TW379270B - Drying device and method for drying - Google Patents

Drying device and method for drying Download PDF

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Publication number
TW379270B
TW379270B TW87106295A TW87106295A TW379270B TW 379270 B TW379270 B TW 379270B TW 87106295 A TW87106295 A TW 87106295A TW 87106295 A TW87106295 A TW 87106295A TW 379270 B TW379270 B TW 379270B
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TW
Taiwan
Prior art keywords
dry
drying
exhaust
air
path
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Application number
TW87106295A
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Chinese (zh)
Inventor
Shunichi Kawagoe
Original Assignee
Tosei Denki Kk
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Priority to TW87106295A priority Critical patent/TW379270B/en
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Publication of TW379270B publication Critical patent/TW379270B/en

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  • Accessory Of Washing/Drying Machine, Commercial Washing/Drying Machine, Other Washing/Drying Machine (AREA)
  • Drying Of Solid Materials (AREA)

Description

A7A7

7 B 明説明發 、五 經 及 類 衣 之 灌 洗 劑 溶 洗 乾 經0 乾 稻1 於 關 係 明 發 本 型 環 循 路 開 型 氣 kl·· 中 〇 氣法 大方 用燥 兼乾 的及 類置 衣裝 之煉 濯乾 洗e) 洗cl 水cy7 B Explanatory instructions for hair, five classics, and clothing-like lavage agents. Dissolve and dry the classics. 0 Dry rice. 1 In relation to Mingfa, this type of open-loop circulation gas kl · · Zhong〇 Qi method should be used dry and dry. Clothing dries dry cleaning e) wash cl water cy

銜 持 之 沣W沣 W

烯 乙 氯 全 用 使 要 主 中 業 作 洗 乾 在 注M 揮之 之等 等染 隆污 氟境 ’ 環 烷止 乙防 Θ 因 lenit y , th劑 oe溶 or洗 hi乾 c -Γ 之 θ ρ 等 劑 溶 成 合 機 有 性 發 用 使 其 制 節 上 點 觀 劑 溶 洗 乾 係 油 石 之 等 劑 溶 係 氫 化 碳 用 使 要 主 來 年 近Μ 所 劑 溶 成 合 機 有 性 發 揮 述 上 之 統 傳 替 代 以 服 衣 之 灌 洗 \J/ 劑 溶 為 略 簡 下 以 /|\ 劑 溶 洗 乾 以 將 要 知 眾 閉 密 該 在 ο 置 裝 燥 乾 用 洗 乾 之 型 環 循 閉 密 用 使 多 時 燥 乾 室 化 燥氣 乾成 進.發 送蒸 氣 ’ 空劑 之溶 熱 之 加服 被衣 將於 係 含 ’ 將 而 類 衣 熱 加 内 室 燥 乾 在 置 裝 燥 乾 用 洗 乾 之 型 環 循 劑 溶 之 中 氣 室 氣 «W 於 含 將 氣 空 之 出 bh 室 燥 乾 從 却 冷 並 室 煉 乾 進 送 而 熱 加 氣 室 之 氣 蒸 劑 溶 了 離 分 將 再 化 液 汽 蒸 環 循 作 燥 乾 類 衣 將 邊1 劑 溶 收 回 邊 ----τ----1 装 — I (讀先閱讀背面之注意事項再填寫本頁)All ethyl chloride is used to make the main business for washing and drying in the injection of M and so on. The naphthene stops the ethyl fluoride. Θ Because of lenit y, th agent oe dissolve or wash hi dry c-Γ θ ρ The equivalence of the dissolving and combining machine can be used to make the point of view of the solvent dissolving and drying of dry oilstones. Instead of rinsing with clothing \ J / agent dissolve for simplicity, use / | \ agent to dissolve and dry to seal the public. It should be installed in a dry and circular type for long time. Drying and drying the room into the dry air into the dry. Send steam 'empty agent of the heat of the plus-coats will be included in the system' will be the same type of heat plus the internal room to dry in the installation of dry-drying cycle Dissolving the gas in the gas chamber «W contains the air from the bh chamber to dry and dry from the cold and the chamber to dry and feed, while the hot gas chamber vaporizer dissolves and separates the steam and recirculates the liquid. Dry clothes Edge 1 agent dissolves and collects back ---- τ ---- 1 Pack — I (Read the precautions on the back before filling this page)

、1T !1 經濟部中央標準局—工消費合作社印製 之 I: 理 處 因 有 而 因 質 物 性 燃 可 為 來 本 係 劑 溶 之 系 油 石 意 注 分 充 要 需 時 m: ux3 TJ 處 在 是 於 虡 之 炸 爆 或 災 火 生 產 而 當 不 起事 止發 防爆 了火 為引 ’ 之 置等 裝電 燥靜 乾生 用發 洗或 乾機 的火 劑打 溶之 之等 系服 油衣 石於 該入 用 混 使誤 在於 ο 因 燥持 乾維 進度 送湄 制體 控氣 未劑 度溶 溫之 側化 口汽 出蒸 之之 室內 煉室 乾煉 自乾 未將 測成 檢度 有溫 知風 已 溫 。 之 故室 氣 氮 或 置 裝 壓 減 備 具 是 或 法 方 的 下 以 限 下 發 爆 之 定 所 在 本紙張尺度適用中國國家標準(CNS ) Λ4規格(210X 297公釐) 1 3 97 2 9、 1T! 1 Printed by the Central Standards Bureau of the Ministry of Economic Affairs-Industrial and Consumer Cooperatives I: The processing department can be used for the injection and dissolution of oil-based oilstones due to the nature and nature of the material. It takes time to m: ux3 TJ is at It is Yu Zhizhi's explosive or catastrophic fire production and can't afford to stop the explosion. The fire is ignited. Equipped with electric hair dryer or hair dryer to dissolve gunpowder, etc. The misunderstanding of Shi Yu's mixed use is that the indoor refining chamber of the side refining mouth of the side opening of the controlled temperature and the temperature of the unsolved solution is sent to the Mekong due to the dryness and maintenance. The dryness has not been measured. Wen Zhifeng is already warm. The reason for the room gas nitrogen or installation pressure reduction equipment is the explosion limit of the French or French. The Chinese standard (CNS) Λ4 specification (210X 297 mm) applies to this paper scale 1 3 97 2 9

