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WO2019228809A1 - Centrale électrique comprenant un électrolysuer et synthèse de combustible - Google Patents

Centrale électrique comprenant un électrolysuer et synthèse de combustible Download PDF

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Publication number
WO2019228809A1
WO2019228809A1 PCT/EP2019/062459 EP2019062459W WO2019228809A1 WO 2019228809 A1 WO2019228809 A1 WO 2019228809A1 EP 2019062459 W EP2019062459 W EP 2019062459W WO 2019228809 A1 WO2019228809 A1 WO 2019228809A1
Authority
WO
WIPO (PCT)
Prior art keywords
power
electrolyzer
power plant
grid
turbine
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/EP2019/062459
Other languages
German (de)
English (en)
Inventor
Thomas ACHTER
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Siemens AG
Siemens Corp
Original Assignee
Siemens AG
Siemens Corp
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 Siemens AG, Siemens Corp filed Critical Siemens AG
Publication of WO2019228809A1 publication Critical patent/WO2019228809A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • 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
    • C25B15/02—Process control or regulation
    • 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
    • C25B3/00—Electrolytic production of organic compounds
    • C25B3/20—Processes
    • C25B3/25—Reduction
    • H—ELECTRICITY
    • H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
    • H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
    • H02J3/00—Circuit arrangements for AC mains or AC distribution networks
    • H02J3/28—Arrangements for balancing of the load in a network by storage of energy
    • H—ELECTRICITY
    • H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
    • H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
    • H02J3/00—Circuit arrangements for AC mains or AC distribution networks
    • H02J3/38—Arrangements for parallely feeding a single network by two or more generators, converters or transformers
    • H02J3/381—Dispersed generators
    • H—ELECTRICITY
    • H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
    • H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
    • H02J3/00—Circuit arrangements for AC mains or AC distribution networks
    • H02J3/38—Arrangements for parallely feeding a single network by two or more generators, converters or transformers
    • H02J3/46—Controlling of the sharing of output between the generators, converters, or transformers
    • G—PHYSICS
    • G06—COMPUTING OR CALCULATING; COUNTING
    • G06Q—INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR
    • G06Q50/00—Information and communication technology [ICT] specially adapted for implementation of business processes of specific business sectors, e.g. utilities or tourism
    • G06Q50/06—Energy or water supply
    • H—ELECTRICITY
    • H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
    • H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
    • H02J2300/00—Systems for supplying or distributing electric power characterised by decentralized, dispersed, or local generation
    • H02J2300/10—The dispersed energy generation being of fossil origin, e.g. diesel generators
    • H—ELECTRICITY
    • H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
    • H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
    • H02J2300/00—Systems for supplying or distributing electric power characterised by decentralized, dispersed, or local generation
    • H02J2300/20—The dispersed energy generation being of renewable origin
    • H—ELECTRICITY
    • H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
    • H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
    • H02J2300/00—Systems for supplying or distributing electric power characterised by decentralized, dispersed, or local generation
    • H02J2300/30—The power source being a fuel cell
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E70/00—Other energy conversion or management systems reducing GHG emissions
    • Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin
    • 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

