- 专利标题: Catalytic cracking catalyst having a higher selectivity, processing method and use thereof
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申请号: US12822493申请日: 2010-06-24
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公开(公告)号: US09611432B2公开(公告)日: 2017-04-04
- 发明人: Youhao Xu , Shouye Cui , Jun Long , Jianhong Gong , Zhijian Da , Jiushun Zhang , Yuxia Zhu , Yibin Luo , Jinlian Tang
- 申请人: Youhao Xu , Shouye Cui , Jun Long , Jianhong Gong , Zhijian Da , Jiushun Zhang , Yuxia Zhu , Yibin Luo , Jinlian Tang
- 申请人地址: CN Beijing CN Beijing
- 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
- 当前专利权人地址: CN Beijing CN Beijing
- 代理机构: Novick, Kim & Lee, PLLC
- 代理商 Allen Xue
- 优先权: CN200910148614 20090625; CN200910148615 20090625; CN201010152745 20100422
- 主分类号: C10G11/18
- IPC分类号: C10G11/18 ; B01J29/06 ; C10G11/05 ; B01J29/08 ; B01J35/00 ; B01J37/04 ; B01J37/10
摘要:
The present invention provides a catalytic cracking catalyst, processing method and use thereof. When the catalyst is added into a commercial catalytic cracking unit, it has an initial activity of not higher than 80, preferably not higher than 75, more preferably not higher than 70, a self-balancing time of 0.1-50 h, and an equilibrium activity of 35-60. Said method enables the activity and selectivity of the catalyst in the catalytic cracking unit to be more homogeneous and notably improves the selectivity of the catalytic cracking catalyst, so as to obviously reduce the dry gas and coke yields, to sufficiently use steam and to reduce the energy consumption of the FCC unit.
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