CN108301922A - Mixing energy supplying system based on gas turbine and molten carbonate fuel cell - Google Patents
Mixing energy supplying system based on gas turbine and molten carbonate fuel cell Download PDFInfo
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- 239000000446 fuel Substances 0.000 title claims abstract description 65
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 title claims abstract description 49
- 239000007789 gas Substances 0.000 claims abstract description 38
- 238000002485 combustion reaction Methods 0.000 claims abstract description 22
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000001301 oxygen Substances 0.000 claims abstract description 8
- 230000005611 electricity Effects 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 8
- 239000003546 flue gas Substances 0.000 claims description 7
- 238000000926 separation method Methods 0.000 claims description 2
- 239000000567 combustion gas Substances 0.000 claims 1
- 239000010763 heavy fuel oil Substances 0.000 claims 1
- 238000004781 supercooling Methods 0.000 claims 1
- 238000001816 cooling Methods 0.000 abstract description 6
- 238000010248 power generation Methods 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000012530 fluid Substances 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000000376 reactant Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 238000012994 industrial processing Methods 0.000 description 1
- 239000010416 ion conductor Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C6/00—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C3/00—Gas-turbine plants characterised by the use of combustion products as the working fluid
- F02C3/34—Gas-turbine plants characterised by the use of combustion products as the working fluid with recycling of part of the working fluid, i.e. semi-closed cycles with combustion products in the closed part of the cycle
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C6/00—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use
- F02C6/18—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/14—Fuel cells with fused electrolytes
- H01M8/141—Fuel cells with fused electrolytes the anode and the cathode being gas-permeable electrodes or electrode layers
-
- 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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- Chemical & Material Sciences (AREA)
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- Combustion & Propulsion (AREA)
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Abstract
本发明涉及基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,属于分布式供能系统领域。该系统包括空气分离器、燃烧室、燃气轮机、VM循环热泵等部件。H2和O2分别在熔融碳酸盐燃料电池的阳极、阴极发生反应产生电能,同时,燃烧室内富氧燃烧产生的高温气体进入燃气轮机膨胀做功,并使发电机发电;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。本混合供能系统不仅可以保证系统电、冷、热用能的需求,而且具有发电效率高、燃料选择多样性、节能环保等特点。
The invention relates to a hybrid energy supply system based on gas turbines and molten carbonate fuel cells, and belongs to the field of distributed energy supply systems. The system includes air separator, combustion chamber, gas turbine, VM cycle heat pump and other components. H 2 and O 2 respectively react at the anode and cathode of the molten carbonate fuel cell to generate electricity. At the same time, the high-temperature gas generated by the oxygen-rich combustion in the combustion chamber enters the gas turbine to expand and perform work, and the generator generates electricity; The VM cycle heat pump provides cooling to users in summer, heat to users in winter, and provides users with domestic hot water load throughout the year. This hybrid energy supply system can not only guarantee the system's demand for electricity, cooling, and heating energy, but also has the characteristics of high power generation efficiency, diverse fuel choices, energy saving and environmental protection.
Description
技术领域technical field
本发明属于分布式供能系统领域,尤其涉及基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统。The invention belongs to the field of distributed energy supply systems, in particular to a hybrid energy supply system based on gas turbines and molten carbonate fuel cells.
背景技术Background technique
熔融碳酸盐燃料电池是一种以熔融碳酸盐为氧离子导体的高温燃料电池,通常被称为第二代燃料电池,工作温度在973-923K左右。与低温燃料电池相比,在熔融碳酸盐燃料电池的工作温度下,燃料(如天然气)可以直接在电池内部进行转化,既降低了成本,又提高了效率;其次,电池反应的高温余热可用于工业加工或锅炉循环;最后,燃料转化产生的CO不但不会使燃料电池电极催化剂中毒,反而可以成为熔融碳酸盐燃料电池的燃料。Molten carbonate fuel cell is a high-temperature fuel cell using molten carbonate as an oxygen ion conductor. It is usually called a second-generation fuel cell, and its working temperature is around 973-923K. Compared with low-temperature fuel cells, at the working temperature of molten carbonate fuel cells, fuel (such as natural gas) can be converted directly inside the battery, which not only reduces the cost, but also improves efficiency; secondly, the high-temperature waste heat of the battery reaction can be used It can be used in industrial processing or boiler cycle; finally, the CO produced by fuel conversion will not poison the fuel cell electrode catalyst, but can be used as fuel for molten carbonate fuel cells.
