201215833 六、發明說明： 【發明所屬之技術領域】 種具捧漆拔 本發明係關於一種吸附式製冷裝置 制功能之吸附式製冷裝置。 為 【先前技術】 隨著經濟的發展與進步，能源 需考慮維持環境生態的前提下，如發二是隨之增〆： 的綠色能源實在是目前世界共同關注的=斜環境不造成心’ 護的糊又特㈣_她源及環境保 二=ΓΓΓ。吸附式製冷裝置主要是由吸附床、蒸 裝置;:生裝置在不斷進行製冷時’吸附式製冷 ㈣^ 度會不斷下降，甚至有可能超過用戶端的 因此，右疋未特別針對吸附式製冷裝置的製冷效果 其’將導致無法有效利用吸附式製冷裝置、之製冷功效， 甚至還會造成浪費的問題。 獎’如何有效控·附式製冷裝置，並使得吸附式製冷 溫控制，以貼近用戶端之使用需求，實為目前需 【發明内容】 發明係*触溫控制之吸附式製冷裝置，藉由福測外 201215833 界溫度或韻式製冷裝置所產出的冰水溫度，並且當冰水溫度 低於預設溫度時即暫停製冷，以解決無法穩定控制吸附式製冷 裝置產出之冰水溫度的問題’進而達到怪溫控制之功效。 本發明係為一種恆溫控制之吸附式製冷裝置，藉由偵測外 界溫度或冰水溫度，並利用溫度作為是否要繼續製冷的控制標 =，以使得吸附式製冷裝置可以達到用戶端所歧之溫度需 求，以更貼近商業需求。 為達上述功效，本發明係提供—種怪溫控制之吸附式製冷 士置’其包括：-第-真空腔，其設置有一第—吸附床、一第 器及-第-蒸發器’其中第—吸附床具有一第一進水口 空腔内設置有一第二吸附床、-第二冷凝器及 第-蒸發㈣’其中第二吸附床具有—第二進水口及一第 水口，一第二真空腔，其頂部係與第一真空 底部接合，第三真空腔内設置有一第三基發心:J礙 :係具有-冰水入口及一冰水出口;以=路 括複數個管路及複數_件，其中管路係透過閥件遠匕 並且水路結構係用以同時將—熱水導人第— 、’ 水導入第二吸附床，或者同時將冷水導人第—吸附^將冷 導入第二吸附床;其中，當一外界溫度或冰水出一 度低於一預設、;® ρ _ μ # 之冰水溫 吸附床^ 卩科導人冷錢人第二”床或第一 藉由本發明的實施，至少可達到下列進步功效： 本發明根據外界溫度或冰水溫度之高低料_暫停製 201215833 冷之依據，進而達到恆溫控制之功效。 二、藉由恆溫控制之機制，以使得吸附式製冷裝置能產出穩定 溫度的冰水，以貼近商業需求。 為了使任何熟習相關技藝者了解本發明之技術内容並據 以實施，且根據本說明書所揭露之内容、申請專利範圍及圖 式，任何熟習相關技藝者可輕易地理解本發明相關之目的及優 點，因此將在實施方式中詳細敘述本發明之詳細特徵以及優 【實施方式】 第1圖為本發明第一實施例之恆溫控制之吸附式製冷裝置 之第一狀態示意圖。第2圖為本發明第一實施例之恆溫控制之 吸附式製冷裝置之第二狀態示意圖。第3圖為本發明第一實施 例之恆溫控制之吸附式製冷裝置之暫停製冷狀態示意圖。第4 圖為本發明第二實施例之恆溫控制之吸附式製冷裝置之第一 狀態示意圖。第5圖為本發明第二實施例之恆溫控制之吸附式 製冷裝置之第二狀態示意圖。第6圖為本發明第二實施例之恆 溫控制之吸附式製冷裝置之第三狀態示意圖。第7圖為本發明 第二實施例之恆溫控制之吸附式製冷裝置之第四狀態示意 圖。第8圖為本發明第二實施例之恆溫控制之吸附式製冷裝置 之暫停製冷狀態示意圖。 如第1圖至第8圖所示，本實施例係為一種恆溫控制之吸 附式製冷裝置，其包括：一第一真空腔10; —第二真空腔20; 一第三真空腔30 ;以及一水路結構。 201215833 第一真空腔ίο，在其中係設置有一第一吸附床η、一第 一冷凝器12及一第一蒸發器13。第一吸附床η具有一第一進 水口 111及一第一出水口 Π2，而熱水或冷水則可由第一進水 口 111流入第一吸附床11中，再由第一出水口 112流出，並 配合第一冷凝器12及第一蒸發器13之作用以進行脫附或吸附 步驟。 第二真空腔20,其係與第一真空腔1〇並列設置，並且於 第二真空腔20中設置有一第二吸附床21、一第二冷凝器22 及一第二蒸發器23。類似地，第二吸附床21具有一第二進水 口 211及一第二出水口 212，而熱水或冷水則可由第二進水口 211流入第二吸附床21中，再由第二出水口 212流出，並配合 第二冷凝器22及第二蒸發器23之作用以進行脫附或吸附; 驟。 第二真空腔30，其頂部係與第一真空腔1〇及第二真空腔 20之底部接合，而第三真空腔3〇内係設置有一第三蒸發器31。 其中’第三蒸發器31係包括：至少―蒸發換熱托盤3ιι ; 以及-換熱管路3124第三蒸發器31中包括多個蒸發換熱托 盤311時，蒸發換熱托盤31丨可以上下並列設置於第三真空腔 30内，並且於每一蒸發換熱托盤311内皆承載有熱傳介質，以 利於進行熱交換。 換熱官路312則設置於每一蒸發換熱托盤311上，並且連 接於一冰水水源’以供冰水通入換熱管路312中。換熱管路Μ〕 可以祕盤繞之形式設置於每一蒸發換熱把盤311 :，並且使 蒸發換熱托盤311内之熱傳介質覆蓋換熱管路312，以利於換 201215833 熱管路312中之冰水與熱傳介f進行熱交換。 換熱管路312之—端係穿透第三蒸發器31，並作為-冰水 =口簡與冰水水源連接，而換熱管路312之另一端又再延伸 穿透出第三蒸發器31並作為一冰水出口腸，而此冰水出口 觸又可再與—用戶端設備，例如―空調設備連接，以使得吸 附式製冷裝置所產出的冰水可應用於空調設備中，但本實施例 之應用範圍並不僅限於此。 # 上述之第一蒸發器13及第二蒸發器23分別包括：至少一 蒸發器托盤13卜231 ;以及—熱傳管路132、232。與第三蒸 發器類似地，第一蒸發器13及第二蒸發器23巾也可包括 多個蒸發器托盤m、23卜並且每一蒸發器托盤m、231可 =上下並列設置於第—真空腔1G或第二真空腔2G内，而且於 每一蒸發器托盤131、231内亦承載有熱傳介質。 熱傳管路132、232，其係設置於蒸發器托盤13卜231上， 並且熱傳管路m'232之兩端分別連通於第三真空腔3〇(圖未 #示）。也就是說，熱傳管路132、232的内部係與第三真空腔3〇 連通，並且熱傳管路132、232内的熱傳介質與蒸發器托盤 13卜231上的熱傳介質並無實質上的交換，而只有熱能間的傳 遞。 上述之第一冷凝器12及第二冷凝器22係共用同一冷凝管 121而冷凝ΐ 121中係通有冷水，並且冷凝管κι係穿設於 第真二腔及第二真空腔20。因此，當第一吸附床η或第 二吸附床21通入熱水，以進行脫附步驟時，第一冷凝器12及 第二冷凝器22則可分別用以凝結第一吸附床η或第二吸附床 201215833 =:==:結後的熱傳介質可以被導流 水m包括複數歸路及複數彳明件，其中管路 係透過η件彼此連接’並且水路結構仙關時將_財導入 第一吸附床11，以使得第—吸附床η進行脫附作/，、並將一 冷水導入第二吸附床2卜以使得第二韻床21進行吸附作用 而達到製冷的效果，又或者可同時將冷水導人第—吸附床^201215833 VI. Description of the Invention: [Technical Field of the Invention] The present invention relates to an adsorption refrigeration apparatus which is a function of an adsorption refrigeration apparatus. For the [previous technology] With the development and progress of the economy, energy needs to consider the premise of maintaining the environment and ecology. For example, the second is the increase: the green energy is the common concern of the world at present. The paste and special (four) _ her source and environmental protection two = ΓΓΓ. The adsorption refrigeration device is mainly composed of an adsorption bed and a steaming device. When the raw device is continuously cooled, the adsorption refrigeration (four) degree will decrease continuously, and may even exceed the user end. Therefore, the right side is not specifically directed to the adsorption refrigeration device. The cooling effect of 'will result in the inefficient use of the adsorption refrigeration unit, the cooling effect, and even the waste. The award 'how to effectively control the attached refrigeration device, and make the adsorption refrigeration temperature control close to the user's use requirements, it is currently required [invention content] invention system * touch temperature control adsorption refrigeration device, by Fu The external temperature of 201215833 is the temperature of the ice water produced by the boundary temperature or rhythm refrigeration device, and the cooling is suspended when the ice water temperature is lower than the preset temperature to solve the problem that the temperature of the ice water produced by the adsorption refrigeration device cannot be stably controlled. 