1293108 •指定代表圖： (一） 本案指定代表圖為：第（一）圖。 (二) 本代表圖之元件符號簡單說明： 10 30 壓縮機 21 22 熱交換器 三通電磁閥 50 儲液室 61 64 R1 R2 R3 G1 蒸發器 ΤΙ T2 管路 R3 逆止閥 膨脹閥 D1 分量電磁閥 八、本案若有化學式時，請揭示最能顯示發明特徵的化學式： 九、發明說明： 【發明所屬之技術領域】 本發明係關於將壓縮機之製冷（或製熱）過程中所產生 之熱能藉由熱交換器加以回收利用之系統及方法。亦即， 本發明係關於一種壓縮機冷凍冷氣、冷凍乾燥及製熱作業 中之熱回收系統及熱回收方法，於壓縮機製冷（或製熱）之 過程中藉由二熱交換器並聯（或串聯）設置，將其中之一熱 交換器做為熱回收裝置，以提供熱水或泳池溫水使用，另 一熱交換器做為散熱裝置者。 1293108 【先前技術】 請參閱第四圖，習用附熱回收裝置冰水機系統圖，其 係包含壓縮機1A、熱交換器1B、冷凝器ic、冰水機iD、 蓄熱槽1F、加熱裝置1G、冷卻水塔1H，藉由壓縮機ία在 製冷之過程中之冷凝器1C所散發之熱利用熱交換器iB回 收原來要排出之廢熱再輔以加熱裝置1G(電熱、重油銷爐 或瓦斯）供應熱水。 【發明内容】 本發明所欲解決之技術問題： 1 ·冷凍壓縮之系統中之四個基本組成即蒸發器、膨脹閥、 冷凝器及壓縮機。液體冷媒在蒸發器中會蒸發成氣體， 而氣體冷媒在冷凝器中會散熱冷凝成液體習用之冷來壓 縮過程中之冷凝器所散發之熱通常藉由空氣而排放於大 氣中造成溫室效應不利於環保。 2·而電能熱水器之電能與熱能轉換效率差太耗電。 3 ·而燃燒重油或瓦斯以加熱安全性差。 4·熱回收熱水溫度太低，使用時需再加熱。 5·不用空調製冷時無法製熱。 6·秋冬季節製冷能力降低，再加熱則浪費能源。 7 ·系統设計需多相考慮安全性及真正回收效率。 解決問題之技術手段及對照先前問題之功效·· 本發明於壓縮機製冷之過程中藉由二熱交換器（冷凝 器）並聯設置，將其中之一熱交換器（冷凝器）做為熱回收裝 置，而另一熱交換器（冷凝器）做為散熱裝置，並藉由三通 電磁閥自動感應熱交換器之溫度以決定熱回收裝置作動與 否’用冷氣時可回收熱能不用冷氣時可專製熱能回收，冷 氣能源散至大氣降低溫室效應，尤其應用至工商業時冷氣 1293108 -¾2¾ 修正 __補充 或製冷能力可利用於冷凍冷藏以達節省能源功效。 【實施方式】 兹為使能進一步瞭解本發明，謹配合圖式再予深入說 明於後·· 清參閲第一圖’壓縮機之冷柬冷氣實施例熱回收系統 圖，其特徵在於：壓縮機10製冷之過程中藉由二熱交換器 21 22並聯設置，將其中之一熱交換器22做為熱回收裝置， 而另一熱交換器21做為分量調整散熱裝置，藉由分量電磁 閥D1感測熱回收之冷凝溫度作分量調節保持儲液室5〇冷 凝溫度以提升冷凝效果使熱回收正常，並保持壓縮機1 〇負 荷在安全係數内，藉由三通電磁閥30自動感應熱交換器之 溫度以決定熱回收裝置或製冷裝置作動與否及回收比例。 冷媒氣體經由壓縮機1 〇後其壓力及溫度均升高，藉由三通 電磁閥30感測溫度以決定通路，當熱回收之溫度未達設定 之溫度時冷媒經由管路T1到達熱交換器22進行熱回收再 利用，其溫度高於冷卻水或冷卻空氣在特定流率下之溫 度’因而冷媒氣體能釋放出熱而冷凝成液體經由逆止閥R1 進入儲液室50，最後，液氣混合體經由膨脹閥gi進入蒸 發器61’在蒸發器61(冷凍冷氣）中液體冷媒不斷吸收冷柬 冷氣空間物鱧之熱而逐漸蒸發成氣體並經由逆止閥r3進 入壓縮機10形成一循環迴路。當熱回收之溫度已達設定之 溫度時管路Τ1關閉冷媒僅經由管路Τ2到達熱交換器21進 行散熱’其溫度高於冷卻水或冷卻空氣在特定流率下之溫 度’因而冷媒氣體能釋放出熱而冷凝成液體經由逆止閥R2 進入儲液室50。當蒸發器61 (冷凍冷氣）溫度已達設定之溫 度但仍需熱回收時，多餘之冷藉由蒸發器64進行散冷至室 外降低溫室效應。 請參閱第二圓，壓縮機之冷柬乾燥實施例熱回收系統 1293108 補凡 圖’其特徵在於：壓縮機10製冷除濕之過程中藉由二冷凝 器23 24串聯設置，將其中之一冷凝器24做為分量調整散 熱裝置，藉由分量電磁閥D2感測熱回收之冷凝溫度作分量 調節保持儲液室50冷凝溫度以提升冷凝效果使製冷及熱 回收正常並保持壓縮機10負荷在安全係數内，而另一冷凝 器23做為熱回收裝置，並藉由三通電磁閥30自動感應冷 束乾燥裝置之溫度及溼度以決定熱回收裝置作動與否者。 冷媒氣體經由壓縮機1 〇後其壓力及溫度均升高，藉由三通 電磁閥30感測溫度以決定通路，當熱回收之溫度及溼度未 達设定之溫度及渔度時冷媒經由管路T3到達冷凝器23進 行熱回收再利用’部分冷媒氣體能釋放出熱而冷凝成液體 形成液氣混合體經由逆止閥R4及逆止閥R5到達冷凝器24 再進行分量散熱後進入儲液室50，最後，液體經由膨脹閥 G3進入蒸發器62,在蒸發器62中液體冷媒進行製冷除濕， 而逐漸蒸發成氣體並進入壓縮機1〇形成一循環迴路，當熱 回收之溫度已達設定之溫度時管路T3關閉，冷媒僅經由管 路T4及逆止閥R5到達冷凝器24進行散熱，而冷媒氣體能 釋放出熱而冷凝成液體進入儲液室5〇,最後，液艘經由膨 脹閥G3進入蒸發器62，液化冷媒喷射至蒸發器62達到低 溫才能凝結空氣及物體中之水分進行製冷除濕乾燥，而逐 漸蒸發成氣體並進入壓縮機1〇形成一循環迴路。 請參閱第三圖，壓縮機之專製熱水實施例熱回收系統 圖，其特徵在於：壓縮機10製熱過程中藉由一熱交換器 25及一冷凝器26以三通電磁閥30串聯設置，藉由其中之 熱交換is 25做為熱回收裝置，藉由其中之冷凝器2 /做為 分量調整散熱裝置，藉由分量電磁閥D3動作比例熱回收之 冷凝溫度作分量調節，以降低壓縮機1 〇負荷提升效率及系 統安全，並藉由三通電磁閥30自動感應熱回收裝置以決定 修正 補充 1293108 散熱裝置作動與否。冷媒氣體經由壓縮機1〇後其壓縮熱溫 度升高’冷媒經由管路Τ7到達熱交換器25進行熱回收再 製熱’因而部分冷媒氣體能釋放出熱而冷凝成液體經由三 通電磁闕30、管路Τ5及逆止閥R6進入儲液室5〇，液體經 由膨脈闕G4進入蒸發器63,在蒸發器63中液體冷媒不斷 吸收外界空氣中之熱而逐漸蒸發成氣體進入壓縮機1〇形 成一循環迴路。經由熱交換器25熱回收後之冷媒，經由三 通電磁，30感測，當熱回收之溫度已達設定之工作壓力溫 度比時管路T5關閉冷媒僅經由管路T6到達冷凝器26進行 分量散，。藉由冷凝壓力容量調節閥pl偵測冷凝壓力及溫 度’當f外溫度偏低時製熱負荷變動造成壓縮比過低時， ，媒經高壓吐出管直接比例調整量，流回壓縮機10低壓回 管保持製熱效率不隨季節而變動，熱回收溫度達到時本 系統即自動停機，以節省能源。 ， 以上揭之本發明冷凍壓縮之熱回收系統及熱回收方 法’至少具有下列優點： 1·本發明於壓縮機製冷之過程中藉由二熱交換器（冷凝器 並聯設置，冑其中之一熱交換器（冷凝器）做為熱回收裝 =，而另一熱交換器（冷凝器）做為散熱裝置，並藉由三 、電磁閥自動感應熱交換器之溫度以決定熱回收裝置作 否用冷凍冷氣時可回收熱能，不用冷凍冷氣時可 旱’熱能回收，冷凍冷氣能源散至大氣降低溫室效應。 、·二用至工商業時冷氣或製冷能力可利用於冷 以 達節省能源功效。 之電熱、鋼爐或瓦斯加熱有較佳之安全性及經 4降低電熱氣用電量及環保。 4· ^由冷凝壓力容量調節閥偵測冷凝壓力及溫度以保 策熱效率不隨季節而變動。 1293108 5 ·重點改善是應用方面更全面實用而且系統設計安全性 及效率更精確。 綜上所述，本發明誠具極佳之進步性，而其系 法就先前技術而言，乃為突破性之創新發明，不奮為及方 異、突出之發明，爰依法申請專利。 ·一優 【圖式簡單說明】 第一圖：係本發明壓縮機之冷凍冷氣實施例熱回收系統圖 第二圖··係本發明壓縮機之冷凍乾燥實施例熱回收系統圏: 第三圖：係本發明壓縮機之專製熱水實施例熱回收系统圖: 第四圖：係習用附熱回收裝置冰水機系統圖。 