DE102008020407A1 - Equipment for producing hydrogen rich gas, comprises burner for activating required heating process from fuel gas and air, reformation reactor, in which overheated reactants are converted into hydrogen-rich product gas - Google Patents
Equipment for producing hydrogen rich gas, comprises burner for activating required heating process from fuel gas and air, reformation reactor, in which overheated reactants are converted into hydrogen-rich product gas Download PDFInfo
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- DE102008020407A1 DE102008020407A1 DE102008020407A DE102008020407A DE102008020407A1 DE 102008020407 A1 DE102008020407 A1 DE 102008020407A1 DE 102008020407 A DE102008020407 A DE 102008020407A DE 102008020407 A DE102008020407 A DE 102008020407A DE 102008020407 A1 DE102008020407 A1 DE 102008020407A1
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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
-
- 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
- B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
- B01J12/007—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
-
- 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
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- 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
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00117—Controlling the temperature by indirect heating or cooling employing heat exchange fluids 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/0015—Controlling the temperature by thermal insulation means
- B01J2219/00155—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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00157—Controlling the temperature by means of a burner
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00159—Controlling the temperature 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
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
-
- 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
- C01B2203/06—Integration with other chemical processes
- C01B2203/066—Integration with other chemical processes with fuel cells
-
- 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
- C01B2203/0816—Heating by flames
-
- 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
- C01B2203/0872—Methods of cooling
- C01B2203/0888—Methods of cooling by evaporation of a fluid
-
- 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
- C01B2203/0872—Methods of cooling
- C01B2203/0888—Methods of cooling by evaporation of a fluid
- C01B2203/0894—Generation of steam
-
- 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
- C01B2203/1217—Alcohols
- C01B2203/1223—Methanol
-
- 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
- C01B2203/1217—Alcohols
- C01B2203/1229—Ethanol
-
- 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
-
- 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
- C01B2203/1205—Composition of the feed
- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
- C01B2203/1235—Hydrocarbons
- C01B2203/1247—Higher hydrocarbons
-
- 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
- C01B2203/1276—Mixing of different feed components
-
- 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
- C01B2203/1288—Evaporation of one or more of the different feed components
- C01B2203/1294—Evaporation by heat exchange with hot process stream
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
Abstract
Description
Gegenstand
der Erfindung ist eine Apparatur zur Erzeugung eines wasserstoffreichen
Gases im Bereich kleiner und mittlerer Leistung nach dem Verfahren
der Dampfreformierung von gasförmigen Kohlenwasserstoffen,
bestehend aus einem Brenner (
Beschreibungdescription
Zur Erzeugung von Wasserstoff aus kohlenwasserstoffhaltigen Gasen wird im großtechnischen Maßstab hauptsächlich das Verfahren der Dampfreformierung genutzt. Insbesondere durch die Entwicklungsaktivitäten auf dem Gebiet der Brennstoffzellentechnik entstand ein Bedarf an kompakten Dampfreformern für den kleinen und mittleren Leistungsbereich (1–50 kW). Als Eduktgas für solche Reformer kommen z. B. Erdgas, Biogase oder Propan zur Anwendung. Auch flüssige Brennstoffe wie Benzin, Heizöl, Ethanol oder Methanol können genutzt werden, wobei eine Apparatur zur Aufbereitung und Verdampfung dieser Brennstoffe vorgeschaltet werden muss.to Generation of hydrogen from hydrocarbon-containing gases is on an industrial scale mainly used the process of steam reforming. In particular by the development activities in the field of fuel cell technology A demand for compact steam reformers for the small and medium power range (1-50 kW). As educt gas for such reformers come z. As natural gas, biogas or propane for use. Also liquid fuels like gasoline, fuel oil, Ethanol or methanol can be used, with a Apparatus for treatment and evaporation of these fuels upstream must become.
Zur
Erklärung der Vorgänge bei der Dampfreformierung
wird im Folgenden beispielhaft die Dampfreformierung von Methan
kurz beschrieben. Im Reformierreaktor (
Soll
das entstandene wasserstoffreiche Reformat z. B. in einer PEM-Brennstoffzelle
genutzt werden, muss das CO nahezu vollständig entfernt werden,
da es die PEM-Brennstoffzelle schädigen würde.
