TWM445687U - Heat exchange device - Google Patents

Heat exchange device Download PDF

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TWM445687U
TWM445687U TW101217855U TW101217855U TWM445687U TW M445687 U TWM445687 U TW M445687U TW 101217855 U TW101217855 U TW 101217855U TW 101217855 U TW101217855 U TW 101217855U TW M445687 U TWM445687 U TW M445687U
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Taiwan
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heat
heat source
water
source medium
conduit
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TW101217855U
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Chinese (zh)
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yu-ren Zhang
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Res Electric Company Ltd
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Description

熱交換裝置Heat exchange device

本創作為一種熱交換裝置,可以使用在利用壓縮機及熱源介質(冷媒)取熱之熱泵式熱水器系統中,並且在熱交換時能夠有效吸收熱源介質的潛熱及顯熱,藉以提高水溫,節省能源。The present invention is a heat exchange device which can be used in a heat pump type water heater system that uses a compressor and a heat source medium (refrigerant medium) to take heat, and can effectively absorb the latent heat and sensible heat of the heat source medium during heat exchange, thereby increasing the water temperature. save energy.

按,熱泵式熱水器的工作原理,是利用熱源介質(即冷媒)收集空氣中的熱能,通過熱泵(即壓縮機)加壓蓄存後,再將熱源介質通過熱交換器與冷水進行熱交換,使冷水逐漸地被加溫而轉換成熱水。由於熱泵式熱水器將冷水熱交換成為熱水的過程中,是利用運轉冷媒來做能源轉換,其能源轉換效率理論上可超過300%以上,相較於電力或火力轉換效率無法到達100%的限制,熱泵式熱水器僅需使用極少的電能即能達到良好的加熱效果,不但具有顯著的經濟效益,而且產生的污染甚少,是目前最環保也最省能源之製熱設備。According to the working principle of the heat pump water heater, the heat source medium (ie, the refrigerant) is used to collect the heat energy in the air, and after being stored and stored by the heat pump (ie, the compressor), the heat source medium is exchanged with the cold water through the heat exchanger. The cold water is gradually warmed and converted into hot water. Since the heat pump water heater converts cold water into hot water, it uses the operating refrigerant to do energy conversion. The energy conversion efficiency can theoretically exceed 300%, which is less than the limit of 100% of the power or fire conversion efficiency. The heat pump water heater can achieve good heating effect with only a small amount of electric energy. It not only has significant economic benefits, but also produces little pollution. It is the most environmentally friendly and energy-efficient heating equipment.

如第一圖所示,既有的熱泵式熱水器系統包括有一壓縮機1、一熱交換器2、一膨脹閥3,以及一蒸發器4;運作時,壓縮機1將冷媒壓縮成高溫高壓的氣態冷媒,以該高溫高壓的氣態冷媒做為熱源介質進入熱交換器2內,並且在熱交換器2中與水流進行熱交換而釋放熱能,使水流得以被加熱昇溫,同時高溫高壓的氣態冷媒經釋放熱能而冷凝,並透過膨脹閥3(或毛細管)之高低壓差成為氣液混合冷媒後,再藉由蒸發器4吸收外界熱源,並通過壓縮機1再將冷媒壓縮成高溫高壓的氣態冷媒進入熱交換器2內,如此不斷循環作熱能移轉之動作,即可以讓水流在熱交換器2中被加熱昇溫。As shown in the first figure, the existing heat pump water heater system includes a compressor 1, a heat exchanger 2, an expansion valve 3, and an evaporator 4. In operation, the compressor 1 compresses the refrigerant into a high temperature and high pressure. The gaseous refrigerant enters the heat exchanger 2 with the high-temperature and high-pressure gaseous refrigerant as a heat source medium, and exchanges heat with the water stream in the heat exchanger 2 to release heat energy, so that the water flow can be heated and heated, and the high-temperature and high-pressure gas refrigerant is simultaneously heated. After condensing by releasing heat energy and passing through the high and low pressure difference of the expansion valve 3 (or capillary tube) to become a gas-liquid mixed refrigerant, the external heat source is absorbed by the evaporator 4, and the refrigerant is compressed into a high-temperature and high-pressure gas state through the compressor 1. The refrigerant enters the heat exchanger 2, and the circulation is continuously performed as a thermal energy transfer operation, that is, the water flow can be heated and heated in the heat exchanger 2.

