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151. 发明申请

US20110174687A1 PROCESS FOR TREATING A HYDROCARBON-CONTAINING FEED 有权
标题翻译：处理含油料饲料的方法
公开(公告)号：US20110174687A1
公开(公告)日：2011-07-21
申请号：US13010927
申请日：2011-01-21
申请人： Michael Anthony Reynolds , Stanley Nemec MILAM , Scott Lee Wellington
发明人： Michael Anthony Reynolds , Stanley Nemec MILAM , Scott Lee Wellington
IPC分类号： C10G49/22
CPC分类号： C10G47/26 , B01J27/04 , B01J27/047 , B01J27/051 , B01J35/002 , B01J35/023 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1061 , B01J37/031 , C01G19/006 , C01G39/006 , C01P2004/62 , C01P2006/12 , C01P2006/14 , C01P2006/16 , C10G47/02 , C10G47/06 , C10G2300/202 , C10G2300/206 , C10G2300/207 , C10G2300/301 , C10G2300/4006 , C10G2300/4012
摘要： A process for treating a hydrocarbon-containing feedstock is provided in which a hydrocarbon-containing feed comprising at least 20 wt. % of heavy hydrocarbons is mixed with hydrogen and at least one catalyst to produce a hydrocarbon-containing product. The hydrocarbon-containing feedstock, the catalyst(s), and the hydrogen are provided to a mixing zone and blended in the mixing zone at a temperature of from 375° C. to 500° C. A vapor comprised of hydrocarbons that are vaporizable at the temperature and pressure within the mixing zone is separated from the mixing zone, and, apart from the mixing zone, the vapor is condensed to produce a liquid hydrocarbon-containing product. The hydrocarbon-containing feedstock is continuously or intermittently provided to the mixing zone at a rate of at least 350 kg/hr per m3 of the mixture volume in the mixing zone.
摘要翻译：提供了一种处理含烃原料的方法，其中含烃进料包含至少20wt。％的重质烃与氢和至少一种催化剂混合以产生含烃产物。将含烃原料，催化剂和氢气提供到混合区并在混合区中在375℃至500℃的温度下共混。由烃组成的蒸汽可以在混合区内的温度和压力与混合区分离，并且除了混合区之外，蒸气冷凝以产生含液体烃的产物。将含烃原料以混合区中每立方米混合物体积至少350kg / hr的速率连续或间歇地提供给混合区。

152. 发明申请

US20110174686A1 PROCESS FOR TREATING A HYDROCARBON-CONTAINING FEED 失效
标题翻译：处理含油料饲料的方法
公开(公告)号：US20110174686A1
公开(公告)日：2011-07-21
申请号：US13010922
申请日：2011-01-21
申请人： Michael Anthony Reynolds , Stanley Nemec Milam , Scott Lee Wellington
发明人： Michael Anthony Reynolds , Stanley Nemec Milam , Scott Lee Wellington
IPC分类号： C10G49/22
CPC分类号： C10G47/02 , B01J27/04 , B01J27/047 , B01J27/051 , B01J27/0515 , B01J35/002 , B01J35/023 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1061 , B01J37/031 , C01G39/006 , C01G39/06 , C01G49/009 , C01G49/12 , C01G53/006 , C01G53/11 , C01P2004/51 , C01P2004/61 , C01P2004/62 , C01P2006/12 , C01P2006/16 , C01P2006/80 , C10G47/06 , C10G47/26 , C10G2300/202 , C10G2300/206 , C10G2300/207 , C10G2300/301 , C10G2300/4006 , C10G2300/4012
摘要： A process for treating a hydrocarbon-containing feed is provided in which a hydrocarbon-containing feed comprising at least 20 wt. % of heavy hydrocarbons is mixed with hydrogen and a catalyst to produce a hydrocarbon-containing product. The catalyst is prepared by mixing a first salt and a second salt in an aqueous mixture under anaerobic conditions at a temperature of from 15° C. to 150° C., where the first salt comprises a cationic component in any non-zero oxidation state selected from the group consisting of Cu, Fe, Ag, Co, Mn, Ru, La, Ce, Pr, Sm, Eu, Yb, Lu, Dy, Ni, Zn, Bi, Sn, Pb, and Sb, and where the second salt comprises an anionic component selected from the group consisting of MoS42−, WS42−, SnS44−, and SbS43.
摘要翻译：提供了一种处理含烃进料的方法，其中含烃进料包含至少20wt。将重质烃的重量与氢气和催化剂混合以产生含烃产物。催化剂通过在厌氧条件下在15℃至150℃的温度下在含水混合物中混合第一盐和第二盐来制备，其中第一盐包含任何非零氧化态的阳离子组分选自由Cu，Fe，Ag，Co，Mn，Ru，La，Ce，Pr，Sm，Eu，Yb，Lu，Dy，Ni，Zn，Bi，Sn，Pb和Sb组成的组，第二盐包含选自MoS42-，WS42-，SnS44-和SbS43的阴离子组分。

