CN102628402A - Fuel cell and organic Rankine cycle combined power generating system based on LNG (Liquefied Natural Gas) cold energy utilization - Google Patents
Fuel cell and organic Rankine cycle combined power generating system based on LNG (Liquefied Natural Gas) cold energy utilization Download PDFInfo
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- 239000000446 fuel Substances 0.000 title claims abstract description 91
- 239000003949 liquefied natural gas Substances 0.000 title description 27
- 239000007789 gas Substances 0.000 claims abstract description 88
- 239000003570 air Substances 0.000 claims abstract description 38
- 239000007787 solid Substances 0.000 claims abstract description 36
- 239000002918 waste heat Substances 0.000 claims abstract description 28
- 238000010248 power generation Methods 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000002485 combustion reaction Methods 0.000 claims abstract description 13
- 239000012530 fluid Substances 0.000 claims description 14
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 9
- 239000001301 oxygen Substances 0.000 claims description 9
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- 230000005611 electricity Effects 0.000 claims description 8
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 claims description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 4
- 229920006395 saturated elastomer Polymers 0.000 claims description 4
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 claims description 3
- MSSNHSVIGIHOJA-UHFFFAOYSA-N pentafluoropropane Chemical compound FC(F)CC(F)(F)F MSSNHSVIGIHOJA-UHFFFAOYSA-N 0.000 claims description 3
- FYIRUPZTYPILDH-UHFFFAOYSA-N 1,1,1,2,3,3-hexafluoropropane Chemical compound FC(F)C(F)C(F)(F)F FYIRUPZTYPILDH-UHFFFAOYSA-N 0.000 claims description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 2
- 239000001569 carbon dioxide Substances 0.000 claims description 2
- 239000003507 refrigerant Substances 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 239000003344 environmental pollutant Substances 0.000 abstract description 5
- 231100000719 pollutant Toxicity 0.000 abstract description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 1
- 239000003546 flue gas Substances 0.000 abstract 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 8
- 238000010586 diagram Methods 0.000 description 5
- 239000003345 natural gas Substances 0.000 description 4
- 238000003487 electrochemical reaction Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
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- 238000005516 engineering process Methods 0.000 description 1
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
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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
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- 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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Abstract
本发明公开了一种基于LNG冷能利用的燃料电池和有机朗肯循环联合发电系统,包括:固体氧化物燃料电池和燃气轮机的联合循环系统、有机朗肯循环系统和LNG冷能源;SOFC中未反应完的燃料和空气在后燃室中继续燃烧,产生高温高压的燃气,进入燃气轮机做功输出电能,燃气轮机的高温排气依次预热空气、燃料和水;有机朗肯循环系统将经预热空气、燃料和水后的中低温烟气余热进行回收利用,转换为电能输出,实现能量的梯级利用;LNG冷能源作为有机朗肯循环的冷源冷凝有机工质透平的排气,使有机工质透平的背压显著降低,增加有机朗肯循环的功率输出,同时回收利用了LNG的冷能。本发明系统可以显著提高了能源转化效率,减少了污染物排放,改善系统的性能。
The invention discloses a fuel cell and organic Rankine cycle combined power generation system based on LNG cold energy utilization, including: a combined cycle system of a solid oxide fuel cell and a gas turbine, an organic Rankine cycle system, and LNG cold energy; The reacted fuel and air continue to burn in the post-combustion chamber to produce high-temperature and high-pressure gas, which enters the gas turbine to do work and output electric energy. The high-temperature exhaust gas from the gas turbine preheats air, fuel and water in sequence; , fuel and water, the waste heat of the medium and low temperature flue gas is recycled and converted into electric energy output to realize the cascade utilization of energy; The back pressure of the high-quality turbine is significantly reduced, the power output of the organic Rankine cycle is increased, and the cold energy of the LNG is recycled. The system of the invention can significantly improve energy conversion efficiency, reduce pollutant discharge and improve system performance.
Description
技术领域 technical field
本发明属于高温和中低温热能回收与动力工程领域,涉及一种基于冷能利用的燃料电池和有机朗肯循环联合发电系统。The invention belongs to the field of high-temperature and medium-low temperature heat energy recovery and power engineering, and relates to a fuel cell and organic Rankine cycle combined power generation system based on cold energy utilization.
