經濟部中央橾準局員工消費合作社印製 Α7 Β7 五、發明説明（1 ) 【商業上之利用領域】 本發明係爲有關固形有機廢棄物之處理裝置*特別是 關於有效的發酵處理廚房殘渣（易腐垃圾）、餐應等的都 市垃圾、再生物等的固形有機廢棄物，且可以廣範的適用 於家庭用、業務用、公共用的固形有機廢棄物之處理裝置 【先行技術】 過去，農產廢棄物或下水道污泥等的固形有機廢棄物 之混合化，由於大部分未稹極的管理維持長時間堆稹野外 的狀態，因而以自然發酵的方式進行。但是，近年，固形 有機廢棄物的良好發酵處理，即是關於堆肥化（混合化） 的技術，開始重新檢討無公害的處理方法，作爲廢棄物再 利用技術及能自然還元的技術》 特別是關於蔚房殘渣即謂易腐垃圾，隨著須要大量剩 飯的畜產業改變爲合成飼料等，期予開發在解決掉臭氣污 染且高速、髙分解下可以發酵之處理裝置。 對於此點，用發酵裝置攪拌、或是部分的管理酵素供 給而將發酵髙速化之技術，例如在日本專利特開昭5 5 -121992號公報、特開昭57-160986號公報 、特開昭5 7 — 1 70 1 8 3號公報、特開昭6 Ο-ΐ 3 1 888 號公報 、特開平 1-1 45 388 號公報等 ，已被公示。 本紙張尺度適用中國囷家橾準（CNS ) Α4規格（210X297公釐） |( ·批衣 I 訂 {.^ (請先閱讀背面之注意事項再填寫本頁) A7 292981 __B7 五、發明説明（2 ) 【發明所欲解決之課題】 (請先閲讀背面之注意事項再填寫本f ) 在於上述所公示的處理裝置，經長期的處理使用，改 變了槽內容物的通氣性或水分保持性等的物理性質而降低 發酵性能，爲了補足所降下的發酵性能，必須定期的全部 交換基材或是隨時追加投入新鮮機材。 【用以解決課題之手段】 使其有效的發酵而處理本專利發明的固形有機廢棄物 之處理裝置，係爲進行基材的攪抨、及攪拌及（或是）破碎 •發酵被處理物之發酵槽、及進行基材的攬拌、及被處理 物的攪拌及（或是）破碎、多餘水分的除去（乾燥）之基材 再生槽，相鄰的配設的同時，基材及處理物的一部分基本 上具備循環發酵槽與基材再生槽間之構成。 【作用】 經濟部中央樣準局員工消費合作社印装 在預先裝入基材的發酵槽內投入固形有機廢棄物，則 隨著攬拌軸的回轉而在固形有機廢棄物混合基材，在攪泮 時，進行對固形有機廢棄物、及附著在固形有機廢棄物的 發酵菌供給空氣。爲了短縮時間，所以將上述基材與發酵 菌一起預先裝入發酵槽內· 發酵槽內處理物的一部分，由於攪拌腕的上推，通過 連絡部而流入至與發酵槽並列所配設的基材再生槽內。處 理物係以攪拌腕攪拌同時移動基材再生槽內，通過連絡部 而從基材再生槽落下，再度回到發酵槽內，由於返復此環 本紙張尺度適用中國困家樑準（CNS ) A4規格（210X297公釐） 5 A7 292981 _ B7 五、發明説明（3 ) 環，因而被處理物產生堆肥化反應且被小顆粒化。 (請先閱讀背面之注意事項再填寫本頁} 所被小顆粒化的處理物被堆積成一定程度以上，則從 被設在基材再生槽的一端之排出口排出所被小顆粒化處理 物的一部分，被貯存在設在處理裝置內的貯存裝置內部。 【實施例】 <第1實施例> 參照圖面說明本發明的實施例。第1圖係靥在本發明 的處理裝置的筐體上部所剖面的上面圇（第2圚的I一I 斷面圖），第2圖係爲第1圖所示本發明的處理裝置之Π -Π斷面圖，第3圖係爲第1圖所示的瓜— HI斷面圓。 處理裝置係爲在筐體5 0內配設發酵槽1與基材再生 槽1 5、及驅動手段等。 經濟部中央標準局員工消费合作社印製 在發酵槽1，其中心部貫通而被配設有第1攪拌軸2 。在此第1搅拌軸2，以所定間隔具有複數個呈放射狀的 被突出設置、固定有用以攪拌或是破碎固形有機廢棄物之 攪拌腕3。在貫通攪拌軸2的發酵槽1的一端部，被固定 有大鏈輪4，介由鏈條5、小鏈輪6而自由回轉的被連結 在驅動用馬達7。 在發酵檜7的底部外壁被配設有加熱器（未圖示）作 爲加熱手段•然且，被投入至發酵槽1內的剩飯、易腐垃 圾、其他的固形有機廢棄物，被保持在能有效而完全發酵 的溫度·在發酵槽1上部的筐體5 0設置固形有機廢棄物 本紙張尺度逋用中國國家標準（CNS > Α4規格（210Χ297公釐） A7 _B7 五、發明説明（4 ) 的投入口 8 ，且自由開關的配設投入口開關門5 5。 另外，在發酵槽1內的底部，預先以所定量充填基材 及發酵菌。進而，正交於第1攪拌軸2而配設隔開發酵槽 1內的分割板2 5。 分割發酵槽1的分割板2 5係爲將高度尺寸設爲基材 再生槽1 5之邊側較高的髙壁部2 5 b，從攪拌軸至發賭 槽1的側壁邊側形成較低的低壁部2 5 a。發酵槽1內的 基材及被處理物係爲從分割板2 5的較低側壁部2 5 a移 動。 在發酵槽1的上部且不干涉到回轉的攪拌腕之位置， 配設吸入在發酵槽1內所發生的水蒸氣之吸入口 9。在此 吸入口 9連結吸入管1 0，吸入管1 0的他端被連結至配 設在處理槽外部的除濕裝置11。 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) 除濕裝置1係以複數個導管所構成，介由上述管1 0 發酵槽1內的水蒸氣被導引至此導管1 1 a內。對應於該 除濕裝置，具備爲了將外氣吹著到導管1 0而使其冷郤凝 縮被導引至導管1 1 a內的水蒸氣之送風風扇1 2，將處 理槽內的蒸氣使其循環在除濕裝置11內之循環風扇13 ，及爲了將凝縮水排出至裝置外的排水導管14等。13 a係爲循環風扇1 3的*8動用馬達。 並列於發酵槽1而配設基材再生槽15· 基材再生槽15係爲在其中心部配設攪拌軸（第2攪 拌軸）1 6 ·基材再生槽1 5的第2攪拌軸1 6係爲幾乎 平行於發酵槽1的第2攪拌軸2，配設位置係爲與第1攪 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） 292981 A7 B7 經濟部中央樣準局員工消资合作社印製 五、發明説明（5 ) 拌軸同高，或是配設在比第1攬拌軸2還稍高的位置。在 第2攪拌軸1 6，以所定間隔多數條呈放射狀被突出設置 ，固定爲了施予在發酵槽1所處理形成爲塊狀物的處理物 之小顆粒化。在此第2攪拌軸16固定攪拌腕17之所定 間隔，係爲比第1攪拌軸2的攪拌腕3之所定間隔還小。 由於此因，在發酵槽1所處理而形成爲塊狀物之處理物就 是在基材再生槽1 5變小顆粒化，也能以攪拌腕1 7移送 〇 在貫通第2攪拌軸19的基材再生槽15之一端部， 被固定有小鏈輪1 8、介由鏈條1 9、小鏈輪2 0而被連 結至發酵槽1的驅動用馬達7。即是基材再生槽1 5的第 2攪拌軸16及發酵槽1的第1攪拌軸2，係以同一驅動 用馬達7而被回轉驅動。 2 1係爲排出简，將基材再生槽1 5內所處理終了的 處理物排出至貯存裝置。在基材再生槽1 5的外壁被配設 有作爲加熱手段的加熱器2 2。 基材再生槽15的攪拌腕17回轉直徑被形成爲比發 醏槽1的攪拌腕3回轉直徑還短。然且，各槽1、1 5的 底面係爲沿著攪拌腕3、1 7的回轉軌道而被形成。即是 發酵槽1的底面形成爲半徑幾乎是攪拌腕3的長度尺寸作 爲半徑尺寸之圖弧狀，基材再生槽15的底面形成爲攪拌 腕1 7的長度尺寸作爲半徑尺寸之園弧狀。並列而連接發 醏槽1與基材再生槽1 5時，在基材再生槽1 5的下部被 形成有空間6 0。 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） 111 n I I ( ·裝 I I jf··^ (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局貝工消費合作社印裝 A7 ___B7 _ 五、發明説明（6 ) 在發酵槽1與基材再生槽1 5的境界部被配設有軸方 向兩端2 7 a較低中央部分2 7 b較髙的隔間構件2 7。 第4圇係爲表示在第1圖從箭頭7方向直視的隔間構 件2 7之部分斷面圇，第5圖係爲表示在第1圖從箭頭Q 方向直視的分割板2 5之部分斷面圖。 分割發酵槽1與基材再生槽1 5的隔間構件2 7，其 隔間構件2 7的高度尺寸被形成爲在基材再生槽1 5的軸 方向兩端2 7 a較低，中央部分2 7b較高。然且裝置內 的基材及處理物通過隔間構件2 7的較低的低壁部2 7 a 以其爲連結，進行從發酵槽1移動至基材再生槽1 5、及 從再生槽1 5循環至發酵槽1。 然且，流入至基材再生槽1 5內的基材及處理物，以 第3圇所示的加熱器2 2加熱後除去而乾燥剩餘水分的同 時，以攪拌腕1 7而成爲塊狀物的處理物被小顆粒化，基 材被再生爲原來的通氣性或水分保持性的良好狀態。 第6圖係爲表示基材再生槽1 5的第2攬拌軸1 6及 攪拌腕1 7之斜視圆，攬拌腕1 7係爲以第2攪拌軸1 6 的回轉方向或是其相反的方向依順毎隔一定的角度偏離而 安裝所鄰接的攬拌腕17·被處理物係被運送至依順而被 配設的攪拌腕17而往下流側移動。 第7圓係爲第2圖的νπ — ΥΙΙ斷面匾* 在基材再生槽1 5的側壁。穿孔排出處理物的排出口 2 3的同時，貯存所被排出的處理物之貯存裝置2 4被設 在處理裝置的筐體5 0內•成爲腐蝕質的處理物係被導引 本紙張尺度逋用中國國家標準（CNS ) Α4規格（210X297公釐） --------^.裝-----——訂~.-----f沐 (請先閱讀背面之注意事項再填寫本頁) —9 — A7 B7 經濟部中央標準局員工消費合作社印製 五、 發明説明 7 ) 1 至 排 出 筒 2 1 而 貯 存 在 貯 存 裝 置 2 4 〇 1 1 在 於 以 此 所 構 成 的 處 理 裝 置 發 酵 槽 1 與 基 材 再 生 槽 1 1 5 的 容 量 比 如 下 所 決 定 y—v 1 1 請 1 I 發 酵槽 1 的 容 量 R 1 = ( 攪 拌 腕 3 的 回 轉直 徑 ) 2 先 閱 1 I 1 1 X 攪 拌 軸 2 的 長 度 ( 槽 長 度 ) 背 ιέ 1 1 基 材 再 生 槽 1 5 的 容 量 R 1 5 = ( 攪 拌 腕 1 7 的 回 注 意 1 I 事 1 轉 直 徑 ) 2x攪拌軸] L 6的長度 (槽長度） 項 再 1 填 因 此 形 成 爲 R 1 R 1 5 1 0 0 3 0 • 3 寫 本 頁 裝 1 進 而 預 先 投 入 至 發 酵 槽 的 基 材 及 發 酵 菌 之 量 決 定 於 1 1 1 如 下 〇 1 ：1 若 將 處 理 裝 置 1 巨 的 固 形 有 機 廢 棄 物 最 大 處 理 重 量 設 訂 爲 1 時 則 基 材 及 發 酵 菌 的 全 重 置 成 爲 4 1 4 的 範 圍 內 '1 1 I 在 預 先 裝 入 1 巨 的 最 大 處 理 量 之 4 1 4 倍 的 基 材 及 1 ，.