CN206397600U - Mixing energy supplying system based on gas turbine and SOFC - Google Patents
Mixing energy supplying system based on gas turbine and SOFC Download PDFInfo
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- CN206397600U CN206397600U CN201720036307.6U CN201720036307U CN206397600U CN 206397600 U CN206397600 U CN 206397600U CN 201720036307 U CN201720036307 U CN 201720036307U CN 206397600 U CN206397600 U CN 206397600U
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- 239000000446 fuel Substances 0.000 claims abstract description 61
- 239000007789 gas Substances 0.000 claims abstract description 54
- 239000007787 solid Substances 0.000 claims abstract description 28
- 238000002485 combustion reaction Methods 0.000 claims abstract description 18
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000003546 flue gas Substances 0.000 claims abstract description 13
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 12
- 239000001301 oxygen Substances 0.000 claims abstract description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 10
- 230000005611 electricity Effects 0.000 claims abstract description 7
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 238000003487 electrochemical reaction Methods 0.000 claims description 3
- 230000003134 recirculating effect Effects 0.000 claims 1
- 238000002407 reforming Methods 0.000 claims 1
- 238000005057 refrigeration Methods 0.000 claims 1
- 230000006641 stabilisation Effects 0.000 claims 1
- 238000011105 stabilization Methods 0.000 claims 1
- 238000001816 cooling Methods 0.000 abstract description 7
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 10
- 239000012530 fluid Substances 0.000 description 6
- 238000010248 power generation Methods 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- -1 reformed CO Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007784 solid electrolyte Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- 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
- Y02E60/50—Fuel cells
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- 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
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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Abstract
本实用新型涉及基于燃气轮机和固体氧化物燃料电池的混合供能系统,属于分布式供能系统领域。该系统包括固体氧化物燃料电池、燃烧室、VM循环热泵等部件。H2与O2在固体氧化物燃料电池中发生反应进行发电;同时,以CH4为主的气体燃料在燃烧室发生富氧燃烧,产生的高温气体进入燃气轮机膨胀做功,使发电机发电;再利用燃气轮机烟气驱动VM循环热泵,在夏季向用户供冷,在冬季向用户供热,并提供用户全年的生活热水负荷。本混合供能系统既可以保证系统电、冷、热用能的需求,又可以使能源得到充分利用。
The utility model relates to a hybrid energy supply system based on gas turbines and solid oxide fuel cells, and belongs to the field of distributed energy supply systems. The system includes solid oxide fuel cells, combustion chambers, VM cycle heat pumps and other components. H 2 and O 2 react in the solid oxide fuel cell to generate electricity; at the same time, the gas fuel mainly CH 4 undergoes oxygen-enriched combustion in the combustion chamber, and the high-temperature gas generated enters the gas turbine to expand and do work, so that the generator generates electricity; The gas turbine flue gas is used to drive the VM cycle heat pump to supply cooling to users in summer, heat to users in winter, and provide users with domestic hot water load throughout the year. The hybrid energy supply system can not only ensure the system's demand for electricity, cooling and heating energy, but also make full use of energy.
Description
技术领域technical field
本实用新型属于分布式供能系统领域,尤其涉及基于燃气轮机和固体氧化物燃料电池的混合供能系统。The utility model belongs to the field of distributed energy supply systems, in particular to a hybrid energy supply system based on gas turbines and solid oxide fuel cells.
背景技术Background technique
在所有的燃料电池中,固体氧化物燃料电池的工作温度最高,属于高温燃料电池。近年,分布式电站由于成本低、可维护性高等优点逐渐成为世界能源供应的重要组成部分,而固体氧化物燃料电池和燃气轮机、蒸汽轮机等组成的联合发电系统,不但具有较高的发电效率(可达70%),还具有低污染的环境效益,非常适用于分布式发电。Among all fuel cells, solid oxide fuel cells have the highest operating temperature and are high-temperature fuel cells. In recent years, due to the advantages of low cost and high maintainability, distributed power plants have gradually become an important part of the world's energy supply, and the combined power generation system composed of solid oxide fuel cells, gas turbines, and steam turbines not only has high power generation efficiency ( Up to 70%), also has low pollution environmental benefits, very suitable for distributed power generation.