  • thermal power plants which are supplied with fossil or biological fuel and emit C02 (hereinafter referred to as thermal power plants), are increasingly under political and legal pressure, emissions
  • C02 carbon dioxide
  • C02Capture wet-chemical scrubbing with an absorbent
  • Thermal power plants are preferably under near
  • thermal power plants which are used for heating purposes of apartments or industrial plants or as process steam in industry for certain
  • thermal processes is needed. This requires that a thermal power plant is run in a heat-controlled manner, which limits the ability to provide network services.
  • Secondary control power reserves are available, for example, by throttled steam valves, additional boiler firing or gas turbine overfire, which can be provided in the second to minute range. Within 10-20 minutes there are more for tertiary control
  • thermal power plants are operated on the grid and
  • the object of the invention is to provide a device and a
  • thermal power plants can be improved together with renewable energy generators in the same power grid of the kind that a higher grid stability exists. It is another object of the invention to avoid or reduce shutdown of volatile regenerative energy sources due to network congestion, so that harmful C02 emissions are reduced in the overall balance, and extends the life of thermal power plants and the
  • the power plant according to the invention according to claim 1 is used to generate electrical and / or thermal energy for
  • Infeed into a power and / or district heating network includes an incinerator for the combustion of a
  • Carbonaceous fuel whereby a C02-containing exhaust gas is produced, a separation device connected downstream of the incinerator for separating CO 2 from the exhaust gas, an electrolyzer for generating hydrogen H 2 and oxygen 0 from water, a synthesis device for
  • a control device is provided by which the electrical power consumption of the electrolyzer in dependence on
  • the invention is based on the consideration that by the electrolyzer an additional adjustable or adjustable load (electrical load) is connected to the power grid, through which the power grid can be stabilized by
  • the electrolyzer is used according to the invention for frequency support.
  • the invention recognizes that this is possible because an electrolyzer can provide load gradients of about 10% per second, and thus also for
  • Frequency support of the primary control can be used.
  • the invention combines a CO 2 separation device, an electrolyzer and a synthesis device of the type
  • a significant advantage of the invention is that the fossil-fired power plant no longer has to be shut down and taken off the grid, since even if the power plant does not have to feed power into the public grid, a minimum power for the electrolyser must be provided.
  • the minimum load of the power plant corresponds to the maximum power consumption of the electrolyzer in this operation.
  • the thermal power plant can be operated more often under full load, and thus efficient, and emitting lower emissions than under partial load. Since the thermal power plants are relieved by the invention and in particular of mains frequency control measures, operation is better under and thermal
  • control measures completely taken over by the electrolyser can also be the technical complexity of a
  • the C02 can either partially or almost completely from the flue gas of the power plant by the
  • the thermal power plant can contribute to the politically desired reduction of the C02 footprint.
  • a complete shutdown of fossil fueled power plants is not foreseeable for lack of storage capacity in the near future and the continued operation of these systems in low load without active power to the network with full power frequency control capability coupled coupled rotating mass offers great benefits for the network. This will lead to a significant increase in public acceptance, so that thermal power plants will also be seen as a reliable and necessary component of the energy mix.
  • Existing thermal power plants can thus continue to be operated by retrofitting and to rebuild the central power supply in the direction of a C02 neutral
  • the separated CO 2 is in the connected synthesis, or other suitable device, together with the
  • Hydrogen from the electrolyzer is processed to high purity methanol or other e-fuel.
  • the methanol or other e-fuel is sold as a product by the operator of the power plant.
  • Methanol e.g. is in demand by the chemical industry. Even fossil fuels can be replaced or
  • regenerative energy generator for frequency support can be kept coupled to the network.
  • the power plant which serves as C02 source, can also be a cogeneration plant.
  • Storage capacity is designed in seconds, and which is located between power grid and electrolyzer.
  • the battery additionally supports a requirement for the mains frequency control.
  • the battery may also serve to maintain a black start capability, rebuild a possible network crash, and provide very fast grid control requirements of less than one second.
  • the battery can
  • the battery is in particular an improvement of
  • the synthetic fuel is methanol. But it is also possible to produce other fuels, such as synthetic diesel or kerosene.
  • the power plant further comprises a turbo set with a Turbine and a generator, which are arranged on a common shaft, and a coupling, which is arranged in the shaft between turbine and generator. Through the coupling of the generator of the turbine can be decoupled.
  • Decoupling allows the generator to remain connected to the mains, even when the turbine is off. Due to the electrical connection to the network, a rotating mass is held in the network, which also serves as a frequency support.
  • the electrolyzer is followed by a compressor and a storage, so that hydrogen produced is compressed and temporarily stored.
  • the electrolyzer is followed by a compressor and a storage, so that hydrogen produced is compressed and temporarily stored.
  • Caching provides additional flexibility in the operation of the power plant.
  • Electrolyzer connects with the combustion device, so that produced in the electrolyzer oxygen in the
  • Combustion device is conductive.
  • the Verbrennungsvor direction is the combustion chamber of a gas turbine.
  • the generated oxygen which is largely pure, the combustion can be made cleaner and the gas turbine can be operated more efficiently, since less inert gas must be transported through the gas turbine. Because less or no nitrogen is passed through the gas turbine, which heats up strongly as a result of the combustion, the loss of hot exhaust gas through the chimney can be reduced.
  • Power plant for generating electrical and / or
  • thermal energy for feeding into a power and / or district heating network is in a combustion process
  • a C02-containing exhaust gas is formed in a C02 deposition process downstream of the combustion process, C02 separated from the exhaust gas, in an electrolysis process hydrogen and oxygen separated from water, and in a synthesis process from the C02 from the deposition process and the generated
  • Hydrogen from the electrolysis process produces a synthetic fuel.
  • a battery is further provided for storage capacity in the
  • Seconds is arranged, and which is arranged between power grid and electrolyzer, so that a requirement for the grid frequency control is additionally supported.
  • methanol is produced as a synthetic fuel.
  • a turbine set with a turbine and a generator is further provided, which are arranged on a common shaft, wherein by a coupling in the shaft between turbine and generator the generator is decoupled from the turbine.
  • the electrolyzer downstream of a compressor and a memory, so that generated hydrogen compressed and
  • FIG. 1 shows a power plant according to the invention with a thermal power plant, a C02
  • FIG. 3 shows diagrams for illustrating cases of
  • Figure 1 shows the power plant 1 according to the invention, comprising a combustion process 2, in which a
