CN108278918A - Organic medium-temperature phase-change heat storage material - Google Patents
Organic medium-temperature phase-change heat storage material Download PDFInfo
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- 238000005338 heat storage Methods 0.000 title claims abstract description 25
- 239000011232 storage material Substances 0.000 title claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims abstract description 18
- 239000000463 material Substances 0.000 claims abstract description 16
- 238000010521 absorption reaction Methods 0.000 claims abstract description 14
- 150000001875 compounds Chemical class 0.000 claims abstract description 12
- 150000002894 organic compounds Chemical class 0.000 claims abstract description 10
- 238000005057 refrigeration Methods 0.000 claims abstract description 5
- 239000012782 phase change material Substances 0.000 claims description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- 230000002123 temporal effect Effects 0.000 claims description 2
- 230000009466 transformation Effects 0.000 claims 3
- 239000002918 waste heat Substances 0.000 claims 3
- 238000009825 accumulation Methods 0.000 claims 1
- 230000004927 fusion Effects 0.000 claims 1
- 239000003507 refrigerant Substances 0.000 claims 1
- 230000008859 change Effects 0.000 abstract description 26
- 239000012071 phase Substances 0.000 abstract description 17
- 239000012074 organic phase Substances 0.000 abstract description 12
- 239000002440 industrial waste Substances 0.000 abstract description 11
- 238000002844 melting Methods 0.000 abstract description 6
- 230000008018 melting Effects 0.000 abstract description 6
- 238000007711 solidification Methods 0.000 abstract description 3
- 230000008023 solidification Effects 0.000 abstract description 3
- 230000005611 electricity Effects 0.000 abstract description 2
- 238000004146 energy storage Methods 0.000 description 5
- 239000011521 glass Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 230000007704 transition Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 238000000113 differential scanning calorimetry Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000013529 heat transfer fluid Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/02—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
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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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
-
- 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
- Y02E70/00—Other energy conversion or management systems reducing GHG emissions
- Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Central Heating Systems (AREA)
Abstract
本发明公布了一种有机化合物作为相变储热材料的用途,该化合物储热时的熔化温度为134~136℃,放热时的凝固温度为111~134℃;相变储热密度为130~136J/g,该有机相变材料吸收并储存热能时,热源温度应该控制在136~160℃范围内。该有机相变材料可以储存源自太阳能、工业余废热或利用电网谷期电能制热而获得的热能,并将储存的热能用于建筑物室内供热或驱动吸收式制冷机制冷,以解决热能供给与使用在空间或时间上的不匹配问题,提高能源的利用效率。The present invention discloses the use of an organic compound as a phase change heat storage material. The melting temperature of the compound during heat storage is 134-136°C, and the solidification temperature during heat release is 111-134°C; the phase change heat storage density is 130-136 J/g, and when the organic phase change material absorbs and stores heat energy, the heat source temperature should be controlled within the range of 136-160°C. The organic phase change material can store heat energy obtained from solar energy, industrial waste heat, or heating using off-peak electricity from the power grid, and the stored heat energy can be used for indoor heating of buildings or for driving absorption refrigeration to solve the problem of mismatch between heat energy supply and use in space or time, and improve energy utilization efficiency.
Description
技术领域technical field
本发明涉及一种有机化合物作为相变储热材料的用途,具体地说是利用一种有机化合物通过相转变吸收或释放大量热能,解决热能供给与使用在空间或时间上的不匹配问题,提高能源的利用效率。The invention relates to the use of an organic compound as a phase-change heat storage material, specifically, using an organic compound to absorb or release a large amount of heat energy through phase transition, so as to solve the problem of mismatch between heat energy supply and use in space or time, and improve Energy efficiency.
