WO2020143860A1 - Centrale électrique à vapeur et à hydrogène - Google Patents

Centrale électrique à vapeur et à hydrogène Download PDF

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Publication number
WO2020143860A1
WO2020143860A1 PCT/DE2019/000337 DE2019000337W WO2020143860A1 WO 2020143860 A1 WO2020143860 A1 WO 2020143860A1 DE 2019000337 W DE2019000337 W DE 2019000337W WO 2020143860 A1 WO2020143860 A1 WO 2020143860A1
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WO
WIPO (PCT)
Prior art keywords
steam
hydrogen
exhaust gas
line
primary
Prior art date
Application number
PCT/DE2019/000337
Other languages
German (de)
English (en)
Inventor
Thomas Lamla
Original Assignee
Thomas Lamla
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 Thomas Lamla filed Critical Thomas Lamla
Priority to EP19849021.1A priority Critical patent/EP3908739A1/fr
Publication of WO2020143860A1 publication Critical patent/WO2020143860A1/fr

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
    • F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
    • F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K21/00—Steam engine plants not otherwise provided for
    • F01K21/04—Steam engine plants not otherwise provided for using mixtures of steam and gas; Plants generating or heating steam by bringing water or steam into direct contact with hot gas
    • F01K21/047—Steam engine plants not otherwise provided for using mixtures of steam and gas; Plants generating or heating steam by bringing water or steam into direct contact with hot gas having at least one combustion gas turbine
    • 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

