公开(公告)号：EP2419497B1

公开(公告)日：2018-05-30

申请号：EP10713265.6

申请日：2010-04-14

Applicant: Stichting Energieonderzoek Centrum Nederland

Inventor： VAN DER MEIJDEN, Christiaan Martinus ,  RABOU, Lucas Petrus Loduvicus Maria

IPC: C10L3/08 ,  C10L3/10 ,  C10J3/00 ,  C10K3/02 ,  C10K3/04 ,  C07C9/04

CPC classification number: C10L3/08 ,  C10J3/00 ,  C10J3/482 ,  C10J3/523 ,  C10J3/84 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/0973 ,  C10J2300/1618 ,  C10J2300/1662 ,  C10J2300/1838 ,  C10K1/005 ,  C10K1/04 ,  C10K1/08 ,  C10K1/143 ,  C10K3/02 ,  C10L3/10 ,  C10L3/102

Abstract: Method and system for the production of a combustible gas from a fuel, comprising the conversion of the fuel, at a temperature that is between 600 and 1000° C. and at a pressure that is lower than 10 bar, into at least a combustible gas that comprises CH4, CO, H2, CO2, H2O and higher hydrocarbons in a reactor installation (1). At least part of the higher hydrocarbons present in the combustible gas is catalytically converted into at least CH4, CO, H2, CO2 and H2O in a reactor (45) at a pressure that is lower than 10 bar. After this catalytic conversion, an amount of H2O and an amount of CO2 are removed from the combustible gas in a separator installation (50) at a pressure that is lower than 10 bar. After the removal of H2O and CO2, the pressure of the combustible gas is raised by a compressor (71).

公开(公告)号：EP3259248A1

公开(公告)日：2017-12-27

申请号：EP15813559.0

申请日：2015-12-18

Applicant: Johnson Matthey Public Limited Company

Inventor： ERLANDSSON, Ola ,  MAGNUSSON, Andreas ,  PACH, John David ,  SHELDON, Daniel

IPC: C07C273/14 ,  C01B3/02 ,  C01C1/04 ,  C07C29/151 ,  C07C45/38 ,  C07C273/04

CPC classification number: C07C273/14 ,  C01B3/025 ,  C01B3/382 ,  C01B3/48 ,  C01B3/52 ,  C01B3/54 ,  C01B3/56 ,  C01B3/586 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0283 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/0445 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/06 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/068 ,  C01B2203/1241 ,  C01B2203/1252 ,  C01B2203/142 ,  C01C1/0488 ,  C07C29/1518 ,  C07C45/29 ,  C07C45/38 ,  C07C273/04 ,  C07C273/10 ,  C10J3/82 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0976 ,  C10J2300/1838 ,  C10J2300/1853 ,  Y02P20/125 ,  Y02P20/52 ,  C07C31/04 ,  C07C47/04

Abstract: The present disclosure relates to an integrated process for the production of formaldehyde-stabilized urea, starting with producing synthesis gas and including the preparation of methanol, ammonia, urea, and formaldehyde in amounts appropriate for the final product.

公开(公告)号：EP2633003B1

公开(公告)日：2016-12-07

申请号：EP11835379.6

申请日：2011-10-18

Applicant: Enerkem, Inc.

Inventor： PAQUET, Antonin ,  GAGNON, Martin ,  CHORNET, Esteban

IPC: C10J3/00 ,  C01B3/36 ,  C10J3/84 ,  C10K1/02 ,  C10K1/04 ,  C10J3/48

CPC classification number: C10K1/046 ,  C01B3/36 ,  C01B2203/0205 ,  C01B2203/06 ,  C01B2203/1241 ,  C10J3/482 ,  C10J3/485 ,  C10J3/84 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/0996 ,  C10J2300/1253 ,  C10J2300/1659 ,  C10J2300/1807 ,  C10J2300/1838 ,  C10J2300/1853 ,  C10K1/026 ,  Y02E50/32 ,  Y02P20/145

