200928261 九、發明說明： 【發明所屬之技術領域】 本發明係有關於一種固體吸附式熱泵裝置’尤指一種 具有製冷、製熱雙重功能之熱泵裝置，同時藉由熱、冷能 回收控制機制，將高溫流體與低溫流體做旁通（by-Pass) 控制，可有效解決水源端水量不均之問題，增加製冷/製熱 能力、提高系統性能係數（C0P)。 e 【先前技術】 傳統一體式固體吸附式製冷系統，例如曰本專利 JP7012420「Adsorption Type Refrigerating Device(吸 著式冷凍裝置）」，其將吸附床、蒸發器及冷凝器整合於同 一真空腔體内，於腔體上方設有吸附床，於腔體下方設有 蒸發/冷凝熱交換器，該蒸發/冷凝熱交換器可於脫附過程 中作為冷凝器，於吸附過程中作為蒸發器使用；其運行原 理為，當吸附床之管件被通以冷卻水（例如3〇°c )時，吸 附床進行吸附作用’此時’蒸發/冷凝熱交換器作為蒸發器 使用並被通以冰水（例如12°C )，冷媒蒸氣上升至吸附床 而被吸附劑吸收，而流過蒸發器管件的水則被降溫（例如 從12°C至7°C);當吸附行程結束後，吸附床的管件改通以 熱水（例如85°C ) ’蒸發/冷凝熱交換器在此時作為冷凝器 使用並被通以冷卻水（例如3(TC )，於是由吸附床^附^ 的冷媒蒸氣在冷凝器上凝結成液態冷媒。實際上，於上述 ^亍程中並無製冷作用，該系統系將兩個（或兩個以上）此種 200928261 製冷裝置加以並聯使用，並適當地錯開其吸、脫附行程， 藉此得到連續而不間斷之製冷作用。 . 紗中華民國發明專财請第93133542號「吸附式製 * 冷控制系統」、第94141639號「固體吸附式製冷裝置」等 案’其主要利用多通閥連結製冷控制系統内各製冷裝置， 以簡化控制系統之加熱源、冷卻水源以及冰水盥吸附式製 冷主機之吸附床、冷凝蒸發熱交換器間迴路間所需之闕數 量，同時具有熱交換器管内侧之熱能回收功效。 由上述習知專利前案所揭露之技術手段可知，當兩床 進行運行操作時，僅以單-製冷魏為主，並無製熱功能， 無法滿足使用端製冷與製熱雙重需求；且於連續式雙床吸 附式主機系統於加熱脫附與冷卻吸附過程結束後，切換閥 組進行回熱過程時，傳統上皆以加熱源切換至另一吸附床 (吸附剛結束）將冷卻水推送回至冷卻水塔侧，同時，冷卻 水源切換至另一吸附床（脫附剛結束）將熱水推送回至^水 槽，於此回熱過程十，雖然有熱能回收效果，但實際運行 時，由於熱水與冷卻水流量不等量，導致某一侧水槽之水 量減少或增加，因而影響整體水源處之循環水量控制管理 之困擾。 【發明内容】 有鑑於習知技術之缺失，本發明之目的在於提出一種 固體吸附式熱栗裝置，具有製冷、製熱雙重功能，且於吸 附式主機運行過程十採取熱、冷能回收控制機制，將高溫 流體與低溫流體做旁通（by-pass)控制，可有效解決水源端 8 200928261 m紐能係數 為達到上述目的’本發明提出—種固體 置，其係由:主機、—模式轉換裝置及一能量回 成，該主機包3複數吸附床及冷凝蒸發器，用 、構 脫附、冷凝=祕料應；賴;切難料m ❹ ❹ 式；該能量回收裝置係與該主機及轉換裝置^或裳熱模 收該主機作動所產生之能量。 接’用以回 為使貴審查委員對於本發明之結構 進一步之了解舆認同，兹配合圖示詳細說明如后有更 【實施方式】 以下將參照隨附之圖式來描述本發 於所列舉圖式❶—“解但本案之技術手段並不限 置，：，明所提供之固體吸附式熱泵裝 腔體2〇〇所構成之：=—Α第Τ真空腔體1〇0及一第二真空 及一冷能回妆Μ, ，以及由一熱能回收閥組3〇〇以 式轉換裝置所構成之能量回收裝置，以及-模 該第~~直 有-第-吸附：100及第二真空腔體200内分別設置 01以及一第二吸附床201，於該等吸附 9 200928261 床101、201下方分別設有一第一冷凝洛發器1〇2以及一第 二冷凝蒸發器202，分別用以進行吸附、脫附、冷凝或蒸 發等反應。 ~ 該模式轉換裝置500,係用以轉換該固體吸附式熱& 裝置進行製冷或製熱模式，其包含相互連接之第—轉換間 501及第二轉換閥502’該等轉換閥501、502均為多通闕， 且該等轉換閥501、502均與一環境單元602及一負载單元 603相連接。該熱能回收閥組300及冷能回收閥組4〇〇所 構成之能量回收裝置，係用以回收該主機A作動所產生之 能量；其中，該熱能回收閥组300包含相互連接之第—熱 能回收閥301、第二熱能回收閥302及第三熱能回收 303 ’該等熱能回收閥301〜303均為多通閥，其中，該第一 熱能回收閥301與一加熱源601連接；該第二熱能回收闕 302與該等吸附床101、201連接；該第三熱能回收闕3〇3 與該第一吸附床101及該第二轉換閥502連接。 該冷能回收閥組400包含相互連接之第一冷能回收閱 401、第二冷能回收閥402及第三冷能回收閥4〇3，該等A 能回收閥401〜403均為多通閥，其中’該第一冷能^收^ 401與該等轉換閥501、502連接；該第二冷能回收闕4〇2 與該第二冷凝蒸發器202及該第一轉換閥5〇1連接；該第 三冷能回收閥403與該等冷凝蒸發器ι〇1、2〇2及第二‘食t 回收閥302連接。 ‘ ' b 上述該等熱能回收閥301〜303、該等冷能回收闊 401〜403可採用兩通閥、三通閥、四通閥等其中之一咬其 組合。 八 200928261 前述該環境單元6〇2可為冷卻水塔等裂置，該負载 兀603則視該固體吸附式熱栗裝置所進行之模式不同而呈 . 現不同功能’例如，當該固體吸附式m置處於製冷模 , 斜’該貞載單元603係作為冷房㈣1當_體^附 式熱泵裝置處於製熱模式時，該負載單元6G3係作為暖房 使用；此外，該環境單元602及負載單元6〇3所提供之流 體溫度依作動模式不同而改變，綜合前述該加埶源6〇1二 及該環境單元602、負載單元603而言，例如該加熱源6〇1 可提供具有第一溫度之流體，該環境單元6〇2可提供具有 第二溫度之流體，該負載單元6〇3可提供具有第三溫度之 流體，當本發明處於製冷模式時，該第一溫度係高於該第 二及第三溫度，且該第二溫度高於該第三溫度，例如，該 第一溫度可為攝氏80度，該第二溫度可為攝氏3〇度，該 第二溫度可為攝氏14度；至於當本發明處於製熱模式時， 該第一溫度係高於該第二及第三溫度，且該第二溫度低於 該第三溫度，例如，該第一溫度可為攝氏8〇度，該第二溫 鬱 度可為攝氏14度，該第三溫度可為攝氏3〇度。 必須說明的是，前述該等熱能回收閥30丨〜303、該等 冷能回收閥401~403、該等轉換閥501、5〇2，及其所連接 之第一真空腔體1〇〇、第二真空腔體2〇〇、模式轉換裝置 500、加熱源601、環境單元6〇2及負載單元603之間，可 a又置官件相互連接，該管件可為直管、—管等等，且該管 件之長度依實際所需而設定，此為相關技術領域人士所熟 知技藝，在此不予贅述。 依據上述本發明各構件組合可知，當切換該模式轉換 200928261 裝置500之該等轉換閥501、502時，可改變該環境單元 602及負载單元6G3輸出人流體之流向’藉此轉換該固體 . 吸附式熱泵裝置進行製冷或製熱模式，藉由以下實施例可 . 充分說明其作動方式。 請參閱圖一及圖一 A至圖一 F，說明本發明進行製冷 模式時之運轉程序，其係以水為流體作為說明例。 首先參閱圖一所示，當本發明進行製冷模式時，該加 ❿ 熱源可提供高溫熱水經由第一熱能回收閥3〇1、第二 熱能回收閥302進入該第一吸附床ιοί内進行加熱脫附動 作，再經由第三熱能回收閥303、第一熱能回收閥3〇1回 流至加熱源601，回流至加熱源6〇1之熱水溫度會略為降 低，例如原本攝氏80度之熱水，大約會降低至攝氏75度 左右；而該環境單元602作為散熱源，可提供中溫冷卻水 (約攝氏30度）經由第一轉換閥5〇1進入該主機a，以進行 - 脫附冷凝與吸附床冷卻散熱，而後再經由第二轉換閥5〇2 ❹ 回至該環境單元602，回流至環境單元602之中溫冷卻水 溫度會略為升高，例如原本攝氏30度之中溫冷卻水，大約 會^高至約攝氏35度左右；而該負載單元603作為冷房， I提供低溫冰水經由第一轉換閥5〇丨進入主機A產生蒸發 製冷後，再經由第二轉換閥5〇2回至該負載單元6〇3，而 回至該負载單元603之冰水溫度會更為降低，例如原本攝 氏14度之冰水，大約可再降低至攝氏9度左右，如此即可 供應冰水提供室内空調冷能負載需求。 關於進行上述流程之過程，將詳細說明於後；必須說 明的是，以下說明所提及之加熱源6〇1、環境單元6〇2及 12 200928261 負載單元603可參閱圖一，於圖一 A至圖一 F所示簡圖中 予以省略。 請參閱圖一 A，其顯示第一吸附床101脫附，以及第 二吸附床201吸附之過程：熱水（由圖一該加熱源601提供） 由管件P1進入第一熱能回收閥301、第二熱能回收閥302, 再進入該第一吸附床101内加熱吸附後，再經由第三熱能 回收閥303、第一熱能回收閥301，由管件P6送回加熱源 601 ;來自環境單元602之冷卻水經由管件P2通過第二冷 能回收閥402進入第一冷凝蒸發器102，此時，該第一冷 凝蒸發器102作為冷凝器使用；最後，冷卻水再經由第三 冷能回收閥403、第二熱能回收閥302進入該第二吸附床 201進行冷卻吸附，再經由第三熱能回收閥303由管件P3 回至環境單元602 ;此時，該第一真空腔體100中之蒸汽 壓力上升，當壓力超過第一冷凝蒸發器102溫度相對應之 飽和蒸汽壓時，即開始冷凝，將第一吸附床101所脫附出 之冷媒蒸汽冷凝為液態冷媒；同時，該第二吸附床201開 始降溫吸附，第二真空腔體200内之冷媒蒸汽壓力隨之下 降；負載單元603將冰水由管件P4送入第一冷能回收閥 401、第二冷能回收閥402進入該第二冷凝蒸發器202，開 始蒸發製冷，所產生之冰水最後離開該第二冷凝蒸發器 202，經由第三冷能回收閥403、第一冷能回收閥401，由 管件P5回至負載單元603。 請參閱圖一 B，其顯示由第一吸附床101至第二吸附 床201之熱能回收過程：本過程與圖一 A之差別在於將第 一熱能回收閥301、第二熱能回收閥302換向；熱水由管 13 200928261 件P1進入第一熱能回收閥301後，由管件P6旁通回流至 加熱源601 ;第一熱能回收閥301、第二熱能回收閥3〇2換 向後，可使原本駐留於第一吸附床101内之熱水經由該等 熱月b回收閥303、301、302推送至第二吸附床2〇1，此時， 原本駐留於第二吸附床201之冷卻水將經由第三熱能回收 閥303排出’由管件P3回至環境單元602。 請參閱圖一 C，其顯示由第二吸附床201至.第一吸附 床101之冷能回收過程：本過程與圖一 B之差別在於將第 一冷能回收閥401、第二冷能回收閥402換向；負載單元 603將冰水經由管件P4送入第一冷能回收閥4〇1後，直接 由管件P5旁通回流至負載單元603 ;原本駐留於第二冷凝 ?备發器202内之冰水可經由該等冷能回收閥4〇3、401、402 流入第一冷凝蒸發器102中，使原本駐留於該第一冷凝蒸 發器102内之冷卻水經由第三冷能回收閥403排出，再串 接第二熱能回收閥302並接續前述圖一 b所示之吸附床熱 能回收過程。 請參閱圖一 D ’其顯示第二吸附床201脫附及第一吸 附床101吸附過程：本過程與圖一 C之差別在於將第三熱 能回收閥303、第一熱能回收閥301、第三冷能回收閥403、 第一冷能回收閥401換向；當前述該熱、冷能回收過程完 成時’熱水經由管件Pi通過第一熱能回收閥301、第二熱 月巨回收閥302進入第二吸附床201内加熱吸附後離開該第 二吸附床201 ’再經由第三熱能回收閥303、第一熱能回收 闊301 ’由管件P6回至加熱源601 ;來自環境單元602之 冷卻水經由管件P2通過第二冷能回收閥402進入第二冷凝 14 200928261 蒸發器202，此時，該第二冷凝蒸發器2〇2係作為冷凝器 使用’冷卻水再經由第三冷能回收閥4〇3再串接第二熱能 .回收閥302進入第一吸附床101内冷卻吸附後離開，進入 . 第三熱能回收閥3〇3,再由管件P3回至環境單元6〇2;此 時:該第二真空腔體200中之蒸汽壓力上升，當壓力超過 第二冷凝蒸發器202溫度相對應之飽和蒸汽壓時，開始冷 凝將第二吸峰2〇1所脫㈣冷職汽核為液態冷媒: 同時，該第一吸附床1G1開始降溫吸附，第-真空腔體1〇〇 内之冷縫汽壓力社下降，·㈣，負鮮元_提供冰 水，經由管件P4通過閥第一冷能回收閥4〇1、第二冷能回 收閥402’再進入該第一冷凝蒸發器逝，其蒸發面開始装 發製冷^斤產生之冰水最後離開該第一冷凝蒸發器1〇2、 經由第三冷能回收閥403、第一冷能回收閥4〇1後，由 件P5回至負載單元6〇3。 請參閱圖一 E，其顯由第二吸附床201至第-吸附床 1G1之熱能时過程：本過程與圖—D之差別在於將第一 熱忐回收閥301、第二熱能回收閥3〇2換向；當第一、第 二吸附床1G卜謝脫附及吸附過程結束時，需進行哉能回 收過程；由環境單元602提供之冷卻水由管件p2通過第二 冷能回收閥402、第二冷凝蒸發器2〇2、第三冷能回收闊 403、第二熱能回收閥302進入第二吸附床2〇1，將原本駐 留於第二吸附床201内之熱水經由該等熱能回收闕3〇3、 301 302推送至第一吸附床ι〇1，此時原本駐留於第一吸 附床101之冷卻水將經由第三熱能回收閥3〇3，再透過 件P3回至環境單元602。 