'In turn, the effect of strange temperature control. The invention relates to a constant temperature controlled adsorption refrigeration device, which can detect the external temperature or the ice water temperature and use the temperature as a control target for whether to continue cooling, so that the adsorption refrigeration device can reach the user end. Temperature requirements to be closer to business needs. In order to achieve the above-mentioned effects, the present invention provides an adsorption-type refrigeration system for controlling temperature control, which comprises: a first-vacuum chamber, which is provided with a first adsorption bed, a first device and a first-evaporator. - the adsorption bed has a first inlet cavity, a second adsorption bed, a second condenser and a first evaporation (four)' wherein the second adsorption bed has a second water inlet and a first water inlet, a second vacuum a cavity, the top of which is engaged with the first vacuum bottom, and the third vacuum chamber is provided with a third base core: a barrier: an ice water inlet and an ice water outlet; a plurality of pipelines and plurals _ piece, wherein the pipeline is through the valve member and the waterway structure is used to simultaneously introduce the hot water to the second adsorption bed, or simultaneously introduce the cold water to the second adsorption port. a second adsorption bed; wherein, when an external temperature or ice water is once lower than a preset;; ρ _ μ # of the ice water temperature adsorption bed ^ 卩科导人冷钱人 second "bed or first by this The implementation of the invention achieves at least the following advancements: The invention is based on ambient temperature or ice The temperature is high and low material _ suspension system 201215833 cold basis, and then achieve the effect of constant temperature control. Second, by the mechanism of constant temperature control, so that the adsorption refrigeration device can produce stable temperature ice water, in order to close to commercial demand. The skilled in the art will understand the technical content of the present invention and implement it, and according to the content, the scope of the patent and the drawings, the related objects and advantages of the present invention can be easily understood by those skilled in the art. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The first embodiment of the present invention is a first state diagram of a constant temperature controlled adsorption refrigeration apparatus according to a first embodiment of the present invention. 2 is a schematic diagram of a second state of the constant temperature controlled adsorption refrigeration apparatus of the embodiment. FIG. 3 is a schematic diagram of a suspended cooling state of the constant temperature controlled adsorption refrigeration apparatus according to the first embodiment of the present invention. FIG. 4 is a second embodiment of the present invention. A schematic diagram of a first state of a constant temperature controlled adsorption refrigeration device. Figure 5 is a second embodiment of the present invention. A schematic diagram of a second state of the temperature-controlled adsorption refrigeration apparatus. Fig. 6 is a third state diagram of the constant temperature controlled adsorption refrigeration apparatus according to the second embodiment of the present invention. Fig. 7 is a second embodiment of the present invention. A schematic diagram of a fourth state of the adsorption refrigeration apparatus. Fig. 8 is a schematic diagram showing the suspension state of the constant temperature controlled adsorption refrigeration apparatus according to the second embodiment of the present invention. As shown in Figs. 1 to 8, the present embodiment is The utility model relates to a constant temperature controlled adsorption refrigeration device, which comprises: a first vacuum chamber 10; a second vacuum chamber 20; a third vacuum chamber 30; and a waterway structure. 201215833 The first vacuum chamber ίο, in which the system is set There is a first adsorption bed η, a first condenser 12 and a first evaporator 13. The first adsorption bed η has a first water inlet 111 and a first water outlet Π2, and the hot water or cold water can be the first The water inlet 111 flows into the first adsorption bed 11, and then flows out of the first water outlet 112, and cooperates with the first condenser 12 and the first evaporator 13 to perform a desorption or adsorption step. The second vacuum chamber 20 is disposed side by side with the first vacuum chamber 1 , and a second adsorption bed 21 , a second condenser 22 and a second evaporator 23 are disposed in the second vacuum chamber 20 . Similarly, the second adsorption bed 21 has a second water inlet 211 and a second water outlet 212, and the hot water or cold water can flow into the second adsorption bed 21 from the second water inlet 211, and then the second water outlet 212. It flows out and cooperates with the second condenser 22 and the second evaporator 23 to perform desorption or adsorption; The second vacuum chamber 30 has a top portion joined to the bottom of the first vacuum chamber 1 and the second