.II- - m ml HI 經濟部中央標準局員工消費合作社印聚 A7 B7 五、發明説明(2 ) 等之惰性氣體產生裝置未減壓乾燥室或填充惰性氣體等來 減低氧氣濃度的方法。 並且,在水洗洗灌之衣服等之乾燥•使用大氣排氣型 之水洗用乾燥裝置,在該大氣中排氣型之水洗用乾燥裝置 ,係將被加熱之空氣送進乾燥室,在乾燥室内加熱衣服而 將含於衣服之水分蒸氣化並將含於水分之空氣放出至大氣 中 0 玆明欲解決之課穎 然而,Μ往之乾燥裝置,係必須分別K用之乾燥裝置 來乾燥以溶劑洗濯之衣服與Μ水洗洗濯之衣服。亦即,兼 用容閉循環型之乾洗用乾燥裝置而欲乾煉以水洗洗灌之衣 服時,由於無法充分回收排氣空氣中之水分而將空氣繼鑛 循環,因此,乾燥效率差,而且回收多量之水而混入溶劑 ,要分離該水與溶劑則必須使用大型之分離裝置•而具有 很難兼用之問題。 並且,在乾燥過程,為了防止衣服之起謅之發生或為 了使乾烽後之衣服具有優異之穿著感而冷却過程,惟即使 例如將外氣導入於乾燥室,也無法充分地冷却,因而無法 得到圓滿之完工狀態,同時需費較久之冷却過程的時間。 並且,由於在冷却採用水冷却方式,且水溫大約在 5〜201C ,為偏高之溫度,因此冷卻效率較低•而且將溶 劑凝结並經液化而回收之回收效率低,並且冷却後之排氣 風溫度也無法充分成為低溫之狀態。 在密閉循環型之乾洗用乾燥裝置,雖在循環途中冷却 ! I 裝------訂------1 一 一 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) Λ4規格(210X297公釐) 2 3 9 72 9 A7 B7 經漪部中央標準局員工消費合作社印掣 五、發明説明 ( 3 ) 1 排 氣 風 並 凝 结 溶 劑 蒸 汽 經 液 化 來 回 收 惟 仍 然 包 含 相 1 1 I 抵 於 冷 却 後 之 排 氣 風 溫 度 的 飽 和 蒸 汽 濃 度 分 量 之 溶 劑 蒸 汽 1 I 下 再 被 循 環 至 乾 燥 室 内 * 因 此 無 法 避 免 降 低 乾 馈 效 率 ,、 1 I 請 ♦ 及 增 加 乾 燥 室 内 之 溶 劑 氣 體 濃 度 〇 而 且 未 慮 在 乾 煉 室 内 先 閱 1 1 1 之 溶 劑 氣 體 的 發 生 狀 況 , 且 僅 檢 測 來 白 乾 燥 室 之 出 口 側 溫 背 I 之 1 1 度 未 控 制 送 進 乾 W 室 由 之 溫 風 溫 度 則 不 但 溶 劑 氣 體 濃 度 /1 意 1 1 事 1 較 高 而 且 考 畺 因 出 □ 側 溫 度 較 低 而 控 制 成 提 高 溫 風 溫 度 項 再 i 1 > 結 果 > 會 增 加 溶 劑 氣 體 濃 度 〇 本 |f 於 此 種 增 加 溶 劑 氣 體 濃 度 在 減 壓 或 填 充 惰 性 氣 體 來 Η 、_- 1 1 I 對 應 之 方 法 > 因 須 附 加 減 壓 泵 或 惰 性 氣 體 發 生 裝 置 t 使 乾 1 1 燥 室 之 密 閉 性 或 強 度 成 為 問 題 因 此 機 械 成 為 昂 貴 相 1 1 對 地 成 為 大 型 化 0 又 、 也 必 需 減 壓 時 間 或 惰 性 氣 體 封 入 時 訂 1 由 而 會 增 加 時 間 0 1 1 本 發 明 係 鑑 於 此 種 問 題 點 而 創 作 者 其 目 的 在 於 提 供 1 1 一 種 可 乾 燥 Η 乾 洗 溶 劑 及 水 洗 所 洗 灌 之 衣 服 等 之 雙 1 Λ 方 的 兼 用 型 且 大 氣 中 排 氣 型 之 乾 燥 裝 置 及 乾 m 方 法 0 1 解 決 課 m 所 用 手 段 1 申 請 專 利 範 圍 第 1項之乾煉裝置 其特徵為具備: 配 1 1 設 乾 燥 鼓 筒 的 乾 燥 室 及 具 有 連 通 於 該 乾 燥 室 之 加 熱 器 的 1 1 供 氣 路 t 及 連 通 於 上 述 乾 燥 室 f 具 有 冷 却 器 之 冷 却 通 路 部 1 與 並 排 設 有 旁 通 該 冷 却 通 路 部 之 旁 通 通 路 部 同 時 設 有 向 I 下 游 側 大 氣 開 放 之 排 氣 口 的 排 氣 路 , 及 連 接 於 上 述 冷 却 通 1 1 I 路 部 的 溶 劑 回 收 路 9 及 通 過 上 述 乾 燥 室 從 供 氣 路 送 風 至 排 1 1 1 氣 路 的 送 風 機 > 及 轉 換 上 述 乾 煉 室 與 上 述 冷 却 通 路 及 旁 通 1 1 本紙張尺度適用中國國家標準(CNS ) Λ4規格(210X 297公釐) 3 3 9 7 2 9 A7 A7 經濟部中央標準局貞工消費合作社印製 B7 五、發明説明(4 ) 通路部之任何一方連通的冷却旁通轉換機構者。 欲乾燥以乾洗溶劑洗灌之衣腋類時,經由在乾燥室連 通排氣路之冷却通路部,而藉由冷却通路部之冷却器來將 乾燥室蒸發氣化之溶劑凝结或液化蒸汽並予Μ回收,同時 將分離溶劑蒸汽之空氣排氣至大氣中以減低乾燥窒之溶劑 氣體濃度。另一方面,欲乾燥Μ水洗洗灌之衣服類時,經 由在乾燥室連通排氣路之旁通通路部•不必回收在乾燥室 被蒸發氣化之水分而排出至大氣中。因此可提供一種可乾 煉Μ乾洗溶劑及水洗洗灌之衣服等雙方之兼用型且大氣中 排氣型之衣服等的乾燥裝置。 申請專利範圍第2項之乾燥裝置,係在申請專利範圍 第1項之乾燥裝置中,具備:連通排氣路之下游側與乾烽 室的循環路,及開放排氣路之排氣口側與循環路側之任何 一方,並轉換成閉鎖另一方的排氣循環轉換手機構,及在 上述排氣口之開放時開放供氣路同時在上述循環路之開放 時閉鎖的供氣路開閉機構。 在乾燥過程中,經由閉鎖循環路及開放供氣路,構成 供氣路及排氣路被開放至大氣中的大氣中排氣型*提髙乾 燥效率,又,在乾燥過程後最後加工衣腋等之冷却過程中 ,經由開放循環路及供氣路,將通過冷却通路部之冷風送 進乾燥室俾急速冷却衣服類,提高冷却效率並縮短冷却過 程所費之時間。 申請專利範圍第3項之乾燥裝置係在申請專利範圍第 1項或第2項之乾燥裝置中,冷却通路郜之冷却器係被分割 、張尺度適用中國國家標準(〇奶)六4規格(210/297公釐) 4 3 9 7 2 9 (锖先閱讀背而之注意事項再填巧本頁) •裝_ 、\=° A7 B7 經滴部中央標率局員工消費合作社印製 五、發明説明 ( 5 ) 成 複 數 個 並 沿 著 通 路 方 向 隔 離 地 配 置 同 時 依 從 冷 却 通 路 1 部 之 上 方 冷 却 器 至 下 方 冷 却 器 之 順 序 流 通 冷 媒 » 流 通 過 乾 1 燥 室 之 冷 却 通 路 部 之 排 氣 » 係 從 冷 却 通 路 部 之 下 方 向 上 方 --V 1 I 讀 1 I 流 通 者 0 先 閱 1 I 讀 1 r 排 氣 溫 度 係 一 面 在 冷 却 通 路 部 上 昇 一 面 階 段 地 冷 却 * 背 1 之 1 而 隨 著 通 過 各 冷 却 器 之 排 氣 溫 度 來 形 成 各 冷 却 器 之 溫 度 坡 旁 % 1 度 、 因 此 白 動 地 分 配 冷 媒 之 熱 交 換 能 力 、 經 濟 又 有 效 率 項 —1 填 » 地 實 行 冷 却 〇 寫 本 裝 | 申 請 專 利 範 圍 第 4項之乾燥裝置 係在申請專利範圍 頁 1 1 第 1項至第3項 中 任 何 一 項 之 乾 燥 裝 置 中 冷 却 器 係 與 具 有 ! 1 凝 结 器 及 壓 縮 機 之 冷 凍 機 機 組 —* 起 構 成 使 用 冷 媒 氣 體 的 冷 1 1 凍 循 環 的 蒸 發 器 而 冷 凍 機 機 組 儀 設 於 屋 外 者 〇 訂 | Μ 蒸 發 溫 度 降 低 至 例 如 0它附近之冷媒氣體來冷却排 1 I 氣 充 分 地 降 低 排 氣 溫 度 提 高 溶 劑 之 回 收 效 率 〇 由 於 將 1 1 | 冷 凍 機 機 組 設 於 屋 外 可 防 止 因 設 有 乾 燥 裝 置 之 室 內 之 溫 1 度 上 昇 或 噪 音 等 所 引 起 的 作 業 環 境 之 惡 化 同 時 可 形 成 冷 1 凍 機 機 組 之 有 效 率 的 運 輸 〇 1 申 請 專 利 範 圍 第 5項之乾燥方法 係使用申請專利範 圍 第 1項至第4項 中 任 何 一 項 之 乾 燥 裝 置 的 乾 tfl. m 方 法 » 其 特 1 I 徵 為 : 在 包 括 從 開 始 乾 煉 至 乾 燥 室 之 溶 劑 氣 體 濃 度 之 尖 峰 1 I 的 第 1階段由乾燥室之入口側溫度來控製加熱器 在連缜 1 於 經 過 乾 燥 室 之 溶 劑 氣 體 濃 度 之 尖 峰 的 第 1階段的第2 階 段 1 1 則 由 乾 燥 室 之 出 □ 側 溫 度 來 控 制 加 埶 器 者 〇 1 1 在 第 1階段, 將乾燥室内之溶劑氣體濃度確實地維持 1 1 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 5 3 9 7 2 9 經濟部中央標率局負工消費合作社印裝 A7 B7 五、發明説明(6 ) 在預定濃度Μ下,而在第2階段提高乾燥效率,同時防止 衣服類之溫度的過度上昇。 發明之昔施形態 以下,參照圖式說明本發明之一實狍形態。 在第1圖,衷示可乾燥以乾洗溶劑及水洗洗灌之衣服 類雙方之兼用型且大氣中排氣型的乾燥裝置。 在第1圖中,1係乾燥室*而在該乾燥室1 Μ衝孔金屬( punsh丨ng raetat)等所形成,而具有多數通過孔之略圓筒 形之乾燥筒(drying drura)2旋轉自如地配設於周圍,從乾 燥室1之未予圖示的前面開閉門扉成為作為被乾燥物之衣 服等之取出放進乾燥筒2內。在乾燥简2内突設有攪拌衣服 的複數攪伴翼3。 在乾燥室1之上部開設有排氣口 9,而在該排氣口 9連 通有排氣路10,該排氣路10係經過乾煉室1之下部而與乾 烽室1之下部而與乾燥室1並聯地配設成略垂直狀,在其上 端亦即在下游側形成有向大氣開設的排氣口 11。在排氣路 10之垂直部分的中間部並聯地形成有冷却通路郜12及旁通 通路部13、而此等冷却通路部12及旁通通路部13之下端及 端係互相連通。排氣路10之排氣口、11近旁連接有連通於 供氣路5之循環路14。 在排氣路10下部之水平部分,配設有經乾燥室1而從 供氣路5側送風至排氣路5側的送風機15,同時在該送風機 15之吸入側配設有棉線過濾器(lint fiUer)16。 在排氣路10之冷郤通路部12,具有連績之冷媒管17的 本紙張尺度適用中國國家標率(CNS ) Λ4規格(210X297公釐) R 39 7 2 9 _ . ^ ^ .裝 訂------J )--- (誚先閱讀背而之注意事項再填艿本頁) 經濟部中央標準局員工消費合作杜印製 A7 B7 五、發明説明(7 ) 兩個冷却器18、19係例如隔著30〜50am之間隔上下地配設 。此等冷却器18、19的冷媒管17之兩端係連通於設在屋外 的冷凍機機組20,冷凍機機組20係內設未予圖示之凝结器 及壓縮機。因此,冷却器18,19功能作為蒸發器;而藉由 凝结器,壓縮機及冷却器18, 19形成有使用代替氟隆等之 冷媒氣體的冷凍循環。如此被壓縮之冷媒從冷凍槠機組20 供應至冷却器1δ之冷媒管17之上部,成為從上向下循環流 通冷媒管17,亦即,從上段之冷却器18至下段之冷却器19 之順序成為循環流通。又,在冷凍機機組20與上段冷却器 18之間的冷媒管17配設有調整冷媒流量的調整閥21。 在排氣路10之冷媒通路部12之下部連通有溶劑回收路 22,而在溶劑回收路22連接有依溶劑與水之化重所分離的 溶劑水分離器23。 在排氣路10之排氣口 11與循環路14之間,配設有作為 能轉換成開放排氣口 11與循環路14之任何一方,並閉鎖另 一方之排氣循環轉換機構的第1轉換擋板29。 在供氣路5之中間部,配設有作為在排氣口 11之開放 時開放供氣路5,同時在循環路14之開放時閉鎖供氣路5之 供氣路開閉機構的第2轉換擋板25。 任冷却通路部12與旁通通路部13之上游部分亦即在下 部連通部分,配設有作為轉換乾燥室1與冷却通路部12Κ 及旁通通路13之任何一方之連通之冷却旁通轉換機構的第 3轉換擋板26。 第1至第3各轉換擋板20〜26,係Μ空氣缸,油壓缸或 本纸張尺度適用中國國家標準(CNS ) Λ4規格(210X 297公釐) _ _____ J . j I 裝------訂-----f 線一 (請先閱讀背面之注意事項再填寫本頁) A7 B7五、發明説明(8 ) 電磁裝置等,施行轉換開閉。 在乾燥室1之入口側配設有第1溫度推出器27,而在乾 器 9 測 2 淠器 檢 Μ Ϊ測 度檢 溫 t 2 度 第溫 有 設 配 側 P 出 之 第 有 設 配 邊 口 出 室 之 ? 2 燥 1 部 路 通 却 冷 在 又 器 測 檢 度 溫 各 等 此 燥 乾 之 服 衣 的 灌 洗 。 劑 用溶 。 作洗 成之乾 構態之 所形泵 等施油 阻實石 電本 K 敏 明 明 熱.說說 由, , 係下先 29M 首 □ 氣 放 4 2 板 擋 換 轉 il 第Μ 係 時 燥 乾 之 洗 乾 在 路 環 循 將 而 板 擋 換 轉 3 第.II--m ml HI Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (2) The inert gas generating device such as (2) does not decompress the drying chamber or fill the inert gas to reduce the oxygen concentration. In addition, for drying and washing clothes and clothes in water, use an air-exhaust-type water-washing drying device. The air-exhaust-type water-washing drying device sends heated air into the drying room, and in the drying room. Heat the clothes to vaporize the water contained in the clothes and release the air containing the moisture to the atmosphere. However, the drying device to be used must be a drying device used to dry the solvent. Wash your clothes and wash your clothes with M water. That is, when using a closed-cycle type dry-cleaning drying device to dry clothes washed with water, the air in the exhaust air cannot be fully recovered and the air is recycled to the mine. Therefore, the drying efficiency is poor and the recycling A large amount of water is mixed into the solvent, and to separate the water and the solvent, a large-scale separation device must be used, and it is difficult to use both. In addition, in the drying process, in order to prevent the occurrence of the rise and fall of the clothes or to make the dried clothes have an excellent wearing feeling, the cooling process is performed. However, even if external air is introduced into the drying room, the cooling cannot be sufficiently performed, so A satisfactory completion state is obtained, and a longer cooling time is required. In addition, because the water cooling method is used for cooling, and the water temperature is about 5 ~ 201C, which is a relatively high temperature, the cooling efficiency is low. Moreover, the recovery efficiency of condensing the solvent and recovering by liquefaction is low. The air-wind temperature cannot be sufficiently low. Dry-drying device for dry-cleaning in a closed cycle type, although it is cooled during the cycle! I installed -------- order ----- 1 1 (please read the precautions on the back before filling this page) Applicable to Chinese National Standard (CNS) Λ4 specification (210X297 mm) 2 3 9 72 9 A7 B7 Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (3) 1 Exhaust air and condensed solvent vapors through liquefaction Recovered but still contains the solvent vapor 1 I of the saturated steam concentration component of phase 1 1 I which is lower than the temperature of the exhaust air after cooling, and then is recycled into the drying chamber * Therefore it is unavoidable to reduce the dry feed efficiency, 1 I please ♦ and increase The concentration of the solvent gas in the drying chamber is 0, and the occurrence of the solvent gas in the dry refining chamber is not taken into consideration, and only the temperature at the outlet side of the white drying chamber is detected. As a result, the temperature of the warm air is not only the concentration of the solvent gas / 1, but the higher the temperature, the higher the temperature of the air temperature due to the lower temperature on the outlet side. I 1 > Result > will increase the concentration of the solvent gas 〇 本 | f In this way, increase the concentration of the solvent gas under reduced pressure or fill it with inert gas. _-1 1 I corresponding method > Since a decompression pump or an inert gas generating device must be added to dry the 1 1 drying chamber. Since the tightness or strength becomes a problem, the machinery becomes an expensive phase. 