CN107202451A - A kind of residents multipotency source absorption type capillary network refrigeration system - Google Patents
A kind of residents multipotency source absorption type capillary network refrigeration system Download PDFInfo
- Publication number
- CN107202451A CN107202451A CN201710147121.2A CN201710147121A CN107202451A CN 107202451 A CN107202451 A CN 107202451A CN 201710147121 A CN201710147121 A CN 201710147121A CN 107202451 A CN107202451 A CN 107202451A
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- capillary network
- generator
- water
- refrigeration
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B27/00—Machines, plants or systems, using particular sources of energy
- F25B27/002—Machines, plants or systems, using particular sources of energy using solar energy
- F25B27/007—Machines, plants or systems, using particular sources of energy using solar energy in sorption type systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/06—Heat pumps characterised by the source of low potential heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/37—Capillary tubes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/002—Compression machines, plants or systems with reversible cycle not otherwise provided for geothermal
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—Component parts or details not otherwise provided for in this subclass
- F25B2400/01—Heaters
-
- 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
- Y02A30/272—Solar heating or cooling
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种制冷系统,尤其是一种多能源吸收式毛细管网制冷系统。The invention relates to a refrigeration system, in particular to a multi-energy absorption capillary network refrigeration system.
背景技术Background technique
随着我国国民经济迅速发展,能源、资源的短缺与环境污染己成为十分严重的问题。我国作为能源消费大国,能源问题一直得到国家重视,而其中建筑能耗占全部能耗的40%~50%,尤其用于暖通空调的则要占到一半以上,是建筑能耗的主体,积极开发利用低品位能源有利于缓解环境压力。With the rapid development of our national economy, the shortage of energy and resources and environmental pollution have become very serious problems. As a big energy consumer in China, energy issues have always been valued by the state, and building energy consumption accounts for 40% to 50% of the total energy consumption, especially for HVAC, accounting for more than half, which is the main body of building energy consumption. Active development and utilization of low-grade energy is conducive to alleviating environmental pressure.
在我国偏远缺电地区,人们无法使用常规的电能制冷系统。但在这些地区,可能存在着较为丰富的太阳能、地热能、低品位可燃气体等能源,基于多能源的制冷系统不仅可以改善当地农民的生活品质,而且不增加传统能耗,同时有利于环境保护,无疑将会有非常广阔的前景。In my country's remote power-deficient areas, people cannot use conventional electric refrigeration systems. However, in these areas, there may be relatively abundant energy sources such as solar energy, geothermal energy, and low-grade combustible gas. Refrigeration systems based on multi-energy sources can not only improve the quality of life of local farmers, but also do not increase traditional energy consumption, and are also conducive to environmental protection. , will undoubtedly have very broad prospects.
同时,德国科学家根据仿生学原理提出的毛细管网辐射制冷系统是以水作为冷媒载体,通过均匀紧密的毛细管网辐射传热,制冷要求供水水温12~18℃。而传统制冷空调往往以对流方式制冷,耗电量大,制冷效果并不理想,而且人们久吹空调容易患上各种疾病,毛细管辐射制冷系统实现制冷所花的能量代价大大低于传统制冷空调。此外,毛细管辐射制冷系统还具有舒适性高、安装方便、节省空间、使用寿命长、洁净环保的特点。At the same time, the capillary network radiative refrigeration system proposed by German scientists based on the principle of bionics uses water as the refrigerant carrier to transfer heat through uniform and tight capillary network radiation. Cooling requires a supply water temperature of 12-18°C. However, traditional refrigeration and air conditioners often use convection cooling, which consumes a lot of power, and the cooling effect is not ideal. Moreover, people are prone to various diseases when using air conditioners for a long time. The energy cost of capillary radiation refrigeration system for cooling is much lower than that of traditional refrigeration . In addition, the capillary radiant refrigeration system also has the characteristics of high comfort, convenient installation, space saving, long service life, clean and environmental protection.
