CN103807009A - Solar energy and alternative fuel complementary distributed internal combustion engine cooling heating and power system and method - Google Patents
Solar energy and alternative fuel complementary distributed internal combustion engine cooling heating and power system and method Download PDFInfo
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- 239000000446 fuel Substances 0.000 title claims abstract description 256
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 156
- 238000001816 cooling Methods 0.000 title claims abstract description 65
- 230000000295 complement effect Effects 0.000 title claims abstract description 61
- 238000010438 heat treatment Methods 0.000 title claims abstract description 57
- 238000000034 method Methods 0.000 title claims abstract description 29
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 118
- 239000003546 flue gas Substances 0.000 claims abstract description 118
- 238000006243 chemical reaction Methods 0.000 claims abstract description 97
- 239000002918 waste heat Substances 0.000 claims abstract description 97
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 73
- 239000007789 gas Substances 0.000 claims abstract description 62
- 238000011084 recovery Methods 0.000 claims abstract description 55
- 238000004146 energy storage Methods 0.000 claims abstract description 38
- 238000010248 power generation Methods 0.000 claims abstract description 32
- 238000005057 refrigeration Methods 0.000 claims abstract description 31
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims description 66
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 57
- 239000007788 liquid Substances 0.000 claims description 45
- 238000010521 absorption reaction Methods 0.000 claims description 44
- 229910052739 hydrogen Inorganic materials 0.000 claims description 26
- 239000001257 hydrogen Substances 0.000 claims description 26
- 239000000463 material Substances 0.000 claims description 26
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 25
- 238000001704 evaporation Methods 0.000 claims description 13
- 230000008020 evaporation Effects 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 9
- 238000000926 separation method Methods 0.000 claims description 8
- 238000000354 decomposition reaction Methods 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims description 4
- 238000006057 reforming reaction Methods 0.000 claims description 4
- 239000003517 fume Substances 0.000 claims 17
- 230000003993 interaction Effects 0.000 claims 11
- 238000007599 discharging Methods 0.000 claims 4
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- 230000005611 electricity Effects 0.000 abstract description 16
- 239000000126 substance Substances 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 description 22
- 230000005855 radiation Effects 0.000 description 13
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 239000002737 fuel gas Substances 0.000 description 5
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- 239000000047 product Substances 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
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- 239000003502 gasoline 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
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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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B10/00—Integration of renewable energy sources in buildings
- Y02B10/20—Solar thermal
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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
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/44—Heat exchange systems
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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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/14—Combined heat and power generation [CHP]
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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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
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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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/30—Use of alternative fuels, e.g. biofuels
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Abstract
本发明公开了一种太阳能与替代燃料互补的分布式内燃机冷热电系统及方法,该系统包括太阳能与替代燃料互补反应的蓄能系统、太阳能燃料内燃机发电系统、太阳能燃料烟气余热吸收式溴化锂制冷系统、烟气余热回收反应装置、尾气余热回收换热器和缸套水板式换热器。利用本发明,采用的太阳能与替代燃料互补实现了太阳能向燃料化学能的转化;使光转化合成气燃料储存,且与内燃机冷热电联产系统耦合,不仅储能密度高、储能装置容积小,而且同时达到低成本、高效的太阳能冷、热、电联供的多功能目的,而非单独的高成本的太阳能发电、供冷、供热,因此有效地解决了现有太阳能热利用蓄能难、成本高和效率低的问题。
The invention discloses a distributed internal combustion engine cooling and heating power system and method in which solar energy and alternative fuels are complementary. Refrigeration system, flue gas waste heat recovery reaction device, tail gas waste heat recovery heat exchanger and cylinder jacket water plate heat exchanger. Utilizing the present invention, the solar energy and alternative fuels used complement each other to realize the conversion of solar energy into fuel chemical energy; the photo-converted syngas fuel is stored, and coupled with the internal combustion engine cooling, heating and power cogeneration system, not only the energy storage density is high, but the volume of the energy storage device is also high. It is small, and at the same time achieves the multi-functional purpose of low-cost, high-efficiency solar cooling, heating, and electricity co-supply, rather than separate high-cost solar power generation, cooling, and heating, so it effectively solves the problem of existing solar thermal utilization storage problems of difficulty, high cost and low efficiency.
Description
技术领域technical field
本发明涉及多能源互补及新能源和节能减排技术领域,具体是一种太阳能与替代燃料互补的分布式内燃机冷热电系统及方法。The invention relates to the technical fields of multi-energy complementarity and new energy, energy saving and emission reduction, in particular to a distributed internal combustion engine cooling, heating and power system and method that complement solar energy and alternative fuels.
背景技术Background technique
利用太阳热能发电、制冷和供热,是实现我国2020年非化石能源占一次能源消费比重达到15%左右目标的主要措施之一。但由于太阳能能量密度低、不连续和蓄能难,造成太阳能利用率低下,开发利用程度受到严重限制。特别是对于太阳能热发电,无论采用槽式还是塔式的太阳能热发电技术,高温不稳定的大热流密度吸收器和发电工质温度低造成的成本高、效率低等技术瓶颈,是太阳能热发电无法规模化应用的主要根源。另外,当单独利用太阳热能来供暖或制冷时,由于太阳能不稳定、不连续性与采暖、制冷需求相对稳定存在矛盾。The use of solar thermal energy for power generation, refrigeration and heating is one of the main measures to achieve the goal of non-fossil energy accounting for about 15% of primary energy consumption in my country by 2020. However, due to the low energy density, discontinuity and difficulty in energy storage of solar energy, the utilization rate of solar energy is low, and the degree of development and utilization is severely limited. Especially for solar thermal power generation, regardless of the trough-type or tower-type solar thermal power generation technology, the technical bottlenecks such as high cost and low efficiency caused by the high heat flux density absorber with high temperature instability and low temperature of the power generation working medium are the key factors for solar thermal power generation. The main root cause of inability to scale applications. In addition, when solar thermal energy is used alone for heating or cooling, there is a contradiction between the instability and discontinuity of solar energy and the relative stability of heating and cooling requirements.
太阳能热利用与其他资源互补,特别是太阳能与化石能源互补,是目前解决太阳能利用率低、不连续问题的一个主要途径。国际上太阳热能与化石能源互补多是在太阳能达不到所需温度或无太阳能时,由化石燃料直接燃烧供给能量。这种简单的太阳能集热与化石燃料直接燃烧的互补技术在太阳能供热、制冷以及太阳能热发电系统中广泛使用。但它没有注重不同资源互补过程的能量品位对口和匹配,仅仅是一种不同资源的简单叠加利用。Solar thermal utilization and other resources complement each other, especially solar energy and fossil energy, which is a main way to solve the problem of low and discontinuous utilization of solar energy. Internationally, the complementarity between solar thermal energy and fossil energy is that when the solar energy does not reach the required temperature or there is no solar energy, the fossil fuel is directly burned to supply energy. This simple complementary technology of solar thermal collection and direct combustion of fossil fuels is widely used in solar heating, cooling and solar thermal power generation systems. However, it does not pay attention to the matching and matching of energy grades in the complementary process of different resources. It is just a simple superimposed utilization of different resources.