1 1 It becomes large-scale on the ground. It also requires a decompression time or an inert gas seal. Ordering 1 will increase the time. 0 1 1 The present invention is based on this problem. The creator's purpose is to provide a pair of dry 1 dry cleaning solvents and clothes washed in the washing room 1 Λ square dual-use type and air-exhaust type drying device and dry m method 0 1 Solving class m Means 1 The patent application scope of the first dry refining device is characterized by: equipped with 1 1 drying with a drying drum The cooling chamber 1 and a gas supply path t having a heater communicating with the drying chamber and the cooling passage 1 having a cooler communicating with the drying chamber f are provided at the same time as a bypass passage portion provided in parallel with the cooling passage portion. There is an exhaust path with an exhaust port open to the atmosphere on the downstream side of I, and a solvent recovery path 9 connected to the above-mentioned cooling passage 1 1 I path, and the air is sent from the air supply path to the exhaust 1 1 1 air path through the drying chamber. Fan > And change the above dry refining chamber to the above cooling path and bypass 1 1 This paper size is applicable to China National Standard (CNS) Λ4 specification (210X 297 mm) 3 3 9 7 2 9 A7 A7 Industry and Consumption Social printed B7 V. Description of the Invention (4) by any one of the cooling bypass switching mechanism portion of the communication passage. When drying the armpits of clothes washed with dry cleaning solvent, the cooling passage of the exhaust passage is connected to the drying chamber, and the cooler of the cooling passage is used to condense or liquefy the solvent evaporated in the drying chamber and liquefy the steam. M is recovered, and at the same time, the air from which the solvent vapor is separated is exhausted to the atmosphere to reduce the concentration of the solvent gas in the drying process. On the other hand, if you want to dry clothes washed and filled with M water, you do not need to collect the water vaporized and vaporized in the drying room and discharge it to the atmosphere. Therefore, it is possible to provide a drying device capable of drying both the dry-cleaning solvent and clothes washed with water and the like, and clothes which are exhausted in the atmosphere. The drying device in the scope of patent application No. 2 is the drying device in the scope of patent application No. 1. It includes: a circulation path connecting the downstream side of the exhaust path and the drying chamber, and an exhaust port side opening the exhaust path Any one of the circulation path side is converted into an exhaust circulation switching hand mechanism for blocking the other side, and an air supply path opening / closing mechanism which opens the gas supply path when the exhaust port is opened and is closed when the circulation path is opened. During the drying process, the closed air circulation path and the open air supply path are used to form an air exhaust type in which the air supply path and the exhaust path are opened to the atmosphere. * The drying efficiency is improved, and the armpit of the garment is finally processed after the drying process. During the cooling process, the cold air passing through the cooling passage part is sent to the drying room via the open circulation path and the air supply path, and the clothes are rapidly cooled to improve the cooling efficiency and shorten the time taken for the cooling process. The drying device in the scope of the patent application No. 3 is among the drying devices in the scope of the patent application No. 1 or 2. The cooler of the cooling passage 郜 is divided, and the scale is applicable to the Chinese National Standard (〇 奶) 6 4 specifications ( 210/297 mm) 4 3 9 7 2 9 (read the precautions before filling in this page) • Install _ 、 \ = ° A7 B7 Printed by the Consumer Standards Cooperative of the Central Standards Bureau of Didi Ministry Description of the Invention (5) A plurality of and arranged in isolation along the passage direction while circulating refrigerant in the order from the upper cooler to the lower cooler of the cooling passage 1 »Exhaust gas flowing through the cooling passage portion of the drying chamber 1» From the bottom of the cooling passage section to the top--V 1 I Read 1 I Circulator 0 Read first 1 I read 1 r The exhaust temperature is gradually cooled as it rises in the cooling passage section * Cooler The exhaust temperature is used to form the temperature slope of each cooler% 1 degree. Therefore, the heat exchange ability of the refrigerant is distributed in a free movement, and it is economical and efficient. —1 Fill in the cooling. The drying device is in the range of patent application page 1 1 The drying device in any one of items 1 to 3 The cooler is connected with the refrigerating machine unit with! 1 condenser and compressor— * constitutes the cooling using refrigerant gas 1 1 The evaporator of the refrigeration cycle and the freezer unit is installed outside the house. Order | Μ Evaporation temperature is reduced to, for example, 0 refrigerant gas near it to cool the exhaust 1 I gas fully reduces the exhaust temperature and improves the solvent recovery efficiency. The 1 1 | freezer unit can be installed outside the house to prevent 1 degree temperature rise or noise in the room with the drying device. The deterioration of the operating environment can also form an efficient transportation of the cold 1 freezer unit. 1 The drying method of the scope of patent application No. 5 uses a drying device of any of the scope of patent applications No. 1 to 4. Dry tfl.m method »Its special 1 I characteristic is: In the first stage including the peak 1 I of the solvent gas concentration from the beginning of the dry refining to the drying chamber, the heater's inlet side temperature is used to control the heater in the flail 1 to After passing the peak of the solvent gas concentration in the drying chamber, the second stage 1 1 of the first stage is controlled by the temperature at the outlet side of the drying chamber. 1 In the first stage, the concentration of the solvent gas in the drying chamber is determined. To maintain 1 1 This paper size applies Chinese National Standard (CNS) A4 specifications (210X297 mm) 5 3 9 7 2 9 Printed A7 B7 by the Consumers ’Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (6) At the concentration M, the drying efficiency is improved in the second stage. Prevent excessive rise in temperature of the fabrics. Embodiments of the Past of the Invention Hereinafter, one embodiment of the present invention will be described with reference to the drawings. In Fig. 1, a drying device capable of drying both dry-cleaning solvents and water-washed clothes is shown. In the first figure, 1 series of drying chambers * are formed by punching metal (punsh 丨 ng raetat) and the like in the drying chamber, and a slightly cylindrical drying drum (2) having a large number of holes is rotated. It is freely arranged in the surroundings, and the clothes which are opened and closed from the front of the drying chamber 1 which is not shown in the drawing are taken out and put into the drying drum 2. A plurality of agitation companion wings 3 for agitating clothes are protruded inside the dry jean 2. An exhaust port 9 is opened at the upper part of the drying chamber 1, and an exhaust path 10 is communicated with the exhaust port 9. The exhaust path 10 passes through the lower part of the drying chamber 1 and communicates with the lower part of the drying chamber 1. The drying chambers 1 are arranged in a substantially vertical shape in parallel, and an exhaust port 11 opened to the atmosphere is formed on the upper end, that is, on the downstream side. A cooling passage 郜 12 and a bypass passage portion 13 are formed in parallel at a middle portion of a vertical portion of the exhaust passage 10, and the lower ends and ends of the cooling passage portions 12 and the bypass passage portion 13 communicate with each other. A circulation path 14 communicating with the air supply path 5 is connected to the exhaust ports 10 and 11 of the exhaust path 10. A blower 15 that sends air from the supply path 5 to the exhaust path 5 through the drying chamber 1 is arranged in the lower part of the exhaust path 10, and a cotton filter is provided on the suction side of the blower 15 ( lint fiUer) 16. In the cooling passage section 12 of the exhaust path 10, the paper size of the refrigerant tube 17 with continuous performance is applicable to the Chinese National Standard (CNS) Λ4 specification (210X297 mm) R 39 7 2 9 _. ^ ^. Binding- ----- J) --- (Please read the precautions and fill in this page first) Consumption Cooperation with Employees of the Central Bureau of Standards of the Ministry of Economic Affairs Du printed A7 B7 V. Description of the invention (7) Two coolers 18 The 19 series are arranged up and down, for example, at intervals of 30 to 50 am. Both ends of the refrigerant pipes 17 of the coolers 18 and 19 are connected to a refrigerator unit 20 provided outside the house. The refrigerator unit 20 is provided with a condenser and a compressor (not shown). Therefore, the coolers 18 and 19 function as evaporators, and the condenser, the compressor, and the coolers 18 and 19 form a refrigeration cycle using a refrigerant gas instead of fluorine. The compressed refrigerant thus supplied is supplied from the refrigerating and cooling unit 20 to the upper part of the refrigerant pipe 17 of the cooler 1δ, and the refrigerant pipe 17 is circulated from top to bottom, that is, the sequence from the upper cooler 18 to the lower cooler 19 Become circular. In addition, the refrigerant pipe 17 between the refrigerator unit 20 and the upper cooler 18 is provided with an adjustment valve 21 for adjusting the refrigerant flow rate. A solvent recovery path 22 is connected to the lower portion of the refrigerant passage portion 12 of the exhaust path 10, and a solvent-water separator 23 separated by the weight of the solvent and water is connected to the solvent recovery path 22. Between the exhaust port 11 and the circulation path 14 of the exhaust path 10, a first exhaust circulation switching mechanism that can be switched to either one of the open exhaust port 11 and the circulation path 14 and lock the other exhaust gas circulation switching mechanism is provided. Converting bezel 29. The second part of the gas supply path opening / closing mechanism for opening the gas supply path 5 when the exhaust port 11 is opened and closing the gas supply path 5 when the circulation path 14 is opened is provided in the middle portion of the gas supply path 5 Baffle 25. An upstream portion of the cooling passage portion 12 and the bypass passage portion 13, that is, a lower communicating portion, is provided with a cooling bypass conversion mechanism that is a communication between the drying chamber 1 and either the cooling passage portion 12K or the bypass passage 13.的 第 3 转 垫 26。 The third conversion baffle 26. The first to third conversion baffles 20 to 26 are M air cylinders, hydraulic cylinders, or paper sizes that comply with Chinese National Standards (CNS) Λ4 specifications (210X 297 mm) _ _____ J. J I Packing- ---- Order ----- f Line one (please read the precautions on the back before filling this page) A7 B7 V. Description of the invention (8) Electromagnetic devices, etc., are switched on and off. A first temperature pusher 27 is provided on the entrance side of the drying chamber 1, and a second temperature measurement is performed on the second measurement device t on the second measurement device t on the second measurement device t on the second measurement device. Out of the room? 2 Drying 1 Lutong is cold and the temperature of the device is different. Dissolve with the agent. As a washed dry structure, pumps and other oil-suppressed stone electric books K are bright and clear. Let ’s talk about the first 29M first □ air release 4 2 plate gear change il dry when the M series The washing and drying in the road cycle will be followed by the block change 3