通过检索,中国专利(CN101793444A)公开了一种太阳能与生物质能联合吸收式制冷装置,它包括太阳能集热器和吸收式制冷机,太阳能集热器出口水与吸收式制冷机的加热器进口水相连,加热器出水口与储液罐相通,太阳能集热器进水口通过循环泵、单向阀与储液罐相通,太阳能集热器;还包括生物质炉具,其出水口与加热器进水口相连,进水口通过循环水泵、单向阀与储液罐相通,其进水口还与太阳能集热器出水口相连。该专利将太阳能与生物质能结合起来,在节约能源的同时可以实现连续制冷,但是目前太阳能的有效利用率很低,并且在阳光不充足的时候只能通过生物质能来为整个系统提供能量,这将导致生物质能占据整个系统能量供给的绝大部分,节能效果不明显;此外该专利没有明确提出各连接部分换热器的设计,可能会导致换热效率较低的现象。Through retrieval, Chinese patent (CN101793444A) discloses a kind of solar energy and biomass energy combined absorption refrigeration device, and it comprises solar collector and absorption refrigerator, the heater inlet of solar collector outlet water and absorption refrigerator The water is connected, the water outlet of the heater is connected with the liquid storage tank, the water inlet of the solar collector is connected with the liquid storage tank through a circulating pump and a one-way valve, and the solar heat collector; it also includes a biomass stove, and its water outlet is connected with the heater The water inlet is connected to each other, and the water inlet is connected to the liquid storage tank through a circulating water pump and a one-way valve, and the water inlet is also connected to the water outlet of the solar heat collector. This patent combines solar energy with biomass energy, which can realize continuous cooling while saving energy, but the current effective utilization rate of solar energy is very low, and when the sun is not sufficient, only biomass energy can be used to provide energy for the entire system , which will lead to biomass energy occupying the vast majority of the energy supply of the entire system, and the energy saving effect is not obvious; in addition, the patent does not clearly propose the design of the heat exchangers of each connecting part, which may lead to low heat exchange efficiency.
中国专利(CN201569099U)公开了一种新型地源热泵毛细管顶板空调系统,它包括地源热泵系统及毛细管顶板空调系统;地源热泵系统包括室外管网系统、热泵工质循环系统及室内空调管网系统;毛细管顶板空调系统包括热交换器、带循环泵的分配站、温控调节系统、毛细管网以及配套除湿系统。该专利仅仅考虑利用地热源热泵为毛细管网辐射制冷系统提供能量,能量来源过于单一从而可能造成制冷过程不连续,制冷量不充足的问题。Chinese patent (CN201569099U) discloses a novel ground source heat pump capillary roof air conditioning system, which includes a ground source heat pump system and a capillary roof air conditioning system; the ground source heat pump system includes an outdoor pipe network system, a heat pump working fluid circulation system and an indoor air conditioning pipe network System; capillary tube roof air conditioning system includes heat exchanger, distribution station with circulation pump, temperature control and adjustment system, capillary tube network and supporting dehumidification system. This patent only considers the use of geothermal source heat pumps to provide energy for the capillary network radiation refrigeration system, and the energy source is too single, which may cause discontinuous refrigeration process and insufficient cooling capacity.
发明内容Contents of the invention
本发明为了克服现有技术不足,提供一种基于太阳能、地热能、低品位可燃气体能源的吸收式毛细管网辐射制冷系统,以互为补充的三种能源:地热能、太阳能和低品位可燃气体的化学能作为制冷系统的能量供给,利用氨—水溶液作为吸收式制冷装置的循环工质,利用毛细管网作为末端的制冷系统,从而为缺电地区的用户提供了低碳环保、健康舒适的制冷方案。In order to overcome the deficiencies of the prior art, the present invention provides an absorption capillary network radiation refrigeration system based on solar energy, geothermal energy, and low-grade combustible gas energy, using three complementary energy sources: geothermal energy, solar energy, and low-grade combustible gas The chemical energy is used as the energy supply of the refrigeration system, the ammonia-water solution is used as the circulating working medium of the absorption refrigeration device, and the capillary network is used as the terminal refrigeration system, thus providing low-carbon, environmentally friendly, healthy and comfortable refrigeration for users in power-deficient areas plan.
