CN205102453U - Solar energy doublestage ejector refrigeration system - Google Patents
Solar energy doublestage ejector refrigeration system Download PDFInfo
- Publication number
- CN205102453U CN205102453U CN201520573040.5U CN201520573040U CN205102453U CN 205102453 U CN205102453 U CN 205102453U CN 201520573040 U CN201520573040 U CN 201520573040U CN 205102453 U CN205102453 U CN 205102453U
- Authority
- CN
- China
- Prior art keywords
- generator
- inlet
- heating coil
- outlet
- intercooler
- 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.)
- Expired - Fee Related
Links
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
本实用新型公开了一种太阳能双级喷射式制冷系统,旨在提供一种以太阳能为驱动的太阳能双级喷射式制冷系统,以提高整个系统的压比,从而可以降低蒸发温度、提高冷凝温度。包括太阳能集热器、第一发生器、第二发生器、第一喷射器、第二喷射器、冷凝器、蒸发器、中间冷却器、四通阀、第一加热盘管、第二加热盘管、第一热力膨胀阀、第二热力膨胀阀和冷却盘管,冷却盘管置于中间冷却器内,第一加热盘管置于所述第一发生器内,第二加热盘管置于第二发生器内;第一发生器的工作温度高于第二发生器的工作温度。该系统不仅可以进行较低蒸发温度、较高冷凝温度的循环,而且可以进行能源的梯级利用,整个系统的能源利用效率高,节能效果好。
The utility model discloses a solar energy two-stage jet refrigeration system, aiming to provide a solar energy two-stage jet refrigeration system driven by solar energy, so as to increase the pressure ratio of the whole system, thereby reducing the evaporation temperature and increasing the condensation temperature . Including solar collector, first generator, second generator, first injector, second injector, condenser, evaporator, intercooler, four-way valve, first heating coil, second heating pan pipe, the first thermal expansion valve, the second thermal expansion valve and the cooling coil, the cooling coil is placed in the intercooler, the first heating coil is placed in the first generator, and the second heating coil is placed in the Inside the second generator; the operating temperature of the first generator is higher than the operating temperature of the second generator. The system can not only carry out the cycle of lower evaporation temperature and higher condensation temperature, but also can carry out cascade utilization of energy, the energy utilization efficiency of the whole system is high, and the energy saving effect is good.
Description
技术领域 technical field
本实用新型涉及一种制冷循环系统,尤其涉及一种太阳能双级喷射式制冷系统。 The utility model relates to a refrigerating cycle system, in particular to a solar energy double-stage jet refrigerating system.
背景技术 Background technique
目前,能源紧缺已成为全世界必须面对和解决的重大问题。提高现有能源利用效率,开发利用可再生能源,实现可持续发展成为当今时代的一个主题。太阳能利用技术现已比较成熟,利用太阳能进行空调制冷也得到了普遍应用,对太阳能进行梯级利用是节能的一项重要措施。 At present, energy shortage has become a major problem that the whole world must face and solve. Improving the efficiency of existing energy utilization, developing and utilizing renewable energy, and realizing sustainable development have become a theme of today's era. Solar energy utilization technology is now relatively mature, and the use of solar energy for air conditioning and refrigeration has also been widely used. Cascade utilization of solar energy is an important measure for energy conservation.
传统的单喷射式制冷系统简单、运动部件少、结构紧凑、占用空间小,且具有利用太阳能、地热等可再生能源及工业余热等低品位能源来实现制冷的优点。传统喷射制冷循环所能获取的制冷温度较高,通常0℃以上,受喷射器压缩比小的限制,难以同时达到较高的冷凝压力和较低的蒸发压力,而且该系统效率较低,要通过蒸发器获得-10℃的制冷温度几乎是不可能的,从而使得传统喷射制冷机应用受到较大限制,利用低温热源提供高温热源也受到限制。 The traditional single-jet refrigeration system is simple, has few moving parts, compact structure, takes up little space, and has the advantages of using renewable energy such as solar energy, geothermal energy, and low-grade energy such as industrial waste heat to achieve refrigeration. The refrigeration temperature that can be obtained by the traditional injection refrigeration cycle is relatively high, usually above 0°C. Due to the limitation of the small compression ratio of the ejector, it is difficult to achieve a high condensation pressure and a low evaporation pressure at the same time, and the efficiency of the system is low. It is almost impossible to obtain a refrigeration temperature of -10°C through the evaporator, which limits the application of traditional jet refrigerators, and the use of low-temperature heat sources to provide high-temperature heat sources is also limited.
