JP2006272103A - Method and apparatus for pretreating garbage - Google Patents

Method and apparatus for pretreating garbage Download PDF

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JP2006272103A
JP2006272103A JP2005093351A JP2005093351A JP2006272103A JP 2006272103 A JP2006272103 A JP 2006272103A JP 2005093351 A JP2005093351 A JP 2005093351A JP 2005093351 A JP2005093351 A JP 2005093351A JP 2006272103 A JP2006272103 A JP 2006272103A
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garbage
tank
cleaning fluid
methane fermentation
sludge
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Tetsuya Yamamoto
哲也 山本
Shinichiro Wakahara
慎一郎 若原
Mitsuo Koike
三男 小池
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Kubota 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method and an apparatus for pretreating garbage capable of recovering garbage attached to impurities in a shredding and separating apparatus and fermentable garbage having a low water content as a material for methane fermentation without increasing processed water and energy consumption. <P>SOLUTION: The method for pretreating garbage comprising pretreating garbage in a pretreatment process when garbage is solubilized in a solubilizing tank and then fed to a methane fermentation tank or an organism treatment tank for waste water treatment, wherein fermented sludge in the methane fermentation tank or an excess sludge in the organism treatment tank is fed to a shredding and separating apparatus 1 from a cleaning fluid feeding system 5 as a cleaning fluid when garbage is coarsely shredded and separated to the shredded garbage and impurities in the shredding and separating apparatus 1 in which the pretreatment process is performed. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は生ごみの前処理方法および装置に関し、生ごみメタン発酵処理施設、汚泥再生処理センター等における生ごみの前処理の技術に係るものである。   The present invention relates to a garbage pretreatment method and apparatus, and relates to a garbage pretreatment technique in a garbage methane fermentation treatment facility, a sludge regeneration treatment center, and the like.

従来、有機性廃棄物をメタン発酵処理するメタン発酵関連施設では、破砕した生ゴミ等の有機性廃棄物を貯留槽(可溶化槽)内で攪拌して液状化(スラリー化もしくはペースト化)し、液状となった有機性廃棄物に含まれる夾雑物を除去装置で除去した後、有機性廃棄物をメタン発酵槽へ供給している。   Conventionally, in methane fermentation-related facilities where organic waste is treated with methane fermentation, organic waste such as crushed garbage is agitated in a storage tank (solubilization tank) and liquefied (slurried or pasted). After removing impurities contained in the organic waste that has become liquid, the organic waste is supplied to the methane fermentation tank.

また、特許文献1では、生ごみを遠心型破砕分別機で粗破砕分別して生ごみ破砕物と夾雑物とに分別し、生ごみ破砕物を可溶化工程で可溶化し、この可溶化処理物を固液分離装置で固液分離した液状分をメタン発酵槽の原料や排水処理における有機炭素源、水素供与体となし、固形分をコンポスト化・飼料化等の再資源化原料としている。
特開2002−336825号公報
In Patent Document 1, garbage is roughly crushed and separated by a centrifugal crushing and separating machine, and is separated into garbage crushed material and foreign matter, and the crushed food waste is solubilized in a solubilization process. The liquid component obtained by solid-liquid separation using a solid-liquid separator is used as a raw material for methane fermentation tanks, an organic carbon source for wastewater treatment, and a hydrogen donor, and the solid content is used as a raw material for recycling such as composting and feed.
JP 2002-336825 A

ところで、従来においては、生ごみを破砕分別機で粗破砕分別して生ごみ破砕物と夾雑物とに分別することで一次除渣しているが、破砕分別機から排出する夾雑物に生ごみ(微小固形物、油脂等の液状物)が付着したり、あるいは、本来であればメタン発酵の原料となり得る紙などの低含水率発酵可能ごみが夾雑物として排出されることがある。   By the way, in the past, raw garbage is roughly crushed and separated by a crushing and sorting machine and sorted into garbage crushed material and foreign matter, but the primary waste is separated. Liquids such as fine solids and oils and fats) may adhere, or low-water-content fermentable garbage such as paper that can be a raw material for methane fermentation may be discharged as impurities.