本发明解决现有技术问题所采用的技术方案是:The technical solution adopted by the present invention to solve the problems of the prior art is:
一种户用型多能源吸收式毛细管网制冷系统,包括户用型太阳能集热系统、低品位可燃气燃烧装置、吸收式制冷装置、地热源换热器、毛细管网系统。太阳能集热系统与吸收式制冷装置相连接;低品位可燃气燃烧装置位于吸收式制冷装置下方;毛细管网系统通过氨—水换热器与吸收式制冷装置相连接;地热源换热器与毛细管网系统相连接构成闭合循环水路。所述的户用型太阳能集热系统包括槽式太阳能集热器和第一循环泵;所述的低品位可燃气燃烧装置包括储气罐和分级燃烧器;所述的吸收式制冷装置包括发生器、油—氨水换热器、冷凝器、节流阀、蒸发器、吸收器;所述的毛细管网系统包括毛细管分水器、毛细管网、毛细管网集水器、氨—水换热器,第二循环泵;槽式太阳能集热器出口与第一循环泵入口连接,第一循环泵出口与油—氨水换热器入口连接;低品位可燃气接入储气罐中,储气罐出口与分级燃烧器连接;油—氨水换热器环套在发生器下部,发生器的上方出口与冷凝器的入口连接,冷凝器出口通过节流阀与蒸发器入口连接,蒸发器出口与吸收器的入口连接,吸收器出口与发生器入口连接;第二循环泵、氨—水换热器、毛细管分水器、毛细管网、毛细管集水器、地热源换热器依次连接,地热源换热器的另一侧与第二循环泵的另一侧连接,从而形成循环水路。A household multi-energy absorption capillary network refrigeration system includes a household solar heat collection system, a low-grade combustible gas combustion device, an absorption refrigeration device, a geothermal source heat exchanger, and a capillary network system. The solar heat collection system is connected to the absorption refrigeration device; the low-grade combustible gas combustion device is located below the absorption refrigeration device; the capillary network system is connected to the absorption refrigeration device through an ammonia-water heat exchanger; the geothermal source heat exchanger is connected to the capillary tube The network system is connected to form a closed circulation waterway. The household solar heat collection system includes a trough solar heat collector and a first circulating pump; the low-grade combustible gas combustion device includes a gas storage tank and a staged burner; the absorption refrigeration device includes a generator device, oil-ammonia water heat exchanger, condenser, throttle valve, evaporator, absorber; the capillary network system includes capillary water separator, capillary network, capillary network water collector, ammonia-water heat exchanger, The second circulation pump; the outlet of the trough solar collector is connected to the inlet of the first circulation pump, the outlet of the first circulation pump is connected to the inlet of the oil-ammonia water heat exchanger; the low-grade combustible gas is connected to the gas storage tank, and the gas storage tank is exported It is connected to the staged burner; the oil-ammonia water heat exchanger is ringed at the lower part of the generator, the upper outlet of the generator is connected to the inlet of the condenser, the outlet of the condenser is connected to the inlet of the evaporator through a throttle valve, and the outlet of the evaporator is connected to the absorber The inlet of the absorber is connected, the outlet of the absorber is connected with the inlet of the generator; the second circulating pump, ammonia-water heat exchanger, capillary water separator, capillary network, capillary water collector, and geothermal source heat exchanger are connected in sequence, and the geothermal source heat exchange The other side of the device is connected with the other side of the second circulating pump to form a circulating water circuit.