实用新型内容 Utility model content
本实用新型的目的是针对现有技术中存在的技术缺陷,而提供一种以太阳能为驱动的太阳能双级喷射式制冷系统,以提高整个系统的压比,从而可以降低蒸发温度、提高冷凝温度。 The purpose of this utility model is to aim at the technical defects existing in the prior art, and provide a solar energy two-stage jet refrigeration system driven by solar energy, so as to increase the pressure ratio of the whole system, thereby reducing the evaporation temperature and increasing the condensation temperature .
为实现本实用新型的目的所采用的技术方案是: The technical scheme adopted for realizing the purpose of this utility model is:
一种太阳能双级喷射式制冷系统,其特征在于,包括太阳能集热器、第一发生器、第二发生器、第一喷射器、第二喷射器、冷凝器、蒸发器、中间冷却器、四通阀、第一加热盘管、第二加热盘管、第一热力膨胀阀、第二热力膨胀阀和冷却盘管,所述冷却盘管置于所述中间冷却器内,所述第一加热盘管置于所述第一发生器内,所述第二加热盘管置于所述第二发生器内;所述第一发生器的制冷剂蒸汽出口与所述第一喷射器的入口连接,所述第一喷射器的出口与所述冷凝器的制冷剂入口连接,所述冷凝器的制冷剂出口与所述四通阀的第一接口连接,所述四通阀的第二接口一路通过第一工质泵与所述第一发生器的入口连接,另一路通过第二工质泵与所述第二发生器的入口连接,所述四通阀的第三接口通过所述第一热力膨胀阀与所述中间冷却器的入口连接,所述四通阀的第四接口与所述冷却盘管的进口连接,所述冷却盘管的出口通过所述第二热力膨胀阀与所述蒸发器的进口连接,所述蒸发器的出口与所述第二喷射器的引射接管连接,所述中间冷却器的蒸汽出口与所述第一喷射器的引射接管连接,所述第二发生器的出口与所述第二喷射器的进口连接,所述第二喷射器的出口与所述中间冷却器液面下方接管连接,所述太阳能集热器的热媒出口与所述第一加热盘管的热媒入口连接,所述第一加热盘管的热媒出口与所述第二加热盘管的热媒入口连接,所述第二加热盘管的热媒出口通过热媒泵与所述太阳能集热器的入口连接;所述第一发生器的工作温度高于所述第二发生器的工作温度。 A solar dual-stage jet refrigeration system is characterized in that it includes a solar heat collector, a first generator, a second generator, a first ejector, a second ejector, a condenser, an evaporator, an intercooler, Four-way valve, first heating coil, second heating coil, first thermal expansion valve, second thermal expansion valve and cooling coil, the cooling coil is placed in the intercooler, the first The heating coil is placed in the first generator, and the second heating coil is placed in the second generator; the refrigerant vapor outlet of the first generator is connected to the inlet of the first ejector The outlet of the first ejector is connected to the refrigerant inlet of the condenser, the refrigerant outlet of the condenser is connected to the first port of the four-way valve, and the second port of the four-way valve One path is connected to the inlet of the first generator through the first working fluid pump, the other path is connected to the inlet of the second generator through the second working fluid pump, and the third port of the four-way valve passes through the first A thermal expansion valve is connected to the inlet of the intercooler, the fourth port of the four-way valve is connected to the inlet of the cooling coil, and the outlet of the cooling coil is connected to the cooling coil through the second thermal expansion valve. The inlet of the evaporator is connected, the outlet of the evaporator is connected to the ejection pipe of the second ejector, the steam outlet of the intercooler is connected to the ejection pipe of the first ejector, and the outlet of the second ejector is connected to the ejection pipe of the first ejector. The outlet of the second generator is connected to the inlet of the second injector, the outlet of the second injector is connected to the connecting pipe below the liquid surface of the intercooler, and the heat medium outlet of the solar collector is connected to the second ejector. The heat medium inlet of a heating coil is connected, the heat medium outlet of the first heating coil is connected with the heat medium inlet of the second heating coil, and the heat medium outlet of the second heating coil passes through the heat medium pump It is connected with the inlet of the solar heat collector; the operating temperature of the first generator is higher than that of the second generator.