背景技术 Background technique
传统的化石燃料包括煤、石油、天然气等,其储量有限,并大多数以燃烧的方式被利用,这样不但使得能源利用效率有限从而导致能源的浪费,而且不可避免地产生大量的污染物排放。固体氧化物燃料电池是一种将存在于燃料与氧化剂中的化学能高效、环境友好地转化成电能的发电装置,燃料中的氢借助于电解质与空气中的氧直接转化为电能,不受卡诺循环效率的限制,是一种能够很好地解决化石燃料发电效率与环境污染这一矛盾的新型发电方式。另外,固体氧化物燃料电池的反应温度较高,通常在1000℃左右,其排放的余热品位较高,有很大的回收利用空间。因此,采用一种基于LNG(liquefied natural gas,液化天然气)冷能利用的固体氧化物燃料电池和有机朗肯循环联合发电系统将燃料电池燃气轮机联合循环、有机朗肯循环和LNG冷能利用进行系统集成,可以实现能源的梯级利用,提高能源的利用效率。Traditional fossil fuels, including coal, oil, and natural gas, have limited reserves, and most of them are used in the form of combustion, which not only makes energy utilization efficiency limited and leads to energy waste, but also inevitably produces a large amount of pollutant emissions. The solid oxide fuel cell is a power generation device that efficiently and environmentally friendly converts the chemical energy present in the fuel and the oxidant into electrical energy. The hydrogen in the fuel is directly converted into electrical energy by means of the electrolyte and oxygen in the air. It is a new power generation method that can well solve the contradiction between fossil fuel power generation efficiency and environmental pollution. In addition, the reaction temperature of the solid oxide fuel cell is relatively high, usually around 1000°C, and the waste heat discharged by it has a high grade, and there is a large space for recycling. Therefore, a solid oxide fuel cell and organic Rankine cycle combined power generation system based on LNG (liquefied natural gas, liquefied natural gas, liquefied natural gas) cold energy utilization is used to systematically combine fuel cell gas turbine combined cycle, organic Rankine cycle and LNG cold energy utilization. Integration can realize cascade utilization of energy and improve energy utilization efficiency.
图1给出了现有技术中的一种固体氧化物燃料电池和燃气轮机的联合循环系统示意图。空气依次经过空气压缩机1’升压,气体加热器4’升温,送入固体氧化物燃料电池8’的阴极。同时,燃料经过燃料压缩机2’升压和气体加热器5’预热;水在水泵3’中加压,经过加热器6’加热,与预热后的燃料在混合器7’中充分混合之后,送入固体氧化物燃料电池8’的阳极。燃料和氧气在固体氧化物燃料电池8’内发生电化学反应后对外输出直流电,经过逆变器12’,转换为交流电输出。另一方面,燃料电池8’排放的未反应完的氧气与阳极未反应完全的可燃气体一同送入燃烧室9’中进行燃烧,产生高温高压燃气,燃气再进入燃气轮机10’中做功,驱动发电机11’发电。最后,燃气轮机10’的高温排气依次被送入加热器4’、加热器5’、加热器6’,分别完成对空气、燃料和水的预热,最后排出系统。Fig. 1 shows a schematic diagram of a combined cycle system of a solid oxide fuel cell and a gas turbine in the prior art. The air is sequentially pressurized by the air compressor 1', heated by the gas heater 4', and sent to the cathode of the solid oxide fuel cell 8'. At the same time, the fuel is boosted by the fuel compressor 2' and preheated by the gas heater 5'; the water is pressurized in the water pump 3', heated by the heater 6', and fully mixed with the preheated fuel in the mixer 7' After that, it is sent to the anode of the solid oxide fuel cell 8'. The fuel and oxygen undergo an electrochemical reaction in the solid oxide fuel cell 8' to output direct current, which is converted into alternating current output through the inverter 12'. On the other hand, the unreacted oxygen discharged from the fuel cell 8' and the unreacted combustible gas from the anode are sent to the combustion chamber 9' for combustion to generate high-temperature and high-pressure gas, which then enters the gas turbine 10' to do work and drive power generation Machine 11 ' generates electricity. Finally, the high-temperature exhaust gas from the gas turbine 10' is sequentially sent to the heater 4', heater 5', and heater 6' to complete the preheating of air, fuel and water respectively, and finally exit the system.
