公开(公告)号：US20190047931A1

公开(公告)日：2019-02-14

申请号：US16076939

申请日：2017-02-10

申请人： GASCONTEC AG

发明人： Wolff BALTHASAR ,  Dierk MÜLLER ,  Ulrich WAGNER

IPC分类号： C07C29/151 ,  C07C31/04 ,  C01B3/38 ,  C01B3/56

CPC分类号： C07C29/1518 ,  B01J8/0457 ,  B01J8/0492 ,  B01J8/0496 ,  B01J23/80 ,  B01J2208/00176 ,  B01J2208/0053 ,  C01B3/38 ,  C01B3/382 ,  C01B3/52 ,  C01B3/56 ,  C01B2203/0244 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/061 ,  C01B2203/0827 ,  C01B2203/1241 ,  C01B2203/127 ,  C07C29/1516 ,  C07C31/04 ,  Y02P20/132

摘要： A method for the synthesis of methanol includes the steps of feeding a hydrogen-containing stream from a hydrogen recovery stage into a synthesis gas stream containing hydrogen and carbon oxides, and feeding the synthesis gas stream to a primary reactor stage for the catalytic and partial conversion of the synthesis gas stream into a gas mixture containing water, methanol, and residual gas, and further including the step of feeding a first portion of the residual gas to the hydrogen recovery stage for separation into the hydrogen-containing stream and a waste gas stream. The method is characterized in that a second portion of the residual gas is fed to a secondary reactor stage for further catalytic and at least partial conversion into a methanol-containing product stream.

公开(公告)号：US20180186710A1

公开(公告)日：2018-07-05

申请号：US15826117

申请日：2017-11-29

申请人： Saudi Arabian Oil Company

发明人： Raed H. Abudawoud ,  Zhonglin Zhang

IPC分类号： C07C4/18 ,  C07C5/10 ,  C07C15/08 ,  C07C15/04 ,  C07C15/24 ,  C07C13/271

CPC分类号： C07C4/18 ,  B01D53/047 ,  B01D2256/16 ,  B01D2257/702 ,  C07C5/10 ,  C07C6/123 ,  C07C6/126 ,  C07C13/271 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08 ,  C07C15/24 ,  C10G63/04 ,  C10G2300/1096 ,  C10G2300/4081 ,  C10G2400/20 ,  C10G2400/30 ,  Y02P20/125 ,  Y02P20/132

摘要： Systems and processes for maximizing the production of benzene and para-xylene from heavy reformate are provided. An integrated process and system may include a C9 dealkylation reactor, a transalkylation reactor, and a C10+ dealkylation reactor. The integrated process and system for producing benzene and para-xylene may be configured to additionally produce alkanes in the presence of hydrogen or olefins in the absence of hydrogen. The transalkylation reactor may perform transalkylation of product from the C9 dealkylation reactor and xylene isomerization.

公开(公告)号：US20180162790A1

公开(公告)日：2018-06-14

申请号：US15375085

申请日：2016-12-11

申请人： ThyssenKrupp Industrial Solutions AG ,  ThyssenKrupp AG

发明人： Muhamad Fouad

IPC分类号： C07C5/327 ,  C07C253/18 ,  C07C51/15 ,  C07C29/151 ,  C01C1/04 ,  B01J19/24

CPC分类号： C07C5/327 ,  B01J19/245 ,  C01B3/025 ,  C01B3/26 ,  C01B2203/061 ,  C01C1/0405 ,  C07C5/3337 ,  C07C29/152 ,  C07C253/18 ,  C07C253/24 ,  Y02P20/132 ,  C07C11/06 ,  C07C31/04 ,  C07C255/08

摘要： Disclosed is a modified propene dehydrogenation (PDH) system and method for producing one or more chemical products from propane as the sole feed stock. The modified PDH system includes a reactor for converting propane into a stream of propene, hydrogen, and waste gas. It further includes a de-ethanizer stripper downstream of the PDH reactor for separating the reactor output gas into a stream of propene as one of an end product or an intermediate product, and a stream of hydrogen and waste gas. The modified PDH system also includes a hydrogen recovery unit disposed downstream of the de-ethanizer stripper system for separating the stream of waste gas and hydrogen into separate streams of waste gas, and hydrogen, with the hydrogen stream being one of an end product or an intermediate product. The modified PDH system can produce propene, hydrogen, ammonia, acrylonitrile, urea, or methanol.

