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1. 发明申请

WO2017172545A1 THERMALLY CONTROLLED IGNITION DEVICE 审中-公开
标题翻译：热控点火装置
公开(公告)号：WO2017172545A1
公开(公告)日：2017-10-05
申请号：PCT/US2017/024197
申请日：2017-03-25
申请人： BELL, Peter, Michael
发明人： BELL, Peter, Michael
IPC分类号： B60H1/03
CPC分类号： F02P15/006 , F02P13/00 , F02P15/02 , F02P15/08 , F02P17/12 , F02P19/021 , F02P2017/121
摘要： Embodiments of the present technology relate to a temperature controllable and variable spark plug, and method of use. An example thermally controlled ignition device may comprise at least one sensor communicatively coupled to a control module for determining whether an engine characteristic is within a desired operating range and at least one heating element for adjusting the temperature of the ignition device.
摘要翻译：本技术的实施例涉及一种温度可控且可变的火花塞及其使用方法。示例热控点火装置可以包括至少一个传感器，其通信地耦合到控制模块，用于确定发动机特性是否在期望的运行范围内，以及至少一个加热元件，用于调节点火装置的温度。

2. 发明申请

WO2015042055A1 THERMAL DECOMPOSITION PROCESS FOR REDUCING AGGLOMERATE FORMATION 审中-公开
标题翻译：用于减少聚集体形成的热分解过程
公开(公告)号：WO2015042055A1
公开(公告)日：2015-03-26
申请号：PCT/US2014/055904
申请日：2014-09-16
申请人： INEOS BIO SA , OCFEMIA, Kim, Carlo, S. , BELL, Peter, Simpson
发明人： OCFEMIA, Kim, Carlo, S. , BELL, Peter, Simpson
IPC分类号： C10J3/00 , C10J3/72
CPC分类号： C01B3/02 , C10J3/00 , C10J3/002 , C10J3/723 , C10J2200/154 , C10J2300/0959 , Y02E50/32
摘要： A process provides for reducing agglomerate formation during thermal decomposition of a carbonaceous material feedstock. A non-catalytic thermal decomposition process includes providing generally solid feedstock to a thermal decomposition unit and moving the feedstock through at least one gasification zone in the thermal decomposition unit with a moving device. The process includes providing oxygen and optionally an additional gas to the gasification zone. In one aspect, the process includes moving feedstock through the gasification zone and providing oxygen to the gasification zone at rates effective for maintaining a material bed temperature not exceeding about 2300° F at any point in the material bed, and for maintaining a material bed temperature of about 500° F to about 2000° F.
摘要翻译：一种方法用于在碳质材料原料的热分解过程中减少附聚物形成。非催化热分解方法包括向热分解单元提供通常固体的原料，并通过移动装置使原料通过热分解单元中的至少一个气化区移动。该方法包括向气化区提供氧气和任选的另外的气体。在一个方面，该方法包括使原料通过气化区并向气化区提供氧，其速率有效地用于在材料床的任何点保持材料床温度不超过约2300°F，并且为了保持材料床温度约500°F至约2000°F

3. 发明申请

WO2014126940A3 A PROCESS FOR FERMENTING CO-CONTAINING GASEOUS SUBSTRATES 审中-公开
标题翻译：一种用于发生含有气相底物的方法
公开(公告)号：WO2014126940A3
公开(公告)日：2014-11-06
申请号：PCT/US2014015892
申请日：2014-02-11
申请人： INEOS BIO SA , BELL PETER SIMPSON , LIU SONG
发明人： BELL PETER SIMPSON , LIU SONG
IPC分类号： C12P7/06
CPC分类号： C12P7/06 , C12P3/00 , C12P7/065 , Y02E50/17
摘要： A process provides high ethanol productivity levels during fermentation of a CO-containing substrate. The process controls CO-substrate feed rates and cell density to avoid culture upset and CO inhibition. The process includes fermenting a CO-containing gaseous substrate to obtain a target cell density and a target CO feed rate, and then periodically reducing and increasing the CO feed rate.
摘要翻译：一种方法在含CO底物的发酵过程中提供高的乙醇生产率水平。该过程控制CO底物进料速率和细胞密度，以避免培养不适和CO抑制。该方法包括发酵含CO气体底物以获得目标细胞密度和目标CO进料速率，然后周期性地降低和提高CO进料速率。

