JP2005131555A - Garbage treatment system - Google Patents

Garbage treatment system Download PDF

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JP2005131555A
JP2005131555A JP2003371075A JP2003371075A JP2005131555A JP 2005131555 A JP2005131555 A JP 2005131555A JP 2003371075 A JP2003371075 A JP 2003371075A JP 2003371075 A JP2003371075 A JP 2003371075A JP 2005131555 A JP2005131555 A JP 2005131555A
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garbage
tank
solid
aerobic
liquid separation
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Katsunori Aoki
勝則 青木
Takeshi Suzuki
鈴木  剛
Kazuhito Suzuki
和仁 鈴木
Kazuya Oguri
和也 小栗
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Energy Support Corp
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Energy Support Corp
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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
    • 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
    • Y02W10/20Sludge processing

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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a garbage treatment system wherein the size of a treatment vessel for treating object water such as general kitchen wastewater, garbage wastewater containing shredded garbage can be reduced. <P>SOLUTION: The treatment vessel 22 is partitioned by a first partition wall 23 and a second partition wall 24 into an aerobic decomposition vessel 25, a solid-liquid separation vessel 26 and an aerobic treatment vessel 27. The solid-liquid separation vessel 26 is further partitioned by a third partition wall 28 into a wastewater inflow chamber 29 and a solid-liquid separation chamber 30. The third partition wall 28 is provided with a first communication port 32 for allowing the wastewater inflow chamber 29 and the solid-liquid separation chamber 30 to communicate with each other in their bottoms. The first partition wall 23 is provided with a second communication port 33 for allowing the aerobic decomposition vessel 25 and the solid-liquid separation chamber 30 to communicate with each other in their bottoms. A first overflow section 34 for transferring a garbage suspension in the wastewater inflow chamber 29 to the aerobic decomposition vessel 25 is formed in the upper part of the first partition wall 23. A second overflow section 35 for transferring the garbage suspension in the solid-liquid separation chamber 30 to the aerobic treatment vessel 27 is formed in the upper part of the second partition wall 24. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、破砕機により破砕された生ゴミ破砕物を含む生ゴミ排水を浄化処理する生ゴミ処理システムに関するものである。   The present invention relates to a garbage disposal system for purifying garbage wastewater containing garbage fragments crushed by a crusher.

生ゴミ破砕機を利用する家庭用生ゴミ処理システムとしては、例えば特許文献1に示される構成が知られている。この生ゴミ処理システムは分離装置、前処理槽、嫌気槽、好気槽及び処理水槽を備えている。分離装置は生ゴミ破砕機により破砕された生ごみの固形物懸濁液を固液分離する。前処理槽は前記分離装置によって分離された固形物が移流される第1の室(下室)及び前記分離装置を通過する懸濁物液が移流される第2の室(上室)とをさらに備えている。固形物懸濁液は分離装置により固液分離(固形物と懸濁物液に分離)される。固形物は前処理槽の第1の室に移流して槽底部へ沈降し、懸濁物液は前処理槽の第2の室に移流する。固形物懸濁液中の固形物は第1の室において可溶化される。第1の室により処理された処理水は嫌気槽へ移流され、処理水中の有機物は嫌気槽内の微生物付着体に付着した嫌気性微生物により分解処理される。嫌気槽により処理された処理水は好気槽内へ移流し、当該好気槽内へ移流した処理水中の有機物は好気槽内の微生物付着体に付着した好気性微生物により好気分解処理される。好気槽において処理された処理済み水は処理水槽に移流する。処理水槽内の処理済み水の一部は前処理槽へ戻されると共に残りの処理済み水は装置外に排出される。   As a household garbage processing system using a garbage crusher, for example, a configuration shown in Patent Document 1 is known. This garbage disposal system includes a separation device, a pretreatment tank, an anaerobic tank, an aerobic tank, and a treated water tank. The separation device performs solid-liquid separation on the solid suspension of food waste crushed by a garbage crusher. The pretreatment tank includes a first chamber (lower chamber) in which the solid separated by the separation device is transferred and a second chamber (upper chamber) in which the suspension liquid passing through the separation device is transferred. It has more. The solid suspension is subjected to solid-liquid separation (separated into solid and suspension liquid) by a separation device. The solid is transferred to the first chamber of the pretreatment tank and settled to the bottom of the tank, and the suspension liquid is transferred to the second chamber of the pretreatment tank. Solids in the solid suspension are solubilized in the first chamber. The treated water treated by the first chamber is transferred to the anaerobic tank, and the organic matter in the treated water is decomposed by the anaerobic microorganisms attached to the microbial adherent in the anaerobic tank. The treated water treated in the anaerobic tank is transferred to the aerobic tank, and the organic matter in the treated water transferred to the aerobic tank is aerobically decomposed by the aerobic microorganisms attached to the microbial adherent in the aerobic tank. The The treated water treated in the aerobic tank is transferred to the treated water tank. A portion of the treated water in the treated water tank is returned to the pretreatment tank and the remaining treated water is discharged out of the apparatus.

また、特許文献2に示されるような生ゴミ処理システムも知られている。この生ゴミ処理システムは、厨芥排水に含まれる固形物中の無機性固形物を分離する沈砂槽、無機性固形物が除去された厨芥排水を処理する好気性消化槽、好気性消化槽中の内部液を濃縮された有機性固形物・汚泥と分離排水とに分離する沈殿槽及び沈殿槽により分離された分離排水を好気的生物処理するための排水処理槽を備えている。排水処理槽で処理された処理水は槽外に放流される。
特開2000−271594号公報 特開2000−279989号公報
A garbage disposal system as shown in Patent Document 2 is also known. This garbage disposal system includes a sand settling tank that separates inorganic solids in solids contained in dredged wastewater, an aerobic digester that treats dredged wastewater from which inorganic solids have been removed, and an aerobic digester A sedimentation tank for separating the internal liquid into concentrated organic solids / sludge and separated wastewater, and a wastewater treatment tank for aerobic biological treatment of the separated wastewater separated by the sedimentation tank are provided. The treated water treated in the wastewater treatment tank is discharged outside the tank.
JP 2000-271594 A JP 2000-279899 A

ところが、特許文献1に記載の生ゴミ処理システムにおいては、前処理槽の前段に分離装置を配置することにより固形物懸濁液中の固形物の好気槽への流れ込みを阻止するようにしている。しかし、分離装置を通り抜けた固形物懸濁液中の浮遊物は前処理槽へ流れ込み、前処理槽へ流れ込んだ浮遊物が好気槽へ流れ込むおそれがある。このような場合には好気処理性能が低下してしまう。このため、前記浮遊物が好気槽へ流れ込むことを防止するために当該好気槽の前段には前記浮遊物を可溶化する嫌気槽を設ける必要があった。嫌気槽の処理能力を確保するために当該嫌気槽の容積は一定以上確保する必要があるので、当該嫌気槽の小型化、ひいては生ゴミ処理システム全体の小型化には限界があった。   However, in the garbage processing system described in Patent Document 1, by disposing a separation device in the previous stage of the pretreatment tank, the solid matter in the solid suspension is prevented from flowing into the aerobic tank. Yes. However, the suspended matter in the solid suspension that has passed through the separator flows into the pretreatment tank, and the suspended matter that has flowed into the pretreatment tank may flow into the aerobic tank. In such a case, the aerobic processing performance deteriorates. For this reason, in order to prevent the floating substance from flowing into the aerobic tank, it is necessary to provide an anaerobic tank for solubilizing the floating substance in the previous stage of the aerobic tank. In order to secure the processing capacity of the anaerobic tank, the volume of the anaerobic tank needs to be secured above a certain level. Therefore, there is a limit to downsizing the anaerobic tank, and thus downsizing the whole garbage disposal system.

また、特許文献2に記載の生ゴミ処理システムにおいては、沈殿槽の容量以上の厨芥排水(被処理水)が沈砂槽に流入した場合、好気性消化槽の汚泥を含む内部水が沈殿槽から溢れて排水処理槽に流入流出することとなる。従って、処理能力を確保するために沈殿槽の容積を一定以上確保する必要があり小型化には限界があった。   Moreover, in the garbage processing system of patent document 2, when dredging waste water (treated water) more than the capacity of a sedimentation tank flows into a sand settling tank, the internal water containing the sludge of an aerobic digestion tank is from a sedimentation tank. It overflows and flows into the wastewater treatment tank. Therefore, it is necessary to secure a certain volume of the settling tank in order to ensure the processing capacity, and there is a limit to downsizing.