15 200928261 請參閱圖一 F，其顯示由第一吸附床101至第二吸附 床201之冷能回收過程：本過程與圖一 E之差別在於將第 一冷能回收閥4 01、第二冷能回收閥4 0 2換向；第一冷凝 蒸發器102内駐留之冰水可經由該等冷能回收閥403、 401、402流入第二冷凝蒸發器202中，將原本駐留於第二 冷凝蒸發器202内之冷卻水排出；而負載單元603之冰水 由管件P4進入第一冷能回收閥401後，可直接由管件P5 旁通回流至負載單元603 ;而來自環境單元602之冷卻水 可經由管件P2進入第一冷凝蒸發器102，將原本駐留於第 一冷凝蒸發器102内之冰水經由該等冷能回收閥403、 401、402推送至第二冷凝蒸發器202，同時將原本駐留於 第二冷凝蒸發器202之冷卻水推送經由第三冷能回收閥 403排出，再串接第二熱能回收閥302並接續前述圖一 E 所示之吸附床熱能回收過程 依上述圖一 A至圖一 F步驟循序週而復始循環運行， 即可連續執行製冷模式。 其次，請參閱圖二及圖二A至圖二F，說明本發明進 行製熱模式時之運轉程序，其係以水為流體作為說明例。 首先參閱圖二所示，本發明之特點在於設有該模式轉 換裝置500，通過簡單的閥切換，即可轉換製冷或製熱模 式；如圖二所示，其與圖一之差別僅在於將該等轉換閥 5(Π、502換向，改變該環境單元602及負載單元603輸出 入流體之流向，藉此進行製熱模式；由加熱源601提供高 溫熱水經由第一熱能回收閥301、第二熱能回收閥302進 入該第一吸附床101内進行加熱脫附動作，再經由第三熱 16 200928261 能回收閥303、第一熱能回收閥301回流至加熱源6〇 1，回 流至加熱源601之熱水溫度會略為降低，例如原本攝氏8〇 . 度之熱水，大約會降低至攝氏75度左右；於製熱模式下， . 該環境單元602作為取熱源’可提供低溫冰水經由第一轉 換閥501進入該主機A，以進行吸附製冷，再經由第二轉 換閥502回至該環境單元602，回流至環境單元602之低 溫冰水溫度會略為降低，例如原本攝氏14度之低溫冰水， 大約會降低至攝氏9度左右；而該負載單元603作為暖房， ® 可提供冷卻水經由第一轉換閥501進入主機a進行脫附冷 凝與吸附冷卻後，再經由第二轉換閥502回至該負載單元 603 ’而回至該負載單元603之冷卻水溫度會更為升高，例 如原本攝氏30度之冷卻水’大約可升高至攝氏35度左右， 如此即可供應室内空調暖房熱能負載需求。 關於進行上述流程之過程，將詳細說明於後；同樣地， 以下說明所提及之加熱源601、環境單元602及負載單元 603可參閱圖二’於圖二A至圖二F所示簡圖中予以省略。 凊參閱圖二A ’其顯示第一吸附床101脫附，以及第 二吸附床201吸附之過程：熱水（由圖二該加熱源6〇1提供） 由管件P1進入第一熱能回收閥30卜第二熱能回收閥302, 再進入該第一吸附床101内加熱吸附後’再經由第三熱能 回收閥303、第一熱能回收閥301，由管件P6送回加熱源 601 ;來自負載單元603提供冷卻水經由管件P2通過第二 冷能回收閥402進入第一冷凝蒸發器102，此時，該第一 冷凝蒸發器102作為冷凝器使用；最後，水再經由第三冷 能回收閥403、第二熱能回收閥302進入該第二吸附床2〇1 17 200928261 進行冷卻吸附，再經由第三熱能回收閥303由管件P3回至 負載單元603 ;此時，該第一真空腔體100中之蒸汽壓力 上升，當壓力超過第一冷凝蒸發器102溫度相對應之飽和 蒸汽壓時，即開始冷凝，將第一吸附床101所脫附出之冷 媒蒸汽冷凝為液態冷媒；同時，該第二吸附床201開始降 溫吸附，第二真空腔體200内之冷媒蒸汽壓力隨之下降； 環境單元602將冰水由管件P4送入第一冷能回收閥401、 第二冷能回收閥402進入該第二冷凝蒸發器202，開始蒸 發製冷，使冷卻水降溫後離開該第二冷凝蒸發器202，經 由第三冷能回收閥403、第一冷能回收閥401，由管件P5 回至環境單元602。 請參閱圖二B，其顯示由第一吸附床101至第二吸附 床201之熱能回收過程：本過程與圖二A之差別在於將第 一熱能回收閥301、第二熱能回收閥302換向；熱水由管 件P1進入第一熱能回收閥301後，由管件P6旁通回流至 加熱源601 ;第一熱能回收閥301、第二熱能回收閥302換 向後，可使原本駐留於第一吸附床101内之熱水經由該等 熱能回收閥303、3(Π、302推送至第二吸附床201，此時， 原本駐留於第二吸附床201之冷卻水將經由第三熱能回收 閥303排出，由管件Ρ3回至負載單元603。 請參閱圖二C，其顯示由第二吸附床201至第一吸附 床101之冷能回收過程：本過程與圖二Β之差別在於將第 一冷能回收閥401、第二冷能回收閥402換向；環境單元 602將冰水經由管件Ρ4送入第一冷能回收閥401後，直接 由管件Ρ5旁通回流至環境單元602 ;原本駐留於第二冷凝 18 200928261 蒸發器202内之冷卻水可經由該等冷能回收閥403、401、 402流入第一冷凝蒸發器1〇2中，使原本駐留於該第一冷 凝蒸發器102内之冰水經由第三冷能回收閥403排出，再 串接第二熱能回收閥302並接續前述圖二B所示之吸附床 熱能回收過程。 請參閱圖二D，其顯示第二吸附床201脫附及第一吸 附床101吸附過程：本過程與圖二C之差別在於將第三熱 能回收閥303、第一熱能回收閥301、第三冷能回收閥403、 第一冷能回收閥401換向；當前述該熱、冷能回收過程完 成時’熱水經由管件P1通過第一熱能回收閥301、第二熱 能回收閥302進入第二吸附床201内加熱吸附後離開該第 二吸附床201，再經由第三熱能回收閥303、第一熱能回收 閥301，由管件P6回至加熱源601 ;來自負載單元603之 冷卻水經由管件P2通過第二冷能回收閥402進入第二冷凝 蒸發器202 ’此時，該第二冷凝蒸發器202係作為冷凝器 使用’冷卻水再經由第三冷能回收閥403再串接第二熱能 回收閥302進入第一吸附床1〇1内冷卻吸附後離開，進入 第三熱能回收閥303，再由管件P3回至負載單元6〇3 ;此 時，該第二真空腔體200中之蒸汽壓力上升，當壓力超過 第二冷凝蒸發器202溫度相對應之飽和蒸汽壓時’開始冷 凝將第二吸附床2〇1所脫附出冷媒蒸汽冷凝為液態冷媒； 同時，該第一吸附床1 〇 1開始降溫吸附，第一真空腔體1 〇〇 内之冷媒蒸汽壓力隨之下降；同時，環境單元602提供冰 水’經由管件P4通過第一冷能回收閥401、第二冷能回收 閥402 ’再進入該第一冷凝蒸發器1〇2 ’其蒸發面開始蒸發 200928261 製熱，所產生之冰水最後離開該第一冷凝蒸發器102，經 由第三冷能回收閥403、第一冷能回收閥401後，由管件 P5回至環境單元602。 請參閱圖二E，其顯由第二吸附床201至第一吸附床 101之熱能回收過程：本過程與圖二D之差別在於將第一 熱能回收閥301、第二熱能回收閥302換向；當第一、第 二吸附床101、201脫附及吸附過程結束時，需進行熱能回 收過程；由負載單元603提供之冷卻水由管件P2通過第二 冷能回收閥402、第二冷凝蒸發器202、第三冷能回收閥 403、第二熱能回收閥302進入第二吸附床201，將原本駐 留於第二吸附床201内之熱水經由該等熱能回收閥303、 301、302推送至第一吸附床101，此時原本駐留於第一吸 附床101之冷卻水將經由第三熱能回收閥303，再透過管 件P3回至負載單元603。 請參閱圖二F，其顯示由第一吸附床101至第二吸附 床201之冷能回收過程：本過程與圖二E之差別在於將第 一冷能回收閥401、第二冷能回收閥402換向；第一冷凝 蒸發器102内駐留之冰水可經由該等冷能回收閥403、 401、402流入第二冷凝蒸發器202中，將原本駐留於第二 冷凝蒸發器202内之冷卻水排出；而環境單元602之冰水 由管件P4進入第一冷能回收閥401後，可直接由管件P5 旁通回流至環境單元602 ;而來自負載單元603之冷卻水 可經由管件P2進入第一冷凝蒸發器102，將原本駐留於第 一冷凝蒸發器102内之冰水經由該等冷能回收閥403、 401、402推送至第二冷凝蒸發器202，同時將原本駐留於 20 200928261200928261 IX. Description of the Invention: [Technical Field] The present invention relates to a solid adsorption heat pump device, in particular to a heat pump device having both refrigeration and heating functions, and a heat and cold energy recovery control mechanism. By-pass control of high-temperature fluid and low-temperature fluid can effectively solve the problem of uneven water supply at the water source, increase cooling/heating capacity, and improve system performance coefficient (C0P). e [Prior Art] A conventional integrated solid adsorption refrigeration system, such as the JP7012420 "Adsorption Type Refrigerating Device", which integrates an adsorption bed, an evaporator, and a condenser into the same vacuum chamber. An adsorption bed is arranged above the cavity, and an evaporation/condensation heat exchanger is arranged below the cavity, and the evaporation/condensation heat exchanger can be used as a condenser in the desorption process and as an evaporator in the adsorption process; The principle of operation is that when the pipe of the adsorption bed is passed through cooling water (for example, 3 〇 °c), the adsorption bed is adsorbed. At this time, the evaporation/condensation heat exchanger is used as an evaporator and is passed through ice water (for example) At 12 ° C), the refrigerant vapor rises to the adsorbent bed and is absorbed by the adsorbent, while the water flowing through the evaporator tube is cooled (for example, from 12 ° C to 7 ° C); when the adsorption stroke is over, the tube of the adsorbent bed Switching to hot water (eg 85 ° C) 'evaporation / condensation heat exchanger at this time used as a condenser and is passed through cooling water (for example 3 (TC), so the refrigerant vapor from the adsorption bed ^ is condensed Condensation It is a liquid refrigerant. In fact, there is no refrigeration in the above process. The system uses two (or