JP2002336821A - Garbage treatment system and treatment method for garbage fermentation decomposition liquid - Google Patents

Garbage treatment system and treatment method for garbage fermentation decomposition liquid

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Publication number
JP2002336821A
JP2002336821A JP2001150312A JP2001150312A JP2002336821A JP 2002336821 A JP2002336821 A JP 2002336821A JP 2001150312 A JP2001150312 A JP 2001150312A JP 2001150312 A JP2001150312 A JP 2001150312A JP 2002336821 A JP2002336821 A JP 2002336821A
Authority
JP
Japan
Prior art keywords
garbage
tank
fermentation
liquefied
filtrate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001150312A
Other languages
Japanese (ja)
Inventor
Hiroaki Kagimoto
博章 鍵本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
KAGIMOTO SHOKKI KK
Original Assignee
KAGIMOTO SHOKKI KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by KAGIMOTO SHOKKI KK filed Critical KAGIMOTO SHOKKI KK
Priority to JP2001150312A priority Critical patent/JP2002336821A/en
Publication of JP2002336821A publication Critical patent/JP2002336821A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To divide the liquefied matter produced by the fermentation decomposition of garbage from solids and to decompose the garbage without making the garbage into sludge so that the liquefied matter of the recovering garbage can be discarded on the spot. SOLUTION: The liquefied matter produced by the fermentation decomposition of the garbage is successively withdrawn out of a fermenter 1 and is housed in a liquid receiving tank 2 where the liquefied matter is filtered under circulation between the same tank and a filtering tank 8. The filtrate obtained as a result thereof is housed into a storage tank 13 and is blown in a foggy form into the upper space of a fermenter 1. The set air containing the spray liquid is sucked outside the fermenter 1 through an exhaust duct 17 and is released into the liquid in a solvent tank 19. While the garbage is maintained at an adequate moisture content, the fermentation decomposition thereof can be promoted according thereto and even more, the drying of the garbage is accelerated without requiring an enormous time and heat quantity and the discharge of the liquefied matter (filtrate) thereof to public water bodies, such as rivers, is prohibited.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、微生物の働きによ
り生ゴミ(食品残渣などの有機系廃棄物)を発酵分解す
る技術に係わり、特に生ゴミの発酵分解により発生する
液化物を固形物と分けて清浄状態にして廃棄するように
した生ゴミ処理システムと生ゴミ発酵分解液の処理方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technology for fermenting and decomposing garbage (organic waste such as food residues) by the action of microorganisms. The present invention relates to a garbage disposal system and a method for treating a garbage fermentation decomposition liquid that are separated and disposed in a clean state.

【0002】[0002]

【従来の技術】近年、大量生産・大量消費が進む中、多
くの廃棄物が発生して深刻な社会問題となっている。特
に、食品残渣などの生ゴミは悪臭を放つ上、多量の水分
を含んでいることから、その処理に苦慮してきた。そこ
で、近年になり家庭用や業務用として、生ゴミを処理す
るための多種多様な装置が開発されている。
2. Description of the Related Art In recent years, with the progress of mass production and mass consumption, a large amount of waste has been generated and has become a serious social problem. In particular, garbage such as food residues has a bad smell and contains a large amount of water, so that it has been difficult to treat it. Therefore, in recent years, various devices for treating garbage have been developed for home use and business use.

【0003】その処理メカニズムとして、生ゴミを温風
などで加熱乾燥して減容するタイプもあるが、その多く
は微生物を利用して生ゴミを発酵分解させるものであ
る。そして、その種の生ゴミ処理装置によれば、微生物
の働きにより生ゴミを究極的に水と二酸化炭素にまで分
解できるとして、一般に広く賞用されている。
[0003] As a treatment mechanism, there is a type in which garbage is heated and dried with hot air or the like to reduce the volume, but most of them use microorganisms to ferment and decompose garbage. According to such a kind of garbage processing apparatus, garbage can be ultimately decomposed into water and carbon dioxide by the action of microorganisms, and is generally widely used.

【0004】[0004]

【発明が解決しようとする課題】然し乍ら、微生物の働
きを利用する従来の生ゴミ処理装置は、微生物を培養し
たおが屑や木質チップなど多量の基剤を生ゴミと混合し
て処理するため、一度に処理できる生ゴミの量が少なく
非効率であった。
However, a conventional garbage disposal apparatus utilizing the action of microorganisms is a method of mixing and processing a large amount of base such as sawdust and wood chips obtained by culturing microorganisms with garbage. The amount of garbage that can be processed quickly was inefficient.

【0005】このため、基剤の投入量を少なくする場合
もあるが、これでは処理中に生じた液化物で生ゴミが汚
泥化してしまい、その水分量を適性値まで低下させるの
に膨大な時間と熱量を必要とした。
[0005] For this reason, there are cases where the amount of the base material to be introduced is reduced. However, in this case, garbage is formed into sludge by the liquefied material generated during the treatment, and it is enormous to reduce the water content to an appropriate value. It required time and heat.

