CN110285398A - A new cogeneration system of concentrated photovoltaics and vapor compression cycle - Google Patents
A new cogeneration system of concentrated photovoltaics and vapor compression cycle Download PDFInfo
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- 230000006835 compression Effects 0.000 title claims abstract description 27
- 238000007906 compression Methods 0.000 title claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 73
- 238000010248 power generation Methods 0.000 claims abstract description 25
- 239000012530 fluid Substances 0.000 claims description 20
- 239000002826 coolant Substances 0.000 claims description 13
- 239000013307 optical fiber Substances 0.000 claims description 3
- 239000012141 concentrate Substances 0.000 claims description 2
- 239000011810 insulating material Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 21
- 239000001257 hydrogen Substances 0.000 abstract description 21
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 16
- 238000005868 electrolysis reaction Methods 0.000 abstract description 14
- 239000000446 fuel Substances 0.000 abstract description 9
- 238000000034 method Methods 0.000 abstract description 8
- 239000002803 fossil fuel Substances 0.000 abstract description 6
- 150000002431 hydrogen Chemical class 0.000 abstract description 5
- 239000007789 gas Substances 0.000 abstract description 4
- 230000007547 defect Effects 0.000 abstract 1
- 239000000110 cooling liquid Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- 230000005611 electricity Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 238000002407 reforming Methods 0.000 description 2
- 230000003595 spectral effect Effects 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/28—Methods of steam generation characterised by form of heating method in boilers heated electrically
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B35/00—Control systems for steam boilers
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Abstract
本发明提供一种聚光光伏与蒸汽压缩循环的新型热电联产系统,属于氢能源的制备装置的技术领域。本发明的热电联产系统包括聚光光伏CPV发电系统和蒸汽压缩循环系统,CPV利用太阳能转换为电能和部分热能,电能输出到外界的水电解槽进行电解制备氢气,热能传导到蒸汽压缩循环系统对水进行加热,使外界水电解槽的水升温增加电解效率。本发明的热电联产系统利用太阳能,可以用来与外界的水电解装置组合,构成一个制备氢气的可循环的完整系统,避免引入化石燃料或者其他电能才可以电解水制备氢气的缺陷,全程不产生尾气污染,特别是为实现高效环保型氢燃料电池打下基础。
The invention provides a novel heat and power cogeneration system of concentrating photovoltaics and a vapor compression cycle, which belongs to the technical field of hydrogen energy preparation devices. The combined heat and power system of the present invention includes a concentrating photovoltaic CPV power generation system and a vapor compression cycle system. The CPV uses solar energy to convert electric energy and part of heat energy. The electric energy is output to an external water electrolyzer for electrolysis to prepare hydrogen, and the heat energy is transferred to the vapor compression cycle system. The water is heated to increase the temperature of the water in the external water electrolysis cell to increase the electrolysis efficiency. The combined heat and power system of the present invention utilizes solar energy and can be used to combine with external water electrolysis devices to form a complete system that can be recycled to prepare hydrogen, avoiding the defect that the introduction of fossil fuels or other electric energy can electrolyze water to prepare hydrogen, and the whole process is seamless. Produce tail gas pollution, especially to lay the foundation for the realization of efficient and environmentally friendly hydrogen fuel cells.
Description
技术领域technical field
本发明属于氢气能源生产装备的技术领域,具体涉及一种新型的热电联产系统。The invention belongs to the technical field of hydrogen energy production equipment, and in particular relates to a novel cogeneration system of heat and power.
背景技术Background technique
目前,氢气作为一种环境友好型的燃料,其生产和应用在民用领域的普及率依然较低,主要问题是制备氢气的效率和成本难以平衡,难以达到理想的商业应用与环保平衡。氢能源已经在燃料电池(Fuel cell“FC”)领域实现商用,FC技术作为商用产品目前主要应用于电动车辆和住宅、工业场所的微型热电联产(m-CHP)系统中。At present, as an environmentally friendly fuel, the penetration rate of hydrogen production and application in the civilian field is still low. The main problem is that the efficiency and cost of hydrogen production are difficult to balance, and it is difficult to achieve the ideal balance between commercial application and environmental protection. Hydrogen energy has been commercialized in the field of fuel cells (Fuel cell "FC"). As a commercial product, FC technology is currently mainly used in electric vehicles and micro combined heat and power (m-CHP) systems in residential and industrial sites.
