201217728 六、發明說明： 【發明所屬之技術領域】 本發明係有關於一種利用低階熱能產生電力及冷來之裝 置與方法，尤指涉及一種使用者可依據電力或冷凍之需求藉由 兩個可控制閥件（如三通閥）改變工作流體流向，進行冷電、 冷凍、發電或空轉等運轉模式之切換，俾使系統熱能達至最適 且最多元化之利用，以充分發揮節能功效，並減少溫室氣體排 放者。 參 【先前技術】 隨著科技之進步與人口之增加，能源消耗亦遠較往日大 幅提昇。過度使用化石能源，造成大量排放二氧化碳導致溫室 效應’使得全球氣候變化異常《因此，解決能源缺乏問題與減 少溫室氣體排放已漸成為國際社會之一大挑戰，更是人類追求 永續生存之瓶頸所在；解決之道，除了開發再生能源外，舊能 源之節用亦為一大重點。過去對於舊能源節用上總強調減少能 ^ 源浪費與提高能源轉換效率兩方向，直至近年來隨著能源轉換 技術之提高，方漸有廢熱能回收再利用之相關技術產生，亦使 能源缺乏問題出現一道新曙光。 對於溫度超過500°C之高階（High Grade)廢熱，一般係 藉由複循環發電（Combined Cycle Power Generation)或熱電 混合（Combined Heat and Power, CHP)作為其廢熱再利用之 裝置。然而，對於溫度小於300°C之低階（Low Grade)廢熱， 例如普遍存在一般工業製程中之溶融、乾燥、熱處理、蒸汽及 燃燒等，少見有經濟有效之熱回收方法。一般而言，低階廢熱 201217728 無法直接轉換至工廠製程或發電循環中，使得多數工薇總直接 將其排放至大氣’僅少數X廠採以將其導人熱交換器（驗 Exchanger)或復熱器（Recuperat〇r)等熱回收裝置再利用。 此類熱與收裝置需要特別設計，方能與製程相容，且只能作為 熱能利用。S此U熱能时裝置，有細倾環（〇rganic Rankine Cycle, ORC)系統逐漸受到重視，其可將低階熱能轉 換成高階能源一電力。此有機朗肯循環係藉由熱力學上之傳統 朗肯蒸氣動力循環發展而出，其運用於蒸氣動力廠或蒸氣引擎 φ 已行之多年’以解決習知卡諾循環（Carnot Cycle)無法對工 作流體產生完全相變化之問題；由於一般廢熱之熱能等級無法 適用於蒸汽朗肯循環以輸出功率發電，因此以其它工作流體例 如有機溶劑等取代水，以形成一有機朗肯循環，而可將中低溫 之廢熱轉換成電力輸出，並可發展成電薇，用以進行工業廢熱 發電、地熱發電，甚至太陽熱能發電等。 根據台電資料顯示，住/商兩部門之耗電量，至2005年 已達全國總用電量之31%，其中住宅佔20%，商業則佔ιι〇/0， • 而當中又以空調與照明用電佔有極高之比例。因此，有效地將 低階熱能轉換成電力及冷凍，將有助於解決能源缺乏問題及減 少溫室氣體之排放。 傳統為回收低階之熱能’如工業廢熱或餘熱、太陽熱能 或地熱等，常利用有機朗肯循環作為熱功轉換之裝置，請參閱 第3圖所示，係習見有機朗肯循環裝置2之基本元件，包含加 熱模組2 0、發電模組2 1、冷凝模組22及加壓泵浦2 3。 上述加熱模組2 0係由鍋爐2 01與熱源2 0 2所組成，該熱 源2 0 2係將流經該鍋爐2 01内之液態工作流體加熱成高 201217728 壓氣態工作流體。該發電模組2 1係由該膨脹渦輪2 1 1與該 發電機2 1 2所組成，由該加熱模組2 0產生之高壓氣態工作 流體可推動該膨脹渦輪2 1 1作功，同時帶動該發電機2 1 2 產生電力。而該冷凝模組2 2係由冷凝器2 2 1與冷卻水塔2 2 2所組成’其作功後之中壓氣態工作流體進入該冷凝器2 2 1 ’被該冷卻水塔2 2 2循環之冰水冷凝為液態工作流體，最 後經該加壓泵浦2 3增壓後送入該加熱模組2 0。當運用時， 上述熱源2 0 2係可為工業廢熱、太陽熱能或地熱等，並採用 有機碳氫化合物、無機小分子化合物（如C02及nh3等）或 含氟氣碳之化合物作為工作流體，將低階熱能之熱能轉換為有 用之機械能或電能；然而’由於低階熱能之溫度低，使得整體 裝置之熱效率並不高，而且只能提供作為產生電力使用。 為提升整體之系統效能，由中華民國專利證書第209954 號提出之一種能量產生方法，請參閱第4圖所示，係習見可提 高熱功效率之循環裝置3 β此裝置3係利用三個熱交換器3 〇 1之蒸發模組3 0、兩個渦輪311之渦輪發電機組31、冷 凝模組3 2、及兩個加壓泵浦3 31之增壓栗組3 3，形成一 種單迴路多重壓力之系統。然後，利用工作流體多重壓力循環 及熱交換器之安排，雖可降低熱源及系統之不可逆性，且其多 重壓力循環藉由混合器34之使用，能有效利用過熱蒸汽，提 升能源使用率及熱效率；惟其熱能轉換亦只侷限於產生電力。 有鑑於此，故，一般習用者係無法符合使用者於實際使 用時之所需，實有必要設計一改良式之有機朗肯循環系統之熱 能利用裝置，以使熱能達至最適利用並有效節能，可同時發電 又兼製冷，不僅節省能源消耗亦可降低溫室氣體排放，無疑是 201217728 此相關研發領域所亟需面對之課題。 【發明内容】 本發明之主要目的係在於，克服習知技藝所遭遇之上述 問題並提供一種讓使用者可依據電力或冷凍之需求以改變流 經其中之工作流體流向，進行冷電、冷凍、發電或空轉等運轉 模式之切換，俾使系統熱能達至最適且最多元化之利用，以充 分發揮節能功效之利用低階熱能產生電力及冷凍之裝置與方 法。 本發明之次要目的係在於，提供一種產生電力與製冷效 果之利用低階熱能產生電力及冷象之裝置與方法。 · 本發明之另一目的係在於，提供一種僅產生電力之熱能 利用裝置。 本發明之再一目的係在於，提供一種僅產生製冷效果之 熱能利用裝置。 本發明之又一目的係在於，提供一種可以空轉之熱能利 用裝置。 本發明之又一目的係在於，提供一種可使系統熱能達至 最適利用並具有節能效果且能降低溫室氣㈣放之有機朗肯 循環與喷射式冷凍系統之熱能利用裝置。 為達以上之目的，本發明係一種利用低階熱能產生電力 及冷康之裝置與方法，係以適當之排列連接一加難組一發 電模組、一·器、—熱交換H 一冷賴組、-低溫蒸發器、 -加壓聚浦、-儲液槽等及兩個可控制工作流體流向之閥件。 透過該熱交換n ’膨麵輪出σ中縫態卫佩體餘熱可以預 201217728 熱加熱模組入口之液態工作流體，藉此，使熱效率得以增加· 同時’使用者亦可依據電力或冷凍之需求藉該兩個可控制間件 改變工作流體流向，進行冷電、冷凍、發電或空轉等運轉模式 之切換，俾使系統熱能達至最適且最多元化之利用，以充分發 揮節能功效，並減少溫室氣體排放。 【實施方式】 請參閱『第1圖及第2圖』所示，係分別為本發明於一 較佳實施例之整體架構示意圖、及本發明於一較佳實施例之噴 射器剖視示意圖。如圖所示：本發明係一種利用低階熱能產生 電力及冷束之裝置與方法1，係藉由兩個可控制工作流鱧流向 之閥件（如二通閥）18、19連接一加熱模組1〇、一發電 模組1 1、一喷射器1 2、一熱交換器1 3、一冷凝模組1 4、 一低溫蒸發器1 5、一儲液槽1 6及一加壓泵浦1 γ所構成^ 讓使用者可依據電力或冷凍之需求改變流經其中之工作流體 流向以決定運轉模式，俾使系統熱能達至最適且最多元化之利 用，以充分發揮節能功效，並減少溫室氣體排放，其中，該工 作流體係可為有機碳氫化合物、無機小分子化合物或含氟氣碳 之化合物，且該無機小分子化合物並可為二氧化碳（c〇2)及 氨氣（nh3)。 上述所提之加熱模組i 0係由一鍋爐i i與一熱源丄 0 2組成。其中’該熱源i 〇 2係可為卫業廢熱或餘熱、太陽 熱能或地熱。 該發電模組11係由-膨脹渦輪111及-發電機11 2組成，其入口端係與該加熱模組10之出口端連接。 201217728 绝該噴射器12係由一喷嘴121、-混合區122、一 = ”23、-擴散區124、一拙吸口 125、一入口 及-出口端127組成，其人σ端126係與該發電 =1之出口端連接。其中，該喷射器12本身具有壓縮機 广係利用高黯體之可虔縮流氣體動力學作用來完成壓縮 過程，並非採用機械裝置達成_作用，因此該喷射器i 2係 一種利用赫進行氣财縮之熱卿式雜組件於構造上無 機械動件，可具有較高之可靠度。 Φ 該熱交換器13之入口端係與該嘴射器12之出口端1 2 6連接，而其出口端則係與該冷凝模組14連接。 該冷凝模組1 4係由-冷凝器χ 4 χ及—冷卻水塔丄4 2組成，其入口端係與該熱交換器i 3之出口端連接。 該低溫蒸發H15之人口端係與該冷凝模組i4之出口 端連接，而其出口端則係與該喷射器i 2之抽吸口125連 接，並於入口端具有一節流閥i 5工。 該儲液槽16之入口端係與該冷凝模組i 4之出口端連 • 接。 該加壓泵浦17之入口端係透過該儲液槽i 6與該冷凝 模組1 4之出口端連接，而其出口端則係透過該熱交換器1 3 與該加熱模組10連接。 該兩個可控制閥件18、19係用以改變工作流體流 向，進行冷電、冷凍、發電或空轉等運轉模式之切換，其至少 包括有設置於該加熱模組1〇與該發電模組i丄間之第一閥 件1 8、以及設置於該發電模組1i與該喷射器}2間之第二 閥件1 9。