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公开(公告)号:US20240228680A1
公开(公告)日:2024-07-11
申请号:US18554053
申请日:2022-03-21
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , BEIJING RESEARCH INSTITUTE OF CHEMICAL INDUSTRY, CHINA PETROLEUM & CHEMICAL CORPORATION
发明人: Rong GAO , Qingqiang GOU , Juan LI , Xiaofan ZHANG , Jingjing LAI , Longgui ZHANG , Junling ZHOU , Jie LIN , Xinyang LI , Jianhui SONG , Junhui ZHANG , Jingyan AN , Hui ZHAO , Yan LI , Dong MA , Yuanning GU
IPC分类号: C08F210/02
CPC分类号: C08F210/02 , C08F2410/03
摘要: A method for preparing polymer includes the steps of enabling olefin and unsaturated carboxylate be subjected to a polymerization reaction in the presence of a catalyst to generate an olefin-unsaturated carboxylate polymer. The catalyst has a primary catalyst and optionally a cocatalyst. The primary catalyst has at least one complex represented by formula I, formula I′, or formula I″. By selecting a reacted unsaturated carboxylate monomer, catalysts, and a suitable polymerization process, a spherical and/or sphere-like polymer having good shape is directly prepared without subsequent processing steps such as granulation, and the obtained polymer product is not prone to fouling in a reactor and is convenient for transportation.
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公开(公告)号:US20240199771A1
公开(公告)日:2024-06-20
申请号:US18554082
申请日:2022-03-18
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , BEIJING RESEARCH INSTITUTE OF CHEMICAL INDUSTRY, CHINA PETROLEUM & CHEMICAL CORPORATION
发明人: Rong GAO , Qingqiang GOU , Xiaofan ZHANG , Jingjing LAI , Junling ZHOU , Jie LIN , Xinyang LI , Jingyan AN
IPC分类号: C08F10/14 , C07F15/04 , C09J123/20
CPC分类号: C08F10/14 , C07F15/045 , C09J123/20 , C08F2800/10
摘要: A branched olefin polymer, a preparation method therefor and the use thereof are provided. The branched olefin polymer is obtained by polymerizing at least one C4-C20 nonterminal olefin monomer with optional ethylene, propylene, and C4-C20 terminal olefin monomers; and the branched olefin polymer has the following characteristics: (a) a molecular weight of 20000 to 500000 g/mol; (b) a molecular weight distribution of 3.5 to 6.0, and a bimodal structure characterized by GPC; (c) a melting point of 0° C. to 110° C. and a glass-transition temperature of −80° C. to −50° C.; and (d) having 20 to 200 methyl groups per 1000 methylene groups.
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公开(公告)号:US11980785B2
公开(公告)日:2024-05-14
申请号:US18156435
申请日:2023-01-19
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , CHINA PETROLEUM & CHEMICAL CORPORATION QINGDAO RESEARCH INSTITUTE OF SAFETY ENGINEERING
发明人: Shanjun Mu , Chunming Jiang , Weihua Zhang , Quanzhen Liu , Xuqing Lang , Xiaodong Mu , Lin Wang , Jingfeng Wu , Longmei Tan , Zuzheng Shang , Rifeng Zhou , Jianxiang Li , Hui Yu
IPC分类号: B01F23/00 , A62C5/02 , B01F23/235 , B01F25/31 , B01F25/313 , B01F27/112 , A62C3/06
CPC分类号: A62C5/02 , B01F23/235 , B01F25/31112 , B01F25/31113 , B01F25/3131 , B01F27/112 , A62C3/065 , B01F2215/0422 , B01F2215/0427 , B01F2215/0431 , B01F2215/045 , B01F2215/0468 , B01F2215/0472
摘要: A foam production method includes mixing liquid nitrogen with a foaming material to produce foam. A gas is produced in situ from liquid nitrogen. As the ratio of the volume of the gas produced by gasification of liquid nitrogen to the volume of the liquid nitrogen is relatively high, when a large gas supply flow is needed to generate a large foam flow, a liquid nitrogen storage device of a small volume can be used instead of bulky air supply devices such as high-pressure gas cylinders, air compressors, air compressor sets and the like, reducing the volume of the air supply device. In addition, the liquid nitrogen used in foaming will release nitrogen gas after the foam blast, such that the nitrogen is also able to inhibit combustion on the surface of burning materials, accelerating the extinguishing of the fire.
