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公开(公告)号：US20100222620A1
公开(公告)日：2010-09-02
申请号：US12377388
申请日：2007-08-15
IPC分类号： C07C1/00
CPC分类号： C10G3/57 , C10G3/46 , C10G3/47 , C10G3/49 , C10G11/18 , C10G51/026 , C10G2300/1011 , C10G2300/1074 , C10G2300/4006 , C10G2300/805 , Y02E50/10 , Y02E50/30 , Y02P30/20
摘要： A process is disclosed for fluid catalytic cracking of oxygenated hydrocarbon compounds such as glycerol and bio-oil.In the process the oxygenated hydrocarbon compounds are contacted with a fluid cracking catalyst material for a period of less than 3 seconds.In a preferred process a crude-oil derived material, such as VGO, is also contacted with the catalyst.
摘要翻译： 公开了一种用于含氧化合物如甘油和生物油的流化催化裂化的方法。 在该过程中，氧化烃化合物与流体裂解催化剂材料接触少于3秒的时间。 在优选的方法中，原油衍生的材料，例如VGO，也与催化剂接触。
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2.发明授权Method to make alkanes and saturated polyhydroxy compounds from carbonyl compounds 有权从羰基化合物制备烷烃和饱和多羟基化合物的方法公开(公告)号：US07671246B2
公开(公告)日：2010-03-02
申请号：US11682021
申请日：2007-03-05
IPC分类号： C07C1/00
CPC分类号： C07C9/14 , B01J21/10 , B01J23/44 , C07D307/12
摘要： A catalytic process for converting biomass-derived carbohydrates to liquid alkanes, alkenes, and/or ethers is described. The process uses combinations of self- and crossed-aldol condensation reactions, dehydration reactions, and hydrogenation reactions, over specified metal-containing catalysts, to yield alkane, alkene, and ether products from carbohydrate reactants.
摘要翻译： 描述了将生物质衍生的碳水化合物转化为液体烷烃，烯烃和/或醚的催化方法。 该方法在特定的含金属催化剂上使用自交联和交叉醛醇缩合反应，脱水反应和氢化反应的组合，从碳水化合物反应物中得到烷烃，烯烃和醚产物。
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3.发明申请PROCESSING OF BIOMASS-DERIVED OXYGENATES WITH PARTICLES COMPRISING A COKE DEPOSIT 有权用含有沉淀物的颗粒加工生物质衍生的氧化剂公开(公告)号：US20130048915A1
公开(公告)日：2013-02-28
申请号：US13196543
申请日：2011-08-02
CPC分类号： C10G11/182 , C01B3/44 , C01B2203/0233 , C01B2203/0238 , C01B2203/1211 , C10G2300/1014 , C10G2300/708 , C10G2300/80 , C10G2300/807 , Y02P20/142 , Y02P20/145 , Y02P20/52 , Y02P30/20
摘要： A method is disclosed for producing a mixture of CO and H2 (syn-gas). The method comprises contacting particles containing a coke deposit with oxygenated molecules derived from biomass. In a preferred embodiment the particles are catalyst particles.The method may be carried out in the regenerator of a conventional fluid catalyst cracking (FCC) unit.
摘要翻译： 公开了一种用于生产CO和H 2（合成气）的混合物的方法。 该方法包括将含有焦炭沉积物的颗粒与衍生自生物质的氧化分子接触。 在优选的实施方案中，颗粒是催化剂颗粒。 该方法可以在常规流化催化剂裂化（FCC）单元的再生器中进行。
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公开(公告)号：US08129575B2
公开(公告)日：2012-03-06
申请号：US12377388
申请日：2007-08-15
IPC分类号： C07C1/00
摘要： A process is disclosed for fluid catalytic cracking of oxygenated hydrocarbon compounds such as glycerol and bio-oil.In the process the oxygenated hydrocarbon compounds are contacted with a fluid cracking catalyst material for a period of less than 3 seconds.In a preferred process a crude-oil derived material, such as VGO, is also contacted with the catalyst.