153. 发明申请

US20110174681A1 HYDROCARBON COMPOSITION 有权
标题翻译：碳氢化合物
公开(公告)号：US20110174681A1
公开(公告)日：2011-07-21
申请号：US13010919
申请日：2011-01-21
申请人： Stanley Nemec Milam , Michael Anthony Reynolds , Scott Lee Wellington
发明人： Stanley Nemec Milam , Michael Anthony Reynolds , Scott Lee Wellington
IPC分类号： C10L1/00
CPC分类号： C10L1/04 , C10G47/00 , C10G47/02 , C10G47/06 , C10G2300/301 , C10G2400/30
摘要： A hydrocarbon composition is provided containing:at least 5 wt. % of hydrocarbons having boiling point in the range from an initial boiling point of the composition up to 204° C.; at least 10 wt. % of hydrocarbons having a boiling point in the range from 204° C. up to 260° C.; at least 25 wt. % of hydrocarbons having a boiling point in the range from 260° C. up to 343° C.; at least 30 wt. % gram of hydrocarbons having a boiling point in the range from 343° C. to 538° C.; and at most 3 wt. % of hydrocarbons having a boiling point of greater than 538° C.; wherein the composition contains aromatic hydrocarbons including mono-aromatic hydrocarbons, di-aromatic hydrocarbons, and polyaromatic hydrocarbons, where the combined mono-aromatic hydrocarbon compounds and di-aromatic hydrocarbon compounds are present in a weight ratio relative to the polyaromatic hydrocarbon compounds of at least 1.5:1.0.
摘要翻译：提供一种烃组合物，其含有：至少5wt。沸点在该组合物的初始沸点至204℃范围内的烃的％。至少10重量％％的沸点在204℃至260℃的烃类; 至少25wt。％的沸点在260℃至343℃的烃类; 至少30wt。沸点在343℃至538℃的烃的％克。至多3wt。％的沸点高于538℃的烃; 其中所述组合物包含芳族烃，包括单芳族烃，二芳族烃和多芳族烃，其中组合的单芳族烃化合物和二芳族烃化合物以至少相对于多芳族烃化合物的重量比存在 1.5：1.0。

