FR3112537B1 - Dispositif et procédé de production hybride de dihydrogène de synthèse et/ou de méthane de synthèse - Google Patents

Dispositif et procédé de production hybride de dihydrogène de synthèse et/ou de méthane de synthèse Download PDF

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Publication number
FR3112537B1
FR3112537B1 FR2008307A FR2008307A FR3112537B1 FR 3112537 B1 FR3112537 B1 FR 3112537B1 FR 2008307 A FR2008307 A FR 2008307A FR 2008307 A FR2008307 A FR 2008307A FR 3112537 B1 FR3112537 B1 FR 3112537B1
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synthetic
dihydrogen
methane
reactor
configuration
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FR3112537A1 (fr
Inventor
Yilmaz Kara
Stéphane Fortin
Maxime Hervy
Jonathan Maistrello
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Engie SA
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Engie SA
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Priority to US18/005,607 priority Critical patent/US20230264950A1/en
Priority to AU2021308293A priority patent/AU2021308293A1/en
Priority to PCT/EP2021/069502 priority patent/WO2022013239A1/fr
Priority to EP21749522.5A priority patent/EP4182421A1/fr
Priority to CA3185723A priority patent/CA3185723A1/fr
Publication of FR3112537A1 publication Critical patent/FR3112537A1/fr
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Publication of FR3112537B1 publication Critical patent/FR3112537B1/fr
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C10K3/02—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment
    • C10K3/04—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment reducing the carbon monoxide content, e.g. water-gas shift [WGS]
    • 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1809—Controlling processes
    • 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • 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
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • C07C1/0405—Apparatus
    • C07C1/041—Reactors
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/08—Production of synthetic natural 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
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0405—Purification by membrane separation
    • 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
    • C01B2203/0415—Purification by absorption in liquids
    • 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
    • C01B2203/042—Purification by adsorption on solids
    • C01B2203/043—Regenerative adsorption process in two or more beds, one for adsorption, the other for regeneration
    • 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
    • C01B2203/046—Purification by cryogenic separation
    • 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
    • C01B2203/0465—Composition of the impurity
    • C01B2203/0475—Composition of the impurity the impurity being carbon dioxide
    • 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
    • C01B2203/062—Hydrocarbon production, e.g. Fischer-Tropsch process
    • 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
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
    • C07C2521/04—Alumina
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74—Iron group metals
    • C07C2523/755—Nickel
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/06—Heat exchange, direct or indirect
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/10—Recycling of a stream within the process or apparatus to reuse elsewhere therein
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/46—Compressors or pumps
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

TITRE DE L’INVENTION : DISPOSITIF ET PROCÉDÉ DE PRODUCTION HYBRIDE DE DIHYDROGÈNE DE SYNTHÈSE ET/OU DE MÉTHANE DE SYNTHÈSE Le dispositif (100) de production hybride de dihydrogène de synthèse et/ou de méthane de synthèse, comporte :- une entrée (105) pour un flux de gaz de synthèse (dit « syngas ») comportant au moins du CO et préférentiellement au moins du CO et du H2,- un réacteur (110) de conversion catalytique, configuré pour opérer selon l’une des deux configurations alternatives suivantes :- une première configuration, dans laquelle les conditions opératoires du réacteur favorisent la réalisation d’une réaction de Sabatier, de manière à produire un gaz de sortie comportant principalement du méthane, - une deuxième configuration, dans laquelle les conditions opératoires du réacteur favorisent la réalisation d’une réaction du gaz à l’eau, de manière à produire un gaz de sortie comportant principalement du dihydrogène,- une sortie (115) pour un flux de dihydrogène de synthèse et/ou de méthane de synthèse et- un système (120) de commande comportant un moyen (121) de sélection d’une configuration d’opération du réacteur et un moyen (122) d’émission d’une commande représentative de la configuration sélectionnée, le réacteur étant configuré pour opérer selon une configuration donnée en fonction de la commande émise par le moyen d’émission. Figure pour l’abrégé : Figure 1
FR2008307A 2020-07-14 2020-08-05 Dispositif et procédé de production hybride de dihydrogène de synthèse et/ou de méthane de synthèse Active FR3112537B1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
US18/005,607 US20230264950A1 (en) 2020-07-14 2021-07-13 Device and method for hybrid production of synthetic dihydrogen and/or synthetic methan
AU2021308293A AU2021308293A1 (en) 2020-07-14 2021-07-13 Device and method for hybrid production of synthetic dihydrogen and/or synthetic methane
PCT/EP2021/069502 WO2022013239A1 (fr) 2020-07-14 2021-07-13 Dispositif et procédé de production hybride de dihydrogène de synthèse et/ou de méthane de synthèse
EP21749522.5A EP4182421A1 (fr) 2020-07-14 2021-07-13 Dispositif et procédé de production hybride de dihydrogène de synthèse et/ou de méthane de synthèse
CA3185723A CA3185723A1 (fr) 2020-07-14 2021-07-13 Dispositif et procede de production hybride de dihydrogene de synthese et/ou de methane de synthese

