CN103017368A - Phase-change heat transfer type intermediate temperature heat reservoir as well as manufacturing and application thereof - Google Patents

Phase-change heat transfer type intermediate temperature heat reservoir as well as manufacturing and application thereof Download PDF

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CN103017368A
CN103017368A CN2012105526461A CN201210552646A CN103017368A CN 103017368 A CN103017368 A CN 103017368A CN 2012105526461 A CN2012105526461 A CN 2012105526461A CN 201210552646 A CN201210552646 A CN 201210552646A CN 103017368 A CN103017368 A CN 103017368A
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刘振华
陈彦君
赵峰
肖红升
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SUNSHORE SOLAR ENERGY CO Ltd
Shanghai Jiao Tong University
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Shanghai Jiao Tong University
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/02Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E70/00Other energy conversion or management systems reducing GHG emissions
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Abstract

本发明公开了一种相变换热型中温储热器及其构成的中温太阳能空调系统,该相变换热型中温储热器为一封闭耐压容器,包括箱体、多个圈架、筛网、蓄热堆积层和换热管,多个圈架分别水平地固定于箱体下部的内壁上,多个筛网分别放置于各圈架上,蓄热堆积层分别铺设于各筛网上,该蓄热堆积层由复合相变储热材料和沙粒混合而成,换热管设置于箱体上部的内腔中,该换热管的管腔与箱体的内部隔绝且与箱体外部相通,其中流动有导热工质,所述中温储热器使用水和水蒸气作为其相变传热工质,该相变传热工质直接在颗粒状复合相变储热材料表面蒸发或冷凝实现相变换热。本发明具有换热能力优异、太阳能热利用率高、结构简单、制造容易和使用寿命长的优点。

Figure 201210552646

The invention discloses a phase-change heat storage type medium-temperature heat storage device and a medium-temperature solar air-conditioning system composed of the phase-change heat storage type medium-temperature heat storage device. The screen, heat storage accumulation layer and heat exchange tubes, multiple hoops are fixed horizontally on the inner wall of the lower part of the box, multiple screens are respectively placed on each hoop, and the heat storage accumulation layer is laid on each screen respectively , the heat storage accumulation layer is made of composite phase change heat storage material and sand, the heat exchange tube is arranged in the inner cavity of the upper part of the box body, the tube cavity of the heat exchange tube is isolated from the inside of the box body and is separated from the outside of the box body The medium-temperature heat storage device uses water and water vapor as its phase-change heat-transfer medium, and the phase-change heat-transfer medium evaporates or condenses directly on the surface of the granular composite phase-change heat storage material Realize phase change heat. The invention has the advantages of excellent heat exchange capacity, high utilization rate of solar heat, simple structure, easy manufacture and long service life.

Figure 201210552646

Description

一种相变换热型中温储热器及其制造和应用A phase-change heat type medium-temperature heat storage device and its manufacture and application

技术领域technical field

本发明涉及一种太阳能利用设备,具体涉及一种相变换热型中温储热器及其制造和应用,属于能源技术领域。The invention relates to a solar energy utilization device, in particular to a phase-change heat type medium-temperature heat storage device and its manufacture and application, belonging to the field of energy technology.

背景技术Background technique

太阳能是一种清洁、环保、高效和永不衰竭的新能源,太阳能热利用产品市场巨大,所以各个国家都将太阳能资源利用作为可持续发展战略的重要内容。目前,在太阳能热利用当中,太阳能热水器的技术已相对成熟,但是仍然有些不尽如人意的地方。例如,这些热水器大多都只能提供80度以下的低温热水用于日常生活,而不能提供工业所需要的水温达到一百多度的高温空气或水蒸气。Solar energy is a clean, environmentally friendly, efficient and inexhaustible new energy. The market for solar heat utilization products is huge, so all countries regard the utilization of solar energy resources as an important part of sustainable development strategies. At present, among solar thermal utilization, the technology of solar water heater is relatively mature, but there are still some unsatisfactory places. For example, most of these water heaters can only provide low-temperature hot water below 80 degrees for daily life, but cannot provide high-temperature air or steam that the water temperature required by industry reaches more than one hundred degrees.

太阳能空调系统是太阳能热利用的一个极有前途的领域,目前已有很多样板性工程运行,也有大量系统专利提出。为了实现阴雨天和夜间也能利用太阳能制冷,太阳能空调系统必须带有完整的储热换热系统,但目前尚没有带有储热换热器的太阳能空调系统在实际运行,其主要原因是现在的太阳能空调系统的太阳能集热器只能将水加热到接近90℃上下,然后热水直接进入溴化锂吸收式制冷机,而溴化锂吸收式制冷机热源工质的温度最低为80℃,如果要使用储热器的储热/放热过程来为溴化锂吸收式制冷机提供热源工质80℃以上的热水,现有的集热器或储热器都无法完成这一任务。目前国内外虽然已经有很多太阳能储热技术的实验研究、工程技术开发和专利,并且使用的储热材料也种类繁多,但是他们多集中于太阳能低温热水储热,而在100℃至200℃区间的太阳能储热应用寥寥无几。此外,已有的各类储热器在结构和储热放热原理方面大致相同:一类方法是在致密性的储热材料内埋设传热管道,通过储热材料和管路间导热方式吸热/放热;另一类是将致密性的储热材料封闭在各种管道和容器中,管道和容器沉浸在换热工质中。这些储热器的性能直接与储热材料的导热系数有关,因为现在储热材料几乎都是低导热系数材料,虽然已经采用各种技术强化储热材料导热系数以及改变换热管道布置方式,但是目前各类储热换热器的换热性能都不高。对于此类储热器,提高储热材料导热系数现在依然是一个研究重点。一般的方法是将储热材料填充进各类泡沫金属或石墨材料组成一种致密性复合储热材料,这类复合相变储热材料研究和专利目前是储热材料技术专利的主流。Solar air-conditioning system is a very promising field of solar heat utilization. At present, many model projects have been operated, and a large number of system patents have been proposed. In order to use solar energy for cooling in rainy days and at night, the solar air-conditioning system must have a complete heat storage and heat exchange system. The solar collector of the solar air-conditioning system can only heat the water to about 90°C, and then the hot water directly enters the lithium bromide absorption refrigerator, and the temperature of the heat source working fluid of the lithium bromide absorption refrigerator is at least 80°C, if you want to use The heat storage/heat release process of the heat storage device is used to provide hot water with a heat source working medium above 80°C for the lithium bromide absorption refrigerator, and the existing heat collectors or heat storage devices cannot complete this task. At present, although there have been many experimental researches, engineering technology developments and patents on solar heat storage technology at home and abroad, and there are various types of heat storage materials used, most of them focus on solar low-temperature hot water heat storage, and at 100°C to 200°C There are very few solar heat storage applications in the interval. In addition, the existing types of heat storage devices are roughly the same in terms of structure and heat storage and release principles: one method is to bury heat transfer pipes in dense heat storage materials, and absorb heat through heat conduction between the heat storage materials and the pipes. Heat/exothermic; the other is to seal the dense heat storage material in various pipes and containers, and the pipes and containers are immersed in the heat exchange working medium. The performance of these heat storage devices is directly related to the thermal conductivity of the heat storage material, because now the heat storage materials are almost all materials with low thermal conductivity. At present, the heat transfer performance of various heat storage heat exchangers is not high. For this type of heat storage, improving the thermal conductivity of heat storage materials is still a research focus. The general method is to fill heat storage materials into various metal foams or graphite materials to form a dense composite heat storage material. The research and patents of this kind of composite phase change heat storage materials are currently the mainstream of heat storage material technology patents.

在已有的相变换热储热器中,虽然也有利用储热器中传热介质的相变换热传递热量,但是全部储热材料依然是被包裹在密封金属管道或密封金属容器中,密封容器沉浸在传热介质中。储热时,高温热源加热传热介质(液体)产生池内沸腾,热量通过金属壁面进入储热材料,通过储热材料整体的导热在内部传递热量。在放热时,储热材料作为热源,通过整体材料导热将热量通过金属壁面传递到传热介质液体中,液体蒸发再将热量传递给冷源工质。储热材料内部导热依然是主要热阻。另外,储热材料的传热面仅仅是金属包裹容器的壁面表面积。而在本专利究中,相变传热介质直接和颗粒状储热材料填层接触,全部颗粒状储热材料的巨大的表面积都是传热面,单个储热材料颗粒的体积很小,内部导热热阻几乎可以忽略。In the existing phase-change heat accumulators, although the phase-change heat of the heat transfer medium in the heat accumulator is also used to transfer heat, all heat storage materials are still wrapped in sealed metal pipes or sealed metal containers. The sealed container is immersed in the heat transfer medium. When storing heat, the high-temperature heat source heats the heat transfer medium (liquid) to cause boiling in the pool, and the heat enters the heat storage material through the metal wall, and transfers heat inside through the overall heat conduction of the heat storage material. When releasing heat, the heat storage material is used as a heat source, and the heat is transferred to the heat transfer medium liquid through the metal wall through the heat conduction of the whole material, and the liquid evaporates and then transfers the heat to the cold source working medium. The heat conduction inside the heat storage material is still the main thermal resistance. In addition, the heat transfer surface of the heat storage material is only the wall surface area of the metal clad container. However, in this patent study, the phase-change heat transfer medium is directly in contact with the filling layer of granular heat storage materials. The huge surface area of all granular heat storage materials is the heat transfer surface, and the volume of a single heat storage material particle is very small. Thermal conduction resistance is almost negligible.

