JP2003126824A - Zero sludge septic tank and fermentation treatment apparatus - Google Patents

Zero sludge septic tank and fermentation treatment apparatus

Info

Publication number
JP2003126824A
JP2003126824A JP2001331613A JP2001331613A JP2003126824A JP 2003126824 A JP2003126824 A JP 2003126824A JP 2001331613 A JP2001331613 A JP 2001331613A JP 2001331613 A JP2001331613 A JP 2001331613A JP 2003126824 A JP2003126824 A JP 2003126824A
Authority
JP
Japan
Prior art keywords
tank
fermentation treatment
sludge
septic tank
chamber
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
JP2001331613A
Other languages
Japanese (ja)
Inventor
Kazuo Onodera
和夫 小野寺
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.)
OK BIO KENKYUSHO KK
Original Assignee
OK BIO KENKYUSHO 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 OK BIO KENKYUSHO KK filed Critical OK BIO KENKYUSHO KK
Priority to JP2001331613A priority Critical patent/JP2003126824A/en
Publication of JP2003126824A publication Critical patent/JP2003126824A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Filtering Materials (AREA)
  • Activated Sludge Processes (AREA)
  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a zero sludge septic tank and a fermentation treatment apparatus capable of discharging zero sludge and composting garbage to full maturity. SOLUTION: The fermentation treatment apparatus is provided with a fermentation treatment tank 1 having an intermittently operating agitator 2 and a plurality chambers 1a and 1b and a septic tank 4 having a filtration means 9. Each chamber of the fermentation treatment tank 1 is capable of storing a garbage A crushed by a crusher 7 through a branch unit 8, the septic tank 4 receives a water content B squeezed out from the garbage A through side wall holes of each chamber of the fermentation treatment tank 1 at the tank bottom, and discharges a filtrated water C to a disinfecting tank 11 through the filtration means 9. And an injection means 12 jetting a part of the filtrated water C with air to the tank bottom wherein sludge is deposited, and a returning means 13 returning a sludge D collected at the tank bottom to the branch unit 8 are provided. While the garbage is fermented and decomposed in one of the fermentation treatment tanks, composting to full maturity is proceeded in the other treatment tanks and the water content squeezed out through the side wall holes of each chamber of the fermentation tanks is discharged through the disinfecting tank after filtration in the septic tank, and the deposited sludge at the bottom of the septic tank is activated to be circulated and returned to the fermentation treatment tank.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、食品加工工場、レスト
ラン、学校、病院等から出される生ごみ(食品残渣)を
汚泥排出がゼロで完熟堆肥化できる汚泥ゼロの浄化槽と
醗酵処理装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a zero sludge septic tank and a fermentation treatment apparatus capable of composting raw garbage (food residues) from food processing factories, restaurants, schools, hospitals, etc. with zero sludge discharge. Is.

【0002】[0002]

【従来の技術】一般に、生ごみ処理には、少なくとも生
ごみを収納する醗酵処理槽と、該醗酵処理槽内の生ごみ
を間欠的に攪拌する攪拌機と、生ごみを醗酵分解させる
微生物の供給が必要であり、生ごみが収納された槽内で
微生物を増殖させて生ごみの体積を20分の1程度に減
少できるように構成されていた。
2. Description of the Related Art Generally, for processing food waste, at least a fermentation treatment tank for storing food waste, a stirrer for intermittently stirring the food waste in the fermentation treatment tank, and a supply of microorganisms for fermentative decomposition of the food waste. Was required, and the volume of the garbage was reduced to about 1/20 by growing the microorganisms in the tank containing the garbage.

【0003】前記微生物は、変温性で好気性の微生物群
であるが、これらの微生物の共生に必要な条件について
は、これまで未解明の部分が多く、酸素不足による腐敗
事故を招くことがあったが、本発明者は中高温で増殖可
能な好気性微生物であるバチルス群の研究を多年にわた
って続けてきた結果、土壌中から取り出した複数の菌
に、発育成分と消臭剤などを加えた特殊複合菌(以下
「OKZ菌」という)を開発し、生ごみ醗酵処理による
資源化の成果を得てきた。
The above-mentioned microorganisms are a thermophilic and aerobic group of microorganisms, but the conditions necessary for the symbiosis of these microorganisms have not been elucidated so far, which may lead to a spoilage accident due to lack of oxygen. However, as a result of continuing the research of the Bacillus group, which is an aerobic microorganism that can grow at medium and high temperatures, for many years, the present inventor added a growth component and a deodorant to a plurality of bacteria extracted from soil. We have developed a special complex bacterium (hereinafter referred to as "OKZ bacterium"), and have obtained the results of resource recycling through food waste fermentation processing.

【0004】こうした成果を踏まえる時、生ごみは最早
廃棄物ではなく、有機農業や低公害畜産の発展に貢献す
る有力な武器であり、地球環境を保全しようという気運
の高まりの中で脚光を浴び、家庭、企業、地方公共団体
などにおいて広く導入される兆しをみせている。
Based on these results, garbage is no longer a waste, but a powerful weapon that contributes to the development of organic agriculture and low-pollution livestock production, and is in the limelight in the wake of the desire to conserve the global environment. , Households, companies, local governments, etc. are showing signs of widespread adoption.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記生
ごみ醗酵処理において汚泥排出をゼロにして完熟堆肥化
することは不可能とされていた。本発明はこの点を解消
したものである。しかして、本発明の目的とするところ
は、汚泥排出をゼロにして生ごみを完熟堆肥化できるよ
うにした汚泥ゼロの浄化槽と醗酵処理装置を提供するこ
とにある。
However, in the above-mentioned food waste fermentation treatment, it has been impossible to make the sludge discharge to zero and to make it into a fully-ripened compost. The present invention solves this problem. Therefore, an object of the present invention is to provide a sludge-free septic tank and a fermentation treatment apparatus capable of completely composting raw garbage with zero sludge discharge.