本発明は前記問題点を解決するためになされたものであって、その目的は、破砕された生ゴミを含んだ生ゴミ排水及び一般台所排水等の被処理水を処理する処理槽の小型化が図られる生ゴミ処理システムを提供することにある。   The present invention has been made to solve the above-mentioned problems, and its purpose is to reduce the size of a treatment tank that treats water to be treated such as garbage wastewater containing crushed garbage and general kitchen wastewater. Is to provide a garbage disposal system.

請求項1に記載の発明は、破砕機により破砕された生ゴミ破砕物を含む生ゴミ排水を浄化処理する処理槽を備えた生ゴミ処理システムにおいて、前記処理槽は、移送手段により移流されてきた生ゴミ排水を固形分である生ゴミ破砕物と液体分である生ゴミ懸濁液とに分離する固液分離槽と、前記固液分離槽の前段に配置されると共に当該固液分離槽により分離された生ゴミ破砕物が移流され当該生ゴミ破砕物を可溶化処理する好気分解槽と、前記固液分離槽の後段に配置されると共に当該固液分離槽の生ゴミ懸濁液及び前記好気分解槽における可溶化処理済みの生ゴミ懸濁液のみが移流され両生ゴミ懸濁液をそれぞれ好気処理する好気処理槽とを備えたことを要旨とする。   The invention described in claim 1 is a garbage processing system including a treatment tank for purifying garbage wastewater containing garbage crushed material crushed by a crusher, wherein the treatment tank is transferred by a transfer means. A solid-liquid separation tank that separates the garbage waste water into a crushed garbage that is a solid content and a garbage suspension that is a liquid content, and the solid-liquid separation tank that is disposed in front of the solid-liquid separation tank The aerobic decomposition tank in which the crushed garbage separated by the above is transferred to solubilize the crushed garbage, and the garbage suspension disposed in the subsequent stage of the solid-liquid separation tank And an aerobic treatment tank in which only the solubilized garbage suspension in the aerobic decomposition tank is transferred to each aerobic treatment of both the garbage suspensions.

請求項2に記載の発明は、請求項1に記載の発明において、前記処理槽は第1隔壁及び第2隔壁により好気分解槽、固液分離槽及び好気処理槽に区画し、前記固液分離槽は浮遊破砕物移流防止壁により前記移送手段からの生ゴミ排水が移流される排水流入室と前記固液分離槽内の生ゴミ懸濁液及び前記好気分解槽における可溶化処理済みの生ゴミ懸濁液が移流される固液分離室とにさらに区画し、前記浮遊破砕物移流防止壁には排水流入室と固液分離室とをそれらの底部において連通する第1連通口を設け、前記第1隔壁には固液分離室と好気分解槽とをそれらの底部において連通する第2連通口を設けると共に当該第1隔壁の上部には生ゴミ排水の流入に伴う排水流入室のオーバーフロー分の生ゴミ懸濁液を前記好気分解槽へ移流可能とした第1オーバーフロー部を設け、前記第2隔壁の上部には生ゴミ排水の流入に伴う固液分離室のオーバーフロー分の生ゴミ懸濁液を好気処理槽へ移流可能とした第2オーバーフロー部を設けるようにしたことを要旨とする。   The invention according to claim 2 is the invention according to claim 1, wherein the treatment tank is divided into an aerobic decomposition tank, a solid-liquid separation tank and an aerobic treatment tank by a first partition and a second partition. The liquid separation tank is a solubilized treatment in the wastewater inflow chamber in which the garbage wastewater from the transfer means is transferred by the floating crushed material advancing prevention wall, the garbage suspension in the solid-liquid separation tank, and the aerobic decomposition tank And a solid-liquid separation chamber to which the raw garbage suspension is transferred, and the floating crushed material advection prevention wall has a first communication port for communicating the drainage inflow chamber and the solid-liquid separation chamber at their bottoms. The first partition is provided with a second communication port that communicates the solid-liquid separation chamber and the aerobic decomposition tank at the bottom thereof, and the drainage inflow chamber accompanying the inflow of garbage wastewater is provided above the first partition. It is possible to transfer the raw garbage suspension for the overflow to the aerobic decomposition tank A first overflow section is provided, and a second overflow section is provided above the second partition wall, which allows the overflow of the garbage waste in the solid-liquid separation chamber accompanying the inflow of garbage wastewater to be transferred to the aerobic treatment tank. The gist is that it is provided.

(作用)
請求項1に記載の発明によれば、移送手段により移流されてきた生ゴミ排水は固液分離槽により生ゴミ破砕物と生ゴミ懸濁液とに分離される。固液分離槽により分離された生ゴミ破砕物(固液分離槽内において沈降する沈降破砕物及び同じく水面に浮遊する浮遊破砕物を含む)は当該固液分離槽の前段に配置された好気分解槽へのみ移流し、当該好気分解槽において可溶化処理される。固液分離槽により分離された生ゴミ破砕物が後段の好気処理槽へ移流することはない。また、固液分離槽の生ゴミ懸濁液及び前記好気分解槽から移流されてきた可溶化処理済みの生ゴミ懸濁液は固液分離槽の後段に配置された好気処理槽へ移流され、当該好気処理槽において好気処理される。
(Function)
According to the first aspect of the present invention, the garbage wastewater transferred by the transfer means is separated into the garbage crushed material and the garbage suspension by the solid-liquid separation tank. Garbage crushed material separated by the solid-liquid separation tank (including sedimentation crushed material that settles in the solid-liquid separation tank and floating crushed material that floats on the water surface) is aerobic arranged in front of the solid-liquid separation tank Advection only to the decomposition tank, solubilized in the aerobic decomposition tank. Garbage crushed material separated by the solid-liquid separation tank is not transferred to the aerobic treatment tank in the subsequent stage. The solid waste separation tank garbage suspension and the solubilized garbage suspension transferred from the aerobic decomposition tank are transferred to the aerobic treatment tank disposed at the subsequent stage of the solid liquid separation tank. Then, the aerobic treatment is performed in the aerobic treatment tank.

生ゴミ排水は好気分解槽において生ゴミ破砕物と生ゴミ懸濁液とに分離されるので、生ゴミ排水を処理槽に流し込む前に生ゴミ排水を生ゴミ破砕物と生ゴミ懸濁液とに分離する分離装置を処理槽の前段に別途設ける必要はない。また、生ゴミ破砕物は好気分解槽へのみ移流して好気処理槽へ移流することはないので、好気処理槽の処理性能を低下させる生ゴミ破砕物を当該好気処理槽の前段で前処理する必要がない。従って、生ゴミ破砕物を嫌気処理するための嫌気分解槽を好気処理槽の前段に設ける必要がない。このため、好気処理槽への未処理生ゴミ破砕物の流入を防止するために好気処理槽の前段に嫌気分解槽を設けるようにした場合に比べて、処理槽の小型化が図られる。   Since garbage wastewater is separated into garbage crushed material and garbage suspension in the aerobic decomposition tank, garbage wastewater is separated into garbage crushed material and garbage suspension before pouring the garbage wastewater into the treatment tank. It is not necessary to separately provide a separation device for separating the two in front of the treatment tank. In addition, since the garbage crushed material is transferred only to the aerobic decomposition tank and is not transferred to the aerobic treatment tank, the garbage crushed material that degrades the processing performance of the aerobic treatment tank is removed from the preceding stage of the aerobic treatment tank. There is no need to pre-process. Therefore, it is not necessary to provide an anaerobic decomposition tank for anaerobically treating the garbage crushed material in the front stage of the aerobic treatment tank. For this reason, compared with the case where an anaerobic decomposition tank is provided in the front | former stage of an aerobic treatment tank in order to prevent the inflow of the untreated garbage crushed material to an aerobic treatment tank, size reduction of a treatment tank is achieved. .

