CN201203297Y - Solar-assisted direct-fired hot and cold water unit - Google Patents
Solar-assisted direct-fired hot and cold water unit Download PDFInfo
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- CN201203297Y CN201203297Y CNU2008200579993U CN200820057999U CN201203297Y CN 201203297 Y CN201203297 Y CN 201203297Y CN U2008200579993 U CNU2008200579993 U CN U2008200579993U CN 200820057999 U CN200820057999 U CN 200820057999U CN 201203297 Y CN201203297 Y CN 201203297Y
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 239000002918 waste heat Substances 0.000 claims abstract description 22
- 238000001816 cooling Methods 0.000 claims abstract description 16
- 239000006096 absorbing agent Substances 0.000 claims abstract description 13
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 239000012530 fluid Substances 0.000 claims description 4
- 239000003517 fume Substances 0.000 claims 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 10
- 239000003546 flue gas Substances 0.000 abstract description 10
- 238000002485 combustion reaction Methods 0.000 abstract description 4
- 239000000446 fuel Substances 0.000 abstract description 4
- 239000000498 cooling water Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 3
- 239000008236 heating water Substances 0.000 abstract 1
- 238000011160 research Methods 0.000 description 13
- 238000010521 absorption reaction Methods 0.000 description 10
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 10
- 238000004378 air conditioning Methods 0.000 description 9
- 238000005265 energy consumption Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 5
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 5
- 239000003345 natural gas Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 3
- 239000003507 refrigerant Substances 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000003112 inhibitor Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 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
- 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
- Y02E10/44—Heat exchange systems
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Abstract
本实用新型涉及一种太阳能辅助直燃式冷热水机组,系统由高压发生器(1)、气水换热器(2)、余热发生器(3)、烟气管(4)、太阳能集热器(5)、低压发生器(6)、冷凝器(7)、吸收器(8)、蒸发器(9)、冷却塔(10)、冷却(加热)盘管(11)、低温溶液热交换器(12)、高温溶液热交换器(13)以及阀门和泵组成。该机组在原有的双效直燃式冷热水机的基础上引入了由太阳能集热器、汽水换热器和余热发生器组成的单效循环,构成新的循环。利用太阳能集热器(5)加热循环水并使温度初步升高后再通入气水换热器(2)使其温度进一步升高,由气水换热器(2)流出的高温热水进入余热发生器,制冷水和制热水时作为辅助驱动热源加热溶液分别提供冷量和热量,同时减少燃料消耗。本实用新型通过充分利用低品位的太阳能热源和直燃机高压发生器内燃烧产生的高温烟气,优化了循环系统,故较双效直燃式冷热水机组提高了能源利用效率节能效果显著,一次能源效率PER可提高9%。
The utility model relates to a solar-assisted direct-fired hot and cold water unit. The system consists of a high-voltage generator (1), an air-water heat exchanger (2), a waste heat generator (3), a flue gas pipe (4), and a solar collector. Heater (5), low pressure generator (6), condenser (7), absorber (8), evaporator (9), cooling tower (10), cooling (heating) coil (11), low temperature solution heat It consists of an exchanger (12), a high-temperature solution heat exchanger (13), valves and pumps. On the basis of the original double-effect direct-fired hot and cold water machine, the unit introduces a single-effect cycle composed of solar collectors, steam-water heat exchangers and waste heat generators to form a new cycle. Use the solar heat collector (5) to heat the circulating water and make the temperature rise initially, then pass it into the air-water heat exchanger (2) to further increase the temperature, and the high-temperature hot water flowing out from the air-water heat exchanger (2) Entering the waste heat generator, when cooling water and heating water, it is used as an auxiliary driving heat source to heat the solution to provide cooling and heat respectively, while reducing fuel consumption. The utility model optimizes the circulation system by making full use of the low-grade solar heat source and the high-temperature flue gas generated by combustion in the high-pressure generator of the direct-fired engine, so that the energy utilization efficiency is improved compared with the double-effect direct-fired hot and cold water unit, and the energy-saving effect is remarkable. , the primary energy efficiency PER can be increased by 9%.
Description
技术领域 technical field
本实用涉及一种直燃式冷热水机组,尤其涉及一种空调用太阳能辅助直燃式冷热水机组。The utility model relates to a direct-fired cold and hot water unit, in particular to a solar-assisted direct-fired cold and hot water unit for air conditioning.
