JP2001205284A - Garbage treatment apparatus - Google Patents

Garbage treatment apparatus

Info

Publication number
JP2001205284A
JP2001205284A JP2000019477A JP2000019477A JP2001205284A JP 2001205284 A JP2001205284 A JP 2001205284A JP 2000019477 A JP2000019477 A JP 2000019477A JP 2000019477 A JP2000019477 A JP 2000019477A JP 2001205284 A JP2001205284 A JP 2001205284A
Authority
JP
Japan
Prior art keywords
liquid
solid
unit
sedimentation
filtration
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
JP2000019477A
Other languages
Japanese (ja)
Inventor
Tatsuhiko Sekiguchi
達彦 関口
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP2000019477A priority Critical patent/JP2001205284A/en
Publication of JP2001205284A publication Critical patent/JP2001205284A/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

  • Biological Treatment Of Waste Water (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To solve such a problem that fine particles are gathered even on the way of the feed of a supernatant liquid to form small lumps and these small lumps are accumulated in a wastewater treatment apparatus and the piping thereto to generate clogging. SOLUTION: In a gargage treatment apparatus equipped with a solid-liquid separation apparatus (3) for separating the crushing liquid supplied from a flow rate adjusting tank (2) into a solid component and a liquid component, a compost apparatus (4) for composting the solid component separated by the solid-liquid separation apparatus (3), a sedimentation separation apparatus (5) for removing floating fine particles from the liquid component supplied from the solid-liquid separation apparatus (3) and a wastewater treatment apparatus (6) for microbially treating the liquid component from which floating fine particles are removed by the sedimentation separation apparatus (5), the sedimentation separation apparatus (5) is equipped with a sedimentation separation part (10) and a filtring decomposition part (11) and the filtring decomposition part (11) is filled with a microorganism carrier not only to filter the flowing fine particles in the liquid component supplied from the solid-liquid separation apparatus (3) but also to microbially treat the organic component in the floating fine particles to oxidize and decompose the same.

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、ディスポーザを使
用して水と共に粉砕した生ごみを導入して、固体分と液
体分とに分離し、それぞれに含有する有機物を微生物に
より分解処理して、固体分は堆肥に、液体分は下水道に
放流できる水質を得ようとするための生ごみ処理装置に
関するものである。
BACKGROUND OF THE INVENTION The present invention relates to a method for introducing garbage crushed with water using a disposer, separating the garbage into solids and liquids, and decomposing organic substances contained in each of the garbage by microorganisms. The present invention relates to a garbage disposal apparatus for obtaining water quality that can be discharged into a compost while solids can be discharged into a sewer.

【0002】[0002]

【従来の技術】近年、好気性の微生物を利用して有機性
排水を処理する方法が活発に研究開発されている。例え
ば、下水処理場等では、活性汚泥法が通常採用され、ま
た合併型の浄化槽では活性汚泥法や浸漬瀘床法が採用さ
れている。
2. Description of the Related Art In recent years, methods for treating organic wastewater using aerobic microorganisms have been actively researched and developed. For example, in a sewage treatment plant or the like, an activated sludge method is usually adopted, and in a combined type septic tank, an activated sludge method or a submerged filter method is adopted.

【0003】また、家庭等から排出される生ごみについ
ては、ディスポーザによって粉砕した生ごみを生ごみ含
有排水として処理することが研究開発されている。
As for garbage discharged from homes and the like, research and development has been conducted to treat garbage crushed by a disposer as garbage-containing wastewater.

【0004】例えば、特開平9−1117号公報には、
生ごみ含有排水を固形物処理部に流入し、ここで固形物
を微生物により分解処理した後、固形物処理装置から排
出された一次処理水を排水処理槽に導入し、ここで曝気
処理することにより、ディスポ−ザにより粉砕されてな
る生ごみ含有排水から固形物を分解除去すると共に、排
水の浄化を行うことが開示されている。
For example, Japanese Patent Application Laid-Open No. 9-1117 discloses that
The garbage-containing wastewater flows into the solids treatment section, where the solids are decomposed by microorganisms, and then the primary treated water discharged from the solids treatment device is introduced into the wastewater treatment tank where it is aerated. Discloses decomposing and removing solids from garbage-containing wastewater pulverized by a disposer and purifying the wastewater.