more) such 200928261 refrigeration units in parallel, and appropriately staggers the suction and desorption strokes. In this way, we can obtain continuous and uninterrupted refrigeration. The yarn of the Republic of China, the invention of the special wealth, please call 93133542 "Adsorption system * Cold control system", No. 94141639 "Solid adsorption refrigeration unit", etc. The valve is connected to each refrigeration device in the refrigeration control system to simplify the heat source of the control system, the cooling water source, and the number of turns required between the adsorption bed of the ice water adsorption adsorption refrigeration host and the circuit between the condensation evaporation heat exchanger, and has heat exchange. The heat energy recovery effect on the inner side of the tube. It can be seen from the technical means disclosed in the above-mentioned prior patents that when the two beds are operated, only the single-cooling Wei is mainly, and there is no heating function, which cannot satisfy the cooling at the use end. Dual demand with heating; and after the end of the heating and desorption and adsorption process in the continuous double bed adsorption host system, the switching valve group is used for the heat recovery process. At the same time, the heating source is switched to another adsorption bed (the end of adsorption is just finished) to push the cooling water back to the cooling water tower side, and at the same time, the cooling water source is switched to another adsorption bed (just after the desorption is finished) to push the hot water back. To the sink, the heat recovery process is ten. Although there is heat recovery effect, in actual operation, because the flow of hot water and cooling water are not equal, the water volume of one side tank is reduced or increased, thus affecting the overall water source. The present invention aims to provide a solid adsorption type hot chest device with dual functions of refrigeration and heating, and takes ten steps in the operation process of the adsorption host The heat and cold energy recovery control mechanism, by high-temperature fluid and low-temperature fluid by-by-pass control, can effectively solve the water source end 8 200928261 m neon energy coefficient to achieve the above purpose 'the present invention proposes a kind of solid, its system By: the main machine, the mode conversion device and an energy recovery, the main package 3 multiple adsorption beds and condensing evaporators, the structure, desorption, condensation = secret material should; Lai; it is difficult to m ❹ ;; the energy recovery device is coupled with the host and the conversion device or the heat model to generate energy generated by the host. In order to make your reviewer further understand and understand the structure of the present invention, the detailed description of the present invention will be described later. [Embodiment] The following description will be made with reference to the accompanying drawings. ❶ ❶ “ “ “ “ “ “ “ “ 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本 本Two vacuum and one cold energy makeup makeup, and an energy recovery device consisting of a heat recovery valve group 3〇〇 type conversion device, and - the mold ~ ~ straight - first - adsorption: 100 and second 01 and a second adsorption bed 201 are respectively disposed in the vacuum chamber 200, and a first condensation hair conditioner 1〇2 and a second condensation evaporator 202 are respectively disposed under the adsorption electrodes 9 200928261 beds 101 and 201, respectively. For performing adsorption, desorption, condensation, or evaporation, etc. ~ The mode conversion device 500 is configured to convert the solid adsorption heat & device to perform a cooling or heating mode, and includes a first-to-conversion chamber 501 and Second switching valve 502', such switching valves 501, 5 02 is a multi-pass, and the switching valves 501, 502 are connected to an environmental unit 602 and a load unit 603. The energy recovery device consisting of the heat recovery valve group 300 and the cold energy recovery valve group 4 For recovering the energy generated by the operation of the host A; wherein the heat recovery valve group 300 includes the first heat energy recovery valve 301, the second heat energy recovery valve 302, and the third heat energy recovery 303' The valves 301 303 303 are all multi-way valves, wherein the first thermal energy recovery valve 301 is connected to a heating source 601; the second thermal energy recovery 阙 302 is connected to the adsorption beds 101, 201; the third thermal energy recovery 阙 3 〇3 is connected to the first adsorption bed 101 and the second switching valve 502. The cold energy recovery valve group 400 includes a first cold energy recovery 401, a second cold energy recovery valve 402, and a third cold energy recovery that are connected to each other. The valve 4〇3, the A-capable recovery valves 401-403 are all multi-way valves, wherein 'the first cold energy source 401 is connected to the switching valves 501, 502; the second cold energy recovery 阙4〇 2 is connected to the second condensing evaporator 202 and the first switching valve 5〇1; the third cold energy The recovery valve 403 is connected to the condensing evaporators ι〇1, 2〇2 and the second 'food t recovery valve 302. ' ' b The above-mentioned heat recovery valves 301 to 303, the cold energy recovery widths 401 to 403 The two-way valve, the three-way