CN102287958A - Lithium bromide solution absorbing type refrigerating process of air-conditioner - Google Patents
Lithium bromide solution absorbing type refrigerating process of air-conditioner Download PDFInfo
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- CN102287958A CN102287958A CN201110165350XA CN201110165350A CN102287958A CN 102287958 A CN102287958 A CN 102287958A CN 201110165350X A CN201110165350X A CN 201110165350XA CN 201110165350 A CN201110165350 A CN 201110165350A CN 102287958 A CN102287958 A CN 102287958A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
- Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
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Abstract
一种溴化锂溶液吸收式空调的制冷工艺,涉及一种空调的制冷工艺,包括有制冷设备,冷媒水换热器、蒸发器、盘管冷凝器、单向阀、发生器、加热器,其特征在于,蒸发器2和第一发生器8及第二发生器11之间用管道连接,管道上连接有蒸发器单向阀4、蒸发器与发生器相连的单向阀5、第二发生器单向阀6、第一发生器单向阀7和盘管冷凝器3,蒸发器2的液体中设有冷媒水换热器1;发生器的液体中设有发生器加热器,冷媒水换热器1与空调空间相连。本发明制冷循环工艺简单,无转动设备,且体积小,涉及设备少、可利用发动机余热制冷。
A refrigeration process of lithium bromide solution absorption type air conditioner, relates to a refrigeration process of air conditioner, including refrigeration equipment, refrigerant water heat exchanger, evaporator, coil condenser, one-way valve, generator, heater, its characteristics That is, the evaporator 2 is connected with the first generator 8 and the second generator 11 with a pipeline, and the pipeline is connected with the evaporator check valve 4, the check valve 5 that the evaporator is connected to the generator, and the second generator One-way valve 6, first generator one-way valve 7 and coil condenser 3, the liquid in evaporator 2 is provided with refrigerant water heat exchanger 1; the liquid in generator is provided with generator heater, and the refrigerant water exchange The heater 1 is connected with the air-conditioned space. The invention has a simple refrigeration cycle process, no rotating equipment, small volume, less equipment involved, and can use the waste heat of the engine to refrigerate.
Description
技术领域 technical field
本发明涉及一种空调的制冷工艺,特别是涉及一种溴化锂溶液吸收式空调的制冷工艺。 The invention relates to a refrigeration process of an air conditioner, in particular to a refrigeration process of a lithium bromide solution absorption type air conditioner.
背景技术 Background technique
目前,公知的溴化锂溶液吸收式制冷的方法是以水作为制冷剂,溴化锂作为吸收剂。通过水的蒸发获得冷量。溴化锂吸收式制冷装置主要由发生器、冷凝器、蒸发器、吸收器、换热器、循环泵等几部分组成。在溴化锂吸收式制冷装置运行过程中,当溴化锂水溶液在发生器内受到加热后,溶液中的水不断汽化;随着水的不断汽化,发生器内的溴化锂水溶液浓度不断升高,进入吸收器;水蒸气进入冷凝器,被冷凝器内的冷却水降温后凝结,成为高压低温的液态水;当冷凝器内的水进入蒸发器时,急速膨胀而汽化,并在汽化过程中大量吸收蒸发器内冷媒水的热量,从而达到降温制冷的目的;在此过程中,低温水蒸气进入吸收器,被吸收器内的溴化锂水溶液吸收,溶液浓度逐步降低,再由循环泵送回发生器,完成一个制冷循环。如此循环下去,连续制取冷量。实际应用的制冷循环中的发生器可以是一个或两个,分别为双效溴化锂吸收式制冷循环和单效溴化锂吸收式制冷循环。现有的溴化锂溶液吸收式制冷方法有以下不足,就是制冷循环涉及的设备较多,并且需要用泵这用的转动设备在容器之间输送溶液。这不仅增大了系统的制造成本,也增加了系统小型化的困难,使其不便于在车辆、船舶空调系统上使用。 At present, the known lithium bromide solution absorption refrigeration method uses water as a refrigerant and lithium bromide as an absorbent. Cooling is obtained by the evaporation of water. The lithium bromide absorption refrigeration device is mainly composed of generator, condenser, evaporator, absorber, heat exchanger, circulation pump and other parts. During the operation of the lithium bromide absorption refrigeration device, when the lithium bromide aqueous solution is heated in the generator, the water in the solution is continuously vaporized; with the continuous vaporization of the water, the concentration of the lithium bromide aqueous solution in the generator continues to increase and enters the absorber; Water vapor enters the condenser, is cooled by the cooling water in the condenser, and then condenses to become liquid water at high pressure and low temperature; when the water in the condenser enters the evaporator, it expands rapidly and vaporizes, and absorbs a large amount in the evaporator during the vaporization process. In this process, the low-temperature water vapor enters the absorber and is absorbed by the lithium bromide aqueous solution in the absorber. The concentration of the solution gradually decreases, and then is sent back to the generator by the circulating pump to complete a refrigeration cycle. cycle. This cycle goes on, and the cooling capacity is continuously produced. There can be one or two generators in the practical refrigeration cycle, which are double-effect lithium bromide absorption refrigeration cycle and single-effect lithium bromide absorption refrigeration cycle. The existing lithium bromide solution absorption refrigeration method has the following disadvantages, that is, more equipment is involved in the refrigeration cycle, and it is necessary to use rotating equipment such as pumps to transport the solution between containers. This not only increases the manufacturing cost of the system, but also increases the difficulty of miniaturization of the system, making it inconvenient to use on vehicles and ship air conditioning systems.
