公开(公告)号：US11959044B2

公开(公告)日：2024-04-16

申请号：US17267568

申请日：2019-08-14

申请人： Green-On AB

发明人： Anders Lorén ,  Marcus Vestergren

IPC分类号： C11C3/02 ,  A23K20/158 ,  A23K50/90 ,  A23L29/00 ,  C01B32/40 ,  C07C1/04 ,  C07C1/20 ,  C07C2/04 ,  C07C11/04 ,  C07C31/04 ,  C07C51/23 ,  C07C51/25 ,  C25B1/04

CPC分类号： C11C3/02 ,  A23K20/158 ,  A23K50/90 ,  A23L29/04 ,  C01B32/40 ,  C07C1/0485 ,  C07C1/20 ,  C07C2/04 ,  C07C11/04 ,  C07C31/04 ,  C07C51/23 ,  C07C51/25 ,  C25B1/04 ,  Y02E60/36

摘要： Edible organic compounds which can serve as food or feed, or as components of food or feed, are synthesized from oxidized carbon and water, through the input of energy, and using well-known and validated synthesis pathways, leading to free fatty acids and optionally esterified to triglycerides. The source of carbon is preferably CO2 from the atmosphere, or more preferably point sources of CO2 from industry and/or energy production.

公开(公告)号：US20230391703A1

公开(公告)日：2023-12-07

申请号：US18447584

申请日：2023-08-10

申请人： The Board of Trustees of The University of Alabama ,  University of South Carolina

发明人： Elizabeth Papish ,  Aaron Vannucci

IPC分类号： C07C41/18 ,  B01J31/22 ,  C07C1/20 ,  B01J31/18

CPC分类号： C07C41/18 ,  B01J31/2295 ,  C07C1/20 ,  B01J31/181 ,  B01J31/1815 ,  B01J2531/821 ,  C07C2601/16

摘要： Disclosed are methods of selective hydrodeoxygenation of aromatic compounds by using catalyst systems comprising N-heterocyclic carbene (NHC) and 4-pyridinol-derived pincer ligands and metal complexes containing these ligands.

公开(公告)号：US20230137544A1

公开(公告)日：2023-05-04

申请号：US17906487

申请日：2021-03-12

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC

发明人： Hongyuan ZONG ,  Guozhen QI ,  Jing CAO ,  Hongtao WANG ,  Zhinan YU ,  Yijun ZHENG

IPC分类号： C07C1/20 ,  B01J29/85 ,  B01J29/90 ,  B01J38/06 ,  B01J8/26 ,  B01J8/18

摘要： The present invention relates to a process of converting methanol to olefins, comprising: feeding a feedstock comprising methanol to a fluidized bed reactor to contact with catalysts to produce an olefin product, wherein the process at least partially deactivates the catalysts to format least partially deactivated catalysts; feeding spent catalysts from the at least partially deactivated catalysts to a regenerator for regeneration, thereby forming regenerated catalysts, and returning the activated catalysts from the regenerated catalysts to the reactor via a regenerated catalyst line; characterized in that on the regenerated catalyst line, the oxygen content by volume in the gas phase component at the outlet of the regenerated catalyst line is controlled to be less than 0.1%, preferably less than 0.05%, and more preferably less than 0.01%.

公开(公告)号：US20230118300A1

公开(公告)日：2023-04-20

申请号：US17906234

申请日：2021-03-12

申请人： CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC

发明人： Guozhen QI ,  Jing CAO ,  Xiaohong LI ,  Hongtao WANG ,  Li WANG ,  Yanxue WANG

IPC分类号： C07C1/20 ,  B01J8/24 ,  B01J29/85 ,  C07C11/06

摘要： The invention relates to a process of converting methanol in a fluidized bed reactor comprising feeding a methanol-containing feedstock into a fluidized bed reactor, contacting the feedstock with a catalyst, to produce a product comprising ethylene and propylene under effective conditions; the fluidized bed reactor comprises a diluent-phase zone and a dense-phase zone, wherein the diluent-phase temperature difference between any regions of the diluent-phase zone having a methanol concentration of more than 0.1 wt % (preferably more than 0.01 wt %) in the fluidized bed reactor is controlled to be less than 20° C., and the dense-phase temperature difference between any regions in the dense-phase zone having a methanol concentration of more than 0.1 wt % (preferably more than 0.01 wt %) in the fluidized bed reactor is controlled to be less than 10° C.

公开(公告)号：US11628428B2

公开(公告)日：2023-04-18

申请号：US17365502

申请日：2021-07-01

申请人： Haldor Topsøe A/S

发明人： Uffe Vie Mentzel ,  Finn Joensen

IPC分类号： B01J29/40 ,  C10G3/00 ,  C07C1/20 ,  B01J27/14 ,  B01J29/90 ,  C10G35/00 ,  B01J21/04 ,  B01J29/85 ,  B01J37/02 ,  B01J37/08 ,  C07C1/22 ,  B01J37/28 ,  B01J21/00 ,  B01J35/00 ,  B01J21/02 ,  C07C43/04 ,  C07C41/00 ,  C07C41/01 ,  C07C29/152 ,  C10G50/00 ,  B01J21/12 ,  B01J23/00 ,  B01J23/06 ,  B01J37/00 ,  B01J27/16

摘要： A bifunctional catalyst for example for conversion of oxygenates, the bifunctional catalyst comprising zeolite, alumina binder, Zn and P, wherein Zn is present at least partly as ZnAl2O4.

