經滴部中央標準局貝工消费合作社印繁 A7 ___B7 五、發明説明（/ ) 發明之詳細說明 本發明係有關於高濃度有機性廢棄物之厭氣性消化處 理方法，以及使用該方法之長期滯留型之多段連續排水發 生控制式厭氣性消化裝置，其目的爲直接在發生來源處， 處理廚房廢棄物及糞尿等之髙濃度有機性廢棄物，預防由 該等廢棄物所引起之各種環境問題，並且將其中所生成的 副產物甲烷氣體作爲輔助熱源而進行再利用。 關於都市廢棄物的處理，在日本利用掩埋來處理已達 到其國土能忍受之極限，特別是腐敗性廢棄物（主要爲廚 房廢棄物），由於其掩埋後的腐敗會導致各種技術上的問 題，因此對於開發這些廢棄物，使其能被有效地處理的技 術之需求就愈來愈大了 =關於這種需求，雖然已有出現針 對廚房廢棄物處理的各種處理技術（如堆肥化、發酵飼料 化），但對於維持、管理，以及處理物的最終處理上，實 際的情況則是仍然有諸多的問題有待解決。 而在國外，腐敗性廢棄物的最終處理方式1主要爲適 用於焚燒和掩埋技術，至於適用於厭氣惶的消化例子的例 子並不多見。又，現今的消化技術大部分都需要機械混合 及中溫狀態（3 5 °C )的運轉條ί牛*且投入物體的性狀也只 適用於5¾左右的濃度，由此而因應產生之前處理等維持、 管理上相當的技術水準，在實際運轉上經濟上的評價並不 高。 試看相關之硏究例，將義大利的大型食品店所產生的 廢棄物1〇〇噸/日置於2 〇〇〇m3反應槽中’中溫消化之結果， 5 本纸張尺度適用中國國家標準（CNS )_A4規格(UO X297公釐）Printed by the Central Standards Bureau of the Ministry of Standards, Shellfish Consumer Cooperatives, A7 ___B7 V. Description of the invention (/) Detailed description of the invention The invention relates to an anaerobic digestion treatment method for high-concentration organic waste, and the long-term use of this method The detention type multi-stage continuous drainage generation controlled anaerobic digestion device is designed to treat kitchen waste and organic waste such as radon concentration directly at the place of occurrence to prevent various environments caused by these wastes. The problem is that the methane gas produced as a by-product is reused as an auxiliary heat source. Regarding the disposal of municipal waste, the use of landfills in Japan has reached the limit to which its territory can tolerate, especially corrupt wastes (mainly kitchen wastes). The corruption after landfills will cause various technical problems, Therefore, there is an increasing demand for the technology to develop these wastes so that they can be effectively treated = regarding this demand, although various treatment technologies (such as composting, fermented feed) for kitchen waste treatment have emerged ), But for maintenance, management, and final disposal of the processed material, the actual situation is that there are still many problems to be solved. In foreign countries, the final treatment method 1 of destructive waste is mainly applicable to incineration and landfill technology. As for the examples of digestion by anaerobic dysentery, there are few examples. In addition, most of today's digestion techniques require mechanical mixing and running at a medium temperature (35 ° C). The characteristics of the input object are only applicable to a concentration of about 5¾. Therefore, it is necessary to deal with the previous processing, etc. The technical level of maintenance and management is quite high, and the actual economic evaluation is not high. Let's take a look at the relevant research example. The waste produced by a large food store in Italy was placed in a 2000m3 reaction tank at a rate of 10,000 tons per day. 'The result of moderate temperature digestion. 5 This paper size applies Chinese national standards. (CNS) _A4 specifications (UO X297 mm)
In ml I----! I- ! I - - ' 1^1 —i - - - -- - I 1 i--- ^^1 ^^1----f (#先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 A7 ____B7 _ 五、發明説明（2) 廢棄物1噸約會產生58.6m3的氣體，接著是24噸的泥渣， 以及38噸的廢排出水。全體而言，約可減少38¾的量， 逆且較焚燒在經濟上更爲優越。又，還發現當碳/氮比率在 1 〇以下時，利用二相消化方式來處理更爲有用，1 5以上 時，單相消化方式則更有利，經濟上的效果評估爲非加溫 狀態之運轉較中溫而言，在各種方面皆更具有競爭力。【文 獻：Mat a-Alvare z J. C e c chi F.，Llabres P. & Pavan P.,In ml I ----! I-! I--'1 ^ 1 —i-----I 1 i --- ^^ 1 ^^ 1 ---- f (#Read the note on the back first Please fill in this page again) A7 printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs ____B7 _ V. Description of the invention (2) One ton of waste produces 58.6m3 of gas, followed by 24 tons of sludge and 38 tons of waste Drain the water. Overall, it can reduce the amount of about 38¾, which is more economically superior to incineration. In addition, it was found that when the carbon / nitrogen ratio is below 10, it is more useful to use a two-phase digestion method. When it is more than 15, a single-phase digestion method is more advantageous, and the economic effect is evaluated as a non-warming state. Compared with medium temperature, the operation is more competitive in various aspects. [Literature: Mat a-Alvare z J. C e c chi F., Llabres P. & Pavan P.,
Anaerobic digestion of the Barocetona central food market organic wastes. Plant design and feasibility, Bioresource Tech. , V o 1. 4 2, p3 3-42, 1 9 92: Weiland P. , One -and two step anaerobic digestion of solid agoindustrial residues, Water Sci. Tech. , Vol. 27, pl45-1 51, 1993:Lusk, Philip D., Comparative economic analysis. Anaerobic Digestion case study, Bioresource Tech. , Vol. 3 6, p223 -228, 1991: Nazir M. , Biogas plants construction techology for rural areas, Bioressource Tech. Vol. 35, p283-289, 1991 】。 但是，現存這種的厭氣性消化裝置，其特殊系統大部 分爲適合各國獨自的氣候等條件，直接要用來反映本國的 現實情況則有其限制，亦即如果適合產生的廢棄物狀態含 量爲20¾左右高濃度的廚房廢棄物處理時，就會發生必須 要對稀釋水再進一步考慮，以及對排出水進行再追加處理 等問題。 在現今狀況下所浮現出的，廚房廢棄物的處理上最重 要的環保問題*便是是否能由既存的處理技術再蛻變開發 本纸張尺度適用肀國國家標準^阳丨以規格㈠⑴以们公弟-) ----------装------訂------^ (讀先閱讀背面之注意事項再填寫本頁·- 經满部中央標準局負工消費合作社印" A7 B7 五、發明説明（5 ) 出新的技術，因爲現行的有機性廢棄物之處理，以及作爲 再活用技術、突然產生的堆肥化方式，已經很淸楚地並不 適於吾等國民之飲食生活特性。是故，新的對策已不可避 免了。 爲解決本課題之方法及作用 本發明之目的，係提供一裝置及方法，其在與F水道 普及相關連的水洗式廁所設備之設置較困難的地區，解決 其所面臨的環境污染，將糞尿及廚房廢棄物配合，或個別 地厭氣性消化處理。 本發明之另一目的，係提供一種功能的、經濟的處理 方法和裝置，其係解決食品加工工廠等會排出髙濃度有機 性廢棄物的產業，因爲其增加的環境負擔所導致之妨礙經 濟活動的問題，並控制不引起廢棄物處理所導致的處理水 相關的維持、管理等問題。 發明的構成及作用 前述本發钥的目的係藉由有機性廢棄物之多段連續式 厭氣性消化處理裝置來達成，其特徵爲， 一本體，其包含氧化分解反應槽，其夾著有機性廢棄 物投入口（ 1 )、氧化分解反應槽（2 )、氧化還原分離膜 (1 )，與該氧化分解反應槽相連接之還原分解反應槽C 3 )， 其夾著內部氣體底流槽（6 )、流動速度調節版〔9 )、附 著有移動式內部氣體底流板（10)的還原反應分離膜（11)， 與該還原分解反應槽相連接的安定槽（4)，以及沿著前 述氧化分解反應槽（2 )和還原分解反應槽（3 )底面之介頁 (讀"閱讀背面之注意事項再填寫本页) *-'β 本紙張尺度適用中國國家標準（〔:^)/\4規格（2】0-乂 297公釐) 1 經濟部中央標準局貝工消費合作社印製 A7 B7 五、發明説明（4) 斜面，雄配置於其下部的底流槽（5) ’以及 一返送裝置，其係由吸入口、返送用送風機（18)、 空氣供給管¢45)、返送管（19)、及返送水噴灑裝置（31) 所構成，其目的爲將前述底流槽的上澄液返送至前述氧化 分解反應槽，以及 一氣體貯藏及活用設備’其係由氣體自動關閉閥門 (25)、防止氣體貯藏設備腐蝕的脫硫裝置（26)、氣體 壓縮幫浦（27 )及氣體貯藏容器筒（28 )’以及燃燒口（ 29 ) * 以及 除去惡臭用之脫臭裝置（35)，以及鍋爐設備（21)。 又，根據本發明所提供之高濃度有機性廢棄物的厭氣性消 化處理方法，其係包括 U)在前述本發明的多段連續式排水抑制式之厭氣性消 化處理裝置的氧化分解反應槽上，將包括廚房廢棄物及糞 尿等有機性廢棄物在發生來源，不經前處理，而以固形物 含量20〜30¾的髙濃度直接投入的階段，以及 (b)將被投入的高濃度有機性廢棄物的一部份加水分 解，一部份氧化的氧化分解反應階段，以及 ⑹經過前述氧化分解反應階段、沿著傾斜面自動地移 到還原分解反應槽的有機性廢棄物，利用甲烷化微生物的 作用分解，而生成包含曱烷氣體、二氧化碳、以及氨氣的 氣體’再藉由產生的氣體在內部氣體底流槽中產生氣體壓 力的還原分解反應階段，以及 (<0在前述內部氣體底流槽中，藉由氣體的底流和排 本紙張尺度適用中國國家標率（CNS ) A4規格（210XD7公釐） I~~, 1 FI! 訂 .^ (讀先閱讀背面之注意事項再填窍本頁) 經滴部中央標準局員工消費合作社印製 458818 A7 B7 五、發明説明（r) 出，來使前述還原分解反應槽的泥渣流動，邀使微生物和 泥渲自動地互相接觸的混合階段，以及 (e) 將經過前述還原分解反應階段、沿著傾斜面自動地 移到安定槽的殘留物，藉著使其進一步分解，然後只留下 非分解性的泥渣之安定化狀態的安定化階段，以及 (f) 在前述氧化、還原及安定化階段中所產生的氣體， 將其中所含有的硫磺成分以及惡臭成分除去之脫硫、脫臭 階段，以及 (g) 將前述底流槽的上澄液返送至前述氧化分解反應槽 的階段，以及 (h) 將最後分解之殘留物底流至前述底流槽的底流階 段。 本發明者們'針對高濃度之有機性廢棄物處理相關之 最現實的問題，即藉厭氣性消化方式來進行更有效率之處 理技術的開發，其結果大大的解決了由於糞尿及廚房廢棄 物等高濃度的有機性廢棄物導致之環境問題。 本發明者們，爲因應這種狀況，在重複一連串的相關 硏究之後，達到可以將廚房廢棄物在發生來源上，直接處 理廢棄物產生量約30%，改善了幾乎已到達臨界點之掩埋 地相關問題，有效地處理有機性廢物，並能控制排水的發 生，進一步其具有對於維持、管理上的技術問題的方便， 而能開發出經濟的處理方法和裝置，完成了本發明。 以下，進一步詳細說明圖1中無 '但表示於圖6的多 段連續排水抑制式厭氣式消化處理裝置，以及使用該裝置 9 本紙張尺度適用中國國家標準（CNS ) Λ4規格（210X29?