公开(公告)号：US20170362724A1

公开(公告)日：2017-12-21

申请号：US15536383

申请日：2015-12-14

申请人： COMMISSARIAT A L'ENERGIE ATOMIQUE ET AUX ENERGIES ALTERNATIVES

发明人： Michel PLANQUE ,  Magali REYTIER ,  Guihem ROUX

IPC分类号： C25B15/08 ,  H01M8/2425 ,  C25B1/12 ,  C25B9/20 ,  C25B9/06 ,  H01M8/0258 ,  H01M8/0282 ,  H01M8/124

CPC分类号： C25B15/08 ,  C25B1/12 ,  C25B9/06 ,  C25B9/20 ,  H01M8/006 ,  H01M8/021 ,  H01M8/0247 ,  H01M8/0258 ,  H01M8/0276 ,  H01M8/0282 ,  H01M8/04671 ,  H01M8/04753 ,  H01M8/2425 ,  H01M8/2432 ,  H01M2008/1293 ,  Y02E60/366 ,  Y02P20/132

摘要： A module for an HTE reactor or an SOFC fuel cell, the module including a circuit for the circulation of a gas, in addition to the reactive gases required for the electrolysis reaction or the reverse reaction in an SOFC cell, the circuit enabling, during the operation under pressure, the additional gas to equalise, on one side of the glass- and/or vitroceramic-based seals, the pressure of the reactive gases generated on the other side.

公开(公告)号：US09845433B2

公开(公告)日：2017-12-19

申请号：US14437298

申请日：2013-10-25

申请人： JX Nippon Oil & Energy Corporation

发明人： Shinichiro Yanagawa ,  Masahide Kobayashi ,  Yukihiro Yoshiwara ,  Ryoji Ida

IPC分类号： C10G11/05 ,  B01J19/24 ,  C10G69/04 ,  C10G35/04 ,  B01J8/02 ,  C10G35/095 ,  C10G63/04 ,  C10G69/06 ,  C10G69/08

CPC分类号： C10G11/05 ,  B01J8/02 ,  B01J2208/027 ,  C10G35/04 ,  C10G35/095 ,  C10G63/04 ,  C10G69/04 ,  C10G69/06 ,  C10G69/08 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/30 ,  Y02P20/132

摘要： A method for producing an olefin and a monocyclic aromatic hydrocarbon of the present invention includes a dicyclopentadiene removal treatment step of removing dicyclopentadienes having a dicyclopentadiene skeleton from a feedstock oil which is a thermally-cracked heavy oil obtained from an apparatus for producing ethylene and which has a 90 volume % distillate temperature, as a distillation characteristic, of 390° C. or lower; and a cracking and reforming reaction step of obtaining a product containing an olefin and a monocyclic aromatic hydrocarbon by bringing the feedstock oil having a content of dicyclopentadienes adjusted to 10% by weight or less by treating a part or all of the feedstock oil through the dicyclopentadiene removal step into contact with a catalyst and reacting the feedstock oil.

公开(公告)号：US20170314144A1

公开(公告)日：2017-11-02

申请号：US15262914

申请日：2016-09-12

申请人： Chun-Yi Yu

发明人： Chun-Yi Yu

IPC分类号： C25B1/04 ,  F17D1/08 ,  F17D1/04 ,  F01D15/10 ,  F01D15/08 ,  F01D9/02 ,  F01D5/02 ,  F17D1/14 ,  C25B1/26

CPC分类号： C25B1/04 ,  C25B1/26 ,  F01D5/02 ,  F01D9/02 ,  F01D15/08 ,  F01D15/10 ,  F17D1/04 ,  F17D1/08 ,  F17D1/14 ,  F17D5/02 ,  Y02E60/34 ,  Y02E60/366 ,  Y02P20/132 ,  Y02P90/45

摘要： A seawater electrolysis hydrogen recovery and power generation system is capable of recovering hydrogen gas and using the hydrogen gas to drive an electric turbine generator during the operation of a seawater electrolyzer for production of sodium hypochlorite. The seawater electrolysis hydrogen recovery and power generation system includes pipelines, booster pumps, a plenum chamber and a condenser chamber.

公开(公告)号：US09610547B2

公开(公告)日：2017-04-04

申请号：US12979565

申请日：2010-12-28

申请人： Yong Ding ,  Benjamin Bikson

发明人： Yong Ding ,  Benjamin Bikson

IPC分类号： B01D71/32 ,  B01D71/78 ,  B01D71/38 ,  B01D69/12

CPC分类号： B01D69/12 ,  B01D71/32 ,  B01D71/38 ,  B01D71/78 ,  B01D2323/18 ,  B01D2325/34 ,  B29C67/202 ,  B29C71/02 ,  B29C2071/022 ,  B29K2071/00 ,  B29K2105/041 ,  B29L2031/755 ,  Y02P20/132

摘要： Composite porous hydrophobic membranes are prepared by forming a perfluorohydrocarbon layer on the surface of a preformed porous polymeric substrate. The substrate can be formed from poly (aryl ether ketone) and a perfluorohydrocarbon layer can be chemically grafted to the surface of the substrate. The membranes can be utilized for a broad range of fluid separations, such as microfiltration, nanofiltration, ultrafiltration as membrane contactors for membrane distillation and for degassing and dewatering of fluids. The membranes can further contain a dense ultra-thin perfluorohydrocarbon layer superimposed on the porous poly (aryl ether ketone) substrate and can be utilized as membrane contactors or as gas separation. membranes for natural gas treatment and gas dehydration.

公开(公告)号：US20170009154A1

公开(公告)日：2017-01-12

申请号：US15121096

申请日：2014-12-23

申请人： SAUDI BASIC INDUSTRIES CORPORATION ,  SABIC GLOBAL TECHNOLOGIES B.V.

