JP2004154712A - Method of disposing garbage - Google Patents

Method of disposing garbage Download PDF

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Publication number
JP2004154712A
JP2004154712A JP2002324208A JP2002324208A JP2004154712A JP 2004154712 A JP2004154712 A JP 2004154712A JP 2002324208 A JP2002324208 A JP 2002324208A JP 2002324208 A JP2002324208 A JP 2002324208A JP 2004154712 A JP2004154712 A JP 2004154712A
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Japan
Prior art keywords
garbage
wastewater
water
sludge
tank
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JP2002324208A
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Japanese (ja)
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JP3720015B2 (en
Inventor
Toshihiro Takahashi
利洋 高橋
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Aoki Electric Industrial Co Ltd
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Aoki Electric Industrial Co Ltd
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    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • 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
    • 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
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

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  • Processing Of Solid Wastes (AREA)
  • Activated Sludge Processes (AREA)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method of promptly deodorizing garbage. <P>SOLUTION: The garbage 41 is crushed together with a waste water 1 containing a host of soil bacteria obtained in a step 10 of purifying the organic waste water 1 and then separated into a liquid portion 46 and a solid portion 47. The liquid portion 46 is subjected to deodorization in the step 10 of purifying the organic waste water 1. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
この発明は、食品加工工場等において採用するのに好適な生ごみの処理方法に関する。
【0002】
【従来の技術】
従来、食品加工工場等で大量に発生する生ごみの悪臭は、日常の生活環境を悪くするものの一因としてよく知られている。この発明の特許出願人と同一の出願人に係る特許第3217654号公報(特許文献1)には、生ごみによる悪臭を解消することができる生ごみの処理方法が開示されている。この処理方法では、粉砕し液状化した後の生ごみを汚泥と混合し攪拌して生ごみのBOD濃度を低下させてから固液分離する。その分離によって得られた液状部分は、前記汚泥を使用する排水処理工程へと導き、その排水処理工程において土壌細菌群とその代謝産物とを使用して無臭化する。
【0003】
【特許文献1】
特許第3217654号公報
【0004】
【発明が解決しようとする課題】
前記公知の処理方法では、生ごみに水道水を加えて粉砕し液状化する。得られた液状化物は、これを高濃度反応工程へ送り、細菌活動が活発な汚泥と混合して土壌細菌群とその代謝産物との作用下に置く。しかる後に、液状化物を一次処理水と固体状の汚泥(脱水ケーキ)とに分離する。一次処理水は、有機性排水を浄化するシステムへ導いて土壌細菌とその代謝産物との作用で無臭化し、二次処理水としてシステムの外へ出す。この方法は、生ごみをトン単位で処理するのに適したバッチシステムであるから、そのシステムを経済的に効率よく運用しようとすると、高濃度反応工程の規模に見合う程度にまで生ごみが溜まるのを待たなければならない。その間に生ごみから悪臭が発生することは避けられない。また、そのような量の生ごみを液状化するには多量の水道水が必要となる。さらにはまた、高濃度反応工程では大きな反応容器が使用されるから、その反応容器のために広いスペースが必要となる。
【0005】
この発明は、生ごみを無臭化処理する前記公知の方法の改良に係り、生ごみが発生したらそれを速やかに無臭化できるようにすることや水道水を使わなくても済むようにすること、生ごみを溜めるためのスペースを減らすことができるようにすること等を課題にしている。
【0006】
【課題を解決するための手段】