154. 发明申请

US20110111315A1 SYSTEMS AND PROCESSES OF OPERATING FUEL CELL SYSTEMS 失效
标题翻译：运行燃料电池系统的系统和工艺
公开(公告)号：US20110111315A1
公开(公告)日：2011-05-12
申请号：US12797538
申请日：2010-06-09
申请人： Jingyu CUI , Erik Edwin Engwall , John William Johnston , Mahendra Ladharam Joshi , Scott Lee Wellington
发明人： Jingyu CUI , Erik Edwin Engwall , John William Johnston , Mahendra Ladharam Joshi , Scott Lee Wellington
IPC分类号： H01M8/06
CPC分类号： H01M8/0618 , H01M8/0662 , H01M8/14 , H01M2008/147 , Y02E60/526
摘要： The present invention is directed to systems and processes for operating molten carbonate fuel cell systems. A process for operating the molten carbonate fuel cell includes providing a hydrogen-containing stream comprising molecular hydrogen to a molten carbonate fuel cell anode; heating a hydrocarbon stream, at least a majority of which is comprised of hydrocarbons that are liquid at 20° C. and atmospheric pressure, with a heat source comprising an anode exhaust from the molten carbonate fuel cell anode; contacting at least a portion of the heated hydrocarbon stream with a catalyst to produce a steam reforming feed comprising gaseous hydrocarbons, hydrogen, and at least one carbon oxide; separating at least a portion of the molecular hydrogen from the steam reforming feed; and providing at least a portion of the separated molecular hydrogen to the molten carbonate fuel cell anode as at least a portion of the stream comprising molecular hydrogen.
摘要翻译：本发明涉及用于操作熔融碳酸盐燃料电池系统的系统和方法。用于操作熔融碳酸盐燃料电池的方法包括向熔融碳酸盐燃料电池阳极提供包含分子氢的含氢流; 加热烃流，其至少大部分由在20℃和大气压下为液体的烃组成，热源包括来自熔融碳酸盐燃料电池阳极的阳极排气; 使至少一部分加热的烃流与催化剂接触以产生包含气态烃，氢和至少一种碳氧化物的蒸汽重整进料; 从蒸汽重整进料中分离至少一部分分子氢; 并且将至少一部分分离的分子氢提供给熔融碳酸盐燃料电池阳极，作为包含分子氢的物流的至少一部分。

155. 发明授权

US07879223B2 Systems and methods of producing a crude product 失效
标题翻译：生产粗产品的系统和方法
公开(公告)号：US07879223B2
公开(公告)日：2011-02-01
申请号：US11013826
申请日：2004-12-16
申请人： Scott Lee Wellington , Thomas Fairchild Brownscombe
发明人： Scott Lee Wellington , Thomas Fairchild Brownscombe
IPC分类号： C10G45/00 , C10G47/02
CPC分类号： C10G45/00 , C10G65/04 , C10L1/04 , Y02P20/142
摘要： Contact of a crude feed with a hydrogen source in the presence of an inorganic salt catalyst produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The inorganic salt catalyst may includes one or more alkali metal salts and/or one or more alkaline-earth metal salts. The crude product is a liquid mixture at 25° C. and 0.101 MPa. One or more properties of the crude product may be changed by at least 10% relative to the respective properties of the crude feed.
摘要翻译：在无机盐催化剂存在下，粗制原料与氢源的接触产生包括粗产物的总产物。原油原料每克原油原料的残留物含量至少为0.2克。无机盐催化剂可以包括一种或多种碱金属盐和/或一种或多种碱土金属盐。粗产物是在25℃和0.101MPa下的液体混合物。原油产品的一种或多种性质相对于原油原料的各自特性可以改变至少10％。

156. 发明申请

US20100280288A1 METHOD FOR RECOVERING A NATURAL GAS CONTAMINATED WITH HIGH LEVELS OF CO2 失效
标题翻译：用于回收以高二氧化碳浓度污染的天然气的方法
公开(公告)号：US20100280288A1
公开(公告)日：2010-11-04
申请号：US12652596
申请日：2010-01-05
申请人： Mahendra Ladharam Joshi , Jingyu Cui , Frederik Arnold Buhrman , Scott Lee Wellington , Stanley Nemec Milam , Rogier Maarten Kamerbeek
发明人： Mahendra Ladharam Joshi , Jingyu Cui , Frederik Arnold Buhrman , Scott Lee Wellington , Stanley Nemec Milam , Rogier Maarten Kamerbeek
IPC分类号： C07C29/04
CPC分类号： C10G5/04 , C07C29/1518 , C10G2300/1025 , C10G2300/807 , C07C31/04
摘要： The present invention provides a method for recovering a natural gas contaminated with high levels of carbon dioxide. A gas containing methane and carbon dioxide is extracted from a reservoir containing natural gas, where carbon dioxide comprises greater than 40 vol. % of the extracted gas. The extracted gas is scrubbed with a wash effective to produce a washed extracted gas containing less carbon dioxide than the extracted gas and at least 20 vol. % carbon dioxide. The washed extracted gas is oxidized with an oxygen containing gas in the presence of a partial oxidation catalyst to produce an oxidation product gas containing hydrogen, carbon monoxide, and carbon dioxide. The oxidation product gas is then utilized to produce a liquid methanol product.
摘要翻译：本发明提供一种回收被高浓度二氧化碳污染的天然气的方法。含有甲烷和二氧化碳的气体从含有天然气的储层中提取，其中二氧化碳包含大于40体积％％的提取气体。提取的气体用洗涤物洗涤，以产生比提取的气体少二氧化碳的洗涤的提取气体，并且至少20体积％。％二氧化碳。在部分氧化催化剂存在下，用含氧气体氧化洗涤后的萃取气体，生成含有氢，一氧化碳和二氧化碳的氧化产物气体。然后将氧化产物气体用于产生液体甲醇产物。

