M39233.0 ♦ 五、新型說明： 【新型所屬之技術領域】 本創作係有關一熱泵的結構與運用技術，尤指一種利用碳 氫冷媒進行製熱與製冷之冷熱雙效節能熱泵。 【先前技術】 一般運用於製冷製熱的熱泵，係利用熱交換手段來達到製 * 冷或製熱的目的，其中採用冷媒進行製冷與製熱的手段，係利 φ 用壓縮機推送，在此過程中使高壓高溫氣態冷媒，通過熱排裴 置，即可利用熱交換的方式來產生熱水，此時冷媒由氣態轉換 成液態而持續降溫’再經膨脹閥與冷排裝置而使冷媒迅速吸收 熱量，此時即可利用熱交換的手段來產生冷風，同時冷媒會變 相而成為氣態再導入壓縮機，而為氣液變相之循環。 准為知熱泉雖然此兼具供應40〜55度熱水、17〜18度冷氣 的功能，惟因為其冷媒的採用較不環保，且相關的壓力設定與 _ 所呈現的供水溫度又不盡理想；有鑑於此，創作人係針對熱泵 之結構技術與填充冷媒的種類及壓力值進行研究，提供一種兼 具環保的冷熱雙效節能熱泵。 【新型内容】 本創作之主要目，係在使熱泵之使用更為環保且兼具熱 水、冰水、冷氣、暖氣的供應；為達上述目的，本創作冷熱雙 效節能熱泵係在一送出碳氫冷媒的壓縮機之輸出端依序接設 3 —第一高壓管路、一熱排裝置、一第二高壓管路、一膨脹閥、 一第一低壓管路、一冷排裝置以及一第二低壓管路，該第二低 壓管係銜接於前述壓縮機之輸入端；所述第一高壓管路内之碳 氣冷媒壓力為 330〜340 psi (1 psi=0. 0702593 kg/cm2)，溫度 為攝氏70〜105度；所述熱排裝置與一第一流體供應裝置接觸 進行熱交換，第一流體供應裝置產出溫熱的流體，例如供產出 暖氣或50〜80度的熱水之用；所述冷排裝置與一第二流體供應 裝置接觸進行熱交換，使第二流體供應裝置產出冰涼之流體， 例如供產出冷氣或7〜15度的冰水之用，以充分有效的利用其 相對冷熱之供應效果。 所述第一流體供應裝置為熱水給水裝置或熱風產生機， 以達產出熱水或暖氣的效果，所述第二流體供應裝置為冰水給 水裝置或冷風產生器，以達產出冰水或冷氣的效果；其次於 第二高壓管路與膨脹閥之間可設置—乾驗，藉以過濾碳氮冷 媒中所夾雜的水分；再者，可於第二高壓管路上設置一多向控 制閥’並令該多向控制閥係銜接於一内建於冷排裝置的除霜裝 置，且可於冷排裝置結霜時對冷排裝置進行除霜之用，此外該 多向控制閥還包含-供碳氫冷媒注人的注人口，於注入口下游 ^設置-供檢罐力值之_壓力錶，細作為·與檢測碳 氫冷媒之用。 相較於-般的熱泵裝置，本創作採用較為環保的碳氯冷 媒，使得齡運作時可節省2G%^%_電量，並且所需的 M39233.0 冷媒使用量可㈣、35如上时，而_又能有效的利用執交 換效果來產线水、魏、冰水與冷氣，實為—歸顧環保的 冷熱雙效節能熱泵。 【實施方式】 以下依據本創作之技解段，縣適於本創作之實施方 式並配合圖式說明如後： 請參閱第-圖及第二騎示，係本創作第—實施例之構 成示意圖及作動流程示跡财揭示冷熱雙效節脉栗之構 成主要包含-魏機u、-第—高壓管路12、—熱排裝置13、 -第二高壓管路14、-膨關15、—第—健管路16、—冷 排裝置17以及-第二健管路18，其中熱排裝置13與一^ 一流體供應裝置21接觸進行熱交換、冷排裝置17與一第二淬 體供應裝置22接觸進行熱交換。 壓縮機1H系用以推動碳氫冷媒依序於前述第一高壓管路 12、熱排裝置13、第二高壓管路14、膨服闕15、第一低壓管 路16、冷排裝置Π以及第二低壓管路18巾進行摘環並產 生液祕氣態之父替變相、壓力變化，而由壓縮機u釋出後 依序產生高壓高溫氣態、高壓巾低溫贱態、低壓低溫液氣 態、低壓低溫液態再回流壓縮機11之循環變化。 其中第-高壓管路12内之碳氫冷媒壓力以33〇〜34〇 psi、預設工作溫度為攝氏70〜1〇5度為最佳。 5 M39233.0 熱排裝置13與第-流體供應裝置接觸進行熱交換， 可使第一流體供應裝置21產生溫熱的流體，所述第一流體供 應裝置21可為熱水給水裝置或熱風產生器其中之—以產生暖 氣或熱水’而熱水之出水溫度又以攝氏5〇〜8〇度為最佳，前述 所指第二流體供應裝置22可為冰水給水裝置、冷風產生器其 中之一，或為冰水給水裝置、冷風產生器之組合，冷排裝置 17與第二流體供應裝置22進行熱交換後可產生7〜15度的冰 水或令人涼爽的冷氣效果。藉此，使得本創作同時能利用熱交 換效果來產生熱水、冰水或冷氣、魏，而碳氫冷媒的使用還 可使熱泵運作時可節省20%~30%的用電量，並且所需的冷媒 使用量可節省35%以上的量。 請參閱第三圖及第四圖所示，係本創作第二實施例之構 成示意®及作滅程示意圖，此第二實施例細第—實施例之 技術手#又為基礎而衍生，其相異之處在於第二高壓管路14與 膨脹閥15之間設有一乾燥瓶31、第二高壓管路14上設有一 多向控制閥32，該多向控制閥32係銜接於一内建於冷排裝置 17的除霜震置33且包含一注入口 34 ’於注入口 34下游設有 一壓力錶35。 乾燥瓶31的設置能用於過濾碳氫冷媒中所夾帶的水分， 而多向控制閥32可用於切換碳氫冷媒流向除霜裝置33，以於 冷排裝置17或相關管路結霜時作為除霜之用；此外注入口 34 之設置係作為碳氫冷媒注入之用，壓力錶35係供檢測壓力值 6 之用，俾利冷熱雙效節能熱泵的組裝、維護與保養更為容易。 惟，以上所述實施說明及各圖式所示，係舉例說明本創 作之較佳實施例者，並非以此侷限本創作，例如第一流體供應 裝置21、第一流體供應裝置22之實施造型、態樣與規格可視 使用需求而予以變更。是以’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 圍之内。 【圖式簡單說明】 第一圖：本創作第一實施例之構成示意圖。 第二圖：本創作第一實絶例之作動流程示意圖。 第三圖：本創作第二實施例之構成示意圖。 第四圖：本創作第二實施例之作動流程示意圖。 【主要元件符號說明】 11壓縮機 12第一高壓管路 13熱排裝置 14第二高壓管路 15膨脹閥 M392330 16第一低壓管路 17冷排裝置 18第二低壓管路 21第一流體供應裝置 22第二流體供應裝置 31乾燥瓶 32多向控制閥 33除霜裝置 34注入口 35壓力錶M39233.0 ♦ V. New description: 【New technical field】 This creation is about the structure and application technology of a heat pump, especially a hot and cold double-effect energy-saving heat pump that uses carbon-hydrogen refrigerant for heating and cooling. [Prior Art] The heat pump generally used for cooling and heating uses the means of heat exchange to achieve the purpose of cooling or heating. The means for cooling and heating using refrigerant is to be pushed by a compressor. During the process, the high-pressure high-temperature gaseous refrigerant can be hot-discharged to generate hot water by means of heat exchange. At this time, the refrigerant is converted from a gaseous state to a liquid state and continuously cooled. Then the refrigerant is quickly expanded by the expansion valve and the cold discharge device. When the heat is absorbed, the cold air can be generated by means of heat exchange, and the refrigerant will be disguised into a gaseous state and then introduced into the compressor, which is a cycle of gas-liquid phase change. Although it has the function of supplying 40~55 degree hot water and 17~18 degree cold air, it is not environmentally friendly because of the use of the refrigerant, and the related pressure setting and the water supply temperature presented by _ are not enough. Ideally; in view of this, the creator researches the structure of the heat pump and the type and pressure value of the refrigerant, and provides an environmentally