5 路 路通 氣旁 供將 25而 放口 開入 板之 I 2 擋 1 換部 轉路 通 却 冷 放 BHQ 鎖 WIJ ptl?r 第Μ 以 而 之 ---.-----1 I裝-- (請先閱讀背面之注意事項再填寫本頁) 態 狀 之 示 所 圖 11 第 如 為 成 此 因 鎖 閉□ 入 灌 洗 劑 溶 洗 乾 之 系 油 石Μ 入 投 內 2 筒 燥 乾 之 ΊΧ 燥 乾 在 服 衣 的 之 8 器 熱 加 在 環 循 汽 蒸 將 轉 6Ε 始 開 之 置 裝 燥 乾Μ 機 風 送 肋 33 驅 時 同 7 管 汽 加 8 器 熱 加 之 5 路 氣 供Μ 蒸熱 衣 之 内 2 筒 燥 乾 之 轉 旋 被 於 著 附 而 11 室 燥 乾 進 送 即 氣 空 之 化 氣 發 蒸 被 即 劑 溶 洗 乾 的 服 訂 踩 經濟部中央橾準局員工消費合作社印製 路 氣 bh «W 進 吸 被 起 1 氣 空 與 係 汽 蒸 劑 溶 之 化 氣 時 同5 way ventilation side for opening 25 and opening into the board of I 2 Block 1 Change the way to pass but cold put BHQ lock WIJ ptl? R No. M and then ---.----- 1 I installed -(Please read the precautions on the back before filling this page) The state of the figure is shown in Figure 11. This is the reason why it is locked. □ Fill in the rinsing agent to dissolve and dry the oilstone Μ. Ί × 8 heaters that are dried in clothing are added to the cycle steaming and will turn to 6E. The opening and installation of the machine will be equipped with dry and air-drying ribs. 33 The drive is the same as the 7-tube steam plus 8 heaters plus 5 circuits of gas for M steaming. Inside the clothes, 2 cylinders of dry and dry rotation are attached to the 11-room dry and dry feed, that is, air-to-air gasification, vaporization, and instant dissolving and washing. The clothes are printed on the staff ’s consumer cooperative of the Central Bureau of Standards, Ministry of Economic Affairs. Road gas bh «W Intake and suction 1 Air and air are the same as the vaporized solvent