发明内容 Invention content
本发明的目的在于提供一种溴化锂溶液吸收式空调的制冷工艺,本发明制冷循环工艺简单,无转动设备,且体积小,涉及设备少、可利用发动机余热制冷。 The object of the present invention is to provide a refrigeration process of a lithium bromide solution absorption air conditioner. The refrigeration cycle process of the present invention is simple, without rotating equipment, small in size, less equipment involved, and can be refrigerated by waste heat of the engine.
本发明的目的是通过以下技术方案实现的: The purpose of the present invention is achieved through the following technical solutions:
一种溴化锂溶液吸收式空调的制冷工艺,包括有制冷设备,冷媒水换热器、蒸发器、盘管冷凝器、单向阀、发生器、加热器,其蒸发器和第一发生器及第二发生器之间用管道连接,管道上连接有蒸发器单向阀、蒸发器与发生器相连的单向阀、第二发生器单向阀、第一发生器单向阀和盘管冷凝器,蒸发器的液体中设有冷媒水换热器;发生器的液体中设有发生器加热器,冷媒水换热器与空调空间相连。 A lithium bromide solution absorption air-conditioning refrigeration process, including refrigeration equipment, refrigerant water heat exchanger, evaporator, coil condenser, one-way valve, generator, heater, the evaporator and the first generator and the second The two generators are connected by pipes, and the pipes are connected with the evaporator check valve, the check valve connecting the evaporator and the generator, the second generator check valve, the first generator check valve and the coil condenser A refrigerant water heat exchanger is arranged in the liquid of the evaporator; a generator heater is arranged in the liquid of the generator, and the refrigerant water heat exchanger is connected with the air-conditioning space.
所述的一种溴化锂溶液吸收式空调的制冷工艺,其所述的蒸发器和发生器及管道、单向阀组成的系统为真空状。 The refrigerating process of the lithium bromide solution absorption air conditioner described above, the system composed of the evaporator, the generator, the pipeline and the one-way valve is vacuum-like.
所述的一种溴化锂溶液吸收式空调的制冷工艺,其所述的第一发生器加热器和第二发生器加热器交替加热第一发生器和第二发生器中的溴化锂溶液使其蒸发浓缩。 The refrigerating process of the described lithium bromide solution absorption air conditioner, the first generator heater and the second generator heater alternately heat the lithium bromide solution in the first generator and the second generator to make it evaporate and concentrate .
所述的一种溴化锂溶液吸收式空调的制冷工艺,其所述的水蒸气通过管道进入盘管冷凝器,通过盘管冷凝器后接近环境温度的冷凝水进入蒸发器。 In the refrigeration process of the lithium bromide solution absorption air conditioner, the water vapor enters the coil condenser through the pipeline, and after passing through the coil condenser, the condensed water close to the ambient temperature enters the evaporator.
所述的一种溴化锂溶液吸收式空调的制冷工艺,其所述的第二发生器中的水蒸气分压低于蒸发器中的压力。 In the refrigeration process of the lithium bromide solution absorption air conditioner, the water vapor partial pressure in the second generator is lower than the pressure in the evaporator.
本发明的优点与效果是: Advantage and effect of the present invention are:
1.本发明克服了现有的溴化锂溶液吸收式制冷技术的制冷系统体积大,涉及设备多的缺点,提供一种制冷循环简单,不包括任何动设备的溴化锂溶液吸收式制冷工艺。 1. The present invention overcomes the large volume of refrigeration system of existing lithium bromide solution absorption refrigeration technology, involves the shortcoming of many equipments, provides a kind of refrigeration cycle simple, does not comprise the lithium bromide solution absorption refrigeration process of any moving equipment.
