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1. 发明申请

WO2013004398A2 METHOD FOR THE PARALLEL PRODUCTION OF HYDROGEN AND CARBON-CONTAINING PRODUCTS 审中-公开
标题翻译：工艺制备氢气和含碳产品的平行生产
公开(公告)号：WO2013004398A2
公开(公告)日：2013-01-10
申请号：PCT/EP2012002877
申请日：2012-07-05
申请人： LINDE AG , MAAS HANS-JUERGEN , GOEKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS , BASF SE
发明人： MAAS HANS-JUERGEN , GOEKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS
CPC分类号： C01B3/24 , C01B3/28 , C01B3/30 , C01B32/05 , C01B2203/0272 , C01B2203/04 , C01B2203/0425 , C01B2203/0485 , C01B2203/049 , C01B2203/06 , C01B2203/0805 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0866 , C01B2203/1235 , C01B2203/1258 , C10B57/005 , Y02P20/128
摘要： The invention relates to a method for the parallel production of hydrogen and of one or more carbon-containing products. In the method, hydrocarbons are introduced into a reaction chamber (R) and are thermally decomposed into carbon and hydrogen in the presence of a carbon-rich granulated material (W). The invention is characterised in that at least a portion of the thermal energy necessary for the decomposition of the hydrocarbon is introduced into the reaction chamber (R) via a gaseous heat transfer medium.
摘要翻译：本发明涉及一种用于同时生产氢和一种或多种含碳产品，其中，在一个反应空间（R）烃被引入的，并在富碳颗粒（W）的存在下热分解成碳和氢。本发明是通过一种气态传热介质到反应空间（R）被引入，其特征在于在所要求的用于烃的热能的分解的至少一个部分。

2. 发明申请

WO2012175625A1 SIMULTANE ENTFERNUNG/UMWANDLUNG VON TEERARTIGEN UND SCHWEFELHALTIGEN KOHLENWASSERSTOFFEN 审中-公开
标题翻译：法同时距离/转换柏油和硫烃类
公开(公告)号：WO2012175625A1
公开(公告)日：2012-12-27
申请号：PCT/EP2012/061996
申请日：2012-06-21
申请人： SÜD-CHEMIE AG , DE TONI, Andrea , MODL, Norbert , ANFANG, Georg
发明人： DE TONI, Andrea , MODL, Norbert , ANFANG, Georg
IPC分类号： C01B3/38 , C01B3/58 , C10K1/34
CPC分类号： C01B3/58 , C01B3/38 , C01B2203/0485 , C01B2203/049 , C01B2203/1058 , C01B2203/1064 , C01B2203/107 , C01B2203/1082 , C10K1/004 , C10K1/32 , C10K1/34
摘要： Die vorliegende Erfindung betrifft ein Verfahren zur Reinigung von Biogas, welches Teer und/oder teerhaltige Kohlenwasserstoffe sowie schwefelhaltige Kohlenwasserstoffe enthält, mit einem edelmetallhaltigen Katalysator. Die Erfindung ist darüber hinaus auf die Verwendung eines edelmetallhaltigen Katalysators zur simultanen Umwandlung von in Biogas enthaltenen Teer oder teerhaltigen Kohlenwasserstoffen zu Synthesegas und schwefelhaltigen Kohlenwasserstoffen zu Schwefelwasserstoff gerichtet. Die Erfindung betrifft darüber hinaus noch eine Reaktoranordnung zur Durchführung des Verfahrens.
摘要翻译：本发明涉及一种用于生物气的纯化，含焦油和/或焦油烃和含硫的烃，具有含贵金属的催化剂。本发明还涉及使用含贵金属的催化剂的包含在生物气，或焦油烃的合成气和含硫烃为硫化氢焦油的同时转换。本发明还涉及到另一个反应器装置，用于执行该方法。