friendly double-effect energy-saving heat pump. [New content] The main purpose of this creation is to make the use of heat pump more environmentally friendly and to supply hot water, ice water, air-conditioning and heating. For the above purposes, the hot and cold double-effect energy-saving heat pump is delivered in one The output end of the compressor of the hydrocarbon refrigerant is sequentially connected to a first high pressure line, a heat exhausting device, a second high pressure line, an expansion valve, a first low pressure line, a cold row device and a a second low pressure line, the second low pressure line is connected to the input end of the compressor; the carbon gas refrigerant pressure in the first high pressure line is 330~340 psi (1 psi=0. 0702593 kg/cm2) The temperature is 70 to 105 degrees Celsius; the heat discharging device is in heat exchange with a first fluid supply device, and the first fluid supply device produces a warm fluid, for example, for heating or 50 to 80 degrees of heat. The cold discharge device is in contact with a second fluid supply device for heat exchange, so that the second fluid supply device produces a cold fluid, for example, for producing cold air or ice water of 7 to 15 degrees, Fully and effectively use its relatively hot and cold supply effect. The first fluid supply device is a hot water supply device or a hot air generator for generating the effect of hot water or heating, and the second fluid supply device is an ice water supply device or a cold air generator to produce ice. The effect of water or cold air; secondly, the second high-pressure pipeline and the expansion valve can be set-dry test to filter the moisture contained in the carbon-nitrogen refrigerant; further, a multi-directional control can be set on the second high-pressure pipeline The valve 'couples the multi-directional control valve to a defrosting device built in the cold-discharge device, and can defros the cold-discharge device when the cold-discharge device is frosted, and the multi-directional control valve further Including - the population of the injection of hydrocarbon refrigerant, downstream of the injection port ^ set - the pressure gauge for the test tank force value, fine as and with the detection of hydrocarbon refrigerant. Compared with the general heat pump device, this creation uses a more environmentally friendly carbon-chloride refrigerant, which can save 2G%^%_ electricity when working in the age, and the required amount of M39233.0 refrigerant can be (4), 35 as above. _ It can effectively use the effect of exchange to produce line water, Wei, ice water and air-conditioning, which is really a hot and cold double-effect energy-saving heat pump that is environmentally friendly. [Embodiment] The following is based on the technical solution of this creation. The county is suitable for the implementation of this creation and with the following description: Please refer to the figure - and the second riding, which is the schematic diagram of the first embodiment of the present creation. And the flow of operation shows that the composition of the hot and cold double-effect section of the pulse mainly includes - Wei machine u, - the first - high pressure pipeline 12, - the heat discharge device 13, - the second high pressure pipeline 14, - the expansion closure 15, - a first pipeline 16 , a cold discharge device 17 and a second health pipe 18 , wherein the heat exhaust device 13 is in contact with a fluid supply device 21 for heat exchange, cold discharge device 17 and a second hard body supply Device 22 is in contact for heat exchange. The compressor 1H is used to push the hydrocarbon refrigerant to the first high pressure line 12, the heat discharging device 13, the second high pressure line 14, the expansion port 15, the first low pressure line 16, the cold discharge device, and the like. The second low-pressure pipeline 18 is used for picking up the ring and generating the father of the liquid secret state for the phase change and pressure change, and is released by the compressor u to sequentially generate a high-pressure high-temperature gas state, a high-pressure towel low-temperature state, a low-pressure low-temperature liquid gas state, and a low pressure. The cyclic change of the low temperature liquid reflow compressor 11 is performed. The hydrocarbon refrigerant pressure in the first high pressure line 12 is preferably 33 〇 34 〇 psi, and the preset working temperature is 70 〜1 〇 5 degrees Celsius. 