WO2005084771A2 - Kompaktdampfreformer - Google Patents
Kompaktdampfreformer Download PDFInfo
- Publication number
- WO2005084771A2 WO2005084771A2 PCT/EP2005/002194 EP2005002194W WO2005084771A2 WO 2005084771 A2 WO2005084771 A2 WO 2005084771A2 EP 2005002194 W EP2005002194 W EP 2005002194W WO 2005084771 A2 WO2005084771 A2 WO 2005084771A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- evaporator
- steam reformer
- reactor
- reformer according
- compact
- Prior art date
Links
Classifications
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- 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
-
- 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
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- 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
- B01J8/0403—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 the fluid flow within the beds being predominantly horizontal
- B01J8/0407—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 the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds
- B01J8/0415—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 the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds the beds being superimposed one above the other
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- 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
- B01J8/0446—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 the flow within the beds being predominantly vertical
- B01J8/0461—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 the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds
- B01J8/0469—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 the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds the beds being superimposed one above the other
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- 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
- B01J8/0492—Feeding reactive fluids
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- 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
- C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
- C01B3/24—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
- C01B3/26—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using catalysts
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- 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
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- 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
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/00044—Temperature measurement
- B01J2208/00061—Temperature measurement of the reactants
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- 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
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00132—Tubes
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- 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
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00141—Coils
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- 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
- B01J2208/00194—Tubes
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- 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
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- 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
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- 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
- B01J2208/00504—Controlling the temperature by means of a burner
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- 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
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- 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
- B01J2208/00539—Pressure
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- 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
- B01J2208/00716—Means for reactor start-up
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- 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
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Definitions
- the invention relates to a compact steam reformer and a method for steam reforming.
- Material flow for heating kept separate. This prevents the dilution of the hydrogen with the nitrogen in the combustion air during steam reforming.
- the compact steam reformer according to the invention has a reactor which is heated by a burner.
- a preheater with high heat recovery is assigned to the burner. This increases the efficiency of the reforming process.
- the reformer has a post-reactor which is set up to carry out a shift reaction, post-oxidation and / or methanation of the carbon monoxide components contained in the tube format.
- the post-reactor is in heat-exchanging connection with a tube evaporator, which keeps the temperature of the post-reactor controlled at a fixed level.
- the tube evaporator brings about an equalization of the temperature in the post-reactor both temporally and spatially.
- the material flow in the tube evaporator causes heat to be transported in the post-reactor so that it can quickly adapt to changes in load. This is especially true when the tube evaporator and the post-reactor work in cocurrent.