上述系统将固体氧化物燃料电池的高温排气通过燃气轮机进行发电,同时利用燃气轮机的排气对燃料、空气和水进行预热,回收了高温排气的热能,提高了系统的效率。但是由于燃气轮机的排气温度很高,即使经过换热器之后仍然有很大的中低温余热利用空间。The above-mentioned system uses the high-temperature exhaust gas of the solid oxide fuel cell to generate electricity through the gas turbine, and uses the exhaust gas of the gas turbine to preheat fuel, air and water, recovers the heat energy of the high-temperature exhaust gas, and improves the efficiency of the system. However, due to the high exhaust temperature of the gas turbine, even after passing through the heat exchanger, there is still a large space for the utilization of medium and low temperature waste heat.
中低温热源发电可以采用有机朗肯循环技术。有机朗肯循环采用低沸点的有机工质,如R123,R113,R245fa,异戊烷等。有机工质在余热锅炉1”中被中低温余热的热量加热为饱和或者过热蒸气,进入有机工质透平2”做功,驱动发电机3”输出发电量,透平2”的排气进入冷凝器4”中冷却为液态,经由增压泵5”升压后重新进入余热锅炉,形成一个完整的循环,系统如图2所示。Medium and low temperature heat source power generation can adopt organic Rankine cycle technology. The organic Rankine cycle uses low-boiling organic working fluids, such as R123, R113, R245fa, isopentane, etc. The organic working medium is heated by the medium and low temperature waste heat in the waste heat boiler 1" to become saturated or superheated steam, which enters the organic working
发明内容 Contents of the invention
针对上述现有技术存在的缺陷或不足,本发明的目的在于,提供一种基于LNG冷能利用的燃料电池和有机朗肯循环联合发电系统,利用燃气轮机的低温余热热量,同时利用液化天然气的冷能,大大增加了系统的发电量,实现了能量的梯级利用,提高了能源利用率,减少了大气环境污染,符合国家节能减排的需求。Aiming at the defects or deficiencies in the above-mentioned prior art, the purpose of the present invention is to provide a fuel cell and organic Rankine cycle combined power generation system based on LNG cold energy utilization, which utilizes the low-temperature waste heat of gas turbines and simultaneously utilizes the cold energy of liquefied natural gas. It can greatly increase the power generation capacity of the system, realize the cascade utilization of energy, improve the energy utilization rate, reduce atmospheric environmental pollution, and meet the needs of the country for energy conservation and emission reduction.
为实现上述目的,本发明采用以下技术方案:To achieve the above object, the present invention adopts the following technical solutions:
一种基于LNG冷能利用的燃料电池和有机朗肯循环联合发电系统,包括:A fuel cell and organic Rankine cycle combined power generation system based on LNG cold energy utilization, including:
固体氧化物燃料电池和燃气轮机的联合循环系统,其中,空气经一级空气压缩机升压后,进入间冷器进行冷却降温,然后进入二级空气压气机,接着经第一加热器预热后进入固体氧化物燃料电池的阴极电极板;燃料经间冷器升温后,依次经过压气机和第二加热器;水经水泵加压后,通过第三加热器加热,之后与预热后的燃料在混合器中充分混合,最后一同进入固体氧化物燃料电池的阳极电极板;固体氧化物燃料电池阴极排放的未反应完的氧气与阳极未反应完全的可燃气体一同进入与之连接的后燃室进行完全燃烧,产生高温高压燃气;燃气轮机与后燃室相连接,燃气轮机的高温排气依次被送入第一加热器、第二加热器、第三加热器,依次预热空气、燃料和水;The combined cycle system of solid oxide fuel cells and gas turbines, in which the air is boosted by the primary air compressor, then enters the intercooler for cooling and cooling, then enters the secondary air compressor, and then is preheated by the first heater Enter the cathode electrode plate of the solid oxide fuel cell; after the fuel is heated up by the intercooler, it passes through the compressor and the second heater in turn; after the water is pressurized by the water pump, it is heated by the third heater, and then the preheated fuel Fully mixed in the mixer, and finally enter the anode electrode plate of the solid oxide fuel cell together; the unreacted oxygen discharged from the cathode of the solid oxide fuel cell and the unreacted combustible gas of the anode enter the after-combustion chamber connected to it Carry out complete combustion to produce high-temperature and high-pressure gas; the gas turbine is connected to the after-combustion chamber, and the high-temperature exhaust gas from the gas turbine is sent to the first heater, the second heater, and the third heater in sequence to preheat air, fuel and water in sequence;
有机朗肯循环系统,包括依次连接的余热锅炉、有机工质透平、冷凝器、增压泵,其中,所述增压泵的一端与冷凝器相连,另一端与余热锅炉相连,所述余热锅炉的余热来自燃气轮机的高温排气依次预热空气、燃料和水后排出的中低温气体;The organic Rankine cycle system includes a waste heat boiler, an organic working fluid turbine, a condenser, and a booster pump connected in sequence, wherein one end of the booster pump is connected to the condenser, and the other end is connected to the waste heat boiler, and the waste heat The waste heat of the boiler comes from the high-temperature exhaust gas of the gas turbine and the medium-low temperature gas discharged after preheating air, fuel and water in sequence;
LNG冷能源,其存储于LNG存储罐中,与有机朗肯循环系统的冷凝器相连,用以冷凝有机工质透平的排气,然后通过冷库换热器释放冷能,最后,一部分进入间冷器,作为燃料供给燃料电池,多余的部分供给燃气管网。LNG cold energy, which is stored in the LNG storage tank, is connected to the condenser of the organic Rankine cycle system to condense the exhaust gas of the organic working fluid turbine, and then releases the cold energy through the cold storage heat exchanger, and finally, a part of it enters the room The cooler is used as fuel to supply the fuel cell, and the excess part is supplied to the gas pipeline network.
