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CN113137780B - Low-temperature refrigeration cold-storage system for efficiently utilizing solar energy - Google Patents

Low-temperature refrigeration cold-storage system for efficiently utilizing solar energy Download PDF

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CN113137780B
CN113137780B CN202110529243.4A CN202110529243A CN113137780B CN 113137780 B CN113137780 B CN 113137780B CN 202110529243 A CN202110529243 A CN 202110529243A CN 113137780 B CN113137780 B CN 113137780B
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adsorption bed
refrigerant
outlet
cold storage
compressor
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CN113137780A (en
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高鹏
王淑
陈彦伶
金胜祥
胡皓
武卫东
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University of Shanghai for Science and Technology
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B27/00Machines, plants or systems, using particular sources of energy
    • F25B27/002Machines, plants or systems, using particular sources of energy using solar energy
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B25/00Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
    • F25B25/02Compression-sorption machines, plants, or systems
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/85Food storage or conservation, e.g. cooling or drying

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Abstract

The invention relates to a low-temperature refrigeration cold accumulation system for efficiently utilizing solar energy, which comprises a compressor (1), a condenser (2), a liquid storage tank (3), an intercooler (4), an evaporator (5), a cooler (6), a first adsorption bed (101), a second adsorption bed (102) and a cold accumulation adsorption bed (11); in the daytime refrigeration/cold accumulation mode, the first adsorption bed and the second adsorption bed work alternately by utilizing solar energy to realize refrigeration, meanwhile, the cold accumulation adsorption bed performs desorption reaction under the suction regulation action of a compressor to gradually complete cold accumulation, and in the night cold release mode, the cold accumulation adsorption bed continuously adsorbs refrigerant to realize continuous refrigeration. Compared with the prior art, the invention introduces the compressor to adjust the desorption pressure of the adsorption bed, reduces the desorption temperature, enables the system to actively adapt to the fluctuating solar hot water temperature, and realizes the desorption and heat absorption at lower temperature; meanwhile, with the assistance of desorption reaction of the adsorption bed, the suction pressure of the compressor is increased, the pressure ratio of the compressor is reduced, the power consumption of the compressor is reduced, and the refrigeration energy efficiency is obviously improved.

Description

一种高效利用太阳能的低温制冷蓄冷系统A low-temperature refrigeration and cold storage system that efficiently utilizes solar energy

技术领域technical field

本发明涉及制冷、蓄冷技术领域,尤其是涉及一种高效利用太阳能的低温制冷蓄冷系统。The invention relates to the technical field of refrigeration and cold storage, in particular to a low-temperature refrigeration and cold storage system for efficiently utilizing solar energy.

背景技术Background technique

果蔬是生活中必不可少的食物,但是一般都很难长期贮藏,可以通过产地低温贮藏及时带走果蔬田地热,降低呼吸热,延长储存期,减少果蔬腐败变质损失,同时,农村田间因为分布较广无法实现供电所的集中管理,且电源点少,电压质量不稳定,供电能力弱及输送线路长导致大量电力损失等问题,很难满足农产品及时冷藏的供电需求。Fruits and vegetables are essential food in daily life, but they are generally difficult to store for a long time. The low-temperature storage in the place of origin can take away the ground heat of fruits and vegetables in time, reduce respiratory heat, prolong the storage period, and reduce the loss of fruits and vegetables from spoilage. At the same time, due to the distribution of It is difficult to realize the centralized management of the power supply station, and there are few power points, unstable voltage quality, weak power supply capacity and long transmission lines leading to a large amount of power loss. It is difficult to meet the power supply demand for timely refrigeration of agricultural products.

低温冷库作为产地低温储藏必不可少的部分,主要用作对食品、果蔬、药品等恒温恒湿贮藏,要求的制冷温度为0℃到-30℃,目前蒸气压缩制冷系统因其结构简单、初始成本低等被广泛用于为低温冷库提供制冷量,然而低蒸发温度会导致高耗电量和低制冷能效,造成贮藏成本显著增加。Low-temperature cold storage is an indispensable part of low-temperature storage in the place of origin. It is mainly used for constant temperature and humidity storage of food, fruits and vegetables, and medicines. Low grades are widely used to provide cooling capacity for low-temperature cold storage, but low evaporation temperatures will result in high power consumption and low refrigeration energy efficiency, resulting in a significant increase in storage costs.

田间具有丰富的太阳能,太阳能作为一种清洁可再生能源,如果可以高效回收利用太阳能制取低温冷量,满足冷库需求,可显著降低贮藏成本;但太阳能所具有的间歇性、不稳定性等特征,如普通真空管太阳能集热器出水温度随太阳辐射强度在55℃-95℃区间内不断地波动,极大限制太阳能回收利用。The field is rich in solar energy. Solar energy is a clean and renewable energy source. If solar energy can be efficiently recycled and utilized to produce low-temperature cooling capacity to meet the needs of cold storage, storage costs can be significantly reduced; however, solar energy has characteristics such as intermittent and unstable , For example, the outlet water temperature of ordinary vacuum tube solar collectors fluctuates continuously with the intensity of solar radiation in the range of 55°C-95°C, which greatly limits the recovery and utilization of solar energy.

经查阅文献发现,赵有信等人公开号为CN209181364U的太阳能冰蓄冷冷库,其原理是利用将太阳能直接转化为电能,驱动传统蒸气压缩制冷装置运行,蒸气压缩装置中的蒸发盘管至于水箱内,蒸发盘管蒸发吸热,水相变为冰储存冷量,在夜晚缺乏太阳能时,进行释冷,保证冷库的冷量需求。该发明专利采用传统蒸气压缩制冷装置制冷,依然面临低蒸发温度导致高耗电量和低制冷能效的问题,太阳能光电转换效率较低,因此需要的太阳能电池板面积很大,太阳能电池板价格昂贵,系统初始成本较高。另外采用冰蓄冷装置,其特点是释冷温度恒定,不能够灵活调整冷库所需制冷温度。After reviewing the literature, it was found that Zhao Youxin and others published a solar ice storage cold storage with the number CN209181364U. The coil evaporates and absorbs heat, and the water phase turns into ice to store cold energy. When there is a lack of solar energy at night, the cooling is released to ensure the cooling capacity of the cold storage. This invention patent adopts traditional vapor compression refrigeration device for refrigeration, but still faces the problems of high power consumption and low refrigeration energy efficiency caused by low evaporation temperature, and the solar photoelectric conversion efficiency is low, so the required solar panel area is large, and the solar panel is expensive , the initial cost of the system is high. In addition, the ice storage device is used, which is characterized by a constant cooling temperature and cannot flexibly adjust the cooling temperature required by the cold storage.

众所周知,太阳能光热转换效率远高于光电转换效率,太阳能集热器成本远低于太阳能电池板成本,但目前热驱动的吸附制冷装置低温制冷时驱动热源温度高于100℃,普通太阳能集热器难以获得如此高温的热水。As we all know, the conversion efficiency of solar energy to heat is much higher than that of photoelectric conversion, and the cost of solar collectors is much lower than that of solar panels. It is difficult for the appliance to obtain such high-temperature hot water.

发明内容Contents of the invention

本发明的目的就是为了克服上述现有技术存在的缺陷而提供一种高效利用太阳能的低温制冷蓄冷系统。The purpose of the present invention is to provide a low-temperature refrigeration and cold storage system that utilizes solar energy efficiently in order to overcome the above-mentioned defects in the prior art.