由上述過程可知,熱泵式熱水器之熱交換的運作過程,大致是由 高溫高壓的氣態冷媒在熱交換器內冷凝,然後再由壓縮機壓縮成為高溫氣態進行下一次熱交換。而冷媒蓄存熱能的過程中,其總熱能包括潛熱(latent heat)以及顯熱(sensible heat),但是在熱交換器內冷凝時,由於冷水在熱交換的初期吸收了冷媒釋放的顯熱而不斷地被提高溫度,直到冷水昇溫、冷媒降溫到二者相同的溫度時,冷媒即不再釋放熱能。It can be seen from the above process that the operation process of the heat exchange of the heat pump water heater is roughly The high temperature and high pressure gaseous refrigerant condenses in the heat exchanger, and then is compressed by the compressor into a high temperature gas state for the next heat exchange. In the process of storing heat in the refrigerant, the total heat energy includes latent heat and sensible heat, but when condensing in the heat exchanger, the cold water absorbs the sensible heat released by the refrigerant at the initial stage of heat exchange. The temperature is continuously increased until the cold water warms up and the refrigerant cools to the same temperature, and the refrigerant no longer releases heat.

舉例來說,冷水在熱交換的初期大約25℃,冷媒溫度大約在70~100℃,此時,冷水可以大幅吸收冷媒的熱能而快速昇溫,同時高溫高壓的冷媒因釋放熱能而降溫,二者一昇溫一降溫而且彼此溫度趨近,當冷水昇溫到大約55℃時,冷媒亦降溫到大約55℃,此時,由於二者溫度已趨近於相同,因此冷媒就無法再對水流釋放熱能,水流亦無法再昇溫。For example, the cold water is about 25 ° C at the beginning of the heat exchange, and the refrigerant temperature is about 70 to 100 ° C. At this time, the cold water can absorb the heat of the refrigerant to rapidly heat up, and the high temperature and high pressure refrigerant cools due to the release of heat energy. When the temperature rises and the temperature drops and the temperature approaches, when the cold water rises to about 55 ° C, the refrigerant also cools to about 55 ° C. At this time, since the temperatures of the two are close to the same, the refrigerant can no longer release heat energy to the water flow. The water can no longer warm up.

換言之,上述習知熱泵式熱水器在冷媒與冷水進行熱交換時,水並沒有完全吸收到冷媒所蓄存的總熱,尤其是在潛熱的部分,因為冷水昇溫、冷媒降溫到相同溫度而使冷媒不再釋放熱能時,冷媒仍然尚未到達釋放潛熱(由氣體轉換為液體相態變化時所釋放的熱能)的溫度,因此也造成冷水加熱溫度上的限制;目前,熱泵式熱水器加熱溫度大約到達55℃即無法突破,這也是業界一直無法克服的重大問題。In other words, when the conventional heat pump water heater exchanges heat between the refrigerant and the cold water, the water does not completely absorb the total heat stored in the refrigerant, especially in the latent heat, because the cold water heats up and the refrigerant cools to the same temperature to make the refrigerant When the heat energy is no longer released, the refrigerant still has not reached the temperature of releasing the latent heat (the heat energy released when the gas is converted into a liquid phase change), thus also causing a limitation on the heating temperature of the cold water; at present, the heating temperature of the heat pump water heater reaches approximately 55. °C can not break through, this is also a major problem that the industry has been unable to overcome.

有鑑於此,本創作人乃累積多年相關領域的實務經驗與研究心得,特創作出一種「熱交換裝置」,不但能夠有效吸收熱源介質的總熱,而且能夠突破既有技術在溫度上的限制,達成提高水溫、節省能源之目的。In view of this, the creator has accumulated many years of practical experience and research experience in related fields, and created a "heat exchange device", which can not only effectively absorb the total heat of the heat source medium, but also break through the temperature limitations of the existing technology. To achieve the purpose of increasing water temperature and saving energy.

