BRPI0514830A - reator catalìtico - Google Patents

reator catalìtico

Info

Publication number
BRPI0514830A
BRPI0514830A BRPI0514830-8A BRPI0514830A BRPI0514830A BR PI0514830 A BRPI0514830 A BR PI0514830A BR PI0514830 A BRPI0514830 A BR PI0514830A BR PI0514830 A BRPI0514830 A BR PI0514830A
Authority
BR
Brazil
Prior art keywords
coil
reaction
reactor
compact
catalytic reactor
Prior art date
Application number
BRPI0514830-8A
Other languages
English (en)
Inventor
Timothy Mark Aaron
Minish Mahendra Shah
Richard Jibb
Original Assignee
Praxair Technology Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Praxair Technology Inc filed Critical Praxair Technology Inc
Publication of BRPI0514830A publication Critical patent/BRPI0514830A/pt

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • B01J8/067—Heating or cooling the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2415—Tubular reactors
    • B01J19/243—Tubular reactors spirally, concentrically or zigzag wound
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/48—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • F28D7/0083—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
    • F28D7/024—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/14—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically both tubes being bent
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00203—Coils
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00309—Controlling the temperature by indirect heat exchange with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00477—Controlling the temperature by thermal insulation means
    • B01J2208/00495—Controlling the temperature by thermal insulation means using insulating materials or refractories
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1041—Composition of the catalyst
    • C01B2203/1047—Group VIII metal catalysts
    • C01B2203/1052—Nickel or cobalt catalysts
    • C01B2203/1058—Nickel catalysts
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205—Composition of the feed
    • C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
    • C01B2203/1235—Hydrocarbons
    • C01B2203/1241—Natural gas or methane
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1258—Pre-treatment of the feed
    • C01B2203/1264—Catalytic pre-treatment of the feed
    • C01B2203/127—Catalytic desulfurisation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

REATOR CATALìTICO. Um reator catalítico (1) é provido com uma ou mais zonas de reação, cada uma formada de conjuntos de tubos de reação (26, 34) contendo um catalisador (27, 35) para promover reação química dentro de uma corrente de alimentação. Os tubos de reação (26, 34) são de configuração helicoidal e são arranjados em uma relação substancialmente coaxial para formar uma estrutura como serpentina. Trocadores de calor e geradores de vapor podem ser formados através de arranjos de tubos semelhantes. De tal maneira, as zonas de reação e conseqüentemente, o reator (1) é compacto e a queda de pressão por componentes é minimizada. A forma compacta resultante melhorou as características de transferência de calor e é muito mais fácil de isolar termicamente do que projetos de reator compacto da arte anterior. Várias reações químicas estão contempladas dentro de tais estruturas como serpentina tal como reforma de metano a vapor seguida por troca de água-gás. As estruturas como serpentina poderiam ser alojadas dentro de câmaras anulares (90, 92, 24) de um alojamento cilíndrico (2) que também provê caminhos de fluxo para vários fluidos de troca de calor para aquecer e esfriar componentes.
BRPI0514830-8A 2004-09-01 2005-08-30 reator catalìtico BRPI0514830A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/931,066 US7500999B2 (en) 2004-09-01 2004-09-01 Catalytic reactor
PCT/US2005/030559 WO2007001350A2 (en) 2004-09-01 2005-08-30 Catalytic reactor

Publications (1)

Publication Number Publication Date
BRPI0514830A true BRPI0514830A (pt) 2008-06-24

Family

ID=35943442

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0514830-8A BRPI0514830A (pt) 2004-09-01 2005-08-30 reator catalìtico

Country Status (6)

Country Link
US (1) US7500999B2 (pt)
EP (1) EP1804962A4 (pt)
CN (1) CN100574859C (pt)
BR (1) BRPI0514830A (pt)
CA (1) CA2578622C (pt)
WO (1) WO2007001350A2 (pt)