本发明的目的可以通过以下技术方案来实现:一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,包括压缩机、冷凝器、储液罐、中冷器、蒸发器、冷却器、第一吸附床、第二吸附床、蓄冷吸附床;所述的压缩机依次连接冷凝器、储液罐、中冷器;所述的中冷器设有多个进出口,分别连接压缩机、蒸发器和冷却器;The purpose of the present invention can be achieved through the following technical solutions: a low-temperature refrigeration storage system for efficiently utilizing solar energy, characterized in that it includes a compressor, a condenser, a liquid storage tank, an intercooler, an evaporator, a cooler, a first Adsorption bed, second adsorption bed, cold storage adsorption bed; the compressor is sequentially connected to the condenser, liquid storage tank, and intercooler; the intercooler is provided with multiple inlets and outlets, respectively connected to the compressor and evaporator and coolers;

所述的蒸发器和冷却器分别连接第一吸附床、第二吸附床、蓄冷吸附床,并在连接管道上设有多个四通阀、三通阀;切换四通阀、三通阀,实现切换第一吸附床、第二吸附、蓄冷吸附床进行吸附和解吸,实现系统白天制冷/蓄冷、晚上释冷,在第一吸附床、第二吸附床、蓄冷吸附床和冷凝器内设有用于冷却水和热水流通的换热管,换热管的进出水管连接蓄水池,蓄水池连接太阳能集热器。The evaporator and the cooler are respectively connected to the first adsorption bed, the second adsorption bed, and the cold storage adsorption bed, and a plurality of four-way valves and three-way valves are arranged on the connecting pipeline; the four-way valve and the three-way valve are switched, Realize the switching of the first adsorption bed, the second adsorption bed, and the cold storage adsorption bed for adsorption and desorption, and realize the cooling/cooling storage of the system during the day and the cooling release at night. The heat exchange tube is used for the circulation of cooling water and hot water. The water inlet and outlet pipes of the heat exchange tube are connected to the water storage tank, and the water storage tank is connected to the solar heat collector.

所述的系统还设有第一四通阀,其第一个接口为冷却水进口,第二个接口为热水进口,第三个接口连接第一吸附床内部换热管的入口端,第四个接口连接第二吸附床内部换热管的进口端。The system is also provided with a first four-way valve, the first port of which is the cooling water inlet, the second port is the hot water inlet, the third port is connected to the inlet end of the heat exchange tube inside the first adsorption bed, and the second port is connected to the inlet of the heat exchange tube inside the first adsorption bed. The four ports are connected to the inlet ends of the internal heat exchange tubes of the second adsorption bed.

所述的系统还设有第二四通阀,其第一个接口为热水出口,第二个接口为冷却水出口,第三个接口连接第一吸附床内部换热管的出口端,第四个接口连接第二吸附床内部换热管的出口端。The system is also provided with a second four-way valve, the first port of which is the hot water outlet, the second port is the cooling water outlet, the third port is connected to the outlet end of the heat exchange tube inside the first adsorption bed, and the second port is connected to the outlet of the heat exchange tube inside the first adsorption bed. The four ports are connected to the outlet ports of the internal heat exchange tubes of the second adsorption bed.

所述的系统还设有第三四通阀,其第一个接口连接第一吸附床制冷剂的进出口,第二个接口连接第二吸附床制冷剂的进出口,第三个接口连接冷却器制冷剂的进口,第四个接口连接第一制冷阀的制冷剂管道,第一制冷阀连接蒸发器;The system is also provided with a third four-way valve, the first port of which is connected to the inlet and outlet of the refrigerant in the first adsorption bed, the second port is connected to the inlet and outlet of the refrigerant in the second adsorption bed, and the third port is connected to the cooling valve. The refrigerant inlet of the refrigerator, the fourth port is connected to the refrigerant pipeline of the first refrigeration valve, and the first refrigeration valve is connected to the evaporator;

所述的系统还设有一个三通阀,其第一个接口连接蓄冷吸附床,第二个接口连接冷却器,第三个接口连接蒸发器。The system is also provided with a three-way valve, the first port of which is connected to the cold storage adsorption bed, the second port is connected to the cooler, and the third port is connected to the evaporator.

所述的中冷器与蒸发器之间的连接管路上设有第一膨胀阀,The connecting pipeline between the intercooler and the evaporator is provided with a first expansion valve,

所述的储液罐与中冷器的连接管路上,并联第二膨胀阀。The connecting pipeline between the liquid storage tank and the intercooler is connected in parallel with a second expansion valve.

所述的中冷器设有四个流体进出口,分别为:与冷却器连通的第一制冷剂进口、与储液罐连通的第二制冷剂进口、与压缩机连通的第一制冷剂出口、与蒸发器连通的第二制冷机出口。The intercooler is provided with four fluid inlets and outlets, which are respectively: the first refrigerant inlet connected with the cooler, the second refrigerant inlet connected with the liquid storage tank, and the first refrigerant outlet connected with the compressor , The outlet of the second refrigerator communicated with the evaporator.

所述的第一吸附床和第二吸附床内部的换热管通过第一四通阀和第二四通阀连接冷却水和热水;The heat exchange tubes inside the first adsorption bed and the second adsorption bed are connected to cooling water and hot water through the first four-way valve and the second four-way valve;

所述的蓄冷吸附床内部的换热管连接冷却水,或者连接热水;The heat exchange tube inside the cold storage adsorption bed is connected to cooling water or hot water;

所述的冷凝器内的换热管与冷却水管相连接。The heat exchange pipes in the condenser are connected with the cooling water pipes.

所述的第一吸附床、第二吸附床和蓄冷吸附床内均填充氯化锶/膨胀石墨复合吸附剂,制冷剂为氨。The first adsorption bed, the second adsorption bed and the cold storage adsorption bed are all filled with strontium chloride/expanded graphite composite adsorbent, and the refrigerant is ammonia.

所述的系统工作有白天制冷/蓄冷、夜晚释冷两种工作模式,根据不同的模式具有不同的连接方式:The described system works in two working modes: cooling/cooling storage during the day and cooling release at night, with different connection modes according to different modes:

第一种白天制冷/蓄冷模式有制冷、蓄冷两种运行模式,白天制冷运行模式:第一吸附床处于吸附状态,第二吸附床处于解吸状态,第一吸附床制冷剂进出口通过第三四通阀与蒸发器出口相连接,第二吸附床制冷剂进出口通过第三四通阀与冷却器进口相连接,冷却器制冷剂出口与中冷器的第一制冷剂进口相连接,中冷器的第一制冷剂出口与压缩机制冷剂进口相连接;压缩机制冷剂出口与冷凝器制冷剂进口相连接,冷凝器制冷剂出口与储液罐制冷剂进口相连接,储液罐制冷剂出口与中冷器的第二制冷剂进口相连接,中冷器的第二制冷剂出口通过第一膨胀阀与蒸发器制冷剂进口相连接,蒸发器制冷剂出口通过第一制冷剂阀与第三四通阀相连,接入吸附床;通过切换第三四通阀,调节第一吸附床处于解吸状态,第二吸附床处于吸附状态,第一吸附床制冷剂进出口通过第三四通阀与冷却器制冷剂进口相连接,第二吸附床制冷剂进出口通过第三四通阀与蒸发器出口相连接;The first type of daytime refrigeration/cooling storage mode has two operating modes: cooling and cold storage. The daytime cooling operation mode: the first adsorption bed is in the adsorption state, the second adsorption bed is in the desorption state, and the refrigerant inlet and outlet of the first adsorption bed pass through the third and fourth The one-way valve is connected to the outlet of the evaporator, the inlet and outlet of the refrigerant of the second adsorption bed are connected to the inlet of the cooler through the third four-way valve, the outlet of the refrigerant of the cooler is connected to the first refrigerant inlet of the intercooler, and the intercooler The first refrigerant outlet of the condenser is connected to the refrigerant inlet of the compressor; the refrigerant outlet of the compressor is connected to the refrigerant inlet of the condenser, the refrigerant outlet of the condenser is connected to the refrigerant inlet of the liquid storage tank, and the refrigerant of the liquid storage tank The outlet is connected to the second refrigerant inlet of the intercooler, the second refrigerant outlet of the intercooler is connected to the refrigerant inlet of the evaporator through the first expansion valve, and the refrigerant outlet of the evaporator is connected to the second refrigerant outlet through the first refrigerant valve. The three and four-way valves are connected and connected to the adsorption bed; by switching the third and four-way valves, the first adsorption bed is adjusted to be in the desorption state, the second adsorption bed is in the adsorption state, and the refrigerant inlet and outlet of the first adsorption bed pass through the third and four-way valves It is connected to the refrigerant inlet of the cooler, and the refrigerant inlet and outlet of the second adsorption bed are connected to the outlet of the evaporator through the third four-way valve;