公麓） (請先閱讀背面之注意事項再填寫本頁) •裝- 經濟部中央標準局員工消費合作社印" 4 5881 8 A7 B7 五、發明説明（έ ) 的高濃度有機性廢棄物的厭氣式消化處理方法。 本發明之多段連續抑制式厭氣式消化處理裝置爲，可 將高濃度有機性廢棄物的厭氣式消化處理過程在一個反應 槽內連續進行，圖1中詳細說明了這些反應階段的必須構 造。 附圖上的所表75之本發明之有機性廢棄物的厭氣式消 化處理裝置爲，指示根據本發明原理所進行廢棄物處理方 法的裝置的一個例子而已，在進行本發明之方法時，其型 態或構造是可以有各種變形的。這些變形皆應被視爲屬於 本發明，而附圖則爲使本發明爲更容易說明起見，在本發 明中，必須注意不論以茌何方法都不應該造成對太發明之 _制。 本發明之長期滯留型多段連續式厭氣性消化處理裝 置，其大致可以分爲主體1返送裝置、脫臭設備（35)、 氣體貯藏和活用設備、以及鍋爐設備等主要構成部分。本 體則包含一本體，其包含廢棄物投入G ( 1 )、氧化分解 反應槽（2)、還原分解反應槽（3)、安定槽（4) '底 流槽（5)、氣體底流槽（6)、相分離膜（7,11)、流動 速度調節钣（9 )、移動式內部氣體底流板（1 〇 )、以及 氣體排出管（I5)。在這種厭棄姓消化裝置中，其特徵爲 主要由具有可在消化反應階段將氧化及還原分解階段分 離、並藉重力將反應物連續進行之氧化分解反應槽（2 )、 還原分解反應槽（3 ) '經過安定槽（4 .)到底流槽（5 ) 的底流構造，以及可針對投人物之固態物質的濃度特性， 10 本紙張尺度適用中國國家標準（CNS ) Α4規格（210Χ 297公釐） --------A------1T------^ (諳先閱讀背面之注意事項再填寫本頁) A7 B7 經濟部中央標準局員工消費合作社印架 五、發明説明（q ) 而調節反應槽內微生物滯留時間之槽分離膜（7, i i )、流 動速度調節版（9 )的設置位置，以及可改變底部傾斜度 以移動固態物質等， 在本體中，之氧化分解反應槽（2 )與還原分解反應 槽（3 ) ’係與氧化還原分離膜相接，而氧化分解反應槽 (2 )與還原分解反應槽（3 )的底面則爲使在氧化分解反 應槽（2)中所處理的廢棄物容易移動之故，將其作成傾 斜面。底流槽（5 )則位於氧化分解反應槽（2 )和還原分 解反應槽¢3)之傾斜面的下方，又，在還原分解反應槽 (3 )和安定槽（4 )之間，則有一T型之還原反應分離膜 (1 1 )。進一步，其構造爲，在還原分解反應槽（3 )上 有氣體底流槽（6 )、內部氣體底流板（8 )、以及流動速 度調節版（9)，其上方則有氣體排出管（15) = T型之還 原反應分離膜（11)有移動式內部氣體底流板（10)附著 於其上。槽分離膜（"Μ 1 )以及流動速度調節版（9 )的設 置位置和前述傾斜面之傾斜角，要考慮微生物在反應槽內 的滯留期間，並配合被投入固態物質之濃度特性來加以設 定。傾斜角一般爲約5-17度的範圍內設定爲宜。 投入口（ 1〕的周圍連結有惡臭氣體吸入管（1 7 )， 在氧化分解反應槽（2 )的上方設置有返送水噴灑裝置 (3 1 )，該裝置係與可將底流槽（5 )的安定化上澄液供 給至氧化分解反應槽（2 )的空氣浮上式返送管（1 9 )相 連結。在氧化分解反應槽（2 )的內部則可配置有促進氧 化分解反應之格子形狀的任意性微生物培養槽（13)，以 11 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） --------政------1T------4 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局負工消費合作社印製 A7 _____ B7_____ 五、發明明（8 ) 及水位調節管（1 4 )。 在此，任意性微生物係指存在於環境系中，在有氧氣 存在的好氣性狀態時，可以好氣性微生物的方式生長，在 嫌氣性狀態時，可以嫌氣性微生物的方式生長，其數難以 估計。任意性微生物在本說明書中只是作爲一般能在氧氣 極端不足的狀態下生存的微生物之通稱。舉例來說，在本 發明中即使用生存於牛第一個胃之微生物（通稱Rumen微 生物）來培養。 還原分解反應槽（3)的上方連結有氣體排出管（15)， 凡是運轉中被產生之氣體皆經由該氣體排出管（15.)來進 行脫硫處理。鍋爐設備（2 1 )則被用來維持底流槽（5 ) 在20°C左右的恆溫狀態》 在廚房等所發生之有機性廢棄物，其係以發生處所原 來的高濃度狀態通過投入口（ η再流入氧化分解反應槽 (2 )。投入物的一部份藉由微生物的體舛細胞分泌物進 行加水分解，其中一部份將經過氧化反應階段，而被氧化 爲揮發性有機酸和氫氣以及乙醛等成分·，此時，可以預防 在投入物的氧化過程中所發生之惡臭，而爲了要確保液體 的流動性所需要適當供應的水分，將底流槽（5 )丙的安 定化上澄液通過空氣浮上式之返送管（1 9 )送回，再利用 返送水噴灑裝置（3〗）平均分配至氧化分解反應槽（2)。 被投入之廢棄物在氧化分解反應槽（2)內的被處理物滯 留時間，其係根據廢棄物的種類、濃度，與是否要再利闬 產生之氣體*以及分離膜的設置間隔與傾斜面的傾斜度等 12 本紙張尺度適用中國國家標準（CNS ) Λ4規格（210Χ 297公漤） ，裝 訂 知 (請先間讀背面之注意事項再填寫本頁) A7 458818 ___ B7_______ 五、發明説明（？） 來決定。 又，本發明爲促進氧化反應之故，在氧化分解反應槽 (2)內設置一格子形狀之任意性微生物培養槽’ 可蓄積供給製造成彈九形狀的特定之任意性微生物群以高 濃度。廢棄物經過氧化分解反應被一次分解成有機酸和乙 醛等，然後藉由重力沿著傾斜面（21)移動至遺原分解反 應槽（3)。在還原分解反應槽（3)藉由甲烷化微生物的 作用氣化形成了甲烷、二氧化碳、以及氨氣體，並且在內 部氣體底流槽（8)生成氣體壓。設置於T型之還原反應 分離膜（11)之上的移動式內部氣體底流板（10)，其藉 由底部氣體之浮力一面上升，一面則亦使傾斜面底部之泥 渣浮上來，當氣體底流槽（6)的內壓達到0.1-0.1 5kg/Cm2 時，藉由與氣體排出管（15)相連接的氣體壓自動調節幫 浦（25 )的作用，氣體被排出，此時氣體底流板（10 )則 與水位共同下降。如上所述的這種藉由氣體底流與排出作 用，其所導致之水位變化作用與移動氣體底流板（10)的 上升'下降，而使得泥渣與微生物互相接觸之過程是完全 自動的。在還原分解過程中所產生之重碳酸鹽 (bicarbonate )成分，其功能係將還原分解反應槽（3 ) 的pH値維持在一棟的水準，並且藉由在氧化分解反應懵 (2 )內所蓄積之過多的有機酸，來預防pH値降低以及微 生物活性減少。固態物質在通過還原分解反應槽（3)， 依序移動至安定化槽（4)，而被最後分解處理，其結果 約有全體投入童5-7¾ (糞尿約有0.8-1.2¾ )左右變成泥 本紙張尺度適用中國國家標準（CNS ) Λ4规格（2!0Χ297公釐） -----------袭------ΐτ------ {請先間讀背而之注意事項再填寫本莨) 經濟部中央榡準局員工消费合作社印繁 經满部中央標準局員工消費合作社印繁 4 5881 8 a7 __B7__ 五、發明説明（/。） 渣殘留於底流槽中。該殘留物係藉由淨化槽掃除方式，以 約每2-3年C糞尿約每4-5年）一次的頻率，經過內部氣 體檢查口而被除去。 經過前述的氧化和還原反應，有機性廢棄物質被分解 成氣體狀態，經過固液分離的方式最後只剩下泥渣，這些 過程之理論關係敘述於下述之反應式（1)中。 【反應式1】 (廚房廢棄物3.3H20 3.55C02 + 3.55CH4 + 0.5NH3 亦即，爲將100kg的飮食廢棄物（固態物質含量20% ) 厭氣分解之故，須要約5.81的水分。預期產生之氣體約有 16.5m3 ( 1.03m3氣體/kg VS/d )，而實際結果在中溫之下 則有0.77 m3氣體/kg VS/d產生，無加溫之下運轉時約爲 0.3m3氣體/kgVS/d產生。另一方面，廚房廢棄物中所包 含之水分平均約有81% ，其中5,5¾藉由有機廢棄物之氣 體反應而被消耗掉，另約4.5¾以水蒸氣的方式與氣體共 同揮發，最後剩下約7 15¾則在滯留時間中藉由蒸發而被除 去。 殘留物經過還原分解反應移動至安定槽（4)，然後 與追加分解一起，成爲只留下泥渣的安定狀態。又，安定 槽（4)係藉由能夠將還原分解反應所產生之氣體來調節 水位的變化的多餘部分，而具有調節部的功能。 殘留物向底流槽（5)移動並蓄積，直至掃除時期爲 止。底流槽中爲避免冬天的寒害所導致之裝置破損，以及 本紙張尺度適用中國國家榡準（CNS ) Λ4规格（210x 297公楚） 裝 訂 —』 (請先閱讀背而之注意事項再填寫本頁) 經漓部中央榡準局貝工消費合作社印架 4 Ε _Ή 1 s A 7 B7 _____五、發明説明（ll ) 提高處理效率之故，設置一自動溫度調節裝置的鍋爐設備 (21)，而能維持底流槽的溫度於20°C左右。 在本發明之處理裝置所產生之氣體，其經過脫硫階段 而被貯藏於氣體貯藏設施中，因應需要而再重新使用。如 圖2所示，氣體通過排出管（1 5 )並藉由氣體自動關閉閥 門（25 )被排出而移送至脫硫裝置（26 )，藉由氣體壓縮 幫浦（27)以約lOkg/cm2的壓力，貯藏於氣體容器（Μ) 之後，再於有需要時使用。廚房廢棄物的硫磺成分，其乾 燥之平均含量約爲0.54¾，此脫硫裝置係避免再利用氣體 時裝置被腐蝕之故而必須設置。如圖5所示之脫硫裝置的 構造，本發明係能適用於各種脫硫裝置，而在此則爲使用 乾式方法之密閉型脫著式的脫硫容器。脫硫用的塡充物 (44)，將氧化鐵（Fe03)的氧化劑加入，以置換摒除去 的方式置換氣體內之硫磺成分爲硫化鐵，其關係式如下反 應式2所示。 Fe03*3H20 + 3Ητ«-► 2FeS + 6H20 將被生成之硫化鐵加熱，使其與空氣接觸而成爲能夠 再生變回氧化鐵之狀態，一般再生利用約可進行2-5次左 右。 本發明中，在有機性廢棄物的消化處理過程上，藉由 廢棄物的腐敗作用，其中的惡臭成分藉由送風器（36)， 通過氧化分解反應槽（2)的吸入管（17)與底硫槽（5) 的吸入□被強迫吸入，通過惡臭移送管（22)移到本管 (33)，而流入到脫臭裝置（35)。 .裝 訂M (請先閱讀背面之注意事項再填寫本頁〕 本紙張尺度適用中國國家標準（CNS ) Λ4規格（210X 297公釐） 經满部中央標隼局貝Η消費合作社印家 A7 B7 五、發明説明（α) 惡臭移送用的本管（33)其管徑因爲比起移送管（22) 的管徑突然擴大約3倍左右，因此惡臭成分在流速減少的 狀態之下，皆流入了脫臭裝置（35)。如圖4所示之惡臭 氣體，惡臭成分通過本管（33)流入到脫臭槽最下方之過 濾層（40)，包含於惡臭成分中之粉塵及水分在此被過濾， 另外，累積的水分則經由污物排出口（ 5 5 )被排出。 爲了將這種污物除去之故，在脫臭設施的底部約有3-5°的傾斜度設計。惡臭成分經過過濾成分後，通過移送管 (41)，與充塡有碎石的支持層（42)，再流入鋸曆脫臭 層（48)中，以物理的吸附與生物學的硝化過程1夾除去 氨氣等各種臭氣成分。在鋸屑脫臭層（48)所沒有被除去 之惡臭成分，則進一步流入土壤脫臭層（49)藉由土壤微 生物來吸附及分解，然後再通過移送管（50)流入脫臭劑 層（51) 1把混合有殘留的氨氣、生物上困難分解之硫化 氫、及微量的CH3SH類等成分及針對上述成分的優良脫臭 劑、以及例如有用來培養髙濃度微生物與微生物生長的營 養素（鐵質、磷、錳）相混合製造出之Ecosob溶液進行 接觸處理。該脫臭劑經過排出口（ 54 )被排出至返送管 (56)，然後送回下方之過濾層（40)，在脫臭設施以最 大的程度滯留之後♦與水分等污物一起通過排出.口（ 5 5 ) 被排出。進一步，在最上方的過濾層（52 )再一次被過濾 之後，通過惡臭物質的最終排出口（ 53 )而排出至大氣中。 如圖5所示之返送系統，其目的係在使底流槽（5) 的安定化上澄液供給至氧化分解反應槽（2 )，其中並以 16 本紙張尺度適用中國國家標準（CNS ) Α4規格（210Χ 297公釐） (請先閱讀背面之注意事項再填寫本頁〕 .裝 訂 18 18 經濟部中央標準局員工消費合作社印^ A7 B7 五'發明説明（β) 空氣浮上式爲最理想》此方式係以返送用送風機（IS)， 藉由供給至空氣供給管（45)的空氣所造成之浮力，使底 流槽（5 )的上澄液浮起，並經返送管（1 9 )以返送水噴 灑裝置（31)進行強迫噴灑。返送裝置的空氣供給管（45) 以約爲返送管（I9)之直徑1/5-〗/1.0倍的程度爲理想，且 以設置於底部起算3 / 8的位置較佳。 圖6係表示一工程圖，其爲與一般廁所所產生之糞尿 與廚房廢棄物相關之聯繫處理方法，糞尿通過下方之傾斜 移送管（47 )被移送至厭氣性消化裝置，並與由上方被投 入之廚房廢棄物一起，經過前述之分解過程進行厭氣性消 化。 由此，若利用本發明之廚房廢棄物與糞尿之處理方法 時： 一·可以$稀釋廚房廢棄物而直接以發生處的高濃度 狀態來處理、 二·因爲可以直接在發生處處理之故，可以有效地解 決其移送與囤積時所產生之腐敗及惡臭等問題、 三·處理過程的副產物甲烷氣體因爲可生產約0.3 m3 氣體/kg VS/d之故，可以將此能源再行利用、 四·因爲處理之殘留物不超過約5-7¾ (糞尿約0.8-1.2 % )，所以在維持、管理相關之處理費用上皆較少且較經 濟、 五·因爲氧化反應分解槽、還原反應分解槽、及安定 槽皆設置於一個反應槽中，可以獨立的連續階段，以及彼 17 本紙张尺度適用中國國家標準ί CNS ) Λ4規格（210Χ 297公t ) ----------裝------訂------Μ (讀先閱讀背面之注意事項再填寫本頁〕 經濟部中央標準局員工消費合作社印製 458818 五、發明説明（/ f) 此互補階段來連續進行i所以可以抑制排出水的發生，並 解決與排出水相關聯之法律方面的規定。 在此，所謂的「彼此互補階段」，其厭氣性曱烷化過 程主要係指酸性發酵與甲烷發酵的兩種功能各自藉由酸形 成的微生物及甲烷形成的微生物來達成，此彼此互補的意 義，係指兩微生物在分解過程中，酸形成微生物RJ把有機 物質轉換成酸性物質，甲烷化微生物則利用酸性物質一方 面生產甲烷、一方面供給酸形成反應槽所正常運作必須之 鹼性物質，因爲這些物質交換若不在適當的狀態之下不會 彼此交流，也就很難正常的運轉之故，因此在本說明書中 將這種作用階段稱爲彼此互補階段。 進一步，如圖6所示，在遊樂場等一起設置簡易的舊 式廁所時，廁所的糞尿係通過下方的傾斜移送管（47 )被 直接投入到氧化分解反應槽中，飲食廢棄物則通過露出於 地上的投入口（1)而被投進，由於飮食廢棄物與糞尿同 時被處理之故’不用再另奍增加處理設備、本身即可消化、 分解，所以可將維持、管理問題等減至最低。此時，厭氣 性處理裝置的高度至少要比廁所的便器高一公尺以上，此 條件在維持、設置上極重要。 寅施例 以下，本發明藉由實施例來作更詳細之說明。但是， 本發明並不限定於這些實施例的範圍之內。 實施例1 如圖1所示將本發明之處理裝置相關之規格明細詳細 18 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐) (請先聞讀背面之注意事項再填寫本I)Anaerobic digestion of the Barocetona central food market organic wastes. Plant design and feasibility, Bioresource Tech., V o 1. 