但是,固体氧化物燃料电池和燃气轮机、蒸汽轮机等组成的联合发电系统的排烟温度在800℃左右,直接排走造成极大的能源浪费。However, the exhaust gas temperature of the combined power generation system composed of solid oxide fuel cells, gas turbines, and steam turbines is about 800°C, and the direct discharge will cause a great waste of energy.
为了实现排烟热量的梯级利用,选用VM循环热泵作为冷热生产设备。VM循环热泵的热源可以是传统的化石能源,也可以是太阳能、生物质能等新能源,配合新能源的开发更是具有重要的节能减排意义,相比其他供暖/制冷设备,VM循环热泵具有明显的社会经济性和环保性优势。In order to realize the cascade utilization of exhaust heat, the VM cycle heat pump is selected as the cold and heat production equipment. The heat source of the VM cycle heat pump can be traditional fossil energy, or new energy such as solar energy and biomass energy. Cooperating with the development of new energy is of great significance for energy saving and emission reduction. Compared with other heating/cooling equipment, the VM cycle heat pump It has obvious socio-economic and environmental advantages.
发明内容Contents of the invention
针对上述存在的问题和现象,本实用新型提供基于燃气轮机和固体氧化物燃料电池的混合供能系统,旨在通过并联系统提高系统运行效率,实现能源梯级利用。In view of the above existing problems and phenomena, the utility model provides a hybrid energy supply system based on a gas turbine and a solid oxide fuel cell, aiming at improving the operating efficiency of the system through a parallel system and realizing cascaded utilization of energy.
为了实现上述目的,本实用新型采取的技术方案为:In order to achieve the above object, the technical scheme that the utility model takes is:
基于燃气轮机和固体氧化物燃料电池的混合供能系统,包括:A hybrid energy supply system based on gas turbines and solid oxide fuel cells, including:
压气机:其配置为将空气进行压缩;Compressor: configured to compress air;
空气分离器:其配置为对空气进行分离;air separator: configured to separate air;
燃料预热器:其配置为对燃料进行加热;fuel preheater: configured to heat fuel;
气体预热器:其配置为对O2进行加热;Gas preheater: configured to heat O2 ;
重整器:其配置为将预热后的燃料进行重整,以产生固体氧化物燃料电池阳极所需的氢;Reformer: configured to reform the preheated fuel to produce hydrogen for the solid oxide fuel cell anode;
固体氧化物燃料电池:其配置为发生电化学反应产生电能;Solid Oxide Fuel Cells: configured to produce electrical energy through an electrochemical reaction;
燃烧室:其配置为发生富氧燃烧,产生高温气体;Combustion chamber: configured for oxygen-enriched combustion to produce high-temperature gases;
燃气轮机:其配置为将高温气体的热能转换为机械能;Gas turbines: configured to convert thermal energy of high temperature gases into mechanical energy;
发电机:其配置为将机械能转变为电能;Generator: configured to convert mechanical energy into electrical energy;
VM循环热泵:其配置为将蒸汽的低温热源转移到高温热源,进行制冷和供暖,满足用户用能需求;VM cycle heat pump: It is configured to transfer the low-temperature heat source of steam to the high-temperature heat source for cooling and heating to meet the energy demand of users;
换热器I:其配置为将VM循环热泵热腔的热流体热量传递给冷流体;Heat exchanger I: it is configured to transfer the heat of the hot fluid in the heat chamber of the VM cycle heat pump to the cold fluid;
换热器II:其配置为将VM循环热泵室温腔的热流体热量传递给冷流体;Heat exchanger II: It is configured to transfer the heat of the hot fluid in the chamber of the VM cycle heat pump to the cold fluid;
换热器III:其配置为将VM循环热泵冷腔的冷流体冷量传递给热流体。Heat exchanger III: It is configured to transfer the cooling capacity of the cold fluid in the cold chamber of the VM cycle heat pump to the hot fluid.
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的空气分离器的产物是O2和N2产品。In the aforementioned hybrid energy supply system based on a gas turbine and a molten carbonate fuel cell, the products of the air separator are O 2 and N 2 products.
