CN2909103Y - Solar double-effect absorption air conditioner - Google Patents
Solar double-effect absorption air conditioner Download PDFInfo
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- CN2909103Y CN2909103Y CNU2006201145954U CN200620114595U CN2909103Y CN 2909103 Y CN2909103 Y CN 2909103Y CN U2006201145954 U CNU2006201145954 U CN U2006201145954U CN 200620114595 U CN200620114595 U CN 200620114595U CN 2909103 Y CN2909103 Y CN 2909103Y
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 239000006096 absorbing agent Substances 0.000 claims abstract description 18
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims abstract description 18
- 239000003507 refrigerant Substances 0.000 claims description 30
- 238000010438 heat treatment Methods 0.000 abstract description 12
- 238000005057 refrigeration Methods 0.000 abstract description 8
- 238000004378 air conditioning Methods 0.000 abstract description 6
- 238000001816 cooling Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 6
- 230000005494 condensation Effects 0.000 abstract description 3
- 238000009833 condensation Methods 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 25
- 239000007864 aqueous solution Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 3
- 238000005485 electric heating Methods 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B10/00—Integration of renewable energy sources in buildings
- Y02B10/20—Solar thermal
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- 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
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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
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- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
所属技术领域Technical field
本实用新型涉及一种利用太阳能的空调系统,特别是一种双效型吸收式空调。The utility model relates to an air conditioning system utilizing solar energy, in particular to a double-effect absorption type air conditioner.
背景技术Background technique
目前,许多国家和地区都存在着能源危机,如何利用太阳能这种既清洁又可再生的能源,越来越受到关注,太阳能空调的开发对节约能源、保护自然环境都具有十分重要的意义。然而,市场上成功的产品很少,存在的问题是:系统结构复杂、造价高,如申请号为01128404.8的(太阳能中高温集热吸收式空调系统);也有构造简单,但热力系数小只有0.7以下、排热量大综合效率底,如专利号为00229377.3的(太阳能吸收式空调)专利。这些都不利于形成产品化,使太阳能资源迟迟得不到利用。At present, there are energy crises in many countries and regions. How to use solar energy, a clean and renewable energy source, has attracted more and more attention. The development of solar air conditioners is of great significance to energy conservation and natural environment protection. However, there are few successful products on the market, and the existing problems are: the system structure is complex and the cost is high, such as the application number 01128404.8 (solar medium and high temperature heat collection absorption air conditioning system); there are also simple structures, but the thermal coefficient is only 0.7 Below, the large comprehensive efficiency of exhaust heat is at the bottom, as the patent No. is 00229377.3 (solar absorption type air conditioner) patent. These are not conducive to the formation of products, so that solar energy resources can not be used for a long time.
发明内容Contents of the invention
为了克服现有技术的不足之处,本实用新型提供一种运用于四季不同的环境下使用,可夏季制冷,冬季制热,全年提供生活热水三大功能的太阳能双效吸收式空调系统。由于采用聚光集热装置,热源直接加热高压发生器内的溶液,可在高压发生器中产生压力较高的冷剂蒸汽,再次做低压发生器的热源,冷凝器冷却时的热能再加热生活用热水,不仅有效利用了冷剂蒸汽的热量,而且减少了机组的排热量起到多重节省热能的效果。根据计算和实测表明:加热量约为单效机1/2~2/3,冷凝器的热负荷约为1/2,热力系数达到1以上,综合效能高,系统简单,利于产品化和推广。In order to overcome the deficiencies of the prior art, the utility model provides a solar double-effect absorption air-conditioning system that can be used in different environments in four seasons, can cool in summer, heat in winter, and provide domestic hot water throughout the year. . Due to the use of a concentrating heat collection device, the heat source directly heats the solution in the high-pressure generator, and high-pressure refrigerant vapor can be generated in the high-pressure generator, which is used as the heat source of the low-pressure generator again, and the heat energy when the condenser cools is reheated. The use of hot water not only effectively utilizes the heat of the refrigerant steam, but also reduces the exhaust heat of the unit to achieve multiple heat saving effects. According to the calculation and actual measurement, the heating capacity is about 1/2 to 2/3 of the single-effect unit, the heat load of the condenser is about 1/2, and the thermal coefficient reaches more than 1. The overall efficiency is high, the system is simple, and it is conducive to productization and promotion. .
