TWI227774B - Heat exchanger using water's liquid-vapor phase transformation to improve heat exchange capability - Google Patents

Abstract

The present invention relates to a type of heat exchanger using water's liquid-vapor phase transformation to improve heat exchange capability. It mainly comprises a main heat exchanger, a water evaporation unit, and an auxiliary heat exchanger. A upper heat exchange tube and a lower heat exchange tube are installed on the top and the bottom, respectively, of the auxiliary heat exchanger and multiple longitudinal heat pipes are equipped to connect the upper and the lower heat exchange tubes. By using coolant and water as heat-exchange media, pre-cool/pre-heat effects on the inlet air can be accomplished. Furthermore, by using the liquid-vapor phase transformation effects generated by cooperating the auxiliary heat exchanger with the water evaporation unit, the water content of air can be increased significantly to enhance the air's heat exchange performances so as to improve the heat exchange capability of the present invention. As the results, energy saving can be accomplished and heat pollution can be minimized.

Description

1227774 五、發明說明（1)1227774 V. Description of the invention (1)

【發明之技術領域】 兩相變化增強熱交換 換器其熱交換能力， 本發明係有關於一種利用水液氣 月匕力之熱交換器’猎以有效提升熱交 進而達到節能及降低熱污染者。 先前技術： 按習式之冷凍 縮機9 ! 一冷凝器9 2、—蒸發器9 3 1控制器9 4及一冷媒切換閥9 5等元件所組 )A，盆主要由一盤管L配置一逆(或熱交換裝置 /、王要甶皿配置送風馬達Μ所組成（如楚 二圖所示），惟此習式熱交換器在運韓上名卩弟 失· 你延轉上部存有以下缺 器之盤管進行熱 ’而此高熱空氣 1 ·在排熱運替時，係利用進氣與熱交換 交換，由於熱空氣直接排放於大氣環境中 會造成環境之熱污染。 2·在溫度較低之季節（如冬季），進行吸熱運轉時由於 空氣中水份含量低’使得熱交換之過程只有顯熱交換，因 而導致熱交換能力及其效率大為降低。 【發明内容】 、[Technical Field of the Invention] Two-phase change enhances the heat exchange capacity of a heat exchanger. The present invention relates to a heat exchanger 'hunting' that uses the power of water, liquid, gas, and gas to increase heat exchange to achieve energy savings and reduce thermal pollution. By. Prior technology: According to the conventional freeze shrinking machine 9! A condenser 9 2,-evaporator 9 3 1 controller 9 4 and a refrigerant switching valve 9 5 (group A), the basin is mainly configured by a coil L Yi reverse (or heat exchange device /, Wang Yaoyi is equipped with a blower motor M (as shown in the second picture of Chu), but this type of heat exchanger is lost in Yunhan ’s famous name. You can transfer it to the upper part. The following coils are used for heating, and this high-heat air1: During the heat removal operation, the intake air is exchanged with the heat exchange, because the hot air is directly discharged into the atmospheric environment, which will cause environmental thermal pollution. 2 · 在In the lower temperature seasons (such as winter), the heat exchange process has only sensible heat exchange due to the low water content in the air during the heat absorption operation, which causes the heat exchange capacity and its efficiency to be greatly reduced. [Content of the Invention],

本案發明人有鑑於上述習式熱交換器其熱交換能力不 佳問題，歷經無數研發改良後，終於完成本案之發明，即 本發明之熱交換器，其主要由一主熱交換器、一水蒸發裝 置及一輔助熱交換器所組成，其中該輔助熱交換器之上、 下端分設有一上熱交換管體及一下熱交換管體，並以複數In view of the poor heat exchange capacity of the conventional heat exchanger, the inventor of this case has finally completed the invention of this case after numerous developments and improvements, that is, the heat exchanger of the present invention is mainly composed of a main heat exchanger, a water It consists of an evaporation device and an auxiliary heat exchanger. The upper and lower ends of the auxiliary heat exchanger are respectively provided with an upper heat exchange tube body and a lower heat exchange tube body.

