CN104359233B - Solar energy tracking focuses on generating and refrigeration system - Google Patents
Solar energy tracking focuses on generating and refrigeration system Download PDFInfo
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- CN104359233B CN104359233B CN201410597106.4A CN201410597106A CN104359233B CN 104359233 B CN104359233 B CN 104359233B CN 201410597106 A CN201410597106 A CN 201410597106A CN 104359233 B CN104359233 B CN 104359233B
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- 238000005057 refrigeration Methods 0.000 title claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 174
- 238000010248 power generation Methods 0.000 claims abstract description 83
- 238000005338 heat storage Methods 0.000 claims abstract description 68
- 239000000498 cooling water Substances 0.000 claims abstract description 30
- 238000001816 cooling Methods 0.000 claims abstract description 20
- 230000005611 electricity Effects 0.000 claims abstract description 11
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims description 22
- 238000010521 absorption reaction Methods 0.000 claims description 16
- 150000003839 salts Chemical class 0.000 claims description 13
- PDEDQSAFHNADLV-UHFFFAOYSA-M potassium;disodium;dinitrate;nitrite Chemical compound [Na+].[Na+].[K+].[O-]N=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O PDEDQSAFHNADLV-UHFFFAOYSA-M 0.000 claims description 11
- 239000011232 storage material Substances 0.000 claims description 6
- 230000008859 change Effects 0.000 claims description 5
- 239000008399 tap water Substances 0.000 claims description 4
- 235000020679 tap water Nutrition 0.000 claims description 4
- 239000007788 liquid Substances 0.000 description 6
- 230000005855 radiation Effects 0.000 description 6
- 239000006096 absorbing agent Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 description 1
- 238000010795 Steam Flooding Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000004323 potassium nitrate Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
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- Sorption Type Refrigeration Machines (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
本发明公开了太阳能跟踪聚焦发电及制冷系统,包括集热器、储热罐、汽包、制冷机、发电装置、冷却塔、冷却水箱、补水水箱、集水缸Ⅰ和集水缸Ⅱ,集热器与汽包相连通,汽包连接有蒸汽主管路,蒸汽主管路在尾端分成并联的两条管路,一条管路为制冷机蒸汽进气管,另一条管路为发电装置蒸汽进气管,制冷机还分别连接有冷冻水回水管路、冷冻水供水管路、塔底支管路Ⅰ、塔顶支管路Ⅰ和制冷机蒸汽出气管,发电装置还分别连接有塔底支管路Ⅱ、塔顶支管路Ⅱ和发电装置蒸汽出气管,集水缸Ⅰ和集水缸Ⅱ沿着自集热器向冷却水箱的方向设置在连接管路上,所有管路上均设置有阀。该系统通过集热器和汽包产生蒸汽,驱动发电装置发电或者制冷机制冷。
The invention discloses a solar tracking and focusing power generation and refrigeration system, including a heat collector, a heat storage tank, a steam drum, a refrigerator, a power generation device, a cooling tower, a cooling water tank, a replenishing water tank, a water collection tank I and a water collection tank II, and The heater is connected to the steam drum, and the steam drum is connected to the main steam pipeline, which is divided into two parallel pipelines at the end, one pipeline is the steam inlet pipe of the refrigerator, and the other pipeline is the steam inlet pipe of the power generation unit , the refrigerator is also connected with the chilled water return pipeline, the chilled water supply pipeline, the tower bottom branch pipeline I, the tower top branch pipeline I and the steam outlet pipe of the refrigerator, and the power generation device is also connected with the tower bottom branch pipeline II, the tower The top branch pipeline II and the steam outlet pipe of the power generation unit, the water collection tank I and the water collection tank II are arranged on the connecting pipeline along the direction from the heat collector to the cooling water tank, and valves are installed on all pipelines. The system generates steam through heat collectors and steam drums to drive power generation devices to generate electricity or refrigerators for cooling.
Description
技术领域technical field
本发明涉及太阳能发电和制冷系统,具体是指太阳能跟踪聚焦发电及制冷系统。The invention relates to a solar power generation and refrigeration system, in particular to a solar tracking focusing power generation and refrigeration system.
背景技术Background technique
太阳能作为取之不尽同时又是生态学上纯净的和不改变地球上燃料平衡的能源,有着能源总量大,又容易实现分散化利用的优点。但是常规的太阳能热利用只能用于低温热应用领域,比如说家用的太阳能热水器、低温热水循环系统等,工质温度低,难以满足工业热能和太阳能热发电需求,应用受到极大限制。As an inexhaustible source of energy that is also ecologically pure and does not change the fuel balance on the earth, solar energy has the advantages of large total energy and easy realization of decentralized utilization. However, conventional solar thermal utilization can only be used in low-temperature thermal applications, such as household solar water heaters, low-temperature hot water circulation systems, etc. The temperature of the working fluid is low, which is difficult to meet the needs of industrial thermal energy and solar thermal power generation, and its application is greatly restricted.
发明内容Contents of the invention
本发明的目的是提供太阳能跟踪聚焦发电及制冷系统。该系统能够利用太阳能集热、储热技术,驱动发电装置发电或者制冷机制冷。The object of the invention is to provide a solar tracking focusing power generation and refrigeration system. The system can use solar heat collection and heat storage technology to drive a power generation device to generate electricity or a refrigerator for cooling.