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公开(公告)号:US11970510B2
公开(公告)日:2024-04-30
申请号:US17286776
申请日:2019-10-15
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , BEIJING RESEARCH INSTITUTE OF CHEMICAL INDUSTRY, CHINA PETROLEUM & CHEMICAL CORPORATION
发明人: Jin Zhao , Xianzhi Xia , Yuexiang Liu , Yang Tan , Chunhong Ren , Weili Li , Long Chen , Futang Gao , Yongtai Ling , Tao Liu
IPC分类号: C08F10/00 , C07F7/28 , C08F110/00 , C08F110/06
CPC分类号: C07F7/28 , C08F110/06
摘要: Disclosed are a catalyst component and a catalyst for olefin polymerization, and an olefin polymerization method. The catalyst component comprises magnesium, titanium, a halogen and an internal electron donor, wherein the internal electron donor comprises a monocarboxylic acid ester compound and a diether compound, and the molar ratio of the monocarboxylic acid ester compound to the diether compound is (0.0035-0.7):1. By using the catalyst, a polymer having both a high isotactic index and a high melt flow index can be prepared.
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65.
公开(公告)号:US20240076559A1
公开(公告)日:2024-03-07
申请号:US18033871
申请日:2021-10-19
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , BEIJING RESEARCH INSTITUTE OF CHEMICAL INDUSTRY, CHINA PETROLEUM & CHEMICAL CORPORATION
发明人: Yan LI , Jun TIAN , Dongfeng LI , Liang GUO , Chunfang LI , Yi YUE , Zhou DU , Zhan SHU , Shujuan LUO , Jieming YE , Ting CUI
CPC分类号: C10G45/32 , C10G5/06 , C10G2300/1092 , C10G2300/4006 , C10G2300/4012 , C10G2300/802 , C10G2300/4018
摘要: The present invention belongs to the field of petrochemical industry, and discloses a method for selective hydrogenation of butadiene extraction tail gas and a selective hydrogenation apparatus thereof. The method for selective hydrogenation of butadiene extraction tail gas comprises: (1) an alkyne-containing tail gas from a butadiene extraction unit is fed into a raw material tank, optionally impurities entrained in the alkyne-containing tail gas are removed before being fed into the raw material tank; (2) a C4 raw material in the raw material tank is pressurized by a feed pump to a pressure required for reaction, then merged with a circulated C4 stream from a first-stage reactor outlet buffer tank and fed into a first-stage mixer, wherein it is mixed with hydrogen gas, and fed into the first-stage reactor to undergo a first-stage hydrogenation reaction, and a first-stage reaction stream obtained by the reaction is fed into the first-stage reactor outlet buffer tank; the hydrogen gas required for the reaction in the first-stage reactor is fed through a first feeding mode or a second feeding mode: the first feeding mode comprises: all the hydrogen gas required for the reaction is fed through the first-stage reactor outlet buffer tank, and then fed into the first-stage reactor through a first route at an outlet of the first-stage reactor outlet buffer tank; the second feeding mode comprises: a part of the hydrogen gas required for the reaction is fed through the first-stage reactor outlet buffer tank, and then fed into the first-stage reactor through the first route at an outlet of the first-stage reactor outlet buffer tank; and the other part of the hydrogen gas is fed through the first-stage mixer, and then fed into the first-stage reactor; (3) there is no gas-phase discharge from the first-stage reactor outlet buffer tank, and a liquid-phase product is divided into at least two streams, the first stream is returned to the first-stage reactor as the circulated C4 stream, and the second stream is used as a feed to a stabilization tower or subjected to further hydrotreatment prior to being fed into the stabilization tower; (4) a C4 hydrogenation product is recovered after separation in the stabilization tower.
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66.
公开(公告)号:US11826743B2
公开(公告)日:2023-11-28
申请号:US17310093
申请日:2019-10-30
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , BEIJING RESEARCH INSTITUTE OF CHEMICAL INDUSTRY, CHINA PETROLEUM & CHEMICAL CORPORATION
发明人: Hongfei Wu , Mingfang Zheng , Songshuang Hu , Tonglin Li , Jun Liu , Ke Xu , Xiaoqing Wang , Feng Pan
CPC分类号: B01J31/2409 , C07C2/36 , C07C2531/24
摘要: A halogen-containing compound represented by a formula I and a use thereof as a ligand of an ethylene oligomerization catalyst composition, an ethylene oligomerization catalyst composition comprising the halogen-containing compound, and an ethylene oligomerization method, ethylene trimerization method and ethylene tetramerization method using the catalyst composition are provided. Serving as the ligand of the ethylene oligomerization catalyst, the halogen-containing polymer may effectively improve the catalytic performance of a catalyst system, especially by displaying a significantly improved catalytic performance in an ethylene oligomerization reaction. The maximum catalyst activity may exceed 4×108 g·mol(Cr)−1·h−1, and the total selectivity of 1-hexene and 1-octene exceeds 92 wt %. In a C6 product, the content of 1-hexene may reach about 97%, and in a C8 product, the content of 1-octene may reach more than 98%.