所述的油—氨水换热器环套于发生器,发生器为竖直圆管,且在油—氨水换热器内部设有半圆形导流挡板,发生器表面均匀焊有具有一定厚度的长方形肋片,长方形肋片向上倾斜并与竖直方向夹角α为40~50度,肋片长度L为发生器管径D的1/6~1/4。The oil-ammonia water heat exchanger is ring-sleeved on the generator, the generator is a vertical circular tube, and a semicircular diversion baffle is arranged inside the oil-ammonia water heat exchanger, and the surface of the generator is evenly welded with certain The thickness of the rectangular fins, the rectangular fins are inclined upward and the angle α with the vertical direction is 40-50 degrees, and the length L of the fins is 1/6-1/4 of the diameter D of the generator.
所述的分级燃烧器包括一级燃烧器和二级燃烧器,一级燃烧器包括燃气管和喷嘴,且位于油—氨水换热器底面近边缘处下方,二级燃烧器包括燃气管和喷嘴,位于发生器底部中心下方,两级燃烧器分别设置独立的燃气控制阀。The staged burner includes a primary burner and a secondary burner, the primary burner includes a gas pipe and a nozzle, and is located below the bottom edge of the oil-ammonia water heat exchanger, and the secondary burner includes a gas pipe and a nozzle , located below the center of the bottom of the generator, and the two-stage burners are respectively equipped with independent gas control valves.
所述的地热源换热器为锥体形螺旋结构的金属圆管,其螺旋角β为10~14度,并且地热源换热器自上而下的浅埋于地表面以下,其入口在地表面以下1.8~2.2米处,其出口在地表面以下2.8~3.2米处。The geothermal source heat exchanger is a metal circular tube with a conical helical structure, its helix angle β is 10-14 degrees, and the geothermal source heat exchanger is buried shallowly below the ground surface from top to bottom, and its entrance is in the ground. 1.8-2.2 meters below the surface, and its outlet is 2.8-3.2 meters below the ground surface.
所述的户用型太阳能集热系统中的槽式太阳能集热器上设置有圆弧形遮光板,圆弧形遮光板的半径R为高温集热管半径r的的1.5~2.0倍,遮光板外表面涂有有机硅耐高温涂料。The trough solar heat collector in the household solar heat collection system is provided with an arc-shaped shading plate, the radius R of the arc-shaped shading plate is 1.5 to 2.0 times the radius r of the high-temperature heat collecting tube, and the shading plate The outer surface is coated with silicone high temperature resistant paint.
本发明的有益效果是,本发明通过设置半圆形导流板和长方形肋片提高了油—氨水换热器的换热效率。设置的分级燃烧器能够提高对太阳能的利用率。锥体形螺旋结构的地源换热器能够提高土壤与金属圆管内工质的换热效率。圆形遮光板的设置有利于调节户用型太阳能集热系统的油温,从而调节毛细管网内工质的温度。本发明采用太阳能、地热能、低品位可燃气体能源联合吸收式制冷的方式,克服了太阳能利用率低,阳光不充足时的诸多弊端以及能量来源单一导致的制冷过程不连续,制冷量不充足的问题。此外,本发明根据系统特点设计了换热器结构,提高了系统制冷效率,为系统连续、高效制冷提供了保障。The beneficial effect of the present invention is that the present invention improves the heat exchange efficiency of the oil-ammonia water heat exchanger by arranging semicircular deflectors and rectangular fins. The arranged staged burners can improve the utilization rate of solar energy. The ground source heat exchanger with the conical spiral structure can improve the heat exchange efficiency between the soil and the working medium in the metal circular tube. The setting of the circular shading plate is beneficial to adjust the oil temperature of the household solar heat collection system, thereby adjusting the temperature of the working medium in the capillary network. The invention adopts solar energy, geothermal energy, and low-grade combustible gas energy combined with absorption refrigeration, which overcomes many disadvantages of low solar energy utilization rate, insufficient sunlight, and discontinuous refrigeration process caused by a single energy source, and insufficient cooling capacity. question. In addition, the present invention designs the heat exchanger structure according to the characteristics of the system, improves the refrigeration efficiency of the system, and provides guarantee for the continuous and high-efficiency refrigeration of the system.
