公开(公告)号：US20130098243A1

公开(公告)日：2013-04-25

申请号：US13807136

申请日：2011-05-17

Applicant: Pablo Beato ,  Poul Erik Højlund Nielsen

Inventor： Pablo Beato ,  Poul Erik Højlund Nielsen

IPC: B01J20/08 ,  B01D53/14

CPC classification number: B01J20/08 ,  B01D53/02 ,  B01D53/14 ,  B01D53/64 ,  B01D2253/1124 ,  B01D2255/20761 ,  B01D2255/2092 ,  B01D2255/405 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2257/60 ,  B01J20/0237 ,  B01J20/06 ,  B01J20/3078 ,  B01J21/04 ,  B01J23/005 ,  B01J23/72 ,  B01J37/0045 ,  B01J37/031 ,  B01J37/08 ,  B01J37/18

Abstract: Method of removing metal carbonyls from a gaseous stream comprising contacting the metal carbonyl containing gaseous stream at elevated temperature with a particulate sorbent comprising modified copper aluminum spinel, wherein the copper aluminium spinel has been modified by a thermal treatment in a reducing atmosphere and a particulate sorbent for use in a method comprising a copper aluminium spinel being modified by thermal treatment in a reducing atmosphere at a temperature of between 250 and 500° C.

Abstract translation: 从气流中除去金属羰基化物的方法，包括使升高的温度下含有金属羰基的气流与包含改性铜铝尖晶石的颗粒吸附剂接触，其中铜铝尖晶石已经通过在还原气氛中的热处理和颗粒吸附剂 用于包括铜铝尖晶石的方法，其通过在还原气氛中在250-500℃的温度下进行热处理而被改性。

公开(公告)号：US20130082211A1

公开(公告)日：2013-04-04

申请号：US13701488

申请日：2011-05-13

Applicant: Kim Aasberg-Petersen ,  Poul Erik Højlund Nielsen ,  Peter Seier Christensen ,  Charlotte Stub Nielsen ,  Burcin Temel

Inventor： Kim Aasberg-Petersen ,  Poul Erik Højlund Nielsen ,  Peter Seier Christensen ,  Charlotte Stub Nielsen ,  Burcin Temel

IPC: C01B3/48

CPC classification number: C01B3/48 ,  C01B3/16 ,  C01B3/36 ,  C01B3/382 ,  C01B3/386 ,  C01B2203/0244 ,  C01B2203/0255 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/062 ,  C01B2203/1264 ,  C10G2/32 ,  C10G2300/1022 ,  C10G2300/807 ,  C10G2400/02

Abstract: Process for the preparation of synthesis gas from an essentially dry hydrocarbon feedstock (1) comprising olefins, hydrogen and carbon monoxide, the process comprising the steps: (a) selectively hydrogenating the olefins in the hydrocarbon feedstock at a temperature between 60 to 190° C. (2) to obtain a hydrogenated hydrocarbon feedstock comprising hydrogen, carbon monoxide and saturated hydrocarbons (3; (b) adding steam (4) to the hydrogenated hydrocarbon feedstock; (c) performing a water gas shift reaction in the presence of steam on the hydrogenated hydrocarbon feedstock (6) to obtain a shifted, hydrogenated hydrocarbon mixture; (d) converting the shifted, hydrogenated hydrocarbon mixture (8) to obtain a synthesis gas.

Abstract translation: 用于从包含烯烃，氢气和一氧化碳的基本上干的烃原料（1）制备合成气的方法，该方法包括以下步骤：（a）在60至190℃的温度下选择性氢化烃原料中的烯烃 （2）获得包含氢气，一氧化碳和饱和烃的氢化烃原料（3;（b）向氢化烃原料中加入蒸汽（4）;（c）在蒸汽存在下进行水煤气变换反应 氢化烃原料（6）以获得偏移的氢化烃混合物;（d）转化转移的氢化烃混合物（8）以获得合成气。

