WO2009126060A1 - Electricity generating system using a combined fuel - Google Patents
Electricity generating system using a combined fuel Download PDFInfo
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- WO2009126060A1 WO2009126060A1 PCT/RU2008/000229 RU2008000229W WO2009126060A1 WO 2009126060 A1 WO2009126060 A1 WO 2009126060A1 RU 2008000229 W RU2008000229 W RU 2008000229W WO 2009126060 A1 WO2009126060 A1 WO 2009126060A1
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- steam
- hydrogen
- oxygen
- boiler
- mixing chamber
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Classifications
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- 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
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/005—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for the working fluid being steam, created by combustion of hydrogen with oxygen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22G—SUPERHEATING OF STEAM
- F22G1/00—Steam superheating characterised by heating method
- F22G1/16—Steam superheating characterised by heating method by using a separate heat source independent from heat supply of the steam boiler, e.g. by electricity, by auxiliary combustion of fuel oil
Definitions
- the device relates to the field of energy and can be used to produce electricity and heat using combined fuel.
- the disadvantage of this device is the need for additional energy costs to produce hydrogen, as well as the presence of large containers for storing explosive hydrogen.
- Closest to the technical nature of the claimed device is the generating complex according to RU patent for utility model JV2 54631 dated 06/08/2005, which contains a steam boiler, an NgOg steam generator playing the role of a high-temperature hydrogen superheater (VVGSh), a steam turbine with an electric generator and a condenser, the production of oxygen and hydrogen (installation for steam conversion of natural gas to hydrogen) with a recovery boiler, the steam from which is fed to the intermediate stage of the steam turbine.
- VVGSh high-temperature hydrogen superheater
- the disadvantage of the device according to patent N ° 54631 is the incomplete use of the calorific value of fuel in a steam boiler and high temperature stresses in the mixing chamber after the H 2 ⁇ 2 steam generator of high temperature steam.
- the objective of the invention is to improve the efficiency, efficiency and reliability of the power generating complex.
- the essence of the invention lies in the fact that in the known power generating complex containing a steam boiler, a high-temperature hydrogen superheater (H 2 O 2 -generator) with a mixing chamber, which is connected by pipelines for supplying fuel (hydrogen and oxygen) with a hydrogen production unit (installation for steam conversion of natural gas into hydrogen) and with an oxygen producing plant, as well as a steam turbine with an electric generator and a condenser, a recovery boiler, pipelines and fittings, in it on pipelines
- a high-temperature hydrogen superheater H 2 O 2 -generator
- heat exchangers are installed to which the flue gas pipeline from the steam boiler is connected, and the steam supply pipe from the steam boiler is connected to the mixing chamber after the runway.
- Using the installation for steam conversion of natural gas to hydrogen allows for continuous operation of a steam turbine with a rated power at high initial temperature and pressure.
- the high temperature of water vapor up to 1700 - 1800 K at the entrance to the steam turbine due to the combustion of hydrogen with oxygen in the runway in the steam medium after it leaves the steam boiler ensures the turbine operates in the regimes typical of gas turbines.
- the output of a steam turbine is connected to a steam condenser, providing a pressure significantly lower than atmospheric, which is typical for such turbines. This makes it possible to have an available heat drop triggered in a high-temperature steam turbine, 25-30 percent more than in a gas turbine.
- Preheating of hydrogen fuel increases the efficiency of the complex, and cooling the mixing chamber with steam from a steam boiler increases its reliability.
- the inventive power generating complex (hereinafter referred to as the complex) is presented in the form of a circuit (see figure 1).
- the complex contains a steam boiler 1, installation 2 for steam conversion of natural gas to hydrogen, installation 3 for oxygen production, a high-temperature hydrogen superheater (VVPP) 4, with a mixing chamber 5, steam turbine b with an electric generator and condenser 7, a recovery boiler 8, and a heat exchanger 9 for heating oxygen and a heat exchanger 10 for heating hydrogen.