在现有的相关太阳能集热储热技术文献中发现:公开号为CN201032291的中国专利,名称为:一种太阳能储热单元及其构成的整体式太阳能热水器,其特征在于包括真空集热管和储热组件,储热组件设置在真空集热管内,储热组件又包括封闭管、进水管和出水管。其储热介质为水,属于一种初级的储热技术,但比较有代表性。与其相似的专利中,储热材料可以是各种相变材料,如石蜡,石蜡和其他材料的混合物等,如中国专利公开号:CN201327216,发明名称为:复合能源太阳能相变蓄热供热装置,其主要含有太阳能集热管、相变蓄热体,特点是相变蓄热体置于太阳能集热管内,出水支管置于相变蓄热体中,进水支管置于出水支管内。其所采用的是石蜡类低温固液相变材料。It is found in the existing relevant solar heat collection and heat storage technology literature: the Chinese patent with the publication number CN201032291, the name is: a solar heat storage unit and an integral solar water heater composed of it, which is characterized in that it includes a vacuum heat collection tube and a heat storage The heat storage component is arranged in the vacuum heat collecting tube, and the heat storage component includes a closed tube, a water inlet pipe and a water outlet pipe. The heat storage medium is water, which belongs to a primary heat storage technology, but it is more representative. In similar patents, the heat storage material can be various phase change materials, such as paraffin, a mixture of paraffin and other materials, etc., such as Chinese patent publication number: CN201327216, the name of the invention is: composite energy solar phase change thermal storage heating device , which mainly contains solar heat collector tubes and phase change heat storage bodies, and is characterized in that the phase change heat storage bodies are placed in the solar heat collector tubes, the outlet branch pipes are placed in the phase change heat storage bodies, and the water inlet branch pipes are placed in the water outlet branch pipes. What it adopts is a paraffin low-temperature solid-liquid phase change material.

在现有的相关太阳能空调系统技术文献中发现:中国专利号为200620050140.0,专利名称:太阳能空调系统。该专利由双效吸收式制冷机和太阳能集热系统两大部分组成,而太阳能集热系统又由太阳能集热器、太阳能控制组、管路构成,太阳能集热器为桁架上固定抛物面板和设于抛物境面焦点处的集热管,集热管通过管路、太阳能控制组与双效吸收式制冷机的高温发生器连通。该专利是一种能够在阴天也能提供较高温度热水太阳能空调系统。中国专利号为200920185550.X,专利名称:太阳能空调系统。该太阳能空调系统有采暖和制冷两部分组成,采暖通过太阳能集热器提供热源,由太阳能集热器直接向室内散热器提供热水;而制冷由太阳能光伏电板提供太阳能转变的电力,向蒸发式冷气机供电,由蒸发式冷气机供冷。这两个专利基本代表了目前太阳能空调系统的主流技术,其特点是;集热器集热温度较低,直接提供热水供给制冷机,没有储热器或者只象征性地带有一个低温储热器。It is found in the existing relevant technical literature of solar air-conditioning system: Chinese patent number is 200620050140.0, patent name: solar air-conditioning system. The patent consists of two parts: a double-effect absorption refrigerator and a solar heat collection system, and the solar heat collection system is composed of a solar heat collector, a solar control group, and a pipeline. The solar heat collector is a parabolic panel fixed on a truss and The heat collecting tube arranged at the focal point of the parabolic surface communicates with the high temperature generator of the double-effect absorption refrigerator through the pipeline and the solar control group. This patent is a solar air-conditioning system that can provide higher temperature hot water even on cloudy days. Chinese patent number is 200920185550.X, patent name: solar air conditioning system. The solar air-conditioning system consists of two parts: heating and cooling. The heating provides heat source through the solar collector, and the solar collector directly provides hot water to the indoor radiator; The power supply is provided by the evaporative air conditioner, and the cooling is provided by the evaporative air conditioner. These two patents basically represent the current mainstream technology of solar air-conditioning systems, which are characterized by: the heat collector has a low heat collection temperature, directly provides hot water to the refrigerator, and has no heat storage or only a symbolic low-temperature heat storage device.

此外,已经授权的、由本申请人持有的中国专利,专利号ZL 200910311344.3,发明专利名称:真空管套管组合式两用型太阳能加热器,是一种由CPC集热板和全玻璃真空集热管组成的中温太阳能集热器,该集热器热效率高且稳定,可以在全年提供120℃以上的水蒸气。In addition, the authorized Chinese patent held by the applicant, the patent number ZL 200910311344.3, the name of the invention patent: vacuum tube casing combined dual-purpose solar heater, is a kind of CPC heat collecting plate and all glass vacuum heat collecting tube A medium-temperature solar collector composed of high thermal efficiency and stability, which can provide water vapor above 120°C throughout the year.

发明内容Contents of the invention

本发明针对现有技术的不足,提供一种相变换热型中温储热器,其采用固液相变材料作为储热的中间介质,并利用该中间介质的相变换热传递热量,从而达到提高储热器换热能力、延长使用寿命的效果;本发明还提供一种应用所述相变换热型中温储热器的中温太阳能空调系统以及一种构成所述相变换热型中温储热器的储热材料的制备方法。Aiming at the deficiencies of the prior art, the present invention provides a phase-change heat storage medium-temperature heat storage device, which adopts a solid-liquid phase change material as an intermediate medium for heat storage, and uses the phase-change heat of the intermediate medium to transfer heat, thereby The effect of improving the heat exchange capacity of the heat storage device and prolonging the service life is achieved; the present invention also provides a medium-temperature solar air-conditioning system using the phase-change heat storage type medium-temperature heat storage device and a medium-temperature heat storage system composed of the phase-change heat storage type. A method for preparing a heat storage material for a heat storage device.

本发明是通过以下技术方案实现的:The present invention is achieved through the following technical solutions:

一种相变换热型中温储热器,其为一封闭耐压容器,包括箱体、多个圈架、筛网、蓄热堆积层和换热管,所述多个圈架分别水平地固定于所述箱体下部的内壁上,所述多个筛网分别放置于各圈架上,所述蓄热堆积层分别铺设于各筛网上,该蓄热堆积层由复合相变储热材料和沙粒混合而成,所述换热管设置于箱体上部的内腔中,该换热管的管腔与箱体的内部隔绝且与箱体外部相通,其中流动有导热工质。A phase-change heat storage medium-temperature heat storage device, which is a closed pressure-resistant container, including a box body, a plurality of hoops, screens, heat storage accumulation layers and heat exchange tubes, and the plurality of hoops are horizontally arranged fixed on the inner wall of the lower part of the box, the plurality of screens are respectively placed on each frame, and the heat storage accumulation layer is respectively laid on each screen, and the heat storage accumulation layer is made of composite phase change heat storage material Mixed with sand, the heat exchange tube is arranged in the inner cavity of the upper part of the box body, the tube cavity of the heat exchange tube is isolated from the inside of the box body and communicated with the outside of the box body, and a heat-conducting working medium flows therein.

所述的复合相变储热材料为颗粒状,其由有机膨润土与聚乙烯腊按2.2∶1的质量比组成,或者由有机膨润土与低密度聚乙烯按2∶1的质量比组成。The composite phase change heat storage material is granular, and it is composed of organic bentonite and polyethylene wax in a mass ratio of 2.2:1, or composed of organic bentonite and low-density polyethylene in a mass ratio of 2:1.