但是,熔融碳酸盐燃料电池有一个显著缺点,即需要向阴极不断地供应CO2。常规的做法是将阳极析出的CO2重新输送到阴极,但也增加了系统结构的复杂性。However, molten carbonate fuel cells have a significant disadvantage of requiring a constant supply of CO2 to the cathode. The conventional practice is to retransmit the CO 2 released from the anode to the cathode, but this also increases the complexity of the system structure.
目前,由天然气驱动燃气轮机是最常见的热电转换装置,但是燃气轮机受卡诺循环限制和燃烧损失影响,系统发电效率仍有待提高。At present, the gas turbine driven by natural gas is the most common thermoelectric conversion device, but the gas turbine is affected by the Carnot cycle limitation and combustion loss, and the power generation efficiency of the system still needs to be improved.
因此,考虑将常见的热电转换装置与熔融碳酸盐燃料电池相结合,既可以充分利用熔融碳酸盐燃料电池发电过程的原材料和产物,实现燃烧室内的富氧燃烧,又可以利用燃烧室产物中的CO2保证熔融碳酸盐燃料电池阴极的CO2含量,进而提高整个系统的发电效率和燃料利用率。Therefore, considering the combination of the common thermoelectric conversion device and the molten carbonate fuel cell, it can not only make full use of the raw materials and products of the molten carbonate fuel cell power generation process, realize the oxygen-enriched combustion in the combustion chamber, but also use the products of the combustion chamber The CO 2 in the molten carbonate fuel cell guarantees the CO 2 content of the cathode, thereby improving the power generation efficiency and fuel utilization of the entire system.
与此同时,燃气轮机的排烟温度高达600℃,直接排走会造成能源浪费,为了对该部分热量进行梯级利用,选用VM循环热泵作为冷热生产设备。At the same time, the exhaust gas temperature of the gas turbine is as high as 600°C, and direct discharge will cause energy waste. In order to use this part of the heat in steps, a VM cycle heat pump is selected as the cold and heat production equipment.
发明内容Contents of the invention
针对上述存在的问题和现象,本发明提供基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,旨在通过混合分布式系统满足用户的用能需求,并对剩余热量进行再回收,实现更好的能量梯级利用模式。In view of the above existing problems and phenomena, the present invention provides a hybrid energy supply system based on gas turbines and molten carbonate fuel cells, aiming to meet the energy demand of users through the hybrid distributed system, and recycle the remaining heat to achieve more Good energy cascade utilization mode.
为了实现上述目的,本发明采取的技术方案为:In order to achieve the above object, the technical scheme that the present invention takes is:
基于燃气轮机和熔融碳酸盐燃料电池的混合供能系统,包括:Hybrid energy supply systems based on gas turbines and molten carbonate fuel cells, including:
压气机:其配置为对空气进行压缩;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;
转化器:其配置为将燃料转化成熔融碳酸盐燃料电池所需的反应物;Converter: configured to convert the fuel into the reactants required for the molten carbonate fuel cell;
熔融碳酸盐燃料电池阳极:其配置为发生还原反应;Molten carbonate fuel cell anode: configured to undergo a reduction reaction;
熔融碳酸盐燃料电池阴极:其配置为方式氧化反应;Molten Carbonate Fuel Cell Cathode: configured for mode oxidation reactions;
燃烧室:其配置为将熔融碳酸盐燃料电池阳极排气中的剩余燃料再燃,并进行富氧燃烧,进一步提高燃烧室排气温度;Combustor: It is configured to reburn the remaining fuel in the anode exhaust of the molten carbonate fuel cell and perform oxygen-enriched combustion to further increase the exhaust temperature of the combustion chamber;
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,生产所需电力;Generator: configured to convert mechanical energy into electrical energy to produce the required electricity;
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,所述的转化器的产物是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 H2.