白天蓄冷运行模式:蓄冷吸附床制冷剂出口通过三通阀、第三四通阀与冷却器制冷剂进口相连接,冷却器制冷剂出口和中冷器的第一制冷剂进口相连接;中冷器的第一制冷剂出口与压缩机制冷剂进口相连接,压缩机制冷剂出口与冷凝器制冷剂进口相连接,冷凝器制冷剂出口与储液罐制冷剂进口相连接;Daytime cold storage operation mode: the refrigerant outlet of the cold storage adsorption bed is connected to the refrigerant inlet of the cooler through the three-way valve and the third four-way valve, and the refrigerant outlet of the cooler is connected to the first refrigerant inlet of the intercooler; the intercooler The first refrigerant outlet of the condenser is connected to the refrigerant inlet of the compressor, the refrigerant outlet of the compressor is connected to the refrigerant inlet of the condenser, and the refrigerant outlet of the condenser is connected to the refrigerant inlet of the liquid storage tank;

第二种夜晚释冷运行模式:储液罐制冷剂出口与中冷器的第二制冷剂进口相连接,中冷器的第二制冷剂出口通过第一膨胀阀与蒸发器制冷剂进口相连接。The second cooling operation mode at night: the refrigerant outlet of the liquid storage tank is connected to the second refrigerant inlet of the intercooler, and the second refrigerant outlet of the intercooler is connected to the refrigerant inlet of the evaporator through the first expansion valve .

从储液罐流出的制冷剂经中冷器、第一膨胀阀进入蒸发器,蒸发吸热后的制冷剂经三通阀回到蓄冷吸附床,被吸附床吸附,实现连续制冷。The refrigerant flowing out of the liquid storage tank enters the evaporator through the intercooler and the first expansion valve, and the refrigerant after evaporating and absorbing heat returns to the cold storage adsorption bed through the three-way valve, and is adsorbed by the adsorption bed to realize continuous refrigeration.

新型系统根据白天制冷/蓄冷和夜晚释冷两种工作模式,具有不同的工作原理:The new system has different working principles according to the two working modes of cooling/cooling storage during the day and cooling release at night:

白天制冷/蓄冷模式具有制冷、蓄冷两种可以同时进行的运行模式:白天制冷运行模式,第一吸附床通入冷却水处于吸附状态、第二吸附床通入太阳能加热的热水,经压缩机的抽吸调节解吸温度处于解吸状态,解吸出的制冷剂经第三四通阀进入冷却器,在进入中冷器去过热,去过热后的制冷剂进入压缩机压缩,压缩后的制冷剂进入冷凝器冷凝,冷凝后的制冷剂经储液罐进入中冷器,经第一膨胀阀进入蒸发器,蒸发吸热后的制冷剂经第一制冷剂阀、第三四通阀进入第一吸附床,被第一吸附床的吸附剂吸附,当第二吸附床解吸完全/第一吸附床吸附饱和时,切换第三四通阀、第一四通阀和第二四通阀,第一吸附床内部换热管流入热水,在压缩机抽吸作用下,处于解吸状态,第二吸附床内部换热管流入冷却水处于吸附状态,继续制冷过程;白天蓄冷运行模式,蓄冷吸附床通入太阳能加热的热水,在压缩机抽吸调节作用下,进行解吸反应,解吸出的制冷剂经三通阀、第三四通阀进入冷却器、中冷器进入压缩机压缩,压缩后的制冷剂经冷凝器冷凝进入储液罐中储存。The daytime cooling/cooling storage mode has two operating modes of cooling and cold storage that can be carried out at the same time: in the daytime cooling operation mode, the first adsorption bed is fed with cooling water and is in an adsorption state, and the second adsorption bed is fed with solar-heated hot water. The desorption temperature is in the desorption state. The desorbed refrigerant enters the cooler through the third and four-way valve, and then enters the intercooler to desuperheat. The desuperheated refrigerant enters the compressor for compression, and the compressed refrigerant enters the The condenser condenses, and the condensed refrigerant enters the intercooler through the liquid storage tank, enters the evaporator through the first expansion valve, and the refrigerant after evaporating and absorbing heat enters the first adsorption through the first refrigerant valve and the third four-way valve. The bed is adsorbed by the adsorbent of the first adsorption bed. When the second adsorption bed is completely desorbed/the first adsorption bed is saturated, the third four-way valve, the first four-way valve and the second four-way valve are switched. The first adsorption The heat exchange pipe inside the bed flows into the hot water, and under the suction of the compressor, it is in the desorption state, and the heat exchange pipe inside the second adsorption bed flows into the cooling water to be in the adsorption state, and the refrigeration process continues; in the daytime cold storage operation mode, the cold storage adsorption bed is fed The hot water heated by solar energy undergoes a desorption reaction under the suction regulation of the compressor. The desorbed refrigerant enters the cooler through the three-way valve and the third four-way valve, and the intercooler enters the compressor for compression. The agent is condensed by the condenser and stored in the liquid storage tank.

第二种模式:夜晚释冷,从储液罐流出的制冷剂经中冷器、第一膨胀阀进入蒸发器,蒸发吸热后的制冷剂经三通阀回到通入冷却水的蓄冷吸附床,被吸附床吸附,实现连续制冷。The second mode: release cooling at night, the refrigerant flowing out of the liquid storage tank enters the evaporator through the intercooler and the first expansion valve, and the refrigerant after evaporating and absorbing heat returns to the cold storage adsorption of the cooling water through the three-way valve The bed is adsorbed by the adsorption bed to realize continuous refrigeration.

本发明所述吸附剂采用氯化锶,所述制冷剂为氨等。吸附剂氯化锶与制冷剂氨之间依靠络合关系形成配合物,释放反应热。The adsorbent of the present invention adopts strontium chloride, and the refrigerant is ammonia and the like. The adsorbent strontium chloride and the refrigerant ammonia rely on the complexation relationship to form a complex, releasing the heat of reaction.

SrCl2与NH3的反应机理如下述方程式所示:The reaction mechanism of SrCl 2 and NH 3 is shown in the following equation:

Figure BDA0003066888810000041
Figure BDA0003066888810000041

其中ΔHr为化学反应焓,J/mol。Where ΔH r is the chemical reaction enthalpy, J/mol.

为强化吸附剂传热传质性能,所述吸附剂采用固化混合吸附剂,包括金属氯化物与基质,所述基质选为硫化膨胀石墨或者膨胀石墨等。In order to enhance the heat and mass transfer performance of the adsorbent, the adsorbent adopts a solidified mixed adsorbent, including metal chloride and a matrix, and the matrix is selected from vulcanized expanded graphite or expanded graphite.