4 2, p3 3-42, 1 9 92: Weiland P., One -and two step anaerobic digestion of solid agoindustrial residues, Water Sci. Tech., Vol. 27, pl45-1 51, 1993: Lusk, Philip D., Comparative economic analysis. Anaerobic Digestion case study, Bioresource Tech., Vol. 3 6, p223 -228, 1991: Nazir M., Biogas plants construction techology for rural areas, Bioressource Tech. Vol. 35, p283-289, 1991]. However, most of the existing anaerobic digestion systems have special systems that are suitable for the climate and other conditions of each country. There are limitations to directly reflecting the actual conditions of the country, that is, if the content of the waste produced is suitable. When processing high-concentration kitchen waste at around 20¾, problems such as the need to further consider the dilution water and the additional treatment of the discharged water will occur. Under the current situation, the most important environmental issue in the treatment of kitchen waste * is whether it can be transformed from the existing treatment technology and developed. This paper applies the national standard ^ Yang 丨 to the specifications. Brother-) ---------- install ------ order ------ ^ (read the precautions on the back before filling in this page. Printed by the Industrial and Consumer Cooperatives " A7 B7 V. Description of the invention (5) New technology, because the current treatment of organic waste, as a reutilization technology, the sudden composting method, is already very clear and uncomfortable Due to the characteristics of the dietary life of our citizens, new countermeasures are unavoidable. In order to solve the problem and the purpose of the present invention, a device and method are provided, which are used for washing in connection with the popularization of F channels. In areas where the installation of toilet facilities is difficult, the environmental pollution that they face is solved, and urine and kitchen waste are matched, or individually anaerobic digestion treatment is provided. Another object of the present invention is to provide a functional and economical Processing method and device, It is to solve the problem of hindering economic activities due to increased environmental burdens in industries that emit radon-concentrated organic waste, such as food processing plants, and to control the maintenance and management of treated water that does not cause waste treatment. The structure and function of the invention The aforementioned purpose of this key is achieved by a multi-stage continuous anaerobic digestion treatment device for organic waste, which is characterized by a body comprising an oxidative decomposition reaction tank and a clamp The organic waste input port (1), the oxidation decomposition reaction tank (2), the redox separation membrane (1), and the reduction decomposition reaction tank C3 connected to the oxidation decomposition reaction tank are sandwiched by the internal gas underflow. A tank (6), a flow rate adjusting plate [9], a reduction reaction separation membrane (11) to which a mobile internal gas underflow plate (10) is attached, a stabilization tank (4) connected to the reduction decomposition reaction tank, and The bottom page of the oxidation decomposition reaction tank (2) and the reduction decomposition reaction tank (3) (read " read the notes on the back and fill in this page) *-'β This paper is applicable National Standards ([: ^) / \ 4 Specifications (2) 0- 乂 297 mm) 1 Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the Invention (4) The bevel, the male The underflow tank (5) 'and a return device are composed of a suction port, a return blower (18), an air supply pipe (45), a return pipe (19), and a return water spray device (31). In order to return the upper liquid of the underflow tank to the aforementioned oxidation decomposition reaction tank, and a gas storage and utilization equipment, it is a gas automatic closing valve (25), a desulfurization device (26) to prevent corrosion of the gas storage equipment, gas Compression pump (27) and gas storage container tube (28) ', combustion port (29) *, deodorizing device (35) for removing malodor, and boiler equipment (21). In addition, the anaerobic digestion treatment method for high-concentration organic waste according to the present invention comprises U) the oxidative decomposition reaction tank of the multi-stage continuous drainage-suppressed anaerobic digestion treatment apparatus of the present invention. In the above stage, organic waste including kitchen waste, feces, urine, etc. will be directly injected at a radon concentration of 20 ~ 30¾ with a solid content of 20 to 30¾ without any pretreatment, and (b) high concentration organic Part of the waste is hydrolyzed, part of the oxidative decomposition reaction stage, and the organic waste that is automatically moved to the reduction decomposition reaction tank along the inclined surface after the aforementioned oxidative decomposition reaction stage, using methanation Decomposition by the action of microorganisms to generate a gas containing pinane gas, carbon dioxide, and ammonia gas, and a reduction and decomposition reaction stage in which an internal gas underflow tank is generated by the generated gas, and (< 0 in the aforementioned internal gas In the underflow tank, the underflow of the gas and the paper size apply the Chinese National Standard (CNS) A4 specification (210XD7mm) I ~~, 1 FI! Order. ^ (Read the precautions on the reverse side and fill in this page) Printed by the Consumer Standards Cooperative of the Ministry of Standards, Bureau of Printing, 458818 A7 B7 V. Description of the invention (r) to make the above reduction decomposition reaction tank Sludge flow, a mixing stage that invites microorganisms and sludge to automatically contact each other, and (e) the residue that is automatically moved to the stabilization tank along the inclined surface after the aforementioned reduction and decomposition reaction stage, and further decomposed by it And then leaving only the stabilization phase of the non-decomposable sludge stabilization state, and (f) the gas generated in the aforementioned oxidation, reduction and stabilization phases, removing the sulfur and odor components contained therein The desulfurization and deodorization stages, and (g) the step of returning the upper solution of the underflow tank to the aforementioned oxidation decomposition reaction tank, and (h) the underflow stage of the final decomposed residue to the underflow tank. The inventors' aiming at the most realistic problem related to the treatment of high-concentration organic waste, that is, the development of a more efficient treatment technology by the anaerobic digestion method, the results are large It solves the environmental problems caused by high-concentration organic waste such as faeces and kitchen waste. In order to cope with this situation, after repeating a series of related investigations, it has been achieved that kitchen waste can be