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1. 发明申请

WO2013008029A1 FISCHER TROPSCH REACTOR 审中-公开
标题翻译： FISCHER TROPSCH反应器
公开(公告)号：WO2013008029A1
公开(公告)日：2013-01-17
申请号：PCT/GB2012/051668
申请日：2012-07-13
申请人： GAS2 LIMITED , BANISTER, James
发明人： BANISTER, James
IPC分类号： B01J12/00 , B01J19/24 , C10G2/00 , B01J35/04
CPC分类号： B01J16/005 , B01J12/007 , B01J19/2485 , B01J19/249 , B01J21/04 , B01J23/8913 , B01J35/0066 , B01J35/023 , B01J35/04 , B01J37/0219 , B01J37/0221 , B01J37/0248 , B01J2219/2404 , B01J2219/2406 , B01J2219/2407 , B01J2219/2411 , B01J2219/2424 , B01J2219/2428 , B01J2219/2438 , B01J2219/2445 , B01J2219/2448 , C10G2/332 , C10G2/341
摘要： There is herein described a Fischer-Tropsch reactor. More particularly, there is described a Fischer-Tropsch reactor that incorporates forced flow through a small pore, thick layer, monolith supported catalyst and high levels of heat transfer that is able to operate with high levels of catalyst effectiveness. The catalyst bed (103) is supported on a distinct porous structure (101) through which the syngas flow is forced and the catalyst layer has a thickness of more than 200 microns.
摘要翻译：在此描述了费 - 托反应器。更具体地，描述了一种费 - 托反应器，其包含强制流过小孔，厚层，整体式负载的催化剂和能够以高水平的催化剂有效性操作的高水平的热传递。催化剂床（103）被支撑在不同的多孔结构（101）上，通过该不同的多孔结构（101），合成气流被强制并且催化剂层的厚度大于200微米。

2. 发明申请

WO2011083332A1 APPARATUS AND METHOD FOR ADIABATIC METHANE CONVERSION 审中-公开
标题翻译：装置和方法适用于甲苯转化
公开(公告)号：WO2011083332A1
公开(公告)日：2011-07-14
申请号：PCT/GB2011/050014
申请日：2011-01-07
申请人： GAS2 LIMITED , QUINTERO, Ruben Dario Rodriguez , DIAZ, Ernesto Manuel Santana , BANISTER, James Andrew
发明人： QUINTERO, Ruben Dario Rodriguez , DIAZ, Ernesto Manuel Santana , BANISTER, James Andrew
IPC分类号： B01J19/24 , C01B3/38
CPC分类号： B01J19/2475 , B01J35/065 , B01J2219/00155 , C01B3/386 , C01B13/0251 , C01B2203/0261 , C01B2203/1047 , C01B2203/1241 , Y02P20/52
摘要： There is herein described a process and apparatus for hydrocarbon conversion. More particularly, there is described a process and apparatus for adiabatic methane conversion into synthetic gas (i.e. syngas).
摘要翻译：本文描述了用于烃转化的方法和装置。更具体地，描述了将绝热甲烷转化成合成气体（即合成气）的方法和装置。

3. 发明申请

WO2009061955A1 APPROACH FOR CONTROLLING ELECTRICAL POWER 审中-公开
标题翻译：控制电力的方法
公开(公告)号：WO2009061955A1
公开(公告)日：2009-05-14
申请号：PCT/US2008/082683
申请日：2008-11-06
申请人： SPROUTLETS, INC. , BANISTER, James, A. , KIM, Francis , ARNOLD, Angela, Lee
发明人： BANISTER, James, A. , KIM, Francis , ARNOLD, Angela, Lee
IPC分类号： G01R21/00
CPC分类号： G06Q50/06
摘要： An electrical power metering system. The electrical power metering system may include a plurality of gated power receptacles, each of the gated power receptacles being configured to selectively provide electrical power in response to receiving a wireless signal. The system may further include a service application configured to receive a request to provide electrical power for one of the plurality of gated power receptacles, the request including an identifier that designates the one of the plurality of gated power receptacles at which electrical power is requested. The system may further include a local host application executable on a computing device, the local host application being configured to send the wireless signal via a coordinator module to the one of the plurality of gated power receptacles to provide electrical power in response to receiving a communication from the service application that includes the identifier.
摘要翻译：电力计量系统。电力计量系统可以包括多个门控电源插座，每个门控电源插座被配置为响应于接收无线信号选择性地提供电力。该系统还可以包括服务应用，其被配置为接收为多个门控电源插座之一提供电力的请求，该请求包括指定多个门控电源插座之一的标识符，在该门控电源插座中请求电力。该系统还可以包括在计算设备上可执行的本地主机应用，本地主机应用被配置为经由协调器模块将无线信号发送到多个门控电源插座中的一个，以响应于接收通信而提供电力从包含标识符的服务应用程序。