3. 发明申请

WO2012030441A2 SYSTEM AND METHOD FOR CONTROLLING AN AIR SEPARATION UNIT 审中-公开
标题翻译：用于控制空气分离单元的系统和方法
公开(公告)号：WO2012030441A2
公开(公告)日：2012-03-08
申请号：PCT/US2011044428
申请日：2011-07-19
申请人： GEN ELECTRIC , STEELE RAYMOND DOUGLAS
发明人： STEELE RAYMOND DOUGLAS
IPC分类号： F25J3/04
CPC分类号： C01B3/36 , C01B2203/0255 , C01B2203/0283 , C01B2203/0475 , C01B2203/0485 , C01B2203/049 , C01B2203/84 , C01B2203/86 , C10J3/723 , C10J2300/0959 , C10J2300/1612 , C10J2300/1653 , C10J2300/1678 , C10J2300/1846 , C10K1/003 , F01K23/068 , F25J3/04545 , F25J3/04575 , F25J3/04593 , F25J3/04606 , F25J3/04848 , F25J2215/50 , Y02C20/20 , Y02E20/16 , Y02E20/18 , Y02E20/185 , Y02P30/30
摘要： A system includes an air separation unit configured to separate air into an oxygen rich stream and a nitrogen rich stream and a purity control system configured to receive input indicative of a target diluent level. The purity control system is configured to control the air separation unit to adjust an oxygen percentage and a nitrogen percentage of the oxygen rich stream based on the target diluent level.
摘要翻译：系统包括空气分离单元，其被配置为将空气分离成富氧流和富氮流，以及净化控制系统，其被配置为接收指示目标稀释液水平的输入。纯度控制系统被配置为基于目标稀释液水平来控制空气分离单元以调节氧气百分比和富氧流的氮百分比。

4. 发明申请

WO2010020655A1 IMPROVED PROCESS FOR PRODUCTION OF ELEMENTAL IRON 审中-公开
标题翻译：改进元素生产工艺
公开(公告)号：WO2010020655A1
公开(公告)日：2010-02-25
申请号：PCT/EP2009/060711
申请日：2009-08-19
申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. , VAN HEERINGEN, Gijsbert Jan , VAN JARWAARDE, Ewout Martijn , VAN DER PLOEG, Hendrik Jan , SMIT, Cornelis Jacobus
发明人： VAN HEERINGEN, Gijsbert Jan , VAN JARWAARDE, Ewout Martijn , VAN DER PLOEG, Hendrik Jan , SMIT, Cornelis Jacobus
IPC分类号： C21B13/00 , B01D53/22 , C01B3/36 , C01B3/50
CPC分类号： C21B13/0073 , B01D53/229 , B01D53/75 , B01D53/77 , B01D2255/20707 , B01D2256/16 , B01D2257/304 , B01D2257/308 , B01D2257/408 , B01D2257/502 , B01D2257/504 , C01B3/36 , C01B2203/025 , C01B2203/04 , C01B2203/0405 , C01B2203/0415 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/049 , C01B2203/0877 , C01B2203/0883 , C01B2203/0894 , C01B2203/1211 , C01B2203/1252 , C01B2203/147 , C01B2203/86 , C10J2300/0916 , C10J2300/0936 , C10J2300/0943 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/1678 , C10K1/08 , C21B2100/282 , C21B2100/42 , C21B2100/64 , Y02C10/10 , Y02P10/122 , Y02P10/128 , Y02P10/136 , Y02P20/152 , Y02P30/30
摘要： Process to prepare elemental iron by contacting an iron ore feed with a reducing gas at a pressure of between 1 and 10 bar to obtain iron and an off-gas, wherein the reducing gas is prepared by performing the following steps (a) partially oxidizing a mixture comprising a solid or liquid carbonaceous fuel and oxygen at a pressure of between 10 and 80 bar, thereby obtaining a gas comprising H 2 and CO; (b) removing CO 2 and H 2 S from, the gas obtained in step (a) to obtain an intermediate gas comprising H 2 and CO; (c) supplying the intermediate gas obtained in step (b) to a H 2 -selective membrane to obtain a H 2 -rich permeate gas and a CO-rich retentate; (d) heating H 2 -rich permeate to obtain a heated H 2 -rich permeate as the reducing gas.
摘要翻译：通过使铁矿石进料与1至10巴之间的压力下的还原气体接触来获得铁和废气来制备元素铁的方法，其中所述还原气体通过以下步骤（a）部分氧化混合物包含固体或液体含碳燃料和压力为10至80巴的氧气，从而获得包含H 2和CO的气体; （b）从步骤（a）获得的气体中除去CO 2和H 2 S，得到包含H 2和CO的中间气体; （c）将步骤（b）中获得的中间气体供应到H 2选择性膜，以获得富H2的渗透气体和富CO的滞留物; （d）加热富H2的渗透物，得到加热的富H2的渗透物作为还原气体。