generated. From the source, the direct treatment of waste generation is about 30%, which improves the landfill-related issues that have almost reached the critical point, effectively treats organic waste, and can control the occurrence of drainage. Furthermore, it has technologies for maintenance and management. The problem is convenient, and an economical treatment method and device can be developed to complete the present invention. Hereinafter, the multi-stage continuous drainage suppression type anaerobic digestion treatment device that is not shown in FIG. 1 but shown in FIG. 6 will be described in further detail, and the use thereof This device 9 paper sizes are applicable to Chinese National Standards (CNS) Λ4 specifications (210X29? Male foot) (Please read the precautions on the back before filling out this page) • Equipment-Printed by the Consumer Standards Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs " 4 5881 8 A7 B7 V. Anaerobic digestion treatment method for high-concentration organic waste according to the invention. The multi-stage continuous suppression anaerobic digestion treatment device of the present invention is capable of continuously performing the anaerobic digestion treatment process of high-concentration organic waste in a reaction tank. FIG. 1 illustrates the necessary structures of these reaction stages in detail . The anaerobic digestion treatment device of the organic waste of the present invention shown in Table 75 in the drawing is only an example of a device indicating a method for treating waste according to the principle of the present invention. When the method of the present invention is performed, Its shape or structure can be variously deformed. These modifications should be regarded as belonging to the present invention, and the drawings are to make the present invention easier to explain. In the present invention, it must be noted that no matter what method is used, the invention should not be made. The long-stay multi-stage continuous anaerobic digestion treatment device of the present invention can be roughly divided into main components such as a main body 1 return device, a deodorization device (35), a gas storage and utilization device, and a boiler device. The body contains a body, which includes waste input G (1), an oxidation decomposition reaction tank (2), a reduction decomposition reaction tank (3), a stabilization tank (4), an underflow tank (5), and a gas underflow tank (6) , A phase separation membrane (7, 11), a flow speed adjusting sheet (9), a movable internal gas underflow plate (10), and a gas exhaust pipe (I5). In this type of abject surname digestion device, it is mainly characterized by having an oxidation decomposition reaction tank (2), a reduction decomposition reaction tank (2) which can separate the oxidation and reduction decomposition stages in the digestion reaction stage and continuously carry out the reaction by gravity. 3) 'The underflow structure passing through the stabilization tank (4.) and the underflow tank (5), and the concentration characteristics of solid substances that can be targeted at the caster. 10 This paper size applies the Chinese National Standard (CNS) A4 specification (210 × 297 mm) ) -------- A ------ 1T ------ ^ (谙 Please read the notes on the back before filling in this page) A7 B7 Stamps 5 of Consumer Cooperatives of Central Standards Bureau, Ministry of Economic Affairs 2. Description of the invention (q) and the position of the tank separation membrane (7, ii) that regulates the residence time of microorganisms in the reaction tank, the setting position of the flow rate adjustment plate (9), and the bottom tilt can be changed to move solid matter, etc., in the body The oxidation decomposition reaction tank (2) and the reduction decomposition reaction tank (3) 'are connected to the redox separation membrane, and the bottom surface of the oxidation decomposition reaction tank (2) and the reduction decomposition reaction tank (3) is to make the oxidation Decomposed reaction tank (2) The disposable was moved so easily, which is made inclined surface. The underflow tank (5) is located below the inclined surface of the oxidation decomposition reaction tank (2) and the reduction decomposition reaction tank ¢ 3), and between the reduction decomposition reaction tank (3) and the stabilization tank (4), there is a T Type reduction reaction separation membrane (1 1). Further, it is structured that the reduction decomposition reaction tank (3) is provided with a gas underflow tank (6), an internal gas underflow plate (8), and a flow rate adjusting plate (9), and a gas exhaust pipe (15) is provided above = T-type reduction reaction separation membrane (11) has a mobile internal gas underflow plate (10) attached to it. The installation position of the tank separation membrane (" M 1), the flow speed adjustment plate (9), and the inclination angle of the aforementioned inclined surface should be considered in accordance with the retention period of the microorganisms in the reaction tank and in accordance with the concentration characteristics of the solid substance being injected. set up. The inclination angle is generally set within a range of about 5-17 degrees. An odor gas suction pipe (1 7) is connected around the inlet (1), and a return water spraying device (3 1) is provided above the oxidation decomposition reaction tank (2). The device is connected with an underflow tank (5). The stabilizing upper liquid is connected to the air-floating return pipe (19) which is supplied to the oxidation decomposition reaction tank (2). Inside the oxidation decomposition reaction tank (2), a lattice-shaped Arbitrary microorganism culture tank (13), with 11 paper sizes, applicable to China National Standard (CNS) A4 specification (210X297 mm) -------- 政 ----- 1T ------ 4 (Please read the notes on the back before filling out this page) A7 __ B7_____ printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. The invention (8) and the water level regulating pipe (1 4). Here, arbitrary microorganisms It refers to the existence in the environment department. In the aerobic state with oxygen, it can grow as aerobic microorganisms. In the aerobic state, it can grow as aerobic microorganisms. The number is difficult to estimate. Arbitrary microorganisms In this description, it is only used as a general A general term for microorganisms living in an extremely insufficient state. For example, in the present invention, microorganisms that live in the first stomach of cattle (commonly known as Rumen microorganisms) are used for cultivation. A gas is connected to the top of the reduction decomposition reaction tank (3) The exhaust pipe (15), all the gas generated during operation is desulfurized through the gas exhaust pipe (15.). The boiler equipment (2 