vacuum chamber 20, and a third evaporator 31 is disposed in the third vacuum chamber 3. Wherein the 'third evaporator 31 includes: at least the evaporative heat exchange tray 3 ιι; and the heat exchange line 3124. When the third evaporator 31 includes a plurality of evaporative heat exchange trays 311, the evaporative heat exchange tray 31 can be arranged side by side. The heat transfer medium is carried in the third vacuum chamber 30 and in each of the evaporation heat exchange trays 311 to facilitate heat exchange. The heat exchange official road 312 is disposed on each of the evaporative heat exchange trays 311 and is connected to an ice water water source for the ice water to pass into the heat exchange tubes 312. The heat exchange line Μ can be disposed in the form of a coiled heat transfer tray 311 : and the heat transfer medium in the evaporation heat exchange tray 311 covers the heat exchange line 312 to facilitate the exchange of ice in the 201215833 heat line 312 The water exchanges heat with the heat transfer f. The end of the heat exchange line 312 penetrates the third evaporator 31, and is connected as an ice water water source to the ice water source, and the other end of the heat exchange line 312 is further extended to the third evaporator 31. As an ice water outlet intestine, the ice water outlet can be connected to the customer equipment, such as "air conditioning equipment," so that the ice water produced by the adsorption refrigeration unit can be applied to the air conditioning equipment, but the implementation The scope of application is not limited to this. # The first evaporator 13 and the second evaporator 23 respectively include: at least one evaporator tray 13 231; and - heat transfer lines 132, 232. Similarly to the third evaporator, the first evaporator 13 and the second evaporator 23 may also include a plurality of evaporator trays m, 23 and each of the evaporator trays m, 231 may be arranged side by side in the first vacuum The heat transfer medium is also carried in the chamber 1G or the second vacuum chamber 2G and in each of the evaporator trays 131, 231. The heat transfer lines 132, 232 are disposed on the evaporator tray 13 231, and the two ends of the heat transfer line m'232 are respectively connected to the third vacuum chamber 3 (not shown). That is, the interior of the heat transfer lines 132, 232 is in communication with the third vacuum chamber 3, and the heat transfer medium in the heat transfer lines 132, 232 and the heat transfer medium on the evaporator tray 13 231 are not Substantial exchange, but only the transfer of heat. The first condenser 12 and the second condenser 22 described above share the same condenser tube 121, and the condensing tank 121 is supplied with cold water, and the condenser tube κ is disposed in the second chamber and the second vacuum chamber 20. Therefore, when the first adsorption bed η or the second adsorption bed 21 is supplied with hot water to perform the desorption step, the first condenser 12 and the second condenser 22 can respectively be used to condense the first adsorption bed η or the Two adsorption bed 201215833 =:==: The heat transfer medium after the junction can be guided by the flow of water m including a plurality of return roads and a plurality of defective parts, wherein the pipelines are connected to each other through the n pieces and the waterway structure is introduced to the gate The first adsorption bed 11 is configured to desorb the first adsorption bed η, and introduce a cold water into the second adsorption bed 2 to cause the second rhyme bed 21 to perform adsorption to achieve the effect of cooling, or At the same time, the cold water guides the first - adsorption bed ^
並將熱水導人第二吸附床21，以使得第-吸附床u進行吸附 作用，而第二吸附床21進行脫附作用。藉由交替地使第一吸 附床11及第二吸附床21進行吸附及脫附作用，以達到連續製 冷之功效。 當於第一吸附床11或第二吸附床21中通入冷水，並進行 吸附作用時，蒸發器托盤131、231中之熱傳介質可再被蒸發， 又因蒸發過程中需要吸收大量的潛熱，進而可降低熱傳管路 132、232及其内部之熱傳介質的溫度，使得熱傳管路132、232 内的熱傳介質被凝結成液體，液態的熱傳介質又可順著熱傳管 路132、232流入蒸發換熱托盤311内。 又由於熱傳管路132、232的管路内部與第三真空腔30相 互連通，並且熱傳管路132、232内之壓力下降，也會連帶使 蒸發換熱托盤311上的熱傳介質大量蒸發，進而帶走換熱管路 312中冰水的熱能，進而達到製冷之功效並使換熱管路312之 冰水出口 IW0流出溫度更低之冰水。 為了能有效控制吸附式製冷裝置的製冷效果，可於冰水出 口 IWO處設置一溫度感測器40以感測冰水出口 IWO處之一 201215833 冰水溫度，或是可於外界環境中設置溫度感測器（圖未示）以感 測一外界溫度。 舉例來說，使用者可設定一預設溫度作為標準，當冰水溫 度低於預設溫度時，即暫停導入冷水進入第二吸附床21或第 一吸附床11，亦即先暫時停止第二吸附床21或第一吸附床11 進行吸附作用，以停止製冷，並直到冰水溫度高於預設溫度 時，再恢復冷水導入第二吸附床21或第一吸附床11以繼續製 冷。 •又或者是將吸附式製冷裝置應用於空調設備時，使用者可 根據使用需求設定所需之外界溫度以作為預設溫度，並當所偵 測到的外界溫度低於預設溫度時，即藉由暫停導入冷水進入第 二吸附床21或第一吸附床1]L以暫停製冷，直到外界溫度高於 預設溫度時’再恢復冷水導入第二吸附床21或第一吸附床U 以繼續製冷並再使冰水溫度繼續下降。 藉此’可使得吸附式製冷裝置能符合用戶端之使用需求， ❿並使吸附式製冷裝置可保持恆溫控制，以貼近商業需求。以下 分別藉由兩實施例說明本發明之實施方式，並且於第1圖至第 8圖中之粗虛線代表熱水之流動路徑，而粗實線則代表冷水之 流動路徑。 如第1圖至第3圖所示，水路結構中之闊件可以包括：一 第一闕件51;—第二閥件52; 一第三閥件53;—第四閥件54; 以及一第五閥件55。 其中’第一閥件51，其係與一熱水進口 HWI連接，並且 亦與第一吸附床11之第一進水口 111及第二吸附床21之第二 11 201215833 進水口 211連接，以使得埶义％ 付热水進口 HWI提供之熱水可通入第 一進水口 111或第二進水口 。 