【0006】そこで、本願出願人は生ゴミの発酵分解に
より発生した液化物(発酵分解液)をスクリーンを通し
て発酵槽内から逐次抜き取ることにより、発酵槽内の水
分量を調整するといった処理装置を先に開発したが、発
酵槽から抜き取った生ゴミの液化物は多量の浮遊固形物
を含んで悪臭を放つため、そのまま河川など公共の用水
域に放流する訳にはいかず、その浄化処理を公的施設な
どに委ねてきたため、これに掛かる処理コストが大きい
という問題があった。
Therefore, the applicant of the present application has first introduced a processing apparatus that adjusts the amount of water in the fermentation tank by sequentially extracting liquefied substances (fermentation decomposition liquid) generated by fermentation decomposition of garbage from the fermentation tank through a screen. However, since the liquefied garbage extracted from the fermenter contains a large amount of suspended solids and emits an offensive odor, it cannot be discharged directly into public water bodies such as rivers. There is a problem that the processing cost involved is large because it is entrusted to facilities and the like.

【0007】本発明は以上のような事情に鑑みて成され
たものであり、その目的は生ゴミを効率よく発酵分解し
つつ、発生した液化物をその場で浄化して廃棄できるよ
うにする事にある。
The present invention has been made in view of the above circumstances, and an object of the present invention is to make it possible to purify and dispose of generated liquefied matter on the spot while efficiently fermenting and decomposing garbage. It is in the thing.

【0008】[0008]

【課題を解決するための手段】本発明は上記目的を達成
するため、生ゴミを撹拌しつつ発酵分解させるための発
酵槽と、この発酵槽の底部に接続して生ゴミの発酵分解
により発生する液化物を収容するための受液槽と、その
受液槽に集められた生ゴミの液化物を濾過して得た濾液
を収容するための貯蔵槽と、この貯蔵槽内に蓄えられた
濾液を発酵槽内の上部空間に霧状にして吹き込む噴霧手
段とを備え、前記発酵槽には噴霧手段により内部に吹き
込まれた濾液を含む湿潤空気を外部に排出するための排
気ダクトが接続され、その排気ダクトの先端に前記湿潤
空気を放出する溶媒槽が設けられて成る生ゴミ処理シス
テムを提供する。
In order to achieve the above object, the present invention provides a fermentation tank for fermenting and decomposing garbage while stirring the garbage, which is connected to the bottom of the fermentation tank to generate garbage by fermentation and decomposition. And a storage tank for storing a filtrate obtained by filtering the garbage liquefied matter collected in the liquid receiving tank, and a storage tank for storing the filtrate obtained in the storage tank. Spraying means for spraying the filtrate into an upper space in the fermenter in the form of mist, and an exhaust duct for discharging wet air containing the filtrate blown into the fermenter to the outside by the spraying means is connected to the fermenter. And a garbage disposal system provided with a solvent tank for discharging the moist air at the end of the exhaust duct.

【0009】又、本発明は生ゴミの発酵分解により発生
する液化物を処理するための方法であって、生ゴミを発
酵分解せしめる発酵槽の内部から生ゴミの液化物を逐次
抜き取って貯蔵槽に収容すると共に、その貯蔵槽内に蓄
えられた液化物を空気圧により前記発酵槽内の上部空間
に噴霧しつつ、該発酵槽に接続する排気ダクト内の気流
に乗せて発酵槽外へ排出することを特徴とする生ゴミ発
酵分解液の処理方法を提供する。
Further, the present invention is a method for treating a liquefied material generated by the fermentation and decomposition of garbage, wherein a liquefied garbage of the garbage is sequentially extracted from a fermentation tank for fermenting and decomposing the garbage. While discharging the liquefied matter stored in the storage tank into the upper space in the fermentation tank by air pressure, and discharging the liquefied substance out of the fermentation tank by putting it in an airflow in an exhaust duct connected to the fermentation tank. The present invention provides a method for treating a garbage fermentation decomposition solution.

【0010】特に、生ゴミの発酵分解により発生する液
化物を処理するための方法であって、生ゴミを発酵分解
せしめる発酵槽の内部から生ゴミの液化物を逐次抜き取
って濾過し、その濾液を貯蔵槽内に収容すると共に、そ
の貯蔵槽内に蓄えられた濾液を空気圧により前記発酵槽
内の上部空間に噴霧しつつ、該発酵槽に接続する排気ダ
クト内の気流に乗せて溶媒槽に送り、その溶媒槽内の液
中に排気ダクトで運ばれた湿潤空気を放出することを特
徴とする。
In particular, the present invention relates to a method for treating a liquefied material generated by fermentation and decomposition of garbage, wherein a liquefied material of garbage is sequentially extracted from the inside of a fermenter for fermenting and decomposing garbage and filtered. While the filtrate stored in the storage tank is sprayed into the upper space in the fermentation tank by air pressure, and placed in an airflow in an exhaust duct connected to the fermentation tank to the solvent tank. The method is characterized in that the wet air carried by the exhaust duct is discharged into the liquid in the solvent tank.