前記課題解決のためにこの発明が対象とするのは、生ごみを粉砕処理して生じる固状部分と液状部分とのうちの前記液状部分を土壌細菌の作用下に有機性排水の浄化を行うシステムへ導いて前記液状部分を無臭化することが可能な生ごみの処理方法である。
【0007】
かかる処理方法において、この発明が特徴とするところは、次のとおりである。
前記工程は、前記工程における前記排水の流路から前記排水の一部を取り出して腐植物質と接触させた後に前記排水の一部を前記流路ヘ返送する前記土壌細菌に対する活性化工程と、前記流路において前記排水と前記土壌細菌との反応を進めて前記排水を浄化された処理水と汚泥とに分離濃縮する浄化工程と、前記浄化工程における前記排水の一部と前記汚泥とを前記生ごみに加えて前記生ごみを粉砕処理し、しかる後に前記生ごみを脱水処理して前記固状部分と前記液状部分とに分離し、前記液状部分を前記浄化工程よりも手前の前記流路および前記浄化工程のうちの初期の前記流路のいずれかに導く生ごみ処理工程とを備えている。
【0008】
この発明には、次のような好ましい実施態様がある。
(1)前記生ごみに前記汚泥を含む排水の他に、前記処理水を加えて前記生ごみを粉砕処理する。
(2)前記生ごみを脱水処理して前記固状部分の含水率を75〜40重量%にする。
(3)前記固状部分を醗酵槽へ送り、前記汚泥を含む排水および前記処理水のいずれかを前記固状部分に加えて醗酵させる。
(4)醗酵させた前記固状部分から堆肥を得る。
【0009】
【発明の実施の形態】
添付の図面を参照してこの発明に係る生ごみの処理方法の詳細を説明すると、以下のとおりである。
【0010】
図1は、この発明に係る排水浄化工程10と生ごみ処理工程40とを含む生ごみ処理のフローチャートである。食品加工工場等の工場Pからは、有機性排水1と生ごみ41とが発生する。排水1は、図の左方から右方ヘ延びる浄化工程10の排水流路にしたがって調整槽2へ進み、さらに反応槽3を通って分離濃縮槽4へと進む。分離濃縮槽4では、浄化されるとともに無臭化処理された排水1が処理水6となって浄化工程10の外へ出る一方、排水1に含まれる固形分は濃縮されて汚泥となる。分離濃縮槽4における排水1の一部は、必要に応じて汚泥とともに調整槽2や反応槽3へ返送することができる。浄化工程10には、分離濃縮槽4における排水1の一部である第1中間処理水12を、必要ならば汚泥とともに、培養槽7へ導く活性化処理工程30が付随している。培養槽7には、これに並置された腐植物質供給装置8から腐植物質を微細粒子9(図2参照)の形態で含む第1混合水31が供給される。培養槽7では、第1中間処理水12が活発な増殖力を有する土壌細菌を多量に含む第2混合水32となり、この第2混合水32が調整槽2および/または反応槽3へ送られる。第2混合水32は、活発な土壌細菌が多量に生息している汚泥を含むことがある。調整槽2は前処理槽と呼ばれることがあり、反応槽3は処理槽とかばっ気槽とか呼ばれ、分離濃縮槽4は汚泥が沈殿するから沈殿槽と呼ばれることがある。これら各槽2,3,4には、当該技術分野において周知慣用のものを使用することができる。
【0011】
図2は、図1における培養槽7と供給装置8との断面図である。培養槽7には、分離濃縮槽4からの第1中間処理水12と供給装置8からの第1混合水31とが供給される。培養槽7は、散気管14と第1送水管16とを有し、散気管14からの給気による好気的条件下で第1中間処理水12と第1混合水31とを混合する。
【0012】
供給装置8は、給水装置20、ホッパー22、モータ23によって駆動される攪拌機24および培養槽7へつながる第2送水管26とを有し、第2送水管26には送水ポンプ27が取り付けられている。給水装置20は給水槽等であって、ここからは、培養槽7の第1中間処理水12と混合して土壌細菌を増殖させるのに適した混合用の水21が連続的または間欠的に供給される。混合用の水21の一例には、図1の処理水6がある。ホッパー22には、腐植物質と無機物質を主成分とする微細粒子9が投入されており、フィーダ25を介して連続的または間欠的にこの微細粒子9が供給装置8へ送られる。水21と微細粒子9とは攪拌機24によって混合されて第1混合水31となり、ポンプ27によって培養槽7へ送られる。
【0013】
培養槽7では、散気管14の作用により第1混合水31と第1中間処理水12とが微細粒子9とともに好気的条件で混合攪拌されて第2混合水32となる。第2混合水32は、かかる攪拌の下にその中に含まれる土壌細菌の増殖と代謝機能の活性化とが促進され、第2混合水32が排水1に混合されたときの排水1に対する浄化能力と無臭化能力とが向上する。この第2混合水32は、第1送水管16を通り調整槽2および/または反応槽3に送られる。
【0014】
かような供給装置8において、微細粒子9には、腐植物質と無機物質との混合物からなり、好ましくは50メッシュ以上の粒度を有するものが使用される。無機物質には、好ましくは鉱物粒子、より好ましくは珪酸塩を含む鉱物粒子、さらに好ましくは軽石、安山岩、流紋岩、火山ガラス、ゼオライト、グリーンタフ、珪藻土、粘土鉱物等の珪酸塩を含む鉱物粒子が使用される。微細粒子9において、無機物質は50〜90重量%を占め、腐食物質を主成分とする有機物が残余の部分を占めている。微細粒子9の使用量は、第1混合水31において0.05〜3重量%の範囲にあることが好ましい。また、第1混合水31は、培養槽7で処理する1日当たりの第1中間処理水12の量の0.5/1000〜5/1000程度をポンプ27によって連続的または間欠的に第1中間処理水12に添加することが好ましい。このように第1混合水31の使用量は、第1中間処理水12の量に比して非常に少ないから、供給装置8の内容積は、通常であれば培養槽7の内容積の0.5〜1%で足りる。ただし、図2では供給装置8の構造を明示するために、供給装置8が培養槽7と同程度の大きさで示されている。また、培養槽7は、従来技術のうように腐植物質のペレットを充填するための容器を内蔵する必要がないから、内容積の小さいもので足りる。
【0015】
再び図1において、生ごみ41は、生ごみ処理工程40へ入り、分離濃縮槽4から送られる第2中間処理水33と必要に応じて加えられる処理水6とともに、粉砕機42において連続的または間欠的に処理されて粉砕物43となる。第2中間処理水33は排水1と汚泥とを含むものであり、このものと処理水6とには、排水1を無臭化できる土壌細菌が多量に含まれているから、生ごみ41は、それが粉砕される過程に入ると同時に無臭化のための作用を受けるようになる。その後に得られる粉砕物43は脱水機44において固液分離されて、液状部分46と含水率が75〜40重量%の固状部分47とに分離する。液状部分46は、浄化工程10における調整槽2へと進んで排水1と合流し、排水1とともに浄化され無臭化される。