附图说明Description of drawings
下面结合附图和具体实施方式对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments.
图1为本发明的结构示意图;Fig. 1 is a structural representation of the present invention;
图2为油—氨水换热器的剖视图;Fig. 2 is the sectional view of oil-ammonia water heat exchanger;
图3为图2的局部放大示意图;Figure 3 is a partial enlarged schematic view of Figure 2;
图4为图2中A-A向视图;Fig. 4 is A-A direction view among Fig. 2;
图5为地热源换热器的结构示意图;Fig. 5 is the structural representation of geothermal source heat exchanger;
图6为图5的局部放大示意图;Fig. 6 is a partially enlarged schematic diagram of Fig. 5;
图7为槽式太阳能集热器的结构示意图;Fig. 7 is the structural representation of trough type solar heat collector;
图8为分级燃烧器的结构示意图Figure 8 is a structural schematic diagram of a staged burner
具体实施方式detailed description
下面结合附图并通过具体实施例对本发明作进一步详述,以下实施例只是描述性的,不是限定性的,不能以此限定本发明的保护范围。The present invention will be further described in detail below in conjunction with the accompanying drawings and through specific embodiments. The following embodiments are only descriptive, not restrictive, and cannot limit the protection scope of the present invention.
户用型多能源吸收式毛细管网制冷系统包括户用型太阳能集热系统17、低品位可燃气燃烧装置20、吸收式制冷装置18、地热源换热器12、毛细管网系统19。其特征在于:所述的户用型太阳能集热系统17包括槽式太阳能集热器1和第一循环泵2;所述的低品位可燃气燃烧装置20包括储气罐16和分级燃烧器15;所述的吸收式制冷装置18包括发生器4、油—氨水换热器3、冷凝器5、节流阀6、蒸发器7、吸收器14;所述的毛细管网系统19包括毛细管分水器9、毛细管网10、毛细管网集水器11、第二循环泵13、氨—水换热器8;槽式太阳能集热器1出口与第一循环泵2入口连接,第一循环泵2出口与油—氨水换热器3入口连接;低品位可燃气接入储气罐16中,储气罐16出口与分级燃烧器15连接;油—氨水换热器3环套在发生器4下部,发生器4的上方出口与冷凝器5的入口连接,冷凝器5出口通过节流阀6与蒸发器7入口连接,蒸发器7出口与吸收器14的入口连接,吸收器14出口与发生器4入口连接;第二循环泵13、氨—水换热器8、毛细管分水器9、毛细管网10、毛细管集水器11、地热源换热器12依次连接,地热源换热器12的另一侧与第二循环泵13的另一侧连接,从而形成循环水路。The household multi-energy absorption capillary network refrigeration system includes a household solar heat collection system 17, a low-grade combustible gas combustion device 20, an absorption refrigeration device 18, a geothermal source heat exchanger 12, and a capillary network system 19. It is characterized in that: the household solar heat collection system 17 includes a trough solar heat collector 1 and a first circulation pump 2; the low-grade combustible gas combustion device 20 includes a gas storage tank 16 and a staged burner 15 The absorption refrigeration unit 18 includes a generator 4, an oil-ammonia water heat exchanger 3, a condenser 5, a throttle valve 6, an evaporator 7, and an absorber 14; the capillary network system 19 includes a capillary water separator Device 9, capillary network 10, capillary network water collector 11, second circulation pump 13, ammonia-water heat exchanger 8; trough solar heat collector 1 outlet is connected with the first circulation pump 2 inlet, the first circulation pump 2 The outlet is connected to the inlet of the oil-ammonia water heat exchanger 3; the low-grade combustible gas is connected to the gas storage tank 16, and the outlet of the gas storage tank 16 is connected to the staged burner 15; , the upper outlet of the generator 4 is connected to the inlet of the condenser 5, the outlet of the condenser 5 is connected to the inlet of the evaporator 7 through the throttle valve 6, the outlet of the evaporator 7 is connected to the inlet of the absorber 14, and the outlet of the absorber 14 is connected to the generator 4 Inlet connections; the second circulating pump 13, ammonia-water heat exchanger 8, capillary water separator 9, capillary network 10, capillary water collector 11, and ground heat source heat exchanger 12 are connected in sequence, and the ground heat source heat exchanger 12 The other side is connected to the other side of the second circulating pump 13, thereby forming a circulating water channel.