以内燃机为动力核心的冷热电联产系统是当前具有较好应用前景的分布式能源系统。相对燃气轮机,内燃机不仅装置成本低,而且在低负荷运行工况下,具有相对好的部分负荷特性。但目前汽油或柴油内燃机为动力核心的冷热电系统大多存在严重污染物排放问题。另外,在冬季,过高温度的排烟余热(400-600℃)直接供暖,造成了大量余热的浪费。因此,如何实现变工况下高效稳定运行,即保证变工况下互补系统的发电功率稳定且太阳能净发电功率接近设计值,同时实现太阳能资源的充分有效利用,成为了太阳能与火电站互补技术的急需解决的重要技术问题。The combined cooling, heating and power system with the internal combustion engine as the power core is currently a distributed energy system with good application prospects. Compared with gas turbines, internal combustion engines not only have low installation costs, but also have relatively good part-load characteristics under low-load operating conditions. However, at present, most of the cooling, heating and power systems with gasoline or diesel internal combustion engines as the power core have serious pollutant emission problems. In addition, in winter, the excessively high temperature exhaust waste heat (400-600°C) is directly used for heating, resulting in a large waste of waste heat. Therefore, how to achieve efficient and stable operation under variable conditions, that is, to ensure that the power generation of the complementary system is stable under variable conditions and the net solar power is close to the design value, and at the same time realize the full and effective use of solar resources has become a complementary technology for solar energy and thermal power stations. Important technical issues that urgently need to be resolved.
发明内容Contents of the invention
(一)要解决的技术问题(1) Technical problems to be solved
有鉴于此,本发明的主要目的在于提供一种太阳能与替代燃料互补的分布式内燃机冷热电系统及方法,以解决现有太阳能热利用蓄能难、成本高和效率低的问题。In view of this, the main purpose of the present invention is to provide a distributed internal combustion engine cold heating and power system and method complementary to solar energy and alternative fuels, so as to solve the problems of difficult energy storage, high cost and low efficiency of existing solar heat utilization.
(二)技术方案(2) Technical solutions
为达到上述目的,本发明提供了一种太阳能与替代燃料互补的分布式内燃机冷热电系统,该系统包括太阳能与替代燃料互补反应的蓄能系统100、太阳能燃料内燃机发电系统200、太阳能燃料烟气余热吸收式溴化锂制冷系统300、烟气余热回收反应装置15、尾气余热回收换热器16和缸套水板式换热器17,其中:In order to achieve the above-mentioned purpose, the present invention provides a distributed internal combustion engine cooling and heating power system in which solar energy and alternative fuels complement each other. Gas waste heat absorption lithium bromide refrigeration system 300, flue gas waste heat recovery reaction device 15, tail gas waste heat recovery heat exchanger 16 and cylinder jacket water plate heat exchanger 17, in which:
太阳能与替代燃料互补反应的蓄能系统100,采用槽式聚光镜4将太阳能聚光投射到沿槽式聚光镜4焦线布置的管式吸热反应器5上,驱动管式吸热反应器5中的替代燃料分解或重整为太阳能燃料;The energy storage system 100 for the complementary reaction of solar energy and alternative fuels uses the trough condenser 4 to concentrate and project the solar energy onto the tubular endothermic reactor 5 arranged along the focal line of the trough condenser 4, and drives the tubular endothermic reactor 5 Alternative fuels decomposed or reformed into solar fuels;
太阳能燃料内燃机发电系统200,包括燃气内燃机11和发电机12,Solar fuel internal combustion engine power generation system 200, including gas internal combustion engine 11 and generator 12,
太阳能与替代燃料互补反应的蓄能系统100产生的太阳能燃料直接驱动内燃机11发电,通过内燃机11气缸内燃烧释放高温热量,经发电机12转化为电能并输出;The solar fuel generated by the energy storage system 100 of complementary reactions between solar energy and alternative fuels directly drives the internal combustion engine 11 to generate electricity, and releases high-temperature heat through combustion in the cylinder of the internal combustion engine 11, which is converted into electrical energy by the generator 12 and output;
太阳能燃料烟气余热吸收式溴化锂制冷系统300,包括烟气换热器13和蒸汽型双效溴化锂制冷机组14,太阳能燃料在内燃机11中燃烧发电后的烟气余热,经烟气换热器13产生蒸汽,驱动蒸汽型双效溴化锂制冷机组14制冷并输出;The solar fuel flue gas waste heat absorption lithium bromide refrigeration system 300 includes a flue gas heat exchanger 13 and a steam type double-effect lithium bromide refrigeration unit 14. The waste heat of the flue gas after the solar fuel is burned in the internal combustion engine 11 for power generation passes through the flue gas heat exchanger 13 Generate steam to drive the steam-type double-effect lithium bromide refrigeration unit 14 to refrigerate and output;
烟气余热回收反应装置15,内燃机11排出的烟气和在太阳能辐照不足或阴天下雨时经预热蒸发器3预热的替代燃料均进入烟气余热回收反应装置15,烟气余热提供替代燃料转换为富氢燃料需要的反应热,使替代燃料全部转换为富氢燃料进入内燃机11,剩余的烟气余热分别进入烟气换热器13和尾气余热回收换热器16;The flue gas waste heat recovery reaction device 15, the flue gas discharged from the internal combustion engine 11 and the substitute fuel preheated by the preheating evaporator 3 when the solar radiation is insufficient or cloudy and rainy all enter the flue gas waste heat recovery reaction device 15, and the flue gas waste heat provides The heat of reaction required for the conversion of the alternative fuel into a hydrogen-rich fuel makes all the alternative fuel converted into a hydrogen-rich fuel and enters the internal combustion engine 11, and the remaining flue gas waste heat enters the flue gas heat exchanger 13 and the tail gas waste heat recovery heat exchanger 16 respectively;
尾气余热回收换热器16,烟气换热器13产生的蒸汽和烟气余热回收反应装置15中送来的烟气经尾气余热回收换热器16加热给水产生生活热水;The exhaust heat recovery heat exchanger 16, the steam generated by the flue gas heat exchanger 13 and the flue gas sent from the flue gas waste heat recovery reaction device 15 pass through the tail gas waste heat recovery heat exchanger 16 to heat the feed water to generate domestic hot water;
缸套水板式换热器17,内燃机11的缸套水通过缸套水板式换热器17加热给水产生生活热水,产生的生活热水同时提供给预热蒸发器3使用。The jacket water plate heat exchanger 17, the jacket water of the internal combustion engine 11 heats the feed water through the jacket water plate heat exchanger 17 to generate domestic hot water, and the generated domestic hot water is simultaneously provided to the preheating evaporator 3 for use.
为达到上述目的,本发明还提供了一种太阳能与替代燃料互补的分布式内燃机冷热电方法,应用于所述的系统,该方法包括:In order to achieve the above purpose, the present invention also provides a distributed cooling and heating method for internal combustion engines in which solar energy and alternative fuels are complementary, which is applied to the above-mentioned system, and the method includes:
太阳能与替代燃料互补反应的蓄能系统100采用槽式聚光镜4将太阳能聚光投射到沿槽式聚光镜4焦线布置的管式吸热反应器5上,驱动管式吸热反应器5中的替代燃料分解或重整为太阳能燃料;The energy storage system 100 for the complementary reaction of solar energy and alternative fuels adopts the trough-type concentrator 4 to concentrate and project the solar energy onto the tubular endothermic reactor 5 arranged along the focal line of the trough-type concentrator 4, and drives the Decomposition or reformation of alternative fuels into solar fuels;
太阳能与替代燃料互补反应的蓄能系统100产生的太阳能燃料直接驱动太阳能燃料内燃机发电系统200中的内燃机11发电,通过内燃机11气缸内燃烧释放高温热量,经太阳能燃料内燃机发电系统200中的发电机12转化为电能并输出;The solar fuel produced by the energy storage system 100 of complementary reactions between solar energy and alternative fuels directly drives the internal combustion engine 11 in the solar fuel internal combustion engine power generation system 200 to generate electricity, and releases high-temperature heat through combustion in the cylinder of the internal combustion engine 11. 12 converted into electrical energy and output;
太阳能燃料在内燃机11中燃烧发电后的烟气余热,经太阳能燃料烟气余热吸收式溴化锂制冷系统300中的烟气换热器13产生蒸汽,驱动太阳能燃料烟气余热吸收式溴化锂制冷系统300中的蒸汽型双效溴化锂制冷机组14制冷并输出。The waste heat of the flue gas after the combustion of the solar fuel in the internal combustion engine 11 generates steam through the flue gas heat exchanger 13 in the solar fuel flue gas waste heat absorption lithium bromide refrigeration system 300 to drive the solar fuel flue gas waste heat absorption lithium bromide refrigeration system 300 The vapor type double-effect lithium bromide refrigeration unit 14 is refrigerated and exported.