本发明白天制冷/蓄冷模式利用太阳能使第一吸附床和第二吸附床交替工作实现制冷,同时蓄冷吸附床在压缩机抽吸调节作用下,进行解吸反应,解吸出的制冷剂经压缩机压缩后进入冷凝器冷凝,最后进入储液罐完成蓄冷过程。夜晚释冷模式中,由蓄冷吸附床不断吸附制冷剂,制冷剂在蒸发器中蒸发吸热产生冷量,从而实现连续制冷。本发明引入压缩机调节吸附床解吸压力,降低解吸温度,使系统主动适应波动的太阳能热水温度,实现较低温度解吸吸热;同时在吸附床解吸反应辅助下,提升压缩机吸气压力,降低压缩机的压比,减小压缩机功耗,显著提高制冷效能。The daytime refrigeration/cold storage mode of the present invention utilizes solar energy to make the first adsorption bed and the second adsorption bed work alternately to realize refrigeration, and at the same time, the cold storage adsorption bed undergoes desorption reaction under the action of compressor suction adjustment, and the desorbed refrigerant is compressed by the compressor Then enter the condenser to condense, and finally enter the liquid storage tank to complete the cold storage process. In the cooling release mode at night, the cold storage adsorption bed continuously absorbs the refrigerant, and the refrigerant evaporates and absorbs heat in the evaporator to generate cooling capacity, thereby realizing continuous refrigeration. The present invention introduces a compressor to adjust the desorption pressure of the adsorption bed, lowers the desorption temperature, makes the system actively adapt to the fluctuating solar hot water temperature, and realizes desorption and heat absorption at a lower temperature; at the same time, with the assistance of the desorption reaction of the adsorption bed, the suction pressure of the compressor is increased, Reduce the pressure ratio of the compressor, reduce the power consumption of the compressor, and significantly improve the cooling efficiency.

与现有技术相比,本发明具有以下优点:Compared with the prior art, the present invention has the following advantages:

(1)本发明采用了压缩机辅助吸附制冷/蓄冷的方式,压缩机抽吸调节解吸压力,降低吸附剂解吸温度,能够主动适应不稳定太阳能热源,实现吸附剂较低温度解吸吸热,实现太阳能的高效回收利用;(1) The present invention adopts the mode of compressor-assisted adsorption refrigeration/cold storage, the compressor suction adjusts the desorption pressure, reduces the desorption temperature of the adsorbent, can actively adapt to the unstable solar heat source, realizes the desorption and heat absorption of the adsorbent at a lower temperature, and realizes Efficient recycling of solar energy;

(2)本发明的压缩机在吸附床解吸反应的辅助下,显著提高吸气压力,降低压缩机压比,降低能耗,提高系统能效比;(2) The compressor of the present invention significantly improves the suction pressure, reduces the compressor pressure ratio, reduces energy consumption, and improves the system energy efficiency ratio under the assistance of the adsorption bed desorption reaction;

(3)本发明工作模式分为白天制冷/蓄冷模式和夜晚释冷模式,夜晚释冷模式中,储液罐流出的制冷剂,经节流进入蒸发器蒸发吸热,产生冷量,最后回到蓄冷吸附床被吸附剂吸附,从而实现连续制冷;(3) The working mode of the present invention is divided into daytime refrigeration/cooling storage mode and night release cooling mode. In the night release cooling mode, the refrigerant flowing out of the liquid storage tank enters the evaporator through throttling to evaporate and absorb heat to generate cooling capacity, and finally returns to the evaporator. Until the cold storage adsorption bed is adsorbed by the adsorbent, so as to realize continuous refrigeration;

(4)本发明采用太阳能集热器回收利用太阳能,系统初始成本显著降低。(4) The present invention adopts solar heat collectors to recycle solar energy, and the initial cost of the system is significantly reduced.

附图说明Description of drawings

图1所示的是实施例1中新型高效利用太阳能的低温制冷/蓄冷系统装置结构示意图;What Fig. 1 shows is the structural schematic diagram of the low-temperature refrigeration/cold storage system device of novel high-efficiency utilization of solar energy in Embodiment 1;

图2所示的是实施例1中中冷器结构示意图;What Fig. 2 shows is the structural representation of intercooler in embodiment 1;

图3所示的是新型高效利用太阳能的低温制冷/蓄冷系统运行时的lnp-T图。Figure 3 shows the lnp-T diagram of the new low-temperature refrigeration/storage system that efficiently utilizes solar energy during operation.

具体实施方式Detailed ways

下面将结合示意图对本发明的新型高效利用太阳能的低温制冷、蓄冷系统进行更详细的描述,其中表示了本发明的优选实施例,应该理解本领域技术人员可以修改在此描述的本发明,而仍然实现本发明的有利效果。因此,下列描述应当被理解为对于本领域技术人员的广泛知道,而并不作为对本发明的限制。The novel high-efficiency solar energy utilization low-temperature refrigeration and cold storage system of the present invention will be described in more detail below in conjunction with the schematic diagram, wherein a preferred embodiment of the present invention is shown, and it should be understood that those skilled in the art can modify the present invention described here, and still The advantageous effects of the present invention are realized. Therefore, the following description should be understood as the broad knowledge of those skilled in the art, but not as a limitation of the present invention.

本发明采用的各种组件均为本领域的常规组件,在本发明的描述中,需要说明的是,对于采用的吸附剂,表示的是本发明的优选实例吸附剂,而并不作为对本发明的限制。The various components used in the present invention are conventional components in the field. In the description of the present invention, it should be noted that, for the adsorbent used, it is a preferred example adsorbent of the present invention, and is not intended as a reference to the present invention. limits.

如图1所示,一种新型高效利用太阳能的低温制冷、蓄冷系统,包括:压缩机1、冷凝器2、储液罐3、中冷器4、蒸发器5、冷却器6、第一四通阀71、第二四通阀72、第三四通阀73、第一膨胀阀81、第二膨胀阀82、第一制冷剂阀83、第一制冷剂阀84、三通阀9、第一吸附床101、第二吸附床102、蓄冷吸附床11。As shown in Figure 1, a new type of low-temperature refrigeration and cold storage system that efficiently utilizes solar energy includes: compressor 1, condenser 2, liquid storage tank 3, intercooler 4, evaporator 5, cooler 6, first four One-way valve 71, second four-way valve 72, third four-way valve 73, first expansion valve 81, second expansion valve 82, first refrigerant valve 83, first refrigerant valve 84, three-way valve 9, second An adsorption bed 101 , a second adsorption bed 102 , and a cold storage adsorption bed 11 .

在第一吸附床101、第二吸附床102以及蓄冷吸附床11内填充氯化锶、膨胀石墨复合吸附剂,制冷剂在第一吸附床101,第二吸附床102以及蓄冷吸附床11之间流通,在第一吸附床101、第二吸附床102、蓄冷吸附床11和冷凝器2内设有用于冷却水和热水流通的换热管。Fill strontium chloride and expanded graphite composite adsorbent in the first adsorption bed 101, the second adsorption bed 102 and the cold storage adsorption bed 11, and the refrigerant is between the first adsorption bed 101, the second adsorption bed 102 and the cold storage adsorption bed 11 Circulation, in the first adsorption bed 101, the second adsorption bed 102, the cold storage adsorption bed 11 and the condenser 2, there are heat exchange tubes for the circulation of cooling water and hot water.