1227774 五、發明說明（2) 支縱向之熱管 作為熱交換之 預熱（吸熱運 蒸發裝置所產 含水量，以増 之熱交換能力 本案之發明目 1 ·係在提供 熱交換器，使 熱交換器產生 高空氣中之含 力’使由顯熱 染者。 2 ·係在提供 熱交換器，使 助熱交換器對 的加溼，有效 器之熱交換能 以下茲配 元件及具體實 請參閱第 圖及其結構示 0内設有一主 熱交換器2 3 連通該上 介質，以 轉時）效 生之液氣 強空氣之 ，進而達 的： 一種利用 在主熱交 預冷效果 水量，藉 交換轉為 、下熱交 使進氣獲 果，再利 兩相變化 熱交換能 到節能及 水液氣兩 換器以排 ’配合水 以提昇該 潛熱交換 換管體，且藉由冷媒與水 得預冷（排熱運轉時）或 用此辅助熱交換器配合水 效應，有效提高空氣中之 力，藉以提升主熱交換器 降低熱污染者。 相變化增強熱交換能力之 熱運轉為主時，利用輔助 蒸發裝置的加溼，有效提 主熱交換器之熱交換能 ’而達到節能及降低熱污 種利用水液氣兩相變化增強熱交換能力之 父換器以吸熱運轉為主時，能利用輔 進軋產生預熱升溫效果，再配 提高空氣中之含水量，_以描斗：:、：裝置 泛卜里 稭以徒升該主熱交換 力’而達到節能效益者。 、 合圖式、圖號說明，‘細介0 A 施例如后： "，，口本發明之組成 二、四、五圖所示，係分別 意圖，本發明主要於一献換^之系統 执交換器？ 1 ,甘…換器2之機殼2 了父換$2 1、-水4發裝置2 2及—輔助1227774 V. Description of the invention (2) A vertical heat pipe is used as preheating for heat exchange (the water content produced by the endothermic transport evaporation device is based on the heat exchange capacity of the invention. The invention's objective 1 in this case is to provide a heat exchanger to enable heat exchange. The sensible heat is generated by the high-efficiency generator in the air. 2 · It is provided with a heat exchanger to humidify the auxiliary heat exchanger pair. The heat exchange energy of the effective device is provided with the following components and specific details. The diagram and its structure show that there is a main heat exchanger 2 3 in the upper medium to communicate with the upper medium in order to transfer the time. The effective liquid-gas-strength air is achieved: The exchange is changed to the lower heat exchange to obtain the intake air, and then the two-phase change heat exchange energy can be used to save energy and the water-liquid-air converter to discharge the water to enhance the latent heat exchange tube body. It must be pre-cooled (when exhaust heat is running) or use this auxiliary heat exchanger with water effect to effectively increase the force in the air, thereby enhancing the main heat exchanger to reduce heat pollution. When the phase change enhances the heat exchange capacity, when the thermal operation is mainly used, the humidification of the auxiliary evaporation device is used to effectively increase the heat exchange energy of the main heat exchanger to achieve energy saving and reduce thermal pollution. Use water, liquid and gas two-phase changes to enhance heat exchange When the father of the ability is mainly heat-absorbing, it can use pre-rolling to produce a pre-heating effect, and then increase the moisture content in the air. Heat exchange force 'to achieve energy saving benefits. The combined drawings and figure numbers indicate, 'Detailed introduction of 0 A after the example: ", the composition of the present invention is shown in Figures 2, 4, and 5, which are intended respectively. Switch? 1, Gan ... changer 2 case 2 changed the parent to $ 2 1, water 4 hair device 2 2 and-auxiliary

