1306934 九、發明說明： 【發明所屬之技術領域】 本發明係為一種固體吸附式製冷裝置，特別係指一種將熱 水源與冰水源作旁通(by_pass)控制，來提升製冷能力之固g 吸附式製冷裝置。 【先前技術】1306934 IX. Description of the Invention: [Technical Field] The present invention relates to a solid adsorption refrigeration device, and particularly relates to a solid-g adsorption for improving the refrigeration capacity by bypassing (by_pass) control of a hot water source and an ice water source. Refrigeration unit. [Prior Art]
固體吸附式製冷裝置係以多孔性物質（矽夥、分子筛及活 性碳等）作為吸附劑，在低溫時吸附大量的冷媒蒸氣(如：水、 甲醇及氨氣等）’這些冷媒在汽化時需要由外界吸取所需之蒸 發潛熱’如此將使的環境溫度降低，而汽化的冷媒蒸氣則由= 附劑吸附’當吸附劑吸附飽和後，吸附質可透過加^的方式從 吸附劑脫附出來後冷卻回收’其再生所需的熱源可採用工業制 成廢熱或太陽能等再生能源來達成。 雖然目前吸附式製冷裝置的使用還未可與一般塵縮式制 冷裝置抗衡’但是吸附式製冷裝置符合環保的需求，同'時U： 以下優點： 〃 氺 低溫流體的選擇較彈性（可選擇非氟氯碳化合物， 如：水、醇類及氨氣等）； * 可利用二级能源及自然能源來驅動裝置； * 無運動元件，内部構造簡單，故無噪音與震動的問 題；及 * 運轉相耗低，使用壽命長，而且維護容易。 由於吸附式製冷裝置有前述種種優點，所以實為一值得發 轉推廣的技術方向。 x 習知的吸附式製冷系統’其水循環管路通常配置切換閥件 作為系統控制，當進行回熱過程時，傳統上皆以熱水源切換至 另一吸附床（吸附剛結束）將殘留冷卻水推送回至冷卻水塔 側，同時，冷卻水源切換至另一吸附床（脫附剛結束）將殘留 1306934The solid adsorption refrigeration system uses porous materials (such as molecular sieves, activated carbon, and activated carbon) as adsorbents, and adsorbs a large amount of refrigerant vapor (such as water, methanol, and ammonia) at low temperatures. These refrigerants are required for vaporization. The desired latent heat of vaporization is taken from the outside. This will reduce the ambient temperature, and the vaporized refrigerant vapor will be adsorbed by the additive. When the adsorbent is saturated, the adsorbate can be desorbed from the adsorbent by means of addition. Post-cooling recovery 'The heat source required for its regeneration can be achieved by industrially making renewable energy such as waste heat or solar energy. Although the use of adsorption refrigeration equipment has not yet been able to compete with general dust-type refrigeration equipment, but the adsorption refrigeration equipment meets the environmental requirements, the same as: U: The following advantages: 〃 氺 low-temperature fluid selection is more flexible (optional non-optional Chlorofluorocarbons, such as water, alcohols and ammonia, etc.; * Can use secondary energy and natural energy to drive the device; * No moving parts, simple internal structure, so there is no noise and vibration problems; and * operation Low phase loss, long life and easy maintenance. Since the adsorption refrigeration device has the above various advantages, it is a technical direction worthy of promotion and promotion. x Conventional adsorption refrigeration system's water circulation line is usually equipped with a switching valve as a system control. When the heat recovery process is carried out, the hot water source is traditionally switched to another adsorption bed (the end of adsorption is just finished). Push back to the side of the cooling tower, while the cooling water source is switched to another adsorption bed (just after the desorption is completed) will remain 1306934
===，題知的式製冷系统在 實際上使 * 很難避免流量不均所衍生問題；* 預冷/預熱時間較長；及 * 吸附初期冰水出溫升高現象。 【發明内容】===, the known refrigeration system actually makes * difficult to avoid the problem of flow unevenness; * pre-cooling / warm-up time is longer; and * the initial rise of ice water temperature. [Summary of the Invention]
韻，主要目的係在於完全避免流量不均所衍生η 由於此製冷裝置於熱回收與冷能回收過程 冰水源作料(by-pass)㈣ 將熱水源與 器’來解決水源减之曰進附床與冷凝/蒸發 =時間，===外 其另一目的則在於細免吸附 本^之_吸附式製冷裝置可包含有回麵構及 Γ?Βΐ架射可設置社部·組、下㈣件組與旁 ^二件、、且，同時以上各件組係與固體吸附式主機之流體側進行 連、、Ό ’而回魏構則與固體吸喊主機之真空側進行連結。Rhyme, the main purpose is to completely avoid the flow unevenness derived η because the refrigeration device in the heat recovery and cold energy recovery process ice source (by-pass) (four) the hot water source and the device to solve the water source reduction into the bed Another purpose of condensation/evaporation=time, === is to avoid adsorption. The adsorption refrigeration unit can include a back surface structure and a Γ Βΐ Βΐ 射 可 可 社 社 社 社 社 社 社 社 社 社The group and the side are two pieces, and at the same time, the above parts are connected with the fluid side of the solid adsorption type host, and the structure is connected with the vacuum side of the solid suction host.