- VVPP high-temperature hydrogen superheater
- the complex also includes a pipe 11, steam supply from the steam boiler, respectively, to the runway 4 and installation 2, a pipe 12 of steam supply from the steam boiler to the mixing chamber 5, a pipe 13 for supplying exhaust gases from the steam boiler 1 to the heat exchanger 9 of oxygen heating, pipe 14 supply of flue gases from the steam boiler 1 to the heat exchanger 10 for heating hydrogen.
- Pipelines 15, 16 for supplying oxygen and for supplying hydrogen, piping 17 for supplying hydrogen to steam boiler 1, piping 18 for supplying mixed steam to turbine 6, piping 19 for secondary combustion products from unit 2 to utilization boiler 8, piping 20 for supplying BBl JJLl 4 are also connected steam from the recovery boiler 8 to the intermediate stage of the steam turbine b.
- the complex also includes other equipment and fittings.
- the device operates as follows.
- steam is supplied via pipeline 1 1 to BBlJJLl-4 and to installation 2 for steam conversion of natural gas to hydrogen, via pipeline 12 to mixing chamber 5, the resulting hydrogen is fed through pipeline 16 to VVPP 4.
- installation 3 for production oxygen for example, by the method of separation of air, receive oxygen, which is also fed through line 15 to the runway.
- part of the steam enters the runway 4, where oxygen and hydrogen are burned in the medium of water vapor.
- Combustion products - high-temperature water vapor is fed into the mixing chamber 5, where it is mixed with another part of the steam supplied through the pipe 12 from the steam boiler 1, this steam cools the walls of the mixing chamber 5, increasing the reliability of the complex and increasing the temperature steam overheating (without intermediate heat exchange surfaces).
- the mixture of vapors through pipeline 18 enters the steam turbine 6 with an electric generator, generating electricity.
- Secondary products of hydrogen production from installation 2 through a pipe 19 are fed to a recovery boiler 8, the steam from which enters the intermediate stage of the steam turbine 6.
- Oxygen and hydrogen from units 2 and 3 are heated in the heat exchangers 9 and 10 before being fed to the runway 4, respectively installed on the oxygen supply line 15 from the installation 3 in the runway 4 and on the hydrogen supply line 16 from the installation 2 to the runway 4.
- oxygen and hydrogen are heated by the flue gases of the steam boiler 1, which are supplied through pipelines 13 and 14.
- Part of the steam after the steam boiler 1, supplied through a pipe 12 to the mixing chamber 5 cools its walls, reduces thermal stresses and increases reliability. Due to the high temperature of the steam coming after the VVPP 4 to the steam turbine b, the power and efficiency of the turbine installation increase.
- the inventive power generating complex allows for continuous operation of a steam turbine with a rated power at a high initial temperature and pressure.
- the advantage of this device is also that for the generation of steam, ensuring its initial overheating and heating of oxygen and hydrogen coal, fuel oil, alternative fuels and renewable energy sources can be used.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The inventive electricity generating system using a combined fuel comprises a steam boiler (1), a hydrogen high-temperature steam superheater (4), which is provided with a mixing chamber (5) and is coupled, via fuel (hydrogen and oxygen) feeding pipes (15, 16) to hydrogen and oxygen producing units (2, 3), a steam turbine (6) with an electric power generator and a condenser (7), a heat-recovery boiler (8) and pipes and fittings; furthermore, heat exchangers (9, 10), to which pipes (13, 14) removing exhaust gas from the steam boiler are connected, are mounted on the pipes (15, 16) for feeding hydrogen and oxygen to the hydrogen high-temperature steam superheater (4), and a pipe (11) for supplying steam from the steam boiler (1) is connected to the mixing chamber (5).
Description
Электрогенерирующий комплекс с комбинированным топливом Combined fuel power generating complex
Устройство относится к области энергетики и может быть использовано для производства электроэнергии и тепла с использованием комбинированного топлива.The device relates to the field of energy and can be used to produce electricity and heat using combined fuel.