1227774 五、發明說明（3) 一主熱交換器2 1 ，係配置有一送風機24，而其内 部設有熱交換盤管210，且在上端與一第一冷媒輸送管 L f相接’可供系統循環冷媒r之流經，而其下端經由一 第二冷媒輸送管L 2，而與該輔助熱交換器2 3之下熱交 換2 3 2連通，而在第二冷媒輸送管^ 2上分流一第 一 ^管1^21 、一第二分管L22 ，且該第一分管L21 上設有一冷媒流量控制器2 1 5，該第二分管L 2 2上設 有一冷媒電磁止閥2 1 4 ;1227774 V. Description of the invention (3) A main heat exchanger 2 1 is provided with a blower 24, and a heat exchange coil 210 is arranged inside, and a first refrigerant conveying pipe L f is connected at the upper end. The system circulates the flow of refrigerant r, and its lower end communicates with the heat exchanger 2 3 2 below the auxiliary heat exchanger 2 3 through a second refrigerant conveying pipe L 2, and splits on the second refrigerant conveying pipe ^ 2. A first ^ pipe 1 ^ 21, a second branch pipe L22, and a refrigerant flow controller 2 1 5 is provided on the first branch pipe L21, and a refrigerant electromagnetic check valve 2 1 4 is provided on the second branch pipe L 2 2;

一水蒸發裝置2 2，係提供水與進氣形成水蒸發效應 、置、其上方设一出水頭2 2 1接設一第一輸送水管2 ^ 7 ’並與該輔助熱交換器2 3相接，以供進水貿利用出 ^頭2 2 1直接喷出水霧，或以出水頭2 2 i延接一本體 $ 〇 ’而該+體2 2 0係由具有透氣性及滲水性材質所 =成，可提供空氣通過時與水分子產生熱交換及加溼作 另該水蒸發裝置2 2之底部設有一集水盤2 2 2，該 送1Ϊ522底部接設一第二輸送水管224與-第三輸 交拖i = 2 3接設，該第三輸送水管2 2 3則與該辅助熱 管？、^ 3之上熱交換管體2 3 1接設，而該第三輸送水 ^23上設有一水泵225; 、A water evaporation device 22 is used to provide water and intake air to form a water evaporation effect. A water outlet head 2 2 1 is arranged above the first water delivery pipe 2 ^ 7 ′ and is in phase with the auxiliary heat exchanger 2 3. Then, for the water inlet to use the outlet head 2 2 1 to spray water mist directly, or to extend a body $ 0 'with the outlet head 2 2 i, and the + body 2 2 0 is made of a breathable and water-permeable material The result is that it can provide heat exchange and humidification with water molecules when air passes through. The bottom of the water evaporation device 2 2 is provided with a water collecting pan 2 2 2. The bottom of the sender 1 522 is connected with a second water pipe 224 and- The third transmission link i = 2 3 is connected, and the third water pipe 2 2 3 is connected to the auxiliary heat pipe? ^ 3 heat exchange pipe body 2 3 1 is connected, and the third water delivery ^ 23 is provided with a water pump 225;

的兮:辅助熱交換器2 3，係位於水蒸發襞置2 2進氣4 埶=μ丄其上、下端分設有一上熱交換管體2 3 1、一-上官體2 3 2，並以複數支縱向之熱管2 3 3連通3 換；：換管體2 3 1及下熱交換管體2 3 2，而該上熱; 、吕體2 3 1之中段橫設有複數支分管2 3 i i，該複jXi: the auxiliary heat exchanger 2 3, which is located in the water evaporation unit 2 2 inlet 4 埶 = μ 丄 there is an upper heat exchange tube 2 3 1 at the upper and lower ends, and an upper body 2 3 2 and A plurality of vertical heat pipes 2 3 3 are connected and exchanged ;: the pipe body 2 3 1 and the lower heat exchange pipe body 2 3 2 and the upper heat are provided; 3 ii ， 此 复 j

第6頁 1227774 五、發明說明（4)Page 6 1227774 V. Description of the invention (4)

