公开(公告)号：WO2017117177A1

公开(公告)日：2017-07-06

申请号：PCT/US2016/068803

申请日：2016-12-28

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： HARANDI, Mohsen, N. ,  LEVIN, Doron ,  GUPTA, Himanshu ,  LATTNER, James, R. ,  WOOD, Glenn, C. ,  ALDOUS, Ketih, K. ,  HILBERT, Timothy, L. ,  CARROLL, Michael, B. ,  DANDEKAR, Ajit, B. ,  YOHE, Sara, L. ,  BROWN, Stephen, H. ,  OWENS, Tracie, L. ,  ROSS, April, D. ,  SENZER, Eric, B. ,  PYL, Steven

IPC: C10G67/04

CPC classification number: C10G67/049 ,  C01B3/48 ,  C01B2203/0283 ,  C01B2203/065 ,  C10G55/02 ,  C10G65/043 ,  C10G67/04 ,  C10G67/0418 ,  C10G67/0445 ,  C10G67/0454 ,  C10G67/0463 ,  C10G67/0481 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2300/301 ,  C10G2300/304 ,  C10G2400/10 ,  C10J3/82 ,  C10J2300/0906 ,  C10J2300/0913 ,  C10J2300/1618 ,  C10K1/004 ,  C10K3/04 ,  C10M101/02 ,  C10M2203/1006 ,  C10M2203/1085 ,  C10N2220/022 ,  C10N2220/023 ,  C10N2230/02

Abstract: Methods are provided for producing lubricant base stocks from deasphalted oils formed by sequential deasphalting. Tile deasphalted oil can be exposed a first deasphalting process using a first solvent that can provide a lower severity of deasphalting and a second deasphalting process using a second solvent that can provide a higher seventy of deasphalting. This can result in formation of at least a deasphalted oil and a resin fraction. The resin fraction can represent a fraction that traditionally would have been included as part of a deasphalter rock fraction.

Abstract translation: 提供了从连续脱沥青形成的脱沥青油生产润滑剂基础油的方法。 瓦片脱沥青油可以使用可提供较低苛化度脱沥青的第一种溶剂和使用可提供较高脱沥青度的第二种溶剂的第二种脱沥青工艺进行第一次脱沥青工艺。 这可以导致形成至少脱沥青油和树脂部分。 树脂部分可以代表传统上将作为脱沥青岩部分的一部分包括在内的部分。

公开(公告)号：WO2017117173A1

公开(公告)日：2017-07-06

申请号：PCT/US2016/068796

申请日：2016-12-28

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： HILBERT, Timothy, L. ,  CARROLL, Michael, B. ,  DANDEKAR, Ajit, B. ,  YOHE, Sara, L. ,  BROWN, Stephen, H. ,  OWENS, Tracie, L. ,  ROSS, April, D ,  SENZER, Eric, B. ,  PYL, Steven ,  PATHARE, Rugved, P. ,  YEH, Lisa, I-Ching ,  FINGLAND, Bradley, R. ,  ALDOUS, Keith, K. ,  KOVVALI, Anjaneya, S. ,  FRUCHEY, Kendall, S. ,  BAKER, Charles, L., Jr. ,  HENDERSON, Camden, N.

IPC: C10G67/04

CPC classification number: C10G67/049 ,  C01B3/48 ,  C01B2203/0283 ,  C01B2203/065 ,  C10G55/02 ,  C10G65/043 ,  C10G67/04 ,  C10G67/0418 ,  C10G67/0445 ,  C10G67/0454 ,  C10G67/0463 ,  C10G67/0481 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2300/301 ,  C10G2300/304 ,  C10G2400/10 ,  C10J3/82 ,  C10J2300/0906 ,  C10J2300/0913 ,  C10J2300/1618 ,  C10K1/004 ,  C10K3/04 ,  C10M101/02 ,  C10M2203/1006 ,  C10M2203/1085 ,  C10N2220/022 ,  C10N2220/023 ,  C10N2230/02

Abstract: Methods are provided for forming lubricant base stocks from feeds such as vacuum resid or other 510°C+ feeds. A feed can be deasphalted and then catalytically and/or solvent processed to form lubricant base stocks, including bright stocks. The catalytic processing can correspond to processing in at least two stages. The amount of conversion performed in each stage can be varied to produce bright stocks with various properties.