  • Hydrogen-steam power plant The invention relates to a hydrogen-steam power plant (H2DKW) for
  • Liquid gas storage known storage in liquefied form known by cooling and compression.
  • liquid organic hydrogen carriers which are also referred to as liquid organic hydrogen carriers (LOHC).
  • Aromatic compounds to which the hydrogen is chemically bound by means of hydrogenation are used in particular as hydrogen carriers.
  • the hydrogen can be extracted and subsequently the stored energy can be released again from the hydrogen.
  • the advantage of LOHC technology is the easy transport of the stored hydrogen, since the hydrogen is chemically bound in a non-volatile manner.
  • the hydrogen After the hydrogen has been dehydrated, it is in the gaseous state and can in turn be used for energy generation, in particular electrical energy generation.
  • the object of the invention is to show a hydrogen-steam power plant which has a high degree of efficiency in the recovery of electrical energy from hydrogen, which is free of environmentally harmful emissions and which can also be provided with little design effort and inexpensively.
  • a turbine power plant has a primary unit and a secondary unit.
  • the primary unit has one compressor, one combustion air line, one
  • Hydrogen pipe an injection water pipe, a combustion chamber, a primary exhaust pipe, an exhaust gas turbine and a primary generator.
  • Atmospheric air from the surroundings can be taken up and compressed by the compressor.
  • the volume of the atmospheric air thus reduced is then available as combustion air and can be introduced into the combustion chamber by means of the combustion air line, which connects the compressor and the combustion chamber to one another.
  • hydrogen is used as fuel by means of a
  • Hydrogen supply line can be introduced into the combustion chamber, so that the
  • Combustion air can be burned together with the hydrogen to form a primary exhaust gas.
  • an injection water can be injected into the combustion chamber by means of the injection water line. The injection water evaporates due to the high temperatures of the combustion process in the combustion chamber and thus forms an injection water vapor component of the primary exhaust gas.
  • Injection water vapor portion of the primary exhaust gas is tensioned water vapor, which can advantageously be subsequently expanded in the exhaust gas turbine and converted into mechanical kinetic energy. It is also advantageous that the necessary for the evaporation of the injection water
  • Evaporation heat is extracted from the primary exhaust gas and thus lowers the temperature of the primary exhaust gas.
  • the temperature of the primary exhaust gas can thus be adjusted before it is introduced into the exhaust gas turbine such that the
  • Exhaust gas turbine is not subjected to high thermal loads. It is in one
  • the primary exhaust gas can then be supplied to the exhaust gas turbine via a primary exhaust gas line connecting the combustion chamber and the exhaust gas turbine.
  • the primary exhaust gas has a high temperature and pressure.
  • the primary exhaust gas is then in the exhaust gas turbine to a secondary exhaust gas relaxable. In this process, a thermal energy of the primary exhaust gas can be converted into a first mechanical energy.
  • the exhaust gas turbine is a simple gas expansion turbine in which the pressurized primary exhaust gas relaxes and does mechanical work.
  • the exhaust gas turbine itself does not have a compressor or its own combustion chamber. Rather, the gas to be relaxed in the
  • the exhaust gas turbine is preferably coupled to the primary generator via a shaft, so that the first mechanical energy provided by the rotation of the exhaust gas turbine can be transmitted to the primary generator and can be converted by the primary generator into a first electrical energy.
  • the first electrical energy can subsequently be fed into the power grid or delivered to an electrical consumer.
  • the compressor is preferably also mechanically coupled to the assembly comprising the exhaust gas turbine and the primary generator and is thus driven by means of the exhaust gas turbine.
  • the compressor is preferably driven via the shaft of the exhaust gas turbine, which couples the primary generator.
  • the primary generator is particularly preferably designed such that it can be operated both in generator operation and in engine operation. Thus, in a start-up process, the primary generator can drive the compressor while supplying electrical energy and perform a first compression of the atmospheric air into combustion air. As soon as the combustion process has started and the exhaust gas turbine emits mechanical energy, the primary generator is switched from engine operation to generator operation.
  • the secondary unit of the hydrogen-steam power plant comprises a steam turbine cycle and a chemical one
  • the steam turbine cycle has a secondary exhaust line, a steam generator, a steam pressure line, a steam turbine, and one
  • the secondary exhaust pipe connects the exhaust turbine and the
