TW513386B

TW513386B - Treating method for organic substance containing waste liquid and its equipment

Info

Publication number: TW513386B
Application number: TW87115407A
Authority: TW
Inventors: Akihiro Ochi; Taro Hara
Original assignee: Toyo Clean Kagaku Kk
Priority date: 1997-10-07
Filing date: 1998-09-16
Publication date: 2002-12-11
Also published as: JPH11116368A; KR19990036792A

Abstract

This invention provides the treating method for organic substance containing waste liquid and its equipment to obtain fine composite or liquid fertile. The treatment comprises the following steps, such as: shit or urine etc containing waste liquid was separated in the first solid-liquid separation treatment, to recycle low specific gravity coarse solid object, for example: plastics, rubber, and high specific gravity coarse solid object, for example: metal, sand etc; and organic fibers that can not be separated by the said first solid-liquid separation treatment was separated recycled in the second solid-liquid separation treatment, and post-treatment were further conducted by other mechanical means, such as solid-liquid separation, dehumidify and incineration treatment or dehumidify and composite treatment.

Description

登明所屬的技術領域沪右物之廢液之處理方法及裝置，尤濟驗行蜮之液肥減良質之^ίϊ 習知拮術 μ 習知的原巧處理方法，於本申請人之日本特公昭 t42^78號公報揭示的「將含有至少麟分解_、纖維素 ^刀解_、蛋白分解論之酵素製劑，對未處理的動物糞尿等之含有機物廢液，添加〇· 〇1〜〇· 05重量％，其次進行固液分離處理，分離出此含有機物之廢液中的固形物後，所得。的濾、，在25〜50Nm3/BODkg/日之曝氣條件，且在5〇〜8〇 C之高溫條件下，施以喜氣性的高溫發酵處理，成為弱鹼性之液肥」，係眾所周知的。此處理方法，具體而言，係以第3圖所示的順序進行。亦即，將藉由没取車101汲取，運送的尿，中介以汲取車之軟管101a ’投入投入槽2内，藉由該投入槽與連接於投入槽之調整槽103之間設置的有效網目寬度約20刪之棒條篩網102a，粗大的石塊或金屬片或木片等i〇2b經予去除的原尿’則流入調整槽103内並予貯留著。於前述調整槽103内所貯留的尿中，自酵素劑添加裝置104，添加酵素製劑，例如「淨化clean」（商品名：東洋clean化學股份有限公司製造）。其次，由壓縮空氣源1〇5 介由壓縮空氣吹入管路106，由已予設置於調整槽之底部 513386 Λ7 B7 五、發明説明（經濟部中央標隼局員工消費合作社印製的喷嘴頭106h，藉由被吹入屎尿中的壓縮空氣邊予氣擾拌屎尿，邊使酵素製劑與屎尿反應約24小時^違卞二乳攪其後，屎尿係藉由設置於調整槽底部之切斷器筒 107 ’對橡膠、塑膠、布類、其他的粗大異物切割，同時吸取，並予傳送至下一個固液分離裝置之旋轉鼓輪型篩網1〇8 上0 此固液分離裝置108，係採用細縫寬度〇·3〜1ππι之篩網，由屎尿分離出如前述般以切斷器唧筒切割的橡膠、塑膠、布類、其他之屎尿中的異物，與以有機物為主體之較細的紙纖維類之混合物而成的央雜物，利用螺旋壓榨機 108a ’脫水至含水率約60%為止。經予脫水的固形物，則祐排出至固形物承接容器i〇8b内。 ^ am 其次，使此夾雜物分離、脫水的尿濾液，係被送入使曝氣唧筒109浸入該槽之底部的第1之喜氣性高溫發酵槽 110内，再予送入使曝氣唧筒111浸入該槽之底部的第^之喜氣性高溫發酵槽112内。在前述第1、第2之喜氣性高溫發酵槽，將槽内之屎尿在25〜50 Nm3 /BODkg/日I曝氣^^ ，，子50〜80°C之高溫條件下，通常施以約28〜30 i之喜氣性南溫發酵處理後，將所得的液肥，送至液肥貯槽U3 内並予貯存。且’在前述固液分離裝置108，由尿分離、脫水至含水率約60°/。的固形物，在大氣下令其自然發酵即成堆肥，與前述的液肥，亦可同時被利用作肥料。 ^ (請先閲讀背面之注意事項再填寫本頁) ;裝_ 訂本紙張尺度適用中國國家標準（CNS ) Α4規格（210Χ297公釐）經衣奶-1 η 澄欲解決的誤顥且因扮於t之處理’係至少使其B〇D值降低，以蟲卵、釣蟲幌、尿中二氮以;鉀ί 液肥之點上優越的方法，惟仍膠(、$ si^v03魄予空_拌，尿巾之橡膠、塑 t处ΐίί比ϊ#父小，且尺度較大的夾雜物，使與被吹入八二士 ^日料起於躲飾上，將之再度於液中均勻用事f ίϊΣ^。藉由被添加入調整槽之酵素製劑用妒pUf機Τ刀解，降低屎尿之黏性，提高固體與液體間之分離性，故上述現象可格外顯著。 ^如此，浮於屎尿液面，形成表層之夾雜物，作業員不以手作業向調整槽之外搔取的所謂原始且不衛生的方除，會增加作業員之負荷，同時較難使裝置成自動運軺化，裝置之運轉上所需的作業員數亦增多。旦又’由調整槽内液面被搔取的前述之夾雜物，由於大 ϊ言有屎尿之液成分，故未能在保持原狀下予以處分，乃進行下述的處理。 ① 藉由設置去除水分槽，於其中長時間貯存，將表面已達某種程度乾燥的部分裝袋，運送至焚燒場並予焚燒，進行掩埋處分。 ② 汲取於桶内，投入螺旋壓榨機内，脫水，並在焚化爐内焚燒。項 t 本紙張尺度適财@]國家縣（CNS)碰見格（21GX297公發）Dengming belongs to the technical field of waste water treatment methods and devices, especially in the field of liquid fertilizer reduction and good quality ^ ϊ 拮知拮术 μ The well-known skillful treatment method is in Japan Gazette No. t42 ^ 78 discloses "the enzyme preparation containing at least lysin, cellulose cleavage, and proteolysis, and organic waste liquid containing untreated animal feces and urine, etc. are added to 〇. 〇1 ~ 〇 · 05% by weight, followed by solid-liquid separation treatment, after separating the solids in the waste liquid containing organic matter, the obtained. The filtration, the aeration conditions of 25 ~ 50Nm3 / BODkg / day, and 50 ~ Under the high temperature conditions of 80 ° C, aerobic high-temperature fermentation treatment is applied to become a weakly alkaline liquid fertilizer ", which is well known. This processing method is specifically performed in the order shown in FIG. 3. In other words, the urine that is drawn and transported by the car 101 is put into the input tank 2 through the hose 101a 'of the pump, and the effective between the input tank and the adjustment tank 103 connected to the input tank The bar screen 102a with a mesh width of about 20 is deleted, and the coarse urine, such as a large stone or a metal piece or a wood piece, is removed into the adjustment tank 103 and stored. To the urine stored in the aforementioned adjustment tank 103, a self-enzyme adding device 104 is used to add an enzyme preparation, such as "purification clean" (trade name: manufactured by Toyo clean Chemical Co., Ltd.). Secondly, the compressed air source 105 is blown into the pipeline 106 through the compressed air, and it has been set on the bottom of the adjustment tank 513386 Λ7 B7 V. Description of the invention (Nozzle head 106h printed by the staff consumer cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs) With the compressed air blown into the feces, the feces are mixed with air, and the enzyme preparation reacts with the feces for about 24 hours. After that, the feces and urine are stirred by a cutter installed at the bottom of the adjustment tank. Cylinder 107 'Cut rubber, plastic, cloth and other coarse foreign materials, suck them at the same time, and transfer them to the rotating drum-type screen 1108 of the next solid-liquid separation device. A sieve with a slit width of 0.3 to 1πm is used to separate the foreign matter in the rubber, plastic, cloth, and other feces that are cut by the cutter tube as described above from the feces, and the thinner ones that are mainly organic matter. The central debris made of a mixture of paper fibers is dewatered to a moisture content of about 60% by the screw press 108a. The pre-dewatered solids are discharged into a solids receiving container i08b. ^ Am Next, Make this clip The separated and dehydrated urine filtrate is sent to the first aerobic high-temperature fermentation tank 110 in which the aerated drum 109 is dipped into the bottom of the tank, and then the first aerated drum 111 is dipped into the bottom of the tank. ^ The aerobic high-temperature fermentation tank 112. In the aforesaid first and second aerobic high-temperature fermentation tanks, the feces in the tank are aerated at 25 ~ 50 Nm3 / BODkg / day I ^^, 50 ~ 80 ° Under the high temperature condition of C, usually a 28 to 30 i aerobic south temperature fermentation treatment is applied, and the obtained liquid fertilizer is sent to the liquid fertilizer storage tank U3 and stored. And 'in the aforementioned solid-liquid separation device 108, urine The solids separated and dehydrated to a moisture content of about 60 ° /. Can be naturally fermented into compost in the atmosphere, and can be used as fertilizer with the aforementioned liquid fertilizer. ^ (Please read the precautions on the back before filling in this Page); Packing _ The size of the paper is in accordance with the Chinese National Standard (CNS) A4 (210 × 297 mm) Jingyimilk-1 η The mistakes to be resolved due to the treatment of 't' make it at least BOD The value is reduced, with the eggs, worms, and dinitrogen in the urine; potassium ί liquid fertilizer is superior Method, but still plastic (, $ si ^ v03 予予空拌 mix, rubber, plastic t ΐίί 比 ϊ # parent small, large-scale inclusions of diapers, so that they are blown into the 82 The material starts from the dome, and it is evenly used in the liquid again. F ί ^ Σ ^. The enzyme preparation added to the adjustment tank is used to solve the problem with the pUf machine to reduce the viscosity of feces and urine and improve the separation between solids and liquids. Therefore, the above phenomenon can be particularly significant. ^ In this way, floating on the surface of the urine and forming inclusions on the surface, the so-called original and unsanitary methods that the operator does not grab outside the adjustment tank by hand, will increase the work At the same time, it is difficult to automate the operation of the device, and the number of operators required for the operation of the device also increases. Once the aforementioned inclusions captured by the liquid surface in the adjustment tank have been said to contain the liquid components of feces and urine, they cannot be disposed of as they are, and the following processing is performed. ① By installing a dehydration tank and storing in it for a long time, the part whose surface has been dried to a certain extent is bagged, transported to an incineration plant and incinerated, and disposed of for disposal. ② It is drawn into a barrel, put into a screw press, dehydrated, and incinerated in an incinerator. Item t This paper is suitable for financial use @] County (CNS) meets grid (21GX297)

手作卖述理，亦又需要作業員之運轉化糊難，以轉作上#=業6〇V〇4±^©^ 經濟部中央標準局員工消費合作社印製 “勻，】與之混人，會使其厢的有機物ΐίΐimiiii呈ί，不均勻，結果’由於局部的阻水刀係自堆肥流出，成為整體堆肥之品質降低的原因。，再者，於堆肥之中，諸如以前述切斷器唧筒1〇7 & 的女性用衛生棉之包覆紙、或衛生棉條之筒條、^ ^市，之購物袋或褲襪等之聚氯乙烯或塑膠製等的失雜 =，若以與之分離的形式包含時，眼觸之印象亦惡劣，亦難成為良好的堆肥。 ③由於有上述的堆肥之品質降低，對前述夾雜物之堆肥化處理本身不存指望，再者有對夾雜物施以脫水、乾燥處理’進行焚化處理，又進行掩理之情形，僅不謀求用作有機物之堆肥的有效利用，或對處理需要額外的能量、費用、又需掩埋的情形，亦有成為土壤污染之原因的可能性。需 -------； ! “衣—— (請先閲讀背面之注意事項再嗔寫表f ) 訂本紙張从適用中國國家榡準（CNS)从祕（21Gx297公瘦 513386 Β7 五、發明説明（類(同3)等再大 112予以發_理，此、 =肥中，招致液肥之品質降低。又，此等 /刀或無機物在液肥散布用機器中會阻塞噴$ g 成内，亦成為料想不到的故障之原因。H飞賴4 (4)於前述液肥貯槽113内，由貯存中之沈降，若此無機成分堆積時，會使貯槽之f 刀運出的液肥之濃度會生成經時的分散性！之貫際谷積減知Hand-made selling theory, but also the operator's operation needs to be difficult, in order to switch to # = 业 6〇V〇4 ± ^ © ^ The Ministry of Economic Affairs Central Standards Bureau ’s Consumer Cooperatives printed "even," mixed with People will make their organic matter ΐίΐimiiii appear uneven and result in 'the local water blocking knife system flowing out of the compost, which will cause the quality of the overall compost to decrease. Moreover, in the compost, such as the aforementioned cutting Broken paper tube 1107 & women's tampons covered with paper, or tampons, ^ ^ city, shopping bags or tights, etc. made of polyvinyl chloride or plastic, etc. =, If it is contained in a form separated from it, the impression of the eye is also bad, and it is difficult to become a good compost. ③ As the quality of the above-mentioned compost is reduced, there is no hope for the composting treatment of the aforementioned inclusions, and In the case where the inclusions are dehydrated and dried for incineration treatment and masking, only the effective use of compost used as organic matter is not sought, or the treatment requires additional energy, cost, and landfilling. The source of soil pollution Requires -------;! "Clothing-(Please read the notes on the back before writing the form f) The bound paper is applicable from China National Standards (CNS) Cong Sei (21Gx297 public thin 513386 Β7 V. Description of the invention (Class (same as 3), etc.) 112 will be dealt with. This, = fat, will cause the quality of liquid fertilizer to be reduced. In addition, these / knives or inorganic substances will block the spray in the liquid fertilizer spreading machine. It is also the cause of unexpected failures. H Feilai 4 (4) settles during storage in the aforementioned liquid fertilizer storage tank 113. If this inorganic component accumulates, the f knife of the storage tank will be transported out. The concentration of liquid fertilizer will produce dispersion over time!