支分管23 1 1兩端分別與第一容室23 14、第二容·室 2315相通，並以隔板231 2、2313封閉各分管 231 1以外之外圍區域231 6 ，使該外圍區域23 1 6與熱管2 3 3相通，且其内則填充有第一冷媒介質R 1 ，而第一容室2314則與第三輸送水管223相接， 第二容室2 3 1 5則與第一輸送水管2 2 7相接，而下熱 交換管體2 3 2之中段橫設有複數支分管2 3 2 1，該複 數支分管2321兩端分別與第三容室2324、第四容 室2325相通，並以隔板23 22、2323封閉各分 管2321以外之外圍區域23 16 ，使該外圍區域23The two ends of the branch pipe 23 1 1 communicate with the first container chamber 23 14 and the second container chamber 2315 respectively, and the peripheral areas 231 6 other than the branch pipes 231 1 are closed by partitions 231 2 and 2313, so that the peripheral area 23 1 6 communicates with the heat pipe 2 3 3, and is filled with the first cold medium R 1, and the first container chamber 2314 is connected with the third conveying water pipe 223, and the second container chamber 2 3 1 5 is connected with the first conveying pipe. The water pipes 2 2 7 are connected, and the middle part of the lower heat exchange pipe body 2 3 2 is provided with a plurality of branch pipes 2 3 2 1 horizontally. The two ends of the plurality of branch pipes 2321 communicate with the third container chamber 2324 and the fourth container chamber 2325 respectively. And close the peripheral area 23 16 outside each branch 2321 with partition plates 23 22 and 2323, so that the peripheral area 23

2 6與熱管2 3 3相通，其内則填充有第一冷媒介質R 1 ，而第三容室2324則與第三冷媒輸送管L3相接， 第四’容室2 3 g 5則與第二冷媒輸送管L 2相接；2 6 communicates with the heat pipe 2 3 3, which is filled with the first refrigerant medium R 1, and the third container chamber 2324 is connected with the third refrigerant transport pipe L3, and the fourth 'capacitor chamber 2 3 g 5 is connected with the first The two refrigerant conveying pipes L 2 are connected;

藉由上述元件之組成，當主熱交換器2 1以排熱運轉 為主時，系統循環冷媒R由第一冷媒輸送管L 1流入主熱 交換器21(如第三、四圖中箭頭所指流向）之熱交換盤 管2 1 0，並自其下端第二冷媒輸送管L2、第二分管L 2 2流入該輔助交換器2 3之下熱交換管體2 3 2 (此時 第二分管L2 2上之冷媒電磁止閥$ 1 4，因受控制器C 之控制呈打開狀態），再由第四容室2 3 2 5經由各分管 2321 ，流往第三容室2324，此時各分管232 1 内之系統循環冷媒R，與外圍區域2 3 2 6之第一冷媒介 質R 1因溫差效應而產生熱交換作用（即產生蒸發作用 )，而上熱交換管體231内之第一容室2314内之進With the composition of the above components, when the main heat exchanger 21 is mainly used for heat removal operation, the system circulating refrigerant R flows into the main heat exchanger 21 from the first refrigerant conveying pipe L 1 (as indicated by the arrows in the third and fourth figures). Refers to the flow direction) of the heat exchange coil 2 1 0, and flows into the heat exchange tube body 2 3 2 below the auxiliary exchanger 2 3 from the second refrigerant conveying pipe L2, the second branch pipe L 2 2 at its lower end (the second at this time The refrigerant electromagnetic check valve $ 1 4 on the branch L2 2 is opened because it is controlled by the controller C), and then flows from the fourth container chamber 2 3 2 5 to the third container chamber 2324 through each branch pipe 2321. The system circulates the refrigerant R in each branch 232 1 and the first refrigerant medium R 1 in the peripheral area 2 3 2 6 generates a heat exchange effect (that is, generates an evaporation effect) due to a temperature difference effect. Inside a room 2314