其中，該第一閥件χ 8係可接收該加熱模組；!^ 〇之 [S] 9 201217728 出口端流出之氣態χ作流體，並改變該氣紅作流體 ^括流往該發電模組！ ！或該第二閥件i 9 ;該第二閥^ ° ’ 係可接收該發電模組；L i或該第—閥件i 8流出之氣離工= 流體’並改魏氣態X作流想之流向，包括流往該喷射器' ^ 或該冷凝模組14^ β201217728 VI. Description of the Invention: [Technical Field] The present invention relates to a device and method for generating electric power and cold using low-order thermal energy, and more particularly to a user who can use two according to the demand of electric power or freezing. The control valve member (such as three-way valve) can change the working fluid flow direction, and switch between operation modes such as cold electricity, freezing, power generation or idling, so that the system heat energy can be optimally and diversified, so as to fully exert energy-saving effects. And reduce greenhouse gas emissions. Participation [Prior Art] With the advancement of technology and the increase in population, energy consumption is much higher than in the past. Excessive use of fossil energy, causing a large amount of carbon dioxide emissions, causing the greenhouse effect 'to make global climate change abnormal. Therefore, solving energy shortages and reducing greenhouse gas emissions has gradually become a major challenge for the international community, and it is the bottleneck for human beings to pursue sustainable survival. In addition to the development of renewable energy, the use of old energy is also a major focus. In the past, for the old energy festival, the emphasis was placed on reducing energy waste and improving energy conversion efficiency. Until the energy conversion technology has been improved in recent years, the related technologies of waste heat recovery and reuse have gradually emerged, which has also caused energy shortage. A new dawn appeared. For high-grade waste heat with a temperature exceeding 500 °C, it is generally used as a waste heat reuse device by Combined Cycle Power Generation or Combined Heat and Power (CHP). However, for low grade waste heat of less than 300 ° C, such as melting, drying, heat treatment, steam and combustion in general industrial processes, it is rare to have a cost-effective heat recovery method. In general, low-level waste heat 201217728 cannot be directly converted to the factory process or power generation cycle, so that most of the workers will directly discharge them to the atmosphere. Only a few X plants use them to introduce heat exchangers (Exchanger) or complex A heat recovery device such as a heat exchanger (Recuperat〇r) is reused. Such heat and receiver devices need to be specially designed to be compatible with the process and can only be used as thermal energy. S This U thermal energy device, with a fine tilting cycle (ORC) system, has gradually gained attention, which can convert low-order thermal energy into high-order energy-electricity. This organic Rankine cycle is developed by the thermodynamically traditional Rankine steam power cycle, which has been used in steam power plants or steam engines for many years to solve the problem that the Carnot Cycle cannot work. The problem of complete phase change of the fluid; since the thermal energy level of general waste heat cannot be applied to the steam Rankine cycle to generate electricity at the output power, the water is replaced by other working fluids such as organic solvents to form an organic Rankine cycle, which can be The low-temperature waste heat is converted into electric power output, and can be developed into electric steam for industrial waste heat power generation, geothermal power generation, and even solar thermal power generation. According to Taipower's data, the electricity consumption of the residential/commercial sector has reached 31% of the country's total electricity consumption by 