【0011】[0011]

【発明の実施の形態】以下、本発明の適用例を図面に基
づいて詳細に説明する。先ず、図1に本発明に係る生ゴ
ミ処理システムの概略を示す。図1において、1は生ゴ
ミを発酵分解せしめるための発酵槽であり、その外周面
には図示せぬヒータパネルが装置されている。又、2は
発酵槽1の底部に接続する受液槽であり、この受液槽2
には発酵槽1内での生ゴミの発酵分解により発生する液
化物が収容されるようになっている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. First, FIG. 1 schematically shows a garbage disposal system according to the present invention. In FIG. 1, reference numeral 1 denotes a fermenter for fermenting and decomposing garbage, and a heater panel (not shown) is provided on an outer peripheral surface thereof. Reference numeral 2 denotes a liquid receiving tank connected to the bottom of the fermenter 1.
The liquefied matter generated by fermentation decomposition of garbage in the fermenter 1 is stored in the fermenter 1.

【0012】特に、本例において、受液槽2は堰板3,
4,5により横並びの4つの部屋6A〜6Dに区分され
た沈殿槽を成し、その一端の部屋6Aに配管7を通じて
発酵槽1内から生ゴミの液化物が流入するようにしてあ
る。又、中間の部屋6B,6Cの底面は傾斜状とされ、
その下流側における一端の部屋6Aに沈殿物を含む生ゴ
ミの液化物が集まるようにしてある。8はその液化物を
濾過するための濾過槽であり、この濾過槽8は発酵槽1
の上部にあって、受液槽2の部屋6Aと管路9(往路)
を介して接続される。10は管路9に接続するポンプ、
11は濾過槽8を通した濾液を受液槽2に戻すための管
路(復路)であり、その先端は中間の部屋6Cに接続さ
れる。
In particular, in the present embodiment, the liquid receiving tank 2 has a weir plate 3,
A sedimentation tank divided into four chambers 6A to 6D arranged side by side by 4 and 5 forms a liquefied garbage from the fermentation tank 1 through a pipe 7 into a chamber 6A at one end. Also, the bottom surfaces of the middle rooms 6B and 6C are inclined,
The liquefied garbage including sediment is collected in the room 6A at one end on the downstream side. Reference numeral 8 denotes a filtration tank for filtering the liquefied product, and the filtration tank 8
6A of the receiving tank 2 and the pipeline 9 (outbound route)
Connected via 10 is a pump connected to the line 9;
Reference numeral 11 denotes a pipe (return path) for returning the filtrate passed through the filtration tank 8 to the liquid receiving tank 2, and the tip thereof is connected to the intermediate room 6C.

【0013】そして、その部屋6Cに戻された濾液の上
澄みが堰板5(越流堰)の上部を越えて上流の部屋6D
に流入するようにしてある。12はその部屋6Dに集め
られた濾液を排出するためのポンプ、13はポンプ12
により取り出された濾液を収容するための貯蔵槽であ
り、この貯蔵槽13には外気を取り込むためのファン1
4とエアコンプレッサ15とが接続され、そのエアコン
プレッサ15による空気圧により貯蔵槽13内に蓄えら
れた濾液が霧状とされて発酵槽1内に吹き込むようにし
てある。16は発酵槽1の上部空間に貯蔵槽13内の濾
液を噴霧する噴霧管であり、その両端は貯蔵槽13と発
酵槽1の上部とに接続される。
[0013] Then, the supernatant of the filtrate returned to the room 6C is over the upper part of the weir plate 5 (overflow weir) and is located in the upstream room 6D.
It is made to flow into. 12 is a pump for discharging the filtrate collected in the room 6D, and 13 is a pump 12
Is a storage tank for storing the filtrate taken out by the above-described method. The storage tank 13 has a fan 1 for taking in outside air.
4 is connected to the air compressor 15, and the filtrate stored in the storage tank 13 is atomized and blown into the fermentation tank 1 by the air pressure of the air compressor 15. Reference numeral 16 denotes a spray tube for spraying the filtrate in the storage tank 13 into the upper space of the fermenter 1, and both ends thereof are connected to the storage tank 13 and the upper part of the fermenter 1.

【0014】そして、以上のように構成される生ゴミ処
理システムによれば、生ゴミの発酵分解により発生する
液化物を発酵槽1の内底部より逐次抜き取って受液槽2
に収容し、これを濾過槽8との間で循環させつつ濾過し
て浄化し、その濾液を貯蔵槽13に収容しつつ発酵槽1
の上部空間に霧状にして吹き込み、その気化を発酵槽1
内の発酵熱にて促進させ、その噴霧液(濾液)を含んだ
湿潤空気を発酵槽1の内部から排気ダクト17を通じて
発酵槽1外へ排出することができる。尚、排気ダクト1
7には排気用のファン18が介在され、その先端には湿
潤空気を放出せしめる凝結用の溶媒槽19が設けられ
る。
According to the garbage disposal system configured as described above, the liquefied matter generated by the fermentation decomposition of the garbage is sequentially extracted from the inner bottom of the fermenter 1 and the liquid receiver 2
The filtrate is purified while being circulated through the filtration tank 8 and purified, and the filtrate is stored in the storage tank 13 while the fermentation tank 1 is stored.
In the form of a mist into the upper space of the
The fermentation heat is accelerated in the inside, and the moist air containing the spray liquid (filtrate) can be discharged from the inside of the fermentation tank 1 to the outside of the fermentation tank 1 through the exhaust duct 17. In addition, exhaust duct 1
An exhaust fan 18 is interposed in 7, and a condensing solvent tank 19 for releasing wet air is provided at the tip of the fan 18.