背景技术 Background technique
国际制冷学会IIR(The International Institute of Refrigeration)做出的估计表明:世界上的15%电能消耗于各种各样的制冷和空调行业,空调的能耗占家居和商业建筑的45%。我国建筑能耗占全部终端用户总能耗的比例将在近年内达到35%。在建筑能耗方面的研究表明,空调能耗占办公楼建筑总能耗的比例最高可达60%,在我国随着经济条件的改善使得建筑空调能耗不断上升,由此给能源、电力和环境带来很大的压力。因此节能是关系到国计民生的大事。而节能的两个主要途径就是:提高能源的利用效率、使用可再生能源。Estimates made by the International Institute of Refrigeration (IIR) show that 15% of the world's electrical energy is consumed in various refrigeration and air-conditioning industries, and air-conditioning consumes 45% of the energy consumed by homes and commercial buildings. The proportion of my country's building energy consumption to the total energy consumption of all end users will reach 35% in recent years. The research on building energy consumption shows that the energy consumption of air-conditioning accounts for up to 60% of the total energy consumption of office buildings. With the improvement of economic conditions in my country, the energy consumption of building air-conditioning continues to rise. The environment brings a lot of pressure. Therefore, energy saving is a major issue related to the national economy and the people's livelihood. The two main ways to save energy are: improving energy utilization efficiency and using renewable energy.
直燃型吸收式冷水机组是以天然气等燃料为驱动能源的空调冷热源设备,以其工质对臭氧层无破坏、有效减少由于电力空调引起电力供应的峰谷差,利于平衡冬夏燃气消耗提高天然气输送管道的利用率,降低天然气输送成本等特点日益得到推广。为缓解能源需求、环境保护、负荷平衡诸矛盾,在天然气气源充足的地区,直接使用天然气为动力的直燃式吸收式制冷机获得应用,可取代中央空调的电动制冷机。但是,理论分析和实际运行都表明,吸收式制冷机在能源消耗、经济性、维护管理和运行寿命等方面指标都较电动式冷水机组差。如何让直燃机能够更好的发挥其优点,业内已经和正在做大量的研究,如:直燃机的循环研究,如三效机、四效机循环的研究;吸收式热泵研究;吸收器和发生器中的表面活性剂强化传热传质研究;缓蚀剂研究;燃烧效率研究等。其中三效溴化锂吸收式制冷循环中溶液的温度较单效机、双效机有了较大幅度的提高。但目前双效溴化锂机组中常用的缓蚀剂已不能满足要求,加之高温区溴化锂溶液的物理性质缺乏标准的数据,开展试验研究存在许多困难,目前的研究主要是理论分析,国内尚没有比较成熟的技术,国外一些研究机构和公司也是处于试验研究阶段。市场上常用的双效直燃机高压发生器内的发生温度,达到160℃左右,实际运行时,烟气排放温度一般在190~200℃以上,这么高的排烟温度不仅浪费能源,对环境也造成热污染。国内已有人做过研究,并提出烟气余热回收的直燃式冷热水机。但是由于烟气的回收量有限,使其经济性不能充分体现。而另一方面,太阳能是一种辐射能,不带任何化学物质,是最洁净,最可靠的巨大能源宝库。近年来太阳能光热技术得到了长足的发展,在此基础之上的太阳能吸收式空调一度受到业内的重视,国内外相继涌现出许多太阳能空调,但是由于太阳能密度较低,大多数太阳能光热技术得到的热源品位较低。同时由于太阳能的不稳定性从而限制了单纯太阳能空调的推广。The direct-fired absorption chiller is an air-conditioning cold and heat source equipment driven by natural gas and other fuels. Its working fluid does not damage the ozone layer and effectively reduces the peak-valley difference in power supply caused by electric air-conditioning, which is conducive to balancing the increase in gas consumption in winter and summer. Features such as the utilization rate of natural gas pipelines and the reduction of natural gas transmission costs are increasingly popularized. In order to alleviate the contradictions of energy demand, environmental protection, and load balance, direct-fired absorption chillers that directly use natural gas as power have been applied in areas with sufficient natural gas sources, which can replace the electric chillers of central air conditioners. However, both theoretical analysis and actual operation show that absorption chillers are worse than electric chillers in terms of energy consumption, economy, maintenance management and operating life. How to make the direct combustion engine play its advantages better, the industry has done and is doing a lot of research, such as: the cycle research of the direct combustion engine, such as the research of the cycle of the three-effect engine and the four-effect engine; the research of the absorption heat pump; the absorber Research on the enhanced heat and mass transfer of surfactants and generators; research on corrosion inhibitors; research on combustion efficiency, etc. Among them, the temperature of the