【主要元件符號說明】 熱交換器 30三通電磁閥 10 壓縮機 21 22 25 冷凝器 儲液室 蒸發器 23 24 26 50 61 62 63 64 管路 逆止閥 膨脹閥 TI T2 T3 T4 T5 T6 T7 T8 R1 R2 R3 R4 R5 R6 G1 G2 G3 G4 D1 D2 D3 分量電磁閥 P1 冷凝壓力容量調節 1A 壓縮機 1B 熱交換器 1C 冷凝器 1D 冰水機 1F 蓄熱槽 1G 加熱裝置 1H 冷卻水塔 閥1293108 • Designated representative map: (1) The representative representative of the case is: (1). (2) The symbol of the symbol of this representative figure is simple: 10 30 Compressor 21 22 Heat exchanger three-way solenoid valve 50 Reservoir 61 64 R1 R2 R3 G1 Evaporator ΤΙ T2 Pipe R3 Check valve expansion valve D1 Component electromagnetic Valve 8. If there is a chemical formula in this case, please disclose the chemical formula that best shows the characteristics of the invention: IX. Description of the invention: [Technical field of the invention] The present invention relates to the process of cooling (or heating) of a compressor. A system and method for recycling thermal energy by means of a heat exchanger. That is, the present invention relates to a heat recovery system and a heat recovery method in a compressor chilled air, freeze drying and heating operation, which are connected in parallel by a heat exchanger during cooling (or heating) of the compressor (or In series, one of the heat exchangers is used as a heat recovery device to provide hot water or swimming pool warm water, and the other heat exchanger is used as a heat sink. 1293108 [Prior Art] Please refer to the fourth figure, the conventional chiller system diagram of the heat recovery device, which includes the compressor 1A, the heat exchanger 1B, the condenser ic, the chiller iD, the heat storage tank 1F, and the heating device 1G. The cooling water tower 1H recovers the waste heat originally discharged by the heat exchanger iB by the heat generated by the condenser 1C of the compressor ία during the cooling process, and is supplemented by the heating device 1G (electric heating, heavy oil furnace or gas) supply. Hot water. SUMMARY OF THE INVENTION The technical problem to be solved by the present invention is as follows: 1. The four basic components of the system for freezing compression are an evaporator, an expansion valve, a condenser and a compressor. The liquid refrigerant evaporates into a gas in the evaporator, and the gas refrigerant condenses and condenses into a liquid in the condenser. The heat emitted by the condenser during the compression process is usually discharged into the atmosphere by air, which is disadvantageous to the greenhouse effect. Environmentally friendly. 2. The electric energy water heater has poor conversion efficiency between electric energy and thermal energy. 3 · Burning heavy oil or gas to heat poorly. 4. The heat recovery hot water temperature is too low and needs to be reheated during use. 5. It is not possible to heat when it is not air-conditioned. 6. In the autumn and winter, the cooling capacity is reduced, and reheating wastes energy. 7 · System design requires multiple phases to consider safety and true recycling efficiency. Technical means for solving the problem and the effect against the previous problem · The present invention is arranged in parallel by the two heat exchangers (condensers) in the process of compressor refrigeration, and one of the heat exchangers (condensers) is used as heat recovery The other heat exchanger (condenser) is used as a heat sink, and the temperature of the heat exchanger is automatically sensed by a three-way solenoid valve to determine whether the heat