4. 发明申请

WO2014126940A2 A PROCESS FOR FERMENTING CO-CONTAINING GASEOUS SUBSTRATES 审中-公开
标题翻译：一种引发含共聚物气相基质的方法
公开(公告)号：WO2014126940A2
公开(公告)日：2014-08-21
申请号：PCT/US2014/015892
申请日：2014-02-11
申请人： INEOS BIO SA , BELL, Peter Simpson , LIU, Song
发明人： BELL, Peter Simpson , LIU, Song
IPC分类号： C12P7/06
CPC分类号： C12P7/06 , C12P3/00 , C12P7/065 , Y02E50/17
摘要： A process provides high ethanol productivity levels during fermentation of a CO-containing substrate. The process controls CO-substrate feed rates and cell density to avoid culture upset and CO inhibition. The process includes fermenting a CO-containing gaseous substrate to obtain a target cell density and a target CO feed rate, and then periodically reducing and increasing the CO feed rate.
摘要翻译：一种方法在含CO底物的发酵过程中提供高乙醇生产率水平。该过程控制CO底物进料速率和细胞密度以避免培养物失调和CO抑制。该方法包括发酵含CO的气态底物以获得目标细胞密度和目标CO进料速率，然后周期性地减少和增加CO进料速率。

5. 发明申请

WO2012138766A2 SYSTEM FOR GENERATING POWER FROM A SYNGAS FERMENTATION PROCESS 审中-公开
标题翻译：从SYNGAS发酵过程中产生电能的系统
公开(公告)号：WO2012138766A2
公开(公告)日：2012-10-11
申请号：PCT/US2012032180
申请日：2012-04-04
申请人： INEOS BIO SA , BELL PETER S , OCFEMIA KIM , BERNSTEAD STEPHEN JOHN , PARKER GRAEME
发明人： BELL PETER S , OCFEMIA KIM , BERNSTEAD STEPHEN JOHN , PARKER GRAEME
IPC分类号： C10J3/86 , C01B3/00 , C12P7/06
CPC分类号： C10J3/84 , C01B2203/0877 , C01B2203/0894 , C01B2203/142 , C01B2203/143 , C10J3/72 , C10J3/721 , C10J3/723 , C10J3/726 , C10J3/86 , C10J2200/09 , C10J2200/15 , C10J2300/0956 , C10J2300/0959 , C10J2300/1606 , C10J2300/1846 , C10J2300/1884 , C10K1/02 , C10K1/04 , C10K3/003 , C10K3/005 , C10K3/008 , F22B1/1838 , Y02E50/17 , Y02E50/32 , Y02E50/343 , Y02E60/324 , Y02P20/124 , Y02P20/129 , Y02T10/16
摘要： A system and process is provided for generating power from a syngas fermentation process. The process includes contacting hot syngas having a temperature above about 1400F with cooled syngas to produce a pre-cooled syngas having a temperature of 1400F or less at an inlet of a waste heat boiler. A waste heat boiler receives the pre-cooled syngas and is effective for producing waste heat boiler high pressure steam and a cooled syngas.
摘要翻译：提供了从合成气发酵过程产生功率的系统和方法。该方法包括将温度高于约1400°F的热合成气与冷却的合成气接触，以在废热锅炉的入口处产生温度为1400°F或更低的预冷合成气。废热锅炉接收预冷合成气，对于生产废热锅炉高压蒸汽和冷却的合成气是有效的。

6. 发明申请

WO2014200817A1 CONTROL OF CONDUCTIVITY IN ANAEROBIC FERMENTATION 审中-公开
标题翻译：厌氧发酵中电导率的控制
公开(公告)号：WO2014200817A1
公开(公告)日：2014-12-18
申请号：PCT/US2014/041141
申请日：2014-06-05
申请人： INEOS BIO SA , SENARATNE, Ryan H. , BELL, Peter Simpson , LIU, Song , SCOTT, Syrona R.
发明人： SENARATNE, Ryan H. , BELL, Peter Simpson , LIU, Song , SCOTT, Syrona R.
IPC分类号： C12N1/20 , C12M1/34 , C12P7/06
CPC分类号： C12P7/065 , C12M41/00 , C12N1/20 , Y02E50/17
摘要： Process are provided which are effective for controlling medium conductivity during fermentation of a CO-containing gaseous substrate while providing an STY of about 10 g ethanol/(L•day) or more. The process includes balancing medium conductivity, specific carbon uptake or cell density levels.
摘要翻译：提供了在含CO气体底物的发酵期间有效控制中等电导率的方法，同时提供约10g乙醇/（L·天）或更高的STY。该过程包括平衡介质电导率，比碳吸收或细胞密度水平。