【0015】図2で明らかなように、溶媒槽19には適
量の溶液L(本例において水)が蓄えられ、その溶液L
中に排気ダクト17で運ばれた湿潤空気が放出されるよ
うにしてある。尚、排気ダクト17は溶媒槽19の底部
に挿入され、その先端には湿潤空気を放出する多孔管1
7Aが接続される。そして、この溶媒槽19によれば、
濾液を含む湿潤空気を凝結し、これによって増量する溶
液Lをオーバフローさせるなどして外部に廃棄すること
ができる。又、同図で明らかなように、溶媒槽19と貯
蔵槽13とは隔壁20で仕切られた一体のユニットとし
て構成される。このうち、貯蔵槽13は隔壁21により
二つの部屋13A,13Bに区分され、その一方の部屋
13Aに上記した受液槽から配管22を通じて生ゴミの
液化物(濾液)が送り込まれるようにしてある。特に、
この部屋13Aは図1に示したファン14により通気が
行われる曝気槽とされる。
As is apparent from FIG. 2, an appropriate amount of solution L (water in this example) is stored in the solvent tank 19, and the solution L
Inside, the humid air carried by the exhaust duct 17 is discharged. Note that the exhaust duct 17 is inserted into the bottom of the solvent tank 19, and the tip of the exhaust duct 17 is a perforated tube 1 for discharging wet air.
7A is connected. And according to this solvent tank 19,
The moist air containing the filtrate is condensed, and the increased amount of the solution L can be discarded outside by overflowing or the like. In addition, as is apparent from the figure, the solvent tank 19 and the storage tank 13 are configured as an integral unit separated by a partition 20. The storage tank 13 is divided into two chambers 13A and 13B by a partition 21, and a liquefied garbage (filtrate) of garbage is sent to one of the chambers 13A from the above-described liquid receiving tank through a pipe 22. . In particular,
This room 13A is an aeration tank to be ventilated by the fan 14 shown in FIG.

【0016】尚、隔壁21の下部にはフロート弁23を
取り付けた連通管24が貫通され、その連通管24を通
じて一方の部屋13Aから他方の部屋13Bに濾液が自
動的に補給されるようにしてある。因に、フロート弁2
3に代えて電磁弁などを利用可能であること勿論であ
る。一方、部屋13Bには発酵槽1の上部空間に向けて
延びる噴霧管16が接続されるほか、その噴霧管16に
向けて底部に溜まった濾液を霧状にして噴射するノズル
25が内蔵される。ノズル25には図1に示したエアコ
ンプレッサ15で得た圧縮空気を供給するための給気管
26が接続されると共に、部屋13Bの底部に溜まった
濾液を吸い上げるための給液管27が接続される。又、
部屋13Bにはダクト28を介して乾燥空気を吹き込む
ためのファン29が接続される。尚、その乾燥空気の熱
源はヒータなどであれば良い。
A communication pipe 24 to which a float valve 23 is attached passes through the lower part of the partition 21 so that the filtrate is automatically supplied from one chamber 13A to the other chamber 13B through the communication pipe 24. is there. By the way, float valve 2
Of course, an electromagnetic valve or the like can be used instead of 3. On the other hand, a spray tube 16 extending toward the upper space of the fermenter 1 is connected to the room 13B, and a nozzle 25 for atomizing and injecting a filtrate collected at the bottom toward the spray tube 16 is incorporated. . An air supply pipe 26 for supplying compressed air obtained by the air compressor 15 shown in FIG. 1 is connected to the nozzle 25, and a liquid supply pipe 27 for sucking up filtrate collected at the bottom of the chamber 13B is connected. You. or,
A fan 29 for blowing dry air through the duct 28 is connected to the room 13B. The heat source of the dry air may be a heater or the like.

【0017】ここで、ノズル25は図3に示すようにス
ロート30をもつベンチュリ31を含んで構成される。
そして、ベンチュリ31の一端に給気管26が接続され
る一方、給液管27はスロート30よりベンチュリ31
の内部に突出される。このため、スロート30を通る圧
縮空気により給液管27から濾液が吸い出され、これが
霧状となってベンチュリ31の先端より噴出されること
になる。
The nozzle 25 includes a venturi 31 having a throat 30, as shown in FIG.
The supply pipe 26 is connected to one end of the venturi 31, while the supply pipe 27 is connected to the venturi 31 from the throat 30.
Protruded inside. Therefore, the filtrate is sucked out of the liquid supply pipe 27 by the compressed air passing through the throat 30, and becomes a mist and is ejected from the tip of the venturi 31.

【0018】次に、発酵槽の好適な態様を図4に示して
説明する。この図で明らかなように、発酵槽1の上部に
は生ゴミを導入するための投入口32が設けられ、その
内部には生ゴミを撹拌するための撹拌翼33が設けられ
る。撹拌翼33は図示せぬ駆動源により回転駆動される
回転軸34と、この回転軸に放射状に取り付けられる撹
拌棒35とで構成され、回転軸34の一端には外部動力
を得るためのスプロケット36が取り付けられる。又、
発酵槽1は投入口32をもつ一次発酵室1Aとこれに隣
接する二次発酵室1Bとに仕切板37で区分される。
Next, a preferred embodiment of the fermenter will be described with reference to FIG. As is clear from this figure, an input port 32 for introducing garbage is provided at the upper part of the fermenter 1, and a stirring blade 33 for stirring garbage is provided inside the inlet 32. The stirring blade 33 includes a rotating shaft 34 driven by a driving source (not shown) and a stirring rod 35 radially attached to the rotating shaft. One end of the rotating shaft 34 has a sprocket 36 for obtaining external power. Is attached. or,
The fermenter 1 is divided by a partition 37 into a primary fermentation chamber 1A having an inlet 32 and a secondary fermentation chamber 1B adjacent thereto.