生产氢气的现有技术包括化石燃料或天然气的重整,这种方法已经在许多基于FC的m-CHP产品中被采用。但是,化石燃料或天然气的重整仍将消耗化石燃料和排放有害污染物,无法从根本上为解决化石能源危机和保护环境。Existing technologies for hydrogen production include reforming of fossil fuels or natural gas, which has been adopted in many FC-based m-CHP products. However, reforming of fossil fuels or natural gas will still consume fossil fuels and emit harmful pollutants, which cannot fundamentally solve the fossil energy crisis and protect the environment.
还有一种现有生产氢的途径是电解水或简单的碳氢化合物,例如甲醇,水的电解更受欢迎,因为它不涉及排放有害的污染,如二氧化碳。实现电解的要求是以纯电、纯热或两者结合的形式输入能量。需要纯热的情况通常被称为热解,然而,这种情况很少在实践中使用,因为达到这种效果所需的温度通常超过2300K。需要纯电的方法是现有应用相对较多的,通常利用高压电来进行电解。然而,阻碍现有电解制氢方法在氢燃料电池上广泛商业化的主要问题是电解槽电源的需求,而输入电源必须由另一种形式的发电提供,这样一来就无法形成一套可高效循环生产氢气能源的体系,应用在氢燃料电池上依旧需要转化化石燃料来提供电解水的电源,无法实现零尾气排放的环保目的。Another existing route to hydrogen production is the electrolysis of water or simple hydrocarbons such as methanol. The electrolysis of water is preferred because it does not involve emitting harmful pollution such as carbon dioxide. Achieving electrolysis requires an input of energy in the form of pure electricity, pure heat, or a combination of both. Situations that require pure heat are often referred to as pyrolysis, however, this is rarely used in practice because the temperatures required to achieve this effect typically exceed 2300K. There are relatively many existing applications that require pure electricity, and high voltage electricity is usually used for electrolysis. However, the main issue preventing the widespread commercialization of existing electrolytic hydrogen production methods on hydrogen fuel cells is the need for electrolyzer power supply, and the input power must be provided by another form of power generation, so that it is impossible to form a set that can be used efficiently. The system of recycling hydrogen energy is still required to convert fossil fuels to provide power for electrolysis of water when applied to hydrogen fuel cells, which cannot achieve the environmental protection goal of zero tail gas emissions.
发明内容Contents of the invention
为解决前述背景技术里提及的现有技术的不足,本发明提供了一种新型的热电联产系统,该系统能够进行自发电并对水进行加热,可以用于配合外部电解槽对水进行电解以获得氢气,并具有自循环发电发热、高效环保无尾气污染的优点。In order to solve the deficiencies of the prior art mentioned in the aforementioned background technology, the present invention provides a new type of combined heat and power system, which can generate electricity by itself and heat water, and can be used to process water with an external electrolyzer. Electrolysis is used to obtain hydrogen, which has the advantages of self-circulation power generation and heat generation, high efficiency, environmental protection and no tail gas pollution.
本发明提供的技术方案如下:The technical scheme provided by the invention is as follows:
一种聚光光伏与蒸汽压缩循环的新型热电联产系统,包括聚光光伏发电装置和蒸汽压缩循环装置;聚光光伏发电装置包括聚光光伏面板;蒸汽压缩循环装置包括蒸汽循环路径和热水箱;蒸汽循环路径内部有冷却液;蒸汽循环路径包括吸热端和放热端,蒸汽循环路径的吸热端连接聚光光伏面板进行热交换,放热端连接热水箱进行热交换;所述热水箱包括进水口和出水口。A new cogeneration system of concentrated photovoltaics and vapor compression cycle, including a concentrated photovoltaic power generation device and a vapor compression cycle device; the concentrated photovoltaic power generation device includes a concentrated photovoltaic panel; the vapor compression cycle device includes a steam cycle path and hot water There is coolant inside the steam circulation path; the steam circulation path includes a heat-absorbing end and a heat-dissipating end, the heat-absorbing end of the steam circulation path is connected to the concentrating photovoltaic panel for heat exchange, and the heat-releasing end is connected to the hot water tank for heat exchange; The hot water tank includes a water inlet and a water outlet.