7. 发明申请

WO2014200810A1 A PROCESS FOR FERMENTING CO-CONTAINING GASEOUS SUBSTRATES IN A LOW PHOSPHATE MEDIUM EFFECTIVE FOR REDUCING WATER USAGE 审中-公开
标题翻译：一种用于在低磷酸盐介质中发生含CO气体基质的方法，用于减少水的使用
公开(公告)号：WO2014200810A1
公开(公告)日：2014-12-18
申请号：PCT/US2014/041115
申请日：2014-06-05
申请人： INEOS BIO SA , SENARATNE, Ryan H. , BELL, Peter Simpson , LIU, Song , SCOTT, Syrona R.
发明人： SENARATNE, Ryan H. , BELL, Peter Simpson , LIU, Song , SCOTT, Syrona R.
IPC分类号： C12P7/06 , C12P7/08 , C12P7/16 , C12N1/00
CPC分类号： C12P7/065 , C12N1/00 , C12N1/20 , C12P7/08 , C12P7/16 , Y02E50/10 , Y02E50/17
摘要： A process is provided for fermenting CO-containing gaseous substrates in a low phosphate medium. The process includes blending a liquid medium that includes at least one transition metal element with a liquid medium that includes at least at least one other transition metal element and one non-metal element to provide a fermentation medium. The process is effective for preventing precipitation of one or more transition metal elements with one or more non-metal elements. The fermentation medium used in the process is prepared in a way that requires significantly lower amounts of water and reduced levels of phosphate.
摘要翻译：提供了一种在低磷酸盐介质中发酵含CO气态底物的方法。该方法包括将包含至少一种过渡金属元素的液体介质与包含至少一种其它过渡金属元素和一种非金属元素的液体介质混合以提供发酵培养基。该方法对于防止一种或多种过渡金属元素与一种或多种非金属元素的沉淀是有效的。在该方法中使用的发酵培养基以需要显着更低量的水和降低磷酸盐水平的方式制备。

8. 发明申请

WO2013002949A1 PROCESS FOR FERMENTATION OF SYNGAS 审中-公开
标题翻译： SYNGAS发酵工艺
公开(公告)号：WO2013002949A1
公开(公告)日：2013-01-03
申请号：PCT/US2012/040327
申请日：2012-05-31
申请人： INEOS BIO SA , BELL, Peter Simpson , KO, Ching-Whan
发明人： BELL, Peter Simpson , KO, Ching-Whan
IPC分类号： C12N1/20
CPC分类号： C12M27/02 , B01F3/04262 , B01F7/00641 , B01F7/1675 , B01F7/18 , B01F2003/04326 , C12M21/04 , C12M21/12 , C12M29/04 , C12M29/06 , C12M29/08 , C12M29/18 , C12M29/26 , C12M47/02 , C12N1/20 , C12P7/06 , C12P7/065 , C12P7/54 , Y02E50/17 , Y02E50/343
摘要： A process for fermenting syngas is provided which is effective for decreasing an amount of time needed to inoculate a main reactor. The process includes propagating a culture of acetogenic bacteria to provide an incoulum for a main reactor and fermenting syngas in the main reactor.
摘要翻译：提供一种发酵合成气的方法，其有效减少接种主反应器所需的时间。该方法包括传播乙酰酵母细菌的培养物，以提供主反应器的入口和在主反应器中发酵合成气。

9. 发明申请

WO2009112335A1 PROCESS FOR THE PRODUCTION OF ETHANOL AND BUTANOL FROM BIOMASS 审中-公开
标题翻译：从生物量生产乙醇和丁醇的方法
公开(公告)号：WO2009112335A1
公开(公告)日：2009-09-17
申请号：PCT/EP2009/051966
申请日：2009-02-19
申请人： INEOS EUROPE LIMITED , BELL, Peter Simpson , BENSTEAD, Stephen John
发明人： BELL, Peter Simpson , BENSTEAD, Stephen John
IPC分类号： C12P7/14 , C12P7/16 , C12P7/06 , C12P7/08
CPC分类号： C12P7/14 , C12P7/065 , C12P7/08 , C12P7/16 , Y02E50/10 , Y02E50/17
摘要： The present invention relates to a process for the production of ethanol and butanol from biomass, and in particular to a process for the production of ethanol and butanol using two separate fermentation steps, said process comprising: a) passing a biomass feedstock to a first fermentation step, b) in said first fermentation step subjecting the biomass feedstock to anaerobic fermentation at a pH below 6.0 and at a temperature in the range 20 to 700°C and so as to convert the biomass to a product predominantly comprising acetic acid and butyric acid with at least a 2:1 ratio by weight of acetic acid to butyric acid, c) treating the product stream of step (b) to separate a solution comprising the acetic acid and butyric acid by: (i) separating a solution comprising the acetic acid and butyric acid from any residual solids and (ii) separating bacteria and/or pasteurising or sterilising the solution from the first fermentation step, and d) in a second fermentation step fermenting the solution comprising the acetic acid and butyric acid from step (c) to form ethanol and butanol.
摘要翻译：本发明涉及从生物质生产乙醇和丁醇的方法，特别涉及使用两个单独的发酵步骤生产乙醇和丁醇的方法，所述方法包括：a）将生物质原料送至第一次发酵步骤，b）在所述第一发酵步骤中，使生物质原料在pH低于6.0，温度范围为20至700℃的条件下进行厌氧发酵，以将生物质转化成主要包含乙酸和丁酸的产物其中乙酸与丁酸的重量比至少为2:1，c）处理步骤（b）的产物流以通过以下步骤分离包含乙酸和丁酸的溶液：（i）将包含乙酸来自任何残留固体的酸和丁酸和（ii）从第一发酵步骤分离细菌和/或将溶液灭菌或灭菌，以及d）在第二发酵步骤中发酵所述溶液包括来自步骤（c）的乙酸和丁酸以形成乙醇和丁醇。