第二閥件52，其係與—熱水出口 HWO、第-吸附床u 之第一出水口 112及第二吸附床21之第二出水口 212連接， 並透過第二閥件52使得第一出水口 112或第二出水口 212得 以與熱水出口 HWO連通，進而使由第一吸附床u或第二吸附 床21流出之熱水可由熱水出口 HWO流出。 第三閥件53 ’其係與一冷水進口 CWI及一冷水出口 CWO 連接。 第四闊件54，其係與第三閥件53連接，並且亦與第一進 水口 111及第二進水口 211連接，以透過第四閥件54使得經 由第三閥件53導入之冷水巧通入第一進水口 m或第二進水 口 21卜 第五閥件55，其係與冷水出口 CW〇、第一出水口 U2及 第二出水口 212連接，以藉由第五閥件55使第一出水口 U2 或第二出水口 212可與冷水出口 CW0連通，進而使由第一吸 附床11或第二吸附床U流出之冷水可自冷水出DCW0流出。 因此，如第1圖所示，當第一吸附床11進行吸附作用時， 冷水可由冷水進口 CWI流人，並透過第二閥件53及第四闕件 54流入第-進水π 1U，冷水再由第一出水口 112流出後，可 再透過第五閥件55由冷水出口 CW〇流出。同日夺，熱水可由熱 水進口 HWI透過第-閥件51请L入第一進水口 211則吏得第 二吸附床21進行脫附作用，之後，熱水可再自第二出水口 212 流出，並透過第二閥件52由熱水出口 HW〇流出。 12 201215833 如第2圖所示，類似地，當第二吸附床21欲進行 用時，冷水進口 CWI提供之冷^透過第三閥件53及第四: 件54流入第二進水口 2U，而冷水自第二出水口 212流出後間 可再透過第五閥件55流至冷水4 d⑽。同時，熱水可由執 水進口廳透過第-閥件51〜第—進水口 lu，而使第;2 π附床11彳·^&行脫附作用’教且熱水自第-出水Π 112产 出後’即可透過第二閥件52由熱水出口 HW0流出。1 又如第3圖所示’若此時所量測到的冰水溫度或外界溫度 低於預設溫㈣，即可切鮮三_ 53，时得由冷水進口 cWI提供之冷水可直接由冷水“ cw〇排出，而不再通入任 :附床11、2”，藉此暫停製冷，直到冰水溫度或外界溫 度局於預設溫度時，再次切換第53並恢復製冷，進而 達到怪溫控制之功效。 又或者，如第4圖至第8圖所；， 固力’水路結構中之閥件可以 包括：-第六闕件61; 一第七間件62; 一第八闊件I 一第 :=64; 一第十閥件65; 一第十1件66;以及-第十二 其中’第六閥件6卜其係與熱水進口麵連接 ^62則與第六閥件61連接，並與熱水出口麵連接以引 導熱水自熱水出口 HWO流出。第八關# , ^ 閥件63，其係與第六閥件 =，並且與第一進水口 U1及第二進水口 2ΐι連接，以使 二、水進口麵提供之熱水可通入第—吸附床u或第二吸附 f 2!。第九閥件64,其係與第七閥件幻連接，並且 一 出水口 112及第二出水口 212連接。此外，第九闕件料又藉 13 201215833 由一旁通管路68與第六閥件61及第八閥件63間之管路連接。 第十閥件65，其係與冷水進口 CWI及冷水出口 CWO連 接。第十一閥件66，其係與第十閥件65連接，並且與第一進 水口 111及第二進水口 211連接，以使得經過第十閥件65之 冷水可透過第十一閥件66通入第一吸附床11或第二吸附床 21。第十二閥件67，其係與冷水出口 CWO連接，並且與第一 出水口 112及第二出水口 212連接，藉此使得由第一出水口 112 或第二出水口 212流出之冷水可透過第十二閥件67流至冷水 出口 CWO。 因此’如第4圖所示’當第一吸附床11進行吸附作用時， 冷水可由冷水進口 CWI流入，並透過第十閥件65及第十一閥 件66流入第一進水口 in。冷水由第一出水口 ι12流出後，可 再透過第十二閥件67由冷水出口 CWO流出。同時，熱水可由 熱水進口 HWI透過第六閥件61及第八閥件63流入第二進水 口 211使第二吸附床21進行脫附作用後，熱水可再由第二出 水口 212流出，並透過第九閥件64及第七閥件62由熱水出口 HWO流出。 如第5圖所示，類似地，當第二吸附床21欲進行吸附作 用時，冷水進口 CWI提供之冷水可透過第十閥件65及第十一 閥件66流入第二進水口 211，而冷水自第二出水口 212流出 後，可再透過第十二閥件67流至冷水出口 CWO。同時，熱水 可由熱水進口 HWI透過第六閥件61及第八閥件63流入第一 進水口 111，而使第一吸附床11得以進行脫附作用，並且熱水 自第一出水口 112流出後，即可透過第九閥件64及第七閥件 201215833 62由熱水出口 HWO流出。 此外’當吸附床U、21欲進行脫附作用及吸附作用的轉 換前，第-真空腔1G及第二真空腔2()間可先進行回質作用及 回熱作用，其中回質作用指的是可開啟兩真空腔1〇、2〇間之 一回質閥（圖未示）’以使得第一真空腔1〇可與第二真空腔 連通，並使得兩真空腔10、20内之氣態的熱傳介質可相互流 通，並可快速平衡兩真空腔10、2〇間之壓力，以提高吸附式 製冷裝置之製冷效率。而回熱作關是使吸附床u、2i降溫， 並利於進行後續之吸附作用或脫附作用。 如第6圖所示，當第-吸附床u完成吸附作用且第二吸 附床21完成脫附作用並欲進行回熱作用時，可將熱水旁通並 藉由第六閥件61及第七閥件62使得熱水不通入任一吸附床 11、21中，進而讓熱水可直接被引導至熱水出口 Hw〇流出。 自冷水進口 cwi提供之冷水則可透過第十閥件65及第十 一閥件66先流入第二進水口 211後，以使得第二吸附床21降 籲溫後，冷水再由第二出水口 212流出。之後，冷水再透過第九 閥件64、旁通管路68及第八閥件63流入第一進水口 111，以 降溫第一吸附床11，而由第一出水口 112流出之冷水又透過第 十二閥件67流至冷水出口 CWO。 又如第7圖所示，當第二吸附床21完成吸附作用且第一 吸附床11完成脫附作用後’並欲進行回熱作用時’可藉由第 六閥件61及第七閥件62使得熱水不通入任一吸附床U、21 中，並使得由熱水可直接被引導至熱水出口 HW0流出。 自冷水進口 CWI提供之冷水則可透過第十閥件65及第十 15 201215833 一閥件66先流入第一進水口 m，以使第一吸附床u降溫後， 冷水再由第一出水口 112流出。之後，冷水再透過第九閥件 64 '旁通管路68及第八閥件63被導引流入第二進水口 211， 以使得第一吸附床21内之溫度可以下降，而由第二出水口 212 流出之冷水又可再透過第十二闊件67由冷水出口 cW〇流出。 如第8圖所示，同樣地，當量測到的冰水溫度或外界溫度 低於預設溫度時，即可切換第十閥件65，以使得由冷水進口 cwi提供之冷水可直接由冷水出口 cw〇排出，而不再通入任 一吸附床11、21中，藉此暫停製冷，直到冰水溫度或外界溫 度尚於預設溫度時，再次切換第十閥件65並恢復製冷，進而 達到恆溫控制之功效。 另外，第一蒸發器13及第二蒸發器23内位於靠近底部的 蒸發器托盤131、231以及第三蒸發器31内位於靠近底部的蒸 發換熱托盤311皆分別與一排水管71a、7比、7k連通，可用 以排除過多的熱傳介質。 此外，本實施例之吸附式製冷裝置又進一步包括至少三調 整管路72a、72b、72c，並且每一調整管路72a、72b、72c係 與對應之第-真空腔10、第二真空腔2〇及第三真空腔3〇連 通。由於真空腔10、20、30間彼此獨立，因此可藉由調整管 路72a、72b、72c分別對對應的第一真空腔1〇、第二真空腔 20及第三真空腔30獨立補充熱傳介質（例如水 二 此，可避免真空腔72a、72b、72c内之蒸發器13、23、31 = 熱傳介質失去平衡’而造成製冷性能不穩定的問題。 惟上述各實施例係用以說明本發明之特點，其目的在使熟 201215833 習該技術者能暸解本發明之内容並據以實施，而非限定本發明 之專利範圍，故凡其他未脫離本發明所揭示之精神而完成之等 效修飾或修改，仍應包含在以下所述之申請專利範圍中。 【圖式簡單說明】 第1圖為本發明第一實施例之恆溫控制之吸附式製冷裝置之第 一狀態示意圖。 第2圖為本發明第一實施例之恆溫控制之吸附式製冷裝置之第 •二狀態示意圖。 第3圖為本發明第一實施例之恆溫控制之吸附式製冷裝置之暫 停製冷狀態示意圖。 ’ 第4圖為本發明第二實施例之恆溫控制之吸附式製冷裝置之第 一狀態示意圖。 第5圖為本發明第二實施例之恆溫控制之吸附式製冷裝置之第 二狀態示意圖。 •第6圖為本發明第二實施例之恆溫控制之吸附式製冷裝置之第 三狀態示意圖。 第7圖為本發明第二實施例之恆溫控制之吸附式製冷裝置之第 四狀態示意圖。 第8圖為本發明第二實施例之恆溫控制之吸附式製冷裝置之暫 停製冷狀態示意圖。 【主要元件符號說明】 10..........................第一真空腔 17 201215833 11.................. ........第一吸附床 Ill ................ ........第一進水口 112................ ........第一出水口 12................... ........第一冷凝器 121................ ........冷凝管 13.................. ........第一蒸發器 131 > 231........ ........蒸發器托盤 132 ' 232........ ........熱傳管路 20................... ........第二真空腔 21................... ........第二吸附床 211................. ........第二進水口 212................. ........第二出水口 22................... ........第二冷凝器 23................... ........第二蒸發器 30................... ........第二真空腔 31................... ........第=蒸發器 311................. ........蒸發換熱托盤 312................. ........換熱管路 40................... ........溫度感測器 51................... ........第一閥件 52................... ........第二閥件 53................... ........第二閥件 54................... ........第四閥件 55................... ........