本創作之目的在於提供一種「熱交換裝置」,不但能夠有效吸收冷 媒蓄存的總熱能包括潛熱(latent heat)以及顯熱(sensible heat),還能夠突破既有技術在溫度上的限制,達成提高水溫、節省能源之目的,具有極高的產業價值。The purpose of this creation is to provide a "heat exchange device" that not only absorbs cold effectively The total thermal energy stored in the medium includes latent heat and sensible heat. It can also break through the limitations of existing technologies in terms of temperature, achieve the goal of increasing water temperature and saving energy, and has extremely high industrial value.

為達成上述目的,本創作之熱交換裝置包含一供水流流通之加熱管,以及一包覆於加熱管外部供熱源介質流通之熱源導管,其中:In order to achieve the above object, the heat exchange device of the present invention comprises a heating pipe through which a water supply flow flows, and a heat source conduit covering the heat supply medium outside the heating pipe, wherein:

該加熱管被包覆在熱源導管內,依水流由上游往下游流通方向,依序包括一水流入口、一連接於水流入口以吸收熱源導管內熱源介質之潛熱的預熱區段、一連接於預熱區段以吸收熱源導管內熱源介質之顯熱的高溫區段,以及一連接於高溫區段以排出高溫熱水的出水口。The heating tube is wrapped in the heat source conduit, and comprises a water inlet, a preheating section connected to the water inlet to absorb the latent heat of the heat source medium in the heat source conduit, and a connection to the water flow direction from upstream to downstream. The preheating section is configured to absorb the sensible high temperature section of the heat source medium in the heat source conduit, and a water outlet connected to the high temperature section to discharge the high temperature hot water.

該熱源導管內的熱源介質流通方向與水流方向相反,依熱源介質由上游往下游流通方向,依序包括一與加熱管出水口相對應以供熱源介質進入的熱源介質入口、一連接於熱源介質入口並且相對於加熱管高溫區段用來釋放熱源介質之顯熱的顯熱釋放區段、一連接於顯熱釋放區段並且相對於加熱管預熱區段用來釋放熱源介質之潛熱的潛熱釋放區段,以及一連通於潛熱釋放區段相對於水流入口的熱源介質出口。The heat source medium in the heat source conduit has a flow direction opposite to the water flow direction, and includes a heat source medium inlet corresponding to the heat pipe medium inlet and a heat source medium inlet, and a heat source medium according to the heat source medium flowing from the upstream to the downstream flow direction. The sensible heat release section of the inlet and relative to the high temperature section of the heating tube for releasing the sensible heat of the heat source medium, a latent heat connected to the sensible heat release section and used to release the latent heat of the heat source medium relative to the heating tube preheating section a release section and a heat source medium outlet connected to the latent heat release section relative to the water flow inlet.

上述構造中,依熱源介質在熱源導管內流通方向來說,熱源介質先在熱源導管的上游釋放顯熱,然後在熱源導管的下游釋放潛熱;相對的,而由於加熱管內的水流方向與熱源導管之熱源介質流通方向相反,使加熱管上游預熱區段之水流可先吸收熱源介質之潛熱,下游高溫區段則可在水流已昇溫的情形下進一步吸收熱源介質之顯熱。In the above configuration, according to the flow direction of the heat source medium in the heat source conduit, the heat source medium first releases sensible heat upstream of the heat source conduit, and then releases latent heat downstream of the heat source conduit; in contrast, due to the direction of the water flow and the heat source in the heating tube The heat source medium of the conduit flows in the opposite direction, so that the water flow in the preheating section of the heating pipe can first absorb the latent heat of the heat source medium, and the downstream high temperature section can further absorb the sensible heat of the heat source medium when the water flow has warmed up.