1) is used to maintain the underflow tank (5) at about 20 ° C The constant temperature state of organic waste produced in the kitchen or the like passes through the input port (η and flows into the oxidative decomposition reaction tank (2) in the original high concentration state of the generated place. Part of the input is passed through the microbial Hydrolysate of body cell secretion, part of which will be oxidized to volatile organic acids and hydrogen and acetaldehyde and other components through the oxidation reaction stage. At this time, it can be prevented from occurring during the oxidation of the input Odor, and in order to ensure the fluidity of the liquid, it is necessary to properly supply the water, the stabilization liquid of the underflow tank (5) C is returned through the air-float return pipe (1 9). The return water spraying device (3) is evenly distributed to the oxidation decomposition reaction tank (2). The residence time of the input waste in the oxidation decomposition reaction tank (2) depends on the type of waste, Concentration, whether it is necessary to re-use the generated gas *, the separation interval of the separation membrane, and the inclination of the inclined surface, etc. 12 This paper size applies the Chinese National Standard (CNS) Λ4 specification (210 × 297 cm), binding (please know first Note on the back of the occasional reading, please fill out this page again) A7 458818 ___ B7_______ 5. The description of the invention (?) To decide. In addition, in order to promote the oxidation reaction, the invention sets a grid shape in the oxidation decomposition reaction tank (2) The arbitrary microorganism culture tank 'can accumulate and supply a specific arbitrary microorganism group manufactured in a bullet shape at a high concentration. The waste is decomposed into organic acids, acetaldehyde, etc. through an oxidative decomposition reaction at one time, and then moved by gravity along the inclined surface (21) to the legacy degradation reaction tank (3). In the reduction decomposition reaction tank (3), methane, carbon dioxide, and ammonia gas are formed by the gasification of methanizing microorganisms, and a gas pressure is generated in the inner gas underflow tank (8). The mobile internal gas underflow plate (10) set on the T-type reduction reaction separation membrane (11) rises by the buoyancy of the bottom gas, and also causes the sludge at the bottom of the inclined surface to float up. When the internal pressure of the underflow tank (6) reaches 0.1-0.1 5kg / Cm2, the role of the pump (25) is automatically adjusted by the gas pressure connected to the gas discharge pipe (15), and the gas is discharged. At this time, the gas underflow plate (10) It goes down with the water level. As mentioned above, the effect of the water level change and the drainage of the gas level caused by the underflow of gas and the rise and fall of the mobile gas underflow plate (10), so that the process of contacting the sludge and microorganisms with each other is completely automatic. The bicarbonate component produced during the reductive decomposition process maintains the pH 値 of the reductive decomposition reaction tank (3) at the level of a building, and is used in the oxidative decomposition reaction 懵 (2). Too much organic acid is accumulated to prevent a decrease in pH and microbial activity. The solid matter passes through the reduction and decomposition reaction tank (3), sequentially moves to the stabilization tank (4), and is finally decomposed. As a result, about 5-7¾ (about 0.8-1.2¾ of feces and urine) is input into the whole body. The size of clay paper is applicable to Chinese National Standard (CNS) Λ4 specification (2! 0 × 297 mm) ----------------------- τ ------ {Please read first Note for the back to fill in this again 莨) Employees' Consumer Cooperatives of the Central and Central Bureau of the Ministry of Economic Affairs of the People's Republic of China printed and printed by the Ministry of Economic Affairs of the Central Standards Bureau of the Consumers' Cooperatives of the Department of Consumers' Printing Cooperatives and Printing 4 5881 8 a7 __B7__ 5. Description of the invention in. This residue is removed through the internal gas inspection port by cleaning the tank at a frequency of about 2-3 years (C feces and urine every 4-5 years). After the aforementioned oxidation and reduction reactions, the organic waste material is decomposed into a gaseous state. After the solid-liquid separation method, only sludge is left. The theoretical relationship between these processes is described in the following reaction formula (1). [Reaction formula 1] (Kitchen waste 3.3H20 3.55C02 + 3.55CH4 + 0.5NH3 That is, in order to anaerobic decomposition of 100kg of food waste (solid content 20%), about 5.81 moisture is required. Expect The generated gas is about 16.5m3 (1.03m3 gas / kg VS / d), and the actual result is that 0.77m3 gas / kg VS / d is generated below the middle temperature, and about 0.3m3 gas when operating without heating / kgVS / d. On the other hand, the average amount of moisture contained in kitchen waste is about 81%, of which 5,5¾ is consumed by the gas reaction of organic waste, and about 4.5¾ is in the form of water vapor. It co-evaporates with the gas, and the remaining approximately 7 15¾ is removed by evaporation during the retention time. The residue moves to the stabilization tank (4) through the reduction decomposition reaction, and then together with the additional decomposition, it is left with only sludge. Stable state. In addition, the stabilization tank (4) has the function of a regulating part by adjusting the excess of the water level change by the gas generated from the reduction and decomposition reaction. The residue moves to the underflow tank (5) and accumulates. Until the cleaning period. Device damage caused by cold damage in winter, and this paper size applies Chinese National Standard (CNS) Λ4 size (210x 297 cm) Binding — "(Please read the precautions on the back before filling this page)榡 Quasi Bureau Shellfish Consumer Cooperative Co., Ltd. 4 Ε _Ή 1 s A 7 B7 _____ V. Description of the Invention (ll) For the purpose of improving the processing efficiency, a boiler device (21) with an automatic temperature adjustment device is installed to maintain the underflow tank The temperature is about 20 ° C. The gas generated in the processing device of the present invention is stored in a gas storage facility after the desulfurization stage, and then reused as needed. As shown in Figure 2, the gas passes through the exhaust pipe (15) The gas is automatically closed by the valve (25) and discharged to the desulfurization device (26). The gas compression pump (27) is stored in a gas container (M) at a pressure of about 10 kg / cm2. Then, use it when