2005, of which 20% is residential and ιι〇/0 is used for commercial use. Lighting electricity accounts for a very high proportion. Therefore, effectively converting low-order thermal energy into electricity and refrigeration will help solve energy shortages and reduce greenhouse gas emissions. Traditionally, in order to recover low-order heat energy, such as industrial waste heat or waste heat, solar heat or geothermal heat, organic Rankine cycle is often used as a device for thermal power conversion. Please refer to Figure 3 for the organic Rankine cycle device. The basic component includes a heating module 20, a power generation module 2 1, a condensation module 22, and a pressurized pump 23. The heating module 20 is composed of a boiler 201 and a heat source 220 which heats the liquid working fluid flowing through the boiler 210 into a high-pressure working fluid of 201217728. The power generating module 2 1 is composed of the expansion turbine 2 1 1 and the generator 2 1 2 , and the high-pressure gaseous working fluid generated by the heating module 20 can push the expansion turbine 2 1 1 to work, and simultaneously drive The generator 2 1 2 generates electricity. The condensing module 2 2 is composed of a condenser 2 2 1 and a cooling water tower 22 2, after which the medium-pressure gaseous working fluid enters the condenser 2 2 1 'cycled by the cooling water tower 2 2 2 The ice water is condensed into a liquid working fluid, and finally pressurized by the pressurized pump 23 and sent to the heating module 20. When used, the heat source 2 0 2 may be industrial waste heat, solar heat or geothermal, etc., and use organic hydrocarbons, inorganic small molecule compounds (such as C02 and nh3, etc.) or fluorine-containing carbon compounds as working fluids. The thermal energy of low-order thermal energy is converted into useful mechanical energy or electrical energy; however, due to the low temperature of the low-order thermal energy, the thermal efficiency of the overall device is not high and can only be provided as a power generation. In order to improve the overall system performance, an energy generation method proposed by the Republic of China Patent Certificate No. 209954, as shown in Fig. 4, is a circulation device that can improve the efficiency of thermal power. The evaporator module 30 of the exchanger 3 〇1, the turbine generator set 31 of the two turbines 311, the condensation module 3 2, and the booster pump set 3 3 of the two pressurized pumps 3 31 form a single loop multiple The system of stress. Then, using the multiple pressure cycles of the working fluid and the arrangement of the heat exchanger, although the irreversibility of the heat source and the system can be reduced, and the multiple pressure cycles are used by the mixer 34, the superheated steam can be effectively utilized, and the energy utilization rate and thermal efficiency can be improved. However, its thermal energy conversion is limited to generating electricity. In view of this, the general practitioners cannot meet the needs of the user in actual use, and it is necessary to design a thermal energy utilization device of an improved organic Rankine cycle system to achieve optimal utilization and energy saving. It can simultaneously generate electricity and cool, not only saving energy consumption but also reducing greenhouse gas emissions. This is undoubtedly a problem that needs to be faced in this related research and development field in 201217728. SUMMARY OF THE INVENTION The main object of the present invention is to overcome the above problems encountered in the prior art and to provide a user with the ability to change the flow of the working fluid flowing therethrough according to the demand of electric power or freezing, for cold