所述的相变换热型中温储热器使用水和水蒸气作为其相变传热工质,该相变传热工质直接在颗粒状复合相变储热材料表面蒸发或冷凝实现相变换热;在储热阶段,相变换热型中温储热器是一个开口流动系统,集热器提供的水蒸汽流入该相变换热型中温储热器,通过蓄热堆积层内冷凝放热,水蒸气的冷凝潜热被所述复合相变储热材料吸收储存;在放热阶段,关闭所述相变换热型中温储热器进出口阀门,将原来开放式的相变换热型中温储热器变为封闭空间,所述复合相变储热材料表面附着的水被加热为水蒸气,该水蒸气上升到换热管表面冷凝,加热换热管内导热工质,而水蒸气再次被冷凝成水滴落到蓄热堆积层内;由此循环往复完成所述复合相变储热材料和换热管间的热传递。The phase-change heat-type medium-temperature heat storage device uses water and water vapor as its phase-change heat-transfer working fluid, and the phase-change heat-transfer medium directly evaporates or condenses on the surface of the granular composite phase-change heat storage material to achieve phase change Heat exchange; in the heat storage stage, the phase-change heat storage medium-temperature heat storage is an open flow system, and the water vapor provided by the heat collector flows into the phase-change heat storage medium-temperature heat storage, and is condensed and discharged through the heat storage stack layer. Heat, the latent heat of condensation of water vapor is absorbed and stored by the composite phase-change heat storage material; in the exothermic stage, close the inlet and outlet valves of the phase-change heat storage medium-temperature heat storage, and turn the original open phase-change heat storage The medium-temperature heat storage becomes a closed space, and the water attached to the surface of the composite phase-change heat storage material is heated into water vapor, and the water vapor rises to the surface of the heat exchange tube to condense, heating the heat-conducting working medium in the heat exchange tube, and the water vapor again It is condensed into water droplets and falls into the heat storage accumulation layer; thus, the heat transfer between the composite phase change heat storage material and the heat exchange tube is completed in a cycle.

本发明的另一技术方案如下:Another technical solution of the present invention is as follows:

一种用于所述相变换热型中温储热器的复合相变储热材料的制备方法,其特征在于:将有机膨润土和聚乙烯腊按2.2∶1的质量比配制后放入一有搅拌装置的加热容器内一边加热一边搅拌,加热到160℃后保持该温度搅拌1小时,使溶解的聚乙烯腊全部被有机膨润土吸附,最后得到平均粒径为3mm的颗粒状的复合相变储热材料。A method for preparing a composite phase-change heat storage material for the phase-change heat-type medium-temperature heat storage device, which is characterized in that organic bentonite and polyethylene wax are prepared in a mass ratio of 2.2:1 and then put into an organic Stir while heating in the heating container of the stirring device, heat to 160°C and keep stirring at this temperature for 1 hour, so that all the dissolved polyethylene wax is absorbed by the organic bentonite, and finally a granular composite phase change storage with an average particle size of 3mm is obtained. hot material.

本发明的又一技术方案如下:Another technical solution of the present invention is as follows:

一种由所述的相变换热型中温储热器构成的中温太阳能空调系统,其包括中温太阳能集热器、相变换热型中温储热器、制冷机、回水泵、热水泵和储水箱,所述的中温太阳能集热器为真空管套管组合式两用型太阳能加热器,该中温太阳能集热器的进口通过回水泵与所述储水箱相连接,并且其出口通过水蒸汽阀门与所述相变换热型中温储热器相连接,所述储水箱通过出水阀门与所述相变换热型中温储热器相连接,所述相变换热型中温储热器的换热管一端通过热水泵与制冷机相连接,另一端直接与制冷机相连接。A medium-temperature solar air-conditioning system composed of the phase-change heating type medium-temperature heat storage device, which includes a medium-temperature solar heat collector, a phase-change heat type medium-temperature heat storage device, a refrigerator, a return pump, a hot water pump, and a storage Water tank, the medium-temperature solar heat collector is a vacuum tube casing combined dual-purpose solar heater, the inlet of the medium-temperature solar heat collector is connected to the water storage tank through a return pump, and its outlet is connected to the water storage tank through a water vapor valve. The phase-change heat type medium-temperature heat storage is connected, the water storage tank is connected with the phase-change heat type medium-temperature heat storage through a water outlet valve, and the heat exchange of the phase-change heat type medium-temperature heat storage One end of the pipe is connected to the refrigerator through a hot water pump, and the other end is directly connected to the refrigerator.

与现有通过致密性储热材料导热换热的储热器相比,本发明所述的相变换热型中温储热器吸热和放热过程的热量传递是通过储热器内中间介质的相变变化进行的,其换热原理不是储热材料的热传导,而是通过中间介质的相变换热来传递热量,故而本专利称之为相变换热型中温储热器。因此本发明所述的相变换热型中温储热器能够达到以下有益效果:Compared with the existing heat storage that conducts heat through dense heat storage materials, the heat transfer of the phase-change heat storage medium-temperature heat storage in the present invention is through the intermediate medium in the heat storage. The heat exchange principle is not the heat conduction of the heat storage material, but the heat is transferred through the phase change heat of the intermediate medium, so this patent is called a phase change heat type medium temperature heat storage device. Therefore, the phase-change heat type medium-temperature heat storage device described in the present invention can achieve the following beneficial effects:

(1)相变换热方式不仅本身换热系数高,而且复合相变储热材料表面整体换热面积非常大,能够实现非常高的储热和放热效率,储热材料与换热管路之间的温差可以忽视,两者之间的传热热阻比传统导热型储热材料要低2个数量级,因此本发明所述储热器的换热能力十分优异。(1) The phase change heat method not only has a high heat transfer coefficient, but also has a very large overall heat transfer area on the surface of the composite phase change heat storage material, which can achieve very high heat storage and heat release efficiency. The temperature difference between them can be ignored, and the heat transfer resistance between the two is 2 orders of magnitude lower than that of traditional heat-conducting heat storage materials, so the heat exchange capacity of the heat storage device of the present invention is very excellent.

(2)储热材料是一种复合相变材料,以多孔质颗粒状态放置在储热器中,储热材料的导热性能与储热/放热特性无关,因此储热器对储热材料的导热性能没有特别要求。(2) The heat storage material is a composite phase change material, which is placed in the heat storage in the state of porous particles. The thermal conductivity of the heat storage material has nothing to do with the heat storage/heat release characteristics. There is no special requirement for thermal conductivity.

(3)复合相变储热材料中的聚乙烯腊以纳米级尺度被吸附封存在膨润土的纳米插层中,因此在反复的相变过程中不会出现溢出现象,从而保证了其长期的重复性使用寿命。(3) The polyethylene wax in the composite phase change heat storage material is adsorbed and sealed in the nano-intercalation of bentonite at the nanoscale, so there will be no overflow during the repeated phase change process, thus ensuring its long-term repeated sexual life.

(4)换热管路安装随意,不需任何强化措施,蓄热堆积层安放更换也十分简单,因此具有结构简单、制造容易的优点。(4) The heat exchange pipeline can be installed freely without any strengthening measures, and the placement and replacement of the heat storage accumulation layer is also very simple, so it has the advantages of simple structure and easy manufacture.

本发明所述的中温太阳能空调系统是一种综合高效太阳能真空管集热和颗粒状中温复合固液相变材料蓄热/放热以及相变储热换热器三种技术为一身的用于全天候运行的太阳能空调系统,其特点是:The medium-temperature solar air-conditioning system of the present invention is a combination of high-efficiency solar vacuum tube heat collection and granular medium-temperature composite solid-liquid phase change material heat storage/heat release and phase change heat storage heat exchanger for all-weather use. The running solar air conditioning system is characterized by:

(1)中温太阳能集热器由CPC集热板和普通的全真空玻璃集热管组成,能够提供120℃左右的中温水蒸气作为高品质热源工质。(1) The medium-temperature solar collector is composed of CPC heat collector plate and ordinary full-vacuum glass heat collector tube, which can provide medium-temperature water vapor at about 120°C as a high-quality heat source working fluid.

(2)集热器的蒸汽工质不直接进入制冷机,而是进入储热器放热后冷凝为水再流回集热器,形成一个回路;而制冷机工质通过换热管在储热器内吸热,形成另一个回路,因此两种工质在储热器中形成相隔离的双回路,储热材料和换热管路分别处于相变换热型中温储热器内不同的空间而没有直接接触。(2) The steam working medium of the heat collector does not directly enter the refrigerator, but enters the heat storage device to release heat, condenses into water and then flows back to the heat collector to form a loop; while the working medium of the refrigerator passes through the heat exchange tube in the storage The heat is absorbed in the heat tank to form another circuit, so the two working fluids form a double circuit isolated in the heat storage, and the heat storage material and the heat exchange pipeline are respectively located in different phase-change heat storage medium-temperature heat storage. space without direct contact.

(3)与所述中温太阳能空调制冷系统配套的相变换热型中温储热器能够在白天提供用于太阳能空调的120℃水蒸气,晚上提供110℃左右的水蒸汽,用以加热制冷机用热水,满足了制冷机运行需要;储热器换热性能的提高使集热器工质的温度能够尽可能降低,从而使整个中温太阳能空调系统的太阳能热利用率有了大幅度提高。(3) The phase-change heat storage medium-temperature heat storage device matched with the medium-temperature solar air-conditioning refrigeration system can provide 120°C water vapor for solar air-conditioning during the day, and provide water vapor at about 110°C at night to heat the refrigerator Hot water is used to meet the operation needs of the refrigerator; the improvement of the heat transfer performance of the heat storage device can reduce the temperature of the working medium of the collector as much as possible, thereby greatly improving the solar heat utilization rate of the entire medium-temperature solar air-conditioning system.