請求項2に記載の発明によれば、請求項1に記載の発明の作用に加えて、前記移送手段からの生ゴミ排水は排水流入室に移流される。排水流入室の生ゴミ懸濁液は第1連通口を介して固液分離室内に移流する。排水流入室の生ゴミ破砕物のうち沈降破砕物は第2連通口を介して好気分解槽内へ移流する。排水流入室において、生ゴミ排水の流入に伴うオーバーフロー分の生ゴミ懸濁液は生ゴミ破砕物のうちの浮遊破砕物と共に第1オーバーフロー部を介して好気分解槽へ移流する。好気分解槽における可溶化処理済みの生ゴミ懸濁液は第2連通口を介して固液分離室内へ移流する。生ゴミ排水の排水流入室への流入に伴って、固液分離室内の生ゴミ懸濁液は第2オーバーフロー部を介して好気処理槽へ移流する。排水流入室内において、水面に浮遊している浮遊破砕物の固液分離室への移流は浮遊破砕物移流防止壁により規制される。この結果、生ゴミ破砕物と生ゴミ懸濁液とはより確実に分離される。   According to invention of Claim 2, in addition to the effect | action of invention of Claim 1, the garbage wastewater from the said transfer means is transferred to a waste_water | drain inflow chamber. The garbage suspension in the drainage inflow chamber is transferred to the solid-liquid separation chamber through the first communication port. Of the crushed garbage in the waste water inflow chamber, the crushed sediment is transferred into the aerobic decomposition tank through the second communication port. In the wastewater inflow chamber, the overflowed garbage suspension resulting from the inflow of the garbage wastewater is transferred to the aerobic decomposition tank through the first overflow section together with the suspended crushed material among the crushed garbage. The solubilized garbage suspension in the aerobic decomposition tank is transferred to the solid-liquid separation chamber through the second communication port. As the garbage wastewater flows into the wastewater inflow chamber, the garbage suspension in the solid-liquid separation chamber is transferred to the aerobic treatment tank through the second overflow portion. In the drainage inflow chamber, the advection of floating crushed material floating on the water surface to the solid-liquid separation chamber is regulated by the floating crushed material advection prevention wall. As a result, the crushed garbage and the garbage suspension are more reliably separated.

本発明によれば、破砕された生ゴミを含んだ生ゴミ排水及び一般台所排水等の被処理水を処理する処理槽の小型化が図られる。   ADVANTAGE OF THE INVENTION According to this invention, size reduction of the processing tank which processes to-be-processed water, such as garbage wastewater containing the crushed garbage and general kitchen wastewater, is achieved.

以下、本発明を生ゴミ処理システムに具体化した一実施形態を図1に従って説明する。
(生ゴミ処理システム全体の構造)
図1に示すように、生ゴミ処理システム11は、キッチンシンクの底部に設けられた破砕機12及び屋外に設置された地上設置式の処理装置13を備えている。破砕機12と処理装置13とは移送管14を介して相互に接続されている。破砕機12により破砕された生ゴミ破砕物を含んだ排水(以下、「生ゴミ排水」という。)は移送管14を介して処理装置13内へ移送される。
Hereinafter, an embodiment in which the present invention is embodied in a garbage disposal system will be described with reference to FIG.
(Structure of the whole garbage disposal system)
As shown in FIG. 1, the garbage processing system 11 includes a crusher 12 provided at the bottom of a kitchen sink and a ground-mounted processing device 13 installed outdoors. The crusher 12 and the processing device 13 are connected to each other via a transfer pipe 14. Wastewater containing crushed garbage (hereinafter referred to as “garbage wastewater”) crushed by the crusher 12 is transferred into the processing device 13 through the transfer pipe 14.

(処理槽)
図1に示すように、処理装置13のケーシング21内には処理槽22が配置されている。処理槽22内は第1隔壁23及び第2隔壁24により好気分解槽25、固液分離槽26及び好気処理槽27の3つの槽に区画されている。固液分離槽26は浮遊破砕物移流防止壁としての第3隔壁28により排水流入室29及び固液分離室30の2つの室にさらに区画されている。排水流入室29の上方には移送管14の出口が配置されており、該移送管14からの生ゴミ排水は排水流入室29に流入可能となっている。
(Treatment tank)
As shown in FIG. 1, a processing tank 22 is disposed in the casing 21 of the processing apparatus 13. The inside of the processing tank 22 is divided into three tanks of an aerobic decomposition tank 25, a solid-liquid separation tank 26 and an aerobic processing tank 27 by the first partition wall 23 and the second partition wall 24. The solid-liquid separation tank 26 is further divided into two chambers, a drainage inflow chamber 29 and a solid-liquid separation chamber 30, by a third partition wall 28 as a floating crushed material advancing prevention wall. An outlet of the transfer pipe 14 is disposed above the drainage inflow chamber 29, and garbage wastewater from the transfer pipe 14 can flow into the drainage inflow chamber 29.

第1隔壁23の下部は第2隔壁24側(好気処理槽27側)に傾斜しており固液分離槽26の底壁31を構成している。底壁31と第3隔壁28の下端縁との間には排水流入室29と固液分離室30とを連通する第1連通口32が形成されている。また、底壁31の下端縁と第2隔壁24との間には好気分解槽25と固液分離槽26とを連通する第2連通口33が形成されている。   The lower part of the first partition wall 23 is inclined toward the second partition wall 24 side (aerobic treatment tank 27 side) and constitutes the bottom wall 31 of the solid-liquid separation tank 26. Between the bottom wall 31 and the lower end edge of the third partition wall 28, a first communication port 32 that connects the drainage inflow chamber 29 and the solid-liquid separation chamber 30 is formed. A second communication port 33 is formed between the lower edge of the bottom wall 31 and the second partition wall 24 to communicate the aerobic decomposition tank 25 and the solid-liquid separation tank 26.

第1隔壁23の上部には第1オーバーフロー部34が形成されている。生ゴミ排水の排水流入室29への流入時において、排水流入室29内のオーバーフロー分の生ゴミ排水は第1オーバーフロー部34を介して好気分解槽25内に流入可能とされている。第2隔壁24の上部には第2オーバーフロー部35が形成されている。排水流入室29内の生ゴミ排水が第1連通口32を介して固液分離室30へ流入する際において、当該固液分離室30内のオーバーフロー分の生ゴミ排水は第2オーバーフロー部35を介して好気処理槽27内に流入可能とされている。処理槽22において、好気処理槽27に面する側壁(即ち、処理槽22の第2隔壁24に対向する側壁)の上部には流出口36が形成されている。好気処理槽27のオーバーフロー分の生ゴミ排水は流出口36を介してケーシング21の外部に流出可能とされている。   A first overflow portion 34 is formed on the first partition wall 23. When the garbage wastewater flows into the drainage inflow chamber 29, the overflow garbage wastewater in the drainage inflow chamber 29 can flow into the aerobic decomposition tank 25 via the first overflow portion 34. A second overflow portion 35 is formed on the second partition wall 24. When the garbage wastewater in the drainage inflow chamber 29 flows into the solid-liquid separation chamber 30 through the first communication port 32, the overflowing garbage wastewater in the solid-liquid separation chamber 30 passes through the second overflow part 35. Through the aerobic treatment tank 27. In the processing tank 22, an outflow port 36 is formed on an upper portion of a side wall facing the aerobic processing tank 27 (that is, a side wall facing the second partition wall 24 of the processing tank 22). Garbage waste water for the overflow of the aerobic treatment tank 27 can flow out of the casing 21 through the outlet 36.

(固液分離槽)
固液分離槽26は移送管14から移送されてきた生ゴミ排水に含まれる固形分(生ゴミ破砕物)と液体分(生ゴミ懸濁液)とを分離する。排水流入室29は、移送管14から流入してきた生ゴミ排水の沈殿処理を行う。生ゴミ破砕物のうち沈降破砕物は排水流入室29内を沈降し、底壁31に案内されながら第1連通口32を通過し、さらに第2連通口33を介して好気分解槽25内に移流可能となっている。生ゴミ破砕物のうち排水流入室29の水面に浮遊する浮遊破砕物は、当該排水流入室29のオーバーフロー分の生ゴミ懸濁液と共に第1オーバーフロー部34を介して好気分解槽25内に移流可能となっている。排水流入室29内で固液分離された生ゴミ懸濁液は第1連通口32を介して固液分離室30内に移流可能となっている。
(Solid-liquid separation tank)
The solid-liquid separation tank 26 separates solids (garbage crushed material) and liquids (garbage suspension) contained in the garbage wastewater transferred from the transfer pipe 14. The drainage inflow chamber 29 performs sedimentation treatment of the garbage wastewater that has flowed in from the transfer pipe 14. Of the crushed garbage, the crushed sediment settles in the drainage inflow chamber 29, passes through the first communication port 32 while being guided by the bottom wall 31, and further passes through the second communication port 33 to enter the aerobic decomposition tank 25. Advection is possible. Among the crushed garbage, the floating crushed material floating on the water surface of the drainage inflow chamber 29 enters the aerobic decomposition tank 25 through the first overflow portion 34 together with the overflowed garbage suspension in the drainage inflow chamber 29. Advection is possible. The garbage suspension that has been solid-liquid separated in the drainage inflow chamber 29 can be transferred into the solid-liquid separation chamber 30 via the first communication port 32.