却組, 冷機18 之機器 段凍却 下冷冷 12從在 部通係 路流體 通中氣 却19媒 冷 ,冷 過18該 通器 , 次却體 依冷氣 而18媒 , 器 冷 12却之 路冷縮 通之壓 却段被 冷上之 進及應 送19供 被器 CM 以 所 ο 近 附 V ο 而 2 卻路 冷收 被回 地劑 激溶 急 至 汽出 如蒸排 例劑被 至溶即 低使劑 降,溶 度觸之 溫接化 之之液 體19被 氣,而 媒18, 冷器化 使却液 而冷 , 發與结 蒸由凝 19M1 本纸張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐) 8 3 9 7 2 9 經濟部中央標準局員工消費合作社印繁 A7 __^_B7_ 五、發明説明(9 ) ,從該溶劑回收路22,導入溶劑水分離器23之後被回收。 經冷却遍路部12,溶劑蒸汽被分離之空氣即從排氣口 11被排至大氣中。繼縯該乾燥行程,衣服被乾燥同時將溶 劑回收。 在乾燥行程中,最後將空氣從排氣口 11排向大氣中排 出,因此可將乾燥室1內之溶劑氣體濃度維持較低之濃度 。再且,因送進乾燥室1内之溫風係完全不含有溶劑氣之 外氣,因此該外氣最可提高乾燥效率。並且,因在該乾燥 行程中從排氣口 11向大氣中排出的排氣風係被冷却至例如 約5Ό之低溫,因此而使在排氣風稍含有容劑蒸汽時也很 少有臭氣。 包含通過下段冷却器19之溶劑蒸汽的空氣之溫度係例 如約601之高溫,惟該空氣為該下段之冷却器19所冷却而 被凝结,液化成為例如約20¾之常溫*通過冷却器18,19 之間的間隙之後,再以上段冷却器1 8冷却而凝结,液化成 為例如約之低溫而從排氣口 11排出。如此因&含被導弓 至排氣路10之冷却通路12的溶劑蒸汽的空氣係在冷却器18 ,19M階段冷却而被凝结,液化,因此可提高冷却效率, 可得到例如80%M上之良好的溶劑回收率,同時,因冷却 器18,19係隔著間隔地配設,因此風路阻力少,可使排氣 圓滑順暢地流通。 因來自冷凍機機組20之冷媒氣體係從連缅之冷媒管17 之上面向下方流通,因而通過上段之冷却器18之空氣之溫 度(例如6〇υ)與通過下段之冷却器19之空氣之溫度(洌如 J ^ \ I 、1T—f (請先閲讀背面之注意事項再填寫本頁) 本纸張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 9 3 9 7 2 9 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(1 _ 20C乃形成下段之冷却器19之溫度比上段冷却器18之溫度 高的溫度坡度,因此可將流通之冷媒有效率地且經濟地利 用在空氣之冷却。 在乾燥過程後實行防止衣服之發生锶紋,或是為了作 成為具有優異觸感之最後完工之衣服的冷却過程時,則停 止加熱器8對於蒸汽管7之蒸汽供應,以第1轉換擋板24關 閉排氣口 11而將循環路14開放,.並以第2轉換擋板25閉鎖 性氣路5。由此,經由冷却通路却12將被冷却成5¾之空氣 經循環路14送進乾燥室,將乾燥後之衣服急速冷却,能提 高冷却效率,縮短冷却過程所需時間,同時可防止衣服皴 紋之發生或可K作成具有優異手觸感之最後完工,之衣服 並且,在取出衣眼時,由於衣服之溫度成為接近常溫因此 可容易處理。 以下,說明經水洗之衣服的乾燥。 在水洗之乾燥時,Μ第1轉換擋板24使排氣口 11開放而 將循環路14閉鎖*並Μ第2轉換擋板25開放供氣路5,而Μ 第3轉換擋板26將冷却通路12之入口閉鎖,將旁通通路部 13之入口開放。 然後,將以水洗洗濯之衣眼投入於乾燥室1之乾燥筒 2内。 由於乾燥裝置之開始蓮轉,蒸汽即在加熱器8之蒸汽 管7循環,同時進風機15即被驅動,Μ供氣路5之加熱器8Λ 熱之空氣即被送進乾燥室1,而附著於旋轉之乾燥筒2內之 衣服的水分即被蒸發,氣化。 本纸張尺度適用中國國家標準(CNS ) Λ4規格(210X297公釐) 1〇 3 9 7 2 9 -------:--丄.—裝------訂-----< 線 (請先閱讀背面之注意事項再填寫本瓦) 五、發明説明(11) A7 B7 被氣化之水分係與空氣一起被吸進排氣路10,同時經 收而 回置 必丨裝 不燥 % 乾 所 之 〇 用 出洗 *EI /S 中為 氣作 大 K 向可 11也 口 此 氣因 Lhr , 從燥 而乾 3 I 1 可 部 即 路分 通水 通量 旁大 用 使 述 所 上 如 燥 乾 服 衣 之 洗 水 經 將 程 行 燥 乾 該 讀 繼 部 路 通 却 冷 之 ο 11 路 氣 khr 0 將 時 服 衣 之 濯 洗 劑 溶 洗 乾 M 煉 乾 冷 以 汽 蒸 劑 溶 之 化 氣 發 蒸 11 室 燥 乾 在 將 11 室 燥 乾 於 通 連 2 11 且 1 時 而室服 , 燥 衣 收乾之 回低濯 可減洗 而可洗 化,水 液氣以 , 排煉 结中乾 凝氣欲 被大 , 19向面 , 氣方 18空一 器之另 却汽 , 冷蒸度 之劑澹 12溶體 部離氣 路分劑 通經溶 却將之 回 必 不 而 1X 室 燥 乾 於 通 3 部 路 通 通 旁 之 ο 1X 路 氣 0 Be 因 中 氣 大 至 出 kl·/ 0 可 而 分 水 之 化 氣 發 蒸 被 11 室 燥 乾 在 收 乾 以型 燥氣 乾排 可氣 種大 一 且 供型 提用 , 兼 此之 溶 J---.-----i I 裝-- (請先閱讀背面之注意事項再填寫本頁)But the group, the machine section of the cold machine 18 is frozen and the cold is cold. The 12 is from the department of the system, the fluid is flowing through the air, but the medium is 19, and the cold is over 18, and the air is cooled by the air, and the medium is 18. The pressure reduction section of the cold contraction is cooled down and should be sent to the quilt CM for ο near the attached V ο, while the 2 cooling road is cold collected and returned to the ground agent. That is, the lower the agent, the lower the solubility of the liquid 19 is, the medium is cooled, and the medium 18 is cooled, so that the liquid is cold, and the steam is generated and condensed by the condensate. 19M1 This paper size applies Chinese national standards (CNS ) A4 specification (210X 297 mm) 8 3 9 7 2 9 Yinfan A7, Consumer Cooperative of the Central Bureau of Standards, Ministry of Economic Affairs __ ^ _ B7_ V. Description of the invention (9), from this solvent recovery path 22, introduce the solvent water separator 23 After being recycled. After the cooling passage portion 12, the air from which the solvent vapor is separated is discharged from the exhaust port 11 into the atmosphere. Following the drying process, the clothes are dried and the solvent is recovered. During the drying process, the air is finally discharged from the exhaust port 11 to the atmosphere, so that the concentration of the solvent gas in the drying chamber 1 can be maintained at a relatively low concentration. Furthermore, since the warm air system sent into the drying chamber 1 does not contain the outside air of the solvent gas at all, this outside air can improve the drying efficiency most. In addition, since the exhaust air system exhausted from the exhaust port 11 to the atmosphere during this drying process is cooled to a low temperature of, for example, about 5 ° C, there is little odor even when the exhaust air contains a container vapor slightly. . The temperature of the air containing the solvent vapor passing through the lower stage cooler 19 is, for example, a high temperature of about 601, but the air is condensed by being cooled by the lower stage cooler 19, and liquefied to a normal temperature of, for example, about 20¾ *. After the gap between them, the upper cooler 18 is cooled and condensed, and liquefied to a low temperature, for example, and discharged from the exhaust port 11. In this way, because the air containing the solvent vapor guided to the cooling passage 12 of the exhaust passage 10 is condensed and liquefied at the cooler 18 and 19M stages, the cooling efficiency can be improved, for example, 80% M can be obtained. It has a good solvent recovery rate. At the same time, the coolers 18 and 19 are arranged at intervals, so the air path resistance is small, and the exhaust gas can be smoothly and smoothly circulated. Since the refrigerant gas system from the freezer unit 20 circulates from above the refrigerant pipe 17 in Lian-Myan, the temperature of the air passing through the upper cooler 18 (for example, 60 °) and the temperature of the air passing through the lower cooler 19 Temperature (such as J ^ \ I, 1T-f (please read the precautions on the back before filling this page) This paper size is applicable to China National Standard (CNS) A4 (210X297 mm) 9 3 9 7 2 9 Economy Printed by A7 B7, Consumer Cooperatives of the Ministry of Standards of the People's Republic of China V. Invention Description (1 _20C is the temperature gradient of the cooler 19 forming the lower stage than the cooler 18 of the upper stage, so the circulating refrigerant can be efficiently and Economical use of air cooling. After the drying process is implemented to prevent the occurrence of strontium lines on the clothes, or to cool the finished clothes with excellent touch, the steam from the heater 8 to the steam pipe 7 is stopped. Supply, close the exhaust port 11 with the first conversion baffle 24 to open the circulation path 14, and close the gas path 5 with the second conversion baffle 25. As a result, the cooling path 12 is cooled to 5½ Air passage The loop 14 is sent to the drying room to rapidly cool the clothes after drying, which can improve the cooling efficiency and shorten the time required for the cooling process. At the same time, it can prevent the occurrence of clothing streaks or can be made into the final completion with excellent hand feel. The clothes can be easily handled when the clothes are taken out because the temperature of the clothes becomes close to normal temperature. The drying of the clothes washed with water will be described below. When the clothes are washed with water, the M first conversion baffle 24 opens the exhaust port 11 The circulation path 14 is closed * and the second conversion baffle 25 opens the gas supply path 5, and the third conversion baffle 26 closes the entrance of the cooling passage 12 and opens the entrance of the bypass passage 13. Then, The clothes and eyes washed with water are put into the drying cylinder 2 of the drying chamber 1. As the drying device starts to rotate, the steam is circulated in the steam pipe 7 of the heater 8, and the fan 15 is driven at the same time, and the gas supply path 5 The heater 8Λ hot air is sent into the drying chamber 1, and the moisture attached to the clothes inside the rotating drying drum 2 is evaporated and vaporized. This paper size applies the Chinese National Standard (CNS) Λ4 specification (210X297) Mm) 1〇3 9 7 2 9 -------:-丄 .-- install -------- order ----- < line (please read the notes on the back before filling in this tile) 5 、 Explanation of the invention (11) A7 B7 The vaporized moisture is sucked into the exhaust path 10 together with the air, and at the same time it must be returned after being collected. Qi Zuo Da K Xiang Ke 11 also breathe this breath due to Lhr, dry from dry 3 I 1 can be divided into two parts, the water flux is used by the side, so that the washing water as described in the clothes drying process will be dry Let ’s read the road, but it ’s cold ο 11 way air khr 0 Dissolve and wash the clothes of the time. M refining the cold and steaming with the steaming agent to dissolve the gas 11 rooms dry and dry the 11 rooms In Tonglian 2 11 and 1 hour, room service, drying clothes can be reduced and washed down, can be reduced and washed, water, liquid and gas, in the process of refining the dry condensate gas to be large, 19 to the surface, gas 18 air one device, but the other steam, cold steaming agent 澹 12 solution part away from the gas path through the solvent dissolve, but will return it to the 1X chamber dry on the side of the 3 road through 1X Qi 0 Be, because the medium gas is as large as kl · / 0, the water can be divided into two parts. The gas is steamed and dried in the 11 room. The dry type is used to dry and exhaust the gas. The type can be larger and available for use. Soluble J ---.----- i I Pack-(Please read the precautions on the back before filling this page)