求 發 酵 菌 之 發 酵 槽 1 內 投 入 固 形 有 機 廢 棄 物 則 隨 著 第 1 攪 1 1 拌 軸 2 的 回 轉 而 以 攪 拌 腕 3 破 碎 固 形 有 機廢 棄 物 的 同 時 9 1 1 基 材 及 發 酵 菌 相 混 合 當 攪 拌腕 3 的 攪 拌 時 > 進 行 對 發 酵 1 1 菌 供 給 空 氣 0 在 固 形 有機 廢 棄 物 因 原 本 附 著 有發 酵菌 所 以 在 不 短 縮 發 酵 時 間 即 可 的 情 況 或 是 限 定 處 理 易 於 發 酵 | 的 固 形 有 機 廢 棄 物 的 情 況 不 須 將 發 酵 菌 預 先 裝 入 發 酵 槽 J 內 〇 1 I | 然 而 被 投 入 到 發 酵 槽 1 內 的 固 形 有機廢 棄 物 以 原 1 Ί 樣較大 型 亦 可 但欲於較短時 間 處 理 時 > 特 別 是 大型 的 固 1 1 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） -10 - A7 A7 經濟部中央標隼局貝工消费合作社印裝 _____B7_ 五、發明説明（8 ) 形有機廢棄物過多且欲於短時間內處理時，投入預先被細 小破碎的廢棄物，若是爲不破碎即可的狀態或者是不須要 過於粉碎時亦可。另外，若是將被投入至發酵槽1內的固 形有機廢棄物一定預先細小破碎後再投時，則可以減小第 1攬拌軸2與攪拌腕2的強度，同時可以使驅動用馬達縮 小输出· 進而，由於在發酵槽1設置電熱器等的手段加熱且保 溫基材及發酵菌，因而與所被投入的固形有機廢棄物自身 所具有的水分相結合：而發酵槽的水分、溫度、空氣滿足 了使其發酵的3要素，則開始發酵。 其次，在發酵及加熱的過程從固形有機廢棄物產生水 蒸氣。該水蒸氣由於循環風扇1 3 ，所以通過被連結在發 酵槽1的吸入導管9而被输送至設在槽外的除濕裝置（熱 交換裝置）1 1。進而，由於在熱交換裝置的導管1 1 a 內*以送風扇使其與低溫的外氣作熱交換，因而水蒸氣被 凝結而成液體，且從排水導管1 4排出裝置外。 發酵槽內被處理物的一部分，通過低壁部2 7 a流入 與發酵槽1並列配設的基材再生槽1 5內。所流入的被處 理物，係以攪拌腕1 7撹拌同時移動基材再生槽1 5內， 從基材再生槽1 5的低壁部2 7 a落下後再度回到發酵槽 1內*由於返復此動作，所以被處理物循環在發酵槽1與 基材再生槽1 5。 因在發酵槽1及基材再生槽1 5設有加熱手段，所以 被處理物循環同時在流動發酵槽1、基材再生槽15內之 本紙張尺度適用中國國家標準（CNS ) A4規格（21〇X297公釐） --------裝-- (請先閲讀背面之注意事項再填寫本f) 訂Printed Α7 Β7 by the Employee Consumer Cooperative of the Central Department of Economic Affairs of the Ministry of Economic Affairs 5. Description of the invention (1) [Commercial application] The present invention is a treatment device for solid organic waste * especially effective fermentation treatment of kitchen residues ( Perishable garbage), municipal solid waste such as meals, and regenerated solid organic waste, etc., and can be widely applied to household, business, and public solid organic waste treatment devices [Advanced Technology] In the past, The mixing of solid organic wastes such as agricultural wastes and sewage sludge is carried out by natural fermentation because most of the non-polluted management is maintained in the field for a long period of time. However, in recent years, the good fermentation treatment of solid organic waste, that is, the technology of composting (mixing), has begun to re-examine the pollution-free treatment methods, as waste recycling technology and technology that can naturally return to waste, especially regarding The residue of Weifang is called perishable garbage. As the livestock industry that requires a large amount of leftover rice is changed to synthetic feed, etc., it is expected to develop a treatment device that can ferment under high speed and high decomposition of odor pollution. In this regard, techniques for speeding up fermentation by stirring with a fermentation device or by partially managing the supply of enzymes are disclosed in, for example, Japanese Patent Laid-Open No. 5-5-121992, Japanese Patent Laid-Open No. 57-160986, and Japanese Unexamined Patent Publication. No. 5 7 — 1 70 1 8 No. 3, Japanese Unexamined Patent No. 6 O-1 3 1 888, No. 1 Japanese Patent No. 1-1 45 388, etc. have been announced. The size of this paper is applicable to China's National Standard (CNS) Α4 specification (210X297 mm) | (· Approval of clothing I order {. ^ (Please read the precautions on the back before filling in this page) A7 292981 __B7 V. Description of invention ( 2) [Problems to be solved by the invention] (Please read the precautions on the back before filling in this f) The treatment device disclosed above, after long-term treatment and use, has changed the aeration or moisture retention of the tank contents, etc. The physical properties of the product decrease the fermentation performance. In order to make up for the reduced fermentation performance, all the substrates must be exchanged regularly or fresh equipment should be added at any time. [Means to solve the problem] Effective fermentation and treatment of the patented invention The solid organic waste treatment device is used for stirring, stirring and / or crushing of the base material • Fermentation tank for fermentation of the processed material, and mixing of the base material, mixing of the