附图说明Description of drawings

图1为本发明的相变换热型中温储热器的结构示意图。Fig. 1 is a schematic structural view of a phase-change heat storage medium-temperature heat storage device of the present invention.

图2为本发明的中温太阳能空调系统的结构示意图。Fig. 2 is a structural schematic diagram of the medium-temperature solar air-conditioning system of the present invention.

图中,In the figure,

1中温太阳能集热器,2相变换热型中温储热器,3制冷机,4回水泵,5热水泵,6 储水箱,7 箱体,8 水蒸汽进口,9水蒸汽阀门,10 出水口,11 出水阀门,12换热管,13换热管支撑架,14圈架,15筛网,16蓄热堆积层,17保温材料,18安全阀,19压力表,20温度传感器,21泄水口,22空气充气口,23充气阀门。1 Medium-temperature solar heat collector, 2 Phase-change heat type medium-temperature heat storage, 3 Refrigerator, 4 Return water pump, 5 Hot water pump, 6 Water storage tank, 7 Cabinet, 8 Water vapor inlet, 9 Water vapor valve, 10 Outlet Water outlet, 11 water outlet valve, 12 heat exchange tube, 13 heat exchange tube support frame, 14 ring frame, 15 screen mesh, 16 heat storage accumulation layer, 17 insulation material, 18 safety valve, 19 pressure gauge, 20 temperature sensor, 21 drain Shuikou, 22 air inflation ports, 23 inflation valves.

具体实施方式Detailed ways

下面结合附图对本发明的实施例作详细说明,本实施例以本发明的技术方案为前提下给出了详细的实施方式和具体的操作过程,但本发明的保护范围不限于下述的实施例。The embodiments of the present invention are described in detail below in conjunction with the accompanying drawings. This embodiment provides detailed implementation methods and specific operating procedures on the premise of the technical solutions of the present invention, but the protection scope of the present invention is not limited to the following implementations example.

请参阅图1,图示相变换热型中温储热器2为一不锈钢制的封闭耐压容器,包括箱体7、多个圈架14、筛网15、蓄热堆积层16和换热管12。Please refer to Fig. 1, the illustrated phase-change heat type medium-temperature heat storage device 2 is a closed pressure-resistant container made of stainless steel, including a box body 7, a plurality of hoops 14, a screen 15, a heat storage accumulation layer 16 and a heat exchange Tube 12.

本实施例中,所述箱体7为一直径1.2m,总高1.5m,壁厚3mm的不锈钢圆筒形容器,其外周包裹有保温材料17;该箱体7上方分别设有依次连接的水蒸汽阀门9和水蒸汽进口8,以及依次连接的压力表19、温度传感器20和安全阀18;箱体7下方分别设有泄水口21,以及依次连接的出水阀门11和出水口10;所述箱体7的外壁上还设置有依次连接的进气阀门23和空气充气口22,以便向箱体7内部充入气压为2个大气压的空气以形成压力环境。所述多个圈架14为圆环形,其分别水平地焊接固定于所述箱体7下部的内壁上。所述多个筛网15分别放置于各圈架14上,该筛网15由不锈钢板和200目的不锈钢丝网制成。所述蓄热堆积层16分别铺设于各筛网15上,该蓄热堆积层16是由复合相变储热材料和沙粒混合而成的多孔质堆积层,蒸汽和水可以通过丝网,而蓄热材料却不会泄露出来;该蓄热堆积层16厚度约50mm,其层数根据需要而定。所述换热管12设置于箱体7上部的内腔中,通过固定于箱体7内壁上的换热管支撑架13悬置于蓄热堆积层16的上方;该换热管12的管腔与箱体7的内部隔绝且与箱体7外部相通,其中流动有向制冷机提供的导热工质;换热管12管路的形状、管径和管路长度可根据需要设定。In the present embodiment, the box body 7 is a stainless steel cylindrical container with a diameter of 1.2m, a total height of 1.5m, and a wall thickness of 3mm, and its outer periphery is wrapped with an insulating material 17; The water vapor valve 9 and the water vapor inlet 8, and the pressure gauge 19, the temperature sensor 20 and the safety valve 18 connected in sequence; the water outlet 21 is respectively arranged under the box body 7, and the water outlet valve 11 and the water outlet 10 connected in sequence; The outer wall of the casing 7 is also provided with an air intake valve 23 and an air charging port 22 connected in sequence, so that the inside of the casing 7 is filled with air with a pressure of 2 atmospheres to form a pressure environment. The plurality of hoops 14 are ring-shaped, and are respectively horizontally welded and fixed on the inner wall of the lower part of the box body 7 . The plurality of screens 15 are respectively placed on the frames 14, and the screens 15 are made of stainless steel plate and 200-mesh stainless steel wire mesh. The heat storage accumulation layer 16 is respectively laid on the screens 15. The heat storage accumulation layer 16 is a porous accumulation layer formed by mixing composite phase change heat storage materials and sand grains. Steam and water can pass through the wire mesh, while The heat storage material will not leak out; the heat storage accumulation layer 16 has a thickness of about 50mm, and the number of layers depends on the needs. The heat exchange tube 12 is arranged in the inner cavity of the upper part of the box body 7, and is suspended above the heat storage accumulation layer 16 by the heat exchange tube support frame 13 fixed on the inner wall of the box body 7; the tube of the heat exchange tube 12 The cavity is isolated from the inside of the box body 7 and communicated with the outside of the box body 7, in which the heat-conducting working fluid provided to the refrigerator flows; the shape, diameter and length of the pipeline of the heat exchange tube 12 can be set as required.

所述的复合相变储热材料为颗粒状,其相变温度在110℃,对其导热性能无特殊要求。本实施例中,该复合相变储热材料由有机膨润土与聚乙烯腊按2.2∶1的质量比组成。The composite phase change heat storage material is in granular form, its phase change temperature is 110°C, and there is no special requirement on its thermal conductivity. In this embodiment, the composite phase change heat storage material is composed of organic bentonite and polyethylene wax in a mass ratio of 2.2:1.

所述的相变换热型中温储热器2使用水和水蒸气作为其相变传热工质,该相变传热工质直接在颗粒状复合相变储热材料表面蒸发或冷凝实现相变换热;在储热阶段,相变换热型中温储热器2是一个开口流动系统,集热器提供的水蒸汽流入该相变换热型中温储热器2,通过蓄热堆积层16内冷凝放热,水蒸气的冷凝潜热被所述复合相变储热材料吸收储存;在放热阶段,关闭所述相变换热型中温储热器2的进出口阀门,将原来开放式的相变换热型中温储热器2变为封闭空间,所述复合相变储热材料表面附着的水被加热为水蒸气,该水蒸气上升到换热管12表面冷凝,加热换热管12内的导热工质,而水蒸气再次被冷凝成水滴落到蓄热堆积层16内;由此循环往复完成所述复合相变储热材料和换热管12间的热传递。The phase-change heat-type medium-temperature heat storage device 2 uses water and water vapor as its phase-change heat-transfer working medium, and the phase-change heat-transfer medium directly evaporates or condenses on the surface of the granular composite phase-change heat storage material to realize phase change. Transformation heat; in the heat storage stage, the phase-change heat storage medium-temperature heat storage 2 is an open flow system, and the water vapor provided by the heat collector flows into the phase-change heat storage medium-temperature heat storage 2, and passes through the heat storage accumulation layer Condensation and heat release in 16, the condensation latent heat of water vapor is absorbed and stored by the composite phase change heat storage material; in the heat release stage, the inlet and outlet valves of the phase change heat type medium temperature heat storage 2 are closed, and the original open The phase-change heat storage medium-temperature heat storage device 2 becomes a closed space, and the water attached to the surface of the composite phase-change heat storage material is heated to water vapor, and the water vapor rises to the surface of the heat exchange tube 12 to condense, and the heat exchange tube is heated. 12, and the water vapor is condensed into water droplets again and falls into the heat storage accumulation layer 16; thus, the heat transfer between the composite phase change heat storage material and the heat exchange tube 12 is completed in a cycle.

根据生产厂家的不同聚乙烯蜡有不同的熔点和相变潜热,熔点大致在95℃到118℃之间,如日本产为113℃,韩国产为118℃上下。本专利所用的聚乙烯蜡由国内某厂家提供,表1列出了其商品聚乙烯蜡的物性。聚乙烯蜡在与有机膨润土组合成复合相变储热材料之后物性几乎没有变化。Polyethylene waxes have different melting points and latent heat of phase change according to different manufacturers. The melting point is roughly between 95°C and 118°C, such as 113°C for Japan and 118°C for South Korea. The used polyethylene wax of this patent is provided by a domestic manufacturer, and Table 1 has listed the physical properties of its commodity polyethylene wax. The physical properties of polyethylene wax hardly changed after being combined with organic bentonite to form a composite phase change heat storage material.