【0016】
固状部分47は、それを醗酵させるのに適当な含水率を有している。必要に応じてこれを醗酵槽48において醗酵させると、堆肥として使用することができる。醗酵槽48には第2中間処理水33や処理水6を供給可能であり、これら第2中間処理水33や処理水6を醗酵の促進に利用したり、醗酵槽48の内部に噴霧して醗酵槽48で発生する悪臭の防止に利用したりすることができる。特に第2中間処理水33は、それに含まれる汚泥に増殖力が旺盛な多数の土壌細菌を有するから、利用価値が高い。
【0017】
この発明では、液状部分46を浄化工程10における初期の流路である調整槽2へ導く図1の例の他に、液状部分46を調整槽2と反応槽3との間の流路へ導いたり、浄化工程10よりも手前の流路ヘ導いたりすることもできる。培養槽7へ腐植物質を供給するには、供給装置8を使用する他に、公知ないし周知の手段を使用することができる。例えば培養槽7の内部に腐植物質が含まれるペレットを充填したかご等の容器を設置し、第1中間処理水12がその容器を通過するときにペレットと接触するようにしてもよい。そのペレットが消耗したならば、新しいペレットを容器に補充する。
【0018】
この発明に係る生ごみの処理方法では、例えば小型の粉砕機42と脱水機44とを使用して、生ごみがキログラム単位で発生するたびにこれを粉砕し脱水するようにすれば、粉砕機42や脱水機44を設置するのに広いスペースを必要としない。このように処理される生ごみ41は、それが発生したならば直ちに見かけの体積が著しく小さい固状部分となる。例えば、粉砕の前後で生ごみの体積は1/3程度になり得るから、生ごみ41を溜めておくためのスペースが殆ど不要になる。生ごみ41は、粉砕される工程において無臭化能力を有する土壌細菌と接触するから、この発明によれば生ごみ発生の初期の段階から悪臭の防止が可能になる。
【0019】
【発明の効果】
この発明に係る生ごみの処理方法によれば、生ごみが発生しても、これをすぐに土壌細菌と接触させながら粉砕し脱水処理することができるから、生ごみによる悪臭の発生がなくなる。生ごみは、小型の粉砕機と脱水機とで処理することが可能で、生ごみ処理のために広いスペースを必要とすることがない。
【図面の簡単な説明】
【図1】生ごみ処理のフローチャート。
【図2】培養槽と供給槽との断面図。
【符号の説明】
1 排水
6 処理水
10 浄化工程
30 活性化工程
40 生ごみ処理工程
41 生ごみ
46 液状部分
47 固状部分
48 醗酵槽
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method for treating garbage suitable for use in food processing factories and the like.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, the bad smell of garbage generated in large quantities in food processing factories and the like is well known as a factor that deteriorates daily living environment. Japanese Patent No. 3217654 (Patent Document 1) of the same applicant as the patent applicant of the present invention discloses a method of treating garbage that can eliminate malodor caused by garbage. In this treatment method, the garbage that has been pulverized and liquefied is mixed with sludge and stirred to reduce the BOD concentration of the garbage and then solid-liquid separated. The liquid portion obtained by the separation is led to a wastewater treatment step using the sludge, and is deodorized using the soil bacteria group and its metabolite in the wastewater treatment step.
[0003]
[Patent Document 1]
Japanese Patent No. 3217654 [0004]
[Problems to be solved by the invention]
In the above-mentioned known treatment method, tap water is added to garbage to pulverize and liquefy. The resulting liquefied product is sent to a high-concentration reaction step, where it is mixed with sludge having high bacterial activity and placed under the action of soil bacteria and its metabolites. Thereafter, the liquefied material is separated into primary treated water and solid sludge (dewatered cake). The primary treated water is led to a system for purifying organic wastewater, deodorized