WO2015055349A1 - Procédé/unité intégrée de stockage du co2 par conversion en un gaz naturel de synthèse - Google Patents

Procédé/unité intégrée de stockage du co2 par conversion en un gaz naturel de synthèse Download PDF

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Publication number
WO2015055349A1
WO2015055349A1 PCT/EP2014/068896 EP2014068896W WO2015055349A1 WO 2015055349 A1 WO2015055349 A1 WO 2015055349A1 EP 2014068896 W EP2014068896 W EP 2014068896W WO 2015055349 A1 WO2015055349 A1 WO 2015055349A1
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WO
WIPO (PCT)
Prior art keywords
electrolysis
industrial
plant
gas
methanation
Prior art date
Application number
PCT/EP2014/068896
Other languages
English (en)
Inventor
Tilman J. Schildhauer
Urs ELBER
Maarten Nachtegaal
Lorenz Gubler
Peter Jansohn
Original Assignee
Paul Scherrer Institut
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Paul Scherrer Institut filed Critical Paul Scherrer Institut
Publication of WO2015055349A1 publication Critical patent/WO2015055349A1/fr

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Classifications

    • 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
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C25B1/04—Hydrogen or oxygen by electrolysis of water
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456—Removing acid components
    • B01D53/1475—Removing carbon dioxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/62—Carbon oxides
    • 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
    • C10L2290/56—Specific details of the apparatus for preparation or upgrading of a fuel
    • C10L2290/562—Modular or modular elements containing apparatus
    • 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
    • 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
    • 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
    • Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Definitions