  • carbon-containing fuel is supplied, and in which a CO 2 -containing exhaust gas 3 is formed, a CO 2 separation device 4 for separating CO 2 from the exhaust gas 3, an electrolyzer 5 for generating hydrogen 12 and
  • the Synthesizer 6 is a device for e-fuel
  • the CO 2 -containing exhaust gas 3 is supplied to the CO 2 precipitation device 4.
  • the CO 2 separation device 4 leaves a partially or largely exempt from C02 exhaust gas 7, as well as separated CO 2 8.
  • the power plant 1 is connected to the
  • Power transmission network 11 connected.
  • regenerative power generators are connected to the power transmission network 11, e.g. Wind turbines 19 and photovoltaic power plants 20.
  • the electric power transmission network 11 has limited transmission capacity C, which results in excess power over production that wind or solar energy must be discarded.
  • a heat engine 9 By combustion of a carbonaceous fuel in the combustion process 2, a heat engine 9 is driven, which in turn drives a generator 10 Stromer generation.
  • the combustion process 2 may be a fired boiler that generates steam that is expanded in a steam turbine.
  • combustion process 2 may also be the combustion chamber of a gas turbine, wherein the fuel gas is expanded in the expansion part of the gas turbine.
  • the combustion process 2 can also be
  • Piston engine be burned in the fuel in cylinders.
  • the components combustion process 2
  • Heat engine 9 and generator 10 form a
  • Carbon-containing fuel is operated.
  • heat E e.g. in the form of steam from the thermal power plant D and sold as a product (e.g., district heating or process steam).
  • the generator 10 is connected to the power grid 11. Also connected to the mains 11 is the electrolyzer 5, which is powered by electricity. The electrolyzer 5 generates
  • Hydrogen 12 and oxygen 13 The hydrogen 12 from the electrolyzer 5 is taken together with the CO 2 8 from the Deposition device 4 passed into the synthesis device or other device for e-fuel production 6.
  • methanol 14 is generated from hydrogen 12 and CO 2 8.
  • the electrolyzer 5 is controlled by a control device R, which determines the electrical power consumption of
  • Electrolyzer 5 depending on one or more parameters controls.
  • a first parameter is the electrical power requirement of the power network 11.
  • the electrolyzer 5 is dependent on the power grid
  • the thermal power plant D does not have to be throttled in the line.
  • a second parameter is the requirement of
  • Electrolyzer 5 as an electrical load more or less
  • a third parameter is the power requirement of the optional existing district heating network.
  • the control device R controls the electrolyzer 5 depending on the amount of energy or steam taken, so that despite a possible, fluctuating energy extraction, the thermal power plant D can be operated at a constant power.
  • the control device R can take into account one of these parameters. It makes sense, however, all parameters are taken into account, which on the driving style of the thermal
  • Power plant D have influence.
  • the aim of the control is always to allow a constant as possible operation of the thermal power plant D.
  • Figure 2 shows a further development of the power plant according to the invention of Figure 1. This includes as well as Figure 1 a combustion process 2, a CO 2 separation device 4, an electrolyzer 5 and a
  • the synthesizer 6 in which the synthetic fuel is produced is a means for producing methanol 14.
  • Battery B is provided, which is designed for a storage capacity in the second range.
  • the battery B is disposed between the power grid 11 and 5 electrolyzer.
  • Battery B can thus make a request to the
  • Grid frequency control can be additionally supported.
  • the battery is preferably located in
  • the power plant D is no longer subjected to strong load fluctuations by avoiding strong temperature fluctuations
  • Electrolyzer in conjunction with the battery ensures full positive and negative controllability.
  • FIG. 2 shows a further embodiment of the invention with a coupling A in the shaft between turbine 9 and Generator 10, which together form a turbo set. Through the coupling of the generator of the turbine can be decoupled.
  • FIG. 2 also shows an embodiment in which
  • Electrolyzer 5 a compressor 17 and a hydrogen storage 18 are connected downstream. Furthermore, the C02
  • the compressors 15, 17 may be operated by an electric motor.
  • the compression of C02 and H2 can occur depending on the process requirements.
  • the design of the memory 16, 18 is to vote on the expected operating regime of the power plant 1 with respect to flow, heat or methanol or e-fuel guided driving style.
  • a connecting line is provided, which connects the electrolyzer 5 with the combustion device 2, so that in the electrolyzer 5 generated oxygen 13 can be conducted into the combustion device 2.
  • Figure 3 shows a diagram I) to IV) by the cases of operations of the control device R to be illustrated.
  • power P is plotted in percent% over time t.
  • the lines show the behavior of the power, measured at different points in the power grid 11.
  • the power 31 is equal to the amount of electricity requested by the power grid 11.
  • the performance 31 is the one demanded
  • the power plant 1 must compensate for the power 32 introduced by the regenerative energy sources 21, so that the power introduced in the power grid is equal to the demanded amount of electricity.
  • the power 33 is the output power of the power plant 1 and is composed of the power 35 of the generator 10, the power 34 of the electrolyzer 5 and the power 36 of the batteries B.
  • Electrolyser 5 absorbs active power in the range of seconds, e.g. 10 seconds
  • the electrolyser operates at full load with a negative power of 20%.
  • the manipulated variable becomes the battery Active power input and output, as well as the voltage, regulated in the millisecond range.
  • the control device R regulates the parameters voltage and active power to generator 10, electrolyzer 5 and battery B so that they to the setpoint at the connection of
  • the proportion of power 32 introduced into the grid by regenerative energy sources 21 is about 20% and the fraction of power 33 introduced by the fossil-fired power plant is about 80%.
  • the power plant runs at full load.
  • the power consumption of the electrolyzer 5 is controlled in this case by the control device to 20%.
  • the regulating device R regulates
  • the electrolyzer is designed at least for this load case. That is, the maximum
  • Load capacity 34 of the electrolyzer corresponds to at least the minimum load in which the fossil-fired power plant can be operated on the grid.
  • the power grid limited in capacity is not burdened and made possible by the amount of electricity from the power plant so that shutdowns of renewable sources such as wind and photovoltaic are avoided or largely reduced.
  • controllability of positive active power, negative active power, frequency (cos cp) and voltage consists of:
  • Electrolysers or shutdown of the heat engine (while the generator is decoupled mechanically via the clutch A remains electrically synchronously coupled to the mains and supports it by its inertia and voltage or power factor control.
  • the aforementioned measures 2 and 3 can be combined and run slower in time.
  • the primary, secondary and tertiary control of the power plant is also available when no active power is supplied to the power grid or even power is absorbed.
  • Restrictions of the power grid with regard to active power the power plant is operated in partial to full load operation with primary fuel.
  • the control device controls the
  • the operation of the electrolyzer at half load allows an active power jump of the power plant by 50% of the electrolysis power in the positive direction by relieve or allow in the negative direction by loading.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Power Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Inorganic Chemistry (AREA)
  • Automation & Control Theory (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

