•第87108116號專利申請案中文專利說明書修正頁 ^ · 88年11月24曰修訂 經濟部中央標糸局負工消资合作社印製 五、發明説明（ 生加熱器30加熱後，第一段的再生風扇29將其導入第一段 的乾式除濕裝置5之再生區域5b內，作爲第一段乾式除濕裝 置5的轉子之再生所用。之後，以排氣EA排出系統外部。 另一方面，沒有通過第一段的再生加熱器30而剩餘的再生 系統ZC的空氣，經由再生剩餘空氣循環進氣管道31被送至 前面已出現的冷卻再生剩餘空氣用的冷卻器3，在此冷卻 後，和導入外面空氣OA混合並被導入至第一段的乾式除濕 裝置5之除濕區域5a內進行除濕。即是作爲處理空氣之一部 份再被使用。又，在圖1上的D1-D8是爲了調節風量而安裝 於進氣管道間的氣門。 以上所述構成使用有關第1實施型態之乾式除濕裝置 10的二段式乾式除濕系統，如上所述，在第一段的乾式除 濕裝置5之除濕區域5a上所被除濕之空氣，經由預冷器8來 冷卻後再由第二段的乾式除濕裝置1 〇之除濕區域11 a再除 濕，之後由加熱器2卜後冷卻器22來調節溫度後送至低露 點空間R內。此外，從低露點空間尺出來的回流空氣RA2被 導入至乾式除濕裝置1〇的轉子Η之淸洗區域11c內，另一方 面，由再生加熱器28所加熱的空氣則被導入轉子11之再生 區域lib內。 此時，位於轉子11兩側的除濕區域llafD再生區域lib 的比例爲9:2，因此通過再生齒域1化之#生空氣的通過風 量爲被除濕處理空氣的2Ζ2，亦即0.22倍，但根據發明者所 調查，如圖4之圖表所示，如此的再生空氣的通過風k即使 爲被除濕處理空氣的0.22倍，也能夠供應低露點空間R內所 14 n J-H- II --- . ! ·--- I . n (請先閱讀背面之注意事項再填寫本頁) 訂 國國家摞卒（（:NS ) Μ規格（2丨0X297公釐 經濟部中央標準局：s：工消费合作社印裝 A 7 ___ B7 _____________：_ 五、發明説明（） 發明之詳細說明 技術領域 本發明係有關於乾式除濕裝置的運轉方法、位於轉子 端面之空氣通過區域面積比例具有特徵的乾式除濕裝置、 具有脫臭功能的乾式除濕裝置、及具備此等乾式除濕裝置 之乾式除濕系統。 習知技術 一般用來減少空氣濕度的方法有冷卻除濕方法’但是 冷卻除濕只能用於露點在-5°C以上的空氣，無法適用低露 點（-50°C以下）。因此對於提供這樣低露點空氣之空調機， 則使用具有旋轉式轉子的乾式除濕機。乾式除濕裝置是由 具備有由吸入有氯化鋰和氯化鈣等吸收液的蜂巢狀轉子和 矽凝膠、沸石等吸附材料所構成的轉子，且將位於該轉子 端面的空氣通過區域分隔成除濕區域和再生區域，一邊讓 轉子旋轉，一邊讓處理的空氣通過除濕區域來製造出乾燥 空氣，同時，藉由讓高溫的再生空氣通過再生區域來令上 述吸收液及吸附材料中的3c分在再生空氣中蒸發，以連續 地進行除濕處理。 此時，轉子若在高溫狀態下移至除濕區域，則由於處 理的空氣在不除濕的狀態下通過轉子以使露點上昇，因此 可在再生區域與除濕區域之間設定一淸洗區域，用以冷卻 由低濕度所控制之空間而來的回流空氣等，使低溫空氣通 過而冷卻轉子。尤其是將乾式除濕裝置連接成二段串聯的 系統，藉此，經第一段乾式除濕裝置除濕過的空氣可再經 2 (請先閲讀背面之注意事項再填寫本F' } ----.• Revised page of Chinese Patent Specification No. 87108116 Patent Application ^ · Revised November 24, 88, printed by the Central Bureau of Standards, Ministry of Economic Affairs, Consumers and Consumers Cooperatives The regeneration fan 29 guides it into the regeneration area 5b of the first-stage dry dehumidifier 5 for regeneration of the rotor of the first-stage dry dehumidifier 5. After that, it is exhausted to the outside by the exhaust EA. On the other hand, it does not pass The air of the regeneration system ZC remaining in the first stage of the regeneration heater 30 is sent to the cooler 3 for cooling and regenerating the surplus air that has appeared before through the regeneration surplus air circulation intake duct 31, and after cooling, it is introduced The outside air OA is mixed and introduced into the dehumidification area 5a of the dry dehumidifier 5 of the first stage for dehumidification. That is, it is used as part of the treated air. Moreover, D1-D8 in Figure 1 are for adjustment. The air volume is installed between the air intake ducts. The above-mentioned configuration is a two-stage dry dehumidification system using the dry dehumidifier 10 according to the first embodiment. As described above, in the first stage, The dehumidified air in the dehumidification area 5a of the type dehumidification device 5 is cooled by the precooler 8 and then dehumidified by the dehumidification area 11a of the second-stage dry dehumidification device 10, and then cooled by the heater 2 The device 22 adjusts the temperature and sends it to the low-dew-point space R. In addition, the return air RA2 from the low-dew-point space ruler is introduced into the washing area 11c of the rotor of the dry dehumidifier 10, and on the other hand, it is regenerated by regeneration The air heated by the heater 28 is introduced into the regeneration area lib of the rotor 11. At this time, the ratio of the dehumidification area llafD regeneration area lib located on both sides of the rotor 11 is 9: 2, so through the regeneration tooth domain 1 化 之 # 生The passing air volume of air is 2Z2, which is 0.22 times of the dehumidified air, but according to the investigation by the inventor, as shown in the graph of FIG. 4, the passing air k of such regenerating air is 0.22 times that of the dehumidified air. 14 n JH- II in low-dew-point space R can also be supplied ---.! --- I. N (Please read the notes on the back before filling this page) Country of the country ((: NS) Μ Specification (2 丨 0X297mm Central Bureau of Standards, Ministry of Economic Affairs : S: printed by industrial and consumer cooperatives A 7 ___ B7 _____________: _ 5. Description of the invention () Detailed description of the invention Technical Field The present invention relates to a method for operating a dry dehumidifier, and the area ratio of the air passing area on the rotor end face has characteristics Dry dehumidifiers, dry dehumidifiers with deodorizing functions, and dry dehumidifier systems with such dry dehumidifiers. Conventional techniques are commonly used to reduce the humidity of the air, including cooling and dehumidifying methods, but cooling and dehumidification can only be used for dew points. At temperatures above -5 ° C, low dew points (below -50 ° C) cannot be applied. Therefore, for an air conditioner that provides such a low dew point air, a dry type dehumidifier having a rotary rotor is used. A dry dehumidifier is a rotor that is composed of a honeycomb rotor that absorbs absorbent liquids such as lithium chloride and calcium chloride, and absorbent materials such as silica gel and zeolite. In the dehumidification area and the regeneration area, while the rotor is rotated, the processed air is passed through the dehumidification area to produce dry air. At the same time, 3c of the absorption liquid and the adsorption material are divided by passing high-temperature regeneration air through the regeneration area. The regeneration air is evaporated to continuously perform a dehumidification process. At this time, if the rotor moves to the dehumidification area at a high temperature, the treated air passes through the rotor without dehumidification to raise the dew point. Therefore, a scrubbing area can be set between the regeneration area and the dehumidification area. Cool the return air from the space controlled by low humidity, etc., and let low-temperature air pass through to cool the rotor. In particular, the dry dehumidifier is connected into a two-stage series system, whereby the air dehumidified by the first dry dehumidifier can pass through 2 (Please read the precautions on the back before filling in this F '} ---- .
、1T ---. 本纸浪尺度適用中闽闽家棉单（) ,Vi规格（2!0：/公筇） 經濟部中央標準局員工消費合作社印裝 A7 B7 五、發明説明（） 由第二段乾式除濕裝置加以除濕。其中，在第二段的乾式 除濕裝置的轉子端面上一般設置有如上述的淸洗區域。 上述習知的乾式除濕裝置所使用的轉子可以圖1〇、圖 11來表示，在乾式除濕裝置200上的轉子201的兩側配置有 小室202、203。該轉子201的端面依圖11中箭頭所示，轉子 201的旋轉方向爲放射狀地被劃分成除濕區域201a、再生區 域201b、淸洗區域201c，3個空氣通過區域。此外在小室202 的外側端面上爲對應此等各區域，形成連接進氣管道等的 除濕入口202a、再生出口202b、淸洗出口202c。又，在小 室203的外部端面也因對應上述3個區域分別形成除濕出 口、再生入口、淸洗入口（均未示於圖中）。 上述轉子201的3個通過區域之除濕區域201a、再生區 域201b、淸洗區域201c的劃分比例，若以放射狀地被劃分· 形成時的中心角0來表示的話，設定除濕區域201a中心角 0爲225° ’再生區域201b中心角爲90。，淸洗區域201c 中心角Θ爲45。。此外各區域的空氣通過風量比和此等通 過區域的面積成比例，再生區域201b爲除濕區域201a的0.4 倍，淸洗區域201c爲除濕區域20la的0.2倍。這樣的劃分比 例、風量比例並非依特別的根據來規定，而是依照經驗來 設定。 — 此外例如鋰2次電池、鈉•硫磺電池、聚合物電池等作 爲電解液來使用碳酸酯和碳酸丙烯等多數的碳酸酯系的有 機溶劑。在此等有機溶劑裡，沸點較低者即使在常溫下也 能擴散至大氣中釋放出臭氣。 3 1— I -1 ---11----- m —^ϋ ί ml !^-^-, tm *n (讀先間讀背面之注意事項再填寫本頁) Γ *τ -- I m>l .n·^— —mV Kan· ft 本紙张尺度適⑴中國阀家標準（CNS ) Λ·4規格（210>· 297公趨、 A7 B7 五、發明説明（） 甚至在鋰2次電池等的製造程序，其材料的鋰金屬等遇 到水分便形成氧化作用。從相對於原料的產能來看應該被 排除，因此使用將處理空氣當作低露點（露點温度-32°C以 下）之乾式除濕裝置，在濕氣少的低露點空間等的環境下 進行鋰2次電池等的製造。在其內作業者作業時的作業空間 爲常溫’電解液產生臭氣’在低露點空間的作業空間內擴 散此臭氣。關於此點，例如以有關作爲放於轉子內之吸濕 材料的上述氯化鋰爲例，令活性炭吸入氯化鋰來除去如上 所述之臭氣。 發明所欲解決之問顆 相較於一般的冷卻除濕，具備上述習知構造之乾式除 濕裝置200雖擁有優越的除濕能力，但其缺點爲能源消耗 多。此種乾式除濕裝置，例如在鋰離子電池的製造工場雖 採用低露點空間，但眾所皆知者，此種製造工場之特徵爲 24小時無休，因此被強烈地要求降低能源。 經濟部中央標準局員工消費合作社印製 (請先閱讀背面之注意事項再填寫本頁) 此外，關於除臭，若使用活性炭吸入氯化鋰之轉子， 則可除去臭氣，但氯化鋰和電解液等臭氣成份發生反應， 會產生氯化觀的墓隨者時間而減少、且除濕機的功能變 差、低露點空間內的水分量上升等問題。甚至爲防止除濕 機功能的降低而定期地來更換轉子，此舉雖可維持除濕功 能，但所需營運成本亦增加。 有鑑於習知技術的問題點，本發明藉由減少：轉子再 生所需要的熱量、通過再生區域風量、通過淸洗區域風量， 其結果爲增大在除濕區域的處理量，即使相同大小的轉子 4 本紙張尺度適川中國固家標準、（，冗）八4現格（210/297公漦） 經濟部中央標隼局員工消费合作社印製 A7 ___B7_ , 五、發明説明（） 也能除濕比習知者更多的風量，提供乾式除濕裝置的運轉 方式及乾式除濕裝置。其能回應上述省能源的需求，甚至 本發明在除濕的同時能除去從臭氣物質處所產生的臭氣， 不用更換轉子.，也以提供乾式除濕裝置及具備此等的乾式 除濕裝置之除濕系統爲目的。 發明槪要 爲達到上述目的，專利請求範圍第1項提供乾式除濕裝 置的運轉方法，此裝置使處理空氣通過自由旋轉的轉子而 使該處理空氣除濕，位於轉子的端面側之空氣通過區域分 爲除濕區域、再生區域和淸洗區域，二段式乾式除濕系統 上配置有上述各區域，藉由轉子的旋轉，淸洗區域被設置 於從再生區域移至除濕區域之再生區域之前的位置上，將 再生區域對上述除濕區域之通過風量比定爲Z、除濕區域定 爲1時，設定0.2€Z<0.4來運轉。 根據發明者所述，即使設定再生區域的風量爲除濕區 域的0.2倍〜0.4倍以下（理想爲0.2〜0.25倍），仍會發現除濕 能力完全沒有改變。設定再生風量爲0.2倍〜0.4倍來運轉是 意味著降低再生風量至較習知者爲低，此外還可同時增加 除濕處理風量至較習知者爲高。換言之，進行與習知者等 量的除濕處理時，只需要較小型的系統即足夠，減少再生、 淸洗所需要的能源、並減少風扇、連接多段除濕裝置時在 第一段的除濕處理時所需的能源，全體而言可獲得較大的 節省能源效果。 此外，根據申請專利範圍第2項所提供之除濕裝置的運 5 本紙張尺度適州中國固家標準（（:\$)六4坭格（2丨〇/ 297公漦） 1LI —----ό衣 (請先閱讀背面之注意事項再填寫本頁) 、1Τ 經濟部中央標隼局員工消費合作社印製 A 7 B7 五、發明説明（） 轉方法，該裝置使處理空氣通過自由旋轉的轉子而使該空 氣除濕，其中位於轉子端面之空氣通過區域分爲除濕區 域、再生區域和淸洗區域，藉由轉子的旋轉，淸洗區域被 設置於從再生區域移至除濕區域之再生區域之前的位置 上，使再生區域上靠近淸洗區域的出口溫度接近既定値， 以控制再生風量。 此時，控制風量如申請專利範圍第3項，反相器控制爲 送風至再生區域的送風機，如申請專利範圍第4項，以調整 連接於再生區域之再生系統上裝設的氣門之開度。 在此，再生區域上靠近淸洗區域的出口溫度接近既定 溫度，即目標溫度爲當除濕區域的通過風量爲1時，再生空 氣的通過風量爲0.2倍〜0·4倍以下（理想爲0.2倍〜0.25倍）的 溫度。因此，事先算出此溫度，再以接近此温度來控制再 生風量的話，同於申請專利範圍第1項者，能將再生風量降 至低於習知者，減少再生、淸洗所需的能源、風扇、在第 一段除濕裝置上的處理所需之能源。而且由於是以溫度來 控制，因此沒有必要依序來求取風量比例，較易控制。 此外，申請專利範圍第5項提供乾式除濕裝置的運轉方 法，該裝置使處理空氣通過自由旋轉的轉子而使該空氣除 濕，位於轉子的端面之空氣通過區域被分爲除濕區域、再 生區域和淸洗區域，藉由該轉子的旋轉，淸洗區域被設置 於從再生區域移至除濕區域之再生區域之前的位置上，將 再生區域對上述除濕區域之通過風量比定爲Ζ、除濕區域定 爲1時，設定0.1 €Ζ<0.2來運轉。· 6 本紙張尺度適用令國國家標準（CNS ) Λ4規格（21()>^7公帮) ~ (請先閱讀背面之注意事項再填寫本頁) -.1© —— 訂—"-- ΑΊ Β7 __ ____ 1 五、發明説明（） 此爲對習知的除濕風量爲1、再生風量爲0.4時，將淸 洗風量定爲0.2，伴隨再生風量的降低而實施淸洗風量之減 少。換言之，淸洗是爲了冷卻由於再生而被加熱之轉子， 因此一旦再生風量減少的話，亦會使淸洗風量降低。由於 淸洗風量只使用於轉子的冷卻，因此少於再生風量即足 夠。而再生是在轉子的加熱與水分的蒸發兩方面均使用 熱，所以在風量比例上，淸洗風量爲再生風量的1/2即已足 夠。因此隨著再生風量的減低，淸洗風量亦可減低。其結 果爲能提高節省能源的效果至習知者以上。 此外，申請專利範圍第6項提供乾式除濕裝置的運轉方 法，該裝置使處理空氣通過自由旋轉的轉子而使該空氣除 濕，位於轉子的端面之空氣通過區域被分爲除濕區域、再 生區域和淸洗區域，藉由該轉子的旋轉’淸洗區域被設置 於從再生區域移至除濕區域之再生區域之前的位置上’使 淸洗區域上靠近除濕區域的出口溫度接近既定値以控制淸 洗風量。上述運轉方法的既定溫度是指當除濕區域的通過 風量爲1時，淸洗空氣的通過風量爲0.1倍〜0.2倍不到（理想 爲0.1倍〜0.15倍）時的溫度。因此，此種情況亦是事先算出 此溫度，再以接近此溫度來控制淸洗風量的話，便能降低 必要的能源。而且由於以溫度來控制’故不需依序來求取 風量比例，變得較易控制。 關於控制淸洗風量，如申請專利範圍第7項所載者，反 相器控制爲送風至淸洗區域的送風機；或如申請專利範圍 第8項所載者，調整連接於淸洗區域之淸洗系統所裝設的氣 7 本紙張尺度適川中國囤家檑準（（—NS ) Λ4現格（210 < 297公f ) -- (請先閲讀背面之注意事項再填寫本頁) TJ - -、-°I— n few---- 經濟部中央標準局員工消費合作社印製 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明（） 門之開度。 