electricity, freezing, Switching between operation modes such as power generation or idling, so that the system heat energy can be optimally and diversified, so as to fully utilize the energy-saving device and method for generating electricity and freezing using low-order heat energy. A secondary object of the present invention is to provide an apparatus and method for generating electric power and cooling images using low-order thermal energy to generate electric power and cooling effects. Another object of the present invention is to provide a thermal energy utilization device that generates only electric power. A further object of the present invention is to provide a thermal energy utilization device that produces only a refrigeration effect. It is still another object of the present invention to provide a thermal energy utilization device that can be idling. Another object of the present invention is to provide a thermal energy utilization device which can optimize the thermal energy of the system and which has an energy saving effect and can reduce the greenhouse gas (4) organic Rankine cycle and the jet refrigeration system. For the purpose of the above, the present invention is a device and method for generating electric power and cold-consumption using low-order thermal energy, and is connected to a difficult-to-group, a power generation module, a device, and a heat exchange H-cooling group in an appropriate arrangement. , - low temperature evaporator, - pressurized polypu, - liquid storage tank, etc. and two valve parts that can control the flow of working fluid. Through the heat exchange n 'expansion wheel out of the σ mid-span state, the residual heat of the body can pre-201217728 hot heating module inlet liquid working fluid, thereby increasing the thermal efficiency · At the same time, the user can also rely on electricity or freezing The two controllable parts are used to change the flow direction of the working fluid, and the operation modes such as cold electricity, freezing, power generation or idling are switched, so that the system heat energy can be optimally and diversified to fully utilize the energy saving effect, and Reduce greenhouse gas emissions. [Embodiment] FIG. 1 is a schematic view showing the overall structure of a preferred embodiment of the present invention, and a schematic cross-sectional view of the injector according to a preferred embodiment of the present invention. As shown in the figure, the present invention is a device and method 1 for generating electric power and cold beam by using low-order thermal energy, which is connected by a valve member (such as a two-way valve) 18, 19 which can control the flow of two working flows. Module 1 , a power generation module 1 1 , an injector 1 2 , a heat exchanger 13 , a condensation module 14 , a cryogenic evaporator 15 , a reservoir 16 and a pressure pump The composition of Pu 1 γ allows the user to change the flow of the working fluid flowing through it according to the demand of electricity or freezing to determine the operation mode, so that the system heat can be optimally and diversified to fully utilize the energy saving effect. Reducing greenhouse gas emissions, wherein the workflow system can be an organic hydrocarbon, an inorganic small molecule compound or a fluorine-containing carbonaceous compound, and the inorganic small molecule compound can be carbon dioxide (c〇2) and ammonia (nh3) ). The above-mentioned heating module i 0 is composed of a boiler i i and a heat source 丄 0 2 . Wherein the heat source i 〇 2 system can be waste heat or waste heat, solar heat or geothermal heat. The power generation module 11 is composed of an expansion turbine 111 and a generator 11 2 , and an inlet end thereof is connected to an outlet end of the heating module 10 . 