necessary. The average dry content of sulfur in the kitchen waste is about 0.54¾. This desulfurization device must be installed to avoid corrosion of the device when the gas is reused. As shown in Figure 5 Desulfurization The structure of the present invention can be applied to various desulfurization devices, and here is a closed type desulfurization container using a dry method. The filling material (44) for desulfurization, iron oxide (Fe03 ) The oxidant is added, and the sulfur component in the replacement gas is replaced by iron sulfide. The relationship is shown in the following reaction formula 2. Fe03 * 3H20 + 3Ητ «-► 2FeS + 6H20 will be heated by the generated iron sulfide, It is brought into contact with air to be able to regenerate back to iron oxide. Generally, recycling can be performed about 2-5 times. In the present invention, in the process of digesting and treating organic waste, the odorous components in the waste are decomposed by the blower (36) through the suction pipe (17) of the oxidation decomposition reaction tank (2) and The inhalation □ of the bottom sulfur tank (5) is forcibly inhaled, moves to the main pipe (33) through the malodor transfer pipe (22), and flows into the deodorizing device (35). Binding M (Please read the notes on the back before filling in this page) This paper size applies to Chinese National Standards (CNS) Λ4 specifications (210X 297 mm) After the Central Bureau of Standards, Beiya Consumer Cooperative, India A7 B7 5 2. Description of the invention (α) The diameter of this pipe (33) for malodor transfer is suddenly enlarged by about 3 times compared to the diameter of the transfer pipe (22), so all the malodor components have flowed in at a reduced flow rate. Deodorizing device (35). The odorous gas shown in Figure 4. The odorous component flows into the filter layer (40) at the bottom of the deodorizing tank through the pipe (33), and the dust and moisture contained in the odorous component are removed here. Filtration, in addition, the accumulated moisture is discharged through the dirt discharge port (55). In order to remove this kind of dirt, the bottom of the deodorization facility is designed with an inclination of about 3-5 °. The malodorous components pass through After filtering the components, it is transferred to the support layer (42) filled with crushed stones through the transfer pipe (41), and then flows into the deodorizing layer (48) of the calendar, and is removed by physical adsorption and biological nitrification process 1 Various odor components such as gas. Not found in sawdust deodorizing layer (48) The removed malodorous components will further flow into the soil deodorizing layer (49) for adsorption and decomposition by soil microorganisms, and then flow into the deodorant layer (51) through the transfer pipe (50). 1 The remaining ammonia, Biologically difficult to decompose hydrogen sulfide, trace amounts of CH3SH and other components, excellent deodorants for the above components, and, for example, mixed with nutrients (iron, phosphorus, manganese) used to cultivate radon concentration microorganisms and microbial growth The Ecosob solution is contacted. The deodorant is discharged to the return pipe (56) through the discharge port (54), and then returned to the lower filter layer (40). After the deodorization facility is retained to the greatest extent Wait for the dirt to be discharged through the discharge port (5 5). Further, after the uppermost filter layer (52) is filtered again, it is discharged to the atmosphere through the final discharge port (53) of the malodorous substance. The purpose of the return system shown in 5 is to supply the stabilization solution of the underflow tank (5) to the oxidation decomposition reaction tank (2), and the Chinese national standard (CNS ) Α4 specification (210 × 297 mm) (Please read the precautions on the back before filling out this page]. Binding 18 18 Printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs ^ A7 B7 Five 'Invention Note (β) The air floating type is the most "Ideal" This method uses a return blower (IS) to float the upper liquid of the underflow tank (5) by the buoyancy caused by the air supplied to the air supply pipe (45), and passes the return pipe (1 9 ) Forced spraying is carried out with a return water spraying device (31). The air supply pipe (45) of the returning device is ideally about 1- 5-1 / 1.0 times the diameter of the return pipe (I9), and is set at the bottom From 3/8 the position is better. Fig. 6 shows an engineering drawing, which is a method of processing related to the feces and kitchen waste generated by general toilets. The feces are transferred to the anaerobic digester through the inclined transfer pipe (47) below, The inputted kitchen waste undergoes anaerobic digestion through the aforementioned decomposition process. Therefore, if the method for treating kitchen waste and faeces of the present invention is used: First, the kitchen waste can be diluted and processed directly in a high concentration state where it occurs, and second, because it can be directly processed in the place where it occurs, It can effectively solve the problems of corruption and malodor generated during its transfer and hoarding. 3. The methane gas, a by-product of the treatment process, can produce about 0.3 m3 gas / kg VS / d, so this energy can be reused. 4. Because the residue of the treatment does not exceed about 5-7¾ (about 0.8-1.2% of feces and urine), the maintenance and management-related treatment costs are less and more economical. 5. Because of the oxidation reaction decomposition tank and reduction reaction decomposition The tank and the stabilization tank are all set in a reaction tank, which can be independent continuous stages, and the 17 paper sizes are applicable to the Chinese national standard ί CNS) Λ4 specification (210 × 297 g t) ---------- Pack ------ order ------ M (read the precautions on the back before filling out this page) Printed by the Employees' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 458818 5. Explanation of the invention (/ f) This complementary stage To continue i so you can Suppresses the occurrence of discharged water and solves the legal regulations related to the discharged water. Here, the so-called "complementary phase", the anaerobic alkaneification process mainly refers to the two functions of acid fermentation and methane fermentation Each is achieved by acid-forming microorganisms and methane-forming microorganisms. This complementary meaning means that during the decomposition of the two microorganisms, the acid-forming microorganism RJ converts organic substances into acidic substances, and methanated microorganisms use acidic substances- On the one hand, it produces methane, and on the other hand, it supplies acid to form