  • the present invention relates to a method and a plant for storing CO 2 stemming from an industrial process as synthetic or substitute natural gas.
  • post-combustion capture e.g. by amine scrubbing of the CO 2
  • oxyfuel-processes which lead to nitrogen-free flue gases. While the disadvantage of the scrubbing is the high energy demand for the scrubbing liquid regeneration, the oxyfuel concepts suffer from the high electricity demand for the air separation unit to deliver the pure oxygen.
  • this goal is achieved according to the present invention by a method for storing CO2 stemming from an industrial process as synthetic or substitute natural gas,
  • a plant for storing C02 stemming from an industrial process as synthetic or substitute natural gas comprising:
  • an industrial operation plant generating CO2 comprised in a flue gas; said industrial operation plant performing an industrial combustion or calcination process or a
  • a CO2 separating unit for separating a CO2 containing gas mixture from the flue gas
  • a methanation unit for converting the C02 containing gas mixture and the H2 by a methanation reaction to a methane rich gas which can be used as or upgraded to synthetic natural gas.
  • the present invention forms an integrated process to combine the four steps (combustion and/or calcination of cement; CO 2 separation; electrolysis to produce H 2 and O 2 ;
  • the industrial C02-source may be a cement plant.
  • the C0 2 -separation can be conducted in a scrubber unit and the heat of the methanation reaction can be at least partly used to regenerate a scrubbing liquid used in the scrubber unit.
  • the C0 2 -separation is conducted in a temperature swing adsorption reactor and the heat of the methanation reaction is at least partly used to regenerate the sorbents used in the temperature swing adsorption reactor.
  • Further suitable alternative may provide for an energy- efficient C0 2 -separation wherein the C02-separation may be conducted in a membrane or a pressure swing adsorber or in a chemical looping reactor.
  • the heat of the methanation reaction may be at least partly used to increase the efficiency of the water electrolysis .
  • the oxygen stream from the water electrolysis and/or the heat from the methanation reaction may be at least partly used in the industrial combustion or calcination process to increase the thermal efficiency and/or to increase the CO 2 partial pressure which facilitates CO 2 separation and/or to regenerate the chemical looping material.
  • a high pressure electrolysis may be applied, and the expansion of the hydrogen and/or oxygen from the electrolysis pressure down to the conditions in the combustion/calcination or the methanation unit is used to generate mechanical energy, which is used for gas compression (e.g. of the flue gas or the C02 rich gas stream) and/or for electricity production in terms of turbine expansion.
  • gas compression e.g. of the flue gas or the C02 rich gas stream
  • electricity production in terms of turbine expansion.
  • a continuous operation may be desirable.
  • hydrogen, oxygen, flue gas and/or CO2 may be stored in local storage devices to enable continuous operation of at least some unit operations.
  • hydrogen and/or CO2 may be separated in a gas up grading downstream of the methanation reaction and may be fed back to the methanation reaction.
  • Figure 1 schematically an overview of the synergetic effects of combining diverse industrial processes
  • Figure 2 schematically an alternative overview with respect to Figure 1.
  • Figure 1 shows an overview of the synergetic effects of the combination of an industrial combustion operation, water electrolysis, CO2 separation and methanation.
  • the CO2 from the combustion process here a cement kiln
  • the CO2 emission of the combustion process which drives the cement kiln is decreased.
  • Hydrogen from a water electrolysis run by cheap or excess electricity is also fed to the methanation unit. This will allow storing cheap or excess electricity.
  • the raw SNG produced in the methanation unit is upgraded and may be injected into the grid where it can be stored, transported, used as fuel (e.g. for CNG cars) or be utilised for electricity production at a different time or location (e.g. by combined cycle power plants or combined heat and power plants) .
  • the heat of the methanation reaction is used for the energy demanding regeneration of scrubbing liquids in case of a liquid scrubber based C02 separation or for the thermal regeneration of sorbents in case of applying temperature swing adsorption.
  • the heat of the methanation reaction can be used for heating up gases, increase the efficiency in the electrolysis or drying of fuels or other heat integration purposes.
  • the oxygen from the water electrolysis is fed to the
  • combustion process in this example the cement kiln and/or the preheater and/or the calciner
  • exhaust gas treatment step and/or into conditioning step for the feedstock fed to the combustion process.
  • the separation is accomplished by a chemical looping process (see Figure 2) .
  • at least part of the oxygen from the electrolysis will be fed to the regeneration of the sorbent (e.g. by calcination) to allow for a nearly nitrogen-free CO 2 stream.
  • the expansion of the hydrogen and oxygen from the electrolysis pressure down to the conditions in the combustion or the methanation unit may be used to generate mechanical energy, which could be used for either gas compression (e.g. of the flue gas or the C02) and/or for electricity production.
  • hydrogen, oxygen, flue gas and/or CO 2 could be stored in local storage devices (e.g. gas containers) to enable more continuous operation of at least some unit operations .
  • hydrogen and/or CO 2 could be fed in excess or be present in the outlet of the methanation unit (e.g. due to incomplete conversion) .
  • 3 ⁇ 4 and or CO 2 would be separated in the gas up grading and fed back to the
  • methanation unit Especially, running 3 ⁇ 4 in excess may help to overcome equilibrium limitations and may support catalyst stability in the methanation reactor.
  • the heat for the regeneration of scrubbing liquids could be taken from other heat sources within the process, e.g. the streams leaving the combustion step or calcination kiln.
  • any heat source within the process i.e. from the calcination, combustion and/or methanation unit, may be used to produce electricity.
  • depleted flue gas could be recycled to the combustion process or cement kiln to improve heat management.
  • part of or even the complete flue gas flow could be fed directly to the gas cleaning and methanation reactor.
  • the methanation unit could be of any reactor type, but
  • the catalyst in the methanation unit could contain any elements helpful for the desired reactions, especially Ni, Ru, Rh, Ir, Co, Mo and/or their oxides, sulphides etc.
  • sulphur resistant catalysts or catalysts allowing for regeneration may be applied. In this case, sulphur resistant catalyst supports may be helpful.
  • the sorbent in the chemical looping CO 2 separation may be chosen, modified or supplemented by suited materials such that besides the C0 2 ⁇ separation, further gas cleaning is accomplished, e.g. desulphurisation or separation of metals, chlorine, nitrogen compounds etc.