Abstract translation: 提供了从诸如减压渣油或其他510℃+进料的原料形成润滑剂基础原料的方法。 进料可以脱沥青，然后催化和/或溶剂处理形成润滑剂基础原料，包括亮料。 催化处理可以对应于至少两个阶段的处理。 在每个阶段执行的转换量可以变化，以产生具有各种属性的明亮的股票。

公开(公告)号：WO2015051439A1

公开(公告)日：2015-04-16

申请号：PCT/CA2013/050936

申请日：2013-12-06

Applicant: PLASCO ENERGY GROUP INC. ,  PLASCOENERGY IP HOLDINGS, S.L., BILBAO, SCHAFFHAUSEN BRANCH

Inventor： GOMAA, Islam ,  NUNNALLY, Thomas ,  TSANGARIS, Andreas ,  HAY, Graeme ,  SHEN, Zhiyuan

IPC: B01J19/08 ,  B01J6/00

CPC classification number: C10K3/005 ,  C10J2300/1618 ,  C10K3/006 ,  H05H1/2406 ,  H05H1/28 ,  H05H1/44 ,  H05H2001/4607 ,  H05H2001/481 ,  H05H2240/20 ,  H05H2245/121

Abstract: A method and apparatus is described for reformulating raw gas and/or reducing and/or converting the tar in a raw gas from a gasification reaction. More specifically, a gas reformulating system having a gas reformulating chamber, one or more sources of or means for generating non-equilibrium plasma, and optionally one or more oxygen source(s) inputs and control system is provided. Methods of reformulation and/or reducing the tar concentration in a raw gas from a gasification reaction that uses non-equilibrium plasma are also provided.

Abstract translation: 描述了用于重整原料气体和/或还原和/或转化来自气化反应的原料气体中的焦油的方法和装置。 更具体地，提供了一种具有气体重整室，一个或多个源或用于产生非平衡等离子体的装置以及可选地一个或多个氧源（多个）输入和控制系统的气体重整系统。 还提供了使用非平衡等离子体的气化反应重新制备和/或降低原料气中焦油浓度的方法。

公开(公告)号：WO2013016702A3

公开(公告)日：2013-05-02

申请号：PCT/US2012048714

申请日：2012-07-27

Applicant: RENTECH INC ,  JIANG WEIBIN ,  MCCOMISH BRUCE ,  BORUM BRYAN C ,  CARRYER BENJAMIN ,  IBSEN MARK ,  ROBERTSON MARK ,  ELROD ERIC ,  WEEKS SIM ,  WRIGHT HAROLD A

Inventor： JIANG WEIBIN ,  MCCOMISH BRUCE ,  BORUM BRYAN C ,  CARRYER BENJAMIN ,  IBSEN MARK ,  ROBERTSON MARK ,  ELROD ERIC ,  WEEKS SIM ,  WRIGHT HAROLD A

IPC: C10J3/48 ,  C07C1/04 ,  C10G2/00 ,  C10J3/72 ,  C10J3/84

CPC classification number: C10J3/466 ,  B01J19/00 ,  C01B3/583 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/062 ,  C10G2/332 ,  C10J3/485 ,  C10J3/56 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0923 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/12 ,  C10J2300/1618 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1659 ,  C10J2300/1671 ,  C10J2300/1807 ,  C10J2300/1823 ,  C10K3/00 ,  F02G3/00 ,  Y02E50/32 ,  Y02P20/129 ,  Y02P20/145

Abstract: A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.