Известно аналогичное устройство (монография Э.Э.Шлильрайн, С.П.Малышенко, Г.Г. Кулешов. «Bвeдeниe в водородную энергетику)). M., Энергоатомиздат, 1984, с. 203), содержащее атомный реактор, камеру сгорания кислородно-водородного топлива (НгОг-парогенератор), паровую турбину с электрогенератором и конденсатором, электролизер, накопители водорода и кислорода.A similar device is known (monograph by E.E. Schlilrain, S.P. Malyshenko, G.G. Kuleshov. “Introduction to Hydrogen Energy”). M., Energoatomizdat, 1984, p. 203), containing an atomic reactor, a combustion chamber of oxygen-hydrogen fuel (NgOg-steam generator), a steam turbine with an electric generator and a condenser, an electrolyzer, hydrogen and oxygen stores.
Недостатком этого устройства является необходимость дополнительных затрат электроэнергии для получения водорода, а также наличие больших емкостей для хранения взрывоопасного водорода. Наиболее близким по технической сущности заявляемому устройству является электрогенерирующий комплекс по патенту RU на полезную модель JV2 54631 от 08.06.2005, который содержит паровой котел, НгОг-парогенератор, играющий роль высокотемпературного водородного пароперегревателя (ВВГШ), паровую турбину с электрогенератором и конденсатором, установки по производству кислорода и водорода (установка для паровой конверсии природного газа в водород) с утилизационным котлом, пар из которого подают в промежуточную ступень паровой турбины.The disadvantage of this device is the need for additional energy costs to produce hydrogen, as well as the presence of large containers for storing explosive hydrogen. Closest to the technical nature of the claimed device is the generating complex according to RU patent for utility model JV2 54631 dated 06/08/2005, which contains a steam boiler, an NgOg steam generator playing the role of a high-temperature hydrogen superheater (VVGSh), a steam turbine with an electric generator and a condenser, the production of oxygen and hydrogen (installation for steam conversion of natural gas to hydrogen) with a recovery boiler, the steam from which is fed to the intermediate stage of the steam turbine.
Недостатком устройства по патенту N° 54631 является неполное использование теплоты сгорания топлива в паровом котле и высокие температурные напряжения в камере смешения после H2θ2-пapoгeнepaтopa высокотемпературного пара.
Задача изобретения заключается в повышении эффективности работы, экономичности и надежности электрогенерирующего комплекса.The disadvantage of the device according to patent N ° 54631 is the incomplete use of the calorific value of fuel in a steam boiler and high temperature stresses in the mixing chamber after the H 2 θ 2 steam generator of high temperature steam. The objective of the invention is to improve the efficiency, efficiency and reliability of the power generating complex.
Сущность изобретения заключается в том, что в известном электрогенерирующем комплексе, содержащем паровой котел, высокотемпературный водородный пароперегреватель (H2O2-пapoгeнepaтop) с камерой смешения, который соединен трубопроводами подачи топлива (водорода и кислорода) с установкой по производству водорода (установкой для паровой конверсии природного газа в водород) и с установкой, производящей кислород, а также паровую турбину с электрогенератором и конденсатором, утилизационный котел, трубопроводы и арматуру, в нем на трубопроводах подачи топлива - водорода и кислорода в высокотемпературный водородный пароперегреватель (H2O2-пapoгeнepaтop) установлены теплообменники, к которым подведен трубопровод уходящих газов из парового котла, а к камере смешения после ВВПП подведен трубопровод подачи пара от парового котла.The essence of the invention lies in the fact that in the known power generating complex containing a steam boiler, a high-temperature hydrogen superheater (H 2 O 2 -generator) with a mixing chamber, which is connected by pipelines for supplying fuel (hydrogen and oxygen) with a hydrogen production unit (installation for steam conversion of natural gas into hydrogen) and with an oxygen producing plant, as well as a steam turbine with an electric generator and a condenser, a recovery boiler, pipelines and fittings, in it on pipelines In order to supply fuel - hydrogen and oxygen to a high-temperature hydrogen superheater (H 2 O 2 -generator), heat exchangers are installed to which the flue gas pipeline from the steam boiler is connected, and the steam supply pipe from the steam boiler is connected to the mixing chamber after the runway.