L'invention concerne une centrale électrique (1) servant à générer de l'énergie électrique et/ou thermique pour alimenter un réseau de production de curant (11) et/ou de chauffage urbain (E). Il comprend une installation de combustion (2) destinée à la combustion d'un combustible contenant du carbone de sorte qu'un effluent gazeux (3) contenant du CO2 est généré, un dispositif de séparation (4) monté en aval de l'installation de combustion (2) et destiné à séparer le CO2 de l'effluent gazeux, un électrolyseur (5) destiné à la production d'hydrogène (12) et d'oxygène (13) à partir de l'eau, un dispositif de synthèse (6) destiné à synthétiser un carburant de synthèse (14) à partir du CO2 séparé et de l'hydrogène (12) généré dans l'électrolyseur (5). Selon l'invention, il est prévu un dispositif de régulation (R) permettant de réguler la consommation électrique de l'électrolyseur (5) en fonction d'un besoin en énergie électrique du réseau électrique (11), d'une demande de régulation de fréquence de réseau et/ou d'un besoin énergétique du réseau de chauffage urbain (E).
PCT/EP2019/062459 2018-05-30 2019-05-15 Centrale électrique comprenant un électrolysuer et synthèse de combustible Ceased WO2019228809A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102018208561.7 2018-05-30
DE102018208561 2018-05-30