processed material and ( Or) The base material regeneration tank for crushing and removal (drying) of excess water, while adjacently arranged, a part of the base material and the processed material are basically equipped with a circulating fermentation tank and a base material. The composition of the tank. [Function] The Employee's Consumer Cooperative of the Central Bureau of Samples of the Ministry of Economic Affairs prints solid organic waste in a fermentation tank preloaded with substrates, and then mixes with the solid organic waste as the mixing shaft rotates. When the substrate is stirred, air is supplied to the solid organic waste and the fermentation bacteria attached to the solid organic waste. In order to shorten the time, the above substrate and the fermentation bacteria are pre-loaded into the fermentation tank and fermentation tank A part of the internally processed product flows into the substrate regeneration tank arranged in parallel with the fermentation tank through the contact portion due to the upward movement of the stirring arm. The processing object is moved by the stirring arm while moving the substrate regeneration tank through the contact Partially fell from the base material regeneration tank, and returned to the fermentation tank again, due to the return of this ring paper size is suitable for China's sleepy home Liang Zhun (CNS) A4 specifications (210X297 mm) 5 A7 292981 _ B7 V. Description of invention ( 3) Ring, so the processed material will be composted and will be granulated. (Please read the precautions on the back before filling in this page) The processed materials that are granulated are stacked into one Above the level, a part of the processed material to be pelletized is discharged from the discharge port provided at one end of the base material regeneration tank and stored in the storage device provided in the processing device. [Examples] < First Implementation Example> An embodiment of the present invention will be described with reference to the drawings. FIG. 1 is the upper wall of the upper portion of the housing of the processing apparatus of the present invention (the I-I cross-sectional view of the second wall), FIG. 2 Fig. 1 is a Π-Π cross-sectional view of the treatment device of the present invention shown in Fig. 1, and Fig. 3 is a melon-HI cross-section circle shown in Fig. 1. The treatment device is a fermentation device arranged in a housing 50 The tank 1 and the base material regeneration tank 15 and the driving means, etc. The Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs is printed on the fermentation tank 1, the center of which passes through and is equipped with the first stirring shaft 2. Here, the first stirring shaft 2 has a plurality of radially arranged stirring arms 3 which are protrudingly arranged and fixed at a predetermined interval to stir or crush solid organic waste. At one end of the fermentation tank 1 penetrating the stirring shaft 2, a large sprocket 4 is fixed, and a drive motor 7 is connected to a sprocket 5 and a small sprocket 6 to freely rotate. A heater (not shown) is provided on the outer wall of the bottom of the fermentation juniper 7 as a heating means. However, leftover rice, perishable garbage, and other solid organic waste that are put into the fermentation tank 1 are kept in Temperature for effective and complete fermentation · Set solid organic waste in the upper casing 50 of the fermentation tank 1 This paper scale adopts the Chinese National Standard (CNS > Α4 specification (210Χ297mm) A7 _B7 V. Description of invention (4 ) Of the inlet 8 and the free opening and closing of the inlet opening and closing door 55. In addition, in the bottom of the fermentation tank 1, the base material and the fermentation bacteria are pre-filled with a predetermined amount. Furthermore, orthogonal to the first stirring shaft 2 In addition, a partition plate 25 that separates the fermentation tank 1 is provided. The partition plate 25 that partitions the fermentation tank 1 is a high wall portion 2 5 b with the height dimension set to be higher on the side of the base material regeneration tank 15. A lower wall portion 25 a is formed from the stirring shaft to the side of the side wall of the betting tank 1. The base