Использование установки для паровой конверсии природного газа в водород позволяет обеспечить непрерывную работу паровой турбины с номинальной мощностью при высоких начальных температуре и давлении. Высокая температура водяного пара до 1700 - 1800 К на входе в паровую турбину за счет сжигания в ВВПП водорода с кислородом в среде водяного пара после его выхода из парового котла обеспечивает работу турбины в режимах, характерных для газовых турбин. Выход паровой турбины связан с конденсатором пара, обеспечивающим давление существенно ниже атмосферного, что характерно для таких турбин. Это дает возможность иметь располагаемый теплоперепад, срабатываемый в высокотемпературной паровой турбине, на 25 - 30 процентов больше, чем в газовой. Предварительный подогрев водородного топлива повышает экономичность комплекса, а охлаждение камеры смешения паром из парового котла повышает его надежность. Нагрев водяного пара в современных паровых котлах выше 900 К фактически невозможен из-за пережога труб независимо от вида топлива (природный газ, водород, уголь и т.д.).
Заявляемый электрогенерирующий комплекс (далее - комплекс) представлен в виде схемы (см. фиг.1).Using the installation for steam conversion of natural gas to hydrogen allows for continuous operation of a steam turbine with a rated power at high initial temperature and pressure. The high temperature of water vapor up to 1700 - 1800 K at the entrance to the steam turbine due to the combustion of hydrogen with oxygen in the runway in the steam medium after it leaves the steam boiler ensures the turbine operates in the regimes typical of gas turbines. The output of a steam turbine is connected to a steam condenser, providing a pressure significantly lower than atmospheric, which is typical for such turbines. This makes it possible to have an available heat drop triggered in a high-temperature steam turbine, 25-30 percent more than in a gas turbine. Preheating of hydrogen fuel increases the efficiency of the complex, and cooling the mixing chamber with steam from a steam boiler increases its reliability. Heating steam in modern steam boilers above 900 K is virtually impossible due to burnout of pipes regardless of the type of fuel (natural gas, hydrogen, coal, etc.). The inventive power generating complex (hereinafter referred to as the complex) is presented in the form of a circuit (see figure 1).
Комплекс содержит паровой котел 1, установку 2 для паровой конверсии природного газа в водород, установку 3 для производства кислорода, высокотемпературный водородный пароперегреватель (ВВПП) 4, с камерой смешения 5, паровую турбину б с электрогенератором и конденсатором 7, утилизационный котел 8, а также теплообменник 9 - для подогрева кислорода и теплообменник 10 - для подогрева водорода.The complex contains a steam boiler 1, installation 2 for steam conversion of natural gas to hydrogen, installation 3 for oxygen production, a high-temperature hydrogen superheater (VVPP) 4, with a mixing chamber 5, steam turbine b with an electric generator and condenser 7, a recovery boiler 8, and a heat exchanger 9 for heating oxygen and a heat exchanger 10 for heating hydrogen.