公开(公告)号：WO2012063034A3

公开(公告)日：2012-09-27

申请号：PCT/GB2011052008

申请日：2011-10-17

Applicant: JOHNSON MATTHEY PLC ,  ABBOTT PETER EDWARD JAMES ,  MACLEOD NORMAN ,  WILSON GORDON EDWARD

Inventor： ABBOTT PETER EDWARD JAMES ,  MACLEOD NORMAN ,  WILSON GORDON EDWARD

IPC: C10K1/32 ,  C01B3/58

CPC classification number: C10L3/08 ,  B01D53/02 ,  B01D53/04 ,  B01D2253/104 ,  B01D2253/1122 ,  B01D2253/1124 ,  B01D2257/306 ,  B01J20/0237 ,  B01J20/0244 ,  B01J20/08 ,  B01J20/28004 ,  B01J20/28016 ,  B01J20/2803 ,  B01J20/3028 ,  C01B3/58 ,  C01B2203/042 ,  C01B2203/0445 ,  C01B2203/047 ,  C01B2203/0485 ,  C01B2203/0495 ,  C01B2203/061 ,  C10G2/32 ,  C10G2300/1011 ,  C10G2300/1022 ,  C10G2300/202 ,  C10J3/00 ,  C10J2300/093 ,  C10J2300/1618 ,  C10K1/20 ,  C10K1/32 ,  C10L2290/02 ,  C10L2290/04 ,  C10L2290/06 ,  C10L2290/08 ,  C10L2290/10 ,  C10L2290/542 ,  Y02P20/145 ,  Y02P30/20

Abstract: A process is described for reducing the thiophene content in a synthesis gas mixture, comprising the steps of (i) passing a synthesis gas mixture comprising hydrogen and carbon oxides and containing thiophene over a copper-containing sorbent disposed in a sorbent vessel at an inlet temperature in the range 200-280°C, (ii) withdrawing a thiophene depleted synthesis gas containing methanol from the sorbent vessel, and (iii) adjusting the temperature of the methanol-containing thiophene-depleted synthesis gas mixture. The resulting gas mixture may be used for production of chemicals, e.g. methanol production or for the Fischer-Tropsch synthesis of liquid hydrocarbons, for hydrogen production by using water gas shift, or for the production of synthetic natural gas.

Abstract translation: 描述了一种降低合成气混合物中噻吩含量的方法，包括以下步骤：（i）使含有氢和碳氧化物并含有噻吩的合成气混合物在设置在吸附剂容器中的含铜吸附剂上通入入口温度 在200-280℃的范围内，（ii）从吸附剂容器中取出含有甲醇的耗氧化噻吩合成气，和（iii）调节含甲醇的噻吩贫乏的合成气混合物的温度。 所得到的气体混合物可用于生产化学品，例如 甲醇生产或液体碳氢化合物的费 - 托合成，通过使用水煤气变换的氢气生产或合成天然气的生产。

公开(公告)号：WO2012093264A1

公开(公告)日：2012-07-12

申请号：PCT/GB2012/050020

申请日：2012-01-06

Applicant: ADVANCED PLASMA POWER LIMITED ,  CHAPMAN, Chris ,  STEIN, Rolf ,  BROOKS, Martin ,  MANUKIAN, Edward S. ,  CLARK, Robert M.

Inventor： CHAPMAN, Chris ,  STEIN, Rolf ,  BROOKS, Martin ,  MANUKIAN, Edward S. ,  CLARK, Robert M.