公开(公告)号：US08404156B2

公开(公告)日：2013-03-26

申请号：US13000578

申请日：2009-06-15

Applicant: Niels Christian Schiødt

Inventor： Niels Christian Schiødt

IPC: C01B3/38 ,  C01B3/24

CPC classification number: C01B3/48 ,  B01J23/002 ,  B01J23/005 ,  B01J23/06 ,  B01J23/10 ,  B01J23/80 ,  B01J37/0201 ,  B01J37/03 ,  B01J2523/00 ,  C01B3/16 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/041 ,  C01B2203/1076 ,  C01B2203/1094 ,  Y02P20/52 ,  B01J2523/17 ,  B01J2523/27 ,  B01J2523/31 ,  B01J2523/13

Abstract: Process for enriching a synthesis gas in hydrogen by conversion of carbon monoxide and steam over a catalyst containing oxides of zinc and aluminum together with one or more promoters.

Abstract translation: 通过一氧化碳和蒸汽在含有锌和铝的氧化物的催化剂以及一种或多种助催化剂的转化中富集氢气中的合成气的方法。

公开(公告)号：US20130000181A1

公开(公告)日：2013-01-03

申请号：US13634504

申请日：2011-03-02

Applicant: Ton V. W. Janssens ,  Pär L.T. Gabrielsson ,  Christophe Duwig ,  Svend-Erik Mikkelsen

Inventor： Ton V. W. Janssens ,  Pär L.T. Gabrielsson ,  Christophe Duwig ,  Svend-Erik Mikkelsen

IPC: C10L1/185 ,  C10L1/12 ,  C10L1/32 ,  C10L1/182

CPC classification number: F02B51/02 ,  C10G2300/1011 ,  C10L1/02 ,  C10L1/026 ,  F02M27/02 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T10/126

Abstract: A compression ignition fuel composition comprising diethyl ether (DEE) and water, in amounts that correspond to the reaction product of dehydration of anhydrous or hydrous ethanol (EtOH) with water content between 0 and 30 wt %, and further characterized by: a) a diethyl ether content in wt % that is larger than or equal to 50, and a water content in wt % that is lower than or equal to 50 minus concentration of ethanol in wt % for mixtures containing 0 to 20 wt % ethanol; or b) a diethyl ether content in wt % that is larger than or equal to 54 minus 0.2 times the ethanol concentration in wt %, and a water content in wt % that is lower than or equal to 46 minus the 0.8 times concentration of ethanol in wt % for mixtures containing 20 to 30 wt % ethanol; or c) a diethyl ether content in wt % that is larger than or equal to 61.5 minus 0.45 times the ethanol concentration in wt %, and a water content in wt % that is lower than or equal to 38.5 minus the 0.55 times concentration of ethanol in wt % for mixtures containing 30 to 70 wt % ethanol.

Abstract translation: 一种压缩点火燃料组合物，其包含二乙醚（DEE）和水，其量对应于无水或含水乙醇（EtOH）的脱水反应产物，水含量为0至30重量％，其特征还在于a）a 以重量％计的乙醚含量大于或等于50，低于或等于50％的水含量，减去含有0-20％（重量）乙醇的混合物的乙醇浓度（wt％）; 或b）以重量％计的乙醚含量，其重量百分比大于或等于54减去乙醇浓度的0.2重量％，水分含量低于或等于46，减去0.8倍乙醇浓度 对于含有20至30重量％乙醇的混合物; 或c）以重量％计的乙醚含量，其重量百分比大于或等于61.5减去0.45重量％的乙醇浓度，并且以wt％计的水含量低于或等于38.5减去乙醇浓度的0.55倍 对于含有30至70重量％乙醇的混合物，其重量％为重量％。

公开(公告)号：US08303923B2

公开(公告)日：2012-11-06

申请号：US12626222

申请日：2009-11-25

Applicant: Pat A. Han

Inventor： Pat A. Han

IPC: C01C1/04 ,  C07C27/00

CPC classification number: C01C1/0405 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/061 ,  C01B2203/068 ,  C01B2203/1241 ,  C01C1/0488 ,  C07C29/1518 ,  Y02P20/52 ,  C07C31/04

Abstract: Process for the co-production of methanol and ammonia from a hydrocarbon feed without venting to the atmosphere carbon dioxide captured from the methanol or ammonia synthesis gas and without using expensive air separation units, water gas shift and carbon dioxide removal steps.