本發巧之課題，係消除上述的習知技術之問題點，調整槽内浮出於屎尿液面上的橡膠、塑膠等之比重蠻 ^需以人手搔取，人手進行後處理之作業，又上述的丄各酵的固形物，會混入成為堆肥材料之紙纖維類或肥原料之屎尿據液中，亦不致使堆肥之品質或液^巴之二暂降低，再者；提供上述的橡膠、塑膠等比重小，可容IThe subject of the present invention is to eliminate the problems of the above-mentioned conventional technology, and adjust the proportion of rubber, plastic, etc. floating on the surface of feces and urine in the tank. ^ It needs to be picked up by human hands, and the post-processing operations are performed by human hands. The solids of each of the above-mentioned fermented yeasts will be mixed into the waste liquid of paper fibers or fertilizer raw materials that become compost materials, and will not temporarily reduce the quality or liquid of the compost. Furthermore, provide the rubber, Small proportion of plastic, etc., can accommodate I

燃性固形物之處理的含有機物H處S 經濟部中央標準局員工消費合作社印裝本發明之另一課題，係於液肥貯槽内來自貯存中的肥之無機成分之沈降、堆積引起的實際容積之減少，. 出的液肥之濃度不致生成經時性的分散性，提供含有之廢液之處理裝置。豕紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） Λ7 B7 經濟部中央標準局貝工消費合作社印製五、發明説明（解決課題而摄之乎矜解為法，係將含有至少脂肪分的動物糞之含有機你蘇=解之酵素製劑，對未處理其次進，添加。_Q1〜。_。5重量％，形物後，所得的滹液1 ^出此含有機物之廢液中的固成為弱驗性之液肥的含有機物之廢液㉝方; 添加有機物之廢液，在橡膠、塑膠、布類、：刖述3有機物之廢液分離體)粗大固形成分之第也固金液屬i處砂，後等的(以無機“ _ίί^ί 離的第1濾液，添加備性的發H、在未滿G c的低溫下使生成預 …:發酵成堆肥，構成含有機物之廢液之處理。；離換5者本發明方别述* 1固液分離處理，於分離橡膠、娜、布類、其他金則、砂鱗之g大的^ 娜（21Gx2977公楚） ---------^ —裝------訂 (請先閲讀背面之注意事項再填寫本頁) 513386 A? B7 經濟部中央標隼局員工消費合作杜印裂五、發明説明（成分之際宜為個別採用具有直控6〜8mm之多數圓孔之謠板；前述第2固液分離處理，於分離以前述第丄固處理未能去除的有機物為主體之微細的紙纖維類之際，為採用具有與寬度0· 5〜1· 5刪之多數細縫或與之約&同黧的過濾效率之多數洞孔的篩板。〜寻在此，「具有約略同等的過濾效率」，係意指「以約略同等的效率可分離，過濾出約略同等的尺度之固形物以下採用相同的意義。〜」有再者，於本發明方法，對在前述第1固液分離處理分離的橡膠、塑膠、布類等比重較液成分小，且具可燃性之粗大固形物，再進行第3固液分離處理，將所得的可燁固2物脫水至指定的含轉為止後，靖之焚化為宜:於處理’以使用具有寬度1〜3咖之多數細縫或與之約略同4的過濾效率之多數洞孔的篩板為宜。人，為解決前述課題，於本發明裝置，係自汲取車 ” 官及管路，直接接納未處理的動物糞尿等含有機物 f廢液，分離出橡膠、塑膠、布類、其他金屬片、砂礫等粗大的固形成分之第1固液分離裝置，該第1固液分離裝置之濾液的貯存調整槽，整槽添加酵素製劑之酵素製劑添加裳置，搜才半則述調整槽中的濾液之調整槽攪拌裝置，有酵素製劑，使在低溫下進行預備性發酵反應的整液，分離出以在前述第1固液分離裝置未 g除的賴物為主體之微細的紙麟類之第2固液分離本紙張 -----!---^--^ 裝------訂 (請先閲讀背面之注意事項再填寫本頁) 513386 Λ7 B7 經濟部中央標準局員工消費合作社印製五、發明説明（ M由费納該第2固液分離裝置之濾液並予貯存，進行喜氣性的高溫發酵處理之複數槽而成的成熟槽，將該成，槽中的濾液曝氣之液中型曝氣裝置，接納在前述成熟槽而得的液肥，並予貯儲的液肥貯槽，攪拌該液肥貯槽中的貯藏液肥之液肥貯槽攪拌裝置，將以於前述第2固液分離裝置分離的有機物為主體之微細的紙纖維類脫水至指定的含水率為止的第1脫水裝置，接納由該第1脫水裝置脫水的紙纖維類，用作堆肥原料而貯存的纖維系固形物貯存手段，接納前述第1固液分離裝置分離的橡膠、塑膠、布類等比重較小，粗大的可燃性固形物，再進行固液分離第 3固液分離裝置，示、接納來自該第3固液分離裝置之可燃性固形物，進行脫水至指定的含水率為止的第2脫水襞置， $由運送手段，由該第2脫水裝置，接納可燃性固形 ^之ίίίΐϊίΐί^_物之焚化爐而構成含有機在前述第2 @液分離裝置及成熟槽之間，前述第2固液分離裝置之據液沈澱去除細砂 ϊΐίϊϊ除砂I置，將來自此除砂裝置的瀘、液移送中繼 ϋϊϊ ί ？者為將來自此中繼裝置之滤液連續且安定供、、、σ至刖述成熱槽而用的液肥原料貯槽。家標準(CNS )八娜(210^^7Processing of flammable solids containing organic matter H S The Ministry of Economic Affairs Central Standards Bureau employee consumer cooperative printed another subject of the present invention is the actual volume caused by the sedimentation and accumulation of inorganic components from the stored fertilizer in the liquid fertilizer storage tank The reduction of the concentration of the produced liquid fertilizer will not cause the dispersion of chronology, and a treatment device for the contained waste liquid is provided.豕 The paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) Λ7 B7 Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Fatty animal manure contains organic enzymes and enzyme preparations, which are added next to the untreated. _Q1 ~ ._. 5% by weight. After the product is formed, the resulting liquid mash 1 ^ out of this organic waste liquid The solid in the liquid becomes a weak liquid fertilizer containing organic matter. The waste liquid containing organic matter is added to the rubber, plastic, cloth, and the waste liquid separator of the 3 organic matter described above. The gold liquid belongs to the sand at i, and the first filtrate (with inorganic "_ίί ^ ί) is added, and the preparation H is added, and the production is performed at a low temperature less than G c ....: Fermented into compost, which contains organic matter Treatment of waste liquid .; 5 changers in the present invention * 1 solid-liquid separation treatment, in the separation of rubber, na, cloth, other gold, sand scales of large ^ Na (21Gx2977 Gongchu)- -------- ^ —Install ------ Order (Please read the notes on the back before filling in this Page) 513386 A? B7 Employees' cooperation of the Central Bureau of Standards of the Ministry of Economic Affairs of the People ’s Republic of China. Du Yinye V. Description of the invention (In the case of ingredients, it is advisable to use individual rumor plates with most circular holes with direct control of 6 to 8 mm; the aforementioned second solid-liquid separation The treatment is to separate fine paper fibers mainly composed of organic matter that cannot be removed by the aforementioned solidification treatment, so as to adopt the majority of slits with a width of 0.5 to 1.5 or the same The filtering efficiency of 之 is the most perforated sieve plate. ~ See here, "having approximately the same filtering efficiency" means "separate with approximately the same efficiency, and filter out approximately the same size solids. The same applies below. The meaning of "~" is that, in the method of the present invention, the coarse solids that have a smaller specific gravity than the liquid component and are flammable are separated in the aforementioned first solid-liquid separation treatment. 3 solid-liquid separation treatment, after dehydrating the obtained solid 2 to a specified content, Jingzhi incineration is suitable: in the treatment 'to use most of the slits with a width of 1 ~ 3 or approximately 4 Filtration efficiency The sieve plate is suitable. In order to solve the aforementioned problem, in the device of the present invention, it is a self-extracting vehicle and the pipeline, which directly receives untreated animal waste and other waste liquids containing organic matter, and separates rubber, plastic, cloth, The first solid-liquid separation device for other coarse solid components such as metal chips and gravel. The filtrate storage adjustment tank of the first solid-liquid separation device, the whole tank is added with the enzyme preparation, and the enzyme preparation is added. The stirring device of the adjustment tank of the filtrate in the tank is provided with an enzyme preparation, so that the whole liquid which undergoes the preliminary fermentation reaction at a low temperature, separates the fine paper mainly composed of the lysate which is not removed by the first solid-liquid separation device. Lin's 2nd solid-liquid separation paper -----! --- ^-^ Pack ------ Order (Please read the precautions on the back before filling this page) 513386 Λ7 B7 Central Ministry of Economic Affairs Printed by the Consumer Bureau of the Standards Bureau. 5. Description of the invention (M is a mature tank formed by a plurality of tanks containing the filtrate of the second solid-liquid separation device of Feiner and subjected to aerobic high-temperature fermentation treatment. Medium aerated liquid The liquid fertilizer storage tank that receives the liquid fertilizer obtained in the aforementioned mature tank and stores it, stirs the liquid fertilizer storage tank stirring device that stores the liquid fertilizer in the liquid fertilizer storage tank, and uses the organic matter separated by the second solid-liquid separation device as the main fine component. The first dewatering device for dewatering paper fibers to a specified moisture content receives the fiber solids storage means for storing the paper fibers dewatered by the first dewatering device as a compost raw material, and receives the first solid-liquid The rubber, plastic, cloth, etc. separated by the separation device have a small specific gravity and a large flammable solid, and then the solid-liquid separation third solid-liquid separation device displays and accepts the flammable solids from the third solid-liquid separation device. The second dehydration unit that performs dehydration to a specified moisture content, is composed of a conveying means and an incinerator with a combustible solid shape ^ 之 ίίίΐϊίΐί__ from the second dehydration device, which contains the machine in the second @ Between the liquid separation device and the maturation tank, fine sand is removed from the second solid-liquid separation device according to the liquid precipitation, and the sand and liquid from this sand removal device are moved. Relay ϋϊϊ ί? This is a liquid fertilizer raw material storage tank for continuously and stably supplying the filtrate from this relay device into a hot tank. Home Standard (CNS) Ba Na (210 ^^ 7

