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1. 发明申请

WO2018081060A1 METHOD, APPARATUS, AND COMPUTER-READABLE MEDIA FOR VORTEX ARC REACTOR 审中-公开
标题翻译： VORTEX ARC反应器的方法，装置和计算机可读介质
公开(公告)号：WO2018081060A1
公开(公告)日：2018-05-03
申请号：PCT/US2017/057998
申请日：2017-10-24
申请人： ROGERS, Michael, W.
发明人： ROGERS, Michael, W.
IPC分类号： B01J19/26 , B01J8/14
CPC分类号： B01J19/2405 , B01J8/14 , B01J19/088 , B01J19/1806 , B01J19/26 , B01J2208/00867 , B01J2219/00119 , B01J2219/0805 , B01J2219/0875 , C01B3/32 , C01B3/36 , C01B2203/0255 , C01B2203/1223 , C01B2203/1241 , C07C2/80 , C07C2/82 , C10G50/00 , C10G2300/1025 , C10G2400/30
摘要： Vortex arc reactor apparatus and method provide a nozzle with converging, throat, and diverging portions. Input structure inputs a reactant and an oxidant into the converging portion. Ignition structure ignites the input reactant and oxidant. A vortex-creating structure creates a vortex of the ignited reactant and oxidant in the converging portion. The input structure, the vortex-creating structure, and the nozzle converging and throat portions are configured to provide a throat-portion-vortex of ignited reactant and oxidant that has an angular velocity which provides (i) negatively-charged particles in an exterior portion of the throat-portion-vortex, (ii) positively-charged particles in an interior portion of the throat-portion-vortex, and (iii) at least one arcing reaction between the positively- charged particles and the negatively-charged particles, to form syngas and at least one aromatic liquid in the nozzle diverging portion. Gas/liquid separation structure is preferably configured to separate the formed syngas from the at least one aromatic liquid.
摘要翻译：涡流电弧反应器装置和方法提供了具有会聚，喉部和发散部分的喷嘴。输入结构将反应物和氧化剂输入会聚部分。点火结构点燃输入反应物和氧化剂。涡流产生结构在会聚部分中产生点燃的反应物和氧化剂的涡流。输入结构，涡流产生结构以及喷嘴会聚部和喉部部分被配置为提供具有角速度的点燃的反应物和氧化剂的喉部涡流，所述角速度提供（i）外部中的带负电的粒子（ii）喉部涡流的内部中的带正电的粒子，和（iii）带正电的粒子与带负电的粒子之间的至少一次电弧反应，以及在喷嘴分叉部分中形成合成气和至少一种芳香液体。气/液分离结构优选构造成将所形成的合成气与至少一种芳香液体分离。

2. 发明申请

WO2016179154A1 PROCESS AND SYSTEM FOR RECOVERING NATURAL GAS LIQUIDS (NGL) FROM FLARE GAS USING JOULE-THOMSON (J-T) COOLING AND MEMBRANE SEPARATION 审中-公开
标题翻译：用JOULE-THOMSON（J-T）冷却和膜分离从燃气回收天然气液体（NGL）的方法和系统
公开(公告)号：WO2016179154A1
公开(公告)日：2016-11-10
申请号：PCT/US2016/030535
申请日：2016-05-03
申请人： MEMBRANE TECHNOLOGY AND RESEARCH, INC
发明人： LOKHANDWALA, Kaaeid A. , JOSHI, Sachin
IPC分类号： C10G70/04 , C10G5/06
CPC分类号： C10L3/101 , C07C7/005 , C07C7/04 , C07C7/12 , C07C7/144 , C07C7/20 , C10G5/06 , C10G70/045 , C10G2300/1025 , C10G2300/1033 , C10L3/106 , C10L3/107 , C10L2200/0461 , C10L2270/04 , C10L2290/06 , C10L2290/08 , C10L2290/10 , C10L2290/46 , C10L2290/541 , C10L2290/543 , C10L2290/548 , F25J3/0635
摘要： A process and system for recovering natural gas liquids (NGL) using a combination of J-T cooling and membrane separation. The process involves compressing, separating, and cooling a flare gas stream comprising at least methane and C 3+ hydrocarbons prior to being introduced to a J-T valve. The cooled stream exiting the J-T valve is further separated, producing a NGL product stream and an uncondensed gas stream. The uncondensed gas stream is directed to a membrane separation step, which results in a C 3+ hydrocarbon enriched stream and a C3+ hydrocarbon depleted stream. The C 3+ hydrocarbon enriched stream may be recycled back to the process to recover more NGL.
摘要翻译：使用J-T冷却和膜分离的组合回收天然气液体（NGL）的方法和系统。该方法包括在引入J-T阀之前压缩，分离和冷却至少包含甲烷和C 3+烃的火炬气流。离开J-T阀的冷却流进一步分离，产生NGL产物流和未冷凝的气流。未冷凝的气流被引导到膜分离步骤，其导致C3 +烃富集流和C3 +烃贫化流。可以将C3 +烃富集流再循环回该过程以回收更多的NGL。