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5.发明授权Systems and processes for catalytic pyrolysis of biomass and hydrocarbonaceous materials for production of aromatics with optional olefin recycle, and catalysts having selected particle size for catalytic pyrolysis 有权用于生产具有可选烯烃循环的芳族化合物的生物质和烃类材料的催化热解的系统和方法，以及具有选择的催化裂解粒度的催化剂公开(公告)号：US09169442B2
公开(公告)日：2015-10-27
申请号：US13394559
申请日：2010-09-09
申请人： George W. Huber , Anne Mae Gaffney , Jungho Jae , Yu-Ting Cheng
发明人： George W. Huber , Anne Mae Gaffney , Jungho Jae , Yu-Ting Cheng
IPC分类号： C10G1/00 , C10G1/10 , C10B49/22 , C10B53/02 , C10B57/06 , C10G3/00 , C10G11/18 , C10G1/02 , B01J29/40 , B01J29/44 , B01J29/46 , B01J29/48 , B01J29/87
CPC分类号： C10G3/49 , B01J29/40 , B01J29/405 , B01J29/44 , B01J29/46 , B01J29/48 , B01J29/87 , C07C45/49 , C10B49/22 , C10B53/02 , C10B57/06 , C10G1/002 , C10G1/02 , C10G1/10 , C10G3/00 , C10G11/18 , C10G45/32 , C10G50/00 , C10G2300/1003 , C10G2300/1014 , C10G2300/4018 , C10G2300/4081 , C10G2300/70 , C10G2400/20 , C10G2400/30 , Y02E50/14 , Y02P20/52 , Y02P30/20 , Y02P30/42
摘要： This invention relates to compositions and methods for fluid hydrocarbon product, and more specifically, to compositions and methods for fluid hydrocarbon product via catalytic pyrolysis. Some embodiments relate to methods for the production of specific aromatic products (e.g., benzene, toluene, naphthalene, xylene, etc.) via catalytic pyrolysis. Some such methods may involve the use of a composition comprising a mixture of a solid hydrocarbonaceous material and a heterogeneous pyrolytic catalyst component. In some embodiments, an olefin compound may be co-fed to the reactor and/or separated from a product stream and recycled to the reactor to improve yield and/or selectivity of certain products. The methods described herein may also involve the use of specialized catalysts. For example, in some cases, zeolite catalysts may be used. In some instances, the catalysts are characterized by particle sizes in certain identified ranges that can lead to improve yield and/or selectivity of certain products.
摘要翻译： 本发明涉及流体烃产物的组合物和方法，更具体地说，涉及通过催化裂解的流化烃产物的组合物和方法。 一些实施方案涉及通过催化热解生产特定芳族产物（例如苯，甲苯，萘，二甲苯等）的方法。 一些这样的方法可以涉及使用包含固体烃类材料和非均相热解催化剂组分的混合物的组合物。 在一些实施方案中，烯烃化合物可以共同进料至反应器和/或从产物流中分离并再循环至反应器以提高某些产物的产率和/或选择性。 本文所述的方法还可以涉及使用专门的催化剂。 例如，在一些情况下，可以使用沸石催化剂。 在一些情况下，催化剂的特征在于可以导致某些产物的产率和/或选择性的某些确定范围内的粒度。
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6.发明授权Catalytic pyrolysis of solid biomass and related biofuels, aromatic, and olefin compounds 有权固体生物质和相关生物燃料，芳烃和烯烃化合物的催化裂解公开(公告)号：US08864984B2
公开(公告)日：2014-10-21
申请号：US13598703
申请日：2012-08-30
申请人： George W. Huber , Yu-Ting Cheng , Torren Carlson , Tushar Vispute , Jungho Jae , Geoff Tompsett
发明人： George W. Huber , Yu-Ting Cheng , Torren Carlson , Tushar Vispute , Jungho Jae , Geoff Tompsett
CPC分类号： C10G1/002 , C10G1/08 , C10G2300/1014 , C10G2300/1018 , C10G2300/305 , C10G2400/02 , C10G2400/20 , C10G2400/30 , Y02P30/42
摘要： This invention relates to compositions comprising fluid hydrocarbon products, and to methods for making fluid hydrocarbon products via catalytic pyrolysis. Some embodiments relate to methods for the production of specific aromatic products (e.g., benzene, toluene, naphthalene, xylene, etc.) via catalytic pyrolysis. Some such methods involve the use of a composition comprising a mixture of a solid hydrocarbonaceous material and a heterogeneous pyrolytic catalyst component. The methods described herein may also involve the use of specialized catalysts. For example, in some cases, zeolite catalysts may be used.
