JPS59193198A - Fermentation treatment of fermentable organic material - Google Patents

Abstract

PURPOSE:To perform a fermentation treatment in a short time by sucking fermentation gas at a rate of 50-150Nl/min m<3> per volume of a fermentable org. material, introducing the gas into a dehumidifier and mixing the same with 10- 50% fresh air then feeding the gas to the bottom of a fermentation tank. CONSTITUTION:Fermentation gas is sucked from a piled fermentable org. material through a suction pipe at a rate of 50-150Nl/min m<3> per volume of the fermentable org. material and is collected and sucked by a suction header 4. The fermentation gas is removed of microobjects by a dust remover 6 according to need and is then introduced into a dehumidifier 7. Fresh air of 10-50% the volume of the sucked fermentation gas is introduced through a fresh air intake port 8 into the dehumidifier 7 to replenish the consumed oxygen and the fermentation gas is maintained at 45-60 deg.C and 80-90% relative humidity. The dehumidified fermentation gas is sucked by a suction and feed blower 9 and is cyclically fed by a feed header 5 from the bottom of the fermentation tank into an air feed pipe 3 having feed holes.

Description

【発明の詳細な説明】 不発明に発＃注Ｍ憔物の発酪カスτ強匍ｊ的に吸引し、
循環送気して好気的栄件下で発酵さぜる発酵処理方法に
関する。[Detailed description of the invention] Inventively, the fermented scum of the waste is strongly sucked,
This invention relates to a fermentation treatment method in which fermentation is carried out under aerobic conditions by circulating air.

従来の堆積発＃、装置に底部の送気孔より強制的に送気
にするもの、又にショベルローダ、人力等による切返し
によめ好気発酵装置が多く利用さｆていゐ。Aerobic fermentation devices are often used, such as those that force air into the device through an air hole at the bottom of the device, or those that are turned by shovel loaders, manual labor, or the like.

この株な発＃装置でに、好気発酔粂件である発酵熱工坏
ルキー、水分τ送気切返しにより、人気に放散丁ゐ為、
発醇熱効率りツ弓み〈水分不足に生じて発酵立上りが遅
くなり発酵期１ｄＪ力ｉ２０〜６０日りの長期［ｉｌｌ
」必要となっている。又、送気切返しによりアンモニア
や硫化水系等の恋臭〃）１人気に放散さγＬゐ裔の六点
力・ある。This strain's generation device uses fermentation heat technology, which is an aerobic intoxicant, and uses water τ air supply to dissipate it, which is popular.
Thermal efficiency of smelting is reduced.Due to lack of water, fermentation start-up is delayed, resulting in a long fermentation period of 20 to 60 days.
” has become necessary. In addition, the smell of ammonia, sulfide water, etc. is dissipated by the air supply and return.

不発明にこのような人魚に危みなさノしたもので、発酵
性胸壁物孕発酵情に人γＬ発鉢愕申に収け１こ吸引部か
ら発醇ガス孕発酵性由伽ｗＪ谷量当’９５０〜１５０　
ＮＩＪＡｎｔｎ−ｍ’の速度で吸引し除湿器に畳人し、
除湿器で吸引発酵カスλの１０〜５０％の菊ｒｗ空気に
混合して除湿除塵処理した鋏、Ｃｎ葡発酵４ｆＪ底部に
循環送気することを待機とする。Uninventively, I did not want to be in danger of such a mermaid, and I was shocked to see that the fermenting parapet was fermented, and the gas was released from the suction part. ~150
Suction at the speed of NIJAntn-m' and put it in a dehumidifier,
10 to 50% of the suction fermentation residue λ is mixed with chrysanthemum air in a dehumidifier, and air is circulated to the bottom of the Cn fermentation 4fJ, which has been dehumidified and dedusted, on standby.