by the action of soil bacteria and its metabolites, and is discharged out of the system as secondary treated water. Since this method is a batch system suitable for processing garbage in ton units, if the system is to be operated economically and efficiently, the garbage will accumulate to an extent commensurate with the scale of the high-concentration reaction process. I have to wait for During that time, it is inevitable that odors will be generated from the garbage. In addition, a large amount of tap water is required to liquefy such an amount of garbage. Furthermore, since a large reaction vessel is used in the high concentration reaction step, a large space is required for the reaction vessel.
[0005]
The present invention relates to an improvement of the known method for deodorizing food waste, and to make it possible to quickly deodorize food waste when it is generated or to eliminate the need for tap water, The task is to reduce the space for storing garbage.
[0006]
[Means for Solving the Problems]
An object of the present invention for solving the problem is to purify organic wastewater under the action of soil bacteria on the liquid portion of the solid portion and the liquid portion generated by crushing garbage. This is a method for treating garbage that can be led to a system to deodorize the liquid portion.
[0007]
In this processing method, the features of the present invention are as follows.
The step is an activation step for the soil bacteria, in which a part of the drainage is taken out from the drainage channel in the step and brought into contact with humic substances, and then a part of the drainage is returned to the channel. A purification step of advancing a reaction between the wastewater and the soil bacteria in the flow path to separate and concentrate the wastewater into purified treated water and sludge; and forming a part of the wastewater and the sludge in the purification step into the raw water. In addition to the garbage, the garbage is crushed, and then the garbage is dewatered and separated into the solid portion and the liquid portion, and the liquid portion and the flow path before the purification step. A garbage treatment step of leading to any of the flow paths in the initial stage of the purification step.
[0008]
The present invention has the following preferred embodiments.
(1) In addition to the wastewater containing the sludge to the garbage, the treated water is added to crush the garbage.
(2) The garbage is dewatered so that the solid portion has a moisture content of 75 to 40% by weight.
(3) The solid portion is sent to a fermenter, and either the wastewater containing the sludge or the treated water is added to the solid portion for fermentation.
(4) A compost is obtained from the fermented solid part.
