WO2020200370A1 - Éolienne comprenant un collecteur de co2 et procédé de fonctionnement ou de commande de collecteur de co2 d'éolienne - Google Patents

Éolienne comprenant un collecteur de co2 et procédé de fonctionnement ou de commande de collecteur de co2 d'éolienne Download PDF

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Publication number
WO2020200370A1
WO2020200370A1 PCT/DE2020/100276 DE2020100276W WO2020200370A1 WO 2020200370 A1 WO2020200370 A1 WO 2020200370A1 DE 2020100276 W DE2020100276 W DE 2020100276W WO 2020200370 A1 WO2020200370 A1 WO 2020200370A1
Authority
WO
WIPO (PCT)
Prior art keywords
collector
heat
carbon dioxide
dioxide recovery
recovery device
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/DE2020/100276
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German (de)
English (en)
Inventor
Jörg Spitzner
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.)
Clean Energy One GmbH
Original Assignee
Clean Energy One GmbH
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 Clean Energy One GmbH filed Critical Clean Energy One GmbH
Publication of WO2020200370A1 publication Critical patent/WO2020200370A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03D—WIND MOTORS
    • F03D9/00—Adaptations of wind motors for special use; Combinations of wind motors with apparatus driven thereby; Wind motors specially adapted for installation in particular locations
    • F03D9/10—Combinations of wind motors with apparatus storing energy
    • F03D9/19—Combinations of wind motors with apparatus storing energy storing chemical energy, e.g. using electrolysis
    • 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
    • B01D53/02—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 adsorption, e.g. preparative gas chromatography
    • B01D53/04—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 adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • 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
    • B01D53/1425—Regeneration of liquid absorbents
    • 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
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/50—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon dioxide with hydrogen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03D—WIND MOTORS
    • F03D80/00—Details, components or accessories not provided for in groups F03D1/00 - F03D17/00
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/50—Carbon oxides
    • B01D2257/504—Carbon dioxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/06—Polluted air
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/65—Employing advanced heat integration, e.g. Pinch technology
    • B01D2259/655—Employing advanced heat integration, e.g. Pinch technology using heat storage materials
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05B—INDEXING SCHEME RELATING TO WIND, SPRING, WEIGHT, INERTIA OR LIKE MOTORS, TO MACHINES OR ENGINES FOR LIQUIDS COVERED BY SUBCLASSES F03B, F03D AND F03G
    • F05B2220/00—Application
    • F05B2220/60—Application making use of surplus or waste energy
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05B—INDEXING SCHEME RELATING TO WIND, SPRING, WEIGHT, INERTIA OR LIKE MOTORS, TO MACHINES OR ENGINES FOR LIQUIDS COVERED BY SUBCLASSES F03B, F03D AND F03G
    • F05B2220/00—Application
    • F05B2220/61—Application for hydrogen and/or oxygen production
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05B—INDEXING SCHEME RELATING TO WIND, SPRING, WEIGHT, INERTIA OR LIKE MOTORS, TO MACHINES OR ENGINES FOR LIQUIDS COVERED BY SUBCLASSES F03B, F03D AND F03G
    • F05B2260/00—Function
    • F05B2260/20—Heat transfer, e.g. cooling
    • 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
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2
    • 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
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/70—Wind energy
    • Y02E10/72—Wind turbines with rotation axis in wind direction
    • 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