r趣ϊΐίί明之詳細内容及技術，兹就配合圖式說明如下·· ι貫施方式J 本毛明係為-種_吸附式製冷衆置，為明4表示本發明 之特點’將藉由-連Φ的製冷實施步驟來絲綱，首先將左 床脫附及右床吸附的過程作一說明，請參照「第丨圖 發明之固體吸附式製冷裝置實施例示意（丨）圖。 本杳明固體吸附式製冷裝置可包含有：左真空腔體1⑻及 右真空腔體200，其中各腔體中亦分別設置有左（右）吸附床 101(201)及左(+右)冷凝/蒸發器102(2〇2)等工作單元，而各單 元中則設置有管路來供液體流通，其中第—切換閥3〇ί、第二 1306934r interesting ϊΐ ί ί 之 ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί 配合 配合 配合 配合 配合 配合 配合 配合 配合 配合 配合 配合 配合 配合 配合 配合 ι ι 本 本 本 本 本 本 本 本 本For the refrigeration implementation step of Φ, the process of desorption of the left bed and adsorption of the right bed is first described. Please refer to the schematic diagram of the embodiment of the solid adsorption refrigeration device of the invention. The solid adsorption refrigeration device may include: a left vacuum chamber 1 (8) and a right vacuum chamber 200, wherein each chamber is also provided with a left (right) adsorption bed 101 (201) and a left (+ right) condensation/evaporator. 102 (2〇2) and other working units, and each unit is provided with a pipeline for liquid circulation, wherein the first-switching valve 3〇ί, the second 1306934
第ί切換閥3〇3可為上部閥件組，而第四切換閥 樣、弟五切換閥402及第六切換闕* 換閥 回質真空閥501則為回質架構中的真空组，二“二的而 口及出口端可裝設旁通管件。^^ *而各抓體的入 組，而下部閥件組為冷凝/蒸發器吸附床流體閥件 當熱水由熱水入口 HWI流經第一切換關3 並由弟三切換閥303及第一切換閥3〇ι後從斡水 水槽’而冷卻水則藉由第五切換閥4G2進入左 =/，發$ 102 ’此時為行使冷凝器的功能，冷卻水最後再 ί 流至冷卻水塔；此時左真空腔體刚中 f f f ί升，綠力超過左冷凝/蒸剌⑽溫度相對岸 壓時’則開始冷凝將左吸附床1〇1所脫附出的冷g 纽冷凝為液態冷媒；同時冷卻水經由第二切換閥搬進入^ 吸附床201再經由第三切換閥3〇3日流至冷卻水塔，此時右吸 附床201開始降溫吸附且使右真空腔體2〇〇内的冷媒蒸汽壓力 之下降，此時冰水則由冰水入口 m流經第四切換^ 4〇ι及 第五切換閥4〇2至右冷凝/蒸發器逝，使蒸發面開始蒸發製 冷丄而產生之冰水由右冷凝/蒸發器2〇2流經第六切換閥4〇^ 及第四切換閥401後回流至負載使用端。 ,接下來就本發明由左至右的熱、冷能回收及回質過程加以 詳細說明，請參照「第2圖」，為本發明之固體吸附式製冷穿 置實施例示意（2)圖。 ^ 當左右吸附床的脫附與吸附（第1圖）過程結束時，熱、冷 能回收及回質過程接續進行，當回質真空閥5〇1打開後，左真 空腔體100内冷媒蒸汽會因為較大壓差的作用下迅速流回g 真空腔體200 ’當左右兩真空腔體的壓力趨於平衡時則關閉回 質真空閥501 ;而熱回收過程主要係將左吸附床1〇ι内駐留的 熱水流入右吸附床201，並將右吸附床201内駐留的冷卻水排 1306934The third switching valve 3〇3 may be an upper valve member group, and the fourth switching valve example, the fifth switching valve 402 and the sixth switching 阙* the valve returning vacuum valve 501 are vacuum groups in the return structure, "The second port and the outlet end can be equipped with bypass pipe fittings. ^^ * and the body of each grab body is incorporated, while the lower valve member group is a condensing/evaporator adsorbing bed fluid valve member when hot water flows from the hot water inlet HWI After the first switching off 3 and the third switching valve 303 and the first switching valve 3〇1 from the water tank 'the cooling water, the fifth switching valve 4G2 enters the left = /, sends $ 102 ' at this time Exercising the function of the condenser, the cooling water finally flows to the cooling tower; at this time, the left vacuum chamber just fff ί rises, the green force exceeds the left condensing/distilling 剌 (10) temperature relative to the shore pressure' then begins to condense the left adsorbent bed The cold g nucleus desorbed from 1〇1 is condensed into a liquid refrigerant; at the same time, the cooling water is transferred into the adsorption bed 201 via the second switching valve and then flows to the cooling tower via the third switching valve 3〇3, at