solution in the three-effect lithium bromide absorption refrigeration cycle has been greatly improved compared with the single-effect machine and the double-effect machine. However, the corrosion inhibitors commonly used in double-effect lithium bromide units can no longer meet the requirements. In addition, the physical properties of lithium bromide solutions in high temperature areas lack standard data, and there are many difficulties in carrying out experimental research. The current research is mainly theoretical analysis, which is not relatively mature in China. Some foreign research institutions and companies are also in the experimental research stage. The temperature generated in the high-pressure generator of a double-effect direct-fired engine commonly used in the market reaches about 160°C. During actual operation, the exhaust gas temperature is generally above 190-200°C. Such a high exhaust gas temperature is not only a waste of energy, but also harmful to the environment. Also cause thermal pollution. Some people in China have done research and proposed a direct-fired hot and cold water machine with flue gas waste heat recovery. However, due to the limited recovery of flue gas, its economy cannot be fully reflected. On the other hand, solar energy is a kind of radiant energy without any chemical substances. It is the cleanest and most reliable huge energy treasure house. In recent years, solar thermal technology has been greatly developed. Based on this, the solar absorption air conditioner was once valued by the industry. Many solar air conditioners have emerged one after another at home and abroad. However, due to the low density of solar energy, most solar thermal technologies The grade of the heat source obtained is lower. Simultaneously because the instability of solar energy has limited the popularization of pure solar air conditioner.
发明内容 Contents of the invention
本实用所要解决的技术问题是提供一种太阳能辅助直燃式冷热水机组,以缓解现有直燃式冷热水技术中能源利用效率低下和燃料耗量高的缺陷。The technical problem to be solved by this utility is to provide a solar-assisted direct-fired hot and cold water unit to alleviate the defects of low energy utilization efficiency and high fuel consumption in the existing direct-fired hot and cold water technology.
技术方案Technical solutions
本实用提供了一种太阳能辅助直燃式冷热水机组,包括高压发生器、气水换热器、余热发生器、烟气管、太阳能集热器、低压发生器、冷凝器、吸收器、蒸发器、冷却塔、冷却(加热)盘管、低温溶液热交换器、高温溶液热交换器以及阀门和泵。该机组在传统的双效吸收式循环的基础上增加了一个由余热发生器、汽水换热器和太阳能集热器组成的余热回路,整个循环相当于一个双效循环加一个由余热回路驱动的单效循环。利用太阳能集热器加热循环水并使温度初步升高后再通入气水换热器使其温度进一步升高,由气水换热器流出的高温热水进入余热发生器产生冷剂蒸汽进入冷凝器。The utility model provides a solar-assisted direct-fired hot and cold water unit, including a high-pressure generator, an air-water heat exchanger, a waste heat generator, a flue gas pipe, a solar heat collector, a low-pressure generator, a condenser, an absorber, Evaporators, cooling towers, cooling (heating) coils, low temperature solution heat exchangers, high temperature solution heat exchangers, and valves and pumps. On the basis of the traditional double-effect absorption cycle, the unit adds a waste heat circuit composed of waste heat generator, steam-water heat exchanger and solar collector. The whole cycle is equivalent to a double-effect cycle plus a waste heat circuit driven Single effect cycle. Use the solar heat collector to heat the circulating water and make the temperature rise initially, and then pass it into the air-water heat exchanger to further increase the temperature. The high-temperature hot water flowing out of the air-water heat exchanger enters the waste heat generator to generate refrigerant steam. condenser.