従来装置でに発解工洋ルギー、水分ケ放散するが、本発
明の方法でに吸引し７こ発酵カスに循環送気することに
よジ発酵熱工坏ルギー〒再オリ用して放ＰＰ忙防ぐこと
がでさ、メ吸引発酵カスと新鮮空気に除湿器内で混合丁
ゐＣとにより発酵ガスに除湿さＩし発酵に逸白な湿度と
１投索含有翔となって循環送気さ７Ｌ短期間急速発搦処
理が町寵となゐ○ 壕だ除湿器内の粕蕗水により吸引弁解カス中の倣小の有
壁物、無づ張？Ｉ忙除去でさ肯昂の閉基π防止すること
かでさゐ０ また従来の万代でに、アンモニア、価化ボ系等の悪臭に
Ｍ敢していたが、弁酵カス年炊引し、餉壌送気丁ゐこと
Ｖこよシ莞酵申の処址吻に吸看し、放散量に少ｌ（丁ゐ
ことかでさ、堆積型発奮装置に易・いてに％に効未がめ
な。Conventional equipment dissipates moisture during fermentation, but with the method of the present invention, air is sucked into the fermentation residue, and air is circulated through the fermentation residue to produce heat-induced fermentation and release PP. To prevent this, the fermentation gas is dehumidified by mixing the suction fermentation scum and fresh air in a dehumidifier, and the fermentation gas is dehumidified and the air is circulated to keep the humidity and humidity high for the fermentation. 7L short-term rapid eruption treatment is popular in the town ○ Is there a small walled object in the scum that is sucked by the lees water in the dehumidifier? Is it possible to prevent the closed group π by removing the oxidation? In addition, in the conventional method, we had to deal with the bad smells of ammonia, chloride, etc., but the fermentation residue was removed. , I sucked in the proboscis of the fermentation monkey, also known as ``V Koyoshi Kan'', and the amount of radiation was small. Na.

さらに除湿器に熱父侠命イルり何げｎば、発酵ガスニオ
・ルキー葡痛１ボ舒に熱父侯し、て回収丁にとかでさ々
という利点も刹している〇以ド、本発明〒図１１覧該照
しつつ計画に胱明する０ 第１図に本発明の方法〒地用丁ゐ吸引式堆積型発酵装置
短忙示す祝明図であゐ〇 図中１に周囲圧Ｉ１１］が壁体でりり底盤〒翁丁□発酵
伯であり、吸引孔を有する発酵ガスの吸引管２か発酵江
南う張物筒きの６０〜８０％の位置にくゐよＶＶＣ叔げ
ら７している。In addition, if you use a dehumidifier with a heat source, you can use a fermented gas instead of a heat source, and it also has many advantages such as being able to collect it. The invention will be clarified with reference to Figure 11. Figure 1 is a congratulatory map showing the method of the present invention - a suction type sedimentary fermentation device. I11] is the wall and the bottom plate is the fermentation tube, and the fermentation gas suction pipe 2 with the suction hole is placed at a position of 60 to 80% of the fermentation gas cylinder. 7.

ＸＡ酵′註／Ｉ−１像物に好ましくは水分率４０〜６５
％、　　ＰＩ−１７〜９に祠祭さγＬ憎円に堆積さｎろ
○不発明に過用を几ゐ発酔性有像物としてａ人台し尿、
下水スラッジ、生ゴミ寺がりゐ〇堆積さγした発醇註有
像物〃・ら吸引官で発酵脣１倉物谷有工当り５０〜１５
０　Ｎ　ｌ／ｒｒｕｒｎ−ｍ’　ｔＤｍＩｉＬ　Ｔ先＝
ｙガスオ吸引ヘッダー４により果合きゼ吸引丁ゐ。この
とき吸引発ｒ″；ｔカス棉度に５ｕ〜６５℃、孔対湿度
にシロ〜９８％、アンモニア―度（１’；Ｊ３，０００
〜１０，００　ｏｐｐｍトｚｚ、ｂｏ　Ｃの発酵カス刀
・ら心安に比１じ除展指６で倣小物π除云し、こｌＬ塗
除湿岳７Ｖこ導入子ゐ。除湿命ｆ／コに粧鮮突気取り人
ｎ口８から吸引発酵カス坦の１０〜５Ｏ％の新鮮空気が
尋人式ｎ吸引発酵カスと混合さ肚、消費酸素が補給さｎ
て発酵カス温度が４５〜６０℃、＠対湿度が８０〜９０
％にｌゐ。XA fermentation note/I-1 image preferably has a moisture content of 40 to 65.
%, enshrined in PI-17 to 9, deposited in the γL hate circle nro○ uninvented overuse as an intoxicating image, human excrement,
Sewage sludge, raw garbage, accumulated molten fused statues, etc. are fermented by suction station, 50 to 15 per warehouse.
0 N l/rrrun-m' tDmIiL T destination=
The result is suction by the gas suction header 4. At this time, the suction temperature is 5u~65℃, the humidity level is 98%, and the ammonia level is 1'; J3,000.
~10,00 oppm zz, bo C's fermented scum sword, compared to Shin'an, I removed the imitation accessory π with the removal finger 6, and this lL painting wet mountain 7V was introduced. In the dehumidifying machine, 10 to 5% of fresh air from the fermented scum is sucked from the air intake 8 and mixed with the suctioned fermented scum, and the consumed oxygen is replenished.
Fermentation residue temperature is 45-60℃, @ relative humidity is 80-90℃.
% to lii.

