JP3877482B2 - Garbage disposal equipment - Google Patents

Garbage disposal equipment Download PDF

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Publication number
JP3877482B2
JP3877482B2 JP2000019475A JP2000019475A JP3877482B2 JP 3877482 B2 JP3877482 B2 JP 3877482B2 JP 2000019475 A JP2000019475 A JP 2000019475A JP 2000019475 A JP2000019475 A JP 2000019475A JP 3877482 B2 JP3877482 B2 JP 3877482B2
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Japan
Prior art keywords
liquid
fluidized bed
solid
garbage
filter bed
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JP2000019475A
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Japanese (ja)
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JP2001205283A (en
Inventor
晴彦 鈴木
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Sanyo Electric Co Ltd
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Sanyo Electric 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
    • 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

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

Description

【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。
【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。
【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。
【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。
【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。
【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)。
【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。
【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。
【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、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、
散水ろ床部と流動床部とを有し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、
を備える生ごみ処理装置において、
前記散水ろ床部には微生物担体が充填され、且つ前記散水ろ床部と前記流動床部の間には連通口を有し前記微生物担体は前記連通口を通って循環移動することを特徴とする。
【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、前記散水ろ床部の底面には孔を有し、前記処理水を通過させて排水することを特徴とする。
【0011】
請求項3に係る発明は、請求項1又は請求項2の何れかに記載の装置において、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。
【0012】
請求項4に係る発明は、請求項1及至請求項3の何れか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前記連通口を通して連通していることを特徴とする。
【0013】
請求項5に係る発明は、請求項1及至請求項4の何れかに記載の装置において、沈殿分離槽を有し、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オーバーフローすることを特徴とする。
【0014】
請求項6に係る発明は、請求項1及至請求項5の何れかに記載の装置において、前記コンポスト装置は、槽内に前記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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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11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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【図面の簡単な説明】
【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。
【図2】排水処理装置の正面方向からの模式図である。
【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。
【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。
【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。
【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。
【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。
【符号の説明】
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
[0001]
BACKGROUND OF THE INVENTION
The present invention introduces raw garbage pulverized with water using a disposer, separates it into a solid content and a liquid content, decomposes the organic matter contained in each by microorganisms, and converts the solid content into compost, The minute relates to a garbage disposal device for obtaining water quality that can be discharged into the sewer.
[0002]
[Prior art]
In recent years, methods for treating organic wastewater using aerobic microorganisms have been actively researched and developed. For example, the activated sludge method is usually employed in sewage treatment plants and the like, and the activated sludge method and the submerged bed method are employed in merged septic tanks.
[0003]
In addition, with regard to garbage discharged from households, etc., research and development has been conducted to treat garbage crushed by a disposer as wastewater containing garbage.
[0004]
For example, in Japanese Patent Laid-Open No. 9-1117, wastewater containing wastewater flows into a solids treatment unit, where the solids are decomposed by microorganisms, and then the primary treated water discharged from the solids treatment device is drained. It is disclosed that by introducing into a treatment tank and performing aeration treatment here, the solid waste is decomposed and removed from the wastewater containing waste ground by a disposer and the wastewater is purified.
[0005]
In the apparatus disclosed in this publication, wastewater is aerated by a diffuser in a wastewater treatment tank, and basically the same treatment as in the activated sludge method is performed.
[0006]
On the other hand, the inventors of the present application use a wastewater treatment device (secondary treatment device) including a packed bed in which a microbial carrier is filled in a subsequent stage of the solid matter treatment device (primary treatment device), thereby It has been found that the purification can be carried out satisfactorily (Japanese Patent Laid-Open No. 11-19664).
[0007]
[Problems to be solved by the invention]
Here, the introduction of the liquid component into the wastewater treatment device in the conventional garbage treatment device is performed by temporarily storing the liquid component separated by the solid-liquid separation device to precipitate and separate the suspended fine particles, and the supernatant liquid is sprinkled through the watering filter bed. It was introduced into the wastewater treatment equipment filled with microorganism carrier. However, this precipitation separation is not sufficient, and in addition to a part of the suspended fine particles being introduced into the wastewater treatment device, the fine particles are aggregated during the transfer of the supernatant liquid, and the aggregated fine particles accumulate in the wastewater treatment device. Occlusion causes a reduction in processing capacity, and it is necessary to remove accumulated substances and replace microbial carriers.