3. 发明申请

WO2016156850A1 PROCESSING A METHANE-CONTAINING FEED GAS 审中-公开
标题翻译：加工含甲烷进料气
公开(公告)号：WO2016156850A1
公开(公告)日：2016-10-06
申请号：PCT/GB2016/050905
申请日：2016-03-31
申请人： COMPACTGTL PLC
发明人： BOWE, Michael Joseph , COETZEE, Michiel Christiaan , GERICKE, Johan , BARCHHA, Asit , MORGAN, Ross Alexander , WEST, David James
IPC分类号： C10G2/00 , C01B3/38 , B01J8/06 , B01J19/24
CPC分类号： C10G2/32 , B01J8/002 , B01J8/067 , B01J19/249 , B01J2208/00752 , B01J2208/00884 , B01J2219/2458 , B01J2219/2459 , B01J2219/2471 , B01J2219/2481 , B01J2219/2497 , B01J2219/2498 , C01B3/382 , C01B2203/0233 , C01B2203/0244 , C01B2203/0405 , C01B2203/042 , C01B2203/0465 , C01B2203/0495 , C01B2203/062 , C01B2203/0872 , C01B2203/1258 , C01B2203/142 , C01B2203/143 , C01B2203/148 , C10G2/341 , C10G2300/1025 , C10G2300/70
摘要： A plant is provided for processing a methane-containing feed gas to form heavier hydrocarbons. The plant comprises: a syngas generation module and a Fischer-Tropsch synthesis module. The syngas generation module is an autothermal reforming module provided with an associated air separation unit. Waste nitrogen from the air separation unit is used to purge or inert the Fischer-Tropsch synthesis reactor.
摘要翻译：提供了一种处理含甲烷进料气体以形成较重碳氢化合物的设备。该工厂包括：合成气生成模块和费 - 托合成模块。合成气生成模块是具有相关联的空气分离单元的自热重整模块。来自空气分离单元的废氮用于吹扫或惰性费 - 托合成反应器。

4. 发明申请

WO2016012371A1 RECYCLE LOOP IN PRODUCTION OF HYDROCARBONS BY OCM 审中-公开
标题翻译：通过OCM生产烃类的回收循环
公开(公告)号：WO2016012371A1
公开(公告)日：2016-01-28
申请号：PCT/EP2015/066444
申请日：2015-07-17
申请人： HALDOR TOPSØE A/S
发明人： POULSEN, Jens Michael , CHIRON, Francois-Xavier
IPC分类号： C07C1/02 , C07C2/78 , C07C2/82
CPC分类号： C07C2/82 , C07C1/0485 , C07C5/03 , C10G50/00 , C10G2300/1025 , C10G2400/02 , C10G2400/04 , C10G2400/06 , C10G2400/08 , C10G2400/30 , C07C11/04 , C07C9/04
摘要： In the present application is described a plant and process for production of hydrocarbons, the process comprising the steps of: - converting at least a feed stream comprising CH4 and O2 feed into a conversion effluent by oxidative coupling of methane (OCM), - withdrawing one or more product streams from the conversion effluent by at least one product retrieval stage; - recycling at least a portion of the remaining conversion effluent as a recycle stream in a recycle loop, said recycle loop comprising a hydrogenation stage and a methanation stage; and - adding at least part of the recycle stream to the feed stream.
摘要翻译：在本申请中描述了用于生产烃的设备和方法，该方法包括以下步骤： - 通过甲烷（OCM）的氧化偶联将至少包含CH 4和O 2进料的进料流转化为转化流出物， - 将甲烷或更多的来自转化流出物的产物流通过至少一个产物检索阶段; - 在循环回路中循环至少一部分剩余的转化流出物作为再循环流，所述循环回路包括氢化阶段和甲烷化阶段; 以及 - 将至少部分循环物流加入进料流中。