1227774 發明說明（5) 欠亦經由各分管2 3 1 1流往第二容室2 3 1 5 ，雨 各刀吕2 3 1 1内之進水w，與外圍區域2 3 1 6之第一 冷媒介質R1因溫差效應亦產生熱交換作用（即產生冷凝 得縱向之熱管233内之第一冷媒介質R1產 然對流之循環效應，使經過熱管2 3 3之進氣發生排 二作用，即當上熱交換管體2 31内之進水W與第 系‘△二，2 1之熱交換，大於下熱交換管體2 3 2内之 交換/、第一冷媒介質R 1之熱交換時，且該輔助熱 助執4ΐ度係低於進入^氣之溫度時，進氣在該補 内：獲得預冷效果；χ當上熱交換管體231 換管體2 S ^第一冷媒介質R 1之熱交換，係小於下熱交 換時，且該辅統？媒尺與第一冷媒介fR 1之熱交 ^ 、父換器之溫度高於進入之空氣溫产昧 進軋在該輔助執交 门％八1工轧/皿度蛉， 度拉高，2"3由於顯熱作用效果而將空氣溫 而增加空氣中之欠==7蒸發裝置2 2以獲得加溼效果， 熱交換能力，=藉此有*提升主熱交換Ml之 者。 此達到節能及降低對環境的熱污染程度 當主熱交換5§ 9， ν R由第三冷媒輸送管L::熱f轉為2 ’系統循環冷媒 換管體2 3 2 3流入辅助熱交換器2 3 媒 由其第三容室，二、四圖中虚線箭頭所指流了熱交 冷媒流量控制器言ΐ輸送管l2、第-分管C 丄5 w入主熱交換器2 1 , 21、 此時冷媒電1227774 Description of the invention (5) The owe also flows to the second container 2 3 1 5 through the branches 2 3 1 1, the water inlet w in the rain 2 3 1 1 and the first in the peripheral area 2 3 1 6 The cold medium substance R1 also generates heat exchange effect due to the temperature difference effect (that is, the first cold medium substance R1 in the longitudinally condensed heat pipe 233 generates a convection cycle effect, which causes the exhaust air passing through the heat pipe 2 3 3 to have a second effect, that is, when When the heat exchange between the water W in the upper heat exchange pipe body 2 31 and the system '△ 2, 2 1 is greater than the heat exchange in the lower heat exchange pipe body 2 3 2 /, the heat exchange between the first cold medium substance R 1, In addition, when the temperature of the auxiliary heat assist is lower than the temperature of entering the air, the intake air is in the supplement: the pre-cooling effect is obtained; χ when the heat exchange tube body 231 is replaced with the tube body 2 S ^ the first cold medium R 1 The heat exchange is less than the lower heat exchange, and the auxiliary system? The heat exchange between the medium scale and the first cold medium fR 1 ^, the temperature of the parent converter is higher than the incoming air. Door% 8 1 work roll / dish degree 蛉, degree is high, 2 " 3 increases air temperature due to sensible heat effect == 7 evaporation device 2 2 to obtain Humidification effect, heat exchange capacity, = which has the effect of * improving the main heat exchange M1. This achieves energy saving and reduces the degree of heat pollution to the environment. When the main heat exchange is 5§ 9, ν R is provided by the third refrigerant pipe L: : The heat f is changed to 2 'The system circulation refrigerant exchange pipe body 2 3 2 3 flows into the auxiliary heat exchanger 2 3 The medium flows from its third chamber, and the hot and cold refrigerant flow controllers are indicated by the dotted arrows in the second and fourth figures. The water pipe l2, the first branch pipe C, 5w enter the main heat exchanger 2 1, 21, and the refrigerant electricity at this time