本发明的上述目的通过如下技术方案来实现的:太阳能跟踪聚焦发电及制冷系统,其特征在于:所述系统包括集热器、储热罐、汽包、制冷机、发电装置、冷却塔、冷却水箱、补水水箱、集水缸Ⅰ和集水缸Ⅱ,所述集热器用于吸收太阳能的热量,集热器的出口与汽包的进口通过高压热水管路相连通,汽包的出口连接有蒸汽主管路,所述的蒸汽主管路在尾端分成并联的两条管路,一条管路为制冷机蒸汽进气管,与制冷机的蒸汽进口相连通,另一条管路为发电装置蒸汽进气管,与发电装置的蒸汽进口相连通,所述的制冷机还分别连接有冷冻水回水管路、冷冻水供水管路、塔底支管路Ⅰ、塔顶支管路Ⅰ和制冷机蒸汽出气管,所述的发电装置还分别连接有塔底支管路Ⅱ、塔顶支管路Ⅱ和发电装置蒸汽出气管,所述的发电装置还与发电机相连接,通过蒸汽做功驱动发电机发电,所述的制冷机蒸汽出气管和发电装置蒸汽出气管相交汇,交汇后与冷却水箱的进水管路相连通,所述冷却塔具有塔顶主管路和塔底主管路,所述的塔底支管路Ⅰ和塔底支管路Ⅱ相交汇,交汇后与所述的塔底主管路相连通,所述的塔顶支管路Ⅰ和塔顶支管路Ⅱ相交汇,交汇后与所述的塔顶主管路相连通,冷却塔塔底还连接有自来水补水管路,所述冷却水箱的出水口通过连接管路与集热器的进口相连通,所述的集水缸Ⅰ和集水缸Ⅱ沿着自集热器向冷却水箱的方向设置在所述连接管路上,所述冷却水箱还具有旁支管路,与所述补水水箱的进水口相连通,补水水箱的出水口通过补水管路与所述的连接管路相连接,连接点位于集水缸Ⅱ与冷却水箱之间的管段,所述汽包还旁支一路与所述集水缸Ⅱ相连接的汽包支管路,所述集水缸Ⅰ还旁支一路回水管路,所述回水管路与集热器的高压热水管路相连接,所述储热罐的两端分别连接有储热进水管路和储热出水管路,储热进水管路与集热器的高压热水管路相交汇,储热出水管路与回水管路相交汇,所述储热进水管路、连接管路、旁支管路和塔底主管路上均设置有循环水泵,所有管路上均设置有阀,以控制管路的切断和连通,该系统通过集热器和汽包产生蒸汽,然后通过蒸汽驱动发电装置发电,或者驱动制冷机制冷。The above object of the present invention is achieved through the following technical solutions: solar tracking focusing power generation and refrigeration system, characterized in that: the system includes a heat collector, a heat storage tank, a steam drum, a refrigerator, a power generation device, a cooling tower, a cooling Water tank, replenishing water tank, water collection tank I and water collection tank II, the heat collector is used to absorb the heat of solar energy, the outlet of the heat collector is connected to the inlet of the steam drum through a high-pressure hot water pipeline, and the outlet of the steam drum is connected to There is a main steam pipeline, and the main steam pipeline is divided into two parallel pipelines at the end, one pipeline is the steam inlet pipe of the refrigerator, which is connected with the steam inlet of the refrigerator, and the other pipeline is the steam inlet pipe of the power generation device. The gas pipe is connected with the steam inlet of the power generation device, and the refrigerator is also connected with the chilled water return pipeline, the chilled water supply pipeline, the branch pipeline I at the bottom of the tower, the branch pipeline I at the top of the tower and the steam outlet pipe of the refrigerator, The power generation device is also respectively connected with the tower bottom branch pipeline II, the tower top branch pipeline II and the steam outlet pipe of the power generation device, and the power generation device is also connected with the generator, and the generator is driven to generate electricity by steam. The steam outlet pipe of the refrigerating machine and the steam outlet pipe of the power generation unit intersect, and after the intersection, they are connected with the water inlet pipeline of the cooling water tank. The cooling tower has a main pipeline at the top of the tower and a main pipeline at the bottom of the tower. The tower bottom branch pipeline II intersects, and after the intersection, it is connected with the tower bottom main pipeline, and the tower top branch pipeline I and tower top branch pipeline II intersect, and after the intersection, it is connected with the tower top main pipeline , the bottom of the cooling tower is also connected with a tap water replenishment pipeline, the water outlet of the cooling water tank is connected with the inlet of the heat collector through the connecting pipeline, and the water collection tank I and the water collection tank II are along the self-collecting The device is arranged on the connecting pipeline in the direction of the cooling water tank, and the cooling water tank also has a bypass pipeline, which communicates with the water inlet of the water supply tank, and the water outlet of the water supply tank is connected to the connecting pipe through the water supply pipeline. The connection point is located in the pipe section between the water collection tank II and the cooling water tank. The steam drum also has a side branch of a steam drum branch pipeline connected to the water collection tank II, and the water collection tank I has a side branch. Return water pipeline, the return water pipeline is connected with the high-pressure hot water pipeline of the heat collector, the two ends of the heat storage tank are connected with the heat storage water inlet pipeline and the heat storage water outlet pipeline respectively, and the heat storage water inlet pipeline It intersects with the high-pressure hot water pipeline of the collector, and the heat storage outlet pipeline intersects with the return water pipeline. The heat storage inlet pipeline, connecting pipeline, side branch pipeline and tower bottom main pipeline are all equipped with circulating water pumps , All pipelines are equipped with valves to control the cut-off and connection of pipelines. The system generates steam through the heat collector and steam drum, and then drives the power generation device to generate electricity through the steam, or drives the refrigerator to cool.