Dazu werden Gasreinigungsstufen nachgeschaltet, in denen die CO-Konvertierung üblicherweise
nach der Wassergas-Shift-Reaktion abläuft:
Als Gasfeinreinigung werden die Selektive Oxidation oder die Methanisierung eingesetzt, um CO nahezu vollständig aus dem Prozessgas zu entfernen. Das erzeugte Reformat wird bei einer Nutzung in Brennstoffzellen mit einem gewissen Überschuss der Anodenseite der Brennstoffzelle zugeführt, während die Kathodenseite der Brennstoffzelle mit Luft versorgt wird. Bei der Brennstoffzellenreaktion reagiert Wasserstoff mit Luftsauerstoff zu Wasser. Dabei wird Strom und Wärme erzeugt. Das Anodenabgas enthält verfahrensbedingt noch einen Anteil an Wasserstoff und Methan.When Fine gas cleaning becomes Selective Oxidation or Methanation used to CO almost completely from the process gas to remove. The generated reformate is when used in fuel cells with a certain excess of the anode side of the fuel cell fed while the cathode side of the fuel cell with Air is supplied. Hydrogen reacts in the fuel cell reaction with atmospheric oxygen to water. This is electricity and heat generated. The anode exhaust gas still contains due to the process a share of hydrogen and methane.
Das
für die Reformierreaktion benötigte Prozesswasser
wird mit einem gewissen Überschuss dem Prozess zugeführt
und muss verdampft und mit dem Eduktgas gemischt dem Reformierreaktor
zugeführt werden. Die für die Reformierreaktion
und die Verdampfung benötigte Enthalpie wird meist durch einen
externen Brenner erzeugt. Wird eine solche Apparatur in ein Brennstoffzellenheizgerät
integriert, ist es vorteilhaft für den Gesamtwirkungsgrad,
wenn dieser Brenner auch mit dem wasserstoffhaltigen Anodenabgas
aus der Brennstoffzelle betrieben wird, wobei als benötigte
Verbrennungsluft das Kathodenabgas genutzt werden kann (z. B.
Die konstruktive Gestaltung von Brennraum, Abgasweg, Reformierreaktor und Verdampfer bestimmt den thermodynamischen Wirkungsgrad des Gesamtsystems, wobei eine möglichst hohe Wärmeübertragung und möglichst geringe Wärmeverluste erreicht werden müssen.The constructive design of combustion chamber, exhaust path, reforming reactor and evaporator determines the thermodynamic efficiency of the overall system, with the highest possible heat transfer and lowest possible heat losses can be achieved have to.
Bisherige
Lösungen für Kompaktreformer sind meist konzentrisch
ausgeführt und beinhalten eine relativ komplizierte Abgasführung
(z. B.
Verfahrensgemäß besitzt
das Produktgas (Reformat) am Austritt des Reformierreaktors eine hohe
Temperatur (600–800°C) und muss bis zum Eintritt
in nachfolgende Gasreinigungsstufen (CO-Konvertierung, Wassergas-Shift-Reaktion)
auf Temperaturen von 250–350°C abgekühlt
werden. Außerdem muss das Prozesswasser verdampft und gemeinsam
mit dem Eduktgas dem Reformierreaktor möglichst überhitzt
zugeführt werden. Daher bietet es sich an, in einem Wärmeübertrager
die Überhitzung der Edukte (
Hierfür
sind bereits Lösungen vorgeschlagen worden, wobei entweder
komplizierte Wärmeübertrager das Abkühlen
des Reformats durch Wärmeübertragung auf das Eduktgemisch
erreichen oder das Brennerabgas durch Rohre zu einem separaten außenliegenden
Verdampfer geleitet wird, wodurch Wärmeverluste entstehen
können (z. B.
Die
vorliegende Erfindung sieht in einer ersten Ausgestaltung vor, den
Abgasweg (
Um
die Enthalpie des Reformats (
Die
gesamte Anordnung kann vorteilhaft mit einer Wärmedämmung
(
Zur
Nutzung des Brennwerteffektes kann in einer weiteren Ausgestaltung
der Erfindung ein Abgaswärmeübertrager (
Die
vorliegende Erfindung wird in Zeichnungen näher erläutert.