- the temperature of the post-reactor is determined within such narrow limits that the CO content can be reduced to values of less than 50 ppm. A catalytic aftertreatment, filtering or other aftertreatment of the process gas is therefore unnecessary.
- the gas generated by the compact steam reformer can be fed directly to hydrogen fuel cells.
- the temperature of the post-reactor can be achieved in the simplest way by regulating the vapor pressure.
- the steam pressure also defines the steam generator temperature for all operating states.
- the compact steam reformer can have a jet pump connected to the tube evaporator or another evaporator, which generates a fuel vapor of an emixed predetermined composition and feeds the reactor. This creates the basis for particularly easy control-related control of the compact steam reformer.
- the amount of steam generated is controlled, for example, by appropriately measuring a quantity of feed water.
- the amount of fuel supplied to the reformer for reforming does not have to be regulated separately, but is metered in by the jet pump.
- FIG. 1 shows a compact steam reformer with a connected fuel cell in a schematic illustration
- FIG. 2 shows the temperature profile of the process gases as a diagram
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020067018135A KR101202605B1 (ko) | 2004-03-06 | 2005-03-02 | 콤팩트형 증기 개질기 |
EP05732059A EP1732658B1 (de) | 2004-03-06 | 2005-03-02 | Kompaktdampfreformer |
JP2007502236A JP4857258B2 (ja) | 2004-03-06 | 2005-03-02 | コンパクト蒸気改質装置 |
CA2557265A CA2557265C (en) | 2004-03-06 | 2005-03-02 | Compact steam reformer |
US11/514,537 US7608120B2 (en) | 2004-03-06 | 2006-09-02 | Compact steam reformer with automatic load matching capability |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102004010910A DE102004010910B4 (de) | 2004-03-06 | 2004-03-06 | Kompaktdampfreformer |
DE102004010910.9 | 2004-03-06 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/514,537 Continuation-In-Part US7608120B2 (en) | 2004-03-06 | 2006-09-02 | Compact steam reformer with automatic load matching capability |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2005084771A2 true WO2005084771A2 (de) | 2005-09-15 |
WO2005084771A3 WO2005084771A3 (de) | 2005-12-01 |
Family
ID=34877449
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2005/002194 WO2005084771A2 (de) | 2004-03-06 | 2005-03-02 | Kompaktdampfreformer |
Country Status (8)
Country | Link |
---|---|
US (1) | US7608120B2 (de) |
EP (2) | EP1732658B1 (de) |
JP (1) | JP4857258B2 (de) |
KR (1) | KR101202605B1 (de) |
CN (1) | CN100556527C (de) |
CA (1) | CA2557265C (de) |
DE (1) | DE102004010910B4 (de) |
WO (1) | WO2005084771A2 (de) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1661854A1 (de) * | 2004-11-29 | 2006-05-31 | Samsung SDI Co., Ltd. | Reformer eines Brennstoffzellensystems |
EP1767265A2 (de) * | 2005-09-27 | 2007-03-28 | Samsung SDI Co., Ltd. | Reformierungsvorrichtung erhitzt mit einem Brenner |
WO2008040470A2 (de) * | 2006-10-05 | 2008-04-10 | Ws Reformer Gmbh | Brennstoffzellensystem |
EP1995516A1 (de) * | 2007-05-23 | 2008-11-26 | WS-Wärmeprozesstechnik GmbH | Rekuperatorbrenner mit abgeflachten Wärmetauscherrohren |
KR100923605B1 (ko) * | 2006-09-27 | 2009-10-23 | 가시오게산키 가부시키가이샤 | 반응장치 및 전자기기 |
WO2017162681A1 (de) * | 2016-03-23 | 2017-09-28 | Karlsruher Institut für Technologie | Reaktor zur herstellung von synthesegas |
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DE102006039039A1 (de) * | 2006-05-23 | 2007-11-29 | Zentrum für Brennstoffzellen-Technik GmbH | Verfahren zum Aufheizen einer Katalysatorstufe sowie Vorrichtung zum Durchführen des Verfahrens |
US8561598B2 (en) * | 2008-01-07 | 2013-10-22 | Mcalister Technologies, Llc | Method and system of thermochemical regeneration to provide oxygenated fuel, for example, with fuel-cooled fuel injectors |
US9188086B2 (en) | 2008-01-07 | 2015-11-17 | Mcalister Technologies, Llc | Coupled thermochemical reactors and engines, and associated systems and methods |
US8441361B2 (en) | 2010-02-13 | 2013-05-14 | Mcallister Technologies, Llc | Methods and apparatuses for detection of properties of fluid conveyance systems |
PL2519342T3 (pl) | 2009-12-30 | 2019-03-29 | Hysytech S.R.L. | Jednostka reakcji endotermicznej i urządzenie do reformingu parowego zawierające tę jednostkę reakcji |
US8318100B2 (en) * | 2010-02-13 | 2012-11-27 | Mcalister Technologies, Llc | Reactor vessels with pressure and heat transfer features for producing hydrogen-based fuels and structural elements, and associated systems and methods |
AU2011216244A1 (en) | 2010-02-13 | 2012-09-06 | Mcalister Technologies, Llc | Reactor vessels with transmissive surfaces for producing hydrogen-based fuels and structural elements, and associated systems and methods |
US9126831B2 (en) * | 2010-03-31 | 2015-09-08 | Council Of Scientific & Industrial Research | Hydrogen/syngas generator with sampling ports |
US8920732B2 (en) | 2011-02-15 | 2014-12-30 | Dcns | Systems and methods for actively controlling steam-to-carbon ratio in hydrogen-producing fuel processing systems |
DE102011013026A1 (de) | 2011-03-04 | 2012-09-06 | Dbi - Gastechnologisches Institut Ggmbh Freiberg | Verfahren und Anordnung zur Dampfreformierung kohlenwasserstoffhaltiger Gase |