(三)有益效果(3) Beneficial effects
从上述技术方案可以看出,本发明具有以下有益效果:As can be seen from the foregoing technical solutions, the present invention has the following beneficial effects:
1、本发明提供太阳能与替代燃料互补的分布式内燃机冷热电系统,采用的太阳能与替代燃料互补实现了太阳能向燃料化学能的转化。内燃机动力采用的是替代燃料二次转化后的燃烧,不是替代燃料的直接燃烧。使光转化合成气燃料储存,且与内燃机冷热电联产系统耦合,不仅储能密度高、储能装置容积小,而且同时达到低成本、高效的太阳能冷、热、电联供的多功能目的;而且还可依据冷热负荷变化,通过调节太阳能燃料燃烧烟气量,既可太阳能热电联供、也可冷电联供。本发明非单独的高成本的太阳能发电、供冷、供热,因此有效地解决了现有太阳能热利用蓄能难、成本高和效率低的问题。1. The present invention provides a distributed internal combustion engine cooling and heating power system in which solar energy and alternative fuels are complementary, and the solar energy and alternative fuels used are complementary to realize the conversion of solar energy into fuel chemical energy. The power of the internal combustion engine is the combustion after the secondary conversion of the alternative fuel, not the direct combustion of the alternative fuel. The photo-converted syngas fuel is stored and coupled with the internal combustion engine cooling, heating and power cogeneration system, which not only has a high energy storage density and a small volume of the energy storage device, but also achieves low-cost, high-efficiency solar cooling, heating, and electricity. Purpose; Moreover, according to the change of cooling and heating load, by adjusting the flue gas volume of solar fuel combustion, it can be used for both solar heat and power cogeneration and cooling and power cogeneration. The invention is not independent high-cost solar power generation, cooling and heating, so it effectively solves the problems of difficult energy storage, high cost and low efficiency of existing solar thermal utilization.
2、本发明提供太阳能与替代燃料互补的分布式内燃机冷热电系统,具有容量小、太阳能能源综合利用率高及经济性好等特点。对于集热面积325m2,集热功率140kW的槽式太阳能吸收反应系统与一台额定功率为380kW的内燃机的冷热电相结合的联产系统。若设定太阳能年运行时间2500h,太阳辐照强度600W/m2,甲醇燃料2000元/吨。该互补系统年供电量可达到90.3万kWh,年供冷量达到53.2万kWh,年供热量达到72.4万kWh,年一次能源节能率达到30.2%,互补系统全年能量综合利用效率达到70-80%。太阳能净发电效率达到25-28%,远超于太阳能单独发电10-17%的水平。若以冷价0.45元/kWh,热价0.3元/kWh,电价1.08元/kWh计算,容量为380kW的太阳能与替代燃料互补的分布式内燃机冷热电联产系统,其单位装置投资成本约5000元/kW,投资回收期在8年左右,远低于现有太阳能热发电技术投资成本。2. The present invention provides a distributed internal combustion engine cooling and heating system complementary to solar energy and alternative fuels, which has the characteristics of small capacity, high comprehensive utilization rate of solar energy, and good economy. For a heat collection area of 325m 2 , a cogeneration system that combines a trough solar absorption reaction system with a heat collection power of 140kW and an internal combustion engine with a rated power of 380kW. If the annual running time of solar energy is set to 2500h, the solar radiation intensity is 600W/m 2 , and the methanol fuel is 2000 yuan/ton. The annual power supply of the complementary system can reach 903,000 kWh, the annual cooling capacity can reach 532,000 kWh, the annual heat supply can reach 724,000 kWh, the annual primary energy saving rate can reach 30.2%, and the annual comprehensive energy utilization efficiency of the complementary system can reach 70- 80%. The net power generation efficiency of solar energy reaches 25-28%, far exceeding the 10-17% level of solar power generation alone. If the cold price is 0.45 yuan/kWh, the heat price is 0.3 yuan/kWh, and the electricity price is 1.08 yuan/kWh, the distributed internal combustion engine cooling, heating and power cogeneration system with a capacity of 380kW complementary to solar energy and alternative fuels has a unit investment cost of about 5,000 yuan Yuan/kW, the investment payback period is about 8 years, which is far lower than the investment cost of existing solar thermal power generation technology.
3、本发明提供太阳能与替代燃料互补的分布式内燃机冷热电系统,如果与单一太阳能光伏发电、太阳能供热、供冷的分产技术比较,保守考虑互补系统的太阳能集热效率50%,太阳能供热及制冷集热效率70%,光伏发电效率15%。在输出相同的冷、电、热的情况下,该互补分布式供能系统可节约太阳能集热面积24%,也就是说,太阳能镜场占地面积和投资成本将比分产减少24%。3. The present invention provides a distributed internal combustion engine cooling and heating power system that is complementary to solar energy and alternative fuels. If compared with a single solar photovoltaic power generation, solar heating, and cooling production technology, it is conservatively considered that the solar heat collection efficiency of the complementary system is 50%, and the solar energy The heat collection efficiency of heating and cooling is 70%, and the efficiency of photovoltaic power generation is 15%. In the case of the same cooling, electricity, and heat output, this complementary distributed energy supply system can save 24% of the solar heat collection area, that is to say, the area occupied by the solar mirror field and the investment cost will be reduced by 24% compared with production.
4、本发明提供太阳能与替代燃料互补的分布式内燃机冷热电系统,采用太阳能与替代燃料互补,通过内燃机冷热电实现中低温太阳能高效、高质利用,突破了太阳能单独发电、制冷和供暖成本高、效率低的技术瓶颈。具有小型化、灵活、分散、和较好的经济性、环保性特点,可广泛应用于荒漠、边防哨所等偏僻地区的小规模供电、制冷及供热,具有重要的经济和社会价值。4. The present invention provides a distributed internal combustion engine cooling and heating power system that complements solar energy and alternative fuels, uses solar energy and alternative fuels to complement each other, realizes high-efficiency and high-quality utilization of medium and low temperature solar energy through internal combustion engine cooling and heating, and breaks through the independent power generation, cooling and heating of solar energy The technical bottleneck of high cost and low efficiency. With the characteristics of miniaturization, flexibility, decentralization, good economy and environmental protection, it can be widely used in small-scale power supply, cooling and heating in remote areas such as deserts and border posts, and has important economic and social value.
附图说明Description of drawings
图1是本发明提供太阳能与替代燃料互补的分布式内燃机冷热电系统的结构示意图。Fig. 1 is a structural schematic diagram of a distributed internal combustion engine cooling, heating and power system that provides complementary solar energy and alternative fuels according to the present invention.