(好気分解槽)
好気分解槽25は排水流入室29から第1オーバーフロー部34を介して流入してきた生ゴミ排水のうちの浮遊物及び第2連通口33を介して好気分解槽25内に移流してきた固形物を好気分解処理して可溶化する。好気分解槽25内において、底壁31の下方には好気分解用散気手段としての散気管41が配置されている。散気管41には連結管42を介してブロワ43が接続されており、このブロワ43の駆動により好気分解槽25内には空気(酸素)が連結管42及び散気管41の各空気噴出口を介して供給される。散気管41からの気泡が底壁31に下方から接触するように散気管41の配置位置(空気噴出方向)は設定されている。
(Aerobic decomposition tank)
The aerobic decomposition tank 25 is a solid that has been transferred to the aerobic decomposition tank 25 via the floating substance in the garbage wastewater flowing in from the drainage inflow chamber 29 via the first overflow portion 34 and the second communication port 33. The product is solubilized by aerobic decomposition. In the aerobic decomposition tank 25, an aeration tube 41 is disposed below the bottom wall 31 as aerobic decomposition aeration means. A blower 43 is connected to the diffuser pipe 41 via a connecting pipe 42, and air (oxygen) flows into the aerobic decomposition tank 25 by driving the blower 43, and the air outlets of the connecting pipe 42 and the diffuser pipe 41. Is supplied through. The arrangement position (air ejection direction) of the air diffuser 41 is set so that the air bubbles from the air diffuser 41 contact the bottom wall 31 from below.

(好気処理槽)
好気処理槽27は固液分離室30から流入してきた生ゴミ懸濁液及び好気分解槽25で可溶化処理された生ゴミ懸濁液を、さらに好気処理する。好気処理槽27内において、処理槽22の好気処理槽27に面する一側壁(第2隔壁24と対向する側壁)の上部には、上部が開口した箱体状のフィルタ支持部材51が着脱可能に設けられている。フィルタ支持部材51は好気処理槽27の流出口36を内側から覆うようにして設けられている。フィルタ支持部材51の底壁51aは処理槽22(好気処理槽27)の内底面に対して所定角度をなすように傾斜している。底壁51aには単数又は複数の所定の目開きを有する網目状のフィルタ52が設けられている。フィルタ支持部材51の下部から中間部にわたって好気処理槽27内の生ゴミ排水に漬かる(水没状態)ように、当該フィルタ支持部材51の取付け位置が設定されている。
(Aerobic treatment tank)
The aerobic treatment tank 27 further aerobically treats the garbage suspension flowing in from the solid-liquid separation chamber 30 and the garbage suspension solubilized in the aerobic decomposition tank 25. In the aerobic treatment tank 27, a box-like filter support member 51 having an upper opening is formed on the upper part of one side wall (side wall facing the second partition wall 24) of the treatment tank 22 facing the aerobic treatment tank 27. It is detachable. The filter support member 51 is provided so as to cover the outflow port 36 of the aerobic treatment tank 27 from the inside. The bottom wall 51a of the filter support member 51 is inclined so as to form a predetermined angle with respect to the inner bottom surface of the processing tank 22 (aerobic processing tank 27). A mesh-like filter 52 having a single or a plurality of predetermined openings is provided on the bottom wall 51a. The attachment position of the filter support member 51 is set so that the filter support member 51 is immersed in the waste water in the aerobic treatment tank 27 from the lower part to the intermediate part (submerged state).

フィルタ支持部材51の底壁51aの下方、即ちフィルタ52の下方には好気処理用散気手段としての散気管61が配置されている。散気管61には連結管62を介してブロワ43が接続されており、このブロワ43の駆動により好気処理槽27内には空気(酸素)が連結管62及び散気管61の各空気噴出口を介して供給される。散気管61からの気泡がフィルタ52に下方から接触するように散気管61の配置位置(空気噴出方向)は設定されている。   A diffuser pipe 61 is disposed below the bottom wall 51 a of the filter support member 51, that is, below the filter 52, as an aerobic treatment diffuser. A blower 43 is connected to the diffuser pipe 61 via a connecting pipe 62, and air (oxygen) flows into the aerobic treatment tank 27 by driving of the blower 43, and the air outlets of the connecting pipe 62 and the diffuser pipe 61. Is supplied through. The arrangement position (air ejection direction) of the air diffuser 61 is set so that the bubbles from the air diffuser 61 come into contact with the filter 52 from below.

好気処理槽27に貯留された生ゴミ懸濁液中には好気性微生物を着床させる複数の担体71が投入され、浮遊している。即ち、好気処理槽27は複数の担体71を浮遊させる流動床となっている。各担体71は多孔質のPVA(ポリビニルアルコール)ゲルにより直径5mm程度の球状(断面円形だけでなく断面楕円形も含む)に形成されている。PVAゲルの表面には細かい凹凸があり、好気性微生物の初期付着性に優れている。また、PVAゲルの内部には表面から無数の細かい孔が連通しており、好気性微生物が侵入及び定着しやすい構造となっている。このため、好気処理槽27内の菌体濃度(好気性微生物の濃度)が高められる。   In the garbage suspension stored in the aerobic treatment tank 27, a plurality of carriers 71 for depositing aerobic microorganisms are charged and floated. That is, the aerobic treatment tank 27 is a fluidized bed in which a plurality of carriers 71 are suspended. Each carrier 71 is formed in a spherical shape (including not only a circular cross section but also an elliptical cross section) with a diameter of about 5 mm by porous PVA (polyvinyl alcohol) gel. The surface of the PVA gel has fine irregularities and is excellent in initial adhesion of aerobic microorganisms. In addition, innumerable fine pores communicate with the inside of the PVA gel from the surface, and a structure in which aerobic microorganisms are easy to enter and settle. For this reason, the bacterial cell concentration (concentration of aerobic microorganisms) in the aerobic treatment tank 27 is increased.

(実施形態の作用)
次に、前述のように構成した生ゴミ処理システムの作用について説明する。キッチンシンクの排水口からキッチン排水(一般台所排水)とともに投下された生ゴミは破砕機12により所定の大きさに破砕される。破砕機12により破砕された生ゴミ破砕物を含んだ生ゴミ排水(被処理水)は移送管14を介して固液分離槽26の排水流入室29内へ移送される。
(Operation of the embodiment)
Next, the operation of the garbage processing system configured as described above will be described. Garbage dropped together with kitchen wastewater (general kitchen wastewater) from the drainage port of the kitchen sink is crushed to a predetermined size by the crusher 12. Garbage wastewater (treated water) containing crushed garbage that has been crushed by the crusher 12 is transferred into the wastewater inflow chamber 29 of the solid-liquid separation tank 26 via the transfer pipe 14.

(固液分離工程)
排水流入室29内へ移送されてきた生ゴミ排水中に含まれている固形物(例えば、生ゴミ破砕物などの有機物成分及び卵の殻などの無機物成分)は当該排水流入室29内を沈降する。この沈降した固形物(以下、「沈降破砕物」という。)は底壁31に案内されながら第1連通口32を通過し、さらに第2連通口33を介して好気分解槽25内に移流する。また、固形分が分離された生ゴミ排水中の液体分(生ゴミ懸濁液)は第1連通口32を介して固液分離室30内へ流れ込む。
(Solid-liquid separation process)
Solids (for example, organic components such as crushed garbage and inorganic components such as egg shells) contained in the wastewater transferred to the wastewater inflow chamber 29 settle in the wastewater inflow chamber 29. To do. This settled solid (hereinafter referred to as “sedimented crushed material”) passes through the first communication port 32 while being guided by the bottom wall 31, and further flows into the aerobic decomposition tank 25 through the second communication port 33. To do. Further, the liquid component (garbage suspension) in the garbage waste water from which the solid content has been separated flows into the solid-liquid separation chamber 30 via the first communication port 32.

一方、生ゴミ排水の流入により排水流入室29の水位は上昇し、当該排水流入室29のオーバーフロー分の液体分(生ゴミ懸濁液)は水面の浮遊物(以下、「浮遊破砕物」という。)とともに第1オーバーフロー部34を介して好気分解槽25に流れ込む。また、固液分離室30のオーバーフロー分の生ゴミ排水のうちの液体分は第2オーバーフロー部35を介して好気処理槽27内へ流れ込む。   On the other hand, the water level of the drainage inflow chamber 29 rises due to the inflow of garbage wastewater, and the liquid content (the garbage suspension) of the overflow of the drainage inflow chamber 29 is called floating matter on the water surface (hereinafter referred to as “floating crushed material”). ) And the aerobic decomposition tank 25 through the first overflow portion 34. In addition, the liquid component of the overflowing garbage waste in the solid-liquid separation chamber 30 flows into the aerobic treatment tank 27 through the second overflow unit 35.

