公开(公告)号：WO2009132449A1

公开(公告)日：2009-11-05

申请号：PCT/CA2009/000575

申请日：2009-04-27

Applicant: ENERKEM, INC. ,  CHORNET, Esteban ,  VALSECCHI, Boris ,  DROLET, Guillaume ,  GAGNON, Martin ,  NGUYEN, Betty

Inventor： CHORNET, Esteban ,  VALSECCHI, Boris ,  DROLET, Guillaume ,  GAGNON, Martin ,  NGUYEN, Betty

IPC: C10J3/54 ,  C10K1/08 ,  C10K1/20

CPC classification number: C10K3/023 ,  B01J23/866 ,  C01B3/38 ,  C01B3/52 ,  C01B3/56 ,  C01B2203/0244 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/0877 ,  C01B2203/147 ,  C10J3/463 ,  C10J3/482 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0946 ,  C10J2300/1612 ,  C10J2300/1621 ,  C10J2300/1659 ,  C10J2300/1861 ,  C10K1/002 ,  C10K1/004 ,  C10K1/005 ,  C10K1/007 ,  C10K1/06 ,  C10K1/08 ,  C10K1/101 ,  C10K1/102 ,  C10K1/12 ,  C10K1/143 ,  C10K1/165 ,  C10K1/32 ,  C10K3/006 ,  C10K3/02 ,  C10K3/04 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P20/52

Abstract: A method of producing end treating synthesis gas in which a biomass-rich material is gasified in a gasifier containing a fluidized bed at a temperature that does not exceed 750°C to produce a crude synthesis gas product. The crude synthesis gas then is quenched, scrubbed, and then subjected to at least one adsorption step to provide a clean synthesis gas. The clean synthesis gas then may be reformed catalytically to provide a synthesis gas with a dosired H 2 :CO ratio, and/or may be employed in the synthesis of desired chemicals.

Abstract translation: 一种生产富含生物质的材料在含有流化床的气化器中在不超过750℃的温度下气化以生产粗合成气产物的方法。 然后将粗合成气淬火，洗涤，然后进行至少一个吸附步骤以提供清洁的合成气。 然后可以将清洁的合成气催化重整以提供具有剂量的H 2 :CO比的合成气，和/或可用于合成所需化学品。

公开(公告)号：WO2008077233A1

公开(公告)日：2008-07-03

申请号：PCT/CA2007/002224

申请日：2007-12-10

Applicant: ENERKEM TECHNOLOGIES INC. ,  CHORNET, Esteban ,  MINCIC, Aca ,  GAGNON, Martin ,  VALSECCHI, Boris

Inventor： CHORNET, Esteban ,  MINCIC, Aca ,  GAGNON, Martin ,  VALSECCHI, Boris

IPC: C10J3/46 ,  B01D53/14 ,  B01D53/48 ,  B01D53/62 ,  C10C3/04 ,  C10J3/48

CPC classification number: C10L9/06 ,  C01B3/52 ,  C01B2203/0415 ,  C01B2203/0475 ,  C01B2203/0485 ,  C01B2203/0495 ,  C10J3/463 ,  C10J3/482 ,  C10J3/84 ,  C10J2300/0906 ,  C10J2300/0923 ,  C10J2300/094 ,  C10J2300/0943 ,  C10J2300/0956 ,  C10J2300/0983 ,  C10J2300/169 ,  C10J2300/1807 ,  C10J2300/1838 ,  C10K1/004 ,  C10K1/005 ,  C10K1/026 ,  C10K1/101 ,  Y02C20/20 ,  Y02E20/18

Abstract: A method for co-producing a sulfur-containing raw synthetic gas and an essentially desulfurized solid residue from a sulfur-containing heavy petroleum residue feedstock, comprising feeding a bubbling fluidized-bed gasification reactor with the feedstock, and converting the feedstock to a raw synthetic gas by a partial oxidation reaction in the presence of water at a temperature at or below about 1000 o C and a pressure at or below about 10 atm, thereby also producing an essentially desulfurized solid residue, while the sulfur components are essentially comprised in the raw synthetic gas; and separately recovering the essentially desulfurized solid residue and the sulfur-containing raw synthetic gas.

Abstract translation: 一种用于从含硫重质石油残渣原料共同生产含硫原始合成气体和基本上脱硫的固体残余物的方法，包括将起泡流化床气化反应器与原料进料，并将原料转化为原始合成 在约1000℃或低于约1000℃的温度和低于约10atm的压力下在水的存在下进行部分氧化反应的气体，从而也产生基本上脱硫的固体残余物，而硫 组分基本上包含在原始合成气中; 并单独回收基本上脱硫的固体残余物和含硫的原始合成气体。

公开(公告)号：WO2009105860A1

公开(公告)日：2009-09-03

申请号：PCT/CA2008/001676

申请日：2008-09-23

Applicant: ENERKEM, INC. ,  CHORNET, Esteban ,  VALSECCHI, Boris ,  AVILA, Yasmin ,  NGUYEN, Betty ,  LAVOIE, Jean-Michel