第五閥件The hot water is introduced into the second adsorption bed 21 so that the first adsorption bed u is adsorbed, and the second adsorption bed 21 is desorbed. The adsorption and desorption of the first adsorbent bed 11 and the second adsorbent bed 21 are alternately performed to achieve the effect of continuous cooling. When cold water is introduced into the first adsorbent bed 11 or the second adsorbent bed 21 and adsorbed, the heat transfer medium in the evaporator trays 131, 231 can be evaporated again, and a large amount of latent heat needs to be absorbed during the evaporation process. Further, the temperature of the heat transfer tubes 132, 232 and the heat transfer medium inside thereof can be lowered, so that the heat transfer medium in the heat transfer lines 132, 232 is condensed into a liquid, and the liquid heat transfer medium can be passed along the heat transfer. The lines 132, 232 flow into the evaporative heat exchange tray 311. Moreover, since the inside of the pipeline of the heat transfer pipelines 132 and 232 and the third vacuum chamber 30 communicate with each other, and the pressure in the heat transfer pipelines 132 and 232 is lowered, the heat transfer medium on the evaporation heat exchange tray 311 is also connected. Evaporation, and then take away the heat energy of the ice water in the heat exchange tube 312, thereby achieving the effect of cooling and allowing the ice water outlet IW0 of the heat exchange line 312 to flow out of the ice water having a lower temperature. In order to effectively control the cooling effect of the adsorption refrigeration device, a temperature sensor 40 may be disposed at the ice water outlet IWO to sense the ice water temperature of 201215833, which is one of the ice water outlets IWO, or may be set in the external environment. A sensor (not shown) senses an outside temperature. For example, the user can set a preset temperature as a standard. When the ice water temperature is lower than the preset temperature, the cold water is temporarily introduced into the second adsorption bed 21 or the first adsorption bed 11, that is, the second temporarily stops. The adsorption bed 21 or the first adsorption bed 11 performs adsorption to stop the cooling, and until the ice water temperature is higher than the preset temperature, the cold water is returned to the second adsorption bed 21 or the first adsorption bed 11 to continue the refrigeration. • When applying the adsorption refrigeration unit to an air conditioner, the user can set the desired outside temperature as the preset temperature according to the usage requirements, and when the detected outside temperature is lower than the preset temperature, By suspending the introduction of cold water into the second adsorption bed 21 or the first adsorption bed 1] L to suspend the cooling until the outside temperature is higher than the preset temperature, and then returning the cold water to the second adsorption bed 21 or the first adsorption bed U to continue Cool and then let the ice water temperature continue to drop. This allows the adsorption refrigeration unit to meet the needs of the user end, and allows the adsorption refrigeration unit to maintain constant temperature control to meet commercial needs. Embodiments of the present invention will be described below by way of two embodiments, respectively, and the thick broken lines in Figs. 1 to 8 represent the flow paths of hot water, and the thick solid lines represent the flow paths of cold water. As shown in FIGS. 1 to 3, the wide member in the waterway structure may include: a first member 51; a second valve member 52; a third valve member 53; a fourth valve member 54; The fifth valve member 55. Wherein the first valve member 51 is connected to a hot water inlet HWI, and is also connected to the first water inlet 111 of the first adsorption bed 11 and the second 11 201215833 water inlet 211 of the second adsorption bed 21 so that埶义% Hot water inlet The hot water supplied by HWI can be passed to the first water inlet 111 or the second water inlet. The second valve member 52 is connected to the hot water outlet HWO, the first water outlet 112 of the first adsorption bed u, and the second water outlet 212 of the second adsorption bed 21, and is passed through the second valve member 52 to make the first The water outlet 112 or the second water outlet 212 is in communication with the hot water outlet HWO, so that the hot water flowing out of the first adsorption bed u or the second adsorption bed 21 can be discharged from the hot water outlet HWO. The third valve member 53' is connected to a cold water inlet CWI and a cold water outlet CWO. The fourth wide member 54 is connected to the third valve member 53 and also connected to the first water inlet 111 and the second water inlet 211 to transmit the cold water through the third valve member 53 through the fourth valve member 54. The first water inlet m or the second water inlet 21 is connected to the fifth valve member 55, which is connected to the cold water outlet CW, the first water outlet U2 and the second water outlet 212 to be made by the fifth valve member 55. The first water outlet U2 or the second water outlet 212 can communicate with the cold water outlet CW0, so that the cold water flowing out of the first adsorption bed 11 or the