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公开(公告)号:US20230226393A1
公开(公告)日:2023-07-20
申请号:US18002136
申请日:2021-01-22
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , CHINA PETROLEUM & CHEMICAL CORPORATION QINGDAO RESEARCH INSTITUTE OF SAFETY ENGINEERING
发明人: Lei BAO , Anfeng YU , Peng WANG , Wenyi DANG , Yongzhong BAI , Chen KUANG , Xiaodong LING , Guoxin CHEN , Houda LI , Meng GU
IPC分类号: A62C4/02
CPC分类号: A62C4/02
摘要: A flame arrester, has a housing having an inlet and an outlet, and a flame retardant core arranged within the housing. Arranged within the flame arrester housing between the flame retardant core and the inlet is a flame arresting mechanism for preventing flames from directly impacting a central zone of the flame retardant core. The flame arresting mechanism may include a flame retardant barrel and a flame retardant plate assembly disposed within the flame arrester housing.
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公开(公告)号:US11541376B2
公开(公告)日:2023-01-03
申请号:US15899988
申请日:2018-02-20
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , BEIJING RESEARCH INSTITUTE OF CHEMICAL INDUSTRY, CHINA PETROLEUM & CHEMICAL CORPORATION
发明人: Wei Dai , Haibin Jiang , Shuliang Lu , Xiaohong Zhang , Guoqing Wang , Jinliang Qiao , Hui Peng
IPC分类号: C07C5/02 , B01J25/02 , B01J25/00 , C07B35/02 , C07B35/06 , C07B35/04 , B01J31/28 , B01J31/34 , B01J37/00 , C07C1/04 , C07C1/06 , C07C29/141
摘要: A supported catalyst and preparation method thereof, the catalyst comprising an organic polymer material carrier and Raney alloy particles supported on the organic polymer material carrier, wherein substantially all of the Raney alloy particles are partially embedded in the organic polymer material carrier. The catalyst can be used in hydrogenation, dehydrogenation, amination, dehalogenation or desulfuration reactions.
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公开(公告)号:US20220403261A1
公开(公告)日:2022-12-22
申请号:US17755415
申请日:2020-10-28
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , BEIJING REASEARCH INSTITUTE OF CHEMICAL INDUSTRY, CHINA PETROLEUM & CHEMICAL CORPORATION
发明人: Tongju LIU , Guoqing WANG , Lijun ZHANG , Zhaobin ZHANG , Cong ZHOU , Bing JIANG , Ying SHI
摘要: A method for cracking crude oil includes delivering the crude oil to a first tube group of a convection section of a cracking furnace for preheating and then performing vaporization to obtain a first gas phase and a first liquid phase; performing high-pressure extraction on the first liquid phase to obtain a non-asphalt oil and an asphalt; and mixing the first gas phase and the non-asphalt oil with water vapor respectively, or mixing the first gas phase with the non-asphalt oil prior to mixing with water vapor, then delivering the same to a second tube group of the convection section of the cracking furnace for heating, followed by delivering same to a radiation section of the cracking furnace for cracking to obtain a cracked product, and separating the cracked product to obtain low-carbon olefins.
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公开(公告)号:US20220396646A1
公开(公告)日:2022-12-15
申请号:US17755542
申请日:2020-10-30
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , BEIJING RESEARCH INSTITUTE OF CHEMICAL INDUSTRY, CHINA PETROLEUM & CHEMICAL CORPORATION
发明人: Rong GAO , Jingjing LAI , Zifang GUO , Qingqiang GOU , Junling ZHOU , Wenbo SONG , Xinyang LI , Xiaofan ZHANG , Jie LIN , Dongbing LIU , Junhui ZHANG , Hongtao WANG , Shijun ZHANG , Yuanning GU , Jingyan AN , Hui ZHAO , Tingjie HUANG , Dong MA , Ruen WANG , Shiyuan XU , Jie FU
IPC分类号: C08F4/70 , C08F220/64
摘要: A method for preparing an olefin-olefinic alcohol copolymer and an olefin-olefinic alcohol copolymer prepared by the method are provided. The catalyst used in the method for preparing the olefin-olefinic alcohol copolymer has a diimine metal complex as shown in Formula I.
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