【0019】特に、それら一次発酵室1Aと二次発酵室
1Bとの底部にはそれぞれU字形の断面をもつトラフ3
8,39が形成され、その各トラフ38,39の内部に
撹拌翼33と並行するスクリュー40,41が装置され
る。このうち、一方のトラフ38は一次発酵室1Aから
二次発酵室1Bの一端部まで達し、その底面は全長に亙
って所定の開口率を有するスクリーン42(濾板)とさ
れ、その下部にはスクリーン42を透過した生ゴミの液
化物を受ける漏斗状をした液溜部43が形成される。そ
して、その液溜部43と上記した受液槽2とが配管7に
て連結され、発酵槽1内における生ゴミの液化物がスク
リーン42にて一次濾過された後、液溜部43を通じて
受液槽2に収容されるようにしてある。
Particularly, troughs 3 each having a U-shaped cross section are provided at the bottoms of the primary fermentation chamber 1A and the secondary fermentation chamber 1B.
8 and 39 are formed, and screws 40 and 41 are installed inside the respective troughs 38 and 39 in parallel with the stirring blade 33. One of the troughs 38 extends from the primary fermentation chamber 1A to one end of the secondary fermentation chamber 1B. The bottom surface of the trough 38 is a screen 42 (filter plate) having a predetermined opening ratio over the entire length. A funnel-shaped liquid reservoir 43 is formed to receive liquefied garbage that has passed through the screen 42. Then, the liquid reservoir 43 and the above-mentioned liquid receiving tank 2 are connected by a pipe 7, and a liquefied garbage in the fermenter 1 is primarily filtered by a screen 42, and then received through the liquid reservoir 43. It is configured to be accommodated in the liquid tank 2.

【0020】尚、スクリュー40はモータ44により回
転され、一次発酵室1A内の生ゴミを図4の左方に送っ
て循環させるが、その発酵分解が進行すると一次発酵室
1Aの生ゴミを二次発酵室1Bへ移送するべく逆転され
る。一方、スクリュー41はモータ45により回転駆動
され、これを内蔵するトラフ39の先端には二次発酵室
1Bでの発酵分解によりコンポスト化した生ゴミを取り
出すための取出口46が形成される。
The screw 40 is rotated by a motor 44, and the garbage in the primary fermentation chamber 1A is sent to the left side of FIG. 4 to circulate the garbage. It is reversed to transfer to the next fermentation room 1B. On the other hand, the screw 41 is driven to rotate by a motor 45, and an outlet 46 for taking out garbage composted by fermentation decomposition in the secondary fermentation chamber 1B is formed at the tip of a trough 39 containing the screw 41.

【0021】又、図4から明らかなように、濾過槽8は
上流端に受液槽から延びる管路9の一端が接続する傾斜
路47と、その内側に形成される貯液部48とから成
り、その貯液部48と傾斜路47とを区分する仕切りの
一部が金網など所定の開口率をもつスクリーン49とさ
れている。特に、傾斜路47の下流端は発酵槽1内に開
通され、貯液部48の底面には受液槽に向けて延びる管
路11の一端が接続される。そして、この濾過槽8によ
れば、受液槽2から管路9を通じて送られた生ゴミの液
化物を傾斜路47に通しつつ、これをスクリーン49に
て濾過し、スクリーン49上に残ったケーク(濾滓)を
発酵槽1内に還元する一方、スクリーン49を透過した
濾液を管路11を通じて受液槽2に戻すことができる。
As is apparent from FIG. 4, the filtration tank 8 has an upstream end connected to an inclined path 47 to which one end of a pipe 9 extending from the liquid receiving tank is connected, and a liquid storage section 48 formed inside the inclined path 47. A part of a partition that separates the liquid storage section 48 from the inclined path 47 is a screen 49 having a predetermined aperture ratio such as a wire mesh. In particular, the downstream end of the ramp 47 is opened into the fermenter 1, and one end of the pipe 11 extending toward the liquid receiving tank is connected to the bottom of the liquid storage 48. According to the filtration tank 8, while the liquefied garbage sent from the liquid receiving tank 2 through the pipe 9 is passed through the slope 47, it is filtered by the screen 49 and remains on the screen 49. While the cake (filter cake) is reduced into the fermenter 1, the filtrate that has passed through the screen 49 can be returned to the liquid receiver 2 through the pipe 11.