valve, the four-way valve and the like are used to bite the combination. Eight 200928261 The environmental unit 6〇2 may be a cooling tower or the like, and the load 兀 603 is regarded as the solid adsorption type hot chest device. The different modes are performed. For example, when the solid adsorption type m is placed in the cooling mode, the load unit 603 is used as the cold room (4) 1 when the heat pump device is in the heating mode. The load unit 6G3 is used as a greenhouse; in addition, the fluid temperature provided by the environment unit 602 and the load unit 6〇3 is changed according to the operating mode, and the above-mentioned twisting source 6〇1 and the environmental unit 602 and the load are integrated. For unit 603, for example, the heating source 〇1 can provide a fluid having a first temperature, the environmental unit 〇2 can provide a fluid having a second temperature, and the load unit 〇3 can provide a fluid having a third temperature When the invention is in a refrigeration mode The first temperature is higher than the second and third temperatures, and the second temperature is higher than the third temperature. For example, the first temperature may be 80 degrees Celsius, and the second temperature may be 3 degrees Celsius. Degree, the second temperature may be 14 degrees Celsius; as when the invention is in the heating mode, the first temperature is higher than the second and third temperatures, and the second temperature is lower than the third temperature, for example The first temperature may be 8 degrees Celsius, the second temperature may be 14 degrees Celsius, and the third temperature may be 3 degrees Celsius. It should be noted that the heat recovery valves 30丨 to 303, the cold energy recovery valves 401 to 403, the switching valves 501 and 5〇2, and the first vacuum chamber 1 to which they are connected, Between the second vacuum chamber 2, the mode switching device 500, the heating source 601, the environmental unit 6〇2, and the load unit 603, the a member may be connected to each other, and the tube may be a straight tube, a tube, or the like. The length of the tube is set according to actual needs, which is well known to those skilled in the relevant art and will not be described herein. According to the combination of the components of the present invention, when the switching valves 501, 502 of the mode conversion 200928261 device 500 are switched, the flow of the human fluid can be changed by the environmental unit 602 and the load unit 6G3 to thereby convert the solid. The heat pump device performs a cooling or heating mode, and the following embodiment can fully explain its operation mode. Referring to Fig. 1 and Fig. 1A to Fig. F, the operation procedure of the present invention in the cooling mode will be described, and water is used as a fluid as an illustrative example. Referring first to FIG. 1, when the present invention performs the cooling mode, the heating heat source can provide high temperature hot water to be heated into the first adsorption bed through the first heat recovery valve 3〇1 and the second heat recovery valve 302. The desorption operation is further returned to the heating source 601 via the third thermal energy recovery valve 303 and the first thermal energy recovery valve 3〇1, and the temperature of the hot water flowing back to the heating source 6〇1 is slightly lowered, for example, the original hot water of 80 degrees Celsius. , the ambient unit 602 acts as a heat sink, and provides intermediate temperature cooling water (about 30 degrees Celsius) to enter the host a via the first switching valve 5〇1 for performing desorption condensation. Cooling heat is dissipated with the adsorption bed, and then returned to the environmental unit 602 via the second switching valve 5〇2, and the temperature of the cooling water flowing back to the environmental unit 602 is slightly increased, for example, the temperature of the first 30 degrees Celsius is cooled. , about ~ about 35 degrees Celsius; and the load unit 603 as a cold room, I provide low-temperature ice water through the first switching valve 5 〇丨 into the host A to produce evaporative cooling, and then through the second switching valve 5 〇 2 Back to the negative Unit 6〇3, and the temperature of the ice water returning to the load unit 603 is further reduced. For example, the ice water of 14 degrees Celsius can be reduced to about 9 degrees Celsius, so that the ice water can be supplied to provide indoor air conditioning. Can load demand. The process of carrying out the above process will be described in detail later; it must be noted that the heating source 6〇1, the environmental unit 6〇2 and 12 200928261 mentioned in the following description can be referred to FIG. 1 in FIG. It is omitted from the diagram shown in Figure F. Please refer to FIG. 1A, which shows the desorption of the first adsorption bed 101 and the adsorption process of the second adsorption bed 201: hot water (provided by the heating source 601 of FIG. 1) enters the first thermal energy recovery valve 301 by the pipe member P1, After the second heat recovery valve 302 is heated and adsorbed into the first adsorption bed 101, the third heat recovery valve 303 and the first thermal energy recovery valve 301 are returned to the heating source 601 by the pipe P6; the cooling from the environmental unit 602 The water enters the first condensing evaporator 102 through the second cold energy recovery valve 402 via the pipe