图2是本发明提供的太阳能与替代燃料互补的分布式内燃机冷热电方法的流程图。Fig. 2 is a flow chart of the distributed internal combustion engine cooling and heating power method provided by the present invention which is complementary to solar energy and alternative fuels.
附图标记:Reference signs:
100太阳能与替代燃料互补反应的蓄能系统:100 Energy storage systems with complementary reactions between solar energy and alternative fuels:
1原料罐,2原料泵,3预热蒸发器,4槽式聚光镜,5管式吸热反应器,6冷凝器,7气液分离器,8压气机,9储气罐,10循环泵;1. Raw material tank, 2. Raw material pump, 3. Preheating evaporator, 4. Slot type condenser, 5. Tube type endothermic reactor, 6. Condenser, 7. Gas-liquid separator, 8. Compressor, 9. Gas storage tank, 10. Circulation pump;
200太阳能燃料内燃机发电系统:200 solar fuel internal combustion engine power generation system:
11内燃机,12发电机;11 internal combustion engine, 12 generator;
300太阳能燃料烟气余热吸收式溴化锂制冷系统:300 solar fuel flue gas waste heat absorption lithium bromide refrigeration system:
13烟气换热器,14蒸汽型双效溴化锂制冷机组;13 flue gas heat exchanger, 14 steam type double-effect lithium bromide refrigeration unit;
15烟气余热回收反应装置;15 Flue gas waste heat recovery reaction device;
16尾气余热回收换热器;16 Exhaust waste heat recovery heat exchanger;
17缸套水板式换热器。17 cylinder jacket water plate heat exchanger.
具体实施方式Detailed ways
为使本发明的目的、技术方案和优点更加清楚明白,以下结合具体实施例,并参照附图,对本发明进一步详细说明。In order to make the object, technical solution and advantages of the present invention clearer, the present invention will be described in further detail below in conjunction with specific embodiments and with reference to the accompanying drawings.
本发明的核心思想是:首先通过集成太阳能与替代燃料转化的热化学互补,取消太阳能热利用的传统蓄能装置;再与内燃机发电系统、吸收式制冷系统和供暖及热水系统的集成,可以为用户同时提供冷、热、电,实现中低温太阳能高效、低成本的综合利用。The core idea of the present invention is: firstly, by integrating the thermochemical complementarity of solar energy and alternative fuel conversion, canceling the traditional energy storage device for solar heat utilization; Provide users with cold, heat, and electricity at the same time, and realize the comprehensive utilization of medium and low temperature solar energy with high efficiency and low cost.
本发明首先通过互补式的管式吸热反应器,将聚集的150~300℃的太阳能通过替代燃料重整或裂解,被提升到高品位二次富氢燃料(H2、CO2、CO)化学能的形式。太阳能燃料经压缩机、储气罐进入小型或中型内燃机燃烧,推动发电机组发电,从而实现了中低温太阳能的高效热发电。夏季,太阳能燃料燃烧后的高温烟气余热,经余热锅炉和溴化锂余热吸收式制冷系统,提供夏季的冷负荷,完成太阳能燃料余热的制冷利用,尾气及缸套冷却水提供热水负荷。冬季,缸套水余热和尾气部分余热通过热交换器提供供暖和生活热水负荷。In the present invention, firstly, the accumulated solar energy at 150-300°C is reformed or cracked by alternative fuels through complementary tubular endothermic reactors, and then upgraded to high-grade secondary hydrogen-rich fuels (H 2 , CO 2 , CO) form of chemical energy. The solar fuel enters the small or medium-sized internal combustion engine for combustion through the compressor and the gas storage tank, and drives the generator set to generate electricity, thus realizing the high-efficiency thermal power generation of medium and low temperature solar energy. In summer, the waste heat of high-temperature flue gas after solar fuel combustion provides cooling load in summer through the waste heat boiler and lithium bromide waste heat absorption refrigeration system to complete the cooling utilization of solar fuel waste heat, and the exhaust gas and cylinder jacket cooling water provide hot water load. In winter, the waste heat of cylinder jacket water and part of exhaust gas provide heating and domestic hot water load through heat exchangers.
如图1所示,本发明提供的太阳能与替代燃料互补的分布式内燃机冷热电系统,包括太阳能与替代燃料互补反应的蓄能系统100,太阳能燃料内燃机发电系统200、太阳能燃料烟气余热吸收式溴化锂制冷系统300、烟气余热回收反应装置15、尾气余热回收换热器16和缸套水板式换热器17。As shown in Figure 1, the distributed internal combustion engine cooling and heating power system with solar energy and alternative fuels complementary provided by the present invention includes an energy storage system 100 for complementary reactions between solar energy and alternative fuels, a solar fuel internal combustion engine power generation system 200, and solar fuel flue gas waste heat absorption Type lithium bromide refrigeration system 300, flue gas waste heat recovery reaction device 15, tail gas waste heat recovery heat exchanger 16 and cylinder jacket water plate heat exchanger 17.
其主要连接方式是:太阳能与替代燃料互补反应的蓄能系统100通过管道分别与太阳能燃料内燃机发电系统200、烟气余热回收反应装置15及缸套水板式换热器17连接,太阳能燃料内燃机发电系统200通过管道分别与太阳能与替代燃料互补反应的蓄能系统100、太阳能燃料烟气余热吸收式溴化锂制冷系统300、烟气余热回收反应装置15及缸套水板式换热器17连接,太阳能燃料烟气余热吸收式溴化锂制冷系统300通过管道分别与太阳能燃料内燃机发电系统200、烟气余热回收反应装置15及尾气余热回收换热器16连接。所有连接管道均设置有阀门进行控制。Its main connection mode is: the energy storage system 100 of the complementary reaction between solar energy and alternative fuels is respectively connected with the solar fuel internal combustion engine power generation system 200, the flue gas waste heat recovery reaction device 15 and the cylinder jacket water plate heat exchanger 17 through pipelines, and the solar fuel internal combustion engine generates electricity. The system 200 is respectively connected with the energy storage system 100 for the complementary reaction of solar energy and alternative fuels, the solar fuel flue gas waste heat absorption lithium bromide refrigeration system 300, the flue gas waste heat recovery reaction device 15 and the cylinder jacket water plate heat exchanger 17 through pipelines. The flue gas waste heat absorption lithium bromide refrigeration system 300 is respectively connected with the solar fuel internal combustion engine power generation system 200 , the flue gas waste heat recovery reaction device 15 and the tail gas waste heat recovery heat exchanger 16 through pipelines. All connecting pipes are provided with valves for control.