-----I---:--^ 裝------訂 (請先閲讀背面之注意事項再填寫本頁J 513386 Λ7 B7 經濟部中央標準局員工消費合作社印製五、發明説明（）、^，於本f明裝置，前述第1固液分離裝置之篩板，以各自具芝直徑6〜8咖之多數的圓洞孔；前述第2固液分離裝置之篩板，具有寬度〇· 5〜1· 5刪之多數的細縫或與之 =略同等的過濾效率之多數孔，前述第3固液分離裝置之篩板具有寬度1〜3麵之多數的細縫或與之約略同等的過濾效率之多數孔，而構成含有機物之廢液之處理裝置為宜。發明之實施形_ |於由上述的構成而得之與本發明方法有關的含有機廢液之處理方法及裝置之實施形態，茲以所附的圖面為準，詳細說明。 J1圖、第2圖為表示本發明方法及本發明裝置之實施形態之構成的流程圖兼構成圖之各自前半部與後半部。禅# Ϊ1ΐ二ί ί圖所示的本發明之含有機物之廢液之處主要基本上係具由没取車1，介由軟管2、偏心夾，納管路4、直接接納未處理的動物糞尿寺各有機物之廢液，分離出橡膠、塑膠、布類、其他金屬 1置言蝶等粗大的固形成分之密勞加麵4第1固液分離濾液’接受前料1 @齡離裝置之於該調整槽6添加酵素製劑之酵素製劑添加裝置7，之喰介氣源8a ’管路8b連接_整槽底部頭8e m奴調整射之舰内，勝滤液之二氣吹入式之調整槽攪拌裝置8， n —ϋ I— I HJi m m In ( 士 x>^ m m In ϋ— n· ϋϋ 、T (請先閱讀背面之注意事項再填寫本頁) 姆尺家標ί ( CNS ) A砸( 513386 Λ7 B7 五、發明説明（）經濟部中央標準局員工消費合作社印製藉由調整槽底部之液中唧筒6p，介由移送管路6〇被送入的酵素製劑予以添加，接納在常溫以上，未滿5〇。〇之低溫使預備潑酵反應的調整液，分離出以前述第1固液分離裝置未能去除的有機物為主體之微細紙纖維類的旋轉鼓輪式篩網而成的第2固液分離裝置9，介由管路，接納該第2固液分離裝置9之濾液貯存，進行喜氣性南溫發酵處理之多數槽而成的成熟槽，將該成熟槽中之濾液曝氣的液中型曝氣裝置11，接納前述成熟槽所得的液肥，貯藏的液肥貯槽12，由設置於介由壓縮空氣源18a及管路18b而連接的液肥貯槽底部之喷嘴頭18c，吹送空氣入液肥貯槽中之液肥並予攪拌液肥之空氣吹入式的液肥貯槽攪拌裝置18 , 將以前述第2固液分離裝置9分離的有機物為主體之微細的紙纖維類脫水至指定（約60%)之含水率為止的螺旋壓榨機而成之第1脫水裝置13，由該第1脫水裝置，介由箱式輸送器13cv接納已予脫水的纖維系固形物，作為堆肥原料貯存的屋内式固形物堆放場而成的纖維系固形物貯存手段14，由前述第1固液分離裝置5，介由移送管路5d，接納橡膠、塑膠、布類等之比重小，粗大的可燃性固形物，再進行固液分離之旋轉鼓輪型篩網而成的第3固液分離裝置 15，由該前述第3固液分離裝置15，接納可燃性固形物並進行脫水至指定（約60%)之含水率為止的螺旋壓榨機而成之第2脫水裝置16， 11 本紙張尺度適用中國國家標準（CNS > A4規格（210X297公釐） ---------J---裝-- (請先閱讀背面之注意事項再填寫本頁) 訂 513386 hi B7 五、發明説明（） if 第2脫水震置被排出的可燃性固形物，由運而成之運送手段16b，與介由該運送手段16b，接納燃性HI形物，將之魏的焚化爐17 ”構成的。第1圖所示的本發明裝置之實施形態，在上述的基本構成之上，再詳細言之，具有下述所示的具體構成。密閉加壓型之第！固液分離裝置5，係由經予連接至刖^接納管路4，接納未處理的含有機物之廢液之接 j一次室5a、挾持篩板5S並與前述一次室連絡，貯存第i 二次室5b，設置於經予連接至該二次室之前述濾液移送官路5c上的自動開閉閥5cv，經予連接至前述一^室之上端的低比重粗大固形物排管路5d，設於該低比重粗形物^管路上的自動開閉閥5dv，經予連接至一次室之上端的加壓洗淨水供給管路5w，設於該加壓洗淨水供給管路之自動開閉閥5wv，將較經予連接至前述一次室之底部，己，澱、堆積於底部之金屬片或砂礫等的含有機物之廢液比重較大的粗大固形物由一次室排出於外部之貯槳（濾液）池（drainer) 5f的沈澱、堆積物排出管路5e，與設該沈殿、堆積物排出管路之自動開閉閥5ev所構成的。前述篩板5s，以構成具有直徑6〜8刪（通常7咖）之多數圓孔般為宜。 I n ϋ I J— I I ^ 辦衣I I I I I 訂 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央榡準局員工消費合作社印製可S 使網，為氧段，阻t 置之篆裝板阻離篩目分述網液前止固止防 1防此第可於之有支型置。壓設宜加以為閉，段密轉手述遷塞上續阻於連目，的網且間止時防長之用適度尺張紙本準標家 f國----- I ---: ------ Install ------ Order (Please read the notes on the back before filling in this page J 513386 Λ7 B7 Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Note (), ^, in this fming device, the sieve plates of the first solid-liquid separation device each have a large number of circular holes with a diameter of 6 to 8; the sieve plates of the second solid-liquid separation device, There are many slits with a width of 0.5 to 1.5, or a number of holes with a filtering efficiency equivalent to that. The sieve plate of the third solid-liquid separation device has a plurality of slits with a width of 1 to 3 sides. Most of the pores having a filtration efficiency that is approximately the same, and it is suitable to constitute a waste liquid containing organic matter. Embodiments of the invention _ | The waste liquid containing organic matter related to the method of the present invention obtained from the above structure The method and the implementation form of the device are described in detail with reference to the attached drawings. Figures J1 and 2 are flowcharts showing the structure of the method of the invention and the embodiment of the device of the invention, as well as the first half of the structure diagram. And the second half. Chan # Ϊ1ΐ 二 ί ί The organic liquid-containing waste liquid of the present invention as shown in the figure The main parts are mainly taken from the car 1, through the hose 2, the eccentric clamp, the receiving line 4, directly accept the untreated animal waste urine organic waste liquid, and separate rubber, plastic, cloth, and other Metal 1 talk about the thick solid content of meloga noodles such as butterflies 4 The first solid-liquid separation filtrate 'receive the former 1 @ age away device of the enzyme preparation addition device 7 adding enzyme preparation to the adjustment tank 6 Air source 8a 'pipe 8b connection _ 8e m slave at the bottom of the whole tank to adjust the shooting of the ship, two of the filtrate to the air blow-in type adjustment tank stirring device 8, n —ϋ I— I HJi mm In (taxi x > ^ mm In ϋ— n · ϋϋ, T (Please read the precautions on the back before filling out this page) M Rule Family Logo (CNS) A (513386 Λ7 B7) 5. Description of the Invention () Staff Consumption of Central Bureau of Standards, Ministry of Economic Affairs The cooperative prints the adjustment of the liquid capsule 6p at the bottom of the tank, and the enzyme preparation fed through the transfer pipe 60 is added, and the temperature is adjusted to a temperature lower than 50. Liquid to separate organic matter that could not be removed by the first solid-liquid separator The second solid-liquid separation device 9 formed by a rotating drum-type screen of fine paper fibers of the main body receives the filtrate of the second solid-liquid separation device 9 through a pipeline for storage, and performs aerobic south temperature fermentation treatment. A mature tank formed by a large number of tanks. The liquid-medium aeration device 11 for aerating the filtrate in the mature tank receives the liquid fertilizer obtained from the mature tank, and the stored liquid fertilizer storage tank 12 is provided through a compressed air source 18a and a tube. The nozzle head 18c at the bottom of the liquid fertilizer storage tank connected to the channel 18b blows air into the liquid fertilizer storage tank and stirs the liquid fertilizer by air blowing type liquid fertilizer storage tank stirring device 18, and separates the organic matter separated by the aforementioned second solid-liquid separation device 9. The first dewatering device 13 is a screw press made of dewatering fine paper fibers to a specified (about 60%) moisture content. The first dewatering device 13 is accepted by a box conveyor 13cv. The dewatered fiber-based solids are stored in a house-type solids storage site as a compost raw material. The fiber-based solids storage means 14 receives rubber through the first solid-liquid separation device 5 through a transfer line 5d. The third solid-liquid separation device 15 formed by a rotating drum-type screen with solid-liquid separation having a small specific gravity and a thick combustible solid, and the solid-liquid separation device 15 The second dewatering device made of a screw press that accepts combustible solids and dewaters to a specified (about 60%) moisture content 16, 11 This paper size applies to Chinese national standards (CNS > A4 specifications (210X297 mm) ) --------- J --- install-(Please read the precautions on the back before filling this page) Order 513386 hi B7 V. Description of the invention () If the 2nd dehydration shock is discharged and combustible The solid solids are composed of the conveying means 16b and the incinerator 17 '' which receives the flammable HI-shaped matter through the conveying means 16b. The embodiment of the apparatus of the present invention shown in Fig. 1 has the above-mentioned basic structure and, in more detail, a specific structure shown below. The first of the sealed pressure type! The solid-liquid separation device 5 is connected to the receiving pipe 4 to receive the unprocessed waste liquid containing organic matter. The primary chamber 5a, the sieve plate 5S is held in contact with the aforementioned primary chamber, and the second one is stored. The secondary chamber 5b is provided with an automatic opening and closing valve 5cv on the aforementioned filtrate transfer official path 5c which is pre-connected to the secondary chamber, and is connected with the low specific gravity coarse solid discharge pipe 5d which is pre-connected to the upper end of the first chamber. The automatic on-off valve 5dv on the low-specific gravity coarse pipe is connected to the pressure washing water supply pipe 5w pre-connected to the upper end of the primary chamber, and the automatic on-off valve is provided on the pressure washing water supply pipe. 5wv, coarse solids with large proportion of waste liquid containing organic matter, such as metal pieces or gravel deposited on the bottom, which are relatively connected to the bottom of the aforementioned primary chamber, will be discharged from the external storage paddles by the primary chamber ( Filtrate) The sedimentation and deposit discharge pipe 5e of the drainer 5f is composed of an automatic on-off valve 5ev provided with the Shen Dian and the deposit discharge pipe. The aforementioned sieve plate 5s is preferably composed of most circular holes having a diameter of 6 to 8 (usually 7 coffee). I n ϋ IJ— II ^ Ordering clothes IIIII (please read the precautions on the back before filling this page) Printed by the Consumer Cooperatives of the Central Government Bureau of the Ministry of Economic Affairs, which can be used as an oxygen segment, and is blocked by t The plate is separated from the mesh, and the net liquid is fixed before it can be prevented. The setting should be kept closed, and the secrets should be changed. The relocation stoppage will continue to block on the net, and it will be used for a long time to prevent long-term use. Moderate rule paper on paper.

A4 S N 12 公 97 2 Μ —------— _ B7 五、發明説明（） ^如日本特開昭60-119291號公報所揭示的，於前述一次室$内接近前述篩板5而設置，使對應於前述篩板5之側的旋轉方向前方接近篩板，隔離後方，藉由高速旋轉，使於與篩板之間設置著引起孔蝕(cavitation)之動葉輪 C impeller)則較具效果。由前述旋轉鼓輪篩網而成的第2固液分離裝置9之篩，9s，以具有寬度〇· 5〜l 5刪(通常^ 〇刪)之多數細縫為宜’惟作成具有與前述寬度之多數細缝約略同等的過濾效率之圓孔或長孔等的多數孔亦可。 /於由前述旋轉鼓輪篩網而成的第2固液分離裝置9之 f後’通常設有备备介由管路9〇，13a接納在此以有機物為主體之微細的紙纖維類經予分離的第2濾液，及自由前述螺旋壓榨機而成的第丨脫水裝置13排出的液分，以約5 分鐘之滯留沈澱去除以前述固液分離裝置9未能去除的細 ^'或$澤等之除砂裝置19。此除砂裝置19，係由前述旋轉鼓，篩網$成的第2固液分離裝置9之篩板9s之細縫寬度，在則述的範圍較大網目之時，例如1· 〇〜1· 5刪之範圍内時，或在該範圍以上較大時，則予設置為宜。 I I I - 1— — Ji 1— - H -....... I^I— m =1 丁 V 、V0 (请先閱讀背面之注意事項存填寫本頁) 經濟部中央標準局員工消費合作社印製 I適度尺 i張紙繼，成液移 bt19或妯 g 4置21介料 2^獅2肥槽除4r槽液h 繼由料繼將10 中0°M中可槽有190剜述成熟設洛_前構成通c P。予前歡^略；；或讀液導M2021 ^%路| 之方麵管貯置也下I送料裝砂流pic御原砂除然# t肥除由自4 P液述介以120個前係體芦筒一 i'0^液10唧下 2將槽型入槽可熟中送準標家一國A4 SN 12 Male 97 2 Μ ———----— _ B7 V. Description of the invention () ^ As disclosed in Japanese Patent Application Laid-Open No. 60-119291, approach the aforementioned sieve plate 5 in the aforementioned primary chamber $ and It is arranged so that the forward direction of the side corresponding to the screen plate 5 is close to the screen plate forward and isolated from the rear. By rotating at high speed, a moving impeller C impeller causing cavitation is set between the screen plate and the screen plate. With effect. The sieve of the second solid-liquid separation device 9 formed by the aforementioned rotating drum screen is 9s, and it is advisable to have a large number of slits with a width of 0.5 to 15 (usually ^ 〇 deleted). Many pores, such as round holes or long holes, having a width of most narrow slits having approximately the same filtration efficiency. / After the second solid-liquid separation device 9 formed by the rotating drum screen, there is usually a preparation for receiving fine paper fibers with organic matter as the main medium via pipes 90 and 13a. The separated second filtrate and the liquid discharged from the dewatering device 13 formed by the aforesaid screw press are removed with a stagnant precipitation of about 5 minutes, and the fines that cannot be removed by the solid-liquid separation device 9 are removed. Ze, etc. of the sand removal device 19. The sand removing device 19 is a slit width of the sieve plate 9s of the second solid-liquid separation device 9 formed by the aforementioned rotating drum and screen. When the range described above is large, for example, 1 · 〇 ~ 1 · If it is within the range of 5 deletions, or larger than the range, it is appropriate to set it. III-1— — Ji 1—-H -....... I ^ I— m = 1 D V, V0 (Please read the notes on the back and fill in this page first) Staff Consumer Cooperatives, Central Standards Bureau, Ministry of Economic Affairs Print I modest scale paper sheet, transfer liquid bt19 or 妯 g 4 set 21 media 2 ^ lion 2 fat tank except 4r tank liquid h Followed by the material will be 10 in 0 ° M can be grooved with 190 description The mature Shilo_ front poses pass c P. Yu Qianhuan slightly; or read the liquid guide M2021 ^% way | the tube storage is also under the I feed sand flow pic 原原沙除然 # t fertilizer removal from the 4 P solution described by 120 precursors Reed tube i'0 ^ Liquid 10 唧下 2 The groove type can be cooked and sent to the standard home country