2325,並自第_4、各分管2321，流向 丄再 1227774 五、發明說明（6) 磁止閥2 1 4受控制器C之控制 3 2 1内之系統循環冷媒R與外 媒介質R1 ，因溫差效應產生熱 在下熱交換管體2 3 2内排熱， 熱蒸發，相對的上熱交換管體2 之進水W，亦經各分管2 3 1 1 使各分管2 3 1 1内之進水W與 冷媒介質R1 ’因溫差效應產生 )，即進水W在上熱交換管體2 上昇，使得縱向之熱管233内 自然對流循環效果；由於進氣為 交換器23的熱管233内之第 於進氣溫度，夺熱交換作用下進 過水蒸發裝置2 2時，由於水與 渥效果，而有效增加進氣其空氣 換器21其熱交換能力的提升， 綜上所述，本發明無論主熱 轉，皆能利用水液氣兩相變化增 熱交換器之運轉效率，能達到節 程度等進步效益者。 在較佳實施例之詳細說明中 以方便說明本發明之技術内容， 於上述實施例，在不超出本發明 範圍的情況下，所作的種種變化 呈關閉狀態）， 圍區域2 3 2 β 交換，即系統德 而第一冷媒介質 3 1之 流向第 外圍區 熱交換 3 1内 之第一 低溫低 一冷媒 氣會產 進氣因 中的含 而達到 交換器 強熱交 能岌降 第一容室 二容室2 域2 3 1 (即產生 進行吸熱 冷媒介質 溼之空氣 介質R 1 生升溫預 水蒸發效 水量，以 節能效益 是在吸熱 換能力， 低對環境 所提出之具體實 而非將本發明狹 之精神與下述之 實施，仍屬於本 各分管2 之第一冷 環冷媒R R 1則吸2 3 14 3 15, 6之第一 冷凝作用 而令水溫 R 1形成 ’辅助熱 的溫度高 熱，再經 應獲得加 利主熱交 者。 或排熱運 藉以提升 的熱污染 施例僅用 義地限制 申請專利 發明之範2325, and from the _4, each branch 2321, flow to 丄 1227774 V. Description of the invention (6) The magnetic stop valve 2 1 4 is controlled by the controller C 3 2 1 The system circulates the refrigerant R and the external medium R1, Due to the temperature difference effect, heat is discharged in the lower heat exchange pipe body 2 3 2 and the heat evaporates. The water inflow W of the upper heat exchange pipe body 2 is also passed through each of the branch pipes 2 3 1 1 The inlet water W and the cold medium R1 'are generated by the temperature difference effect), that is, the inlet water W rises on the upper heat exchange pipe body 2, so that the natural convection circulation effect in the longitudinal heat pipe 233; because the air intake is in the heat pipe 233 of the exchanger 23 At the temperature of the intake air, when it passes through the water evaporation device 22 under the effect of heat exchange, due to the effect of water and water, it effectively increases the intake air and the heat exchange capacity of its air exchanger 21. In summary, the present invention Regardless of the main heat transfer, those who can use water-liquid-gas two-phase changes to increase the operating efficiency of the heat exchanger can achieve progressive benefits such as savings. In the detailed description of the preferred embodiment to facilitate the description of the technical content of the present invention, in the above embodiment, the various changes made are in the closed state without exceeding the scope of the present invention), the surrounding area is exchanged by 2 3 2 β, That is to say, the flow of the first refrigerant medium 31 in the system to the first peripheral zone of the heat exchange 31. The first low temperature and low refrigerant gas in the 1 will generate the intake air due to the inclusion of the refrigerant, which will reach the heat exchange capacity of the exchanger and drop the first container. Two-capacity room 2 domain 2 3 1 (that is, the heat-generating pre-water evaporation effect water volume that generates endothermic cold medium wet air medium R 1. The energy-saving benefit is the ability to absorb heat and change the environment. The spirit of the invention and the following implementation still belong to the first cold ring refrigerant RR 1 of each branch 2 and absorb the first condensation effect of 2 3 14 3 15, 6 to make the water temperature R 1 form an auxiliary heat temperature. If the heat is high, the heat should be obtained by the main heat exchanger of California. Or the heat pollution by heat removal can be used to limit the scope of patent application.