5 M39233.0 The heat-discharging device 13 is in heat exchange with the first fluid supply device, so that the first fluid supply device 21 can generate a warm fluid, and the first fluid supply device 21 can be a hot water feed device or hot air generation. The water supply temperature of the hot water is preferably 5 Torr to 8 Torr, and the second fluid supply device 22 may be an ice water water supply device or a cold air generator. One, or a combination of an ice water water supply device and a cold air generator, the cold discharge device 17 and the second fluid supply device 22 exchange heat to produce 7 to 15 degrees of ice water or a cool air-cooling effect. In this way, the creation can use the heat exchange effect to generate hot water, ice water or cold air, and the use of hydrocarbon refrigerant can save 20%~30% of the electricity consumption when the heat pump operates, and The amount of refrigerant required can save more than 35%. Please refer to the third embodiment and the fourth figure, which is a schematic diagram of the second embodiment of the present invention and a schematic diagram of the process of destroying the second embodiment, and the technical hand of the second embodiment is derived from the foundation. The difference is that a dry bottle 31 is disposed between the second high pressure line 14 and the expansion valve 15, and a multi-directional control valve 32 is disposed on the second high pressure line 14. The multi-directional control valve 32 is coupled to the inside. The defrosting device 33 is built in the cold discharge device 17 and includes an injection port 34'. A pressure gauge 35 is disposed downstream of the injection port 34. The arrangement of the drying bottle 31 can be used to filter the moisture entrained in the hydrocarbon refrigerant, and the multi-directional control valve 32 can be used to switch the flow of the hydrocarbon refrigerant to the defroster 33 for use as a frosting device 17 or associated piping. In addition, the installation of the injection port 34 is used for the injection of the hydrocarbon refrigerant, and the pressure gauge 35 is used for detecting the pressure value of 6. The assembly, maintenance and maintenance of the double-effect energy-saving heat pump is easier. However, the above description of the embodiments and the various figures are illustrative of the preferred embodiment of the present invention, and are not limited thereto, such as the first fluid supply device 21 and the first fluid supply device 22. The appearance and specifications can be changed according to the needs of use. Therefore, it is within the scope of the creation of this creation and the scope of application for patents that are similar or identical to the structure, installation, and features of this creation. [Simple description of the drawing] First figure: A schematic diagram of the composition of the first embodiment of the present creation. The second picture: the schematic diagram of the first real process of this creation. Third figure: A schematic diagram of the structure of the second embodiment of the present creation. The fourth figure is a schematic diagram of the operation flow of the second embodiment of the present creation. [Main component symbol description] 11 compressor 12 first high pressure line 13 hot exhaust device 14 second high pressure line 15 expansion valve M392330 16 first low pressure line 17 cold discharge device 18 second low pressure line 21 first fluid supply Device 22 second fluid supply device 31 drying bottle 32 multi-directional control valve 33 defroster device 34 injection port 35 pressure gauge