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Patent Agency Ranking1.发明授权REACTOR COMPRISING A PLASMA SOURCE AND A CATALYST COMPRISING A MESOPOROUS SUPPORT MATERIAL FOR THE PREPARATION OF ETHENE FROM METHANE 有权包含等离子体载体材料的催化剂和包含等离子体源的催化剂用于从甲烷制备乙烯的反应器
公开(公告)号：EP3036034B1
公开(公告)日：2017-07-26
申请号：EP14789610.4
申请日：2014-08-20
Applicant: Saudi Basic Industries Corporation
Inventor： ILIYAS, Abduljelil , ABDELGHANI, Mohamed Sabri
CPC classification number: B01J19/088 , B01J2219/0805 , B01J2219/0875 , B01J2219/0892 , B01J2219/0894 , B01J2219/0896 , B01J2219/0898 , C01B3/26 , C01B2203/1058 , C01B2203/107 , C01B2203/1082 , C01B2203/1241 , C07C2/76 , C07C2/84 , C07C2523/44 , C07C2529/74 , C08F110/02 , C10G50/00 , Y02P20/52 , C07C11/04
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2.发明公开CATALYST COMPOSITION PRE-FORMATION UNIT FOR PREPARING A CATALYST COMPOSITION FOR OLIGOMERIZATION OF ETHYLENE 审中-公开催化剂组合物BLANK装置，来生成的催化剂组合物乙烯齐聚
公开(公告)号：EP3102616A1
公开(公告)日：2016-12-14
申请号：EP15709995.3
申请日：2015-02-03
Applicant: Saudi Basic Industries Corporation
Inventor： KHURRAM, Shehzada , AZAM, Shahid , AL-QAHTANI, Abdullah Mohammad , ILIYAS, Abduljelil , MEISWINKEL, Andreas , MUELLER, Wolfgang , WOEHL, Anina , HARFF, Marco Marco , BOELT, Heinz
CPC classification number: B01J31/143 , B01J31/0239 , B01J31/0268 , B01J31/1885 , B01J31/22 , B01J2231/20 , B01J2531/007 , B01J2531/62
Abstract: A pre-formation unit, includes: a first vessel comprising a solution of co-catalyst and modifier; a second vessel comprising chromium compound and ligand; wherein the first and second vessel are connected via lines to a mixing unit, wherein each line has a flow control valve; wherein the mixing unit is connected via a line having a flow control valve to an oligomerization reactor; wherein gas inlets are each connected to the first vessel and to the second vessel, and wherein a portion of each of the first vessel, the second vessel, the mixing unit, and the flow control valves are within a temperature controlled enclosure.
Abstract translation: 阿形成预单元，包括：第一容器，包括助催化剂和改性剂的溶液; 第二容器包含铬化合物和配体; worin所述第一和第二容器通过管路与混合单元被连接时，worin每一行都有一个流量控制阀; worin混合单元通过具有在低聚反应器的流量控制阀，以直线连接; worin气体入口分别连接到所述第一容器和所述第二容器中，并且每个worin第一容器，第二容器中，将混合单元的一部分，并且所述流量控制阀是一温度控制的外壳内。
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3.发明公开REACTOR COMPRISING A PLASMA SOURCE AND A CATALYST COMPRISING A MESOPOROUS SUPPORT MATERIAL FOR THE PREPARATION OF ETHENE FROM METHANE 有权配备了等离子源和催化剂介孔reactor支持材料中产生的甲烷ETHEN的生产
公开(公告)号：EP3036034A1
公开(公告)日：2016-06-29
申请号：EP14789610.4
申请日：2014-08-20
Applicant: Saudi Basic Industries Corporation
Inventor： ILIYAS, Abduljelil , ABDELGHANI, Mohamed Sabri
CPC classification number: B01J19/088 , B01J2219/0805 , B01J2219/0875 , B01J2219/0892 , B01J2219/0894 , B01J2219/0896 , B01J2219/0898 , C01B3/26 , C01B2203/1058 , C01B2203/107 , C01B2203/1082 , C01B2203/1241 , C07C2/76 , C07C2/84 , C07C2523/44 , C07C2529/74 , C08F110/02 , C10G50/00 , Y02P20/52 , C07C11/04
Abstract: The invention relates to a reactor comprising a plasma source and a catalyst comprising a mesoporous support. The invention also relates to a process comprising feeding methane to said reactor in order to obtain one or more of ethene, hydrogen and carbon as well as downstream products derived from ethene thus obtained. The invention relates to a reactor comprising as reactor parts: a. a housing and in said housing; b. a plasma source; and c. a catalyst, wherein said catalyst comprises as catalyst parts: i) a mesoporous support; ii) a metal selected from the group Pd, Ni, Ag or at least two thereof, wherein the metal is carried by said mesoporous support; wherein at least a part of said plasma source is located in said housing upstream of said catalyst.