本实用新型的工作原理是利用太阳能聚光板产生高温热源,溴化锂和水作为工质的双效吸收式制冷原理。系统结构主要由聚光板、集热高压发生器、低压发生器、冷凝器、节流阀、蒸发器、吸收器、溶液泵、高温热交换器、低温热交换器、引射器、生活用水换热器组成,附件有控制阀、管路等组成。制冷时由聚光板产生150~200℃高温加热高压发生器里的溴化锂水溶液,产生高温高压冷剂水蒸汽,水蒸汽经管道到达低压发生器,水蒸汽再加热低压发生器里的溴化锂水溶液再次产生冷剂水蒸汽,此时低压发生器相当于高压发生器的冷凝器,冷剂蒸汽在低压发生器里放出热量凝结成冷剂水,冷剂水节流减压后进入冷凝器,同时低压发生器中产生的冷剂蒸汽也进入冷凝器,被冷凝器冷凝为冷剂水,另外大量的冷凝热经过生活用水换热器同时加热了生活用水。两股冷剂水一同经节流进入蒸发器,由于蒸发器压力很底,冷剂水在其中蒸发产生冷效应;由高压发生器和低压发生器出口的浓溶液,分别经高温热交换器和低温热交换器,温度降低后进入吸收器,溶液也可以通过引射器与稀溶液混合后进入吸收器,在吸收器中冷却并吸收来自蒸发器的冷剂蒸汽。吸收后的溶液成为稀溶液,由溶液泵输送分别经高温热交换器和低温热交换器升温后到达高压发生器和低压发生器,再重新发生过程,这样制冷装置便完成一个吸收制冷循环。高低温热交换器是为了提高热效率。The working principle of the utility model is the principle of double-effect absorption refrigeration using solar concentrating panels to generate high-temperature heat sources, and lithium bromide and water as working fluids. The system structure is mainly composed of concentrating plate, heat collecting high pressure generator, low pressure generator, condenser, throttle valve, evaporator, absorber, solution pump, high temperature heat exchanger, low temperature heat exchanger, ejector, domestic water exchange It is composed of a heater, and the accessories are composed of control valves and pipelines. When cooling, the concentrating plate generates 150-200°C high temperature to heat the lithium bromide aqueous solution in the high-pressure generator to generate high-temperature and high-pressure refrigerant water vapor. The water vapor reaches the low-pressure generator through the pipeline, and the water vapor reheats the lithium bromide aqueous solution in the low-pressure generator to generate again Refrigerant water vapor. At this time, the low-pressure generator is equivalent to the condenser of the high-pressure generator. The refrigerant steam releases heat in the low-pressure generator and condenses into refrigerant water. The refrigerant vapor generated in the condenser also enters the condenser and is condensed into refrigerant water by the condenser. In addition, a large amount of condensation heat passes through the domestic water heat exchanger to heat domestic water at the same time. The two streams of refrigerant water enter the evaporator through throttling. Since the pressure of the evaporator is very low, the refrigerant water evaporates in it to produce a cooling effect; the concentrated solution from the outlet of the high-pressure generator and the low-pressure generator passes through the high-temperature heat exchanger and the The low-temperature heat exchanger enters the absorber after the temperature is lowered. The solution can also be mixed with the dilute solution through the ejector and then enter the absorber, where it cools down and absorbs the refrigerant vapor from the evaporator. The absorbed solution becomes a dilute solution, which is transported by the solution pump, passes through the high-temperature heat exchanger and the low-temperature heat exchanger, and then reaches the high-pressure generator and low-pressure generator, and then repeats the process, so that the refrigeration device completes an absorption refrigeration cycle. High and low temperature heat exchangers are used to improve thermal efficiency.
制热时高压发生器产生的高温高压蒸汽经控制阀、生活用水换热器再到蒸发器,产生制热供暖效果并同时加热生活用水。During heating, the high-temperature and high-pressure steam generated by the high-pressure generator passes through the control valve, the domestic water heat exchanger, and then to the evaporator to produce heating effect and heat domestic water at the same time.
高压发生器内装配有电辅助加热棒,当阴天或夜晚时可采用电辅助加热达到制冷或制热的效果。The high-voltage generator is equipped with an electric auxiliary heating rod, which can be used for cooling or heating when it is cloudy or at night.
本实用新型的有益效果是,可以多重利用太阳能的热能,提高制冷装置的热力系数,减少了机组的热排放量,同时采用聚光型集热高压发生器减小了发生器的尺寸,降低了制造成本,易于产品化和推广。The beneficial effect of the utility model is that the thermal energy of solar energy can be utilized multiple times, the thermal coefficient of the refrigeration device can be improved, and the heat discharge of the unit can be reduced. Manufacturing cost, easy productization and promotion.
附图说明Description of drawings
下面结合附图和实施例对本实用新型进一步说明。Below in conjunction with accompanying drawing and embodiment the utility model is further described.