Abstract

L'objectif de la présente invention consiste à fournir un procédé et une unité pour l'exploitation la plus efficace d'une opération industrielle, en stockant de ce fait le CO2 généré par cette opération industrielle de telle sorte que des procédés ultérieurs tirent avantage de l'énergie stockée dans le CO2 séparé de l'opération industrielle (où le CO2 peut être soumis à une conversion en un autre produit, tel que le GNS). Cet objectif est atteint selon la présente invention par un procédé et une unité pour le stockage du CO2 provenant d'un processus industriel sous forme d'un gaz naturel de synthèse ou de substitution, comprenant : a) une unité d'exploitation industrielle produisant du CO2 compris dans un gaz de carneau ; ladite unité d'opération industrielle réalisant un processus industriel de combustion ou de calcination ou un processus métallurgique ; b) une unité de séparation du CO2 pour séparer un mélange gazeux contenant du CO2 du gaz de carneau ; c) une unité d'électrolyse pour dissocier l'eau par électrolyse pour produire du H2 et du O2 ; d) une unité de méthanation pour convertir le mélange gazeux contenant du CO2 et le H2 par une réaction de méthanation pour donner un gaz riche en méthane qui peut être utilisé en l'état, ou valorisé en gaz naturel de synthèse. En conséquence, la présente invention forme un processus intégré pour combiner les quatre étapes (combustion et/ou calcination du ciment ; séparation du CO2 ; électrolyse pour produire du H2 et du O2 ; méthanation) d'une manière synergique pour résoudre les deux problèmes décrits ci-dessus avec une efficacité significativement plus élevée que ce qui est possible dans des unités non intégrées.
PCT/EP2014/068896 2013-10-16 2014-09-05 Procédé/unité intégrée de stockage du co2 par conversion en un gaz naturel de synthèse WO2015055349A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP13188902 2013-10-16
EP13188902.4 2013-10-16

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Publication Number Publication Date
WO2015055349A1 true WO2015055349A1 (fr) 2015-04-23

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Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105647608A (zh) * 2016-01-12 2016-06-08 东华大学 一种沼气脱硫干燥贮存一体式装置
CN105695013A (zh) * 2016-01-20 2016-06-22 中国海洋石油总公司 一种利用过剩电制替代天然气的方法
EP3156519A1 (fr) * 2015-10-16 2017-04-19 Volkswagen Aktiengesellschaft Procédé et appareil de production d'un hydrocarbure
DE102016208938A1 (de) * 2015-10-16 2017-04-20 Volkswagen Aktiengesellschaft Verfahren und Anlage zur Erzeugung eines Kohlenwasserstoffs
EP3196177A1 (fr) 2016-01-21 2017-07-26 HeidelbergCement AG Hydrogene comme combustible dans la fabrication de ciment
EP3231779A1 (fr) 2016-04-15 2017-10-18 HeidelbergCement AG Procédé et installation de fabrication de ciment dans le mode d'oxycombustion
WO2018099709A1 (fr) 2016-11-29 2018-06-07 Climeworks Ag Procédés d'élimination de co2 de l'air atmosphérique ou d'un autre gaz contenant du co2 afin d'obtenir des réductions d'émissions de co2 ou des émissions de co2 négatives
CN112011377A (zh) * 2020-07-23 2020-12-01 桂林电子科技大学 一种用于含碳燃料的钙基化学链气化制备高热值合成气的系统及方法
WO2021246314A1 (fr) * 2020-06-04 2021-12-09 三菱マテリアル株式会社 Procédé d'utilisation de co2 dans des gaz de fumées de production de ciment, et système d'utilisation de co2
WO2021246318A1 (fr) * 2020-06-04 2021-12-09 三菱マテリアル株式会社 Procédé de production de méthane à partir de co2 dans un gaz d'échappement de production de ciment et appareil de méthanation
WO2021246315A1 (fr) * 2020-06-04 2021-12-09 三菱マテリアル株式会社 Procédé et système d'utilisation de co2 dans un gaz de fumées de production de ciment
WO2021246316A1 (fr) * 2020-06-04 2021-12-09 三菱マテリアル株式会社 Procédé de fabrication de substances de valeur à partir de gaz d'échappement de fabrication de ciment
WO2021246317A1 (fr) * 2020-06-04 2021-12-09 三菱マテリアル株式会社 Procédé de séparation et de récupération de co2 dans un gaz d'échappement de production de ciment, et dispositif de séparation et de récupération de co2
WO2021246319A1 (fr) * 2020-06-04 2021-12-09 三菱マテリアル株式会社 Procédé de production de ciment et système de production de ciment
JP2021187720A (ja) * 2020-06-04 2021-12-13 三菱マテリアル株式会社 セメント製造排ガス中のｃｏ２活用方法及びｃｏ２活用システム
JP2021187721A (ja) * 2020-06-04 2021-12-13 三菱マテリアル株式会社 セメント製造排ガス中のｃｏ２活用方法及びｃｏ２活用システム
JP2021191731A (ja) * 2020-06-05 2021-12-16 三菱マテリアル株式会社 セメント製造排ガス中のｃｏ２活用方法及びｃｏ２活用システム
JP2021191732A (ja) * 2020-06-05 2021-12-16 三菱マテリアル株式会社 セメント製造排ガスからの有価物製造方法
JP2021195270A (ja) * 2020-06-11 2021-12-27 三菱マテリアル株式会社 セメント製造排ガス中のｃｏ２分離回収方法及びｃｏ２分離回収装置
JP2021195318A (ja) * 2020-06-11 2021-12-27 三菱マテリアル株式会社 セメント製造排ガス中のｃｏ２からのメタン製造方法及びメタン化装置
JP2022000405A (ja) * 2020-06-19 2022-01-04 三菱マテリアル株式会社 セメント製造方法及びセメント製造システム
CN114522518A (zh) * 2022-01-26 2022-05-24 哈尔滨工业大学（深圳） 一种含碳循环利用的燃气电厂低成本减碳排放系统及方法
WO2023089373A1 (fr) * 2021-11-17 2023-05-25 Shahar Golan Technology Solutions Ltd Procédé, système et appareil de méthanation et de récupération
WO2024041863A1 (fr) * 2022-08-22 2024-02-29 Ecole Polytechnique Federale De Lausanne (Epfl) Système de traitement et de transport de gaz multiples