IPC: C10J3/18 ,  C10K1/12 ,  C10J3/16 ,  C10J3/12 ,  C01B3/52 ,  C01B3/56 ,  C10K3/00 ,  C10K1/00 ,  E21B43/16 ,  H01M8/06 ,  C10J3/46

CPC classification number: C01B3/02 ,  C01B3/12 ,  C01B3/52 ,  C01B3/56 ,  C01B32/40 ,  C01B32/50 ,  C01B2203/0283 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/066 ,  C01B2203/86 ,  C10J3/00 ,  C10J3/463 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0946 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1612 ,  C10J2300/1618 ,  C10J2300/1646 ,  C10K1/005 ,  C10K1/103 ,  C10K1/143 ,  C10K1/32 ,  C10K3/00 ,  C10K3/001 ,  C10K3/003 ,  C10K3/04 ,  E21B43/164 ,  H01M8/0612 ,  H01M8/0618 ,  H01M8/0662 ,  H01M8/0668 ,  H01M8/0687 ,  Y02P30/30 ,  Y02P70/56

Abstract: Gas Stream Production The present invention provides a method for the production of carbon dioxide and/or hydrogen gas streams, the method comprising: (i) thermally treating a feedstock material to produce a syngas comprising carbon monoxide and hydrogen and plasma-treating the syngas in a plasma treatment unit; (ii) reacting the plasma-treated syngas with water in a further treatment unit, whereby at least some of the carbon monoxide is converted into carbon dioxide; and (iii) recovering hydrogen and/or, separately, carbon dioxide from the syngas.

Abstract translation: 气流生产本发明提供了一种生产二氧化碳和/或氢气流的方法，所述方法包括：（i）热处理原料以产生包含一氧化碳和氢的合成气，并对 等离子体处理单元; （ii）在另外的处理单元中使等离子体处理的合成气与水反应，由此至少一些一氧化碳转化为二氧化碳; 和（iii）从合成气中回收氢气和/或分离地回收二氧化碳。

公开(公告)号：WO2012039749A1

公开(公告)日：2012-03-29

申请号：PCT/US2011/001611

申请日：2011-09-19

Applicant: JURANITCH, James Charles

Inventor： JURANITCH, James Charles

IPC: A62D3/19

CPC classification number: C10L3/003 ,  C10J3/18 ,  C10J2200/12 ,  C10J2300/0906 ,  C10J2300/0946 ,  C10J2300/0976 ,  C10J2300/0996 ,  C10J2300/1238 ,  C10J2300/1618 ,  C10J2300/1621 ,  C10J2300/165 ,  C10J2300/1653 ,  C10K1/06 ,  C10K3/06 ,  H02K99/10 ,  Y02E20/16 ,  Y02E20/18 ,  Y02P20/129

Abstract: A method and system for cost-effectively converting a feedstock using thermal plasma, or other styles of gassifiers, into an energy transfer system using a blended syngas. The feedstock is any organic material or fossil fuel to generate a syngas. The syngas is blended with any fuel of a higher thermal content (BTU) level, such as natural gas. The blended syngas high thermal content fuel can be used in any energy transfer device such as a boiler for simple cycle Rankine systems, an internal combustion engine generator, or a combined cycle turbine generator system. The quality of the high thermal content fuel is monitored using a thermal content monitoring feedback system and a quenching arrangement.

Abstract translation: 一种使用热等离子体或其他类型的放气器将原料成本有效地转化成使用混合合成气的能量转移系统的方法和系统。 原料是产生合成气的任何有机材料或化石燃料。 合成气与任何具有较高热容（BTU）水平的燃料混合，如天然气。 混合合成气高热含量燃料可用于任何能量转移装置，例如用于简单循环兰金系统的锅炉，内燃机发电机或联合循环涡轮发电机系统。 使用热含量监测反馈系统和淬火装置监测高热含量燃料的质量。

公开(公告)号：WO2010132551A2

公开(公告)日：2010-11-18

申请号：PCT/US2010034519

申请日：2010-05-12

Applicant: GREATPOINT ENERGY INC ,  SIRDESHPANDE AVINASH ,  ROBINSON EARL T

Inventor： SIRDESHPANDE AVINASH ,  ROBINSON EARL T

IPC: C10J3/00

CPC classification number: C10J3/86 ,  C01B3/16 ,  C01B3/501 ,  C01B3/506 ,  C01B3/52 ,  C01B3/56 ,  C01B3/586 ,  C01B32/50 ,  C01B2203/0415 ,  C01B2203/0445 ,  C01B2203/0465 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/0485 ,  C01B2203/86 ,  C10J3/00 ,  C10J2300/093 ,  C10J2300/0973 ,  C10J2300/0986 ,  C10J2300/1618 ,  C10J2300/1662 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10L3/08 ,  Y02P30/30

Abstract: The present invention relates to processes for preparing gaseous products, and in particular methane, via the hydromethanation of carbonaceous feedstocks in the presence of steam, carbon monoxide, hydrogen and a hydromethanation catalyst.