ま／こ除湿器内でに水が粕蕗し、こｎに１０μ以下の倣
小ｌ有像物、無機物が捕捉さｎる。暇「鮮空気に人気中
の空気が用いらＫＬろが、好１しくに０℃〜６５℃、相
対湿度５０％程度のものが用いら扛る０ 除湿さ７’した発酵カスは吸込気プロワ−９で、独力さ
ｎ送気ヘッダー５により発酔憎の１氏部より送気孔ケ有
した送気貨６に循環送気きｎゐ０ヤして発船引安物＊、
ｉｏ日１ｕｊ以下程度の短誹り」向で好気発酵し、堆肥
や土壕改良拐として使用さｎる発酵完了物とｌゐ０ 第２図に、堆積型発酵惰χ多憎配列したＪ易付の吸引官
送気看の配置タリの図でめゐＱ第３１ａに不発明に用い
ら７Ｌる光彫カス除湿装血の一実施？ＩＪ孕ボ丁祝明凶
であゐ０角面状の発酵カス除湿器は不休１１の肉倶ＩＬ
［Ｉ］にＣユ光ｔ４カス取り人ス１１口１２と発酵カス
出口１６〃）肢けらｆｌており、発酵カス流路ＶＣにル
ーバー状の除去板１４が収けらＩｌｌ”Ｌ、取９人７ム
ロ１２の近辺にに耕鮮空気取り人ｎ口１６か設けらｎ、
本俸下部には除去口１５が収けら１１．ていゐ。Water forms in the dehumidifier, and small image objects and inorganic objects of 10 μm or less are captured in this water. If fresh air is used, preferably one with a temperature of 0°C to 65°C and a relative humidity of about 50% is used.The dehumidified fermentation scum is transferred to a suction air blower. At -9, I used the air supply header 5 to supply circulating air from the 1st part of the intoxication unit to the air supply cargo 6 which had an air supply hole, and then departed the ship.
Figure 2 shows the fermented product that undergoes aerobic fermentation in a short period of less than 1 day, and is used as compost or soil improvement material. In the accompanying diagram of the arrangement of the suction unit and air supply unit, is the 7L light carved waste dehumidifying blood used inventively in Q.31a? The square-shaped fermentation scum dehumidifier is the best choice for IJ pregnant women.
[I] has a C light t4 scum remover 11 inlet 12 and a fermented scum outlet 16), and a louver-shaped removal plate 14 is housed in the fermented scum flow path VC. 7. 16 air intakes were established near Muro 12.
A removal port 15 is housed in the lower part of the book 11. Teii.

この除湿装置に発酵カス出口１２より発酵惰力・ら吸引
した高温多湿の発酵カス忙取人几。This dehumidifier is used to collect high-temperature and humid fermented scum from the fermentation scum outlet 12.

＊ｒ鮮債気忙吸引力で妙丁鮮空気取入口１６より取入′
ｎ１装置ｍＪ都で発酵カスと耕緋空気忙混合し。*Intake fresh air from Myocho fresh air intake 16 with suction power
The fermentation waste is mixed with the cultivation air in the n1 equipment mJ city.