1227774 五、發明說明（7) 圍。 〇 S II 11 第ίο頁 \； 1227774 圖式簡單說明 〔圖式說明〕 第一圖，係習 第二圖，係習 第三圖，係本 第四圖，係本 第五圖，係第 〔圖號說明〕 熱交換器·· 主熱交換器· 冷媒電磁止閥 冷媒流量控制 水蒸發裝置· 出水頭··· 第三輸送水管 水泵· · · · 輔助熱交換器 分管·· 隔板·· 第一容室 外圍區域 分管·· 隔板·· 第三容室 外圍區域 式冷凍空調系統圖。 式冷凍空調熱交換器剖視圖。 發明其熱交換器之剖視圖。 發明其輔助熱交換器之剖視圖 四圖之 I剖視圖 2 2 機殼· · · 熱交換盤管 2 0 2 10 器 2 2 4 5 ❹ 2 2 本 體 2 2 0 2 2 1 集 水 盤 參 • • 2 2 2 2 2 3 第 二 輸 送 水 管 2 2 4 2 2 5 第 一 輸 送 水 管 2 2 7 2 3 上 熱 交 換 管 體 2 3 1 2 3 1 1 2 3 1 2、 2 3 1 3 2 3 1 4 第 二 室 • • · 2 3 1 2 3 1 6 下 熱 交 換 管 體· 2 3 2 2 3 2 1 2 3 2 2 2 3 2 4 2 3 2 6 2 3 2 3 第四容室 熱管· · 2 3 2 5 2 3 31227774 V. Description of Invention (7). 〇S II 11 page \\ 1227774 Brief description of the diagrams [Illustration of the diagrams] The first picture, the second picture, the third picture, the fourth picture, the fifth picture, and the [ Description of drawing number] Heat exchanger ·· Main heat exchanger · Refrigerant electromagnetic check valve · Refrigerant flow control water evaporation device · Outlet head · · · Third delivery water pipe pump · · · · Auxiliary heat exchanger branch · · Baffle · · Peripheral area of the first storage room is divided into ... · Partitions ... Sectional view of a freezer air-conditioning heat exchanger. A sectional view of the invention heat exchanger. Sectional view of the auxiliary heat exchanger invented. Section I of the fourth figure. 2 2 Chassis · · · Heat exchange coil 2 0 2 10 Device 2 2 4 5 ❹ 2 2 Body 2 2 0 2 2 1 Gathering pan ginseng • • 2 2 2 2 2 3 Second water pipe 2 2 4 2 2 5 First water pipe 2 2 7 2 3 Upper heat exchange pipe body 2 3 1 2 3 1 1 2 3 1 2, 2 3 1 3 2 3 1 4 Second Room • • 2 3 1 2 3 1 6 Lower heat exchange tube body 2 3 2 2 3 2 1 2 3 2 2 2 3 2 4 2 3 2 6 2 3 2 3 Fourth chamber heat tube 2 3 2 5 2 3 3

第11頁 1227774 圖式簡單說明 送風機· · · · 2 4 習式之冷凍空調系統·· 9 壓縮機· · · · 9 1 冷凝器·，··92 蒸發器*···93 冷媒流量控制器· · · · 9 4 冷媒切換閥·· 9 5Page 111227774 Schematic description of blower ···· 2 4 Freezer Air Conditioning System · 9 Compressor · · · 9 1 Condenser ··· 92 Evaporator * ·· 93 Refrigerant Flow Controller 9 4 Refrigerant switching valve 9 5

熱交換器· · · Α 控制器· · · · CHeat exchanger · Α controller · · · C

盤管.....L 第一冷媒輸送管···.L1 第二冷媒輸送管····L2 第一分管第二分管.....L22 第三冷媒輸送管·.L3 送風馬達···Μ 系統循環冷媒· R 第一冷媒介質.R1 ▼Coil ..... L First Refrigerant Conveying Pipe ... L1 Second Refrigerant Conveying Pipe ... L2 First Dividing Pipe Second Sub ......... L22 Third Refrigerant Conveying Pipe ... L3 Air Supply Motor ·· M system circulating refrigerant · R The first refrigerant. R1 ▼

進水.....WWater in ..... W

第12頁Page 12

Claims (1)