该系统中的能量转移过程为:聚光光伏面板接收太阳能,对聚光光伏发电装置的外部输出电能,对蒸汽压缩循环装置输出热能;蒸汽压缩循环装置连接在聚光光伏面板向阳侧之外的位置;蒸汽循环路径内的冷却液从聚光光伏面板接收热能,接着将热能传导到与热水箱连接处交换释放,再回到蒸汽循环路径的吸热端处继续接收热能。The energy transfer process in this system is: the concentrated photovoltaic panel receives solar energy, outputs electric energy to the outside of the concentrated photovoltaic power generation device, and outputs heat energy to the vapor compression cycle device; the vapor compression cycle device is connected to the outside of the concentrated photovoltaic panel facing the sun Position; the cooling liquid in the steam circulation path receives heat energy from the concentrated photovoltaic panel, then conducts the heat energy to the connection with the hot water tank for exchange and release, and then returns to the heat-absorbing end of the steam circulation path to continue to receive heat energy.
进一步地,聚光光伏发电装置还包括集线器,集线器为汇集了光学纤维的部件,连接在聚光光伏面板的向阳侧,集线器用于集中外界太阳光输入到聚光光伏面板。Furthermore, the concentrated photovoltaic power generation device further includes a hub, which is a component that collects optical fibers and is connected to the sunny side of the concentrated photovoltaic panel. The hub is used to concentrate external sunlight input to the concentrated photovoltaic panel.
更进一步地,蒸汽循环路径包括流体热交换器、压缩机、换热器、空气散热器、扩展器、第一三通阀门和第二三通阀门;流体热交换器与聚光光伏面板连接,接收聚光光伏面板的热能;压缩机一端连接流体热交换器,另一端连接第二三通阀门的第一端口;第二三通阀门的第二端口、第三端口分别连接换热器、空气散热器;换热器与热水箱连接,向热水箱输出热能;第一三通阀门的第二端口、第三端口分别连接换热器、空气散热器,第三端口连接扩展器的其中一端;扩展器的另一端连接流体热交换器。Furthermore, the steam cycle path includes a fluid heat exchanger, a compressor, a heat exchanger, an air radiator, an expander, a first three-way valve, and a second three-way valve; the fluid heat exchanger is connected to the concentrated photovoltaic panel, Receive the thermal energy of the concentrated photovoltaic panel; one end of the compressor is connected to the fluid heat exchanger, and the other end is connected to the first port of the second three-way valve; the second port and the third port of the second three-way valve are respectively connected to the heat exchanger, air Radiator; the heat exchanger is connected with the hot water tank, and outputs heat energy to the hot water tank; the second port and the third port of the first three-way valve are respectively connected with the heat exchanger and the air radiator, and the third port is connected with one of the expanders one end; the other end of the expander connects to the fluid heat exchanger.
优选地,蒸汽压缩循环装置还包括热管理控制器,热管理控制器为具有温度传感器、控制开关和微处理器的电子设备,温度传感器设置于热水箱处,控制开关分别设置于第二和第二三通阀门处;微处理器分别与温度传感器、控制开关电性连接。Preferably, the vapor compression cycle device also includes a thermal management controller, which is an electronic device with a temperature sensor, a control switch and a microprocessor, the temperature sensor is arranged at the hot water tank, and the control switch is respectively arranged at the second and second At the second three-way valve; the microprocessor is electrically connected with the temperature sensor and the control switch respectively.
优选地,空气散热器为风冷式散热器。Preferably, the air radiator is an air-cooled radiator.
进一步地,蒸汽循环路径内的冷却液的具体循环路径依次为流体热交换器、压缩机、第二三通阀门、空气散热器或者换热器、第一三通阀门、扩展器、流体热交换器。Further, the specific circulation path of the cooling liquid in the steam circulation path is the fluid heat exchanger, the compressor, the second three-way valve, the air radiator or heat exchanger, the first three-way valve, the expander, and the fluid heat exchange device.