換言之,在進行熱交換的過程中,對熱源介質而言,溫度由高至低逐步釋放熱能,水溫則相對應由低至高逐步吸收熱能,如此即可以讓水流在經過熱交換後,幾乎能夠完全吸收熱源介質的總熱,並且能突破既有技術在溫度上的限制,達成提高水溫、節省能源之目的。In other words, in the process of heat exchange, for the heat source medium, the temperature gradually releases the heat from high to low, and the water temperature gradually absorbs the heat from low to high, so that the water can be almost exchanged after heat exchange. It completely absorbs the total heat of the heat source medium, and can break through the limitation of the temperature of the existing technology, and achieve the purpose of increasing the water temperature and saving energy.

值得一提的是,在既有技術中,並未考慮到熱源介質的總熱包括 顯熱與潛熱,所以其水流與熱源介質熱交換時,溫度為相向式的遞增及遞減,使遞增的水溫最多只能到達與遞減後熱源介質相同的溫度,熱源介質即無法再釋放熱能,一般大約在55℃左右。反觀本案,由於低溫水流先在預熱區段吸收熱源介質處於較低溫的潛熱,之後在水流已昇溫的情形下又進一步吸收熱源介質處於較高溫的顯熱,因此其溫度可以突破既有技術的限制,到達趨近於冷媒初期釋放顯熱的溫度;根據本案創作人實際實驗的結果,水流可以昇溫到70~100℃,不僅能夠突破既有技術溫度大約在55℃左右的限制,還能有效提高能源效率比值C.O.P。It is worth mentioning that in the prior art, the total heat of the heat source medium is not considered. Sensible heat and latent heat, so when the water flow is exchanged with the heat source medium, the temperature is increasing and decreasing in the opposite direction, so that the increasing water temperature can only reach the same temperature as the decreasing heat source medium, and the heat source medium can no longer release heat energy. It is usually around 55 °C. In contrast, in this case, since the low-temperature water first absorbs the latent heat of the heat source medium in the preheating section at a lower temperature, and then further absorbs the sensible heat of the heat source medium at a higher temperature in the case where the water flow has warmed up, the temperature can break through the existing technology. Restricted, reaching the temperature at which the sensible heat is released at the beginning of the refrigerant; according to the actual experiment results of the creator of the case, the water flow can be heated to 70~100 °C, which can not only break the limit of the existing technical temperature of about 55 °C, but also effective Improve energy efficiency ratio COP.

根據上述結構特徵,本創作實施時,所述之熱源導管以及位於熱源導管內供水流流通之加熱管,二者之管體是呈直線形狀或者連續彎曲形狀,連續彎曲形狀可以在相同熱交換距離的情形下節省配置長度,以便於安裝實施。According to the above structural features, in the implementation of the present invention, the heat source conduit and the heating pipe located in the heat source conduit through which the water supply flows, the tubular bodies of the two are linear or continuously curved, and the continuous curved shape can be at the same heat exchange distance. In the case of the situation, the configuration length is saved to facilitate the installation implementation.

根據上述結構特徵,本創作實施時,所述之熱源導管外部披覆有一層隔熱層,俾能使熱源介質只對內部加熱管之水流釋放熱能。According to the above structural features, when the present invention is implemented, the heat source conduit is covered with a heat insulating layer, and the heat source medium can release heat energy only to the water flow of the internal heating pipe.

根據上述結構特徵,本創作實施時,所述熱源導管之熱源介質出口依序連接一膨脹閥、一蒸發器、一壓縮機,再由壓縮機連接於熱源介質入口,使熱源介質循環流通。According to the above structural feature, in the implementation of the present invention, the heat source medium outlet of the heat source conduit is sequentially connected with an expansion valve, an evaporator, a compressor, and then connected to the heat source medium inlet by the compressor to circulate the heat source medium.

根據上述根據上述結構特徵,本創作實施時,所述加熱管之出水口進一步連接至儲存熱水之儲水桶,以供蓄存熱水。According to the above structural feature, in the implementation of the present invention, the water outlet of the heating pipe is further connected to a water storage bucket for storing hot water for storing hot water.