second adsorption bed U can flow out from the cold water outlet DCW0. Therefore, as shown in Fig. 1, when the first adsorption bed 11 performs adsorption, the cold water can flow from the cold water inlet CWI, and flows into the first-influent water π 1U through the second valve member 53 and the fourth valve member 54, cold water. After flowing out of the first water outlet 112, the fifth valve member 55 can be further flowed out through the cold water outlet CW. On the same day, the hot water can be removed from the hot water inlet HWI through the first valve member 51, and then enter the first water inlet 211 to obtain the second adsorption bed 21 for desorption, after which the hot water can flow out from the second outlet 212 again. And flowing out through the hot water outlet HW〇 through the second valve member 52. 12 201215833 As shown in Fig. 2, similarly, when the second adsorbent bed 21 is to be used, the cold water inlet CWI provides cold through the third valve member 53 and the fourth: member 54 flows into the second water inlet 2U, and The cold water flows out of the second water outlet 212 and then flows through the fifth valve member 55 to the cold water 4 d (10). At the same time, the hot water can be passed through the first valve member 51 to the first water inlet lu through the water inlet chamber, and the second; π bed 11 彳·^& line desorption function and the hot water from the first water outlet After 112 is produced, it can be discharged from the hot water outlet HW0 through the second valve member 52. 1 As shown in Figure 3, if the temperature of the ice water or the outside temperature measured at this time is lower than the preset temperature (four), the cold water supplied by the cold water inlet cWI can be directly cut by the fresh water. The cold water “cw〇 is discharged, but no longer passes: bed 11, 2”, thereby suspending the cooling until the ice water temperature or the outside temperature is at the preset temperature, switching the 53rd again and restoring the cooling, and then reaching the strange The effect of temperature control. Alternatively, as shown in Figures 4 to 8, the valve member in the solid-water structure may include: - a sixth member 61; a seventh member 62; an eighth member I: 64; a tenth valve member 65; a tenth one member 66; and - twelfth wherein the 'sixth valve member 6 is connected to the hot water inlet face ^ 62 is connected with the sixth valve member 61, and The hot water outlet surface is connected to guide the hot water from the hot water outlet HWO. The eighth closing #, ^ valve member 63, the system and the sixth valve member =, and connected with the first water inlet U1 and the second water inlet 2ΐ, so that the hot water provided by the water inlet surface can pass into the first Adsorption bed u or second adsorption f 2!. The ninth valve member 64 is singly connected to the seventh valve member, and a water outlet 112 and a second water outlet 212 are connected. In addition, the ninth piece of material is connected by a bypass line 68 to a line between the sixth valve member 61 and the eighth valve member 63 by means of 13 201215833. The tenth valve member 65 is connected to the cold water inlet CWI and the cold water outlet CWO. The eleventh valve member 66 is connected to the tenth valve member 65 and is connected to the first water inlet 111 and the second water inlet 211 such that the cold water passing through the tenth valve member 65 is permeable to the eleventh valve member 66. It is introduced into the first adsorption bed 11 or the second adsorption bed 21. The twelfth valve member 67 is connected to the cold water outlet CWO and is connected to the first water outlet 112 and the second water outlet 212, so that the cold water flowing out from the first water outlet 112 or the second water outlet 212 is permeable. The twelfth valve member 67 flows to the cold water outlet CWO. Therefore, as shown in Fig. 4, when the first adsorbent bed 11 is adsorbed, the cold water can flow into the cold water inlet CWI and flow into the first water inlet in through the tenth valve member 65 and the eleventh valve member 66. After the cold water flows out of the first water outlet ι12, it can be discharged through the cold water outlet CWO through the twelfth valve member 67. At the same time, the hot water can be discharged from the hot water inlet HWI through the sixth valve member 61 and the eighth valve member 63 into the second water inlet 211 to desorb the second adsorption bed 21, and the hot water can be discharged from the second water outlet 212. And flowing out of the hot water outlet HWO through the ninth valve member 64 and the seventh valve member 62. As shown in FIG. 5, similarly, when the second adsorption bed 21 is to be adsorbed, the cold water supplied from the cold water inlet CWI can flow into the second water inlet 211 through the tenth valve member 