排水流入室29内の浮遊破砕物の固液分離室30側への移流は第3隔壁28により規制される。このため、排水流入室29内の浮遊破砕物が固液分離室30を介して好気処理槽27内へ流れ込むことはない。また、浮遊破砕物は第1オーバーフロー部34から好気分解槽25へ流入し、沈降破砕物は第2連通口33を介して好気分解槽25内へ移流する。このため、移送管14からの生ゴミ排水の流入量の多少にかかわらず、浮遊破砕物及び沈降破砕物は必ず好気分解槽25内へ流入する。浮遊破砕物及び沈降破砕物が好気処理槽27内へ流れ込むことはないので、固液分離槽26(厳密には排水流入室29)の容量を一定以上確保する必要はない。   The advancing of the floating crushed material in the drainage inflow chamber 29 to the solid-liquid separation chamber 30 side is regulated by the third partition wall 28. For this reason, the floating crushed material in the drainage inflow chamber 29 does not flow into the aerobic treatment tank 27 through the solid-liquid separation chamber 30. Further, the suspended crushed material flows into the aerobic decomposition tank 25 from the first overflow portion 34, and the settled crushed material is transferred into the aerobic decomposition tank 25 through the second communication port 33. For this reason, regardless of the amount of inflow of the garbage wastewater from the transfer pipe 14, the suspended crushed material and the settled crushed material always flow into the aerobic decomposition tank 25. Since the suspended crushed material and the settled crushed material do not flow into the aerobic treatment tank 27, it is not necessary to secure a capacity of the solid-liquid separation tank 26 (strictly, the drainage inflow chamber 29) above a certain level.

(好気分解処理工程)
第1オーバーフロー部34から好気分解槽25内に流れ込んできた浮遊破砕物及び第2連通口33から好気分解槽25内に移流してきた沈降破砕物は、当該好気分解槽25において好気分解処理される。好気分解処理とは、溶存酸素の存在のもとに様々な好気性微生物が関与して有機性物質、アンモニア性窒素及び臭気などを酸化分解して除去する処理である。即ち、ブロワ43の駆動により空気(酸素)が連結管42及び散気管41を介して好気分解槽25内へ供給されること(曝気処理)により、生ゴミ破砕物などの有機物の表面に付着した好気性微生物や好気分解槽25内の好気性微生物が活性化される。この活性化された好気性微生物により生ゴミ排水に含まれる生ゴミ破砕物などの有機物成分が分解され、可溶化(液状化)する。
(Aerobic decomposition process)
The suspended crushed material flowing into the aerobic decomposition tank 25 from the first overflow portion 34 and the settled crushed material transferred to the aerobic decomposition tank 25 from the second communication port 33 are aerobic in the aerobic decomposition tank 25. Disassembled. The aerobic decomposition process is a process in which various aerobic microorganisms are involved in the presence of dissolved oxygen to remove organic substances, ammoniacal nitrogen, odors and the like by oxidative decomposition. That is, when the blower 43 is driven, air (oxygen) is supplied into the aerobic decomposition tank 25 through the connection pipe 42 and the diffuser pipe 41 (aeration treatment), and thereby adheres to the surface of organic matter such as garbage crushed material. The aerobic microorganisms and the aerobic microorganisms in the aerobic decomposition tank 25 are activated. The activated aerobic microorganisms decompose organic components such as crushed garbage contained in the trash wastewater and solubilize (liquefy).

散気管41が固液分離槽26の底壁31の下方に配置されていることから、散気管41の各空気噴出口から噴出した気泡は好気分解槽25内を上昇して底壁31に下方から接触する。気泡は傾斜した底壁31により下方から上方に案内されて好気分解槽25の第1隔壁23に対向する壁面側へ導かれる。この結果、好気分解槽25内には図1に矢印で示す左回りの旋回流C1が生成される。   Since the air diffuser 41 is disposed below the bottom wall 31 of the solid-liquid separation tank 26, the bubbles ejected from the air outlets of the air diffuser 41 rise in the aerobic decomposition tank 25 and reach the bottom wall 31. Contact from below. The bubbles are guided upward from below by the inclined bottom wall 31 and are guided to the wall surface facing the first partition wall 23 of the aerobic decomposition tank 25. As a result, a counterclockwise swirling flow C1 indicated by an arrow in FIG.

好気分解槽25内の生ゴミ排水に含まれる未分解の生ゴミ破砕物も旋回流C1により好気分解槽25内を左回りするように流動し、底壁31に接触しながら好気分解槽25の第1隔壁23に対向する壁面側へ導かれる。即ち、好気分解槽25内の生ゴミ破砕物は旋回流C1により撹拌される。未分解の生ゴミ破砕物は水流による撹拌により互いにぶつかり合うと共に好気分解槽25の底壁に接触することによりその微細化が促進される。好気分解処理により例えば1mm以下に分解された生ゴミ破砕物を含む可溶化処理済みの生ゴミ懸濁液は第2連通口33を通過して固液分離室30内に流入し、第2オーバーフロー部35を介して好気処理槽27へ流れ込む。   Undecomposed garbage crushed material contained in the wastewater drainage in the aerobic decomposition tank 25 also flows counterclockwise in the aerobic decomposition tank 25 by the swirling flow C1, and aerobically decomposes while contacting the bottom wall 31. The tank 25 is guided to the wall surface facing the first partition wall 23. That is, the crushed garbage in the aerobic decomposition tank 25 is agitated by the swirl flow C1. The undecomposed raw garbage crushed materials collide with each other by agitation by a water flow, and are brought into contact with the bottom wall of the aerobic decomposition tank 25 to promote the miniaturization thereof. The solubilized garbage suspension containing the garbage crushed material decomposed to, for example, 1 mm or less by the aerobic decomposition treatment passes through the second communication port 33 and flows into the solid-liquid separation chamber 30, and the second It flows into the aerobic treatment tank 27 through the overflow part 35.

(好気処理工程)
排水流入室29及び好気分解槽25から固液分離室30を介して、それぞれ好気処理槽27内に流れ込んできた生ゴミ懸濁液や可溶化処理済みの生ゴミ懸濁液は、当該好気処理槽27において好気処理される。好気処理とは、溶存酸素の存在のもとに様々な好気性微生物が関与して、有機性物質、アンモニア性窒素及び臭気などを酸化分解して除去する処理方法である。即ち、ブロワ43の駆動により空気(酸素)が連結管62及び散気管61を介して好気処理槽27内に供給されること(曝気処理)により好気分解処理済みの生ゴミ破砕物などの有機物の表面に付着している好気性微生物や担体71の表面及び内部の好気性微生物が活性化される。この活性化された好気性微生物により生ゴミ排水に含まれる有機物成分が分解される。
(Aerobic treatment process)
The garbage suspension and the solubilized garbage suspension that have flowed into the aerobic treatment tank 27 from the drainage inflow chamber 29 and the aerobic decomposition tank 25 through the solid-liquid separation chamber 30, respectively, Aerobic treatment is performed in the aerobic treatment tank 27. The aerobic treatment is a treatment method in which various aerobic microorganisms are involved in the presence of dissolved oxygen to oxidize and remove organic substances, ammoniacal nitrogen, odors, and the like. That is, when the blower 43 is driven, air (oxygen) is supplied into the aerobic treatment tank 27 through the connecting pipe 62 and the diffuser pipe 61 (aeration treatment), and the like, such as crushed garbage that has undergone aerobic decomposition treatment. The aerobic microorganisms adhering to the surface of the organic matter and the aerobic microorganisms on the surface and inside of the carrier 71 are activated. The activated aerobic microorganisms decompose organic components contained in the garbage wastewater.

散気管61がフィルタ支持部材51のフィルタ52の下方に配置されていることから、散気管61の空気噴出口から噴出した気泡は好気処理槽27内を上昇してフィルタ52に下方から接触する。気泡は傾斜したフィルタ52に沿うようにして下方から上方に案内される。この結果、好気処理槽27内には図1に矢印で示す左回りの旋回流C2が生成される。気泡がフィルタ52に接触することにより、当該フィルタ52の網目に生ゴミ排水中の有機物成分が付着することが抑制される。即ち、気泡をフィルタ52に接触させることにより、当該フィルタ52のクリーニング効果が得られ、当該フィルタ52の目詰まりが抑制される。   Since the air diffuser 61 is disposed below the filter 52 of the filter support member 51, the bubbles ejected from the air outlet of the air diffuser 61 rise in the aerobic treatment tank 27 and come into contact with the filter 52 from below. . The bubbles are guided upward from below along the inclined filter 52. As a result, a counterclockwise swirling flow C2 indicated by an arrow in FIG. 1 is generated in the aerobic treatment tank 27. When the bubbles come into contact with the filter 52, it is possible to suppress the organic component in the garbage wastewater from adhering to the mesh of the filter 52. That is, by bringing bubbles into contact with the filter 52, the cleaning effect of the filter 52 is obtained, and clogging of the filter 52 is suppressed.