このため、破砕分別機において水や温水を洗浄水として噴霧することにより、夾雑物に付着した微小固物、油脂等の液状物である生ごみを除去して生ごみ破砕物として回収し、低含水率発酵可能ごみを生ごみ破砕物とともに回収している。   For this reason, by spraying water or warm water as washing water in the crushing / separating machine, the garbage, which is a liquid such as fine solids and fats and oils attached to the contaminants, is removed and recovered as a garbage crushed material. Recoverable water content fermentable waste together with crushed garbage.

しかし、破砕分別機において夾雑物に付着した生ごみを除去するために水や温水を使用すると、プロセス水の使用量が増加し、温水とするためのエネルギーを必要とする。また、洗浄水が生ごみ破砕物とともに可溶化槽へ流入し、意図しない不要な希釈が可溶化槽において生じる問題があった。   However, if water or hot water is used to remove garbage attached to foreign substances in the crushing / separating machine, the amount of process water used is increased, and energy for making the hot water is required. In addition, there is a problem that the washing water flows into the solubilization tank together with the garbage crushed material and unintended unnecessary dilution occurs in the solubilization tank.

本発明は上記した課題を解決するものであり、生ごみメタン発酵処理施設、汚泥再生処理センター等で使用するプロセス水および消費エネルギーを増加させることなく、破砕分別機において夾雑物に付着する生ごみ、および低含水率発酵可能ごみをメタン発酵の原料として回収することができる生ごみの前処理方法および装置を提供することを目的とする。   The present invention solves the above-mentioned problems, and does not increase the process water and energy consumption used in the garbage methane fermentation treatment facility, sludge regeneration treatment center, etc., and the garbage attached to the contaminants in the crushing and separating machine. Another object of the present invention is to provide a garbage pretreatment method and apparatus capable of recovering low-moisture fermentable waste as a raw material for methane fermentation.

上記課題を解決するために、本発明の生ごみの前処理方法は、生ごみを可溶化槽で可溶化してメタン発酵槽もしくは排水処理の生物処理槽へ供給するに際して前処理工程で生ごみを前処理するものであって、前処理工程をなす破砕分別機で生ごみを粗破砕分別して生ごみ破砕物と夾雑物とに分別するに際し、メタン発酵槽の発酵汚泥もしくは生物処理槽の余剰汚泥を洗浄流体として破砕分別機に供給するものである。   In order to solve the above-mentioned problem, the pretreatment method for garbage according to the present invention is based on the pretreatment process when the garbage is solubilized in a solubilization tank and supplied to a biological treatment tank for methane fermentation or wastewater treatment. When the raw garbage is roughly crushed and separated into crushed garbage and foreign substances using a crushing / separating machine that performs the pretreatment process, fermented sludge in the methane fermentation tank or surplus in the biological treatment tank Sludge is supplied to the crushing and separating machine as a cleaning fluid.

上記した構成により、生ごみメタン発酵処理施設、汚泥再生処理センター等の処理プロセスにおいて、破砕分別機で生ごみを粗破砕分別して生ごみ破砕物と夾雑物とに分別するに際し、夾雑物に付着する生ごみを除去する洗浄流体として処理プロセスで生じる発酵汚泥もしくは余剰汚泥を用いることにより以下の作用効果を生じる。   With the above configuration, when processing garbage such as raw garbage methane fermentation treatment facility, sludge regeneration processing center, etc., roughly crushing and separating the raw garbage with a crushing and sorting machine, the garbage adheres to the garbage. By using fermented sludge or surplus sludge generated in the treatment process as a cleaning fluid for removing garbage, the following effects are produced.