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,所述的熔融碳酸盐燃料电池阳极内的反应物是H2和CO3 2-,产物是H2O和CO2。The above-mentioned hybrid energy supply system based on a gas turbine and a molten carbonate fuel cell, wherein the reactants in the anode of the molten carbonate fuel cell are H 2 and CO 3 2- , and the products are H 2 O and CO 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,所述的熔融碳酸盐燃料电池阴极内的反应物是O2和CO2,产物是CO3 2-。In the aforementioned hybrid energy supply system based on a gas turbine and a molten carbonate fuel cell, the reactants in the cathode of the molten carbonate fuel cell are O 2 and CO 2 , and the product is CO 3 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烟气一部分进入燃烧室,另一部分进入转化器。In the aforementioned hybrid energy supply system based on a gas turbine and a molten carbonate fuel cell, a part of the flue gas generated by the gas turbine enters the combustion chamber, and the other part enters the converter.
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、熔融碳酸盐燃料电池工作温度高,电极反应活化能小,无论氢的氧化还是氧的还原,都不需要贵金属作催化剂,降低了系统发电成本。1. Molten carbonate fuel cell has a high working temperature and low activation energy of electrode reaction. It does not require precious metals as catalysts for hydrogen oxidation or oxygen reduction, which reduces the cost of power generation of the system.
2、燃烧室富氧燃烧得到的CO2产物直接通入熔融碳酸盐燃料电池阴极作为反应物参加反应,既减少了碳氧化物排放,又保证熔融碳酸盐燃料电池连续工作。2. The CO 2 product obtained by the oxygen-enriched combustion in the combustion chamber is directly passed into the cathode of the molten carbonate fuel cell as a reactant to participate in the reaction, which not only reduces the emission of carbon oxides, but also ensures the continuous operation of the molten carbonate fuel cell.
3、燃气轮机排烟通入转化器、燃烧室进行热量回收后,最后驱动VM循环热泵工作,此烟气利用途径既能保证各级用能需求,又可节约能源。3. After the exhaust gas from the gas turbine is passed into the converter and the combustion chamber for heat recovery, the VM cycle heat pump is finally driven to work. This method of flue gas utilization can not only ensure the energy demand at all levels, but also save energy.
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,本发明及其特征、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,重点在于示出本发明的主旨。The invention and its characteristics, configurations and advantages will become more apparent by reading the detailed description of non-limiting embodiments made with reference to the following drawings. Like numbers designate like parts throughout the drawings. The drawings are not intended to be drawn to scale, emphasis instead being placed upon illustrating the gist of the invention.
图1.基于燃气轮机和熔融碳酸盐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 molten carbonate fuel cell
图2.熔融碳酸盐燃料电池工作原理图Figure 2. Working principle diagram of molten carbonate fuel cell
图中各标号含义如下:1-压气机;2-空气分离器;3-转化器;4-熔融碳酸盐燃料电池阳极;5-熔融碳酸盐燃料电池阴极;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;The meanings of the symbols in the figure are as follows: 1-compressor; 2-air separator; 3-converter; 4-molten carbonate fuel cell anode; 5-molten carbonate fuel cell cathode; 6-combustion chamber; Gas turbine; 8-generator; 9-VM cycle heat pump; 10-heat exchanger I; 11-heat exchanger II; 12-heat exchanger III;
具体实施方式Detailed ways
下面结合附图和具体实施例对本发明作进一步的说明,但是不作为本发明的限定。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments, but not as a limitation of the present invention.