【0006】[0006]

【課題を解決するための手段】上記の目的を達成するた
め、本発明に係る汚泥ゼロの浄化槽と醗酵処理装置は間
欠作動する攪拌機を有し、複数室を持つ醗酵処理槽と、
濾過手段を有する浄化槽とを備え、前記醗酵処理槽の各
室は破砕機にて破砕された生ごみを分岐機を介して収容
できるようになっており、前記浄化槽は前記醗酵処理槽
の各室の側壁の穴を通して生ごみより搾水された水分を
槽底から受け入れ、前記濾過手段を通した濾過水を消毒
槽へ流出させるようになっており、かつ、濾過水の一部
を汚泥が堆積する槽底へエアーとともに噴出させる噴射
手段と、槽底に集積させた汚泥を前記分岐機に戻す返送
手段とを備えたことを特徴とし、1つの醗酵処理槽で生
ごみを醗酵分解している間に、他の処理槽で完熟堆肥化
を進行させるとともに、醗酵処理槽の各室の側壁を通し
て搾水された水分は浄化槽にて濾過して消毒槽を介して
排水し、浄化槽の底部に堆積する汚泥は活性化して醗酵
処理槽へ循環返送できるように構成した。
In order to achieve the above object, a sludge-free septic tank and a fermentation treatment apparatus according to the present invention have an agitator that operates intermittently, and a fermentation treatment tank having a plurality of chambers,
And a septic tank having a filtering means, each chamber of the fermentation treatment tank is adapted to be able to accommodate the food waste crushed by a crusher through a branching machine, and the septic tank is each chamber of the fermentation treatment tank. The water squeezed from raw garbage is received from the tank bottom through the hole in the side wall of the tank, and the filtered water that has passed through the filtering means is allowed to flow out to the disinfection tank, and a part of the filtered water is accumulated by sludge. It is characterized in that it is equipped with an injection means for ejecting together with air to the bottom of the tank, and a returning means for returning the sludge accumulated on the bottom of the tank to the branching machine, in which one garbage is fermented and decomposed in one fermentation treatment tank. In the meanwhile, while proceeding to full-fledged composting in other treatment tanks, the water squeezed through the side walls of each chamber of the fermentation treatment tank is filtered by the septic tank, drained through the disinfection tank, and accumulated on the bottom of the septic tank. Activated sludge is activated and circulated back to the fermentation tank It was configured to kill.

【0007】また、請求項2に記載の発明は、前記攪拌
機の間欠作動が、10分間作動し、3時間50分間停止
するものであることを特徴とし、空気が過剰になること
を避け、微生物の呼吸熱を奪わないように構成した。
The invention according to claim 2 is characterized in that the intermittent operation of the stirrer operates for 10 minutes and stops for 3 hours and 50 minutes. It was constructed so as not to take away the respiratory fever of.

【0008】さらに、請求項3に記載の発明は、前記浄
化槽の濾過手段が、プラスチック繊維層を穴あきプラス
チック板で挟んでなることを特徴とし、醗酵処理槽の各
室の側壁を通して搾水された水分中に浮遊する固形分を
も確実に捕捉できるように構成した。
Furthermore, the invention according to claim 3 is characterized in that the filtering means of the septic tank comprises a plastic fiber layer sandwiched between perforated plastic plates, and water is squeezed through the side wall of each chamber of the fermentation processing tank. Also, it was configured so that solid matters floating in water can be reliably captured.

【0009】さらにまた、請求項4に記載の発明は、前
記噴射手段が、ミクロポンプを利用してなることを特徴
とし、浄化槽の底部に堆積する汚泥をマイナスイオン化
できるように構成した。
Furthermore, the invention as set forth in claim 4 is characterized in that the injection means uses a micropump, and the sludge deposited on the bottom of the septic tank can be negatively ionized.

【0010】[0010]

【発明の実施の態様】次に、本発明の実施の態様を図面
に基いて説明する。図1は本願装置の全体の構成を示す
略示的説明図、図2は醗酵処理槽の側壁の拡大断面図、
図3は濾過手段の略示的断面図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, embodiments of the present invention will be described with reference to the drawings. 1 is a schematic explanatory view showing the overall configuration of the apparatus of the present application, FIG. 2 is an enlarged sectional view of a side wall of a fermentation treatment tank,
FIG. 3 is a schematic sectional view of the filtering means.

【0011】図において、1は生ごみの醗酵処理槽で、
該醗酵処理槽1は複数室1a、1bに分割されている。
これら各室1a、1bには駆動機2aを共通にする攪拌
機2が備えられている。また、前記処理槽1の各室1
a、1bの外底部には室内の温度調整のためのヒーター
1c、1cがそれぞれ別個に制御できるように設けられ
ている。
In the figure, 1 is a fermentation treatment tank for food waste,
The fermentation treatment tank 1 is divided into a plurality of chambers 1a and 1b.
Each of these chambers 1a and 1b is provided with a stirrer 2 having a common drive unit 2a. In addition, each chamber 1 of the processing tank 1
Heaters 1c and 1c for controlling the temperature inside the room are provided on the outer bottom portions of a and 1b so that they can be individually controlled.