P2. At this time, the first condensing evaporator 102 is used as a condenser; finally, the cooling water is further passed through the third cold energy recovery valve 403, The second heat recovery valve 302 enters the second adsorption bed 201 for cooling adsorption, and then returns to the environmental unit 602 from the pipe member P3 via the third heat energy recovery valve 303; at this time, the steam pressure in the first vacuum chamber 100 rises. When the pressure exceeds the saturated vapor pressure corresponding to the temperature of the first condensing evaporator 102, the condensation starts, and the refrigerant vapor desorbed from the first adsorption bed 101 is condensed into a liquid refrigerant; meanwhile, the second adsorption bed 201 starts to drop. Adsorption, the pressure of the refrigerant vapor in the second vacuum chamber 200 decreases; the load unit 603 sends the ice water from the pipe member P4 to the first cold energy recovery valve 401 and the second cold energy recovery valve 402 to the second condensing evaporator. 202, evaporative cooling is started, and the generated ice water finally leaves the second condensing evaporator 202, and returns to the load unit 603 from the pipe member P5 via the third cold energy recovery valve 403 and the first cold energy recovery valve 401. Referring to FIG. 1B, the heat energy recovery process from the first adsorption bed 101 to the second adsorption bed 201 is shown: the process differs from FIG. 1A in that the first thermal energy recovery valve 301 and the second thermal energy recovery valve 302 are reversed. The hot water is returned to the first heat recovery valve 301 by the pipe 13 200928261 piece P1, and is bypassed by the pipe member P6 to the heating source 601; the first heat energy recovery valve 301 and the second heat energy recovery valve 3〇2 are reversible, so that the original The hot water residing in the first adsorption bed 101 is pushed to the second adsorption bed 2〇1 via the heat recovery b recovery valves 303, 301, 302. At this time, the cooling water originally residing on the second adsorption bed 201 will pass through The third thermal energy recovery valve 303 is discharged 'returned from the pipe member P3 to the environmental unit 602. Please refer to FIG. 1C, which shows the cold energy recovery process from the second adsorption bed 201 to the first adsorption bed 101. The difference between this process and FIG. 1B is that the first cold energy recovery valve 401 and the second cold energy recovery are recovered. The valve 402 is reversed; the load unit 603 sends the ice water to the first cold energy recovery valve 4〇1 via the pipe member P4, and is directly bypassed by the pipe member P5 to the load unit 603; originally resident in the second condensation/reservoir 202 The ice water can flow into the first condensing evaporator 102 via the cold energy recovery valves 4〇3, 401, 402, so that the cooling water originally resident in the first condensing evaporator 102 passes through the third cold energy recovery valve. 403 is discharged, and then the second heat recovery valve 302 is connected in series and the adsorption bed heat energy recovery process shown in FIG. 1b is continued. Please refer to FIG. 1D' for showing the second adsorption bed 201 desorption and the first adsorption bed 101 adsorption process: the difference between this process and FIG. 1C is that the third thermal energy recovery valve 303, the first thermal energy recovery valve 301, and the third The cold energy recovery valve 403 and the first cold energy recovery valve 401 are reversed; when the heat and cold energy recovery process is completed, the hot water enters through the first heat recovery valve 301 and the second heat recovery valve 302 via the pipe Pi. After the second adsorbent bed 201 is heated and adsorbed, it leaves the second adsorbent bed 201' and then passes through the third heat energy recovery valve 303, and the first heat energy recovery wide 301' is returned from the pipe member P6 to the heating source 601; the cooling water from the environmental unit 602 is passed through The pipe P2 enters the second condensing 14 200928261 evaporator 202 through the second cold energy recovery valve 402. At this time, the second condensing evaporator 2 〇 2 is used as a condenser and then passes through the third cold energy recovery valve 4 . 3, the second heat energy is connected in series. The recovery valve 302 enters the first adsorption bed 101 and is cooled and adsorbed to leave, enters the third heat energy recovery valve 3〇3, and then returns to the environmental unit 6〇2 by the pipe member P3; The vapor pressure in the second vacuum chamber 200 rises, When the pressure exceeds the saturated vapor pressure corresponding to the temperature of the second condensing evaporator 202, the condensing starts to remove the second peak 2〇1 (4) the cold steam core is the liquid refrigerant: At the same time, the first adsorption bed 1G1 starts to be cooled and adsorbed. The cold seam steam pressure in the first vacuum chamber 1 is lowered, (4), the negative fresh water_ provides ice water, passes through the valve P4 through the valve first cold energy recovery valve 4〇1, and the second cold energy recovery valve 402 'Re-entering the first condensing evaporator, the evaporation surface begins to be loaded with refrigeration, and the ice water generated by the chilling finally leaves the first condensing evaporator 