本发明中,所述的集热器优选线性菲涅尔跟踪聚焦集热器,也可以采用其他能够吸收太阳能热量,产生高温高压水的集热器。线性菲涅尔跟踪聚焦集热器使用的是平面镜列,采用单轴东西跟踪太阳的方式,保证太阳光一直线聚焦于镜列上方的吸收器。吸收器采用直通型真空集热管,内管为不锈钢管,钢管外表面有选择性吸收涂层。外层的玻璃管和内层不锈钢管之间是真空隔热层。In the present invention, the heat collector is preferably a linear Fresnel tracking and focusing heat collector, and other heat collectors capable of absorbing solar heat and generating high-temperature and high-pressure water can also be used. The linear Fresnel tracking and focusing collector uses a flat mirror column, and adopts a single-axis east-west tracking method to ensure that sunlight is focused on the absorber above the mirror column in a straight line. The absorber adopts a straight-through vacuum heat collecting tube, the inner tube is a stainless steel tube, and the outer surface of the steel tube has a selective absorption coating. There is a vacuum insulation layer between the outer glass tube and the inner stainless steel tube.
本发明中,所述的制冷机优选蒸汽型溴化锂吸收式制冷机,也可以选用其他类型的制冷机。In the present invention, the refrigerating machine is preferably a vapor-type lithium bromide absorption refrigerating machine, and other types of refrigerating machines can also be selected.
本发明中,所述的发电装置优选有机朗肯循环发电装置,也可以选用其他类型的发电装置。In the present invention, the power generation device is preferably an organic Rankine cycle power generation device, and other types of power generation devices can also be selected.
本发明中,所述储热罐的蓄热材料为HITEC熔盐,HITEC熔盐为硝酸钾、硝酸钠和亚硝酸的混合物,配比为:7%NaNO3±53%KNO3±49%NaNO2,利用HITEC熔盐的相变潜热进行蓄热。储热罐蓄热材料为HITEC熔盐,熔点约为142℃。从线性菲涅尔跟踪聚焦集热器出来的液态承压的中温热水进入储热罐中的盘管,将热量传给HITEC熔盐,然后仍以液态水的形式流出储热罐。储热罐放热时,温度较低的水流经储热罐内的盘管,吸收熔盐的热量后变成温度较高的水流出储热罐。In the present invention, the heat storage material of the heat storage tank is HITEC molten salt, and the HITEC molten salt is a mixture of potassium nitrate, sodium nitrate and nitrous acid, and the proportion is: 7% NaNO 3 ± 53% KNO 3 ± 49% NaNO 2. Use the latent heat of phase change of HITEC molten salt to store heat. The heat storage material of the heat storage tank is HITEC molten salt with a melting point of about 142°C. The liquid pressurized medium-temperature hot water from the linear Fresnel tracking collector enters the coil in the heat storage tank, transfers heat to HITEC molten salt, and then flows out of the heat storage tank in the form of liquid water. When the heat storage tank releases heat, the water with a lower temperature flows through the coil in the heat storage tank, absorbs the heat of the molten salt and becomes water with a higher temperature and flows out of the heat storage tank.
本发明中,所述汽包内还设置有电加热器,需要时给进入汽包的水加热,使水汽化。In the present invention, an electric heater is also arranged in the steam drum to heat the water entering the steam drum to vaporize the water when necessary.
本发明中,所述冷却水箱与补水水箱之间还增设一路并联回水管路。In the present invention, a parallel return water pipeline is additionally provided between the cooling water tank and the replenishing water tank.
本发明系统的集热器采用线性菲涅尔跟踪聚焦集热器,能将水加热到200℃,能够驱动双效吸收式制冷机,并能驱动有机朗肯循环发电设备发电。能实现制冷和发电两个基本功能,同时储热罐具有能量存储和放热利用的功能,熔盐相变储热技术因其储热密度大的特点,应用在太阳能集热系统中能增加系统的可靠性和稳定性,并提高能源利用率。The heat collector of the system of the present invention adopts a linear Fresnel tracking and focusing heat collector, which can heat water to 200°C, drive a double-effect absorption refrigerator, and drive an organic Rankine cycle power generation device to generate electricity. It can realize the two basic functions of refrigeration and power generation. At the same time, the heat storage tank has the functions of energy storage and heat release utilization. The molten salt phase change heat storage technology is used in the solar heat collection system because of its high heat storage density. reliability and stability, and improve energy efficiency.
该系统中,集热器吸收太阳能的热量后,加热水至饱和状态,进入汽包变成蒸汽,然后蒸汽驱动有机朗肯循环发电装置发电,或驱动蒸汽型溴化锂吸收式制冷机制冷。集热器出来水的热量不够时,可启动电加热器作为辅助热源。当集热器收集热量富余,或不进行制冷和发电时,可将多余的热量存储在储热罐中,以备集热器集热量不足时使用。本发明使用了中温线性菲涅尔跟踪聚焦集热器,最大限度地采集太阳能,能实现发电和制冷两个基本功能。同时加入了电加热和蓄热装置,增加了系统的可靠性,并提高能量利用率。In this system, after the heat collector absorbs the heat of solar energy, the water is heated to saturation, and enters the steam drum to become steam, and then the steam drives the organic Rankine cycle power generation device to generate electricity, or drives the steam type lithium bromide absorption refrigerator for refrigeration. When the heat of the water coming out of the collector is not enough, the electric heater can be started as an auxiliary heat source. When the heat collector collects excess heat, or when there is no refrigeration and power generation, the excess heat can be stored in the heat storage tank for use when the heat collector does not collect enough heat. The invention uses a medium-temperature linear Fresnel tracking and focusing heat collector to collect solar energy to the greatest extent, and can realize two basic functions of power generation and refrigeration. At the same time, electric heating and heat storage devices are added to increase the reliability of the system and improve energy utilization.