生ごみ中の紙等の低含水率発酵可能ごみは、発酵汚泥もしくは余剰汚泥を吸収して破砕され易い状態となり、さらに比重が増加することで、生ごみ破砕物として分別される態様に変化する。また、洗浄流体が固液混相流体であることから夾雑物に付着する生ごみを除去する洗浄流体の除去能が高くなり、発酵汚泥は発酵プロセスの温度にあるので、洗浄流体を昇温するためにエネルギーを消費することなく、夾雑物に付着する油脂等の除去能が高くなる。よって、生ごみから回収する生ごみ破砕物の回収率が高まり、可溶化槽で可溶化されて、メタン発酵の原料もしくは排水処理における有機炭素源、水素供与体となり得る可溶化処理物が増加する。   Garbage that can be fermented with low water content, such as paper in raw garbage, is in a state where it can be easily crushed by absorbing fermented sludge or excess sludge. . In addition, since the cleaning fluid is a solid-liquid mixed phase fluid, the cleaning fluid removal capability to remove garbage adhering to contaminants is increased, and the fermentation sludge is at the temperature of the fermentation process. In addition, the ability to remove oils and fats adhering to foreign matters is increased without consuming energy. Therefore, the recovery rate of the garbage crushed material collected from the garbage is increased, solubilized in the solubilization tank, and the solubilized product that can be used as a raw material for methane fermentation or an organic carbon source and hydrogen donor in wastewater treatment increases. .

さらに、洗浄流体の発酵汚泥もしくは余剰汚泥が生ごみ破砕物とともに汚泥混合生ごみとなって可溶化槽で可溶化されることで、可溶化槽における酸発酵を促進することができ、メタン発酵槽もしくは排水処理の生物処理槽へ供給する可溶化処理物の質が向上する。   Furthermore, the fermented sludge or excess sludge of the cleaning fluid becomes sludge mixed garbage with the crushed garbage and solubilized in the solubilization tank, so that acid fermentation in the solubilization tank can be promoted, and the methane fermentation tank Alternatively, the quality of the solubilized product supplied to the biological treatment tank for wastewater treatment is improved.

また、洗浄流体として系外から新鮮水等を導入する必要がなくなり、処理プロセスで消費するプロセス水を抑制できる。
本発明の生ごみの前処理装置は、可溶化槽で可溶化してメタン発酵槽もしくは排水処理の生物処理槽へ供給する生ごみを前処理するものであって、生ごみを粗破砕分別して生ごみ破砕物と夾雑物とに分別する破砕分別機に、メタン発酵槽の発酵汚泥もしくは生物処理槽の余剰汚泥を洗浄流体として供給する洗浄流体供給系を備えたものである。
In addition, it is not necessary to introduce fresh water or the like as a cleaning fluid from outside the system, and process water consumed in the treatment process can be suppressed.
The garbage pre-treatment apparatus of the present invention pre-treats the garbage solubilized in a solubilization tank and supplied to a biological treatment tank for a methane fermentation tank or wastewater treatment, and the garbage is roughly crushed and separated. A crushing / separating machine that separates garbage into crushed garbage and impurities is provided with a cleaning fluid supply system that supplies fermentation sludge in a methane fermentation tank or surplus sludge in a biological treatment tank as a cleaning fluid.

以上のように本発明によれば、メタン発酵槽の発酵汚泥もしくは生物処理槽の余剰汚泥を洗浄流体として破砕分別機に供給することにより、紙等の低含水率発酵可能ごみを生ごみ破砕物として分別される態様に変化させ、洗浄流体の除去能を向上させることができ、結果として、生ごみ破砕物の回収率の高まりによる可溶化処理物の増加と、可溶化処理物の質の向上を図ることができる。   As described above, according to the present invention, by supplying fermented sludge from a methane fermentation tank or surplus sludge from a biological treatment tank to a crushing / separating machine as a cleaning fluid, wastes that can be fermented with low water content such as paper are crushed by garbage. As a result, it is possible to improve the ability to remove the cleaning fluid, resulting in an increase in the solubilized product due to an increase in the recovery rate of the crushed garbage and an improvement in the quality of the solubilized product. Can be achieved.