与现有技术相比,本实用新型的有益效果是: Compared with the prior art, the beneficial effects of the utility model are:
1、本实用新型的太阳能双级喷射式制冷系统中的第二发生器产生的蒸汽作为第二喷射器的工作流体引射来自蒸发器的蒸汽,增压后与经过第一节流阀后的液体和闪蒸汽在中间冷却器内混合产生蒸汽,第一发生器产生的蒸汽作为第一喷射器的工作流体引射来自中间冷却器内的蒸汽,增压后进入冷凝器发生冷凝,一部分冷凝液体经过中间冷却器过冷后经第二节流阀进入蒸发器吸热,蒸汽压力依次增高,提高了整个系统的压比,从而可以降低蒸发温度、提高冷凝温度,扩大了喷射式制冷机的应用,扩大了利用低温热源提供高温热源的应用。 1. The steam generated by the second generator in the solar dual-stage jet refrigeration system of the present invention is used as the working fluid of the second jet to eject the steam from the evaporator, after pressurization and after passing through the first throttle valve The liquid and flash steam are mixed in the intercooler to generate steam. The steam generated by the first generator is used as the working fluid of the first ejector to guide the steam from the intercooler. After pressurization, it enters the condenser to condense, and a part of the condensed liquid After being supercooled by the intercooler, it enters the evaporator through the second throttle valve to absorb heat, and the steam pressure increases sequentially, which increases the pressure ratio of the entire system, thereby reducing the evaporation temperature and increasing the condensation temperature, and expanding the application of jet refrigerators. , expanding the application of using a low temperature heat source to provide a high temperature heat source.
2、本实用新型的制冷系统中,第一发生器、第二发生器分别通过其内置的第一加热盘管、第二加热盘管为制冷剂加热,第一加热盘管、第二加热盘管的热媒由太阳能集热器提供,太阳能集热器的热媒出口与所述第一加热盘管的热媒入口连接,第一加热盘管的热媒出口与所述第二加热盘管的热媒入口连接,第二加热盘管的热媒出口经热媒泵与太阳能集热器入口连接,使热媒依次通过第一加热盘管、第二加热盘管对制冷剂进行加热,实现了低品位能源的梯级利用,提高整个系统的能源利用效率。 2. In the refrigeration system of the present utility model, the first generator and the second generator heat the refrigerant through their built-in first heating coil and second heating coil respectively, and the first heating coil and the second heating coil The heat medium of the tube is provided by the solar collector, the heat medium outlet of the solar heat collector is connected with the heat medium inlet of the first heating coil, and the heat medium outlet of the first heating coil is connected with the second heating coil The heat medium inlet of the second heating coil is connected, and the heat medium outlet of the second heating coil is connected with the inlet of the solar collector through the heat medium pump, so that the heat medium passes through the first heating coil and the second heating coil to heat the refrigerant in sequence, realizing It improves the cascade utilization of low-grade energy and improves the energy utilization efficiency of the entire system.
3、本实用新型的太阳能双级喷射式制冷系统不仅可以进行较低蒸发温度、较高冷凝温度的循环,而且可以进行能源的梯级利用,整个系统的能源利用效率高,节能效果好。 3. The solar dual-stage jet refrigeration system of the present invention can not only carry out the cycle of lower evaporation temperature and higher condensation temperature, but also can carry out cascade utilization of energy, the energy utilization efficiency of the whole system is high, and the energy saving effect is good.