material and the object to be treated in the fermentation tank 1 move from the lower wall portion 25 a of the dividing plate 25 It is located in the upper part of the fermentation tank 1 and does not interfere with the position of the rotating stirring arm. The suction port 9 of water vapor generated in 1. The suction port 9 is connected to the suction pipe 10, and the other end of the suction pipe 10 is connected to the dehumidifier 11 disposed outside the treatment tank. Employees of the Central Standards Bureau of the Ministry of Economic Affairs Printed by a consumer cooperative (please read the precautions on the back before filling in this page) The dehumidifier 1 is composed of a plurality of pipes, and the water vapor in the fermentation tank 1 is led to the pipe 1 1 a through the above pipe 10 Corresponding to this dehumidifier, a blower fan 12 is provided to blow outside air to the duct 10 to cool and condense the water vapor guided into the duct 1 1 a, and the steam in the treatment tank is made A circulation fan 13 circulating in the dehumidifier 11 and a drainage duct 14 for discharging condensed water to the outside of the device. 13a is a * 8 motor for circulation fan 13 3. It is arranged in parallel with the fermentation tank 1 Regeneration tank 15 · The base material regeneration tank 15 is equipped with a stirring shaft (second stirring shaft) 1 6 at its center. The second mixing shaft 16 of the base material regeneration tank 15 is almost parallel to the fermentation tank 1 The second agitating shaft 2 is arranged at the same position as the first agitating paper standard for China Standard (CNS) A4 specification (210X297mm) 292981 A7 B7 Printed by the Central Provincial Bureau of the Ministry of Economic Affairs Employee Consumer Cooperatives V. Invention description (5) The mixing shaft is at the same height, or it is arranged at the second mixing shaft 2 At a slightly higher position. On the second agitating shaft 16, a large number of strips are protrudingly arranged at a predetermined interval, and are fixed to give small particles of the processed material processed into a mass in the fermentation tank 1. The second stirring shaft 16 fixes the predetermined interval of the stirring arm 17, which is smaller than the predetermined interval of the stirring arm 3 of the first stirring axis 2. For this reason, the processing in the fermentation tank 1 forms a lump The material is reduced into particles in the base material regeneration tank 15 and can be transferred by the stirring arm 17. At one end of the base material regeneration tank 15 penetrating the second stirring shaft 19, a small sprocket 18 is fixed. The drive motor 7 of the fermentation tank 1 is connected to the chain 19 and the small sprocket 20. That is, the second stirring shaft 16 of the base material regeneration tank 15 and the first stirring shaft 2 of the fermentation tank 1 are rotatably driven by the same driving motor 7. 2 1 is for discharging, and the processed material processed in the base material regeneration tank 15 is discharged to the storage device. A heater 22 as a heating means is arranged on the outer wall of the base material regeneration tank 15. The rotation diameter of the stirring arm 17 of the base material regeneration tank 15 is formed to be shorter than the rotation diameter of the stirring arm 3 of the hair tank 1. However, the bottom surfaces of the grooves 1, 15 are formed along the orbits of the stirring arms 3, 17. That is, the bottom surface of the fermentation tank 1 is formed into a circular arc shape whose radius is almost the length dimension of the stirring arm 3 as the radius dimension, and the bottom surface of the base material regeneration tank 15 is formed into a circular arc shape with the length dimension of the stirring arm 17 as the radius dimension. When the hair growth tank 1 and the base material regeneration tank 15 are connected in parallel, a space 60 is formed in the lower part of the base material regeneration tank 15. This paper scale is applicable to China National Standard (CNS) A4 (210X297 mm) 111 n II (· installed II jf ·· ^ (please read the precautions on the back before filling in this page) Beigong Consumer Cooperative, Central Bureau of Standards, Ministry