以下、本発明の実施の形態を図面に基づいて説明する。図1において、本実施の形態に係る前処理装置は、生ごみメタン発酵処理施設、汚泥再生処理センター等の処理プロセスにおいて、生ごみを可溶化槽で可溶化し、可溶化槽の可溶化処理物をメタン発酵槽もしくは排水処理の生物処理槽へ供給するに際して、可溶化槽への投入の前に生ごみを前処理するものである。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. In FIG. 1, the pretreatment apparatus according to the present embodiment is configured to solubilize garbage in a solubilization tank and solubilize the solubilization tank in a treatment process such as a garbage methane fermentation treatment facility and a sludge regeneration treatment center. When the product is supplied to a methane fermentation tank or a biological treatment tank for wastewater treatment, the garbage is pretreated before being put into the solubilization tank.

前処理装置は、破砕分別機1、破砕機2、一時貯留槽3、移送装置4を備えている。破砕分別機1はメタン発酵槽の発酵汚泥もしくは生物処理槽の余剰汚泥を洗浄流体として供給する洗浄流体供給系5を備え、所定量の洗浄流体を噴霧しながら生ごみ6を粗破砕分別して生ごみ破砕物と夾雑物7とに分別し、生ごみ破砕物と洗浄流体の混合物を汚泥混合生ごみ8として一時貯留槽3に排出する。この破砕分別機1の構成は後に詳述する。   The pretreatment device includes a crushing / separating device 1, a crushing device 2, a temporary storage tank 3, and a transfer device 4. The crushing / separating machine 1 includes a cleaning fluid supply system 5 that supplies fermented sludge from a methane fermentation tank or surplus sludge from a biological treatment tank as a cleaning fluid, and roughly pulverizes and separates garbage 6 while spraying a predetermined amount of cleaning fluid. The waste crushed material and the foreign matter 7 are separated, and the mixture of the garbage crushed material and the cleaning fluid is discharged to the temporary storage tank 3 as sludge mixed food waste 8. The configuration of the crushing / separating machine 1 will be described in detail later.

破砕機2は、一軸破砕機、多軸破砕機などの剪断型破砕機からなり、破砕分別機1から排出する夾雑物7を剪断して破砕し、破砕物は夾雑物ホッパ等へ移送する。
移送装置4はポンプ、ケースコンベア等からなり、一時貯留槽3に貯留する汚泥混合生ごみ8を可溶化槽へ供給する。
The crusher 2 is composed of a shear type crusher such as a uniaxial crusher or a multi-axis crusher. The crushing material 7 discharged from the crushing / separating machine 1 is sheared and crushed, and the crushed material is transferred to a foreign material hopper or the like.
The transfer device 4 includes a pump, a case conveyor, and the like, and supplies the sludge mixed garbage 8 stored in the temporary storage tank 3 to the solubilization tank.

破砕分別機1は、衝撃破砕機能、風力選別機能、スクリーン選別機能を有するものであり、基本的な構成は公知のものである。図2に示すように、破砕分別機1は、本体胴10の一端側に生ごみ6を投入するための生ごみ投入口11を有し、他端側に夾雑物7を排出するための夾雑物排出口12を有し、本体胴10の下部に汚泥混合生ごみ8を排出するためのスクリューコンベア13を有し、スクリューコンベア13の一端に生ごみ排出口14を有している。   The crushing / separating machine 1 has an impact crushing function, a wind power sorting function, and a screen sorting function, and a basic configuration is known. As shown in FIG. 2, the crushing / separating machine 1 has a garbage input port 11 for introducing garbage 6 on one end side of the main body barrel 10, and a dust for discharging impurities 7 on the other end side. It has a product discharge port 12, a screw conveyor 13 for discharging the sludge mixed garbage 8 at the bottom of the main body cylinder 10, and a garbage discharge port 14 at one end of the screw conveyor 13.