附图说明 Description of drawings
图1所示为本实用新型一种太阳能双级喷射式制冷系统的示意图。 Figure 1 is a schematic diagram of a solar dual-stage jet refrigeration system of the present invention.
具体实施方式 detailed description
以下结合附图和具体实施例对本实用新型作进一步详细说明。 Below in conjunction with accompanying drawing and specific embodiment the utility model is described in further detail.
本实用新型一种太阳能双级喷射式制冷系统的示意图如图1所示,包括太阳能集热器14、第一发生器15、第二发生器10、第一喷射器2、第二喷射器1、冷凝器3、蒸发器9、中间冷却器8、四通阀4、第一加热盘管16、第二加热盘管17、第一热力膨胀阀5、第二热力膨胀阀7和冷却盘管6,所述冷却盘管6置于所述中间冷却器8内,所述第一加热盘管16置于所述第一发生器15内,所述第二加热盘管17置于所述第二发生器10内。所述第一发生器15的制冷剂蒸汽出口与所述第一喷射器2的入口连接,所述第一喷射器2的出口与所述冷凝器3的制冷剂入口连接,所述冷凝器3的制冷剂出口与所述四通阀4的第一接口a连接,所述四通阀的第二接口b一路通过第一工质泵12与所述第一发生器15的入口连接,另一路通过第二工质泵13与所述第二发生器17的入口连接,所述四通阀4的第三接口c通过所述第一热力膨胀阀5与所述中间冷却器8的入口连接,所述四通阀的第四接口d与所述冷却盘管6的进口连接,所述冷却盘管6的出口通过所述第二热力膨胀阀7与所述蒸发器9的进口连接,所述蒸发器9的出口与所述第二喷射器1的引射接管连接,所述中间冷却器8的蒸汽出口与所述第一喷射器2的引射接管连接,所述第二发生器10的出口与所述第二喷射器1的进口连接,所述第二喷射器1的出口与所述中间冷却器8液面下方接管连接。所述太阳能集热器14的热媒出口与所述第一加热盘管16的热媒入口连接,所述第一加热盘管16的热媒出口与所述第二加热盘管17的热媒入口连接,所述第二加热盘管17的热媒出口通过热媒泵11与所述太阳能集热器14的入口连接。所述第一发生器的工作温度高于所述第二发生器的工作温度。 A schematic diagram of a solar dual-stage jet refrigeration system of the utility model is shown in Figure 1, including a solar heat collector 14, a first generator 15, a second generator 10, a first injector 2, and a second injector 1 , condenser 3, evaporator 9, intercooler 8, four-way valve 4, first heating coil 16, second heating coil 17, first thermal expansion valve 5, second thermal expansion valve 7 and cooling coil 6. The cooling coil 6 is placed in the intercooler 8, the first heating coil 16 is placed in the first generator 15, and the second heating coil 17 is placed in the first Inside the second generator 10 . The refrigerant vapor outlet of the first generator 15 is connected to the inlet of the first ejector 2, and the outlet of the first ejector 2 is connected to the refrigerant inlet of the condenser 3, and the condenser 3 The outlet of the refrigerant is connected to the first interface a of the four-way valve 4, the second interface b of the four-way valve is connected to the inlet of the first generator 15 through the first working medium pump 12, and the other The second working fluid pump 13 is connected to the inlet of the second generator 17, the third port c of the four-way valve 4 is connected to the inlet of the intercooler 8 through the first thermal expansion valve 5, The fourth port d of the four-way valve is connected to the inlet of the cooling coil 6, and the outlet of the cooling coil 6 is connected to the inlet of the evaporator 9 through the second thermal expansion valve 7. The outlet of the evaporator 9 is connected to the ejector pipe of the second injector 1, the steam outlet of the intercooler 8 is connected to the ejector pipe of the first ejector 2, and the outlet of the second generator 10 The outlet is connected to the inlet of the second injector 1 , and the outlet of the second injector 1 is connected to the connecting pipe below the liquid surface of the intercooler 8 . The heat medium outlet of the solar heat collector 14 is connected to the heat medium inlet of the first heating coil 16, and the heat medium outlet of the first heating coil 16 is connected to the heat medium of the second heating coil 17. The inlet is connected, and the outlet of the heat medium of the second heating coil 17 is connected with the inlet of the solar heat collector 14 through the heat medium pump 11 . The operating temperature of the first generator is higher than the operating temperature of the second generator.
