WO2014053217A1 - Anlage und verfahren zur herstellung von synthesegas - Google Patents
Anlage und verfahren zur herstellung von synthesegas Download PDFInfo
- Publication number
- WO2014053217A1 WO2014053217A1 PCT/EP2013/002810 EP2013002810W WO2014053217A1 WO 2014053217 A1 WO2014053217 A1 WO 2014053217A1 EP 2013002810 W EP2013002810 W EP 2013002810W WO 2014053217 A1 WO2014053217 A1 WO 2014053217A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- feed stream
- combustion chamber
- reformer tube
- reformer
- cooling
- Prior art date
Links
Classifications
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
- B01J2219/00054—Controlling or regulating the heat exchange system
- B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
- B01J2219/00058—Temperature measurement
- B01J2219/00063—Temperature measurement of the reactants
-
- 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
- B01J2219/00121—Controlling the temperature by direct heating or cooling
- B01J2219/00123—Controlling the temperature by direct heating or cooling adding a temperature modifying medium to the reactants
-
- 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
- B01J2219/00164—Controlling or regulating processes controlling the flow
-
- 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
- B01J2219/24—Stationary reactors without moving elements inside
-
- 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
- C01B2203/08—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
- C01B2203/08—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
- C01B2203/0877—Methods of cooling by direct injection of 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
- C01B2203/1235—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
- C01B2203/1276—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
- C01B2203/16—Controlling the process
- C01B2203/1614—Controlling the temperature
- C01B2203/1619—Measuring the temperature
-
- 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
- C01B2203/16—Controlling the process
- C01B2203/169—Controlling the feed
Definitions
- the invention relates to a process for the production of synthesis gas from a
- Devices of the aforementioned kind can e.g. for generating synthesis gas, have a steam reformer which has a combustion chamber through which at least one reformer tube runs. In the combustion chamber is the for the
- Synthesis gas generation generates heat by burning a fuel at an upper end of the combustion chamber.
- Reformerrohr a feed stream (feed) comprising hydrocarbons and water vapor is introduced and with the help of a in the at least one
- the feed stream Depending on the composition of the feed stream, the feed stream must have a certain temperature in order to obtain as complete a conversion of the feedstock stream as possible to synthesis gas.
- the feed stream is adjusted to an appropriate inlet temperature before entering the at least one reformer tube.
- To set the desired inlet temperature of the feed stream is divided into a to be cooled and a non-cooling partial flow.
- the partial flow to be cooled Feed stream is passed through one or more heat exchangers ("trim coolers") in which the partial stream of the feed stream to be cooled transfers its heat indirectly to a cooling medium and then with the non-cooled partial stream of the feed stream, not by the at least a matching cooler was passed, merged again.
- the combined feed stream is then passed through a heat exchanger ("Superheater” to German: superheater), which is arranged in the combustion chamber of the furnace of the steam reformer.
- a control eg feedback loop
- the temperature sensor at the inlet of the reformer tube can be variably adjusted by means of controllable valves to be cooled and not to be cooled partial flow of the feed stream, so that adjusts the desired inlet temperature of the feed stream at the inlet of the at least one reformer tube.
- the present invention seeks to provide a relatively inexpensive method of the generic type and a relatively inexpensive means for performing the method.
- the stated object is procedurally achieved according to the invention that the feed stream for cooling the feed stream before being introduced into the reformer tube with H 2 0 is mixed.
- a pressurization of the feed stream with liquid H 2 0 is provided for cooling the feed stream before its introduction into the reformer tube.
- said water can be introduced in particular via at least one nozzle in the feedstream.
- the injected for cooling H 2 0 has a good quality
- Cation exchanger is present, which is smaller than 1 ⁇ / ⁇ , O ⁇ S / cm or 0.2 pS / cm. It is preferably provided that the feed stream is introduced via at least one arranged in the combustion chamber of the furnace heat exchanger for preheating the feed stream into the at least one reformer tube, wherein the feed stream is preferably mixed for cooling the feed stream upstream of the heat exchanger with said water, in particular outside the combustion chamber or outside the furnace.
- an actual temperature of the feed stream is measured prior to its entry into the reformer tube and compared with a predefinable setpoint temperature, wherein when the actual temperature exceeds the setpoint temperature, the feed stream H 2 0 is mixed to equalize the actual temperature to the set temperature.
- liquid introduced H 2 0 is preferably included in the balance, so that the reformer with the minimum possible
- Hydrocarbon can be operated.
- the injected amount of water is preferably measured and / or calculated and during mixing of the feed gas from water vapor and
- the temperature-controlled plant according to the method mentioned here in an optimal ratio of steam (liquid H 2 0 plus H 2 0 in the feed stream) are operated to gas.