  • the secondary exhaust gas available in the exhaust gas turbine after expansion which still has high temperatures and thus high thermal energy, can thus be fed to the steam generator and used there for evaporation.
  • a condensate water can be introduced into the steam generator and evaporated to a superheated steam by means of a transfer of the thermal energy of the secondary exhaust gas.
  • the condensate water is introduced into this by means of a condensate line which connects the condenser and the steam generator and is then evaporated in the steam generator.
  • the superheated steam can be fed to the steam turbine by means of a steam pressure line which connects the steam generator and the steam turbine. In this the superheated steam becomes one
  • Exhaust steam can be expanded, wherein a thermal energy of the superheated steam can be converted into a second mechanical energy by means of the steam turbine.
  • the steam turbine is also a gas expansion turbine in a construction known per se.
  • the second mechanical energy can now be transmitted mechanically, preferably via a shaft, to the secondary generator and converted by the latter into a second electrical energy.
  • the second electrical energy can then be delivered to any electrical consumer
  • the exhaust steam generated by the expansion within the steam turbine can be fed to the condenser via an exhaust steam line, which connects the steam turbine and the condenser, and can be converted into condensate water by this condensation.
  • Condensate water is introduced into the condensate line and fed to the steam generator so that the steam turbine cycle is closed.
  • the steam turbine cycle of the secondary unit thus forms a closed thermodynamic cycle.
  • the chemical hydrogen carrier unit has a hydrogen carrier tank, a dehydrator and a heat exchanger.
  • a hydrogenated hydrogen carrier can be accommodated in the hydrogen carrier tank, which according to the invention is a Liquid Organic Hydrogen Carrier (LOHC).
  • LOHC Liquid Organic Hydrogen Carrier
  • Aromatic compounds whose ability to absorb hydrogen are reversible can be used in particular as LOHC.
  • the LOHC used should have a liquid physical state in the entire relevant temperature range and should preferably be non-toxic.
  • the chemical hydrogen carrier unit is also referred to below as the LOHC unit and the processes taking place here are also referred to below as the LOHC process.
  • the hydrogenated hydrogen carrier can be fed to the dehydrator by means of a hydrogen carrier line which connects the hydrogen carrier tank to the dehydrator.
  • the thermal energy of the exhaust steam can be transferred from the heat exchanger to the dehydrator.
  • the heat exchanger therefore has a connection to that running between the steam turbine and the condenser
  • the hydrogenated hydrogen carrier is now in the dehydrator by splitting off the hydrogen into a dehydrated hydrogen carrier
  • the reaction preferably takes place with the participation of a
  • the provision of the hydrogenated hydrogen carrier for carrying out this process is not part of the device according to the invention.
  • the hydrogen carrier is hydrogenated again after the dehydrogenation and then returned to the hydrogen carrier tank, so that a closed circuit is created.
  • the dehydrated hydrogen carrier can be hydrogenated in an external device, so that the hydrogen carrier tank must then always be refilled with hydrogenated hydrogen carrier from an external source.
  • the present invention thus does not relate to the LOHC process in its
  • a hydrogen-steam power plant according to the invention is also present if, in addition to the aforementioned elements of the hydrogen-steam power plant, additional elements such as further exhaust gas or drainage channels or
  • the hydrogen-steam power plant according to the invention has the following advantages in particular.
  • Energy generation is usable within the secondary unit.
  • the efficiency can be significantly increased both in the primary unit and in the secondary unit by introducing injection water.
  • the heat of combustion is used by the evaporation of the injection water and an additional volume of expandable gas is made available.
  • a mass flow of hot gas is available in the secondary unit with the water vapor portion of the secondary exhaust gas, the specific heat capacity of water vapor also being significantly higher than the specific heat capacity of air.
  • the thermal energy of the secondary exhaust gas resulting from the combustion process in the combustion chamber and remaining after passing through the exhaust gas turbine can be used to evaporate the condensate water within the steam generator while reducing the heat loss.
  • the thermal energy of the secondary exhaust gas is preferably also sufficient for the complete evaporation of the condensate water, so that no additional burners or similar devices are required.
  • thermal energy can then also be coupled out from the secondary unit, in particular from the capacitor, and used, for example for heating purposes.
  • the combustion process involves only combustion air and hydrogen.