2.由于该制冷系统体积小,且无任何转动设备,非常适合在车辆、船舶这类安装空间有限,并且存在发动机余热的场合使用,充分发挥了溴化锂溶液吸收式制冷可以利用低品位热源的固有优点。 2. Due to the small size of the refrigeration system and the lack of any rotating equipment, it is very suitable for vehicles and ships where the installation space is limited and there is waste heat from the engine. It fully utilizes the inherent ability of lithium bromide solution absorption refrigeration to utilize low-grade heat sources advantage.
附图说明 Description of drawings
图1是本发明的制冷工艺流程图。 Fig. 1 is a refrigeration process flow chart of the present invention.
具体实施方式 Detailed ways
下面结合附图对本发明作进一步描述。 The present invention will be further described below in conjunction with the accompanying drawings.
图中:冷媒水换热器1、蒸发器2、盘管冷凝器3、蒸发器单向阀4、蒸发器与发生器相连的单向阀5、第二发生器单向阀6、第一发生器单向阀7、第一发生器8、第一发生器加热器9、第二发生器加热器10、第二发生器11。 In the figure: refrigerant water heat exchanger 1, evaporator 2, coil condenser 3, evaporator one-way valve 4, evaporator and generator one-way valve 5, second generator one-way valve 6, first Generator check valve 7, first generator 8, first generator heater 9, second generator heater 10, second generator 11.
蒸发器2和第一发生器8及第二发生器11之间用管道连接,管道上连接有蒸发器单向阀4、蒸发器与发生器相连的单向阀5、第二发生器单向阀6、第一发生器单向阀7和盘管冷凝器3。 The evaporator 2 is connected with the first generator 8 and the second generator 11 with a pipeline, and the pipeline is connected with the evaporator check valve 4, the evaporator check valve 5 connected with the generator, and the second generator check valve. Valve 6, first generator check valve 7 and coil condenser 3.
以上由蒸发器和发生器及管道、单向阀等组成的系统是抽真空的。 The above system composed of evaporator, generator, pipeline, one-way valve, etc. is vacuumized.
蒸发器2中注有占有其部分容积的水,第一发生器8和第二发生器11注有占有其部分容积的溴化锂溶液。部分容积的水或部分容积的溴化锂溶液的比例、压力、真空等指标可参照现有吸收式溴化锂制冷介质的有关制冷参数选用。 The evaporator 2 is filled with water occupying part of its volume, and the first generator 8 and the second generator 11 are filled with lithium bromide solution occupying part of its volume. The ratio, pressure, vacuum and other indicators of the partial volume of water or partial volume of lithium bromide solution can be selected with reference to the relevant refrigeration parameters of the existing absorption lithium bromide refrigeration medium.
蒸发器2的液体中有冷媒水换热器1; There is a refrigerant water heat exchanger 1 in the liquid of the evaporator 2;
第一发生器8的液体中有第一发生器加热器9; There is a first generator heater 9 in the liquid of the first generator 8;
第二发生器11的液体中有第二发生器加热器10。 The second generator heater 10 is present in the liquid of the second generator 11 .
第一发生器加热器9和第二发生器加热器10交替加热第一发生器8和第二发生器11中的溴化锂溶液。蒸发器和发生器中的液体注入后,蒸发器2中的水由于系统中溴化锂溶液的存在而快速蒸发。发生器中的溴化锂溶液由于吸收了来自蒸发器的水蒸气浓度变稀。为了使得蒸发器2中的水不断地蒸发,用第一发生器加热器9和第二发生器加热器10交替加热第一发生器8和第二发生器11中的溴化锂溶液使其蒸发浓缩。当第一发生器加热器9加热第一发生器8中的溴化锂溶液时,第一发生器8中的水蒸气分压升高,第一发生器单向阀7开启,水蒸气通过管道进入盘管冷凝器3,通过盘管冷凝器3后接近环境温度的冷凝水进入蒸发器2;在这一过程中,第二发生器11中的溴化锂溶液具有较高浓度,第二发生器11中的水蒸气分压低于蒸发器2中的压力,蒸发器与发生器相连的单向阀5开启,蒸发器2中的水蒸发,水蒸气经过蒸发器与发生器相连的单向阀5和管道进入第二发生器11并被其中的溴化锂溶液吸收,同时溴化锂溶液浓度有所降低,当溴化锂溶液浓度下降到不能有效蒸发发生器2中的水时,第二发生器加热器10开始加热,第一发生器加热器9停止加热。当第二发生器加热器10加热第二发生器11中的溴化锂溶液时,第二发生器11中的水蒸气分压升高,第二发生器单向阀6开启,水蒸气通过管道进入盘管冷凝器3,通过盘管冷凝器3后接近环境温度的冷凝水进入蒸发器2;在这一过程中,第一发生器8中的溴化锂溶液具有较高浓度,第一发生器8中的水蒸气分压低于蒸发器2中的压力,蒸发器单向阀4开启,蒸发器2中的水蒸发,水蒸气经过蒸发器单向阀4和管道进入第一发生器8并被其中的溴化锂溶液吸收,同时溴化锂溶液浓度有所降低,当溴化锂溶液浓度下降到不能有效蒸发蒸发器2中的水时,第一发生器加热器9开始加热,第二发生器加热器10停止加热。如此循环下去,蒸发器2中的水被不断地蒸发,水蒸发使其温度下降,冷媒水换热器1将冷量送至空调空间。 