太阳能与替代燃料互补反应的蓄能系统100包括原料罐1、原料泵2、预热蒸发器3、槽式聚光镜4、管式吸热反应器5、冷凝器6、气液分离器7、压气机8、储气罐9和循环泵10。太阳能与替代燃料互补反应的蓄能系统100采用槽式聚光镜4将太阳能聚光投射到沿槽式聚光镜4焦线布置的管式吸热反应器5上,驱动管式吸热反应器5中的替代燃料分解或重整为太阳能燃料。替代燃料是甲醇和二甲醚等。经太阳能热化学反应,转化并直接储存为H2、CO2、CO等太阳能燃料。太阳能经槽式聚光镜4聚集,投射到沿槽式聚光镜4的焦线布置的管式吸收反应器5;原料罐1中的替代燃料经混合后,由原料泵2送至预热蒸发器3中进行预热、蒸发和过热,形成的原料气进入管式吸热反应器5,在管式吸热反应器5内吸收150℃~300℃太阳热能,进行分解或重整反应;自管式吸热反应器5出口的产物,包括H2、CO、CO2及未反应物料,进入冷凝器6中冷却降温,产生的气液混合物进入气液分离器7实现气液分离,气液分离器7生成的燃料经压气机8进入太阳能燃料储气罐9。The energy storage system 100 for the complementary reaction of solar energy and alternative fuels includes a raw material tank 1, a raw material pump 2, a preheating evaporator 3, a trough condenser 4, a tubular endothermic reactor 5, a condenser 6, a gas-liquid separator 7, a compressed air Machine 8, gas storage tank 9 and circulation pump 10. The energy storage system 100 for the complementary reaction of solar energy and alternative fuels adopts the trough-type concentrator 4 to concentrate and project the solar energy onto the tubular endothermic reactor 5 arranged along the focal line of the trough-type concentrator 4, and drives the Alternative fuels are broken down or reformed into solar fuels. Alternative fuels are methanol and dimethyl ether etc. After solar thermochemical reaction, it is converted and directly stored as solar fuels such as H 2 , CO 2 , and CO. The solar energy is collected by the trough condenser 4 and projected to the tubular absorption reactor 5 arranged along the focal line of the trough condenser 4; the substitute fuel in the raw material tank 1 is mixed and sent to the preheating evaporator 3 by the raw material pump 2 Carry out preheating, evaporation and overheating, and the formed raw material gas enters the tubular endothermic reactor 5, absorbs 150 ℃ ~ 300 ℃ solar heat energy in the tubular endothermic reactor 5, and performs decomposition or reforming reaction; The products at the outlet of the thermal reactor 5, including H 2 , CO, CO 2 and unreacted materials, enter the condenser 6 for cooling and cooling, and the gas-liquid mixture produced enters the gas-liquid separator 7 to realize gas-liquid separation, and the gas-liquid separator 7 The generated fuel enters the solar fuel gas storage tank 9 through the compressor 8 .
太阳能燃料内燃机发电系统200包括燃气内燃机11和发电机12。在所述太阳能燃料内燃机发电系统200中,太阳能与替代燃料互补反应的蓄能系统100产生的太阳能燃料与来自外部的空气经空气混合器和气体压缩机后进入内燃机11燃烧,释放高温热量,产生的高温烟气经发电机组12发电,实现电力输出。其中,高温烟气中含有H2O、N2、O2,以及少量的CO2。内燃机11内燃烧的是太阳能燃料,排出的烟气进入到烟气余热回收反应装置15。The solar fuel internal combustion engine power generation system 200 includes a gas internal combustion engine 11 and a generator 12 . In the solar fuel internal combustion engine power generation system 200, the solar fuel generated by the energy storage system 100 in which solar energy and alternative fuels are complementary reacts and the air from the outside enters the internal combustion engine 11 for combustion after passing through an air mixer and a gas compressor, releasing high-temperature heat and generating The high-temperature flue gas generates electricity through the generator set 12 to realize power output. Among them, the high-temperature flue gas contains H 2 O, N 2 , O 2 and a small amount of CO 2 . The internal combustion engine 11 burns solar fuel, and the exhausted flue gas enters the flue gas waste heat recovery reaction device 15 .
太阳能燃料烟气余热吸收式溴化锂制冷系统300包括烟气换热器13和蒸汽型双效溴化锂制冷机组14。在所述太阳能燃料烟气余热吸收式溴化锂制冷系统300中,烟气换热器13将内燃机11排出的烟气转化为蒸汽,在夏季制冷季节驱动蒸汽型双效溴化锂制冷机组14实现制冷,完成内燃机排烟余热的制冷利用;在冬季供暖季节产生供暖热水,经尾气余热回收换热器16加热给水产生生活热水,完成内燃机排烟余热的供暖利用。The solar fuel flue gas waste heat absorption lithium bromide refrigeration system 300 includes a flue gas heat exchanger 13 and a steam type double-effect lithium bromide refrigeration unit 14 . In the solar fuel flue gas waste heat absorption type lithium bromide refrigeration system 300, the flue gas heat exchanger 13 converts the flue gas discharged from the internal combustion engine 11 into steam, and drives the steam type double-effect lithium bromide refrigeration unit 14 to realize refrigeration in the summer cooling season, and completes Refrigeration utilization of exhaust heat from internal combustion engines; hot water for heating is generated during the winter heating season, and the exhaust heat recovery heat exchanger 16 heats the feed water to generate domestic hot water to complete the heating utilization of exhaust heat from internal combustion engines.
所述缸套水板式换热器17利用所述内燃机11的缸套水加热给水产生生活热水,产生的生活热水同时提供给预热蒸发器3来满足燃料的预热和蒸发的热量需求。The jacket water plate heat exchanger 17 utilizes the jacket water of the internal combustion engine 11 to heat the feed water to generate domestic hot water, and the generated domestic hot water is simultaneously provided to the preheating evaporator 3 to meet the heat requirements for fuel preheating and evaporation .
烟气余热回收反应装置15与太阳能与替代燃料互补反应的蓄能系统100并行。在太阳能辐照不足或阴天下雨时,启动烟气余热回收反应装置15,经预热蒸发器3预热的替代燃料与内燃机11排出的烟气均进入烟气余热回收反应装置15,烟气余热提供替代燃料转换为富氢燃料需要的反应热,使替代燃料全部转换为富氢燃料进入内燃机11,剩余的烟气余热分别进入烟气换热器13和尾气余热回收换热器16,在烟气换热器13产生蒸汽,在夏季制冷季节驱动蒸汽型双效溴化锂制冷机组14实现制冷;在尾气余热回收换热器16中加热给水产生生活热水。在烟气余热回收反应装置15中,甲醇可以转换为合成气,以保证内燃机工作过程中的燃料供应。The flue gas waste heat recovery reaction device 15 is parallel to the energy storage system 100 for the complementary reaction of solar energy and alternative fuels. When the solar radiation is insufficient or it is cloudy and rainy, start the flue gas waste heat recovery reaction device 15, the alternative fuel preheated by the preheating evaporator 3 and the flue gas discharged from the internal combustion engine 11 all enter the flue gas waste heat recovery reaction device 15, and the flue gas The waste heat provides the reaction heat required to convert the alternative fuel into hydrogen-rich fuel, so that all the alternative fuel is converted into hydrogen-rich fuel and enters the internal combustion engine 11, and the remaining flue gas waste heat enters the flue gas heat exchanger 13 and the exhaust heat recovery heat exchanger 16 respectively, The flue gas heat exchanger 13 generates steam, and drives the steam-type double-effect lithium bromide refrigeration unit 14 to realize cooling in the summer cooling season; heats feed water in the tail gas waste heat recovery heat exchanger 16 to generate domestic hot water. In the flue gas waste heat recovery reaction device 15, methanol can be converted into synthesis gas to ensure fuel supply during the operation of the internal combustion engine.
在烟气余热回收反应装置15中,内燃机11排出的烟气和在太阳能辐照不足或阴天下雨时经预热蒸发器3预热的替代燃料均进入烟气余热回收反应装置15,烟气余热提供替代燃料转换为富氢燃料需要的反应热,使替代燃料全部转换为富氢燃料进入内燃机11,剩余的烟气余热分别进入烟气换热器13和尾气余热回收换热器16。In the flue gas waste heat recovery reaction device 15, the flue gas discharged from the internal combustion engine 11 and the substitute fuel preheated by the preheating evaporator 3 when the solar radiation is insufficient or cloudy and rainy all enter the flue gas waste heat recovery reaction device 15, and the flue gas The waste heat provides the reaction heat needed to convert the alternative fuel into hydrogen-rich fuel, so that all the alternative fuel is converted into hydrogen-rich fuel and enters the internal combustion engine 11, and the remaining flue gas waste heat enters the flue gas heat exchanger 13 and the tail gas waste heat recovery heat exchanger 16 respectively.