this time, the right adsorption bed 201 starts to cool down and absorbs and reduces the pressure of the refrigerant vapor in the right vacuum chamber 2, at which time the ice water enters the ice water. The mouth m flows through the fourth switch ^ 4〇ι and the fifth switching valve 4〇2 to the right condensing/evaporator, so that the evaporation surface starts to evaporate and the chilled water is generated by the right condensing/evaporator 2〇2 The sixth switching valve 4〇 and the fourth switching valve 401 are returned to the load use end. Next, the left-to-right heat and cold energy recovery and recovery process of the present invention will be described in detail, please refer to "Fig. 2" Fig. 2 is a schematic view (2) showing an embodiment of the solid adsorption refrigeration passage of the present invention. ^ When the process of desorption and adsorption of the left and right adsorption beds (Fig. 1) is completed, the heat and cold energy recovery and recovery processes are continued. When the recovery vacuum valve 5〇1 is opened, the refrigerant vapor in the left vacuum chamber 100 is Will quickly flow back to the vacuum chamber 200 due to the large differential pressure. When the pressure of the left and right vacuum chambers tends to balance, the return vacuum valve 501 is closed; and the heat recovery process mainly involves the left adsorption bed. The hot water remaining in the ι flows into the right adsorption bed 201, and the cooling water remaining in the right adsorption bed 201 is discharged 1306934
出，首先由苐一切換閥301作旁通(by-pass)控制，將熱水入 口 HWI的熱水直接導向熱水出口 JJWO回流至熱水槽，並使 冷卻水由冷卻水入口 CWI流經第二切換閥3〇2後流入左吸附 于101，並將左吸附床1〇1内駐留的熱水由第三切換閥3〇3、 第一切換閥301及第二切換閥302推送至右吸附床2〇1内，並 將右吸附床201内駐留的冷卻水藉由第三切換閥3〇3排出至冷 卻水塔。 冷能回收的過程則係使右冷凝/蒸發器2〇2内駐留的冰水 流^左冷凝/蒸發器1〇2中，並使左冷凝/蒸發器1〇2内駐留的 冷卻水排出，首先由第四切換閥401作旁通(by-pass)控制， 將冰水入口 IWI的冰水直接導向冰水出口 IW0回流至冰水 槽，並使冷卻水由冷卻水入口 CWI流經第五切換閥4〇2後流 入^冷凝/蒸發器202，並將右冷凝/蒸發器202内駐留的冰水 由第六切換闕403、第四切換閥401及第五切換閥4〇2推送至 左^凝<蒸發器102内，並將左冷凝/蒸發器1〇2内駐留的冷卻 水藉由第六切換閥403排出至冷卻水塔，如此則完成了熱、冷 能回收及回質過程。 ^ 接下來將右床脫附及左床吸附的過程作一詳細說明，請參 照「第3圖」’為本發明之固體吸附式製冷裝置實施例示意（3) 圖。 “ 當熱、冷能回收完成後，裝置則循環進入到右床脫附及左 床吸附的程序，此時第三切換閥303、第一切換閥3〇1、第六 切換閥403及第四切換閥4〇1會切換導流方向，此時熱水由g 水入口 HWI流經第一切換閥301及第二切換閥3〇2^進入^ 吸附床201，加熱吸附劑後離開右吸附床201，並流經由第三 切換閥303及第一切換閥301後從熱水出口 HW〇回流至熱^ 槽’而冷卻水則藉由第五切換閥402進入右冷凝/蒸發器go〗， 此時為行使冷凝器的功能，冷卻水最後再經由第六切換閥4〇3 回流至冷卻水塔；此時右真空腔體200中的蒸氣壓力上升，當 1306934First, the first hot water inlet HWI hot water is directly directed to the hot water outlet JJWO to the hot water tank, and the cooling water is passed through the cooling water inlet CWI through the first-by-pass control. After the switching valve 3〇2 flows into the left and adsorbs to 101, and the hot water residing in the left adsorption bed 1〇1 is pushed by the third switching valve 3〇3, the first switching valve 301 and the second switching valve 302 to the right adsorption. Inside the bed 2〇1, the cooling water residing in the right adsorption bed 201 is discharged to the cooling water tower through the third switching valve 3〇3. The process of cold energy recovery is to cause the ice water flowing in the right condensing/evaporator 