basic substances necessary for the normal operation of the reaction tank. Because these substances cannot be exchanged with each other under proper conditions, it is difficult to operate normally. Such an action phase is called a complementary phase. Further, as shown in FIG. 6, when a simple old-style toilet is installed together in a playground or the like, the feces and urine system of the toilet is directly injected into the oxidation through the inclined transfer pipe (47) below. In the decomposition reaction tank, the food waste is injected through the input port (1) exposed on the ground. Because food waste and urine are processed at the same time, 'there is no need to add additional processing equipment, which can be digested and decomposed by itself, so maintenance and management problems can be minimized. At this time, the height of the anaerobic treatment device must be at least It is more than one meter higher than the toilet bowl of the toilet. This condition is extremely important for maintaining and setting. In the following embodiments, the present invention will be described in more detail through examples. However, the present invention is not limited to these examples. Within the scope of Example 1. As shown in Figure 1, the specifications of the processing device of the present invention are detailed. 18 This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) (Please read the precautions on the back first) Refill this I)
L 丁 458 8 1 A7 B7 五、發明説明（K ) 表示於表1，使用本裝置可以將在大餐廳所產生之廚房廢 棄物以及人的排泄物等，各自獨立地進行厭氣性消化處 理。 經濟部中央標準局員工消費合作社印紫 表1 Mi 3S 機器明細 備註 厭氣性消化處理裝置 28m3 (有效容積25 m3) 內部覆膜鐵板 本體 微生物培養槽（13) 0.3X0.3X0.3 m3 格子形的箱子 氣體開關閥門（25) 0,1-0.15kg/cm3 握力型圓筒型線圈閥門 返送用送風機08) 40升/分 空氣浮起之幫浦甩 安全排氣管（I9) 微量殘留氣體排岀周 說硫裝置（26) 直徑0.3，高0.75 密閉式 脫臭設備（35) 0.45X0—45X1.5 m3 土壤脫臭式 氣體壓縮幫浦（27) 壓縮力l〇kg/cm3 氣體貯藏容器（28) 容器容量：10天份 產生氣體的底流 氣體燃燒口（ 29) 產生氣體的再利用設備 鍋爐設備（21) 自動溫度調節式 -~- 加溫 泥渣檢查棒 長4.5 檢查口的泥渣高度檢查 控制板 1 涘Μ墦的楹作調節 ^木 訂I ， (請先閱讀背而之注意事項再填寫本頁) 收集在大餐廳所產生之飮食加工前後的廢棄物，將塗 膠袋等不可能分解的廢棄物分離除去之後，將其投入一天 約5 0kg、有效容量2 5«^規模的處理裝置中。所產生之廢 19 本紙張尺度適用中國國家標準（CNS ) Λ4規格（210X297公漦） 經濟部中央標準局肩工消費合作社印^ ^ 4 5 B y 1 A7 ___B7 五 '發明説明（It ) 棄物固態物質的含量約爲1 6-2 1 %，平均約爲1 9%，又， 有機物的含量約爲7 8-83 ¾ ，平均約爲80¾。其中，骨類 約爲49½ (重量比）爲第一多，其次依序爲肉類、蔬菜、 等其他。在飮食廢棄物投入前，試驗初期的處理裝置中， 將目的在造成厭氣性環境的甲烷槽（還原分解臣應嘈）， 其兩端的分離膜在可浸潤的程度κ，加人水、人糞、雞蓂 等，而利用裝置內的空氣在此迅速的分解作用之下將其除 去。在小規模的室內硏究階段中，以水將兩端充滿，再灌 入氮氣體以造成厭氣性環境。 然後，開始加入廚房廢棄物以及糞尿等，約經過20 天後氣體的發生量到達安定的階段。 藉由本實施例所進行之廚房廢棄物以及糞尿等處理裙 果·表示於下式表2。 表 2 _______ 廚房廢棄物 糞尿 流入 上澄液 其他 流入 上澄__ 其他 i—— 項目 濃度 濃度 項目 結果 項冃 濃度 項目 結果 pH 3.88 7.24 氣體 0.30 r^ pH 7.82 7.86 氣體 0.13 量 量 TS/VS 19/81% 0.6/0.27 i 甲烷i69% r — TS/VS 2.4 2.3 0.52/0.21 甲烷 66% 含量 含量 BOD 14,76% - 2665 mg/i 泥渣 7.5% BOD 2.1% 1547 mg/1 泥渣 0.8% 量 __ 量 本紙張尺度適用中國國家標率（CNS ) Λ4規格（210X297公麓） I ....... JU m ϊ^ιϋ 一 s - - I· ^11^1 ^^^^1 ^^^^1 (诗先閲讀背而之注意事項再填寫本頁) B7 B7 經濟部中*標隼局員工消費合作社印製 五、發明説明（IΊ) TOC 22.7% 6367 mg/1 有機 酸 3840 TOC 2.68% 842 mg/1 有機 酸 143 TKN 2.18% 1104mg/l 鹼性 程度 3853 TKN 0.51% 1 | 1433 mg/1 i鹼性 1程度 4333 *其他項目之實測値爲常溫條悴下，檢查口與投入□皆密 閉狀態下之測定値， *泥渣量爲殘留泥渣量相對於投入流量的％ -氣體：m3氣體/kg VS/d，有機酸：mg·醋酸/升，鹼性度： mg，碳酸耗/升。 前述之結果，係爲1995年2月開始到現在爲止之無 排出水狀態資料。利用物質不滅來檢查水分變化，其結果， 投入水分約有6.8%被利周於反應上，約5.5¾與氣體一起 供同以水蒸氣的方式發散，剩下的約87.6¾則従檢查口與 投入口的表面蒸發，由此而得之所有水分蒸發的方式。因 ，利用本發明*含有廚房廢棄物及糞尿的有機性廢棄物 之處理，係爲相當時間內即使無排出水的情況下亦可進 行。殘留的廢棄物發生亦在10¾，所以要維持設備等所須 之費用可以減至最少= 發明的效果 本發明之方法及裝置，係改良現存之厭氣性消化技 術，而生產出最少的泥渣，解決了排出水的發生問題，同 時1在維持、管理方面也不需要高度的技術的一種消化處 理方式。藉由這種系統處理廚房廢棄物時，不用稀釋發生 處所之物質而直接以高濃度狀態來處理，投入物約有93¾ 21 本紙張尺度適用中國國家標準（CNS ) Λ4規格（210X 297公嫠） 裝 I 訂 知 (請先閱讀背面之注意事項再填符本頁) 經濟部中央標準局員工消費合作社印製 -Obj1 - A7 ___B7___ 五、發明説明（） 藉由蒸發及分解，以水分、甲烷及二氧化碳的型態被除去 之後，剩下的約7¾的泥渣與水分的殘留物，只要以每2-4 年的頻率一次來掃除，即可解決維持及管理的問題。 圖示之簡單說明 圖1:藉由本發明提供之高濃度有機性廢棄物之多段 連續式厭氣性消化處理裝置之斷面工程圖。 圖2:藉由本發明提供之高濃度有機性廢棄物之多段 連續式厭氣性消化處理裝置之平面工程圖。 圖3:藉由本發明提供之髙濃度有機性廢棄物之多段 連纘式厭氣性消化處理裝置之側面工程圖。 圖4:藉由本發明提供之脫臭裝置的構造圖與惡臭移 送管之非配構造圖。 圖5:藉由本發明提供之脫硫裝置與空氣浮上式返送 裝置之構造圖。 圖6:藉由本發明提供之高濃度有機性廢棄物之多段 連續式厭氣性消化處理裝置，所構成之廚房廢棄物與糞尿 的混合處理工程圖。 符號的說明 1. 投入口 2. 氧化分解反應槽 3 ·還原分解反應槽 4. 安定槽 5. 底流槽 6. 內部氣體底流槽 本紙張尺度適用中國國家標準（CNS ) Λ4規格（2!0X 297公釐） u^i -I i---l— ^^—-1 - —-—I- ^^^^1 —.n ^ϋ.— nn - f^i ^111 n ^ u? Ί-^, (請先聞讀背而之·ii意事項再填寫本頁) 4588 1 8 A7 經"部中央標準局員工消費合作社印繁 B7五、發明説明（^ ) 7 .氧化還原分解膜 8 .內部氣體底流板 9. 流動速度調節板 10. 移動式氣體底流板 11. T型還原反應分離膜 12. 傾斜面 13. 任意性微生物之培養槽 14. 水位調節管 15. 氣體排出管 17. 惡臭氣體吸入管 18. 返送用送風機 19. 返送管 20. 溫水供給管 21 . 鍋爐設備 22. 惡臭吸入管 24. 污泥及水分捕捉機 2 5. 氣體自動開關元件 26. 脫硫裝置 27. 氣體壓縮幫浦及流量劑 28. 氣體貯藏容器 30. 泥渣剪斷用鋸齒 31. 返送用水噴灑裝置 32. 鍋爐設備用上澄液吸入管 35. 脫臭設備 --------扯衣------、玎------^ (請先閱讀背'&之注意事項再填寫本買) 本紙張尺度適用中國國家標準（CNS ) A4規格（2〗0X 297公釐） 經濟部中央標準局員工消費合作社印製 4 588 1 8 五、發明説明（>。） 3 6. 惡臭移送用送風器 40. 過濾層 41. 50.移送管 42. 支持層 44 . 脫硫用充塡物 45 . 返送用空氣供給管 4 7. 傾斜移送管 48. 鋸屑脫臭層 49. 土壤脫臭層 5 1 . 脫臭劑層 52. 過濾層 53 . 最終排出口 54. 排出口 5 5. 污物排出口 56. 返送管 ---------裝------訂------纹 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐）L Ding 458 8 1 A7 B7 5. The invention description (K) is shown in Table 1. Using this device, the kitchen waste and human waste produced in the large restaurant can be independently processed for anaerobic digestion. Ministry of Economic Affairs, Central Bureau of Standards, Consumer Consumption Cooperative, printed purple watch 1 Mi 3S machine details Remarks Anaerobic digestion treatment device 28m3 (effective volume 25m3) Internally coated iron plate body microorganism culture tank (13) 0.3X0.3X0.3 m3 grid Shaped box gas switching valve (25) 0,1-0.15kg / cm3 Grip cylinder coil valve return blower 08) 40 liters / minute air floating pump dump safety exhaust pipe (I9) trace residual gas Desulfurization and desulfurization device (26) 0.3 diameter, 0.75 height closed deodorization equipment (35) 0.45X0—45X1.5 m3 soil deodorizing gas compression pump (27) compression force 10kg / cm3 gas storage container (28) Vessel capacity: Underflow gas burner that produces gas in 10 days (29) Gas reuse equipment Boiler equipment (21) Automatic temperature adjustment-~-Heating sludge check rod length 4.5 Sludge at the check mouth Operation control of the height check control board 1 涘 Μ ^ wooden order I, (please read the precautions before filling this page) Collect the waste before and after the food processing in the large restaurant, and put the plastic bag Waste that cannot be decomposed After the waste is separated and removed, it is put into a processing device of about 50 kg a day and an effective capacity of 25 «^. Waste generated 19 This paper size is applicable to Chinese National Standard (CNS) Λ4 specification (210X297 gong) Printed by the Central Laboratories of the Ministry of Economic Affairs and Consumer Cooperatives ^ ^ 4 5 B y 1 A7 ___B7 Five 'Invention Note (It) Waste The solid matter content is about 16-2 1%, with an average of about 19%, and the organic matter content is about 7 8-83 ¾, with an average of about 80¾. Among them, bones are about 49½ (weight ratio) first, followed by meat, vegetables, and others. Before the incineration waste was put into operation, in