5. 发明申请

WO2009059819A1 WASTE WATER TREATMENT FROM A BIOMASS-TO-LIQUID PROCESS COMPRISING SYNTHESIS GAS PRODUCTION AND INTEGRATED FACTORY FACILITY 审中-公开
标题翻译：从包括合成气生产和一体化工厂设备的生物质 - 液体过程的废水处理
公开(公告)号：WO2009059819A1
公开(公告)日：2009-05-14
申请号：PCT/EP2008/059439
申请日：2008-07-18
申请人： UPM-KYMMENE OYJ , KUKKONEN, Petri , KNUUTTILA, Pekka , JOKELA, Pekka
发明人： KUKKONEN, Petri , KNUUTTILA, Pekka , JOKELA, Pekka
IPC分类号： C02F11/10 , C02F9/00
CPC分类号： C01B3/323 , C01B3/382 , C01B3/48 , C01B3/52 , C01B13/0248 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/043 , C01B2203/0465 , C01B2203/048 , C01B2203/049 , C01B2203/1223 , C01B2210/0046 , C02F1/00 , C02F3/00 , C02F2101/34 , C02F2103/023 , C02F2103/16 , C02F2103/28 , C02F2103/365 , C10G2/30 , C10G2/32 , C10G3/00 , C10G3/50 , C10G45/58 , C10G2300/1003 , C10G2300/1011 , C10J3/00 , C10J2300/0916 , C10J2300/0959 , C10J2300/16 , C10J2300/1659 , C10J2300/1678 , C10J2300/169 , C10K1/101 , C10K3/04 , C10L1/04 , C10L2200/0469 , C10L2290/42 , C10L2290/54 , D21C11/0007 , D21C11/06 , Y02E20/16 , Y02E20/18 , Y02E50/32 , Y02P20/145 , Y02P30/20
摘要： Treatment of waste water from a biomass-to-liquid process, said process comprising producing synthesis gas from biomass and conversion of said synthesis gas into liquid hydrocarbons by a Fisher-Tropsch process. The waste waters obtained are purified in common with waste waters from another industrial process to which said biomass-to- liquid process is integrated, such as in forestry, power and/or heat generation, waste incineration or a process in a metal-, petrochemical and/or oil refining industry. The biomass-to-liquid. process and said another industrial process may have a common feed water process unit, a common cooling water process unit and a common waste water treatment unit. The waste water treatment process may comprise a biological purification process and said Fischer-Tropsch process may utilize a cobalt catalyst. An integrated factory comprising a biomass-to-liquid plant and another industrial facility in which both plants are connected to a common waste water treatment facilit is also described.
摘要翻译：从生物质到液体方法处理废水，所述方法包括从生物质产生合成气并通过费 - 托法将所述合成气转化成液态烃。所获得的废水与来自另一个工业过程的废水同样地被净化，所述生物质 - 液化过程被整合到其中，例如在林业，动力和/或发热，废物焚化或金属，石油化工和/或炼油工业。生物质到液体。并且所述另一工业过程可以具有共同的给水处理单元，普通的冷却水处理单元和普通的废水处理单元。废水处理方法可以包括生物净化方法，并且所述费 - 托法可以使用钴催化剂。还描述了一个综合工厂，其中包括一个生物质液化设备和另一个工业设施，两个工厂都连接到一个常见的废水处理设施。