The first generator heater 9 and the second generator heater 10 alternately heat the lithium bromide solution in the first generator 8 and the second generator 11 . After the liquid in the evaporator and generator is injected, the water in the evaporator 2 evaporates rapidly due to the presence of lithium bromide solution in the system. The lithium bromide solution in the generator becomes thinner due to the absorption of water vapor from the evaporator. In order to make the water in the evaporator 2 continuously evaporate, the lithium bromide solution in the first generator 8 and the second generator 11 is alternately heated by the first generator heater 9 and the second generator heater 10 to evaporate and concentrate. When the first generator heater 9 heats the lithium bromide solution in the first generator 8, the water vapor partial pressure in the first generator 8 rises, the first generator check valve 7 opens, and the water vapor enters the disk through the pipeline. Tube condenser 3, the condensed water close to ambient temperature enters evaporator 2 after passing through coil condenser 3; In this process, the lithium bromide solution in the second generator 11 has relatively high concentration, and the The water vapor partial pressure is lower than the pressure in the evaporator 2, the one-way valve 5 connected to the evaporator and the generator opens, the water in the evaporator 2 evaporates, and the water vapor enters through the one-way valve 5 and the pipeline connected to the evaporator and the generator The second generator 11 is also absorbed by the lithium bromide solution therein, while the concentration of the lithium bromide solution decreases to some extent. When the concentration of the lithium bromide solution drops to the water that cannot effectively evaporate the generator 2, the second generator heater 10 starts heating, and the first The generator heater 9 stops heating. When the second generator heater 10 heats the lithium bromide solution in the second generator 11, the water vapor partial pressure in the second generator 11 rises, the second generator check valve 6 opens, and the water vapor enters the disk through the pipeline. Tube condenser 3, the condensed water close to ambient temperature after passing through the coil condenser 3 enters the evaporator 2; in this process, the lithium bromide solution in the first generator 8 has a relatively high concentration, the The water vapor partial pressure is lower than the pressure in the evaporator 2, the evaporator check valve 4 is opened, the water in the evaporator 2 evaporates, and the water vapor enters the first generator 8 through the evaporator check valve 4 and the pipeline and is absorbed by the lithium bromide therein. Solution absorbs, and lithium bromide solution concentration reduces to some extent simultaneously, and when lithium bromide solution concentration drops to the water in evaporator 2 effectively, first generator heater 9 starts heating, and second generator heater 10 stops heating. This cycle continues, the water in the evaporator 2 is continuously evaporated, and the temperature of the water evaporates to drop, and the refrigerant water heat exchanger 1 sends the cooling capacity to the air-conditioned space.
Claims (5)
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Cited By (4)
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CN103512267A (en) * | 2013-09-28 | 2014-01-15 | 昆山市周市溴化锂溶液厂 | Lithium bromide solution absorption refrigeration device for gas phase adding interfacial agent |
CN103512268A (en) * | 2013-09-28 | 2014-01-15 | 昆山市周市溴化锂溶液厂 | Lithium bromide solution absorption compression type refrigerating device |
CN103512265A (en) * | 2013-09-28 | 2014-01-15 | 昆山市周市溴化锂溶液厂 | Lithium bromide solution absorption type refrigerating device |
CN113563148A (en) * | 2021-07-26 | 2021-10-29 | 华南理工大学 | Coal-based natural gas and methanol poly-generation system and method integrating waste heat refrigeration |
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CN113563148A (en) * | 2021-07-26 | 2021-10-29 | 华南理工大学 | Coal-based natural gas and methanol poly-generation system and method integrating waste heat refrigeration |
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