recovery device is activated or not. When the cold air is used, the heat energy can be recovered without using cold air. Dedicated heat energy recovery, air-conditioning energy to the atmosphere to reduce the greenhouse effect, especially when applied to industrial and commercial air-conditioning 1293108 -3⁄423⁄4 Correction __ Supplementary or cooling capacity can be used in refrigeration to achieve energy efficiency. [Embodiment] In order to further understand the present invention, it is to be further explained in conjunction with the drawings. Referring to the first figure, the heat recovery system diagram of the cold shower system of the compressor is characterized in that: During the cooling process of the machine 10, two heat exchangers 21 22 are arranged in parallel, one of the heat exchangers 22 is used as a heat recovery device, and the other heat exchanger 21 is used as a component adjustment heat dissipation device by a component solenoid valve. D1 senses the condensing temperature of heat recovery as a component adjustment to maintain the condensing temperature of the liquid storage chamber 5〇 to improve the condensation effect, so that the heat recovery is normal, and keep the compressor 1 load load within the safety factor, and automatically induce heat by the three-way solenoid valve 30. The temperature of the exchanger determines whether the heat recovery unit or the refrigeration unit is actuated or recycled. After the refrigerant gas passes through the compressor 1, the pressure and temperature thereof rise, and the temperature is sensed by the three-way solenoid valve 30 to determine the passage. When the temperature of the heat recovery does not reach the set temperature, the refrigerant reaches the heat exchanger via the pipeline T1. 22 performing heat recovery and reuse, the temperature of which is higher than the temperature of the cooling water or the cooling air at a specific flow rate', so that the refrigerant gas can release heat and condense into liquid to enter the liquid storage chamber 50 via the check valve R1, and finally, the liquid gas The mixture enters the evaporator 61' via the expansion valve gi. In the evaporator 61 (freezing cold air), the liquid refrigerant continuously absorbs the heat of the cold space and gradually evaporates into a gas and enters the compressor 10 via the check valve r3 to form a cycle. Loop. When the temperature of the heat recovery has reached the set temperature, the line Τ1 closes the refrigerant and only reaches the heat exchanger 21 via the line Τ2 for heat dissipation 'the temperature is higher than the temperature of the cooling water or the cooling air at a specific flow rate', so the refrigerant gas can The heat is released and condensed into a liquid that enters the liquid storage chamber 50 via the check valve R2. When the temperature of the evaporator 61 (chilled air) has reached the set temperature but heat recovery is still required, the excess cold is cooled by the evaporator 64 to the outside to reduce the greenhouse effect. Please refer to the second circle, the cold shower drying embodiment of the compressor, the heat recovery system 1293108, which is characterized in that: during the refrigeration and dehumidification of the compressor 10, two condensers 23 24 are arranged in series, one of the condensers is set. 24 as a component adjustment heat sink, by the component