【0022】ここで、以上のように構成される生ゴミ処
理システムの作用と、これを例に生ゴミ発酵分解液の処
理方法を主体とする生ゴミの処理方法を説明する。先
ず、発酵槽1内を図示せぬヒータパネルにて加熱すると
共に、その内部(一次発酵室1A)に投入口32より適
量の生ゴミを投入する。そして、撹拌翼33を所定方向
に回転させ、これにより発酵槽1内の生ゴミを撹拌しつ
つ、モータ44を駆動してスクリュー40を所定方向に
回転させることにより撹拌中の生ゴミを一次発酵室1A
の底部で循環させる。つまり、発酵槽1内の生ゴミは、
撹拌翼33にて撹拌されつつ其の回転軸34方向に送ら
れ、このとき其の一部がトラフ38内に落下し、そのト
ラフ38内のスクリュー40にて撹拌翼33と逆方向に
送られつつ圧搾され、圧搾後にスクリュー40の一端側
より上方に吐き出されて撹拌翼33で再び撹拌されるこ
とになる。
Here, the operation of the garbage disposal system configured as described above and a method of treating garbage mainly using the method of treating a garbage fermentation decomposition solution will be described. First, the inside of the fermenter 1 is heated by a heater panel (not shown), and an appropriate amount of garbage is put into the inside (primary fermentation chamber 1A) through the inlet 32. Then, the stirring wings 33 are rotated in a predetermined direction, whereby the garbage in the fermenter 1 is stirred while the motor 44 is driven to rotate the screw 40 in the predetermined direction. Room 1A
Circulate at the bottom. That is, the garbage in the fermenter 1
While being stirred by the stirring blade 33, it is sent in the direction of the rotation axis 34, and at this time, a part thereof falls into the trough 38, and is sent in the opposite direction to the stirring blade 33 by the screw 40 in the trough 38. After being squeezed, it is discharged upward from one end of the screw 40 after being squeezed, and is again stirred by the stirring blade 33.

【0023】このように、生ゴミは撹拌翼33による撹
拌とスクリュー40による圧搾とを繰り返されながら循
環され、その過程で微生物の働きによる発酵分解が進
み、これによって発生した液化物がスクリーン42によ
り一次濾過されて液溜部43に集められる。そこで、そ
の液化物を配管7を通じて発酵槽1内から逐次抜き取
り、これを受液槽2に収容する。そして、その液化物を
濾過槽8との間で循環させつつ二次濾過し、受液槽2に
戻った濾液をポンプ12により貯蔵槽の部屋13Aに移
し替え、ここでファン14による活発な通気を行いつ
つ、これをフロート弁23の作動により隣の部屋13B
に適量ずつ補給する。
As described above, the garbage is circulated while being repeatedly stirred by the stirring blades 33 and squeezed by the screw 40. In the process, the fermentation and decomposition by the action of microorganisms proceed. It is primarily filtered and collected in a liquid reservoir 43. Therefore, the liquefied material is sequentially extracted from the fermenter 1 through the pipe 7 and stored in the liquid receiver 2. Then, the liquefied material is subjected to secondary filtration while circulating with the filtration tank 8, and the filtrate returned to the liquid receiving tank 2 is transferred to the storage tank room 13 </ b> A by the pump 12. While the float valve 23 is activated, the next room 13B
Replenish in appropriate amounts.

【0024】而して、部屋13B内にファン29からダ
クト28を通じて乾燥空気を吹き込む一方、エアコンプ
レッサ15を作動させてノズル25に給気管26を通じ
て圧縮空気を供給し、その空気圧により貯蔵槽の部屋1
3Bの底部に溜まった濾液をノズル25の先端より霧状
として噴射し、これを噴霧管16を通して発酵槽1内の
上部空間に吹き込む。すると、発酵槽1内の発酵熱によ
る暖気と上記の乾燥空気とにより濾液の気化が急速に進
行し、これが飽和蒸気と化して発酵槽1の上部空間に滞
留するようになる。そこで、ファン18を作動させて発
酵槽1内の湿潤空気を吸い出し、その湿潤空気に含まれ
る濾液を排気ダクト17中の気流に乗せて運び、これを
溶媒槽19内の溶液L中に放出する。これにより、濾液
は凝結し、ドレンとなって溶液L中に混合されることに
なる。
While the dry air is blown into the room 13B from the fan 29 through the duct 28, the air compressor 15 is operated to supply the compressed air to the nozzle 25 through the air supply pipe 26. 1
The filtrate collected at the bottom of 3B is sprayed as a mist from the tip of the nozzle 25, and is blown into the upper space in the fermenter 1 through the spray pipe 16. Then, the vaporization of the filtrate proceeds rapidly due to the warm air due to the fermentation heat in the fermentation tank 1 and the above-described dry air, which turns into saturated steam and stays in the upper space of the fermentation tank 1. Then, the fan 18 is operated to suck out the humid air in the fermenter 1, and the filtrate contained in the humid air is carried by the airflow in the exhaust duct 17 and discharged into the solution L in the solvent tank 19. . As a result, the filtrate condenses, becomes a drain, and is mixed in the solution L.

【0025】そして、以上のような方法によれば、生ゴ
ミを好適な水分量に保ったままその発酵分解を促進させ
ることができ、しかも多大な時間や熱量を必要とする事
なく生ゴミの乾燥を促し、回収した液化物(濾液)を河
川など公共用水域に放流しないようにできる。
According to the above-mentioned method, it is possible to promote the fermentation and decomposition of the garbage while keeping the garbage at a suitable amount of water, and furthermore, to reduce the amount of the garbage without requiring much time and heat. It promotes drying and prevents the collected liquefied matter (filtrate) from being discharged into public water bodies such as rivers.