1〇2, passes through the third cold energy recovery valve 403, and the first cold energy is recovered. After valve 4〇1, it is returned to load unit 6〇3 by piece P5. Referring to FIG. 1E, the process of the thermal energy from the second adsorbent bed 201 to the first adsorbent bed 1G1 is shown. The difference between the present process and FIG. D is that the first heat recovery valve 301 and the second heat recovery valve 3 are 2 reversing; when the first and second adsorption beds 1G are desorbed and the adsorption process is finished, a helium energy recovery process is required; the cooling water provided by the environmental unit 602 passes through the second cold energy recovery valve 402 from the pipe fitting p2, The second condensing evaporator 2〇2, the third cold energy recovery 403, the second thermal energy recovery valve 302 enters the second adsorption bed 2〇1, and the hot water originally residing in the second adsorption bed 201 is recovered through the thermal energy.阙3〇3, 301 302 is pushed to the first adsorption bed ι〇1, at which time the cooling water originally residing on the first adsorption bed 101 will be returned to the environmental unit 602 via the third thermal energy recovery valve 3〇3 and then through the P3. . 15 200928261 Please refer to FIG. 1F, which shows the cold energy recovery process from the first adsorption bed 101 to the second adsorption bed 201: the difference between this process and FIG. 1E is that the first cold energy recovery valve 4 01, the second cold The recovery valve can be recirculated; the ice water residing in the first condensing evaporator 102 can flow into the second condensing evaporator 202 via the cold energy recovery valves 403, 401, 402, and will reside in the second condensing evaporation. The cooling water in the device 202 is discharged; after the ice water of the load unit 603 enters the first cold energy recovery valve 401 by the pipe member P4, it can be directly bypassed and returned to the load unit 603 by the pipe member P5; and the cooling water from the environmental unit 602 can be Entering the first condensing evaporator 102 via the pipe P2, the ice water originally residing in the first condensing evaporator 102 is pushed to the second condensing evaporator 202 via the cold energy recovery valves 403, 401, 402, and will remain originally The cooling water pumping in the second condensing evaporator 202 is discharged through the third cold energy recovery valve 403, and then connected in series with the second heat energy recovery valve 302 and continuing the heat recovery process of the adsorption bed shown in FIG. Figure 1 step F step by step Starting cycle operation, a cooling mode can be continuously performed. Next, referring to Fig. 2 and Fig. 2A to Fig. 2F, the operation procedure of the present invention in the heating mode will be described, and water is used as a fluid as an illustrative example. Referring first to FIG. 2, the present invention is characterized in that the mode switching device 500 is provided, and the cooling or heating mode can be switched by simple valve switching; as shown in FIG. 2, the difference from FIG. 1 is only that The switching valves 5 (Π, 502 are reversed, changing the flow direction of the environmental unit 602 and the load unit 603 into and out of the fluid, thereby performing a heating mode; providing the high temperature hot water by the heating source 601 via the first heat recovery valve 301, The second heat energy recovery valve 302 enters the first adsorption bed 101 for heating and desorption operation, and then recovers the valve 303 via the third heat 16 200928261, and the first heat energy recovery valve 301 returns to the heating source 6〇1 and returns to the heating source. The temperature of the hot water of 601 will be slightly reduced. For example, the hot water of 8 摄 Celsius will be reduced to about 75 degrees Celsius. In the heating mode, the environmental unit 602 can be used as a heat source to provide low temperature ice water. The first switching valve 501 enters the host A to perform adsorption refrigeration, and then returns to the environmental unit 602 via the second switching valve 502, and the temperature of the low temperature ice water flowing back to the environmental unit 602 is slightly lowered, for example, the original photo The 14 degree low temperature ice water will be reduced to about 9 degrees Celsius; and the load unit 603 acts as a greenhouse, and the cooling water can be supplied to the host a via the first switching valve 501 for desorption condensation and adsorption cooling, and then The temperature of the cooling water returned to the load unit 603 is further increased, for example, the cooling water of the original 30 degrees Celsius can be raised to about 35 degrees Celsius, so that The indoor air conditioning greenhouse heat energy load demand is supplied. The process of performing the above process will be described in detail later; similarly, the heating source 601, the environmental unit 602 and the load unit 603 mentioned in the following description can be referred to FIG. 2' It is omitted in the diagram shown in Fig. 2F. 