本发明太阳能跟踪聚焦发电及制冷系统可以采用如下多种运行模式:The solar tracking and focusing power generation and refrigeration system of the present invention can adopt the following multiple operating modes:
运行模式一:当太阳辐射强度足够时,线性菲涅尔跟踪聚焦集热器运行产生的热水进入汽包,气化成蒸汽进入蒸汽型溴化锂吸收式制冷机或有机朗肯循环发电装置进行制冷或发电,此时冷却塔启用。从蒸汽型溴化锂吸收式制冷机或有机朗肯循环发电装置出来的水经过冷却水箱冷却,再经循环水泵加压进入线性菲涅尔跟踪聚焦集热器吸收聚焦后的太阳热量,完成循环。Operation mode 1: When the solar radiation intensity is sufficient, the hot water generated by the linear Fresnel tracking and focusing collector enters the steam drum, is gasified into steam, and enters a steam-type lithium bromide absorption refrigerator or an organic Rankine cycle power generation device for refrigeration or Power generation, at this time the cooling tower is activated. The water from the steam-type lithium bromide absorption refrigerator or organic Rankine cycle power generation device is cooled by the cooling water tank, and then pressurized by the circulating water pump and enters the linear Fresnel tracking and focusing collector to absorb the focused solar heat to complete the cycle.
运行模式二:当线性菲涅尔跟踪聚焦集热器运行产生的热水热量富余,部分热水流经储热罐进行蓄热,然后进入线性菲涅尔跟踪聚焦集热器完成循环。Operation mode 2: When the hot water heat generated by the linear Fresnel tracking and focusing collector is surplus, part of the hot water flows through the heat storage tank for heat storage, and then enters the linear Fresnel tracking and focusing collector to complete the cycle.
运行模式三:当太阳能跟踪聚焦发电及制冷系统的不需要制冷或发电时,从线性菲涅尔跟踪聚焦集热器出来的全部热水流经储热罐进行蓄热,然后进入线性菲涅尔跟踪聚焦集热器完成循环。Operation mode three: when the solar tracking and focusing power generation and refrigeration system do not need cooling or power generation, all the hot water from the linear Fresnel tracking and focusing collector flows through the heat storage tank for heat storage, and then enters the linear Fresnel Tracking focused collectors complete the cycle.
运行模式四:当太阳辐射强度不够、线性菲涅尔跟踪聚焦集热器产生热水的热量不足时,启用电加热器,给从集热器出来的水再次加热,至满足热量需求。Operation mode 4: When the solar radiation intensity is not enough and the heat of hot water produced by the linear Fresnel tracking and focusing collector is insufficient, the electric heater is activated to reheat the water coming out of the collector to meet the heat demand.
运行模式五:当太阳辐射强度不够、线性菲涅尔跟踪聚焦集热器产生热水的热量不足时,启用储热罐,给从集热器出来的水再次加热,至满足热量需求。Operation mode five: When the solar radiation intensity is not enough and the heat of hot water produced by the linear Fresnel tracking and focusing collector is insufficient, the heat storage tank is activated to reheat the water coming out of the collector to meet the heat demand.
运行模式六:当太阳辐照条件不好,或在阴雨天、夜间时,线性菲涅尔跟踪聚焦集热器无法运行,可以启用储热罐,给管路回水加热,驱动蒸汽型溴化锂吸收式制冷机或有机朗肯循环发电装置。Operation mode 6: When the solar irradiation conditions are not good, or in rainy days or at night, the linear Fresnel tracking focusing collector cannot operate, and the heat storage tank can be activated to heat the return water of the pipeline and drive the steam-type lithium bromide absorption type refrigerator or organic Rankine cycle power generation device.
在本发明中,蒸汽型溴化锂吸收式制冷机和有机朗肯循环发电装置不同时工作;储热罐和电加热器不同时工作。In the present invention, the steam-type lithium bromide absorption refrigerator and the organic Rankine cycle power generation device do not work at the same time; the heat storage tank and the electric heater do not work at the same time.
与现有技术相比,本发明具有如下显著效果:Compared with prior art, the present invention has following remarkable effect:
(1)本发明采用的是直接蒸汽产生系统,产生的蒸汽直接驱动吸收式制冷机或有机朗肯循环发电装置,系统热损失小,热利用率高。(1) The present invention adopts a direct steam generation system, and the generated steam directly drives an absorption refrigerator or an organic Rankine cycle power generation device, the system has small heat loss and high heat utilization rate.
(2)本发明的集热器采用的是线性菲涅尔跟踪聚焦集热器,能充分采集太阳能,同时线性菲涅尔跟踪聚焦集热器维护方便,成本较低、抗风性好.(2) The heat collector of the present invention adopts a linear Fresnel tracking and focusing collector, which can fully collect solar energy. At the same time, the linear Fresnel tracking and focusing collector is easy to maintain, has low cost, and has good wind resistance.
(3)本发明储热罐储热材料使用相变储热材料,罐体储热密度大,体积小。(3) The heat storage material of the heat storage tank of the present invention uses a phase-change heat storage material, and the tank body has a high heat storage density and a small volume.
(4)本发明系统有电加热器和储热罐作为辅助热源,可靠性好。(4) The system of the present invention has an electric heater and a heat storage tank as an auxiliary heat source, and has good reliability.