Inventor： CHORNET, Esteban ,  VALSECCHI, Boris ,  AVILA, Yasmin ,  NGUYEN, Betty ,  LAVOIE, Jean-Michel

IPC: C07C29/00 ,  C01B3/00 ,  C07C31/08 ,  C10J3/00

CPC classification number: C07C29/32 ,  C07C29/149 ,  C07C51/12 ,  C07C67/08 ,  C07C67/36 ,  Y02E60/324 ,  C07C31/08 ,  C07C53/08 ,  C07C69/14

Abstract: A process for converting methanol to ethanol which comprises reacting methanol and carbon monoxide in the presence of a catalyst to produce a product comprising at least 25 mole% methyl acetate and, in some instances, acetic acid. The acetic acid then is reacted with at least one alcohol to produce at least one acetate selected from methyl acetate, ethyl acetate, and butyl acetate. The at least one acetate (if produced) and the methyl acetate produced as a result of reacting methanol and carbon monoxide then are hydrogenated to produce ethanol. Syngas may be produced from biomass to produce all or a portion of the methanol, hydrogen, and carbon monoxide requirements for the process.

Abstract translation: 一种将甲醇转化为乙醇的方法，其包括使甲醇和一氧化碳在催化剂存在下反应，生成包含至少25摩尔％乙酸甲酯和在一些情况下为乙酸的产物。 然后将乙酸与至少一种醇反应以产生至少一种选自乙酸甲酯，乙酸乙酯和乙酸丁酯的乙酸酯。 由甲醇和一氧化碳反应生成的至少一种乙酸盐（如果生产的话）和乙酸甲酯被氢化生成乙醇。 合成气可以由生物质生产，以产生该方法的甲醇，氢气和一氧化碳的全部或一部分。

公开(公告)号：WO2010069068A8

公开(公告)日：2011-05-19

申请号：PCT/CA2009001851

申请日：2009-12-18

Applicant: ENERKEM INC ,  CHORNET ESTEBAN ,  VALSECCHI BORIS ,  RHEAULT SEBASTIEN ,  GAGNON MARTIN

Inventor： CHORNET ESTEBAN ,  VALSECCHI BORIS ,  RHEAULT SEBASTIEN ,  GAGNON MARTIN

IPC: C10J3/54

CPC classification number: C10J3/463 ,  C10J3/16 ,  C10J3/66 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0923 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/0996 ,  C10J2300/1603 ,  C10J2300/1615 ,  C10J2300/169 ,  C10J2300/1838 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/003 ,  C10K1/004 ,  C10K1/026 ,  C10K1/101 ,  C10K1/12 ,  C10K3/005 ,  C10K3/006 ,  Y02E50/32 ,  Y02P20/145

Abstract: A process for producing synthesis gas from biomass in which biomass is contacted with oxygen and steam, wherein the oxygen is present in an amount effective to oxidize the biomass partially and to heat the biomass to a temperature of at least 500°C and no greater than 750°C At least a portion of the partially oxidized biomass then is treated with oxygen and steam to heat the biomass to a temperature of at least 800°C, thereby producing a synthesis gas, which then is recovered

Abstract translation: 从生物质生产生物质与氧气和蒸汽接触的生产合成气的方法，其中氧以有效氧化生物质的方式部分地存在并将生物质加热至至少500℃且不大于 750℃将部分氧化的生物质的至少一部分用氧气和蒸汽处理以将生物质加热到至少800℃的温度，从而产生合成气，然后将其回收

公开(公告)号：WO2010069068A1

公开(公告)日：2010-06-24

申请号：PCT/CA2009/001851

申请日：2009-12-18

Applicant: ENERKEM, INC. ,  CHORNET, Esteban ,  VALSECCHI, Boris ,  RHEAULT, Sébastien ,  GAGNON, Martin

Inventor： CHORNET, Esteban ,  VALSECCHI, Boris ,  RHEAULT, Sébastien ,  GAGNON, Martin

IPC: C10J3/54

CPC classification number: C10J3/463 ,  C10J3/16 ,  C10J3/66 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0923 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/0996 ,  C10J2300/1603 ,  C10J2300/1615 ,  C10J2300/169 ,  C10J2300/1838 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/003 ,  C10K1/004 ,  C10K1/026 ,  C10K1/101 ,  C10K1/12 ,  C10K3/005 ,  C10K3/006 ,  Y02E50/32 ,  Y02P20/145

Abstract: A process for producing synthesis gas from biomass in which biomass is contacted with oxygen and steam, wherein the oxygen is present in an amount effective to oxidize the biomass partially and to heat the biomass to a temperature of at least 500°C and no greater than 750°C At least a portion of the partially oxidized biomass then is treated with oxygen and steam to heat the biomass to a temperature of at least 800°C, thereby producing a synthesis gas, which then is recovered

Abstract translation: 从生物质生产生物质与氧气和蒸汽接触的生产合成气的方法，其中氧以有效氧化生物质的方式部分地存在并将生物质加热至至少500℃且不大于 750℃将部分氧化的生物质的至少一部分用氧气和蒸汽处理以将生物质加热到至少800℃的温度，从而产生合成气，然后将其回收