所述第一加热盘管16、第二加热盘管17的热媒由太阳能集热器14提供,太阳能集热器14的热媒出口与所述第一加热盘管16的热媒入口连接,所述第一加热盘管16的热媒出口与所述第二加热盘管17的热媒入口连接,所述第二加热盘管17的热媒出口经热媒泵11与太阳能集热器14入口连接,使受太阳能集热器14加热的热媒依次通过第一加热盘管16、第二加热盘管17对制冷剂进行加热产生蒸汽,实现能源的梯级利用。 The heat medium of the first heating coil 16 and the second heating coil 17 is provided by the solar heat collector 14, and the heat medium outlet of the solar heat collector 14 is connected with the heat medium inlet of the first heating coil 16, The heat medium outlet of the first heating coil 16 is connected to the heat medium inlet of the second heating coil 17, and the heat medium outlet of the second heating coil 17 passes through the heat medium pump 11 and the solar heat collector 14 The inlet is connected so that the heat medium heated by the solar heat collector 14 passes through the first heating coil 16 and the second heating coil 17 in sequence to heat the refrigerant to generate steam, thereby realizing cascaded utilization of energy.
所述第二发生器10产生的蒸汽作为第二喷射器1的工作流体引射来自蒸发器9的蒸汽,增压后与经过第一热力膨胀阀5后的液体和闪蒸汽在中间冷却器8内混合产生蒸汽,第一发生器15产生的蒸汽作为第一喷射器2的工作流体引射来自中间冷却器8内的蒸汽,增压后进入冷凝器3发生冷凝,一部分冷凝液体经过中间冷却器8过冷后经第二热力膨胀阀7进入蒸发器9吸热,蒸汽压力依次增高,提高了整个系统的压比,如此周而复始,同时实现较低蒸发温度、较高冷凝温度的制冷循环。 The steam generated by the second generator 10 is used as the working fluid of the second ejector 1 to guide the steam from the evaporator 9, and after pressurization, the liquid and flash steam after passing through the first thermal expansion valve 5 are transferred to the intercooler 8 Internal mixing generates steam. The steam generated by the first generator 15 is used as the working fluid of the first ejector 2 to eject the steam from the intercooler 8. After pressurization, it enters the condenser 3 for condensation, and a part of the condensed liquid passes through the intercooler. After 8 is supercooled, it enters the evaporator 9 through the second thermal expansion valve 7 to absorb heat, and the steam pressure increases successively, which increases the pressure ratio of the entire system. This cycle repeats itself, and at the same time realizes a refrigeration cycle with a lower evaporation temperature and a higher condensation temperature.