4. 发明申请

WO2002096555A1 PROCESS FOR RECOVERING HOMOGENEOUS METAL HYDRATE CATALYSTS 审中-公开
标题翻译：回收均质金属氢化物催化剂的方法
公开(公告)号：WO2002096555A1
公开(公告)日：2002-12-05
申请号：PCT/GB2002/002577
申请日：2002-05-29
申请人： DAVY PROCESS TECHNOLOGY LIMITED , CRABTREE, Simon, Peter , WILD, Robert , JACKSON, Simon, Wayne , BANISTER, James, Andrew
发明人： CRABTREE, Simon, Peter , WILD, Robert , JACKSON, Simon, Wayne , BANISTER, James, Andrew
IPC分类号： B01J31/40
CPC分类号： B01J31/121 , B01J21/08 , B01J31/08 , B01J31/20 , B01J31/2404 , B01J31/4038 , B01J31/4046 , B01J31/4069 , B01J31/4092 , B01J38/74 , B01J2231/321 , B01J2531/82 , B01J2531/822 , C07C45/50 , Y02P20/544 , Y02P20/584 , C07C47/02
摘要： The present invention relates to a process for recovery of homogeneous metal hydride catalyst from a reactor stream as catalyst suitable for recycle to a reactor comprising the steps of: removing a stream from a reactor, said stream comprising the homogeneous metal hydride catalyst; contacting the stream with a solid acidic absorbent under process conditions which allow at least some of the metal to become bound to the absorbent; subjecting the metal bound to the absorbent, under process conditions which allow desorption of the metal, to a fluid stripping medium comprising hydrogen and solvent; and recovering the active metal hydride catalyst.
摘要翻译：本发明涉及从反应器料流中回收均相金属氢化物催化剂的方法，该催化剂适于再循环到反应器中，所述催化剂包括以下步骤：从反应器中除去流，所述物流包含均相金属氢化物催化剂; 在工艺条件下使流与固体酸性吸收剂接触，这使得至少一些金属能够结合到吸收剂上; 在允许金属解吸的工艺条件下将结合到吸收剂上的金属经受包含氢和溶剂的流体汽提介质; 并回收活性金属氢化物催化剂。

5. 发明申请

WO2013008009A1 APPARATUS FOR ADIABATIC METHANE PARTIAL OXIDATION 审中-公开
标题翻译：用于甲苯部分氧化的装置
公开(公告)号：WO2013008009A1
公开(公告)日：2013-01-17
申请号：PCT/GB2012/051634
申请日：2012-07-11
申请人： GAS2 LIMITED , BANISTER, James
发明人： BANISTER, James
IPC分类号： C01B3/38 , B01J15/00 , B01J19/24 , B01J4/00
CPC分类号： C01B3/386 , B01J4/004 , B01J15/005 , B01J19/2425 , B01J19/2475 , B01J2219/00155 , C01B2203/0261 , C01B2203/12 , C01B2203/1241 , C01B2203/1614
摘要： There is herein described a process and apparatus for hydrocarbon conversion. More particularly, there is described a process and apparatus for adiabatic methane conversion into synthetic gas (i.e. syngas).
摘要翻译：本文描述了用于烃转化的方法和装置。更具体地，描述了将绝热甲烷转化成合成气体（即合成气）的方法和装置。

6. 发明申请

WO2012131385A3 HIGH PRESSURE GAS TO LIQUID PROCESS 审中-公开
标题翻译：高压气体对液体过程的影响
公开(公告)号：WO2012131385A3
公开(公告)日：2012-11-15
申请号：PCT/GB2012050716
申请日：2012-03-30
申请人： GAS2 LTD , BANISTER JAMES
发明人： BANISTER JAMES
IPC分类号： C01B3/36 , C10G2/00
CPC分类号： C10G2/32 , B01J12/007 , B01J19/2475 , B01J19/2485 , B01J19/249 , B01J2219/00078 , B01J2219/2408 , B01J2219/2411 , B01J2219/2423 , B01J2219/2428 , B01J2219/2438 , B01J2219/2453 , B01J2219/2459 , B01J2219/2462 , B01J2219/2475 , B01J2219/2479 , B01J2219/2485 , B01J2219/2487 , C01B3/386 , C01B2203/0261 , C01B2203/04 , C01B2203/0495 , C01B2203/062 , C01B2203/1035 , C01B2203/1064 , C01B2203/1241 , C01B2203/127 , C10G2300/1025 , C10G2400/02 , C10G2400/04
摘要： There is herein described a high pressure gas to liquid (GTL) process. More particularly, there is described a once through high pressure GTL process utilising a porous catalytic membrane reactor capable of being connected to a novel structured fixed bed reactor that incorporates forced flow through the porous catalytic structured catalyst in combination with high levels of heat transfer where there is no compression of syngas between reforming and Fischer-Tropsch steps.
摘要翻译：这里描述了高压气体到液体（GTL）过程。更具体地说，描述了一次通过高压GTL方法，该方法利用能够连接到新型结构化固定床反应器的多孔催化膜反应器，该反应器结合了强制流动通过多孔催化结构化催化剂和高水平传热在重整和费托步骤之间没有压缩合成气。