Комплекс включает также трубопровод 11, подачи пара от парового котла, соответственно, к ВВПП 4 и установке 2, тртрубопровод 12 подачи пара от парового котла к камере смешения 5, трубопровод 13 подачи уходящих газов из парового котла 1 к теплообменнику 9 подогрева кислорода, трубопровод 14 подачи уходящих газов из парового котла 1 к теплообменнику 10 для подогрева водорода. К BBl JJLl 4 подведены также трубопроводы 15, 16 подачи кислорода и подачи водорода, трубопровод 17 подачи водорода в паровой котел 1, трубопровод 18 подачи смешанного пара к турбине 6, трубопровод 19 вторичных продуктов сгорания из установки 2 в утилизационный котел 8, трубопровод 20 подачи пара из утилизационного котла 8 в промежуточную ступень паровой турбины б. Комплекс включает также другое оборудование и арматуру.The complex also includes a pipe 11, steam supply from the steam boiler, respectively, to the runway 4 and installation 2, a pipe 12 of steam supply from the steam boiler to the mixing chamber 5, a pipe 13 for supplying exhaust gases from the steam boiler 1 to the heat exchanger 9 of oxygen heating, pipe 14 supply of flue gases from the steam boiler 1 to the heat exchanger 10 for heating hydrogen. Pipelines 15, 16 for supplying oxygen and for supplying hydrogen, piping 17 for supplying hydrogen to steam boiler 1, piping 18 for supplying mixed steam to turbine 6, piping 19 for secondary combustion products from unit 2 to utilization boiler 8, piping 20 for supplying BBl JJLl 4 are also connected steam from the recovery boiler 8 to the intermediate stage of the steam turbine b. The complex also includes other equipment and fittings.
Устройство работает следующим образом.The device operates as follows.
Из парового котла 1 пар поступает по трубопроводу 1 1 в BBlJJLl- 4 и к установке 2 для паровой конверсии природного газа в водород, по трубопроводу 12 - в камеру смешения 5, образовавшийся водород подают по трубопроводу 16 в ВВПП 4. В установке 3 для производства кислорода, например, методом разделения воздуха, получают кислород, который также подают по трубопроводу 15 в ВВПП. Из парового котла 1 часть пара поступает в ВВПП 4, где происходит сгорание кислорода и водорода в среде водяного пара. Продукты сгорания - высокотемпературный водяной пар подают в камеру смешения 5, где он смешивается с другой частью пара, поданной по трубопроводу 12 из парового котла 1, этот пар охлаждает стенки камеры смешения 5, повышая надежность комплекса и увеличивая температуру
перегрева пара (без промежуточных теплообменных поверхностей). Смесь паров по трубопроводу 18 поступает в паровую турбину 6 с электрогенератором, вырабатывая электроэнергию. Вторичные продукты производства водорода из установки 2 по трубопроводу 19 подают в утилизационный котел 8, пар из которого поступает в промежуточную ступень паровой турбины 6.From the steam boiler 1 steam is supplied via pipeline 1 1 to BBlJJLl-4 and to installation 2 for steam conversion of natural gas to hydrogen, via pipeline 12 to mixing chamber 5, the resulting hydrogen is fed through pipeline 16 to VVPP 4. In installation 3 for production oxygen, for example, by the method of separation of air, receive oxygen, which is also fed through line 15 to the runway. From the steam boiler 1, part of the steam enters the runway 4, where oxygen and hydrogen are burned in the medium of water vapor. Combustion products - high-temperature water vapor is fed into the mixing chamber 5, where it is mixed with another part of the steam supplied through the pipe 12 from the steam boiler 1, this steam cools the walls of the mixing chamber 5, increasing the reliability of the complex and increasing the temperature steam overheating (without intermediate heat exchange surfaces). The mixture of vapors through pipeline 18 enters the steam turbine 6 with an electric generator, generating electricity. Secondary products of hydrogen production from installation 2 through a pipe 19 are fed to a recovery boiler 8, the steam from which enters the intermediate stage of the steam turbine 6.
Кислород и водород из установок 2 и 3 перед подачей в ВВПП 4 подогреваются в теплообменниках 9 и 10, установленных, соответственно на трубопроводе 15 подачи кислорода из установки 3 в ВВПП 4 и на трубопроводе 16 подачи водорода из установки 2 в ВВПП 4. В теплообменниках 9 и 10 кислород и водород подогреваются уходящими газами парового котла 1, которые подают по трубопроводам 13 и 14.Oxygen and hydrogen from units 2 and 3 are heated in the heat exchangers 9 and 10 before being fed to the runway 4, respectively installed on the oxygen supply line 15 from the installation 3 in the runway 4 and on the hydrogen supply line 16 from the installation 2 to the runway 4. In the heat exchangers 9 and 10, oxygen and hydrogen are heated by the flue gases of the steam boiler 1, which are supplied through pipelines 13 and 14.