2〇2 to be in the left condensing/evaporator 1〇2, and to discharge the cooling water residing in the left condensing/evaporator 1〇2, firstly By the fourth switching valve 401 as a by-pass control, the ice water of the ice water inlet IWI is directly directed to the ice water outlet IW0 to return to the ice water tank, and the cooling water flows through the cooling water inlet CWI through the fifth switching valve. After 4〇2, it flows into the condensation/evaporator 202, and pushes the ice water residing in the right condensation/evaporator 202 from the sixth switching port 403, the fourth switching valve 401, and the fifth switching valve 4〇2 to the left side. < Inside the evaporator 102, the cooling water residing in the left condensing/evaporator 1〇2 is discharged to the cooling tower by the sixth switching valve 403, thus completing the heat and cold energy recovery and recovery process. ^ Next, the process of desorption of the right bed and adsorption of the left bed will be described in detail. Please refer to "Fig. 3" as an illustration (3) of the embodiment of the solid adsorption refrigerating apparatus of the present invention. “When the heat and cold energy recovery is completed, the device circulates into the right bed desorption and left bed adsorption process. At this time, the third switching valve 303, the first switching valve 3〇1, the sixth switching valve 403, and the fourth The switching valve 4〇1 will switch the flow guiding direction. At this time, the hot water flows from the g water inlet HWI through the first switching valve 301 and the second switching valve 3〇2^ into the adsorption bed 201, and after heating the adsorbent, leaving the right adsorption bed. 201, the flow through the third switching valve 303 and the first switching valve 301 is returned from the hot water outlet HW to the hot tank '', and the cooling water enters the right condensing/evaporator go by the fifth switching valve 402. In order to exercise the function of the condenser, the cooling water is finally returned to the cooling water tower via the sixth switching valve 4〇3; at this time, the vapor pressure in the right vacuum chamber 200 rises when 1306934
壓力超過右冷凝/蒸發器202溫度相對應之飽和蒸汽壓時，則 開始冷凝將右吸附床201所脫附出的冷媒蒸汽冷凝為液態冷 媒，同時冷卻水經由第二切換閥3〇2進入左吸附床1〇1再經由 第三切換閥303回流至冷卻水塔，此時左吸附床1〇1開始降溫 吸附且使左真空腔體100内的冷媒蒸汽壓力隨之下降，此時冰 水則由冰水入口 IWI流經第四切換閥401及第五切換閥402至 左冷凝/蒸發102，使蒸發面開始蒸發製冷，而產生之冰水 由左冷凝/蒸發器102流經第六切換閥403及第四切換閥401 後回流至負載使用端。 接下來就本發明由右至左的熱、冷能回收及回質過程加以 詳細說明，請參照「第4圖」，為本發明之固體吸附式製冷裝 置實施例示意（4)圖。 當左右吸附床的脫附與吸附（第3圖）過程結束時，熱、冷 能回收及回質過程接續進行，當回質真空闊5〇1打開後，右真 空腔體200内冷媒蒸汽會因為較大壓差的作用下迅速流回左 真空腔體100 ’當左右兩真空腔體的壓力趨於平衡時則關閉回 質真空閥501 ;而熱回收過程主要係將右吸附床2〇1内駐留的 熱水流入左吸附床101，並將左吸附床1〇1内駐留的冷卻水排 出，首先由第一切換閥301作旁通(by-pass)控制，將熱水入 口 HWI的熱水直接導向熱水出口 HW〇回流至熱水槽，並使 冷卻水由冷卻水入口 CWI流經第二切換閥302後流入右吸附 床20卜並將右吸附床201内駐留的熱水由第三切換閥3〇3、 第一切換閥301及第二切換閥302推送至左吸附床101内，並 將左吸附床101内駐留的冷卻水藉由第三切換閥3〇3排出至冷 卻水塔。 冷能回收的過程則係使左冷凝/蒸發器1〇2内駐留的冰水 流入右冷凝/蒸發器202中，並使右冷凝/蒸發器202内駐留的 冷卻水排出，首先由弟四切換閥401作旁通(by-pass)控制， 將冰水入口 IWI的冰水直接導向冰水出口 IWO回流至冰水 1306934 ： 槽’並使冷卻水由冷卻水入口 CWI流經第五切換閥402後流 ；_ 入士冷凝/蒸發器1⑽，並將左冷凝/蒸發器102内駐留的冰^ 由第六切換閥403、第四切換閥401及第五切換閥402推送至 - 右士凝/j矣發器202内，並將右冷凝/蒸發器2〇2内駐留的冷卻 水藉由第六切換閥403排出至冷卻水塔，如此則完成了熱、冷 能回收及回質過程，此程序結束後系統又將回到左床脫^及^ 床吸附的過程，開始週而復始的重複製冷循環的運作。 