S N 1¾ 13iw 513386 A7 Β7 五、發明説明（）卺肥？料貯槽21，對含動物糞尿等有機物之廢液分散性過大且不安定的情形，或在大雪 ίΤ 法長期間接納的情形，本發明之處理裝置，尤 si 热槽10之連續運轉，將供給至成熟槽10之液 ’使具有當作緩衝器之功能而設置者。此液肥槽^ ’對在含動物糞尿等的有機物之廢液之接納時間間隔之分散性較小呈安定的情形，則不需要。述成熟槽1〇之上端部，由於以旋轉葉片會破壞液，士的氣泡層，未予圖示出成熟槽内上部空間之氣體，為抽吸風扇導入未予圖示的土壤脫臭裝置内，故設有消 f機10af。再者’為測定及管理發酵中的液溫，設置著液中浸潰型之測溫計l〇t。於前述液肥貯槽12内，為進行貯藏中的液肥之攪拌，自设於介由壓縮空氣源18a及管路18b而連接的液肥貯槽底部之喷嘴頭18c ,將空氣吹入液肥貯槽中的液肥内以攪拌液肥之空氣吹入式的液肥貯槽攪拌裝置18則係通常被設置的。又，於前述液肥貯槽内，設置著藉由散布車32之汲取哪请自貝丁槽及出液肥而設的浸潰管12p，及軟管接頭i2j。 —由前述的旋轉鼓輪型篩網而成的第3固液分離裝置15 之篩板15s ’以具有寬度1〜3刪（通常2腿）之多數細縫為宜’惟亦可作成具有與前述寬度之多數細缝約略同等的過濾效率之圓孔或長孔等多數洞孔。 (讀先閱讀背面之注意事項再填寫本頁) ί装· 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規枱（21〇Χ297^# ) 513386 Μ B7 經濟部中央標準局員工消費合作社印製五、發明説明（有機ti廢mum，與本f明有關的含的含顿.絲之處理之 1、ίί==ίί納，及於第1固液分離步驟之粗路之第1固液分離裝置5之滤液移送管 ί白Sfpfpfp?閥5c ’以低比重粗大固形物移送管路5d i=隹積物排出管5e之自動開閉閥5ev 壓ί ί U之自動開閉閥5wv各自關閉的狀等未處理的有機物之廢液，輪送至前述密閉加壓型第丄固液分離裝置5之第1次室5a内。 Ο被充滿前述1次室5a内的含有機物之廢液，係以前，没取車之哪筒之吐出壓力（〇. 3〜1· 0kg/cm2)為動力源，藉由具有多數直徑6〜8腿(通常7mm)之圓孔的篩板5s，使邊予分離出粗大的夾雜物，邊予過濾。含有通過該筛板之微細紙纖維類之第1濾液，則流入2次室5b内，介由前述自動開關閥5c濾液移送管路5c，予以移送至調節槽6内。且，於第1固液分離裝置5，採用具有直徑6〜8刪之多數圓孔的篩板，係基於下述的理由。亦即， 1、採用細縫取代圓孔的情形，則會有聚氣乙烯等不具厚度之夾雜物通過的顧慮。 15 本紙張尺度適用中國國家標準（CNS ) A4規格（210X 297公# ) ί ! ί I I I- =1- - -- — ----- _i— -i— -- /~、-0 (請先閱讀背面之注意事項再填寫本頁) 513386 A7 B7 五、發明説明（ I、右作成直徑未滿6刪時，過濾速度降低，且處理效辱二又，若作成直徑超過8刪時，纖維性固形物以外的爽雜物，例如，形成砂礫等多數通過，於堆肥素材内大夕混有粗大的無機物，並不適當。前述1次室化内的含有機物之廢液中的粗大夾中，以橡膠、塑膠、布類等較含有機物之廢液亦比 ίϊί、的固形物，會浮於1次室内之上部、形成浮起物層起物層之厚度增厚。又，含有機物之廢液中的粗物之中，砂礫、金屬片等之較含有機物之廢液比重形物，在前述1次内沈降，堆積於1次室底部，堆積物置亦逐漸增加。次室内5a之浮起物層若經過被推測成到達指曰ί時間（此時間可由預備實驗決定），則關閉前 ίίϊίί官路5c之自動開關閱5cv，開啟低比重粗大固二ί官路5d之自動開關閥5dv，以前述没取車之ϋ即筒 S3 〜L0kg/cm2)為動力源，將由含有機物之 fit已化σ的橡膠、塑膠、布類等而成的浮起物，與1 Κ;，ίΙίί;= 時移送至由旋轉式鼓輪筛網而綠闕娜測成減少 I由預備實驗決定)，則再經濟部中央標準局員工消費合作社印製之移送至前賴顏，㈣第1叙本紙張尺度適用中國國家標準（CNS ) A4規桔（210X 297公發了 513386 A7 五、發明説明（經濟部中央標準局員工消費合作社印製次複上述⑵〜⑸之Μ，i -欠齡严，經過被推測成到達指定量之沪定 =有機物之廢液至密如 …-人，開啟沈殿堆積物排出管路$ ^洗=管路5w之自動鯭=由了次ί =。屬片叙堆積物上，將堆積物排出至貯漿 2、於調整槽之第1濾液之處理操作⑴政如ϋ般H於使含有機物之廢液中的橡膠、塑 f、布類、金屬片、砂礫等粗大的夾雜物分二Ί氏iiff之有機物為主體之夾雜物懸浮的第ί fΐ? 气之f整槽6内，由酵素製劑ί加ϊί之酵ίίΐί 0_05重量％(通常〇·03重 i去述Ϊ酵素製劑，含有至少脂肪分鮮酶、纖士素乂解鷗、蛋白質分解繭，此外含有粉分解 3、或喜氣性生物處理法用特_生ί勿、耆養源及反應緩術劑等，以淨tclean(商品名年clean化學股份有限公司製造)較適用。 ^ (mtt8b，由壓縮空氣源8a，將被輸送至設於膽槽底部之，嘴頭8c的壓縮空氣吹入添加有前述 17 ........·--- 皿= - I- «I ϋϋ i. 士mi I - -1 囂- - ji - - , 5. 、-口 f請先閲讀背面之注意事項再填寫本頁j 本紙張尺度適用中國國家標準（匚奶）/\4規指（210\297公蝥） ΑΊ五、發明説明（S N 1¾ 13iw 513386 A7 B7 V. Description of the invention () Manure? The material storage tank 21 is too dispersive and unstable for the waste liquid containing organic matter such as animal manure or urine, or is accepted during the long period of heavy snow. The processing device of the present invention, especially the si hot tank 10, is continuously operated and will be supplied. The liquid 'to the maturation tank 10 is provided with a function as a buffer. This liquid fertilizer tank ^ 'does not need to be stable in the case where the dispersion time of the waste liquid containing organic matter such as animal manure and urine is small and stable. Rotating blades on the upper end of the mature tank 10 will destroy the liquid and the bubble layer of the driver. The gas in the upper space in the mature tank is not shown. It is introduced into the soil deodorization device (not shown) for the suction fan. Therefore, there is a 10f machine. In addition, in order to measure and manage the temperature of the liquid in the fermentation, a thermometer 10 immersion type was installed. In the aforementioned liquid fertilizer storage tank 12, in order to stir the liquid fertilizer during storage, a nozzle head 18c provided at the bottom of the liquid fertilizer storage tank connected via the compressed air source 18a and the pipeline 18b blows air into the liquid fertilizer in the liquid fertilizer storage tank. The liquid fertilizer storage tank stirring device 18 which stirs the liquid fertilizer by air is generally provided. In addition, in the liquid fertilizer storage tank, an immersion pipe 12p and a hose connector i2j, which are drawn from the squirting tank and liquid fertilizer, are provided by the pump 32 of the spreader 32. —The sieve plate 15s of the third solid-liquid separation device 15 formed by the aforementioned rotating drum-type screen is suitable for most slits with a width of 1 to 3 (usually 2 legs), but it can also be made with Most of the narrow slits of the aforementioned width have round holes or long holes such as round holes or long holes that have approximately the same filtration efficiency. (Read the precautions on the back before you fill in this page.) 装 Binding and ordering. Printed on the paper by the Consumer Standards Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. Applicable to China National Standards (CNS) A4. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. 5. Description of the invention (organic ti waste mum, containing Hanton. Silk processing of the 1st, ίί == ίί, and the first solid-liquid separation The filtrate transfer pipe of the first solid-liquid separation device 5 of the rough path of the step ί white Sfpfpfp? Valve 5c 'The thick solid transfer pipe with a low specific gravity 5d i = the automatic opening and closing valve 5e of the scum discharge pipe 5e pressure ί U The automatically opened and closed valves 5wv are closed, and the waste liquid of untreated organic matter is sent to the first chamber 5a of the aforementioned sealed and pressurized third solid-liquid separation device 5. It is filled in the first chamber 5a. The waste liquid containing organic materials is the power source of the cylinder (0.3 ~ 1.0kg / cm2) without taking out the discharge pressure of the cylinder, through a circular hole with a majority of 6 ~ 8 legs (usually 7mm) in diameter. Sieve plate for 5s, so that coarse inclusions are separated and filtered. The first filtrate of the fine paper fibers flows into the secondary chamber 5b and is transferred to the adjustment tank 6 through the filtrate transfer line 5c of the automatic opening and closing valve 5c. In the first solid-liquid separation device 5, The use of sieve plates with a large number of circular holes with a diameter of 6 to 8 is based on the following reasons. That is, 1. In the case of using narrow slits instead of circular holes, there will be inclusions such as polyethylene gas without thickness. Concerns. 15 This paper size applies Chinese National Standard (CNS) A4 specification (210X 297 public #) ί! Ί II I- = 1--------- _i— -i—-/ ~ 、- 0 (Please read the precautions on the back before filling this page) 513386 A7 B7 V. Description of the invention (I. When the diameter of the right is less than 6, the filtering speed will be reduced, and the processing efficiency will be reduced. If the diameter is more than 8, In this case, most of the impurities other than fibrous solids, such as the formation of gravel, pass through, and it is not appropriate to mix coarse inorganic materials in the compost material. In the large clamp, the waste liquid containing rubber, plastic, cloth and other organic materials is also more than The solid material will float on the upper part of the room once to form a floating layer. The thickness of the layer will increase. In addition, among the coarse materials in the waste liquid containing organic objects, gravel, metal pieces, etc. The specific gravity of the waste liquid settles in the above-mentioned 1 time, accumulates at the bottom of the 1st chamber, and the accumulation is gradually increased. If the floating layer of 5a in the sub-chamber is supposed to reach the indicated time (this time can be preliminarily tested) (Decision), then close the automatic switch 5cv of Guanlu Road 5cv, open the automatic switch valve 5dv with low specific gravity and thick Guerlu Road 5dv, and use the aforementioned tube S3 ~ L0kg / cm2) as the power source , The floating object made of rubber, plastic, cloth, etc. with a fit of σ, including organic objects, and 1 Κ ;, ίΙίί; = time shifted to the rotary drum screen and the green jelly was measured to reduce I (Determined by preliminary experiments), then the printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Re-economy will be transferred to the former Lai Yan, ㈣ The paper size of the first paper applies the Chinese National Standard (CNS) A4 regulations (210X 297 issued 513386 A7 V. Description of Invention (Member of Central Standards Bureau, Ministry of Economic Affairs The consumer cooperative prints the above-mentioned ⑵ ~ ⑸ of the M, i-under-aged, after being presumed to reach the specified amount of Huding = organic waste liquid to as dense as ...-person, open the Shen Dian deposits drainage pipeline $ ^ Washing = automatic 5w of pipeline 5 = 由了次 ί =. Dispose of the deposits on the sheet, and discharge the deposits to the storage slurry 2. The treatment operation of the first filtrate in the adjustment tank is as follows: The rubber, plastic, cloth, and metal in the waste liquid containing organic matter Thick inclusions such as flakes and gravel are divided into the second ifΊ? Gas f whole tank 6 whose organic matter is the main body of iiff ’s iiff. 0_05 wt% (usually 0 · 03I I describe the enzyme preparations, which contain at least fat-separating enzymes, cellulin to decompose gulls, and protein to decompose cocoons. In addition, it contains powdery decomposition3, or special fungal biological treatment methods. The reaction slowing agent and the like are more suitable for clean tclean (trade name: Clean Chemical Co., Ltd.). ^ (Mtt8b, compressed air source 8a, will be delivered to the compressed air at the bottom of the gallbladder, mouth 8c) Blow in with the aforementioned 17 .............. --- Dish =-I- «I ϋϋ i. 士 mi I--1---ji--, 5.,-口 f Please read first Note on the back page, please fill in this page j This paper size applies Chinese national standard (标准奶) / \ 4 (210 \ 297) 蝥 ΑΊ 5. Description of the invention

Tild中常二 ^半，邊以指定時間(約24發酵處理，分解液;之—部②亍預備性低溫提升固體及液體之分離性P。刀的有機物’降低液體黏度， ⑶1予巧狀時間所得的調 ί^ί置調整液移送管路60，被：下個第23用具於有由寬旋度轉 ^同等的猶鱗之鼠或長祕之約 t離出以經予供給的調整液中之有機物為▲的 s 纖維類。調整液，係藉由前述酵素製劑i 、蚀;骑： =低’使固體與液體成為its劑；效部 -----Μ----------丁 * 、、5· (請先閱讀背面之注意事項再填寫本頁} 且，於第2固液分離裝置9、採用呈右嘗声n R ς mm 經濟部中央標準局負工消費合作社印製遂L、/、l寬度f未滿〇·5刪時，過滤速度會降低，處理效 ίίί °ν爻，若超過L 5腿時，在前述第1固液分離步驟， f月b充为为離，於第1濾液中與紙纖維類同時混入的無物〃’或紙纖維類、在第2固液分離步驟變成較難分離，、乃在弟2濾、液中含有多數。砂、或金屬粉等比重較大者，由除砂裝置將第2渡液導入下一個槽内，即可去除沈殿。然而，未能去除沈澱的無機物粒子，或比較大的紙纖維類本紙張尺度適用中國國家標準^奶丨以規秸“⑴/)^》^) 6 8 3 3 Λ7 — —_ B?發明説明（）在保持懸浮的狀態，若第2濾液終於被導入成熟槽内，則會生成下述的問題。、甲、無機物粒子在未予分解的狀態下殘存於液肥中，在液肥貯槽内沈殿、堆積、可減少貯槽之實際體乙、有機物之紙纖維類，在成熟槽内會引起發酵，分解反應，惟若尺度較大的（尤指直徑過粗)纖維類大量混入時，則醱酵反應時間即有增長的必要，又對在成熟槽内之處理時間較短的情形，部分的紙纖維類在保持未分解的狀態下殘存於液肥中，在液肥貯槽内沈殿、堆積，不僅會減少貯槽之實際體積，被運出的液肥之濃度會生成經時的分散性。又成為散布車之散布喷嘴或管路阻塞，意外的故障之原因。 --------—,--裝-- {請先閱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褽 2、亦可作成具有與前述寬度之細縫約略同等的過濾效率圓孔或長孔等之洞孔，取代細縫。然而，細縫之情形、掛於篩網上的夾雜物，對朝向細縫延展的圓周方向上’藉由使正形成篩網之棒子上旋轉行進以防止洞孔阻塞效果係可予期待，而洞孔之情形，在此種防止洞孔阻塞效果之點上，係較細縫低劣，就任一者而言，以細縫者較佳。又’採用旋轉型鼓輪篩網作為前述第2固液分離裝置之理由，如下所述。 ①利用旋轉方式藉由鼓輪狀篩板9s過濾的屎潰（固形物），由於篩網之旋轉，及形成沿篩網之軸方向延展的 19 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公t ) 513386 _____B7 五、發明説明（）經濟部中央標準局員工消費合作社印製Tild is often two and a half times, while the specified time (about 24 fermentation treatment, decomposition liquid; part-part 亍亍 preparative low temperature to improve the separation of solids and liquids P. Organic materials of the knife to reduce the viscosity of the liquid, ⑶1 obtained by the shape time The adjustment liquid transfer line 60 is placed in the adjustment liquid transfer tube 60, which is: the next 23rd device is removed from the adjustment liquid supplied by the spinner with the same degree of rotation as the equivalent ^ The organic substance is s fiber of ▲. The adjusting liquid is through the aforementioned enzyme preparation i, erosion; riding: = low 'makes the solid and liquid into its agent; the effective part ----- M ------- --- ding *, 、 5 · (Please read the precautions on the back before filling in this page} And, in the second solid-liquid separation device 9, use the right sound n R ι mm Off-line consumption by the Central Standards Bureau of the Ministry of Economic Affairs When the cooperative prints L, /, and l width f is less than 0.5, the filtering speed will be reduced, and the processing efficiency will be reduced. If it exceeds L 5 legs, in the aforementioned first solid-liquid separation step, f month b It is isolated, and it is mixed with paper fibers in the first filtrate, or paper fibers, which becomes difficult to separate in the second solid-liquid separation step. Brother 2 has a large amount in the filter and the liquid. If the specific gravity of sand or metal powder is large, the second fluid is introduced into the next tank by the sand removal device to remove Shen Dian. However, the precipitated inorganic particles have not been removed. Or larger paper fibers. This paper standard applies the Chinese national standard ^ milk 丨 in accordance with the standard "⑴ /) ^" ^ 8 6 3 3 Λ7 — —_ B? Description of the invention () In the state of suspension, if the first 2 The filtrate is finally introduced into the mature tank, and the following problems will occur. A, inorganic particles remain in the liquid fertilizer without being decomposed, and they can be deposited in the liquid fertilizer storage tank, which can reduce the actual volume of the storage tank. Organic paper fibers can cause fermentation and decomposition reactions in mature tanks. However, if large-scale (especially over-diameter) fibers are mixed in a large amount, it is necessary to increase the fermentation reaction time. In the case where the processing time in the mature tank is relatively short, some of the paper fibers remain in the liquid fertilizer in an undecomposed state, and sinking and accumulation in the liquid fertilizer storage tank will not only reduce the actual volume of the storage tank, but also the amount of liquid fertilizer transported. Will cause dispersion over time. It also becomes the cause of accidental failure of the spray nozzles or pipes of the spreader. ----------,-installation-{Please read the precautions on the back first Please fill in this page again}-Order · Seal of the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 2. It is also possible to make holes with round or long holes that have a filtering efficiency approximately equal to that of the aforementioned narrow slits, instead of the narrow slits. However In the case of fine slits, the inclusions hanging on the screen will extend in the circumferential direction toward the fine slits. The effect of preventing the hole from blocking by rotating the rod that is forming the screen can be expected. In the case of a hole, in terms of the effect of preventing the hole from being blocked, it is inferior to the fine seam, and in any case, the fine seam is better. The reason why a rotary drum screen is used as the second solid-liquid separator is as follows. ① The dross (solid matter) filtered through the drum-shaped screen 9s by the rotating method, due to the rotation of the screen and the formation of 19 extensions along the axis of the screen. This paper size applies to China National Standard (CNS) A4 specifications. (210X297 male t) 513386 _____B7 V. Description of the invention () Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs

Λ7 棒狀固形物，轉動篩網圓周面，依序剝取已附著於篩網面上的屎渣（固形夾雜物），故無需附加複雜的揭:造，具備有可防止洞孔阻塞的功能。 ② 於簡單的密閉容器之中可運轉，防止臭氣之擴散，同時經由透視透明的玻璃窗，可觀察出運轉狀況。 ③ 由於可密閉，可容易提出防止臭氣擴散之對策。 ④ 運轉中無需手作業，可自動無人運轉。 ⑤ 已使用液肥之洗淨可較容易。且’若為具有上述的特徵之固液分離裝置時，則不一疋需為旋轉型鼓輪篩網，即使其他形式者亦可。 (2) 所得的第2濾液，係介由濾液移送管路9〇被移送至 =一個除砂装置19。且，除砂裝置19，係介由管路 Ί33接納由後述的第1脫水裝置13排出的液分。、關於除砂裝置、中繼槽、液肥原料貯槽 (^置19，在以前述第2眺分離裝置9未能細砂或泥澤等約5分鐘左右之滯留時間中，可 +ιϋ除。結果’在以後的步驟之管路内’貯槽内成成I、、槽内，可防止此等異物之沈降、堆積。 mi除砂裝置19，介由移送管路19。，除以自然可將液體移送入後述的液肥原料貯槽21或 tSii以的情形外，可將液肥原料液暫時移送至 (3) 可槽2G，介由移送原2GP、移送管路200，内。等液肥原料移送至液肥原料貯槽21或成熟槽10 •I n m i HI n — J n I . m n n —I- - n n ^ (請先閲讀背面之注意事項再填寫本頁)Λ7 Rod-shaped solid object, rotating the circumferential surface of the screen to sequentially remove the dross (solid inclusions) already attached to the surface of the screen, so there is no need to add complicated demolition: it has the function of preventing hole blocking . ② It can be operated in a simple airtight container to prevent the diffusion of odor. At the same time, the operation can be observed through transparent glass windows. ③ Since it can be sealed, it is easy to propose countermeasures to prevent the spread of odor. ④ There is no need for manual operation during operation, it can be operated automatically and unmanned. ⑤ It is easier to clean the liquid fertilizer. In addition, if it is a solid-liquid separation device having the above-mentioned characteristics, it does not need to be a rotary drum screen at all, even if it is in other forms. (2) The obtained second filtrate is transferred to a sand removal device 19 through the filtrate transfer line 90. In addition, the sand removing device 19 receives the liquid discharged from the first dewatering device 13 described later via a pipe Ί33. About the sand removal device, the relay tank, and the liquid fertilizer raw material storage tank (set at 19, in the residence time of about 5 minutes, such as the failure of the fine sand or mud to be separated by the second overlooking separation device 9), it can be removed. 'In the pipeline of the subsequent steps' The storage tank is formed into I, and the tank can prevent the sedimentation and accumulation of these foreign materials. Mi Desanding device 19, through the transfer pipeline 19. The liquid can be divided by natural division. In the case of liquid fertilizer raw material storage tank 21 or tSii described below, liquid fertilizer raw material liquid can be temporarily transferred to (3) 2G tank, which can be transferred through the original 2GP and transfer pipeline 200, etc. Transfer of liquid fertilizer raw materials to liquid fertilizer raw materials Storage tank 21 or mature tank 10 • I nmi HI n — J n I. Mnn —I--nn ^ (Please read the precautions on the back before filling this page)

本紙狀舰财關 Λ7 B7 經濟部中央標準局員工消費合作社印製五、發明説明（） 4、产i液肥原料貯槽21，對含動物糞尿等有機物之廢，之接納時間間隔之分散性過大且不安定的情形，或雪地帶冬季無法長期間接納的情形，本發明之處理裝’尤其為確保成熟槽10之連續運轉，將供給熟槽10之液肥原料貯存，使具有當作緩衝器之功能而設置者。此液肥原料貯槽21，對在含動物糞尿等的有機物之廢液之接納時間間隔之分散性較小呈安定的情形，則不需要。且，设置液肥原料貯槽21之情形，液肥原料在長時貯藏中’懸浮於液肥原料中的無機固形物或有機固形沈降、堆積、降低貯槽之實際容積，又為防止生成被 If至下一個步驟之成熟槽10的液肥原料之成分濃度之經時性分散性’如與前述液肥貯槽12之情形相同般，設置液 ^原料貯槽攪拌裝置，以由接納液肥原料開始進行液肥原料之連續攪拌為宜。且’於前述調整槽6與前述第2固液分離裝置之間，亦考慮設置成為緩衝器之貯槽，以取代前述液肥原料貯槽 21然而，此時，被認為調整液中之微細的紙纖維類等未分離夾雜物沈降，為防止此沈降現象，若進行空氣攪拌時，則過度進行預備性低溫發酵反應，在成熟槽内的喜氣性高溫發酵處理條件不完備，液肥化未能妥善進行，又有招致液肥品質降低的顧慮，並不適宜。又，於接納至前述第1固液分離槽裝置5之前，亦可考慮設置成為緩衝器之未處理的動物糞用貯槽。然而，此本紙張尺度適用中國國家榡準（CNS ) A4規格（210X297公釐） ----------^1------訂 (諸先閲讀背面之注意事項真填寫本貢) 513386 五、發明説明（圖之s闕尿處理袭置之調整槽内，有成為問璲之橡膠、塑膠、布類等比重較或^礫、金則等比動交大的夾雜物沈J不適。 (5)已設置上述液肥原料貯槽21之情形，視必要介由汲出唧筒21p、移送管路21〇，液肥原料^1移送至下一個成熟槽10。 4·關於在成熟槽之喜氣性高溫發酵處理 (1) 成熟槽10，係由至少第1成熟槽l〇a及與之並聯設寻的弟2成熟槽10b之複數槽而成，前述第2攄液，係被導入第1成熟槽l〇a或第2成熟槽之任一者。在此，藉由液中型曝氣裝置，在25〜50mm3/BODkg/日之曝氣條件下曝氣，且在50〜80°C之高溫條件下，藉由已殘留的分解酵素及已增加的微生物之作用，將前述調整槽已予預備性發酵處理的液體，進一步進行有機物之分解、發酵反應的喜氣性高溫發酵處理，進行指定時間(28〜30日間）。 (2) 上述的喜氣性高溫發酵處理，例如在第1成熟槽i〇a 進行之間，前述第2濾液則被導入另一側之第2成熟槽10b内。經濟部中央標準局員工消費合作社印製 n mu —ϋ -111 m ml —II I. > . ϋ- m·^ .m --i^n , 穿 i (請先閱讀背面之注意事項再填寫本頁) (3)設於上述成熟槽之上部的消泡機l〇af，係藉由液中型曝氣裝置11，形成被吹入液中的空氣，與由於發酵而生成的二氧化碳氣體等微細的氣泡，在液體表面上浮起並形成氣泡層，故由成熟槽排出已生成的二氧 ^張尺度適用中關家標準（CNS )八4娜（210X297“ 五、發明説明（經濟部中央播準局員工消費合作社印裝二為促進發酵反應，以旋轉葉片破壤氣泡、介不的抽吸風扇容易將成熟槽内之氣體導人未予圖不的土壌脫臭裝置。 (4)藉由上述成熟槽所設的測溫計1〇t，測定出成孰 =液^，可予管理是否成為上述高溫發酵上較宜的溫未達上述下限溫度5(rc^，若提高含未二=動，糞尿等的有機物之廢水之有機物濃度即二二常由於發酵反應之進行引起的溫度上升大，並非未達成上述下限溫度501，因此，上述的升等之處置即成為不需要的，又，液溫超過上 ^限ί度肋力時，調整前述液中型曝氣裝置11之争止時間，猎由抑制由於發酸反應引起的溫度上升，可予管理。關於液肥貯槽之製品液肥之貯藏及液肥之散布 ⑴艺#述在成熟槽内製造的液肥，以移送哪筒予移至液肥貯槽12内，並予貯藏。在靜卜壯能、 ^藏中^液肥僅有少許的無機成分之沈降，若。予堆，會降低貯藏之有效實際容積，運送出的液肥之 /辰度S生成經時性的分散性。為防止此螯拌裝置18進灯液肥之攪拌，經常均勻:曰成分’以謀安定供給成==上 (2)液肥貯槽12内之液肥，視必要時，通常介由抽吸管本紙浪尺度適用中國國家標準（CNS ) A4規格（210χ297公釐） (請先聞讀背面之注意事項再填寫本頁}This paper-like ship wealth customs Λ7 B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention () 4. Storage tank 21 for the production of liquid fertilizer raw materials, the acceptance time interval of waste containing organic waste such as animal manure is too large and Unstable conditions, or conditions that cannot be accepted for a long period of time in the winter in a snowy area, the processing device of the present invention is especially to ensure the continuous operation of the mature tank 10, and stores the liquid fertilizer raw materials supplied to the mature tank 10 so as to function as a buffer. And the setter. This liquid fertilizer raw material storage tank 21 does not need to be stable in the case where the dispersion time of the waste liquid containing the organic matter such as animal dung is small, and it is stable. In addition, in the case of the liquid fertilizer raw material storage tank 21, the long-term storage of the liquid fertilizer raw material 'suspends the inorganic solid or organic solid suspended in the liquid fertilizer raw material to settle, accumulate, and reduce the actual volume of the storage tank. In order to prevent the formation of the If, the next step The time-dependent dispersibility of the component concentration of the liquid fertilizer raw material in the mature tank 10 is the same as that of the liquid fertilizer storage tank 12 described above. A liquid ^ raw material storage tank stirring device is provided to continuously stir the liquid fertilizer raw material from the receiving of the liquid fertilizer raw material. . In addition, it is also considered to provide a storage tank serving as a buffer between the adjustment tank 6 and the second solid-liquid separation device to replace the liquid fertilizer raw material storage tank 21. However, at this time, it is considered that the fine paper fibers in the adjustment liquid In order to prevent the sedimentation of unseparated inclusions, in order to prevent this sedimentation phenomenon, if the air is stirred, the preliminary low-temperature fermentation reaction is excessively performed. The conditions of the aerobic high-temperature fermentation in the mature tank are not complete, and the liquid fertilizer cannot be properly carried out. There is a concern that the quality of the liquid fertilizer is reduced, which is not suitable. It is also conceivable to provide an untreated animal waste storage tank as a buffer before receiving the first solid-liquid separation tank device 5. However, this paper size is applicable to China National Standard (CNS) A4 (210X297 mm) ---------- ^ 1 ------ Order (please read the notes on the back first and fill it in (Bongon) 513386 V. Description of the Invention (Picture s) In the adjustment tank placed in the urine treatment tank, there is a relatively large proportion of rubber, plastic, cloth and other gravels, gold, etc. J is not suitable. (5) If the liquid fertilizer raw material storage tank 21 is installed, the liquid fertilizer raw material ^ 1 is transferred to the next mature tank 10 through the extraction tank 21p and the transfer pipe 21 as necessary. 4 · About the joy in the mature tank High-temperature fermentation treatment (1) The maturation tank 10 is made up of at least a first maturation tank 10a and a plurality of maturity tanks 10b which are arranged in parallel with each other. The aforementioned second liquid is introduced into the first Either the maturation tank 10a or the second maturation tank. Here, the liquid-medium aeration device is used to aerate under an aeration condition of 25 to 50 mm3 / BODkg / day, and at 50 to 80 ° C. Under the condition of high temperature, the liquid which has been subjected to preliminary fermentation treatment in the aforementioned adjustment tank is put into use by the action of the remaining degrading enzymes and the increased microorganisms. The aerobic high-temperature fermentation treatment of organic matter decomposition and fermentation reaction is performed in a single step for a specified time (28 to 30 days). (2) The above-mentioned aerobic high-temperature fermentation treatment is performed, for example, between the first maturation tank i0a. The second filtrate is introduced into the second maturation tank 10b on the other side. Printed by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy n mu —ϋ -111 m ml —II I. >. Ϋ- m · ^ .m- -i ^ n, wear i (please read the precautions on the back before filling in this page) (3) The defoamer 10af located on the upper part of the above mature tank is formed by the liquid medium aeration device 11 Air blown into the liquid and fine bubbles such as carbon dioxide gas generated by fermentation float on the surface of the liquid to form a bubble layer. Therefore, the dioxin generated from the mature tank is discharged according to the Zhongguanjia standard (CNS standard). ) Ba Na (210X297 "V. Description of the invention (Printed by the Consumer Cooperative of the Central Broadcasting Bureau of the Ministry of Economic Affairs of the People's Republic of China.) 2. To promote the fermentation reaction, the rotating blades break the air bubbles and the suction fan easily guides the gas in the mature tank. The soil deodorization device that people did not plan. 4) Using the thermometer 10t set in the maturation tank, the measured 孰 = liquid ^ can be managed to manage whether the temperature that is more suitable for the high-temperature fermentation does not reach the lower limit temperature 5 (rc ^, if it is increased) The concentration of organic matter in wastewater containing organic matter such as organic matter, feces, urine, etc., means that the temperature rise caused by the progress of the fermentation reaction is large, and the above-mentioned lower limit temperature 501 is not reached. Therefore, the above-mentioned treatment of upgrading is unnecessary. In addition, when the liquid temperature exceeds the upper limit of the rib force, the contention time of the liquid medium-sized aeration device 11 is adjusted, and the temperature rise caused by the acid reaction can be suppressed, which can be managed. Regarding the products of the liquid fertilizer storage tank, the storage of the liquid fertilizer and the distribution of the liquid fertilizer ⑴ 艺 # describe the liquid fertilizer manufactured in the mature tank, which cylinder is to be transferred to the liquid fertilizer storage tank 12, and stored. In Jingbu Zhuangneng, ^ Zang, ^ Liquid fertilizer has only a small amount of sedimentation of inorganic components. Pre-stacking will reduce the effective storage volume in storage, and the liquid fertilizer delivered will have a time-dependent dispersibility. In order to prevent the liquid fertilizer from being stirred by the chelating device 18, it is often uniform: the ingredients are supplied in a stable manner == upper (2) the liquid fertilizer in the liquid fertilizer storage tank 12, and if necessary, usually through the suction tube paper paper scale Applicable to Chinese National Standard (CNS) A4 specification (210x297 mm) (Please read the precautions on the back before filling in this page}