また、好気処理槽27内の生ゴミ排水に含まれる未分解の生ゴミ破砕物及び各担体71も旋回流C2により撹拌され、好気処理槽27内を左回りに流動する。これにより、生ゴミ排水は担体71の表面及び内部に効率的に接触し、この担体71の表面や内部の好気性微生物により生ゴミ排水中の有機物成分が分解される。好気分解処理済みの生ゴミ排水に含まれる生ゴミ破砕物は可溶化されているので、好気処理が効率的に行われる。また、排水流入室29における浮遊破砕物や沈降破砕物が好気処理槽27内に流れ込むこともないので、浮遊物が担体71の表面に付着したり絡みついたりすることによる好気処理性能の低下も抑制される。このため、好気処理槽27における好気処理性能が維持される。さらに、各担体71が旋回流C2により撹拌されることにより当該各担体71がフィルタ支持部材51の底壁51aに接触しながら下方から上方に移動する。これにより、底壁51aの網目のクリーニング効果がいっそう向上する。   In addition, undecomposed garbage crushed material and each carrier 71 contained in the wastewater drainage in the aerobic treatment tank 27 are also agitated by the swirling flow C2, and flow in the aerobic treatment tank 27 counterclockwise. Thereby, the garbage wastewater efficiently contacts the surface and the inside of the carrier 71, and the organic components in the garbage wastewater are decomposed by the aerobic microorganisms on the surface and inside of the carrier 71. Since the garbage crushed material contained in the wastewater drained after the aerobic decomposition treatment is solubilized, the aerobic treatment is performed efficiently. In addition, since the suspended crushed material and the settled crushed material in the drainage inflow chamber 29 do not flow into the aerobic treatment tank 27, the aerobic treatment performance is deteriorated due to the floating material adhering to or entangled with the surface of the carrier 71. Is also suppressed. For this reason, the aerobic processing performance in the aerobic processing tank 27 is maintained. Furthermore, each carrier 71 is stirred by the swirl flow C <b> 2, so that each carrier 71 moves upward from below while contacting the bottom wall 51 a of the filter support member 51. Thereby, the mesh cleaning effect of the bottom wall 51a is further improved.

(排出処理工程)
好気処理により微生物分解された処理済み水(生ゴミ懸濁液)はフィルタ支持部材51のフィルタ52の網目を通過して流出口36から処理装置13の外部(例えば下水道)へ流出する。
(Discharge treatment process)
The treated water (garbage suspension) that has been microbially decomposed by the aerobic treatment passes through the mesh of the filter 52 of the filter support member 51 and flows out from the outflow port 36 to the outside (for example, sewer).

(実施形態の効果)
従って、本実施形態によれば、以下の効果を得ることができる。
(1)排水流入室29と固液分離室30とは第3隔壁28により隔離されており、当該第3隔壁28により生ゴミ排水中の浮遊破砕物の固液分離室30への移流が防止される。生ゴミ排水中の浮遊破砕物は排水流入室29のオーバーフロー分の生ゴミ排水と共に第1隔壁23の第1オーバーフロー部34を介して好気分解槽25へ流れ込む。このため、生ゴミ排水中の浮遊破砕物が好気処理槽27へ流れ込むことはない。また、沈降破砕物は第2連通口33を介して好気分解槽25へ移流する。従って、移送管14と処理槽22との間に生ゴミ排水中の生ゴミ破砕物(固形物)と生ゴミ懸濁液(液体分)とを分離する分離装置を別途設ける必要はない。また、前述のオーバーフローにより浮遊破砕物は好気分解槽25へのみ流れ込むことから、好気処理槽27の処理性能を低下させる浮遊破砕物を前段で処理する必要がない。即ち、好気処理槽27の前段に嫌気槽を設ける必要はない。従って、処理槽22の小型化が図られる。
(Effect of embodiment)
Therefore, according to the present embodiment, the following effects can be obtained.
(1) The drainage inflow chamber 29 and the solid-liquid separation chamber 30 are separated by the third partition wall 28, and the third partition wall 28 prevents the transfer of floating crushed material in the garbage wastewater to the solid-liquid separation chamber 30. Is done. The floating crushed material in the wastewater drainage flows into the aerobic decomposition tank 25 through the first overflow part 34 of the first partition wall 23 together with the overflowing garbage wastewater in the drainage inflow chamber 29. For this reason, the floating crushed material in the garbage wastewater does not flow into the aerobic treatment tank 27. Further, the sedimentation crushed material is transferred to the aerobic decomposition tank 25 through the second communication port 33. Therefore, it is not necessary to separately provide a separation device for separating the garbage crushed material (solid matter) and the garbage suspension (liquid component) in the garbage waste water between the transfer pipe 14 and the treatment tank 22. Further, since the floating crushed material flows only into the aerobic decomposition tank 25 due to the overflow described above, it is not necessary to treat the floating crushed material that degrades the processing performance of the aerobic treatment tank 27 in the previous stage. That is, it is not necessary to provide an anaerobic tank in front of the aerobic treatment tank 27. Accordingly, the processing tank 22 can be downsized.

(2)排水流入室29に流れ込んできた生ゴミ排水中の生ゴミ破砕物は浮遊破砕物と沈降破砕物へ容易に分離し、これら浮遊破砕物及び沈降破砕物が固液分離室30へ流れ込むこと、ひいては好気処理槽27へ流れ込むことはない。一方、好気処理槽27の生ゴミ排水中には好気性微生物を着床させる複数の担体71(微生物担体)を浮遊させる流動床としたので、好気処理槽27では有機物成分を容易に処理可能である。このため、排水流入室29へ流入する生ゴミ排水の量に基づいて当該排水流入室29の容量を一定以上確保する必要はない。即ち、排水流入室29の容量以上の生ゴミ排水が当該排水流入室29内へ流入した場合であっても、生ゴミ破砕物(沈降破砕物及び浮遊破砕物)が固液分離室30、ひいては好気処理槽27へ流出することがないので、排水流入室29への生ゴミ排水の流入量を考慮する必要はない。従って、排水流入室29、ひいては固液分離槽26の小型化が可能となる。   (2) Garbage crushed material in the garbage wastewater flowing into the wastewater inflow chamber 29 is easily separated into floating crushed material and sedimented crushed material, and these suspended crushed material and sedimented crushed material flow into the solid-liquid separation chamber 30. In other words, it does not flow into the aerobic treatment tank 27. On the other hand, since a plurality of carriers 71 (microorganism carriers) for depositing aerobic microorganisms are suspended in the wastewater drainage of the aerobic treatment tank 27, the organic components are easily treated in the aerobic treatment tank 27. Is possible. For this reason, it is not necessary to ensure the capacity | capacitance of the said waste_water | drain inflow chamber 29 more than fixed based on the quantity of the garbage wastewater which flows into the waste_water | drain inflow chamber 29. FIG. That is, even when garbage wastewater having a capacity larger than that of the drainage inflow chamber 29 flows into the drainage inflow chamber 29, the garbage crushed material (sedimentation crushed material and floating crushed material) remains in the solid-liquid separation chamber 30, by extension. Since it does not flow out to the aerobic treatment tank 27, it is not necessary to consider the amount of inflow of garbage wastewater into the drainage inflow chamber 29. Accordingly, it is possible to reduce the size of the drainage inflow chamber 29 and consequently the solid-liquid separation tank 26.

(3)固液分離槽26(排水流入室29)へ流れ込んだ生ゴミ排水中の沈降破砕物は排水流入室29内を沈降し、第2連通口33を介して好気分解槽25へ移流する。固液分離槽26(排水流入室29)の水面に浮遊する浮遊破砕物はオーバーフローにより好気分解槽25へ流れ込むようにした。このため、生ゴミ排水中の固形分と液体分とを予め分離して当該固形分を好気分解槽25へ移送する分離装置が不要となる。また、生ゴミ排水中の固形分と液体分とを分離する分離装置(図示略)を別途設けて、当該分離装置により予め分離した固形分を好気分解槽25へ移流するようにした場合に比べて、構成が簡単になる。   (3) The sedimentation crushed material in the garbage wastewater flowing into the solid-liquid separation tank 26 (drainage inflow chamber 29) settles in the drainage inflow chamber 29 and is transferred to the aerobic decomposition tank 25 through the second communication port 33. To do. The floating crushed material floating on the water surface of the solid-liquid separation tank 26 (drainage inflow chamber 29) was allowed to flow into the aerobic decomposition tank 25 due to overflow. For this reason, the separation apparatus which isolate | separates beforehand the solid content and liquid content in garbage wastewater, and transfers the said solid content to the aerobic decomposition tank 25 becomes unnecessary. In addition, when a separation device (not shown) for separating the solid content and the liquid content in the garbage wastewater is separately provided, and the solid content previously separated by the separation device is transferred to the aerobic decomposition tank 25 In comparison, the configuration becomes simple.

