公开(公告)号：US20140275673A1

公开(公告)日：2014-09-18

申请号：US14292945

申请日：2014-06-02

申请人： CHINA PETROLEUM CHEMICAL CORPORATION ,  RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPEC

发明人： Jun LONG ,  Zhijian DA ,  Dadong LI ,  Xieqing WANG ,  Xingtian SHU ,  Jiushun ZHANG ,  Hong NIE ,  Chaogang XIE ,  Zhigang ZHANG ,  Wei WANG

IPC分类号： C07C5/11 ,  C07C5/05 ,  C07C4/06

CPC分类号： C10G69/04 ,  C07C4/06 ,  C07C5/05 ,  C07C5/11 ,  C10G11/18 ,  C10G69/02 ,  C10G69/06 ,  C10G69/14 ,  C10G2300/1044 ,  C10G2300/1055 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4018 ,  C10G2300/4093 ,  C10G2300/44 ,  C10G2300/807 ,  C10G2400/20 ,  C10G2400/30

摘要： A process for producing light olefins and aromatics, which comprises reacting a feedstock by contacting with a catalytic cracking catalyst in at least two reaction zones, wherein the reaction temperature of at least one reaction zone among the reaction zones downstream of the first reaction zone is higher than that of the first reaction zone and its weight hourly space velocity is lower than that of the first reaction zone, separating the spent catalyst from the reaction product vapor, regenerating the separated spent catalyst and returning the regenerated catalyst to the reactor, and separating the reaction product vapor to obtain the desired products, light olefins and aromatics. This process produces maximum light olefins such as propylene, ethylene, etc from heavy feedstocks, wherein the yield of propylene exceeds 20% by weight, and produces aromatics such as toluene, xylene, etc at the same time.

摘要翻译： 一种用于生产轻质烯烃和芳族化合物的方法，其包括使原料与至少两个反应区中的催化裂化催化剂接触反应，其中第一反应区下游的反应区中的至少一个反应区的反应温度较高 比第一反应区的重量小时空速低于第一反应区，将废催化剂与反应产物蒸气分离，再生分离的废催化剂并将再生催化剂返回反应器，并将 反应产物蒸气得到所需产物，轻质烯烃和芳族化合物。 该方法从重质原料中产生最大的轻质烯烃，例如丙烯，乙烯等，其中丙烯的产率超过20重量％，同时产生芳烃如甲苯，二甲苯等。

公开(公告)号：US20190225897A1

公开(公告)日：2019-07-25

申请号：US15768437

申请日：2016-10-17

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPEC

发明人： Youhao XU ,  Tao LIU ,  Xin WANG ,  Lishun DAI ,  Tian LAN ,  Hong NIE ,  Dadong LI

IPC分类号： C10G69/04

摘要： A process for converting inferior feedstock oil includes several steps. In step a) the inferior feedstock oil is subjected to a low severity hydrogenation reaction. The reaction product is separated to produce a gas, a hydrogenated naphtha, a hydrogenated diesel and a hydrogenated residual oil. In step b) the hydrogenated residual oil obtained in step a) is subjected to a first catalytic cracking reaction, the reaction product is separated to produce a first dry gas, a first LPG, a first gasoline, a first diesel and a first FCC-gas oil. In step c) the first FCC-gas oil obtained in step b) is subjected to a hydrogenation reaction of gas oil, the reaction product is separated to produce a hydrogenated gas oil, and in step d) the hydrogenated gas oil obtained in step c) is subjected to the first catalytic cracking reaction of step b) or a second catalytic cracking reaction.

公开(公告)号：US20220372385A1

公开(公告)日：2022-11-24

申请号：US17772799

申请日：2020-10-30

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPEC

发明人： Qinghe YANG ,  Shuling SUN ,  Dawei HU ,  Chuanfeng NIU ,  Yanzi JIA ,  Lishun DAI ,  Zhen WANG ,  Anpeng HU ,  Liang REN ,  Dadong LI

IPC分类号： C10G69/00

摘要： Described are a process and a system for hydrotreating a deoiled asphalt. The process includes: (2) introducing a deoiled asphalt and an aromatics-containing stream into a first reaction unit for hydrogenation reaction, wherein the first reaction unit comprises a mineral-rich precursor material and/or a hydrogenation catalyst, and the first reaction unit is a fixed bed hydrogenation unit; (21) fractionating the liquid-phase product from the first reaction unit to provide a first light component and a first heavy component; (31) introducing the first light component into a second reaction unit for reaction, to provide a gasoline component, a diesel component and/or a BTX feedstock component; and (32) introducing the first heavy component to a delayed coking unit for reaction; or using the first heavy component as a low sulfur ship fuel oil component.