157. 发明授权

US07736490B2 Systems, methods, and catalysts for producing a crude product 有权
标题翻译：用于生产粗产品的系统，方法和催化剂
公开(公告)号：US07736490B2
公开(公告)日：2010-06-15
申请号：US11014363
申请日：2004-12-16
申请人： Opinder Kishan Bhan , Scott Lee Wellington
发明人： Opinder Kishan Bhan , Scott Lee Wellington
IPC分类号： C10G11/08
CPC分类号： C10G29/06 , C10G45/02 , C10G45/04 , C10G45/08 , C10G2300/107 , C10G2300/1074 , C10G2300/202 , C10G2300/203 , C10G2300/205 , C10G2300/301 , C10G2300/302 , C10G2300/308
摘要： Systems and methods for contacting a crude feed with one or more catalysts produces a total product that include a crude product are described. The crude product is a liquid mixture at 25° C. and 0.101 MPa. The one or more catalysts may include one or more vanadium catalysts. Methods and compositions of the one or more vanadium catalysts are described. One or more properties of the crude product may be changed by at least 10% relative to the respective properties of the crude feed. In some embodiments, hydrogen is generated.
摘要翻译：将原油原料与一种或多种催化剂接触的系统和方法产生包括粗产物的总产物。粗产物是在25℃和0.101MPa下的液体混合物。一种或多种催化剂可以包括一种或多种钒催化剂。描述一种或多种钒催化剂的方法和组成。原油产品的一种或多种性质相对于原油原料的各自特性可以改变至少10％。在一些实施方案中，产生氢。

158. 发明申请

US20100098602A1 SYSTEMS, METHODS, AND CATALYSTS FOR PRODUCING A CRUDE PRODUCT 审中-公开
标题翻译：用于生产原料产品的系统，方法和催化剂
公开(公告)号：US20100098602A1
公开(公告)日：2010-04-22
申请号：US12616555
申请日：2009-11-11
申请人： Opinder Kishan BHAN , Scott Lee Wellington
发明人： Opinder Kishan BHAN , Scott Lee Wellington
IPC分类号： B01J8/04
CPC分类号： C10G29/06 , C10G45/02 , C10G45/04 , C10G45/08 , C10G65/04 , C10G65/12 , C10G2300/107 , C10G2300/203
摘要： Methods and systems for contacting a crude feed that has a total acid number (TAN) of at least 0.3 with one or more catalysts produces a total product that includes a crude product are described. The one or more catalysts may include a first catalyst and a second catalyst. The crude product is a liquid mixture at 25° C. and 0.101 MPa and the crude product has a TAN of at most 90% of the TAN of the crude feed. One or more other properties of the crude product may be changed by at least 10% relative to the respective properties of the crude feed.
摘要翻译：将总酸值（TAN）至少为0.3的原油原料与一种或多种催化剂接触的方法和系统产生包括粗产物的总产物。一种或多种催化剂可以包括第一催化剂和第二催化剂。粗产物是在25℃和0.101MPa下的液体混合物，粗产物的TAN为原油原料的TAN的至多90％。原油产品的一种或多种其它性质可以相对于原油原料的各自特性改变至少10％。