【0012】前記醗酵処理槽1の各室1a、1bの側壁
には、図2の如く、無数の小穴1dが設けられ、該小穴
1dを通して生ごみA中に含まれる水分が搾水されるよ
うになっている。この側壁の小穴1dは1mmφ程度で
よく、これを通して搾水された水分(未処理水)Bは集
水部材3にて集められ、導管3′を通して浄化槽4内に
その槽底から流入させるようになっている。この槽底へ
の流入は落差を利用してもよく、また、導管3′の途中
にポンプ(図示せず)を設けてもよい。
As shown in FIG. 2, innumerable small holes 1d are provided on the side walls of the chambers 1a and 1b of the fermentation treatment tank 1 so that water contained in the garbage A can be squeezed through the small holes 1d. It has become. The small hole 1d on the side wall may have a diameter of about 1 mmφ, and the water (untreated water) B squeezed through the small hole 1d is collected by the water collecting member 3 and introduced into the septic tank 4 through the conduit 3'from its bottom. Has become. The inflow to the bottom of the tank may utilize a head, and a pump (not shown) may be provided in the middle of the conduit 3 '.

【0013】前記醗酵処理槽1の各室1a、1bには、
生ごみ投入ホッパー5から投入された生ごみが導管6の
途中に設けた破砕機7にて破砕され、分岐機8にて振り
分けて分岐支管6a又は6bを経て収容されるようにな
っている。
In each of the chambers 1a and 1b of the fermentation treatment tank 1,
The garbage thrown from the garbage throwing hopper 5 is crushed by a crusher 7 provided in the middle of the conduit 6, sorted by a branching machine 8 and stored through a branch branch pipe 6a or 6b.

【0014】前記導管6の途中に設けた破砕機7は、ホ
ッパー5から投入された生ごみをほぼ1cm大に破砕で
きる回転式カッター7a、7bを対設してなる。該回転
式カッター7a、7bは、導管6外に備えた駆動機(図
示せず)にて駆動され、破砕したもの(生ごみ)を前記
分岐機8に向けて輸送できる機能を有している。本図面
上では輸送には落差が利用できるようになっているが、
配管が水平又は水平に近くなって落差が利用できない場
合もあるからである。
The crusher 7 provided in the middle of the conduit 6 is provided with a pair of rotary cutters 7a, 7b which can crush the garbage thrown from the hopper 5 to a size of about 1 cm. The rotary cutters 7a and 7b are driven by a driving machine (not shown) provided outside the conduit 6 and have a function of transporting crushed pieces (garbage) toward the branch machine 8. . Although the head can be used for transportation in this drawing,
This is because the pipe may be horizontal or nearly horizontal and the head cannot be used.

【0015】前記分岐機8は、前記導管6を流下してき
た生ごみの破砕物を前記醗酵処理槽1の一方の室1a
(又は1b)に振り分けるためのもので、可動羽根8′
を有している。この可動羽根8′の駆動は自動制御手段
であるか手動制御手段であるかは問わない。
The branching machine 8 treats the crushed food waste flowing down the conduit 6 in one chamber 1a of the fermentation treatment tank 1.
(Or 1b), the movable blade 8 '
have. It does not matter whether the movable blade 8'is driven by automatic control means or manual control means.

【0016】前記攪拌機2の駆動機2aは間欠作動する
ようになっている。具体的には10分間回転し、3時間
50分間停止するように調整されている。これは醗酵処
理槽の各室内に供給される空気が過剰になりすぎること
を避け、微生物の呼吸熱を奪わないようにするために有
効である。また、回転数は1分間に3回転程度のゆっく
りした回転でよい。
The drive unit 2a of the agitator 2 is adapted to operate intermittently. Specifically, it is adjusted to rotate for 10 minutes and stop for 3 hours and 50 minutes. This is effective in avoiding excessive supply of air into each chamber of the fermentation treatment tank and preventing deprivation of the respiratory heat of microorganisms. The rotation speed may be a slow rotation of about 3 rotations per minute.

【0017】前記浄化槽4の中層には濾過手段9が設け
られている。該濾過手段9は前記醗酵処理槽1の各室の
側壁に設けた小穴1dを通して生ごみより搾水されて集
水部材3にて集められ、槽底から流入してきた水分(未
処理水)Bが槽上に溢上する間に濾過処理され、槽上よ
り連通管10を経て消毒槽11へ濾過水Cとして流出さ
せることができるようになっている。該濾過水Cは消毒
槽11にて消毒後、最終処理水C′として流出管11a
を通して一般の下水道などへ排水される。
A filtering means 9 is provided in the middle layer of the septic tank 4. The filtering means 9 squeezes water from raw garbage through small holes 1d provided on the side walls of each chamber of the fermentation treatment tank 1 and collects it with the water collecting member 3, and the water (untreated water) B flowing from the bottom of the tank B Is filtered while it overflows onto the tank, and can be made to flow out as filtered water C from the tank to the disinfection tank 11 via the communication pipe 10. The filtered water C is sterilized in the sterilization tank 11, and then the outflow pipe 11a is used as the final treated water C '.
Through which it is drained to the general sewer.