公开(公告)号：EP2771436A1

公开(公告)日：2014-09-03

申请号：EP12784458.7

申请日：2012-10-26

Applicant: Ligento Green Power GmbH

Inventor： ZUCKERMAIER, Martin ,  TSCHAFTARY, Thomas

IPC: C10J3/26 ,  C10J3/34 ,  C10J3/72

CPC classification number: C10J3/26 ,  C10J3/34 ,  C10J3/723 ,  C10J2200/152 ,  C10J2300/092 ,  C10J2300/0923 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0976 ,  C10J2300/1838

Abstract: There is specified a gasification reactor (1) having a reaction chamber (4) for the autothermal gasification of carbon-containing fuel to form useful gases, wherein the reaction chamber has a plurality of control inputs (10) which are at least partially independent of one another. The gasification process is controlled by means of the recirculation of the gas within the reactor and/or by means of the addition of gasification agents via the control inputs (10).

Abstract translation: 具有气化反应器（1），其具有用于使含碳燃料自热气化以形成有用气体的反应室（4），其中所述反应室具有多个控制输入（10），所述控制输入至少部分地独立于 另一个。 气化过程通过反应器内的气体的再循环和/或通过经由控制输入（10）添加气化剂来控制。

公开(公告)号：EP2505632A3

公开(公告)日：2013-12-11

申请号：EP12001452.7

申请日：2012-03-03

Applicant: E.ON New Build & Technology GmbH

Inventor： Adelt, Marius, Dr.

IPC: C10J3/20 ,  C10J3/00 ,  F01K23/06 ,  C10J3/48 ,  F01K17/02 ,  C10L3/08 ,  C10L3/10

CPC classification number: C10J3/00 ,  C10J3/485 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/12 ,  C10J2300/1653 ,  C10J2300/1662 ,  C10J2300/1838 ,  C10L3/08 ,  C10L3/104 ,  F01K17/025 ,  F01K23/065 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E50/11 ,  Y02E50/343 ,  Y02P20/129

Abstract: Die Erfindung betrifft ein Verfahren und eine Anlage zum Erzeugen von Brenngas und elektrischer Energie mit folgenden Schritten
a) Erzeugen eines Produktgases in einer Biomassevergasungseinrichtung (1) aus holzartiger Biomasse,
b) Umwandeln des Produktgases in einem Methanisierungsreaktor (3) in einem exothermen Methanisierungsprozess zu einem methanhaltigen Brenngas und
c) Erzeugen eines mit Erdgas austauschbaren Gases (Bio-SNG), indem aus dem methanhaltigen Brenngas CO 2 entfernt wird.
Erfindungsgemäß wird
c) die Abwärme des exothermen Prozesses in dem Methanisierungsreaktor (3) in einem Gas- und Dampfturbinen-Kraftwerk (2) zur Zwischenüberhitzung von Wasserdampf genutzt, der eine Dampfturbine antreibt

公开(公告)号：EP2635369A1

公开(公告)日：2013-09-11

申请号：EP11838896.6

申请日：2011-11-04

Applicant: Thermochem Recovery International, Inc.

Inventor： CHANDRAN, Ravi ,  ZENZ, Jonathan A. ,  NEWPORT, Dave G. ,  WHITNEY, Hamilton Sean Michael

IPC: B01J8/18 ,  C07C1/00

CPC classification number: C10J3/721 ,  B01J8/004 ,  B01J8/0055 ,  B01J8/26 ,  B01J8/388 ,  B01J2208/00132 ,  B01J2208/00398 ,  B01J2208/00415 ,  B01J2208/00752 ,  B01J2208/00761 ,  C01B3/02 ,  C10J3/466 ,  C10J3/48 ,  C10J3/482 ,  C10J3/485 ,  C10J3/723 ,  C10J2200/09 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/094 ,  C10J2300/0946 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/0983 ,  C10J2300/0986 ,  C10J2300/1246 ,  C10J2300/1261 ,  C10J2300/1625 ,  C10J2300/1637 ,  C10J2300/1687 ,  C10J2300/1807 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  C10J2300/1892 ,  C10K1/026 ,  Y02P20/13