优选的,后燃室产生高温高压燃气进入燃气轮机中做功,驱动与燃气轮机连接的第一发电机发电。Preferably, the high-temperature and high-pressure gas generated by the afterburner enters the gas turbine to perform work, and drives the first generator connected to the gas turbine to generate electricity.
优选的,燃气轮机的高温排气依次预热空气、燃料和水后排出的中低温气体进入余热锅炉,将能量传递给有机工质,使有机工质达到饱和状态或者过热状态,之后工质进入有机工质透平中做功,驱动与有机工质透平同轴连接的第二发电机发电。Preferably, the high-temperature exhaust gas from the gas turbine preheats air, fuel and water in sequence, and the discharged medium-low temperature gas enters the waste heat boiler, transfers energy to the organic working medium, and makes the organic working medium reach a saturated state or a superheated state, and then the working medium enters the organic working medium. Working in the working medium turbine to drive the second generator coaxially connected with the organic working medium turbine to generate electricity.
优选的,燃料和氧气在固体氧化物燃料电池内发生电化学反应后对外输出直流电,经过与固体氧化物燃料电池连接的逆变器转换为交流电输出。Preferably, the fuel and oxygen undergo an electrochemical reaction in the solid oxide fuel cell to output direct current, which is converted into alternating current output by an inverter connected to the solid oxide fuel cell.
优选的,有机朗肯循环系统可运行于亚临界工况下,采用R123、R245fa、R600、R134a、异戊烷、正戊烷、R113、R11、R152a、R236fa、R236ea或R141b制冷剂作为系统运行的工质。Preferably, the organic Rankine cycle system can operate under subcritical conditions, using R123, R245fa, R600, R134a, isopentane, n-pentane, R113, R11, R152a, R236fa, R236ea or R141b refrigerant as the system operation working medium.
优选的,有机朗肯循环系统可运行于超临界工况下,采用二氧化碳、R125或R227ea作为系统运行的工质。Preferably, the organic Rankine cycle system can operate under supercritical conditions, using carbon dioxide, R125 or R227ea as the working fluid for system operation.
与现有技术相比,本发明基于冷能利用的燃料电池和有机朗肯循环联合发电系统至少具有以下优点:Compared with the prior art, the fuel cell and organic Rankine cycle combined power generation system based on cold energy utilization of the present invention has at least the following advantages:
1)显著提高了能源转化效率,减少了污染物排放。固体氧化物燃料电池与燃气轮机的高温排气经过预热燃料、空气和水之后,仍有很高的温度等级,属于中低温余热,采用有机朗肯循环将这些中低温余热进行回收利用,转换为电能输出,可以大大提高了能源转换效率,减少了污染物向环境中的排放。有机朗肯循环的工作介质选择低沸点的有机工质,较常规朗肯循环具有结构尺寸小、效率高、循环压力高、在透平膨胀过程工质不会进入两相区等优点,适合用于中低温余热利用。1) Significantly improved energy conversion efficiency and reduced pollutant emissions. After preheating fuel, air and water, the high-temperature exhaust of solid oxide fuel cells and gas turbines still has a high temperature level, which belongs to medium and low temperature waste heat. The organic Rankine cycle is used to recycle the medium and low temperature waste heat and convert it into The output of electric energy can greatly improve the energy conversion efficiency and reduce the discharge of pollutants into the environment. The working medium of the organic Rankine cycle is an organic working medium with a low boiling point. Compared with the conventional Rankine cycle, it has the advantages of small structure size, high efficiency, high cycle pressure, and the working medium will not enter the two-phase region during the turbine expansion process. It is suitable for Utilize waste heat at medium and low temperature.