、1T 開 型 方 雙 服 〇 衣置 之裝 灌烽 洗乾 經的 洗服 水衣 及之 劑丨 路 環 循 鎖 閉 中 程 過 燥 乾 在 路 氣 供 放 開 及 型 氣 氣 大 的 放 中 氣 大 向 ο 1X 路 氣 0 及 5 路 氣 供 將 成 構而 二線 經濟部中央標準局員工消費合作社印裂 之 Η 完 後 最 在5· 後路 程氣 過 供 燥鎖 乾閉室 服及燥 衣,乾 將14進 , 路 送 且環風 並循冷 , 放 之 率開12 效,部 燥中路 乾程通 髙過却 提却冷 可冷過 通 將 可 即 可 服 衣 却 冷 W 急 而 11 沿 個 兩 成 。 割 間分 tr 9 時 1 之 , 費18 所器 程却 過冷 却之 冷12 短部 縮路 可通 又却 ’ 冷 率將 效 ’ 却且 冷並 高 提 上 自 之來 2 <-1 因 部, 路且 通再 却, 冷媒 從冷 序通 順流 依19 時器 同却 ’ 冷 置的 配方 地下 離向 隔18 向器 方却 路冷 通的 著方 之 2 11 部 路 通, 却 冷 從 氣 bl· 0 之 1X 室 燥 乾 的 2 部 路 通 却 冷 通 流 本紙張尺度適用中國國家標準(CNS )厶私見格(210X 297公釐) 11 11 3 9 7 2 9 五、發明説明(1 2) A7 B7 上 2 11 部 路 通 却 冷 在 面 1 係 度 溫 氣 bui HW 此 因 通 流 方 上 向 方 下 器 却 冷 各 過 通 於 應 陲 却 冷 地 段 階 面 一 昇 溫 氣 Lhr 之 器配 却分 冷地 各動 成 自 形被 而力 度 能 換 交 熱 之 媒 冷 此 因 度 坡 度 溫 之 却 冷 行 進 地 率 效 有 且 濟 經 可 冷 § 排 5 器卩 的 i 却 機 i 冷 壓β體 環 及 — 氣 循 器纟媒 凍 結」 冷 令凝/之 之 有體近 具 ί 附 與 為 器 發 蒸 的 環 循 凍 冷 之 體 氣 媒 冷至 ,1用低 18使降 器成如 却構例 冷起度 因 一 溫 , 2 發 且組蒸 再機 Μ 機此 凍因 V ο 且 所 而置 。 裝 率燥 效乾 收依 回止 之防 劑可 溶此 高 因 提 ’ 可 外 ’ 屋 度 於 溫設 氣20 排組 低機 降機 分凍 充冷 可將 , 因 氣 , 時將 同 可 ’ 也 化 ’ 惡 且 之並 境 ’ 環能 業可 作為 的成 等轉 音 運 噪地 或率 昇效 上有 度之 溫20 之 組 内機 室機 的凍 置冷 設 ’ 所 埸 窄 狭 於 設 地 易 容 置 裝 燥 乾 之 內 屋 於 設 室 燥 乾 之 時 洗 乾 明 說 下Μ 加 被 將 〇 度 溫 制 控 之 J. ..---_---- -- (請先閲讀背面之注意事項再填寫本頁) 訂 1 劑 室溶 燥之 乾中 至 服 應衣 供久 風不 熱 ’ 之 熱 熱 加 被 劑 溶 之 服 衣 於 含 及 服 衣 時 走 tuaU 3 風 熱 被 化 氣 發 蒸 始 開 即 時室 化烽 氣乾 成之 完間 當期 。 該 氣示 排所 而圖 2 第 如 ο 態 狀 之 燥 乾 為 成 係 腋 衣 從 係 況 狀 之 度 濃 體 氣 劑 溶 的 银 經濟部中央標準局員工消費合作社印製 之 峰 尖 山 如 為 。 成零 後於 鐘近 分接 10半 至 幾 如時 例束 ’ 结 昇燥 上乾 地在 連而 急 少 燥減 乾始 始開 開後 □ 出 之 風 熱 的 出 bp 所□ 出 之 室 烽 乾 或 劑 溶 之 中 腋 衣 或 服 室衣 燥在 乾費 從耗 面為 方初 一 最 另係 度 溫之 側内 11 顛溫 1 之之室 燥服燥 乾衣乾 行著制 進隨抑 在又了 , 後 為 熱之 加 ’ 熱 潛 化 氣 之 。 劑昇 溶上 在時 費同 耗而 則昇 時上 況漸 狀逐 峯 度 下 發 爆 在 持 維 而 度 濃 體 氣 劑 溶 之 本纸張尺度適用中國國家標準(CNS ) Λ4規格(210X297公釐) 2 1Χ 3 9 7 2 9 經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) 3 9 7 2 9 A7 B7 五、發明説明(U) 限界K下,必須控’制供氣在乾燥室1内的熱風溫度,並抑 制溶劑氣體濃度之尖峰值。但是,如K注·推測出口側溫 度,並控制熱風溫度時,則如上所述,由於最初出口側溫 度輕低因而控制高熱風溫度,導致乾燥室1内之平均溫度 會上昇,故無法抑制溶劑氣體濃度。 於是,將例如30分鐘乾燥過程,分割成包括乾燥室1 之熔劑氣體濃度之峯值的前半之第1階段及後半之第2階段 ,前半之第1段階係在第1溫度檢出器27檢測供氣於乾燥室 1的熱風之入口側溫度,控制熱風溫度來抑制乾燥室1C內 之平均溫度而將溶劑氣體濃度維持爆發下限界限K下,在 減弱溶劑或氣化乾燥室1內之平均溫度容易反映在出口側 溫度的後半之第2階段,則以第2溫度檢測電路28被檢測, 來控制熱風溫度。 如此,在從開始乾燥或包括乾燥室1之溶劑氣體濃度 之尖峰的第1階段,藉由乾燥室1之入口側溫度來控制加熱 器18,19,從連纊於經過乾燥室1之溶劑氣體濃度之尖峰 的第1階段的第2階段由乾烽室1之出口側溫度來控制加熱 器18,19因此在第1階段可將乾燥室1內之溶劑氣體濃度確 實維持在預定濃度Μ下,而在第2階段可提高乾燥效率, 同時可防止衣服溫度之過高。 在上述實施形態係說明Κ上下方向配設冷却器18, 19者,惟並不被限定於此者,也可將3個Κ上之冷却器隔 著間隔上下方方向配量。 發明夕效果 13 J--'---^---1 -裝------訂-----1 練 (請先閱讀背面之注意事項再填寫本頁) A7 B7五、發明説明(l4) 依照申請專利範圖第1項所述之乾燥裝置,欲乾燥Μ 乾洗溶劑洗濯之衣服時*由在乾燥室連通排氣路之冷却通 經濟部中央標準局員工消費合作社印製 j ^--!ί1 I 裝------訂-----I 線 L-----------.------- (請先閱讀背面之注意事項再填寫本頁) 化汽一排化水等 j# 大程氣服 之同通通通溫 氣蒸另通水及服IfiM 至過供衣 J 部,流却却氣 發劑,連 之劑衣 I? 放燥及却 丨 路置地冷冷排 蒸溶度室化溶之 δ , 開乾路冷。 通配序從在之 申’ 青 室離濃燥氣洗型 了中被在環連間"却地順係面器 燥分體乾發乾氣 纟— 路-循急時申冷離之氣一却 除 程 了 乾將氣在蒸 Κ 排 氣又放俾之 於隔器排係冷 , 過 除 在時劑由被烽中 排,開室費 U 由向却之度各 置躁 置 將同溶經室乾氣 I纟及率經燥所 I ,方冷室溫過 來,之’燥可大 在路效介乾程 外路方烽.氣通 器收室時乾種且 氣燥,進過SJI果通下乾排著 却回燥服在一型 卜供乾中送却 Μ 效著至之,隨 冷以乾衣收供用 Μ 成高程風冷 之沿器部此因 之 予低之 回提兼 2 構提 過冷短 3 置並却 路因, 部並減濯必可之 第之,能却之縮第裝個冷通,却 路化以洗不此方 圍 ί 路,冷部並圍燥數方却通冷 置 通液中被,因雙 範 t 氣型之路率範乾複上 冷流地 却、氣洗部。等 利纟供氣等通效利之成之通方段 冷结大水路中服 專 放排服却却專項 割路流上階 由凝至 Μ 通氣衣。請 ,開中衣冷冷請 2 分通自向面 之 5® 藉汽氣燥通大之置申 及氣工過高申 被却來方 一 頃" 而蒸排 乾旁至 濯裝照 1 路大加通提照 3 係冷 又下昇 , 劑氣欲 之出洗 烽依第環的後將可除1«器從,之上 部溶空面路排被乾 圍循中最, , 第却依媒部部 路之 之力氣 而洗的 範鎖氣後路等 圍冷時冷路路 本紙張尺度適用中國國家標準(CNS )八4規格(210Χ297公釐) 3 9 72 9 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(l5) 度來形成各冷却器之溫度坡度,因此,自動地分配冷媒之 熱交換能力,經濟又有效率地被冷却。 依照申請專利範圍第4項之乾燥裝置,除了申請專利 範圍第1項至第3項中任何一項之乾燥裝置之效果外,由於 冷却器係與具有凝结器及壓縮機之冷凍機機組一起構成使 用冷媒氣體的冷凍循環的蒸發器,因此K蒸發溫度降低至 例如0C附近之冷媒體來冷却排氣,充分地降低排氣溫度 ,提高溶劑之回收效率,而且由於將冷凍機機組設於屋外 ,因此,可防止依設有乾燥裝置之室内之溫度上昇或噪音 等所引起的作業環境之惡化,同時可形成冷凍機機組之有 效率的運轉。 依照申請專利範圍第5項之乾燥方法,係使用申請專 利範圍第1項至第4項中任何一項所述之乾燥裝置的乾燥方 法,由於在包括從開始乾燥至乾烽室之溶劑氣體濃度之尖 峰的第1階段,藉由乾烽室之入口側溫度來控制加熱器, 在連壤於經過乾燥室之溶劑氣體濃度之尖峰的第1階段的 第2階段,藉由乾燥室之出口側溫度來控制加熱器|因此 ,在第1階段,將乾煉室内之溶劑氣體濃度確實地維持在 所定濃度Μ下,而在第2階級,可提高乾燥效率,同時可 防止衣腋等之溫度的過度上昇。 圃式夕簡罝說明 第1圖係表示本發明之一實施形態之乾烽裝置的構成 圖。 第2圖係表示隨著時間經過的乾燥室之溶劑氣體濃度 本紙張尺度適用中國國家標( CNS ) Λ4規格(210X297公釐) 〇 〇 7 〇 〇 —Γ ---1-----_ —裝------訂-----/ 線 (請先閱讀背面之注意事項再填寫本頁) A7 B7五、發明説明(16) ,入口側溫度及出口側溫度之闞係的說明圖。 明 說 之 號 記 室 燥 乾 2 筒 燥 乾 5 路 氣 供 8 器 熱 加、 1T open type square double service 〇The clothes are filled with the washing clothes and the washing agent and the agent 丨 road loop cyclic locking mid-range dry and dry in the road air supply release and large gas air release Qi Dao ο 1X road gas 0 and 5 road gas supply will be structured and the second-line Ministry of Economic Affairs Central Standards Bureau staff consumer cooperatives printed cracks after the completion of the most air after 5 · , Will be 14 into the road, the road and the wind and cold, the rate of opening the 12 effects, the Ministry of dry road pass through the pass but raised the cold can pass the cold can be ready for clothing but cold W emergency and 11 along 20%. The time between tr is 9: 1, it costs 18 times, but it is too cold. 12 The short part can be shortened, but the 'cooling rate will work,' but it is cold and high. 2 < -1 because Department, Road and pass again, Refrigerant flows from the cold sequence through the flow at 19 o'clock and the same time, the cold formula departs to the side of the 18-way Qi Fang Road, the author of the cold pass 2 11 Road, but the cold Gas bl · 0 in 1X room with 2 dry and cold-flowing channels. The paper size is in accordance with Chinese National Standards (CNS) (210X 297 mm). 11 11 3 9 7 2 9 V. Description of the invention (1 2) A7 B7 2 11 roads are cold on the surface 1 system of warm air bui HW This is because the flow side is up and down, but it is cold, and each of them is on the level surface of the cold but cold area. A gas heating Lhr device Equipped with cold grounds, each with its own strength and strength, which can be exchanged with hot medium. This is because the slope is gentle, but the cold travel rate is effective and can be cooled. β body ring and — air cycler media freezing There is a body with a cold circulation body air medium attached to the device for steaming. 1 uses a low 18 to make the lowering device as cold as possible. The cold start is due to one temperature, 2 rounds, and the group is steamed again. The machine is frozen due to V ο and is set. The loading rate is dry and the effect of drying is based on the back of the anti-soluble agent. This high factor can be 'outside'. The room is set at a temperature of 20 rows. It also reduces the "cold environment of the evil and the environment". The environmental energy industry can be used as a transponder to transport noise, or increase the efficiency of a room with a temperature of 20 degrees. The easy-to-fit interior house was dry and cleaned when the room was dry, and said that the M plus was controlled by 0 ° C ...------------- (Please read the back first Note: Please fill in this page again.) Order 1 Dissolve in the dry room until the clothing should be applied for a long time without being hot. Add heat to the clothing and dissolve the clothing. Qifa begins to evaporate immediately when the thoron is dry. The gas is shown in Figure 2. The peaks and peaks printed by the staff's cooperative of the Central Standards Bureau of the Ministry of Economic Affairs of the Bank of China are as follows. The dryness of the state of the system is as follows. After the completion of the zero, I will take 10 and a half to the same time as in the past. The knot will dry up and then dry and then dry and reduce the dryness before it starts to open. □ Out of the wind and heat out of the room □ Out of the room 烽Drying or dissolving in the armpit or room clothes. Drying costs from the consumption side to the side of the first day of the most different temperature. 11 The temperature 1 room drying clothes dry clothes dry make progress. After again, after the heat is added 'The heat latent gasification. When the agent is dissolved, it takes the same amount of time and expense, but it rises gradually when the situation rises. Under the peak-to-peak degree, the paper is exploded in the dimension and the concentration of the gas is dissolved. The paper size applies to the Chinese National Standard (CNS) Λ4 specification (210X297). 2 1 × 3 9 7 2 9 The paper size printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs applies to Chinese National Standards (CNS) A4 specifications (210X297 mm) 3 9 7 2 9 A7 B7 V. Description of the invention (U) Under the limit K, it is necessary to control the hot air temperature of the supply air in the drying chamber 1 and suppress the peak value of the concentration of the solvent gas. However, if the K-note is estimated at the outlet temperature and the hot air temperature is controlled, as described above, the high temperature of the hot air is controlled because the outlet temperature is initially low, which causes the average temperature in the drying chamber 1 to rise, so the solvent cannot be suppressed. Gas concentration. Therefore, for example, the 30-minute drying process is divided into the first half of the first half and the second half of the second half including the peak of the flux gas concentration of the drying chamber 1. The first half of the first half is detected by the first temperature detector 27. The temperature of the inlet side of the hot air that is in the drying chamber 1 is controlled, and the hot air temperature is controlled to suppress the average temperature in the drying chamber 1C and maintain the solvent gas concentration below the lower explosive limit K. It is easy to weaken the average temperature of the solvent or gasification drying chamber 1 The second stage, which is reflected in the second half of the outlet temperature, is detected by the second temperature detection circuit 28 to control the hot air temperature. Thus, in the first stage from the beginning of drying or including the peak of the solvent gas concentration of the drying chamber 1, the heaters 18, 19 are controlled by the temperature of the inlet side of the drying chamber 1, and the solvent gas passing through the drying chamber 1 is connected. In the second stage of the first stage of the concentration peak, the heaters 18 and 19 are controlled by the temperature on the outlet side of the drying chamber 1. Therefore, in the first stage, the concentration of the solvent gas in the drying chamber 1 can be maintained at a predetermined concentration M. In the second stage, the drying efficiency can be improved, and the temperature of the clothes can be prevented from being too high. In the above-mentioned embodiment, it is described that the coolers 18 and 19 are arranged in the vertical direction of K, but it is not limited to this, and the three coolers on K may be metered in the up-down direction with an interval. The effect of the invention 13 J --'--- ^ --- 1-equipment ------ order ----- 1 practice (please read the notes on the back before filling this page) A7 B7 V. Invention Note (l4) According to the drying device described in item 1 of the patent application diagram, if you want to dry your clothes washed with dry cleaning solvents * Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs through the cooling through the exhaust chamber in the drying room. ^-! ί1 I install ------ order ----- I line L -----------.------- (Please read the precautions on the back before (Fill in this page) One line of chemical steam, one row of water, and other j # long-distance gas service, all pass through warm air, steam, and pass water and service IfiM to the J section of the clothing, but the hair-generating agent is flowing, and even the drug coat I? Dry and cool 丨 The cold-discharged δ of the steam dissolution chamber dissolves, and the dry road is cold. The wild order from the "Zhenzhishen" Qingshili thick dry air wash type was in the ring room "quote but the facial smoother dry split dry hair dry air 纟 — Lu-Xunxian Shen cold away air Once removed, the gas will be exhausted in the steamer and exhausted into the separator row. The cold air will be removed from the bed when the agent is removed. The dry air through the chamber I and the rate I dry the room I, come over at room temperature, the 'dryness can be greater in the road effect medium outside the dry road side. The air vent is dry and air dry when closing the room, enter SJI Guotong is in the dry row, but is back to dry clothes. It is delivered in a type of cloth for drying, but it is effective. The cold clothes are used for drying and the clothes are supplied for use. The altitude is air-cooled along the device. 2 The structure is too cold and short 3 and the road is closed, the road is reduced and the first must be reduced, the power can be reduced to install the first cold pass, but the road is changed to wash this side, the road, the cold and closed Shufang was placed in the cold through the liquid, because of the double-fan t air mode, Fan Qian returned to the cold-flow, air-washing department. Waiting for the benefit of the gas supply and other benefits of the pass through the cold section of the large waterway in the middle of the service, dedicated to discharge the service, but the special cut off the flow of the upper stage from condensate to Μ ventilators. Please, open the coat, please coldly, please pass 2 minutes from the side of the 5®, use the steam to dry the air, and the air is too high, but it ’s one hectare, and the steam is drained to the side of the outfit. Dajiatong's photo 3 is cold and rises. After the breath is washed out, the first ring will be removed after the first ring. The upper part of the empty air surface is lined up in the middle. Fans Department of the Ministry of Media and the power to wash the roads and other roads in the cold and cold roads. The paper size applies to China National Standards (CNS) 8 4 specifications (210 × 297 mm) 3 9 72 9 Employees of the Central Standards Bureau of the Ministry of Economic Affairs The consumer cooperative prints A7 B7 V. Description of the invention (15) degrees to form the temperature gradient of each cooler. Therefore, the heat exchange capacity of the refrigerant is automatically distributed, and it is economically and efficiently cooled. The drying device according to item 4 of the patent application scope, in addition to the effect of the drying device of any one of the patent application scope items 1 to 3, because the cooler is constituted together with a refrigerator unit with a condenser and a compressor The evaporator using the refrigeration cycle of the refrigerant gas, so the K evaporation temperature is reduced to, for example, a cold medium near 0C to cool the exhaust gas, sufficiently reduce the exhaust gas temperature, improve the solvent recovery efficiency, and because the refrigerator unit is installed outside the house, Therefore, it is possible to prevent the deterioration of the working environment caused by the temperature rise or noise in the room provided with the drying device, and at the same time, the efficient operation of the refrigerator unit can be formed. The drying method in accordance with the scope of the patent application No. 5 is a drying method using the drying device described in any of the scope of the patent application Nos. 1 to 4, due to the concentration of the solvent gas in the drying chamber including the drying from the beginning. In the first stage of the peak, the heater is controlled by the temperature on the inlet side of the drying chamber. In the second stage of the first stage adjacent to the peak of the concentration of the solvent gas passing through the drying chamber, the second stage is controlled by the outlet side of the drying chamber. The heater is controlled by the temperature | Therefore, in the first stage, the concentration of the solvent gas in the drying chamber is reliably maintained at a predetermined concentration M, and in the second stage, the drying efficiency can be improved, and the temperature of the armpits and the like can be prevented. Excessive rise. Brief description of the garden style Fig. 1 is a diagram showing the configuration of a drying apparatus according to an embodiment of the present invention. Figure 2 shows the solvent gas concentration of the drying chamber over time. The paper size is applicable to the Chinese National Standard (CNS) Λ4 specification (210X297 mm). 〇07 〇〇—Γ --- 1 -----_ —Installation ------ Order ----- / (Please read the precautions on the back before filling this page) A7 B7 V. Description of the invention (16), the relationship between the inlet temperature and the outlet temperature Illustrating. Ming Shuo No. Recording Room Drying 2 cylinders Drying 5 channels Gas supply 8 Heater