本体胴10は、スクリューコンベア13との間に配置するパンチングメタルからなるスクリーンと、回転羽根と、本体胴10の内壁面に設置する破砕刃、洗浄流体の噴霧ノズルを有し、回転羽根が本体胴10の生ごみ投入口11を設けた一端側から夾雑物排出口12を設けた他端側に至る回転軸廻りに回転する。   The main body cylinder 10 includes a screen made of punching metal disposed between the screw conveyor 13, a rotary blade, a crushing blade installed on the inner wall surface of the main body cylinder 10, and a spray nozzle for cleaning fluid. The drum 10 rotates around a rotation axis from one end side where the garbage input port 11 is provided to the other end side where the dust discharge port 12 is provided.

以下、上記した構成における作用を説明する。生ごみとしてビニル袋やプラスチック容器等の夾雑物7を伴う生ごみ6を破砕分別機1へ生ごみ投入口11から投入する。洗浄流体供給系5から供給する洗浄流体としてのメタン発酵槽の発酵汚泥もしくは生物処理槽の余剰汚泥を破砕分別機1の内部に噴霧ノズルから所定量ずつ噴霧し、生ごみ6を粗破砕分別して生ごみ破砕物と夾雑物7とに分別しながら夾雑物7に付着した生ごみ6を洗浄流体で洗い流す。   Hereinafter, the operation of the above-described configuration will be described. Garbage 6 accompanied by foreign matter 7 such as a vinyl bag or a plastic container is thrown into the crushing and sorting machine 1 from the garbage input port 11 as garbage. As a cleaning fluid supplied from the cleaning fluid supply system 5, fermented sludge from the methane fermentation tank or surplus sludge from the biological treatment tank is sprayed into the crushing / separating machine 1 by a predetermined amount from the spray nozzle, and the garbage 6 is roughly crushed and separated. The garbage 6 adhering to the contaminants 7 is washed away with the cleaning fluid while being separated into crushed garbage and impurities 7.

破砕分別機1の内部では、高速に回転する回転羽根によって生ごみ6に衝撃を与えるとともに遠心力を与え、生ごみ6を破砕刃に衝突させて衝撃破砕し、本体胴10の内部を生ごみ投入口11の側から夾雑物排出口12の側へ移動させる間に、夾雑物7に付着した生ごみを洗浄流体で洗い流しながら、スクリーンのパンチングメタルを通過可能なまでに生ごみ6を破砕し、生ごみ破砕物と洗浄流体からなる汚泥混合生ごみ8をスクリューコンベア13に排出しつつ、回転羽根の回転によって生じる風力によって夾雑物7を風選し、風選した夾雑物7を夾雑物排出口12から排出する。この夾雑物7は生ごみを洗浄流体で洗い流しているので夾雑物7から発する臭気を低減できる。   Inside the crushing / separating machine 1, impacts are given to the garbage 6 by centrifugal blades rotating at high speed and centrifugal force is applied. While moving from the inlet 11 side to the contaminant outlet 12 side, the garbage 6 is crushed until it can pass through the punching metal of the screen while washing away the garbage attached to the contaminant 7 with the cleaning fluid. While the sludge mixed garbage 8 composed of the garbage crushed material and the cleaning fluid is discharged to the screw conveyor 13, the dust 7 is wind-selected by the wind generated by the rotation of the rotary blades, and the wind-cleaned dust 7 is discharged as the dust. Discharge from outlet 12. Since the contaminants 7 are washed away with the cleaning fluid, the odor emitted from the contaminants 7 can be reduced.

分別した汚泥混合生ごみ8は、スクリューコンベア13によって生ごみ排出口14から一時貯留槽3へ供給し、一時貯留槽3から移送装置4によって可溶化槽へ供給する。このとき、汚泥混合生ごみ8は含水率が高く、破砕分別機1でペースト化が進行しているので、ポンプ移送が容易である。   The separated sludge mixed garbage 8 is supplied from the garbage discharge port 14 to the temporary storage tank 3 by the screw conveyor 13 and supplied from the temporary storage tank 3 to the solubilization tank by the transfer device 4. At this time, the sludge mixed garbage 8 has a high moisture content, and since the pasting is progressing in the crushing / separating machine 1, the pump transfer is easy.