Families Citing this family (42)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101155924B1 (ko) * 2005-02-28 2012-06-20 삼성에스디아이 주식회사 연료 전지 시스템, 개질기 및 버너
DE102006019409B4 (de) * 2006-04-23 2010-02-04 Zentrum für Brennstoffzellen-Technik GmbH Reformer-Reaktor, seine Verwendung und Verfahren zum Betrieb des Reformers
ITVR20060186A1 (it) * 2006-12-04 2008-06-05 I C I Caldaie S P A Apparecchiatura per la produzione di idrogeno particolarmente per l'alimentazione di celle a combustibile o simili
US20090022635A1 (en) * 2007-07-20 2009-01-22 Selas Fluid Processing Corporation High-performance cracker
WO2010024792A1 (en) * 2008-08-18 2010-03-04 Black & Veatch Corporation Reformer for converting biomass into synthesis gas
US8168144B2 (en) * 2009-01-15 2012-05-01 Eventix, Inc. System and method for providing an integrated reactor
WO2010087791A1 (en) * 2009-01-27 2010-08-05 Utc Power Corporation Distributively cooled, integrated water-gas shift reactor and vaporizer
CA2753217A1 (en) * 2009-02-21 2010-08-26 Sofradim Production Apparatus and method of reacting polymers passing through metal ion chelated resin matrix to produce injectable medical devices
FR2945478B1 (fr) * 2009-05-13 2015-07-17 Valeo Systemes Thermiques Installation de ventilation, de chauffage et/ou de climatisation comprenant quatre echangeurs de chaleur
US9039934B2 (en) * 2010-12-01 2015-05-26 Air Liquide Process & Construction, Inc. Coiled reformer catalyst tube for compact reformer
US8496733B2 (en) 2011-01-11 2013-07-30 Praxair Technology, Inc. Large scale pressure swing adsorption systems having process cycles operating in normal and turndown modes
US8551217B2 (en) 2011-01-11 2013-10-08 Praxair Technology, Inc. Six bed pressure swing adsorption process operating in normal and turndown modes
US8491704B2 (en) 2011-01-11 2013-07-23 Praxair Technology, Inc. Six bed pressure swing adsorption process operating in normal and turndown modes
US8435328B2 (en) 2011-01-11 2013-05-07 Praxair Technology, Inc. Ten bed pressure swing adsorption process operating in normal and turndown modes
FR2979257B1 (fr) * 2011-08-26 2013-08-16 Ifp Energies Now Reacteur echangeur pour la production d'hydrogene avec faisceau de generation vapeur integre
WO2013086190A1 (en) * 2011-12-06 2013-06-13 Hy9 Corporation Catalyst-containing reactor system and associated methods
US20130195735A1 (en) * 2012-02-01 2013-08-01 Delphi Technologies, Inc. Heat exchanger reformer with thermal expansion management
US8574501B1 (en) 2012-05-16 2013-11-05 Greenway Innovative Energy, Inc. Natural gas to liquid fuels
CN104755870B (zh) * 2012-10-18 2017-07-28 林德股份公司 多个入口的缠绕式传热器和用于适配传热器热表面的方法
US8955467B1 (en) * 2013-01-08 2015-02-17 William Parrish Horne Steam boiler
ES2729602T3 (es) 2013-01-28 2019-11-05 Carrier Corp Unidad de intercambio de calor con varios bancos de tubos con un conjunto de colector
EP2951521B1 (en) * 2013-01-30 2017-08-23 Tetra Laval Holdings & Finance SA A tubular heat treatment apparatus with improved energy efficiency
WO2015076927A1 (en) 2013-11-25 2015-05-28 Carrier Corporation Dual duty microchannel heat exchanger
CN105642197A (zh) * 2014-09-24 2016-06-08 楼韧 一种大型反应器及其装置和工艺
US10112830B2 (en) * 2014-12-08 2018-10-30 Clariant Corporation Shaped catalyst for sour gas shift reactions and methods for using them
DE102014226282A1 (de) * 2014-12-17 2016-06-23 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Reaktor zur Dehydrierung von flüssigen Wasserstoffträgermaterialien
CN104479394B (zh) * 2014-12-31 2016-06-08 苏州世名科技股份有限公司 偶氮颜料在分支螺旋管中的连续化制备方法
AT518216A1 (de) * 2016-01-21 2017-08-15 Ge Jenbacher Gmbh & Co Og Brennkraftmaschine
CN105782962A (zh) * 2016-03-04 2016-07-20 常州市蓝博净化科技有限公司 一种催化燃烧节能供热系统
EP3267100B1 (de) * 2016-07-08 2021-04-14 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Dampferzeugungsanlage
CN106365118B (zh) * 2016-11-15 2018-09-14 晋城市阿邦迪能源有限公司 带有co净化及温度监控功能的甲醇重整反应室
EP3603795B1 (de) * 2018-07-31 2022-04-06 Siemens Aktiengesellschaft Reaktor zum leiten von wenigstens zwei reaktanten und verfahren zum herstellen eines reaktors
CN108686612A (zh) * 2018-08-02 2018-10-23 汤铁 管式逆流换热反应器
CN109759000B (zh) * 2019-01-18 2024-04-12 山东诺为制药流体系统有限公司 一种多线程折流管箱及反应器
US10478794B1 (en) 2019-02-26 2019-11-19 Chevron Phillips Chemical Company Lp Bi-modal radial flow reactor
CN111889036B (zh) * 2019-05-05 2023-01-10 中国石油集团工程股份有限公司 环戊二烯固定床催化加氢反应装置、系统及方法
CN110975767B (zh) * 2019-10-24 2022-07-12 中石化宁波工程有限公司 一种双冷却系统的双等温变换炉
CN112080305B (zh) * 2020-10-08 2021-06-15 杨松 废旧轮胎热解反应炉专用回转耙辊的制备方法
US11667728B1 (en) 2022-03-02 2023-06-06 David T. Camp Reactor and processes for endothermic reactions at high temperatures
CN114797736B (zh) * 2022-04-07 2023-04-11 西安交通大学 一种具有梯级保温功能的管流式水热和溶剂热合成反应器
CN115181590B (zh) * 2022-07-29 2023-06-13 重庆科技学院 一种分级解耦模式下的生物质双循环气化脱碳反应系统
CN114984863B (zh) * 2022-08-04 2022-11-08 江苏铧德氢能源科技有限公司 制氢装置中重整反应室反应物料的进料机构