(5)本发明利用线性菲涅尔太阳能跟踪聚焦型集热器,将太阳能中高温集热技术用于有机朗肯循环发电系统和吸收式制冷系统中,为线性菲涅尔太阳能光热技术国产化奠定基础。(5) The present invention utilizes the linear Fresnel solar tracking focusing type heat collector, and uses the solar medium and high temperature heat collection technology in the organic Rankine cycle power generation system and the absorption refrigeration system, which is a domestically produced linear Fresnel solar photothermal technology. Lay the foundation.
(6)本发明中汽包内有电加热器,在必要的时候给进入汽包的水加热,使水气化。(6) There is an electric heater in the steam drum in the present invention, and when necessary, the water entering the steam drum is heated to vaporize the water.
(7)本发明中,从蒸汽型溴化锂吸收式制冷机,或者有机朗肯循环发电装置出口处的水要经过冷却水箱进行冷却,防止出口处的水仍为蒸汽状态,影响循环水泵工作。(7) In the present invention, from the vapor type lithium bromide absorption refrigerator, or the water at the outlet of the organic Rankine cycle power generation device will be cooled through the cooling water tank, preventing the water at the outlet from still being in a steam state, which will affect the work of the circulating water pump.
(8)本发明中,冷却水箱和补水水箱通过管路连接成回路,通过回路水循环,保持冷却水箱中水的温度较低的状态。(8) In the present invention, the cooling water tank and the replenishing water tank are connected into a circuit through pipelines, and the water in the cooling water tank is kept in a low temperature state through the circuit water circulation.
(9)本发明中,蒸汽型溴化锂吸收式制冷机和有机朗肯循环发电装置共用一个冷却塔,初投资节省成本。(9) In the present invention, the steam-type lithium bromide absorption refrigerator and the organic Rankine cycle power generation device share a cooling tower, and the initial investment saves costs.
附图说明Description of drawings
下面结合附图和具体实施方式对本发明做进一步详细说明。The present invention will be described in further detail below in conjunction with the accompanying drawings and specific embodiments.
图1是本发明太阳能跟踪聚焦发电及制冷系统的整体结构框图。Fig. 1 is a block diagram of the overall structure of the solar tracking focusing power generation and refrigeration system of the present invention.
附图标记说明Explanation of reference signs
1、集热器;2、储热罐;3、汽包;4、电加热器;5、制冷机;6、冷却塔;1. Heat collector; 2. Heat storage tank; 3. Steam drum; 4. Electric heater; 5. Refrigerator; 6. Cooling tower;
7、发电装置;8、冷却水箱;9、补水水箱;10、集水缸Ⅱ;11、集水缸Ⅰ;7. Power generation device; 8. Cooling water tank; 9. Water supply tank; 10. Water collection tank II; 11. Water collection tank I;
12~15、循环水泵;16~25、电磁阀;26~31、截止阀;32、发电机;12~15, circulating water pump; 16~25, solenoid valve; 26~31, stop valve; 32, generator;
33、减压阀;34、安全排气阀;35、蒸汽流量计;33. Pressure reducing valve; 34. Safety exhaust valve; 35. Steam flow meter;
101、高压热水管路;102、蒸汽主管路;103、制冷机蒸汽进气管;101. High-pressure hot water pipeline; 102. Main steam pipeline; 103. Refrigerator steam inlet pipe;
104、发电装置蒸汽进气管;105、冷冻水回水管路;106、冷冻水供水管路;104. Steam intake pipe of power generation device; 105. Chilled water return pipeline; 106. Chilled water supply pipeline;
107、塔底支管路Ⅰ;108、塔顶支管路Ⅰ;109、制冷机蒸汽出气管;107. Tower bottom branch pipeline Ⅰ; 108. Tower top branch pipeline Ⅰ; 109. Refrigerator steam outlet pipe;
110、塔底支管路Ⅱ;111、塔顶支管路Ⅱ;112、发电装置蒸汽出气管;110. Branch pipeline II at the bottom of the tower; 111. Branch pipeline II at the top of the tower; 112. Steam outlet pipe of the power generation unit;
113、汽包支管路;114、自来水补水管路;115、塔顶主管路;113. Steam drum branch pipeline; 114. Tap water replenishment pipeline; 115. Tower top main pipeline;
116、塔底主管路;117、进水管路;118、连接管路;119、旁支管路;116, the main pipe at the bottom of the tower; 117, the water inlet pipe; 118, the connecting pipe; 119, the side branch pipe;
120、补水管路;121、并联回水管路;122、回水管路;120, water supply pipeline; 121, parallel return water pipeline; 122, return water pipeline;
123、储热出水管路;124、储热进水管路;123. Heat storage water outlet pipeline; 124. Heat storage water inlet pipeline;
具体实施方式detailed description
如图1所示的太阳能跟踪聚焦发电及制冷系统,该系统包括集热器1、储热罐2、汽包3、制冷机5、发电装置7、冷却塔6、冷却水箱8、补水水箱9、集水缸Ⅰ11和集水缸Ⅱ10,集热器1为线性菲涅尔跟踪聚焦集热器,制冷机5为蒸汽型溴化锂吸收式制冷机,发电装置7为有机朗肯循环发电装置,集热器1用于吸收太阳能的热量。线性菲涅尔跟踪聚焦集热器使用的是平面镜列,采用单轴东西跟踪太阳的方式,保证太阳光一直线聚焦于镜列上方的吸收器。吸收器采用直通型真空集热管,内管为不锈钢管,钢管外表面有选择性吸收涂层。外层的玻璃管和内层不锈钢管之间是真空隔热层。As shown in Figure 1, the solar tracking focusing power generation and refrigeration system includes a heat collector 1, a heat storage tank 2, a steam drum 3, a refrigerator 5, a power generation device 7, a cooling tower 6, a cooling water tank 8, and a water supply tank 9 , water collecting tank I11 and water collecting tank II10, the heat collector 1 is a linear Fresnel tracking focusing heat collector, the refrigerator 5 is a steam lithium bromide absorption refrigerator, and the power generation device 7 is an organic Rankine cycle power generation device. Heater 1 is used for absorbing the heat of solar energy. The linear Fresnel tracking and focusing collector uses a flat mirror column, and adopts a single-axis east-west tracking method to ensure that sunlight is focused on the absorber above the mirror column in a straight line. The absorber adopts a straight-through vacuum heat collecting tube, the inner tube is a stainless steel tube, and the outer surface of the steel tube has a selective absorption coating. There is a vacuum insulation layer between the outer glass tube and the inner stainless steel tube.