- the invention relates to a device for the production of synthesis gas with:
- an oven having a combustion chamber, a reformer tube arranged in the combustion chamber for receiving a feedstock stream comprising hydrocarbon and water vapor,
- the object is the device side inventively achieved in that the device comprises a means which is adapted to H 2 0 for cooling the feed stream into the pipeline for feeding the
- a means is provided which is adapted to initiate water for cooling the feed stream in the pipeline or with the
- the pipeline has a first and an associated second section, wherein the first section of the pipeline extends at least partially outside the combustion chamber or the furnace and is connected to at least one heat exchanger arranged in the combustion chamber, so that an in can be performed by the at least one heat exchanger and thereby can be heated by indirect heat transfer (eg against a cooled other stream), and wherein the second section of the pipe also at least partially outside the combustion chamber or the furnace and the heat exchanger connects with the at least one reformer tube, so that the correspondingly heated feed stream can be fed into the at least one reformer tube.
- the combustion chamber of the furnace - with respect to a
- the at least one reformer tube extends along the vertical from the upper region of the combustion chamber into the lower one Down the region of the combustion chamber and has at the top of an inlet for feeding the feed stream in the reformer tube.
- the means for cooling the feed stream is preferably at least partially disposed in the first section of the pipeline, preferably in an area of the first section of the furnace outside of the furnace
- This first section preferably has a length which, under the given conditions, allows the H 2 O introduced into the pipeline to be completely vaporized before entering the heat exchanger (and before entering the reformer).
- the first section of the pipeline can be kept as short as possible, and e.g. a length of 0.2x steam velocity (the
- Feedstock stream in meters.
- the means for cooling the feed stream is preferably connected to a feed line through which water used for cooling can be supplied to said means.
- the supply line further comprises a valve, which is designed to set an amount of water to be supplied to the agent per unit of time.
- the system further comprises a control unit for opening or
- Fuel flow cooperates, and is adapted to the valve so control (ie to open or close) that the actual temperature to the predefinable setpoint temperature cools or possibly heated.
- Fig. 1 is a schematic representation of a device according to the invention for the production of synthesis gas.
- FIG. 1 shows a device 5 for producing a synthesis gas, by means of a steam reformer 2, which has at least one reformer tube 1 arranged in a combustion chamber I of a furnace 3, into which a feed stream E, consisting of at least one hydrocarbon, by means of a pipeline 6 and
- the combustion chamber I has an upper region I ', at the upper end thereof e.g. Heat is generated by means of at least one burner by burning a fuel, wherein that upper portion I 'extends longitudinally along the vertical Z, and a lower portion connected thereto I ", which transversely to the vertical Z from the upper region ⁇ , so that the combustion chamber in particular has an L-shaped profile.
- the at least one reformer tube 1 extends - in relation to an intended (ready) state of the device 5 along the vertical Z from the upper region ⁇ of the combustion chamber I down to the lower region I "of the combustion chamber I.
- the feed stream E is now fed from an upper side of the furnace 3 forth through an inlet 8 in the at least one reformer tube 1 and passed through it and thereby arranged with the aid of a in the at least one reformer tube 1
- Catalyst converted into synthesis gas Before it is fed into the at least one reformer tube 1, the feedstock stream E is regulated to a specific temperature.
- a means 7 for cooling the feed stream E and at least one heat exchanger 4 for heating the feed stream E provided, which is arranged in the lower region I "of the combustion chamber I, which comes from the upper region ⁇ of the combustion chamber I.
- the means 7 for cooling is preferably in a first portion 6a of
- Piping 6 is arranged, which is partially outside the furnace 3 and the combustion chamber I is located.
- the means 7 for cooling the feed stream E is arranged on a first section of the pipeline 6a which lies outside the furnace 3 or the combustion chamber I.
- the water for cooling is introduced via a supply line 9 in the means 7.
- the amount of water added to the feed stream E per unit time by the means for cooling 7 is preferably regulated via a controllable valve 10 of the feed line 9 which is upstream of the means 7 for cooling. Downstream of the means 7 for cooling the feed stream E, the first section 6a of the pipe 6 opens into the lower section I "
- Combustion chamber I of the furnace 3 provided heat exchanger 4, in which the feed stream E is heated.
- a second section 6b of the pipeline 6 connects the heat exchanger 4 to the inlet 8 for feeding the heated feed stream E into the reformer tube 1.
- the second section 6b of the pipeline 6 extends in sections outside the furnace 3 or the combustion chamber I.