Abstract translation: 用于从烃进料共同生产甲醇和氨的方法，而不排放到从甲醇或氨合成气中捕获的大气中的二氧化碳，并且不使用昂贵的空气分离单元，水煤气变换和二氧化碳去除步骤。

公开(公告)号：US08261700B2

公开(公告)日：2012-09-11

申请号：US13000786

申请日：2009-06-17

Applicant: Henrik Otto Stahl ,  Pat A. Han

Inventor： Henrik Otto Stahl ,  Pat A. Han

IPC: F22G3/00

CPC classification number: C01C1/0405 ,  C01B3/025 ,  C01B3/382 ,  C01B3/384 ,  C01B3/48 ,  C01B3/52 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0283 ,  C01B2203/0415 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/068 ,  C01B2203/0811 ,  C01B2203/0844 ,  C01B2203/0894 ,  C01B2203/1241 ,  C01B2203/1258 ,  C01B2203/141 ,  C01C1/0452 ,  C01C1/0488 ,  F22B1/1838 ,  F28D7/0075 ,  F28D7/06 ,  F28F9/26 ,  Y02P20/129 ,  Y02P20/52

Abstract: Process for the production of ammonia from a hydrocarbon feedstock all steam produced in the waste heat boilers of the reforming and ammonia section of the plant is superheated in one or more steam superheaters located downstream the ammonia converter in the ammonia section of the plant. There is no need for steam superheater (s) in the reforming section of the plant to cool the synthesis gas. A steam superheater for use in the process is also provided. The superheater comprises two compartments in which the first and second compartments are connected in series with respect to the steam flow and in parallel with respect to the process gas flow.

Abstract translation: 用于从烃原料生产氨的方法在设备的氨部分中的氨转化器下游的一个或多个蒸汽过热器中过热在废气热锅炉中产生的所有蒸汽的重整和氨段的蒸汽过热。 在工厂的重整部分不需要蒸汽过热器来冷却合成气。 还提供了用于该过程的蒸汽过热器。 过热器包括两个室，其中第一和第二隔室相对于蒸汽流串联连接并且相对于处理气体流平行连接。

公开(公告)号：US08202413B2

公开(公告)日：2012-06-19

申请号：US12209499

申请日：2008-09-12

Applicant: Finn Joensen ,  Bodil Voss ,  Niels Christian Schiødt

Inventor： Finn Joensen ,  Bodil Voss ,  Niels Christian Schiødt

IPC: C10G35/04 ,  C07C1/06

CPC classification number: C10G3/49 ,  C10G2300/4081 ,  C10G2400/02 ,  Y02P30/20

Abstract: A process for the preparation of hydrocarbon products including the steps of (a) providing a stream containing oxygenates; (b) mixing the stream with a recycle stream to form a gasoline feed stream; (c) contacting the gasoline feed stream with one or more gasoline synthesis catalysts to obtain an effluent stream with higher hydrocarbons boiling in the gasoline range; (d) withdrawing from step (c) the effluent stream; and (e) splitting a part of the effluent stream to form the recycle stream which is optionally further reduced in content of water or enriched in hydrogen, then pressurized and recycled to step (b).