本实施例中,第一四通阀71,其第一个接口为冷却水进口,第二个接口为热水进口,第三个接口连接第一吸附床101内部换热管的入口端,第四个接口连接第二吸附床102内部换热管的进口端。In this embodiment, for the first four-way valve 71, the first port is the cooling water inlet, the second port is the hot water inlet, the third port is connected to the inlet end of the internal heat exchange tube of the first adsorption bed 101, and the second port is The four ports are connected to the inlet ends of the internal heat exchange tubes of the second adsorption bed 102 .

本实施例中,第二四通阀72,其第一个接口为热水出口,第二个接口为冷却水出口,第三个接口连接第一吸附床101内部换热管的出口端,第四个接口连接第二吸附床102内部换热管的出口端。In this embodiment, the first port of the second four-way valve 72 is the hot water outlet, the second port is the cooling water outlet, and the third port is connected to the outlet end of the heat exchange tube inside the first adsorption bed 101. The four ports are connected to the outlet ends of the heat exchange tubes inside the second adsorption bed 102 .

本实施例中,第三四通阀73,其第一个接口连接第一吸附床101制冷剂的进出口,第二个接口连接第二吸附床102制冷剂的进出口,第三个接口连接冷却器6制冷剂的进口,第四个接口连接第一制冷阀81的制冷剂管道,第一制冷阀81连接蒸发器5;In this embodiment, the third four-way valve 73 has its first interface connected to the inlet and outlet of the refrigerant in the first adsorption bed 101, the second interface connected to the inlet and outlet of the refrigerant in the second adsorption bed 102, and the third interface connected to The inlet of the refrigerant of the cooler 6, the fourth port is connected to the refrigerant pipeline of the first refrigeration valve 81, and the first refrigeration valve 81 is connected to the evaporator 5;

本实施例中,三通阀9,其第一个接口连接蓄冷吸附床11,第二个接口连接冷却器6,第三个接口连接蒸发器5。In this embodiment, the first port of the three-way valve 9 is connected to the cold storage adsorption bed 11 , the second port is connected to the cooler 6 , and the third port is connected to the evaporator 5 .

本实施例中,中冷器4与蒸发器5之间的连接管路上设置第一膨胀阀83,In this embodiment, a first expansion valve 83 is provided on the connecting pipeline between the intercooler 4 and the evaporator 5,

本实施例中,储液罐3与中冷器4的连接管路上,并联第二膨胀阀84。In this embodiment, the second expansion valve 84 is connected in parallel on the connecting pipeline between the liquid storage tank 3 and the intercooler 4 .

如图2所示,所述的中冷器4设有四个流体进出口,分别为:与冷却器6连通的第一制冷剂进口41、与储液罐3连通的第二制冷剂进口42、与压缩机1连通的第一制冷剂出口43、与蒸发器5连通的第二制冷机出口44。As shown in Figure 2, the intercooler 4 is provided with four fluid inlets and outlets, which are respectively: a first refrigerant inlet 41 communicated with the cooler 6, and a second refrigerant inlet 42 communicated with the liquid storage tank 3 , the first refrigerant outlet 43 communicating with the compressor 1 , and the second refrigerator outlet 44 communicating with the evaporator 5 .

在换热流体侧,第一吸附床101和第二吸附床102内部的换热管通过第一四通阀71和第二四通阀72连接冷却水和热水;蓄冷吸附床11内部的换热管可连接冷却水,也可连接热水;冷凝器2内的换热管与冷却水管相连接;On the heat exchange fluid side, the heat exchange tubes inside the first adsorption bed 101 and the second adsorption bed 102 are connected to cooling water and hot water through the first four-way valve 71 and the second four-way valve 72; The heat pipe can be connected to cooling water or hot water; the heat exchange pipe in the condenser 2 is connected to the cooling water pipe;

在制冷剂侧,当第一吸附床101处于吸附状态,第二吸附床102处于解吸状态时,第一吸附床101制冷剂进出口通过第三四通阀73与蒸发器5出口相连接;第二吸附床102制冷剂进出口通过第三四通阀73与冷却器进口相连接;冷却器6制冷剂出口与中冷器4第一制冷剂进口41相连接;中冷器4第一制冷剂出口43与压缩机1制冷剂进口相连接;压缩机1制冷剂出口与冷凝器2制冷剂进口相连接;冷凝器2制冷剂出口与储液罐3制冷剂进口相连接;储液罐3制冷剂出口与中冷器4第二制冷剂进口42相连接;中冷器4第二制冷剂出口44通过第一膨胀阀83与蒸发器5制冷剂进口相连接;蒸发器5制冷剂出口通过第一制冷剂阀81与第三四通阀73相连,通过第二膨胀阀82与冷却器6制冷剂出口管道相连接;蓄冷吸附床11制冷剂出口通过三通阀9与冷却器6制冷剂进口和蒸发器5制冷剂出口相连接;通过第三四通阀73调节第一吸附床101和第二吸附床102的工作状态,当第一吸附床101处于解吸状态,第二吸附床102处于吸附状态时,第一吸附床101制冷剂进出口通过第三四通阀73与冷却器6制冷剂进口相连接;第二吸附床102制冷剂进出口通过第三四通阀73与蒸发器出口5相连接。On the refrigerant side, when the first adsorption bed 101 is in the adsorption state and the second adsorption bed 102 is in the desorption state, the refrigerant inlet and outlet of the first adsorption bed 101 are connected to the outlet of the evaporator 5 through the third four-way valve 73; The refrigerant inlet and outlet of the second adsorption bed 102 are connected to the inlet of the cooler through the third four-way valve 73; the refrigerant outlet of the cooler 6 is connected to the first refrigerant inlet 41 of the intercooler 4; the first refrigerant of the intercooler 4 The outlet 43 is connected to the refrigerant inlet of the compressor 1; the refrigerant outlet of the compressor 1 is connected to the refrigerant inlet of the condenser 2; the refrigerant outlet of the condenser 2 is connected to the refrigerant inlet of the liquid storage tank 3; the liquid storage tank 3 is refrigerated The refrigerant outlet is connected to the second refrigerant inlet 42 of the intercooler 4; the second refrigerant outlet 44 of the intercooler 4 is connected to the refrigerant inlet of the evaporator 5 through the first expansion valve 83; the refrigerant outlet of the evaporator 5 is connected through the second A refrigerant valve 81 is connected to the third four-way valve 73, and is connected to the refrigerant outlet pipe of the cooler 6 through the second expansion valve 82; the refrigerant outlet of the cold storage adsorption bed 11 is connected to the refrigerant inlet of the cooler 6 through the three-way valve 9 It is connected with the refrigerant outlet of the evaporator 5; the working state of the first adsorption bed 101 and the second adsorption bed 102 is adjusted through the third four-way valve 73. When the first adsorption bed 101 is in the desorption state, the second adsorption bed 102 is in the adsorption state. state, the refrigerant inlet and outlet of the first adsorption bed 101 are connected to the refrigerant inlet of the cooler 6 through the third four-way valve 73; the refrigerant inlet and outlet of the second adsorption bed 102 are connected to the outlet of the evaporator 5 through the third four-way valve 73 connected.

本实施例中,第一吸附床101、第二吸附床102以及蓄冷吸附床11内均填充氯化锶/膨胀石墨复合吸附剂,制冷剂为氨等。吸附剂氯化锶与制冷剂氨之间依靠络合关系形成配合物,释放高温反应热。In this embodiment, the first adsorption bed 101 , the second adsorption bed 102 and the cold storage adsorption bed 11 are all filled with strontium chloride/expanded graphite composite adsorbent, and the refrigerant is ammonia or the like. The adsorbent strontium chloride and the refrigerant ammonia rely on complexation to form a complex, releasing high-temperature reaction heat.