发明人： Arno Johannes Maria OPRINS

IPC分类号： C10G69/00

CPC分类号： C10G69/00 ,  C10B57/045 ,  C10G9/00 ,  C10G9/005 ,  C10G9/36 ,  C10G69/06 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/30 ,  Y02P20/132

摘要： An integrated hydrocracking process for production of olefinic and aromatic petrochemicals from a hydrocarbon feedstock having crude oil. An object of the present invention is to provide an integrated hydrocracking process for the production of olefinic and aromatic petrochemicals from a hydrocarbon feedstock comprising crude oil in which the portion of crude oil converted to LPG is increased significantly.

摘要翻译： 一种用于从具有原油的烃原料生产烯烃和芳族石化产品的综合加氢裂化方法。 本发明的目的是提供一种用于从包含原油的烃原料生产烯烃和芳族石化产品的综合加氢裂化方法，其中转化成LPG的原油部分显着增加。

公开(公告)号：US09080240B2

公开(公告)日：2015-07-14

申请号：US13863988

申请日：2013-04-16

申请人： Liquid Light, Inc.

发明人： Kyle Teamey ,  Jerry J. Kaczur ,  Emily Barton Cole

IPC分类号： C25B3/02 ,  C25B15/08 ,  C07C51/15 ,  C07C29/149 ,  C07C51/02 ,  C25B1/00 ,  C25B9/10 ,  C25B3/04 ,  C25B3/06 ,  C25B9/08 ,  C25B3/00 ,  C25B1/24 ,  C07C51/367 ,  C07C67/08 ,  C07C1/26 ,  C07C29/58 ,  C25B15/00 ,  C25B13/08 ,  C25B3/10

CPC分类号： C25B3/00 ,  C07C1/26 ,  C07C29/149 ,  C07C29/58 ,  C07C51/02 ,  C07C51/15 ,  C07C51/367 ,  C07C67/08 ,  C25B1/00 ,  C25B1/24 ,  C25B3/02 ,  C25B3/04 ,  C25B3/06 ,  C25B3/10 ,  C25B9/08 ,  C25B9/10 ,  C25B13/08 ,  C25B15/00 ,  C25B15/08 ,  Y02P20/127 ,  Y02P20/132 ,  Y02P20/133 ,  Y02P20/582

摘要： The present disclosure is a method and system for electrochemically co-producing a first product and a second product. The system may include a first electrochemical cell, a first reactor, a second electrochemical cell, at least one second reactor, and at least one third reactor. The method and system for for co-producing a first product and a second product may include co-producing a glycol and an alkene employing a recycled halide.

摘要翻译： 本公开是用于电化学共同生产第一产品和第二产品的方法和系统。 该系统可以包括第一电化学电池，第一反应器，第二电化学电池，至少一个第二反应器和至少一个第三反应器。 用于共同生产第一产物和第二产物的方法和系统可以包括使用再循环卤化物共同生产二醇和烯烃。

公开(公告)号：US08882890B2

公开(公告)日：2014-11-11

申请号：US13728568

申请日：2012-12-27

申请人： UOP LLC

发明人： Frank S. Rosser ,  Larry D. Awe

IPC分类号： B01D53/14 ,  B01D53/18 ,  B01D47/02 ,  C07C7/11

CPC分类号： B01D53/14 ,  B01D47/02 ,  B01D53/002 ,  B01D53/1487 ,  B01D53/18 ,  B01D2252/205 ,  B01D2256/16 ,  B01D2257/702 ,  C07C7/11 ,  C10G70/043 ,  C10G70/048 ,  Y02P20/132

摘要： Embodiments of apparatuses and methods for separating liquefiable hydrocarbons from H2-, hydrocarbon-containing gas streams are provided. In one example, a method comprises positioning a H2-, hydrocarbon-containing gas stream in an internal volume of a vessel below a heat exchange absorption section. A hydrocarbon-containing liquid stream is positioned in the internal volume above the heat exchange absorption section. The hydrocarbon-containing liquid stream is countercurrent contacted with at least a portion of the H2-, hydrocarbon-containing gas stream along a tube portion of the heat exchange absorption section to separate H2 and C3+ hydrocarbons. The hydrocarbon-containing liquid stream and the at least the portion of the H2-, hydrocarbon-containing gas stream are cooled along the tube portion to facilitate separating H2 and C3+ hydrocarbons.

摘要翻译： 提供了将液化烃与含H2-烃的气流分离的装置和方法的实施例。 在一个实例中，一种方法包括将H2-含烃气流定位在热交换吸收段下方的容器的内部体积中。 含烃液体流定位在热交换吸收部分上方的内部体积中。 含烃液体物流与沿热交换吸收部分的管部分的至少一部分含H2-烃的气流逆流接触以分离H 2和C 3 +烃。 含烃液体物流和至少部分含H2-烃的气流沿着管部分被冷却，以便于分离H 2和C 3+烃。