申請專利範圍第9項提供一種乾式除濕裝置，使處理空 氣通過自由旋轉的轉子而將該空氣除濕’位於上述轉子的 端面之空氣通過區域被分爲除濕區域、再生區域和淸洗區 域，藉由該轉子的旋轉，淸洗區域被設置於從再生區域移 至除濕區域之再生區域之前的位置上’位於上述轉子端面 之除濕區域和其他區域面積（再生區域+淸洗區域）的比 例爲3:1 〇 由方令改變上述除濕區域和其他區域（再生區域+淸洗 區域）的面積比，所以可進行較習知之同一種類的乾式除 濕裝置更多的除濕處理。因此當欲對於與習知者相同量的 空氣進行除濕，僅需要較小型的系統即可，能節省再生、 淸洗所需的能源’而且風扇的額定、第一段除濕裝置等也 比習知來的小即可，因此全體而言能獲得較大的節省能源 效果。 有關於再生區域和淸冼區域的面積比例，可採用如申 請專利範圍第10項的2:1;或採用如申請專利範圍第u項的 1:1，其適用於較低速旋轉上的使用。 再者，關於麵麵上臓腦轉子吸濕材 料，如帽專利=，13項，駐祕若爲編夕酸 鹽’則不纖去:^勺欢東好，而且金屬矽麵麵酿 氣物讎獅’ _不喷_試關麵嶋子。刪 金屬雜鹽的情況二例如在鋰2次電池等的製造過程上使用 成爲電解液的碳酸-甲酷和碳酸甲•乙酯等的碳酸酯系，能 本、紙張尺度適中國®家惊準（CNS ) Λ4現格（ (請先聞讀背面之注意事項再填寫本頁)、 1T ---. The scale of this paper is suitable for the cotton sheets of China, Fujian, and Fujian (), Vi specifications (2! 0: / public money), printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs, printed A7 B7 5. Description of the invention () by The second stage of the dry dehumidification device dehumidifies. Among them, the end face of the rotor of the dry dehumidifier of the second stage is generally provided with a rinsing area as described above. The rotors used in the above-mentioned conventional dry dehumidifier can be shown in FIGS. 10 and 11. The chambers 202 and 203 are arranged on both sides of the rotor 201 in the dry dehumidifier 200. The end surface of the rotor 201 is indicated by arrows in FIG. 11, and the rotation direction of the rotor 201 is radially divided into a dehumidification area 201a, a regeneration area 201b, and a washing area 201c, and three air passage areas. Dehumidification inlets 202a, regeneration outlets 202b, and rinsing outlets 202c are formed on the outer end surface of the chamber 202 so as to correspond to these areas. In addition, a dehumidification outlet, a regeneration inlet, and a rinsing inlet are formed on the outer end surface of the cell 203 corresponding to the three areas (not shown in the figure). The division ratio of the dehumidification area 201a, the regeneration area 201b, and the washing area 201c of the three passing areas of the rotor 201 is represented by the central angle 0 when they are divided and formed radially, and the central angle 0 of the dehumidification area 201a is set. The center angle of the reproduction region 201b is 225 ° and is 90. The central angle Θ of the washing region 201c is 45. . In addition, the ratio of the passing air volume of each area is proportional to the area of these passing areas. The regeneration area 201b is 0.4 times the dehumidification area 201a, and the scrubbing area 201c is 0.2 times the dehumidification area 20la. Such division ratios and air volume ratios are not specified according to special grounds, but are set based on experience. — In addition, for example, lithium secondary batteries, sodium-sulfur batteries, and polymer batteries are used as electrolytes, and most carbonate-based organic solvents such as carbonates and propylene carbonates are used. Among these organic solvents, those with a lower boiling point can diffuse into the atmosphere and release odors even at ordinary temperatures. 3 1— I -1 --- 11 ----- m — ^ ϋ ί ml! ^-^-, Tm * n (Read the precautions on the back before filling this page) Γ * τ-I m > l .n · ^ — —mV Kan · ft This paper is suitable for Chinese valve standard (CNS) Λ · 4 specification (210 > · 297 public trend, A7 B7 V. Description of invention () Even in lithium 2 times In the manufacturing process of batteries, the lithium metal, etc., is oxidized when it encounters moisture. It should be excluded from the viewpoint of the production capacity of the raw materials. Therefore, the process air is used as the low dew point (dew point temperature -32 ° C or less). The dry dehumidifier is used to manufacture lithium secondary batteries in an environment such as a low dew point space with little moisture. The working space for the operator during work is normal temperature 'the electrolyte produces odors' in a low dew point space. This odor is diffused in the work space. In this regard, for example, the above-mentioned lithium chloride as a hygroscopic material placed in the rotor is taken as an example, and activated carbon is sucked into the lithium chloride to remove the odor as described above. Compared to general cooling and dehumidification, the dry-type dehumidifier 200 having the above-mentioned conventional structure has It has superior dehumidification capability, but its disadvantage is that it consumes a lot of energy. This type of dry dehumidification device, for example, uses low dew point space in the lithium ion battery manufacturing plant, but it is well known that this manufacturing plant is characterized by 24 hours It's open all the time, so it is strongly demanded to reduce energy. Printed by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs (please read the precautions on the back before filling this page). In addition, for deodorization, if activated carbon is used to suck the lithium chloride rotor, then The odor can be removed, but the reaction of lithium chloride and odor components such as the electrolyte will reduce the time of chlorination, decrease the function of the dehumidifier, and increase the water content in the low dew point space. Even if the rotor is periodically replaced to prevent the dehumidifier function from being reduced, this operation can maintain the dehumidification function, but the required operating cost also increases. In view of the problems of the conventional technology, the present invention reduces The amount of heat required, the amount of air passing through the regeneration zone, and the amount of air passing through the rinsing zone, as a result, the amount of processing in the dehumidified area is increased, even if the same size 4 This paper is in accordance with China's solid standard in Sichuan, (redundant) 8 4 grids (210/297 gigabytes) Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs A7 _B7_, 5. Description of the invention () Also dehumidification ratio The learner has more air volume, and provides a dry dehumidification device operation mode and a dry dehumidification device. It can respond to the above-mentioned energy-saving requirements, and even the present invention can remove odors generated from odorous substances while dehumidifying, and does not need to be replaced. The rotor also aims at providing a dry dehumidifier and a dehumidification system provided with such a dry dehumidifier. Invention: To achieve the above purpose, the first item of the scope of the patent application provides a method of operating a dry dehumidifier, which is used to process air The processing air is dehumidified by a freely rotating rotor. The air passing area on the end face side of the rotor is divided into a dehumidification area, a regeneration area, and a rinsing area. The two-stage dry dehumidification system is provided with the above-mentioned areas. Rotate, the washing area is set at a position before the regeneration area from the regeneration area to the dehumidification area, and the regeneration area The air passing through the dehumidification area ratio as Z, dehumidification region set to 1, setting 0.2 € Z < 0.4 to operate. According to the inventor, even if the air volume in the regeneration area is set to 0.2 to 0.4 times or less (ideally 0.2 to 0.25 times) the dehumidification area, the dehumidification capacity is not changed at all. Setting the regenerative air volume to 0.2 to 0.4 times for operation means reducing the regenerative air volume to be lower than the conventional one, and also increasing the dehumidification process air volume to be higher than the conventional one. In other words, for the same amount of dehumidification treatment as a conventional person, only a smaller system is needed, which reduces the energy required for regeneration and cleaning, and reduces the number of fans and multi-stage dehumidification equipment. The required energy, as a whole, can achieve greater energy savings. In addition, according to the dehumidification device provided in item 2 of the scope of the patent application, 5 paper sizes are suitable for the China Gujia Standard of China ((: \ $) six 4 grids (2 丨 〇 / 297 cm) 1LI ----- -Clothing (please read the precautions on the back before filling this page), 1T printed by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A 7 B7 V. Description of the invention () Transfer method, the device allows the processed air to pass through freely rotating The rotor dehumidifies the air. The air passing area on the rotor end surface is divided into a dehumidification area, a regeneration area, and a washing area. By the rotation of the rotor, the washing area is set before the regeneration area moved from the regeneration area to the dehumidification area. Position, make the outlet temperature close to the washing area in the regeneration area close to the predetermined temperature, in order to control the regeneration air volume. At this time, the control air volume is as the third item in the patent application scope, and the inverter is controlled to send air to the regeneration area, such as The fourth scope of the patent application is to adjust the opening degree of the valve installed on the regeneration system connected to the regeneration area. Here, the temperature of the exit of the regeneration area near the scrubbing area is close to a predetermined value. The target temperature is the temperature when the passing air volume in the dehumidification area is 1, and the passing air volume of the regeneration air is 0.2 times to 0.4 times or less (ideally 0.2 times to 0.25 times). Therefore, calculate this temperature in advance, and then If the regeneration air volume is controlled near this temperature, it can reduce the regeneration air volume to less than those who are familiar with the scope of the first patent application, reduce the energy, fans, and dehumidifiers in the first stage. The energy required for the above processing. And because it is controlled by temperature, there is no need to sequentially obtain the air volume ratio, which is easier to control. In addition, the fifth item of the scope of patent application provides a method of operating a dry dehumidifier, which makes The processing air is dehumidified by the freely rotating rotor. The air passing area at the end face of the rotor is divided into a dehumidification area, a regeneration area, and a washing area. By the rotation of the rotor, the washing area is set from the regeneration area. Move to a position before the regeneration area of the dehumidification area, and set the passing air volume ratio of the regeneration area to the above dehumidification area as Z and the dehumidification area as 1. 