油—氨水换热器3环套于发生器4,发生器4为竖直圆管,且在油—氨水换热器3内部设有半圆形导流挡板21,发生器4表面均匀焊有具有一定厚度的长方形肋片22,长方形肋片22向上倾斜并与竖直方向夹角α为40~50度,肋片长度L为发生器管径D的1/6~1/4。The oil-ammonia water heat exchanger 3 is looped on the generator 4. The generator 4 is a vertical circular tube, and a semicircular guide baffle 21 is arranged inside the oil-ammonia water heat exchanger 3. The surface of the generator 4 is evenly welded. There are rectangular ribs 22 with a certain thickness, the rectangular ribs 22 are inclined upward and the angle α with the vertical direction is 40-50 degrees, and the length L of the ribs is 1/6-1/4 of the diameter D of the generator.
低品位可燃气燃烧装置20中的分级燃烧器15包括一级燃烧器26和二级燃烧器27,一级燃烧器26包括燃气管28和喷嘴29,且位于油—氨水换热器3底面近边缘处下方,二级燃烧器27包括燃气管30和喷嘴31,位于发生器4底部中心下方,一、二级燃烧器分别设置独立的燃气控制阀32、33。The staged burner 15 in the low-grade combustible gas combustion device 20 includes a primary burner 26 and a secondary burner 27. The primary burner 26 includes a gas pipe 28 and a nozzle 29, and is located near the bottom surface of the oil-ammonia water heat exchanger 3. Below the edge, the secondary burner 27 includes a gas pipe 30 and a nozzle 31, and is located below the center of the bottom of the generator 4. The primary and secondary burners are respectively provided with independent gas control valves 32 and 33.
地热源换热器12为锥体形螺旋结构的金属圆管,其螺旋角β为10~14度,并且地热源换热器12自上而下的浅埋于地表面以下,其入口在地表面以下1.8~2.2米处,其出口在地表面以下2.8~3.2米处。The geothermal source heat exchanger 12 is a metal circular tube with a conical spiral structure, and its helix angle β is 10-14 degrees, and the geothermal source heat exchanger 12 is buried shallowly below the ground surface from top to bottom, and its entrance is on the ground surface 1.8-2.2 meters below, and its exit is 2.8-3.2 meters below the ground surface.
户用型太阳能集热系统17中的槽式太阳能集热器1上设置有圆弧形遮光板23,圆弧形遮光板23的半径R为高温集热管24半径r的的1.5~2.0倍,遮光板23外表面涂有有机硅耐高温涂料25。The trough solar heat collector 1 in the household solar heat collection system 17 is provided with an arc-shaped shading plate 23, and the radius R of the arc-shaped shading plate 23 is 1.5 to 2.0 times the radius r of the high-temperature heat collecting tube 24, The outer surface of the light-shielding plate 23 is coated with an organosilicon high-temperature-resistant coating 25 .