of Economic Affairs Printed A7 ___B7 _ V. Description of the invention (6) At the boundary between the fermentation tank 1 and the base material regeneration tank 15 are arranged two ends in the axial direction 2 7 a lower central part 2 7 b relatively high compartment 2 7. The fourth wall is a partial cross-sectional view of the partition member 2 7 viewed directly from the direction of arrow 7 in FIG. 1, and the fifth wall is a partition plate 2 5 viewed directly from the direction of arrow Q in FIG. Partial cross-sectional view. The partition member 27 of the fermentation tank 1 and the substrate regeneration tank 15 is divided, and the height dimension of the partition member 27 is formed at both ends of the substrate regeneration tank 15 in the axial direction 2 7 a is lower, and the central portion 27b is higher. However, the base material and the processed material in the device are connected through the lower low wall portion 2 7a of the compartment member 27, and are moved from the fermentation tank 1 to the base. Material regeneration tank 15 and the circulation from the regeneration tank 15 to the fermentation tank 1. However, the base material and the processed material flowing into the base material regeneration tank 15 are The heater 2 shown in Fig. 2 2 is removed after heating to dry the remaining moisture, while the agglomerate 17 is turned into a lump to make the processed material into small particles, and the base material is regenerated to the original air permeability or moisture retention Figure 6 is the squint circle showing the second stirring shaft 16 and the stirring arm 17 of the substrate regeneration tank 15 and the stirring arm 17 is the rotation direction of the second stirring shaft 16 Or the opposite direction is deviated by a certain angle and the adjacent mixing arm 17 is attached. The processed object is transported to the mixing arm 17 arranged in sequence and moves to the downstream side. It is the νπ — ΥΙΙ cross-sectional plaque of Figure 2 * on the side wall of the substrate regeneration tank 15. At the same time as the discharge port 23 for discharging the processed material is perforated, a storage device 24 for storing the discharged processed material is provided in Inside the casing of the treatment device 50 • The treatment system that becomes corrosive is guided to this paper standard using the Chinese National Standard (CNS) Α4 specification (210X297 mm) -------- ^. 装- ------- Subscribe ~ .----- fmu (please read the precautions on the back before filling in this page) —9 — A7 B7 Member of the Central Standards Bureau of the Ministry of Economic Affairs Printed by the consumer cooperative 5. Description of the invention 7) 1 to the discharge cylinder 2 1 and stored in the storage device 2 4 〇1 1 is the capacity of the processing device fermentation tank 1 and substrate regeneration tank 1 1 5 constructed as follows Decide y-v 1 1 Please 1 I Capacity of fermentation tank 1 R 1 = (Rotating diameter of stirring arm 3) 2 First reading 1 I 1 1 X Length of stirring shaft 2 (tank length) Back 1 1 Substrate regeneration tank The capacity of 1 5 R 1 5 = (recall of the stirring arm 1 7 1 I thing 1 turn diameter) 2x stirring shaft] L 6 length (groove length) The item is refilled by 1 and thus formed as R 1 R 1 5 1 0 0 3 0 • 3 Write this page to install 1 and the amount of substrate and fermentation bacteria that are put into the fermentation tank in advance is determined by 1 1 1 as follows 〇1: 1 If the treatment device 1 is huge When the maximum processing weight of organic waste is set to 1, the total replacement of the substrate and fermentation bacteria will be within the range of 4 1 4 '1 1 I pre-loaded a substrate with 4 1 4 times the maximum treatment capacity of 1 huge And 1. The solid organic waste put into the fermentation tank 1 of the fermentation bacteria will be crushed by the stirring arm 3 with the rotation of the first stirring 1 1 mixing shaft 2 9 while the solid organic waste is broken 9 1 1 Base material and fermentation bacteria When mixing, stir the stirring arm 3> Supply the air to the fermentation 1 1 bacteria 0 The solid organic waste is originally attached to the fermentation bacteria, so it can be fermented without shortening the fermentation time or the limited treatment is easy to ferment. In the case of organic waste, it is not necessary to pre-load the fermentation bacteria into the fermentation tank J. 