2)LNG冷能的利用以及整个联合发电系统性能的改善。LNG首先用来作为动力循环的冷源冷凝有机工质透平的排气,可以使有机工质透平的背压显著降低,增加有机朗肯循环的功率输出。经过冷凝器出来的LNG仍然具有大量冷能,经过冷库换热器释放冷能后,进入空气压缩机的间冷器,冷却一级空气压缩机的排气,从而减小空气压缩机的耗功。2) Utilization of LNG cold energy and improvement of the performance of the entire combined power generation system. LNG is firstly used as a cold source of the power cycle to condense the exhaust gas of the organic working fluid turbine, which can significantly reduce the back pressure of the organic working fluid turbine and increase the power output of the organic Rankine cycle. The LNG coming out of the condenser still has a lot of cold energy. After the cold storage heat exchanger releases the cold energy, it enters the intercooler of the air compressor to cool the exhaust of the first-stage air compressor, thereby reducing the power consumption of the air compressor. .
附图说明 Description of drawings
图1是传统的固体氧化物燃料电池和燃气轮机的联合循环系统的结构框图;Fig. 1 is the structural block diagram of the combined cycle system of traditional solid oxide fuel cell and gas turbine;
图2是传统的有机朗肯循环系统的结构框图;Fig. 2 is a structural block diagram of a traditional organic Rankine cycle system;
图3是本发明基于冷能利用的燃料电池和有机朗肯循环联合发电系统的结构框图。Fig. 3 is a structural block diagram of the fuel cell and organic Rankine cycle combined power generation system based on cold energy utilization in the present invention.
其中,图中标号与元件的对应关系为:Among them, the corresponding relationship between the labels and components in the figure is:
具体实施方式 Detailed ways
下面结合附图对本发明系统的一种实施例进行详细描述:A kind of embodiment of the system of the present invention is described in detail below in conjunction with accompanying drawing:
本发明涉及一种基于LNG冷能利用的固体氧化物燃料电池和有机朗肯循环联合发电系统,采用富氢燃料天然气作为固体氧化物燃料电池的燃料,有机工质作为朗肯循环发电系统的工作介质,可以向外界输出电能。本发明由固体氧化物燃料电池、后燃室、燃气轮机、换热器、透平、冷凝器、增压泵泵、压缩机等组成。固体氧化物燃料电池中未反应完的可燃气体和空气在后燃室中继续燃烧,产生高温高压的燃气,进入燃气轮机做功输出电能,燃气轮机的高温排气依次预热空气、燃料和水,实现燃气余热利用;经预热后燃气排气仍然具有较高的温度等级,属于中低温余热,采用有机朗肯循环将这些中低温余热进行回收利用,转换为电能输出,实现能量的梯级利用;LNG用来作为有机朗肯循环的冷源冷凝有机工质透平的排气,可以使有机工质透平的背压显著降低,增加有机朗肯循环的功率输出,同时利用了LNG的冷能。经过冷凝器出来的LNG仍然具有大量冷能,经过冷库换热器释放冷能后,一部分进入空气压缩机的间冷器,冷却一级空气压缩机的排气,从而减小空气压缩机的耗功,多余的部分供给燃气管网。所发明的系统可以显著提高了能源转化效率,减少了污染物排放,改善系统的性能。The invention relates to a solid oxide fuel cell and organic Rankine cycle combined power generation system based on LNG cold energy utilization, using hydrogen-rich fuel natural gas as the fuel of the solid oxide fuel cell, and organic working fluid as the working medium of the Rankine cycle power generation system A medium that can output electrical energy to the outside world. The invention consists of a solid oxide fuel cell, an afterburner, a gas turbine, a heat exchanger, a turbine, a condenser, a booster pump, a compressor, and the like. The unreacted combustible gas and air in the solid oxide fuel cell continue to burn in the afterburner to generate high-temperature and high-pressure gas, which enters the gas turbine to do work and output electric energy. The high-temperature exhaust of the gas turbine preheats air, fuel and water in sequence to realize gas Waste heat utilization: After preheating, the gas exhaust gas still has a high temperature level, which belongs to the medium and low temperature waste heat. The organic Rankine cycle is used to recycle the medium and low temperature waste heat and convert it into electric energy output to realize the cascade utilization of energy; for LNG Condensing the exhaust gas of the organic working fluid turbine as the cold source of the organic Rankine cycle can significantly reduce the back pressure of the organic working fluid turbine, increase the power output of the organic Rankine cycle, and utilize the cold energy of LNG at the same time. The LNG coming out of the condenser still has a lot of cold energy. After the cold storage heat exchanger releases the cold energy, part of it enters the intercooler of the air compressor to cool the exhaust of the first-stage air compressor, thereby reducing the consumption of the air compressor. work, and the excess is supplied to the gas pipeline network. The invented system can significantly improve energy conversion efficiency, reduce pollutant discharge and improve system performance.