相較於先前技術,本創作熱交換裝置中的水流可以先在預熱區段吸收熱源介質之潛熱,之後在水流已昇溫的情形下進一步吸收熱源介質之顯熱,因此其溫度可以突破既有技術大約在55℃左右的限制,被加熱到達70~100℃,不但能突破既有技術溫度的限制,而且能有效提昇熱交換效率,提高能源效率比值,達到節省能源之目的,具有極高 的產業價值。Compared with the prior art, the water flow in the present heat exchange device can first absorb the latent heat of the heat source medium in the preheating section, and then further absorb the sensible heat of the heat source medium when the water flow has been heated, so that the temperature can break through the existing The technology is limited to about 55 ° C, heated to 70 ~ 100 ° C, not only can break through the limitations of the existing technology temperature, but also can effectively improve the heat exchange efficiency, improve the energy efficiency ratio, to achieve energy-saving purposes, is extremely high Industrial value.

以下依據本創作之技術手段,列舉出適於本創作之實施方式,並配合圖式說明如後:如第二圖所示,本創作之熱交換裝置包含一供水流流通之加熱管10,以及一包覆於加熱管10外部供熱源介質流通之熱源導管20,其中:該加熱管10被包覆在熱源導管20內,其水流由上游往下游流通方向,如圖中所示由左向右,依序包括一水流入口11、一連接於水流入口11以吸收熱源導管20內熱源介質之潛熱的預熱區段12、一連接於預熱區段12以吸收熱源導管20內熱源介質之顯熱的高溫區段13,以及一連接於高溫區段13以排出高溫熱水的出水口14。Hereinafter, according to the technical means of the present creation, the implementation method suitable for the present creation is listed, and the following description is accompanied by the following description: As shown in the second figure, the heat exchange device of the present invention includes a heating pipe 10 through which the water supply flow flows, and a heat source conduit 20 covering the heat supply medium outside the heating pipe 10, wherein the heating pipe 10 is wrapped in the heat source conduit 20, and the water flow flows from upstream to downstream, as shown in the figure from left to right. And a water inlet port 11 , a preheating section 12 connected to the water inlet 11 to absorb the latent heat of the heat source medium in the heat source conduit 20 , and a preheating section 12 connected to the heat source medium in the heat source conduit 20 . The hot high temperature section 13 and a water outlet 14 connected to the high temperature section 13 to discharge high temperature hot water.

該熱源導管20內的熱源介質流通方向與水流方向相反,依熱源介質由上游往下游流通方向,如圖中所示由右向左,依序包括一熱源介質入口21、一顯熱釋放區段22、一潛熱釋放區段23,以及一熱源介質出口24。The heat source medium in the heat source conduit 20 has a flow direction opposite to the water flow direction, and the heat source medium flows from the upstream to the downstream, as shown in the figure from right to left, sequentially including a heat source medium inlet 21 and a sensible heat release portion. 22. A latent heat release section 23 and a heat source medium outlet 24.

上述熱源介質入口21與出水口14相對應供熱源介質進入;該顯熱釋放區段22與加熱管10的高溫區段13相對應用來釋放熱源介質之顯熱;潛熱釋放區段23與加熱管10的預熱區段12相對應用來釋放熱源介質之潛熱;該熱源介質出口24則與水流入口11相對應以供熱源介質排出。The heat source medium inlet 21 corresponds to the water outlet 14 for the heat source medium to enter; the sensible heat release section 22 is opposite to the high temperature section 13 of the heating tube 10 to release the sensible heat of the heat source medium; the latent heat release section 23 and the heating tube The preheating section 12 of 10 is relatively applied to release the latent heat of the heat source medium; the heat source medium outlet 24 is corresponding to the water inlet 11 for the heat source medium to be discharged.