(4)好気分解槽25内において、固液分離槽26の底壁31の下方には散気管41を配置し、当該散気管41から噴出した気泡を固液分離槽26の底壁31に下方から接触させるようにした。散気管41からの気泡が固液分離槽26の底壁31により下方から上方へ案内されることにより、好気分解槽25内には図1における左回りの旋回流C1が発生する。このため、好気分解槽25内の生ゴミ破砕物及び生ゴミ懸濁液の撹拌効果が得られ、好気分解処理効率を向上させることができる。
(別例)
尚、前記実施形態は以下のような別例に変更して実施してもよい。
(4) In the aerobic decomposition tank 25, a diffuser pipe 41 is disposed below the bottom wall 31 of the solid-liquid separation tank 26, and bubbles blown from the diffuser pipe 41 are placed on the bottom wall 31 of the solid-liquid separation tank 26. Contact was made from below. Air bubbles from the air diffusion pipe 41 are guided from below to above by the bottom wall 31 of the solid-liquid separation tank 26, whereby a counterclockwise swirling flow C1 in FIG. For this reason, the stirring effect of the garbage crushed material and garbage suspension in the aerobic decomposition tank 25 is acquired, and aerobic decomposition processing efficiency can be improved.
(Another example)
In addition, you may implement the said embodiment by changing into the following other examples.

・本実施形態では、排水流入室29内の沈降破砕物は固液分離槽26の底壁31により案内されながら第2連通口33を介して好気分解槽25内に移流するようにしたが、次のようにしてもよい。即ち、底壁31に単数又は複数のフィルタを設ける。このようにすれば、好気分解槽25内の生ゴミ懸濁液の固液分離槽26(厳密には、固液分離室30)内への移流が円滑に行われる。好気分解槽25内の未処理生ゴミ破砕物(前記フィルタの目開きよりも大きな粒度を有する未分解固形物)の固液分離槽26(排水流入室29及び固液分離室30)への移流が防止される。   In the present embodiment, the crushed sediment in the drainage inflow chamber 29 is transferred to the aerobic decomposition tank 25 through the second communication port 33 while being guided by the bottom wall 31 of the solid-liquid separation tank 26. The following may also be used. That is, one or more filters are provided on the bottom wall 31. By doing so, the agglomeration suspension in the aerobic decomposition tank 25 is smoothly transferred to the solid-liquid separation tank 26 (strictly speaking, the solid-liquid separation chamber 30). Untreated garbage crushed material in the aerobic decomposition tank 25 (undecomposed solid material having a particle size larger than the opening of the filter) to the solid-liquid separation tank 26 (drainage inflow chamber 29 and solid-liquid separation chamber 30). Advection is prevented.

・本実施形態では、処理槽22を第1隔壁23及び第2隔壁24により好気分解槽25、固液分離槽26及び好気処理槽27の3槽に区画するようにしたが、各槽をそれぞれ別体とし、それらを組み合わせることにより処理槽22を構成するようにしてもよい。このようにしても、本実施形態における(1)〜(4)と同様の効果を得ることができる。   In the present embodiment, the treatment tank 22 is divided into three tanks of an aerobic decomposition tank 25, a solid-liquid separation tank 26, and an aerobic treatment tank 27 by the first partition wall 23 and the second partition wall 24. May be configured as separate bodies, and the treatment tank 22 may be configured by combining them. Even if it does in this way, the effect similar to (1)-(4) in this embodiment can be acquired.

(付記)
次に前記実施形態及び別例から把握できる技術的思想を以下に追記する。
(イ)前記好気分解槽と固液分離槽とを区画する第1隔壁の下部側を好気処理槽側へ傾斜させることにより当該固液分離槽の底壁を構成し、当該底壁と浮遊破砕物移流防止壁の下端縁との間に前記第1連通口を形成すると共に、当該底壁の下端縁と第2隔壁との間に前記第2連通口を形成するようにした請求項2に記載の生ゴミ処理システム。
(Appendix)
Next, a technical idea that can be grasped from the embodiment and another example will be added below.
(B) The bottom wall of the solid-liquid separation tank is configured by inclining the lower side of the first partition wall that partitions the aerobic decomposition tank and the solid-liquid separation tank toward the aerobic treatment tank, The first communication port is formed between the lower end edge of the suspended crushed material advancing prevention wall and the second communication port is formed between the lower end edge of the bottom wall and the second partition wall. The garbage processing system of 2.

この構成によれば、請求項2に記載の発明の作用に加えて、好気分解槽内に固液分離槽が区画形成されるので、いっそう小型化が図られる。また、固液分離槽の底壁が好気処理槽側へ傾斜することにより、排水流入室内において沈降する沈降破砕物は当該固液分離槽の底壁に案内されながら第1連通口を通過し、さらに第2連通口を介して好気分解槽内へ円滑に移流される。   According to this configuration, in addition to the operation of the invention described in claim 2, since the solid-liquid separation tank is partitioned in the aerobic decomposition tank, further downsizing can be achieved. In addition, since the bottom wall of the solid-liquid separation tank is inclined toward the aerobic treatment tank, the sedimentation crushed material that settles in the drainage inflow chamber passes through the first communication port while being guided by the bottom wall of the solid-liquid separation tank. Further, the gas is smoothly transferred into the aerobic decomposition tank through the second communication port.

(ロ)前記好気分解槽内において、前記固液分離槽の底壁の下方には好気分解槽内に空気を送り込む好気分解用散気手段を配置し、当該好気分解用散気手段により発生した気泡を前記固液分離槽の底壁に下方から接触させるようにした前記(イ)項に記載の生ゴミ処理システム。   (B) In the aerobic decomposition tank, an aerobic decomposition diffuser for sending air into the aerobic decomposition tank is disposed below the bottom wall of the solid-liquid separation tank, and the aerobic decomposition diffuser. The garbage disposal system according to item (a), wherein bubbles generated by the means are brought into contact with the bottom wall of the solid-liquid separation tank from below.

この構成によれば、(イ)項に記載の発明の作用に加えて、好気分解槽内に置いて、好気分解用散気手段により発生した気泡は固液分離槽の底壁に下方から接触する。気泡が固液分離槽の底壁により下方から上方へ案内されることにより、好気分解槽内には所定方向の旋回流が発生する。このため、好気分解槽内の生ゴミ破砕物及び生ゴミ懸濁液の撹拌効果が得られる。   According to this configuration, in addition to the operation of the invention described in (a), the bubbles generated by the aerobic decomposition aeration means are placed below the bottom wall of the solid-liquid separation tank. Contact from. As the bubbles are guided from below to above by the bottom wall of the solid-liquid separation tank, a swirling flow in a predetermined direction is generated in the aerobic decomposition tank. For this reason, the stirring effect of the garbage crushed material and garbage suspension in an aerobic decomposition tank is acquired.

(ハ)前記好気処理槽の生ゴミ排水中には好気性微生物を着床させる複数の微生物担体を浮遊させる流動床とした請求項1、請求項2、(イ)項及び(ロ)項のうちいずれか一項に記載の生ゴミ処理システム。   (C) A fluidized bed in which a plurality of microbial carriers for depositing aerobic microorganisms are suspended in the wastewater drainage of the aerobic treatment tank. The garbage processing system as described in any one of these.

この構成によれば、請求項1、請求項2、(イ)項及び(ロ)項のうちいずれか一項に記載の発明の作用に加えて、好気処理槽へ移流されてきた生ゴミ懸濁液中の可溶化成分は微生物担体に着床された好気性微生物により処理される。   According to this configuration, in addition to the action of the invention according to any one of claims 1, 2, (a) and (b), the garbage which has been transferred to the aerobic treatment tank The solubilized components in the suspension are treated with aerobic microorganisms that are implanted in a microbial carrier.