进一步地,热水箱由隔热材料制成,热水箱还包括热水出口。Further, the hot water tank is made of heat insulating material, and the hot water tank also includes a hot water outlet.
与现有技术相比,本发明的聚光光伏与蒸汽压缩循环的新型热电联产系统,其有益效果在于:聚光光伏面板CPV是现有的一项高效率的发电技术,配合采用低成本的集线器可以捕获多个不同的光谱范围,有效地利用了太阳光的全部光谱,提高了光伏电池在单位面积上所能放置的数量,从而为实现装置小型化带来可能性。蒸汽循环路径作为主动冷却系统,将聚光光伏发电装置发电过程中产生的热能传导到其他地方,避免了CPV面板温度过高造成的CPV电池发电效率急剧下降的问题,也保护了CPV面板因高温产生的不可逆损伤。现有的主动冷却系统要么过于简单而效率低精准度差,要么装置结构过于复杂无法实现小型化。蒸汽循环路径将聚光光伏发电装置产生的热能,通过冷却液在循环路径内传导到热水箱中,对热水箱中的水进行加热,热水箱中的水升温后再流动到外部电解槽,可以用于提高水电解过程产生氢气的电解效率,冷却液放热扩展后回到聚光光伏面板处进行下一轮的压缩制冷循环。同时由于装置的结构简单且压缩机、扩展器、热交换器等都是小型的部件,配合聚光光伏发电CPV装置和外部水电解槽,在太阳光的驱动下,可以实现一个可再生自循环且零尾气排放的氢燃料电池等其他的小型热电联产系统CHP。Compared with the prior art, the new cogeneration system of concentrating photovoltaics and vapor compression cycle of the present invention has the beneficial effect that: the concentrating photovoltaic panel CPV is an existing high-efficiency power generation technology, and it adopts low-cost The hub can capture multiple different spectral ranges, effectively utilize the entire spectrum of sunlight, and increase the number of photovoltaic cells that can be placed per unit area, thereby bringing the possibility of device miniaturization. As an active cooling system, the steam circulation path conducts the heat energy generated during the power generation process of the concentrated photovoltaic power generation device to other places, avoiding the problem of a sharp drop in the power generation efficiency of the CPV battery caused by the excessive temperature of the CPV panel, and also protecting the CPV panel due to high temperature. resulting irreversible damage. Existing active cooling systems are either too simple and have low efficiency and poor precision, or the device structure is too complicated to achieve miniaturization. The steam circulation path conducts the heat energy generated by the concentrated photovoltaic power generation device to the hot water tank through the cooling liquid in the circulation path, and heats the water in the hot water tank. After the water in the hot water tank is heated up, it flows to the external electrolysis The tank can be used to improve the electrolysis efficiency of hydrogen generated in the water electrolysis process, and the cooling liquid returns to the concentrating photovoltaic panel after exothermic expansion for the next round of compression and refrigeration cycle. At the same time, due to the simple structure of the device and the compressor, expander, heat exchanger, etc. are all small components, combined with the concentrated photovoltaic power generation CPV device and the external water electrolyzer, driven by sunlight, a renewable self-circulation can be realized And other small cogeneration systems CHP such as hydrogen fuel cells with zero exhaust emissions.
附图说明Description of drawings
图1为本发明其中一种实施方式的系统结构示意图;Fig. 1 is a schematic diagram of the system structure of one of the embodiments of the present invention;
图2为图1中实施方式的电、热和化学能的能量转换示意图;Fig. 2 is the schematic diagram of energy conversion of electricity, heat and chemical energy of the embodiment in Fig. 1;
图3为图1中实施方式的热管理控制器的控制算法流程图。FIG. 3 is a flow chart of the control algorithm of the thermal management controller in the embodiment shown in FIG. 1 .
具体实施方式Detailed ways
为进一步阐述本发明的原理与系统结构以及工作过程,现结合说明书附图的内容对其中的一种实施方式进行具体说明。In order to further illustrate the principle, system structure and working process of the present invention, one implementation mode will be described in detail in combination with the contents of the accompanying drawings.
一种聚光光伏与蒸汽压缩循环的新型热电联产系统的其中一种实施方式如图1至3所示。One of the implementations of a novel cogeneration system of concentrated photovoltaics and a vapor compression cycle is shown in Figures 1 to 3 .