[0008]
This invention is made in view of the said subject, Comprising: A waste-water-treatment apparatus is comprised from a trickling filter part, a fluidized bed part, and a sedimentation separation tank, The microorganisms carrier with which the trickling filter part was filled is made into a fluidized bed part. Circulates between the two, providing a garbage treatment machine that eliminates suspended particulates accumulated in the sprinkling filter bed by self-cleaning, suppresses blockage of the sprinkling filter bed, and allows high-efficiency treatment of drainage to continue for a long period of time. The purpose is to do.
[0009]
[Means for Solving the Problems]
The garbage processing apparatus according to claim 1 includes a flow rate adjusting tank for temporarily storing garbage crushed liquid obtained by pulverizing food waste together with water,
A solid-liquid separator for separating the crushed liquid supplied from the flow rate adjusting tank into a solid component and a liquid component;
A composting device for composting the solids separated by the solid-liquid separation device;
A wastewater treatment apparatus for obtaining treated water by microbial treatment of the liquid component supplied from the solid-liquid separator having a sprinkling filter bed and a fluidized bed ;
In a garbage disposal apparatus comprising:
The sprinkling filter bed is filled with a microbial carrier, and has a communication port between the sprinkling filter bed and the fluidized bed, and the microbial carrier circulates and moves through the communication port. To do.
[0010]
The invention according to claim 2 is characterized in that, in the apparatus according to claim 1, the bottom surface of the sprinkling filter bed has a hole, and the treated water is allowed to pass through to drain.
[0011]
The invention according to claim 3 is the apparatus according to claim 1 or 2, wherein the microbial carrier is a carrier having a specific gravity smaller than that of water and / or having closed cells. And
[0012]
According to a fourth aspect of the present invention, in the apparatus according to any one of the first to third aspects, the lower part of the sprinkling filter bed part and the upper part of the fluidized bed part communicate with each other through the communication port. Features.
[0013]
The invention according to claim 5 is the apparatus according to any one of claims 1 to 4, further comprising a precipitation separation tank, wherein the upper part of the fluidized bed portion and the upper part of the precipitation separation tank are communicated with each other. The liquid component overflows from the fluidized bed to the precipitation separation tank.
[0014]
The invention according to claim 6 is the apparatus according to any one of claims 1 to 5, wherein the composting apparatus is filled with the microorganism carrier in a tank and composts the solid content with microorganisms. It is characterized by that.
[0021]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments according to the present invention will be described with reference to the drawings.
[0022]
FIG. 1 is a diagram showing a configuration of a garbage disposal system 1 according to the present embodiment. The garbage disposal system 1 is a flow rate adjustment tank 2 in which garbage disposed of in a sink is pulverized by a disposer together with water, and the garbage crushing liquid and kitchen drainage are introduced and temporarily stored. Solid-liquid separation device 3 that separates the mixture of garbage and wastewater into a solid component and a liquid component, a wastewater treatment device 4 that biologically removes organic substances in the liquid component separated by the solid-liquid separation device 3, and a solid component It has a solid matter processing device (composting device) 5 for performing composting treatment for a minute.
[0023]
The wastewater containing crushed garbage temporarily stored in the flow rate adjusting tank 2 is pumped up to the solid-liquid separator 3 at regular time intervals. This pumping time interval is determined by the processing capacity of the waste water treatment device 4 at the subsequent stage.
[0024]
In the solid-liquid separator 3, the crushed garbage-containing wastewater pumped up is separated into a solid content such as crushed garbage and sludge and a liquid content of organic wastewater. The separated solid is sent to the composting device 5 and composted. On the other hand, the liquid component is introduced into the waste water treatment device 4 and the organic matter in the liquid component is removed by microbial treatment and then discharged into sewage.
[0025]
Next, FIG. 2 is a schematic diagram for illustrating the configuration of the waste water treatment apparatus 4.
[0026]
The waste water treatment device 4 includes a fluidized bed portion 10, a sprinkling filter bed portion 11, and a precipitation separation tank 12.
[0027]
The organic wastewater, which is the liquid component separated by the solid-liquid separation device 3, is introduced into the fluidized bed 10 of the wastewater treatment device 4, and is carried on the microorganism carrier 13 having a specific gravity smaller than that of water and / or having closed cells. The organic matter in the liquid is decomposed by the microorganisms.
[0028]
A part of the liquid in the fluidized bed 10 is pumped together with the microorganism carrier 13 from near the water surface and introduced into the sprinkling filter bed 11. The flow of the liquid and the carrier is indicated by an arrow 14 in the figure.