【0026】尚、濾液を含んだ湿潤空気を溶媒槽19内
の液中に放出するのでなく、これを排気ダクト17を通
じて直接大気中に放出するようにしても良い。又、液溜
部43に代えて受液槽2を発酵槽1の底部に一体的に形
成したり、その種の受液槽2を用いずに発酵槽1の底部
から抜き取った生ゴミの液化物(一次濾過液)を貯蔵槽
13に導いて該貯蔵槽13内に収容するようにしても良
い。この場合、多数の浮遊固形物が存在しても、発酵槽
1内への噴霧時にその固形物を比重差により風選分離し
て発酵槽1内に落下させることができる。一方、貯蔵槽
13内の濾液を発酵槽1の上部空間に吹き込む噴霧手段
として、空気圧を必要としない液圧ノズルを用いること
もできる。又、発酵槽1や貯蔵槽13は二槽式に限らず
単槽式でも良い。更に、濾過槽8は同様な装置であれば
上記のような態様に限らず、その設置位置も発酵槽1の
上部に限らない。
Instead of releasing the moist air containing the filtrate into the liquid in the solvent tank 19, the moist air may be directly discharged to the atmosphere through the exhaust duct 17. Further, instead of the liquid reservoir 43, the liquid receiving tank 2 is formed integrally with the bottom of the fermenter 1 or the liquefaction of garbage extracted from the bottom of the fermenter 1 without using such a liquid receiving tank 2. An object (primary filtrate) may be guided to the storage tank 13 and stored in the storage tank 13. In this case, even when a large number of suspended solids are present, the solids can be separated by air separation and dropped into the fermentation tank 1 due to a difference in specific gravity when sprayed into the fermentation tank 1. On the other hand, as a spraying means for blowing the filtrate in the storage tank 13 into the upper space of the fermentation tank 1, a hydraulic nozzle that does not require air pressure can be used. Further, the fermenter 1 and the storage tank 13 are not limited to the two-tank type and may be a single-tank type. Further, the filtration tank 8 is not limited to the above-described mode as long as it is a similar device, and the installation position is not limited to the upper part of the fermentation tank 1.

【0027】[0027]

【発明の効果】以上の説明から明らかなように、本発明
によれば生ゴミの発酵分解により発生する液化物を発酵
槽内から逐次抜き取り、これを貯蔵槽に収容しながら発
酵槽内の上部空間に霧状にして吹き込み、その噴霧液を
排気ダクト中の気流に乗せて発酵槽外へ排出するように
していることから、生ゴミを汚泥化させる事なく好適に
発酵分解させる事ができ、しかも多量の熱量を消費する
事なく短時間で生ゴミの水分量を低下させる事ができ
る。
As is clear from the above description, according to the present invention, liquefied substances generated by fermentation and decomposition of garbage are sequentially extracted from the fermentation tank, and while the liquefied matter is stored in the storage tank, the upper part of the fermentation tank is removed. Since the mist is blown into the space and the sprayed liquid is discharged to the outside of the fermentation tank by the airflow in the exhaust duct, the garbage can be suitably fermented and decomposed without turning sludge into sludge. Moreover, the water content of the garbage can be reduced in a short time without consuming a large amount of heat.

【0028】又、発酵槽内から抜き取った生ゴミの液化
物を濾過して貯蔵槽に収容するようにしている事から、
噴霧系統が目詰まりする虞れがなく、しかもその噴霧液
(濾液)を含んだ湿潤空気を排気ダクトの先端から溶媒
槽内の液中に放出するようにしていることから、生ゴミ
の液化物を河川など公共用水域に放流しないことが可能
になる。
Also, since the liquefied garbage extracted from the fermentation tank is filtered and stored in the storage tank,
There is no danger of clogging of the spray system, and the humid air containing the spray liquid (filtrate) is discharged from the end of the exhaust duct into the liquid in the solvent tank. Can be released to public water bodies such as rivers.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明に係る生ゴミ処理システムのフロー図FIG. 1 is a flowchart of a garbage disposal system according to the present invention.

【図2】貯蔵槽と溶媒槽を示した断面概略図FIG. 2 is a schematic sectional view showing a storage tank and a solvent tank.

【図3】噴霧手段を構成するノズルの概略図FIG. 3 is a schematic view of a nozzle constituting a spray unit.

【図4】発酵槽の好適な態様を示した断面図FIG. 4 is a sectional view showing a preferred embodiment of the fermenter.