在烟气余热回收反应装置15中,烟气余热提供甲醇燃料转换为富氢燃料需要的反应热,使替代燃料全部转换,以保证进入内燃机11的燃料燃烧是富氢燃料的燃烧,而非替代燃料的直接燃烧。In the flue gas waste heat recovery reaction device 15, the flue gas waste heat provides the reaction heat required for methanol fuel to be converted into hydrogen-rich fuel, so that all alternative fuels are converted, so as to ensure that the combustion of fuel entering the internal combustion engine 11 is the combustion of hydrogen-rich fuel, rather than alternative fuel. direct combustion of fuel.
烟气换热器13产生的蒸汽和烟气余热回收反应装置15中送来的烟气经尾气余热回收换热器16加热给水产生生活热水。The steam generated by the flue gas heat exchanger 13 and the flue gas sent from the flue gas waste heat recovery reaction device 15 heat the feed water through the tail gas waste heat recovery heat exchanger 16 to generate domestic hot water.
本发明提供的这种太阳能与替代燃料互补的分布式内燃机冷热电系统,可以在不同负荷、不同场合下,通过控制系统采用不同方式运行,具有共同实现中低温太阳能高效、高质的发电、制冷、供热的功能。The distributed internal combustion engine cooling, heating and power system that complements solar energy and alternative fuels provided by the present invention can operate in different ways through the control system under different loads and different occasions, and has the ability to jointly realize high-efficiency and high-quality power generation of medium and low temperature solar energy, Cooling and heating functions.
太阳能与替代燃料互补反应具有蓄能作用,但不需要设置蓄热装置。在太阳能充足时,甲醇燃料预热、蒸发过程由太阳能提供热量;阴天和冬天由内燃机尾气及缸套冷却水等余热提供。太阳能驱动替代燃料是通过物料循环的反应过程,不是物料一次通过反应过程。在太阳能辐照高于设计辐照强度时,可用燃料气罐,将多余生产的合成气储存。The complementary reaction of solar energy and alternative fuels has the function of energy storage, but no heat storage device is required. When the solar energy is sufficient, the preheating and evaporation process of methanol fuel is provided by solar energy; on cloudy days and winter, it is provided by waste heat such as exhaust gas of internal combustion engine and cylinder jacket cooling water. Solar-driven alternative fuels are a reaction process through material circulation, not a material-pass reaction process. When the solar radiation is higher than the design radiation intensity, the fuel gas tank can be used to store the excess produced synthesis gas.
根据冷热负荷变化,本发明提供的这种太阳能与替代燃料互补的分布式内燃机冷热电系统,通过调节烟气换热器13产生的蒸汽量,既可热电联供也可冷电联供。没有冷热负荷时,可以通过控制装置,解耦制冷和供热子系统,进行太阳能与替代燃料互补的内燃机单独发电。According to the change of cooling and heating load, the distributed internal combustion engine cooling, heating and power system provided by the present invention, which is complementary to solar energy and alternative fuels, can be used for combined heat and power supply or combined cooling and power supply by adjusting the amount of steam generated by the flue gas heat exchanger 13 . When there is no cooling and heating load, the cooling and heating subsystems can be decoupled through the control device, and the internal combustion engine that complements the solar energy and alternative fuels can generate electricity independently.
在太阳能与替代燃料互补反应的蓄能系统100中,管式吸热反应器5采用一次通过反应和物料循环反应两种方式。在控制策略上,满足太阳能利用份额最大化和物料流量最大条件下,根据太阳能辐照变化,通过关启原料循环泵10,可以采用一次通过反应和物料循环反应两种模式。当太阳辐照强度很大,能满足替代燃料完全反应需要温度,关闭循环泵10,采用一次通过转化运行方式;自管式吸热反应器5出口的产物,包括H2、CO、CO2及未反应物料,进入冷凝器6中冷却降温,产生的气液混合物进入气液分离器7实现气液分离,气液分离器7生成的燃料经压气机8进入太阳能燃料储气罐9。当太阳辐照强度不能保证物料最大流量下的完全转化,开启循环泵10,采用物料循环和物料部分反应的方式;未反应物料从气液分离器7进入原料罐1,与原料罐1中的替代燃料混合后,经原料泵2送至预热蒸发器3中进行预热、蒸发和过热,形成的原料气进入管式吸热反应器5,进行循环使用。In the energy storage system 100 of complementary reaction of solar energy and alternative fuels, the tubular endothermic reactor 5 adopts two modes of one-pass reaction and material circulation reaction. In terms of control strategy, under the conditions of maximizing the utilization of solar energy and maximizing the material flow rate, according to the variation of solar radiation, by turning on and off the raw material circulation pump 10, two modes of one-pass reaction and material circulation reaction can be adopted. When the solar radiation intensity is very high and the temperature required for the complete reaction of the alternative fuel can be satisfied, the circulating pump 10 is turned off, and a one-pass conversion operation mode is adopted; the products from the outlet of the tubular endothermic reactor 5 include H 2 , CO, CO 2 and The unreacted materials enter the condenser 6 to cool down, and the gas-liquid mixture produced enters the gas-liquid separator 7 to realize gas-liquid separation, and the fuel generated by the gas-liquid separator 7 enters the solar fuel gas storage tank 9 through the compressor 8. When the solar radiation intensity cannot guarantee the complete conversion under the maximum flow rate of the material, the circulation pump 10 is turned on, and the mode of material circulation and partial reaction of the material is adopted; the unreacted material enters the raw material tank 1 from the gas-liquid separator 7, and the After the substitute fuel is mixed, it is sent to the preheating evaporator 3 by the raw material pump 2 for preheating, evaporation and superheating, and the formed raw material gas enters the tubular endothermic reactor 5 for recycling.
管式吸热反应器5出口的反应产物主要是H2、CO、CO2和未参加反应的甲醇燃料。反应产物经冷凝器6冷却和气液分离器7分离,以H2、CO、CO2为主要成分的太阳能燃料被压缩进入储气罐9。未反应的反应产物进入原料罐1,通过原料泵2、预热蒸发器3和管式吸热反应器5,进行循环使用。The reaction products at the outlet of tubular endothermic reactor 5 are mainly H 2 , CO, CO 2 and unreacted methanol fuel. The reaction product is cooled by the condenser 6 and separated by the gas-liquid separator 7 , and the solar fuel mainly composed of H 2 , CO, and CO 2 is compressed into the gas storage tank 9 . The unreacted reaction product enters the raw material tank 1, and is recycled through the raw material pump 2, the preheating evaporator 3 and the tubular endothermic reactor 5.
太阳能与替代燃料互补反应的蓄能系统100的储气罐9出口管道与内燃机11燃料进口管道相连。太阳能燃料在内燃机11汽缸内燃烧,释放高温热量,驱动内燃机,转化为高质电能利用。内燃机11燃烧的是太阳能燃料,是太阳能驱动替代燃料重整或热解带来组分发生变化和热值增加的二次燃料的燃烧。The outlet pipeline of the gas storage tank 9 of the energy storage system 100 for the complementary reaction of solar energy and alternative fuels is connected with the fuel inlet pipeline of the internal combustion engine 11 . The solar fuel burns in the internal combustion engine 11 cylinders, releases high-temperature heat, drives the internal combustion engine, and converts it into high-quality electric energy for utilization. The internal combustion engine 11 burns solar fuel, which is the combustion of secondary fuel with composition change and calorific value increase brought about by reforming or pyrolysis of alternative fuel driven by solar energy.