5. 发明申请

WO2015195091A2 HYBRID FUEL AND METHOD OF MAKING THE SAME 审中-公开
标题翻译：混合燃料及其制备方法
公开(公告)号：WO2015195091A2
公开(公告)日：2015-12-23
申请号：PCT/US2014/042632
申请日：2014-06-17
申请人： FUELINA TECHNOLOGIES, LLC
发明人： GOERZ, David
IPC分类号： C10L1/02 , C10G15/08 , C10G15/12
CPC分类号： C10L1/02 , C10G15/08 , C10G15/12 , C10G2300/1011 , C10G2300/1025 , C10G2300/304 , C10L1/328 , F02D19/0652 , F02D19/0671 , F02D19/081 , F02M27/042 , Y02P30/10 , Y02P30/20 , Y02T10/36

6. 发明申请

WO2015109221A1 COMPOSITIONS AND METHODS FOR RECOVERY OF STRANDED GAS AND OIL 审中-公开
标题翻译：用于回收气体和油的组合物和方法
公开(公告)号：WO2015109221A1
公开(公告)日：2015-07-23
申请号：PCT/US2015/011806
申请日：2015-01-16
申请人： CALYSTA, INC.
发明人： FONG, Howard, Lam Ho , GRATE, John, H , NGUYEN, Luan , SILVERMAN, Joshua, A. , NEWMAN, Lisa, Marie , GIVER, Lorraine, Joan , REGITSKY, Drew, D.
IPC分类号： B01D53/84
CPC分类号： C12N1/20 , A23K10/10 , A23N17/00 , B01D53/85 , B01D2251/95 , B01D2256/24 , B01D2256/245 , B01D2257/304 , B01D2258/05 , C10G3/00 , C10G2300/1025 , C10G2300/202 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L1/04 , C10L1/06 , C10L1/08 , C10L3/102 , C10L2290/544 , C12N9/0051 , C12N9/0069 , C12N15/74 , C12P7/6463 , C12R1/01 , Y02A50/2359 , Y02P30/20
摘要： The present disclosure provides compositions and methods for using recombinant C1 metabolizing microorganisms capable of metabolizing sulfur containing compounds and other contaminants to biologically convert sour or acidic natural gas into high-value molecules, and to allow recovery of stranded oil.
摘要翻译：本公开提供了使用能够代谢含硫化合物和其它污染物的重组C1代谢微生物的组合物和方法，以将酸性或酸性天然气生物转化为高价值分子，并允许回收绞股油。