(ニ)前記好気処理槽における好気処理済みの生ゴミ懸濁液の流出口を内側から覆うようにフィルタ支持部材を設けると共に当該フィルタ支持部材の底壁を斜状に且つ水没状態に設け、当該底壁には単数又は複数のフィルタを設けると共に当該フィルタの下方には該好気処理槽内に空気を送り込む好気処理用散気手段を配置し、当該好気処理用散気手段により発生した気泡を前記フィルタに下方から接触させるようにした請求項1、請求項2、(イ)項、(ロ)項及び(ハ)項のうちいずれか一項に記載の生ゴミ処理システム。   (D) A filter support member is provided so as to cover the outlet of the aerobic-treated garbage suspension in the aerobic treatment tank from the inside, and the bottom wall of the filter support member is provided obliquely and submerged. The bottom wall is provided with one or a plurality of filters, and an aerobic treatment aeration means for sending air into the aerobic treatment tank is disposed below the filter, and the aerobic treatment aeration means The garbage disposal system according to any one of claims 1, 2, (a), (b) and (c), wherein the generated bubbles are brought into contact with the filter from below.

この構成によれば、請求項1、請求項2、前記(イ)項、(ロ)項及び(ハ)項のうちいずれか一項に記載の発明の作用に加えて、好気処理槽内の好気処理済みの生ゴミ懸濁液は流出口を介して外部に流出する。この際、好気処理槽の流出口に設けられたフィルタにより固形物(未分解の生ゴミ破砕物や余剰汚泥など)の流出が抑制される。また、フィルタ支持部材のフィルタには、散気手段からの気泡が下方から接触する。このため、フィルタの目詰まりが抑制される。   According to this configuration, in addition to the action of the invention according to any one of claims 1, 2, (a), (b) and (c), the inside of the aerobic treatment tank The aerobic treated garbage suspension flows out to the outside through the outlet. At this time, the outflow of solid matter (undecomposed raw garbage crushed material, excess sludge, etc.) is suppressed by a filter provided at the outlet of the aerobic treatment tank. In addition, bubbles from the air diffuser come into contact with the filter of the filter support member from below. For this reason, clogging of the filter is suppressed.

本実施形態の生ゴミ処理システムの概略構成図。The schematic block diagram of the garbage processing system of this embodiment.

符号の説明Explanation of symbols

11…生ゴミ処理システム、12…破砕機、14…移送管(移送手段)、
22…処理槽、23…第1隔壁、24…第2隔壁、25…好気分解槽、
26…固液分離槽、27…好気処理槽、28…第3隔壁(浮遊破砕物移流防止壁)、
29…排水流入室、30…固液分離室、31…固液分離槽の底壁、32…第1連通口、33…第2連通口、34…第1オーバーフロー部、35…第2オーバーフロー部、
36…流出口、41,61…散気管(散気手段)、51…フィルタ支持部材、
51a…底壁、52…フィルタ、71…担体(微生物担体)。
DESCRIPTION OF SYMBOLS 11 ... Garbage disposal system, 12 ... Crusher, 14 ... Transfer pipe (transfer means),
22 ... treatment tank, 23 ... first partition, 24 ... second partition, 25 ... aerobic decomposition tank,
26 ... solid-liquid separation tank, 27 ... aerobic treatment tank, 28 ... third partition (floating crushed material advection prevention wall),
DESCRIPTION OF SYMBOLS 29 ... Waste water inflow chamber, 30 ... Solid-liquid separation chamber, 31 ... Bottom wall of solid-liquid separation tank, 32 ... 1st communication port, 33 ... 2nd communication port, 34 ... 1st overflow part, 35 ... 2nd overflow part ,
36 ... Outlet, 41, 61 ... Air diffuser (air diffuser), 51 ... Filter support member,
51a ... bottom wall, 52 ... filter, 71 ... carrier (microorganism carrier).

Claims (2)

破砕機により破砕された生ゴミ破砕物を含む生ゴミ排水を浄化処理する処理槽を備えた生ゴミ処理システムにおいて、
前記処理槽は、
移送手段により移流されてきた生ゴミ排水を固形分である生ゴミ破砕物と液体分である生ゴミ懸濁液とに分離する固液分離槽と、
前記固液分離槽の前段に配置されると共に当該固液分離槽により分離された生ゴミ破砕物が移流され当該生ゴミ破砕物を可溶化処理する好気分解槽と、
前記固液分離槽の後段に配置されると共に当該固液分離槽の生ゴミ懸濁液及び前記好気分解槽における可溶化処理済みの生ゴミ懸濁液のみが移流され両生ゴミ懸濁液をそれぞれ好気処理する好気処理槽とを備えた生ゴミ処理システム。
In a garbage processing system equipped with a treatment tank for purifying garbage wastewater containing garbage crushed material crushed by a crusher,
The treatment tank is
A solid-liquid separation tank that separates the garbage wastewater transferred by the transfer means into a garbage crushed material that is solid and a garbage suspension that is a liquid;
An aerobic decomposition tank that is disposed in the previous stage of the solid-liquid separation tank and is solubilized with the garbage crushed material transferred by the solid-liquid separation tank,
Only the garbage suspension in the solid-liquid separation tank and the solubilized garbage suspension in the aerobic decomposition tank are transferred to the both ends of the solid-liquid separation tank. A garbage disposal system equipped with an aerobic treatment tank for aerobic treatment.
前記処理槽は第1隔壁及び第2隔壁により好気分解槽、固液分離槽及び好気処理槽に区画し、
前記固液分離槽は浮遊破砕物移流防止壁により前記移送手段からの生ゴミ排水が移流される排水流入室と前記固液分離槽内の生ゴミ懸濁液及び前記好気分解槽における可溶化処理済みの生ゴミ懸濁液が移流される固液分離室とにさらに区画し、
前記浮遊破砕物移流防止壁には排水流入室と固液分離室とをそれらの底部において連通する第1連通口を設け、
前記第1隔壁には固液分離室と好気分解槽とをそれらの底部において連通する第2連通口を設けると共に当該第1隔壁の上部には生ゴミ排水の流入に伴う排水流入室のオーバーフロー分の生ゴミ懸濁液を前記好気分解槽へ移流可能とした第1オーバーフロー部を設け、
前記第2隔壁の上部には生ゴミ排水の流入に伴う固液分離室のオーバーフロー分の生ゴミ懸濁液を好気処理槽へ移流可能とした第2オーバーフロー部を設けるようにした請求項1に記載の生ゴミ処理システム。
The treatment tank is divided into an aerobic decomposition tank, a solid-liquid separation tank and an aerobic treatment tank by a first partition and a second partition,
The solid-liquid separation tank is a solubilization in the waste water inflow chamber in which the garbage wastewater from the transfer means is transferred by the floating crushed material advancing prevention wall, the garbage suspension in the solid-liquid separation tank, and the aerobic decomposition tank. It is further divided into a solid-liquid separation chamber to which the treated garbage suspension is transferred,
The floating crushed material advancing prevention wall is provided with a first communication port for communicating the drainage inflow chamber and the solid-liquid separation chamber at the bottom thereof,
The first partition is provided with a second communication port for communicating the solid-liquid separation chamber and the aerobic decomposition tank at the bottom thereof, and the upper portion of the first partition is overflowed with a drainage inflow chamber accompanying the inflow of garbage wastewater. Provided with a first overflow portion that can transfer the waste garbage suspension to the aerobic decomposition tank,
2. A second overflow portion is provided at the upper portion of the second partition wall, which allows a waste suspension of an overflow of a solid-liquid separation chamber accompanying the inflow of garbage waste water to be transferred to an aerobic treatment tank. The garbage disposal system described in 1.
JP2003371075A 2003-10-30 2003-10-30 Garbage treatment system Pending JP2005131555A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008012491A (en) * 2006-07-10 2008-01-24 Hitachi Housetec Co Ltd Aerobic digestion tank and sewage cleaning tank equipped with the same
JP2009045534A (en) * 2007-08-17 2009-03-05 Fuji Kankyo Seibi:Kk Garbage disposer
JP2014144407A (en) * 2013-01-28 2014-08-14 Osaka Gas Co Ltd Drainage treatment apparatus and method for operating the same
JP2015180492A (en) * 2014-03-05 2015-10-15 大阪瓦斯株式会社 Apparatus for treating waste water

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008012491A (en) * 2006-07-10 2008-01-24 Hitachi Housetec Co Ltd Aerobic digestion tank and sewage cleaning tank equipped with the same
JP2009045534A (en) * 2007-08-17 2009-03-05 Fuji Kankyo Seibi:Kk Garbage disposer
JP2014144407A (en) * 2013-01-28 2014-08-14 Osaka Gas Co Ltd Drainage treatment apparatus and method for operating the same
JP2015180492A (en) * 2014-03-05 2015-10-15 大阪瓦斯株式会社 Apparatus for treating waste water

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