Abstract translation: 一种制备烃产物的方法，包括以下步骤：（a）提供含有氧化物的料流; （b）将料流与再循环料流混合以形成汽油进料流; （c）使汽油进料流与一种或多种汽油合成催化剂接触以获得在汽油范围内沸腾的高级烃的流出物流; （d）从步骤（c）退出流出物流; 和（e）分离一部分流出物流以形成循环物流，其任选地进一步减少水的含量或富含氢气，然后加压并再循环至步骤（b）。

公开(公告)号：US08119099B2

公开(公告)日：2012-02-21

申请号：US12957496

申请日：2010-12-01

Applicant: Niels Christian Schiødt

Inventor： Niels Christian Schiødt

IPC: C01B3/16

CPC classification number: C01B3/16 ,  B01J23/002 ,  B01J23/005 ,  B01J23/06 ,  B01J35/023 ,  B01J37/0201 ,  B01J37/03 ,  B01J2523/00 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/1076 ,  Y02P20/52 ,  B01J2523/12 ,  B01J2523/27 ,  B01J2523/31 ,  B01J2523/13 ,  B01J2523/15

Abstract: Catalyst for use in the high temperature shift reaction comprising in its active form a mixture of zinc alumina spinel and zinc oxide in combination with an alkali metal selected from the group consisting of Na, K, Rb, Cs and mixtures thereof.

Abstract translation: 在高温转移反应中使用的催化剂，其活性形式包括与选自Na，K，Rb，Cs及其混合物的碱金属组合的锌铝尖晶石和氧化锌的混合物。

公开(公告)号：US07790776B2

公开(公告)日：2010-09-07

申请号：US12065166

申请日：2006-08-28

Applicant: Claus Hviid Christensen ,  Martin Andersson ,  Arkady Kustov ,  Tue Johannesen ,  Thomas Bligaard ,  Kasper E. Larsen ,  Jens K. Nørskov ,  Jens Sehested

Inventor： Claus Hviid Christensen ,  Martin Andersson ,  Arkady Kustov ,  Tue Johannesen ,  Thomas Bligaard ,  Kasper E. Larsen ,  Jens K. Nørskov ,  Jens Sehested

IPC: C07C27/00

CPC classification number: B01J23/75 ,  B01J21/005 ,  B01J23/745 ,  B01J23/755 ,  B01J23/78 ,  B01J37/0201 ,  C07C1/044 ,  C07C2523/75 ,  C07C2523/755 ,  H01M8/0668 ,  C07C9/04

Abstract: A process for hydrogenation of carbon oxides comprising contacting a gas mixture containing carbon oxides and of hydrogen with a catalyst comprising bimetallic iron-nickel or iron-cobalt alloys as the active catalytic material supported on a carrier of an oxide. The carrier is preferably formed to have a surface area greater than 20 m2/g.

Abstract translation: 一种用于碳氧化物氢化的方法，包括使含有碳氧化物和氢气的气体混合物与包含双金属铁镍或铁 - 钴合金的催化剂作为负载在氧化物载体上的活性催化材料接触。 载体优选形成为具有大于20m 2 / g的表面积。

公开(公告)号：US07713408B2

公开(公告)日：2010-05-11

申请号：US11976297

申请日：2007-10-23

Applicant: Rasmus Breivik ,  Kim Grøn Knudsen

Inventor： Rasmus Breivik ,  Kim Grøn Knudsen

IPC: C10G45/04

CPC classification number: C10G65/04 ,  C10G2300/201 ,  C10G2300/202 ,  C10G2300/4006

Abstract: Process for the catalytic hydrotreating of a hydrocarbon feed stock containing silicon compounds comprising the steps of contacting the feed stock in presence of hydrogen with a first hydrotreating catalyst being arranged in at least two reactors being connected in series at an outlet temperature of up to 410° C. to reduce content of the silicon compounds in the feed stock; cooling of the feed stock such treated to a temperature of between 280° and 350° C.; and contacting the cooled feed stock with a second hydrotreating catalyst at conditions being effective in reduction of sulphur compound and nitrogen compound concentration.

Abstract translation: 含有硅化合物的烃原料的催化加氢处理方法包括以下步骤：在氢存在下使原料与第一加氢处理催化剂接触，所述第一加氢处理催化剂布置在至少两个反应器中，串联出口温度高达410° 以减少原料中硅化合物的含量; 将原料冷却至280℃至350℃之间的温度; 并在有效降低硫化合物和氮化合物浓度的条件下使冷却的原料与第二加氢处理催化剂接触。