凊 Refer to Fig. 2A', which shows the desorption of the first adsorption bed 101, and the adsorption process of the second adsorption bed 201: hot water (the heating source 6〇1 from Fig. 2) Provided by the pipe member P1 entering the first heat energy recovery valve 30 and the second heat energy recovery valve 302, and then entering the first adsorption bed 101 to heat the adsorption, and then passing through the third heat energy recovery valve 303 and the first heat energy recovery valve 301, The piece P6 is sent back to the heating source 601; the cooling water from the load unit 603 is supplied to the first condensing evaporator 102 through the second cold energy recovery valve 402 via the pipe P2, and at this time, the first condensing evaporator 102 is used as a condenser; The water is further cooled to the second adsorption bed 2〇1 17 200928261 via the third cold energy recovery valve 403 and the second thermal energy recovery valve 302, and then returned to the load unit 603 via the third heat recovery valve 303. At this time, the vapor pressure in the first vacuum chamber 100 rises, and when the pressure exceeds the saturated vapor pressure corresponding to the temperature of the first condensing evaporator 102, the condensation starts, and the refrigerant desorbed from the first adsorption bed 101 is discharged. The steam is condensed into a liquid refrigerant; at the same time, the second adsorption bed 201 starts to be cooled and adsorbed, and the pressure of the refrigerant vapor in the second vacuum chamber 200 decreases; the environmental unit 602 sends the ice water from the pipe P4 to the first cold energy recovery valve. 401, the second cold energy recovery valve 402 enters the second condensing evaporator 202, starts evaporative cooling, cools the cooling water, and leaves the second condensing evaporator 202, via the third cold energy recovery valve 403, first Valve 401 can be recycled back to the pipe P5 to the environment unit 602. Referring to FIG. 2B, the heat energy recovery process from the first adsorption bed 101 to the second adsorption bed 201 is shown. The difference between this process and FIG. 2A is that the first thermal energy recovery valve 301 and the second thermal energy recovery valve 302 are reversed. After the hot water is passed from the pipe member P1 into the first heat energy recovery valve 301, the pipe member P6 is bypassed and returned to the heating source 601; after the first heat energy recovery valve 301 and the second heat energy recovery valve 302 are reversed, the first adsorption may be performed in the first adsorption. The hot water in the bed 101 is pushed to the second adsorption bed 201 via the thermal energy recovery valves 303, 3 (at this time, the cooling water originally residing on the second adsorption bed 201 will be discharged through the third thermal energy recovery valve 303). Returning from the tube Ρ3 to the load unit 603. Please refer to FIG. 2C, which shows the cold energy recovery process from the second adsorption bed 201 to the first adsorption bed 101: the difference between this process and the second embodiment is that the first cold energy is The recovery valve 401 and the second cold energy recovery valve 402 are reversing; the environmental unit 602 sends the ice water to the first cold energy recovery valve 401 via the pipe Ρ 4, and is directly bypassed by the pipe Ρ 5 to the environmental unit 602; Two condensation 18 200928261 Cooling in evaporator 202 The cold energy recovery valves 403, 401, and 402 can flow into the first condensing evaporator 1〇2, so that the ice water originally residing in the first condensing evaporator 102 is discharged through the third cold energy recovery valve 403, and then The second thermal energy recovery valve 302 is connected in series and continues to the adsorption bed thermal energy recovery process shown in Figure 2B. Please refer to Figure 2D, which shows the second adsorption bed 201 desorption and the first adsorption bed 101 adsorption process: the process and The difference between FIG. 2C is that the third thermal energy recovery valve 303, the first thermal energy recovery valve 301, the third cold energy recovery valve 403, and the first cold energy recovery valve 401 are reversed; when the heat and cold energy recovery process is completed. 'The hot water enters the second adsorption bed 201 through the first heat energy recovery valve 301 and the second heat energy recovery valve 302 through the pipe P1, and is heated and adsorbed to leave the second adsorption bed 201, and then passes through the third heat energy recovery valve 303 and the first heat energy. The recovery valve 301 is returned from the pipe member P6 to the heating source 601; the cooling water from the load unit 603 enters the second condensing evaporator 202 through the second cold energy recovery valve 402 via the pipe member P2. At this time, the second condensing evaporator 202 is Use as a condenser Then, the third heat energy recovery valve 403 is connected in series to the second heat energy recovery valve 302 to enter the first adsorption bed 1〇1 to be cooled and adsorbed, then left, enters the third heat energy recovery valve 303, and then returns to the load unit 6 by the pipe member P3. 