Использование уходящих газов парового котла 1 для подогрева кислорода и водорода перед подачей их в ВВПП 4 уменьшает потери тепла, повышает эффективность работы комплекса в целом.The use of the exhaust gases of the steam boiler 1 for heating oxygen and hydrogen before feeding them to the runway 4 reduces heat loss, increases the overall efficiency of the complex.
Часть пара после парового котла 1, подаваемая по трубопроводу 12 к камере смешения 5 охлаждает ее стенки, снижает термические напряжения и повышает надежность. Благодаря высокой температуре пара поступающего после ВВПП 4 к паровой турбине б увеличивается мощность и КПД турбинной установки.Part of the steam after the steam boiler 1, supplied through a pipe 12 to the mixing chamber 5 cools its walls, reduces thermal stresses and increases reliability. Due to the high temperature of the steam coming after the VVPP 4 to the steam turbine b, the power and efficiency of the turbine installation increase.
Заявляемый электрогенерирующий комплекс позволяет обеспечить непрерывную работу паровой турбины с номинальной мощностью при высокой начальной температуре и давлении.The inventive power generating complex allows for continuous operation of a steam turbine with a rated power at a high initial temperature and pressure.
Перечисленные конструктивные особенности позволяют достигнуть коэффициента полезного действия по выработанной электроэнергии до 70 % по отношению к теплоте сгорания водорода (статья С.П.Малышенко, О.В.Назаров,The listed design features make it possible to achieve a coefficient of efficiency in generated electricity of up to 70% with respect to the calorific value of hydrogen (article by S.P. Malyshenko, O.V. Nazarov,
Ю.А.Сарумов «Heкoтopыe теоретические и технико-экономические аспекты применения водорода как энергоносителя в электроэнергетике)), Сб. статейYu.A. Sarumov “Some theoretical and technical and economic aspects of the use of hydrogen as an energy carrier in the electric power industry)), Sat. articles
«Aтoмнo-вoдopoднaя энергетика и технология)), Энергоатомиздат, 1988, N° 8, c.16-38).“Atomic-Hydrogen Energy and Technology)), Energoatomizdat, 1988, N ° 8, p.16-38).
Достоинством данного устройства также является то, что для генерации пара, обеспечения его начального перегрева и подогрева кислорода и водорода
могут быть использованы уголь, мазут, альтернативные виды топлива и возобновляемые источники энергии.
The advantage of this device is also that for the generation of steam, ensuring its initial overheating and heating of oxygen and hydrogen coal, fuel oil, alternative fuels and renewable energy sources can be used.
Claims
Формула изобретенияClaim
Электрогенерирующий комплекс с комбинированным топливом, включающий паровой котел (1), высокотемпературный водородный пароперегреватель (4) с камерой смешения (5), соединенный трубопроводами (15, 16) подачи топлива - водорода и кислорода с установками (2,3) по производству водорода и кислорода, а также паровую турбину (б) с электрогенератором и конденсатором (7), утилизационный котел (8), трубопроводы и арматуру, отличающийся тем, что в нем на трубопроводах (15, 16) подачи водорода и кислорода в высокотемпературный водородный пароперегреватель (4), соответственно, установлены теплообменники (9, 10), к которым подведены трубопроводы (13,14) уходящих газов из парового котла (1), а к камере смешения (5) подведен трубопровод (11) подачи пара из парового котла (1).
An electric generating complex with combined fuel, including a steam boiler (1), a high-temperature hydrogen superheater (4) with a mixing chamber (5), connected by pipelines (15, 16) for supplying fuel - hydrogen and oxygen with installations (2,3) for hydrogen production and oxygen, as well as a steam turbine (b) with an electric generator and a condenser (7), a recovery boiler (8), pipelines and fittings, characterized in that it contains pipelines (15, 16) for supplying hydrogen and oxygen to a high-temperature hydrogen superheater (4 ), respectively Accordingly, heat exchangers (9, 10) were installed to which the pipelines (13.14) of the exhaust gases from the steam boiler (1) were connected, and the pipeline (11) for supplying steam from the steam boiler (1) was brought to the mixing chamber (5).