上述した破砕分別機1の作用において、生ごみ6に含まれた紙等の低含水率発酵可能ごみは、発酵汚泥もしくは余剰汚泥からなる洗浄流体を吸収して破砕され易い状態となるとともに、比重が増加することで生ごみ破砕物として分別される態様に変化し、風選によって夾雑物7として分別されることなく衝撃破砕されて生ごみ破砕物としてスクリーンを通過する。   In the operation of the crushing / separating machine 1 described above, the low water content fermentable waste such as paper contained in the garbage 6 becomes easy to be crushed by absorbing the cleaning fluid made of fermented sludge or excess sludge and has a specific gravity. As a result of the increase, it is changed to a mode of being separated as garbage crushed material, and is impact crushed without being separated as dust 7 by wind selection and passes through the screen as garbage crushed material.

また、洗浄流体が固液混相流体であることから夾雑物7に付着する生ごみ6を除去する洗浄流体の除去能が高くなり、特に洗浄流体として発酵汚泥を使用する場合には、発酵汚泥が発酵プロセスの温度にあるので、洗浄流体を昇温するためにエネルギーを消費することなく、夾雑物7に付着する油脂等の除去能が高くなる。   In addition, since the cleaning fluid is a solid-liquid mixed phase fluid, the cleaning fluid removal ability to remove the garbage 6 adhering to the contaminants 7 is enhanced. Especially when fermented sludge is used as the cleaning fluid, Since it is at the temperature of the fermentation process, the ability to remove oils and fats adhering to the contaminants 7 is increased without consuming energy to raise the temperature of the cleaning fluid.

よって、生ごみ6から回収する生ごみ破砕物の回収率が高まり、可溶化槽で可溶化されて、メタン発酵の原料もしくは排水処理における有機炭素源、水素供与体となる可溶化処理物が増加する。   Therefore, the recovery rate of the garbage crushed material collected from the garbage 6 is increased, solubilized in the solubilization tank, and the solubilized processed material that becomes a raw material for methane fermentation or an organic carbon source and a hydrogen donor in wastewater treatment increases. To do.

さらに、破砕分別機1において洗浄流体の発酵汚泥もしくは余剰汚泥が生ごみ破砕物と攪拌・混合されて汚泥混合生ごみ8となって可溶化槽で可溶化されることで、可溶化槽における攪拌動力を減少させることができるとともに、可溶化槽における酸発酵を促進することができ、メタン発酵槽もしくは排水処理の生物処理槽へ供給する可溶化処理物の質が向上する。また、洗浄流体として系外から新鮮水等を導入する必要がなくなり、処理プロセスで消費するプロセス水を抑制できる。   Furthermore, in the crushing / separating machine 1, the fermented sludge or surplus sludge of the cleaning fluid is agitated and mixed with the crushed garbage to become sludge mixed garbage 8 and solubilized in the solubilization tank. Power can be reduced and acid fermentation in the solubilization tank can be promoted, so that the quality of the solubilized product supplied to the methane fermentation tank or the biological treatment tank for wastewater treatment is improved. Moreover, it is not necessary to introduce fresh water or the like as a cleaning fluid from outside the system, and process water consumed in the treatment process can be suppressed.

本発明の実施の形態における生ごみの前処理装置を示すブロック図The block diagram which shows the pre-processing apparatus of the garbage in embodiment of this invention 同実施の形態における前処理装置をなす破砕分別機の正面図Front view of the crushing / separating machine constituting the pretreatment device in the embodiment

符号の説明Explanation of symbols

1 破砕分別機
2 破砕機
3 一時貯留槽
4 移送装置
5 洗浄流体供給系
6 生ごみ
7 夾雑物
8 汚泥混合生ごみ
10 本体胴
11 生ごみ投入口
12 夾雑物排出口
13 スクリューコンベア
14 生ごみ排出口
DESCRIPTION OF SYMBOLS 1 Crushing and separating machine 2 Crushing machine 3 Temporary storage tank 4 Transfer device 5 Cleaning fluid supply system 6 Garbage 7 Waste 8 Sludge mixed garbage 10 Main body trunk 11 Garbage inlet 12 Waste outlet 13 Screw conveyor 14 Garbage waste Exit