集热器1的出口与汽包3的进口通过高压热水管路101相连通,汽包3内还设置有电加热器4,需要时给进入汽包3的水加热,使水汽化,汽包3的出口连接有蒸汽主管路102,蒸汽主管路102在尾端分成并联的两条管路,一条管路为制冷机蒸汽进气管103,与制冷机5的蒸汽进口相连通,另一条管路为发电装置蒸汽进气管104,与发电装置7的蒸汽进口相连通,制冷机5还分别连接有冷冻水回水管路105、冷冻水供水管路106、塔底支管路Ⅰ107、塔顶支管路Ⅰ108和制冷机蒸汽出气管109,发电装置7还分别连接有塔底支管路Ⅱ110、塔顶支管路Ⅱ111和发电装置蒸汽出气管112,发电装置7还与发电机36相连接,通过蒸汽做功驱动发电机发电,制冷机蒸汽出气管109和发电装置蒸汽出气管112相交汇,交汇后与冷却水箱8的进水管路117相连通,冷却塔6具有塔顶主管路115和塔底主管路116,塔底支管路Ⅰ107和塔底支管路Ⅱ110相交汇,交汇后与塔底主管路116相连通,塔顶支管路Ⅰ108和塔顶支管路Ⅱ111相交汇,交汇后与塔顶主管路115相连通,冷却塔6塔底还连接有自来水补水管路114,冷却水箱8的出水口通过连接管路118与集热器1的进口相连通,集水缸Ⅰ11和集水缸Ⅱ10沿着自集热器1向冷却水箱8的方向设置在连接管路118上,冷却水箱8还具有旁支管路119,与补水水箱9的进水口相连通,补水水箱9的出水口通过补水管路120与连接管路118相连接,连接点位于集水缸Ⅱ10与冷却水箱8之间的管段,冷却水箱8与补水水箱9之间还增设一路并联回水管路121,汽包3还旁支一路与集水缸Ⅱ10相连接的汽包支管路113,集水缸Ⅰ10还旁支一路回水管路122,回水管路122与集热器1的高压热水管路101相连接,储热罐2的两端分别连接有储热进水管路124和储热出水管路123,储热进水管路124与集热器1的高压热水管路101相交汇,储热出水管路123与回水管路122相交汇。The outlet of the heat collector 1 is connected with the inlet of the steam drum 3 through a high-pressure hot water pipeline 101, and an electric heater 4 is also arranged in the steam drum 3 to heat the water entering the steam drum 3 to vaporize the water when necessary. The outlet of package 3 is connected with main steam pipeline 102, which is divided into two parallel pipelines at the tail end, one pipeline is the steam inlet pipe 103 of the refrigerator, which is connected with the steam inlet of refrigerator 5, and the other pipe is The road is the steam inlet pipe 104 of the power generation device, which is connected with the steam inlet of the power generation device 7. The refrigerator 5 is also connected with the chilled water return pipeline 105, the chilled water supply pipeline 106, the tower bottom branch pipeline I 107, and the tower top branch pipeline Ⅰ 108 and the steam outlet pipe 109 of the refrigerating machine. The power generation device 7 is also connected to the tower bottom branch pipeline II 110, the tower top branch pipeline II 111 and the steam outlet pipe 112 of the power generation device. The power generation device 7 is also connected to the generator 36 and driven by steam. The generator generates electricity, and the steam outlet pipe 109 of the refrigerating machine and the steam outlet pipe 112 of the power generation device intersect and communicate with the water inlet pipeline 117 of the cooling water tank 8 after the intersection. The cooling tower 6 has a main pipeline 115 at the top of the tower and a main pipeline 116 at the bottom of the tower. The tower bottom branch pipeline I107 and the tower bottom branch pipeline II110 intersect, and after the intersection, they are connected to the tower bottom main pipeline 116. The tower top branch pipeline I108 and the tower top branch pipeline II111 intersect, and after the intersection, they are connected to the tower top main pipeline 115. The bottom of the cooling tower 6 is also connected with a tap water replenishment pipeline 114, and the outlet of the cooling water tank 8 is connected with the inlet of the heat collector 1 through a connection pipeline 118. 1 is set on the connecting pipeline 118 in the direction of the cooling water tank 8. The cooling water tank 8 also has a bypass pipeline 119, which communicates with the water inlet of the replenishing water tank 9. The water outlet of the replenishing water tank 9 is connected to the connecting pipeline through the replenishing water pipeline 120 118, the connection point is located in the pipe section between the water collection tank II10 and the cooling water tank 8, and a parallel return water pipeline 121 is added between the cooling water tank 8 and the replenishment water tank 9, and the steam drum 3 is also connected to the water collection tank II10. The connected steam drum branch pipeline 113, and the water collection tank I10 also branch off a return water pipeline 122, the return water pipeline 122 is connected with the high-pressure hot water pipeline 101 of the heat collector 1, and the two ends of the heat storage tank 2 are respectively connected with storage The hot water inlet pipeline 124 and the heat storage water outlet pipeline 123 , the heat storage water inlet pipeline 124 intersects with the high-pressure hot water pipeline 101 of the heat collector 1 , and the heat storage outlet pipeline 123 intersects with the return water pipeline 122 .