In
Bauteile:
- 1
- Brenner
- 2
- Reformierreaktor
- 3
- Verdampfer
- 4
- Konditionierer
- 5
- Abgaswärmeübertrager zur Nutzung des Brennwerteffektes
- 6
- Abgasanschluss an der Apparatur
- 7
- Wärmedämmung
- 8
- Gehäuse
- 9
- Verbraucher
- 1
- burner
- 2
- reforming
- 3
- Evaporator
- 4
- conditioner
- 5
- Exhaust gas heat exchanger for using the condensing effect
- 6
- Exhaust connection to the apparatus
- 7
- thermal insulation
- 8th
- casing
- 9
- consumer
Medienströme:
- 10
- Brenngaszuführung
- 11
- Brenngas zum Brenner
- 12
- Brennraum, Abgas
- 13
- Abgasweg, Abgas
- 20
- Brenngas/Eduktgas zum Reformer
- 21
- Prozesswasser
- 22
- Eduktgas-Wasserdampf-Gemisch (Eduktgemisch)
- 23
- Reformat/Produktgas
- 24
- abgekühltes Reformat/Übergang zur Gasreinigung
- 30
- Anodenabgas aus der Brennstoffzelle (wasserstoffhaltiges Gas)
- 31
- Kathodenabgas aus der Brennstoffzelle (sauerstoffarme Luft)
- 40
- Heizungswasser/Heizkreis
- 10
- Fuel gas supply
- 11
- Fuel gas to the burner
- 12
- Combustion chamber, exhaust gas
- 13
- Exhaust path, exhaust
- 20
- Fuel gas / educt gas to the reformer
- 21
- process water
- 22
- Feedstock-water vapor mixture (educt mixture)
- 23
- Reformat / product gas
- 24
- cooled reformate / transition to gas purification
- 30
- Anode exhaust from the fuel cell (hydrogen-containing gas)
- 31
- Cathode exhaust gas from the fuel cell (oxygen-poor air)
- 40
- Heating water / heating circuit
ZITATE ENTHALTEN IN DER BESCHREIBUNGQUOTES INCLUDE IN THE DESCRIPTION
Diese Liste der vom Anmelder aufgeführten Dokumente wurde automatisiert erzeugt und ist ausschließlich zur besseren Information des Lesers aufgenommen. Die Liste ist nicht Bestandteil der deutschen Patent- bzw. Gebrauchsmusteranmeldung. Das DPMA übernimmt keinerlei Haftung für etwaige Fehler oder Auslassungen.This list The documents listed by the applicant have been automated generated and is solely for better information recorded by the reader. The list is not part of the German Patent or utility model application. The DPMA takes over no liability for any errors or omissions.
Zitierte PatentliteraturCited patent literature
- - DE 10136970 C2 [0006] - DE 10136970 C2 [0006]
- - DE 19721630 C1 [0008] - DE 19721630 C1 [0008]
- - DE 1021135464 [0008] - DE 1021135464 [0008]
- - DE 1014299964 [0010] - DE 1014299964 [0010]
- - DE 10211354 B4 [0010] - DE 10211354 B4 [0010]
Claims (12)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102008020407A DE102008020407A1 (en) | 2007-11-03 | 2008-04-24 | Equipment for producing hydrogen rich gas, comprises burner for activating required heating process from fuel gas and air, reformation reactor, in which overheated reactants are converted into hydrogen-rich product gas |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE202007015296 | 2007-11-03 | ||
DE202007015296.5 | 2007-11-03 | ||
DE102008020407A DE102008020407A1 (en) | 2007-11-03 | 2008-04-24 | Equipment for producing hydrogen rich gas, comprises burner for activating required heating process from fuel gas and air, reformation reactor, in which overheated reactants are converted into hydrogen-rich product gas |
Publications (1)
Publication Number | Publication Date |
---|---|
DE102008020407A1 true DE102008020407A1 (en) | 2009-05-07 |
Family
ID=40514511
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE102008020407A Withdrawn DE102008020407A1 (en) | 2007-11-03 | 2008-04-24 | Equipment for producing hydrogen rich gas, comprises burner for activating required heating process from fuel gas and air, reformation reactor, in which overheated reactants are converted into hydrogen-rich product gas |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE102008020407A1 (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19721630C1 (en) | 1997-05-23 | 1999-02-11 | Fraunhofer Ges Forschung | Device for reforming hydrocarbons containing starting materials |
DE10136970C2 (en) | 2001-07-28 | 2003-11-27 | Ballard Power Systems | Device for generating hydrogen-containing gas for a fuel cell system |
DE10142999B4 (en) | 2001-09-03 | 2006-07-06 | Zentrum für Brennstoffzellen Technik ZBT Duisburg GmbH | Highly efficient, compact reformer unit for hydrogen production from gaseous hydrocarbons in the small power range |
DE10211354B4 (en) | 2001-03-15 | 2006-11-16 | Aisin Seiki K.K., Kariya | fuel reformer |
-
2008
- 2008-04-24 DE DE102008020407A patent/DE102008020407A1/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19721630C1 (en) | 1997-05-23 | 1999-02-11 | Fraunhofer Ges Forschung | Device for reforming hydrocarbons containing starting materials |
DE10211354B4 (en) | 2001-03-15 | 2006-11-16 | Aisin Seiki K.K., Kariya | fuel reformer |
DE10136970C2 (en) | 2001-07-28 | 2003-11-27 | Ballard Power Systems | Device for generating hydrogen-containing gas for a fuel cell system |
DE10142999B4 (en) | 2001-09-03 | 2006-07-06 | Zentrum für Brennstoffzellen Technik ZBT Duisburg GmbH | Highly efficient, compact reformer unit for hydrogen production from gaseous hydrocarbons in the small power range |
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