〇1 I | However, the solid organic waste put into the fermentation tank 1 is the original 1 Ί Larger can also be processed in a shorter period of time > especially large-scale solid 1 1 paper size applicable to the Chinese National Standard (CNS) A4 specifications (210X297 mm) -10-A7 A7 Central Standard Falcon Bureau of the Ministry of Economic Affairs Printed by the industrial and consumer cooperative _____B7_ V. Description of the invention (8) When there are too many organic wastes and want to be processed within a short period of time, throw in the waste that has been finely broken in advance, if it is in a state where it is not broken or it does not need to be too much It can also be crushed. In addition, if the solid organic waste charged into the fermentation tank 1 must be finely crushed in advance and then thrown in, the strength of the first stirring shaft 2 and the stirring arm 2 can be reduced, and the output of the driving motor can be reduced · Furthermore, since the fermentation tank 1 is provided with an electric heater or the like to heat and keep the substrate and the fermentation bacteria, it is combined with the moisture contained in the solid organic waste input: the moisture, temperature, and air of the fermentation tank Satisfying the three elements for fermentation, fermentation begins. Second, steam is generated from solid organic waste during fermentation and heating. This water vapor is conveyed to the dehumidifier (heat exchange device) 11 provided outside the tank by the suction fan 9 connected to the fermentation tank 1 due to the circulation fan 1 3. Furthermore, since the duct 11 1 a of the heat exchanging device uses a blower fan to exchange heat with the low-temperature outside air, the water vapor is condensed into a liquid, and is discharged from the drain duct 14 out of the device. A part of the to-be-processed material in the fermentation tank flows into the base material regeneration tank 15 arranged in parallel with the fermentation tank 1 through the low-wall portion 27a. The inflowing object is stirred with the stirring arm 17 to move the substrate regeneration tank 15 at the same time. After dropping from the lower wall portion 2 7 a of the substrate regeneration tank 15, it returns to the fermentation tank 1 again. By repeating this operation, the object to be processed circulates in the fermentation tank 1 and the base material regeneration tank 15. Since the fermentation tank 1 and the base material regeneration tank 15 are provided with heating means, the current paper standard in the flow fermentation tank 1 and the base material regeneration tank 15 is circulated while applying the Chinese National Standard (CNS) A4 specification (21 〇X297mm) -------- installed-- (Please read the precautions on the back before filling in this f)
A -11 - 292981 A7 B7 五、發明説明（9 ) 過程，蒸發剩餘水分，並且破碎塊狀物而被小顆粒化。 該所被小顆粒化的處理物，稹蓄一定程度以上，則從 被設在基材再生槽1 5的一端之排出口 2 3排出處理物的 一部分，且被貯存在設於處理裝置內的貯存裝置2 4內部 〇 上述排出口 2 3被設於從第7圖所示的基材再生槽 1 5的上端部至所定尺寸的較低的位置。由於被設置在該 較低的位置，所以表示每單位容積的物質重量之整體密度 (bulk density ) *使其易於排出比基材還大的處理物並 且不致排出基材。乾燥後的整體密度，係爲在基材爲 2 0 0 k g/m3〜3 0 0 k g/m3時處理物爲 5 0 0 k g/m3〜6 0 0 k g/m3 在上述所形成的處理裝置，連續投入不易發酵處理的 髙含油脂動物性殘渣時，對於投入棄物物重量所排出的處 理物之置，其減量率爲1/1 0。並且得到基材幾乎未劣 化之結果。 經濟部中央梂準局貝工消费合作社印製 (請先閲讀背面之注意事項再填寫本頁) <第2實施例> 第8圖係爲表示處理裝置的第2實施例之橫斷面圓， 第9圖係爲從基材再生槽側正視之縱斷面圓。在與第1實 施例相同構成之構件附註同一圖猇其說明省略· 發酵槽1係以分割板2 5分割而形成第1發酵槽1 A 與第2發酵槽1B·在第1發酵槽1A配設第1攪拌軸 2A，在第2發酵槽1B配設第2攪拌軸2B。進而，配 本纸張尺度適用中國國家揉準（CNS ) A4規格（210X297公釐） -12 - 經濟部中央標準局員工消費合作社印製 kl _B7_ 五、發明説明（10) 設驅動第1攪拌軸2A的第1驅動用馬達7A，用鏈輪作 連結。另外設置驅動第2攪拌軸2 B的第2驅動用馬達7 B，用鏈輪作連結。第1攪拌軸2A與第2攪拌軸2 B係 隔著發酵槽的分割板2 5而相互反方向的被驅動。 配設在基材再生槽15的攪拌軸16係以第1發酵槽 1 A的第1攪拌軸2 A的驅動用馬達7 A而被驅動。 以此所形成的裝罝，因基材再生槽1 5的攪拌軸1 6 與第1發酵槽1 A的第1攪拌軸2 A係爲同方向的回轉， 所以發酵槽1A的第1攪拌軸2A爲耙起從基材再生槽 15落下的基材及處理物之作用。 第2發酵槽1 B的第2攪拌軸2 B由於是與第1攪拌 軸反方向的回轉，所以發酵槽1 B的第2攬拌軸2 B的回 轉爲將第2發酵槽1B的基材及處理物耙至基材再生槽 1 5內之作用。 在基材再生槽1 5的攪拌軸1 6，螺旋狀的被配設具 有與攪拌腕17的突出尺寸幾乎近似的突出尺寸· 在基材再生槽1 5的下側空間6 0配設熱交換裝置 1 1。由於熱交換裝置1 1係爲將其較長方向配設在基材 再生槽1 5的軸方向，因此可以將處理裝置的軸方向尺寸 形成爲小型化。 進而，在基材再生槽1 5下側的空間6 0鄰接於熱交 換裝置，配設驅動發酵槽1的攪拌軸2A、2 B之驅動用 馬達7A、7B，由於利用基材再生槽下側的空間6 0而 達成處理裝置的小型化。 