6. 发明申请

WO2009027007A3 METHOD AND APPARATUS FOR THE PRODUCTION OF SYNGAS FROM HEAVY OIL 审中-公开
标题翻译：用于从重油生产合成的方法和装置
公开(公告)号：WO2009027007A3
公开(公告)日：2009-04-30
申请号：PCT/EP2008006439
申请日：2008-08-05
申请人： LINDE AG , GLASER JUERGEN
发明人： GLASER JUERGEN
IPC分类号： C01B3/36
CPC分类号： C01B3/36 , C01B2203/0244 , C01B2203/0255 , C01B2203/0465 , C01B2203/049 , C01B2203/0877 , C01B2203/1252 , C01B2203/148
摘要： The invention relates to a method and an apparatus for producing a gas (syngas) (6) containing carbon monoxide and hydrogen by partially oxidizing a charge (1) containing higher-boiling hydrocarbons (heavy oil) (11) in a gasification device (POX reactor) (R) and cooling and washing (W) the gasification product (4) obtained in the POX reactor (R). Accumulated soot-laden waste water (5) is mixed with naphtha (7) and is then introduced into a separating device (D) from which a largely soot-free water fraction (10) and a water-free naphtha/soot mixture (9) are separately withdrawn. The naphtha/soot mixture is fed to the POX reactor (R) along with the heavy oil (11) as a charge.
摘要翻译：本发明涉及一种方法以及一种用于制造一氧化碳和含氢气体（合成气）的装置（6）由含有插入一个较高沸点的烃的部分氧化（重油）（11）（1）在气化装置（POX）反应器（R ）和所得到的冷却和洗涤（W）（在POX反应器R）气化产物（4），其特征在于，累积，装载有碳黑废水（5）用石脑油混合（7），然后进入分离器（d）被引入，从中分别抽出大量无烟灰的水馏分（10）和无水石脑油/烟灰混合物（9）。将无水石脑油/炭黑混合物（9）与重油（11）一起作为嵌入物加入到POX反应器（R）中。

7. 发明申请

WO2008010717A2 METHOD AND SYSTEM FOR PURIFYING A PRODUCT GAS FORMED FROM BIOMASS 审中-公开
标题翻译：用于净化生物质形成的产品气体的方法和系统
公开(公告)号：WO2008010717A2
公开(公告)日：2008-01-24
申请号：PCT/NL2007050360
申请日：2007-07-20
申请人： STICHTING ENERGIE , VAN PAASEN SANDER VINCENT BERN
发明人： VAN PAASEN SANDER VINCENT BERN
IPC分类号： C10K1/00 , C10J3/84
CPC分类号： C10J3/84 , B01D47/05 , B01D51/04 , C01B3/50 , C01B2203/04 , C01B2203/049 , C10J3/56 , C10J2300/1807 , C10K1/02 , C10K1/026 , C10K1/028 , C10K1/046 , C10K1/16 , C10K1/18 , Y02P20/145
摘要： A method for purifying a combustible gas that is contaminated with contaminants, such as tar and/or dust particles, comprises feeding oil to the contaminated gas. The oil evaporates through contact with the contaminated gas. Said evaporated oil is condensed on a quantity of the contaminants in such a manner that said contaminants grow in size to form particles of increased size in the gas. An electric field between electrodes is applied, by means of which said particles of increased size are electrically charged and removed from the gas. The condensation of the oil takes place at a temperature above the water dew point of the contaminated gas. This water dew point is preferably between 50-100 °C, in particular between 50-80 °C.
摘要翻译：用于净化被污染物如焦油和/或灰尘颗粒污染的可燃气体的方法包括将油输送到污染气体。油通过与受污染的气体接触而蒸发。所述蒸发的油以一定量的污染物浓缩，使得所述污染物的尺寸增长，以形成气体中尺寸增大的颗粒。施加电极之间的电场，通过该电场，所述增大尺寸的颗粒被充电并从气体中除去。油的冷凝发生在高于受污染气体的水露点的温度下。该露点优选在50-100℃之间，特别是在50-80℃之间。