储热进水管路124、连接管路118、旁支管路119和塔底主管路116上均设置有循环水泵12~15,通过循环水泵泵压液态水,所有管路上均设置有阀,以控制管路的切断和连通,管路上设置的阀包括电磁阀16~25、截止阀、排气阀等,该系统还包括温度传感器、压力传感器、流量计等部件,这些阀、传感器、流量计的设置均采用常规技术手段即可实现。该系统通过集热器1和汽包3产生蒸汽,然后通过蒸汽驱动发电装置7发电,或者驱动制冷机5制冷。The heat storage inlet pipeline 124, connecting pipeline 118, side branch pipeline 119 and tower bottom main pipeline 116 are all provided with circulating water pumps 12-15, through which the liquid water is pumped, and all pipelines are provided with valves to control The valves on the pipeline include solenoid valves 16-25, stop valves, exhaust valves, etc. The system also includes temperature sensors, pressure sensors, flow meters and other components. The valves, sensors, and flow meters The settings can be realized by conventional technical means. The system generates steam through the heat collector 1 and the steam drum 3, and then drives the power generation device 7 to generate electricity through the steam, or drives the refrigerator 5 to cool.
本实施例中,集热器1、制冷机5、发电装置7均为优选的现有设备或装置,集热器1除了选取线性菲涅尔跟踪聚焦集热器,也可以采用其他能够吸收太阳能热量,产生高温高压水的集热器。制冷机5除了选取蒸汽型溴化锂吸收式制冷机,也可以选用其他类型的制冷机。发电装置7除了选取有机朗肯循环发电装置,也可以选用其他类型的发电装置。In this embodiment, the heat collector 1, the refrigerator 5, and the power generation device 7 are all preferred existing equipment or devices. In addition to selecting a linear Fresnel tracking and focusing heat collector for the heat collector 1, other solar energy absorbers can also be used. Heat, a heat collector that produces high temperature and high pressure water. Refrigerator 5 can also select other types of refrigerators besides steam lithium bromide absorption refrigerators. In addition to the organic Rankine cycle power generation device for the power generation device 7 , other types of power generation devices can also be selected.
储热罐2的蓄热材料为HITEC熔盐,利用HITEC熔盐的相变潜热进行蓄热。从集热器1出来的液态承压的温度为200℃热水进入储热罐2中的盘管,将热量传给HITEC熔盐,然后仍以液态水的形式流出储热罐2。储热罐放热时,温度较低的水流经储热罐内的盘管,吸收HITEC熔盐的热量后变成温度较高的水流出储热罐。The heat storage material of the heat storage tank 2 is HITEC molten salt, and the latent heat of phase change of the HITEC molten salt is used for heat storage. The liquid pressurized hot water coming out of the heat collector 1 with a temperature of 200°C enters the coil in the heat storage tank 2, transfers the heat to the HITEC molten salt, and then flows out of the heat storage tank 2 in the form of liquid water. When the heat storage tank releases heat, the water with a lower temperature flows through the coil in the heat storage tank, absorbs the heat of HITEC molten salt, and becomes water with a higher temperature to flow out of the heat storage tank.
本实施例的系统在运行时,可以采用如下多种运行模式:When the system of this embodiment is in operation, the following multiple operating modes can be adopted:
运行模式一:当太阳辐射强度足够时,运行集热器1,关闭截止阀26、29、30,开启截止阀28、31,关闭循环泵13,关闭电加热器4,让从集热器1出来的温度为200℃、压力为20个大气压的高温高压热水进入汽包3,在汽包内气化成温度为150℃、压力为5个大气压的蒸汽进入制冷机5或发电装置7进行制冷或发电,此时冷却塔6启用。制冷机5和发电装置7不同时工作。Operation mode one: when the solar radiation intensity is sufficient, run the heat collector 1, close the shut-off valves 26, 29, 30, open the shut-off valves 28, 31, turn off the circulation pump 13, turn off the electric heater 4, and let the heat collector 1 The high-temperature and high-pressure hot water with a temperature of 200°C and a pressure of 20 atmospheres enters the steam drum 3, and is vaporized in the steam drum to form steam at a temperature of 150°C and a pressure of 5 atmospheres, which enters the refrigerator 5 or the power generation device 7 for refrigeration Or generate electricity, and now the cooling tower 6 is enabled. The refrigerating machine 5 and the power generating device 7 do not work at the same time.
制冷机5制冷时,电磁阀18、21、23关闭,电磁阀19、20、22、25打开,制冷机蒸汽出气管109出来的蒸汽温度为120℃,从冷冻水回水管路105进入制冷机5的水温为12℃,从制冷机5流入冷冻水供水管路106的水温为7℃,来自塔底主管路116的水温为28℃,经换热后,进入塔顶主管路115的水温为35℃.When the refrigerator 5 is cooling, the solenoid valves 18, 21, and 23 are closed, and the solenoid valves 19, 20, 22, and 25 are opened. The temperature of the steam coming out of the steam outlet pipe 109 of the refrigerator is 120°C, and the steam enters the refrigerator from the chilled water return pipeline 105 The water temperature of 5 is 12 ℃, the water temperature of the water flowing into the chilled water supply pipeline 106 from the refrigerator 5 is 7 ℃, and the water temperature from the main pipeline 116 at the bottom of the tower is 28 ℃. After heat exchange, the water temperature entering the main pipeline 115 at the top of the tower is 35°C.