513386 五、發明説明（） 30p、軟管接頭3〇 j，散布車32之軟管31、散布車32 之抽吸唧筒（省略圖示），使積存於散布車32之貯槽内，被-送至田間作業場33，藉由散布車之散布裝置（省略圖示）予以散布。 6、關於經予分離的微細紙纖維類之堆肥化 (1) 沿用由前述旋轉滾筒型篩網而成的第2固液分離裝置9分離的有機物為主體之紙纖維類，係藉由連接設置於此固巧分離裝置之固形物排出側的螺旋壓榨機而成的第1脫水裝置13、予以脫水至較適於堆肥化之指定的含水率（約60%)。 (2) 前述的纖維系脫水固形物、係藉由箱式輸送器 ljcv，例如被移送至由屋内固形物置於場而成的纖維糸固形物置於場14，並予暫時貯存著。 (3)經予貯，存的纖維系固形物、係被送至堆肥製造場、邊予，當反覆切斷，邊予適度的保持著與大氣之接觸、藉由包含於正被包含在纖維系固形物内之液中的動物糞内殘存的消化酵素，與當作前述酵素製劑被添加的酵素類及喜氣性微生物、經予發酵、分解有機物而成為堆肥。經濟部中央標準局員工消費合作社印製 I n I I —J I I I l n n n n I (I T (讀先閱讀背面之注意事項存填寫本莨) 於用作堆肥材料之前述纖維系固形物内、以前述第1固液分離裝置5分離出不能發酵的橡膠、塑膠等之固形物、使不予混入，在成分、通氣性、營養均衡等方面整體上為均勻、進行均勻的發酵，乃形成良質的堆肥。關於以第1固液分離裝置分離的低比重粗大固形物之處 — ____ 24 一513386 V. Description of the invention () 30p, hose connector 30j, hose 31 of the dispersing car 32, suction pump (not shown) of the dispersing car 32, so that it will accumulate in the storage tank of the dispersing car 32 and be-sent They are distributed to the field operation site 33 by a spreading device (not shown) of the spreading vehicle. 6. Composting of pre-separated fine paper fibers (1) Paper fibers with organic matter as the main body separated by the second solid-liquid separation device 9 formed by the aforementioned rotating drum-type screen are installed by connection. The first dewatering device 13 formed by the screw press on the solids discharge side of the solid separation device is dewatered to a specified moisture content (approximately 60%) suitable for composting. (2) The aforementioned fiber-based dehydrated solids are transported to the fiber formed by the solids placed in the house through the box conveyor ljcv, and the solids are placed in the field 14 and temporarily stored. (3) After storage, the stored fiber solids are sent to the compost manufacturing site, while being repeatedly cut, while maintaining moderate contact with the atmosphere, they are contained in the fiber being contained in the fiber. It binds the digestive enzymes remaining in the animal dung in the liquid in the solid matter, and the enzymes and aerobic microorganisms added as the aforementioned enzyme preparation, which are pre-fermented to decompose organic matter and become compost. Printed by the Consumers' Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs I n II —JIII lnnnn I (IT (read the precautions on the back of the book and fill in this card) in the above-mentioned fiber-based solids used as compost material, using the first solid The liquid separation device 5 separates solids such as rubber and plastic that cannot be fermented, prevents them from being mixed in, and uniformly ferments uniformly in terms of composition, air permeability, and nutritional balance, etc., and forms a good quality compost. Where the solid matter with a low specific gravity is separated by the first solid-liquid separator — ____ 24 一

本紙張尺度適用中國國家標隼（CNS ) Λ4規枱（210X 297^ T M3386 A7 B7 五、發明説明（）經濟部中央標隼局員工消費合作社印製 (1)以前述密閉加壓型之第1固液分離裝置5分離而被運送至由前述旋轉鼓輪型篩網而成的前述第三固液分離裝置15的橡膠、塑膠、布類等比重較小的可燃性之粗大固形物、係採用具有密度1〜3醒(通常2咖)之多數的細缝，或有與之約略同等的過濾效率之多數的圓孔或長孔之篩板15s，再度進行固液分離。於上述的第3固液分離裝置15，採用具有寬度1〜3mm ，多數，縫或與之約略同等的過濾效率之多數洞孔的師板’係基於下述的理由。 ①細縫密度若未滿1咖時，過濾速度會降低，處理效率變差。 ^ ’若超過3刪時，聚氣乙烯等不具厚度之夾雜物或直徑 ^小的粒狀無機物，大多通過篩網，與濾液同時流入調整，、再者，由調整槽被帶往前述第2固液分離裝置，在此與紙纖維類同時經予分離而混入堆肥素材中，成為据高造肥發酵之騎轉礙，物之品料彳堆之1述^之細縫約略同等的過遽效率 3孔或長等之洞孔、取代細縫。然而、細 ί ’對朝向細縫延展的圓周方向上、夢由使正形成師網之棒子上旋轉行進以防止 :s縫s孔之就情任⑽^ 之理離裝置 25 本紙張尺度適用中國國家標準（CNS ) Α4規FT210X2975f (請先閲讀背面之注意事項再填寫本頁) 裝· 訂 513386 A7 ____ ______ β7五、發明説明（） (2)經予分離的可燃性固形物，係於由經予連接設置在上述旋轉型鼓輪篩網15之固形物排出口的螺旋壓榨機而成之第二脫水裝置16，予以脫水至指定的含水率（約60%)為止，被收容於運送台車之容器内，被運送至焚化爐17為止，在此予以焚燒。經滴部中央標準局員工消費合作社印製以上採用第1圖、第2圖，就本發明裝置及採用本發明裝置之本發明方法之實施態樣，雖可具體的說明直構成士作^，惟本發明裝置及本發明方法，並非侷限於i述的貫施態樣’至於其他構成，在不脫離技術内容之要旨的筘圍内，當然亦包含於本發明。例如，於前述的實施態樣，係就由將成熟槽1〇並置的第1成熟槽10a及第2成熟槽l〇b之二槽^構成x 子予以說明。然而，由四槽構成此成熟槽10，其中三样依序每隔開10天使其開始喜氣性高溫發酵處理：以各^ ‘ t loatation) 效ϊ 1發明有關的處理裝置之連續運轉成為可能，有所謂提高處理能力之功效。 ^ ^ 少又，於土述第f圖、第2圖所示的本發明裝置之似早，採用運送台車，作為由前述第2脫水裝置Μ之中化爐17 *止的可燃性固形物之運送手側至焚帶輸送帶或箱式輸送H等之連續的觀裝置皮段，此情形，運送及將可燃性固形物成為可容易自動化及無人化者。 A匕爐之作業即 26·，本紙張尺度適用中國國家標準（CNS ) A4規枱（210X297公 (請先閱讀背面之注意事項存填寫本頁) 装- 513386 Λ7 五、發明説明（本發明有關的含有機物之廢液之處理方法及裝置， ^於，理时有家畜之躲絲尿等祕翼尿及其他，橡 ί維2^、布類等、或金屬片、砂礫等粗大的夾雜物與紙 1固液分離步驟、裝置，分離、夾雜物，在第2固液分離步驟，裝置，分離。回收前述微有機性夾雜物，可將之各別焚燒或堆肥化等的後處理，故與習用的處理方法及裝置相比，可發揮以下所述的優越功效。 (1) 有需要採用習用的屎尿處理裝置之情形，且在調整槽内浮出於屎尿液面上的橡膠、塑膠等之低比重的粗大固形物之浮起物層之搔取、或搔取後的固形物之焚燒或掩埋等的後處理，即成為不需要採用人手之不衛生作業，可減輕作業員之負擔，可達成處理裝置運轉所需人力之省力，省人匕。 (2) 於以成為堆肥原料之紙纖維類為主體之微細的有機物性夾雜物内，不致混入無法發酵的粗大夾雜物，使堆肥材料之成分、通氣性、營養均衡等整體成為均勻，進行均勻的發酵，可製得良質的堆肥。經濟部中央標準局員工消費合作社印製 W機於等 ⑽無、塞 f的少阻 14中齋之 f槽之物 ½貯積雜 _肥{4夹 £液際機 W表實無g低I於 4降的管 #之起或务質引嘴，品積喷中巴良亡月& fr液、置米土降裝轉防沈布 U可^/散 W，物之於物雜肥。丨雜夹液等 3 /1\ 適準標家國 27 釐公 97This paper size applies to China National Standards (CNS) Λ4 gauge (210X 297 ^ T M3386 A7 B7 V. Description of the invention () Printed by the Consumer Cooperatives of the Central Standardization Bureau of the Ministry of Economic Affairs (1) 1 Solid-liquid separation device 5 Separated and transported to the third solid-liquid separation device 15 formed by the rotating drum-type screen, rubber, plastic, cloth, etc. The solid-liquid separation is performed again by using sieving plates with a density of 1 to 3 (usually 2 coffee) or a round or long hole sieve plate with a majority of approximately the same filtration efficiency for 15 seconds. 3 The solid-liquid separation device 15 uses a division board having a width of 1 to 3 mm, a large number of holes, or a large number of holes with a filtering efficiency approximately equal to that of the plate, for the following reasons. ① When the density of the fine slits is less than 1 coffee , The filtration speed will be reduced, and the processing efficiency will be worse. ^ 'If it exceeds 3, the inclusions such as polyethylene gas, which have no thickness, or small inorganic particles with a diameter of ^, mostly pass through the screen and flow into the adjustment at the same time as the filtrate. Or is brought to the aforementioned by the adjusting groove 2Solid-liquid separation device, which is simultaneously separated with paper fibers and mixed into compost material, which is an obstacle to high-fertilization fermentation, which is about the same as the fine slits described in ^遽 Effective 3 holes or longer holes instead of fine slits. However, thin 'pairs' in the circumferential direction extending towards the fine slits, and the dream is made to rotate on the stick that is forming the division's net to prevent: Regarding the love and separation of the device 25, this paper size applies the Chinese National Standard (CNS) Α4 regulations FT210X2975f (Please read the precautions on the back before filling out this page) Binding and ordering 513386 A7 ____ ______ β7. Description of the invention () (2) The pre-separated flammable solids are dewatered to the designated dewatering device 16 in the second dewatering device 16 formed by a screw press pre-connected to the solids discharge port of the rotary drum screen 15 described above. Up to about 60% moisture content, it is contained in a container of a transport trolley and transported to the incinerator 17, where it is incinerated. Printed by the Consumers Cooperative of the Central Standards Bureau of the Ministry of Dripping. Figure 2 shows the device according to the invention Although the implementation mode of the method of the present invention using the device of the present invention can be specifically described as a masterpiece, the device of the present invention and the method of the present invention are not limited to the consistent implementation mode described above. As for other configurations, It goes without saying that the scope of the technical content is also included in the present invention. For example, in the aforementioned embodiment, the first mature tank 10a and the second mature tank 10b juxtaposed with the mature tanks 10 juxtaposed. Two troughs are formed by x. However, this mature trough 10 is formed by four troughs, three of which are separated by 10 angels in sequence, and they start the aerobic high-temperature fermentation process: each of them is related to the invention The continuous operation of the processing device becomes possible, which has the effect of improving the processing capacity. ^ ^ At the same time, the apparatus of the present invention shown in Figures f and 2 of the soil description is as early as possible, and a transport trolley is used as the flammable solids in the chemical furnace 17 * of the second dewatering device M. Conveying the continuous viewing device skins such as the incineration belt conveyor or the box conveyor H, in this case, the flammable solids can be easily automated and unmanned. The operation of the A dagger is 26 ·. The paper size is applicable to the Chinese National Standard (CNS) A4 gauge (210X297) (please read the precautions on the back and fill in this page). Installation-513386 Λ7 5. Description of the invention (This invention is related to The method and device for processing organic liquid waste, such as the secretion of urine and other wing urine of livestock, etc., and large inclusions such as rubber, cotton, etc., or metal pieces, gravel, etc. The solid-liquid separation step, device, and inclusions are separated from the paper 1 in the second solid-liquid separation step, device, and separated. The aforementioned microorganic inclusions are recovered and can be separately burned or composted for post-treatment, so Compared with conventional treatment methods and devices, the following superior effects can be exhibited: (1) In the case where a conventional stool treatment device is required, and rubber, plastic, etc. floating on the urine surface in the adjustment tank The low-specific gravity post-treatment of the floating solid layer, or the incineration or burial of the solid after the extraction, becomes an unsanitary operation that does not require manual work, which can reduce the burden on the operator. Reachable (2) In the fine organic physical inclusions mainly composed of paper fibers which are used as compost raw materials, it will not be mixed into coarse inclusions that cannot be fermented, so that the compost materials' components, The air permeability and nutritional balance become uniform as a whole, and homogeneous fermentation can be performed to produce good quality compost. The Employees' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs printed the W machine to wait for the lack of resistance and to plug the f. Storage and storage of miscellaneous materials_Fertilizer {4 clips. The liquid machine does not have a lower g or lower tube than the lower 4 tubes or the quality of the mouth. The rice soil can be lowered and transferred to anti-sinking cloth U can ^ / scattered W, things are mixed with other things. 丨 Miscellaneous liquid, etc. 3/1 \ Appropriate standard home country 27 cm 97