0.1 € Z < 0.2 to run. · 6 This paper size applies the national standard (CNS) Λ4 specification (21 () > ^ 7 public help) ~ (Please read the precautions on the back before filling this page)-. 1 © —— Order— "-ΑΊ Β7 __ ____ 1 V. Description of the invention () This is the conventional dehumidification air volume is 1. When the regeneration air volume is 0.4, the cleaning air volume is set to 0.2. Decrease the amount of decontamination air. In other words, decontamination is to cool the rotor that is heated due to regeneration. Therefore, once the regeneration air volume is reduced, the decontamination air volume will be reduced. Since the decontamination air volume is only used for cooling the rotor, Therefore, less than the regeneration air volume is sufficient. Regeneration uses heat in both the heating of the rotor and the evaporation of water, so in the proportion of air volume, the cleaning air volume is 1/2 of the regeneration air volume. Therefore, as the regeneration air volume is reduced, the cleaning air volume can also be reduced. As a result, it is possible to increase the energy saving effect to a person skilled in the art. In addition, item 6 of the scope of the patent application provides a method for operating a dry dehumidification device that dehumidifies the processed air through a freely rotating rotor. The air passing area on the end face of the rotor is divided into a dehumidification area, a regeneration area, and The washing area is rotated by the rotor 'the washing area is set at a position before the regeneration area moved from the regeneration area to the dehumidification area' so that the outlet temperature of the washing area close to the dehumidification area is close to the predetermined temperature to control the washing air volume . The predetermined temperature of the above operation method is a temperature when the passing air volume of the dehumidification area is 1, and the passing air volume of the scrubbing air is less than 0.1 to 0.2 times (preferably 0.1 to 0.15 times). Therefore, in this case, if the temperature is calculated in advance, and the amount of cleaning air is controlled near this temperature, the necessary energy can be reduced. Moreover, since it is controlled by temperature, it is not necessary to sequentially obtain the air volume ratio, and it becomes easier to control. Regarding the control of the washing air volume, as described in item 7 of the scope of the patent application, the inverter is controlled as a blower that sends air to the washing area; or as described in item 8 of the scope of the patent application, adjust the connection to the washing area. Gas installed in the washing system 7 This paper is suitable for Sichuan China storehouse standard ((-NS) Λ4 is present (210 < 297 male f)-(Please read the precautions on the back before filling this page) TJ --,-° I— n few ---- Printed by the Consumers 'Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Printed A7 B7 V. Description of the invention () Opening of the door. Nine items provide a dry dehumidification device that allows the process air to pass through a freely rotating rotor to dehumidify the air. The air passing area located on the end face of the rotor is divided into a dehumidifying area, a regeneration area, and a washing area. The cleaning area is set at a position before the regeneration area that is moved from the regeneration area to the dehumidification area. The ratio of the area of the dehumidification area and other areas (regeneration area + cleaning area) on the rotor end face is 3: 1. 〇The area ratio of the above-mentioned dehumidification area and other areas (regeneration area + washing area) can be changed by order, so more dehumidification treatment can be performed than the conventional dry dehumidification device of the same type. A small amount of air can be used to dehumidify, which can save energy required for regeneration and cleaning. Moreover, the fan rating and the first stage dehumidifier can be smaller than conventional ones. In order to obtain a greater energy saving effect. Regarding the area ratio of the regeneration area and the plutonium area, it can be used as 2: 1 in the patent application scope item 10; or as 1: 1 in the patent application scope item u, It is suitable for use at lower speeds. Furthermore, as for the hygroscopic material of the brain-brain rotor, such as the cap patent =, 13 items, if the secret is banyanate, it will not be removed: Dong Hao, and the metal silicon surface and the gas-producing substance 雠 Lion '_ 不 喷 _Test off the noodle dumplings. Case 2 of deleting metal miscellaneous salt, such as the use of carbonic acid-formaldehyde as the electrolyte in the manufacturing process of lithium secondary batteries Carbonic acid such as Cool and Methyl Ethyl Carbonate Department, to this, the paper scale suitable for Chinese home scared quasi ® (CNS) Λ4 current cell ((please read the Notes on the back of the smell and then fill the page)
經濟部中央標準局員工消費合作社印製 A7 ι____B7 _ _ 1 五、發明説明（） 除去從其他的有機化合物所造成的臭氣。 申請專利範圍第14項提供一種除濕裝置，包含：容納 室，圍繞室，圍繞容納室；如申請專利範圍第9、10、或11 項之乾式除濕裝置；空氣供給系，將上述乾式除濕裝置所 供應的除濕空氣送入容納室；空氣排出系，將容納室內的 臭氣物質排出圍繞室外部；及循環系，將乾式除濕裝置裡 所除濕的空氣送入圍繞室，並將包含從容納室漏入圍繞室 內的臭氣物質之混合空氣送回乾式除濕裝置，空氣供給系 和循環系是使用同一個乾式除濕裝置，將被除濕的空氣分 別分配至空氣供給系和循環系來構成該乾式除濕裝置，容 納室則由比圍繞室還高的高壓所構成。此情況亦如申請專 利範圍第15項，放於轉子內的吸濕材料其主成份最好爲金 屬Ϊ夕酸鹽。 根據申請專利範圍第14或15項的除濕系統，使外面空 通過乾式除濕裝置來形成除濕空氣，將該除濕空氣通過空 氣供給系連續地送入容納室內，容納室的內部將比圍繞室 還被高壓化。然後容納室內的臭氣物質和被送入的空氣所 形成的混合空氣的一部份經由空氣排出系被排出的同時， 亦從容納室漏出流入圍繞室的內部。流入該圍繞室內的混 合空氣通過循環系被送入乾式除濕裝置內，在乾式除濕裝 置上除濕的同時，吸附臭氣物質來進行脫臭。然後被脫臭 的空氣再一次地被送入圍繞室和容納室內。 因此，在圍繞室的臭氣和在容納室的相較之下少許 多。由生產過程配置於容納室來局部地限定惡臭發源處， 9 本紙張尺度適用中國國家標隼（> Λ4規格（21〇κ2Μ公筇） (請先閲讀背面之注意事項再填寫本頁) • --- :,玎丨：----ιό>. A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明（） “ 而且用ΐ父少的處裡空氣量能確保產品的品質。 容納室是由比圍繞室還高的高壓來構成容納室內部， 從作業性方面來考量，像容納室內的空氣漏入圍繞室內那 樣半封閉的空間是較佳的。圍繞室是圍繞容納室而成，因 此不問其形狀爲何。 圖不之簡單說明 圖1表示有關本發明的實施型態之二段式乾式除濕系 統的構成槪略之說明圖； 圖2表示使用圖1的二段式乾式除濕系統之第二段的乾 式除濕裝置之轉子部份的斜視圖； 圖3表示從圖2的乾式除濕裝置的軸方向所看到的正面 圖， 圖4表示對於除濕風量之乾式除濕裝置的再生風量比 及和除濕區域出口溫度的露點溫度關係之圖表； 圖5表示能使用圖1的二段式乾式除濕系統，從其他乾 式除濕裝置之轉子的軸方向所看到的正面圖； 圖6表示在乾式除濕裝置上，測定在再生區域和淸洗區 域的出口温度時的測定地方之說明圖； 圖7表示在乾式除濕裝置上，在再生區域和淸洗區域的 出口溫度和風量的關係之圖表； ^ 圖8表示在有關其他實施型態之乾式除濕裝置上，溫g 偵測器的設置位置之說明圖； 圖9表示第2實施型態之構成槪略的說明圖； 圖10表示習知的二段式乾式除濕裝置系統所使用的第 10 (請先間讀背面之注意事項再填寫本頁) .,—0. ，-° 壽· 本紙張尺度適用中國國家標卒（（:阳）八4規格（2丨0/297公趁） 經濟部中央標準局員工消費合作社印製 A7 ____B7_ , 五、發明説明（） 二段乾式除濕裝置之轉子部份的斜視圖； 圖11表示從圖10的乾式除濕裝置的軸方向所看到的正 面圖； 元件編號之說明 1 .乾式除濕裝置（第一段) 10 乾式除濕裝置（第二段) 11 轉子 11a 除濕區域 lib 再生區域 11c 淸洗區域 12、 13 小室 14、 15 溫度偵測器 D1-D8 氣門 R 低露點空間 發明之實施塑態 以下以圖式來說明本發明的實施型態。圖1是表示採用 有關於第1實施型態的乾式除濕裝置之二段式除濕系統的 系統槪略，該二段式乾式除濕系統是由供應低露點空氣至 低露點空間R之系統所構成。 導入外面空氣OA是由輸進外面空氣之進氣管道1所導 入，由處理外面空氣冷卻器2來冷卻除濕。被冷卻除濕之後 的空氣在冷卻再生剩餘空氣冷卻器3上和被冷卻的再生剩 餘空氣混合，由處理外面空氣風扇4將其導入第一段的乾式 除濕裝置5的除濕區域5a裡，被除濕至例如露點溫度-10 11 (請先閲讀背面之注意事項再填寫本頁)Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs A7 ι ____ B7 _ _ 1 V. Description of the Invention () Remove the odor caused by other organic compounds. Item 14 of the scope of patent application provides a dehumidification device, which includes: a accommodating chamber, a surrounding room, and a surrounding accommodating room; for example, a dry dehumidifier device of the scope of patent application No. 9, 10, or 11; The supplied dehumidified air is sent to the accommodating chamber; the air exhaust system is to discharge the odorous substances in the accommodating chamber to the outside of the surrounding chamber; and the circulation system is to send the dehumidified air in the dry dehumidifier to the surrounding chamber and contain the leakage The mixed air entering the indoor odorous substance is sent back to the dry dehumidifier. The air supply system and the circulation system use the same dry dehumidifier, and the dehumidified air is distributed to the air supply system and the circulation system to form the dry dehumidifier. The accommodating chamber is composed of a higher pressure than the surrounding chamber. In this case, as in item 15 of the patent application scope, the main component of the hygroscopic material placed in the rotor is preferably metal acetate. According to the dehumidification system in the scope of application patent No. 14 or 15, the outer space is passed through a dry dehumidifier to form dehumidified air, and the dehumidified air is continuously sent into the accommodation chamber through the air supply system. The interior of the accommodation chamber will be more than the surrounding chamber. High pressure. Then, a part of the mixed air formed by the odorous substance in the accommodating chamber and the air being sent in is discharged through the air exhaust system, and also leaks from the accommodating chamber into the surrounding chamber. The mixed air that has flowed into the surrounding room is sent to the dry type dehumidifier through the circulation system, and while the dry type dehumidifier is dehumidified, odorous substances are adsorbed to perform deodorization. The deodorized air is then sent into the surrounding room and the containing room again. Therefore, the odor around the chamber is slightly more than that of the receiving chamber. The production process is arranged in the storage room to locally limit the origin of malodor. 