1227774 六、申請專利範圍 ---- 口 1 · 一種利用水液氣兩相變化增強熱交換能力之熱爻 換器，其主要係由一主熱交換器、一水蒸發裝置及一辅助 熱交換器所組成，其中： 一一主熱交換器，其係配置有一送風機，而其内部設有 熱交換盤管，可供系統循環冷媒之流經； 一水蒸發裝置’係提供水與進氣形成水蒸發效應之裝 置，使空氣通過時能與水分子產生熱交換及加溼作用； 一輔助熱交換器，係位於水蒸發裝置進氣側的前方， 其上、下端分設有一上熱交換管體、一下熱交換管體，並 以複數支縱向之熱管連通該上熱交換管體及下熱交換管 | 體，，該上熱交換管體之中段橫設有複數支分管，該複數 支分管，端分別與第一容室、第二容室相通，並以隔板封 閉各分官以外孓外圍區域，使該外圍區域與熱管相通，且 ，内則填充有第一冷媒介質，而第一容室則與第三輸送水-管相接，第二容室則與第一輸送水管相接，而下熱交換管 體之中段橫設有複數支分管，該複數支分管兩端分別與第 三容室、第四容室相通，並以隔板封閉各分管以外之外圍 區域，使該外圍區域與熱管相通，且其内則填充有第一冷 媒介質，而第二容室則與第三冷媒备送管相接，第四容 則與第二冷媒輸送管相接。 || 2 .如申請專利範圍第1項所述之「利用水液氣兩相 變化增強熱交換能力之熱交換器」，其中該水蒸發裝置之 出水頭延接一本體，該本體係由具有透氣性及滲水性 所製成。 貝1227774 VI. Scope of patent application-口 1 · A heat exchanger using two phases of water, liquid and gas to enhance heat exchange capacity, which is mainly composed of a main heat exchanger, a water evaporation device and an auxiliary heat exchange It consists of: a main heat exchanger, which is equipped with a blower, and a heat exchange coil is arranged inside the system to allow the system to circulate the refrigerant; a water evaporation device is provided to form water and air intake. The water evaporation effect device can make the air exchange with the water molecules to produce heat and humidification effect when passing through; an auxiliary heat exchanger is located in front of the inlet side of the water evaporation device, and an upper heat exchange tube is arranged on the upper and lower ends. The upper and lower heat exchange tubes are connected by a plurality of longitudinal heat pipes, and the upper and lower heat exchange tubes are connected by a plurality of longitudinal heat pipes. A middle branch of the upper heat exchange tube body is provided with a plurality of branch pipes, and the plurality of branch pipes The ends are in communication with the first and second chambers, respectively, and the peripheral areas of the outer walls of the subdivisions are closed by partitions, so that the peripheral areas communicate with the heat pipes, and the interior is filled with the first cold medium, and the first Content It is connected with the third conveying water-pipe, the second container is connected with the first conveying water pipe, and the middle section of the lower heat exchange pipe body is provided with a plurality of branches, and the ends of the plurality of branches are respectively connected with the third container. The fourth container room is in communication with each other, and the peripheral area outside each branch is closed by a partition, so that the peripheral area is in communication with the heat pipe, and the first container is filled with the first refrigerant, and the second container is connected with the third refrigerant. The delivery tube is connected, and the fourth container is connected to the second refrigerant delivery tube. || 2. As described in item 1 of the scope of the patent application, "a heat exchanger that enhances heat exchange capacity by using two-phase change of water, liquid and gas", wherein the water outlet of the water evaporation device is extended to a body, the system consists of Made of breathability and water permeability. shell 1227774 六、申請專利範圍 3 ·如申請專利範圍第1項所述之「利用水液氣兩相 變化增強熱交換能力之熱交換器」，其中該主熱交換器其 上端與一第一冷媒輸送管相接。 4 ·如申請專利範圍第1項所述之「利用水液氣兩相 變化增強熱交換能力之熱交換器」，其中該主熱交換器下 端接設有一第二冷媒輸送管，該第二冷媒輸送管並與輔助 熱交換器相接。 5 ·如申請專利範圍第1項所述之「利用水液氣兩相 變化增強熱交換能力之熱交換器」，其中該水蒸發裝置之1227774 VI. Scope of patent application 3 · As described in item 1 of the scope of patent application, "a heat exchanger that uses two phases of water, liquid and gas to enhance heat exchange capacity", wherein the upper end of the main heat exchanger is transported with a first refrigerant The pipes are connected. 4 · As described in item 1 of the scope of patent application, "a heat exchanger using two phases of water, liquid and gas to enhance heat exchange capacity", wherein a lower end of the main heat exchanger is provided with a second refrigerant conveying pipe, and the second refrigerant The pipe is connected to the auxiliary heat exchanger. 5 · "Heat exchanger using water, liquid and gas two-phase change to enhance heat exchange capacity" as described in item 1 of the scope of patent application, wherein the water evaporation device