【0005】この公報に開示された装置では、排水処理
槽において、散気装置により排水を曝気処理しており、
基本的には活性汚泥法と同様の処理を行っている。
[0005] In the apparatus disclosed in this publication, wastewater is aerated by a diffuser in a wastewater treatment tank.
Basically, the same treatment as the activated sludge method is performed.

【0006】これに対して、本願発明者らは、固形物処
理装置(一次処理装置)の後段に微生物担体が充填され
てなる充填層を備える排水処理装置(二次処理装置)を
用いることにより、排水の浄化が良好に行えることを見
出している(特開平11−19674号公報)。
[0006] On the other hand, the present inventors have used a wastewater treatment device (secondary treatment device) provided with a packed bed in which a microorganism carrier is filled at the subsequent stage of a solid matter treatment device (primary treatment device). It has been found that the purification of wastewater can be carried out well (Japanese Patent Laid-Open No. 11-19674).

【0007】[0007]

【発明が解決しようとする課題】ここで、従来の生ごみ
処理装置における排水処理装置への液体分の導入は、固
液分離装置で分離した液体分を一時貯留することで浮遊
微粒子を沈殿分離し、その上澄み液を散水ろ床方式の微
生物担体充填排水処理装置へ導入していた。
Here, the introduction of the liquid into the wastewater treatment apparatus in the conventional garbage disposal apparatus is performed by temporarily storing the liquid separated by the solid-liquid separator to separate the suspended fine particles. Then, the supernatant was introduced into a microorganism carrier-filled wastewater treatment apparatus of a sprinkling filter type.

【0008】しかし、この沈殿分離装置を設けるだけで
は不十分で、浮遊微粒子の一部が排水処理装置に導入さ
れるのに加え、上澄み液の搬送途中でも微粒子が凝集
し、排水処理装置及びそこへの配管にその凝集物が蓄積
して閉塞してしまうことで、処理能力の低下を招き、蓄
積物の除去や微生物担体の交換を行う必要性があった。
However, it is not enough to provide this sedimentation / separation device alone. In addition to the introduction of a part of the suspended particulates into the wastewater treatment device, the particulates also aggregate during the transfer of the supernatant, and the wastewater treatment device and the Agglomerates accumulate in the piping to the pipes and block the pipes, resulting in a decrease in processing capacity, and there is a need to remove accumulated substances and replace microorganism carriers.

【0009】[0009]

【課題を解決するための手段】そこで、本発明は前述の
問題点に鑑みなされたものであり、請求項1に係る生ご
み処理装置は、台所から出る生ごみを水と一緒に粉砕し
た生ごみ破砕液を一時貯留するための流量調整槽と、該
流量調整槽から供給された、前記破砕液を固体分と液体
分とに分離するための固液分離装置と、該固液分離装置
により分離された固体分を堆肥にするためのコンポスト
装置と、前記固液分離装置から供給された液体分から浮
遊微粒子を除くための沈殿分離装置と、該沈殿分離装置
で浮遊微粒子を除いた液体分を微生物処理して処理水を
得るための排水処理装置と、を具備する生ごみ処理装置
において、前記沈殿分離装置は、沈殿分離部と、ろ過分
解部と、を具備することを特徴とする。
SUMMARY OF THE INVENTION Accordingly, the present invention has been made in view of the above-mentioned problems, and a garbage disposal apparatus according to claim 1 is a garbage disposal apparatus that crushes garbage discharged from a kitchen together with water. A flow control tank for temporarily storing the refuse crushed liquid, a solid-liquid separation device supplied from the flow control tank, for separating the crushed liquid into a solid component and a liquid component, A composting device for composting the separated solid content, a sedimentation separation device for removing suspended particulates from the liquid component supplied from the solid-liquid separation device, and a liquid component from which the suspended particulates are removed by the sedimentation separation device. In a garbage treatment apparatus including a wastewater treatment apparatus for obtaining treated water by microbial treatment, the sedimentation separation apparatus includes a sedimentation separation section and a filtration decomposition section.

【0010】請求項2に係る発明は、請求項1に記載の
装置において、前記ろ過分解部は、内部に微生物担体が
充填されており、前記固液分離装置から供給された液体
分中の浮遊微粒子をろ過すると共に、該浮遊微粒子中の
有機成分を微生物処理して酸化分解することを特徴とす
る。
According to a second aspect of the present invention, in the apparatus according to the first aspect, the filtration / decomposition unit is filled with a microbial carrier, and is suspended in a liquid supplied from the solid-liquid separation device. The method is characterized in that the fine particles are filtered and the organic components in the floating fine particles are treated with microorganisms to be oxidatively decomposed.

【0011】請求項3に係る発明は、請求項1〜2のい
ずれか1つに記載の装置において、前記沈殿分離部の下
部と前記ろ過分解部の下部とは連通しており、前記液体
分を前記ろ過分解部の上部から前記排水処理装置に移送
する際に生じる、前記沈殿分離部と前記ろ過分解部の間
の水圧差によって、前記液体分が前記沈殿分離部から前
記ろ過分解部に移動することを特徴とする。
According to a third aspect of the present invention, in the apparatus according to any one of the first to second aspects, the lower part of the sedimentation separation part and the lower part of the filtration decomposition part communicate with each other, and The liquid component moves from the sedimentation separation unit to the filtration decomposition unit due to a water pressure difference between the sedimentation separation unit and the filtration decomposition unit, which is generated when transferring from the upper part of the filtration decomposition unit to the wastewater treatment device. It is characterized by doing.

【0012】請求項4に係る発明は、請求項2に記載の
装置において、前記沈殿分離部を導入部、及び調整部の
2室に分離する仕切板を立設し、前記調整部の下部と前
記ろ過分解部の下部とは連通しており、前記液体分を前
記導入部の上部から前記調整部に移送し、前記液体分を
前記ろ過分解部の上部から前記排水処理装置に移送する
際に生じる、前記調整部と前記ろ過分解部の間の水圧差
によって、前記液体分が前記導入部から前記調整部に移
動することを特徴とする。
According to a fourth aspect of the present invention, in the apparatus according to the second aspect, a partition plate for separating the sedimentation separation section into two chambers, an introduction section and an adjustment section, is erected, and a lower portion of the adjustment section is provided. When communicating with the lower part of the filtration and decomposition part, transferring the liquid component from the upper part of the introduction part to the adjustment part, and transferring the liquid part from the upper part of the filtration and decomposition part to the wastewater treatment device. The liquid component moves from the introduction section to the adjustment section due to a water pressure difference generated between the adjustment section and the filtration / decomposition section.

【0013】[0013]

【発明の実施の形態】本発明に係る実施の形態を図面に
基づいて説明する。
An embodiment according to the present invention will be described with reference to the drawings.

【0014】図1は本実施の形態に係る生ごみ処理シス
テム1の構成を示す図である。
FIG. 1 is a diagram showing a configuration of a garbage processing system 1 according to the present embodiment.

【0015】生ごみ処理システム1は、流し台で廃棄さ
れた生ごみが水と一緒にディスポーザによって粉砕さ
れ、その生ごみ破砕液と台所排水等とが導入されて一時
的に貯留される流量調整槽2、破砕生ごみと排水との混
合物を固体分と液体分とに分離する固液分離装置3、固
液分離装置3によって分離された固体分の堆肥化処理を
行う固形物処理装置(コンポスト装置)4、固液分離装
置3によって分離された液体分中の浮遊微粒子を除去す
る沈殿分離装置5、沈殿分離装置5によって浮遊微粒子
を除去された排水中の有機物を微生物によって分解する
排水処理装置6、を有している。
The garbage processing system 1 is a flow control tank in which garbage discarded in a sink is crushed by a disposer together with water, and the garbage crushed liquid and kitchen wastewater are introduced and temporarily stored therein. 2. A solid-liquid separator 3 for separating a mixture of crushed garbage and wastewater into a solid component and a liquid component, and a solid material processing device (composting device) for performing composting of the solid separated by the solid-liquid separator 3 4) 4, a sedimentation / separation device 5 for removing suspended particulates in the liquid component separated by the solid-liquid separation device 3, and a wastewater treatment device 6 for decomposing organic matter in wastewater from which the suspended particulates have been removed by the sedimentation / separation device 5 by microorganisms. ,have.

【0016】流量調整槽2に一時的に貯留された破砕生
ごみ含有排水は、一定の時間間隔で固液分離装置3に汲
み上げられる。この汲み上げの時間間隔は後段の排水処
理装置6の処理能力によって決められる。
The crushed garbage-containing wastewater temporarily stored in the flow control tank 2 is pumped to the solid-liquid separation device 3 at regular time intervals. The time interval of this pumping is determined by the processing capacity of the waste water treatment device 6 at the subsequent stage.

【0017】固液分離装置3では、汲み上げられた破砕
生ごみ含有排水が破砕生ごみや汚泥などの固体分と有機
排水の液体分とに分離される。分離された固体分はコン
ポスト装置4へ送られて堆肥化処理される。一方、液体
分は沈殿分離装置5によって浮遊微粒子が除かれたの
ち、排水処理装置6に導入され、液体分中の有機物を微
生物処理で除去した後に下水へ排出される。
In the solid-liquid separator 3, the crushed garbage-containing wastewater pumped up is separated into solids such as crushed garbage and sludge and liquids of organic wastewater. The separated solids are sent to the composting device 4 and composted. On the other hand, the liquid component is introduced into the wastewater treatment device 6 after the suspended particulates are removed by the sedimentation / separation device 5, and is discharged to the sewage after removing the organic matter in the liquid component by the microorganism treatment.

【0018】次に、図2は沈殿分離装置5の構成を示す
ための模式図である。
Next, FIG. 2 is a schematic view showing the structure of the sedimentation / separation device 5.

【0019】沈殿分離装置5は、沈殿分離部10と、ろ
過分解部11とから構成されている。
The sedimentation / separation device 5 comprises a sedimentation / separation unit 10 and a filtration / decomposition unit 11.

【0020】固液分離装置3で分離された液体分は、沈
殿分離装置5の沈殿分離部10に導入され、一定時間静
置されることで、液体中の浮遊微粒子が沈殿される。
The liquid separated by the solid-liquid separator 3 is introduced into the sedimentation / separation unit 10 of the sedimentation / separation device 5, and is allowed to stand for a certain period of time to precipitate suspended particles in the liquid.

【0021】ろ過分解部11には微生物担体である粒径
2〜4ミリメートルの木質砕片12が充填されており、
沈殿分離部10において沈殿分離を行った上澄み液がこ
こを通過する際に沈殿しきれなかった浮遊微粒子をろ過
する役割を持つ。更に木質細片12中に生息する微生物
により、ろ過された浮遊微粒子中の有機物は分解され
る。
The filtration / decomposition unit 11 is filled with wood fragments 12 having a particle size of 2 to 4 mm, which are microbial carriers.
It has a role of filtering the suspended fine particles that have not been completely precipitated when the supernatant liquid subjected to the precipitation separation in the precipitation separation section 10 passes therethrough. Furthermore, the microorganisms inhabiting the woody strip 12 decompose the organic matter in the filtered suspended fine particles.

【0022】微生物担体には、粒径15ミリメートル以
下、のぞましくは2〜10ミリメートルの多孔性のも
の、例えばセラミックボール、スポンジなどを用いても
よい。
As the microorganism carrier, a porous carrier having a particle size of 15 mm or less, preferably 2 to 10 mm, such as a ceramic ball or sponge, may be used.

【0023】ろ過分解部11の上部には空間13が存在
し、ポンプなどによって浮遊微粒子が除去された排水は
配管16を通って排水処理装置6に移送される。
A space 13 exists above the filtration / decomposition unit 11, and the waste water from which suspended particulates have been removed by a pump or the like is transferred to a waste water treatment device 6 through a pipe 16.

【0024】沈殿分離部10の下部とろ過分解部11の
下部はつながっているので、排水処理装置6に排水が移
送されると沈殿分離部10とろ過分解部11の間に圧力
差が生じ、結果として沈殿分離部10からろ過分解部1
1への液体の移動が起こる。
Since the lower part of the sedimentation / separation unit 10 and the lower part of the filtration / decomposition unit 11 are connected, when the wastewater is transferred to the wastewater treatment device 6, a pressure difference is generated between the sedimentation / separation unit 10 and the filtration / decomposition unit 11, As a result, the sedimentation separation unit 10 to the filtration decomposition unit 1
The transfer of liquid to 1 occurs.

【0025】同様に、固液分離装置3から沈殿分離部1
0へ液体分が導入されると、同様の圧力差が生じ、沈殿
分離部10からろ過分解部11への液体の移動が起こ
る。
Similarly, the solid-liquid separator 3 separates the sedimentation separation unit 1
When the liquid component is introduced to 0, a similar pressure difference occurs, and the liquid moves from the precipitation separation unit 10 to the filtration decomposition unit 11.

【0026】沈殿分離槽10に沈降して蓄積した微粒子
の沈殿層14は、返送汚泥15として最終的にコンポス
ト装置4へ搬送されて堆肥化処理される。
The sedimentary layer 14 of the fine particles that settles and accumulates in the sedimentation separation tank 10 is finally conveyed to the composting device 4 as returned sludge 15 for composting.

【0027】この結果、従来の沈殿分離のみでは排水処
理装置6の上面付近に滞留していた汚泥が、本発明では
沈殿分離槽5のろ過分解部11でトラップされ、微生物
分解されるので、排水処理装置6及び沈殿分離装置5か
ら排水処理装置6への配管16の蓄積汚泥による閉塞を
解消し、汚泥除去のメンテナンスが軽減される。同時
に、処理能力も長期にわたり高い状態で運転することが
可能になる。
As a result, the sludge that has stayed in the vicinity of the upper surface of the wastewater treatment apparatus 6 by only the conventional sedimentation and separation is trapped in the filtration / decomposition unit 11 of the sedimentation / separation tank 5 and decomposed by microorganisms. The clogging of the pipe 16 from the treatment device 6 and the sedimentation separation device 5 to the wastewater treatment device 6 due to accumulated sludge is eliminated, and maintenance for sludge removal is reduced. At the same time, it is possible to operate at a high processing capacity for a long time.

【0028】更に、図3には、別の実施形態を示す。FIG. 3 shows another embodiment.

【0029】図2において、ろ過分解部11への浮遊微
粒子の蓄積が多い場合、沈殿分離部10とろ過分解部1
1の間に調整部17を設けてもよく、沈殿分離部10の
うち仕切板18で仕切られた調整部17以外の部分を導
入部20という(図3参照)。
In FIG. 2, when a large amount of suspended particulates accumulates in the filtration / decomposition unit 11, the precipitation / separation unit 10 and the filtration / decomposition unit 1
An adjusting section 17 may be provided between the two sections 1. A portion of the sedimentation / separation section 10 other than the adjusting section 17 partitioned by the partition plate 18 is referred to as an introduction section 20 (see FIG. 3).

【0030】沈殿分離部10と調整部17の間の仕切板
18は水面19より低く設定されており、固液分離装置
3から液体分が導入された時に導入部20からオーバー
フローすることにより、上澄み液が調整部17に送られ
る。この上澄み液は、図2の沈殿分離部10からろ過分
解部11に直接導入される液体よりも浮遊微粒子含量が
少ないので、ろ過分解部11への負担を小さくすること
ができる。
The partition plate 18 between the sedimentation separation unit 10 and the adjustment unit 17 is set lower than the water surface 19, and when a liquid component is introduced from the solid-liquid separation device 3, the liquid overflows from the introduction unit 20, thereby causing a supernatant. The liquid is sent to the adjusting unit 17. This supernatant liquid has a lower content of suspended particulates than the liquid directly introduced from the sedimentation / separation unit 10 to the filtration / decomposition unit 11 in FIG. 2, so that the burden on the filtration / decomposition unit 11 can be reduced.

【0031】[0031]

【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、沈殿分離装置を沈殿分離部とろ過分解部とか
ら構成し、排水処理装置に送られる浮遊微粒子をろ過、
分解することにより、排水処理装置および沈殿分離装置
から排水処理装置への配管の蓄積汚泥による閉塞を抑制
して、有機排水の効率の良い処理が長期間にわたって可
能になった。
As is apparent from the above description, according to the present invention, the sedimentation / separation unit is constituted by the sedimentation / separation unit and the filtration / decomposition unit, and filters the suspended fine particles sent to the wastewater treatment unit.
By decomposing, the clogging of the pipes from the wastewater treatment device and the sedimentation separation device to the wastewater treatment device due to accumulated sludge was suppressed, and efficient treatment of organic wastewater became possible over a long period of time.

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

【図1】本発明の一実施形態に係る生ごみ処理装置の正
面方向からの模式構成図である。
FIG. 1 is a schematic configuration diagram of a garbage processing apparatus according to an embodiment of the present invention as viewed from the front.

【図2】排水処理装置の正面方向からの模式図である。FIG. 2 is a schematic diagram of the wastewater treatment device as viewed from the front.

【図3】排水処理装置の別の実施形態を示す正面方向か
らの模式図である。
FIG. 3 is a schematic diagram showing another embodiment of the wastewater treatment device as viewed from the front.

【符号の説明】[Explanation of symbols]

1…生ごみ処理装置 2…流量調整槽 3…固液分離装置 4…コンポスト装置 5…沈殿分離装置 6…排水処理装置 10…沈殿分離部 11…ろ過分解部 12…微生物担体(木質細片) 13…移送用空間 14…沈殿層 15…返送汚泥 16…沈殿分離装置から排水処理装置への配管 17…調整部 18…仕切板 19…水面 DESCRIPTION OF SYMBOLS 1 ... Garbage processing apparatus 2 ... Flow control tank 3 ... Solid-liquid separation apparatus 4 ... Composting apparatus 5 ... Sedimentation separation apparatus 6 ... Wastewater treatment apparatus 10 ... Sedimentation separation part 11 ... Filtration decomposition part 12 ... Microorganism carrier (wood fines) DESCRIPTION OF SYMBOLS 13 ... Transfer space 14 ... Sedimentation layer 15 ... Return sludge 16 ... Pipe from a sedimentation separation apparatus to a wastewater treatment apparatus 17 ... Adjustment part 18 ... Partition plate 19 ... Water surface

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 台所から出る生ごみを水と一緒に粉砕
した生ごみ破砕液を一時貯留するための流量調整槽と、 該流量調整槽から供給された、前記破砕液を固体分と液
体分とに分離するための固液分離装置と、 該固液分離装置により分離された固体分を堆肥にするた
めのコンポスト装置と、 前記固液分離装置から供給された液体分から浮遊微粒子
を除くための沈殿分離装置と、 該沈殿分離装置で浮遊微粒子を除いた液体分を微生物処
理して処理水を得るための排水処理装置と、を具備する
生ごみ処理装置において、 前記沈殿分離装置は、沈殿分離部と、ろ過分解部と、を
具備することを特徴とする生ごみ処理装置。
1. A flow control tank for temporarily storing a garbage crushed liquid obtained by crushing garbage discharged from a kitchen together with water, and a solid content and a liquid content of the crushed liquid supplied from the flow control tank. A solid-liquid separation device for separating the solid component, a compost device for composting the solid component separated by the solid-liquid separation device, and a compost device for removing suspended particulates from the liquid component supplied from the solid-liquid separation device. A garbage disposal device comprising: a sedimentation separation device; and a wastewater treatment device for microbial treatment of a liquid component from which suspended particulates have been removed by the sedimentation separation device to obtain treated water. A garbage disposal device comprising: a filter unit;
【請求項2】 請求項1に記載の装置において、前記
ろ過分解部は、内部に微生物担体が充填されており、前
記固液分離装置から供給された液体分中の浮遊微粒子を
ろ過すると共に、該浮遊微粒子中の有機成分を微生物処
理して酸化分解することを特徴とする生ごみ処理装置。
2. The apparatus according to claim 1, wherein the filtration / decomposition unit is filled with a microbial carrier and filters suspended particulates in a liquid component supplied from the solid-liquid separation device. A garbage disposal apparatus characterized in that organic components in the suspended fine particles are treated with microorganisms to oxidatively decompose them.
【請求項3】 請求項1〜2のいずれか1つに記載の
装置において、前記沈殿分離部の下部と前記ろ過分解部
の下部とは連通しており、前記液体分を前記ろ過分解部
の上部から前記排水処理装置に移送する際に生じる、前
記沈殿分離部と前記ろ過分解部の間の水圧差によって、
前記液体分が前記沈殿分離部から前記ろ過分解部に移動
することを特徴とする生ごみ処理装置。
3. The apparatus according to claim 1, wherein a lower part of the sedimentation / separation unit and a lower part of the filtration / decomposition unit communicate with each other, and the liquid component is supplied to the filtration / decomposition unit. Due to the water pressure difference between the sedimentation separation unit and the filtration decomposition unit, which occurs when transferring from the upper part to the wastewater treatment device,
The garbage disposal apparatus, wherein the liquid component moves from the sedimentation separation section to the filtration decomposition section.
【請求項4】 請求項2に記載の装置において、前記
沈殿分離部を導入部、及び調整部の2室に分離する仕切
板を立設し、前記調整部の下部と前記ろ過分解部の下部
とは連通しており、前記液体分を前記導入部の上部から
前記調整部に移送し、前記液体分を前記ろ過分解部の上
部から前記排水処理装置に移送する際に生じる、前記調
整部と前記ろ過分解部の間の水圧差によって、前記液体
分が前記導入部から前記調整部に移動することを特徴と
する生ごみ処理装置。
4. The apparatus according to claim 2, wherein a partition plate for separating the sedimentation / separation unit into an introduction unit and an adjustment unit is provided upright, and a lower part of the adjustment unit and a lower part of the filter disassembly unit are provided. And communicating with the liquid component from the upper part of the introduction part to the adjusting part, and the liquid part is generated when the liquid part is transferred from the upper part of the filtration / decomposition unit to the wastewater treatment device, the adjusting part, The garbage disposal device, wherein the liquid component moves from the introduction section to the adjustment section due to a water pressure difference between the filtration and decomposition sections.
JP2000019477A 2000-01-28 2000-01-28 Garbage treatment apparatus Pending JP2001205284A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000019477A JP2001205284A (en) 2000-01-28 2000-01-28 Garbage treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000019477A JP2001205284A (en) 2000-01-28 2000-01-28 Garbage treatment apparatus

Publications (1)

Publication Number Publication Date
JP2001205284A true JP2001205284A (en) 2001-07-31

Family

ID=18546166

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000019477A Pending JP2001205284A (en) 2000-01-28 2000-01-28 Garbage treatment apparatus

Country Status (1)

Country Link
JP (1) JP2001205284A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012051662A1 (en) * 2010-10-21 2012-04-26 Everhard Industries Pty Ltd An effluent treatment unit

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012051662A1 (en) * 2010-10-21 2012-04-26 Everhard Industries Pty Ltd An effluent treatment unit

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