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的燃料预热器加热热源是燃气轮机的高温烟气。In the above-mentioned hybrid energy supply system based on gas turbine and molten carbonate fuel cell, the heating heat source of the fuel preheater is the high-temperature flue gas of the gas turbine.
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的气体预热器的加热热源是燃气轮机的高温烟气。In the above-mentioned hybrid energy supply system based on gas turbine and molten carbonate fuel cell, the heating heat source of the gas preheater is the high-temperature flue gas of the gas turbine.
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的重整器的产物是CO和H2。In the aforementioned hybrid energy supply system based on a gas turbine and a molten carbonate fuel cell, the products of the reformer are CO and H 2 .
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的固体氧化物燃料电池内发生电化学反应的是H2和O2。In the aforementioned hybrid energy supply system based on a gas turbine and a molten carbonate fuel cell, the electrochemical reaction in the solid oxide fuel cell is H 2 and O 2 .
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的燃气轮机产生的高温烟气一部分进入燃烧室,另一部分先进入重整器,再进入燃料预热器和气体预热器。The above-mentioned hybrid energy supply system based on gas turbine and molten carbonate fuel cell, wherein, part of the high-temperature flue gas generated by the gas turbine enters the combustion chamber, and the other part first enters the reformer, and then enters the fuel preheater and gas preheater. heater.
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的VM循环热泵通过热腔供应生活热水负荷,通过冷腔供应用户所需冷量,通过室温腔供应热量。In the above-mentioned hybrid energy supply system based on gas turbine and molten carbonate fuel cell, the VM cycle heat pump supplies the domestic hot water load through the hot cavity, supplies the cooling capacity required by users through the cold cavity, and supplies heat through the room temperature cavity.
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的换热器I与VM循环热泵热腔连接,全年运行。The above-mentioned hybrid energy supply system based on gas turbine and molten carbonate fuel cell, wherein, the heat exchanger I is connected with the heat chamber of the VM cycle heat pump and operates throughout the year.
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的换热器II与VM循环热泵室温腔连接,冬季运行,夏季停运。In the aforementioned hybrid energy supply system based on gas turbines and molten carbonate fuel cells, the heat exchanger II is connected to the chamber of the VM cycle heat pump at room temperature, and operates in winter and stops in summer.
上述的基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,其中,所述的换热器III与VM循环热泵冷腔连接,夏季运行,冬季停运。In the aforementioned hybrid energy supply system based on gas turbines and molten carbonate fuel cells, the heat exchanger III is connected to the cold chamber of the VM cycle heat pump, and operates in summer and stops in winter.
上述技术方案具有如下优点或者有益效果;The above technical solution has the following advantages or beneficial effects;
1、利用固体氧化物燃料电池和富氧燃烧相结合的发电方式,既可保证系统的发电量,又使得能源得以充分利用。1. The combination of solid oxide fuel cell and oxygen-enriched combustion power generation method can not only ensure the power generation of the system, but also make full use of energy.
2、燃气轮机排烟先经过重整器加热燃料,再驱动VM循环热泵,最后将VM循环热泵热腔的热水用来预热燃料和空气,此烟气利用途径既能保证各级用能需求,又可节约能源。2. The exhaust gas from the gas turbine first passes through the reformer to heat the fuel, then drives the VM cycle heat pump, and finally uses the hot water in the hot chamber of the VM cycle heat pump to preheat the fuel and air. , and save energy.
3、本系统将VM循环热泵与固体氧化物燃料电池相结合,供能方式多样,进一步挖掘出VM循环热泵的节能潜力和驱动灵活性。3. This system combines the VM cycle heat pump with the solid oxide fuel cell, and has various energy supply methods, further excavating the energy-saving potential and driving flexibility of the VM cycle heat pump.
附图说明Description of drawings
通过阅读参考以下的附图对非限制性实施例所作的详细描述,本实用新型及其特征、外形和优点将会变得更加明显。在全部附图中相同的标记指示相同的部分。并未刻意按照比例绘制附图,重点在于示出本实用新型的主旨。The invention and its features, shapes and advantages will become more apparent by reading the detailed description of non-limiting embodiments with reference to the following drawings. Like numbers designate like parts throughout the drawings. The drawings are not intentionally drawn to scale, and the emphasis is on illustrating the gist of the present invention.