201217728 The injector 12 is composed of a nozzle 121, a mixing zone 122, a = "23, a diffusion zone 124, a suction port 125, an inlet and an outlet end 127, and the human σ end 126 is connected to the power generation. The outlet end of the =1 is connected, wherein the ejector 12 itself has a compressor that utilizes the colloidal flow gas dynamics of the sorghum body to complete the compression process, and does not use a mechanical device to achieve the action, so the injector i 2 is a kind of heat-clearing component that utilizes He's gas to shrink and has no mechanical moving parts, which can have higher reliability. Φ The inlet end of the heat exchanger 13 and the outlet end of the mouthpiece 12 1 2 6 is connected, and the outlet end thereof is connected to the condensation module 14. The condensation module 14 is composed of a condenser χ 4 χ and a cooling water tower 丄 4 2, and the inlet end is connected to the heat exchange. The outlet end of the low temperature evaporation H15 is connected to the outlet end of the condensation module i4, and the outlet end thereof is connected to the suction port 125 of the injector i2, and is connected to the inlet end. There is a throttle valve i. The inlet end of the liquid storage tank 16 is connected to the condensation module i 4 The outlet end of the pressurized pump 17 is connected to the outlet end of the condensation module 14 through the reservoir i 6 , and the outlet end thereof passes through the heat exchanger 13 The two controllable valve members 18, 19 are used to change the flow direction of the working fluid, and perform switching modes such as cold electricity, freezing, power generation or idling, and at least include the heating module 1 a first valve member 18 between the power generating module and a second valve member 19 disposed between the power generating module 1i and the injector 2, wherein the first valve member 8 The heating module can be received; !^ 〇[S] 9 201217728 The gaseous state flowing out at the outlet end is used as a fluid, and the gas red is changed to flow to the power generation module!! or the second valve member i 9 The second valve ^ ° ' can receive the power generation module; Li or the first valve member i 8 out of the air separation = fluid 'and change the Wei gas X flow direction, including flow to the injection ' ^ or the condensation module 14^ β
當本發明採冷電模式運轉時，該第一間件工8與該第二 閥件1 9之流向均控制為“連通，由該第—閥件i 8'^該^ 態工作流體流向該發電模組1 1 ’而該第二閥件1 9令該氣離 工作流體流向該器i 2。運料，以上述加熱模組^ 熱其鋼爐1 Q 1内之液態玉作流體，使成為高溫高壓之氣態工 作流體。該氣態工作流體流出該鍋爐i 0 i後，經過該第:閥 件之a-b迴路，進入該發電模組1 1，藉該高溫高壓之氣態工 作流趙在該膨脹渴輪1 1 1内作功同時，帶動該發電機11 2 輸出電力’並由該膨脹渦輪1 11流出之中溫中壓之氣態工作 hi·體，經該第二閥件1 9之a-b迴路，進入該喷射器1 2 ,將 經由其入口端126進入之中溫中壓之氣態工作流體，逐漸膨 脹並加速，於該喷嘴121出口處加速成低壓超音速氣流，與 透過該抽吸口12 5抽引由該低溫蒸發器15流出之低麼氣 態工作流體，將此兩股氣流在該混合區12 2内，經混合與動 量交換後，形成超音速混合氣流，經過在該等截面區12 3產 生震涑，壓力驟升，然後流入該擴散區1 2 4中繼續減速並升 壓。上述低壓氣態工作流體因此被壓縮至該出口端12 7之中 壓混合氣態工作流體。流出該喷射器1 2之中壓混合氣態工作 流體隨即進入該熱交換器1 3 ’將以其餘熱預熱該加壓泵浦1 7出口之液態工作流體，俾以達到同時減少該加熱模組1 〇與 201217728 該冷凝模組1 4之負擔。繼之，該氣態工作流體進入該冷凝模 組1 4之冷凝器1 4 1中，由該冷卻水塔1 4 2循環之冰水冷 凝為液態工作流體。冷凝後之液態工作流體，其中一部分經該 節流閥1 5 1流入該低溫蒸發器1 5，藉蒸發吸熱而產生製冷 效果，令内部之液態工作流體蒸發而形成低壓氣態工作流體。 另由該冷凝器1 4 1流出之其餘冷凝液態工作流體，則流入該 儲存槽1 6中儲存’使該儲液槽1 6有足夠之液態工作流體提 供該加壓系浦1 7運轉而免其空轉損壞，再經由該加壓泵浦1 7送回該加熱模組1 〇中繼續受熱蒸發，完成一熱力循環，同 時發電和製冷。 當採冷康模式運轉時’該第一閥件1 8之流向控制為a_c 連通’而該第《一間件1 9之流向控制為a-b連通，由該第一閥 件1 8係令該氣態工作流體流向該第二閥件1 9 ,而該第二閥 件1 9令該氣態工作流體流向該喷射器1 2，使流出該鍋爐1 0 1之氣態工作流體，經過該第一閥件丄8ia_c迴路，旁通 該發電模組1 1 ’經該第二閥件1 9之a-b迴路，進入該喷射 器1 2，其餘同上述冷電模式，經該熱交換器i 3進入該冷凝 模組14後，分別藉流入該低溫蒸發器丄5產生製冷，以及透 過該加壓栗满1 7回到該加熱模組1 〇入口，完成冷象模式循 環；此時，本裝置1僅產生製冷效果。 當採發電模式運轉時，該第一閥件i8之流向控制為“ 連通，而該第二閥件1 9之流向控制為a_c連通，由該第一閥 件1 8係令該氣態工作流體流向該發電模組1 1，而該第二閥 件1 9令該氣態工作流體流向該冷凝模組1 4，使流出該銷爐 1 0 1之氣態工作流體，經過該第一閥件1 8之a-b迴路，進 201217728 入該發電模組1 1產生電力，並使流出該膨脹渦輪i丄丄之中 溫中壓之氣態工作流體，經該第二閥件丄9之㈣迴路，旁通 該喷射器12，經該熱交換器χ 3進入該冷凝模組丄4。