Abstract translation: 本发明涉及通过含水原料在蒸汽，一氧化碳，氢气和氢化甲烷化催化剂的存在下制备气体产物，特别是甲烷的方法。

公开(公告)号：WO2010077950A3

公开(公告)日：2010-09-23

申请号：PCT/US2009068263

申请日：2009-12-16

Applicant: TEXACO DEVELOPMENT CORP ,  BRYAN PAUL F ,  LIU YUNQUAN ,  KRAUSE CURTIS L

Inventor： BRYAN PAUL F ,  LIU YUNQUAN ,  KRAUSE CURTIS L

IPC: C10J3/00 ,  C10J1/213 ,  C10L3/10

CPC classification number: C10J3/721 ,  C10J3/00 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/1618 ,  C10J2300/1659 ,  C10K1/004 ,  C10K1/008 ,  C10K3/026 ,  C10K3/04 ,  Y02E20/18 ,  Y02P20/145 ,  Y02P20/146

Abstract: The present invention discloses a system for biomass treatment which addresses the need to find economical solutions to transport biomass. In the present invention, small, distributed gasifiers convert the biomass into synthesis gas ("syngas"). The syngas is then transported via a pipeline network to a central fuel production facility.

Abstract translation: 本发明公开了一种用于生物质处理的系统，其解决了寻找运输生物质的经济解决方案的需求。 在本发明中，小型分布式气化器将生物质转化成合成气（“合成气”）。 合成气然后通过管道网络运输到中央燃料生产设施。

公开(公告)号：WO2009124666A3

公开(公告)日：2010-04-01

申请号：PCT/EP2009002267

申请日：2009-03-27

Applicant: LINDE AG ,  INNOCENZI STEFANO ,  FREITAG CHRISTIAN

Inventor： INNOCENZI STEFANO ,  FREITAG CHRISTIAN

IPC: C10J3/84 ,  C10J3/86 ,  C10K1/02 ,  C10K3/04 ,  C10K3/06

CPC classification number: C10J3/00 ,  C01B3/12 ,  C01B3/506 ,  C01B3/52 ,  C01B2203/04 ,  C01B2203/0415 ,  C01B2203/0475 ,  C01B2203/0485 ,  C10J3/84 ,  C10J3/86 ,  C10J2300/094 ,  C10J2300/0943 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/0973 ,  C10J2300/1618 ,  C10J2300/1807 ,  C10J2300/1838 ,  C10J2300/1884 ,  C10K1/02 ,  C10K1/08 ,  C10K1/20

Abstract: The invention relates to a method and a device for obtaining hydrogen (19) and/or carbon monoxide (17) from coke (1), the coke (1) being converted by partial oxidation (V) at pressures of between 2 and 8 bar and temperatures of between 500 and 1,000 °C into a gas (waste gas) (20) containing carbon monoxide and carbon dioxide. An oxidant (2) consisting of water vapour (4) and/or oxygen (3) and carbon dioxide (5) is used to convert the coke (1).

Abstract translation: 本发明涉及从焦炭的方法和用于生产氢气（19）的装置和/或一氧化碳（17）（1），焦炭（1）通过在2-8巴的压力下的（V）部分氧化和在之间的温度下 含有一氧化碳和二氧化碳（气体）（20）的气体中被转换500和1000℃。 从水蒸汽（4）和/或氧气（3）和二氧化碳的焦炭（1）的实现，则使用（5）现有的氧化装置（2）。