表1聚乙烯腊的物理特性Table 1 Physical properties of polyethylene wax

有机膨润土的物性随厂家的不同也有较大变化,但对复合相变储热材料的储热性能本身影响很小。下面给出某厂家生产的有机膨润土的一般物性:比热0.78KJ/(KgK),导热系数0.83W/(mK),密度2g/cm3,表观粘度24mPas,蒙脱石含量≥95%,白度88,膨胀倍数23,硬度2.8,粒度/目数400目,形状白色精细粉末,PH值6-7。The physical properties of organic bentonite also vary greatly with different manufacturers, but it has little effect on the heat storage performance of the composite phase change heat storage material itself. The general physical properties of organic bentonite produced by a certain manufacturer are given below: specific heat 0.78KJ/(KgK), thermal conductivity 0.83W/(mK), density 2g/cm3, apparent viscosity 24mPas, montmorillonite content ≥ 95%, white Degree 88, expansion multiple 23, hardness 2.8, particle size/mesh 400 mesh, shape white fine powder, pH value 6-7.

当有机膨润土与聚乙烯蜡两种材料混合后,复合相变储热材料的熔点、凝固点和相变潜热几乎没有变化。试验发现,在反复加热冷凝3次后,复合相变储热材料的质量溢出率(加热/冷却后的相变材料质量与加热/冷却前的相变材料质量之比)约为3%,此后继续反复加热冷却,质量溢出率几乎为零,显示了本复合相变储热材料优异的可重复使用性能。When organic bentonite and polyethylene wax are mixed, the melting point, freezing point and latent heat of phase change of the composite phase change heat storage material hardly change. The test found that after repeated heating and condensation for 3 times, the mass overflow rate of the composite phase change heat storage material (the ratio of the mass of the phase change material after heating/cooling to the mass of the phase change material before heating/cooling) was about 3%. After repeated heating and cooling, the mass overflow rate is almost zero, which shows the excellent reusability of the composite phase change heat storage material.

上述复合相变储热材料的制备方法如下:将有机膨润土和聚乙烯腊按2.2∶1的质量比配制后放入一有搅拌装置的加热容器内一边加热一边搅拌,加热到160℃后保持该温度搅拌1小时,使溶解的聚乙烯腊全部被有机膨润土吸附,最后得到平均粒径为3mm的颗粒状的复合相变储热材料。对少量大颗粒材料可以用木榔头轻轻敲碎,所述加热温度和材料混合比例对复合相变储热材料表观性能影响很大,需要十分注意。The preparation method of the above-mentioned composite phase-change heat storage material is as follows: prepare organic bentonite and polyethylene wax according to a mass ratio of 2.2:1, put them into a heating container with a stirring device and stir while heating, and keep the temperature after heating to 160°C. The temperature was stirred for 1 hour, so that all the dissolved polyethylene wax was absorbed by the organic bentonite, and finally a granular composite phase change heat storage material with an average particle diameter of 3mm was obtained. A small amount of large-grained materials can be gently crushed with a wooden hammer. The heating temperature and material mixing ratio have a great influence on the apparent performance of the composite phase change heat storage material, so great attention must be paid.

所述储热材料即需要有一定储水性同时又要保证透气性,由于有机膨润土是疏水性材料,因而复合相变储热材料表面是疏水性的。为了增加复合相变储热材料的储水性和透气性,将复合相变储热材料和少量细砂混合后,再次放入加热容器内一边加热一边搅拌,加热到160℃后保持该温度搅拌1小时,绝大部分细沙将粘附在复合相变储热材料颗粒表面上形成亲水表面结构,从而制备成蓄热堆积层16,实验测量后得到的蓄热堆积层16堆放空隙率约为40%。The heat storage material needs to have a certain water storage capacity and at the same time ensure air permeability. Since organic bentonite is a hydrophobic material, the surface of the composite phase change heat storage material is hydrophobic. In order to increase the water storage and air permeability of the composite phase change heat storage material, mix the composite phase change heat storage material with a small amount of fine sand, put it into the heating container again while stirring while heating, and keep stirring at this temperature for 1 hour after heating to 160°C hours, most of the fine sand will adhere to the surface of the composite phase change heat storage material particles to form a hydrophilic surface structure, thereby preparing the heat storage accumulation layer 16. The heat storage accumulation layer 16 obtained after the experimental measurement has a stacking porosity of about 40%.

所述复合相变储热材料也可以由有机膨润土与低密度聚乙烯按2∶1的质量比组成,其制备方法与上述方法类同。The composite phase-change heat storage material can also be composed of organic bentonite and low-density polyethylene in a mass ratio of 2:1, and its preparation method is similar to the above-mentioned method.

所述的相变换热型中温储热器2的工作原理如下:在白天,集热器提供的水蒸汽温度(120℃左右)高于复合相变储热材料相变温度(110℃左右),一部分水蒸气在换热管12外冷凝放热,从而对管道中流过的制冷用热水进行加热,热水在制冷机中循环工作;另外大部分水蒸气在蓄热堆积层16内部冷凝放热,水蒸气的冷凝潜热被复合相变储热材料吸收,复合相变储热材料由固相变为液相。而在夜晚,关闭相变换热型中温储热器2的各进出口阀门,将原来开放式的相变换热型中温储热器2变为封闭空间,此时换热管12中仍然循环流动的制冷用热水不停地从相变换热型中温储热器2中的水蒸气冷凝过程中吸热,相变换热型中温储热器2内水蒸汽不断持续被冷凝成水滴,水蒸气质量减少,相变换热型中温储热器2内蒸汽压力和温度将逐渐下降到复合相变储热材料的相变温度(110℃)以下;在此之后复合相变储热材料开始相变放热(液态变为固态),颗粒状复合相变储热材料表面附着的水被加热为水蒸气,这些水蒸气上升到换热管12表面冷凝,加热换热管12内的流动热水(温度由85℃增加到90℃),而水蒸气再次被冷凝成水滴落到蓄热堆积层16内,如此循环往复,完成复合相变储热材料和换热管12间的热传递。这种换热机理非常类似于热管换热机理。所述相变换热型中温储热器2利用热管换热特性实现了非常高的储热和放热效率,其复合相变储热材料和换热管12之间的传热热阻比储热材料导热换热方式要低1到2个数量级。同时,颗粒状复合相变储热材料充满水和水蒸气,相变换热过程在蓄热堆积层16内各处同时进行,颗粒表面有效传热面积非常大,使得相变换热型中温储热器2的相变传热能力非常优异,复合相变储热材料与换热管12之间的温差几乎可以忽略,复合相变储热材料颗粒内部的温差也几乎可以忽略。The working principle of the phase-change heat storage medium-temperature heat storage device 2 is as follows: during the day, the temperature of the water vapor provided by the heat collector (about 120°C) is higher than the phase change temperature (about 110°C) of the composite phase-change heat storage material A part of the water vapor condenses and releases heat outside the heat exchange tube 12, thereby heating the hot water for cooling flowing through the pipe, and the hot water circulates in the refrigerator; in addition, most of the water vapor condenses and releases heat inside the heat storage accumulation layer 16. Heat, latent heat of condensation of water vapor is absorbed by the composite phase change heat storage material, and the composite phase change heat storage material changes from a solid phase to a liquid phase. And at night, close each inlet and outlet valves of the phase-change heat storage type medium-temperature heat storage device 2, and the original open phase-change heat type medium-temperature heat storage device 2 becomes a closed space, and now the heat exchange tube 12 still circulates The flowing hot water for refrigeration continuously absorbs heat from the condensation process of the water vapor in the phase-change heat storage type medium-temperature heat storage device 2, and the water vapor in the phase-change heat storage type medium-temperature heat storage device 2 is continuously condensed into water droplets. As the mass of water vapor decreases, the steam pressure and temperature in the phase-change heat storage type medium-temperature heat storage device 2 will gradually drop below the phase change temperature (110°C) of the composite phase-change heat storage material; after that, the composite phase-change heat storage material begins to The phase change releases heat (from liquid to solid), and the water attached to the surface of the granular composite phase change heat storage material is heated to water vapor. water (the temperature increases from 85°C to 90°C), and the water vapor is condensed again into water droplets and falls into the heat storage accumulation layer 16, and so on, completing the heat transfer between the composite phase change heat storage material and the heat exchange tube 12. This heat transfer mechanism is very similar to that of a heat pipe. The phase-change heat-type medium-temperature heat storage device 2 utilizes the heat exchange characteristics of heat pipes to achieve very high heat storage and heat release efficiency. The heat conduction and heat transfer mode of the material is 1 to 2 orders of magnitude lower. At the same time, the granular composite phase-change heat storage material is filled with water and water vapor, and the phase-change heat process is simultaneously carried out everywhere in the heat storage accumulation layer 16. The effective heat transfer area on the surface of the particles is very large, making the phase-change heat storage medium temperature The heat transfer capability of the heat exchanger 2 is very excellent, the temperature difference between the composite phase change heat storage material and the heat exchange tube 12 is almost negligible, and the temperature difference inside the particles of the composite phase change heat storage material is also almost negligible.