以上所述仅是本实用新型的优选实施方式,应当指出的是,对于本技术领域的普通技术人员来说,在不脱离本实用新型原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本实用新型的保护范围。 The above is only a preferred embodiment of the utility model, it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the utility model, some improvements and modifications can also be made, these Improvement and retouching should also be regarded as the protection scope of the present utility model.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520573040.5U CN205102453U (en) | 2015-07-31 | 2015-07-31 | Solar energy doublestage ejector refrigeration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520573040.5U CN205102453U (en) | 2015-07-31 | 2015-07-31 | Solar energy doublestage ejector refrigeration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205102453U true CN205102453U (en) | 2016-03-23 |
Family
ID=55518232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520573040.5U Expired - Fee Related CN205102453U (en) | 2015-07-31 | 2015-07-31 | Solar energy doublestage ejector refrigeration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205102453U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112629066A (en) * | 2020-12-02 | 2021-04-09 | 浙江省送变电工程有限公司 | Solar-driven pressurizing injection refrigerating system |
| CN113883741A (en) * | 2021-10-14 | 2022-01-04 | 青岛海信日立空调系统有限公司 | Absorption refrigeration system |
| CN115406217A (en) * | 2022-08-12 | 2022-11-29 | 嵊州市浙江工业大学创新研究院 | Solar vacuum freezing combined hot air drying device |
-
2015
- 2015-07-31 CN CN201520573040.5U patent/CN205102453U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112629066A (en) * | 2020-12-02 | 2021-04-09 | 浙江省送变电工程有限公司 | Solar-driven pressurizing injection refrigerating system |
| CN112629066B (en) * | 2020-12-02 | 2022-07-19 | 浙江省送变电工程有限公司 | Solar Powered Booster Jet Refrigeration System |
| CN113883741A (en) * | 2021-10-14 | 2022-01-04 | 青岛海信日立空调系统有限公司 | Absorption refrigeration system |
| CN115406217A (en) * | 2022-08-12 | 2022-11-29 | 嵊州市浙江工业大学创新研究院 | Solar vacuum freezing combined hot air drying device |
| CN115406217B (en) * | 2022-08-12 | 2023-08-22 | 嵊州市浙江工业大学创新研究院 | Solar vacuum freezing combined hot air drying device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103629860B (en) | Trans-critical cycle CO 2cool and thermal power combined cycle system | |
| CN109763948A (en) | A supercritical carbon dioxide solar thermal power generation system and operation method | |
| CN110887278A (en) | Energy self-sufficient carbon dioxide cogeneration system for low-grade heat source | |
| CN205002435U (en) | Utilize solar energy steam -jet ejector formula overlapping cooling cycle system | |
| CN101949609B (en) | Low-temperature heat source-driven air-cooling ammonia water absorption refrigerating machine | |
| CN105402926A (en) | Combined cooling and power system and refrigeration, power generation and combined cooling and power method based on combined cooling and power system | |
| CN204987534U (en) | Solar energy vortex refrigerating system | |
| CN104033199B (en) | A kind of organic rankine cycle system using the built-in heat pump of mixing organic working medium | |
| CN108362026B (en) | A carbon dioxide transcritical cycle cooling, heating and power combined system | |
| CN104930752B (en) | The injection compression refrigerating system driven using the low grade heat energy of subcooler | |
| CN205102453U (en) | Solar energy doublestage ejector refrigeration system | |
| CN208222902U (en) | A kind of carbon dioxide trans-critical cycle cool and thermal power combined system | |
| CN104930751B (en) | Injection compression refrigerating system with subcooler and utilization low grade heat energy | |
| CN201387143Y (en) | High-temperature energy-saving water heater device for low-temperature air source heat pump with storing and dividing device | |
| CN103438609A (en) | Refrigeration system by utilizing tail gas of fishing boat | |
| CN102654326B (en) | Double-injection refrigeration device synergized by gas-liquid ejector | |
| CN103017399A (en) | Two-level absorption refrigeration device with injector | |
| CN103954069A (en) | Multi-heat source jet type refrigerator | |
| CN203454458U (en) | Solar efficient spraying refrigeration system | |
| CN103644675A (en) | Solar energy direct expansion type jet refrigerating machine | |
| CN104990302A (en) | Jet-compression refrigeration system being provided with gas-liquid separator and using low-grade heat energy | |
| CN103411342A (en) | Solar high-efficient spraying and cooling system | |
| CN103994599A (en) | Transcritical injection refrigeration system based on gas-liquid injection pump | |
| CN204716400U (en) | The air inlet air conditioning system of Combined cycle gas-steam turbine power plant | |
| CN106403355A (en) | Ejection refrigeration system with double evaporators |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160323 Termination date: 20160731 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |