JP2001205283A - Garbage treatment apparatus - Google Patents

Garbage treatment apparatus

Info

Publication number
JP2001205283A
JP2001205283A JP2000019475A JP2000019475A JP2001205283A JP 2001205283 A JP2001205283 A JP 2001205283A JP 2000019475 A JP2000019475 A JP 2000019475A JP 2000019475 A JP2000019475 A JP 2000019475A JP 2001205283 A JP2001205283 A JP 2001205283A
Authority
JP
Japan
Prior art keywords
fluidized bed
liquid
garbage disposal
wastewater treatment
sprinkling filter
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.)
Granted
Application number
JP2000019475A
Other languages
Japanese (ja)
Other versions
JP3877482B2 (en
Inventor
Haruhiko Suzuki
晴彦 鈴木
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 JP2000019475A priority Critical patent/JP3877482B2/en
Publication of JP2001205283A publication Critical patent/JP2001205283A/en
Application granted granted Critical
Publication of JP3877482B2 publication Critical patent/JP3877482B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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)
  • Activated Sludge Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To solve such as problem that the water sprinkling filter bed part of a wastewater treatment apparatus is clogged by the accumulation of sludge and the treatment efficiency of the apparatus is lowered and the treatment life thereof is also shortened. SOLUTION: A garbage treatment apparatus is equipped with a flow rate adjusting device for temporary storing a garbage crushing liquid, a solid-liquid separation device for separating the crushing liquid into a solid component and a liquid component, a composting device for changing the solid component into compost and a wastewater treatment apparatus for microbially treating organic matter in the liquid component. The wastewater treatment apparatus is constituted of a fluidized bed part, a water sprinkling filter bed part and a sedimentation separation tank and, by circulating a microorganism carrier between the water sprinkling filter bed part and the fluidized bed part, the clogging of the water sprinkling filter bed part caused by accumulated sludge is suppressed to keep the high treatment efficiency of organic wastewater in the wastewater treatment apparatus over a long period of time.

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
用して水ととも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 of introducing garbage crushed with water using a disposer, separating the garbage into a solid component and a liquid component, and decomposing organic substances contained in each component by a microorganism. 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。しかし、こ
の沈殿分離だけでは不十分で、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
も微粒子同士が凝集し、排水処理装置にその凝集微粒子
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。
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. However, this sedimentation alone is not sufficient. In addition to introducing some of the suspended particles into the wastewater treatment device, the particles also aggregate during the transfer of the supernatant, and the aggregated particles accumulate in the wastewater treatment device. As a result, the treatment capacity is reduced, and there is a need to remove accumulated substances and replace the microorganism carrier.

【0008】本発明は、前記課題に鑑みなされたもので
あって、排水処理装置を散水ろ床部と流動床部と沈殿分
離槽とから構成し、散水ろ床部に充填した微生物担体を
流動床部との間で循環させることで、散水ろ床部に蓄積
した浮遊微粒子を自浄作用で排除し、散水ろ床部の閉塞
を抑制して排水の高効率処理が長期にわたって継続でき
る生ごみ処理機を提供することを目的とする。
The present invention has been made in view of the above-mentioned problems, and has a wastewater treatment device comprising a sprinkling filter bed, a fluidized bed, and a sedimentation separation tank. Garbage treatment that circulates between the floor and the sprinkling filter to remove suspended particulates that have accumulated on the floor by self-cleaning, suppresses blockage of the sprinkling filter, and enables high-efficiency drainage to continue for a long time The purpose is to provide a machine.

【0009】[0009]

【課題を解決するための手段】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
ことを特徴とする。
According to a first aspect of the present invention, there is provided a garbage disposal apparatus, comprising: a flow rate adjusting tank for temporarily storing a garbage crushed liquid obtained by crushing garbage discharged from a kitchen together with water; A solid-liquid separator for separating the crushed liquid into a solid component and a liquid component supplied from a tank, a compost device for composting the solid component separated by the solid-liquid separator, And a wastewater treatment device for treating the liquid supplied from the liquid separation device with microorganisms to obtain treated water.

【0010】請求項2に係る発明は、請求項1記載の生
ごみ処理装置において、前記コンポスト装置は、槽内に
微生物担体が充填されており、前記固体分を微生物によ
りコンポスト化することを特徴とする。
According to a second aspect of the present invention, in the garbage disposal apparatus according to the first aspect, the composting apparatus is characterized in that a microorganism carrier is filled in a tank, and the solid component is composted by microorganisms. And

【0011】請求項3に係る発明は、請求項1または2
記載の生ごみ処理装置において、前記排水処理装置は、
散水ろ床部と、流動床部と、沈殿分離槽と、を具備する
ことを特徴とする。
The invention according to claim 3 is the invention according to claim 1 or 2
In the garbage disposal device according to the above, the wastewater treatment device,
It is characterized by comprising a sprinkling filter bed, a fluidized bed, and a sedimentation separation tank.

【0012】請求項4に係る発明は、請求項1〜3のい
ずれか1つに記載の装置において、前記排水処理装置
は、散水ろ床部と流動床部、および流動床部と沈殿分離
槽とがそれぞれ連通していることを特徴とする。
According to a fourth aspect of the present invention, in the apparatus according to any one of the first to third aspects, the wastewater treatment apparatus includes a sprinkling filter section and a fluidized bed section, and a fluidized bed section and a sedimentation separation tank. Are connected to each other.

【0013】請求項5に係る発明は、請求項4に記載の
装置において、前記散水ろ床部の下部と前記流動床部の
上部とが連通口を通して連通していることを特徴とす
る。
According to a fifth aspect of the present invention, in the apparatus according to the fourth aspect, the lower part of the water trickling filter part and the upper part of the fluidized bed part communicate with each other through a communication port.

【0014】請求項6に係る発明は、請求項4または5
のいずれか1つに記載の装置において、前記流動床部の
上部と前記沈殿分離槽の上部とは連通しており、前記液
体分が前記流動床部から前記沈殿分離槽へとオーバーフ
ローすることを特徴とする。
The invention according to claim 6 is the invention according to claim 4 or 5.
In the apparatus according to any one of the above, the upper part of the fluidized bed and the upper part of the sedimentation / separation tank communicate with each other, and the liquid component overflows from the fluidized bed to the sedimentation / separation tank. Features.

【0015】請求項7に係る発明は、請求項3〜6のい
ずれか1つに記載の生ごみ処理装置において、前記排水
処理装置は、前記散水ろ床部と前記流動床部において、
前記液体分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 seventh aspect of the present invention, in the garbage disposal apparatus according to any one of the third to sixth aspects, the wastewater treatment apparatus includes a sprinkling filter section and a fluidized bed section.
The organic component in the liquid component is treated with a microorganism to oxidatively decompose.

【0016】請求項8に係る発明は、請求項3〜7のい
ずれか1つに記載の生ごみ処理装置において、前記排水
処理装置は、前記微生物担体が前記散水ろ床部に充填さ
れており、該微生物担体は前記散水ろ床部と前記流動床
部とを前記連通口を通って循環移動することを特徴とす
る。
According to an eighth aspect of the present invention, in the garbage disposal apparatus according to any one of the third to seventh aspects, in the wastewater treatment apparatus, the microorganism carrier is filled in the water trickling filter section. The microorganism carrier circulates through the sprinkling filter section and the fluidized bed section through the communication port.

【0017】請求項9に係る発明は、請求項4〜8のい
ずれか1つに記載の生ごみ処理装置において、前記排水
処理装置の散水ろ床部に充填された微生物担体は、前記
連通口を通って前記流動床部へと移動する速度と、前記
流動床部から前記散水ろ床部に汲み上げられる移動速度
とがほぼ等しく、前記散水ろ床部に充填された微生物担
体の層の厚みはほぼ一定に保持されることを特徴とす
る。
According to a ninth aspect of the present invention, in the garbage disposal apparatus according to any one of the fourth to eighth aspects, the microorganism carrier filled in a sprinkling filter section of the wastewater treatment apparatus is connected to the communication port. The speed of moving to the fluidized bed through the fluidized bed and the speed of pumping from the fluidized bed to the sprinkling filter are almost equal, and the thickness of the layer of the microorganism carrier filled in the sprinkling filter is It is characterized by being kept substantially constant.

【0018】請求項10に係る発明は、請求項3〜9の
いずれか1つに記載の生ごみ処理装置において、前記散
水ろ床部の底面には充填されている微生物担体の粒径よ
りも小さな直径の孔を開けてあり、処理水のみを通過さ
せて排水することを特徴とする。
According to a tenth aspect of the present invention, in the garbage disposal apparatus according to any one of the third to ninth aspects, the particle size of the microorganism carrier packed on the bottom surface of the water trickling filter portion is smaller than the particle size of the microorganism carrier. A hole with a small diameter is formed, and only the treated water is passed and drained.

【0019】請求項11に係る発明は、請求項3〜10
のいずれか1つに記載の生ごみ処理装置において、前記
散水ろ床部および前記流動床部に充填されている前記微
生物担体は多孔質で、微生物を担持する能力が高いこと
を特徴とする。
The invention according to claim 11 is the invention according to claims 3 to 10.
In the garbage disposal apparatus according to any one of the above, the microorganism carrier filled in the sprinkling filter section and the fluidized bed section is porous and has a high ability to carry microorganisms.

【0020】請求項12に係る発明は、請求項3〜11
のいずれか1つに記載の生ごみ処理装置において、前記
微生物担体は水よりも比重が小さく、および/または、
独立気泡を持った担体であることを特徴とする。
The invention according to claim 12 is the invention according to claims 3 to 11
In the garbage processing apparatus according to any one of the above, the specific gravity of the microorganism carrier is smaller than water, and / or
It is characterized by being a carrier having closed cells.

【0021】[0021]

【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.

【0022】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。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液体
分中の有機物を生物処理して除去する排水処理装置4、
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)5を有している。
FIG. 1 is a diagram showing a configuration of a garbage processing system 1 according to the present embodiment. Garbage disposal system 1
, The garbage discarded in the sink is crushed by the disposer together with the water, and the garbage crushed liquid and kitchen wastewater are introduced and temporarily stored, and the flow control tank 2, the crushed garbage and the wastewater A solid-liquid separator 3 for separating the mixture into a solid component and a liquid component, a wastewater treatment device 4 for biologically removing organic matter in the liquid component separated by the solid-liquid separator 3,
It has a solid material processing device (composting device) 5 for performing composting of solids.

【0023】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4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 separator 3 at regular time intervals. The time interval of this pumping is determined by the processing capacity of the waste water treatment device 4 at the subsequent stage.

【0024】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5へ送られて堆肥化処理される。一方、液体
分は排水処理装置4に導入されて、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 solid components such as crushed garbage and sludge and liquid components of organic wastewater. The separated solids are sent to the composting device 5 and composted. On the other hand, the liquid component is introduced into the wastewater treatment device 4 and discharged into the sewage after removing the organic matter in the liquid component by microbial treatment.

【0025】次に、図2は排水処理装置4の構成を示す
ための模式図である。
Next, FIG. 2 is a schematic view showing the configuration of the wastewater treatment apparatus 4. As shown in FIG.

【0026】排水処理装置4は、流動床部10と、散水
ろ床部11と、沈殿分離槽12とから構成されている。
The wastewater treatment apparatus 4 comprises a fluidized bed section 10, a sprinkling filter bed section 11, and a sedimentation separation tank 12.

【0027】固液分離装置3で分離された液体分である
有機排水は、排水処理装置4の流動床部10に導入さ
れ、水より比重が小さく、および/または、独立気泡を
持った微生物担体13に担持されている微生物によっ
て、液体分中の有機物は分解処理される。
The organic wastewater, which is a liquid component separated by the solid-liquid separation device 3, is introduced into the fluidized bed 10 of the wastewater treatment device 4, and has a specific gravity smaller than that of water and / or a microorganism carrier having closed cells. The organic matter in the liquid component is decomposed by the microorganisms carried on 13.

【0028】流動床部10の液体分の一部は水面近くか
ら微生物担体13と一緒に汲み上げられ、散水ろ床部1
1に導入される。この液体分と担体の流れは図中の矢印
14に示した。
A part of the liquid in the fluidized bed 10 is pumped together with the microbial carrier 13 from near the water surface, and the water is filtered from the sprinkling filter 1.
Introduced in 1. The flow of the liquid and the carrier is shown by arrow 14 in the figure.

【0029】散水ろ床部11に導入された液体分は、散
水ろ床部11に充填されている微生物担体13に接触す
ることで微生物処理され、散水ろ床部11の底面に開け
られた孔15から処理水16として排出される。一方、
散水ろ床部11に導入された微生物担体13は、散水ろ
床部11に充填されている微生物担体13の上に充填さ
れる。この時、散水ろ床部11の底面は流動床部10に
向けて傾斜が設けられているので、散水ろ床部11に充
填されていた微生物担体13は散水ろ床部11の下方に
設けた連通口17を通って流動床部10へ押し出され
る。従って、この微生物担体13は常に流動床部10と
散水ろ床部11との間を循環することになる。
The liquid introduced into the sprinkling filter section 11 is treated with microorganisms by contacting the microorganism carrier 13 filled in the sprinkling filter section 11, and a hole formed in the bottom of the sprinkling filter section 11. It is discharged from 15 as treated water 16. on the other hand,
The microorganism carrier 13 introduced into the trickling filter part 11 is filled on the microorganism carrier 13 filled in the trickling filter part 11. At this time, the bottom of the trickling filter part 11 is inclined toward the fluidized bed part 10, so that the microorganism carrier 13 filled in the trickling filter bed part 11 is provided below the trickling filter bed part 11. It is extruded to the fluidized bed section 10 through the communication port 17. Therefore, the microorganism carrier 13 always circulates between the fluidized bed 10 and the trickling filter bed 11.

【0030】連通口17において、微生物担体13の移
動が容易に行えるよう、図3に示すようなローラー30
を設けてもよい。
At the communication port 17, a roller 30 as shown in FIG.
May be provided.

【0031】別の形態として、図4に示すようなモータ
ー31とベルト32を設置し、モーター31の駆動力を
連結ベルト33とプーリー34を介してベルト32を動
かしてもよい。
As another form, a motor 31 and a belt 32 as shown in FIG. 4 may be provided, and the driving force of the motor 31 may be moved through the connecting belt 33 and the pulley 34.

【0032】更には、図5に示すように、流動床部10
と連通口17とを結ぶバイパス35を設置し、そのバイ
パス35にポンプ36を介することで、連通口17から
流動床部10に向けて水流を起こし、その水圧で微生物
担体13を移動させてもよい。
Further, as shown in FIG.
By installing a bypass 35 connecting the communication port 17 with the communication port 17, a water flow is generated from the communication port 17 toward the fluidized bed 10 by passing the pump 35 through the bypass 35, and the microorganism carrier 13 is moved by the water pressure. Good.

【0033】更に、図6に示すように、微生物担体循環
パイプ37を設置し、その中で自由に移動するようにし
た微生物担体13を水中ポンプ38で強制的に循環させ
てもよい。この場合は微生物担体循環パイプ37に小孔
39、39、…を開けることで、流動床部10の液体分
を微生物担体13と一緒に散水ろ床部11に汲み上げる
ことができる。
Further, as shown in FIG. 6, a microorganism carrier circulating pipe 37 may be provided, and the microorganism carrier 13 which is freely moved therein may be forcibly circulated by a submersible pump 38. In this case, by opening small holes 39, 39,... In the microorganism carrier circulation pipe 37, the liquid component in the fluidized bed 10 can be pumped together with the microorganism carrier 13 to the sprinkling filter bed 11.

【0034】流動床部10と沈殿分離槽12とは上部が
連通しており、流動床部10の液体分はオーバーフロー
して沈殿分離槽12に流入し、液体分中の浮遊微粒子は
静置状態で沈殿層18を形成する。沈降して蓄積した微
粒子の沈殿層18は、返送汚泥19としてコンポスト装
置5へ搬送されて堆肥化処理される。
The upper part of the fluidized bed 10 and the sedimentation / separation tank 12 communicate with each other. The liquid component in the fluidized bed part 10 overflows and flows into the sedimentation / separation tank 12, and the suspended fine particles in the liquid part are kept stationary. To form a precipitation layer 18. The sediment layer 18 of the fine particles that has settled and accumulated is transported to the composting apparatus 5 as returned sludge 19 and is subjected to a composting process.

【0035】流動床部10の液体分の水面20は、散水
ろ床部11の底面に開けられた最下部の孔15よりは低
く、沈殿分離槽12との仕切りよりは高く、保持してお
くことで、前記の動作が可能になる。
The water level 20 of the liquid in the fluidized bed 10 is lower than the lowermost hole 15 formed in the bottom of the sprinkling filter 11 and higher than the partition from the sedimentation / separation tank 12. This enables the above-described operation.

【0036】この結果、従来の散水ろ床方式のみでは上
面に蓄積していた汚泥が、本発明では、微生物担体13
と一緒に循環するので、散水ろ床部11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 had accumulated on the upper surface only in the conventional trickling filter system was changed to the microorganism carrier 13 in the present invention.
Therefore, clogging of the sprinkling filter section 11 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.

【0037】ここで、図7に散水ろ床部11で処理され
た水を更に処理する形態を示す。
Here, FIG. 7 shows an embodiment in which the water treated in the sprinkling filter floor 11 is further treated.

【0038】散水ろ床部11だけでは水を処理する能力
が低い場合、散水ろ床部11を微生物担体13の水切り
と蓄積汚泥除去の目的のみに利用し、その下段に従来の
散水ろ床方式の排水処理槽21を独立に設けてもよい。
When the water treatment capacity is low only with the sprinkling filter bed section 11, the sprinkling filter bed section 11 is used only for the purpose of draining the microorganism carrier 13 and removing the accumulated sludge. May be independently provided.

【0039】[0039]

【発明の効果】本発明は叙述のように、排水処理装置を
流動床部と、散水ろ床部と、沈殿分離槽とから構成し、
微生物担体を散水ろ床部と流動床部との間で循環させる
ことで、散水ろ床部の蓄積汚泥による閉塞を抑制して、
排水処理装置における有機排水の効率よい処理が長期間
にわたって可能になった。
According to the present invention, as described above, the wastewater treatment apparatus comprises a fluidized bed, a sprinkling filter, and a sedimentation separation tank.
By circulating the microbial carrier between the sprinkling filter bed and the fluidized bed, the clogging of the sprinkling filter bed with accumulated sludge is suppressed,
Efficient treatment of organic wastewater in wastewater treatment equipment has become 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】連通口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 view from the front showing another embodiment of the communication port.

【図4】連通口の別の実施形態を示す正面方向からの模
式図である。
FIG. 4 is a schematic view from the front showing another embodiment of the communication port.

【図5】連通口の別の実施形態を示す正面方向からの模
式図である。
FIG. 5 is a schematic view from the front showing another embodiment of the communication port.

【図6】連通口の別の実施形態を示す正面方向からの模
式図である。
FIG. 6 is a schematic view from the front showing another embodiment of the communication port.

【図7】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. 7 is a schematic view from the front showing another embodiment of the wastewater treatment device.

【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…排水処理装置 5…コンポスト装置 10…流動床部 11…散水ろ床部 12…沈殿分離槽 13…微生物担体 14…液体分と微生物担体の流れ 15…散水ろ床部底面の排水孔 16…処理水 17…散水ろ床部と流動床部とを結ぶ連通口 18…浮遊微粒子の沈殿層 19…返送汚泥 20…液体分水面 21…排水処理槽 30…ローラー 31…モーター 32…ベルト 33…連結ベルト 34…プーリー 35…バイパス 36…ポンプ 37…微生物担体循環パイプ 38…水中ポンプ 39…小孔 DESCRIPTION OF SYMBOLS 1 ... Garbage disposal apparatus 2 ... Flow control tank 3 ... Solid-liquid separation apparatus 4 ... Wastewater treatment apparatus 5 ... Compost apparatus 10 ... Fluidized bed part 11 ... Sprinkling filter bed part 12 ... Sedimentation separation tank 13 ... Microorganism carrier 14 ... Liquid content Flow of water and microorganism carrier 15 Drainage hole at bottom of sprinkler filter 16 Treatment water 17 Communication port connecting sprinkler filter and fluidized bed 18 Sediment layer of suspended particulates 19 Return sludge 20 Liquid level 21 ... wastewater treatment tank 30 ... roller 31 ... motor 32 ... belt 33 ... connecting belt 34 ... pulley 35 ... bypass 36 ... pump 37 ... microorganism carrier circulation pipe 38 ... submersible pump 39 ... small hole

Claims (12)