在相变换热型中温储热器2的储热和放热过程中,相变换热型中温储热器2内水蒸汽的温度是不一样的(储热时水蒸汽温度大约120℃,放热时水蒸汽温度大约110℃)。而换热管12内热水温度要保持稳定,因此在白天和晚间要通过调节换热管12管路的回路流量来调节换热管12内的水流速,以保证相同的换热功率。During the heat storage and heat release process of the phase-change heat storage type medium-temperature heat storage device 2, the temperature of the water vapor in the phase-change heat type medium-temperature heat storage device 2 is different (the temperature of the water vapor during heat storage is about 120°C, The water vapor temperature is about 110°C when exothermic). The temperature of the hot water in the heat exchange tube 12 should be kept stable, so the flow rate of the water in the heat exchange tube 12 should be adjusted by adjusting the loop flow of the heat exchange tube 12 pipeline during the day and night, so as to ensure the same heat exchange power.

图2为本发明的中温太阳能空调系统的结构示意图。图示中温太阳能空调系统包括中温太阳能集热器1、相变换热型中温储热器2、制冷机3、回水泵4、热水泵5和储水箱6。所述中温太阳能集热器1的进口通过回水泵4与所述储水箱6相连接,并且其出口通过水蒸汽阀门9与所述相变换热型中温储热器2相连接,所述储水箱6通过出水阀门11与所述相变换热型中温储热器2相连接,所述相变换热型中温储热器2的换热管12一端通过热水泵5与制冷机3相连接,另一端直接与制冷机3相连接。Fig. 2 is a structural schematic diagram of the medium-temperature solar air-conditioning system of the present invention. The medium-temperature solar air-conditioning system shown in the figure includes a medium-temperature solar heat collector 1 , a phase-change heat storage type medium-temperature heat storage 2 , a refrigerator 3 , a return water pump 4 , a hot water pump 5 and a water storage tank 6 . The inlet of the medium-temperature solar heat collector 1 is connected to the water storage tank 6 through a return pump 4, and its outlet is connected to the phase-change heat type medium-temperature heat storage 2 through a water vapor valve 9. The water tank 6 is connected to the phase-change heat storage type medium-temperature heat storage device 2 through the water outlet valve 11, and one end of the heat exchange tube 12 of the phase-change heat type medium-temperature heat storage device 2 is connected to the refrigerator 3 through the hot water pump 5 , and the other end is directly connected with the refrigerator 3.

所述的中温太阳能集热器1为真空管套管组合式两用型太阳能加热器,该真空管套管组合式两用型太阳能加热器是已经授权的、由本申请人持有的中国专利(发明专利名称;真空管套管组合式两用型太阳能加热器,专利号ZL 200910311344.3),为一种由CPC集热板和全玻璃真空集热管组成的中高温承压式集热器。该集热器1可以在白天向吸收式空调制冷机3提供120℃以上的水蒸汽用做制冷热源,同时相变换热型中温储热器2内的复合相变储热材料吸收储存多余热量,晚间相变换热型中温储热器2可以向吸收式空调制冷机3提供110℃水蒸汽用做制冷热源。所述相变换热型中温储热器2的大小、体积和使用复合相变储热材料的质量根据整个太阳能空调系统的功率而定,整体系统可以包括数个并联的相变换热型中温储热器2。Described medium-temperature solar heat collector 1 is a combined dual-purpose solar heater of a vacuum tube casing, which is an authorized Chinese patent (invention patent) held by the applicant. Name: Vacuum tube casing combined dual-purpose solar heater, patent number ZL 200910311344.3), is a medium-high temperature pressure-bearing collector composed of CPC collector plates and all-glass vacuum collector tubes. The heat collector 1 can provide water vapor above 120°C to the absorption air-conditioning refrigerator 3 during the day as a cooling heat source, and at the same time, the composite phase-change heat storage material in the phase-change heat storage medium-temperature heat storage 2 absorbs and stores excess heat At night, the phase-change heat storage medium-temperature heat storage device 2 can provide 110°C water vapor to the absorption air-conditioning refrigerator 3 as a cooling heat source. The size, volume, and quality of the composite phase-change heat storage material used for the phase-change heat storage medium-temperature heat storage device 2 are determined according to the power of the entire solar air-conditioning system. The overall system may include several parallel phase-change heat-type medium-temperature Heat storage 2.

本实施例的制冷机3的功率为7.5kW,效率0.75。按白天中温太阳能集热器2工作时间8小时、晚间工作8小时计算,对应的中温太阳能集热器2的输出功率大于20kW,其中10kW直接用于白天制冷,相变换热型中温储热器2将剩余的热能储存起来供晚间8个小时工作使用,储热量大于384000kJ,所需聚乙烯腊的质量约为1500kg。The power of the refrigerator 3 in this embodiment is 7.5kW, and the efficiency is 0.75. Calculated according to the working time of medium-temperature solar collector 2 for 8 hours in the daytime and 8 hours in the evening, the output power of the corresponding medium-temperature solar collector 2 is greater than 20kW, of which 10kW is directly used for cooling during the day, and the phase-change heat storage type medium-temperature heat storage 2. Store the remaining heat energy for 8 hours of work at night. The heat storage capacity is greater than 384000kJ, and the quality of polyethylene wax required is about 1500kg.

相变换热型中温储热器2的直径为1.2m,总高1.5m,数量为5个相同尺寸的相变换热型中温储热器2,每个相变换热型中温储热器2使用聚乙烯腊300kg,分别铺设于10个筛网,每个筛网上堆积30kg。复合相变储热材料采用有机膨润土和聚乙烯腊按2.2∶1的质量比配制,总质量接近5000kg,复合相变储热材料的颗粒大小为3mm左右,蓄热堆积层16的空隙率保持在30%-40%左右,以利于吸收水分和透过蒸汽。The diameter of the phase-change heat storage type medium-temperature heat storage device 2 is 1.2m, the total height is 1.5m, and the number is 5 phase-change heat type medium-temperature heat storage devices 2 of the same size. 2Use 300kg of polyethylene wax, lay on 10 sieves respectively, and accumulate 30kg on each sieve. The composite phase change heat storage material is prepared with organic bentonite and polyethylene wax at a mass ratio of 2.2:1, the total mass is close to 5000kg, the particle size of the composite phase change heat storage material is about 3mm, and the void ratio of the heat storage accumulation layer 16 is maintained at About 30%-40%, in order to absorb moisture and transmit steam.

制冷机3的换热管12以串联方式通过每个相变换热型中温储热器2,根据计算,换热管12采用内径12mm,总长20m的铜管,即每个相变换热型中温储热器2内只要2m长换热管12,一般采用一根U型管即可。热水泵5的扬程为20m,一个50W小功率水泵就能满足要求。The heat exchange tubes 12 of the refrigerator 3 pass through each phase-change heat storage medium-temperature heat storage 2 in series. According to calculations, the heat exchange tubes 12 are copper tubes with an inner diameter of 12mm and a total length of 20m, that is, each phase-change heat storage type As long as the heat exchange tube 12 is 2m long in the medium-temperature heat storage device 2, a U-shaped tube is generally used. The head of the hot water pump 5 is 20m, and a 50W low-power water pump can meet the requirements.

在整体系统安装调试完成后,通过空气充气口22和进气阀门23向相变换热型中温储热器2内充入空气使相变换热型中温储热器2和中温太阳能集热器1管路压力达到2个大气压,以保证水在中温太阳能集热器1内被加热到120度左右,沸腾蒸发为水蒸汽后进入相变换热型中温储热器2,因为水蒸汽温度必须高于复合相变储热材料的相变温度(110℃),水蒸汽最后才能冷凝成过冷水流回储水箱6,再被回水泵4打入中温太阳能集热器1完成循环;反之,如果水蒸汽温度低于复合相变储热材料的相变温度,水蒸汽将回流到储水箱6和回水泵4中,从而造成回水泵4堵塞。为避免此情况发生,实际复合相变储热材料的置放量应比计算值多一些。After the installation and commissioning of the overall system is completed, air is charged into the phase-change heat storage type medium-temperature heat storage device 2 through the air charging port 22 and the air intake valve 23 to make the phase-change heat type medium-temperature heat storage device 2 and the medium-temperature solar heat collector 1. The pressure of the pipeline reaches 2 atmospheres to ensure that the water is heated to about 120 degrees in the medium-temperature solar collector 1. After boiling and evaporating into water vapor, it enters the phase-change heat storage type medium-temperature heat storage 2, because the temperature of the water vapor must be Higher than the phase change temperature (110°C) of the composite phase change heat storage material, the water vapor can finally condense into supercooled water and flow back to the water storage tank 6, and then be pumped into the medium temperature solar collector 1 by the return water pump 4 to complete the cycle; otherwise, if The water vapor temperature is lower than the phase change temperature of the composite phase change heat storage material, and the water vapor will flow back into the water storage tank 6 and the return water pump 4, thereby causing the return water pump 4 to be blocked. In order to avoid this situation, the actual placement of composite phase change heat storage materials should be more than the calculated value.