Abstract translation: 本发明涉及的电抗器，其包括等离子源和一种催化剂，包含一中孔载体。 因此，本发明涉及包含以获得一个或多个乙烯，氢和碳，以及来自乙烯由此获得衍生的下游产品的供给甲烷到所说的反应器的方法。 本发明涉及的电抗器，其包含如反应器部分组成：一个。 在所述外壳中的壳体和; 湾 等离子体源; 和c。 的催化剂，worin所述催化剂包括催化部分：ⅰ）中孔载体; ii）从所述组钯，镍，银或它们的至少两种，worin金属是由所述中孔支撑件承载的金属; worin至少所述等离子体源的一部分位于所述壳体所述催化剂的上游。
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公开(公告)号：EP2872468A1
公开(公告)日：2015-05-20
申请号：EP13727521.0
申请日：2013-06-05
Applicant: Saudi Basic Industries Corporation , Linde AG
Inventor： WÖHL, Anina , MÜLLER, Wolfgang , BÖLT, Heinz , MEISWINKEL, Andreas , HARFF, Marco , WELLENHOFER, Anton , HOFMANN, Karl-Heinz , ZANDER, Hans-Jörg , ILIYAS, Abduljelil , KHURRAM, Shahid , AZAM, Shahid , AL-QAHTANI, Abdullah
CPC classification number: C07C2/36 , B01J31/143 , B01J31/187 , B01J31/1885 , B01J2231/20 , B01J2531/62 , C07C2531/14 , C07C2531/24 , C07C11/08 , C07C11/107 , C08F210/16 , C08F4/22 , C08F4/69 , C08F2500/02
Abstract: The present invention relates to a method for oligomerization of ethylene, comprising the steps: a) feeding ethylene, solvent and a catalyst composition comprising catalyst and cocatalyst into a reactor, b) oligomerizing ethylene in the reactor, c) discharging a reactor effluent comprising linear alpha-olefins including I-butene, solvent, unconsumed ethylene dissolved in the reactor effluent, and catalyst composition from the reactor, d) separating ethylene and 1-butene collectively from the remaining reactor effluent, and e) recycling at least a part of the ethylene and the 1-butene separated in step d) into the reactor.
Abstract translation: 本发明涉及乙烯低聚方法，包括以下步骤：a）将乙烯，溶剂和包含催化剂和助催化剂的催化剂组合物进料到反应器中，b）在反应器中使乙烯低聚，c）将包含线性 从反应器流出物中溶解的α-烯烃，溶剂，未消耗的乙烯，以及来自反应器的催化剂组合物，d）从剩余的反应器流出物中分离乙烯和1-丁烯，和e）将至少一部分 乙烯和步骤d）中分离的1-丁烯进入反应器。
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公开(公告)号：EP2872468B1
公开(公告)日：2017-11-15
申请号：EP13727521.0
申请日：2013-06-05
Applicant: Saudi Basic Industries Corporation , Linde AG
Inventor： WÖHL, Anina , MÜLLER, Wolfgang , BÖLT, Heinz , MEISWINKEL, Andreas , HARFF, Marco , WELLENHOFER, Anton , HOFMANN, Karl-Heinz , ZANDER, Hans-Jörg , ILIYAS, Abduljelil , KHURRAM, Shahid , AZAM, Shahid , AL-QAHTANI, Abdullah
CPC classification number: C07C2/36 , B01J31/143 , B01J31/187 , B01J31/1885 , B01J2231/20 , B01J2531/62 , C07C2531/14 , C07C2531/24 , C07C11/08 , C07C11/107 , C08F210/16 , C08F4/22 , C08F4/69 , C08F2500/02
Abstract: The present invention relates to a method for oligomerization of ethylene, comprising the steps: a) feeding ethylene, solvent and a catalyst composition comprising catalyst and cocatalyst into a reactor, b) oligomerizing ethylene in the reactor, c) discharging a reactor effluent comprising linear alpha-olefins including I-butene, solvent, unconsumed ethylene dissolved in the reactor effluent, and catalyst composition from the reactor, d) separating ethylene and 1-butene collectively from the remaining reactor effluent, and e) recycling at least a part of the ethylene and the 1-butene separated in step d) into the reactor.
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