solenoid valve D2 sensing the heat recovery condensing temperature as a component adjustment to maintain the condensing temperature of the liquid storage chamber 50 to enhance the condensation effect so that the refrigeration and heat recovery is normal and the compressor 10 load is maintained at a safety factor The other condenser 23 is used as a heat recovery device, and the temperature and humidity of the cold beam drying device are automatically sensed by the three-way solenoid valve 30 to determine whether the heat recovery device is actuated or not. After the refrigerant gas passes through the compressor 1, the pressure and temperature thereof increase, and the temperature is sensed by the three-way solenoid valve 30 to determine the passage. When the temperature and humidity of the heat recovery are less than the set temperature and the degree of fishing, the refrigerant passes through the tube. The road T3 reaches the condenser 23 for heat recovery and reuse. 'Part of the refrigerant gas can release heat and condense into a liquid to form a liquid-gas mixture. The reactor reaches the condenser 24 via the check valve R4 and the check valve R5, and then dissipates heat to enter the liquid storage. Chamber 50. Finally, the liquid enters the evaporator 62 via the expansion valve G3. In the evaporator 62, the liquid refrigerant is cooled and dehumidified, and gradually evaporates into a gas and enters the compressor 1 to form a circulation loop. When the temperature of the heat recovery has reached the set value. At the temperature, the pipe T3 is closed, and the refrigerant reaches the condenser 24 through the pipe T4 and the check valve R5 to dissipate heat, and the refrigerant gas can release heat and condense into liquid to enter the liquid storage chamber 5, and finally, the liquid tank expands. The valve G3 enters the evaporator 62, and the liquefied refrigerant is sprayed to the evaporator 62 to reach a low temperature to condense the air and the moisture in the object for cooling and dehumidifying and drying, and gradually evaporate into a gas and enter the compressor. Into a circulation loop. Referring to the third figure, a heat recovery system diagram of an exclusive hot water embodiment of a compressor is characterized in that: a heat exchanger 25 and a condenser 26 are connected in series by a three-way solenoid valve 30 during heating of the compressor 10. The heat exchange is 25 is used as a heat recovery device, and the condenser 2 / as a component adjustment heat sink is used to adjust the condensing temperature of the proportional heat recovery by the component solenoid valve D3 to reduce the compression. The machine 1 increases the load efficiency and system safety, and automatically activates the heat recovery device through the three-way solenoid valve 30 to determine whether the correction 1293108 heat sink is activated or not. After the refrigerant gas passes through the compressor, its compression heat temperature rises. 