65 and the eleventh valve member 66. After the cold water flows out from the second water outlet 212, it can flow through the twelfth valve member 67 to the cold water outlet CWO. At the same time, the hot water can be discharged from the hot water inlet HWI through the sixth valve member 61 and the eighth valve member 63 into the first water inlet 111, so that the first adsorption bed 11 can be desorbed, and the hot water is discharged from the first water outlet 112. After flowing out, it can flow out through the hot water outlet HWO through the ninth valve member 64 and the seventh valve member 201215833 62. In addition, before the adsorption bed U, 21 is to be desorbed and the adsorption is converted, the first vacuum chamber 1G and the second vacuum chamber 2 () may be first subjected to the reversion and regenerative action, wherein the re-massing refers to It is possible to open one of the two vacuum chambers 1 〇 and 2 回 between the two valves (not shown) so that the first vacuum chamber 1 连通 can communicate with the second vacuum chamber, and the two vacuum chambers 10, 20 The gaseous heat transfer medium can circulate through each other, and the pressure between the two vacuum chambers 10 and 2 can be quickly balanced to improve the refrigeration efficiency of the adsorption refrigeration unit. The regenerative action is to cool the adsorption beds u, 2i and facilitate subsequent adsorption or desorption. As shown in Fig. 6, when the first adsorption bed u completes the adsorption and the second adsorption bed 21 completes the desorption and wants to perform the regenerative action, the hot water can be bypassed by the sixth valve member 61 and the The seven valve member 62 prevents hot water from passing into any of the adsorption beds 11, 21, so that the hot water can be directly directed to the hot water outlet Hw. The cold water supplied from the cold water inlet cwi can be first flowed into the second water inlet 211 through the tenth valve member 65 and the eleventh valve member 66, so that the second adsorption bed 21 is cooled down, and the cold water is further discharged by the second water outlet. 212 outflow. Then, the cold water flows through the ninth valve member 64, the bypass line 68 and the eighth valve member 63 into the first water inlet 111 to cool the first adsorption bed 11, and the cold water flowing out from the first water outlet 112 passes through the first The twelve valve member 67 flows to the cold water outlet CWO. As shown in Fig. 7, when the second adsorption bed 21 completes the adsorption and the first adsorption bed 11 completes the desorption, 'when it is intended to perform the reheating action', the sixth valve member 61 and the seventh valve member are available. 62 causes the hot water to not pass into any of the adsorption beds U, 21, and allows the hot water to be directly directed to the hot water outlet HW0. The cold water supplied from the cold water inlet CWI can first flow into the first water inlet m through the tenth valve member 65 and the tenth 15th 201215833 one valve member 66, so that after the first adsorption bed u is cooled, the cold water is again discharged from the first water outlet 112. Flow out. Thereafter, the cold water is again guided through the ninth valve member 64' bypass line 68 and the eighth valve member 63 into the second water inlet 211, so that the temperature in the first adsorption bed 21 can be lowered, and the second out The cold water flowing out of the nozzle 212 can be further flowed through the twelfth wide piece 67 from the cold water outlet cW. As shown in Fig. 8, similarly, when the equivalent ice water temperature or the outside temperature is lower than the preset temperature, the tenth valve member 65 can be switched so that the cold water supplied by the cold water inlet cwi can be directly cooled by cold water. The outlet cw is discharged, and is no longer passed into any of the adsorption beds 11, 21, thereby suspending the cooling until the ice water temperature or the outside temperature is still at the preset temperature, switching the tenth valve member 65 again and restoring the refrigeration, and further Achieve the effect of constant temperature control. In addition, the evaporator plates 131 and 231 located near the bottom of the first evaporator 13 and the second evaporator 23 and the evaporative heat exchange tray 311 located near the bottom in the third evaporator 31 are respectively compared with a drain pipe 71a, 7 respectively. , 7k connected, can be used to eliminate too much heat transfer medium. In addition, the adsorption refrigeration apparatus of the present embodiment further includes at least three adjustment lines 72a, 72b, and 72c, and each of the adjustment lines 72a, 72b, and 72c is associated with the corresponding first-vacuum chamber 10 and the second vacuum chamber 2. The third vacuum chamber is connected