8. 发明申请

WO2005021421B1 PROCESS AND APPARATUS FOR THE PRODUCTION OF USEFUL PRODUCTS FROM CARBONACEOUS FEEDSTOCK 审中-公开
公开(公告)号：WO2005021421B1
公开(公告)日：2005-08-04
申请号：PCT/US2004026951
申请日：2004-08-20
申请人： PEARSON TECHNOLOGIES INC , PEARSON STANLEY R
发明人： PEARSON STANLEY R
IPC分类号： B01J4/02 , B01J8/06 , B01J19/20 , B01J21/18 , B01J23/80 , B01J23/86 , B01J23/889 , B01J37/00 , B01J37/04 , B01J37/18 , C01B3/34 , C01B3/52 , C01B32/40 , C07C29/151 , C10G2/00 , C10J3/46 , C07C27/00 , A61L2/00 , B01D11/02 , B01D50/00 , B01J7/00 , B01J8/08 , B01J10/00 , B01J23/00 , C07C1/02
CPC分类号： B01J23/864 , B01J21/18 , B01J23/80 , B01J23/8892 , B01J37/0009 , B01J37/04 , B01J37/18 , C01B3/34 , C01B3/52 , C01B2203/0216 , C01B2203/0415 , C01B2203/043 , C01B2203/0465 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/049 , C01B2203/061 , C01B2203/062 , C01B2203/84 , C07C29/1518 , C07C29/32 , C10G2/331 , C10G2/34 , C10G2/50 , C10J3/00 , C10J3/466 , C10J2200/156 , C10J2300/0906 , C10J2300/0909 , C10J2300/092 , C10J2300/0946 , C10J2300/0973 , C10J2300/1621 , C10J2300/1659 , C10J2300/1665 , C10J2300/1884 , C10J2300/1892 , C10K1/005 , C10K1/101 , C10K1/16 , C10K1/32 , Y02E50/18 , Y02E50/32 , Y02P20/145 , Y02P20/52 , C07C31/04 , C07C31/08
摘要： A carbonaceous feedstock to alcohol conversion process in which carbon dioxide is removed from the syngas stream issuing from a feedstock reformer, to yield a carbon dioxide depleted syngas stream including hydrogen, carbon monoxide and methane. This carbon dioxide depleted syngas stream is then passed through a Fischer-Tropsch reactor ultimately yielding a mixed alcohol product which is preferably largely ethanol. The removed carbon dioxide stream is passed through a methane reformer along with methane, which is produced in or has passed through a Fischer-Tropsch reactor, to yield primarily carbon monoxide and hydrogen. The carbon monoxide and hydrogen stream from the methane reformer are passed through the alcohol reactor. Also disclosed are a unique catalyst, a method for controlling the content of the syngas formed in the feedstock reformer, and a feedstock handling system.

9. 发明申请

WO2004076594A2 PROCESS FOR THE CONVERSION OF FEEDSTOCKS AND APPARATUS FOR PERFORMING THE SAME 审中-公开
标题翻译：饲料转化过程和设备进行处理
公开(公告)号：WO2004076594A2
公开(公告)日：2004-09-10
申请号：PCT/US2004/005139
申请日：2004-02-20
申请人： MC INTERNATIONAL RESEARCH, INC.
发明人： STICKNEY, Michael, J. , JONES, Edward, M., Jr. , CHANDRASEKHARIAH, Mallasetty, S.
IPC分类号： C10G
CPC分类号： B01J3/042 , B01J3/08 , B01J12/007 , B01J19/0053 , B01J19/12 , B01J2208/00716 , C01B3/36 , C01B2203/00 , C01B2203/0255 , C01B2203/049 , C01B2203/0495 , C01B2203/0805 , C01B2203/0811 , C01B2203/0877 , C01B2203/1241 , C01B2203/1276 , C01B2203/1282 , C01B2203/1604 , C01B2203/1628 , C01B2203/1676 , C01B2203/169
摘要： A process is provided for conversion of a feedstock, in particular a hydrocarbon feedstock such as methane or natural gas, in which a reactive mixture containing the feedstock is prepared and fed to a reaction zone. A reaction is initiated in the reactive mixture within the reaction zone so as to generate a conversion wave of increased temperature and pressure. The conversion wave is allowed to pass through the reaction zone, from where converted feedstock is recovered. An apparatus for carrying out the process is also provided. The process operates with a high conversion and selectivity to desirable products and is particularly suitable for the conversion of methane to carbon monoxide and hydrogen.
摘要翻译：提供了用于转化原料，特别是烃原料如甲烷或天然气的方法，其中制备含有原料的反应混合物并将其进料至反应区。在反应区内的反应混合物中开始反应，以产生升高的温度和压力的转化波。允许转化波通过反应区，从其中回收转化的原料。还提供了一种用于执行该过程的装置。该方法以对所需产物的高转化率和选择性运行，并且特别适用于将甲烷转化为一氧化碳和氢气。