Definitions

  • the invention relates generally to the field of renewable energy generation by means of wind turbines, both in the onshore and offshore areas, and additionally to the area of C02 outside air filtration and C02 collection, namely the area of
  • the invention relates to a wind turbine with a CO 2 collector with a machine house with a generator and electrical components, the generator and the electrical components producing heat in the form of waste heat for operational reasons and a thermally regenerable carbon dioxide recovery device
  • Adsorption collector is formed.
  • the invention also relates to a wind turbine - C02 collector - control /
  • DE 10 2017 125 415 B8 discloses a wind power plant with a CO2 collector, in particular with a fanless outside air intake device for drawing in the outside air into the wind power plant, an outside air duct for guiding the outside air drawn in through the wind power plant or at least through parts of the wind power plant up to the wind power plant rotor blades , wherein air outlets for blowing out the sucked in and guided outside air are provided in the wind turbine rotor blades and a
  • Carbon dioxide separation and / or recovery / collection device / C02 collector for carbon dioxide separation and / or recovery from the outside air with fanless air supply, the outside air being sucked in and guided through the
  • Carbon dioxide separation and / or recovery / collecting device / C02 collector is guided by means of an air duct and is guided out of the air outlets of the rotor blades, with a suction effect caused by the rotation of the wind turbine rotor blades an air flow is caused when blowing out and this ultimately causes the air flow of the outside air. Furthermore, a wind energy installation - C02 collector - control / operating method with a corresponding wind energy installation with C02
  • Wind turbine system components namely a central hub at which the two or three, currently there are essentially three, wind turbine rotor blades are combined to form a central assembly, a nacelle, which is also referred to as a nacelle, in which the mechanical drive train, namely the machine train , which includes the rotating parts such as hub, rotor shaft, possibly gearbox and corresponding bearings and seals, and furthermore the generator arranged thereon belongs to it. All of these components, in particular the electrical components, the generator and any transmission upstream of the generator generate operational heat, also referred to in this disclosure as waste heat, which has to be dissipated in some way, with corresponding heat being generated for this purpose.
  • the environment-emitting heat exchangers or cooling devices or ventilation systems for air conditioning the machine house or the nacelle have been identified as a solution and are known in the prior art.
  • Sea air which means that the wind turbine generators are at great risk of corrosion, has become more or less standard, including the use of seawater-resistant materials, the improvement of corrosion protection, the complete encapsulation of certain assemblies and the use of machine houses and towers equipped with outside air intake devices, which in turn the problem of cooling the inside of the
  • Wind turbine components are further tightened.
  • the related problem of the prior art can essentially be represented in such a way that the operationally produced heat and the waste heat without any further Use must be released into the environment, since any intermediate storage or even use would be pointless due to a lack of consumers. This release to the environment must take place, otherwise these components would be damaged if they were not cooled.
  • the object of the present invention is to use the operationally generated heat sensibly in such a way that it is not simply given off into the environment and, at the same time, synergies are created or created for both the wind turbine itself and for the CO2 collectors , whereby overall the aspects of durability,
  • Energy sources is obtained and at the same time at least C02 is filtered from the air and at least collected.
  • the essential aspect here should be the maximum CO2 yield, taking into account the energy efficiency of the entire system.
  • the wind energy installation which is equipped with a CO 2 collector, has as essential components a machine house with a generator and electrical components, the generator and the electrical components producing operationally heat in the form of waste heat, and furthermore a thermally regenerable one
  • Carbon dioxide separation and / or C02 recovery from the ambient air the carbon dioxide recovery device / the C02 collector being designed as an adsorption collector with regeneration phases and / or as a cycle-guided adsorption collector.
  • Such a wind turbine is characterized by the features essential to the invention, namely that:
  • a regeneration heat exchanger device is provided in and / or on and / or in the area of the carbon dioxide recovery device / the C02 collector
  • Heat transfer liquid are provided between the waste heat heat exchanger device and the regeneration heat exchanger device, a feed pump being provided in which circulates the heat transfer medium and / or the heat transfer liquid in a circuit between the heat exchangers,
  • the extracted operationally generated waste heat can be transported via the heat transport lines to the regeneration heat exchanger device and by means of the
  • the carbon dioxide recovery device / the C02 collector have ventilators operated with regeneratively generated electrical energy for supplying air.
  • Wind turbine on the one hand can be brought out and on the other hand useful and
  • a highly efficient regeneration of the C02 collector can be carried out, which in the prior art would otherwise have had to be regenerated with resource-wasting effort or by means of waste heat from external systems that do not belong to the wind turbine, for example through heat generated specially for the regeneration process.
  • the additional energy required for the regeneration is therefore dispensed with and the waste heat from the generator and from the machine house of the wind energy installation is also removed and used.
  • the wind energy installation with the CO 2 collector as such is operated energetically and with a synergetic effect without the need for further additional external energy, for example from a downstream synthesis installation.
  • the C02 yield is maximized, since it was recognized for the C02 collectors overall that the energy requirement for the regeneration process is higher than the energy requirement for the additional one Supply of air to the CO2 collector.
  • the wind power plant can also be designed in such a way that an electrical storage device is provided for the electrical energy generated regeneratively by the wind energy plant, this electrical storage device being able to continue to operate the fans operated with regeneratively generated electrical energy in times of power shortage, and alternatively or alternatively also complementary to the previous one
  • Design variant can be a thermal and / or chemical storage for the