  • the secondary exhaust gas resulting from the combustion can thus be removed from the hydrogen-steam power plant without any problems and without filtering or separating devices.
  • Another advantage is the structurally simple and robust design, in that the combustion chamber is separate from the exhaust gas turbine and the exhaust gas turbine is designed as a simple gas expansion turbine with all the advantages resulting therefrom. This includes that the technical separation of the compressor, combustion chamber and exhaust gas turbine can result in a design simplification and cost savings compared to an integrated gas turbine.
  • the hydrogen stored by means of a hydrogen carrier can be replaced locally and efficiently for energy recovery. This eliminates the time-consuming and costly transport of the gaseous hydrogen after the dehydrogenation.
  • Hydrogen in a hydrogen carrier is a suitable alternative to balance generation peaks.
  • LOHC Low-term and efficient storage
  • the thermal energy dissipated by the condenser during the condensation can be transferred to a heating system.
  • the residual thermal energy generated in the secondary unit can also be used.
  • the primary unit has at least one alternative fuel feed line, which is connected to the combustion chamber and by means of which an alternative fuel can be introduced into the combustion chamber and combustible with the combustion air to the primary exhaust gas.
  • the at least one alternative fuel preferably any known alternative fuel, can be combined with the hydrogen that comes from the
  • Dehydrator obtained is used as fuel. Especially in the event that temporarily no hydrogen is provided for the
  • Combustion process can take place, it is provided as a further variant to continue the combustion exclusively by means of the alternative fuel in order to be able to maintain the supply of electrical energy and optionally thermal energy.
  • Any suitable fuels known from the prior art such as in particular natural gas, LPG or petroleum, can be used as alternative fuels. If necessary, additional facilities for enabling the switchover are to be provided in the case of such a multifunctional further training.
  • Hydrogen conduction can also be built in whole or in sections
  • the hydrogen-steam power plant also has an exhaust gas condenser. This is trained the Condensate water vapor portion of the secondary exhaust gas after it emerges from the steam generator to an exhaust gas condensate water.
  • the secondary exhaust gas can thus be predominantly or at least partially removed from the water contained therein in gaseous form before it is discharged into the environment.
  • the water vapor content of the secondary exhaust gas goes first to the evaporated injection water and second to water as a combustion product of hydrogen and oxygen from the
  • the exhaust gas condensation water can be fed to the injection water line and thus as injection water
  • a material cycle of water is thus formed in the hydrogen-steam power plant.
  • no or less water has to be added for the injection water.
  • the thermal energy which arises from the release of the heat of condensation of the water vapor when it is condensed becomes from a cooling circuit of the exhaust gas condenser
  • decoupled can either for the dehydrator, for other thermal auxiliary processes of the hydrogen-steam power plant or for external
  • Heat consumers such as district heating can be provided.
  • the hydrogen-steam power plant has an upstream distillation stage.
  • This upstream distillation stage is designed to evaporate and condense salt water, in particular sea water, so that the salinity is separated and a fresh water is obtained.
  • the fresh water is then introduced into the combustion chamber as injection water via the injection water line.
  • the thermal energy required for the operation of the upstream distillation stage specifically the heat of vaporization, is preferably taken from the primary unit or the secondary unit.
  • the hydrogen-steam power plant can have other means such as, in particular, heat exchangers.
  • Fig. 2 block diagram of the secondary unit explained in more detail.
  • Fig. 1 shows an embodiment of a hydrogen-steam power plant as a block diagram.
  • the hydrogen-steam power plant is divided into a primary unit 1 and a secondary unit 2, the primary unit 1 comprising a compressor 3, a combustion air line 4, a hydrogen line 5, a combustion chamber 6, a primary exhaust gas output 7, an exhaust gas turbine 8 and a primary generator 9 has.
  • the secondary unit 2 is composed of a steam turbine cycle 10 and a chemical hydrogen carrier unit 11, the
  • Steam turbine circuit 10 has a secondary exhaust line 12, a steam generator 13, a steam pressure line 14, a steam turbine 15, a secondary generator 16, an exhaust steam line 17, a condenser 18 and a condensate line 19.
  • the chemical hydrogen carrier unit 11 has one Hydrogen carrier tank 20, a dehydrator 21, a heat exchanger 22 and a hydrogen carrier line 23.
  • Atmospheric air can be taken up and compressed by the compressor 3 as ambient air with the oxygen required therein for the combustion.