the treatment device in the initial stage of the test, the methane tank (reduction and decomposition) should be used to create an anaerobic environment. Human feces, chicken gizzards, etc. are removed by the rapid decomposition of the air in the device. In a small-scale indoor research phase, the ends are filled with water and then filled with nitrogen to create an anaerobic environment. Then, the kitchen waste and urine were added, and the amount of gas generation reached a stable stage after about 20 days. The processing wastes such as kitchen waste and feces in this example are shown in Table 2 below. Table 2 _______ Kitchen waste faeces flowing into Shangcheng liquid Other flowing into Shangcheng__ Other i—— Item Concentration Concentration Item Result Concentration Item Result pH 3.88 7.24 Gas 0.30 r ^ pH 7.82 7.86 Gas 0.13 Volume TS / VS 19 / 81% 0.6 / 0.27 i methane i69% r — TS / VS 2.4 2.3 0.52 / 0.21 methane 66% content BOD 14,76%-2665 mg / i sludge 7.5% BOD 2.1% 1547 mg / 1 sludge 0.8% __ The size of this paper is applicable to China National Standards (CNS) Λ4 specification (210X297 Gonglu) I ....... JU m ϊ ^ ιϋ s--I · ^ 11 ^ 1 ^^^^ 1 ^ ^^^ 1 (Read the poem first and then fill in this page) B7 B7 Printed by the Ministry of Economic Affairs * Standards Bureau Employee Consumer Cooperatives V. Invention Description (IΊ) TOC 22.7% 6367 mg / 1 Organic Acid 3840 TOC 2.68% 842 mg / 1 organic acid 143 TKN 2.18% 1104mg / l alkalinity level 3853 TKN 0.51% 1 | 1433 mg / 1 i alkalinity level 1 4333 * The actual measurement of other items is under normal temperature, check the mouth and input □ Measurement in a closed state 値, * The amount of sludge is the percentage of residual sludge relative to the input flow-gas : M3 of gas / kg VS / d, an organic acid: mg · acetic acid / liter, basicity: mg, consumption carbonate / liter. The above results are data on the state of no discharged water from February 1995 to the present. Use the material to check the moisture change. As a result, about 6.8% of the input water is used to facilitate the reaction. About 5.5¾ is supplied with the gas and is emitted in the form of water vapor. The remaining about 87.6¾ is checked by the inspection port and The surface of the inlet is evaporated, so that all the water evaporates. Therefore, the treatment of the organic waste containing kitchen waste and feces using the present invention * can be carried out without a discharge of water for a considerable period of time. The residual waste also occurs at 10¾, so the cost required to maintain the equipment can be minimized = the effect of the invention. The method and device of the present invention improve the existing anaerobic digestion technology and produce minimal sludge. It solves the problem of the occurrence of discharged water, and at the same time, it is a digestion treatment method that does not require high technology in maintenance and management. When using this system to treat kitchen waste, it is directly treated in a high concentration state without diluting the material in the place where it is produced. The input is about 93¾ 21 This paper size applies to the Chinese National Standard (CNS) Λ4 specification (210X 297 cm) Installation I Order (Please read the notes on the back before filling in this page) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs -Obj1-A7 ___B7___ 5. Description of the invention () By evaporation and decomposition, water, methane and After the type of carbon dioxide is removed, about 7¾ of the remaining sludge and moisture residues can be removed once every 2-4 years to solve the problems of maintenance and management. Brief description of the figure Figure 1: Sectional engineering drawing of a multi-stage continuous anaerobic digestion treatment device with high-concentration organic waste provided by the present invention. Figure 2: Plane engineering drawing of a multi-stage continuous anaerobic digestion treatment plant with high-concentration organic waste provided by the present invention. Figure 3: A side engineering drawing of a multi-stage flail anaerobic digestion treatment device with organic waste of radon concentration provided by the present invention. Fig. 4: A structural diagram of a deodorizing device and a non-arranged structural diagram of a malodor transfer pipe provided by the present invention. Fig. 5: Structure diagram of a desulfurization device and an air-float return device provided by the present invention. Fig. 6: A mixed treatment engineering drawing of kitchen waste and feces formed by a multi-stage continuous anaerobic digestion treatment device with a high concentration of organic waste provided by the present invention. Explanation of symbols 1. Inlet 2. Oxidation decomposition reaction tank 3 · Reduction decomposition reaction tank 4. Stabilization tank 5. Underflow tank 6. Internal gas underflow tank This paper applies the Chinese National Standard (CNS) Λ4 specification (2! 0X 297 Mm) u ^ i -I i --- l— ^^ —- 1-—-— I- ^^^^ 1 —.n ^ ϋ.— nn-f ^ i ^ 111 n ^ u? Ί- ^, (Please read the back of the page and read the meaning of the matter, and then fill out this page) 4588 1 8 A7 Economic " Industrial Consumer Cooperatives of the Central Bureau of Standards Printing Co., Ltd. B7 V. Invention Description (^) 7. Redox Decomposition Film 8 Internal gas underflow plate 9. Flow rate adjustment plate 10. Mobile gas underflow plate 11. T-type reduction reaction separation membrane 12. Inclined surface 13. Arbitrary microorganism culture tank 14. Water level adjustment pipe 15. Gas exhaust pipe 17. Foul gas suction pipe 18. Return fan 19. Return pipe 20. Warm water supply pipe 21. Boiler equipment 22. Odor suction pipe 24. Sludge and moisture trap 2 5. Automatic gas switching element 26. Desulfurization device 27. Gas compression pump and flow agent 28. Gas storage container 30. Saw for cutting sludge 31. Water spraying device for returning water 32. Upper liquid for boiler equipment Into the tube 35. Deodorizing equipment -------- pull clothes --------, 玎 ------ ^ (please read the precautions of the back '& before filling in this purchase) Applicable to China National Standard (CNS) A4 specification (2〗 0X 297 mm) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 4 588 1 8 V. Description of the invention (>) 3 6. Odor transfer air blower 40. Filter layer 41. 50. Transfer tube 42. Support layer 44. Filler for desulfurization 45. Air supply tube for return 4 7. Inclined transfer tube 48. Deodorizing layer for sawdust 49. Deodorizing layer for soil 5 1. Deodorizing Agent layer 52. Filter layer 53. Final discharge port 54. Discharge port 5 5. Dirt discharge port 56. Return pipe (Please read the notes on the back before filling out this page) This paper size is applicable to China National Standard (CNS) A4 specification (210X297 mm)