  • Intermediate storage of the waste heat can be provided, whereby the operationally generated waste heat can be temporarily stored in the heat accumulator and can be used for regeneration with a time delay, so that even in times of calm wind, the C02 collectors can continue to flow with air through the correspondingly arranged fans and, in particular, can be regenerated , for example if the electrical components or the generator are none
  • Potassium carbonate at approx. 80 ° C or, in the case of an amine, at approx. 100 ° C, whereby this is fed to the wind turbine through the waste heat. If necessary, by means of
  • a corresponding temperature can be achieved than the temperature of the waste heat, but these are also in the range of 80 ° C to 100 ° C.
  • the generator of the wind energy installation can technically also be equipped with a higher Temperature can be controlled in order to be able to withdraw a higher amount of heat from the generator or to reach higher temperatures, e.g. up to 105 ° C.
  • the carbon dioxide recovery device / the C02 collector can be formed from at least two individually controllable units, the operating mode of which can be controlled individually, namely “C02 collection” and “regeneration”, so that at least one unit is run in collector mode while the other Unit is either being operated in collector mode or is being regenerated, which means that a
  • a supplementary transmission waste heat heat exchanger device for extracting operationally generated waste heat from the transmission in and / or on a transmission assigned to the generator can be provided to increase the amount of heat, at least if the system has a transmission that is connected upstream of the generator , whereby this can be controlled in parallel or as required in addition or as an alternative to the generator heat exchanger device.
  • a storage arrangement and / or a storage system can be used at the CO 2 withdrawal of the carbon dioxide recovery device / the CO 2 collector
  • a reprocessing device for C02 can be provided, which either stores or forwards the C02 or at least processes it further, with C02 and H20 being too synthetic, in particular in a particularly preferred embodiment variant
  • methane / gaseous and / or liquid hydrocarbons can be processed in a methane or Fischer-Tropsch synthesis or other suitable hydrocarbon synthesis, whereby ultimately liquid and / or gaseous fuels are artificially produced and these can be transported away via existing transport routes, such as the natural gas network or corresponding pipelines or tank trucks.
  • Hydrocarbon synthesis can also be used in addition, but by no means necessarily, any waste heat to regenerate the adsorber material, although it is very likely that not every wind energy installation in a wind farm has a corresponding one
  • Synthesis arrangement will be provided, but a central synthesis arrangement could preferably be provided which, with appropriate supply lines, processes the CO 2 collected in the many wind turbines of a wind park into liquid and / or gaseous fuels.
  • excess regeneratively generated electrical energy from the wind power plant can be used at times to operate the synthesis processes of hydrocarbon synthesis or any associated water electrolysis.
  • Synthesis processors can be operated with regenerative energy, which can be provided by the wind turbines.
  • the carbon dioxide recovery device / the C02 collector can be used as an adsorption collector with regeneration phases and / or as
  • this C02 collector could be on the
  • carbon dioxide recovery devices or C02 collectors can be arranged horizontally or vertically.
  • a vertically arranged column could be mounted outside or inside of the tower with appropriate air supply by fans operated with regeneratively generated electrical energy, so that a long adsorber path is realized.
  • the tower of a wind power installation is therefore suitable, since this structure also withstands corresponding loads from the weight.
  • the air duct can in particular be arranged at least in partial areas of the tower and / or the foundation area so that, depending on the design or arrangement of the CO 2 collector, a corresponding air supply is ensured by the fans operated with regeneratively generated electrical energy.
  • the air duct can also be implemented in large parts via pipes, for example via plastic pipes, or the fans operated with regeneratively generated electrical energy are arranged directly in front of the adsorber sections.
  • the C02 can be used in the production of synthetically produced fuels or for fertilization, fertilizers for agriculture and food production, or the like, such as mineral water production, packaging of meat products (preservation), production of dry ice or the production of plastics.
  • the ambient air is quasi-C02-filtered and the C02 is thus extracted.
  • the collector filters are saturated with C02 via an adsorption-desorption process, which can in particular be a catalytic process.
  • Heat (approx. 100 ° C) is required for desorption, which is supplied by supplying the waste heat by means of the heat transfer fluid.
  • the C02 is dissolved in gaseous form from the filter and transported away and collected or further processed.
  • a central C02 collection point is particularly useful, with this being fed via a pipeline system.
  • Wind turbine with C02 collector has the essential steps, namely:
  • Waste heat is carried out, whereby released C02 is collected and / or
  • a method that synergistically combines the CO 2 collection with the optimized generation of electricity by means of a wind energy installation or the operation of a wind energy installation.
  • Unused operational heat from the electrical components or the generator, or waste heat for short, as well as any other operationally generated supplementary or additional optional heat from any other system components such as gear or electronics can now be used from the machine house for the regeneration of the C02 collectors and does not have to be via additionally provided in the prior art
  • Ventilation and / or air conditioning systems or heat exchangers are senselessly discharged to the environment or are not generated specifically for regeneration by means of electrical heating using electricity. Complex ventilation of the machine house, especially the
  • Generators can be omitted, whereby the valuable operational waste heat is used for regeneration at the same time. It is, as it were, a synergetic process for operating a wind turbine in combination with a C02 collector.
  • controllable units is formed, with at least one unit being operated in the "C02 collecting” operating mode and at least one unit being operated at least temporarily in the "Regenerating” operating mode, or alternatively the units are continuously and simultaneously C02 collecting and thermally regenerated, with a The cycle process of the C02 collector desorbent is driven.
  • the waste heat in normal operation can be stored internally at least in certain times and / or immediately or offset in time
  • Ambient air can penetrate into the nacelle.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Power Engineering (AREA)
  • Electrochemistry (AREA)
  • Organic Chemistry (AREA)
  • Wind Motors (AREA)