SrCl2与NH3的反应机理如下述方程式所示:The reaction mechanism of SrCl 2 and NH 3 is shown in the following equation:

Figure BDA0003066888810000071
Figure BDA0003066888810000071

其中ΔHr为化学反应焓,J/mol。Where ΔH r is the chemical reaction enthalpy, J/mol.

为强化吸附剂传热传质性能,所述吸附剂采用固化混合吸附剂,包括金属氯化物与基质,所述基质选为硫化膨胀石墨或者膨胀石墨等。In order to enhance the heat and mass transfer performance of the adsorbent, the adsorbent adopts a solidified mixed adsorbent, including metal chloride and a matrix, and the matrix is selected from vulcanized expanded graphite or expanded graphite.

本实施例的工作原理如下:The working principle of this embodiment is as follows:

(a)白天制冷/蓄冷模式:(a) Daytime cooling/cooling storage mode:

第一吸附床在压缩机抽吸调节作用下,解吸温度由Tdes降至T'des,被太阳能热水加热发生解吸反应,第二吸附床被冷却水冷却发生吸附反应,第一吸附床解吸出来的制冷剂经冷却器冷却去过热后,被吸压缩机压缩,然后高温高压的制冷剂流向冷凝器冷凝,冷凝液经膨胀阀节流进入蒸发器蒸发吸热,产生制冷量,最后制冷剂被第二吸附床中的吸附剂为吸附,吸附温度为Tsor,如图3所示;切换第三四通阀,第一吸附床被冷却水冷却发生吸附反应,第二吸附床在压缩机抽吸调节作用下,被太阳能热水加热发生解吸反应,重复以上制冷过程;The desorption temperature of the first adsorption bed is lowered from T des to T' des under the suction adjustment of the compressor, and the desorption reaction occurs when the solar hot water is heated, the second adsorption bed is cooled by the cooling water and the adsorption reaction occurs, and the first adsorption bed desorbs After being cooled by the cooler to desuperheat, the refrigerant that comes out is compressed by the suction compressor, and then the high-temperature and high-pressure refrigerant flows to the condenser to condense. Adsorbed by the adsorbent in the second adsorption bed, the adsorption temperature is Tsor , as shown in Figure 3; switch the third four-way valve, the first adsorption bed is cooled by cooling water to undergo adsorption reaction, and the second adsorption bed is in the compressor Under the action of suction adjustment, the desorption reaction occurs when heated by solar hot water, and the above refrigeration process is repeated;

蓄冷吸附床在压缩机抽吸调节作用下,被太阳能热水加热发生解吸反应,解吸出来的制冷剂经压缩机压缩,流向冷凝器冷凝,制冷剂冷凝液积存在储液罐中.Under the suction regulation of the compressor, the cold storage adsorption bed is heated by solar hot water to undergo a desorption reaction. The desorbed refrigerant is compressed by the compressor and flows to the condenser to condense. The refrigerant condensate is stored in the liquid storage tank.

(b)夜晚释冷模式:(b) Cooling mode at night:

白天积存在储液罐中的冷凝液经膨胀阀节流进入蒸发器蒸发吸热产生制冷量,制冷剂流进通入冷却水的蓄冷吸附床,被蓄冷吸附床中的吸附剂吸附。During the day, the condensate accumulated in the liquid storage tank is throttled by the expansion valve and enters the evaporator to evaporate and absorb heat to generate cooling capacity. The refrigerant flows into the cold storage adsorption bed that flows into the cooling water, and is adsorbed by the adsorbent in the cold storage adsorption bed.

压缩辅助吸附的制冷/蓄冷方式,通过压缩机抽吸作用,使吸附床解吸温度由Tdes降至T'des,同时压缩机的吸气压力由pe提升至p'des,主动适应不稳定太阳能热源,实现较低温度解吸吸热,降低了压缩机压比,实现连续制冷,减小了能耗,提高了能效比。Compression-assisted adsorption refrigeration/cold storage method, through the suction of the compressor, the desorption temperature of the adsorption bed is reduced from T des to T' des , and the suction pressure of the compressor is increased from p e to p' des , actively adapting to the instability The solar heat source realizes desorption and heat absorption at a lower temperature, reduces the pressure ratio of the compressor, realizes continuous refrigeration, reduces energy consumption, and improves the energy efficiency ratio.

本发明一个具体实施方式如下所述:选取氯化锶为吸附剂,氨为制冷剂。假设蒸发温度为-25℃。表1显示了蒸发温度为-25℃时新型制冷/蓄冷系统与蒸气压缩制冷系统在不同热源温度下的COP。在热源温度为65-95℃,新型制冷/蓄冷系统COP均远高于蒸气压缩制冷系统的COP,这克服吸附制冷系统对高热源温度的要求,实现了较低温度解吸,主动适应不稳定太阳能热水温度。A specific embodiment of the present invention is as follows: select strontium chloride as the adsorbent, and ammonia as the refrigerant. Assume that the evaporation temperature is -25°C. Table 1 shows the COP of the new refrigeration/cool storage system and the vapor compression refrigeration system at different heat source temperatures when the evaporation temperature is -25°C. When the temperature of the heat source is 65-95°C, the COP of the new refrigeration/cold storage system is much higher than that of the vapor compression refrigeration system, which overcomes the requirement of the adsorption refrigeration system for high heat source temperature, realizes desorption at a lower temperature, and actively adapts to unstable solar energy hot water temperature.

表2显示了热源温度为90℃时新型制冷/蓄冷系统与蒸气压缩制冷系统在不同蒸发温度下的压缩机压比,新型制冷/蓄冷系统压缩机压比均远低于蒸气压缩制冷系统的压缩机压比。Table 2 shows the compressor pressure ratios of the new refrigeration/cool storage system and the vapor compression refrigeration system at different evaporation temperatures when the heat source temperature is 90°C. The compressor pressure ratios of the new refrigeration/cool storage system are much lower than those of the vapor compression refrigeration system. Machine pressure ratio.

表1新型系统与蒸气压缩制冷系统COP(蒸发温度为-25℃)Table 1 COP of new system and vapor compression refrigeration system (evaporation temperature is -25°C)

Figure BDA0003066888810000081
Figure BDA0003066888810000081

表2新型系统与蒸气压缩制冷系统压缩机压比(热源温度为90℃)Table 2 Compressor pressure ratio between the new system and the vapor compression refrigeration system (heat source temperature is 90°C)

Figure BDA0003066888810000082
Figure BDA0003066888810000082

需要说明的是,本发明使用的序数形容词“第一”、“第二”、“第三”、“第四”等用来描述共同的对象,仅表示指代相同对象的不同实例,而并不是要暗示这样描述的对象必须采用给定的顺序,无论是时间地、空间地、排序地或任何其它方式。It should be noted that the ordinal adjectives "first", "second", "third", "fourth" and the like used in the present invention are used to describe common objects, and only indicate different instances of the same object, and do not It is not intended to imply that objects so described must be in a given order, whether temporally, spatially, sequentially or in any other way.

上述仅为本发明的优选实施例而已,并不对本发明起到任何限制作用。任何所属技术领域的技术人员,在不脱离本发明的技术方案的范围内,对本发明揭露的技术方案和技术内容做任何形式的等同替换或修改等变动,均属未脱离本发明的技术方案的内容,仍属于本发明的保护范围之内。The foregoing are only preferred embodiments of the present invention, and do not limit the present invention in any way. Any person skilled in the technical field, within the scope of the technical solution of the present invention, makes any form of equivalent replacement or modification to the technical solution and technical content disclosed in the present invention, which does not depart from the technical solution of the present invention. The content still belongs to the protection scope of the present invention.