Claims (2)

生ごみを可溶化槽で可溶化してメタン発酵槽もしくは排水処理の生物処理槽へ供給するに際して前処理工程で生ごみを前処理するものであって、前処理工程をなす破砕分別機で生ごみを粗破砕分別して生ごみ破砕物と夾雑物とに分別するに際し、メタン発酵槽の発酵汚泥もしくは生物処理槽の余剰汚泥を洗浄流体として破砕分別機に供給することを特徴とする生ごみの前処理方法。 When food waste is solubilized in a solubilization tank and supplied to a methane fermentation tank or a biological treatment tank for wastewater treatment, the food waste is pretreated in a pretreatment process, When the waste is roughly crushed and separated into crushed garbage and foreign materials, the fermentation sludge from the methane fermentation tank or surplus sludge from the biological treatment tank is supplied to the crushing and separating machine as a cleaning fluid. Pre-processing method. 可溶化槽で可溶化してメタン発酵槽もしくは排水処理の生物処理槽へ供給する生ごみを前処理するものであって、生ごみを粗破砕分別して生ごみ破砕物と夾雑物とに分別する破砕分別機に、メタン発酵槽の発酵汚泥もしくは生物処理槽の余剰汚泥を洗浄流体として供給する洗浄流体供給系を備えたことを特徴とする生ごみの前処理装置。 This is a pre-treatment of the garbage that is solubilized in the solubilization tank and supplied to the methane fermentation tank or the biological treatment tank for wastewater treatment. The raw garbage is roughly crushed and separated into crushed garbage and impurities. A garbage pretreatment device comprising a crushing and separating machine equipped with a cleaning fluid supply system for supplying fermentation sludge from a methane fermentation tank or surplus sludge from a biological treatment tank as a cleaning fluid.
JP2005093351A 2005-03-29 2005-03-29 Method and apparatus for pretreating garbage Pending JP2006272103A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106903128A (en) * 2017-02-28 2017-06-30 四川六叶草环保科技有限公司 House refuse and the multigroup multistage fermentation disposing technique of kitchen garbage
CN112916197A (en) * 2021-01-28 2021-06-08 内蒙古金陶股份有限公司 Pretreatment method before ore processing

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JPH0623337A (en) * 1992-07-09 1994-02-01 Matsushita Electric Ind Co Ltd Treatment of carbage and kitchen waste water
JPH09201599A (en) * 1996-01-26 1997-08-05 Kubota Corp Method for recovering useful substance from organic waste and utilizing the same as resources
JP2002336825A (en) * 2001-05-17 2002-11-26 Kubota Corp Method for recycling organic waste
JP2004154624A (en) * 2002-11-01 2004-06-03 Kajima Corp Deodorized sorter of foreign matter

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Publication number Priority date Publication date Assignee Title
JPH0623337A (en) * 1992-07-09 1994-02-01 Matsushita Electric Ind Co Ltd Treatment of carbage and kitchen waste water
JPH09201599A (en) * 1996-01-26 1997-08-05 Kubota Corp Method for recovering useful substance from organic waste and utilizing the same as resources
JP2002336825A (en) * 2001-05-17 2002-11-26 Kubota Corp Method for recycling organic waste
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Publication number Priority date Publication date Assignee Title
CN106903128A (en) * 2017-02-28 2017-06-30 四川六叶草环保科技有限公司 House refuse and the multigroup multistage fermentation disposing technique of kitchen garbage
CN106903128B (en) * 2017-02-28 2023-10-31 广东东实环境股份有限公司 Multi-group multi-stage fermentation treatment process for household garbage and kitchen garbage
CN112916197A (en) * 2021-01-28 2021-06-08 内蒙古金陶股份有限公司 Pretreatment method before ore processing

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