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008801286009A CN102027201A (en) | 2008-04-11 | 2008-04-11 | Electricity generating system using a combined fuel |
| EA201001472A EA017175B1 (en) | 2008-04-11 | 2008-04-11 | Electricity generating system using a combined fuel |
| PCT/RU2008/000229 WO2009126060A1 (en) | 2008-04-11 | 2008-04-11 | Electricity generating system using a combined fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/RU2008/000229 WO2009126060A1 (en) | 2008-04-11 | 2008-04-11 | Electricity generating system using a combined fuel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2009126060A1 true WO2009126060A1 (en) | 2009-10-15 |
Family
ID=41162064
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/RU2008/000229 WO2009126060A1 (en) | 2008-04-11 | 2008-04-11 | Electricity generating system using a combined fuel |
Country Status (3)
| Country | Link |
|---|---|
| CN (1) | CN102027201A (en) |
| EA (1) | EA017175B1 (en) |
| WO (1) | WO2009126060A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2708936C1 (en) * | 2019-02-14 | 2019-12-12 | федеральное государственное бюджетное образовательное учреждение высшего образования "Национальный исследовательский университет "МЭИ" (ФГБОУ ВО "НИУ "МЭИ") | Multigenerating complex with combined fuel at additional production of hydrogen and oxygen |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113339092A (en) * | 2021-05-17 | 2021-09-03 | 江阴市尚疯新能源技术开发有限公司 | Method for carbon gasification and neutralization power generation by using hydrogen and oxygen |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1724905A1 (en) * | 1990-04-09 | 1992-04-07 | Научно-производственный центр при Николаевском кораблестроительном институте им.адм.С.О.Макарова | Method of peak power generation |
| SU1765610A1 (en) * | 1989-12-11 | 1992-09-30 | Войсковая часть 27177 | Steam generator |
| RU2065978C1 (en) * | 1994-05-20 | 1996-08-27 | Вячеслав Семенович Муравин | Steam-power unit |
| RU54631U1 (en) * | 2005-06-08 | 2006-07-10 | Владимир Алексеевич Федоров | ELECTRIC GENERATING COMPLEX WITH COMBINED FUEL |
-
2008
- 2008-04-11 WO PCT/RU2008/000229 patent/WO2009126060A1/en active Application Filing
- 2008-04-11 EA EA201001472A patent/EA017175B1/en not_active IP Right Cessation
- 2008-04-11 CN CN2008801286009A patent/CN102027201A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1765610A1 (en) * | 1989-12-11 | 1992-09-30 | Войсковая часть 27177 | Steam generator |
| SU1724905A1 (en) * | 1990-04-09 | 1992-04-07 | Научно-производственный центр при Николаевском кораблестроительном институте им.адм.С.О.Макарова | Method of peak power generation |
| RU2065978C1 (en) * | 1994-05-20 | 1996-08-27 | Вячеслав Семенович Муравин | Steam-power unit |
| RU54631U1 (en) * | 2005-06-08 | 2006-07-10 | Владимир Алексеевич Федоров | ELECTRIC GENERATING COMPLEX WITH COMBINED FUEL |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2708936C1 (en) * | 2019-02-14 | 2019-12-12 | федеральное государственное бюджетное образовательное учреждение высшего образования "Национальный исследовательский университет "МЭИ" (ФГБОУ ВО "НИУ "МЭИ") | Multigenerating complex with combined fuel at additional production of hydrogen and oxygen |
Also Published As
| Publication number | Publication date |
|---|---|
| EA017175B1 (en) | 2012-10-30 |
| CN102027201A (en) | 2011-04-20 |
| EA201001472A1 (en) | 2011-02-28 |
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