9 paper sizes are applicable to the Chinese national standard (> Λ4 specification (21〇κ2Μ)) (Please read the precautions on the back before filling this page) • ---:, 玎 丨: ---- ιό >. A7 B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. 5. Description of the invention () "Also, the quality of the product can be ensured by using a small amount of air in my father's place. The accommodating chamber is composed of a high pressure higher than the surrounding chamber. From the aspect of workability, a semi-closed space such as the air in the accommodating chamber leaking into the surrounding chamber is preferable. The surrounding chamber is formed around the accommodating chamber. Therefore, it does not ask what the shape is. The figure is simply explained. FIG. 1 is a diagram illustrating the structure of a two-stage dry dehumidification system according to the embodiment of the present invention. FIG. 2 is a diagram showing a two-stage dry dehumidification system using FIG. 1. A perspective view of a rotor portion of the dry dehumidifier of the second stage; FIG. 3 shows a front view seen from the axial direction of the dry dehumidifier of FIG. 2, and FIG. 4 shows the dry dehumidifier for the dehumidification air volume Graph of the regeneration air volume ratio and the dew point temperature relationship with the outlet temperature of the dehumidification area; Figure 5 shows the front view of the two-stage dry dehumidification system of Figure 1 as seen from the axial direction of the rotor of other dry dehumidification devices; Figure 6 An explanatory diagram showing a measurement place when measuring the outlet temperature in the regeneration area and the rinsing area on the dry dehumidifier; FIG. 7 shows the relationship between the outlet temperature and the air volume in the regeneration area and the rinsing area on the dry dehumidifier. Diagram; ^ FIG. 8 is an explanatory diagram of the installation position of a temperature g detector on a dry dehumidifier of another embodiment; FIG. 9 is an explanatory diagram of a structure of a second embodiment; No. 10 used in the known two-stage dry dehumidifier system (please read the precautions on the back before filling this page)., —0.,-° Shou · This paper standard is applicable to Chinese national standard ((: 阳) 8 size 4 (2 丨 0/297) While printing A7 ____B7_ by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs, V. Description of the invention () The perspective view of the rotor part of the two-stage dry dehumidifier; Front view seen from the axial direction of the dry dehumidifier in Fig. 10; Description of component numbers 1. Dry dehumidifier (first stage) 10 Dry dehumidifier (second stage) 11 Rotor 11a Dehumidification area lib Regeneration area 11c 淸Washing area 12, 13 Cells 14, 15 Temperature detectors D1-D8 Valves R Low dew point space Invention implementation mode The following describes the embodiment mode of the present invention with a diagram. FIG. 1 shows the use of the first embodiment System strategy of a two-stage dehumidification system for a dry dehumidifier in a state of state. The two-stage dry dehumidification system is composed of a system that supplies low dew point air to a low dew point space R. The outside air OA is introduced by the outside air. The intake duct 1 is introduced, and is cooled and dehumidified by a process outside air cooler 2. The cooled and dehumidified air is mixed with the cooled and regenerated surplus air on the cooling and regenerating surplus air cooler 3, and is introduced into the dehumidifying area 5a of the first-stage dry dehumidifying device 5 by the processing outside air fan 4 and dehumidified to For example, dew point temperature -10 11 (Please read the precautions on the back before filling this page)
本紙張尺度適州中國阄家標準（CNS ) Λ4規格U10X 297公籍） 經濟部中央標隼局員工消费合作社印製 kl B7__;_ 五、發明説明（） °C。在該第一段的乾式除濕裝置5上的轉子（未顯示於圖 中），因處理之露點溫度高，有在轉子端面分割成除濕區 域5a和再生區域5b兩個空氣通過區域之類型。此外轉子的 厚度爲200_，除濕區域5a和再生區域5b的面積比例爲 3:1 ° 之後，外面空氣通過第一段乾式除濕裝置5之除濕區域 5a後，被處理的空氣和從低露點空間R經由空氣回流進氣管 道6返回的一部份回流空氣RA1混合後，由處理風扇7送至 預冷器8。處理的空氣由預冷器8冷卻後，將其導入有關本 實施型態的第二段乾式除濕裝置10之轉子11的除濕區域 11 a來作除濕處理。 第二段乾式除濕裝置10如圖2、圖3所示，由在旋轉轉' 子11的兩側配置小室12、13所構成。在轉子11的端面上， 依圖3的箭頭所示在轉子11的旋轉方向上劃分除濕區域 .11a、再生區域lib、淸洗區域11c等3個空氣通過區域。然 後在小室12的外側端面上爲對應此等各區域而形成連接進 氣管道等的除濕入口 12a、再生出口 12b、淸洗出口 12c。在 小室13的外部端面也爲了對應上述3個區域而形成各各除 濕出口、再生入口、淸洗入口（任何一個均無圖示）。在 該乾式除濕裝置10的轉子11裡，放有以氯化鋰、砂凝膠、 沸石或金屬矽酸鹽等主成份的吸濕材料。 上述3個通過區域之除濕區域11a、再生區域lib、淸洗 區域11c是以放射狀地被劃分而成的其中一個型態，即略像 扇形狀，每個通過區域的中心角Θ被設定爲除濕區域11a 12 本紙張尺度適州中闽國家標夺（CNS ) Λ4現格（2!^<2W公释) " (諳先閒讀背面之注意事項再填寫本頁)This paper is scaled to the China Standard for Chinese Family (CNS) Λ4 Specification U10X 297 Citizenship) Printed by the Consumer Cooperatives of the Central Bureau of Standardization of the Ministry of Economic Affairs kl B7 __; _ 5. Description of the invention () ° C. The rotor (not shown in the figure) of the dry-type dehumidifier 5 in this first stage is divided into two types of air passage areas, namely a dehumidification area 5a and a regeneration area 5b, on the end surface of the rotor due to the high dew point temperature of the treatment. In addition, the thickness of the rotor is 200 mm, and the area ratio between the dehumidification area 5a and the regeneration area 5b is 3: 1 °. After the outside air passes through the dehumidification area 5a of the first dry dehumidification device 5, the processed air and the space from the low dew point R A part of the return air RA1 returned through the air return air inlet duct 6 is mixed and sent to the precooler 8 by the processing fan 7. After the processed air is cooled by the precooler 8, it is introduced into the dehumidification area 11a of the rotor 11 of the second-stage dry dehumidifier 10 related to this embodiment for dehumidification. As shown in FIGS. 2 and 3, the second-stage dry dehumidifier 10 is composed of small chambers 12 and 13 arranged on both sides of the rotor 11. On the end surface of the rotor 11, three air passage areas, such as a dehumidification area .11a, a regeneration area lib, and a washing area 11c, are divided in the rotation direction of the rotor 11 as shown by the arrows in FIG. 3. Dehumidification inlets 12a, regeneration outlets 12b, and scrubbing outlets 12c are formed on the outer end surface of the chamber 12 to connect the air ducts and the like corresponding to these areas. Dehumidification outlets, regeneration inlets, and rinsing inlets are also formed on the outer end surface of the cell 13 to correspond to the above three areas (none of which are shown). The rotor 11 of the dry dehumidifier 10 contains a hygroscopic material containing lithium chloride, sand gel, zeolite, or metal silicate as a main component. The dehumidification area 11a, the regeneration area lib, and the washing area 11c of the above three passing areas are one of the types that are radially divided, that is, they are slightly fan-shaped, and the central angle Θ of each passing area is set as Dehumidification area 11a 12 This paper is suitable for China and Fujian National Standards (CNS) Λ4 now (2! ^ ≪ 2W public release) " (谙 Please read the precautions on the back side and fill in this page)
ΑΊ B7 經濟部中央標率局員工消費合作社印製 五、發明説明（） 中心角Θ1爲27〇。，再生區域lib中心角Θ2爲60° ’淸洗 區域11c中心角Θ 3爲30° 。因此各各通過區域的面積比爲 9:2:1，除濕區域11a和其他區域（再生區域llb +淸洗區域· 11c)的面積比爲3:1。又轉子11的厚度爲400mm。此外’ 轉子11的旋轉速度爲6次旋轉/小時。 在上述乾式除濕裝置1 〇之轉子11的除濕區域11 a上所 除濕成爲低露點的空氣，由加熱器21及後冷卻器22來調節 成既定的溫度後，經由空氣供給SA來供應至低露點空間R 內。從低露點空間R出來的其他一部份回流空氣RA2 ’作爲 淸洗空氣經由淸洗系回流空氣進氣管道23導入乾式除濕裝 置10的轉子11之淸洗區域11c，藉此來進行轉子11的冷卻。 之後，通過轉子11之淸洗區域lie的淸洗空氣由再生系 統ZC引導並藉由第二段的再生風扇26來和再生循環系統P 的空氣匯合並混合之。混合後的大部分空氣經由再生系統 進氣管道27被送至第二段的再生加熱器28，由該再生加熱 器28加熱至例如12(TC後，將其導入至乾式除濕裝置1〇的轉 子11之再生區域1A內。導入淸洗區域lie的空氣亦可使用 從除濕區域1 la所出來的空氣。 又，於低露點空間R上安裝爲了將室內的混合空氣排出 低露點空間R外部的排出風扇71，亦可另外設置排出進氣管 道72。排出進氣管道72被設置於產生惡臭處的附近。在連 續裝設有氣流室等排風機之生產裝置的狀況下則可不要排 出風扇71。 從再生系統ZC而來的一部份空氣，在通過第一段的再 13 請先閱讀背面之注意事項再填寫本頁) ~ ----- 訂 —,— 本紙張尺度適丨Π中國ϋ家標孪（CNS ) Λ4规格（2丨297公f ) •第87108116號專利申請案中文專利說明書修正頁 ^ · 88年11月24曰修訂 經濟部中央標糸局負工消资合作社印製 五、發明説明（ 生加熱器30加熱後，第一段的再生風扇29將其導入第一段 的乾式除濕裝置5之再生區域5b內，作爲第一段乾式除濕裝 置5的轉子之再生所用。之後，以排氣EA排出系統外部。 另一方面，沒有通過第一段的再生加熱器30而剩餘的再生 系統ZC的空氣，經由再生剩餘空氣循環進氣管道31被送至 前面已出現的冷卻再生剩餘空氣用的冷卻器3，在此冷卻 後，和導入外面空氣OA混合並被導入至第一段的乾式除濕 裝置5之除濕區域5a內進行除濕。即是作爲處理空氣之一部 份再被使用。又，在圖1上的D1-D8是爲了調節風量而安裝 於進氣管道間的氣門。 以上所述構成使用有關第1實施型態之乾式除濕裝置 10的二段式乾式除濕系統，如上所述，在第一段的乾式除 濕裝置5之除濕區域5a上所被除濕之空氣，經由預冷器8來 冷卻後再由第二段的乾式除濕裝置1 〇之除濕區域11 a再除 濕，之後由加熱器2卜後冷卻器22來調節溫度後送至低露 點空間R內。此外，從低露點空間尺出來的回流空氣RA2被 導入至乾式除濕裝置1〇的轉子Η之淸洗區域11c內，另一方 面，由再生加熱器28所加熱的空氣則被導入轉子11之再生 區域lib內。 此時，位於轉子11兩側的除濕區域llafD再生區域lib 的比例爲9:2，因此通過再生齒域1化之#生空氣的通過風 量爲被除濕處理空氣的2Ζ2，亦即0.22倍，但根據發明者所 調查，如圖4之圖表所示，如此的再生空氣的通過風k即使 爲被除濕處理空氣的0.22倍，也能夠供應低露點空間R內所 14 n J-H- II --- . ! ·--- I . n (請先閱讀背面之注意事項再填寫本頁) 訂 國國家摞卒（（:NS ) Μ規格（2丨0X297公釐 經濟部中央標挲局負工消贽合作社印製 * A7 __B7_. 五、發明説明（） ‘ 需的露點溫度（_50°C )。此外，根據該圖表，再生空氣的 通過風量即使爲被除濕處理之空氣的0.25倍，亦能確認可 獲得大約相同的除濕能力。但若爲0.15倍左右，則因露點 溫度上升至-47°C故較不理想。因此，如同本發明所述，如 將風量比設爲高於0.2倍，則可供應在低露點空間R內所需 要的露點溫度。又，在該圖表上，導入除濕區域內的處理 空氣的入口絕對溼度爲lg/kg,(露點溫度-20°C )。. 儘管如此的除濕能力和習知的該種乾式除濕裝置相 同，但若將本實施型態上所使用的乾式除濕裝置10的轉子 11端面（圖3)和習知的乾式除濕裝置200的轉子201端面（圖 11)相較，便能很淸楚地看出在本實施型態上所使用的乾 式除濕裝置10的除濕區域11a之面積爲習知的1.2倍。換言 之，使用同一直徑的轉子時，本實施型態能獲得1.2倍的除 濕風量。