7. 发明申请

WO2015082689A1 PLASMA REACTOR AND METHOD FOR DECOMPOSING A HYDROCARBON FLUID 审中-公开
标题翻译：等离子体反应器和分解烃油的方法
公开(公告)号：WO2015082689A1
公开(公告)日：2015-06-11
申请号：PCT/EP2014/076737
申请日：2014-12-05
申请人： CCP TECHNOLOGY GMBH
发明人： KÜHL, Olaf
IPC分类号： B01J19/08 , C01B3/24
CPC分类号： B01J19/088 , B01J7/02 , B01J15/005 , B01J2219/00247 , B01J2219/00351 , B01J2219/0059 , B01J2219/00594 , B01J2219/00596 , B01J2219/0072 , B01J2219/0809 , B01J2219/0826 , B01J2219/0869 , B01J2219/0875 , B01J2219/0877 , B01J2219/0884 , B01J2219/0894 , C01B3/06 , C01B3/24 , C01B31/02 , C01B32/05 , C01B2203/0272 , C01B2203/062 , C01B2203/0861 , C01B2203/1241 , C10G2/35 , C10G2300/1025 , H05H1/48 , Y02E60/36
摘要： In a plasma reactor (1) for decomposing a hydrocarbon fluid, the deposition of C particles is to be reduced or completely prevented. In order to achieve this object, there is described a plasma reactor (1) for decomposing a hydrocarbon fluid which comprises a reactor chamber (2) enclosed by a reactor wall (3, 3a) and having at least one hydrocarbon fluid inlet (5) and at least one outlet (15), and in addition it comprises a plasma burner (7) having at least two elongated electrodes which each have a base part (9) that is fixed to the reactor wall (3b) and a burner part (11) which projects into the reactor chamber (2) and has a free end. The hydrocarbon fluid inlet (5) opens out into the reactor chamber (2) in such a manner that a hydrocarbon fluid flowing out therefrom flows in a space between the reactor wall and the electrodes along at least one electrode to the free end (12) thereof. A high flow rate of the fluid is thereby achieved and the direction of flow of the incoming fluid is directed away from the hydrocarbon fluid inlet (5).
摘要翻译：在用于分解烃流体的等离子体反应器（1）中，要减少或完全防止C颗粒的沉积。为了实现该目的，描述了一种用于分解烃流体的等离子体反应器（1），其包括由反应器壁（3,3a）包围并具有至少一个烃流体入口（5）的反应室（2）和至少一个出口（15），并且另外还包括具有至少两个细长电极的等离子体燃烧器（7），每个细长电极具有固定到反应器壁（3b）的基部（9）和燃烧器部分 11），其投射到反应器室（2）中并具有自由端。碳氢化合物流体入口（5）以这样的方式开启到反应器室（2）中，使得从其流出的烃流体沿着至少一个电极在反应器壁和电极之间的空间流动到自由端（12）它们。从而实现流体的高流速，并且将进入流体的流动方向指向远离烃流体入口（5）。

8. 发明申请

WO2015015312A3 A PROCESS FOR THE PRODUCTION OF OLEFINS THROUGH FISCHER-TROPSCH BASED SYNTHESIS 审中-公开
标题翻译：通过基于FISCHER-TROPSCH的合成来生产烯烃的方法
公开(公告)号：WO2015015312A3
公开(公告)日：2015-05-14
申请号：PCT/IB2014002425
申请日：2014-07-28
申请人： SAUDI BASIC IND CORP
发明人： BASHIR MUBARIK ALI , KARIM KHALID , ALHAMMAD ALI ESSA
IPC分类号： C10K3/02 , C10G2/00 , C10K3/06
CPC分类号： C10G2/332 , C01B3/34 , C01B3/38 , C01B2203/0216 , C01B2203/0244 , C01B2203/04 , C01B2203/062 , C01B2203/1241 , C01B2203/127 , C01B2203/148 , C10G2/34 , C10G45/02 , C10G2300/1025 , C10G2400/20 , C10G2400/22 , C10K3/026 , C10K3/06 , Y02P30/40
摘要： The present disclosures and inventions relate to a method comprising: a) introducing a natural gas; b) reforming the natural gas; wherein the reforming step comprises contacting the natural gas with steam to produce a syngas: c) converting the syngas to a product mixture comprising an olefin, carbon dioxide, and hydrogen; wherein the converting step comprises contacting the syngas with a Co/Mn catalyst; and d) converting at least some process hydrogen and at least some process and/or external carbon dioxide to syngas by a reverse water gas shift reaction, and recycling such reverse water gas shift reaction produced syngas to before step c).
摘要翻译：本公开和发明涉及一种方法，包括：a）引入天然气; b）改造天然气; 其中所述重整步骤包括使所述天然气与蒸汽接触以产生合成气：c）将所述合成气转化为包含烯烃，二氧化碳和氢的产物混合物; 其中所述转化步骤包括使所述合成气与Co / Mn催化剂接触; 和d）通过反向水煤气变换反应将至少一些工艺氢气和至少一些工艺和/或外部二氧化碳转化成合成气，并且将这种反向水煤气变换反应再循环产生合成气到步骤c）之前。