背景技术Background technique
当前化石能源高昂的价格以及日益严重的环境问题,使人们越来越重视清洁能源的开发利用和能源的高效利用。其中,太阳能是清洁能源的杰出代表,而工业余(废)热回收利用以及电网调峰填谷则是提高能源利用效率的有效手段。The current high price of fossil energy and increasingly serious environmental problems make people pay more and more attention to the development and utilization of clean energy and the efficient use of energy. Among them, solar energy is an outstanding representative of clean energy, while industrial waste (waste) heat recovery and power grid peak-shaving and valley-filling are effective means to improve energy utilization efficiency.
通过光-热转换开发利用太阳能,也就是太阳能热利用,具有转化效率高,无污染的优点。但是太阳辐射存在波动,同时通过太阳能热利用产热与热能的使用之间通常存在时间或空间上的差异,因此必须解决热能存储的问题。热能是人们利用最多的能源形式,人们的生产生活中,许多活动或过程都要利用热能。工业余废热具有温度较高,热能品位高,热能产生量大的特点。因此,实现工业余废热回收利用是实现热能高效利用的重要手段。但是通常工业余废热的产生与热能的利用也存在时间或空间上的不匹配,因此,也要解决热能存储的问题。此外,电力系统运行时在使用端总是存在着周期性的波动,将谷期电网提供的电能转换成热能存储起来供用电峰期时使用不仅可以产生巨大的经济效益,也有利于电网平稳运行。因此,热能的存储是开发新能源,提高能源利用效率的重要手段。而相变储热材料是解决热能存储问题的首选。The development and utilization of solar energy through light-to-heat conversion, that is, solar thermal utilization, has the advantages of high conversion efficiency and no pollution. However, there are fluctuations in solar radiation, and there are usually temporal or spatial differences between heat production by solar thermal utilization and the use of thermal energy, so the problem of thermal energy storage must be solved. Heat energy is the energy form that people use most. In people's production and life, many activities or processes need to use heat energy. Industrial waste heat has the characteristics of high temperature, high heat energy grade and large heat energy generation. Therefore, realizing the recovery and utilization of industrial waste heat is an important means to realize the efficient utilization of heat energy. However, there is usually a mismatch in time or space between the generation of industrial waste heat and the utilization of heat energy. Therefore, the problem of heat energy storage must also be solved. In addition, when the power system is running, there are always periodic fluctuations at the user end. Converting the electric energy provided by the power grid during the valley period into heat energy and storing it for use during the peak period of power consumption can not only generate huge economic benefits, but also contribute to the stability of the power grid. run. Therefore, thermal energy storage is an important means to develop new energy sources and improve energy utilization efficiency. Phase change heat storage materials are the first choice to solve the problem of thermal energy storage.
吸收式制冷是通过热能驱动制冷机工作以获得冷能。通过太阳光-热转换、工业余废热回收以及电网调峰谷获得的热能均能用来驱动吸收式制冷机工作,但其前提条件是热源温度需在80℃以上,而且在一定范围内,热源温度越高,制冷机工作效率越高。要实现这一目标,首先要求从相变储热材料中提取的热能温度要高于这一温度,因此要求相变储热材料的放热相变温度要高于80℃。由于这一温度非常接近水的沸点,且双效吸收式制冷机要求的热源温度还要更高,导致可选择的相变储热材料非常有限。如常见的水合盐相变材料会因失水而失效;具有合适相变温度的有机相变材料种类也非常少。因此,非常有必要寻找新的具有合适相变温度和良好储热能力的相变储热材料,以满足新能源开发及提高能源利用效率的需求。Absorption refrigeration uses thermal energy to drive a refrigerator to work to obtain cold energy. The heat energy obtained through solar-to-heat conversion, industrial waste heat recovery, and power grid peak-shaving valleys can all be used to drive the absorption chiller, but the prerequisite is that the temperature of the heat source must be above 80°C, and within a certain range, the heat source The higher the temperature, the more efficiently the refrigerator works. To achieve this goal, it is first required that the temperature of the heat energy extracted from the phase change heat storage material be higher than this temperature, so the exothermic phase change temperature of the phase change heat storage material is required to be higher than 80 °C. Since this temperature is very close to the boiling point of water, and the heat source temperature required by the double-effect absorption refrigerator is even higher, the choice of phase change heat storage materials is very limited. For example, common hydrated salt phase-change materials will fail due to dehydration; there are very few types of organic phase-change materials with suitable phase-change temperatures. Therefore, it is very necessary to find new phase change heat storage materials with suitable phase change temperature and good heat storage capacity to meet the needs of new energy development and energy utilization efficiency improvement.