'The refrigerant reaches the heat exchanger 25 via the line Τ7 to perform heat recovery and reheating'. Therefore, part of the refrigerant gas can release heat and condense into liquid through the three-way electromagnetic 阙30. The pipe Τ5 and the check valve R6 enter the liquid storage chamber 5, and the liquid enters the evaporator 63 via the swell enthalpy G4. In the evaporator 63, the liquid refrigerant continuously absorbs the heat in the outside air and gradually evaporates into a gas into the compressor. Form a loop. The refrigerant recovered through the heat exchanger 25 is sensed via a three-way electromagnetic, 30. When the temperature of the heat recovery has reached the set working pressure temperature ratio, the line T5 closes the refrigerant and only reaches the condenser 26 via the line T6. Scattered. The condensing pressure and the temperature are detected by the condensing pressure capacity adjusting valve pl. When the heating load is changed, the compression ratio is too low, and the medium is directly adjusted by the high pressure discharging pipe, and flows back to the compressor 10 for low pressure. The heat recovery efficiency of the return pipe does not change with the season, and the system automatically stops when the heat recovery temperature is reached to save energy. The above-mentioned refrigeration compression heat recovery system and heat recovery method of the present invention have at least the following advantages: 1. The invention is provided in the process of refrigeration of the compressor by two heat exchangers (the condensers are arranged in parallel, one of which is hot The exchanger (condenser) is used as a heat recovery device, and the other heat exchanger (condenser) is used as a heat sink, and the temperature of the heat exchanger is automatically induced by the solenoid valve to determine whether the heat recovery device is used or not. When the cold air is chilled, the heat energy can be recovered. When the cold air is not used, the heat can be recovered, and the cold air energy can be released to the atmosphere to reduce the greenhouse effect. The air-conditioning or refrigeration capacity can be utilized for cooling and energy saving. Steel furnace or gas heating has better safety and reduces electricity consumption and environmental protection by 4. 4· The condensing pressure and temperature are detected by the condensing pressure capacity regulating valve to ensure that the thermal efficiency does not change with the season. 1293108 5 · The key improvement is that the application aspect is more comprehensive and practical, and the system design safety and efficiency are more accurate. In summary, the present invention has excellent progress and its As far as the prior art is concerned, the law is a breakthrough innovation. It is not an innovative and outstanding invention. It applies for patents according to law. ·一优 [Simple description of the diagram] The first picture: the compressor of the present invention REFRIGERATED AIR CONDITIONING EXAMPLES Heat Recovery System FIG. 2 is a lyophilization embodiment of the compressor of the present invention. Heat recovery system 第三: Third drawing: heat recovery system of the exclusive hot water embodiment of the compressor of the present invention: fourth Figure: Diagram of the chiller system with the heat recovery device. [Main component symbol description] Heat exchanger 30 three-way solenoid valve 10 Compressor 21 22 25 Condenser reservoir evaporator 23 24 26 50 61 62 63 64 Road check valve expansion valve TI T2 T3 T4 T5 T6 T7 T8 R1 R2 R3 R4 R5 R6 G1 G2 G3 G4 D1 D2 D3 Component solenoid valve P1 Condensing pressure capacity adjustment 1A Compressor 1B Heat exchanger 1C Condenser 1D Ice water machine 1F Heat storage tank 1G heating device 1H cooling water tower valve