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1.发明申请公开(公告)号：US20140134099A1
公开(公告)日：2014-05-15
申请号：US14076321
申请日：2013-11-11
Applicant: Phillips 66 Company
Inventor： Uchenna P. Paul , Bruce B. Randolph , Jon M. Nelson , Kristi A. Fjare , Danielle K. Smith , Mark Rumel Cragun , Richard D. Sadok
IPC: C01B3/32
CPC classification number: C01B3/323 , C01B2203/0233 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/1041 , C01B2203/1058 , C01B2203/1076 , C01B2203/1082 , C01B2203/1094 , C01B2203/1211 , C01B2203/1217 , C01B2203/1223 , C01B2203/1229
Abstract: A process is described for flowing an oxygenate feed over a catalyst in an adiabatic fixed bed reactor to product a reactor effluent and heat. The reaction inside the adiabatic fixed bed reactor occurs at a reaction temperature from about 200° C. to about 375° C. The reactor effluent is then condensed to separate the liquid products and the gaseous products. A separation step then separates the gaseous products into hydrogen and off-gas.
Abstract translation: 描述了一种将含氧化合物进料在绝热固定床反应器中的催化剂上流动以产生反应器流出物和热量的方法。 绝热固定床反应器中的反应在约200℃至约375℃的反应温度下进行。然后将反应器流出物冷凝以分离液体产物和气态产物。 然后分离步骤将气态产物分离成氢气和废气。
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公开(公告)号：US09862891B2
公开(公告)日：2018-01-09
申请号：US15433569
申请日：2017-02-15
Applicant: PHILLIPS 66 COMPANY
Inventor： Uchenna P. Paul , Jianhua Yao
CPC classification number: C10G3/49 , C10G2300/202 , C10G2300/305 , C10G2400/02 , C10L1/06 , C10L2200/0469 , C10L2270/023 , Y02P30/20
Abstract: The present invention relates to processes for converting a feedstream comprising predominantly light alcohols into liquid transportation fuels in the gasoline boiling range. In certain embodiments, the feedstream is a bio-waste stream derived from the conversion of sorbitol or glycerol to propanediol.
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公开(公告)号：US20170067169A1
公开(公告)日：2017-03-09
申请号：US15243281
申请日：2016-08-22
Applicant: PHILLIPS 66 COMPANY
Inventor： David B. Ingram , Bruce B. Randolph , Mitchell E. Loescher , Aalo K. Gupta , Uchenna P. Paul , Chris J. LaFrancois , Neal D. McDaniel , Danielle K. Smith , David M. Bierschenk , Ting He
CPC classification number: C25B3/02 , C25B9/08 , C25B11/0478 , C25B13/04 , C25B15/08
Abstract: The current embodiment describes a process of flowing an oxidant species over the reducing side of an oxygen transport membrane. O2− anions are then continuously transported from the reducing side through the oxygen transport membrane to the oxidizing side where an organic compound is converted to a partially oxidized organic compound on the oxidizing side.
Abstract translation: 目前的实施方案描述了使氧化剂物质在氧传输膜的还原侧上流动的过程。 然后，将阴离子从还原侧通过氧传输膜连续输送到氧化侧，在氧化侧将有机化合物转化为氧化侧的部分氧化的有机化合物。
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公开(公告)号：US09302250B2
公开(公告)日：2016-04-05
申请号：US14071077
申请日：2013-11-04
Applicant: PHILLIPS 66 COMPANY
Inventor： Jimmy A. Faria , Jon M. Nelson , Uchenna P. Paul , Danielle K. Smith
CPC classification number: B01J23/8946 , B01J21/04 , B01J23/755 , B01J23/78 , B01J23/892 , B01J23/894 , B01J35/1019 , B01J35/1061 , C01B3/326 , C01B2203/0283 , C01B2203/043 , Y02P20/145 , Y02P20/52
Abstract: A method of steam reforming where a reaction occurs in which an oxygenated feed contacts a catalyst to produce hydrogen. The catalyst of the reaction comprises a metal/metal promoter on a nickel/transition metal blend catalyst supported on a high-energy lattice metal oxide.
Abstract translation: 发生反应的蒸汽重整方法，其中含氧进料与催化剂接触以产生氢气。 反应的催化剂包含负载在高能晶格金属氧化物上的镍/过渡金属共混物催化剂上的金属/金属助催化剂。
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Patent Agency Ranking
公开(公告)号：US20140134098A1
公开(公告)日：2014-05-15
申请号：US14071077
申请日：2013-11-04
Applicant: Phillips 66 Company
Inventor： Jimmy A. Faria , Jon M. Nelson , Uchenna P. Paul , Danielle K. Smith
CPC classification number: B01J23/8946 , B01J21/04 , B01J23/755 , B01J23/78 , B01J23/892 , B01J23/894 , B01J35/1019 , B01J35/1061 , C01B3/326 , C01B2203/0283 , C01B2203/043 , Y02P20/145 , Y02P20/52
Abstract: A method of steam reforming where a reaction occurs in which an oxygenated feed contacts a catalyst to produce hydrogen. The catalyst of the reaction comprises a metal/metal promoter on a nickel/transition metal blend catalyst supported on a high-energy lattice metal oxide.