公开(公告)号：US20220403263A1

公开(公告)日：2022-12-22

申请号：US17772317

申请日：2020-10-30

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPEC

发明人： Qinghe YANG ,  Yanzi JIA ,  Dawei HU ,  Chuanfeng NIU ,  Shuling SUN ,  Lishun DAI ,  Zhen WANG ,  Anpeng HU ,  Liang REN ,  Dadong LI

IPC分类号： C10G69/00

摘要： Described are a process and a system for processing aromatics-rich fraction oil. The process includes: (1) introducing an aromatics-rich fraction oil into a fifth reaction unit for hydrosaturation, followed by fractionation, to provide a first light component and a first heavy component; (2) introducing a deoiled asphalt and an aromatics-comprising stream including the first heavy component into a hydrogen dissolving unit to be mixed with hydrogen, and introducing the mixed material into a first reaction unit for a hydrogenation reaction; (3) fractionating a liquid-phase product from the first reaction unit to provide a second light component and a second heavy component; (41) introducing the second light component into a second reaction unit for reaction; and (42) introducing the second heavy component into a delayed coking unit for reaction; or using the second heavy component as a component of low sulfur ship fuel oil.

公开(公告)号：US20210094023A1

公开(公告)日：2021-04-01

申请号：US17044817

申请日：2019-04-09

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPEC

发明人： Wenbin CHEN ,  Le ZHANG ,  Xiangyun LONG ,  Hong NIE ,  Mingfeng LI ,  Dadong LI ,  Qinghe LIU ,  Xueyan JU

IPC分类号： B01J23/888 ,  B01J23/882 ,  B01J23/883 ,  B01J21/18 ,  B01J21/06 ,  B01J23/02 ,  B01J21/04 ,  B01J27/16 ,  B01J35/10 ,  B01J37/02 ,  B01J37/08 ,  B01J37/20 ,  C10G45/08

摘要： Disclosed is a hydrofining catalyst comprising: an inorganic refractory component comprising a first hydrodesulfurization catalytically active component in a mixture with at least one oxide selected from the group consisting of alumina, silica, magnesia, calcium oxide, zirconia and titania; a second hydrodesulfurization catalytically active component; and an organic component comprising a carboxylic acid and optionally an alcohol. The hydrofining catalyst of the present application shows improved performance in the hydrofining of distillate oils. Also disclosed are a hydrofining catalyst system comprising the hydrofining catalyst, a method for preparing the catalyst and catalyst system, and a process for the hydrofining of distillate oils using the catalyst or catalyst system.

公开(公告)号：US20200040266A1

公开(公告)日：2020-02-06

申请号：US16339681

申请日：2017-10-20

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPEC

发明人： Youhao XU ,  Junyi MAO ,  Xin WANG ,  Qing YUAN ,  Jingchuan YU ,  Hong NIE ,  Dadong LI

IPC分类号： C10G67/14 ,  C10L1/02 ,  C10L1/06 ,  B01J23/08 ,  B01J21/12 ,  B01J19/24 ,  B01D3/14

摘要： The present application relates to a process for treating gasoline, comprising the steps of: splitting a gasoline feedstock into a light gasoline fraction and a heavy gasoline fraction; optionally, subjecting the resulting light gasoline fraction to etherification to obtain an etherified oil; contacting the heavy gasoline fraction with a mixed catalyst and subjecting it to desulfurization and aromatization in the presence of hydrogen to obtain a heavy gasoline product; wherein the mixed catalyst comprises an adsorption desulfurization catalyst and an aromatization catalyst. The process of the present application is capable of reducing the sulfur and olefin content of gasoline and at the same time increasing the octane number of the gasoline while maintaining a high yield of gasoline.