发明授权
- 专利标题: Process for hydrocracking heavy distillate oil under middle pressure
- 专利标题(中): 中压下加氢裂化重馏油的工艺
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申请号: US884813申请日: 1997-06-30
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公开(公告)号: US5954944A公开(公告)日: 1999-09-21
- 发明人: Yanping Zhang , Yulin Shi , Zhenlin Xiong , Jianwen Shi , Hong Nie , Yahua Shi , Yigin Zhu , Zhihai Hu
- 申请人: Yanping Zhang , Yulin Shi , Zhenlin Xiong , Jianwen Shi , Hong Nie , Yahua Shi , Yigin Zhu , Zhihai Hu
- 申请人地址: CNX Beijing CNX Beijing
- 专利权人: China Petrochemical Corp.,Research Institute of Petroleum Processing Sinopec
- 当前专利权人: China Petrochemical Corp.,Research Institute of Petroleum Processing Sinopec
- 当前专利权人地址: CNX Beijing CNX Beijing
- 优先权: CNX96106587 19960628; CNX96106724 19960628; CNX96109007 19960722
- 主分类号: B01J23/888
- IPC分类号: B01J23/888 ; B01J27/132 ; B01J29/076 ; B01J29/16 ; B01J29/26 ; C10G45/08 ; C10G47/16 ; C10G47/18 ; C10G65/12 ; C10G69/02
摘要:
A process for producing middle distillates by hydrocracking a heavy distillate oil under middle pressure uses a hydrofining catalyst and a hydrocracking catalyst in series and once-through operation. The once-through volume conversion to 350.degree. C.--products is up to 80 vol. %. The yield and selectivity of middle distillates are greater than 40 wt % and less than 50 wt %, respectively. The process is particularly suited to treat heavy distillate oil having the nitrogen content of up to 1500 ppmw, the sulfur content of up to 3.5 wt % and dry point in the boiling range of higher than 500.degree. C. to produce the feed for reforming process, jet fuel, the low sulfur content diesel, the feed for catalytic cracker and the feed for producing ethylene.
公开/授权文献
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