[0009]
BEST MODE FOR CARRYING OUT THE INVENTION
The details of the method for treating garbage according to the present invention will be described below with reference to the accompanying drawings.
[0010]
FIG. 1 is a flowchart of the garbage processing including the wastewater purification step 10 and the garbage processing step 40 according to the present invention. From a factory P such as a food processing factory, organic wastewater 1 and garbage 41 are generated. The wastewater 1 proceeds to the regulating tank 2 according to the drainage flow path of the purification step 10 extending from the left to the right in the drawing, and further proceeds to the separation / concentration tank 4 through the reaction tank 3. In the separation / concentration tank 4, the wastewater 1 that has been purified and deodorized has become treated water 6 and goes out of the purification step 10, while the solids contained in the wastewater 1 are concentrated to sludge. Part of the wastewater 1 in the separation / concentration tank 4 can be returned to the adjustment tank 2 or the reaction tank 3 together with sludge as required. The purification step 10 is accompanied by an activation treatment step 30 in which the first intermediate treatment water 12, which is a part of the wastewater 1 in the separation / concentration tank 4, is guided to the culture tank 7 together with sludge if necessary. A first mixed water 31 containing humic substances in the form of fine particles 9 (see FIG. 2) is supplied to the culture tank 7 from a humic substance supply device 8 juxtaposed thereto. In the culture tank 7, the first intermediate treated water 12 becomes the second mixed water 32 containing a large amount of soil bacteria having an active growth ability, and the second mixed water 32 is sent to the adjusting tank 2 and / or the reaction tank 3. . The second mixed water 32 may include sludge in which a large amount of active soil bacteria inhabit. The adjusting tank 2 may be called a pretreatment tank, the reaction tank 3 may be called a processing tank or an aeration tank, and the separation / concentration tank 4 may be called a sedimentation tank because sludge precipitates. For each of the tanks 2, 3, and 4, those well-known and used in the art can be used.
[0011]
FIG. 2 is a sectional view of the culture tank 7 and the supply device 8 in FIG. The first intermediate treated water 12 from the separation / concentration tank 4 and the first mixed water 31 from the supply device 8 are supplied to the culture tank 7. The culture tank 7 has an air diffuser 14 and a first water pipe 16, and mixes the first intermediate treatment water 12 and the first mixed water 31 under aerobic conditions by air supply from the air diffuser 14.
[0012]
The supply device 8 includes a water supply device 20, a hopper 22, a stirrer 24 driven by a motor 23, and a second water supply pipe 26 connected to the culture tank 7, and a water supply pump 27 is attached to the second water supply pipe 26. I have. The water supply device 20 is a water supply tank or the like, from which water for mixing 21 suitable for mixing with the first intermediate treatment water 12 in the culture tank 7 and growing soil bacteria is continuously or intermittently supplied. Supplied. One example of the mixing water 21 is the treated water 6 in FIG. The hopper 22 is loaded with fine particles 9 mainly composed of humic substances and inorganic substances, and the fine particles 9 are continuously or intermittently sent to the supply device 8 via a feeder 25. The water 21 and the fine particles 9 are mixed by the stirrer 24 to become the first mixed water 31 and sent to the culture tank 7 by the pump 27.
[0013]
In the culture tank 7, the first mixed water 31 and the first intermediate treatment water 12 are mixed and agitated under aerobic conditions together with the fine particles 9 by the action of the air diffuser 14 to form the second mixed water 32. The second mixed water 32 promotes the growth of soil bacteria contained in the second mixed water 32 and the activation of the metabolic function under such stirring, and purifies the wastewater 1 when the second mixed water 32 is mixed with the wastewater 1. The ability and the ability to deodorize are improved. The second mixed water 32 is sent to the adjustment tank 2 and / or the reaction tank 3 through the first water pipe 16.