所述的太阳能辅助直燃式冷热水机组其特征是:从吸收器出来的稀溶液经过低温溶液热交换器后分为三路,一路经过高温溶液热交换器去向高压发生器、另两路分别进入低压发生器和余热发生器。最后,三路浓缩后的溶液在低温溶液热交换器前汇合后经热交换器进入吸收器,被稀释后开始新一轮的循环。The solar-assisted direct-fired hot and cold water unit is characterized in that: the dilute solution from the absorber passes through the low-temperature solution heat exchanger and is divided into three paths, one path goes through the high-temperature solution heat exchanger to the high-pressure generator, and the other two paths Enter the low pressure generator and waste heat generator respectively. Finally, the three-way concentrated solutions are combined in front of the low-temperature solution heat exchanger, and then enter the absorber through the heat exchanger, and start a new round of circulation after being diluted.
有益效果Beneficial effect
本实用太阳能辅助直燃式冷热水机组由于使用了更加优化的循环系统,一方面能充分利用低品位的太阳能将低温热源运用于吸收式空调冷热水机组中;另一方面余热发生器和太阳能集热器的同时使用可以在减少燃料消耗的同时,提高能源利用效率。既降低了常规双效直燃式循环的排烟温度,又使得单纯使用太阳能集热器的吸收式空调易受天气影响的不稳定性得到克服。提高了一次能源效率PER,从而降低运行费用,适用范围广。Due to the use of a more optimized circulation system in this practical solar-assisted direct-fired hot and cold water unit, on the one hand, it can make full use of low-grade solar energy to apply low-temperature heat sources to absorption air-conditioning cold and hot water units; on the other hand, the waste heat generator and The simultaneous use of solar thermal collectors can reduce fuel consumption while increasing energy efficiency. It not only reduces the exhaust gas temperature of the conventional double-effect direct-fired cycle, but also overcomes the instability of the absorption air conditioner that only uses solar collectors and is easily affected by the weather. The primary energy efficiency PER is improved, thereby reducing operating costs and having a wide range of applications.
附图说明 Description of drawings
图1太阳能辅助直燃式冷热水机组原理图。Fig. 1 Schematic diagram of solar-assisted direct-fired hot and cold water unit.
具体实施方式 Detailed ways
下面结合具体实施例,进一步阐述本实用。应理解,这些实施例仅用于说明本实用而不用于限制本实用的范围。此外应理解,在阅读了本实用讲授的内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。Below in conjunction with specific embodiment, further set forth the utility model. It should be understood that these embodiments are only used to illustrate the present invention but not to limit the scope of the present invention. In addition, it should be understood that after reading the contents of this practical teaching, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of this application.
实施例1Example 1
如图1所示,太阳能辅助直燃式冷热水机组主要由:高压发生器1、气水换热器2、余热发生器3、烟气管4、太阳能集热器5、低压发生器6、冷凝器7、吸收器8、蒸发器9、冷却塔10、冷却(加热)盘管11、低温溶液热交换器12、高温溶液热交换器13以及阀门和泵组成。As shown in Figure 1, the solar-assisted direct-fired hot and cold water unit is mainly composed of: high-pressure generator 1, air-water heat exchanger 2, waste heat generator 3, flue gas pipe 4, solar collector 5, and low-
利用太阳能集热器5初步加热循环太阳能水,将升温后的太阳能热水通入到气水换热器2中,使得太阳能热水和烟气充分换热后通入到余热发生器3中,余热回路中降温后的热水再回流到太阳能集热器重复循环,废气由烟气管4排出。从吸收器8出来的稀溶液经过低温溶液热交换器12后分为三路,一路经过高温溶液热交换器13去向高压发生器1、另两路分别进入低压发生器6和余热发生器3。溶液在高压发生器1内受热浓缩,高压发生器1产生的蒸汽进入低压发生器6作为低温热源,加热其中的溶液后进入冷凝器7冷凝,低压发生器6产生的蒸汽直接进入冷凝器7冷凝,第三路溶液进入余热发生器3进一步利用烟气和太阳能中的热量,产生的蒸汽也进入冷凝器7。最后,三路浓缩后的溶液在低温溶液热交换器12前汇合后经热交换器换热:制冷时,阀门14关闭、15开启,自低温溶液热交换器12流出的浓溶液进入吸收器8吸收来自蒸发器9的冷剂蒸汽,被稀释后开始新一轮的循环,同时由冷却塔10、冷凝器7和吸收器8组成的冷却水回路将向大气环境排放空调热负荷和吸收式制冷循环的补偿热能,由蒸发器9和冷却盘管组成的冷水回路完成为冷却(加热)盘管11提供冷量。制热时,阀门14开启、15关闭,自低温溶液热交换器12流出的浓溶液直接被来自冷凝器7的冷剂水稀释,冷凝器7、吸收器8与冷却塔10脱开和加热盘管连接构成热水回路,即将冷却水回路切换成热水回路完成为冷却(加热)盘管11提供热量。Utilize the solar heat collector 5 to preliminarily heat and circulate solar water, and pass the heated solar hot water into the air-water heat exchanger 2, so that the solar hot water and flue gas are fully exchanged and then passed into the waste heat generator 3, The cooled hot water in the waste heat circuit returns to the solar heat collector for repeated circulation, and the exhaust gas is discharged from the flue gas pipe 4. The dilute solution from the