0 1 2 3 4 5 IX 11 1X 11 1X 路口 氣氣 tl· 部 路 通 却 冷 部 路 通 通 旁 路機 環風 循送 器 却 冷 9 1i 組 機 ajv 冷 路 收 回 劑 溶 板 擋 換 轉 1 第 的 構 構 換 換 轉 環 循 氣 UF 0 為 作 板 擋 換 轉 2 第 的 構 機 閉 開 路 氣 供 為 作 (讳先閱讀背面之注意事項再填寫本頁) 裝· 經濟部中央標準局員工消費合作社印製 板 擋 換 轉 3 第 的 構 機 換 轉 通 旁 却 冷 為 作 本紙張尺度適用中國國家標準(CNS ) Λ4規格(210X 297公釐) 16 3 9 72 90 1 2 3 4 5 IX 11 1X 11 1X Crossing air tl · Bu Lutong but cold Bulu Tongtong bypass machine ring air circulation device is cold 9 1i group machine ajv cold circuit retractor dissolving plate gear shift 1 UF 0 is used as a board stop and 2 is used for closing the circuit of the machine. (Please read the precautions on the back before filling out this page.) Printed board stop change 3 The first machine switch is bypassed, and the paper size is used as the paper size. Applicable to China National Standard (CNS) Λ4 specification (210X 297 mm) 16 3 9 72 9