上述構造中,熱源介質在熱源導管20內的流通方向,是先在熱源導管20上游(圖示右側)的顯熱釋放區段22釋放熱源介質之顯熱,然後在熱源導管20下游(圖示左側)的潛熱釋放區段23釋放熱源介質之潛熱。In the above configuration, the flow direction of the heat source medium in the heat source conduit 20 is to first release the sensible heat of the heat source medium in the sensible heat release section 22 upstream of the heat source conduit 20 (on the right side of the figure), and then downstream of the heat source conduit 20 (illustrated The latent heat release section 23 on the left side releases the latent heat of the heat source medium.

相對的,由於加熱管10內的水流方向與熱源導管20之熱源介質流通方向相反,使加熱管10上游(圖示左側)預熱區段12之低溫水流可先吸收熱源介質在潛熱釋放區段23所釋放較低溫的潛熱,而加熱管10下游(圖示右側)高溫區段13則可在水流已昇溫的情形下,進一步吸收熱源介質在顯熱釋放區段22所釋放較高溫的顯熱。如此即可以讓水流在經過熱交換後,幾乎能夠完全吸收熱源介質的總熱,並且能突破既有技術在溫度上的限制,達成提高水溫、節省能源之目的。In contrast, since the direction of the water flow in the heating pipe 10 is opposite to the flow direction of the heat source medium of the heat source conduit 20, the low temperature water flow in the preheating section 12 upstream of the heating pipe 10 (left side of the drawing) can first absorb the heat source medium in the latent heat release section. 23 releases the lower temperature latent heat, and the high temperature section 13 downstream of the heating tube 10 (the right side of the figure) can further absorb the higher temperature sensible heat released by the heat source medium in the sensible heat release section 22 when the water flow has warmed up. . In this way, the water flow can almost completely absorb the total heat of the heat source medium after the heat exchange, and can break the limitation of the temperature of the existing technology, thereby achieving the purpose of increasing the water temperature and saving energy.

如第三圖所示,本創作實施時,所述之熱源導管20以及位於熱源導管20內供水流流通之加熱管10,二者之管體可以為直線或呈連續彎曲形狀;連續彎曲形狀可以在相同熱交換距離的情形下節省配置長度,以便於安裝實施,讓水流在越接近加熱管10下游出水口14及熱源導管20之上游熱源介質入口21的位置(圖示下方),其溫度即能越接近熱源介質初期釋放顯熱的溫度,大約70~100℃。As shown in the third figure, in the implementation of the present invention, the heat source conduit 20 and the heating pipe 10 located in the heat source conduit 20 through which the water supply flows, the tubular bodies of the two may be straight or continuously curved; the continuous curved shape may be In the case of the same heat exchange distance, the arrangement length is saved to facilitate the installation, so that the water flow is closer to the position of the heat source medium inlet 21 upstream of the water outlet 14 and the heat source conduit 20 downstream of the heating pipe 10 (lower in the figure), and the temperature is The closer to the temperature at which the heat source medium releases sensible heat, the temperature is about 70~100 °C.

此外,本創作實施時,可以在熱源導管20外部披覆一層隔熱層25,該層隔熱層25可以讓熱源導管20與外界溫度隔離,使熱源導管20內的熱源介質只對其內部加熱管10之水流釋放熱能。In addition, in the implementation of the present invention, a heat insulating layer 25 may be disposed on the outside of the heat source conduit 20, and the heat insulating layer 25 may isolate the heat source conduit 20 from the outside temperature, so that the heat source medium in the heat source conduit 20 only heats the interior thereof. The water flow of tube 10 releases thermal energy.

如第四圖所示,為本創作實施時配合一般熱泵式熱水器系統示意圖,圖中揭示,所述熱源導管20之熱源介質出口24依序連接一膨脹閥30、一蒸發器40、一壓縮機50,再由壓縮機50連接於熱源導管20另一端的熱源介質入口21,使熱源介質得以經膨脹閥30、蒸發器40、壓縮機50的運作而循環流通,進而不斷地在熱源導管20內進行熱交換。As shown in the fourth figure, in the implementation of the present invention, a schematic diagram of a general heat pump water heater system is shown. The heat source medium outlet 24 of the heat source conduit 20 is sequentially connected to an expansion valve 30, an evaporator 40, and a compressor. 50, the compressor 50 is connected to the heat source medium inlet 21 at the other end of the heat source conduit 20, so that the heat source medium can be circulated through the operation of the expansion valve 30, the evaporator 40, and the compressor 50, and is continuously in the heat source conduit 20. Perform heat exchange.