太阳能辅助直燃式冷热水机组由于使用了双效循环加余热回路驱动的单效循环提高了能源利用效率,同时由于清洁能源太阳能的使用使得能源消耗进一步减少,计算数据表明,该循环系统可较常规双效直燃机的一次能源效率PER提高9%,同时可以使得烟气排放温度降低到120℃,节能效果明显。The solar-assisted direct-fired hot and cold water unit uses a double-effect cycle plus a single-effect cycle driven by a waste heat circuit to improve energy utilization efficiency. At the same time, due to the use of clean energy solar energy, energy consumption is further reduced. Calculation data show that the cycle system can Compared with the conventional double-effect direct-fired engine, the primary energy efficiency PER is increased by 9%, and at the same time, the flue gas discharge temperature can be reduced to 120°C, and the energy-saving effect is obvious.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102080898A (en) * | 2011-02-22 | 2011-06-01 | 王红斌 | Lithium bromide absorbing evaporative condensing water chilling unit |
| CN105571204A (en) * | 2016-03-01 | 2016-05-11 | 中节能先导城市节能有限公司 | Direct-fired machine and solar energy coupled full-automatic cooling, heating and hot water supplying system |
| CN107631517A (en) * | 2017-09-06 | 2018-01-26 | 同方节能装备有限公司 | A kind of flue gas flashes back formula direct combustion type heat pump |
| CN109631393A (en) * | 2018-11-28 | 2019-04-16 | 山西大学 | The double-effect lithium bromide absorption type refrigerating plant of fume afterheat and solar energy coupling driving |
| CN113503657A (en) * | 2021-06-17 | 2021-10-15 | 燕山大学 | Solar auxiliary heat pump system integrating waste heat recovery and self-cleaning functions |
| CN113739248A (en) * | 2021-07-26 | 2021-12-03 | 浙江大学 | A solar heat collector system for waste heat recovery and utilization of small and micro data centers |
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2008
- 2008-05-04 CN CNU2008200579993U patent/CN201203297Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102080898A (en) * | 2011-02-22 | 2011-06-01 | 王红斌 | Lithium bromide absorbing evaporative condensing water chilling unit |
| CN105571204A (en) * | 2016-03-01 | 2016-05-11 | 中节能先导城市节能有限公司 | Direct-fired machine and solar energy coupled full-automatic cooling, heating and hot water supplying system |
| CN107631517A (en) * | 2017-09-06 | 2018-01-26 | 同方节能装备有限公司 | A kind of flue gas flashes back formula direct combustion type heat pump |
| CN109631393A (en) * | 2018-11-28 | 2019-04-16 | 山西大学 | The double-effect lithium bromide absorption type refrigerating plant of fume afterheat and solar energy coupling driving |
| CN113503657A (en) * | 2021-06-17 | 2021-10-15 | 燕山大学 | Solar auxiliary heat pump system integrating waste heat recovery and self-cleaning functions |
| CN113503657B (en) * | 2021-06-17 | 2022-03-22 | 燕山大学 | A solar-assisted heat pump system with integrated waste heat recovery and self-cleaning functions |
| CN113739248A (en) * | 2021-07-26 | 2021-12-03 | 浙江大学 | A solar heat collector system for waste heat recovery and utilization of small and micro data centers |
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