to the third vacuum chamber. Since the vacuum chambers 10, 20, 30 are independent of each other, the corresponding first vacuum chamber 1 〇, the second vacuum chamber 20, and the third vacuum chamber 30 can be independently supplemented with heat transfer by adjusting the tubes 72a, 72b, and 72c, respectively. The medium (for example, water can avoid the evaporators 13, 23, 31 in the vacuum chambers 72a, 72b, 72c = the heat transfer medium is out of balance) and causes unstable refrigeration performance. However, the above embodiments are for explaining The features of the present invention are intended to be understood by those skilled in the art and are to be understood by those skilled in the art, and are not intended to limit the scope of the invention. The modification or modification should still be included in the scope of the patent application described below. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a first schematic view showing the first state of the constant temperature controlled adsorption refrigeration apparatus according to the first embodiment of the present invention. The figure is a second state diagram of the constant temperature controlled adsorption refrigeration apparatus according to the first embodiment of the present invention. Fig. 3 is a pause cooling state of the constant temperature controlled adsorption refrigeration apparatus according to the first embodiment of the present invention. 4 is a schematic diagram of a first state of a constant temperature controlled adsorption refrigeration apparatus according to a second embodiment of the present invention. FIG. 5 is a second state diagram of a constant temperature controlled adsorption refrigeration apparatus according to a second embodiment of the present invention. Fig. 6 is a view showing a third state of the constant temperature controlled adsorption refrigeration apparatus according to the second embodiment of the present invention. Fig. 7 is a view showing a fourth state of the constant temperature controlled adsorption refrigeration apparatus according to the second embodiment of the present invention. Figure 8 is a schematic view showing the suspended cooling state of the constant temperature controlled adsorption refrigeration apparatus according to the second embodiment of the present invention. [Description of main components] 10................... .......The first vacuum chamber 17 201215833 11..............................The first adsorption bed Ill ..... ........... ........The first water inlet 112.................................. Water outlet 12...............................The first condenser 121.................. . . ....... Condensing tube 13........................ First evaporator 131 > 231.... .... ........Evaporator tray 132 ' 232........ ........heat transfer line 20........... ........ ........Second vacuum chamber 21...............................Second adsorption bed 211.... .........................The second water inlet 212....................... Second outlet 22...............................second condenser 23............. ..................Second evaporator 30...............................The second vacuum chamber 31.....................................=Evaporator 311................. ........ Evaporative heat exchange tray 312.............................heat exchange line 40........ ........... ........temperature sensor 51......................... .First valve member 52...............................Second valve member 53............ ...................Second valve member 54...........................fourth valve Pieces 55........................... fifth valve
18 201215833 61...·................... ...第六閥件 62....................... ...第七閥件 63....................... ...第八閥件 64....................... ...第九閥件 65....................... ...第十閥件 66....................... ...第十一閥件 67....................... ...第十一閥件 68....................... ...旁通管路 71a、71b、71c... ...排水管 72a、72b、72c... ...調整管路 IWI..................... ...冰水入口 IWO................... ...冰水出口 HWI................... ...熱水進口 HWO.................. ...熱水出口 CWI.................... ...冷水進口 CWO.................. ...冷水出口 1918 201215833 61...·...................the sixth valve member 62................ ....... ...the seventh valve member 63.......................the eighth valve member 64.... .........................Ninth valve member 65...................... ...the tenth valve member 66.......................the eleventh valve member 67.......... ...................The eleventh valve member 68............................bypass Pipes 71a, 71b, 71c ... drain pipes 72a, 72b, 72c ... adjust the pipe IWI.................... ....Ice water inlet IWO......................Ice water outlet HWI................ ...hot water import HWO.................. ...hot water outlet CWI............... ..... ...cold water import CWO.....................cold water outlet 19