如图1所示,该实施方式的热电联产系统包括了聚光光伏发电装置和蒸汽压缩循环装置。聚光光伏发电装置包括了聚光光伏CPV面板、用以汇集光学纤维的集线器。蒸汽压缩循环装置内包括流体热交换器、压缩机、三通阀门V2、风冷式的空气散热器、换热器、三通阀门V1、扩展器、带温度计和控制开关以及微处理器的热管理控制器、由隔热材料制成的热水箱。流体热交换器、压缩机、三通阀门V2、风冷式的空气散热器、换热器、三通阀门V1、扩展器构成了蒸汽压缩循环装置的蒸汽循环路径,整个蒸汽循环路径内依靠冷却液来传导热能;其中空气散热器、换热器、三通阀门V1、扩展器构成了蒸汽循环路径的放热端,流体热交换器、压缩机、三通阀门V2构成了蒸汽循环路径的吸热端;热管理控制器构成了蒸汽循环路径内热能传导路径的控制台。热水箱还具有进水口、热水出口和电解水出口。As shown in FIG. 1 , the cogeneration system of this embodiment includes a concentrated photovoltaic power generation device and a vapor compression cycle device. The concentrating photovoltaic power generation device includes a concentrating photovoltaic CPV panel and a hub for collecting optical fibers. The vapor compression cycle device includes a fluid heat exchanger, a compressor, a three-way valve V2, an air-cooled air radiator, a heat exchanger, a three-way valve V1, an expander, a heat exchanger with a thermometer and a control switch, and a microprocessor. Management controller, hot water tank made of thermal insulation. The fluid heat exchanger, compressor, three-way valve V2, air-cooled air radiator, heat exchanger, three-way valve V1, and expander constitute the steam cycle path of the vapor compression cycle device, and the entire steam cycle path relies on cooling Liquid to conduct heat energy; among them, the air radiator, heat exchanger, three-way valve V1, and expander constitute the exothermic end of the steam circulation path, and the fluid heat exchanger, compressor, and three-way valve V2 constitute the suction end of the steam circulation path. The hot end; the thermal management controller constitutes the console for the thermal energy transfer path within the steam cycle path. The hot water tank also has a water inlet, a hot water outlet and an electrolyzed water outlet.
如图1所示的本实施方式结构原理、图2所示的能量转移途径和图3所示的热能控制算法流程,其中图2的功率变换器指的是前述的CPV面板与蒸汽循环装置内的各种热交换部件。The structural principle of this embodiment shown in Figure 1, the energy transfer path shown in Figure 2, and the thermal energy control algorithm flow shown in Figure 3, wherein the power converter in Figure 2 refers to the aforementioned CPV panel and steam cycle device Various heat exchange components.
聚光光伏CPV面板的向阳侧连接有集线器,太阳光通过集线器汇聚照射到聚光光伏CPV面板内的电池,由太阳能电池将太阳能转换产生电能Ppv,再将电能Ppv输出到压缩机、扩展器、外部水电解槽,同时还可以将多余的电能输出到外部电网,产生的热能则传导到蒸汽压缩循环装置。聚光光伏CPV面板在向阳侧之外的位置连接有流体热交换器,CPV面板产生的热能在此处进入蒸汽压缩循环装置内的冷却液。流体热交换器的一端连接压缩机,冷却液在流体热交换器获得从CPV面板传导来的热能后进入压缩机。压缩机接收CPV面板电能的电源Wc进行工作,压缩机还连接着三通阀门V2的第一端口,冷却液在压缩机内进一步压缩提升热能后通过三通阀门V2,在热管理控制器的控制下,选择流动到空气散热器或者换热器。三通阀门V2的第二和第三端口分别连接空气散热器、换热器。空气散热器将多余热能Qamb辐射到空气中。换热器与热水箱连接,将冷却液中携带的热能交换到热水箱中,从热水箱进水口输入的水经过热交换而升温,热水箱再将热水从电解水出口输出到外部水电解槽电解出氢气、从热水出口将热水输出到外部用户热水终端。三通阀门V1的第二和第三端口分别连接空气散热器或者换热器,第一端口连接扩展器,冷却液经过换热器和三通阀门V1后,在扩展器内进一步降压释放热能。扩展器的另一端与流体热交换器连接,冷却液被扩展器运送到流体热交换器进行下一个循环。The sun-facing side of the concentrated photovoltaic CPV panel is connected to a hub, and the sunlight is concentrated and irradiated to the battery in the concentrated photovoltaic CPV panel through the hub. device, external water electrolyzer, and at the same time, excess electric energy can be exported to the external power grid, and the heat energy generated is conducted to the vapor compression cycle device. The concentrating photovoltaic CPV panel is connected to a fluid heat exchanger at a position other than the sunny side, where the heat energy generated by the CPV panel enters the cooling liquid in the vapor compression cycle device. One end of the fluid heat exchanger is connected to the compressor, and the coolant enters the compressor after the fluid heat exchanger obtains heat energy conducted from the CPV