此外,本創作實施時,由於加熱管10之出水口14水流溫度可以到達70~100℃,在一般家庭使用時,可以直接混入適當冷水立即使用,即所謂即熱型熱水器;若使用在飯店、機關宿舍等熱水使用量較 大的場所時,可以進一步將出水口14連接至一儲水桶60,以供蓄存熱水,則可以使用在儲熱式熱水器系統中。In addition, in the implementation of this creation, since the water flow temperature of the water outlet 14 of the heating pipe 10 can reach 70 to 100 ° C, in general household use, it can be directly mixed with appropriate cold water for immediate use, that is, a so-called instant water heater; if used in a restaurant, The use of hot water in the dormitory In a large location, the water outlet 14 can be further connected to a water storage tank 60 for storing hot water, which can be used in a heat storage water heater system.

綜上所述,本創作可以讓水流先在預熱區段吸收熱源介質之潛熱,之後在水流已昇溫的情形下進一步吸收熱源介質之顯熱,因此其溫度可以有效突破既有技術溫度大約在55℃左右的限制,達成提高水溫及節省能源之目的;惟,以上之實施說明及圖式所示,僅舉例說明本創作之較佳實施例而已,並非以此侷限本創作;舉凡與本創作之構造、裝置、特徵等近似或相雷同者,均應屬本創作之創設目的及申請專利範圍之內,謹此聲明。In summary, the creation allows the water to first absorb the latent heat of the heat source medium in the preheating section, and then further absorb the sensible heat of the heat source medium when the water flow has warmed up, so that the temperature can effectively break through the existing technical temperature. The limitation of about 55 °C is achieved for the purpose of improving the water temperature and saving energy; however, the above description and drawings show only the preferred embodiments of the present invention, and are not intended to limit the creation; The approximation or similarity of the structure, installation, and features of the creation shall be within the creation purpose of the creation and the scope of the patent application. I hereby declare.

10‧‧‧加熱管10‧‧‧heating tube

11‧‧‧水流入口11‧‧‧Water inlet

12‧‧‧預熱區段12‧‧‧Preheating section

13‧‧‧高溫區段13‧‧‧High temperature section

14‧‧‧出水口14‧‧‧Water outlet

20‧‧‧熱源導管20‧‧‧heat source conduit

21‧‧‧熱源介質入口21‧‧‧Heat source media inlet

22‧‧‧顯熱釋放區段22‧‧‧ sensible heat release section

23‧‧‧潛熱釋放區段23‧‧‧ latent heat release section

24‧‧‧熱源介質出口24‧‧‧Hot source media outlet

25‧‧‧隔熱層25‧‧‧Insulation

30‧‧‧膨脹閥30‧‧‧Expansion valve

40‧‧‧蒸發器40‧‧‧Evaporator

50‧‧‧壓縮機50‧‧‧Compressor

60‧‧‧儲水桶60‧‧ ‧ water bucket

第一圖為習知熱泵式熱水器之系統示意圖。The first picture is a schematic diagram of a conventional heat pump water heater system.

第二圖為本創作熱交換裝置之第一實施例結構示意圖。The second figure is a schematic structural view of a first embodiment of the creative heat exchange device.

第三圖為本創作熱交換裝置之第二實施例結構示意圖。The third figure is a schematic structural view of a second embodiment of the creative heat exchange device.

第四圖為本創作配合一般熱泵式熱水器系統之使用示意圖。The fourth picture is a schematic diagram of the use of the general heat pump water heater system.