Abstract

L'invention concerne une éolienne comprenant un collecteur de CO2 comprenant une construction de machine comprenant un générateur et des composants électriques, le générateur et les composants électrique produisant en raison du fonctionnement de la chaleur sous forme de chaleur perdue, et un dispositif de récupération de dioxyde de carbone / un collecteur de CO2 thermiquement régénérable pour la séparation de dioxyde de carbone et/ou la récupération de CO2 à partir de l'air ambiant, le dispositif de récupération de dioxyde de carbone / le collecteur de CO2 étant conçu comme collecteur par adsorption présentant des phases de régénération et/ou comme collecteur par adsorption dans un circuit, un dispositif d'échange thermique de chaleur perdue étant prévu pour l'extraction de chaleur générée en raison du fonctionnement dans et/ou au niveau des composants électriques et/ou dans et/ou au niveau du générateur et/ou dans la zone du générateur, et un dispositif d'échange thermique de régénération étant prévu dans le et/ou sur le et/ou dans la zone du dispositif de récupération de dioxyde de carbone / collecteur de CO2 et des conduites de transport thermique comprenant un moyen de transport thermique ou un liquide de transport thermique étant prévues entre le dispositif d'échange thermique de chaleur perdue et le dispositif d'échange thermique de régénération, une pompe d'alimentation étant prévue, qui fait circuler le moyen de transport thermique et/ou le liquide de transport thermique dans un circuit entre les échangeurs de chaleur, la chaleur perdue générée en raison du fonctionnement extraite pouvant être transportée au dispositif d'échange thermique de régénération par les conduites de transport thermique et la régénération thermique / désorption de CO2 du dispositif de récupération de dioxyde de carbone / du collecteur de CO2 peut être exploitée au moyen de la chaleur perdue générée en raison du fonctionnement et le dispositif de récupération de dioxyde de carbone / le collecteur de CO2 présentant des ventilateurs fonctionnant avec de l'énergie électrique régénérée produite pour l'alimentation en air. L'invention concerne en outre un procédé de fonctionnement / commande de collecteur de CO2 d'éolienne comprenant une éolienne comprenant un collecteur de CO2.
PCT/DE2020/100276 2019-04-05 2020-04-02 Éolienne comprenant un collecteur de co2 et procédé de fonctionnement ou de commande de collecteur de co2 d'éolienne Ceased WO2020200370A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102019108991.3A DE102019108991A1 (de) 2019-04-05 2019-04-05 Windenergieanlage mit CO2 Sammler und Windenergieanlagen-CO2-Sammler-Steuerungs- bzw. Betriebsverfahren
DE102019108991.3 2019-04-05

Publications (1)

Publication Number Publication Date
WO2020200370A1 true WO2020200370A1 (fr) 2020-10-08

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PCT/DE2020/100276 Ceased WO2020200370A1 (fr) 2019-04-05 2020-04-02 Éolienne comprenant un collecteur de co2 et procédé de fonctionnement ou de commande de collecteur de co2 d'éolienne

Country Status (2)

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DE (1) DE102019108991A1 (fr)
WO (1) WO2020200370A1 (fr)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7992409B1 (en) * 2010-07-21 2011-08-09 Willard Cooper Cryogenic process for separation of carbon dioxide from the atmosphere using a superconducting wind turbine
WO2016161998A1 (fr) * 2015-04-08 2016-10-13 Sunfire Gmbh Procédé et installation de production de méthane/d'hydrocarbures gazeux et/ou liquides
DE102017125415B8 (de) 2017-10-30 2018-10-25 clean energy one gmbh Windenergieanlage mit CO2 Sammler und Windenergieanlagen-CO2-Sammler-Steuerungs- bzw. Betriebsverfahren

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102006035893A1 (de) * 2006-07-31 2008-02-07 Wolf, Bodo M., Dr. Verfahren zur Wiederaufarbeitung von Verbrennungsprodukten fossiler Brennstoffe

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7992409B1 (en) * 2010-07-21 2011-08-09 Willard Cooper Cryogenic process for separation of carbon dioxide from the atmosphere using a superconducting wind turbine
WO2016161998A1 (fr) * 2015-04-08 2016-10-13 Sunfire Gmbh Procédé et installation de production de méthane/d'hydrocarbures gazeux et/ou liquides
DE102017125415B8 (de) 2017-10-30 2018-10-25 clean energy one gmbh Windenergieanlage mit CO2 Sammler und Windenergieanlagen-CO2-Sammler-Steuerungs- bzw. Betriebsverfahren

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