本發明之固體吸附式製冷裝置除了前述之步驟外，為了完 王避免及附初期冰水出溫過高的現象，在不違反同一創作精神 • 的原則下’更可增加有以下的實施方式，請參照「第5圖」， 為本發明之固體吸附式製冷裝置實施例示意（5)圖。 、當本發明之固體吸附式製冷裝置由左至右的完成冷能回 收過程後(請參照第2圖）’待冷卻水由左冷凝/蒸發器丨〇2完全 排出^，則切換第六切換閥403來改變導流方向，使右冷凝/ ，發器202之冷卻水直接經由第六切換閥4〇3排出至冷卻水 塔，此時左冷凝/蒸發器1〇2並無冰水流入，等到左真空腔體 100溫度降至冰水入溫以下，再切換第四切換閥4⑴並U右 床脫附及左床吸附的過程（請參照第3圖）。 相同的在由右至左的完成冷能回收過程後，為了完全避免 韻^冰水出溫過高的現象’同樣可增加有以下的實施方 式，請參照「第6圖」’為本㈣之隨韻式製冷裝施 例示意（6)圖。 ' 、當本發明之固體吸附式製冷裝置由右至左的完成冷能回 收過私後(明參照第4圖），待冷卻水由右冷凝/蒸發器完全 ^出，，則切換第六切換閥4〇3來改變導流方向，使左冷凝/ 瘵發器102之冷卻水直接經由第六切換闕4〇3排出至冷7卻水 塔’此時右冷凝/蒸發器202並無冰水流入，等到右真空腔 2f〇/:度降至冰水入溫以下，再切換第四切換閥401並重^循 環進行左床脫附及右床吸附的過程（請參照第〗圖）。 1306934 *、畜=⑹遣本每日月之各切換間’可依據設計上的需要來遽用 =式;式的間件二“藉^ 本剌之11體吸赋製冷裝置具有以下之 氺 氺 =，的切換來達成熱、冷回收之功效，並有效 解決^罝不均之衍生問題； 氺 t入in气過程’進而加速縮短預冷/預熱時 ’進而&升錢性能，增加系統製冷能力；及 Φ t吸附與脫_初期運關件的導流設計來使冰 7，遲進入，可完全避免吸附初期冰水出溫過高的 現象。 雖然本發日脑前述之較佳實關揭露 ，任何熟習此技藝者，在不脫離本發明 後附之申請專利範圍所界定者為準。 觀圍田視 1306934 【圖式簡單說明】 第1圖，為本發明之固體吸附式製冷裝置實施例示意圖； 第2圖，為本發明之固體吸附式製冷裝置實施例示意圖； 第3圖，為本發明之固體吸附式製冷裝置實施例示意圖； 第4圖，為本發明之固體吸附式製冷裝置實施例示意圖； 第5圖，為本發明之固體吸附式製冷裝置實施例示意圖；及 第6圖，為本發明之固體吸附式製冷裝置實施例示意圖。When the pressure exceeds the saturated vapor pressure corresponding to the temperature of the right condensing/evaporator 202, the condensation is started to condense the refrigerant vapor desorbed from the right adsorbent bed 201 into a liquid refrigerant, and the cooling water enters the left via the second switching valve 3〇2. The adsorption bed 1〇1 is further returned to the cooling water tower via the third switching valve 303. At this time, the left adsorption bed 1〇1 starts to cool down and adsorbs, and the pressure of the refrigerant vapor in the left vacuum chamber 100 decreases accordingly, and the ice water is then The ice water inlet IWI flows through the fourth switching valve 401 and the fifth switching valve 402 to the left condensation/evaporation 102, so that the evaporation surface starts to evaporate and cool, and the generated ice water flows from the left condensation/evaporator 102 through the sixth switching valve 403. And the fourth switching valve 401 is returned to the load use end. Next, the right-to-left heat and cold energy recovery and recovery process of the present invention will be described in detail. Please refer to Fig. 4, which is a schematic view (4) of the solid adsorption refrigeration apparatus of the present invention. When the process of desorption and adsorption of the left and right adsorption beds (Fig. 3) is completed, the heat and cold energy recovery and recovery processes are continued. When the recovery vacuum is 5〇1, the refrigerant vapor in the right vacuum chamber 200 will be Because of the large pressure difference, it quickly flows back to the left vacuum chamber 100'. When the pressures of the left and right vacuum chambers tend to balance, the returning vacuum valve 501 is closed; and the heat recovery process mainly involves the right adsorption bed 2〇1. The hot water residing in the water flows into the left adsorption bed 101, and discharges the cooling water residing in the left adsorption