[0029]
The liquid component introduced into the sprinkling filter bed 11 is subjected to microbial treatment by contacting the microbial carrier 13 filled in the sprinkling filter bed 11 and processed from the holes 15 formed in the bottom surface of the sprinkling filter bed 11. It is discharged as water 16. On the other hand, the microbial carrier 13 introduced into the trickling filter bed 11 is filled on the microbial carrier 13 filled in the trickling filter bed 11. At this time, since the bottom surface of the water trickling filter part 11 is inclined toward the fluidized bed part 10, the microorganism carrier 13 filled in the water trickling filter part 11 is provided below the water trickling filter part 11. It is pushed out to the fluidized bed 10 through the communication port 17. Therefore, the microbial carrier 13 always circulates between the fluidized bed 10 and the sprinkling filter bed 11.
[0030]
A roller 30 as shown in FIG. 3 may be provided at the communication port 17 so that the microorganism carrier 13 can be easily moved.
[0031]
As another form, a motor 31 and a belt 32 as shown in FIG. 4 may be installed, and the driving force of the motor 31 may be moved via the connecting belt 33 and the pulley 34.
[0032]
Furthermore, as shown in FIG. 5, a bypass 35 connecting the fluidized bed portion 10 and the communication port 17 is installed, and a water flow is made from the communication port 17 toward the fluidized bed portion 10 via the pump 36. And the microbial carrier 13 may be moved by the water pressure.
[0033]
Furthermore, as shown in FIG. 6, a microorganism carrier circulation pipe 37 may be installed, and the microorganism carrier 13 that is freely moved therein may be forcibly circulated by an underwater pump 38. In this case, by opening the small holes 39, 39,... In the microorganism carrier circulation pipe 37, the liquid content of the fluidized bed portion 10 can be pumped together with the microorganism carrier 13 into the sprinkling filter bed portion 11.
[0034]
The upper part of the fluidized bed part 10 and the sedimentation separation tank 12 communicate with each other, the liquid content in the fluidized bed part 10 overflows and flows into the sedimentation separation tank 12, and the suspended fine particles in the liquid content are allowed to settle in a stationary state. 18 is formed. The sedimentation layer 18 of fine particles accumulated by sedimentation is conveyed to the composting device 5 as return sludge 19 and composted.
[0035]
The water surface 20 of the liquid portion of the fluidized bed 10 is lower than the lowermost hole 15 opened in the bottom surface of the sprinkling filter bed 11 and higher than the partition with the sedimentation separation tank 12, and is retained. The above operation becomes possible.
[0036]
As a result, the sludge accumulated on the upper surface only by the conventional trickling filter system is circulated together with the microorganism carrier 13 in the present invention. Maintenance is reduced. At the same time, it is possible to operate with a high processing capacity for a long time.
[0037]
Here, the form which further processes the water processed by the sprinkling filter floor part 11 in FIG. 7 is shown.
[0038]
In the case where the water treatment capacity is low only with the sprinkling filter bed 11, the sprinkling filter bed 11 is used only for the purpose of draining the microorganism carrier 13 and removing the accumulated sludge. The tank 21 may be provided independently.
[0039]
【The invention's effect】
As described above, the present invention comprises a wastewater treatment apparatus comprising a fluidized bed part, a sprinkling filter bed part, and a sedimentation separation tank, and circulating a microorganism carrier between the sprinkling filter bed part and the fluidized bed part. In addition, it is possible to suppress the clogging by the accumulated sludge in the sprinkling filter floor and to efficiently treat the organic wastewater in the wastewater treatment apparatus over a long period of time.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram from the front of a garbage disposal apparatus according to an embodiment of the present invention.
FIG. 2 is a schematic view from the front direction of the waste water treatment apparatus.
FIG. 3 is a schematic view from the front showing another embodiment of the communication port.
FIG. 4 is a schematic view from the front showing another embodiment of the communication port.
FIG. 5 is a schematic view from the front showing another embodiment of the communication port.
FIG. 6 is a schematic view from the front showing another embodiment of the communication port.
FIG. 7 is a schematic view from the front showing another embodiment of the waste water treatment apparatus.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Raw garbage processing apparatus 2 ... Flow rate adjustment tank 3 ... Solid-liquid separation apparatus 4 ... Waste water treatment apparatus 5 ... Composting apparatus 10 ... Fluidized bed part 11 ... Sprinkling filter bed part 12 ... Precipitation separation tank 13 ... Microorganism carrier 14 ... Liquid content And microbial carrier flow 15 ... drainage hole 16 on the bottom of the sprinkling filter bed ... treated water 17 ... communication port 18 connecting the sprinkling filter bed and fluidized bed ... sedimentary bed 19 of suspended particulates ... return sludge 20 ... liquid spill surface 21 ... Waste water treatment tank 30 ... Roller 31 ... Motor 32 ... Belt 33 ... Connection belt 34 ... Pulley 35 ... Bypass 36 ... Pump 37 ... Microorganism carrier circulation pipe 38 ... Submersible pump 39 ... Small hole