- a control unit 1 1 is provided, which cooperates with a temperature sensor 12, which is located on an outside of the furnace 3 and the combustion chamber I lying region of the second
- Section 6b of the pipe 6 is arranged, and to form the current temperature of the feed stream E (at this point) to detect (actual temperature) and pass it on to the control unit 1 1, which is adapted and intended to open the valve 10 or close, so that the actual temperature can be equalized to a predefinable setpoint temperature of the feed stream E.
- the instantaneous mass flow of the liquid H 2 0 is measured prior to injection into the first section 6 a of the pipeline 6 to the injected H 2 0 during mixing of the feed stream E. to take into account.
- Feed stream E can be set exactly to the respectively desired, opimal hydrocarbon / steam ratio (in accordance with the stoichiometry of the respective reaction equation), preference being given to using water in excess
- this ratio is therefore preferably greater than 1, in particular greater than 1.8, in particular 2.0, in particular 2.3, in particular 2.8.
- I combustion chamber (interior furnace)
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (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)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU2015116168A RU2015116168A (ru) | 2012-10-02 | 2013-09-18 | Установка и способ получения синтез-газа |
US14/431,333 US20150251907A1 (en) | 2012-10-02 | 2013-09-18 | Plant and process for producing synthesis gas |
CA2884410A CA2884410A1 (en) | 2012-10-02 | 2013-09-18 | Installation and method for producing synthesis gas |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102012019382.3A DE102012019382A1 (de) | 2012-10-02 | 2012-10-02 | Anlage und Verfahren zur Herstellung von Synthesegas |
DE102012019382.3 | 2012-10-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2014053217A1 true WO2014053217A1 (de) | 2014-04-10 |
Family
ID=49231419
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2013/002810 WO2014053217A1 (de) | 2012-10-02 | 2013-09-18 | Anlage und verfahren zur herstellung von synthesegas |
Country Status (5)
Country | Link |
---|---|
US (1) | US20150251907A1 (de) |
CA (1) | CA2884410A1 (de) |
DE (1) | DE102012019382A1 (de) |
RU (1) | RU2015116168A (de) |
WO (1) | WO2014053217A1 (de) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2671634B1 (de) * | 2012-06-08 | 2017-08-09 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Verfahren zur Homogenisierung der Rohrtemperaturen zwischen Rohren während Verfahren zur Erwärmung von in den Rohren strömendem Gas |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0200825A1 (de) * | 1985-05-08 | 1986-11-12 | Exxon Research And Engineering Company | Verfahren zur Dampfreformierung von Kohlenwasserstoff mit in Reihe angeordneten Überhitzern |
CA1321711C (en) * | 1988-03-24 | 1993-08-31 | Warwick John Lywood | Hydrogen |
EP1403215A1 (de) * | 2002-09-26 | 2004-03-31 | Haldor Topsoe A/S | Verfahren und Vorrichtung zur Herstellung von Synthesegas |
WO2010086635A1 (en) * | 2009-01-30 | 2010-08-05 | Johnson Matthey Plc | Hydrogen process |
US20100264373A1 (en) * | 2009-04-15 | 2010-10-21 | Air Products And Chemicals, Inc. | Process for producing a hydrogen-containing product gas |
-
2012
- 2012-10-02 DE DE102012019382.3A patent/DE102012019382A1/de not_active Withdrawn
-
2013
- 2013-09-18 CA CA2884410A patent/CA2884410A1/en not_active Abandoned
- 2013-09-18 WO PCT/EP2013/002810 patent/WO2014053217A1/de active Application Filing
- 2013-09-18 US US14/431,333 patent/US20150251907A1/en not_active Abandoned
- 2013-09-18 RU RU2015116168A patent/RU2015116168A/ru not_active Application Discontinuation
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0200825A1 (de) * | 1985-05-08 | 1986-11-12 | Exxon Research And Engineering Company | Verfahren zur Dampfreformierung von Kohlenwasserstoff mit in Reihe angeordneten Überhitzern |
CA1321711C (en) * | 1988-03-24 | 1993-08-31 | Warwick John Lywood | Hydrogen |
EP1403215A1 (de) * | 2002-09-26 | 2004-03-31 | Haldor Topsoe A/S | Verfahren und Vorrichtung zur Herstellung von Synthesegas |
WO2010086635A1 (en) * | 2009-01-30 | 2010-08-05 | Johnson Matthey Plc | Hydrogen process |
US20100264373A1 (en) * | 2009-04-15 | 2010-10-21 | Air Products And Chemicals, Inc. | Process for producing a hydrogen-containing product gas |
Also Published As
Publication number | Publication date |
---|---|
US20150251907A1 (en) | 2015-09-10 |
RU2015116168A (ru) | 2016-11-27 |
CA2884410A1 (en) | 2014-04-10 |
DE102012019382A1 (de) | 2014-04-03 |
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