【0018】前記濾過手段9は、醗酵処理槽1の側壁よ
り搾水された未処理水B中に含まれる浮遊物(固形分)
を濾過するためのもので、図3の如く、プラスチック繊
維層9aを、無数の穴9b′を有するプラスチック板9
bにて挟んでなる。この穴あきプラスチック板9bの穴
径は3cm位にし目詰まりがないようにしている。ま
た、プラスチック繊維層9aと穴あきプラスチック板9
bとは生ごみの性質を考慮して複数段に積層構成しても
よい。
The filtering means 9 is a suspended matter (solid content) contained in the untreated water B squeezed from the side wall of the fermentation treatment tank 1.
For filtering the plastic fiber layer 9a and the plastic plate 9 having numerous holes 9b 'as shown in FIG.
It is sandwiched by b. The hole diameter of the perforated plastic plate 9b is set to about 3 cm to prevent clogging. Also, the plastic fiber layer 9a and the perforated plastic plate 9
The b may be laminated in a plurality of stages in consideration of the property of food waste.

【0019】前記浄化槽4には、前記濾過水Cの一部を
取り込み口12aより取り込み、導管12bを介してエ
アーとともに槽底へ噴射させる噴射手段12が備えられ
ている。この噴射手段12による噴流は、未処理水Bに
満たされている浄化槽4の槽底に堆積する汚泥Dを奥側
(噴射手段12の噴射口12cに対向する壁側)に備え
た汚泥集積室13に集積されるようになっている。
The septic tank 4 is equipped with an injection means 12 for taking in a part of the filtered water C from the intake port 12a and injecting it into the tank bottom together with air through the conduit 12b. The jet flow by the jetting means 12 has a sludge accumulating chamber provided with sludge D accumulated on the bottom of the septic tank 4 filled with the untreated water B on the back side (the wall side facing the jet port 12c of the jetting means 12). It is supposed to be accumulated in 13.

【0020】前記噴射手段12はミクロポンプを利用し
て満足できる。即ち、ミクロポンプは前記濾過水Cをエ
ヤーとともにミクロ粒子状に、未処理水Bに満たされて
いる槽底にて噴射させるからマイナスイオンを生成さ
せ、前記汚泥集積室13に集積された汚泥D中に含まれ
る微生物を活性化(約5倍の増殖)させることが実験的
に確認されているからである。
The injection means 12 can be satisfied by using a micro pump. That is, the micropump injects the filtered water C together with the air into microparticles at the bottom of the tank filled with the untreated water B, so that negative ions are generated and the sludge D accumulated in the sludge accumulation chamber 13 is generated. This is because it has been experimentally confirmed that the microorganisms contained therein are activated (growth about 5 times).

【0021】前記浄化槽4には、更に、前記汚泥集積室
13に集積された汚泥Dを汲み上げて前記分岐機8へ戻
す返送手段14が備えられている。該返送手段14は汲
み上げポンプ(ギヤポンプ)14aの入力端14bを前
記汚泥集積室13に開口し、出力端14cを導管14d
を介して前記分岐機8の上流側に開口してなる。このギ
アポンプ14aを作動させるときは、前記汚泥集積室1
3の入口に設けた開閉シャッター13aを閉じる。これ
は汚泥集積室13に既に集積され、マイナスイオンの作
用により活性化されている微生物が含まれる汚泥Dを前
記分岐機8に返送するためである。
The septic tank 4 is further provided with a returning means 14 for pumping up the sludge D accumulated in the sludge accumulating chamber 13 and returning it to the branching machine 8. The returning means 14 opens an input end 14b of a pumping pump (gear pump) 14a into the sludge accumulation chamber 13 and an output end 14c of the conduit 14d.
It is opened to the upstream side of the branching machine 8 via the. When operating the gear pump 14a, the sludge accumulation chamber 1
The opening / closing shutter 13a provided at the entrance of 3 is closed. This is because the sludge D containing microorganisms already accumulated in the sludge accumulation chamber 13 and activated by the action of negative ions is returned to the branching machine 8.

【0022】次に、上記実施の態様にて示した本願装置
の作用について説明する。まず、醗酵処理槽1の各室1
a、1bに、菌床(例えば、米ヌカ10〜15Kgに前
述したOKZ菌をその体積比で1/1000程度混合し
たものを投入し、攪拌機2を廻して攪拌混合しておく。
Next, the operation of the apparatus of the present invention shown in the above embodiment will be described. First, each room 1 of the fermentation treatment tank 1
To a and 1b, a mixture of a fungal bed (for example, 10 to 15 kg of rice bran rice mixed with the above-mentioned OKZ bacteria at a volume ratio of about 1/1000 is introduced, and the agitator 2 is rotated to agitate and mix.

【0023】次いで、生ごみ投入ホッパー5より生ごみ
(例えば、野菜くず、魚のあら、大豆かす、パン屑、残
飯などの食品残渣)を投入する。該生ごみは導管6の途
中に設けた破砕機7にてほぼ1cm大に破砕され、分岐
機8を経て分岐支管6a(又は6b)から醗酵処理槽1
の一方の室1a(又は1b)に収容される。
Next, raw garbage (for example, food waste such as vegetable scraps, fish roe, soybean meal, bread scraps, and leftover food) is charged from the garbage disposal hopper 5. The raw garbage is crushed to a size of about 1 cm by a crusher 7 provided in the middle of the conduit 6, and then passed through the branching machine 8 to branch the branch pipe 6a (or 6b) to the fermentation treatment tank 1
It is housed in one chamber 1a (or 1b).