【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 separator for separating the solid-liquid separator, a compost device for composting the solid component separated by the solid-liquid separator, and a microorganism component for treating the liquid component supplied from the solid-liquid separator. A garbage disposal device, comprising: a wastewater treatment device for obtaining water.
【請求項2】 前記コンポスト装置は、槽内に微生物
担体が充填されており、前記固体分を微生物によりコン
ポスト化することを特徴とする請求項1記載の生ごみ処
理装置。
2. The garbage disposal apparatus according to claim 1, wherein the composting apparatus has a tank filled with a microorganism carrier, and the solids are composted by microorganisms.
【請求項3】 前記排水処理装置は、散水ろ床部と、
流動床部と、沈殿分離槽と、を具備することを特徴とす
る請求項1または2記載の生ごみ処理装置。
3. The wastewater treatment device according to claim 1, further comprising: a sprinkling filter floor;
3. The garbage disposal apparatus according to claim 1, further comprising a fluidized bed and a sedimentation separation tank.
【請求項4】 請求項1〜3のいずれか1つに記載の
装置において、前記排水処理装置は、散水ろ床部と流動
床部、および流動床部と沈殿分離槽とがそれぞれ連通し
ていることを特徴とする生ごみ処理装置。
4. The apparatus according to any one of claims 1 to 3, wherein the wastewater treatment apparatus includes a sprinkling filter section and a fluidized bed section, and a fluidized bed section and a sedimentation separation tank, respectively. A garbage disposal device characterized by the following.
【請求項5】 請求項4に記載の装置において、前記
散水ろ床部の下部と前記流動床部の上部とが連通口を通
して連通していることを特徴とする生ごみ処理装置。
5. The garbage disposal apparatus according to claim 4, wherein a lower part of the trickling filter part and an upper part of the fluidized bed part communicate with each other through a communication port.
【請求項6】 請求項4または5のいずれか1つに記
載の装置において、前記流動床部の上部と前記沈殿分離
槽の上部とは連通しており、前記液体分が前記流動床部
から前記沈殿分離槽へとオーバーフローすることを特徴
とする生ごみ処理装置。
6. The apparatus according to claim 4, wherein an upper portion of the fluidized bed portion and an upper portion of the sedimentation separation tank communicate with each other, and the liquid component is discharged from the fluidized bed portion. A garbage disposal apparatus characterized by overflowing into the sedimentation separation tank.
【請求項7】 前記排水処理装置は、前記散水ろ床部
と前記流動床部において、前記液体分中の有機成分を微
生物処理して酸化分解することを特徴とする請求項3〜
6のいずれか1つに記載の生ごみ処理装置。
7. The wastewater treatment device according to claim 3, wherein the sprinkling filter section and the fluidized bed section treat the organic component in the liquid component with microorganisms to oxidatively decompose the organic component.
6. The garbage disposal apparatus according to any one of 6.
【請求項8】 前記排水処理装置は、前記微生物担体
が前記散水ろ床部に充填されており、該微生物担体は前
記散水ろ床部と前記流動床部とを前記連通口を通って循
環移動することを特徴とする請求項3〜7のいずれか1
つに記載の生ごみ処理装置。
8. The wastewater treatment device, wherein the microbial carrier is filled in the sprinkling filter section, and the microbial carrier circulates through the sprinkling filter section and the fluidized bed section through the communication port. The method according to claim 3, wherein
A garbage disposal device according to any one of the above.
【請求項9】 前記排水処理装置の散水ろ床部に充填
された微生物担体は、前記連通口を通って前記流動床部
へと移動する速度と、前記流動床部から前記散水ろ床部
に汲み上げられる移動速度とがほぼ等しく、前記散水ろ
床部に充填された微生物担体の層の厚みはほぼ一定に保
持されることを特徴とする請求項4〜8のいずれか1つ
に記載の生ごみ処理装置。
9. The microorganism carrier filled in the sprinkling filter section of the wastewater treatment device moves at a rate of moving to the fluidized bed section through the communication port, and moves from the fluidized bed section to the sprinkling filter section. 9. The method according to claim 4, wherein the speed of pumping is substantially equal, and the thickness of the microbial carrier layer filled in the trickling filter bed is kept substantially constant. Waste treatment equipment.
【請求項10】 前記散水ろ床部の底面には充填され
ている微生物担体の粒径よりも小さな直径の孔を開けて
あり、処理水のみを通過させて排水することを特徴とす
る請求項3〜9のいずれか1つに記載の生ごみ処理装
置。
10. The bottom surface of the water trickling filter unit is provided with a hole having a diameter smaller than the particle diameter of the microorganism carrier packed therein, and only treated water is allowed to pass therethrough for drainage. A garbage disposal apparatus according to any one of 3 to 9.
【請求項11】 前記散水ろ床部および前記流動床部
に充填されている前記微生物担体は多孔質で、微生物を
担持する能力が高いことを特徴とする請求項3〜10の
いずれか1つに記載の生ごみ処理装置。
11. The method according to claim 3, wherein the microorganism carrier filled in the sprinkling filter bed and the fluidized bed is porous and has a high ability to carry microorganisms. A garbage disposal apparatus according to item 1.
【請求項12】 前記微生物担体は水よりも比重が小
さく、および/または、独立気泡を持った担体であるこ
とを特徴とする請求項3〜11のいずれか1つに記載の
生ごみ処理装置。
12. The garbage disposal apparatus according to claim 3, wherein the microorganism carrier has a specific gravity lower than that of water and / or is a carrier having closed cells. .
JP2000019475A 2000-01-28 2000-01-28 Garbage disposal equipment Expired - Fee Related JP3877482B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000019475A JP3877482B2 (en) 2000-01-28 2000-01-28 Garbage disposal equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000019475A JP3877482B2 (en) 2000-01-28 2000-01-28 Garbage disposal equipment

Publications (2)

Publication Number Publication Date
JP2001205283A true JP2001205283A (en) 2001-07-31
JP3877482B2 JP3877482B2 (en) 2007-02-07

Family

ID=18546164

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000019475A Expired - Fee Related JP3877482B2 (en) 2000-01-28 2000-01-28 Garbage disposal equipment

Country Status (1)

Country Link
JP (1) JP3877482B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003070873A3 (en) * 2002-02-19 2004-04-08 Hoefer Bioreact Gmbh Cultivation method for micro-organisms and bioreactor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003070873A3 (en) * 2002-02-19 2004-04-08 Hoefer Bioreact Gmbh Cultivation method for micro-organisms and bioreactor

Also Published As

Publication number Publication date
JP3877482B2 (en) 2007-02-07

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