159. 发明申请

US20090283444A1 SYSTEMS, METHODS, AND CATALYSTS FOR PRODUCING A CRUDE PRODUCT 审中-公开
标题翻译：用于生产原料产品的系统，方法和催化剂
公开(公告)号：US20090283444A1
公开(公告)日：2009-11-19
申请号：US12512595
申请日：2009-07-30
申请人： Opinder Kishan Bhan , Scott Lee Wellington
发明人： Opinder Kishan Bhan , Scott Lee Wellington
IPC分类号： C10G47/04 , C10G47/02
CPC分类号： C10G29/06 , C10G45/02 , C10G45/04 , C10G45/08 , C10G2300/107 , C10G2300/1074 , C10G2300/202 , C10G2300/203 , C10G2300/205 , C10G2300/301 , C10G2300/302 , C10G2300/308
摘要： Contact of a crude feed with one or more catalysts containing a Column 6 metal and having a pore size distribution having a median pore size diameter of at least 90 Å wherein at least 60% of the total number of pores in the pore size distribution have a pore diameter within about 45 Å of the median pore diameter produces a total product that includes a crude product. The crude feed includes organic oxygen containing compounds and has a TAN of at least 0.3. The crude product is a liquid mixture at 25 ° C. and 0.101 MPa and has a TAN of at most 90% of the TAN of the crude feed and an organic oxygen content of at most 90% of the organic oxygen content of the crude feed.
摘要翻译：原油原料与一种或多种含有第6列金属的催化剂的接触，其孔径分布具有至少90的中值孔径直径，其中孔径分布中孔的总数的至少60％具有孔径在中等孔径的约45Å内，产生包括粗产物的总产品。粗饲料包括含有机氧的化合物，并且具有至少0.3的TAN。粗产物是在25℃和0.101MPa下的液体混合物，并且具有至少原料原料的TAN的90％的TAN和原油原料的有机氧含量的至多90％的有机氧含量。

160. 发明申请

US20090155644A1 SYSTEM AND PROCESS FOR GENERATING ELECTRICAL POWER 审中-公开
标题翻译：电力系统及其制造方法
公开(公告)号：US20090155644A1
公开(公告)日：2009-06-18
申请号：US12335387
申请日：2008-12-15
申请人： Jingyu CUI , Erik Edwin Engwall , Mahendra Ladharam Joshi , Scott Lee Wellington
发明人： Jingyu CUI , Erik Edwin Engwall , Mahendra Ladharam Joshi , Scott Lee Wellington
IPC分类号： H01M8/04
CPC分类号： H01M8/0618 , C01B3/384 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0405 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0495 , C01B2203/06 , C01B2203/066 , C01B2203/0805 , C01B2203/0811 , C01B2203/1047 , C01B2203/1058 , C01B2203/142 , C01B2203/84 , H01M8/04097 , H01M8/04164 , H01M8/04462 , H01M8/04514 , H01M8/04746 , H01M8/04753 , H01M8/0631 , H01M8/0662 , H01M8/0687 , H01M2008/1293
摘要： The present invention relates to a process for generating electricity with a solid oxide fuel cell system. A liquid hydrocarbon feed is cracked in a first reaction zone, and fed as a gaseous feed to a second reaction zone. The feed is steam reformed in the second reaction zone to provide a reformed product gas containing hydrogen. Hydrogen is separated from the reformed product gas and is fed as a fuel to the anode of a solid oxide fuel cell. Electricity is generated in the fuel cell by oxidizing the hydrogen in the fuel. An anode exhaust stream containing hydrogen and steam is fed back into the first reaction zone to provide heat to drive the endothermic reactions in the first and second reaction zone, and to recycle unused hydrogen back to the fuel cell.
摘要翻译：本发明涉及一种用固体氧化物燃料电池系统发电的方法。液体烃进料在第一反应区中裂解，并作为气态进料进料至第二反应区。进料在第二反应区中进行蒸汽重整，以提供含有氢的重整产物气体。氢气与重整产物气体分离，并作为燃料供入固体氧化物燃料电池的阳极。通过氧化燃料中的氢，在燃料电池中产生电。含有氢气和蒸汽的阳极废气流被反馈到第一反应区以提供热量以驱动第一和第二反应区中的吸热反应，并将未使用的氢气再循环回燃料电池。

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