发明内容Contents of the invention
本发明的目的是提供一种有机化合物作为相变储热材料在热能存储领域的应用。该化合物可通过相变来储存或释放热能,解决热能供给与使用在空间或时间上不匹配的问题,提高能源的利用效率。The object of the present invention is to provide an application of an organic compound as a phase change heat storage material in the field of thermal energy storage. The compound can store or release heat energy through phase change, solve the problem of mismatching heat energy supply and use in space or time, and improve energy utilization efficiency.
为达到上述目的,本发明采用如下技术方案:一种有机化合物作为相变储热材料的用途。该化合物分子具有如下结构:;该化合物可通过相变来储存或释放热能;该化合物储热时的熔化温度为134~139℃,放热时的凝固温度为111~134℃;相变储热密度为130~136 J/g,该化合物在固态时-75 ~125℃之间的热容与温度之间的关系为:,在液态时140 ~160℃之间的热容与温度之间的关系为:, 上两式中C p (s)和C p (l)分别为固态和液态时的热容,单位为J/(℃·g),T为温度,单位为℃;该化合物用作相变储热材料吸收并储存热能时,热源温度应该在140~160℃范围内。In order to achieve the above object, the present invention adopts the following technical solution: the use of an organic compound as a phase change heat storage material. The compound molecule has the following structure: ; The compound can store or release thermal energy through phase transition; the melting temperature of the compound is 134~139°C when storing heat, and the solidification temperature is 111~134°C when exothermic; the heat storage density of phase change is 130~136 J/ g, the relationship between the heat capacity and temperature of the compound in the solid state between -75 and 125°C is: , the relationship between heat capacity and temperature between 140 ~ 160 ℃ in liquid state is: , C p ( s ) and C p ( l ) in the above two formulas are the heat capacity of solid and liquid respectively, the unit is J/(℃·g), T is the temperature, the unit is ℃; this compound is used for phase transition When the heat storage material absorbs and stores heat energy, the temperature of the heat source should be in the range of 140~160°C.
该有机相变材料可以储存源自太阳能、工业余废热或利用电网谷期电能制热而获得的热能,并将储存的热能用于建筑物室内供热或驱动吸收式制冷机制冷。The organic phase-change material can store heat energy obtained from solar energy, industrial waste heat, or electricity heating during off-peak periods of the power grid, and use the stored heat energy for indoor heating of buildings or to drive absorption refrigerators for cooling.
所述有机相变材料储存源自太阳能、工业余废热或利用电网谷期电能制热而获得的热能时,是将相变材料置于一定容器内,再将盛有相变材料的容器与太阳能集热器、工业余废热热源或电加热器直接接触以加热相变材料使之熔化,或通过传热工质将热能从太阳能集热器、工业余废热热源或电加热器传递给容器内的相变材料并加热相变材料使之熔化等方法来实现,所述传热工质可以是水蒸汽或导热油。When the organic phase-change material stores heat energy obtained from solar energy, industrial waste heat, or heating by using electric energy in the off-peak period of the power grid, the phase-change material is placed in a certain container, and then the container containing the phase-change material is combined with the solar energy. Heat collectors, industrial waste heat sources or electric heaters are in direct contact to heat the phase change material to melt, or transfer heat energy from solar collectors, industrial waste heat sources or electric heaters to the container through heat transfer fluid phase change material and heating the phase change material to melt it, etc., the heat transfer medium can be water vapor or heat conduction oil.