US8911703B2 (en) | 2011-08-12 | 2014-12-16 | Mcalister Technologies, Llc | Reducing and/or harvesting drag energy from transport vehicles, including for chemical reactors, and associated systems and methods |
US8821602B2 (en) | 2011-08-12 | 2014-09-02 | Mcalister Technologies, Llc | Systems and methods for providing supplemental aqueous thermal energy |
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CN104226206A (zh) * | 2014-07-28 | 2014-12-24 | 河北新启元能源技术开发股份有限公司 | 一种利用有机溶剂冲洗反应器的降压差装置 |
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KR101866500B1 (ko) * | 2016-11-14 | 2018-07-04 | 한국에너지기술연구원 | 일산화탄소 제거부를 포함한 수소제조 반응기 |
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 |
US11480364B2 (en) * | 2017-11-28 | 2022-10-25 | Anderson Industries, Llc | Flameless heater system to generate heat and humidity |
US11026791B2 (en) | 2018-03-20 | 2021-06-08 | Medtronic Vascular, Inc. | Flexible canopy valve repair systems and methods of use |
US11285003B2 (en) | 2018-03-20 | 2022-03-29 | Medtronic Vascular, Inc. | Prolapse prevention device and methods of use thereof |
KR20220100351A (ko) | 2021-01-08 | 2022-07-15 | 엘지전자 주식회사 | 개질기 |
KR20220100350A (ko) | 2021-01-08 | 2022-07-15 | 엘지전자 주식회사 | 개질기 |
FR3129608A1 (fr) * | 2021-11-30 | 2023-06-02 | Naval Group | Structure de reformeur |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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WO1998008771A2 (en) * | 1996-08-26 | 1998-03-05 | Arthur D. Little, Inc. | Method and apparatus for converting hydrocarbon fuel into hydrogen gas and carbon dioxide |
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- 2005-03-02 EP EP09156079A patent/EP2070591A3/de not_active Withdrawn
- 2005-03-02 JP JP2007502236A patent/JP4857258B2/ja not_active Expired - Fee Related
- 2005-03-02 KR KR1020067018135A patent/KR101202605B1/ko active IP Right Grant
- 2005-03-02 CA CA2557265A patent/CA2557265C/en not_active Expired - Fee Related
- 2005-03-02 CN CNB2005800071843A patent/CN100556527C/zh not_active Expired - Fee Related
- 2005-03-02 WO PCT/EP2005/002194 patent/WO2005084771A2/de not_active Application Discontinuation
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2006
- 2006-09-02 US US11/514,537 patent/US7608120B2/en not_active Expired - Fee Related
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Cited By (18)
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EP1661854A1 (de) * | 2004-11-29 | 2006-05-31 | Samsung SDI Co., Ltd. | Reformer eines Brennstoffzellensystems |
US7687042B2 (en) | 2004-11-29 | 2010-03-30 | Samsung Sdi Co., Ltd | Reformer of fuel cell system |
US7662350B2 (en) | 2005-09-27 | 2010-02-16 | Samsung Sdi Co., Ltd. | Fuel reforming apparatus with first pipe ends closed onto second pipe |
EP1767265A2 (de) * | 2005-09-27 | 2007-03-28 | Samsung SDI Co., Ltd. | Reformierungsvorrichtung erhitzt mit einem Brenner |
EP1767265A3 (de) * | 2005-09-27 | 2007-07-25 | Samsung SDI Co., Ltd. | Reformierungsvorrichtung erhitzt mit einem Brenner |
US7981373B2 (en) | 2006-09-27 | 2011-07-19 | Casio Computer Co., Ltd. | Reaction device and electronic device |
KR100923605B1 (ko) * | 2006-09-27 | 2009-10-23 | 가시오게산키 가부시키가이샤 | 반응장치 및 전자기기 |
DE102006047493B4 (de) * | 2006-10-05 | 2010-01-07 | Ws Reformer Gmbh | Brennstoffzellensystem und Verfahren zur Erzeugung von Strom und Wärme aus flüssigen und gasförmigen Brennstoffen |
WO2008040470A3 (de) * | 2006-10-05 | 2008-05-29 | Ws Reformer Gmbh | Brennstoffzellensystem |
DE102006047493A1 (de) * | 2006-10-05 | 2008-04-10 | Ws Reformer Gmbh | Brennstoffzellensystem |
WO2008040470A2 (de) * | 2006-10-05 | 2008-04-10 | Ws Reformer Gmbh | Brennstoffzellensystem |
RU2443040C2 (ru) * | 2006-10-05 | 2012-02-20 | Вс Реформер Гмбх | Система топливных элементов |
KR101413388B1 (ko) * | 2006-10-05 | 2014-06-27 | 베에스 레포머 게엠베하 | 연료 전지 시스템 |
EP1995516A1 (de) * | 2007-05-23 | 2008-11-26 | WS-Wärmeprozesstechnik GmbH | Rekuperatorbrenner mit abgeflachten Wärmetauscherrohren |
WO2008141723A1 (de) * | 2007-05-23 | 2008-11-27 | Ws-Wärmeprozesstechnik Gmbh | Rekuperatorbrenner mit abgeflachten wärmetauscherrohren |
US8622736B2 (en) | 2007-05-23 | 2014-01-07 | Ws-Wärmeprozesstechnik Gmbh | Recuperator burner having flattened heat exchanger pipes |
WO2017162681A1 (de) * | 2016-03-23 | 2017-09-28 | Karlsruher Institut für Technologie | Reaktor zur herstellung von synthesegas |
US10888833B2 (en) | 2016-03-23 | 2021-01-12 | Karlsruher Institut Fuer Technologie | Reactor for producing synthesis gas |
Also Published As
Publication number | Publication date |
---|---|
JP4857258B2 (ja) | 2012-01-18 |
WO2005084771A3 (de) | 2005-12-01 |
EP1732658A2 (de) | 2006-12-20 |
EP2070591A2 (de) | 2009-06-17 |
KR101202605B1 (ko) | 2012-11-19 |
EP2070591A3 (de) | 2009-08-26 |
JP2007527842A (ja) | 2007-10-04 |
EP1732658B1 (de) | 2011-09-14 |
KR20070019986A (ko) | 2007-02-16 |
US7608120B2 (en) | 2009-10-27 |
US20070006529A1 (en) | 2007-01-11 |
CA2557265A1 (en) | 2005-09-15 |
CA2557265C (en) | 2012-10-30 |
CN1980732A (zh) | 2007-06-13 |
DE102004010910A1 (de) | 2005-09-22 |
DE102004010910B4 (de) | 2006-10-26 |
CN100556527C (zh) | 2009-11-04 |
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