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EP3156519A1 (fr) * 2015-10-16 2017-04-19 Volkswagen Aktiengesellschaft Procédé et appareil de production d'un hydrocarbure
DE102016208938A1 (de) * 2015-10-16 2017-04-20 Volkswagen Aktiengesellschaft Verfahren und Anlage zur Erzeugung eines Kohlenwasserstoffs
CN105647608A (zh) * 2016-01-12 2016-06-08 东华大学 一种沼气脱硫干燥贮存一体式装置
CN105647608B (zh) * 2016-01-12 2018-10-23 东华大学 一种沼气脱硫干燥贮存一体式装置
CN105695013A (zh) * 2016-01-20 2016-06-22 中国海洋石油总公司 一种利用过剩电制替代天然气的方法
CN105695013B (zh) * 2016-01-20 2019-03-08 中国海洋石油集团有限公司 一种利用过剩电制替代天然气的方法
EP3196177A1 (fr) 2016-01-21 2017-07-26 HeidelbergCement AG Hydrogene comme combustible dans la fabrication de ciment
EP3231779A1 (fr) 2016-04-15 2017-10-18 HeidelbergCement AG Procédé et installation de fabrication de ciment dans le mode d'oxycombustion
WO2017178254A1 (fr) 2016-04-15 2017-10-19 Heidelbergcement Ag Procédé et usine servant à la fabrication de ciment en mode oxygaz
WO2018099709A1 (fr) 2016-11-29 2018-06-07 Climeworks Ag Procédés d'élimination de co2 de l'air atmosphérique ou d'un autre gaz contenant du co2 afin d'obtenir des réductions d'émissions de co2 ou des émissions de co2 négatives
US11712652B2 (en) 2016-11-29 2023-08-01 Climeworks Ag Methods for the removal of CO2 from atmospheric air or other CO2-containing gas in order to achieve CO2 emissions reductions or negative CO2 emissions
JP2021187720A (ja) * 2020-06-04 2021-12-13 三菱マテリアル株式会社 セメント製造排ガス中のｃｏ２活用方法及びｃｏ２活用システム
WO2021246314A1 (fr) * 2020-06-04 2021-12-09 三菱マテリアル株式会社 Procédé d'utilisation de co2 dans des gaz de fumées de production de ciment, et système d'utilisation de co2
WO2021246315A1 (fr) * 2020-06-04 2021-12-09 三菱マテリアル株式会社 Procédé et système d'utilisation de co2 dans un gaz de fumées de production de ciment
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JP7215462B2 (ja) 2020-06-04 2023-01-31 三菱マテリアル株式会社 セメント製造排ガス中のｃｏ２活用方法及びｃｏ２活用システム
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