Claims (9)

1.一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,包括压缩机(1)、冷凝器(2)、储液罐(3)、中冷器(4)、蒸发器(5)、冷却器(6)、第一吸附床(101)、第二吸附床(102)、蓄冷吸附床(11);所述的压缩机(1)依次连接冷凝器(2)、储液罐(3)、中冷器(4);所述的中冷器(4)设有多个进出口,分别连接压缩机(1)、蒸发器(5)和冷却器(6);1. A low-temperature refrigeration storage system for efficiently utilizing solar energy, characterized in that it includes a compressor (1), a condenser (2), a liquid storage tank (3), an intercooler (4), an evaporator (5), Cooler (6), first adsorption bed (101), second adsorption bed (102), cold storage adsorption bed (11); the compressor (1) is sequentially connected to the condenser (2), liquid storage tank (3 ), an intercooler (4); the intercooler (4) is provided with multiple inlets and outlets, respectively connected to the compressor (1), evaporator (5) and cooler (6); 所述的蒸发器(5)和冷却器(6)分别连接第一吸附床(101)、第二吸附床(102)、蓄冷吸附床(11),并在连接管道上设有多个四通阀或三通阀;通过四通阀或三通阀的作用,使第一吸附床(101)和第二吸附床(102)、蓄冷吸附床(11)进行吸附和解吸的切换,实现白天制冷和蓄冷、晚上释冷运行,在第一吸附床(101)、第二吸附床(102)、蓄冷吸附床(11)和冷凝器(2)内设有用于冷却水和热水流通的换热管,换热管的进出水管连接蓄水池,蓄水池连接太阳能集热器;The evaporator (5) and cooler (6) are respectively connected to the first adsorption bed (101), the second adsorption bed (102), and the cold storage adsorption bed (11), and a plurality of four-way connections are arranged on the connecting pipes valve or three-way valve; through the action of the four-way valve or three-way valve, the first adsorption bed (101), the second adsorption bed (102), and the cold storage adsorption bed (11) are switched between adsorption and desorption to achieve daytime refrigeration and cold storage, cooling operation at night, in the first adsorption bed (101), the second adsorption bed (102), the cold storage adsorption bed (11) and the condenser (2) are equipped with heat exchange for cooling water and hot water circulation The inlet and outlet pipes of the heat exchange tubes are connected to the reservoir, and the reservoir is connected to the solar collector; 所述的系统还设有第三四通阀(73),其第一个接口连接第一吸附床(101)制冷剂的进出口,第二个接口连接第二吸附床(102)制冷剂的进出口,第三个接口连接冷却器(6)制冷剂的进口,第四个接口连接第一制冷阀(81)的制冷剂管道,第一制冷阀(81)连接蒸发器(5);The system is also provided with a third four-way valve (73), the first interface of which is connected to the inlet and outlet of the refrigerant in the first adsorption bed (101), and the second interface is connected to the outlet of the refrigerant in the second adsorption bed (102). The inlet and outlet, the third interface is connected to the refrigerant inlet of the cooler (6), the fourth interface is connected to the refrigerant pipeline of the first refrigeration valve (81), and the first refrigeration valve (81) is connected to the evaporator (5); 所述的系统还设有一个三通阀(9),其第一个接口连接蓄冷吸附床(11),第二个接口连接冷却器(6),第三个接口连接蒸发器(5);The system is also provided with a three-way valve (9), the first port of which is connected to the cold storage adsorption bed (11), the second port is connected to the cooler (6), and the third port is connected to the evaporator (5); 所述的系统运行有白天制冷/蓄冷、夜晚释冷两种工作模式,白天制冷/蓄冷模式利用太阳能使第一吸附床(101)和第二吸附床(102)交替工作实现制冷,同时蓄冷吸附床(11)在压缩机(1)抽吸调节作用下,进行解吸反应,解吸出的制冷剂经压缩机(1)压缩后进入冷凝器(2)冷凝,最后进入储液罐(3)完成蓄冷过程;夜晚释冷模式中,由蓄冷吸附床(11)不断吸附制冷剂,制冷剂在蒸发器(5)中蒸发吸热产生冷量,从而实现连续制冷。The system operates in two working modes: daytime cooling/cooling storage and night cooling release. The daytime cooling/cooling storage mode uses solar energy to make the first adsorption bed (101) and the second adsorption bed (102) work alternately to achieve refrigeration, while cold storage and adsorption The bed (11) undergoes a desorption reaction under the suction regulation of the compressor (1), and the desorbed refrigerant is compressed by the compressor (1) and enters the condenser (2) for condensation, and finally enters the liquid storage tank (3) to complete Cold storage process: In the cooling release mode at night, the cold storage adsorption bed (11) continuously adsorbs the refrigerant, and the refrigerant evaporates and absorbs heat in the evaporator (5) to generate cold energy, thereby realizing continuous refrigeration. 2.根据权利要求1所述的一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,所述的系统还设有第一四通阀(71),其第一个接口为冷却水进口,第二个接口为热水进口,第三个接口连接第一吸附床(101)内部换热管的入口端,第四个接口连接第二吸附床(102)内部换热管的进口端。2. A low-temperature refrigeration and cold storage system that efficiently utilizes solar energy according to claim 1, characterized in that the system is also provided with a first four-way valve (71), the first interface of which is the cooling water inlet, The second interface is the hot water inlet, the third interface is connected to the inlet end of the internal heat exchange tube of the first adsorption bed (101), and the fourth interface is connected to the inlet end of the internal heat exchange tube of the second adsorption bed (102). 3.根据权利要求1所述的一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,所述的系统还设有第二四通阀(72),其第一个接口为热水出口,第二个接口为冷却水出口,第三个接口连接第一吸附床(101)内部换热管的出口端,第四个接口连接第二吸附床(102)内部换热管的出口端。3. A low-temperature refrigeration and cold storage system that efficiently utilizes solar energy according to claim 1, characterized in that the system is also provided with a second four-way valve (72), the first interface of which is a hot water outlet, The second interface is the cooling water outlet, the third interface is connected to the outlet end of the internal heat exchange tube of the first adsorption bed (101), and the fourth interface is connected to the outlet end of the internal heat exchange tube of the second adsorption bed (102). 4.根据权利要求1所述的一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,所述的中冷器(4)与蒸发器(5)之间的连接管路上设有第一膨胀阀(83),4. A low-temperature refrigeration and cold storage system that efficiently utilizes solar energy according to claim 1, characterized in that, the connecting pipeline between the intercooler (4) and the evaporator (5) is provided with a first expansion valve (83), 所述的储液罐(3)与中冷器(4)的连接管路上,并联第二膨胀阀(84)。A second expansion valve (84) is connected in parallel on the connecting pipeline between the liquid storage tank (3) and the intercooler (4). 5.根据权利要求1所述的一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,所述的中冷器(4)设有四个流体进出口,分别为:与冷却器(6)连通的第一制冷剂进口(41)、与储液罐(3)连通的第二制冷剂进口(42)、与压缩机(1)连通的第一制冷剂出口(43)、与蒸发器(5)连通的第二制冷剂出口(44)。