[0014]
In such a supply device 8, as the fine particles 9, those made of a mixture of humic substances and inorganic substances, preferably having a particle size of 50 mesh or more are used. Inorganic substances, preferably mineral particles, more preferably silicate-containing mineral particles, even more preferably pumice, andesite, rhyolite, volcanic glass, zeolite, green tough, diatomaceous earth, minerals containing silicates such as clay minerals Particles are used. In the fine particles 9, the inorganic substance accounts for 50 to 90% by weight, and the organic substance mainly composed of the corrosive substance occupies the remaining part. The use amount of the fine particles 9 is preferably in the range of 0.05 to 3% by weight in the first mixed water 31. In addition, the first mixed water 31 is continuously or intermittently pumped by the pump 27 at about 0.5 / 1000 to 5/1000 of the amount of the first intermediate treated water 12 to be treated in the culture tank 7 per day. It is preferable to add to the treated water 12. As described above, the amount of the first mixed water 31 used is very small as compared with the amount of the first intermediate treated water 12, so that the internal volume of the supply device 8 is normally 0% of the internal volume of the culture tank 7. 0.5 to 1% is sufficient. However, in FIG. 2, in order to clearly show the structure of the supply device 8, the supply device 8 is shown to be approximately the same size as the culture tank 7. Further, the culturing tank 7 does not need to incorporate a container for filling humic substance pellets as in the prior art, so that a small internal volume is sufficient.
[0015]
Referring again to FIG. 1, the garbage 41 enters a garbage processing step 40 and is continuously or in a crusher 42 together with the second intermediate treated water 33 sent from the separation / concentration tank 4 and the treated water 6 added as necessary. The pulverized material 43 is intermittently processed. The second intermediate treated water 33 contains wastewater 1 and sludge, and the wastewater 1 and treated water 6 contain a large amount of soil bacteria capable of deodorizing the wastewater 1. As soon as it enters the pulverizing process, it becomes deodorized. The pulverized material 43 obtained thereafter is subjected to solid-liquid separation in a dehydrator 44 to be separated into a liquid portion 46 and a solid portion 47 having a water content of 75 to 40% by weight. The liquid portion 46 proceeds to the adjusting tank 2 in the purification step 10 and merges with the waste water 1, and is purified together with the waste water 1 to be deodorized.
[0016]
The solid portion 47 has a suitable moisture content for fermenting it. If this is fermented in the fermenter 48 as needed, it can be used as compost. The second intermediate treated water 33 and the treated water 6 can be supplied to the fermentation tank 48. The second intermediate treated water 33 and the treated water 6 can be used for promoting fermentation or sprayed into the fermentation tank 48. It can be used for preventing bad smell generated in the fermenter 48. In particular, the second intermediate treatment water 33 has a high utility value because it has a large number of soil bacteria having a strong proliferation ability in the sludge contained therein.
[0017]
In the present invention, in addition to the example of FIG. 1 in which the liquid portion 46 is guided to the adjustment tank 2 which is an initial flow path in the purification step 10, the liquid portion 46 is guided to a flow path between the adjustment tank 2 and the reaction tank 3. Alternatively, it can be guided to a flow path before the purification step 10. In order to supply the humic substances to the culture tank 7, a known or well-known means can be used in addition to the use of the supply device 8. For example, a container such as a basket filled with pellets containing humic substances may be provided inside the culture tank 7 so that the first intermediate treated water 12 comes into contact with the pellets when passing through the container. When the pellets are exhausted, refill the container with new pellets.
[0018]
In the method for treating garbage according to the present invention, for example, a small crusher 42 and a dehydrator 44 are used to crush and dewater garbage every time it is generated in kilograms. A large space is not required for installing the 42 and the dehydrator 44. The garbage 41 treated in this way immediately becomes a solid part with a very small apparent volume when it is generated. For example, the volume of the garbage can be reduced to about 1/3 before and after the pulverization, so that the space for storing the garbage 41 becomes almost unnecessary. Since the garbage 41 comes into contact with soil bacteria having a deodorizing ability in the pulverizing step, according to the present invention, it is possible to prevent malodor from the initial stage of garbage generation.
[0019]
【The invention's effect】
According to the method for treating garbage according to the present invention, even if garbage is generated, the garbage can be immediately crushed and dewatered while being brought into contact with soil bacteria, thereby eliminating the generation of malodor due to the garbage. Garbage can be processed by a small crusher and a dehydrator, and does not require a large space for processing the garbage.
[Brief description of the drawings]
FIG. 1 is a flowchart of garbage processing.