【0024】前記醗酵処理槽1の一方の室1a(又は1
b)には、破砕機7で生ごみを破砕したときに発生する
水分をも含めて収容される。しかして、前記菌床(OK
Z菌を含む米ヌカなど)は水分調整材としても機能し、
含水率50%〜60%になるように調整されるが、余剰
水分は醗酵処理槽1の各室1a(又は1b)の側壁に設
けた無数の小穴1dより搾水されて集水部材3を介して
浄化槽4の槽底に導かれる。
One chamber 1a (or 1) of the fermentation treatment tank 1
In b), the water contained when the food waste is crushed by the crusher 7 is also stored. Then, the bacterial bed (OK
Rice bran containing Z bacteria, etc.) also functions as a moisture regulator,
The water content is adjusted to 50% to 60%, but the excess water is squeezed from the numerous small holes 1d provided in the side wall of each chamber 1a (or 1b) of the fermentation treatment tank 1 to collect the water collecting member 3. It is guided to the bottom of the septic tank 4 via.

【0025】前記醗酵処理槽1の一つの室1a(又は1
b)内で前記攪拌機2により攪拌されることにより菌床
の温度は徐々に上がり、OKZ菌誘導期を経て生ごみの
温度を50°C前後で持続させる。この過程で必要に応
じて外底部に設けたヒーター1cを働かせることもあ
る。かくして、槽室内の含水率が減少するとともに、生
ごみの体積も大幅に減少する。また、上記過程で必要に
応じ、槽室内の水分量とpHを計測し、アルカリ化のた
めに炭酸カルシウムなどの調整剤を用いることもある。
One chamber 1a (or 1) of the fermentation treatment tank 1
By being stirred by the agitator 2 in b), the temperature of the fungus bed gradually rises, and the temperature of the food waste is maintained at about 50 ° C after the OKZ bacterium induction period. In this process, the heater 1c provided on the outer bottom may be operated as needed. Thus, the water content in the tank chamber is reduced and the volume of food waste is also significantly reduced. In addition, in the above process, the water content and pH in the tank chamber may be measured and a regulator such as calcium carbonate may be used for alkalization, if necessary.

【0026】一方、前記醗酵処理槽1の側壁より搾水さ
れ、集水部材3にて集められて導管3′を通して浄化槽
4の槽底からに流入した未処理水Bは、濾過手段9によ
り濾過処理され、その濾過水Cは連通管10より消毒槽
11へ流出させ、消毒して下水道へ排水される。そし
て、消毒槽11へ流出させる濾過水Cの一部は噴射手段
(ミクロポンプ)12により取り込まれ、前記浄化槽4
の槽底にエヤーとともに噴射される。
On the other hand, the untreated water B squeezed from the side wall of the fermentation treatment tank 1 and collected by the water collecting member 3 and flowing into the bottom of the purification tank 4 through the conduit 3'is filtered by the filtering means 9. The filtered water C that has been treated is discharged from the communication pipe 10 to the disinfection tank 11, is disinfected, and is drained to the sewer. Then, a part of the filtered water C flowing out to the disinfection tank 11 is taken in by the injection means (micro pump) 12, and the septic tank 4 is
It is sprayed with the air on the bottom of the tank.

【0027】このミクロポンプによりエヤーとともに噴
射されたミクロ粒子状の噴流中にはマイナスイオンが生
成されるため、前記槽底に連通している汚泥集積室13
に集積される汚泥D中の微生物は活性化される。従っ
て、ギヤポンプ13aにて汲み上げられて分岐機8から
再び前記処理槽1の処理が継続されている一方の室1a
(又は1b)に供給される。この汚泥Dの返送は、醗酵
処理槽1の槽室内部の温度が好気性菌(OKZ菌)の吸
収熱により上昇した結果、乾燥が進んだ生ごみへの水分
の補給としての意味もある。
Negative ions are generated in the jet of microparticulates jetted together with the air by the micropump, so that the sludge accumulation chamber 13 communicating with the bottom of the tank is formed.
The microorganisms in the sludge D accumulated in the are activated. Therefore, one chamber 1a is pumped up by the gear pump 13a and the processing of the processing tank 1 is continued from the branching machine 8 again.
(Or 1b). The return of the sludge D also has the meaning of supplying water to the dried garbage as a result of the temperature inside the tank of the fermentation treatment tank 1 rising due to the absorption heat of aerobic bacteria (OKZ bacteria).

【0028】かくして、汚泥Dの返送を受けた醗酵処理
槽1の一方の室1a(又は1b)では、堆肥化が進行し
ている生ごみ(破砕物)と、新たに追加された生ごみ
(破砕物)と、返送汚泥の三者が攪拌機2により攪拌混
合され、含水率が再び上昇するようになる。その時の余
剰水分は、再び、醗酵処理槽1の側壁より搾水されて浄
化槽4へと繰り返し導入される。
Thus, in the one chamber 1a (or 1b) of the fermentation treatment tank 1 which has received the return of the sludge D, the garbage (crushed material) which is being composted and the newly added garbage ( The crushed material) and the returned sludge are agitated and mixed by the agitator 2 and the water content again increases. The excess water at that time is again squeezed from the side wall of the fermentation treatment tank 1 and repeatedly introduced into the septic tank 4.