附图是本实用新型的工作示意图Accompanying drawing is the working schematic diagram of the utility model
图中1、聚光板,2、电加热棒,3、高压发生器,4、低温热交换器,5、引射器,6、吸收器,7、减压阀,8、低压发生器,9、减压阀,10、冷凝器,11、节流阀,12、蒸发器,13、溶液泵,14、引射器,15、高温热交换器,16、17、控制阀,18、生活用水换热器,19、热水出口,20、冷水进口。In the figure 1. Concentrating plate, 2. Electric heating rod, 3. High voltage generator, 4. Low temperature heat exchanger, 5. Ejector, 6. Absorber, 7. Pressure reducing valve, 8. Low pressure generator, 9 , Pressure reducing valve, 10, Condenser, 11, Throttle valve, 12, Evaporator, 13, Solution pump, 14, Ejector, 15, High temperature heat exchanger, 16, 17, Control valve, 18, Domestic water Heat exchanger, 19, hot water outlet, 20, cold water import.
具体实施方式Detailed ways
下面结合附图对本实用新型的具体实施做进一步的描述Below in conjunction with accompanying drawing, the concrete implementation of the present utility model is described further
如图所示,一种利用太阳能的双效吸收式空调系统,以水为制冷剂,溴化锂为吸收剂。主要包括聚光板(1)、电加热棒(2)、高压发生器(3)、低温热交换器(4)、引射器(5)(14)、吸收器(6)、减压阀(7)(9)、低压发生器(8)、冷凝器(10)、节流阀(11)、蒸发器(12)、溶液泵(13)、高温热交换器(15)、控制阀(16)(17)、生活用水换热器(18)。制冷时高压发生器(3)内的溴化锂水溶液被加热,产生高温冷剂蒸汽经高压发生器(3)顶部的冷剂蒸汽出口、控制阀(17)到达低压发生器(8)的蒸汽进口,高温冷剂蒸汽再加热低压发生器(8)内的溴化锂水溶液再次产生冷剂蒸汽,经顶部出口与冷凝器(10)进口连接,低压发生器(8)此时相当与高压发生器(3)的冷凝器,冷剂蒸汽在低压发生器(8)里放热后成为冷剂水,冷剂水出口经减压阀(9)也与冷凝器(10)进口连接,这样就会有两股冷剂进入冷凝器(10),在冷凝器(10)内被冷凝为冷剂水后通过冷剂水出口经节流阀(11)与蒸发器(12)进口连接,冷剂水被节流减压后在蒸发器(12)中蒸发吸收热量,从而产生制冷效应。蒸发器(12)的出口与吸收器(6)的冷剂蒸汽进口连接,使蒸汽不断地被吸收器(6)吸走,高压发生器(3)的浓溶液出口经高温热交换器(15)引射器(14)减压阀(7)与吸收器(6)的溶液进口连接;低压发生器(8)的浓溶液出口经低温热交换器(4)引射器(5)减压阀(7)与吸收器(6)的溶液进口连接。高压发生器(3)、低压发生器(8)内的溴化锂水溶液被加热蒸发后成为浓溶液,分别经高温热交换器(15)、低温热交换器(4)、引射器(14)(5)、减压阀(7)到达吸收器(6)吸收冷剂蒸汽成为稀溶液,吸收器(6)的稀溶液出口经溶液泵(13)、高温热交换器(15)与高压发生器(3)稀溶液进口连接,同时吸收器(6)稀溶液出口经溶液泵(13)、低温热交换器(4)与低压发生器(8)的稀溶液进口连接,稀溶液经溶液泵(13)加压在分别经高温热交换器(15)、低温热交换器(4)增加温度后分别送到高压发生器(3)和低压发生器(8)完成吸收和发生的过程。制冷时冷凝器(10)大量的冷凝热同时加热了生活用水换热器(18)内的水,满足生活使用。As shown in the figure, a double-effect absorption air-conditioning system using solar energy uses water as the refrigerant and lithium bromide as the absorbent. It mainly includes concentrating plate (1), electric heating rod (2), high voltage generator (3), low temperature heat exchanger (4), ejector (5) (14), absorber (6), pressure reducing valve ( 7) (9), low pressure generator (8), condenser (10), throttle valve (11), evaporator (12), solution pump (13), high temperature heat exchanger (15), control valve (16 ) (17), domestic water heat exchanger (18). During refrigeration, the lithium bromide aqueous solution in the high-pressure generator (3) is heated to generate high-temperature refrigerant steam, which passes through the refrigerant steam outlet on the top of the high-pressure generator (3) and the control valve (17) to the steam inlet of the low-pressure generator (8). The high-temperature refrigerant vapor reheats the lithium bromide aqueous solution in the low-pressure generator (8) to generate refrigerant vapor again, which is connected to the inlet of the condenser (10) through the top outlet, and the low-pressure generator (8) is now equivalent to the high-pressure generator (3). The condenser, the refrigerant steam becomes refrigerant water after releasing heat in the low-pressure generator (8), and the outlet of the refrigerant water is also connected to the inlet of the condenser (10) through the pressure reducing valve (9), so that there will be two The refrigerant enters the condenser (10), is condensed into refrigerant water in the condenser (10), and is connected to the inlet of the evaporator (12) through the refrigerant water outlet through the throttle valve (11), and the refrigerant water is throttled After decompression, it evaporates and absorbs heat in the evaporator (12), thereby producing a refrigeration effect. The outlet of the evaporator (12) is connected to the refrigerant steam inlet of the absorber (6), so that the steam is continuously sucked away by the absorber (6), and the concentrated solution outlet of the high-pressure generator (3) passes