bed 1〇1, first by the first switching valve 301 for by-pass control, and the heat of the hot water inlet HWI The water is directly directed to the hot water outlet HW, and is returned to the hot water tank, and the cooling water flows from the cooling water inlet CWI through the second switching valve 302, flows into the right adsorption bed 20, and the hot water residing in the right adsorption bed 201 is third. The switching valve 3〇3, the first switching valve 301, and the second switching valve 302 are pushed into the left adsorption bed 101, and the cooling water residing in the left adsorption bed 101 is discharged to the cooling water tower through the third switching valve 3〇3. The process of cold energy recovery is such that the ice water residing in the left condensing/evaporator 1〇2 flows into the right condensing/evaporator 202, and the cooling water residing in the right condensing/evaporator 202 is discharged, first switched by the younger brother. The valve 401 is controlled by by-pass, and the ice water of the ice water inlet IWI is directly directed to the ice water outlet IWO to return to the ice water 1306934: the tank 'and the cooling water flows from the cooling water inlet CWI through the fifth switching valve 402 Afterflow; _ entrant condensing/evaporator 1 (10), and pushing the ice remaining in the left condensing/evaporator 102 from the sixth switching valve 403, the fourth switching valve 401, and the fifth switching valve 402 to - 右士凝/ In the hair expander 202, the cooling water residing in the right condensing/evaporator 2〇2 is discharged to the cooling tower by the sixth switching valve 403, thus completing the heat and cold energy recovery and recovery process. After the end, the system will return to the left bed and ^ bed adsorption process, and start the repeated refrigeration cycle operation. In addition to the aforementioned steps, the solid adsorption refrigeration apparatus of the present invention can increase the following embodiments in order to avoid the phenomenon that the initial ice water temperature is too high, and not to violate the same creative spirit. Please refer to FIG. 5, which is a schematic view (5) of an embodiment of the solid adsorption refrigeration apparatus of the present invention. When the solid adsorption refrigeration apparatus of the present invention completes the cold energy recovery process from left to right (please refer to FIG. 2), the water to be cooled is completely discharged by the left condensation/evaporator 丨〇2, and then the sixth switching is switched. The valve 403 is used to change the direction of the flow, so that the cooling water of the right condensing device 202 is directly discharged to the cooling tower via the sixth switching valve 4〇3, and the left condensing/evaporator 1〇2 has no ice water flowing in, and waits until The temperature of the left vacuum chamber 100 is reduced to below the ice water temperature, and then the fourth switching valve 4 (1) is switched and the U bed is desorbed and the left bed is adsorbed (refer to Fig. 3). After the completion