此外，再生區域lib的面積也比習知來的小，有關 再生風量也比習知來的少量即可。因此，反過來在進行既 定風量的除濕膚理時，本實施型態可將轉子的直徑變小， 且連同再生空氣的風量亦可比習知來的少。因此可節約再 生加熱器28所需要的能源σ此外，由於亦可同時降低淸洗 風量，因此亦能降低導入外面空氣ΟΑ的導入量，其結果爲 能將第一段的乾式除濕裝置5變小°另外在系統上所使用的 風扇之額定也比習知來的小即定夠。因ih，預計系統全體 能比習知更加地省能源，並且亦能將設備機器小型化。 將使用有關本實施型態之乾式除濕裝置10的二段式除 濕系統，和習知的該種二段乾式除濕系統，即代替第二段 ί.——-----!——-fe— (請先閱讀背面之注意事項再填寫本頁) 訂 (210X297公釐） 五、發明説明 A 7 B7 經濟部中央標準局員工消費合作社印製 的乾式除濕裝置10而使用圖9、10所表示的乾式除濕裝置 200之系統相較，能確認可降低在冷熱爲25%，在溫熱爲40% 合計約30°/〇的能源消耗： 此外第二段的乾式除濕裝置10的轉子U的大小也爲習 知姐83%即足夠，而且有關第一段的乾式除濕裝置5的轉子 也以習知的第一段轉子的太小就能進行同一程度的除 濕處理。其他如以上所述，因能將各種加熱器、冷卻器、 風扇等的設備小型化，所以也能大幅地降低設備費用。因 此均能降低原價和週轉資金雙方之費用。 該種乾式除濕裝置的能力和轉子的旋轉次數也有關 係。亦即旋轉次數到達某個數値爲止，則較高數値的旋轉 數能提高除濕能力，但若旋轉次數過高則再生能力會變得 不足，反而降低除濕能力。特別是在第二段有配置低露點 用之乾式除濕裝置上，若一提高旋轉次數則在淸洗上的冷 卻會變得不足，和一般的除濕裝置相較之下，用低旋轉次 數則除濕能力有降低的傾向。由於熱量的旋轉次數越高則 加熱轉子本身的熱量（再生區域）及冷卻的熱量（淸洗區 域及除濕區域）便越大，因此相當於除濕量的熱量便增加。 所以在低露點用的該種乾式除濕裝置上採用低旋轉次數來 進行運轉較爲理想。 圖5所表示的乾式除濕裝置50就是採用低旋轉，例如以 適於4次旋轉/小時的例子來表示，在位於該乾式除濕裝置 50之轉子51的端面之空氣通過區域和前面已出現的乾式除 濕裝置10相同，由被晝！)分成除濕區域51a、再生區域51b、 16 請 注ΑΊ B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention () The central angle Θ1 is 27 °. The center angle Θ2 of the reproduction area lib is 60 °, and the center angle Θ3 of the wash area 11c is 30 °. Therefore, the area ratio of each passing area is 9: 2: 1, and the area ratio of the dehumidification area 11a and other areas (regeneration area 11b + washing area 11c) is 3: 1. The thickness of the rotor 11 is 400 mm. The rotation speed of the rotor 11 is 6 rotations / hour. The air dehumidified in the dehumidification area 11 a of the rotor 11 of the dry dehumidification device 10 is adjusted to a predetermined temperature by the heater 21 and the after cooler 22, and then supplied to the low dew point through the air supply SA. Within space R. The other part of the return air RA2 ′ coming out of the low dew point space R is introduced into the cleaning area 11c of the rotor 11 of the dry dehumidifier 10 as the cleaning air through the cleaning system return air intake duct 23, thereby performing the rotor 11 cool down. Thereafter, the cleaning air passing through the cleaning area lie of the rotor 11 is guided by the regeneration system ZC and is combined with the air of the regeneration circulation system P by the regeneration fan 26 of the second stage and mixed. Most of the mixed air is sent to the regeneration heater 28 in the second stage through the regeneration system intake duct 27, and the regeneration heater 28 is heated to, for example, 12 ° C, and is then introduced to the rotor of the dry dehumidifier 10. In the regeneration area 1A of 11. The air introduced into the washing area lie can also use the air from the dehumidification area 1 la. Also, it is installed in the low dew point space R to discharge the indoor mixed air out of the low dew point space R. The fan 71 may be additionally provided with an exhaust air intake duct 72. The exhaust air intake duct 72 is provided near the place where the malodor is generated. The exhaust fan 71 may not be required in a case where a production device such as an airflow chamber is continuously installed. Part of the air from the regeneration system ZC passes through the first paragraph and then 13 Please read the precautions on the back before filling in this page) ~ ----- Order —, — This paper is suitable for China 丨 Π Family Standard Twin (CNS) Λ4 Specification (2 丨 297gf) • No. 87108116 Patent Application Chinese Patent Specification Revision Page ^ · November 24, 88 Revised Printed by the Central Standards Bureau of the Ministry of Economic Affairs , Invention description ( After the raw heater 30 is heated, the first-stage regeneration fan 29 guides it into the regeneration area 5b of the first-stage dry dehumidifier 5 for regeneration of the rotor of the first-stage dry dehumidifier 5. After that, the exhaust gas is exhausted. The EA is discharged from the outside of the system. On the other hand, the air of the regeneration system ZC that has not passed through the regeneration heater 30 in the first stage is sent to the previously-existing cooling regeneration air through the regeneration surplus air circulation intake duct 31. After cooling, the cooler 3 is mixed with the outside air OA and is introduced into the dehumidification area 5a of the dry dehumidifier 5 in the first stage for dehumidification. That is, it is reused as part of the process air. Also, D1-D8 in Fig. 1 are valves installed between intake ducts for adjusting the air volume. The above-mentioned configuration uses the two-stage dry dehumidification system of the dry dehumidifier 10 according to the first embodiment, as described above, The air dehumidified in the dehumidification area 5a of the first-stage dry dehumidifier 5 is cooled by the precooler 8 and then dehumidified by the dehumidification area 11a of the second-stage dry dehumidifier 10. After that, the temperature is adjusted by the heater 2 and the after cooler 22 and sent to the low dew point space R. In addition, the return air RA2 from the low dew point space is introduced into the washing area 11c of the rotor of the dry dehumidifier 10. Inside, on the other hand, the air heated by the regeneration heater 28 is introduced into the regeneration area lib of the rotor 11. At this time, the ratio of the dehumidification area llafD regeneration area lib located on both sides of the rotor 11 is 9: 2, so it passes The passing air volume of the regenerating tooth field 1 Huazhi # raw air is 2Z2 of the dehumidified air, which is 0.22 times, but according to the investigation by the inventor, as shown in the graph of Fig. 4, the passing air k of such regenerating air is even 0.22 times of the dehumidified air, can also supply 14 n JH- II in the low dew point space R ---.! --- I. N (Please read the precautions on the back before filling this page) ((: NS) Μ specifications (2 丨 0X297 mm printed by the Central Bureau of Standards, Ministry of Economic Affairs and Consumer Cooperatives) * A7 __B7_. 5. Description of the invention () 'Dew point temperature required (_50 ° C). In addition, according to the graph, even if the passing air volume of the regeneration air is 0.25 times that of the air to be dehumidified, it can be confirmed that approximately the same dehumidifying capacity can be obtained. However, if it is about 0.15 times, the dew point temperature rises to -47 ° C, which is not ideal. Therefore, as described in the present invention, if the air volume ratio is set to be higher than 0.2 times, the required dew point temperature in the low dew point space R can be supplied. In addition, on this graph, the absolute humidity at the inlet of the process air introduced into the dehumidification area is lg / kg, (dew point temperature -20 ° C). Although the dehumidification capacity is the same as that of the conventional dry dehumidifier, if the end face of the rotor 11 of the dry dehumidifier 10 used in this embodiment (Fig. 3) and the rotor of the conventional dry dehumidifier 200 Compared with the 201 end surface (FIG. 11), it can be clearly seen that the area of the dehumidification area 11a of the dry dehumidifier 10 used in this embodiment is 1.2 times that of the conventional one. In other words, when a rotor with the same diameter is used, this embodiment can obtain 1.2 times the dehumidifying air volume. In addition, the area of the regeneration area lib is also smaller than the conventional one, and the regeneration air volume may be smaller than the conventional one. Therefore, in turn, when performing a dehumidifying skin treatment with a predetermined air volume, the present embodiment can reduce the diameter of the rotor, and the air volume with the regeneration air can also be smaller than conventional. Therefore, the energy σ required for the regenerative heater 28 can be saved. In addition, since the amount of scrubbing air can also be reduced at the same time, the amount of outside air OA introduced can also be reduced. As a result, the dry dehumidifier 5 in the first stage can be made smaller. ° In addition, the rating of the fan used in the system is smaller than the conventional one. Because of ih, the overall system is expected to be more energy efficient than conventional, and equipment can also be miniaturized. The two-stage dehumidification system of the dry dehumidification device 10 related to this embodiment and the conventional two-stage dry dehumidification system will be used instead of the second stage. — (Please read the precautions on the back before filling out this page) Order (210X297 mm) V. Description of the invention A 7 B7 The dry dehumidifier 10 printed by the staff consumer cooperative of the Central Standards Bureau of the Ministry of Economic Affairs is shown in Figures 9 and 10 Compared with the system of 200 dry dehumidifier 200, it can be confirmed that the energy consumption can be reduced by 25% in cold and heat, and 40% in warm. The total energy consumption is about 30 ° / 〇: In addition, the size of the rotor U of the second stage dry dehumidifier 10 83% is enough for the acquaintance, and the rotor of the first-stage dry dehumidifier 5 is too small to perform the same degree of dehumidification. In addition, as described above, since equipment such as various heaters, coolers, fans, and the like can be miniaturized, equipment costs can also be significantly reduced. Therefore, the cost of both the original price and working capital can be reduced. The capacity of this type of dry dehumidifier is also related to the number of rotations of the rotor. That is, until the number of rotations reaches a certain number, a higher number of rotations can increase the dehumidification capacity, but if the number of rotations is too high, the regeneration capacity becomes insufficient, and the dehumidification capacity is reduced. Especially on the second stage of the dry dehumidifier with a low dew point, if the number of rotations is increased, the cooling on the rinsing will become insufficient. Compared with ordinary dehumidifiers, dehumidification with a low number of rotations Ability to decrease. The higher the number of rotations of the heat, the greater the heat of the heating rotor itself (regeneration area) and cooling heat (washing area and dehumidification area), so the amount of heat equivalent to the amount of dehumidification increases. Therefore, it is ideal to use a low dew-point dehumidifier of this type to operate with a low number of rotations. The dry dehumidifier 50 shown in FIG. 5 uses low rotation, for example, an example suitable for 4 rotations / hour. The air passing area on the end face of the rotor 51 of the dry dehumidifier 50 and the dry type that has appeared in the front The dehumidifying device 10 is the same, by the day! ) Divided into dehumidification area 51a, regeneration area 51b, 16 Please note