【0029】しかして、前記処理槽1の一方の室1a
(又は1b)での堆肥化物が一定量に達したならば、前
記分岐機8の可動羽根8′を切り替え、新たな生ごみの
追加分は他方の室1b(又は1a)に供給させる。そし
て他方の室1b(又は1a)において前述したところと
同様の醗酵処理(堆肥化)が進行する。この間には既に
堆肥化している先の室1a(又は1b)でも攪拌機2は
一定のタイミング(10分間作動、3時間50分間停
止)で活動しているから、給水と吸収とが繰り返され
(切り返しの役目)、完熟肥料化に移行する。
Thus, one chamber 1a of the processing tank 1
When the amount of compost in (or 1b) reaches a certain amount, the movable blades 8'of the branching machine 8 are switched, and the additional amount of new food waste is supplied to the other chamber 1b (or 1a). Then, in the other chamber 1b (or 1a), the same fermentation process (composting) as described above proceeds. During this time, even in the previous chamber 1a (or 1b) that has already been composted, the agitator 2 is operating at a constant timing (operating for 10 minutes, stopping for 3 hours and 50 minutes), so water supply and absorption are repeated (returning). Role of), shift to fully fertilized fertilizer.

【0030】このように、複数の室を持つ醗酵処理槽1
の一つの室で醗酵処理を行うと同時にもう一つの室では
完熟堆肥化処理が行われる。換言すれば、一つの室では
醗酵処理(肥料化)が済めば、続いて完熟肥料化に移行
し、完熟肥料化が済めばそれを取り出して空にし、再
度、醗酵処理(肥料化)に移行する。この作動の切り替
えは、前記分岐機8の可動羽根8′の切り替えのみで行
える。しかも、この間に発生する汚泥は、活性化され、
醗酵処理槽に返送(循環)されて有効に利用されるた
め、外部には一切排出されることはない。
Thus, the fermentation treatment tank 1 having a plurality of chambers
Fermentation treatment is performed in one room while ripe composting treatment is performed in the other room. In other words, if fermentation processing (fertilization) is completed in one room, then it shifts to fully fertilized fertilizer, and when fully fermented fertilizer is completed, it is taken out and emptied, and again fermented (fertilization) shifts. To do. This operation can be switched only by switching the movable blades 8'of the branching machine 8. Moreover, the sludge generated during this period is activated,
Since it is returned (circulated) to the fermentation treatment tank and used effectively, it is never discharged outside.

【0031】前述の如く、醗酵処理槽1の一つの室から
取り出された完熟肥料は、ふるい機に掛けられ選別され
て袋詰めされて出荷される。なお、本願装置では生ごみ
(破砕物)は、醗酵処理槽1の一室への投入後、2日目
でその中心内部温度は60〜70°C位となり、3日目
で75°C以上となり、pHも上昇するから、病原菌や
寄生虫又は雑草種子などは完全に死滅する。
As described above, the fully fertilized fertilizer taken out from one chamber of the fermentation treatment tank 1 is put on a sieving machine, sorted, packed in bags, and shipped. In the device of the present application, the raw garbage (crushed material) has a center internal temperature of about 60 to 70 ° C on the second day after being put into one chamber of the fermentation treatment tank 1, and 75 ° C or higher on the third day. Since the pH also rises, pathogenic bacteria, parasites, weed seeds, etc. are completely killed.

【0032】[0032]

【発明の効果】以上説明した如く、本発明に係る汚泥ゼ
ロの浄化槽と醗酵処理装置は、間欠作動する攪拌機を有
し、複数室を持つ醗酵処理槽と、濾過手段を有する浄化
槽とを備え、前記醗酵処理槽の各室は破砕機にて破砕さ
れた生ごみを分岐機を介して収容できるようになってお
り、前記浄化槽は前記醗酵処理槽の各室の側壁の穴を通
して搾水された水分を槽底から受け入れ、前記濾過手段
を通した濾過水を消毒槽へ流出させるようになってお
り、かつ、濾過水の一部を汚泥が堆積する槽底へエアー
とともに噴出させる噴射手段と、槽底に集積させた汚泥
を前記分岐機に戻す返送手段とを備えたことを特徴とし
ているから、処理槽の1つの室で生ごみの破砕物を醗酵
分解している間に、他の槽室では完熟堆肥化が進行で
き、しかも、処理槽の各室から排出された水分は浄化槽
にて濾過して消毒槽を介して排水するとともに、浄化槽
の底部に堆積する汚泥は活性化して醗酵処理に寄与する
ように返送するから一切外部に排出させることがないと
いう優れた効果を奏するものである。
As described above, the sludge-free septic tank and the fermentation treatment apparatus according to the present invention include an agitator that operates intermittently, a fermentation treatment tank having a plurality of chambers, and a septic tank having a filtering means. Each chamber of the fermentation treatment tank is configured to be able to accommodate raw garbage that has been crushed by a crusher through a branching machine, and the septic tank has been squeezed through holes in the side wall of each chamber of the fermentation treatment tank. Injecting means for receiving water from the bottom of the tank and discharging filtered water that has passed through the filtering means to the disinfection tank, and ejecting a part of the filtered water together with air to the tank bottom where sludge is accumulated, Since the sludge accumulated at the bottom of the tank is provided with a returning means for returning the sludge to the branching machine, while the crushed food waste is fermented and decomposed in one chamber of the processing tank, the other tank In the room, ripe composting can proceed and the treatment tank The water discharged from the chamber is filtered in the septic tank and drained through the disinfection tank, and the sludge accumulated at the bottom of the septic tank is activated and returned to contribute to the fermentation process, so it can be discharged to the outside. It has an excellent effect that it does not exist.