  • the air is compressed from atmospheric pressure to about 3 bar and is then available as combustion air, which can be introduced into the combustion chamber 6 via the combustion air line 4.
  • hydrogen is by means of
  • Hydrogen line 5 can be introduced as fuel into the combustion chamber 6. Furthermore, an injection water can be introduced into the combustion chamber 6 via the injection water line 24.
  • the combustion air is now combustible into a primary exhaust gas by means of the hydrogen in the combustion chamber 6.
  • the injection water evaporates while absorbing heat from the combustion process.
  • the evaporation creates tensioned water vapor, which forms part of the exhaust gas.
  • the Brennkam mer 6 also has safety flaps in the present exemplary embodiment, which enable an independent closure in the presence of overpressure.
  • the primary exhaust gas can be fed to the exhaust gas turbine 8 by means of the primary exhaust gas line 7 and can be expanded there to convert a secondary exhaust gas by converting the thermal energy into a first mechanical energy.
  • the exhaust gas turbine 8 is mechanically connected to the shaft
  • Primary generator 9 coupled so that the first mechanical energy can be transmitted from the exhaust gas turbine 8 to the primary generator 9 and can be converted by the latter into a first electrical energy.
  • the first electrical energy can subsequently be fed into a power grid or can be supplied to an electrical consumer.
  • the secondary exhaust gas which has a temperature of approximately 600 to 800 ° C., preferably approximately 700 ° C., after exiting the exhaust gas turbine 8 can be fed to the steam generator 13 by means of the secondary exhaust line 12.
  • the entry of the secondary exhaust gas into the secondary exhaust line 12 also represents the transition of the working medium from the primary unit 1 into the
  • Secondary unit 2 represents.
  • a condensate water can be introduced into the steam generator 13.
  • the condensate water is passed in a closed pipe, the condensate line 19, meandering through the interior of the steam generator and can be evaporated to a superheated steam by transferring the thermal energy of the secondary exhaust gas.
  • an outlet opening is also provided at the upper end of the steam generator 13, through which the secondary exhaust gas can subsequently exit.
  • the resulting superheated steam is supplied to the steam turbine 15 in a steam pressure line 14.
  • the superheated steam can be expanded into an exhaust steam by converting its thermal energy into a second mechanical energy.
  • the second mechanical energy is after that
  • Secondary generator 16 can be transmitted and converted into a second electrical energy.
  • the generated second electrical energy can be transmitted and converted into a second electrical energy.
  • the exhaust steam emitted by the steam turbine 15 can be supplied to the condenser 18 via the exhaust steam line 17 and can be converted by this to a condensate water by condensation, which can then be conducted into the condensate line 19 and thus in turn can be supplied to the steam generator 13.
  • the steam turbine cycle 10 of the secondary unit 2 thus forms a closed thermodynamic cycle in its entirety.
  • the thermal energy dissipated from the capacitor 18 during the condensation process becomes Operating a heating system. From the heating system, cooled water can also be introduced into the condenser 18 via a return line and from there can be introduced together with the condensate water into the steam generator 13.
  • the chemical hydrogen carrier unit 11 is a further component of the secondary unit 2.
  • a hydrogenated hydrogen carrier which is present as an LOHC according to the invention, can be accommodated in the hydrogen carrier tank 20.
  • the main requirements for the LOHC are that it enables reversible hydrogen uptake and release and that it is relevant overall
  • Temperature range has a liquid physical state. Some aromatic compounds have proven to be particularly suitable for this purpose.
  • the hydrogenated hydrogen carrier can be fed to the dehydrator 21 by means of the hydrogen carrier line 23.
  • the hydrogen carrier line 23 first leads into the heat exchanger 22, from which a thermal energy of the exhaust steam can be transferred to the hydrogen carrier.
  • the heat exchanger 22 therefore has a closable connection to the exhaust steam line 17.
  • the still liquid hydrogen carrier has a temperature of about 250 to 400 ° C, preferably of about 320 ° C.
  • the embodiment for this is the injection water line 24 to the
  • Injection water can be used again. A cycle of evaporation of the injection water, guidance of the water vapor content in the exhaust gas, condensation and recycling of the liquid water for re-injection is thus formed. At a connection point 26, depending on the process state, either excess exhaust gas condensate water can be removed from the circuit or the required injection water can be supplied.
  • Fig. 2 shows an enlarged view of the secondary unit 2 for spatial