Claims (6)

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、
散水ろ床部と流動床部とを有し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、
を備える生ごみ処理装置において、
前記散水ろ床部には微生物担体が充填され、且つ前記散水ろ床部と前記流動床部の間には連通口を有し前記微生物担体は前記連通口を通って循環移動することを特徴とする生ごみ処理装置。
A flow rate adjusting tank for temporarily storing garbage crushed liquid obtained by pulverizing food waste together with water;
A solid-liquid separator for separating the crushed liquid supplied from the flow rate adjusting tank into a solid component and a liquid component;
A composting device for composting the solids separated by the solid-liquid separation device;
A wastewater treatment apparatus for obtaining treated water by microbial treatment of the liquid component supplied from the solid-liquid separator having a sprinkling filter bed and a fluidized bed ;
In a garbage disposal apparatus comprising:
The sprinkling filter bed is filled with a microbial carrier, and has a communication port between the sprinkling filter bed and the fluidized bed, and the microbial carrier circulates and moves through the communication port. Garbage disposal device.
請求項1に記載の装置において、前記散水ろ床部の底面には孔を有し、前記処理水を通過させて排水することを特徴とする生ごみ処理装置。2. The garbage processing apparatus according to claim 1, wherein a bottom surface of the sprinkling filter bed has a hole, and the treated water is allowed to pass through to drain. 請求項1又は請求項2の何れかに記載の装置において、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生ごみ処理装置。3. The garbage processing apparatus according to claim 1, wherein the microbial carrier is a carrier having a specific gravity smaller than that of water and / or having closed cells. 請求項1及至請求項3の何れか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前記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。4. The garbage processing apparatus according to claim 1, wherein a lower part of the sprinkling filter bed part and an upper part of the fluidized bed part communicate with each other through the communication port. 請求項1及至請求項4の何れかに記載の装置において、沈殿分離槽を有し、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オーバーフローすることを特徴とする生ごみ処理装置。5. The apparatus according to claim 1, further comprising a sedimentation separation tank, wherein the upper part of the fluidized bed portion and the upper part of the precipitation separation tank are in communication with each other, and the liquid component is contained in the fluidized bed. A garbage disposal apparatus overflows from the section into the precipitation separation tank. 請求項1及至請求項5の何れかに記載の装置において、前記コンポスト装置は、槽内に前記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生ごみ処理装置。The apparatus according to any one of claims 1 to 5, wherein the composting apparatus is filled with the microorganism carrier in a tank, and the solid content is composted by microorganisms. apparatus.
JP2000019475A 2000-01-28 2000-01-28 Garbage disposal equipment Expired - Fee Related JP3877482B2 (en)

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