【符号の説明】[Explanation of symbols]

1 発酵槽 1A 一次発酵室 1B 二次発酵室 2 受液槽 8 濾過槽 13 貯蔵槽 15 エアコンプレッサ 16 噴霧管 17 排気ダクト 18 ファン 19 溶媒槽 25 ノズル 42,49 スクリーン DESCRIPTION OF SYMBOLS 1 Fermentation tank 1A Primary fermentation room 1B Secondary fermentation room 2 Receiving tank 8 Filtration tank 13 Storage tank 15 Air compressor 16 Spray tube 17 Exhaust duct 18 Fan 19 Solvent tank 25 Nozzle 42, 49 Screen

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 生ゴミを撹拌しつつ発酵分解させるため
の発酵槽と、この発酵槽の底部に接続して生ゴミの発酵
分解により発生する液化物を収容するための受液槽と、
その受液槽に集められた生ゴミの液化物を濾過して得た
濾液を収容するための貯蔵槽と、この貯蔵槽内に蓄えら
れた濾液を発酵槽内の上部空間に霧状にして吹き込む噴
霧手段とを備え、前記発酵槽には噴霧手段により内部に
吹き込まれた濾液を含む湿潤空気を外部に排出するため
の排気ダクトが接続され、その排気ダクトの先端に前記
湿潤空気を放出する溶媒槽が設けられて成る生ゴミ処理
システム。
1. A fermentation tank for fermenting and decomposing garbage while stirring, a liquid receiving tank connected to the bottom of the fermentation tank for containing a liquefied substance generated by fermentation decomposition of garbage,
A storage tank for containing a filtrate obtained by filtering liquefied garbage of the garbage collected in the liquid receiving tank, and the filtrate stored in this storage tank is atomized into an upper space in the fermentation tank. And an exhaust duct for discharging the wet air containing the filtrate blown into the inside of the fermenter by the spray means to the outside, and discharges the wet air to the tip of the exhaust duct. A garbage treatment system provided with a solvent tank.
【請求項2】 生ゴミの発酵分解により発生する液化物
を処理するための方法であって、生ゴミを発酵分解せし
める発酵槽の内部から生ゴミの液化物を逐次抜き取って
貯蔵槽に収容すると共に、その貯蔵槽内に蓄えられた液
化物を空気圧により前記発酵槽内の上部空間に噴霧しつ
つ、該発酵槽に接続する排気ダクト内の気流に乗せて発
酵槽外へ排出することを特徴とする生ゴミ発酵分解液の
処理方法。
2. A method for treating a liquefied material generated by fermentation and decomposition of garbage, wherein a liquefied material of garbage is sequentially extracted from a fermenter for fermenting and decomposing garbage and stored in a storage tank. At the same time, while liquefied matter stored in the storage tank is sprayed into the upper space in the fermentation tank by air pressure, the liquefied matter is discharged to the outside of the fermentation tank by being put on an airflow in an exhaust duct connected to the fermentation tank. A method for treating a garbage fermentation decomposition solution.
【請求項3】 生ゴミの発酵分解により発生する液化物
を処理するための方法であって、生ゴミを発酵分解せし
める発酵槽の内部から生ゴミの液化物を逐次抜き取って
濾過し、その濾液を貯蔵槽内に収容すると共に、その貯
蔵槽内に蓄えられた濾液を空気圧により前記発酵槽内の
上部空間に噴霧しつつ、該発酵槽に接続する排気ダクト
内の気流に乗せて溶媒槽に送り、その溶媒槽内の液中に
排気ダクトで運ばれた湿潤空気を放出することを特徴と
する生ゴミ発酵分解液の処理方法。
3. A method for treating a liquefied material generated by fermentation decomposition of garbage, wherein a liquefied material of garbage is sequentially extracted from a fermentation tank for fermenting and decomposing garbage, and the filtrate is filtered. While the filtrate stored in the storage tank is sprayed into the upper space in the fermentation tank by air pressure, and placed in an airflow in an exhaust duct connected to the fermentation tank to the solvent tank. A method for treating a garbage fermentation decomposed liquid, comprising feeding and discharging wet air carried by an exhaust duct into the liquid in the solvent tank.
JP2001150312A 2001-05-21 2001-05-21 Garbage treatment system and treatment method for garbage fermentation decomposition liquid Pending JP2002336821A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001150312A JP2002336821A (en) 2001-05-21 2001-05-21 Garbage treatment system and treatment method for garbage fermentation decomposition liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001150312A JP2002336821A (en) 2001-05-21 2001-05-21 Garbage treatment system and treatment method for garbage fermentation decomposition liquid

Publications (1)

Publication Number Publication Date
JP2002336821A true JP2002336821A (en) 2002-11-26

Family

ID=18995345

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001150312A Pending JP2002336821A (en) 2001-05-21 2001-05-21 Garbage treatment system and treatment method for garbage fermentation decomposition liquid

Country Status (1)

Country Link
JP (1) JP2002336821A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002361209A (en) * 2001-06-06 2002-12-17 Ohama Kiko Kk Apparatus for treating wet refuse
JP2008200570A (en) * 2007-02-19 2008-09-04 Waki Sangyo:Kk Apparatus for decomposing garbage
JP2009226353A (en) * 2008-03-25 2009-10-08 Clean Tec Kk Dry garbage treatment apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002361209A (en) * 2001-06-06 2002-12-17 Ohama Kiko Kk Apparatus for treating wet refuse
JP4541593B2 (en) * 2001-06-06 2010-09-08 大浜機工株式会社 Garbage disposal equipment
JP2008200570A (en) * 2007-02-19 2008-09-04 Waki Sangyo:Kk Apparatus for decomposing garbage
JP2009226353A (en) * 2008-03-25 2009-10-08 Clean Tec Kk Dry garbage treatment apparatus

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