10. 发明申请

WO2006061552A1 METHOD FOR THE CO-PRODUCTION OF OLEFINS AND GTL PRODUCTS 审中-公开
标题翻译：生产烯烃和GTL产品的方法
公开(公告)号：WO2006061552A1
公开(公告)日：2006-06-15
申请号：PCT/GB2005/004026
申请日：2005-10-18
申请人： INNOVENE EUROPE LIMITED , BELL, Peter, Simpson , BURNS, Andrew, Lindsey , GRIFFITHS, David, Charles , WOODFIN, William, Terence
发明人： BELL, Peter, Simpson , BURNS, Andrew, Lindsey , GRIFFITHS, David, Charles , WOODFIN, William, Terence
IPC分类号： C10G2/00 , C07C1/04 , C10G9/38
CPC分类号： C10G11/22 , C01B3/38 , C01B3/386 , C01B2203/0233 , C01B2203/0261 , C01B2203/0283 , C01B2203/0415 , C01B2203/046 , C01B2203/0475 , C01B2203/062 , C01B2203/1047 , C01B2203/1058 , C01B2203/1064 , C01B2203/107 , C01B2203/1088 , C01B2203/1094 , C01B2203/1241 , C01B2203/1247 , C01B2203/142 , C01B2203/84 , C07C4/025 , C07C11/02 , C07C2523/40 , C07C2523/74 , C10G2/32 , C10G2400/20 , Y02P30/40
摘要： The present invention provides a method for the co-production of product streams comprising hydrocarbons boiling in the diesel range and olefins, said method comprising: (a) providing a Gas-to-Liquids (GTL) process and an autothermal cracking (ATC) process, said GTL process comprising a reforming reactor and a Fischer-Tropsch (FT) reactor, (b) reforming a methane-containing feed stream in said reforming reactor to produce a first reactant stream comprising synthesis gas, (c) reacting the first reactant stream comprising synthesis gas in said FT reactor to produce a product stream comprising hydrocarbons, (d) treating the product stream comprising hydrocarbons to produce a first product stream comprising ethane and propane, and a second product stream comprising hydrocarbons boiling in the diesel range, (e) feeding the first product stream comprising ethane and propane to said autothermal cracking process, wherein said first product stream reacts with a molecular oxygencontaining gas in the presence of a catalyst to produce a product stream comprising olefins and synthesis gas, ( f ) treating the product stream comprising olefins and synthesis gas to separate a second reactant stream comprising synthesis gas and a product stream comprising olefins, and (g) feeding the second reactant stream comprising synthesis gas to the reformer of step (b) or to the Fischer-Tropsch reactor of step (c), wherein said autothermal cracking process shares one or more process facilities with the GTL process.
摘要翻译：本发明提供了一种用于共同生产包含在柴油范围内沸腾的烃和烯烃的产物流的方法，所述方法包括：（a）提供气 - 液（GTL）方法和自热裂解（ATC）方法所述GTL方法包括重整反应器和费 - 托（FT）反应器，（b）在所述重整反应器中重整含甲烷的进料流，以产生包含合成气的第一反应物流，（c）使第一反应物流包括在所述FT反应器中的合成气以产生包含烃的产物流，（d）处理包含烃的产物流以产生包含乙烷和丙烷的第一产物流和包含在柴油范围内沸腾的烃的第二产物流（e ）将包含乙烷和丙烷的第一产物流进料至所述自热裂解过程，其中所述第一产物流与含分子氧的气体在催化剂的存在下，产生包含烯烃和合成气的产物流，（f）处理包含烯烃和合成气的产物流，以分离包含合成气的第二反应物流和包含烯烃的产物流，和（g）所述第二反应物流包含合成气到步骤（b）的重整器或步骤（c）的费 - 托反应器，其中所述自热裂解过程与GTL方法共用一个或多个处理设备。

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