Q 訂 本紙张K度適屮中國S家標卑K_NS ) Λ4堤格（2丨0乂 297公1 ) A7 _________ B7 , 五、發明説明（） 淸洗區域51c3個通過區域所形成，各通過區域的中心角㊀ 設定爲除濕區域51a中心角Θ1爲270°C、再生區域51b中心 角Θ2爲45°C、淸洗區域51(：中心角Θ3爲45°C。因此各各通 '過區域的面積比例爲6:1:1。 若以使用該乾式除濕裝置50來代替上述乾式除濕裝置 10，則其除濕能力雖比上述實施型態的情況還低，但因再 生區域5lb的面積比上述乾式除濕裝置10還來的小，因此能 更加降低有關再生所需風量、能源，全體所消耗之能源能 比上述實施型態的系統還少。.、 使用通過高溫的再生區域之再生空氣的熱度來蒸發在 靠近除濕區域轉子加熱的地區偏中間的地方（靠淸洗區域 的地方）的水分。 因此再生空氣的出口溫度分布爲在除濕區域上溫度 低，在靠近淸洗區域的地方則溫度高。如此的溫度分布隨 著除濕負荷的增加，在除濕區域方面的變化少，但在淸洗 區域方面會出現溫度降低。 經濟部中央標準局員工消費合作社印製 ,-, . -b I I I11-· - I- - ii m HI I . 請先閱讀背面之注意事I再填寫本頁) 因此發明人既著眼於如此的分布特性，也能建議以在 再生區域上靠進淸洗區域的出口溫度，或在淸洗區域上靠 .近除濕區域的出口溫度來控制再生風量或淸洗風量，當除 濕負荷小時，降低習知投入所需以上之再生的熱能源，設 法以節省能源爲目的發明。 就以圖10所表示的習知型的乾式除濕裝置200的轉子 201來看，若以圖6來詳述，則從轉子201的軸方向來看，將 位於該轉子201的端面上將再生區域20lb五等分之線a、b、 ^17 本紙 —--------------------------------------——-- 、Λ、砲用屮國阀家標準（CNS )八4現格（21()/297公釐） 經濟部中央標準局員工消費合作社印絮 A7 B7Q The size of the paper is suitable for Chinese papers. K_NS) Λ4 Tige (2 丨 0 乂 297 1) A7 _________ B7, V. Description of the invention () The washing area is formed by 51c3 passing areas, each passing area The central angle ㊀ of the dehumidification area 51a is set to 270 ° C, the central angle Θ2 of the regeneration area 51b is 45 ° C, and the washing area 51 (: the central angle θ3 is 45 ° C. Therefore, The area ratio is 6: 1: 1. If the dry dehumidification device 50 is used instead of the dry dehumidification device 10, the dehumidification capacity is lower than that in the above embodiment, but the area of 5 lb in the regeneration area is higher than the dry type. The dehumidifier 10 is also small, so it can reduce the amount of air and energy required for regeneration. The energy consumed by the whole is less than the system of the above implementation type .. Use the heat of the regeneration air passing through the high-temperature regeneration area to Evaporates moisture near the middle of the area heated by the rotor in the dehumidification area (where it is near the decontamination area). Therefore, the outlet temperature of the regeneration air is lower in the dehumidification area and near the decontamination area. . Such a temperature distribution changes with the increase of the dehumidification load, and there is less change in the dehumidification area, but the temperature will decrease in the washing area. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs,-,. -B II I11- ·-I--ii m HI I. Please read the notes on the back I before filling out this page.) Therefore, the inventor not only focused on such distribution characteristics, but also suggested that the outlet temperature should be closer to the regeneration area on the regeneration area. Or, in the decontamination area, the regeneration air volume or decontamination air volume is controlled near the outlet temperature of the dehumidification area. When the dehumidification load is small, the conventionally-renewed heat energy required to reduce the conventional input is reduced, and an attempt is made to save energy for the purpose of invention. Regarding the rotor 201 of the conventional dry dehumidifier 200 shown in FIG. 10 and referring to FIG. 6 in detail, from the axial direction of the rotor 201, the regeneration region will be located on the end surface of the rotor 201 20lb fifths line a, b, ^ 17 paper -------------------------------------- --——--, Λ, 屮, National Standard for the Use of Guns (CNS) 8 and 4 (21 () / 297 mm) Printed by the Consumers Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7
— ----------- I 五、發明説明（） c、d上和將淸洗區域201c3等分之線e、f上，而且在靠近轉 子201的端面的地方（距離轉子201端面50mm的地方）設置 溫度偵測器（無圖示），於圖6在上述的各線上標示◦符號 的地點，讓通過除濕區域201a的風量對通過再生區域201b 的風量變化時，藉該溫度偵測器調查在a、b、c、d、e、f 各線上被測定之測定點的溫度分布。 其結果得到如圖7之圖表所示之特性。又，在同圖表 中，最適當的風量爲通過除濕區域201a的風量，也就是相 對於處理風量之通過再生區域201b的風量，即意指再生風 量的比爲0.2時，所謂風量過大是意指同比爲0.4時，所謂風 量過小是意指同比爲0.15時。 根據上述，在再生區域20lb線d上的測定點上，當除濕 負荷小時溫度變高，除濕負荷大時溫度變低。因此，事先 求取在d上最適當風量時的溫度（目標溫度），以接近該目 標溫度來控制再生風量，由此可獲得最適當的再生風量。 相同地，在淸洗區域201c上，在線酌測定點上的溫度 特性其溫度是以過小風量、最適當風量、過大風量之序來 降低。因此，事先求取在f上最適當風量時的溫度（目標溫 度），以接近該目標溫度來控制淸洗風量，由此可獲得最 適當的淸洗風量。 ' 如上所述，藉由在既定的地方設置溫度偵測器來控制 讓被測定的再生出口溫度和淸洗出口溫度接近目標溫度的 話，便不需要過大的風量就能執行必要的運轉。 圖8所示之乾式除濕裝置60爲以控制讓上述出口溫度 18 本紙張尺度適用中网家標CNS )八4験（2UVX 297公釐） (請先閱讀背面之注意事項再填寫本頁) -- L------. 訂 經濟部中央標準局員工消費合作社印掣 Μ Β7 _^_ 五、發明説明（） " 接近目標溫度來設法節省能源之物。即是位於乾式除濕裝 置60之轉子61端面上的小室62內的空氣通過區域，和前面 已出現的乾式除濕裝置1〇—樣，依轉子61的旋轉順序劃分 成除濕區域61a、再生區域61b、淸洗區域61c3個區域。但 是，各區域的面積比例設定成和圖9、圖10所表示之習知型 的乾式除濕裝置200上的面積比例相同。 然後從在小室62內的再生區域61b上的轉子61之端 面，在距離例如軸方向50mm左右且接近淸洗區域61c的地 方設置檢查出再生空氣之出口溫度的溫度偵測器63 〇 由上述所構成的乾式除濕裝置60能替代有關上述實施 型態之乾式除濕裝置10，可使用於圖1所表示之二段式乾式 除濕系統。此時，讓由溫度偵測器63所檢測出的溫度接近 事先被求取的目標溫度（圖7線d之最適當風量的溫度）， 反相器控制再生風扇26 (例如再生風扇26的發動機之反相 器控制）來調整再生風量，或是控制氣門D5的開度來調整 再生風量的話，均能獲得最適當的再生風量。因此，可設 法節省再生所需的熱能源，此外隨之亦能設法以排氣風 量、外面空氣導入量來節省能源。而且由於以溫度偵測器 63所檢測出的溫度來執行如上述的控制，因此控制容易， 且應對性也良好。由於被防止去製造出過大的風量，因此 省能源效果比習知還高。 又’上述乾式除濕裝置60是以由設於再生區域的溫度 偵測器63所檢測出的再生空氣的出口溫度來執行上述控 制’但如圖8所示，在淸洗區域61c上靠近除濕區域61a的地 19 本紙張尺度適用中國國家慄唪（CNS ) Λ4規格（21〇y 297公漦） ' - -) "二 -ΐ—m m· - 1 t^l I I I -- In ·! (請先閲讀背面之注意事項再填寫本頁) 訂 - 經濟部中央標準局員工消費合作社印髮 A7 ——------B7_^___ 五、發明説明（） 方設置檢測出淸洗空氣的出口溫度之溫度偵測器64，讓由 該溫度偵測器64所檢測出的淸洗空氣的出口溫度接近事先 求取的淸洗空氣的出口溫度的目標溫度（圖7線β：最適當 風量的溫度）來控制淸洗風量亦可。如此一來，能降低比 習知還低的淸洗風量，且隨之亦能降低排氣風量、輸入外 面空氣的釐，可提高比習知還高的省能源性。 又，對於以溫度偵測器64所檢測出的淸洗空氣的出口 溫度來控制淸洗風量，而使用於圖1所示之二段式乾式除濕 系統時，調整氣門D4的開度或以反相器控制設於淸洗系統 上的淸洗風扇65 (例如反相器控制淸洗風扇65的發動機） 來進行均可。 在低露點空間R內，使用成爲鋰2次電池之電解液的碳 酸二甲酯和碳酸甲。乙酯的碳酸酯系有機溶劑時，由於碳 酸二甲酯和碳酸甲。乙酯的沸點比較低（碳酸二甲酯爲90 °C，碳酸甲。乙酯爲l〇7°C )，因此即使常温也會擴散產生 臭氣。但是若使用在上述實施型態上之乾式除濕裝置1〇所 使用主成份爲金屬矽酸鹽之轉子11的吸濕材料和矽凝膠， 則不僅除濕，而且同時也能獲得較佳的脫臭功能，可較佳 地除去上述臭氣。也就是包含流經回流空氣進氣管道6之臭 氣的空氣，在導入預冷器8後被冷卻，該被冷卻的混合空氣 在導入第二段的乾式除濕裝置10之轉子11的除濕區域lla 內後進行除濕處理的同時也被進行脫臭處理。此外，經由 淸洗系回流空氣進氣管道23來通過淸洗區域1。時，也被進 行脫臭處理。在再生系統上’例如由於加熱至12〇〇C的高 20 用中國國家標準（CNS ) Λ4規格（2丨OX_297公梦.) ' - ^7 =?-· HH — :1-·- n l#an ^^^^1 · (請先閲讀背面之注意事項再填寫本頁) 訂-- B7 B7 經濟部中央標準局員工消f合作社印製 五、發明説明（） 溫，因此能讓因脫臭而吸附於轉子上的有機溶劑在再生系 統上完全地從轉子去蒸發。故能連續地除去有機溶劑。而 且由於第二段的乾式除濕裝置1〇之轉子11使用以砍凝膠或 金屬矽酸鹽爲主成份的吸濕材料，因此轉子11的壽命變 長，該轉子可不用更換，預計能降低鋰2次電池等的製造成 本。 (第2實施型態） 以下，以圖9來說明有關第2實施型態的除濕系統。圖9 是脫臭防濕裝置的構成圖，該實施型態是作爲鋰2次電池等 製造線路之容納室和供給低露點空熱至园繞該谷納室成爲 作業場的圍繞室之狀態。在容納室裡簡易型的潔淨室裝置 和氣流室等裝置（無圖示）並列於圖的垂直方向。 和輸入外面空氣進氣管道101連接的第1除濕機158，經 由送氣進氣管道105和第2除濕機160連接。該第1除濕機158 至少需具備上述第1實施型態上第一段的乾式除濕裝置5和 處理外面空氣之冷卻器，第2除濕機160至少需具備第1實施 型態上第二段的乾式除濕裝置10的轉子11、預冷器8、加熱 器21和後冷卻器22。當然從輸入外面空氣進氣管道101至後 冷卻器22的送氣系和從回流空氣進氣管道6至第一段的乾 式除濕裝置5的排氣系，以及第二段的乾式除濕裝置1〇的淸 洗系統等，可採用和第1實施型態相同的構成。 在送氣進氣管道105上，在其上游設置外面空氣處理風 扇113和氣門D11。第2除濕機160連接和圍繞室162相通的 回流空氣進氣管道125。圍繞室162其內部收納有容納室 21 J—J------© — (請先間讀背面之注意事項再填寫本頁) 訂 -----蟲了. 本紙張尺度適州中K國家榡莩（CNS )八4规格（2丨〇乂 297公筇) 經濟部中央標隼局負工消費合作社印製 Λ7 B7 , 五、發明説明（） 157，爲鋰2次電池等的製造作業空間。 在該回流空氣進氣管道125上，在其上游設置處理風扇 1 ιΥ爾鬥丽醜——®莉國機τ爾流圃麵空氣— 和從回流空氣進氣管道125所導入的空氣，在第2除濕機160 上進行除濕處理和脫臭處理。 第2除濕機160和連通容納室157的送氣進氣管道159相 連接。容納室157爲半封閉的空間，該室的下方爲開放式(無 圖示），圍繞室162和容納室157互通。在容納室157內製造 鋰2次電池等，在該鋰2次電池等的製造過程上使用成爲電 解液的碳酸二甲酯和碳酸甲。乙酯（臭氣物質）。 因此，利用提高容納室157內的氣壓比圍繞室162內的 氣壓還高，將由送氣進氣管道159所送來的空氣，包含容納 室157內的臭氣之空氣排出圍繞室162。 在送氣進氣管道159上方設置送氣風扇161和氣門D13 以及無圖示的ΗΡΑ過濾器等空氣淨化裝置。即空氣供給系 是由送氣進氣管道159、送氣風扇161、氣門D13以及空氣 淨化裝置所構成。 .. 送氣風扇161和氣門D13之間的送氣進氣管道159和連 通圍繞室162之圍繞室用的送氣進氣管道163連接。該圍繞 室用的送氣進氣管道163在其途中分歧爲兩邊.，一邊爲圍繞 室用的送氣進氣管道163a，經由過濾器單元165和圍繞室 162—方的上面連接，此外另一邊爲圍繞室用的送氣進氣管 道163b，經由過濾器單元165和圍繞室162另一方的上面連 接。 22 (請先閱讀背面之注意事項再填寫本頁) 訂 -----^^1. 本紙張尺度適,:丨1中國阑家標準（)八4規格（210/2叼公^^ ' 經濟部中央標隼局員工消费合作社印製 A7 B7 五、發明説明（) 在圍繞室用的送氣進氣管道163a、163b上各設置氣門 D14、D15。因此由調整氣門D13、D14、D15可調整送氣至 容納室157和圍繞室162的空氣流量。即循環系是由送氣進 氣管道159、送氣風扇161、和氣門D13及圍繞室用的送氣 進氣管道163、氣門D14、氣門D15、過濾器單元165、165、 回流空氣進氣管道125和處理風扇117、氣門D12所構成。 排出風扇167的設置是和第1實施型態相同。 以下說明有關第2實施型態的作用。被處理外面空氣風 扇113所吸引進來的外面空氣經由外面空氣抽入進氣管道 101通過第1除濕機來進行除濕。該除濕空氣被送氣風扇161 所吸引，經由送氣進氣管道105被送入第2除濕機160進行除 濕。和此同時，圍繞室162內的混合空氣被處理風扇117所 吸引之同時，亦被送氣風扇161所吸弓晒經由回流空氣進氣 管道125被導入第2除濕機160內來同時進行除濕處理和脫 臭處理。 被除濕之後的外面空氣和被除濕且進行脫臭處理之圍 繞室162內的混合空氣被送氣風扇161所吸引，進入第2除濕 機160內進行除濕。脫臭後，經由送氣進氣管道159送氣至 容納室157內。此外，該空氣通過圍繞室用的送氣進氣管道 163a、163b後經由過濾器單元165、165也送氣至圍繞室162 內。 容納室157是由比圍繞室162還局的局壓所構成’如下 所述。送氣至容納室157內的空氣流量和送氣至圍繞室162 內的空氣流量是由氣門D13、D14、D15來調整，亦可將送 23 本紙張尺度適;fl中冢標率（（_NS ) Λ4現格（2丨0〆》7公漦） n u n n (請先閱讀背面之注意事碩再填寫本頁) 訂 Φ. 經濟部中央標準局員工消費合作社印掣 A7 _ ___ B7 . 五、發明説明（） 氣至容納室157內的混合空氣流量調整成比送氣至圍繞室 162的空氣流量還多。此外，若讓容納室157的容積小於圍 繞室162的容積，且讓送氣至容納室157內的空氣體積（流 量）和送氣至圍繞室162內的空氣體積（流量）相同，則溫 度在一定的條件下，根據波義耳定律，容積小的容納室157 內的氣壓經常比容積大的圍繞室162內的氣壓還來的高 壓。考慮從排氣進氣管道166所排出的排出量來調整氣門 D13、D14、D15。 如上所述，由於經常是比圍繞室162還高的氣壓來構成 容納室157內的氣壓，因此包含從作業人的人體所發出的濕 氣之圍繞室162內的空氣不流入討厭濕氣的容納室157內。 又，爲了調整容納室157內的氣壓，亦能以排出風扇167的 翼輪之旋轉次數來作爲控制的要素。 被送至容納室15 7內的空氣和在容納室15 7內氣化之碳 酸二甲酯和碳酸甲。乙酯等的臭氣物質混合成爲混合空 氣，靠近惡臭產生處的空氣被排氣風扇167吸引，通過排氣 進氣管道166被排出圍繞室162的外部。 此外，剩餘的混合空氣，從容納室157開放的下方流出 .進入氣壓低的圍繞室162內。該流出的混合空氣擴散至圍繞 室162內和圍繞室162內的空氣混合。該混合空氣被處理風 扇117所吸引，通過回流空氣進氣管道125後被導入第2除濕 機160內。然後該混合空氣由第2除濕機來進行除濕處理的 同時亦進行脫臭處理。因此容納室157內的空氣可經常維持 乾燥的狀態且能脫臭。