公开(公告)号：US20230085715A1

公开(公告)日：2023-03-23

申请号：US17801811

申请日：2020-10-16

申请人： DALIAN INSTITUTE OF CHEMICAL PHYSICS, CHINESE ACADEMY OF SCIENCES

发明人： Tao ZHANG ,  Mao YE ,  Jinling ZHANG ,  Shuliang XU ,  Hailong TANG ,  Xiangao WANG ,  Cheng ZHANG ,  Jinming JIA ,  Jing WANG ,  Hua LI ,  Chenggong LI ,  Zhongmin LIU

IPC分类号： C07C1/20 ,  B01J8/18 ,  B01J8/22 ,  B01J8/26

摘要： A coke control reactor, a device for preparing low-carbon olefins from an oxygen-containing compound, and a use thereof are provided. The coke control reactor includes a riser reactor and a bed reactor; the bed reactor includes a bed reactor shell, and the bed reactor shell encloses a reaction zone I, a transition zone, and a gas-solid separation zone I from bottom to top; a bed reactor distributor is arranged in the reaction zone I; a coke controlled catalyst delivery pipe is arranged outside the reaction zone I; an upper section of the riser reactor penetrates through a bottom of the bed reactor and is axially inserted in the bed reactor; and an outlet end of the riser reactor is located in the transition zone. The coke control reactor can control the conversion and generation of coke species in a catalyst.

公开(公告)号：US11534732B2

公开(公告)日：2022-12-27

申请号：US16801822

申请日：2020-02-26

申请人： UOP LLC

发明人： Benjamin F. Ketter ,  Ernest J. Boehm ,  Michael J. Tobin ,  Joseph A. Montalbano ,  John J. Senetar ,  Joe Haas ,  Paul C. Steacy

IPC分类号： C07C7/09 ,  B01J8/24 ,  B01J8/18 ,  B01D5/00 ,  C07C1/20

摘要： A process and apparatus cool and remove catalyst from a hot vaporous reactor effluent stream by feeding the hot vaporous reactor effluent stream comprising catalyst and a first quench liquid stream to a first quench chamber. The hot vaporous reactor effluent stream is directly contacted with the first quench liquid stream to cool the hot reactor effluent stream and wash catalyst therefrom into the first quench liquid stream. The first quench liquid stream and the vaporous reactor effluent stream are passed together through a bed while disengaging catalyst from the vaporous reactor effluent stream and transferring catalyst into the first quench liquid stream.

公开(公告)号：US11479518B2

公开(公告)日：2022-10-25

申请号：US17623077

申请日：2020-07-06

申请人： SEKISUI CHEMICAL CO., LTD.

发明人： Noritoshi Yagihashi ,  Haruka Nishiyama ,  Yuki Nakama

IPC分类号： C07C1/20 ,  C07C7/06

摘要： The method of the present invention for producing 1,3-butadiene includes: vaporizing an ethanol feedstock in a vaporizer (104), supplying the feedstock to two or more parallel first reactors (108) to convert ethanol into acetaldehyde in the presence of a first catalyst; supplying a resulting intermediate gas to a second reactor (110) to convert ethanol and acetaldehyde into 1,3-butadiene in the presence of a second catalyst; purifying a resulting crude gas containing 1,3-butadiene by a gas-liquid separator (112), a first distillation column (114), a fourth reactor (116), and a second distillation column (118); and supplying an oxygen-containing gas to at least one of the two or more parallel first reactors (108) under specific conditions, while discharging a carbon dioxide-containing gas from the first reactor (108), to thereby regenerate the first catalyst, while continuing the conversion reaction.

公开(公告)号：US11465949B2

公开(公告)日：2022-10-11

申请号：US17453241

申请日：2021-11-02

申请人： LUMMUS TECHNOLOGY LLC

发明人： Rosette Barias ,  Liang Chen ,  Michael Jon Scott

IPC分类号： C07C1/20 ,  C07C7/04 ,  C07C7/10

摘要： Systems and methods for the production of a high purity isoamylene product. The isoamylene in a mixed hydrocarbon stream may initially be converted to TAME via etherification, and a subsequent decomposition of the TAME may result in a high purity isoamylene stream with very low impurities that is suitable for a variety of petrochemical applications, such as for use in the production of fragrances, pesticides, peroxides, polymer antioxidants, UV stabilizers and hydrocarbon resins.

公开(公告)号：US11407694B2

公开(公告)日：2022-08-09

申请号：US16478802

申请日：2018-08-17

申请人： LG CHEM, LTD.

发明人： Min Suk Kang ,  Sang Beom Lee ,  Sung Ho Lee ,  Joon Ho Shin ,  Chul Han Park

IPC分类号： C07C1/20 ,  C07C37/52 ,  C07C45/82

摘要： In a process of decomposing byproducts of a phenol production process using a reactive distillation column in which a reactor and a distillation column are integrated, since acetophenone is mixed with tar recovered to a lower part of the reactive distillation column and transferred, viscosity of the tar may be lowered so that the tar may be transferred at room temperature, and since the reactive distillation column may be operated at 0.5 to 3 bar, an operating temperature of the reactive distillation column is low as compared with a method of separating acetophenone by pressurization with high pressure, significantly reducing an operation cost of a heater required for a reaction. Also, since acetophenone is separately recovered at a position of 25 to 90% of a total number of stages in the reactive distillation column, recovery of an active ingredient may be enhanced.