through the high-temperature heat exchanger (15 ) ejector (14) pressure reducing valve (7) is connected with the solution inlet of absorber (6); the concentrated solution outlet of low pressure generator (8) is decompressed through low temperature heat exchanger (4) Valve (7) is connected to the solution inlet of absorber (6). The lithium bromide aqueous solution in the high-pressure generator (3), the low-pressure generator (8) becomes a concentrated solution after being heated and evaporated, and passes through the high-temperature heat exchanger (15), the low-temperature heat exchanger (4), and the ejector (14) ( 5), the pressure reducing valve (7) reaches the absorber (6) to absorb the refrigerant vapor to become a dilute solution, and the dilute solution outlet of the absorber (6) passes through the solution pump (13), the high temperature heat exchanger (15) and the high pressure generator (3) The inlet of the dilute solution is connected, and the outlet of the dilute solution of the absorber (6) is connected to the inlet of the dilute solution of the low-pressure generator (8) through the solution pump (13), the low-temperature heat exchanger (4), and the dilute solution is passed through the solution pump ( 13) Pressurization is sent to the high-pressure generator (3) and the low-pressure generator (8) after the temperature is increased by the high-temperature heat exchanger (15) and the low-temperature heat exchanger (4) respectively to complete the process of absorption and generation. During refrigeration, a large amount of heat of condensation of the condenser (10) heats the water in the domestic water heat exchanger (18) simultaneously, which satisfies domestic use.
制热时高压发生器(3)产生的高温高压蒸汽经控制阀(16)、生活用水换热器(18)到达蒸发器(12),直接产生制热效应和提供生活热水,高压发生器(3)的蒸汽出口通过控制阀(16)与生活用水换热器(18)进口连接,出口与蒸发器(12)的进口连接。冷凝水由溶液泵(13)加压后补充到高压发生器内,完成制热循环。控制阀(16)(17)的开与关可控制着机组的制冷或制热以及既不制冷也不制热。During heating, the high-temperature and high-pressure steam generated by the high-pressure generator (3) reaches the evaporator (12) through the control valve (16) and the domestic water heat exchanger (18), directly producing heating effect and providing domestic hot water. The high-pressure generator ( 3) The steam outlet is connected to the inlet of the domestic water heat exchanger (18) through the control valve (16), and the outlet is connected to the inlet of the evaporator (12). Condensed water is added to the high pressure generator after being pressurized by the solution pump (13) to complete the heating cycle. The opening and closing of the control valve (16) (17) can control the cooling or heating of the unit and neither cooling nor heating.
Claims (4)
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101865541A (en) * | 2010-06-30 | 2010-10-20 | 苏州新亚科技有限公司 | Solar system |
CN104613670A (en) * | 2015-02-13 | 2015-05-13 | 海南泰立来科技有限公司 | Solar thermal lithium bromide-water absorbing refrigerator |
CN106595119A (en) * | 2016-12-19 | 2017-04-26 | 鲁奎 | Environment-friendly solar central air conditioner host machine |
CN108645073A (en) * | 2018-05-03 | 2018-10-12 | 昆明理工大学 | A kind of absorption system of solar energy energy supply |
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2006
- 2006-05-16 CN CNU2006201145954U patent/CN2909103Y/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101865541A (en) * | 2010-06-30 | 2010-10-20 | 苏州新亚科技有限公司 | Solar system |
CN104613670A (en) * | 2015-02-13 | 2015-05-13 | 海南泰立来科技有限公司 | Solar thermal lithium bromide-water absorbing refrigerator |
CN106595119A (en) * | 2016-12-19 | 2017-04-26 | 鲁奎 | Environment-friendly solar central air conditioner host machine |
CN108645073A (en) * | 2018-05-03 | 2018-10-12 | 昆明理工大学 | A kind of absorption system of solar energy energy supply |
CN108645073B (en) * | 2018-05-03 | 2023-12-26 | 昆明理工大学 | Solar energy-powered absorption refrigeration system |
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