放をδと共に発ｍガス帖ｉ点迄湖吸葡下ける。この混８
発１悴カス釦除去板１４にあて、混合発酵カス中の倣小
市嶺物及び無磯吻牙粕蕗水により除去下めとともにヤｄ
露水、水分除去オ行い、水噴霧湿式除塵装置と同僚の効
果に島えゐ０除塵除湿芒扛た発１ｔガスｔコ発ｍカス出
口１６よりプロワ−へ供Ａ８さｎゐ。又粕繕寺の水及び
除塵の塵芥は除去口１５ｊ９排出σせる。The emission is lowered along with δ until the emission point i. This mix 8
1. Apply to the scum removal plate 14, and remove the imitation small grains in the mixed fermentation scum with water.
Dew water and moisture were removed, and a water spray wet type dust removal device and a co-worker's effect were used to remove dust and dehumidify the air.One ton of gas was generated from the waste outlet 16 and sent to the blower. In addition, the water and dust from the kasu-kei temple are discharged through the removal port 15j9.

第４図ｉＪ光ｉｌｌ？カス除湿装珈の円面力式例図でめ
ゐ。第６凶のものと基不Ｈｊにに同様の構造葡している
か、不休に円筒状でロート状の来ガス体７が収げらγし
、除去板ａロート出口Ｖこ囲し７こ円板となっている。Figure 4 iJ light ill? An example of the circular force formula for a waste dehumidifier. It has the same structure as the sixth one, and the cylindrical and funnel-shaped gas body 7 is collected, and the removal plate a funnel outlet V is surrounded by 7 circles. It is a board.

第６図及び第４図のような構造の除湿器ケ用いると従来
のサイクロンでに捕捉でさｌかっ１ζ１０μ以下の倣小
竹磯ｑｖＪ、無磯物ン惚めで簡単な構造の装置により除
去丁ゐことかでさ〉０次に実施例について説明丁ゐ。When using a dehumidifier with a structure as shown in Figures 6 and 4, it is possible to remove particles of Kotakeiso qvJ with a size of 1ζ10μ or less that could not be captured with a conventional cyclone, using a device with a simple structure that makes it easy to remove particles. Next, I will explain the example.

装置としては第１図、第２凶、第６図のものを用いた。The apparatuses shown in Fig. 1, Fig. 2, and Fig. 6 were used.

発酵槽に縦１４ｍ、横１５ｍ１而さ１．８ｍで、吸引管
が面芒０．７ｍのところに平行に３ｍ）ＭＪ隔に設けた
。The fermenter was 14 m long, 15 m wide, and 1.8 m wide, and suction pipes were installed parallel to the 0.7 m awn at 3 m (MJ) intervals.

水分率５８〜６０％、ＰＨ８，５〜９の牛糞法４５、７
００　ｋｇケ発酵槽内に増殖し、吸引會開始した０発［
＃カスの吸引速度は８０〜１００Ｎ４／巌ｔｒ−ｍ’で
、吸引した発酵カスの崗度ｒ１．５５〜６５℃、相対湿
度に９５〜９８％であった０（の吸引発酵ガスに８〜１
５℃、５０〜６０％の紡鮮孕気紮発訃カス童の２０〜５
０％混台した。その釦朱混合発酊カス温度にＨ湿装置ｎ
、の放熱）Ｋ：宮め釦１ユ４５〜５５℃となった。また
除湿器内でガスの相対湿度ｆＩ８５〜９０％に低下し、
１０μ互での除＆能力忙発憚しブロワ−動力損失が減少
した。Cow dung method with moisture content 58-60% and pH 8,5-9 45,7
0.00 kg The 0 shots that multiplied in the fermenter and started a suction session [
#The suction speed of the scum was 80-100N4/Iwa tr-m', the suction rate of the fermentation scum was 1.55-65℃, and the relative humidity was 95-98%. 1
5℃, 50-60% of 20-5
0% mix. The button vermilion mixed intoxication scum temperature H humidity device n
, heat dissipation) K: 1 unit of the shrine button became 45 to 55°C. In addition, the relative humidity of the gas decreases to fI 85-90% in the dehumidifier,
The power loss of the blower has been reduced due to the 10μ mutual division and capacity loss.

除湿カスは発酵佃底部に吸引音と互い違いに設けらｎた
送気管から発酵性徊゛恢物に返送した。The dehumidified scum was returned to the fermentation container from air pipes arranged alternately with suction at the bottom of the fermentation tank.