图3是本发明一种基于LNG冷能利用的固体氧化物燃料电池与有机朗肯循环联合发电系统的结构框图,该系统包括一级空气压缩机1、间冷器2、二级空气压缩机3、燃料压缩机4、水泵5、第一加热器6、第二加热器7、第三加热器8、混合器9、固体氧化物燃料电池10、后燃室11、燃气轮机12、发电机I 13、逆变器14、余热锅炉15、有机工质透平16、发电机II 17、冷凝器18、增压泵19、冷库换热器20、燃气管网21和LNG存储罐22。Fig. 3 is a structural block diagram of a solid oxide fuel cell and organic Rankine cycle combined power generation system based on LNG cold energy utilization in the present invention, the system includes a primary air compressor 1, an
实施方案为:空气经过一级空气压缩机1升压后,再通过间冷器2冷却降温,进入二级空气压缩机3,然后经过加热器I 6被燃气透平的高温排气预热,送入固体氧化物燃料电池10的阴极电极板;来自间冷器2升温之后的燃料(天然气)分别经过燃料压缩机4,第二加热器7加热;水在水泵5中加压后,通过第三加热器8加热,与预热后的燃料在混合器9中充分混合,一同送入固体氧化物燃料电池10的阳极电极。燃料和氧气在固体氧化物燃料电池10内发生电化学反应后对外输出直流电,经过逆变器14转换为交流电输出。之后,阴极排放的未反应的氧气与阳极未反应完全的可燃气体进入与之连接的后燃室11进行完全燃烧,产生高温高压燃气,燃气轮机12与后燃室11相连接。高温高压燃气进入燃气轮机12中做功,驱动与其连接的第一发电机13发电。燃气轮机12的高温排气依次被送入第一加热器6、第二加热器7、第三加热器8,依次预热空气、燃料和水,最后排出的中低温气体进入余热锅炉15,将能量传递给有机工质,使有机工质达到饱和状态或者过热状态,之后工质进入有机工质透平16中做功,驱动与其同轴连接的第二发电机17发电,有机工质透平16的排气在冷凝器18中被LNG冷凝成液态,然后经过增压泵19加压后,送入余热锅炉15中被燃气轮机的排气加热。液化天然气(LNG)作为冷源从LNG存储罐22中进入冷凝器18中冷凝有机工质透平16的排气,然后进入冷库换热器20中,释放冷能,之后一部分进入空气压缩机的间冷器2,冷却一级空气压缩机1的排气,然后作为固体氧化物燃料电池10的燃料送到燃料压缩机4;从冷库换热器20中排出的多余部分天然气通入燃气管网。The implementation plan is: after the air is boosted by the primary air compressor 1, it is cooled and cooled by the
本发明系统既可以提高能源转换效率,实现能量梯级利用,又可以利用LNG富含的大量冷能,实现能量梯级利用。The system of the present invention can not only improve the energy conversion efficiency, realize energy cascade utilization, but also utilize a large amount of cold energy rich in LNG to realize energy cascade utilization.
以上所述仅为本发明的一种实施方式,不是全部或唯一的实施方式,本领域普通技术人员通过阅读本发明说明书而对本发明技术方案采取的任何等效的变换,均为本发明的权利要求所涵盖。The above is only one embodiment of the present invention, not all or the only embodiment. Any equivalent transformation of the technical solution of the present invention adopted by those of ordinary skill in the art by reading the description of the present invention is the right of the present invention. covered by the requirements.
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