10‧‧‧加熱管10‧‧‧heating tube

11‧‧‧水流入口11‧‧‧Water inlet

12‧‧‧預熱區段12‧‧‧Preheating section

13‧‧‧高溫區段13‧‧‧High temperature section

14‧‧‧出水口14‧‧‧Water outlet

20‧‧‧熱源導管20‧‧‧heat source conduit

21‧‧‧熱源介質入口21‧‧‧Heat source media inlet

22‧‧‧顯熱釋放區段22‧‧‧ sensible heat release section

23‧‧‧潛熱釋放區段23‧‧‧ latent heat release section

24‧‧‧熱源介質出口24‧‧‧Hot source media outlet

25‧‧‧隔熱層25‧‧‧Insulation

Claims (5)

一種熱交換裝置,包含一供水流流通之加熱管,以及一包覆於加熱管外部供熱源介質流通之熱源導管,其中:該加熱管依水流方向依序包括一水流入口、一連接於水流入口以吸收熱源導管內熱源介質之潛熱的預熱區段、一連接於預熱區段以吸收熱源導管內熱源介質之顯熱的高溫區段,以及一連接於高溫區段以排出高溫熱水的出水口;該熱源導管依熱源介質流通方向,依序包括一與出水口相對應供熱源介質進入之熱源介質入口、一連接於熱源介質入口並且相對於加熱管的高溫區段用來釋放熱源介質之顯熱的顯熱釋放區段、一連接於顯熱釋放區段並且相對於加熱管的預熱區段用來釋放熱源介質之潛熱的潛熱釋放區段,以及一連通於潛熱釋放區段相對於水流入口的熱源介質出口。A heat exchange device comprising a heating pipe through which a water supply flow flows, and a heat source conduit covering the heat supply medium outside the heating pipe, wherein the heating pipe includes a water flow inlet and a water flow inlet in sequence according to the water flow direction. a preheating section for absorbing latent heat of the heat source medium in the heat source conduit, a high temperature section connected to the preheating section to absorb the sensible heat of the heat source medium in the heat source conduit, and a high temperature section connected to the high temperature section for discharging the high temperature hot water. The heat source conduit comprises a heat source medium inlet corresponding to the water outlet corresponding to the heat source medium, a heat source medium inlet connected to the heat source medium inlet and a high temperature section relative to the heat pipe for releasing the heat source medium according to the heat source medium circulation direction. a sensible heat sensible heat release section, a latent heat release section connected to the sensible heat release section and relative to the preheating section of the heating tube for releasing latent heat of the heat source medium, and a communication to the latent heat release section The heat source medium outlet at the water inlet. 如申請專利範圍第1項所述之熱交換裝置,其中,所述之熱源導管以及位於熱源導管內供水流流通之加熱管,二者之管體是呈直線形狀或者連續彎曲形狀。The heat exchange device according to claim 1, wherein the heat source conduit and the heating pipe through which the water supply flow flows in the heat source conduit are linear or continuously curved. 如申請專利範圍第1項所述之熱交換裝置,其中,所述之熱源導管外部披覆有一層隔熱層。The heat exchange device according to claim 1, wherein the heat source conduit is covered with a heat insulating layer. 如申請專利範圍第1項所述之熱交換裝置,其中,所述熱源導管之熱源介質出口依序連接一膨脹閥、一蒸發器、一壓縮機,再由壓縮機連接於熱源介質入口。The heat exchange device of claim 1, wherein the heat source medium outlet of the heat source conduit is sequentially connected to an expansion valve, an evaporator, a compressor, and then connected to the heat source medium inlet by the compressor. 如申請專利範圍第1項所述之熱交換裝置,其中,所述加熱管之出水口進一步連接至儲存熱水的儲水桶。The heat exchange device according to claim 1, wherein the water outlet of the heating pipe is further connected to a water storage tank storing hot water.
TW101217855U 2012-09-14 2012-09-14 Heat exchange device TWM445687U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI582369B (en) * 2014-05-12 2017-05-11 林聖梁 Heat exchanging device and water heater using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI582369B (en) * 2014-05-12 2017-05-11 林聖梁 Heat exchanging device and water heater using the same

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