发电装置7发电时,电磁阀19、20、22关闭,电磁阀18、21、23、24打开发电装置蒸汽出气管112出来的蒸汽温度为120℃,来自塔底主管路116的水温为28℃,经换热后,进入塔顶主管路115的水温为35℃。When the power generation device 7 generates power, the solenoid valves 19, 20, and 22 are closed, and the solenoid valves 18, 21, 23, and 24 are opened. The temperature of the steam coming out of the steam outlet pipe 112 of the power generation device is 120°C, and the temperature of the water from the main pipeline 116 at the bottom of the tower is 28°C. , after heat exchange, the temperature of the water entering the tower top main pipeline 115 is 35°C.
从制冷机5或发电装置7出来的水经过冷却水箱8冷却至液体水,再经循环水泵12加压进入集热器1吸收聚焦后的太阳热量,完成循环。从制冷机5或者发电装置7出来的水经过冷却水箱8进行冷却,为了防止出口处的水仍为蒸汽状态,影响循环水泵12、15的工作。制冷机5和发电装置7共用一个冷却塔6,初投资节省成本。The water from the refrigerator 5 or the power generation device 7 is cooled to liquid water through the cooling water tank 8, and then pressurized by the circulating water pump 12 and enters the heat collector 1 to absorb the focused solar heat to complete the cycle. The water coming out from the refrigerating machine 5 or the power generating unit 7 is cooled through the cooling water tank 8, in order to prevent the water at the outlet from still being in a steam state, affecting the work of the circulating water pumps 12 and 15. The refrigeration machine 5 and the power generation device 7 share a cooling tower 6, and the initial investment saves costs.
运行模式二:当集热器1运行产生的热水热量富余,在运行模式一的基础上,同时开启电磁阀16、17,并开启循环水泵3,关闭截止阀26、27,让部分热水流经储热罐2进行蓄热,然后进入集水缸Ⅰ11,同集水缸Ⅱ10过来的水汇合后进入集热器1。另一部分水进入汽包5,流程同运行模式一。Operation mode 2: When the hot water heat generated by the operation of the heat collector 1 is surplus, on the basis of operation mode 1, open the solenoid valves 16 and 17 at the same time, turn on the circulating water pump 3, close the shut-off valves 26 and 27, and let part of the hot water It flows through the heat storage tank 2 for heat storage, then enters the water collection tank I11, joins with the water from the water collection tank II10, and then enters the heat collector 1. Another part of water enters the steam drum 5, and the flow process is the same as the operation mode one.
运行模式三:当太阳能跟踪聚焦发电及制冷系统的不需要制冷或发电时,开启电磁阀16、17,并开启循环水泵3,关闭截止阀26、27、28,从集热器1出来的全部热水流经储热罐2进行蓄热,然后进入集热器1完成循环。Operation mode three: when the solar tracking focus power generation and the refrigeration system do not need refrigeration or power generation, open the solenoid valves 16 and 17, open the circulating water pump 3, close the stop valves 26, 27, and 28, and all the heat coming out of the collector 1 The hot water flows through the heat storage tank 2 for heat storage, and then enters the heat collector 1 to complete the cycle.
运行模式四:当太阳辐射强度不够、集热器1产生热水的热量不足时,在运行模式一的基础上,启用电加热器4,给从集热器出来的水再次加热,至满足热量需求。Operation mode 4: When the solar radiation intensity is not enough and the heat of hot water produced by collector 1 is insufficient, on the basis of operation mode 1, the electric heater 4 is activated to reheat the water from the collector to meet the heat requirements. need.
运行模式五:当太阳辐射强度不够、线性菲涅尔跟踪聚焦集热器产生热水的热量不足时,在运行模式一的基础上,开启截止阀26、27和电磁阀17,关闭截止阀30和电磁阀16,关闭循环水泵13,启用储热罐2,给从集热器出来的水再次加热,至满足热量需求。Operation mode five: when the solar radiation intensity is not enough and the heat of hot water produced by the linear Fresnel tracking focusing collector is insufficient, on the basis of operation mode one, open the shut-off valves 26, 27 and solenoid valve 17, and close the shut-off valve 30 And solenoid valve 16, close circulating water pump 13, enable heat storage tank 2, reheat the water coming out from heat collector, to meet heat demand.
运行模式六:当太阳辐照条件不好,或在阴雨天、夜间时,线性菲涅尔跟踪聚焦集热1无法运行,关闭截止阀26、31,关闭循环水泵13,开启截止阀27和电磁阀17,启用储热罐2,给管路回水加热,驱动制冷机5或发电装置7。Operation mode six: When the solar irradiation conditions are not good, or in rainy days or at night, the linear Fresnel tracking and focusing heat collector 1 cannot operate, close the stop valves 26 and 31, turn off the circulating water pump 13, open the stop valve 27 and the electromagnetic The valve 17 activates the heat storage tank 2, heats the return water of the pipeline, and drives the refrigerator 5 or the power generation device 7.
本发明的上述实施例并不是对本发明保护范围的限定,本发明的实施方式不限于此,凡此种种根据本发明的上述内容,按照本领域的普通技术知识和惯用手段,在不脱离本发明上述基本技术思想前提下,对本发明上述结构做出的其它多种形式的修改、替换或变更,均应落在本发明的保护范围之内。The above-mentioned embodiments of the present invention do not limit the protection scope of the present invention. Under the premise of the above-mentioned basic technical ideas, other modifications, replacements or changes made to the above-mentioned structure of the present invention in various forms shall fall within the protection scope of the present invention.
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