因的與 0^1—，置肥少裝液減。理於之& 處由積氣之止《4分液防際的廢可實性之，tt-Φ 物置貯經機裝的之免拌起分含瘦引成的置積肥關設堆液有内、的明槽降出發貯沈汲本肥之與液物槽，i、機貯又係無由之態形施實之置裝明發* 本。及圖法成方構明兼發圖本程示流表之為先圖構 1价第部半前之態形施實之置裝明發本。及圖法成方構明兼發圖本程示流表之為灰圖構 2 ^ 第部半後兼圖程流的成構之置裝 ίι 4: 尿原的用習示表為圖 3 0 第圖成構 ---Ί·裝-- (請先閲讀背面之注意事項再填寫本頁) 、1Τ 經濟部中央榡準局員工消費合作杜印製 Μ1···沒取車、2···軟管、3···偏心夾式軟管接頭、4...接納管路、5.··密閉加壓型之第1固液分離裝置、5a..」次室、 5b...2次室、5s…師板、6…調整槽、7…酵素製劑添加裝置、8···空氣吹入式調整槽攪拌裝置、9···第2固液分離裝置(旋轉鼓輪型篩網）、9s.··篩板、10···成熟槽、11…液中型曝氣裝置、12…液肥貯槽、13…第1脫水裝置(螺旋壓榨機）、14…纖維系固形物貯存手段(屋内式固形物置放埸）、 15···第3固液分離裝置(旋轉鼓輪型篩網）、16…第2脫水裝置(螺旋壓榨機）、17…焚化爐、18…空氣吹入式液肥貯本紙張从適用中國國家樣準（CNS )八4祕（210X297公釐) 513386 A7 B7 五、發明説明（）槽攪拌裝置、19…除砂裝置、20…中繼槽、21···液肥原料貯槽、30ρ·"液肥抽吸管、30j…軟管接頭、31…軟管、32 散布車、33…田間作業場。 · -----p----裝------訂 (請先閲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 29 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐）Because of the same as 0 ^ 1—, put less fertilizer and less liquid. Reasons & by the accumulation of gas, "the waste of 4 liquid separation, the feasibility of the waste, the tt-Φ material storage and storage of the machine installed without mixing, the thin accumulation of the fertilizer, the accumulation of liquid storage The inner and lower tanks start to store the sink of the fertilizer and the liquid tank, and i and the mechanical storage are installed in the form of the unrecognizable *. The drawing and the method are used to construct and publish the map. The flow chart of this process is to first construct the first price of the first half of the state. And the drawing method is shown in the figure. The flow chart of this process is a gray picture structure 2 ^ The first half of the rear part and the process flow of the structure is installed. 4: Urea's usage chart is shown in Figure 3 0 The figure is structured --- Ί ・ install-(please read the precautions on the back before filling this page), 1T consumer cooperation of the Central Government Bureau of the Ministry of Economic Affairs, printed M1 ··· No car, 2 ·· · Hose, 3 ··· eccentric clamp hose connector, 4 ... receiving pipe, 5. ·· The first solid-liquid separation device of the sealed and pressurized type, 5a ... "Secondary chamber, 5b ... 2nd chamber, 5s ... master board, 6 ... adjustment tank, 7 ... enzyme preparation adding device, 8 ... air-injection type adjustment tank stirring device, 9 ... second solid-liquid separation device (rotary drum type sieve Net), 9s ..... sieve plate, 10 ... maturing tank, 11 ... liquid medium-sized aeration device, 12 ... liquid fertilizer storage tank, 13 ... first dewatering device (screw press), 14 ... fiber-based solid storage means (Indoor type solid matter placement), 15 ... Third solid-liquid separation device (rotary drum-type screen), 16 ... Second dehydration device (screw press), 17 ... Incinerator, 18 ... Air blowing Liquid fertilizer This paper is from China National Sample Standard (CNS), 8th secret (210X297mm) 513386 A7 B7 V. Description of the invention () Tank mixing device, 19 ... sand removal device, 20 ... relay tank, 21 ... liquid fertilizer raw materials Storage tank, 30ρ · " liquid fertilizer suction pipe, 30j ... hose connector, 31 ... hose, 32 spreader truck, 33 ... field work field. · ----- p ---- Installation ------ Order (please read the notes on the back before filling this page) Printed by the Staff Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (CNS) A4 specification (210X297 mm)

1999.10.30 (修正補充) ΐ·操作實施例所達成之功效根據本發明實施例之功效，在說明書「發明之功效」攔内已略迷’但為更理解本發明，本發明之主要目的及達成功效如下所述：本發明之主要目的為二階段固液分離處理，即在第一固液分離處理時將粗大夾雜物分離、回收，在第二固液分離處理時將細子有機性夾雜物分離、回收；且對藉由前述第一固液分離處理而得的第一濾液，添加酵素製劑，使生成預備性的醱酵反應。 (針對二階段固液分離處理）原來，在有關製造液肥的原料中，不要混合夾雜物（多餘物）是最理想的。但是，事實上，通常均混有橡膠、聚氯乙烯、布類、内衣、衛生綿、紙巾、衛生紙、砂礫、金屬類等雜物，為能去除這些夾雜物，使其能保持良好輯狀態，故本發明採行二階段固液分離處理。隹弟一固液分離處理中 ^ 从调土叩，寻將紙中、術生紙等紙纖維_外的錄物去除。將分離後之低比重粗大阳物用螺旋壓榨機16脫水至指定的含水率（約㈣後，收容至運送台車16b的容器中，搬運至焚化爐17中焚燒。其次’在第二|11液分離處理巾，主要將沒有在第理中分離的紙巾、衛錢等__去除，分雜的咖祕義13脫_定齡轉㈤_，做雜肥原抖。、 q生=社的分離處理’針對大致上僅剩液體成分的原料進行二=_處理。夾雜物藉由二階段的分離處理完全去除，了/、剩液體成分，故需使__的水同時準備好嫩舰_。爾_+=== 1 513386 氣裝置運轉時’會阻塞在人水孔的篩板上，料在轉時若無分授拌’則空氣的吸力會降低，而無法維持喜氣性環境。、/ 此外，經過第二固液分離處理的遽液，可製造出完全沒有夹雜物的良質液肥，同時，藉由第二固液分離處理而分離出的: 物細子紙纖維類，也可有效成為良質堆肥原料。而且，在第-及第二固液分離固定的固形物含有量的變化量，即可藉由4述_p^的赚分離處理完成。階段性去除具體的效果如下表所示：物1999.10.30 (correction and supplement) ΐ · Effects achieved by operating examples According to the effects of the embodiments of the present invention, it is slightly lost in the description of the "effects of the invention". However, in order to better understand the present invention, the main purpose of the present invention and The achieved effect is as follows: The main object of the present invention is a two-stage solid-liquid separation process, that is, coarse inclusions are separated and recovered during the first solid-liquid separation process, and fine particles are organically included during the second solid-liquid separation process. The first filtrate obtained by the aforementioned first solid-liquid separation treatment is added with an enzyme preparation to generate a preliminary fermentation reaction. (For the two-stage solid-liquid separation process) It turns out that in the raw materials for manufacturing liquid fertilizers, it is ideal not to mix inclusions (excess). However, in fact, rubber, polyvinyl chloride, cloth, underwear, sanitary towels, paper towels, toilet paper, grit, metal and other debris are usually mixed. In order to remove these debris and keep it in a good state, Therefore, the present invention adopts a two-stage solid-liquid separation process. My brother is in the solid-liquid separation process ^ Remove the recordings of paper fibers such as paper and technical paper from the soil-adjusting 叩. The separated low-density coarse positive substance is dewatered with a screw press 16 to a specified moisture content (after about 20 minutes, it is stored in a container of a transport trolley 16b and transported to an incinerator 17 for incineration. Secondly, in the second | 11 liquid Separation and treatment of towels, mainly removing paper towels, health money, etc. that are not separated in the first order, removing miscellaneous coffee secrets 13__ age change to _, and making the original fat shake of the fertilizer., Q 生 = company's separation treatment 'Two = _ processing is performed on the raw materials with almost only liquid components. The inclusions are completely removed by the two-stage separation process, and / or the remaining liquid components, so it is necessary to prepare the __ water at the same time as the tender ship. _ + === 1 513386 When the air device is in operation, it will be blocked on the sieve plate of the manhole. If the material is not mixed during rotation, the suction of air will be reduced, and the aerobic environment cannot be maintained. After the second solid-liquid separation treatment, the liquid liquor can produce good quality liquid fertilizers without inclusions. At the same time, the fine solid paper fibers separated by the second solid-liquid separation process can also effectively become Good quality compost raw materials, and fixed in the first and second solid-liquid separation Shape variation amount of the composition comprising, by 4 to make the separation of said _p ^ stepwise removal process is completed specific performance in the following table: thereof

SS測定值 (mg/公升) 33^500 測定值 (mg/公升) 29^800 SS測定值 (mg/公升) 34200 (mg/公升） 32^500~ 207560^ (去除率37°/0) ΓοΓδΟΪ (去除率49°/〇) 搬入原料第二固液分離處理第二固液分離處理 22, 70010,200 17, 300 9, 700 21,700 11,600 在此’在第一固液分離處理中，除去的物質有橡膠、聚氯乙烯、布類、内衣、衛生錦、紙巾、衛生紙、砂蝶、金屬類。此外，在第二固液分離處理巾，除去的鮮以紙巾、衛线f紙_類為主。經過第二固齡離處理的綠分析值，能通麟板的細小成分，為纖維性少、未消化之細小粒狀物。 (針對第一濾液，添加酵素製劑，使生成預備性的醱酵反應）對於第一濾液，添加含有脂肪分解〇·4〜〇· 5重量％、纖維素 2 分解0· 45〜0· 55重量％、蛋白皙八切，_ , r 、，貝刀解1. 25〜1· 55重量％之前述酵素製劑0· 01〜0· 55重量〇/〇，在當、、西L + ^ 、仳吊，皿以上，未滿50 C的低温下，使生成預備性的酿酵反應。 a如說明書中所提’分解液中之_部分的有機物，降低液體|έ度，提升固體聽體之分雜。目此仙在第二隨分離處射，固體及/夜體容易分離，分離處理的效率也十分良好。 2·在請求項1中，酵素製劑中各成分含量的補充說明 D酵素製劑的成分限定使用含有脂肪分解〇· 4〜〇· 5重量％、纖維素分解〇· 45〜〇· 55 重里％、蛋白質分解1· 25〜1· 55重量。/〇之酵素製劑。實際商品（東洋清淨化學製）油脂分解酵素纖維素分解酵素蛋白質分解酵素炭水化合物分解酵素 (依場合在條件中添加即可）酵素製劑含量（製品1噸中）脂肪分解 4.5kg 纖維素分解 5· 0kg 蛋白質分解 l4.〇kg 炭水化合物分解 24· 0kg 上冗酵素類，其他含防潮劑、安定材、營養劑、著色劑等。 2)酵素製劑的添加量添加〇. 01〜〇· 05重量％。添加要領，在水桶用常溫的水加以溶解，一旦將液體溶解後，周正^内。溶解濃度為公升水中溶溶解後將意体4从人* 哪0 酵素製劑。失去安定性。无W水分會使酵素劑此外，將酵素溶解液投入的理由為，如果易飛㈣中而附輸上；纖丸子狀，㈣ 3)酵素製劑的添加時期如申請專利範圍第-項所述，在第一固液分離處理完成後，將第-固液分離處理後_液移送至調鶴，投人調整槽内。 4)添加酵素製劑後使生成預備性的醱酵處理溫度條件：常溫以上未滿5〇。〇。時間：24小時左右（若能完成，並不限定於請求範圍内）。操作：空氣曝氣。SS measured value (mg / liter) 33 ^ 500 measured value (mg / liter) 29 ^ 800 SS measured value (mg / liter) 34200 (mg / liter) 32 ^ 500 ~ 207560 ^ (removal rate 37 ° / 0) ΓοΓδΟΪ (Removal rate: 49 ° / 〇) Material carried in Second solid-liquid separation process Second solid-liquid separation process 22, 700 10, 200 17, 300 9, 700 21, 700 11, 600 Here, the substances removed in the first solid-liquid separation process There are rubber, polyvinyl chloride, cloth, underwear, sanitary brocade, paper towels, toilet paper, sand butterfly, metal. In addition, in the second solid-liquid separation treatment towel, mainly fresh paper towels and sanitary papers were removed. The green analysis value after the second solid-age separation treatment can pass through the fine components of Linlin plate, which is a small granular material with little fibrousness and no digestion. (Enzyme preparation is added to the first filtrate to generate a preliminary fermentation reaction.) The first filtrate is added to contain 0.4 to 0.5% by weight of lipolysis and 0.45 to 0.55 weight of cellulose 2. %, Protein, eight cuts, _, r ,, Badao solution 1. 25 ~ 1.55 wt% of the aforementioned enzyme preparations 0.01 ~ 0.55 weight 〇 / 〇, in Dang, Xi L + ^, 仳Hang above the dish, at a low temperature of less than 50 C, to produce a preparative fermentation reaction. a As mentioned in the description, _ part of the organic matter in the decomposition liquid reduces the liquid degree and improves the impurity of the solid hearing body. In this case, the second shot is separated at the second separation point, and the solid and / or night body are easily separated, and the efficiency of the separation process is also very good. 2. In claim 1, supplementary explanation of the content of each component in the enzyme preparation. The composition of the enzyme preparation D is limited to include fat decomposition of 0.4 to 0.05% by weight, cellulose decomposition of 45 to 0.05% by weight, Proteolysis 1.25 ~ 1.55 weight. / 〇的酶制作。 Enzyme preparation. Actual product (manufactured by Toyo Seika Chemical Co., Ltd.) Lipase-degrading enzyme Cellulose-degrading enzyme Protein-degrading enzyme Carbohydrate-decomposing enzyme (you can add it as appropriate under the conditions) Enzyme content (1 ton of product) Fat decomposition 4.5kg Cellulose decomposition 5 · 0kg protein decomposition 14.00kg carbohydrates decomposition 24.0kg superfluous enzymes, others contain moisture-proofing agents, stabilizers, nutrients, colorants, etc. 2) Added amount of enzyme preparation Add 0.01% to 0.05% by weight. Add the essentials, and dissolve in the bucket with water at normal temperature. Once the liquid is dissolved, within Zhou Zheng ^. The dissolved concentration is dissolved in liters of water. After dissolution, the body 4 is prepared from human * which 0 enzyme preparation. Loss of stability. The absence of W water causes enzymes. In addition, the reason why the enzyme solution is put in is that if it is easy to fly, it will be infused; fibrous pill-shaped,) 3) The addition period of the enzyme preparation is as described in the first item of the scope of the patent application. After the first solid-liquid separation process is completed, the first-solid-liquid separation process_liquid is transferred to the regulating crane and thrown into the regulating tank. 4) Preparing fermenting treatment after adding an enzyme preparation Temperature conditions: less than 50 ° C or more. 〇. Time: about 24 hours (if it can be completed, it is not limited to the scope of the request). Operation: Air aeration.