其餘 同上述冷電模式，透過該加壓泵浦！ 7_該加減组丄〇入 口，完成發電模式循環；此時，本裝置i僅產生電力。 畲採空轉模式運轉時H閥件丨8與該第二間件丄 9之流向均控制為a-c連通，由該第一閥件1 8令該氣態工作 流禮流向該第二閥件1 9 ’而該第二閥件丄9令該氣態工作流 • 體流向該冷凝模組14，使流出該鍋爐玉〇 χ之氣態工作流 體’經過該第一閥件1 8之a-c迴路，旁通該發電模組1 1， 經該第二閥件1 9之a-c迴路，旁通該喷射器1 2 ,經該熱交 換器1 3進入該冷凝模组1 4。其餘同上述冷電模式，透過該 加壓泵浦17回到該加熱模組1〇入口，完成空轉模式循環； 此時，本裝置1暨無製冷效果亦無電力輸出。 由上述可知，本發明係一種結合有機朗肯循環與喷射式 冷凍系統之熱能利用裝置，可應用於工業廢熱或餘熱、太陽熱 # 能或地熱等低階熱源。其係以適當之排列連接一加熱模組、一 發電模組、一喷射器、一熱交換器、一冷凝模組、一低溫蒸發 器、一加壓泵浦、一儲液槽等及兩個可控制工作流體流向之閥 件。透過該熱交換器，膨脹渦輪出口中壓氣態工作流體餘熱可 以預熱加熱模組入口之液態工作流體，藉此，使熱效率得以增 加；同時，使用者亦可依據電力或冷凍之需求藉該兩個可控制 閥件改變工作流艎流向，進行冷電、冷凍、發電或空轉等運轉 模式之切換，俾使系統熱能達至最適且最多元化之利用，以充 分發揮節能功效，並減少溫室氣體排放。 [s] 12 201217728 综上所述’本發明係一種利用低階熱能產生電力及冷象 之裝置與方法，可有效改善習用之種種缺點，係藉由兩個可控 制閥件改變工作流體流向，進行冷電、冷凍、發電或空轉等運 轉模式之切換，讓使用者可依據電力或冷凍之需求改變流經其 中之工作流體流向以決定運轉模式，俾使系統熱能達至最適且 最多元化之利用，以充分發揮節能功效，並減少溫室氣體排 放，進而使本發明之産生能更進步、更實用、更符合使用者之 所須，確已符合發明專利申請之要件，爰依法提出專利申請。 惟以上所述者’僅為本發明之較佳實施例而已，當不能 以此限定本發明實施之範圍；故，凡依本發明申請專利範圍及 發明說明書内容所作之簡單的等效變化與修飾，皆應仍屬本發 明專利涵蓋之範圍内。 【圖式簡單說明】 第1圖’係本發明於一較佳實施例之整體架構示意圖。 第2圖，係本發明於一較佳實施例之喷射器剖視示意圖。 第3圖，係習見之有機朗肯循環裝置示意圖。 第4圖，係習見可提高熱功致率之循環裝置示意圖。 【主要元件符號說明】 (本發明部分） 熱能利用裴置1 加熱模組1〇 鍋爐1 0 1 熱源1 0 2 發電模組11 [S] 13 201217728 膨脹渦輪111 發電機112 喷射器1 2 喷嘴1 2 1 混合區12 2 等截面區12 3 擴散區12 4 抽吸口12 5 • 入口端12 6 出口端12 7 熱交換器13 冷凝模組14 冷凝器141 冷卻水塔14 2 低溫蒸發器15 節流閥151 φ 儲液槽16 加壓泵浦17 第一閥件18 第二閥件19 (習用部分） 有機朗肯循環裝置2 加熱模組2 0 鍋爐2 0 1 熱源2 0 2 14 201217728 發電模組21 膨脹渦輪211 發電機212 冷凝模組2 2 冷凝器2 21 冷卻水塔2 2 2 加壓泵浦2 3 可提高熱功效率之循環裝置3 蒸發模組30 熱交換器3 01 渦輪發電機組31 渴輪3 1 1 冷凝模組3 2 加壓泵浦3 31 增壓泵組3 3When the cold-charging mode of the present invention is operated, the flow direction of the first piece of the workpiece 8 and the second valve piece 19 are both controlled to be "connected, and the working fluid flows from the first valve member i 8" The power generation module 1 1 'and the second valve member 19 causes the gas separation working fluid to flow to the device i 2 . The material is heated by the heating module to heat the liquid jade in the steel furnace 1 Q 1 The high temperature and high pressure gaseous working fluid flows out of the boiler i 0 i , passes through the ab loop of the first valve member, enters the power generating module 1 1, and the high temperature and high pressure gaseous working flow Zhao expands in the expansion While the thirsty wheel 1 1 1 works, the generator 11 2 outputs electric power 'and flows out of the expansion turbine 1 11 from the medium-temperature medium-pressure working state, and the ab loop through the second valve member 19 And entering the ejector 12, the gaseous working fluid entering the medium-temperature and medium-pressure via the inlet end 126 thereof, gradually expanding and accelerating, accelerating into the low-pressure supersonic flow at the outlet of the nozzle 121, and passing through the suction port 12 5 pumping the low-level working fluid flowing out of the low-temperature evaporator 15, and mixing the two streams in the mixture In the junction 12 2 , after mixing and momentum exchange, a supersonic mixed gas flow is formed, and after the vibration is generated in the cross-sectional area 12 3 , the pressure is suddenly increased, and then flows into the diffusion zone 1 24 to continue decelerating and boosting. The low-pressure gaseous working fluid is thus compressed to the intermediate-pressure mixed working fluid at the outlet end 12. The medium-pressure mixed working fluid flowing out of the ejector 12 then enters the heat exchanger 13 3 'will be preheated with the remaining heat The liquid pumping fluid of the outlet of the pump 17 is pumped to reduce the burden of the heating module 1 〇 and the condensing module 14 of 201217728. Then, the gaseous working fluid enters the condensing module 14 In the condenser 141, the ice water circulated by the cooling water tower 142 is condensed into