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

L'invention concerne une centrale électrique à vapeur et à hydrogène comprenant une unité primaire (1) et une unité secondaire (2). L'unité primaire (1) comporte un compresseur (3), un conduit d'air de combustion (4), un conduit d'hydrogène (5), un conduit d'eau d'injection (24), une chambre de combustion (6), un conduit de gaz d'échappement (7) primaire, une turbine à gaz d'échappement (8) ainsi qu'un générateur primaire (9). L'unité secondaire (2) comporte un circuit de turbine à vapeur (10) et une unité de support d'hydrogène (11) chimique. L'unité de support d'hydrogène (11) chimique comporte un réservoir de support d'hydrogène (20), un déshydrateur (21) ainsi qu'un échangeur de chaleur (22). Un support d'hydrogène hydrogéné peut être logé dans le réservoir de support d'hydrogène (20). Le support d'hydrogène hydrogéné peut être amené au déshydrateur (21) au moyen d'un conduit (23) de support d'hydrogène, lequel relie le réservoir (20) de support d'hydrogène au déshydrateur (21). Une énergie thermique de l'eau de condensation peut être transmise au déshydrateur (21) au moyen de l'échangeur de chaleur (22). Le support d'hydrogène hydrogéné peut être transformé en un support d'hydrogène déshydraté au moyen de l'énergie thermique de l'eau de condensation dans le déshydrateur (21) en ajoutant l'hydrogène. L'hydrogène peut être amené à la chambre de combustion (6) au moyen du conduit (5) d'hydrogène, lequel relie le déshydrateur (21) à la chambre de combustion (6). En outre, une partie de vapeur d'eau des gaz d'échappement peut être condensée après un perfectionnement et peut être introduite dans le conduit (24) d'eau d'injection en tant qu'eau d'injection.
PCT/DE2019/000337 2019-01-07 2019-12-30 Centrale électrique à vapeur et à hydrogène WO2020143860A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP19849021.1A EP3908739A1 (fr) 2019-01-07 2019-12-30 Centrale électrique à vapeur et à hydrogène

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DEDE102019000019.6 2019-01-07
DE102019000019.6A DE102019000019A1 (de) 2019-01-07 2019-01-07 Wasserstoff-Dampf-Kraft-Werk

Publications (1)

Publication Number Publication Date
WO2020143860A1 true WO2020143860A1 (fr) 2020-07-16

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Application Number Title Priority Date Filing Date
PCT/DE2019/000337 WO2020143860A1 (fr) 2019-01-07 2019-12-30 Centrale électrique à vapeur et à hydrogène

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Country Link
EP (1) EP3908739A1 (fr)
DE (1) DE102019000019A1 (fr)
WO (1) WO2020143860A1 (fr)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6148602A (en) * 1998-08-12 2000-11-21 Norther Research & Engineering Corporation Solid-fueled power generation system with carbon dioxide sequestration and method therefor
WO2003001046A2 (fr) * 2001-06-21 2003-01-03 Alstom Technology Ltd Procede pour faire fonctionner un moteur
WO2003049122A2 (fr) * 2001-12-03 2003-06-12 Clean Energy Systems, Inc. Systemes de production alimente en charbon et en gaz de synthese a emission atmospherique zero
WO2005106224A1 (fr) * 2004-04-23 2005-11-10 Dow Corning Corporation Procede ameliore de production d'energie electrique
US20060032228A1 (en) * 2004-08-02 2006-02-16 Ovidiu Marin Power generation system including a gas generator combined with a liquified natural gas supply
DE202017003690U1 (de) * 2017-07-13 2018-10-16 Thomas Lamla Wasserstoff-Dampf-Kraft-Werk

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6148602A (en) * 1998-08-12 2000-11-21 Norther Research & Engineering Corporation Solid-fueled power generation system with carbon dioxide sequestration and method therefor
WO2003001046A2 (fr) * 2001-06-21 2003-01-03 Alstom Technology Ltd Procede pour faire fonctionner un moteur
WO2003049122A2 (fr) * 2001-12-03 2003-06-12 Clean Energy Systems, Inc. Systemes de production alimente en charbon et en gaz de synthese a emission atmospherique zero
WO2005106224A1 (fr) * 2004-04-23 2005-11-10 Dow Corning Corporation Procede ameliore de production d'energie electrique
US20060032228A1 (en) * 2004-08-02 2006-02-16 Ovidiu Marin Power generation system including a gas generator combined with a liquified natural gas supply
DE202017003690U1 (de) * 2017-07-13 2018-10-16 Thomas Lamla Wasserstoff-Dampf-Kraft-Werk

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EP3908739A1 (fr) 2021-11-17
DE102019000019A1 (de) 2020-07-09

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