图1.基于燃气轮机和固体氧化物燃料电池的混合供能系统结构示意图Figure 1. Schematic diagram of the hybrid energy supply system based on gas turbine and solid oxide fuel cell
图2.固体氧化物燃料电池工作原理图Figure 2. Working principle diagram of solid oxide fuel cell
图中各标号含义如下:1-压气机;2-空气分离器;3-燃料预热器;4-气体预热器;5-重整器;6-固体氧化物燃料电池;7-燃烧室;8-燃气轮机;9-发电机;10-VM循环热泵;11-换热器I;12-换热器II;13-换热器III;The meanings of the symbols in the figure are as follows: 1-compressor; 2-air separator; 3-fuel preheater; 4-gas preheater; 5-reformer; 6-solid oxide fuel cell; 7-combustion chamber ; 8-gas turbine; 9-generator; 10-VM cycle heat pump; 11-heat exchanger I; 12-heat exchanger II; 13-heat exchanger III;
具体实施方式detailed description
下面结合附图和具体实施例对本实用新型作进一步的说明,但是不作为本实用新型的限定。The utility model will be further described below in conjunction with the accompanying drawings and specific embodiments, but not as a limitation of the utility model.
VM循环热泵的工作原理参考中国专利CN101865566A。The working principle of the VM circulation heat pump refers to the Chinese patent CN101865566A.
如图1所示,本系统包括:压气机1、空气分离器2、燃料预热器3、气体预热器4、重整器5、固体氧化物燃料电池6、燃烧室7、燃气轮机8、发电机9、VM循环热泵10、换热器I 11、换热器II 12、换热器III 13。空气经过压气机1压缩后进入空气分离器2进行气体分离得到O2和N2产品,一部分O2经过气体预热器4加热后进入固体氧化物燃料电池6,另一部分O2进入燃烧室7;燃料经燃料预热器3加热后,一部分燃料经过重整器5重整后得到H2进入固体氧化物燃料电池6,与O2发生电化学反应并发电;另一部分燃料、重整得到的CO、烟气、O2以及固体氧化物燃料电池6的产物H2O进入燃烧室7进行富氧燃烧,产生的高温烟气进入燃气轮机8膨胀做功,并使发电机9发电;最后,燃气轮机8的800℃高温烟气一部分回流至燃烧室7调节富氧燃烧的O2含量在合理范围内,另一部分高温烟气先加热重整器5,稳定固体氧化物燃料电池6所需的H2产量,再加热燃料预热器3和气体预热器2,使固体氧化物燃料电池6保持合理的工作温度范围,最后驱动VM循环热泵10,夏季通过换热器II 12从外界吸收热量进行制冷,冬季通过换热器III 13向用户供暖,换热器I 11则供应全年生活热水。As shown in Figure 1, the system includes: compressor 1, air separator 2, fuel preheater 3, gas preheater 4, reformer 5, solid oxide fuel cell 6, combustion chamber 7, gas turbine 8, Generator 9, VM cycle heat pump 10, heat exchanger I 11, heat exchanger II 12, heat exchanger III 13. The air is compressed by the compressor 1 and enters the air separator 2 for gas separation to obtain O2 and N2 products. Part of the O2 enters the solid oxide fuel cell 6 after being heated by the gas preheater 4, and the other part of O2 enters the combustion chamber 7 After the fuel is heated by the fuel preheater 3, a part of the fuel is reformed by the reformer 5 to obtain H 2 enters the solid oxide fuel cell 6, and O 2 electrochemically reacts and generates electricity; another part of the fuel, reformed CO, flue gas, O 2 and the product H 2 O of the solid oxide fuel cell 6 enter the combustion chamber 7 for oxygen-enriched combustion, and the high-temperature flue gas generated enters the gas turbine 8 to expand and perform work, and makes the generator 9 generate electricity; finally, the gas turbine 8 Part of the 800°C high-temperature flue gas is returned to the combustion chamber 7 to adjust the O2 content of the oxygen-enriched combustion within a reasonable range, and the other part of the high-temperature flue gas is first heated to the reformer 5 to stabilize the H2 output required by the solid oxide fuel cell 6 , reheat the fuel preheater 3 and the gas preheater 2, so that the solid oxide fuel cell 6 maintains a reasonable operating temperature range, and finally drives the VM cycle heat pump 10, and absorbs heat from the outside through the heat exchanger II 12 in summer for cooling. Heat is supplied to users through heat exchanger III 13 in winter, and heat exchanger I 11 supplies domestic hot water throughout the year.