9. 发明申请

WO2014031477A1 METHANE CONVERSION APPARATUS AND PROCESS USING A SUPERSONIC FLOW REACTOR 审中-公开
公开(公告)号：WO2014031477A1
公开(公告)日：2014-02-27
申请号：PCT/US2013/055277
申请日：2013-08-16
申请人： UOP LLC
发明人： BEDARD, Robert L. , NAUNHEIMER, Christopher , TOWLER, Gavin P. , LEONARD, Laura E. , DUDEBOUT, Rodolphe , WOODCOCK, Gregory O. , MITTENDORF, Donald L.
IPC分类号： C07C2/00 , C07C11/24 , B01J19/10
CPC分类号： B01J19/10 , B01J3/008 , B01J6/008 , B01J19/02 , B01J19/2415 , B01J19/26 , B01J2219/00094 , B01J2219/00123 , B01J2219/00157 , B01J2219/0204 , B01J2219/0236 , B01J2219/0263 , B01J2219/0281 , B01J2219/0286 , B01J2219/029 , C07C2/78 , C10G50/00 , C10G2300/1025 , C10G2400/24 , C07C11/24
摘要： Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

10. 发明申请

WO2011016981A3 HYDROCARBON TREATMENT METHOD AND APPARATUS 审中-公开
标题翻译：石油处理方法和装置
公开(公告)号：WO2011016981A3
公开(公告)日：2013-04-25
申请号：PCT/US2010042422
申请日：2010-07-19
申请人： PRAXAIR TECHNOLOGY INC , DRNEVICH RAYMOND FRANCIS , PAPAVASSILIOU VASILIS , RAYBOLD TROY M , PACOULOUTE PERRY RAYMOND
发明人： DRNEVICH RAYMOND FRANCIS , PAPAVASSILIOU VASILIS , RAYBOLD TROY M , PACOULOUTE PERRY RAYMOND
IPC分类号： C10G70/02 , C01B3/38 , C10G70/04
CPC分类号： C10G70/02 , C01B3/382 , C01B3/56 , C01B2203/0233 , C01B2203/0244 , C01B2203/0455 , C01B2203/0485 , C01B2203/1258 , C01B2203/142 , C10G70/046 , C10G2300/1025 , C10G2300/1088 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/4018 , C10G2300/807
摘要： A method and apparatus for producing a treated hydrocarbon containing stream for use as a feed to a hydrogen plant having a steam methane reformer in which an untreated hydrocarbon containing stream is introduced into two reaction stages connected in series to hydrogenate olefins and to convert organic sulfur species to hydrogen sulfide. The second of the two stages can also be operated in a pre-reforming mode to generate additional hydrogen through introduction of the oxygen and steam into such stage. A sulfur tolerant catalyst is used in both stages to promote hydrogenation and oxidation reactions. Sulfur is removed between stages by adsorption of the hydrogen sulfide to prevent deactivation of the catalyst in the second of the stages that would otherwise occur during operation of the second reaction stage in a pre-reforming mode of operation.
摘要翻译：一种用于生产经处理的含烃流的方法和装置，其用于具有蒸汽甲烷重整器的氢气设备的进料，其中将未处理的含烃流引入串联连接的两个反应阶段以氢化烯烃并转化有机硫物质到硫化氢。这两个阶段中的第二阶段也可以在预重整模式下操作，以通过将氧气和蒸汽引入该阶段来产生额外的氢。两个阶段都使用耐硫催化剂来促进氢化和氧化反应。通过吸附硫化氢来除去硫，以防止在预重整操作模式中在第二反应阶段的操作期间将发生的第二阶段催化剂失活。

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