5. A low-temperature refrigeration and cold storage system for efficient utilization of solar energy according to claim 1, characterized in that the intercooler (4) is provided with four fluid inlets and outlets, which are respectively: and the cooler (6) The first refrigerant inlet (41) communicated with the liquid storage tank (3), the second refrigerant inlet (42) communicated with the compressor (1), the first refrigerant outlet (43) communicated with the compressor (1), and the evaporator ( 5) The connected second refrigerant outlet (44). 6.根据权利要求1所述的一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,所述的第一吸附床(101)和第二吸附床(102)内部的换热管通过第一四通阀(71)和第二四通阀(72)连接冷却水和热水;6. A low-temperature refrigeration and cold storage system that efficiently utilizes solar energy according to claim 1, characterized in that the heat exchange tubes inside the first adsorption bed (101) and the second adsorption bed (102) pass through the first The four-way valve (71) and the second four-way valve (72) are connected to cooling water and hot water; 所述的蓄冷吸附床(11)内部的换热管连接冷却水,或者连接热水;The heat exchange tube inside the cold storage adsorption bed (11) is connected to cooling water or hot water; 所述的冷凝器(2)内的换热管与冷却水管相连接。The heat exchange pipes in the condenser (2) are connected with the cooling water pipes. 7.根据权利要求1所述的一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,所述的第一吸附床(101)、第二吸附床(102)和蓄冷吸附床(11)内均填充氯化锶/膨胀石墨复合吸附剂,制冷剂为氨。7. A low-temperature refrigeration storage system for efficiently utilizing solar energy according to claim 1, characterized in that, the first adsorption bed (101), the second adsorption bed (102) and the cold storage adsorption bed (11) Both are filled with strontium chloride/expanded graphite composite adsorbent, and the refrigerant is ammonia. 8.根据权利要求1~7中任一所述的一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,所述的系统运行有白天制冷/蓄冷、夜晚释冷两种工作模式,根据不同的模式具有的连接方式如下:8. A low-temperature refrigeration and cold storage system that efficiently utilizes solar energy according to any one of claims 1 to 7, characterized in that the system operates in two working modes: cooling/cooling storage during the day and cooling release at night. The schema has the following connections: 第一种白天制冷/蓄冷模式,具有制冷、蓄冷两种运行方式:白天制冷运行模式:第一吸附床(101)处于吸附状态,第二吸附床(102)处于解吸状态,第一吸附床(101)制冷剂进出口通过第三四通阀(73)与蒸发器(5)出口相连接,第二吸附床(102)制冷剂进出口通过第三四通阀(73)与冷却器(6)进口相连接,冷却器(6)制冷剂出口与中冷器(4)的第一制冷剂进口(41)相连接,中冷器(4)的第一制冷剂出口(43)与压缩机(1)制冷剂进口相连接;压缩机(1)制冷剂出口与冷凝器(2)制冷剂进口相连接,冷凝器(2)制冷剂出口与储液罐(3)制冷剂进口相连接,储液罐(3)制冷剂出口与中冷器(4)的第二制冷剂进口(42)相连接,中冷器(4)的第二制冷剂出口(44)通过第一膨胀阀(83)与蒸发器(5)制冷剂进口相连接,蒸发器(5)制冷剂出口通过第一制冷剂阀(81)与第三四通阀(73)相连,接入吸附床(101);通过切换第三四通阀(73),调节第一吸附床(101)处于解吸状态,第二吸附床(102)处于吸附状态,第一吸附床(101)制冷剂进出口通过第三四通阀(73)与冷却器(6)制冷剂进口相连接,第二吸附床(102)制冷剂进出口通过第三四通阀(73)与蒸发器(5)出口相连接;The first type of daytime refrigeration/cooling storage mode has two operation modes of cooling and cold storage: daytime cooling operation mode: the first adsorption bed (101) is in the adsorption state, the second adsorption bed (102) is in the desorption state, and the first adsorption bed ( 101) The refrigerant inlet and outlet are connected to the outlet of the evaporator (5) through the third four-way valve (73), and the refrigerant inlet and outlet of the second adsorption bed (102) are connected to the cooler (6) through the third four-way valve (73). ) inlet, the refrigerant outlet of the cooler (6) is connected with the first refrigerant inlet (41) of the intercooler (4), and the first refrigerant outlet (43) of the intercooler (4) is connected with the compressor (1) The refrigerant inlet is connected; the compressor (1) refrigerant outlet is connected to the condenser (2) refrigerant inlet, and the condenser (2) refrigerant outlet is connected to the liquid storage tank (3) refrigerant inlet, The refrigerant outlet of the liquid storage tank (3) is connected to the second refrigerant inlet (42) of the intercooler (4), and the second refrigerant outlet (44) of the intercooler (4) passes through the first expansion valve (83 ) is connected to the refrigerant inlet of the evaporator (5), and the refrigerant outlet of the evaporator (5) is connected to the third four-way valve (73) through the first refrigerant valve (81) and connected to the adsorption bed (101); Switch the third four-way valve (73), adjust the first adsorption bed (101) in the desorption state, the second adsorption bed (102) in the adsorption state, and the refrigerant inlet and outlet of the first adsorption bed (101) pass through the third four-way valve (73) is connected to the refrigerant inlet of the cooler (6), and the refrigerant inlet and outlet of the second adsorption bed (102) is connected to the outlet of the evaporator (5) through the third four-way valve (73); 白天蓄冷运行模式:蓄冷吸附床(11)制冷剂出口通过三通阀(9)、第三四通阀(73)与冷却器(6)制冷剂进口相连接,冷却器(6)制冷剂出口和中冷器(4)的第一制冷剂进口(41)相连接;中冷器(4)的第一制冷剂出口(43)与压缩机(1)制冷剂进口相连接,压缩机(1)制冷剂出口与冷凝器(2)制冷剂进口相连接,冷凝器(2)制冷剂出口与储液罐(3)制冷剂进口相连接;Daytime cold storage operation mode: the refrigerant outlet of the cold storage adsorption bed (11) is connected to the refrigerant inlet of the cooler (6) through the three-way valve (9) and the third four-way valve (73), and the refrigerant outlet of the cooler (6) It is connected with the first refrigerant inlet (41) of the intercooler (4); the first refrigerant outlet (43) of the intercooler (4) is connected with the refrigerant inlet of the compressor (1), and the compressor (1 ) The refrigerant outlet is connected to the refrigerant inlet of the condenser (2), and the refrigerant outlet of the condenser (2) is connected to the refrigerant inlet of the liquid storage tank (3); 第二种夜晚释冷运行模式:储液罐(3)制冷剂出口与中冷器(4)的第二制冷剂进口(42)相连接,中冷器(4)的第二制冷剂出口(44)通过第一膨胀阀(83)与蒸发器(5)制冷剂进口相连接。The second cooling operation mode at night: the refrigerant outlet of the liquid storage tank (3) is connected to the second refrigerant inlet (42) of the intercooler (4), and the second refrigerant outlet of the intercooler (4) ( 44) Connect to the refrigerant inlet of the evaporator (5) through the first expansion valve (83). 9.根据权利要求8所述的一种高效利用太阳能的低温制冷蓄冷系统,其特征在于,从储液罐(3)流出的制冷剂经中冷器(4)、第一膨胀阀(83)进入蒸发器(5),蒸发吸热后的制冷剂经三通阀(9)回到蓄冷吸附床(11),被吸附床吸附,实现连续制冷。9. A low-temperature refrigeration and cold storage system that efficiently utilizes solar energy according to claim 8, characterized in that the refrigerant flowing out from the liquid storage tank (3) passes through the intercooler (4) and the first expansion valve (83) Entering the evaporator (5), the refrigerant after evaporating and absorbing heat returns to the cold storage adsorption bed (11) through the three-way valve (9), and is adsorbed by the adsorption bed to realize continuous refrigeration.
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