因此，在討厭水分的鋰2次電池等的 24 (請先閱讀背面之注意事項再填寫本頁)— ----------- I V. Description of the invention () c, d and the line e, f that divides the washing area 201c3 into halves, and is near the end face of the rotor 201 (distance from the rotor Where the end surface of 201 is 50 mm), a temperature detector (not shown) is provided, and the positions marked with symbols on the above lines are shown in FIG. 6 to change the air volume passing through the dehumidification area 201a to the air volume passing through the regeneration area 201b. The temperature detector investigates the temperature distribution of the measurement points measured on the lines a, b, c, d, e, and f. As a result, the characteristics shown in the graph of FIG. 7 were obtained. In the same chart, the most appropriate air volume is the air volume passing through the dehumidification area 201a, that is, the air volume passing through the regeneration area 201b relative to the processing air volume, which means that when the ratio of the regeneration air volume is 0.2, the so-called excessive air volume means that When the year-on-year is 0.4, the so-called air volume is too small when the year-on-year is 0.15. As described above, at the measurement point on the line 20d of the regeneration area, the temperature becomes higher when the dehumidification load is small, and becomes lower when the dehumidification load is large. Therefore, the temperature (target temperature) at which the most appropriate air volume at d is obtained in advance, and the regeneration air volume is controlled close to the target temperature, thereby obtaining the most appropriate regeneration air volume. Similarly, in the scrubbing area 201c, the temperature characteristics at the online measurement points are decreased in the order of excessively small air volume, optimum air volume, and excessive air volume. Therefore, by obtaining the temperature (target temperature) at the most appropriate air volume at f in advance, and controlling the scrub air volume close to the target temperature, the most appropriate scrub air volume can be obtained. '' As mentioned above, by setting a temperature detector at a predetermined place to control the measured regeneration outlet temperature and the scrubbing outlet temperature to be close to the target temperature, the necessary operation can be performed without excessive air volume. The dry dehumidifier 60 shown in Fig. 8 is designed to control the above-mentioned outlet temperature. The paper size is applicable to the Chinese net home standard CNS) 8 4 験 (2UVX 297 mm) (Please read the precautions on the back before filling this page)- -L ------. Ordered by the Consumer Standards Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Β7 _ ^ _ V. Description of Invention () " Close to the target temperature to try to save energy. That is, the air passage area in the small chamber 62 located on the end face of the rotor 61 of the dry dehumidification device 60 is divided into a dehumidification area 61a, a regeneration area 61b, Rinse area 61c3 areas. However, the area ratio of each region is set to be the same as the area ratio on the conventional dry-type dehumidifier 200 shown in Figs. Then, from the end face of the rotor 61 on the regeneration area 61b in the cell 62, a temperature detector 63 for detecting the outlet temperature of the regeneration air is installed at a distance of about 50 mm in the axial direction and close to the washing area 61c. The constructed dry dehumidifier 60 can replace the dry dehumidifier 10 related to the above embodiment, and can be used in the two-stage dry dehumidifier system shown in FIG. 1. At this time, the temperature detected by the temperature detector 63 is brought close to the target temperature obtained in advance (the temperature of the most appropriate air volume in line d in FIG. 7), and the inverter controls the regeneration fan 26 (for example, the engine of the regeneration fan 26). (Inverter control) to adjust the regeneration air volume, or control the opening of valve D5 to adjust the regeneration air volume, you can get the most appropriate regeneration air volume. Therefore, it is possible to save the heat energy required for regeneration. In addition, it is possible to save energy by exhaust air volume and outside air introduction volume. Furthermore, since the control described above is performed using the temperature detected by the temperature detector 63, the control is easy and the response is good. Because it is prevented from producing too much air volume, the energy saving effect is higher than the conventional one. The above-mentioned dry dehumidifier 60 performs the above-mentioned control based on the outlet temperature of the regeneration air detected by the temperature detector 63 provided in the regeneration area. However, as shown in FIG. 8, the dehumidification area is close to the dehumidification area 61c. Floor 19a of 61a This paper size applies to the Chinese National Chestnut (CNS) Λ4 specification (21〇y 297 cm) '--) " 二 -ΐ—mm ·-1 t ^ l III-In ·! (Please (Please read the notes on the back before filling in this page) Order-A7 issued by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs ------------ B7 _ ^ ___ V. Description of the invention () The outlet is set to detect the cleaned air The temperature temperature detector 64 allows the outlet temperature of the scrubbing air detected by the temperature detector 64 to be close to the target temperature of the outlet temperature of the scrubbing air obtained in advance (line β in FIG. 7: Temperature) to control the amount of air. In this way, the amount of scrubbing air that is lower than the conventional one can be reduced, and the exhaust air volume can also be reduced, and the amount of input air can be reduced, which can improve the energy saving performance higher than the conventional one. In addition, the outlet air temperature of the scrubbing air detected by the temperature detector 64 is used to control the amount of scrubbing air. When it is used in the two-stage dry dehumidification system shown in FIG. 1, the opening degree of the valve D4 is adjusted or reversed. The phaser controls the cleaning fan 65 provided on the cleaning system (for example, the inverter controls the engine of the cleaning fan 65). In the low-dew-point space R, dimethyl carbonate and methyl carbonate, which are electrolytes of a lithium secondary battery, are used. In the case of ethyl carbonate-based organic solvents, dimethyl carbonate and methyl carbonate are used. Ethyl ester has a relatively low boiling point (90 ° C for dimethyl carbonate, and methyl carbonate. 107 ° C for ethyl ester), so it will diffuse and generate odor even at normal temperature. However, if the moisture-absorbing material and silicone gel whose main components are the metal silicate rotor 11 used in the dry dehumidification device 10 in the above embodiment type, not only dehumidification, but also a better deodorization can be obtained. The function can better remove the above-mentioned odor. That is, the air containing the odor flowing through the return air inlet duct 6 is cooled after being introduced into the precooler 8, and the cooled mixed air is introduced into the dehumidification area 11a of the rotor 11 of the dry dehumidifier 10 of the second stage. The inside and after dehumidification treatments are also deodorized. In addition, it passes through the rinsing area 1 via the rinsing system return air intake duct 23. It is also deodorized. On the regeneration system, for example, because it is heated to a high temperature of 120 ° C, it uses the Chinese National Standard (CNS) Λ4 specification (2 丨 OX_297 public dream.) '-^ 7 =?-· HH —: 1- ·-nl # an ^^^^ 1 · (Please read the notes on the back before filling out this page) Order-B7 B7 Printed by the staff of the Central Standards Bureau of the Ministry of Economic Affairs, F Cooperative, V. Invention Description () Warm, so it can deodorize The organic solvent adsorbed on the rotor is completely evaporated from the rotor on the regeneration system. Therefore, the organic solvent can be continuously removed. Moreover, since the rotor 11 of the second-stage dry dehumidifier 10 uses a hygroscopic material mainly composed of chopping gel or metal silicate, the life of the rotor 11 becomes longer, and the rotor can be replaced without replacement, which is expected to reduce lithium. Manufacturing costs for secondary batteries, etc. (Second Embodiment Mode) Hereinafter, a dehumidification system according to a second embodiment mode will be described with reference to FIG. 9. Fig. 9 is a configuration diagram of a deodorizing and moisture-proof device. This embodiment is a state in which a storage room for manufacturing circuits such as a lithium secondary battery and a low-dew-point air heat is supplied to the surrounding chamber to become a working room. In the storage room, simple clean room devices and airflow devices (not shown) are juxtaposed in the vertical direction of the figure. The first dehumidifier 158 connected to the input outside air intake duct 101 is connected to the second dehumidifier 160 via the air supply intake duct 105. The first dehumidifier 158 needs to have at least the dry dehumidifier 5 and the cooler for the outside air in the first stage of the first embodiment, and the second dehumidifier 160 needs to have at least the second stage in the first embodiment. The rotor 11, the pre-cooler 8, the heater 21 and the after-cooler 22 of the dry dehumidifier 10. Of course, the air supply system from the input air intake duct 101 to the aftercooler 22 and the return air intake duct 6 to the exhaust system of the dry dehumidifier 5 of the first stage, and the dry dehumidifier 10 of the second stage The washing system and the like may have the same configuration as the first embodiment. The air intake duct 105 is provided with an outside air processing fan 113 and a valve D11 upstream of the air intake duct 105. The second dehumidifier 160 is connected to a return air intake duct 125 communicating with the surrounding chamber 162. The surrounding room 162 contains a accommodating room 21 J—J ------ © — (Please read the precautions on the back before filling out this page) Order ----- worm. K Country (CNS) 8-4 specification (2 丨 〇 乂 297 筇) Printed by Λ7 B7 of the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. 