FIG. 2 is a sectional view of a culture tank and a supply tank.
[Explanation of symbols]
Reference Signs List 1 wastewater 6 treated water 10 purification step 30 activation step 40 garbage processing step 41 garbage 46 liquid part 47 solid part 48 fermenter

Claims (5)

生ごみを粉砕処理して生じる固状部分と液状部分とのうちの前記液状部分を土壌細菌の作用下に有機性排水の浄化を行う工程へ導いて前記液状部分を無臭化することが可能な生ごみの処理方法において、
前記工程が、前記工程における前記排水の流路から前記排水の一部を取り出して腐植物質と接触させた後に前記排水の一部を前記流路ヘ返送する前記土壌細菌に対する活性化工程と、前記流路において前記排水と前記土壌細菌との反応を進めて前記排水を浄化された処理水と汚泥とに分離濃縮する浄化工程と、前記浄化工程における前記排水の一部と前記汚泥とを前記生ごみに加えて前記生ごみを粉砕処理し、しかる後に前記生ごみを脱水処理して前記固状部分と前記液状部分とに分離し、前記液状部分を前記浄化工程よりも手前の前記流路および前記浄化工程のうちの初期の前記流路のいずれかに導く生ごみ処理工程とを備えていることを特徴とする前記処理方法。
It is possible to deodorize the liquid portion by guiding the liquid portion of the solid portion and the liquid portion generated by crushing the garbage to a step of purifying organic wastewater under the action of soil bacteria. In the method of processing garbage,
The step, an activation step for the soil bacteria, wherein a part of the drainage is taken out from the drainage channel in the step and brought into contact with humic substances, and then a part of the drainage is returned to the channel. A purification step of advancing a reaction between the wastewater and the soil bacteria in the flow path to separate and concentrate the wastewater into purified treated water and sludge; and forming a part of the wastewater and the sludge in the purification step into the raw water. In addition to the garbage, the garbage is crushed, and then the garbage is dewatered and separated into the solid portion and the liquid portion, and the liquid portion and the flow path before the purification step. A garbage treatment step of introducing the garbage to any of the initial flow paths in the purification step.
前記生ごみに前記汚泥を含む排水の他に、前記処理水を加えて前記生ごみを粉砕処理する請求項1記載の処理方法。The treatment method according to claim 1, wherein the garbage is pulverized by adding the treated water in addition to the wastewater containing the sludge to the garbage. 前記生ごみを脱水処理して前記固状部分の含水率を75〜40重量%にする請求項1または2記載の処理方法。The processing method according to claim 1, wherein the garbage is dewatered to make the water content of the solid portion 75 to 40% by weight. 前記固状部分を醗酵槽へ送り、前記汚泥を含む排水および前記処理水のいずれかを前記固状部分に加えて醗酵させる請求項1記載の処理方法。The treatment method according to claim 1, wherein the solid portion is sent to a fermenter, and either the wastewater containing the sludge or the treated water is added to the solid portion for fermentation. 醗酵させた前記固状部分から堆肥を得る請求項4記載の処理方法。The processing method according to claim 4, wherein compost is obtained from the fermented solid portion.
JP2002324208A 2002-11-07 2002-11-07 Garbage disposal method Expired - Fee Related JP3720015B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010088302A (en) * 2007-11-14 2010-04-22 Shinjiro Kanazawa Manufacturing method of odor-assimilating (decomposing) bacteria and compost, and utilization method thereof
JP4482717B1 (en) * 2009-07-03 2010-06-16 龍男 白方 Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same
KR101519389B1 (en) * 2008-07-28 2015-05-18 서희동 Method for treating organic-wastes

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010088302A (en) * 2007-11-14 2010-04-22 Shinjiro Kanazawa Manufacturing method of odor-assimilating (decomposing) bacteria and compost, and utilization method thereof
KR101519389B1 (en) * 2008-07-28 2015-05-18 서희동 Method for treating organic-wastes
JP4482717B1 (en) * 2009-07-03 2010-06-16 龍男 白方 Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same
JP2011011175A (en) * 2009-07-03 2011-01-20 Tatsuo Shirakata Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same

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