Claims

3 33 3

六、申請專利範圍申請專利範圍： 1' f ΙίΐίΠϊΜ，翁含有至少脂肪分分解之酵素㈣、對未處勿糞^^寺之3有機物廢液，添加〇· 〇1〜〇· 〇5重量 '分離出此含有機物之廢液 5 物後i所付的遽、液在25〜50Nm3/BODkg/曰之曝在H8()°C之高溫條件下，施以喜氣性的 2Ξίί處Uϊ弱驗性之液肥的含有機物之廢液之 ΪΣί^ΐί ί在Ϊ、：以對含前述未處理的動物糞尿 1、+、ϊίΐ5廢液，在添加醋酵製劑之前階段，進行由月述^有機物之廢液分離橡膠、塑膠、布其 i分2ίί⑽機物為主體)粗大固形成‘第= 第i ΐ液分離處理而得的第1滤液，添如前 ίϊϊί劑，在f溫以上、未滿5(rc的低溫下使生成預備性的酵反應，，由前述第1濾液.，進行分離出以前述第i固液分 ff、理未能除去的有機物為主體之微細的紙纖維類之第 I液$離處理，藉由前述的喜氣性的高溫醱酵處理使的第2濾液成為弱驗性液肥，將以前述第2固液分分離的有機物為主體之微細的紙纖維類脫水處理主才曰定的含水率後，令其於大氣中自然醱酵成堆肥。 2 =申ί專利圍第1項之含有機物之廢液之處理方法，其中於前述第1固液分離處理，於分離橡膠、塑膠、布類， ^規格(21。 ---I--1------裝·--II---訂--— 1-----線 (請先閱讀背面^/注意乾項再填寫本頁) 經濟部智慧財產局員工-¾費合作社印製Sixth, the scope of patent application The scope of patent application: 1 'f ΙίΐίΠϊΜ, Weng contains at least an enzyme that decomposes fat, 对 ^^ Temple No. 3 organic waste liquid, add 〇. 〇1〜〇 · 〇5 weight' After separating the waste liquid containing 5 organic matter, the hydrazone and liquid paid by i are exposed to a high temperature of H8 () ° C at 25 ~ 50Nm3 / BODkg / y, and the aerobic 2 is used. Liquid fertilizer containing organic matter waste liquid 液 Σί ^ ΐί ίΪ: To the waste liquid containing the aforementioned untreated animal feces 1, +, ϊίϊ5 waste liquid, before the addition of vinegar preparations, the waste described by the month ^ organic matter waste Liquid-separated rubber, plastic, cloth, etc. (the main unit is the main body) is coarsely formed to form the first filtrate obtained by the i-th liquid separation process, and the same is added as before, at a temperature above f and less than 5 ( At the low temperature of rc, a preparative fermentation reaction is generated, and the first filtrate is used to separate the first liquid of fine paper fibers mainly composed of the i-th solid-liquid fraction ff and organic matter that cannot be removed. $ 离处理, the second by the above-mentioned happy high temperature fermentation treatment The liquid becomes a weak liquid fertilizer, and the fine paper fiber dehydration treatment mainly composed of the organic matter separated from the second solid and liquid is used to determine the moisture content, and then it is naturally fermented into compost in the atmosphere. 2 = The method for treating waste liquid containing organic matter in item 1 of the patent application, wherein the above-mentioned first solid-liquid separation treatment is used to separate rubber, plastic, and cloth, and the specification (21. --- I--1-- ---- Installation --- II --- Order --- 1 ----- line (please read the back ^ / note the dry items before filling out this page) Printed by the staff of the Intellectual Property Bureau of the Ministry of Economic Affairs

513386 A8 B8 C8 D8 六、申請專利範圍經濟部智慧財產局員工消費合作社印製其他金屬片、砂礫等之粗大的固形成分之際，係採用具有直徑6〜8mm之多數圓孔之蒒板；於前述第2固液分離處理，於分離以前述第1固液分離處理未能去除的有機物為主體之微細的紙纖維類之際，係採用具有與寬度〇. 5〜1· 5mm之多數細縫或與之約略同等的過淚效率之多數洞孔的篩板。一、如申請專矛j範圍第1項或第2項之含有機物之廢液之處 1方法，係對在前述第1固液分離處理分離的橡膠、塑 ^^^5等比重較液成分小，且具可燃性之粗大固形物，行第3固液分離處理，將所得的可燃性固形物脫水至指定的含水率為止後，將之焚化。、，申請專利範圍第3項之含有機物之廢液之處理方法，第3固液分離處理，使用具有寬度1〜3mm之多數細縫或與之約略同等的過濾效率之多數洞礼的篩板。 'ifίϊϊ物ϊίίϊ處理裝置’係指含有機物之廢液 2 3膠、塑膠、布類、其他金屬片、砂礫寻粗大的固形成分之第丨固液分離裝置（5)，接納該第1固液分離裝置⑸之遽液的貝宁存調整槽⑹，於該調整槽(6)添加酵素製劑之酵素製劑添加裝置⑺，攪拌前述調整槽⑹中的毅之調整槽勝裝置⑻， 31 x 297^iy 請先閱讀背面之产注意事. 項再I裝頁訂線513386 A8 B8 C8 D8 6. Scope of patent application When the consumer cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs print other solid pieces of metal, grit, etc., they use slabs with a large number of circular holes with a diameter of 6 to 8 mm; The aforementioned second solid-liquid separation process uses a plurality of fine slits having a width of 0.5 to 1.5 mm when separating fine paper fibers mainly composed of organic substances that cannot be removed by the first solid-liquid separation process. Or most of the perforated sieve plates that have approximately the same tearing efficiency. 1. If the method of applying waste liquid containing organic substances in item 1 or item 2 of the scope of the special spear 1 method is applied, the specific gravity of the rubber, plastic, etc. separated by the aforementioned first solid-liquid separation treatment is higher than the liquid composition The small and flammable coarse solids are subjected to a third solid-liquid separation treatment. The obtained combustible solids are dehydrated to a specified moisture content and then incinerated. 3. The method for treating waste liquid containing organic matter in the scope of patent application No. 3, and the third solid-liquid separation treatment, using a sieve plate with a majority of fine slits with a width of 1 to 3 mm or a number of holes with a filtration efficiency of approximately the same . 'ifίϊϊ 物 ϊίίϊ treatment device' refers to the first solid-liquid separation device (5) that contains solid liquids containing glue, plastics, cloths, other metal pieces, and gravel. The first solid-liquid separator (5) contains the first solid-liquid. Benin adjustment tank 遽 of the liquid separation device ⑸, and an enzyme preparation adding device 酵 for adding an enzyme preparation to the adjustment tank (6), stirring the above-mentioned adjustment tank 毅 of the adjustment tank ⑻, 31 x 297 ^ iy Please read the Product Precautions on the back.

A8B8C8D8 接納添加有酵素製劑、使在低溫下進行預的調整槽⑹巾之調魏，分離在麵 5 2 f Ιϋϋ的i機物為主體之微細的紙ϊί i 之第2固液分離裝置(9), $納該5 2固液分離裝置⑼之濾液並予貯吾氣性的咼溫發酵處理之複數槽而成的成熟槽（ι〇 )，將該成熟槽（10)中的濾液曝氣之液中型曝氣梦η 接納在前述成熟槽（10)而得的液肥，並予貯 2以)置⑶該液肥貯槽(12)中的貯藏液肥之液肥貯槽將以於前述第2固液分離裝置(9)分離的有機物為主體之微細的紙纖維類脫水至指定的含水率為止的第裝置（13)。接納由該第1脫水裝置（13)脫水的紙纖維類’用作堆肥原料而貯存的纖維系固形物貯存手段、，接納f前述第1固液分離裝置(5)分離的橡膠、塑膠、布類等比重較小、粗大的可燃性固形物，再進行固^分離之第3固液分離裝置（15)，經濟部智慧財產局員工消費合作社印製A8B8C8D8 The second solid-liquid separation device (9) that accepts the enzyme preparations and pre-adjusts the grooved towels at low temperature, and separates the fine paper ϊ, i, which is the main body of the machine 5 2 f Ιϋϋ. ), The matured tank (ι0) formed by the filtrate of the 5 2 solid-liquid separation device and stored in a gas-phase temperature-fermented fermentation tank is aerated, and the filtrate in the matured tank (10) is aerated The liquid medium-sized aeration dream η receives the liquid fertilizer obtained in the mature tank (10), and stores 2) The liquid fertilizer storage tank storing the liquid fertilizer in the liquid fertilizer storage tank (12) will be separated from the second solid-liquid The device (9) is a device (13) for dewatering the fine paper fibers mainly composed of organic matter to a specified moisture content. The paper-based fibers dewatered by the first dewatering device (13) are accepted as fiber-based solid matter storage means stored as compost material, and the rubber, plastic, and cloth separated by the first solid-liquid separation device (5) are received. The third kind of solid-liquid separation device (15) with solid and small flammable solids with similar specific gravity and coarse solid separation, printed by the Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs

本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公髮）This paper size applies to China National Standard (CNS) A4 (210 X 297)

513386 A8B8C8D8 六、申請專利範圍 ΪIΐ it ΐ圍第5項之含有機物之廢液之處理裝置，述第2固液分離裝置及成熟槽之間，具備有自固液分離裝置之渡液沈殿去除細砂或泥澤等的 ΐ&ίΐ、’將來自此除砂裝置的濾、液移送中繼之中繼裝 ί二將來自此中繼裝置之濾、液連續且安定供給i 則述成熟槽而用的液肥原料貯槽。 7、如^请專利範圍第5項或第6項之含有機物之廢液之處理^置，其中前述於第i固液分離裝置之篩板，係具有直控^^刪$多數的圓洞孔；於第2固液分離裝置之篩係具有寬度〇· 5〜1.5刪之多數的細缝或與之約略同管的過，效率之多數孔；於第3固液分離裝置之篩板，係具有寬度1〜3麵之多數的細缝或與之約略同等的過濾效率之多數孔。 ---— II----I I I « ^ ·1111111 ^-11111111 ^ (請先閱讀背面I注意事*項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 33 μ氏張尺度適用中關家標準（CNS)TI規格⑵G χ 297公沒513386 A8B8C8D8 6. Application scope of patents ΐIΐ it ΐWhere the waste liquid containing organic matter is treated in the fifth item, between the second solid-liquid separation device and the maturation tank, there is a liquid-removing Shen Shendian with a self-solid-liquid separation device Ϊ́ & ίΐ, such as sand or mud, 'relay the filter and liquid transfer relay from the sand removal device, and then continuously and stably supply the filter and liquid from this relay device. Used liquid fertilizer raw material storage tank. 7. For example, please request the disposal of waste liquid containing organic matter in item 5 or item 6 of the patent scope, wherein the sieve plate of the i-th solid-liquid separation device has a direct control ^^ Holes; the sieve in the second solid-liquid separation device has a majority of fine slits with a width of 0.5 to 1.5 or the same number of holes, and the most efficient holes; in the sieve plate of the third solid-liquid separation device, These are pores with many slits with a width of 1 to 3 sides or a filtration efficiency approximately equal to that. ---— II ---- III «^ · 1111111 ^ -11111111 ^ (please read the notes on the back I before filling in this page) The Intellectual Property Bureau of the Ministry of Economic Affairs's Consumer Cooperatives printed 33 μs scales applicable Guan Family Standard (CNS) TI Specification ⑵G χ 297