【0033】また、請求項2に記載の発明は、前記攪拌
機の間欠作動が、10分間作動し、3時間50分間停止
するものであることを特徴としているから、醗酵処理槽
内の空気が過剰になることを避け、微生物の呼吸熱を奪
わず、従って、堆肥化及び完熟堆肥化処理を効率的に行
えるという優れた効果を奏するものである。
Further, the invention according to claim 2 is characterized in that the intermittent operation of the stirrer operates for 10 minutes and stops for 3 hours and 50 minutes. Therefore, the air in the fermentation treatment tank is excessive. It has the excellent effect of avoiding the above-mentioned problem and not depriving the respiratory heat of microorganisms, and therefore can efficiently perform composting and ripe composting.

【0034】さらに、請求項3に記載の発明は、前記浄
化槽の濾過手段が、プラスチック繊維層を穴あきプラス
チック板で挟んでなることを特徴としているから、前記
浄化槽の濾過手段は、プラスチック繊維層と穴あきプラ
スチック板とを交互に積層してなることを特徴とし、生
ごみの固形分を除去した後に水分中に含まれる固形分を
も確実に補足でき、処理水をより綺麗にできるという優
れた効果を奏するものである。
Further, the invention according to claim 3 is characterized in that the filtering means of the septic tank comprises a plastic fiber layer sandwiched between perforated plastic plates. Therefore, the filtering means of the septic tank is a plastic fiber layer. It is characterized by alternately stacking perforated plastic plates and perforated plastic plates, it is possible to reliably capture the solid content contained in the water after removing the solid content of raw garbage, making it possible to make the treated water cleaner It has a great effect.

【0035】さらにまた、請求項4に記載の発明は、前
記浄化槽に備えた噴射手段が、ミクロポンプを利用して
なることを特徴としているから、浄化槽の底部に堆積す
る汚泥をマイナスイオン化でき、活性汚泥の形成に寄与
できるという優れた効果を奏するものである。
Furthermore, the invention as set forth in claim 4 is characterized in that the injection means provided in the septic tank uses a micro pump, so that the sludge accumulated at the bottom of the septic tank can be negatively ionized, It has an excellent effect that it can contribute to the formation of activated sludge.

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

【図1】本願装置の全体の構成を示す略示的断面図であ
る。
FIG. 1 is a schematic cross-sectional view showing the overall configuration of the device of the present application.

【図2】醗酵処理槽の側壁の拡大断面図である。FIG. 2 is an enlarged sectional view of a side wall of a fermentation treatment tank.

【図3】濾過手段の略示的断面図である。FIG. 3 is a schematic sectional view of a filtering means.

【符号の説明】[Explanation of symbols]

1 生ごみの処理槽 1a、1b 処理槽の分割された各室 1c 小穴 2 攪拌機 2a 駆動機 3 集水部材 3′ 導管 4 浄化槽 5 生ごみ投入ホッパー 6 導管 6a、6b 分岐支管 7 破砕機 7a、7b 回転式カッター 8 分岐機 8′ 可動羽根 9 濾過手段 9a プラスチック繊維層 9b 穴あきプラスチック板 9b′ 穴 10 連通管 11 消毒槽 11a 流出管 12 噴射手段 12a 取り込み口 12b 導管 12c 噴射口 13 汚泥集積室 13a 開閉シャッター 14 返送手段 14a 汲み上げポンプ(ギヤポンプ) 14b 入力端 14c 出力端 14d 導管 A 生ごみ(破砕物) B 生ごみより搾水された水分(未処理水) C 濾過水 C′ 最終処理水 D 汚泥 Treatment tank of 1 garbage 1a, 1b Each divided chamber of the processing tank 1c small hole 2 stirrer 2a drive 3 Water collecting member 3'conduit 4 septic tank 5 Garbage input hopper 6 conduits 6a, 6b Branch branch pipe 7 crusher 7a, 7b rotary cutter 8 branching machines 8'movable blade 9 Filtering means 9a plastic fiber layer 9b Perforated plastic plate 9b 'hole 10 communication tubes 11 disinfection tank 11a Outflow pipe 12 injection means 12a Intake port 12b conduit 12c injection port 13 Sludge accumulation chamber 13a Open / close shutter 14 Returning means 14a Pumping pump (gear pump) 14b Input end 14c Output end 14d conduit A garbage (crushed materials) B Water extracted from kitchen garbage (untreated water) C filtered water C'Final treated water D sludge

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 11/02 B01D 23/10 C Fターム(参考) 4D004 AA03 BA04 CA04 CA19 CA35 CB05 CB12 CB28 CB32 CB42 CC07 CC12 DA09 DA13 4D019 AA03 BA13 BB13 CB04 4D028 AB00 AC00 BC03 BC17 BC24 BD12 BD17 4D041 AA21 BB06 BB10 BB21 CB04 4D059 AA07 BA22 BA28 BA56 BE02 BE13 BE34 BE35 BE51 BF14 BF15 BJ03 BJ14 CC01 DA03 DA38 EA01 EA05 EB16 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) C02F 11/02 B01D 23/10 CF term (reference) 4D004 AA03 BA04 CA04 CA19 CA35 CB05 CB12 CB28 CB32 CB42 CC07 CC12 DA09 DA13 4D019 AA03 BA13 BB13 CB04 4D028 AB00 AC00 BC03 BC17 BC24 BD12 BD17 4D041 AA21 BB06 BB10 BB21 CB04 4D059 AA07 BA22 BA28 BA56 BE02 BE13 BE34 BE35 BE51 BF14 BF15 BJ03 BJ14 CC16 DA03 DA38 DA38 DA38