3; at this time, the vapor pressure in the second vacuum chamber 200 rises, and when the pressure exceeds the saturated vapor pressure corresponding to the temperature of the second condensing evaporator 202, 'starts condensation to desorb the second adsorption bed 2〇1 The refrigerant vapor is condensed into a liquid refrigerant; at the same time, the first adsorption bed 1 〇 1 starts to be cooled and adsorbed, and the pressure of the refrigerant vapor in the first vacuum chamber 1 随之 decreases; meanwhile, the environmental unit 602 provides ice water 'via the pipe P4 The first cold energy recovery valve 401 and the second cold energy recovery valve 402' re-enter the first condensing evaporator 1〇2', and the evaporation surface starts to evaporate 200928261, and the generated ice water finally leaves the first condensation evaporation. After passing through the third cold energy recovery valve 403 and the first cold energy recovery valve 401, the device 102 is returned to the environmental unit 602 by the pipe member P5. Referring to FIG. 2E, the heat energy recovery process from the second adsorption bed 201 to the first adsorption bed 101 is shown. The difference between this process and FIG. 2D is that the first thermal energy recovery valve 301 and the second thermal energy recovery valve 302 are reversed. When the first and second adsorption beds 101, 201 are desorbed and the adsorption process is completed, a heat energy recovery process is required; the cooling water supplied from the load unit 603 passes through the second cold energy recovery valve 402 and the second condensation evaporation from the pipe member P2. The second cold energy recovery valve 403 and the second thermal energy recovery valve 302 enter the second adsorption bed 201, and the hot water originally residing in the second adsorption bed 201 is pushed to the thermal energy recovery valves 303, 301, 302 to The first adsorption bed 101, at this time, the cooling water originally residing on the first adsorption bed 101 will be returned to the load unit 603 through the third heat recovery valve 303 and then through the pipe P3. Please refer to FIG. 2F, which shows the cold energy recovery process from the first adsorption bed 101 to the second adsorption bed 201. The difference between this process and FIG. 2E is that the first cold energy recovery valve 401 and the second cold energy recovery valve are 402 is reversing; the ice water residing in the first condensing evaporator 102 can flow into the second condensing evaporator 202 via the cold energy recovery valves 403, 401, 402, and the cooling originally resident in the second condensing evaporator 202 The water is discharged; and the ice water of the environmental unit 602 enters the first cold energy recovery valve 401 by the pipe member P4, and can be directly bypassed and returned to the environmental unit 602 by the pipe member P5; and the cooling water from the load unit 603 can enter the first portion through the pipe member P2. A condensing evaporator 102, the ice water originally residing in the first condensing evaporator 102 is pushed to the second condensing evaporator 202 via the cold energy recovery valves 403, 401, 402, and will remain at 20 200928261
卻水推送經“三冷能回收閥 所示之吸附床熱能回收過=口收間3G2並接續前述圖二E 即可= F步驟猶序週而復始循環運行， 與管二:之體吸附式熱泵裝置’將閥 使用者所需變換製二戈製：功：合於固體吸附裝置，可隨 暖製熱之季節性季製冷、冬季採 能回收、冷能回收等㈣機η機運行雜中採取熱 控制’可有效解決水源端之水量與冰，做旁通 具有高效熱冷能回收功能，以及問題’同時 體系统之性能錄(GGP)。 q H、&力提高整 ^以上所述者，僅為本糾之最佳實 :^限^本發明所實施之範圍。即大凡依本發明申芯 蓋之r:=r=員皆應仍屬於本發明專利涵 禱。心貝審查委員明鏗，並祈惠准，是所至 【明武簡單說明】 圖-係本發明實施罐於製冷模式之架構示意圖。 圖-A至圖-F係本發明製冷程序之連續步驟圖。 ^二係本發明實施例處於製熱模式之架構示意圖。 至圖二F係本發明製熱程序之連續步驟圖。 200928261 【主要元件符號說明】 100- 第一真空腔體 101- 第一吸附床 102- 第一冷凝蒸發器 200- 第二真空腔體 201- 第二吸附床 202- 第二冷凝蒸發器 300- 熱能回收閥組 301- 第一熱能回收閥 302- 第二熱能回收閥 303- 第三熱能回收閥 400-冷能回收閥組 40卜第一冷能回收閥 402- 第二冷能回收閥 403- 第三冷能回收閥 500- 模式轉換裝置 501- 第一轉換閥 502- 第二轉換閥 601- 加熱源 602- 環境單元 603- 負載單元 A-主機 22 200928261 P1〜P6-管件 ❹ Ο 23However, the water is pumped through the “three cold energy recovery valve”, and the heat recovery of the adsorption bed is as follows: 3G2 in the mouth and then in the above-mentioned Figure 2E. The F step can be repeated in the cycle, and the tube 2: the body adsorption heat pump device 'The valve user needs to change the system to two systems: work: combined with the solid adsorption device, can be used with heating and heating seasonal seasonal refrigeration, winter energy recovery, cold energy recovery, etc. (4) machine η machine operation miscellaneous heat Control 'can effectively solve the water quantity and ice at the water source end, do the bypass with high efficiency heat and cold energy recovery function, and the problem 'the performance of the simultaneous body system (GGP). q H, & force increase the above ^, It is only the best of this correction: ^ Limits the scope of the implementation of the invention. That is, the R:=r= members of the core cover according to the invention should still belong to the patent of the invention. BRIEF DESCRIPTION OF THE DRAWINGS Figure-A to Figure-F are diagrams showing the continuous steps of the refrigeration program of the present invention. The schematic diagram of the architecture of the invention in the heating mode is shown in Fig. 2F. Continuous step chart of heating program. 200928261 [Description of main component symbols] 100- First vacuum chamber 101 - First adsorption bed 102 - First condensation evaporator 200 - Second vacuum chamber 201 - Second adsorption bed 202- Second condensing evaporator 300 - heat energy recovery valve group 301 - first heat energy recovery valve 302 - second heat energy recovery valve 303 - third heat energy recovery valve 400 - cold energy recovery valve group 40 - first cold energy recovery valve 402 - Second cold energy recovery valve 403 - third cold energy recovery valve 500 - mode conversion device 501 - first switching valve 502 - second switching valve 601 - heating source 602 - environmental unit 603 - load unit A - host 22 200928261 P1 ~ P6 -Pipe fittings ❹ Ο 23