公开(公告)号：US20190201882A1

公开(公告)日：2019-07-04

申请号：US16235932

申请日：2018-12-28

申请人： China Petroleum & Chemical Corporation ,  Dalian Research Institute of Petroleum and Petrochemicals, SINOPEC CORP.

发明人： Tao LIU ,  Baozhong LI ,  Ronghui ZENG ,  Yuzhuo ZHAO ,  Zhenmin BAI ,  Xiangchen FANG ,  Yan WANG ,  Xuehui ZHANG ,  Chang LIU

IPC分类号： B01J29/70 ,  B01J29/80

CPC分类号： B01J29/7007 ,  B01J29/80 ,  B01J2229/36

摘要： A method of wax oil hydrocracking includes the steps of pre-hydrotreating wax oil to obtain a pre-hydrotreated material flow; controlling the pre-hydrotreated material flow and a hydrogen-containing material flow to contact with a first hydrocracking catalyst to obtain a first hydrocracked material flow, and dividing the first hydrocracked material flow into a first hydrocracked material flow A and a first hydrocracked material flow B; controlling the flow B and a hydrogen-containing material flow to contact with a second hydrocracking catalyst to obtain a second hydrocracked material flow, and then separating and fractionating the second hydrocracked material flow to obtain a hydrocracked tail oil product; controlling the flow A, at least a part of the hydrocracked tail oil product, and a hydrogen-containing material flow to contact with a hydrogenation isocracking catalyst to obtain a hydrogenation isocracked material flow, and then separating and fractionating the obtained hydrogenation isocracked material flow.

公开(公告)号：US20230381728A1

公开(公告)日：2023-11-30

申请号：US18249927

申请日：2021-10-21

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  DALIAN RESEARCH INSTITUTE OF PETROLEUM AND PETROCHEMICALS, SINOPEC CORP.

发明人： Yuzhuo ZHAO ,  Tao LIU ,  Bingbing GUO ,  Xiaobing HUANG ,  Genhai XUAN ,  Tong XU ,  Jingjing WANG

IPC分类号： B01J8/02

CPC分类号： B01J8/0257 ,  B01J8/0278 ,  B01J2208/0084 ,  B01J2208/00938 ,  B01J2208/027

摘要： A catalytic reaction unit has a plurality of catalyst bed layers arranged vertically, each of the catalyst bed layers being filled with a solid catalyst, and an inclined surface on the upper part of the corresponding solid catalyst arranged between adjacent catalyst bed layers; a liquid phase feeding subunit arranged above the topmost catalyst bed layer, and the liquid phase feed is guided by the inclined surface to sequentially enter each catalyst bed layer from top to bottom; a gas phase feeding subunit arranged between the catalyst bed layer of an upper layer and the inclined surface of the next layer, and a gas phase channel relatively isolated from the gas phase feeding subunit. The gas phase product generated after the gas-phase feed and the liquid phase feed react in the catalyst bed layer directly enters the gas phase channel.