本紙張尺度通用中國囷家標準（CNS ) A4規格（210X297公釐） ^ 裝-----__訂-----^冰 (請先閱讀背面之注意事項再填寫本頁) -13 - A7 B7 五、發明説明（11) 【發明效果】 如以上所說明，本發明固形有機廢棄物的處理裝置， 由於攪拌，加熱流入基材再生槽內之基材及處理物除去剩 餘水分的同時，發酵且或爲塊狀物的處理物被小顆粒化， 基材被再生爲原來的通氣性或水分保持性的良好狀態。 另外困基材被再生爲原來的通氣性或水分保持性的良 好狀態，所以就是不投入新基材，在長時間的處理下，也 不會改變槽內容物的通氣性或水分保持性等之物理性質， 而維持良好的發酵。 因此，不必要定期的全更換基材或隨時追加投入新鮮 的基材，而可以提供簡單管理的處理裝置。 【圖面之簡單說明】 第1圖係爲在本發明固形有機廢棄物的處理裝置之筐 體上部所斷面的上面圖（第2圖的I — I斷面圖）。 經濟部中央標準局員工消费合作社印製 (請先閲讀背面之注意事項再填寫本頁) 第2圖係爲在第1圖所示處理裝置的Π_Π斷面圖。 第3圖係爲在第1圖所示處理裝置的m—π斷面圖。 第4圖係爲表示從第1圖的P方向正視的隔間構件之 部分斷面圖· 第5圖係爲表示從第1圖的Q方向正視的分割板之部 分斷面圖· 第6圈係爲表示本發明的攪拌軸及攪拌腕之斜視圖· 第7圈係爲第2圓所示處理裝置之W—W斷面圖。 本紙張尺度適用_中國國家橾準（CNS ) A4規格（210X297公釐） — A7 B7 五、發明説明（12 ) 第8圖係爲表示本發明第2實施例的處理裝置之橫斷 面圖" 第9圚係爲從本發明第2實施例的處理裝置之基材再 生裝置側正視之縱斷面圖。 【圖號說明】 1:發酵槽 2:攪拌軸 3:攬拌腕 7:馬達 8:投入口 11:熱交換裝置 15:基材再生槽 16:攪拌軸 17:攪拌腕 22:馬達 (請先閲讀背面之注意事項再填寫本頁) 裝. 2 3 :排出口 2 4 貯存裝置 2 5 分割板 2 5 ; a :低壁部 2 5 b :高壁部 2 7 =隔間構件 2 7 ; a :低壁部 2 7 b :高壁部 6 0 :空間 -訂 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 ) A4規格（210X297公釐） -15 -A -11-292981 A7 B7 5. Description of the invention (9) The process evaporates the remaining water, and breaks up the lumps and becomes small particles. If the processed material that has been reduced into small grains is stored to a certain degree or more, a part of the processed material is discharged from the discharge port 23 provided at one end of the substrate regeneration tank 15 and stored in the processing device. Inside the storage device 24. The discharge port 23 is provided from the upper end of the substrate regeneration tank 15 shown in FIG. 7 to a lower position of a predetermined size. Since it is set at this lower position, it represents the bulk density per unit volume of the substance * It makes it easier to discharge the processed material larger than the substrate and does not discharge the substrate. The overall density after drying is the treatment device when the substrate is 200 kg / m3 ~ 3 0 0 kg / m3. The treatment device is 5 0 0 kg / m3 ~ 6 0 0 kg / m3. When continuously feeding animal residues containing fat and oil that are not easily fermentable, the reduction rate for the disposal of the waste discharged by the weight of the input waste is 1/1 0. And the result that the substrate is hardly deteriorated is obtained. Printed by the Beigong Consumer Cooperative of the Central Bureau of Economic Affairs of the Ministry of Economic Affairs (please read the precautions on the back before filling in this page) < Second Embodiment > Figure 8 is a cross section showing the second embodiment of the processing device The circle, Figure 9 is the longitudinal cross-section circle viewed from the side of the substrate regeneration groove. The same structure as in the first embodiment is appended to the same figure. The description is omitted. The fermentation tank 1 is divided by a dividing plate 25 to form the first fermentation tank 1 A and the second fermentation tank 1B. In the first fermentation tank 1A The first stirring shaft 2A is provided, and the second stirring shaft 2B is disposed in the second fermentation tank 1B. Furthermore, the size of the matching paper is applicable to China National Standard (CNS) A4 (210X297mm) -12-Printed by the Ministry of Economic Affairs, Central Standards Bureau employee consumer cooperative Kl _B7_ V. Description of invention (10) The first stirring shaft 2A is set The first driving motor 7A is connected by a sprocket. In addition, a second driving motor 7 B that drives the second stirring shaft 2 B is provided, and a sprocket is used for connection. The first agitating shaft 2A and the second agitating shaft 2 B are driven in opposite directions to each other across the partition plate 25 of the fermentation tank. The stirring shaft 16 arranged in the base material regeneration tank 15 is driven by a driving motor 7 A of the first stirring shaft 2 A of the first fermentation tank 1 A. In this case, the stirring shaft 16 of the substrate regeneration tank 15 rotates in the same direction as the first stirring shaft 2 A of the first fermentation tank 1 A, so the first stirring shaft of the fermentation tank 1A 2A is a function of raking up the substrate and the processed material dropped from the substrate regeneration tank 15. Since the second stirring shaft 2 B of the second fermentation tank 1 B rotates in