Claims (1)

A8 B8 C8 D8 經漓部中央標準局員工消費合作社印製 六、申請專利範圍 1 1 . 一 種 乾 燥 裝 置 其 特 徵 為 具 備 : 1 配 設 乾 煉 鼓 輪 的 乾 燥 室 及 1 具 有 連 通 於 該 乾 燥 室 之 加 熱 器 的 供 氣 路 及 1 I 連 通 於 上 述 乾 燥 室 > 具 有 冷 却 器 之 冷 卻 通 路 部 與 並 排 請 先 閲 1 I 設 有 旁 通 該 冷 却 通 路 部 之 旁 通 通 路 部 同 時 設 有 向 下 讀 背 vfj 1 I 游 側 大 氣 開 放 之 排 氣 P 的 排 氣 路 及 冬 旁 1 連 接 於 上 述 冷 却 通 路 部 的 溶 劑 回 收 路 及 華 項 1 通 過 上 述 乾 燥 室 從 供 氣 路 送 風 至 排 氣 路 的 送 風 機 及 寫 太 i 轉 換 上 述 乾 燥 室 與 上 述 冷 却 通 路 及 旁 通 通 路 部 之 任 何 頁 ___· 1 1 一 方 連 通 的 冷 却 旁 通 轉 換 機 構 〇 1 1 2 .如 申 請 專 利 範 圍 第 1項所述之乾燥裝置 其中 具備; 1 1 連 通 排 氣 路 之 下 游 側 與 乾 燥 室 的 循 環 路 及 訂 I 開 放 排 氣 路 之 排 氣 D 側 與 循 環 路 側 之 任 何 一 方 1 I 並 轉 換 成 閉 鎖 另 一 方 的 排 氣 循 環 轉 換 機 構 及 1 1 1 在 上 述 排 氣 口 之 開 放 時 開 放 供 氣 路 同 時 在 上 述 循 1 環 路 之 開 放 時 閉 鎖 的 供 氣 路 開 閉 機 構 0 .-Λ 1 3 .如 串 請 專 範 圍 第 1項或第2項 之 乾 燥 裝 置 其 中 冷 却 1 通 路 部 之 冷 卻 器 被 分 割 成 複 數 個 並 沿 著 通 路 方 向 隔 i 1 離 地 配 置 同 時 依 從 冷 却 通 路 部 之 上 方 冷 却 器 至 下 方 1 1 冷 却 器 之 順 序 地 流 通 冷 媒 ί 1 I 來 白 流 通 過 乾 燥 室 之 冷 却 通 路 部 之 排 氣 係 從 冷 1 却 通 路 部 之 下 方 向 上 方 流 通 者 〇 1 1 4 .如 串 請 專 利 範 圍 第 1項至第3項 中 任 何 一 項 之 乾 燥 裝 置 1 1 9 其 中 該 冷 却 器 係 與 具 有 凝 结 器 及 壓 縮 機 之 冷 凍 機 機 1 1 本紙張尺度適用中國國家標隼(CNS ) Λ4規格(2丨0X297公釐) j 7 3 9 7 2 9 A8 B8 C8 D8 六、申請專利範圍 組一起構成使用冷媒氣體的冷凍循環的蒸發器;而 任 中 項 4 第 至 1 為 項 S 1 徵 第特 圍其 C 範 , 者利法 外專方 屋請燥 於申乾 設用的 係使置 組係裝 機法燥 機方乾 凍燥之 冷 I項 • Hint- 種 一 一 何 5 包 在第 的 峰 尖 之 度 濃 體 氣 劑 溶 之 室 燥 乾 至 燥 乾 始 屏 從 括 器 熱 加 制 控 來 度 溫 側□ 人 之 室 燥 乾 由 藉 設 階 而 第加 的制 峰控 尖來 之度 度溫 濃側 體口 氣出 劑之 溶室 之燥 室乾 烽由 乾則 過 , 經级 於階 壤2 里第 連的 在 段 階 者 器 熱 (讀先閱讀背面之注意事項再填寫本頁) .裝- 訂 經濟部中央標準局員工消費合作社印製 本紙張&度適用中國國家標準(CNS ) Α4規格(2lOX297公釐) 8 1Χ 3 9 7 2 9A8 B8 C8 D8 Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Liability 6. The scope of patent application 1 1. A drying device is characterized by: 1 a drying chamber equipped with a dry drum and 1 with a drying chamber connected to the drying chamber The air supply path of the heater and 1 I communicate with the above-mentioned drying chamber.> The cooling passage section with a cooler is side by side. Please read 1 I. The bypass passage section that bypasses the cooling passage section is also provided with a downward reading back. vfj 1 I Exhaust path and exhaust side of exhaust P that is open to the atmosphere on the side of the stream 1 Solvent recovery path and Huaxiang 1 connected to the cooling path section 1 The blower that sends air from the supply path to the exhaust path through the drying chamber and writes Tai i converts the cooling chamber and any of the pages of the cooling passage and the bypass passage ___ · 1 1 The cooling bypass conversion mechanism connected to one side 〇 1 1 2. The drying device described in the first item of the patent scope includes: 1 1 a circulation path connecting the downstream side of the exhaust path and the drying chamber, and any one of the exhaust D side and the circulation path side of the open exhaust path 1 I and switched The other side of the exhaust cycle switching mechanism and 1 1 1 are closed when the above-mentioned exhaust port is opened, and at the same time when the above-mentioned 1 loop circuit is opened, the opening-and-closing mechanism of the gas supply path is closed. For example, please refer to the drying device of the first or second range of the range. The cooler of the cooling channel 1 is divided into a plurality of pieces and arranged along the direction of the channel at intervals i 1 while following the cooler above the cooling channel to the bottom. 1 1 Cooler sequentially circulates refrigerant ί 1 I Exhaust system for white flow passing through the cooling passage part of the drying chamber from the bottom of the cooling passage part to the upper part 0 1 1 4. If you ask for a drying device in any of items 1 to 3 of the patent scope 1 1 9 where the cooler is a refrigerator with a condenser and a compressor 1 1 This paper size applies to Chinese national standards 隼(CNS) Λ4 specification (2 丨 0X297 mm) j 7 3 9 7 2 9 A8 B8 C8 D8 6. The scope of the patent application group together constitutes the evaporator using the refrigeration cycle of the refrigerant gas; The item S 1 is specifically designed to cover its C model. For those special-purpose houses outside the law, please dry it in the application system, install it, install it, install it, install it, install it, install it, install it, install it, dry it, and freeze it. 5 Enclosed in the top of the peak, the room where the thick body aerosol is dissolved is dried to dry. The initial temperature is controlled from the heat of the bracket to control the temperature side. The degree of control of the temperature and concentration of the side body breath out of the solution chamber of the drying chamber dry up by dry, pass through the ranks of the second step of the second stage of the stage of the device (read the precautions on the back before reading (Fill in this page) -Ordered by the Consumers' Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs This paper & degree applies to China National Standard (CNS) Α4 specification (2lOX297 mm) 8 1X 3 9 7 2 9
TW87106295A 1998-04-24 1998-04-24 Drying device and method for drying TW379270B (en)

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