panel. The compressor works by receiving the power W c of the electric energy of the CPV panel. The compressor is also connected to the first port of the three-way valve V2. After the coolant is further compressed in the compressor to increase heat energy, it passes through the three-way valve V2. Under control, select flow to air radiator or heat exchanger. The second and third ports of the three-way valve V2 are respectively connected to the air radiator and the heat exchanger. The air radiator radiates excess thermal energy Q amb into the air. The heat exchanger is connected to the hot water tank to exchange the heat energy carried in the coolant into the hot water tank, the water input from the water inlet of the hot water tank is heated up through heat exchange, and the hot water tank then outputs hot water from the electrolyzed water outlet The hydrogen is electrolyzed to the external water electrolyzer, and the hot water is output from the hot water outlet to the external user hot water terminal. The second and third ports of the three-way valve V1 are respectively connected to the air radiator or heat exchanger, and the first port is connected to the expander. After the coolant passes through the heat exchanger and the three-way valve V1, the pressure is further reduced in the expander to release heat energy. . The other end of the expander is connected with the fluid heat exchanger, and the coolant is transported by the expander to the fluid heat exchanger for the next cycle.
热管理控制器的温度计设计在热水箱处。控制开关分别设置于三通阀门V1、V2处,能控制三通阀门V1、V2的三个端口各自的开合状态。热管理控制器的微处理器内置有控制算法的程序。如图3所示,热水箱处的温度均表示为Tw,控制算法内设定有一个温度上限阀值为Th,还设定有一个温度下限阀值为Tl。开始时,温度计读取热水箱中的水温Tw,经过微处理器与设定的温度阀值Th与Tl进行比较,当Tw低于Tl,控制开关使三通阀门V1和V2关闭冷却液流经空气散热器的通道,由冷却液将热量全部带到换热器处对热水箱中的水进行交换;在继续加热热水箱中的水,使得Tw大于Tl且小于Th时,控制开关使三通阀门V1和V2保持当前通道;当Tw高于Th时,则控制开关使三通阀门V1和V2关闭冷却液流经换热器的路径,使冷却液在空气散热器处将过多的热能辐射到空气中;最后当Tw的数值回到大于Tl且小于Th时,继续保持关闭冷却液流经换热器的路径而只通过空气散热器的通道。The thermometer of the thermal management controller is designed at the hot water tank. The control switches are arranged at the three-way valves V1 and V2 respectively, and can control the respective opening and closing states of the three ports of the three-way valves V1 and V2. The microprocessor of the thermal management controller is programmed with a control algorithm. As shown in Figure 3, the temperature at the hot water tank is denoted as T w , an upper temperature threshold value T h is set in the control algorithm, and a temperature lower limit threshold value T l is also set. At the beginning, the thermometer reads the water temperature Tw in the hot water tank, and compares it with the set temperature threshold Th and Tl through the microprocessor . When Tw is lower than Tl , the control switch makes the three-way valve V1 and V2 closes the channel through which the coolant flows through the air radiator, and the coolant takes all the heat to the heat exchanger to exchange the water in the hot water tank; continue to heat the water in the hot water tank so that T w is greater than T l and is less than T h , the control switch makes the three-way valves V1 and V2 maintain the current channel; when T w is higher than T h , the control switch makes the three-way valves V1 and V2 close the path of the coolant flowing through the heat exchanger, so that The coolant radiates too much heat energy into the air at the air radiator; finally when the value of T w returns to be greater than T l and less than T h , continue to close the path of the coolant flowing through the heat exchanger and only pass through the air Channels for radiators.