所述将相变材料储存的热能用于建筑物室内供热或驱动吸收式制冷机制冷时,需使用传热工质将热能从相变材料输送给室内加热器或吸收式制冷机,所述工质可以是水或导热油;当使用水作为传热工质时,经过相变材料加热的热水也可直接作为生活热水使用。When the thermal energy stored in the phase change material is used for indoor heating of a building or to drive an absorption refrigerator for cooling, it is necessary to use a heat transfer medium to transfer the heat energy from the phase change material to the indoor heater or the absorption refrigerator. The working medium can be water or heat transfer oil; when water is used as the heat transfer working medium, the hot water heated by the phase change material can also be directly used as domestic hot water.
所述将相变材料储存的热能通过工质传热用于建筑物室内供热或驱动吸收式制冷机制冷时,经相变储热材料加热后的工质温度可在加热前工质温度到130℃的范围内连续可调。When the thermal energy stored by the phase change material is used for heating in the building or driving an absorption refrigerator to cool through the heat transfer of the working medium, the temperature of the working medium heated by the phase change heat storage material can be reached before heating. Continuously adjustable within the range of 130°C.
本发明具有如下优点。The present invention has the following advantages.
本发明提供了将一种有机化合物作为相变储热材料储存源自太阳能、工业余废热及电网谷期电能的热能的用途。该有机相变储热材料具有合适的吸放热温度、较高的储热能力和良好的长期使用稳定性。该有机相变储热材料存储的热能可用作驱动吸收式制冷机工作的热源或直接作为室内生活热源。The invention provides the application of using an organic compound as a phase-change heat storage material to store heat energy derived from solar energy, industrial waste heat and power grid valley period electric energy. The organic phase change heat storage material has suitable heat absorption and release temperature, high heat storage capacity and good long-term use stability. The heat energy stored by the organic phase change heat storage material can be used as a heat source for driving an absorption refrigerating machine or directly as an indoor living heat source.
具体实施方式Detailed ways
下面结合具体实施例对本发明作进一步详细描述,下述实施例中,以电加热器直接加热相变储热材料模拟各种类型的热源为相变储热材料提供热能,但这些实施例并不限制本发明的范围。The present invention will be described in further detail below in conjunction with specific examples. In the following examples, various types of heat sources are used to directly heat the phase-change heat storage material with an electric heater to simulate providing thermal energy for the phase-change heat storage material, but these examples do not limit the scope of the invention.
实施例1。Example 1.
取约5mg有机相变材料,在TA Q2000差示扫描量热仪上,以10℃/min的升温速度,从室温到150℃进行差示扫描量热,测得该有机相变材料的熔点为137 ~139℃,熔化焓约为136 J/g;取约5mg有机相变材料,在TA Q2000差示扫描量热仪上,以10℃/min的升降温速度,在50℃到150℃范围进行50次循环差示扫描量热,测得该有机相变材料的熔点一直稳定在134 ~139℃范围内,凝固温度在111~134℃范围内,熔化焓一直稳定在130~136 J/g范围内。Take about 5 mg of organic phase change material, and carry out differential scanning calorimetry on TA Q2000 differential scanning calorimeter at a heating rate of 10 °C/min from room temperature to 150 °C, and the melting point of the organic phase change material is measured as 137 ~ 139°C, the melting enthalpy is about 136 J/g; take about 5mg of organic phase change material, on the TA Q2000 differential scanning calorimeter, at a heating rate of 10°C/min, in the range of 50°C to 150°C After 50 cycles of differential scanning calorimetry, the melting point of the organic phase change material has been stable in the range of 134-139°C, the solidification temperature has been in the range of 111-134°C, and the melting enthalpy has been stable in the range of 130-136 J/g. within range.
实施例2。Example 2.