of the cold energy recovery process from right to left, in order to completely avoid the phenomenon that the temperature of the ice water is too high, the following embodiments can be added. Please refer to "6th figure" as the basis (4). The rhyme-type refrigeration installation example is shown in (6). When the solid adsorption refrigeration device of the present invention recovers the cold energy from the right to the left (refer to FIG. 4), the cooling water is completely discharged by the right condensation/evaporator, and then the sixth switching is switched. The valve 4〇3 changes the direction of the flow, so that the cooling water of the left condensing/deflector 102 is directly discharged to the cold 7 through the sixth switching 〇4〇3. At this time, the right condensing/evaporator 202 has no ice water inflow. Wait until the right vacuum chamber 2f〇/:degree falls below the ice water temperature, then switch the fourth switching valve 401 and repeat the process of left bed desorption and right bed adsorption (please refer to the figure). 1306934 *, Animals = (6) Dispatched in the daily shifts of each month 'can be used according to the design needs = type; type of the second two "borrowed ^ this 11 body suction refrigeration device has the following =, switch to achieve the effect of heat and cold recovery, and effectively solve the problem of derivation of unevenness; 氺t into the gas process 'and then accelerate the shortening of pre-cooling / preheating' and then & money performance, increase the system Refrigeration capacity; and Φ t adsorption and desorption _ initial flow control design of the diversion to make ice 7, late entry, can completely avoid the phenomenon of excessive ice water temperature at the initial stage of adsorption. 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 2 is a schematic view of an embodiment of a solid adsorption refrigeration apparatus according to the present invention; FIG. 3 is a schematic view of an embodiment of a solid adsorption refrigeration apparatus of the present invention; and FIG. 4 is a solid adsorption refrigeration of the present invention. Apparatus embodiment ; Figure 5, the present invention the solid adsorption refrigerating apparatus schematic embodiment; and FIG. 6, a schematic diagram of the present invention the solid adsorption refrigerating apparatus embodiment.
【主要元件符號說明】 100 左真空腔體 101 左吸附床 102 左冷凝/蒸發器 200 右真空腔體 201 右吸附床 202 右冷凝/蒸發器 301 第一切換閥 302 第二切換閥 303 第三切換閥 401 第四切換閥 402 第五切換閥 403 第六切換閥 501 回質真空閥 CWI 冷卻水入口 CW0 冷卻水出口 IWI 冰水入口 IW0 冰水出口 HWI 熱水入口 HWO 熱水出口 12[Main component symbol description] 100 left vacuum chamber 101 left adsorption bed 102 left condensation/evaporator 200 right vacuum chamber 201 right adsorption bed 202 right condensation/evaporator 301 first switching valve 302 second switching valve 303 third switching Valve 401 Fourth switching valve 402 Fifth switching valve 403 Sixth switching valve 501 Regeneration vacuum valve CWI Cooling water inlet CW0 Cooling water outlet IWI Ice water inlet IW0 Ice water outlet HWI Hot water inlet HWO Hot water outlet 12