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2507293A (en) * 1947-01-22 1950-05-09 Clayton Manufacturing Co Water tube coil steam generating apparatus
US3357916A (en) * 1965-06-25 1967-12-12 Mobil Oil Corp Catalytic reactor for the conversion of hydrocarbons employing high space velocities
US3976129A (en) * 1972-08-17 1976-08-24 Silver Marcus M Spiral concentric-tube heat exchanger
DE3631365A1 (de) * 1986-09-15 1988-03-24 Steinmueller Gmbh L & C Reformer fuer die katalytische spaltung gasfoermiger kohlenwasserstoffe mit wasserdampf
US4737161A (en) * 1987-01-27 1988-04-12 International Fuel Cells Corporation Compact hydrogen generator
GB9225188D0 (en) * 1992-12-02 1993-01-20 Rolls Royce & Ass Combined reformer and shift reactor
US6126908A (en) * 1996-08-26 2000-10-03 Arthur D. Little, Inc. Method and apparatus for converting hydrocarbon fuel into hydrogen gas and carbon dioxide
US6245303B1 (en) * 1998-01-14 2001-06-12 Arthur D. Little, Inc. Reactor for producing hydrogen from hydrocarbon fuels
KR100209989B1 (ko) * 1996-12-23 1999-07-15 남창우 천연가스형 수소발생장치
CN1496589A (zh) * 2000-10-30 2004-05-12 用作燃料电池、重整炉或热电设备的多功能能量系统
US6713040B2 (en) * 2001-03-23 2004-03-30 Argonne National Laboratory Method for generating hydrogen for fuel cells
KR100423544B1 (ko) * 2001-04-23 2004-03-18 주식회사 경동도시가스 컴팩트형 수증기 개질장치
DE10144285A1 (de) * 2001-09-08 2003-03-27 Viessmann Werke Kg Apparat zur Erzeugung von Wasserstoff

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CN100574859C (zh) 2009-12-30
US20060045828A1 (en) 2006-03-02
CA2578622A1 (en) 2007-01-04
US7500999B2 (en) 2009-03-10
WO2007001350A3 (en) 2007-11-08
EP1804962A4 (en) 2012-08-29

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