Abstract: A solids circulation system receives a gas stream containing char or other reacting solids from a first reactor. The solids circulation system includes a cyclone configured to receive the gas stream from the first reactor, a dipleg from the cyclone to a second reactor, and a riser from the second reactor which merges with the gas stream received by the cyclone. The second reactor has a dense fluid bed and converts the received materials to gaseous products. A conveying fluid transports a portion of the bed media from the second reactor through the riser to mix with the gas stream prior to cyclone entry. The bed media helps manipulate the solids that is received by the cyclone to facilitate flow of solids down the dipleg into the second reactor. The second reactor provides additional residence time, mixing and gas-solid contact for efficient conversion of char or reacting solids.

Abstract translation: 甲固体循环系统接收来自第一反应器含有炭或彼此反应的固体的气体流。 固体循环系统包括配置成从所述第一反应器接收所述气体流，从旋风分离器浸入管至第二反应器的旋风分离器，并从与由旋流器接收的气流汇合的第二反应器的立管。 第二反应器具有致密流化床和将接收到的材料的气态产物转换。 的输送流体通过立管传输从第二反应器中床介质的一部分与前项气旋气流混合。 该床介质有助于操纵固体并通过旋风分离器接收以促进固体的流动向下浸入管进入第二反应器。 第二反应器中提供额外的停留时间，混合和用于char或起反应的固体的有效转化的气体 - 固体接触。

公开(公告)号：EP2612896A3

公开(公告)日：2013-08-14

申请号：EP13150240.3

申请日：2013-01-04

Applicant: General Electric Company

Inventor： Kumar, Anand ,  Marikatti, Prashant

IPC: C10J3/84 ,  C10J3/48

CPC classification number: C10J3/845 ,  C10J3/485 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1838 ,  C10J2300/1846 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E60/324

Abstract: A system includes a dip tube configured to direct a gas toward a sump. The dip tube includes an inner surface and an outer surface. The system also includes a quench ring coupled to the dip tube. The quench ring is configured to provide a quench fluid flow to the sump over both the inner surface and the outer surface of the dip tube.

Abstract translation: 系统包括配置成将气体朝向贮槽引导的汲取管。 汲取管包括内表面和外表面。 该系统还包括联接到浸管的淬火环。 急冷环构造成在浸渍管的内表面和外表面两者上提供急冷流体流到贮槽。

公开(公告)号：EP2376607A1

公开(公告)日：2011-10-19

申请号：EP09832782.8

申请日：2009-12-18

Applicant: Enerkem, Inc.

Inventor： CHORNET, Esteban ,  VALSECCHI, Boris ,  RHEAULT, Sébastien ,  GAGNON, Martin

IPC: C10J3/54

CPC classification number: C10J3/463 ,  C10J3/16 ,  C10J3/66 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0923 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/0996 ,  C10J2300/1603 ,  C10J2300/1615 ,  C10J2300/169 ,  C10J2300/1838 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/003 ,  C10K1/004 ,  C10K1/026 ,  C10K1/101 ,  C10K1/12 ,  C10K3/005 ,  C10K3/006 ,  Y02E50/32 ,  Y02P20/145

Abstract: A process for producing synthesis gas from biomass in which biomass is contacted with oxygen and steam, wherein the oxygen is present in an amount effective to oxidize the biomass partially and to heat the biomass to a temperature of at least 500°C and no greater than 750°C At least a portion of the partially oxidized biomass then is treated with oxygen and steam to heat the biomass to a temperature of at least 800°C, thereby producing a synthesis gas, which then is recovered

公开(公告)号：EP1348011B1

公开(公告)日：2010-03-17

申请号：EP01990822.7

申请日：2001-12-04

Applicant: Emery Energy Company L.L.C.