7. 发明申请

WO2012131385A2 HIGH PRESSURE GAS TO LIQUID PROCESS 审中-公开
标题翻译：高压气体到液体过程
公开(公告)号：WO2012131385A2
公开(公告)日：2012-10-04
申请号：PCT/GB2012/050716
申请日：2012-03-30
申请人： GAS2 LIMITED , BANISTER, James
发明人： BANISTER, James
IPC分类号： C01B3/36
CPC分类号： C10G2/32 , B01J12/007 , B01J19/2475 , B01J19/2485 , B01J19/249 , B01J2219/00078 , B01J2219/2408 , B01J2219/2411 , B01J2219/2423 , B01J2219/2428 , B01J2219/2438 , B01J2219/2453 , B01J2219/2459 , B01J2219/2462 , B01J2219/2475 , B01J2219/2479 , B01J2219/2485 , B01J2219/2487 , C01B3/386 , C01B2203/0261 , C01B2203/04 , C01B2203/0495 , C01B2203/062 , C01B2203/1035 , C01B2203/1064 , C01B2203/1241 , C01B2203/127 , C10G2300/1025 , C10G2400/02 , C10G2400/04
摘要： There is herein described a high pressure gas to liquid (GTL) process. More particularly, there is described a once through high pressure GTL process utilising a porous catalytic membrane reactor capable of being connected to a novel structured fixed bed reactor that incorporates forced flow through the porous catalytic structured catalyst in combination with high levels of heat transfer where there is no compression of syngas between reforming and Fischer-Tropsch steps.
摘要翻译：这里描述了高压气体到液体（GTL）过程。更具体地，描述了一次通过高压GTL方法，其利用能够连接到新型结构化固定床反应器的多孔催化膜反应器，其结合强度流过多孔催化结构化催化剂并结合高水平的热传递，在重整和费 - 托步骤之间没有压缩合成气。

8. 发明申请

WO2007096699A3 MULTIPLE REACTOR CHEMICAL PRODUCTION SYSTEM 审中-公开
标题翻译：多反应器化学生产系统
公开(公告)号：WO2007096699A3
公开(公告)日：2008-01-03
申请号：PCT/IB2006003279
申请日：2006-09-22
申请人： HEATRIC , BANISTER JAMES ANDREW , JOHNSTON ANTHONY MATTHEW , HAYNES BRIAN S
发明人： BANISTER JAMES ANDREW , JOHNSTON ANTHONY MATTHEW , HAYNES BRIAN S
IPC分类号： B01J8/04 , C07C29/151
CPC分类号： B01J8/0473 , B01D3/009 , B01J8/0442 , B01J8/0488 , B01J8/0496 , B01J19/006 , B01J2208/00176 , B01J2208/00212 , B01J2208/0053 , B01J2219/00006 , B01J2219/00038 , B01J2219/0004 , B01J2219/00096 , B01J2219/00159 , C07C29/152 , F28D9/00 , Y02P20/127 , Y02P20/582 , C07C31/04
摘要： The present invention is a multiple reaction set for the production of chemicals by equilibrium limited reactions utilizing plate-type or extended surface heat exchangers. The heat exchangers effectively cool the reaction products in order to condense the methanol contained within the reaction products for separation, and also to warm incoming feed reactants prior to entrance of the reactants into a reactor utilized for the production of methanol. The various reactors, heat exchangers, and separators can be formed as separated zones within the enclosed vessels, thereby eliminating the need for separately constructed reactors, heat exchangers, and separators. Multi-stream plate-type of extended surface heat exchangers can be utilized to allow efficient cooling and methanol separation. The multiple reaction set can also be used for the recovery of methanol from a waste or purge gas stream utilizing multiple reactors, multiple plate-type or extended surface heat exchangers and multiple separators as a substitute for or in conjunction with a conventional methanol synthesis loop.
摘要翻译：本发明是利用板式或扩展式表面热交换器的平衡限制反应生产化学品的多重反应装置。热交换器有效地冷却反应产物以冷凝反应产物中所含的甲醇以分离，并且在将反应物进入用于生产甲醇的反应器中之前，还能温热进料的反应物。各种反应器，热交换器和分离器可以形成为封闭容器内的隔离区域，从而不再需要单独构建的反应器，热交换器和分离器。可以使用多流板式延伸表面热交换器来实现有效的冷却和甲醇分离。多反应组合还可以用于利用多个反应器，多个板式或扩展的表面热交换器和多个分离器作为常规甲醇合成回路的替代或与常规甲醇合成回路结合从废物或吹扫气流中回收甲醇。