本实施方式相比现有的热电联产系统,抛弃了传统的化石燃料发电为水电解槽提供电源,发热为水加热的方式,改用高效率的聚光光伏CPV面板进行发电和加热,即避免了尾气污染,也构成了一个自循环的热电联产系统。集线器应用在CPV面板上,可以捕获多个不同的光谱范围,有效地利用了太阳光的全部光谱,提高了光伏电池在单位面积上所能放置的数量,进而为实现发电产热装置的小型化带来基础。蒸汽压缩循环装置充分利用CPV面板产生的大量余热,既对水相内的水进行加热,为外部电解水制备氢气提供了更好的反应条件,也同时也实现了对CPV面板进行降温,避免CPV面板温度过高造成发电效率大幅降低甚至损坏光伏电池的问题。蒸汽压缩循环优于其他典型技术,如热电冷却器,因为它可以提供更高的性能系数,这意味着能耗更低。此外,为了进一步提高系统的功率效率,所采用的蒸汽压缩循环还涉及到由空气散热器组成的备选路径,以及一组开关阀来决定是否使用该组件或热水的路径。两个不同的蒸汽压缩循环路径,配合热管理控制器对冷却液的循环路径进行选择,使得整个热电联产系统可以维持一个能量输入输出动态平衡的过程。由于蒸汽压缩循环装置和聚光光发电装置都可以实现小型化,那么本实施方式的热电联产系统可以结合外部水电解槽形成一个小型的依靠太阳能进行可再生发电的氢燃料系统,为新型氢燃料电池及产热设备的小型化带来良好前景。Compared with the existing combined heat and power generation system, this embodiment abandons the traditional fossil fuel power generation to provide power for the water electrolyzer, and uses the high-efficiency concentrating photovoltaic CPV panel for power generation and heating, namely It avoids tail gas pollution and also constitutes a self-circulating combined heat and power system. The hub is applied to the CPV panel, which can capture multiple different spectral ranges, effectively utilize the entire spectrum of sunlight, increase the number of photovoltaic cells that can be placed per unit area, and further contribute to the miniaturization of power generation and heat generation devices. Bring the base. The vapor compression cycle device makes full use of the large amount of waste heat generated by the CPV panel, which not only heats the water in the water phase, but also provides better reaction conditions for the external electrolysis of water to produce hydrogen, and also realizes the cooling of the CPV panel to avoid CPV Excessive panel temperature will greatly reduce the power generation efficiency and even damage the photovoltaic cells. The vapor compression cycle is superior to other typical technologies, such as thermoelectric coolers, because it can provide a higher coefficient of performance, which means lower energy consumption. Furthermore, to further increase the power efficiency of the system, the employed vapor compression cycle also involves an alternate path consisting of an air radiator, and a set of on-off valves to decide whether to use this component or the hot water path. Two different vapor compression circulation paths, combined with the thermal management controller to select the cooling liquid circulation path, enable the entire combined heat and power system to maintain a dynamic balance process of energy input and output. Since both the vapor compression cycle device and the concentrated photoelectric power generation device can be miniaturized, the combined heat and power system of this embodiment can be combined with an external water electrolyzer to form a small hydrogen fuel system that relies on solar energy for renewable power generation. The miniaturization of fuel cells and heat generating equipment brings good prospects.
以上实施方式只是本发明的其中一种方案,用以解释本发明的技术原理,并非本发明的全部实施例。本领域技术人员应当清楚,在上述实施方式的基础上,任何没有做出突出实质性特定和显著进步的等同替换方案,均落入本发明的范围。本发明技术方案的保护范围由权利要求书界定。The above implementation is only one of the schemes of the present invention, and is used to explain the technical principle of the present invention, but not all the embodiments of the present invention. It should be clear to those skilled in the art that, on the basis of the above-mentioned embodiments, any equivalent replacement scheme without outstanding substantive specificity and significant progress falls within the scope of the present invention. The protection scope of the technical solution of the present invention is defined by the claims.
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