a liquid working fluid. The condensed liquid working fluid, a part of which flows into the low-temperature evaporator 15 through the throttle valve 151, Evaporating heat to produce a cooling effect, causing the internal liquid working fluid to evaporate to form a low-pressure gaseous working fluid. The remaining condensed liquid working fluid flowing out of the condenser 141 flows into the storage tank 16 for storage. The liquid storage tank 16 has sufficient liquid working fluid to provide the pressurized system to operate without idling damage, and then sent back to the heating module 1 through the pressurized pump 1 to continue to be heated and evaporated. Completing a thermodynamic cycle, simultaneous power generation and cooling. When the cold mode is running, 'the flow control of the first valve member 18 is a_c communication' and the flow control of the first component 19 is ab communication. The first valve member 18 is configured to flow the gaseous working fluid to the second valve member 19, and the second valve member 19 causes the gaseous working fluid to flow to the injector 12 to cause a gaseous state to flow out of the boiler 110. The working fluid passes through the first valve member 丄8ia_c circuit, bypasses the power module 1 1 'through the ab loop of the second valve member 19, enters the ejector 12, and the rest is in the same cold power mode as the After entering the condensing module 14, the heat exchanger i3 is cooled by flowing into the low-temperature evaporator 丄5, and is returned to the inlet of the heating module 1 through the pressurized chestnut 17 to complete the cold image mode cycle; At this time, the device 1 produces only a cooling effect. When the power generation mode is running, the flow direction of the first valve member i8 is controlled to be "connected, and the flow direction of the second valve member 19 is controlled to be a_c communication, and the first valve member 18 is configured to flow the gaseous working fluid. The power module 1 1 and the second valve member 19 direct the gaseous working fluid to the condensing module 14 to pass the gaseous working fluid flowing out of the pin furnace 110 through the first valve member 18. The ab circuit enters the power generation module 1 1 in 201217728 to generate electric power, and causes the gaseous working fluid flowing out of the expansion turbine to be warmed and medium-pressured, bypassing the injection through the (four) circuit of the second valve member 丄9 The heat exchanger 进入3 enters the condensing module 丄4 through the heat exchanger 。3. The rest is the same as the above-mentioned cold power mode, through the pressure pumping! 7_ the addition and subtraction group 丄〇 inlet, complete the power generation mode cycle; The device i generates only electric power. In the idling mode, the flow direction of the H valve member 丨8 and the second member 丄9 are both controlled to ac, and the first valve member 18 causes the gaseous working flow to flow to the first a second valve member 99 and the second valve member 丄9 causes the gaseous working fluid to flow to the condensing module 14 The gaseous working fluid of the boiler jade passes through the ac circuit of the first valve member 18, bypasses the power generating module 1 1, passes through the ac circuit of the second valve member 19, bypasses the injector 1 2, the heat exchanger 13 enters the condensation module 14. The rest is the same as the above-mentioned cold electricity mode, and the pressure pump 17 is returned to the inlet of the heating module 1 to complete the idle mode cycle; The device 1 has no cooling effect and no power output. It can be seen from the above that the present invention is a thermal energy utilization device combining organic Rankine cycle