Abstract translation: 发生反应的蒸汽重整方法，其中含氧进料与催化剂接触以产生氢气。 反应的催化剂包含负载在高能晶格金属氧化物上的镍/过渡金属共混物催化剂上的金属/金属助催化剂。
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公开(公告)号：US20140110271A1
公开(公告)日：2014-04-24
申请号：US14047084
申请日：2013-10-07
Applicant: PHILLIPS 66 COMPANY
Inventor： Mahaprasad Kar , Sourabh Pansare , John T. Gorke , Edgar Lotero , Neal D. McDaniel , Danielle K. Smith , Dennis G. Schultz , Kristi A. Fjare , Bruce B. Randolph , Sikta Patnaik , Uchenna P. Paul , Madhu Anand
CPC classification number: C25B11/0415 , C25B1/02 , C25B11/0473
Abstract: The process describes performing electrolysis on an alkaline oxygenate mixture to produce hydrogen. In this process the electrolysis does not form any significant amounts of oxygen.
Abstract translation: 该方法描述了在碱性含氧化合物混合物上进行电解以产生氢。 在这个过程中，电解不会形成任何显着量的氧气。
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公开(公告)号：US20140076213A1
公开(公告)日：2014-03-20
申请号：US14021573
申请日：2013-09-09
Applicant: PHILLIPS 66 COMPANY
Inventor： David B. Ingram , Uchenna P. Paul
CPC classification number: F23L7/007 , B01D53/047 , B01D53/76 , B01D2256/16 , B01D2257/504 , C01B3/38 , C01B3/384 , C01B2203/0233 , C01B2203/0283 , C01B2203/043 , C01B2203/1241 , C25B1/00 , C25B1/04 , C25B15/08 , F23C9/00 , F23J2215/40 , F23J2215/50 , F23L7/005 , Y02E20/322 , Y02E20/344 , Y02E60/366 , Y02P20/152
Abstract: A process of producing a feed from a solid oxide electrolysis cell. A first portion of the flue gas produced from a combustion process is directed to the anode side of the solid oxide electrolysis cell. The feed and a second portion of the flue gas are then mixed to produce an enhanced feed. The enhanced feed is then mixed with fuel and combusted in the combustion process to produce flue gas. The flue gas comprises greater than 50 wt % CO2 and less than 1 wt % N2.
Abstract translation: 从固体氧化物电解槽生产原料的方法。 从燃烧过程产生的烟道气的第一部分被引导到固体氧化物电解池的阳极侧。 然后将进料和烟道气的第二部分混合以产生增强的进料。 然后将增强的进料与燃料混合并在燃烧过程中燃烧以产生烟道气。 烟气包括大于50重量％的CO 2和小于1重量％的N 2。
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公开(公告)号：US09664385B2
公开(公告)日：2017-05-30
申请号：US14021573
申请日：2013-09-09
Applicant: PHILLIPS 66 COMPANY
Inventor： David B. Ingram , Uchenna P. Paul
CPC classification number: F23L7/007 , B01D53/047 , B01D53/76 , B01D2256/16 , B01D2257/504 , C01B3/38 , C01B3/384 , C01B2203/0233 , C01B2203/0283 , C01B2203/043 , C01B2203/1241 , C25B1/00 , C25B1/04 , C25B15/08 , F23C9/00 , F23J2215/40 , F23J2215/50 , F23L7/005 , Y02E20/322 , Y02E20/344 , Y02E60/366 , Y02P20/152
Abstract: A process of producing a feed from a solid oxide electrolysis cell. A first portion of the flue gas produced from a combustion process is directed to the anode side of the solid oxide electrolysis cell. The feed and a second portion of the flue gas are then mixed to produce an enhanced feed. The enhanced feed is then mixed with fuel and combusted in the combustion process to produce flue gas. The flue gas comprises greater than 50 wt % CO2 and less than 1 wt % N2.
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9.发明授权Process scheme for catalytic production of renewable hydrogen from oxygenate feedstocks 有权从含氧化合物原料催化生产可再生氢的工艺方案公开(公告)号：US09452931B2
公开(公告)日：2016-09-27
申请号：US14076321
申请日：2013-11-11
Applicant: PHILLIPS 66 COMPANY
Inventor： Uchenna P. Paul , Bruce B. Randolph , Jon M. Nelson , Kristi A. Fjare , Danielle K. Smith , Mark Rumel Cragun , Richard D. Sadok
IPC: C01B3/32
CPC classification number: C01B3/323 , C01B2203/0233 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/1041 , C01B2203/1058 , C01B2203/1076 , C01B2203/1082 , C01B2203/1094 , C01B2203/1211 , C01B2203/1217 , C01B2203/1223 , C01B2203/1229
Abstract: A process is described for flowing an oxygenate feed over a catalyst in an adiabatic fixed bed reactor to product a reactor effluent and heat. The reaction inside the adiabatic fixed bed reactor occurs at a reaction temperature from about 200° C. to about 375° C. The reactor effluent is then condensed to separate the liquid products and the gaseous products. A separation step then separates the gaseous products into hydrogen and off-gas.
Abstract translation: 描述了一种将含氧化合物进料在绝热固定床反应器中的催化剂上流动以产生反应器流出物和热量的方法。 绝热固定床反应器中的反应在约200℃至约375℃的反应温度下进行。然后将反应器流出物冷凝以分离液体产物和气态产物。 然后分离步骤将气态产物分离成氢气和废气。
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