 公开/授权日:2014-04-15