10. 发明申请

WO2015173352A1 METHOD AND APPARATUS FOR PRODUCING H2-RICH SYNTHESIS GAS 审中-公开
标题翻译：用于生产氢气合成气的方法和装置
公开(公告)号：WO2015173352A1
公开(公告)日：2015-11-19
申请号：PCT/EP2015/060687
申请日：2015-05-13
申请人： CCP TECHNOLOGY GMBH
发明人： KÜHL, Dr. Olaf
IPC分类号： C01B3/24 , C01B31/18 , C01B3/48 , C10G2/00
CPC分类号： C01B3/24 , C01B3/12 , C01B2203/0272 , C01B2203/0283 , C01B2203/0288 , C01B2203/049 , C01B2203/061 , C01B2203/062 , C01B2203/0805 , C01B2203/0844 , C01B2203/0861 , C01B2203/0883 , C01B2203/1276 , C01B2203/141 , C01B2203/145 , C10G2/30 , C10G2/32 , C10G2/34 , C10J2300/1618 , C10J2300/1853 , C10K3/04 , Y02P20/129
摘要： A method for producing ¾-rich synthesis gas comprises the following steps: decomposing a hydrocarbon- containing fluid into an H 2 /C-aerosol in a first hydrocarbon converter by supplying energy which is at least partly provided in the form of heat; introducing at least a first stream of the H 2 /C-aerosol into a first sub-process which comprises the following steps: directing at least a part of the H 2 /C-aerosol from the first hydrocarbon converter into a first C-converter; introducing CO 2 into the first C-converter and mixing the CO 2 with the H 2 /C-aerosol introduced into the first C-converter; converting the mixture of H 2 /C-aerosol and CO 2 into a synthesis gas at a temperature of 800 to 1700°C; mixing additional H 2 with the synthesis gas for the production of H 2 -rich synthesis gas. In a second sub-process running in parallel with the first sub-process, hydrogen H 2 and carbon dioxide CO 2 are produced from a hydrocarbon-containing fluid, wherein at least a portion of the CO 2 produced in the second sub-process is introduced into the first C-converter; and wherein at least a portion of the H 2 produced in the second sub-process is mixed with the synthesis gas from the first C-converter. The CO 2 which is needed for the conversion of C in the first C-converter can thereby be provided independently of an external source, and the entire operational sequence is easily controllable.
摘要翻译：一种生产富氘合成气的方法包括以下步骤：通过提供至少部分以热的形式提供的能量将烃类流体分解成第一烃转化器中的H 2 / C-气溶胶; 将至少第一流的H2 / C-气溶胶引入到第一子过程中，其包括以下步骤：将来自第一烃转化器的H 2 / C-气溶胶的至少一部分引导到第一C转换器中; 将CO 2引入到第一C转化器中并将CO 2与引入到第一C转换器中的H 2 / C气溶胶混合; 将H 2 / C气溶胶和CO 2的混合物在800至1700℃的温度下转化为合成气; 将额外的H2与合成气混合，用于生产富H2合成气。在与第一子方法并行运行的第二子方法中，氢气H2和二氧化碳CO 2由含烃流体产生，其中在第二子方法中产生的CO 2的至少一部分被引入第一个C转换器; 并且其中在所述第二子过程中产生的所述H 2的至少一部分与来自所述第一C转换器的合成气混合。因此，可以独立于外部源来提供在第一C转换器中转换C所需的CO 2，并且整个操作顺序容易控制。

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