and jet refrigeration system, and can be applied to low-order industrial waste heat or waste heat, solar heat energy or geothermal heat. a heat source, which is connected to a heating module, a power generation module, an injector, a heat exchanger, a condensation module, a cryogenic evaporator, a pressurized pump, a liquid storage tank, etc. Two valve members for controlling the flow of the working fluid. Through the heat exchanger, the residual heat of the gaseous working fluid in the outlet of the expansion turbine can preheat the liquid working fluid at the inlet of the heating module, thereby increasing the thermal efficiency; Can also The demand for electricity or refrigeration can be changed by the two controllable valve members to change the flow direction of the working flow, such as cold electricity, freezing, power generation or idling, so that the system heat can be optimally and diversified to fully utilize To achieve energy-saving effects and reduce greenhouse gas emissions. [s] 12 201217728 In summary, the present invention is a device and method for generating electricity and cold images using low-order heat energy, which can effectively improve various disadvantages of the conventional use. The controllable valve member changes the flow direction of the working fluid, and performs switching modes such as cold electricity, freezing, power generation or idling, so that the user can change the flow of the working fluid flowing through it according to the demand of electric power or freezing to determine the operation mode. The system heat energy is optimized and most diversified to fully exert energy-saving effects and reduce greenhouse gas emissions, so that the invention can be more advanced, more practical and more suitable for users, and has indeed met the invention patent. For the requirements of the application, the patent application is filed according to law. However, the above description is only a preferred embodiment of the present invention, and the scope of the present invention is not limited thereto; therefore, the simple equivalent changes and modifications made in accordance with the scope of the present invention and the contents of the description of the present invention All should remain within the scope of the invention patent. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing the overall structure of the present invention in a preferred embodiment. Figure 2 is a schematic cross-sectional view of an injector of a preferred embodiment of the present invention. Figure 3 is a schematic diagram of the organic Rankine cycle device. Figure 4 is a schematic diagram of a circulation device that can improve the thermal power efficiency. [Explanation of main component symbols] (Part of the present invention) Thermal energy utilization device 1 Heating module 1 Boiler 1 0 1 Heat source 1 0 2 Power generation module 11 [S] 13 201217728 Expansion turbine 111 Generator 112 Ejector 1 2 Nozzle 1 2 1 mixing zone 12 2 equal section zone 12 3 diffusion zone 12 4 suction port 12 5 • inlet end 12 6 outlet end 12 7 heat exchanger 13 condensation module 14 condenser 141 cooling water tower 14 2 low temperature evaporator 15 throttling Valve 151 φ Reservoir 16 Pressure pump 17 First valve member 18 Second valve member 19 (used part) Organic Rankine cycle device 2 Heating module 2 0 Boiler 2 0 1 Heat source 2 0 2 14 201217728 Power module 21 Expansion turbine 211 Generator 212 Condensation module 2 2 Condenser 2 21 Cooling tower 2 2 2 Pressurized pump 2 3 Cycle unit for improved thermal efficiency 3 Evaporation module 30 Heat exchanger 3 01 Turbine generator set 31 Thirsty Wheel 3 1 1 condensation module 3 2 pressure pump 3 31 booster pump set 3 3
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