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
WOPCT/2020/051265 2020-07-14
FR2020051265 2020-07-14

Publications (2)

Publication Number Publication Date
FR3112537A1 FR3112537A1 (fr) 2022-01-21
FR3112537B1 true FR3112537B1 (fr) 2023-03-31

Family

ID=72046928

Family Applications (2)

Application Number Title Priority Date Filing Date
FR2008307A Active FR3112537B1 (fr) 2020-07-14 2020-08-05 Dispositif et procédé de production hybride de dihydrogène de synthèse et/ou de méthane de synthèse
FR2104177A Pending FR3112538A1 (fr) 2020-07-14 2021-04-21 Dispositif et procédé de production hybride de dihydrogène de synthèse et/ou de méthane de synthèse

Family Applications After (1)

Application Number Title Priority Date Filing Date
FR2104177A Pending FR3112538A1 (fr) 2020-07-14 2021-04-21 Dispositif et procédé de production hybride de dihydrogène de synthèse et/ou de méthane de synthèse

Country Status (6)

Country Link
US (1) US20230264950A1 (fr)
EP (1) EP4182421A1 (fr)
AU (1) AU2021308293A1 (fr)
CA (1) CA3185723A1 (fr)
FR (2) FR3112537B1 (fr)
WO (1) WO2022013239A1 (fr)

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2662911A (en) 1948-10-01 1953-12-15 Metallgesellschaft Ag Temperature control in the catalytic hydrogenation of carbon monoxide
US2740803A (en) 1950-01-19 1956-04-03 Ruhrchemie Ag Catalytic hydrogenation of carbon monoxide with indirect heat exchange cooling
DE2651567A1 (de) 1976-11-12 1978-05-24 Didier Eng Verfahren und vorrichtung zum einstellen und konstanthalten der temperatur beim methanisieren
DE3007202A1 (de) 1980-02-26 1981-09-10 Linde Ag, 6200 Wiesbaden Methanol-reaktor
DE3217066A1 (de) 1982-05-06 1983-11-10 Linde Ag, 6200 Wiesbaden Reaktor zur durchfuehrung katalytischer reaktion
GB9723669D0 (en) 1997-11-07 1998-01-07 Univ Aberdeen Skin penetration enhancing components
EP1568674A1 (fr) 2004-02-12 2005-08-31 Paul Scherrer Institut Procédé de préparation de méthane
US7618558B2 (en) 2005-04-15 2009-11-17 Haldor Topsoe A/S Process for cleaning gases from gasification units
WO2009007061A1 (fr) 2007-07-10 2009-01-15 Paul Scherrer Institut Procédé destiné à produire un mélange gazeux riche en méthane à partir de gaz de synthèse contenant du soufre provenant d'une gazéification
AU2011302248B2 (en) * 2010-09-13 2016-07-07 Lummus Technology Llc Low temperature sulfur tolerant tar removal with concomitant synthesis gas conditioning
GB201119960D0 (en) 2011-11-18 2012-01-04 Johnson Matthey Plc Process
CN104152199B (zh) * 2014-08-19 2017-01-25 赛鼎工程有限公司 一种煤制合成气进行耐硫甲烷化制备天然气的工艺
FR3038909A1 (fr) * 2015-07-16 2017-01-20 Gdf Suez Dispositif et procede de production de methane de synthese
CN109071215A (zh) 2016-04-25 2018-12-21 托普索公司 生产富氢气体的方法
GB2556665A (en) 2016-10-14 2018-06-06 Linde Ag Methods for hydrogen production
DE102018113743A1 (de) 2018-06-08 2019-12-12 Thyssenkrupp Ag Verfahren und Vorrichtungen zur Durchführung einer Wassergas-Shift-Reaktion sowie die Verwendung mindestens zweier seriell oder parallel geschalteter Einheiten zur Niedertemperatur-CO-Konvertierung

Also Published As

Publication number Publication date
US20230264950A1 (en) 2023-08-24
AU2021308293A1 (en) 2023-02-09
FR3112537A1 (fr) 2022-01-21
EP4182421A1 (fr) 2023-05-24
FR3112538A1 (fr) 2022-01-21
CA3185723A1 (fr) 2022-01-20
WO2022013239A1 (fr) 2022-01-20

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