下面结合图2介绍固体氧化物燃料电池工作原理图。The working principle diagram of the solid oxide fuel cell is introduced below in combination with FIG. 2 .
图2中的固体氧化物燃料电池6主要包括固体电解质E、阳极A和阴极C三部分,固体氧化物燃料电池6工作时,电子由阳极经外电路流向阴极,氧分子得到电子被还原成氧离子,氧离子在电位差和氧浓度差驱动力的作用下,通过电解质中的氧空位定向跃迁至阳极发生氧化反应,阳极反应释放出的电子通过外电路流回到阴极。The solid oxide fuel cell 6 in Fig. 2 mainly includes three parts: solid electrolyte E, anode A, and cathode C. When the solid oxide fuel cell 6 is working, electrons flow from the anode to the cathode through an external circuit, and oxygen molecules get electrons and are reduced to oxygen Under the action of the potential difference and the driving force of the oxygen concentration difference, the oxygen ions transition to the anode through the oxygen vacancies in the electrolyte to undergo an oxidation reaction, and the electrons released by the anode reaction flow back to the cathode through an external circuit.
本领域技术人员应该理解,本领域技术人员结合现有技术以及上述实施例可以实现所述变化例,在此不予赘述。这样的变化例并不影响本实用新型的实质内容,在此不予赘述。Those skilled in the art should understand that those skilled in the art can implement the variation examples in combination with the prior art and the foregoing embodiments, which will not be repeated here. Such variations do not affect the essential content of the present invention, and will not be repeated here.
以上对本实用新型的较佳实施例进行了描述。需要理解的是,本实用新型并不局限于上述特定实施方式,其中未尽详细描述的设备和结构应该理解为用本领域中的普通方式予以实施;任何熟悉本领域的技术人员,在不脱离本实用新型技术方案作出许多可能的变动和修饰,或修改为等同变化的等效实施例,这并不影响本实用新型的实质内容。因此,凡是未脱离本实用新型技术方案的内容,依据本实用新型的技术实质对以上实施例所做的任何简单修改、等同变化及修饰,均仍属于本实用新型技术方案保护的范围内。The preferred embodiments of the present utility model have been described above. It should be understood that the utility model is not limited to the above-mentioned specific embodiments, and the devices and structures not described in detail should be understood as being implemented in a common way in the art; any person familiar with the art, without departing from Many possible changes and modifications are made in the technical scheme of the utility model, or modified into equivalent embodiments with equivalent changes, which do not affect the essential content of the utility model. Therefore, any simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention are still within the protection scope of the technical proposal of the present invention.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN108301924A (en) * | 2017-01-13 | 2018-07-20 | 华北电力大学(保定) | Mixing energy supplying system based on gas turbine and solid oxide fuel cell |
CN108798898A (en) * | 2018-04-20 | 2018-11-13 | 华电电力科学研究院有限公司 | The system and method for Proton Exchange Membrane Fuel Cells and combustion turbine combined supply steam and hot water |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN108301924A (en) * | 2017-01-13 | 2018-07-20 | 华北电力大学(保定) | Mixing energy supplying system based on gas turbine and solid oxide fuel cell |
CN108798898A (en) * | 2018-04-20 | 2018-11-13 | 华电电力科学研究院有限公司 | The system and method for Proton Exchange Membrane Fuel Cells and combustion turbine combined supply steam and hot water |
CN108798898B (en) * | 2018-04-20 | 2023-11-28 | 华电电力科学研究院有限公司 | System and method for supplying steam and hot water by combining proton exchange membrane fuel cell and gas turbine |
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