Inventor： HASSETT, Scott

IPC: C10B3/00 ,  C10J3/16

CPC classification number: C10J3/84 ,  C01B3/36 ,  C10J3/08 ,  C10J3/16 ,  C10J3/20 ,  C10J3/26 ,  C10J3/34 ,  C10J3/487 ,  C10J3/506 ,  C10J3/64 ,  C10J3/66 ,  C10J3/72 ,  C10J3/721 ,  C10J3/723 ,  C10J2200/09 ,  C10J2300/0936 ,  C10J2300/1838 ,  C10K1/024 ,  C10K1/32 ,  C10K3/04 ,  Y02E20/18 ,  Y10S48/03

Abstract: A gasifier (1) is disclosed combining a fixed bed gasification section (4, 5, 8, 11 and 13) where coarse fuel entering through inlet (2) is gasified and an entrained flow gasification section (7) where fine fuel entering through one or more tangentially fired burners (19) or from a combustion gasification cylindrical chamber (18) is gasified. The fixed bed section includes upper (4 and 5) and lower (8, 11 and 13) sections. Coarse fuel is devolatilized in the upper fixed bed section (4 and 5) and subjected to elevated temperatures sufficient to crack and destroy tars and oils in the effluent gases. The entrained flow gasification section (17) is disposed in a lower plenum adjacent the lower fixed bed section (13). A plurality of injection ports (6, 10) is configured to introduce oxygen, steam, or air into different sections of the gasifier (1) to control temperature and operating conditions. Activated carbon may be formed in the upper fixed bed section (4, 5, 8, 11 and 13) and in the entrained flow section (17). The activated carbon may be used as a sorbent to remove pollutants from the effluent gases leaving the gasifier (1) through exit pipe (15). The gasifier (1) may be used with various coarse and fine fuel feedstocks.

公开(公告)号：EP1753064A2

公开(公告)日：2007-02-14

申请号：EP06112070.5

申请日：2006-03-31

Applicant: Voith Patent GmbH

Inventor： Döling, Fabian

IPC: H01M8/06

CPC classification number: H01M8/0612 ,  C01B3/34 ,  C01B3/48 ,  C01B2203/0216 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0255 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/043 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/06 ,  C01B2203/061 ,  C01B2203/066 ,  C01B2203/1235 ,  C01B2203/146 ,  C10J3/00 ,  C10J3/16 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/0973 ,  C10J2300/1838 ,  C10K3/005 ,  C10K3/006 ,  C10K3/04 ,  H01M8/04022 ,  H01M8/0668 ,  H01M8/1011 ,  H01M2250/00 ,  Y02E60/523 ,  Y02P20/145

Abstract: Bei einem Verfahren zur Erzeugung von Prozesswärme und/oder elektrischer Energie für die Zellstoffherstellung, für die Stoffaufbereitung und/oder für eine Maschine zur Herstellung und/oder Veredelung einer Faserstoffbahn, insbesondere Papier- oder Kartonbahn, wird aus den bei der Zellstoffherstellung, der Stoffaufbereitung und/oder der Herstellung und/oder Veredelung der Faserstoffbahn anfallenden Abfallprodukten und/oder aus den bei wenigstens einem anderen Herstellungsprozess anfallenden Abfallprodukten Gas mit möglichst hohem Wasserstoffanteil erzeugt und dieses wasserstoffreiche Gas zur Erzeugung der erforderlichen Prozesswärme und/oder erforderlichen elektrischen Energie verwendet.

Abstract translation: 该方法包括以高氢比例生产气体，其中气体产生工艺热和/或电能。 气体由生产纸浆，材料制备和/或纤维网的制造或整理过程中产生的废物产生。 通过使用重整器（10）通过自动热重整将废物的烃转化为富氢和一氧化碳的气体。