9. 发明申请

WO02096848A3 HYDROFORMYLATION PROCESS 审中-公开
标题翻译：氢化工艺
公开(公告)号：WO02096848A3
公开(公告)日：2003-02-20
申请号：PCT/GB0202510
申请日：2002-05-29
申请人： DAVY PROCESS TECHN LTD , BANISTER JAMES ANDREW , HARRISON GEORGE EDWIN
发明人： BANISTER JAMES ANDREW , HARRISON GEORGE EDWIN
IPC分类号： B01J31/24 , B01J31/40 , B01J38/00 , B01J38/04 , B01J38/12 , C07B61/00 , C07C45/50 , C07C47/02 , C07C45/79
CPC分类号： C07C45/50 , Y02P20/584 , C07C47/02
摘要： The present invention relates to a continuous hydroformylation process for the production of an aldehyde by hydroformylation of an olefin which comprises: providing a hydroformylation zone containing a charge of a liquid reaction medium having dissolved therein a rhodium hydroformylation catalyst comprising rhodium in combination with carbon monoxide and a ligand; supplying the olefin to the hydroformylation zone; maintaining temperature and pressure conditions in the hydroformylation zone conducive to hydroformylation of the olefin; recovering from the liquid hydroformylation medium a hydroformylation product comprising aldehyde; recovering from the hydroformylation zone a stream comprising the rhodium catalyst; contacting at least a portion of the stream with a solid acidic absorbent under process conditions which allow at least some of the rhodium to become bound to the absorbent; subjecting the rhodium bound to the absorbent, under process conditions which allow desorption of the metal, to a fluid stripping medium comprising hydrogen and solvent; recovering the rhodium hydride catalyst; and recycling the rhodium hydride catalyst to the hydroformylation zone.
摘要翻译：本发明涉及通过烯烃的加氢甲酰化生产醛的连续加氢甲酰化方法，该方法包括：提供含有液体反应介质的加氢甲酰化区，该液体反应介质溶解有铑加氢甲酰化催化剂，该催化剂包含铑与一氧化碳和配体; 将烯烃供应到加氢甲酰化区; 维持加氢甲酰化区中有利于烯烃加氢甲酰化的温度和压力条件; 从液体加氢甲酰化介质中回收含有醛的加氢甲酰化产物; 从加氢甲酰化区回收包含铑催化剂的物流; 在工艺条件下使至少一部分流与固体酸性吸收剂接触，使得至少一些铑与吸收剂结合; 在允许金属解吸的工艺条件下将结合到吸收剂上的铑经受包含氢气和溶剂的流体汽提介质; 回收氢化铑催化剂; 并将氢化铑催化剂再循环到加氢甲酰化区。

10. 发明申请

WO2013008020A1 ISOTHERMAL REACTOR FOR PARTIAL OXIDATION OF METHANE 审中-公开
标题翻译：甲烷部分氧化的同位素反应器
公开(公告)号：WO2013008020A1
公开(公告)日：2013-01-17
申请号：PCT/GB2012/051655
申请日：2012-07-12
申请人： GAS2 LIMITED , BANISTER, James
发明人： BANISTER, James
IPC分类号： C01B3/38 , B01J19/24
CPC分类号： C01B3/386 , B01J8/009 , B01J8/0214 , B01J8/0221 , B01J8/0278 , B01J8/0285 , B01J8/065 , B01J8/067 , B01J15/005 , B01J19/2475 , B01J2208/00132 , B01J2208/00176 , B01J2208/00221 , B01J2208/00309 , B01J2208/00495 , B01J2208/0053 , B01J2208/00902 , C01B2203/0233 , C01B2203/0261 , C01B2203/1035 , C01B2203/1047 , C01B2203/1241 , C01B2203/141 , C01B2203/142
摘要： There is herein described a process and apparatus for partial oxidation of hydrocarbons. More particularly, there is described a process and an isothermal reactor apparatus for the partial oxidation of methane which uses a heat transfer surface but does not utilize an ion-transport membrane for the transport of oxygen. [Figure 6]
摘要翻译：本文描述了烃的部分氧化的方法和装置。更具体地，描述了一种用于部分氧化甲烷的方法和等温反应器装置，其使用传热表面，但不利用离子迁移膜来输送氧气。 [图6]

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