the opposite direction to the first stirring shaft, the rotation of the second stirring shaft 2 B of the fermentation tank 1 B is the base material for the second fermentation tank 1B And the treatment object raked into the substrate regeneration tank 15. The stirring shaft 16 of the base material regeneration tank 15 is spirally arranged to have a protrusion size almost similar to the protrusion size of the stirring arm 17 · Heat exchange is arranged in the lower space 60 of the base material regeneration tank 15 Device 1 1. Since the heat exchanging device 11 is arranged in the axial direction of the base material regeneration tank 15 in the longer direction, the axial dimension of the processing device can be reduced in size. Furthermore, the space 60 below the base material regeneration tank 15 is adjacent to the heat exchange device, and the driving motors 7A, 7B that drive the stirring shafts 2A, 2 B of the fermentation tank 1 are arranged. The space is 60% to achieve the miniaturization of the processing device. The size of this paper is universal Chinese Standard (CNS) A4 specification (210X297mm) ^ Pack -----__ order ----- ^ Bing (please read the precautions on the back before filling this page) -13 -A7 B7 V. Description of the invention (11) [Effects of the invention] As described above, the solid organic waste treatment device of the present invention heats the substrate and the processed material flowing into the substrate regeneration tank due to agitation while removing excess moisture The processed material that is fermented or agglomerates is made into small particles, and the substrate is regenerated into the original good state of air permeability or water retention. In addition, the trapped base material is regenerated to the original good state of air permeability or water retention, so even if the new base material is not put in, it will not change the air permeability or water retention of the tank contents under long-term treatment. Physical properties while maintaining good fermentation. Therefore, it is not necessary to completely replace the substrate on a regular basis or to add fresh substrate at any time, and it is possible to provide a processing device with simple management. [Brief Description of Drawings] Figure 1 is a top view of the upper section of the casing of the solid organic waste treatment device of the present invention (sectional view II in Figure 2). Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs (please read the precautions on the back before filling in this page) Figure 2 is a Π_Π cross-sectional view of the processing device shown in Figure 1. Figure 3 is an m-π cross-sectional view of the processing device shown in Figure 1. Figure 4 is a partial cross-sectional view showing the partition member as viewed from the P direction of Figure 1 · Figure 5 is a partial cross-sectional view showing the dividing plate as seen from the Q direction in Figure 1 · Circle 6 It is a perspective view which shows the stirring shaft and stirring arm of this invention. The 7th circle is the W-W sectional view of the processing apparatus shown by the 2nd circle. This paper standard is applicable_China National Standards (CNS) A4 Specification (210X297mm) — A7 B7 5. Description of the invention (12) Figure 8 is a cross-sectional view of the processing device showing the second embodiment of the present invention & quot 9th is a longitudinal sectional view from the front side of the substrate regeneration device of the processing device of the second embodiment of the present invention. [Explanation of figure number] 1: Fermentation tank 2: Mixing shaft 3: Mixing wrist 7: Motor 8: Input port 11: Heat exchange device 15: Base material regeneration tank 16: Mixing shaft 17: Mixing wrist 22: Motor (please first Read the precautions on the back and then fill out this page) Install. 2 3: Discharge port 2 4 Storage device 2 5 Dividing plate 2 5; a: Low-wall part 2 5 b: High-wall part 2 7 = compartment member 2 7; a : Low-wall section 2 7 b: High-wall section 6 0: Space-Ordered by the Ministry of Economic Affairs Central Standards Bureau Employee Consumer Cooperatives. This paper is printed in accordance with the Chinese National Standard (CNS) A4 specification (210X297 mm) -15-