甲醇燃料预热、蒸发过程可以由太阳能提供热量,阴天和冬天,可以采用由缸套水板式换热器17冷却水的余热提供。Methanol fuel preheating, evaporation process can be provided by solar energy heat, cloudy day and winter, can adopt the waste heat provided by the cooling water of jacket water plate heat exchanger 17.
基于图1所示的系统,图2示出了本发明提供的太阳能与替代燃料互补的分布式内燃机冷热电方法的流程图,该方法包括:Based on the system shown in Fig. 1, Fig. 2 shows a flow chart of the distributed internal combustion engine cooling and heating power method provided by the present invention, which is complementary to solar energy and alternative fuels. The method includes:
步骤1:太阳能与替代燃料互补反应的蓄能系统100采用槽式聚光镜4将太阳能聚光投射到沿槽式聚光镜4焦线布置的管式吸热反应器5上,驱动管式吸热反应器5中的替代燃料分解或重整为太阳能燃料;Step 1: The energy storage system 100 for the complementary reaction of solar energy and alternative fuels adopts the trough condenser 4 to concentrate and project the solar energy onto the tubular endothermic reactor 5 arranged along the focal line of the trough condenser 4, and drives the tubular endothermic reactor Alternative fuels in 5 decompose or reform into solar fuels;
步骤2:太阳能与替代燃料互补反应的蓄能系统100产生的太阳能燃料直接驱动太阳能燃料内燃机发电系统200中的内燃机11发电,通过内燃机11气缸内燃烧释放高温热量,经太阳能燃料内燃机发电系统200中的发电机12转化为电能并输出;Step 2: The solar fuel generated by the energy storage system 100 of the complementary reaction between solar energy and alternative fuels directly drives the internal combustion engine 11 in the solar fuel internal combustion engine power generation system 200 to generate electricity, and releases high-temperature heat through combustion in the cylinder of the internal combustion engine 11 , and passes through the solar fuel internal combustion engine power generation system 200 The generator 12 is converted into electrical energy and output;
步骤3:太阳能燃料在内燃机11中燃烧发电后的烟气余热,经太阳能燃料烟气余热吸收式溴化锂制冷系统300中的烟气换热器13产生蒸汽,驱动太阳能燃料烟气余热吸收式溴化锂制冷系统300中的蒸汽型双效溴化锂制冷机组14制冷并输出。Step 3: The waste heat of the flue gas after the solar fuel is burned in the internal combustion engine 11 for power generation is generated by the flue gas heat exchanger 13 in the solar fuel flue gas waste heat absorption lithium bromide refrigeration system 300 to drive the solar fuel flue gas waste heat absorption lithium bromide refrigeration system The steam-type double-effect lithium bromide refrigeration unit 14 in the system 300 refrigerates and outputs.
在步骤1中,所述太阳能与替代燃料互补反应的蓄能系统100包括原料罐1、原料泵2、预热蒸发器3、槽式聚光镜4、管式吸热反应器5、冷凝器6、气液分离器7、压气机8和储气罐9,其中:太阳能经槽式聚光镜4聚集,投射到沿槽式聚光镜4的焦线布置的管式吸收反应器5;原料罐1中的替代燃料经混合后,由原料泵2送至预热蒸发器3中进行预热、蒸发和过热,形成的原料气进入管式吸热反应器5,在管式吸热反应器5内吸收150℃~300℃太阳热能,进行分解或重整反应;自管式吸热反应器5出口的产物,包括H2、CO、CO2及未反应物料,进入冷凝器6中冷却降温,产生的气液混合物进入气液分离器7实现气液分离,气液分离器7生成的燃料经压气机8进入太阳能燃料储气罐9。In step 1, the energy storage system 100 for the complementary reaction of solar energy and alternative fuels includes a raw material tank 1, a raw material pump 2, a preheating evaporator 3, a trough condenser 4, a tubular endothermic reactor 5, a condenser 6, Gas-liquid separator 7, gas compressor 8 and gas storage tank 9, wherein: solar energy is collected through trough-type concentrator 4, and projected to tubular absorption reactor 5 arranged along the focal line of trough-type concentrator 4; After the fuel is mixed, it is sent to the preheating evaporator 3 by the raw material pump 2 for preheating, evaporation and superheating, and the formed raw material gas enters the tubular endothermic reactor 5 and absorbs 150°C ~300℃ solar heat energy, for decomposition or reformation reaction; the products from the outlet of tubular endothermic reactor 5, including H 2 , CO, CO 2 and unreacted materials, enter the condenser 6 to cool down and produce gas-liquid The mixture enters the gas-liquid separator 7 to realize gas-liquid separation, and the fuel generated by the gas-liquid separator 7 enters the solar fuel gas storage tank 9 through the compressor 8 .
进一步地,所述太阳能与替代燃料互补反应的蓄能系统100还包括循环泵10,连接于气液分离器7与原料罐1之间,当太阳辐照强度不能保证物料最大流量下的完全转化,开启循环泵10,采用物料循环和物料部分反应的方式;未反应物料从气液分离器7进入原料罐1,与原料罐1中的替代燃料混合后,经原料泵2送至预热蒸发器3中进行预热、蒸发和过热,形成的原料气进入管式吸热反应器5,进行循环使用。当太阳辐照强度很大,能满足替代燃料完全反应需要温度,关闭循环泵10,采用一次通过转化运行方式;自管式吸热反应器5出口的产物,包括H2、CO、CO2及未反应物料,进入冷凝器6中冷却降温,产生的气液混合物进入气液分离器7实现气液分离,气液分离器7生成的燃料经压气机8进入太阳能燃料储气罐9。Further, the energy storage system 100 for the complementary reaction of solar energy and alternative fuels also includes a circulation pump 10, connected between the gas-liquid separator 7 and the raw material tank 1, when the solar radiation intensity cannot guarantee the complete conversion of the material under the maximum flow rate , turn on the circulation pump 10, adopt the mode of material circulation and material partial reaction; the unreacted material enters the raw material tank 1 from the gas-liquid separator 7, and after mixing with the alternative fuel in the raw material tank 1, it is sent to the preheating evaporation via the raw material pump 2 Preheating, evaporation and superheating are carried out in the reactor 3, and the raw material gas formed enters the tubular endothermic reactor 5 for recycling. When the solar radiation intensity is very high and the temperature required for the complete reaction of the alternative fuel can be satisfied, the circulating pump 10 is turned off, and a one-pass conversion operation mode is adopted; the products from the outlet of the tubular endothermic reactor 5 include H 2 , CO, CO 2 and The unreacted materials enter the condenser 6 to cool down, and the gas-liquid mixture produced enters the gas-liquid separator 7 to realize gas-liquid separation, and the fuel generated by the gas-liquid separator 7 enters the solar fuel gas storage tank 9 through the compressor 8.