将外径为5mm,壁厚0.3mm的铜管弯制成管间距为5mm,圆盘直径为4.5 cm,共4层圆盘构成的盘管,将盘管放入周围被1cm厚的石棉材料包裹的150mL直型玻璃杯中,再加入100g有机相变材料,将盘管埋入,再将杯口用保温材料盖住,盘管的端口升出盖子2cm再与耐热胶管连接;控制电加热器的温度为140℃,从底部加热玻璃杯,使有机相变材料全部熔化,停止加热,往盘管中通入25℃的自来水,控制水的流量,可控制出口水温度为60℃。Bending a copper tube with an outer diameter of 5mm and a wall thickness of 0.3mm into a coil tube with a tube spacing of 5mm and a disc diameter of 4.5 cm, a total of 4 layers of discs, and put the coil tube into a 1cm-thick asbestos material around it Add 100g of organic phase change material to the wrapped 150mL straight glass, bury the coil, cover the mouth of the cup with insulation material, lift the end of the coil 2cm out of the cover and connect it to the heat-resistant rubber hose; The temperature of the heater is 140°C. Heat the glass from the bottom to melt all the organic phase change materials. Stop heating and feed tap water at 25°C into the coil to control the flow of water. The outlet water temperature can be controlled to 60°C.
实施例3。Example 3.
将实施例2中的电加热器温度控制为160℃,从底部加热玻璃杯,使有机相变材料全部熔化,停止加热,往盘管中通入25℃的导热油,控制油的流量,可控制出口油温度为110℃。Control the temperature of the electric heater in Example 2 to 160°C, heat the glass from the bottom to completely melt the organic phase change material, stop heating, and pass heat conduction oil at 25°C into the coil to control the flow of the oil. Control the outlet oil temperature to 110°C.
实施例4。Example 4.
将实施例2中的电加热器温度控制为160℃,从底部加热玻璃杯,使有机相变材料全部熔化,停止加热,往盘管中通入25℃的导热油,控制油的流量,可使出口油温度逐渐升高到130℃,并稳定在此温度。Control the temperature of the electric heater in Example 2 to 160°C, heat the glass from the bottom to completely melt the organic phase change material, stop heating, and pass heat conduction oil at 25°C into the coil to control the flow of the oil. Make the outlet oil temperature gradually rise to 130°C and stabilize at this temperature.
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110749226A (en) * | 2019-11-28 | 2020-02-04 | 兰州理工大学 | A solid-liquid phase variable heat storage device with built-in movable heat exchanger and using method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102620336A (en) * | 2012-04-05 | 2012-08-01 | 镇江新梦溪能源科技有限公司 | Heat accumulation type solar heating tank |
CN204574560U (en) * | 2015-03-18 | 2015-08-19 | 广州虹能节能技术有限公司 | A kind of Engineering-type energy-saving solar energy-storage system |
CN205718000U (en) * | 2016-06-24 | 2016-11-23 | 连云港聚天利新能源有限公司 | A kind of solar water heater system |
-
2018
- 2018-01-16 CN CN201810037767.XA patent/CN108278918A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102620336A (en) * | 2012-04-05 | 2012-08-01 | 镇江新梦溪能源科技有限公司 | Heat accumulation type solar heating tank |
CN204574560U (en) * | 2015-03-18 | 2015-08-19 | 广州虹能节能技术有限公司 | A kind of Engineering-type energy-saving solar energy-storage system |
CN205718000U (en) * | 2016-06-24 | 2016-11-23 | 连云港聚天利新能源有限公司 | A kind of solar water heater system |
Non-Patent Citations (3)
Title |
---|
SOLABANNAVAR, S. B.: "Heck reaction in aqueous medium using Amberlite IRA-400", 《GREEN CHEMISTRY》 * |
刘坚: "《储能技术应用潜力与经济性研究》", 30 September 2016 * |
王如竹等: "《绿色建筑能源系统》", 31 October 2013 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110749226A (en) * | 2019-11-28 | 2020-02-04 | 兰州理工大学 | A solid-liquid phase variable heat storage device with built-in movable heat exchanger and using method |
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