本发明的工作原理:Working principle of the present invention:
当太阳光照充足时,槽式太阳能集热器内的工质油上升到工作温度320摄氏度,户用型太阳能集热系统开始启动,第一循环泵为户用型太阳能集热系统的工质油提供循环动力,工质油通过油—氨水换热器加热发生器中的氨水溶液;当工质油的温度低于320摄氏度,但仍在260摄氏度以上时,户用型太阳能集热系统仍处于工作状态,低品位可燃气燃烧装置同时启动工作,分级燃烧器中的一级燃烧器通过燃烧可燃气加热油—氨水换热器,从而加热发生器中的氨水溶液;当工质油温度低于260摄氏度时,只有低品位可燃气燃烧装置启动工作,分级燃烧器中的二级燃烧器燃烧可燃气加热发生器,从而加热发生器中的氨水溶液;此外,当太阳光照过于强烈时,可通过调整圆弧形遮光板实现调节工质油的温度。When the sunlight is sufficient, the working medium oil in the trough solar collector rises to the working temperature of 320 degrees Celsius, and the household solar heat collection system starts to start, and the first circulation pump is the working medium oil of the household solar heat collection system To provide circulating power, the working medium oil heats the ammonia solution in the generator through the oil-ammonia water heat exchanger; when the temperature of the working medium oil is lower than 320 degrees Celsius, but still above 260 degrees Celsius, the household solar thermal collection system is still in the In the working state, the low-grade combustible gas combustion device starts to work at the same time, and the primary burner in the staged burner heats the oil-ammonia water heat exchanger by burning combustible gas, thereby heating the ammonia solution in the generator; when the temperature of the working medium oil is lower than At 260 degrees Celsius, only the low-grade combustible gas combustion device starts to work, and the secondary burner in the staged burner burns combustible gas to heat the generator, thereby heating the ammonia solution in the generator; in addition, when the sun is too strong, it can pass Adjust the arc-shaped shading plate to adjust the temperature of the working medium oil.
发生器中的氨水溶液受热后,部分氨气从溶液中分离出来。氨气通过冷凝器,节流阀后在蒸发器中蒸发吸热。水在整个毛细管网系统中循环流动,第二循环泵将水输送到毛细管分水器和毛细管网。水在流经毛细管网时,带走用户建筑内的热量。吸收热量后的水经毛细管集水器汇合后,依次通过地热源换热器、氨—水换热器换热降温,从而实现为用户循环制冷。After the ammonia solution in the generator is heated, part of the ammonia gas is separated from the solution. Ammonia gas passes through the condenser and evaporates in the evaporator to absorb heat after the throttle valve. The water circulates through the whole capillary network system, and the second circulation pump delivers the water to the capillary water separator and the capillary network. When the water flows through the capillary network, it takes away the heat in the user's building. After absorbing the heat, the water is combined by the capillary water collector, and then passes through the geothermal source heat exchanger and the ammonia-water heat exchanger to exchange heat and cool down in order, thereby realizing circulating refrigeration for users.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710147121.2A CN107202451A (en) | 2017-03-13 | 2017-03-13 | A kind of residents multipotency source absorption type capillary network refrigeration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710147121.2A CN107202451A (en) | 2017-03-13 | 2017-03-13 | A kind of residents multipotency source absorption type capillary network refrigeration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107202451A true CN107202451A (en) | 2017-09-26 |
Family
ID=59904914
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710147121.2A Pending CN107202451A (en) | 2017-03-13 | 2017-03-13 | A kind of residents multipotency source absorption type capillary network refrigeration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107202451A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111998573A (en) * | 2020-07-02 | 2020-11-27 | 河北工程大学 | Light hydrocarbon gas driven air source heat pump |
| CN114046673A (en) * | 2021-10-21 | 2022-02-15 | 山东旭能环保科技有限公司 | A high-efficiency and energy-saving cooling water tower |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103398436A (en) * | 2013-07-29 | 2013-11-20 | 华南理工大学 | Solar diffusion and absorption refrigeration type air conditioning system based on radiation thermoregulation |
| CN103512273A (en) * | 2013-09-30 | 2014-01-15 | 青岛科技大学 | Novel cold-hot integrated system based on terrestrial heat and solar energy |