在图2所示的方法中,在太阳能辐照不足或阴天下雨时,启动烟气余热回收反应装置15,经预热蒸发器3预热的替代燃料与内燃机11排出的烟气均进入烟气余热回收反应装置15,烟气余热提供替代燃料转换为富氢燃料需要的反应热,使替代燃料全部转换为富氢燃料进入内燃机11,剩余的烟气余热分别进入烟气换热器13和尾气余热回收换热器16,在烟气换热器13产生蒸汽,在夏季制冷季节驱动蒸汽型双效溴化锂制冷机组14实现制冷;在尾气余热回收换热器16中加热给水产生生活热水。在所述烟气余热回收反应装置15中,内燃机11排出的烟气余热提供替代燃料转换为富氢燃料需要的反应热,使替代燃料全部转换,以保证进入内燃机11的燃料燃烧是富氢燃料的燃烧,而非替代燃料的直接燃烧。In the method shown in Figure 2, when the solar radiation is insufficient or it is cloudy and rainy, the flue gas waste heat recovery reaction device 15 is started, and the alternative fuel preheated by the preheating evaporator 3 and the flue gas discharged from the internal combustion engine 11 all enter the flue gas. Gas waste heat recovery reaction device 15, the flue gas waste heat provides the reaction heat required for the conversion of alternative fuels into hydrogen-rich fuels, so that all the alternative fuels are converted into hydrogen-rich fuels and enter the internal combustion engine 11, and the remaining flue gas waste heat enters the flue gas heat exchanger 13 and The exhaust heat recovery heat exchanger 16 generates steam in the flue gas heat exchanger 13, and drives the steam-type double-effect lithium bromide refrigeration unit 14 to realize cooling in the summer cooling season; the exhaust heat recovery heat exchanger 16 heats feed water to generate domestic hot water. In the flue gas waste heat recovery reaction device 15, the waste heat of the flue gas discharged from the internal combustion engine 11 provides the reaction heat needed to convert the alternative fuel into a hydrogen-rich fuel, so that all the alternative fuels are converted to ensure that the fuel entering the internal combustion engine 11 is hydrogen-rich fuel. Combustion of fuel, rather than direct combustion of alternative fuels.
内燃机11排出的烟气和在太阳能辐照不足或阴天下雨时经预热蒸发器3预热的替代燃料均进入烟气余热回收反应装置15,烟气余热提供替代燃料转换为富氢燃料需要的反应热,使替代燃料全部转换为富氢燃料进入内燃机11,剩余的烟气余热分别进入烟气换热器13和尾气余热回收换热器16。内燃机11的缸套水通过缸套水板式换热器17加热给水产生生活热水,产生的生活热水同时提供给预热蒸发器3使用。烟气换热器13产生的蒸汽和烟气余热回收反应装置15中送来的烟气经尾气余热回收换热器16加热给水产生生活热水。The flue gas discharged from the internal combustion engine 11 and the alternative fuel preheated by the preheating evaporator 3 all enter the flue gas waste heat recovery reaction device 15 when the solar radiation is insufficient or it is cloudy and rainy. The heat of reaction of the alternative fuel is converted into hydrogen-rich fuel and enters the internal combustion engine 11, and the remaining flue gas waste heat enters the flue gas heat exchanger 13 and the tail gas waste heat recovery heat exchanger 16 respectively. The jacket water of the internal combustion engine 11 is heated by the jacket water plate heat exchanger 17 to generate domestic hot water, and the generated domestic hot water is simultaneously provided to the preheating evaporator 3 for use. The steam generated by the flue gas heat exchanger 13 and the flue gas sent from the flue gas waste heat recovery reaction device 15 heat the feed water through the tail gas waste heat recovery heat exchanger 16 to generate domestic hot water.
下面以一个具体例子来说明。西部某边防哨所地区,需要有电力、供暖、生活热水和制冷需求。该地区太阳能可利用的时间段内年平均辐照强度约为400W/m2。年均电力负荷(全年)为110kW,年均生活热水负荷为70kW,制冷负荷为100kW(制冷季节),供暖负荷为80kW(供暖季节)。Let's take a specific example to illustrate. A border post area in the west needs electricity, heating, domestic hot water and cooling. The annual average irradiance intensity in this region is about 400W/m 2 during the period when solar energy is available. The annual average electricity load (annual year) is 110kW, the annual average domestic hot water load is 70kW, the cooling load is 100kW (cooling season), and the heating load is 80kW (heating season).
若采用本发明提出的太阳能与替代燃料互补的分布式内燃机冷热电系统,根据负荷情况,可采用方案的主要设备及参数如表1所示。If the distributed internal combustion engine cooling and heating power system proposed by the present invention is complementary to solar energy and alternative fuels, the main equipment and parameters of the scheme that can be used are shown in Table 1 according to the load conditions.
表1主要设备及参数Table 1 main equipment and parameters
本实施例太阳能净发电量116kW,制冷110kW,年满负荷运行时间为8760小时,年供电量100万kWh,年耗甲醇650吨,年制冷量为32万kWh,年供暖量24万kWh,年供热水量52万kWh。系统可在7年内回收投资。In this embodiment, the net solar power generation is 116kW, the refrigeration is 110kW, the annual full-load operation time is 8760 hours, the annual power supply is 1 million kWh, the annual methanol consumption is 650 tons, the annual cooling capacity is 320,000 kWh, and the annual heating capacity is 240,000 kWh. The hot water supply capacity is 520,000 kWh. The system can pay back the investment within 7 years.
若采用甲醇燃烧的分产系统,即购买网电,并使用甲醇锅炉加热生活热水。按照网电效率为30.4%(考虑8%的网损后),甲醇热水锅炉效率为85%,则在与联产相同产出的情况下,分产系统共需要消耗甲醇800吨。由此可以看出,本发明提供的太阳能与替代燃料互补的分布式内燃机冷热电系统节能率可达23%。If the methanol burning system is adopted, the grid electricity is purchased and the methanol boiler is used to heat domestic hot water. According to the grid power efficiency of 30.4% (after considering the 8% grid loss), the efficiency of the methanol hot water boiler is 85%, then in the case of the same output as the joint production, the separate production system needs to consume a total of 800 tons of methanol. It can be seen from this that the energy saving rate of the distributed internal combustion engine cooling, heating and power system complementary to solar energy and alternative fuels provided by the present invention can reach 23%.
如果夏季制冷季节和冬季供暖季节用20%的烟气余热分解甲醇,则年供电量为100万kWh,年制冷量为26万kWh,年供暖量为19万kWh,年供热水量为50万kWh,年耗甲醇量650吨,系统可在8年内回收投资。If methanol is decomposed with 20% waste heat of flue gas in summer cooling season and winter heating season, the annual power supply is 1 million kWh, the annual cooling capacity is 260,000 kWh, the annual heating capacity is 190,000 kWh, and the annual heating capacity is 500,000 kWh kWh, the annual methanol consumption is 650 tons, and the system can recover the investment within 8 years.
若采用甲醇燃烧的分产系统,即购买网电,并使用甲醇锅炉加热生活热水。按照网电效率为30.4%(考虑8%的网损后),甲醇热水锅炉效率为85%,则在与联产相同产出的情况下,分产系统共需要消耗甲醇789吨。由此可以看出,本发明提供的太阳能与替代燃料互补的分布式内燃机冷热电系统节能率可达20.2%。If the methanol burning system is adopted, the grid electricity is purchased and the methanol boiler is used to heat domestic hot water. According to the grid power efficiency of 30.4% (after considering the 8% grid loss), the efficiency of the methanol hot water boiler is 85%, then in the case of the same output as the joint production, the separate production system needs to consume a total of 789 tons of methanol. It can be seen from this that the energy saving rate of the distributed internal combustion engine cooling, heating and power system complementary to solar energy and alternative fuels provided by the present invention can reach 20.2%.
以上所述的具体实施例,对本发明的目的、技术方案和有益效果进行了进一步详细说明,所应理解的是,以上所述仅为本发明的具体实施例而已,并不用于限制本发明,凡在本发明的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The specific embodiments described above have further described the purpose, technical solutions and beneficial effects of the present invention in detail. It should be understood that the above descriptions are only specific embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included within the protection scope of the present invention.
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