所述的中温太阳能空调系统的工作过程如下:The working process of the medium temperature solar air conditioning system is as follows:

在白天相变换热型中温储热器2储热阶段,打开回水泵4向中温太阳能集热器1供水,太阳辐射能被中温太阳能集热器1吸收,加热中温太阳能集热器1管内流动的水,过冷水最终在中温太阳能集热器1的出口蒸发为水蒸汽,向相变换热型中温储热器2提供2个大气压左右,120℃的水蒸汽。然后开启制冷机3的供水循环系统,调节热水泵5流量,保证制冷机3供水温度在90℃到95℃之间。中温太阳能集热器1的水蒸汽进入相变换热型中温储热器2后经过换热管12表面和通过蓄热堆积层16,一部分水蒸汽与换热管12内的流动热水进行热交换,在换热管12表面冷凝成饱和水滴落,大部分水蒸汽通过复合相变储热材料并与之进行热交换,在复合相变储热材料表面冷凝成饱和水。在相变换热型中温储热器2的最下方蓄热堆积层16内,饱和水放热变成过冷水,这些过冷水被回水泵4抽回中温太阳能集热器1完成集热器工质循环。过程开始时调节回水泵4的供水流量,使相变换热型中温储热器2的入口蒸汽温度略高于相变换热型中温储热器2内压力所对应的水饱和温度,即水蒸汽应达到干蒸汽程度,此后运行时水蒸汽温度只要高于复合相变储热材料相变温度即可。During the heat storage stage of the phase-change heat storage type medium-temperature heat storage device 2 during the day, the return water pump 4 is turned on to supply water to the medium-temperature solar heat collector 1, and the solar radiation energy is absorbed by the medium-temperature solar heat collector 1 to heat the flow in the pipe of the medium-temperature solar heat collector 1 The supercooled water finally evaporates into water vapor at the outlet of the medium-temperature solar heat collector 1, and provides water vapor at about 2 atmospheres and 120°C to the phase-change heat storage type medium-temperature heat storage 2. Then start the water supply circulation system of the refrigerator 3, adjust the flow rate of the hot water pump 5, and ensure that the water supply temperature of the refrigerator 3 is between 90°C and 95°C. The water vapor from the medium-temperature solar heat collector 1 enters the phase-change heat type medium-temperature heat storage device 2 and then passes through the surface of the heat exchange tube 12 and the heat storage accumulation layer 16, and a part of the water vapor is heated with the flowing hot water in the heat exchange tube 12. Exchange, condensed on the surface of the heat exchange tube 12 to become saturated water dripping, most of the water vapor passes through the composite phase change heat storage material and exchanges heat with it, and condenses on the surface of the composite phase change heat storage material to become saturated water. In the lowermost heat storage accumulation layer 16 of the phase-change heat type medium-temperature heat storage device 2, the saturated water releases heat and becomes supercooled water, and the supercooled water is pumped back to the medium-temperature solar heat collector 1 by the return water pump 4 to complete the work of the heat collector. quality cycle. At the beginning of the process, the water supply flow rate of the return pump 4 is adjusted so that the steam temperature at the inlet of the phase-change heat storage medium-temperature heat storage 2 is slightly higher than the water saturation temperature corresponding to the internal pressure of the phase-change heat storage medium-temperature heat storage 2, that is, the water The steam should reach the level of dry steam, and the temperature of the water vapor during operation thereafter only needs to be higher than the phase change temperature of the composite phase change heat storage material.

在晚间相变换热型中温储热器2放热阶段,关闭相变换热型中温储热器2的进出口阀门形成封闭空间。由于制冷机3的供水循环依然在运行,制冷机工质仍然在换热管12内流动吸热,所以相变换热型中温储热器2内的剩余水蒸汽在换热管12表面不断冷凝放热,相变换热型中温储热器2内的水蒸汽质量减少,蒸汽压力下降,对应的相变换热型中温储热器2内水蒸汽温度也不断下降。在温度下降到复合相变储热材料的相变温度(110℃)以下后,复合相变储热材料开始相变放热,加热其表面粘附的水变为110℃左右的水蒸汽,这些水蒸汽上升后与换热管12进行热交换,再冷凝成水滴落到蓄热堆积层16层内,如此循环反复实现复合相变储热材料和换热管12内流动水之间的热量传递。这时由于水蒸汽与制冷机3供水温度之间的温差减小,传热性能降低,因而为了保证制冷机3供水温度依然在90℃左右,需要适当手动调节制冷机3的水流量。During the heat release stage of the phase-change heat storage medium-temperature heat storage device 2 at night, the inlet and outlet valves of the phase-change heat storage medium-temperature heat storage device 2 are closed to form a closed space. Since the water supply cycle of the refrigerator 3 is still running, the working medium of the refrigerator still flows and absorbs heat in the heat exchange tube 12, so the remaining water vapor in the phase-change heat storage type medium-temperature heat storage 2 is continuously condensed on the surface of the heat exchange tube 12 Heat release, the mass of water vapor in the phase-change heat storage type medium-temperature heat storage device 2 decreases, the steam pressure drops, and the corresponding phase-change heat type medium-temperature heat storage device 2 also continuously drops in water vapor temperature. After the temperature drops below the phase transition temperature (110°C) of the composite phase change heat storage material, the composite phase change heat storage material begins to phase change and release heat, and the water adhering to its surface is heated to become water vapor at about 110°C. After the water vapor rises, it exchanges heat with the heat exchange tube 12, and then condenses into water droplets and falls into the heat storage accumulation layer 16. This cycle repeatedly realizes the heat transfer between the composite phase change heat storage material and the flowing water in the heat exchange tube 12. . At this time, since the temperature difference between the water vapor and the water supply temperature of the refrigerator 3 decreases, the heat transfer performance decreases. Therefore, in order to ensure that the water supply temperature of the refrigerator 3 is still around 90°C, it is necessary to manually adjust the water flow of the refrigerator 3 appropriately.

在白天中温太阳能集热器1工作时,相变换热型中温储热器2进出口阀门打开,相变换热型中温储热器2与中温太阳能集热器1加热管形成一个循环流路,流出相变换热型中温储热器2的热水用回水泵4泵回中温太阳能集热器1。在晚间中温太阳能集热器1不工作时,关闭相变换热型中温储热器2进出口阀门,使之形成封闭容器。When the medium-temperature solar collector 1 is working during the day, the inlet and outlet valves of the phase-change heat storage type medium-temperature heat storage device 2 are opened, and the phase-change heat storage type medium-temperature heat storage device 2 and the heating tube of the medium-temperature solar heat collector 1 form a circulation flow path , the hot water flowing out of the phase-change heat type medium-temperature heat storage device 2 is pumped back to the medium-temperature solar heat collector 1 by the return water pump 4 . When the medium-temperature solar heat collector 1 is not working at night, close the inlet and outlet valves of the phase-change heat storage type medium-temperature heat storage device 2 to form a closed container.

本实施例中的中温太阳能空调制冷系统和与之配套的相变换热型中温储热器2可在白天提供用于太阳能空调的120℃水蒸气,晚上提供110℃左右水蒸汽以加热制冷机3用热水,满足制冷机3运行需要。所述相变换热型中温储热器2利用多孔质复合相变储热材料的巨大传热表面和热管相变换热技术实现了非常高的储热和放热效率,其复合相变储热材料和换热管12之间的传热热阻比传统导热型储热材料的要低2个数量级,复合相变储热材料和换热管12管路之间的温差可以忽略。相变换热型中温储热器2性能的提高能够使中温太阳能集热器1的工质温度尽量降低,从而大幅度提高整体系统的太阳能热利用率。The medium-temperature solar air-conditioning and refrigeration system in this embodiment and the matching phase-change heat storage medium-temperature heat storage device 2 can provide 120°C water vapor for solar air-conditioning during the day, and 110°C water vapor for heating the refrigerator at night 3. Hot water is used to meet the operation needs of the refrigerator 3. The phase-change heat storage medium-temperature heat storage device 2 utilizes the huge heat transfer surface of the porous composite phase-change heat storage material and the heat pipe phase-change heat technology to achieve very high heat storage and heat release efficiency, and its composite phase-change heat storage The heat transfer resistance between the material and the heat exchange tube 12 is two orders of magnitude lower than that of the traditional heat conduction heat storage material, and the temperature difference between the composite phase change heat storage material and the heat exchange tube 12 can be ignored. The improvement of the performance of the phase-change heat storage type medium-temperature heat storage device 2 can reduce the working medium temperature of the medium-temperature solar heat collector 1 as much as possible, thereby greatly improving the solar heat utilization rate of the overall system.