その粕来発酵開始羨８〜１２時間で発酵温度は８０〜８
４℃に達し１発酵日数４日で発＃か児了しｈ−〇発酵光
了物は水分率４０〜４５％、ＰＦＩ７〜８となり、’ｎ
　ｍｗＩＪｒｌｌ　０〜１５　％Ｗ少した。父、装置収
置場所の臭酸に２以下となり／乙０ ４、図面の藺年ｌ祝明 第１凶に仝発明に用いら扛る吸引式堆積型発けｔ装置の
説明用系統図である。It took 8-12 hours for Kasuko to start fermenting, and the fermentation temperature was 80-8.
The temperature reached 4℃, and the fermentation product was completed in 4 days.
mwIJrll 0-15%W a little. My father, the amount of hydrochloric acid in the place where the device is stored is less than 2. be.

第２図ａ不発明に用いらｎゐ吸引式堆積型発酵装置の内
の　Ｑ　１惇僧ケ多情自己タリした場合の吸引管、送気
管の配隨廿り凶であゐ０ ノ 弔牛図に仝発明に用いしｎゐ発酵カス除湿装置汎の説明
図である。Fig. 2a Of the suction-type sedimentary fermentation equipment used in the non-inventive manner, the arrangement of suction pipes and air pipes in the case of Q1. FIG. 2 is an explanatory diagram of a general fermentation scum dehumidifying device used in the present invention.

ぐ 第を図に本発明に用いら７Ｌゐ他の形式の発酵ガス除湿
装置の説明図である。FIG. 7 is an explanatory diagram of another type of fermentation gas dehumidification device used in the present invention.

符号の説明 １　堆積型発酵借　　　　２　奴引孔〒凋した吸引管６
　送気孔を有し凡送気営　４　吸引ヘッダー５　送気ヘ
ノター　　　６　除藏器 ７　除湿器　　　　　　８　〃１鮮空気取入口９　吸送
気ブロワ− １１発酵カス師し直不体　　１２　　発酵カス取入口１
６　　新用：窒気）Ｉｙ、人口　　１４　　除去叡１５
　　除去口　　　　　　１６　　発酵ガス出口１７　　
東ガス体 ５１Explanation of symbols 1 Sediment type fermentation 2 Suction hole Decayed suction pipe 6
4 Suction header 5 Air supply vent 6 Dehumidifier 8 〃1 Fresh air intake 9 Suction air blower 11 Fermentation scum filter 12 Fermentation scum intake 1
6 New use: Nitrogen) Iy, population 14 Elimination 15
Removal port 16 Fermentation gas outlet 17
East gas body 51

Claims (1)

【特許請求の範囲】 １、　発酵性有機物孕発酵憎に入ｌし発酵槽中に設けた
吸引部から発酵ガスオ発酵性肩僚物容重当９５０〜１５
ＯＮ＃Δ票・醪の速度で吸引し除湿器に導入し、除湿器
で吸引発酵ガス重の１０〜５０％の耕鮮窒気に混合して
除湿除塵処理した抜、ｃｆオ促酵情ノ欣部に循環送気す
ること才時賊とする発酢性刹戦物の発酵処理方法。 ２、発＃僧の周囲が壁体で底盤に刹し、該発酵槽に堆積
ざぜる発４性南伽物の堆憤物筒さの底盤〃・ら６０〜８
０％の位置で吸引都孕収けた特許請求のヰＢ囲第１項の
発１シ１午有磯物の発酵処理方法。[Scope of Claims] 1. Fermentable organic matter is introduced into the fermenter and fermented gas is discharged from a suction section provided in the fermenter, with a volume of 950 to 15%.
ON#ΔVote・The fermentation gas was sucked at the same speed as the moromi, introduced into a dehumidifier, and mixed with cultivated nitrogen of 10 to 50% of the weight of the suctioned fermentation gas in the dehumidifier to dehumidify and remove dust. A method for fermentation treatment of vinegar-producing food products, which involves circulating air to the base. 2. The bottom plate is a wall with a wall around the monk, and the bottom plate of the cylindrical bottom plate is the sediment of the four-pronged Nangari, which is deposited in the fermentation tank. 60-8
1. A method for fermenting a seaweed material according to Paragraph 1 of the patent claim, in which the suction density is achieved at a position of 0%.