5. Description of the invention () 157, for the manufacture of lithium secondary batteries, etc. Job space. On the return air intake duct 125, a processing fan 1 Υ 斗 斗 Dou Li — 莉 Li Guoji τ Erliu surface air — and the air introduced from the return air intake duct 125 are provided upstream. 2 The dehumidifier 160 performs a dehumidifying process and a deodorizing process. The second dehumidifier 160 is connected to an air intake duct 159 communicating with the storage chamber 157. The accommodating chamber 157 is a semi-closed space. The lower part of the accommodating chamber 157 is open (not shown), and communicates with the surrounding chamber 162 and the accommodating chamber 157. A lithium secondary battery and the like are manufactured in the storage chamber 157, and dimethyl carbonate and methyl carbonate which are electrolytes are used in the manufacturing process of the lithium secondary battery and the like. Ethyl esters (odorous substances). Therefore, by raising the air pressure in the containing chamber 157 to be higher than the air pressure in the surrounding chamber 162, the air sent from the air supply duct 159, including the odorous air in the containing chamber 157, is discharged from the surrounding chamber 162. An air purification device such as an air supply fan 161, a valve D13, and a HPA filter (not shown) is provided above the air supply duct 159. That is, the air supply system is composed of an air supply duct 159, an air supply fan 161, a valve D13, and an air purification device. The air-intake duct 159 between the air-supply fan 161 and the valve D13 is connected to the air-intake duct 163 for the surrounding chamber that communicates with the surrounding chamber 162. The air inlet duct 163 for the surrounding room is divided into two sides on the way. One side is the air inlet duct 163a for the surrounding room, which is connected to the upper side of the surrounding room 162 via the filter unit 165, and the other side is surrounded by The air intake duct 163b for the chamber is connected to the other upper surface surrounding the chamber 162 via the filter unit 165. 22 (Please read the precautions on the back before filling this page) Order ----- ^^ 1. This paper is of suitable size: 丨 1 Chinese standard () 8 specifications (210/2 叼 public ^^ ' Printed by the Consumers' Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 B7 V. Description of the invention () The valves D14 and D15 are set on the air inlet ducts 163a and 163b for the surrounding room. Air flow to the accommodating chamber 157 and the surrounding chamber 162. That is, the circulation system is composed of the air inlet duct 159, the air fan 161, and the valve D13, and the air inlet duct 163, the valve D14, the valve D15, and the filter for the surrounding chamber. The units 165, 165, the return air intake duct 125, the processing fan 117, and the valve D12 are configured. The setting of the exhaust fan 167 is the same as that of the first embodiment. The function of the second embodiment is described below. The outside air sucked in by the fan 113 is sucked into the intake duct 101 through the outside air and dehumidified by the first dehumidifier. The dehumidified air is attracted by the air-supply fan 161 and is sent to the second dehumidifier 160 via the air-supply intake duct 105. Dehumidify. And this At the same time, while the mixed air in the surrounding chamber 162 is attracted by the processing fan 117, it is also sucked by the exhaust fan 161 and is introduced into the second dehumidifier 160 through the return air intake duct 125 to perform dehumidification and deodorization at the same time. The outside air after dehumidification and the mixed air in the surrounding chamber 162 that has been dehumidified and deodorized are attracted by the air supply fan 161 and enter the second dehumidifier 160 for dehumidification. After deodorization, the air is sent through the air inlet duct 159 bleeds air into the accommodating chamber 157. In addition, the air passes through the air inlet ducts 163a and 163b for the perimeter chamber and is also evacuated to the perimeter chamber 162 through the filter units 165 and 165. The accommodating chamber 157 is more rigid than the perimeter chamber 162 The pressure formed by the local pressure is as follows. The air flow rate of the air supply to the accommodating chamber 157 and the air flow rate of the air supply to the surrounding chamber 162 are adjusted by the valves D13, D14, and D15. 23 paper sizes can also be sent; fl Nakazuka standard rate ((_NS) Λ4 present grid (2 丨 0〆> 7gong) nunn (Please read the note on the back before filling in this page) Order Φ. Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 _ ___ B7. V. Description of the invention () The flow rate of the mixed air from the air to the containing chamber 157 is adjusted to be greater than the air flow to the surrounding chamber 162. In addition, if the volume of the containing chamber 157 is smaller than the volume of the surrounding chamber 162 , And let the volume of air (flow) that is fed into the containing chamber 157 and the volume of air (flow) that is fed into the surrounding chamber 162 be the same, then under certain conditions, according to Boyle's law, the small volume of the storage chamber 157 The air pressure inside is often higher than the air pressure in the surrounding chamber 162 having a large volume. The valves D13, D14, and D15 are adjusted in consideration of the discharge amount discharged from the exhaust intake duct 166. As described above, since the air pressure in the accommodating chamber 157 is often higher than that of the surrounding chamber 162, the air in the surrounding chamber 162 containing moisture emitted from the human body of the operator does not flow into the accommodating humidity chamber. Room 157. In addition, in order to adjust the air pressure in the accommodating chamber 157, the number of rotations of the wing wheel of the exhaust fan 167 can also be used as a control element. The air sent to the containing chamber 15 7 and the dimethyl carbonate and methyl carbonate vaporized in the containing chamber 15 7. An odorous substance such as ethyl ester is mixed to form mixed air, and the air near the place where the malodor is generated is sucked by the exhaust fan 167, and is exhausted outside the surrounding chamber 162 through the exhaust air intake duct 166. In addition, the remaining mixed air flows out from below the opening of the containing chamber 157 and enters the surrounding chamber 162 having a low air pressure. The outflowing mixed air is diffused into the surrounding chamber 162 and mixed with the air in the surrounding chamber 162. This mixed air is attracted by the processing fan 117, passes through the return air intake duct 125, and is introduced into the second dehumidifier 160. The mixed air is then dehumidified by a second dehumidifier, and deodorized. Therefore, the air in the accommodating chamber 157 can always be kept dry and deodorized. Therefore, in lithium secondary batteries that hate moisture, etc. 24 (Please read the precautions on the back before filling out this page)
本紙張尺度適用中阐國家標準（) A4現格（2丨0 , 公漦） A7 A7 經濟部中央標隼局員工消f合作社印製 五、發明説明（） 製造上，能讓製品的使用原料比例降低，實現低廉的製造 成本。 此外，在圍繞室162裡，由於能防止臭氣的脫臭和濕氣 的增加，因此能經常提供好條件的作業性環境。在第2實施 型態上，和有機化合物全體的除去率爲82.3%相較，碳酸二 甲酯爲93.6%、碳酸甲。乙酯爲94.6%，更能獲得非常大得 除去率。 發明的效果 根據本發明可降低比習知的同種乾式除濕裝置運轉所 需還低的能源，而且亦可將以送風機爲首的各種設備機器 小型化。甚至除濕的同時可不用替換轉子來脫臭。而且由 於在圍繞室內可防止脫臭和濕度的增加，因此能讓圍繞室 內成爲良好條件的作業性環境。 (請先閱讀背面之注意事項再填寫本頁)National standards for this paper are applicable (A4) (2 丨 0, public) A7 A7 Printed by the staff of the Central Bureau of Standards of the Ministry of Economic Affairs and printed by the cooperative V. Invention description () In manufacturing, raw materials for products can be used The proportion is reduced, and low manufacturing costs are realized. In addition, in the surrounding chamber 162, deodorization of odor and increase of moisture can be prevented, so that a good working environment can always be provided. In the second embodiment, the removal rate of the whole organic compound is 82.3%, the dimethyl carbonate is 93.6%, and the methyl carbonate is 93.6%. The ethyl ester was 94.6%, and a very large removal rate was obtained. Effects of the Invention According to the present invention, it is possible to reduce the energy required to operate the conventional dry dehumidifier of the same type, and to reduce the size of various equipment including a blower. Even dehumidification can be done without replacing the rotor to deodorize. In addition, since deodorization and humidity increase can be prevented in the surrounding room, the surrounding room can be made into a good working environment. (Please read the notes on the back before filling this page)
本纸張尺度適用中國國家掠準（CNS ) Λ4規格（ΉΟ/ 297公漦）This paper size is applicable to China National Graduation Standard (CNS) Λ4 specification (ΉΟ / 297 公 漦)