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 間欠作動する攪拌機を有し複数室を持つ
醗酵処理槽と、濾過手段を有する浄化槽とを備え、前記
醗酵処理槽の各室は破砕機にて破砕された生ごみを分岐
機を介して収容できるようになっており、前記浄化槽は
前記醗酵処理槽の各室の側壁の穴を通して生ごみより搾
水された水分を槽底から受け入れ、前記濾過手段を通し
た濾過水を消毒槽へ流出させるようになっており、か
つ、濾過水の一部を汚泥が堆積する槽底へエアーととも
に噴出させる噴射手段と、槽底に集積させた汚泥を前記
分岐機に戻す返送手段とを備えたことを特徴とする汚泥
ゼロの浄化槽と醗酵処理装置。
1. A fermentation treatment tank having an agitator that operates intermittently and having a plurality of chambers, and a septic tank having a filtration means, each chamber of the fermentation treatment tank being a branching machine for crushing food waste crushed by a crusher. The septic tank receives the water squeezed from raw garbage from the tank bottom through the holes in the side wall of each chamber of the fermentation treatment tank, and disinfects the filtered water that has passed through the filtering means. An ejecting means for ejecting a part of the filtered water together with air to the tank bottom where sludge is accumulated, and a returning means for returning the sludge accumulated in the tank bottom to the branching machine. A sludge-free septic tank and fermentation treatment device, which are equipped with
【請求項2】 前記攪拌機の間欠作動が、10分間作動
し、3時間50分間停止するものであることを特徴とす
る請求項1に記載の汚泥ゼロの浄化槽と醗酵処理装置。
2. The sludge-free septic tank and the fermentation treatment apparatus according to claim 1, wherein the intermittent operation of the stirrer operates for 10 minutes and stops for 3 hours and 50 minutes.
【請求項3】 前記浄化槽の濾過手段が、プラスチック
繊維層を穴あきプラスチック板で挟んでなることを特徴
とする請求項1又は2に記載の汚泥ゼロの浄化槽と醗酵
処理装置。
3. The sludge-free septic tank and the fermentation treatment apparatus according to claim 1, wherein the filtration means of the septic tank comprises a plastic fiber layer sandwiched between perforated plastic plates.
【請求項4】 前記噴射手段が、ミクロポンプを利用し
てなることを特徴とする請求項1〜3のうちの1に記載
の汚泥ゼロの浄化槽と醗酵処理装置。
4. The sludge-free septic tank and the fermentation treatment apparatus according to claim 1, wherein the injection means uses a micropump.
JP2001331613A 2001-10-29 2001-10-29 Zero sludge septic tank and fermentation treatment apparatus Pending JP2003126824A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001331613A JP2003126824A (en) 2001-10-29 2001-10-29 Zero sludge septic tank and fermentation treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001331613A JP2003126824A (en) 2001-10-29 2001-10-29 Zero sludge septic tank and fermentation treatment apparatus

Publications (1)

Publication Number Publication Date
JP2003126824A true JP2003126824A (en) 2003-05-07

Family

ID=19147148

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001331613A Pending JP2003126824A (en) 2001-10-29 2001-10-29 Zero sludge septic tank and fermentation treatment apparatus

Country Status (1)

Country Link
JP (1) JP2003126824A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009091523A (en) * 2007-10-12 2009-04-30 Three S Kk Manufacturing method of soil activator
KR100959901B1 (en) 2007-12-10 2010-05-26 신세기 시스템 (주) Food waste handler
KR100966158B1 (en) 2010-04-29 2010-06-25 강창수 Process apparatus of organic waste
CN103372564A (en) * 2013-08-12 2013-10-30 张共敏 Enclosed horizontal aerobic fermentation cylinder with double-layer cylinders
CN104174627A (en) * 2013-05-24 2014-12-03 山东金王电器有限公司 Food waste harmless decomposition recovery reutilization device
CN110252770A (en) * 2019-06-10 2019-09-20 诸暨市众创机械设备厂 A waste feather recycling equipment based on the principle of biological fermentation
CN110420968A (en) * 2019-08-02 2019-11-08 窦志刚 One kind handling reclaimer for medical cotton

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009091523A (en) * 2007-10-12 2009-04-30 Three S Kk Manufacturing method of soil activator
KR100959901B1 (en) 2007-12-10 2010-05-26 신세기 시스템 (주) Food waste handler
KR100966158B1 (en) 2010-04-29 2010-06-25 강창수 Process apparatus of organic waste
CN104174627A (en) * 2013-05-24 2014-12-03 山东金王电器有限公司 Food waste harmless decomposition recovery reutilization device
CN103372564A (en) * 2013-08-12 2013-10-30 张共敏 Enclosed horizontal aerobic fermentation cylinder with double-layer cylinders
CN110252770A (en) * 2019-06-10 2019-09-20 诸暨市众创机械设备厂 A waste feather recycling equipment based on the principle of biological fermentation
CN110420968A (en) * 2019-08-02 2019-11-08 窦志刚 One kind handling reclaimer for medical cotton

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