Claims (7)

1.一种相变换热型中温储热器,其特征在于:所述中温储热器为一耐压容器,其包括箱体、多个圈架、筛网、蓄热堆积层和换热管,所述多个圈架分别水平地固定于所述箱体下部的内壁上,所述多个筛网分别放置于各圈架上,所述蓄热堆积层分别铺设于各筛网上,该蓄热堆积层由复合相变储热材料和沙粒混合而成,所述换热管设置于箱体上部的内腔中,该换热管的管腔与箱体的内部隔绝且与箱体外部相通,其中流动有导热工质。1. A phase-change heat storage type medium-temperature heat storage device, characterized in that: the medium-temperature heat storage device is a pressure-resistant container, which includes a box body, a plurality of hoops, screens, heat storage accumulation layers and heat exchange tube, the plurality of hoops are respectively horizontally fixed on the inner wall of the lower part of the box, the plurality of screens are respectively placed on each hoop, and the heat storage accumulation layer is respectively laid on each screen, the The heat storage accumulation layer is made of composite phase change heat storage material and sand. The heat exchange tube is arranged in the inner cavity of the upper part of the box. The lumen of the heat exchange tube is isolated from the inside of the box and is separated from the outside In communication, there is a heat-conducting working medium flowing therein. 2.根据权利要求1所述的相变换热型中温储热器,其特征在于:所述的复合相变储热材料为颗粒状,其由有机膨润土与聚乙烯腊按2.2∶1的质量比组成。2. The phase-change heat-type medium-temperature heat storage device according to claim 1, characterized in that: the composite phase-change heat storage material is granular, and it is composed of organic bentonite and polyethylene wax in a mass ratio of 2.2:1. Than composition. 3.根据权利要求1所述的相变换热型中温储热器,其特征在于:所述的复合相变储热材料为颗粒状,其由有机膨润土与低密度聚乙烯按2∶1的质量比组成。3. The phase-change heat-type medium-temperature heat storage device according to claim 1, characterized in that: the composite phase-change heat storage material is granular, and it is composed of organic bentonite and low-density polyethylene at a ratio of 2:1. mass ratio composition. 4.根据权利要求1所述的相变换热型中温储热器,其特征在于:使用水和水蒸气作为所述相变换热型中温储热器内的相变传热工质,该相变传热工质直接在颗粒状复合相变储热材料表面蒸发或冷凝实现相变换热;在储热阶段,相变换热型中温储热器是一个开口流动系统,集热器提供的水蒸汽流入该相变换热型中温储热器,通过蓄热堆积层内冷凝放热,水蒸气的冷凝潜热被所述复合相变储热材料吸收储存;在放热阶段,关闭所述相变换热型中温储热器进出口阀门,将原来开放式的相变换热型中温储热器变为封闭空间,所述复合相变储热材料表面附着的水被加热为水蒸气,该水蒸气上升到换热管表面冷凝,加热换热管内导热工质,而水蒸气再次被冷凝成水滴落到蓄热堆积层内;由此循环往复完成所述复合相变储热材料和换热管间的热传递。4. The phase-change heat type medium temperature heat storage device according to claim 1, characterized in that: water and steam are used as the phase change heat transfer working medium in the phase change heat type medium temperature heat storage device, the The phase change heat transfer working medium directly evaporates or condenses on the surface of the granular composite phase change heat storage material to realize phase change heat; in the heat storage stage, the phase change heat type medium temperature heat storage is an open flow system, and the collector provides The water vapor flows into the phase-change heat storage medium-temperature heat storage device, and heat is released through condensation in the heat storage stack layer, and the condensation latent heat of water vapor is absorbed and stored by the composite phase-change heat storage material; in the heat release stage, the The inlet and outlet valves of the phase-change heat storage medium-temperature heat storage device turn the original open phase-change heat storage type medium-temperature heat storage device into a closed space, and the water attached to the surface of the composite phase change heat storage material is heated into water vapor. The water vapor rises to the surface of the heat exchange tube to condense, heats the heat-conducting working medium in the heat exchange tube, and the water vapor is condensed again into water droplets and falls into the heat storage accumulation layer; thus, the composite phase change heat storage material and heat exchange process are completed in a cycle. Heat transfer between heat pipes. 5.一种用于权利要求2所述相变换热型中温储热器的复合相变储热材料的制备方法,其特征在于:将有机膨润土和聚乙烯腊按2.2∶1的质量比配制后放入一有搅拌装置的加热容器内一边加热一边搅拌,加热到160℃后保持该温度搅拌1小时,使溶解的聚乙烯腊全部被有机膨润土吸附,最后得到平均粒径为3mm的颗粒状的复合相变储热材料。5. A method for preparing a composite phase-change heat storage material for a phase-change heat-type medium-temperature heat storage device according to claim 2, characterized in that: organic bentonite and polyethylene wax are prepared in a mass ratio of 2.2:1 Then put it into a heating container with a stirring device and stir while heating. After heating to 160°C, keep the temperature and stir for 1 hour, so that all the dissolved polyethylene wax is absorbed by the organic bentonite, and finally obtain granular particles with an average particle size of 3 mm. Composite phase change heat storage materials. 6.一种由权利要求1所述的相变换热型中温储热器构成的中温太阳能空调系统,其特征在于:所述的太阳能空调系统包括中温太阳能集热器、相变换热型中温储热器、制冷机、回水泵、热水泵和储水箱,所述中温太阳能集热器的进口通过回水泵与所述储水箱相连接,并且其出口通过水蒸汽阀门与所述相变换热型中温储热器相连接,所述储水箱通过出水阀门与所述相变换热型中温储热器相连接,所述相变换热型中温储热器的换热管一端通过热水泵与制冷机相连接,另一端直接与制冷机相连接。6. A medium-temperature solar air-conditioning system composed of the phase-change heat type medium-temperature heat storage device according to claim 1, characterized in that: the solar air-conditioning system includes a medium-temperature solar heat collector, a phase-change heat type medium-temperature Heat storage, refrigerator, return water pump, hot water pump and water storage tank, the inlet of the medium temperature solar collector is connected with the water storage tank through the return water pump, and its outlet is exchanged heat with the phase through the water vapor valve The water storage tank is connected to the phase-change heat storage type medium-temperature heat storage device through a water outlet valve, and one end of the heat exchange tube of the phase-change heat storage type medium-temperature heat storage device is connected to the The refrigerator is connected, and the other end is directly connected with the refrigerator. 7.根据权利要求6所述的中温太阳能空调系统,其特征在于:所述的中温太阳能集热器为真空管套管组合式两用型太阳能加热器。7. The medium-temperature solar air-conditioning system according to claim 6, characterized in that: said medium-temperature solar heat collector is a combined dual-purpose solar heater of vacuum tube casing.
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CN106595366A (en) * 2016-11-15 2017-04-26 桑夏太阳能股份有限公司 Hot pipe-type medium-temperature heat storage device with shaping PCM
CN106556165B (en) * 2016-11-28 2018-06-01 桑夏太阳能股份有限公司 A kind of solar steam hold over system for being installed on factory roof
CN106556165A (en) * 2016-11-28 2017-04-05 桑夏太阳能股份有限公司 A kind of solar steam hold over system for being installed on factory roof
CN108120037A (en) * 2018-02-06 2018-06-05 江苏贝德莱特太阳能科技有限公司 A kind of organic phase-change heat storage type solar water heater
CN108548340A (en) * 2018-04-27 2018-09-18 武汉科技大学 Solar energy storage tank
CN109140805A (en) * 2018-08-20 2019-01-04 上海工程技术大学 A kind of steaming utensil type phase transition thermal storage water tank
CN109222667A (en) * 2018-11-09 2019-01-18 南京林业大学 A kind of temperature-adjustable food constant temperature tray rack based on phase-change heat-exchange
CN109297339A (en) * 2018-12-05 2019-02-01 上海宝钢节能环保技术有限公司 A kind of flooded steam heat accumulator and preparation method of composite phase change heat storage material
CN111397247A (en) * 2020-04-03 2020-07-10 江苏省新能源开发股份有限公司 Heat-storage refrigeration integrated system
CN111394065A (en) * 2020-04-15 2020-07-10 电子科技大学中山学院 Building envelope system based on phase-change material

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Application publication date: 20130403