VM循环热泵的工作原理参考中国专利CN101865566A。The working principle of the VM cycle 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、转化器3、熔融碳酸盐燃料电池阳极4、熔融碳酸盐燃料电池阴极5、燃烧室6、燃气轮机7、发电机8、VM循环热泵9、换热器I 10、换热器II 11、换热器III 12。经过压气机1压缩后的空气进入空气分离器2进行气体分离,得到O2和N2产品,一部分O2进入熔融碳酸盐燃料电池阴极5,另一部分O2进入燃烧室6;燃料经过转化器3转化后得到的H2进入熔融碳酸盐燃料电池阳极4,与O2发生电化学反应进行发电;同时,燃料、CO、O2、烟气以及阳极排气中的剩余燃料在燃烧室6混合,将富氧燃烧产生的高温烟气送入燃气轮机7膨胀做功,并使发电机8发电;再利用燃气轮机7的烟气驱动VM循环热泵9,冬季通过换热器II 11向用户供暖,夏季通过换热器III 12从外界吸收热量进行制冷,换热器I 10则供应全年生活热水。As shown in Figure 1, the system includes: compressor 1, air separator 2, converter 3, molten carbonate fuel cell anode 4, molten carbonate fuel cell cathode 5, combustion chamber 6, gas turbine 7, generator 8. VM cycle heat pump 9, heat exchanger I 10, heat exchanger II 11, heat exchanger III 12. The air compressed by the compressor 1 enters the air separator 2 for gas separation to obtain O2 and N2 products, a part of O2 enters the cathode 5 of the molten carbonate fuel cell, and the other part of O2 enters the combustion chamber 6; the fuel is converted The H 2 obtained after conversion by the device 3 enters the anode 4 of the molten carbonate fuel cell, and undergoes an electrochemical reaction with O 2 to generate electricity; at the same time, fuel, CO, O 2 , flue gas and the remaining fuel in the anode exhaust are discharged in the combustion chamber 6 mixing, the high-temperature flue gas produced by oxygen-enriched combustion is sent to the gas turbine 7 to expand and perform work, and the generator 8 is used to generate electricity; the flue gas from the gas turbine 7 is then used to drive the VM cycle heat pump 9, and heat is supplied to users through the heat exchanger II 11 in winter. In summer, the heat exchanger III 12 absorbs heat from the outside for cooling, and the heat exchanger I 10 supplies domestic hot water throughout the year.
下面结合图2介绍熔融碳酸盐燃料电池工作原理。The working principle of the molten carbonate fuel cell will be introduced below in conjunction with FIG. 2 .
图2中,熔融碳酸盐燃料电池的结构主要包括上隔板、下隔板、熔融碳酸盐燃料电池阳极4、熔融碳酸盐燃料电池阴极5和电解质板。O2和CO2在阴极与电子进行氧化反应产生CO3 2-,电解质板中的CO3 2-直接从阴极移动到阳极;燃料中的H2与CO3 2-在阳极发生反应生成CO2、H2O和电子,电子被集流板收集后到达隔板;最后,通过上、下隔板与负载设备相连构成了包括电子传输和离子移动在内的完整的回路。In Fig. 2, the structure of the molten carbonate fuel cell mainly includes an upper separator, a lower separator, an anode 4 of a molten carbonate fuel cell, a cathode 5 of a molten carbonate fuel cell and an electrolyte plate. O 2 and CO 2 undergo oxidation reaction with electrons at the cathode to produce CO 3 2- , CO 3 2- in the electrolyte plate moves directly from the cathode to the anode; H 2 in the fuel reacts with CO 3 2- at the anode to produce CO 2 , H 2 O and electrons, and the electrons are collected by the collector plate and then reach the partition; finally, they are connected to the load device through the upper and lower partitions to form a complete circuit including electron transmission and ion movement.
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发明的实质内容,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 essence of the present invention, and will not be repeated here.
以上对本发明的较佳实施例进行了描述。需要理解的是,本发明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,在不脱离本发明技术方案做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,这并不影响本发明的实质内容。因此,凡是未脱离本发明技术方案的内容,依据本发明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,均仍属于本发明技术方案保护的范围内。The preferred embodiments of the present invention have been described above. It should be understood that the present invention is not limited to the specific embodiments described above, and the devices and structures that are not described in detail should be understood to be implemented in a common manner in the art; Many possible changes and modifications are made in the technical solution of the invention, or modified into equivalent embodiments with equivalent changes, which do not affect the essence of the present invention. Therefore, any simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention, which do not deviate from the technical solution of the present invention, still fall within the protection scope of the technical solution of the present invention.
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