| CN103900287A (en) * | 2014-04-04 | 2014-07-02 | 东南大学 | Heat exchange system in combined operation of solar energy and geothermal energy |
| CN103925635A (en) * | 2014-04-28 | 2014-07-16 | 中国建筑西北设计研究院有限公司 | All-weather solar energy supply system |
| CN206724513U (en) * | 2017-03-13 | 2017-12-08 | 西安交通大学 | A kind of residents multipotency source absorption type capillary network refrigeration system |
-
2017
- 2017-03-13 CN CN201710147121.2A patent/CN107202451A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103398436A (en) * | 2013-07-29 | 2013-11-20 | 华南理工大学 | Solar diffusion and absorption refrigeration type air conditioning system based on radiation thermoregulation |
| CN103512273A (en) * | 2013-09-30 | 2014-01-15 | 青岛科技大学 | Novel cold-hot integrated system based on terrestrial heat and solar energy |
| CN103900287A (en) * | 2014-04-04 | 2014-07-02 | 东南大学 | Heat exchange system in combined operation of solar energy and geothermal energy |
| CN103925635A (en) * | 2014-04-28 | 2014-07-16 | 中国建筑西北设计研究院有限公司 | All-weather solar energy supply system |
| CN206724513U (en) * | 2017-03-13 | 2017-12-08 | 西安交通大学 | A kind of residents multipotency source absorption type capillary network refrigeration system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111998573A (en) * | 2020-07-02 | 2020-11-27 | 河北工程大学 | Light hydrocarbon gas driven air source heat pump |
| CN114046673A (en) * | 2021-10-21 | 2022-02-15 | 山东旭能环保科技有限公司 | A high-efficiency and energy-saving cooling water tower |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103925635B (en) | A kind of all-weather solar energy supplying system | |
| CN101334220B (en) | Convective photoelectric conversion enhancement and light heat recovery full working condition composite heat source device | |
| CN104864630B (en) | A kind of multi-temperature gradient of use solar energy heating utilizes system | |
| CN108036544B (en) | Hybrid energy system driven by solar/biomass integration | |
| CN1807995B (en) | Solar water-heating and air-conditioning heating system employing gas or oil to aid heating | |
| CN204963255U (en) | Solar energy heat supplying system | |
| CN105605661A (en) | Solar phase-change heat storage type warmer | |
| CN104482664A (en) | Novel low-energy consumption solar low-temperature water heater | |
| CN101929765A (en) | A kind of solar absorption refrigeration system of separate type | |
| CN114264000B (en) | A distributed energy center application system | |
| CN108151359A (en) | A kind of two level heat accumulating type domestic solar utilizes system | |
| CN107202451A (en) | A kind of residents multipotency source absorption type capillary network refrigeration system | |
| CN206724513U (en) | A kind of residents multipotency source absorption type capillary network refrigeration system | |
| CN206888173U (en) | A kind of passive type heating ventilation solar house | |
| CN112856831B (en) | Multifunctional heat pipe type photovoltaic photo-thermal high-low temperature phase change floor coupling system and method | |
| CN106931679B (en) | Solar heating and refrigerating system based on energy storage and operation control method thereof | |
| CN106595067A (en) | Micro-channel solar heating system based on superconducting heat pipe technology | |
| CN202675650U (en) | Water-heating and electricity-generating integrated type superconducting wall-mounted solar water heater | |
| CN211503320U (en) | Solar ground source heat pump system | |
| CN218764075U (en) | Heat pump heating system with composite heat source | |
| CN107917458A (en) | Solar energy wall-hung boiler hot-water heating system | |
| CN109737615B (en) | Small Household Solar Thermoelectric Cooling Polygeneration System | |
| CN209676196U (en) | A kind of photovoltaic and photothermal solar integral system using capillary recycling waste heat | |
| CN220524375U (en) | An annular heat pipe coupled capillary photovoltaic photothermal energy-saving wall system | |
| CN208154693U (en) | Solar heat collection ventilation system for passive house |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170926 |