Publications (1)

Publication Number Publication Date
WO2019228809A1 true WO2019228809A1 (fr) 2019-12-05

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WO (1) WO2019228809A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112003309A (zh) * 2020-07-13 2020-11-27 上海发电设备成套设计研究院有限责任公司 一种电力调峰系统
WO2021156685A1 (fr) * 2020-01-10 2021-08-12 Exergo Sa Procédés et systèmes de transport de co2 de système énergétique collectif
EP4012884A1 (fr) * 2020-12-10 2022-06-15 Siemens Energy Global GmbH & Co. KG Procédé de fonctionnement d'une installation industrielle et installation industrielle
WO2024249094A1 (fr) * 2023-05-30 2024-12-05 Arcadia eFuels US Inc. Production d'hydrocarbures synthétiques

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013029701A1 (fr) * 2011-08-29 2013-03-07 Ostsee Maritime Gmbh Installation d'alimentation en énergie, destinée notamment au domaine des technologies domestiques
DE102012018031A1 (de) * 2011-10-19 2013-04-25 Georg Harzfeld Verfahren und Anordnung zur Vorhaltung und Bereitstellung von Regelleistung von elektrischen Stromnetzen
DE102014225063A1 (de) * 2014-12-05 2016-06-09 Siemens Aktiengesellschaft Kraftwerk
DE202009019105U1 (de) * 2008-12-18 2016-07-14 Silicon Fire Ag Anlage zum Bereitstellen eines Energieträgers unter Einsatz von Kohlenstoffdioxid als Kohlenstofflieferant und von elektrischer Energie

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE202009019105U1 (de) * 2008-12-18 2016-07-14 Silicon Fire Ag Anlage zum Bereitstellen eines Energieträgers unter Einsatz von Kohlenstoffdioxid als Kohlenstofflieferant und von elektrischer Energie
WO2013029701A1 (fr) * 2011-08-29 2013-03-07 Ostsee Maritime Gmbh Installation d'alimentation en énergie, destinée notamment au domaine des technologies domestiques
DE102012018031A1 (de) * 2011-10-19 2013-04-25 Georg Harzfeld Verfahren und Anordnung zur Vorhaltung und Bereitstellung von Regelleistung von elektrischen Stromnetzen
DE102014225063A1 (de) * 2014-12-05 2016-06-09 Siemens Aktiengesellschaft Kraftwerk

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021156685A1 (fr) * 2020-01-10 2021-08-12 Exergo Sa Procédés et systèmes de transport de co2 de système énergétique collectif
US20230039702A1 (en) * 2020-01-10 2023-02-09 Exergo Sa Methods and Systems for District Energy CO2 Support
US11965659B2 (en) 2020-01-10 2024-04-23 Exergo Sa Methods and systems for district energy CO2 support
CN112003309A (zh) * 2020-07-13 2020-11-27 上海发电设备成套设计研究院有限责任公司 一种电力调峰系统
CN112003309B (zh) * 2020-07-13 2021-12-10 上海发电设备成套设计研究院有限责任公司 一种电力调峰系统
EP4012884A1 (fr) * 2020-12-10 2022-06-15 Siemens Energy Global GmbH & Co. KG Procédé de fonctionnement d'une installation industrielle et installation industrielle
WO2022122371A1 (fr) * 2020-12-10 2022-06-16 Siemens Energy Global GmbH & Co. KG Procédé de fonctionnement d'une installation industrielle et installation industrielle
WO2024249094A1 (fr) * 2023-05-30 2024-12-05 Arcadia eFuels US Inc. Production d'hydrocarbures synthétiques

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