摘要翻译： 本发明涉及包含流体烃产物的组合物，以及通过催化热解制备流体烃产物的方法。 一些实施方案涉及通过催化热解生产特定芳族产物（例如苯，甲苯，萘，二甲苯等）的方法。 一些这样的方法涉及使用包含固体烃类材料和非均相热解催化剂组分的混合物的组合物。 本文所述的方法还可以涉及使用专门的催化剂。 例如，在一些情况下，可以使用沸石催化剂。
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7.发明授权Processing of biomass-derived oxygenates with particles comprising a coke deposit 有权用包含焦炭沉积物的颗粒处理生物质来源的含氧化合物公开(公告)号：US08501043B2
公开(公告)日：2013-08-06
申请号：US12373731
申请日：2007-07-13
CPC分类号： C10G11/182 , C01B3/44 , C01B2203/0233 , C01B2203/0238 , C01B2203/1211 , C10G2300/1014 , C10G2300/708 , C10G2300/80 , C10G2300/807 , Y02P20/142 , Y02P20/145 , Y02P20/52 , Y02P30/20
摘要： A method is disclosed for producing a mixture of CO and H2 (syn-gas). The method comprises contacting particles containing a coke deposit with oxygenated molecules derived from biomass. In a preferred embodiment the particles are catalyst particles. The method may be carried out in the regenerator of a conventional fluid catalytic cracking (FCC) unit.
摘要翻译： 公开了一种用于生产CO和H 2（合成气）的混合物的方法。 该方法包括将含有焦炭沉积物的颗粒与衍生自生物质的氧化分子接触。 在优选的实施方案中，颗粒是催化剂颗粒。 该方法可以在常规流化催化裂化（FCC）单元的再生器中进行。
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公开(公告)号：US20120198756A1
公开(公告)日：2012-08-09
申请号：US13196489
申请日：2011-08-02
CPC分类号： C10G3/57 , C10G3/46 , C10G3/47 , C10G3/49 , C10G11/18 , C10G51/026 , C10G2300/1011 , C10G2300/1074 , C10G2300/4006 , C10G2300/805 , Y02E50/10 , Y02E50/30 , Y02P30/20
摘要： A process is disclosed for fluid catalytic cracking of oxygenated hydrocarbon compounds such as glycerol and bio-oil.In the process the oxygenated hydrocarbon compounds are contacted with a fluid cracking catalyst material for a period of less than 3 seconds. In a preferred process a crude-oil derived material, such as VGO, is also contacted with the catalyst.
摘要翻译： 公开了一种用于含氧化合物如甘油和生物油的流化催化裂化的方法。 在该过程中，氧化烃化合物与流体裂解催化剂材料接触少于3秒的时间。 在优选的方法中，原油衍生的材料，例如VGO，也与催化剂接触。
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9.发明申请PROCESSING OF BIOMASS-DERIVED OXYGENATES WITH PARTICLES COMPRISING A COKE DEPOSIT 有权用含有沉淀物的颗粒加工生物质衍生的氧化剂公开(公告)号：US20100051874A1
公开(公告)日：2010-03-04
申请号：US12373731
申请日：2007-07-13
IPC分类号： C01B3/02
CPC分类号： C10G11/182 , C01B3/44 , C01B2203/0233 , C01B2203/0238 , C01B2203/1211 , C10G2300/1014 , C10G2300/708 , C10G2300/80 , C10G2300/807 , Y02P20/142 , Y02P20/145 , Y02P20/52 , Y02P30/20
摘要： A method is disclosed for producing a mixture of CO and H2 (syn-gas). The method comprises contacting particles containing a coke deposit with oxygenated molecules derived from biomass. In a preferred embodiment the particles are catalyst particles. The method may be carried out in the regenerator of a conventional fluid catalytic cracking (FCC) unit.
摘要翻译： 公开了一种用于生产CO和H 2（合成气）的混合物的方法。 该方法包括将含有焦炭沉积物的颗粒与衍生自生物质的氧化分子接触。 在优选的实施方案中，颗粒是催化剂颗粒。 该方法可以在常规流化催化裂化（FCC）单元的再生器中进行。
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公开(公告)号：US08524960B2
公开(公告)日：2013-09-03
申请号：US13196489
申请日：2011-08-02
IPC分类号： C10L1/00
CPC分类号： C10G3/57 , C10G3/46 , C10G3/47 , C10G3/49 , C10G11/18 , C10G51/026 , C10G2300/1011 , C10G2300/1074 , C10G2300/4006 , C10G2300/805 , Y02E50/10 , Y02E50/30 , Y02P30/20
摘要： A process is disclosed for fluid catalytic cracking of oxygenated hydrocarbon compounds such as glycerol and bio-oil.In the process the oxygenated hydrocarbon compounds are contacted with a fluid cracking catalyst material for a period of less than 3 seconds.In a preferred process a crude-oil derived material, such as VGO, is also contacted with the catalyst.
摘要翻译： 公开了一种用于含氧化合物如甘油和生物油的流化催化裂化的方法。 在该过程中，氧化烃化合物与流体裂解催化剂材料接触少于3秒的时间。 在优选的方法中，原油衍生的材料，例如VGO，也与催化剂接触。
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