JP3995662B2 - Organic waste treatment equipment - Google Patents

Organic waste treatment equipment Download PDF

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JP3995662B2
JP3995662B2 JP2004131356A JP2004131356A JP3995662B2 JP 3995662 B2 JP3995662 B2 JP 3995662B2 JP 2004131356 A JP2004131356 A JP 2004131356A JP 2004131356 A JP2004131356 A JP 2004131356A JP 3995662 B2 JP3995662 B2 JP 3995662B2
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organic waste
decomposition
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JP2005313023A (en
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喜十 矢澤
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株式会社ニューテック
喜十 矢澤
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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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Description

本発明は、レストランやホテル、食品加工工場等から排出される生ごみ等の有機性排出物(主として固体有機廃棄物)を微生物の分解作用で分解するための有機性排出物分解装置を有機性排出物処理ラインに配設して、有機性排出物の搬送と分解を可能にするための有機性排出物処理装置に関する。 The present invention provides an organic waste decomposition apparatus for decomposing organic waste such as garbage (mainly solid organic waste) discharged from restaurants, hotels, food processing factories, etc. by the decomposition action of microorganisms . The present invention relates to an organic waste treatment apparatus that is disposed in an waste treatment line to enable transportation and decomposition of organic waste.

レストランやホテル、食品加工工場等から排出される有機性排出物(主として固体有機廃棄物)の処理方法として、従来は焼却したり埋め立て処分したりする方法が一般的であったが、焼却ではダイオキシン等の人体に有毒なガスが発生するという問題があり、また、埋め立て処分では埋め立て地を確保することができる残余年数が激減しているという問題があるので今までとは違った有機性排出物の処理方法が求められている。
この目的にかなう有機性排出物の処理装置の一つとして、有機性排出物と微生物とを攪拌手段で破砕・混合し、これを加熱しながら好気性下で微生物により分解処理して土壌改良材や有機肥料として回収できる有機性排出物分解装置がよく知られている。
特開2000−550号公報
Conventional methods for treating organic waste (mainly solid organic waste) emitted from restaurants, hotels, food processing factories, etc. have been incinerated or disposed of in landfills. There is a problem that toxic gas is generated in the human body, etc., and there is a problem that the remaining years that can secure a landfill site is drastically reduced in landfill disposal, so organic emissions different from before There is a need for a processing method.
As one of the processing equipment for organic effluent that meets this purpose, organic effluent and microorganisms are crushed and mixed by agitation means and decomposed by microorganisms under aerobic condition while heating them. Organic waste decomposition devices that can be recovered as organic fertilizers are well known.
JP 2000-550 A

しかしながら、このような有機性排出物分解装置は、一般に有機性排出物の分解効率を高めるため、分解処理室の床下にヒータを複数配置し、床や床下の空気をヒータで直接加熱することが行われている。そのため、
(1)ヒータ近傍とヒータから離れた位置との間ではどうしても温度差が生じ易く、ヒータのレイアウトを工夫しても分解処理室の床を均一な温度で加熱することが難しかった。
(2)また、最適な攪拌手段の回転速度が、例えば6~10min−1程度と遅いのでヒータに近いところでは分解処理室内の被処理物が局部的に加熱され易くなり(加熱ムラが発生しやすくなり)、高温に加熱されたところでは有機性排出物を分解する効果がある微生物の一部が死滅してしまい、有機性排出物の分解処理速度があがらないという問題があった。
However, in order to increase the decomposition efficiency of organic waste, such an organic waste decomposition apparatus generally has a plurality of heaters arranged under the floor of the decomposition treatment chamber and directly heats the floor or the air under the floor with the heater. It has been broken. for that reason,
(1) A temperature difference is apt to occur between the vicinity of the heater and a position away from the heater, and it is difficult to heat the floor of the decomposition chamber at a uniform temperature even if the heater layout is devised.
(2) Since the optimum rotation speed of the stirring means is as slow as about 6 to 10 min-1, for example, the workpiece in the decomposition chamber is likely to be heated locally near the heater (heating unevenness occurs). When heated to a high temperature, a part of the microorganisms that have the effect of decomposing the organic effluent is killed, and the decomposition rate of the organic effluent does not increase.

本発明は前記課題を解決するためになされたものであって、本発明の目的は、分解処理室の床を均一な温度で加熱することができる有機性排出物分解装置を有機性排出物処理ラインに配設して、有機性排出物の搬送と分解が可能な有機性排出物処理装置を提供することである。 The present invention has been made to solve the above-described problems, and an object of the present invention is to provide an organic waste decomposition apparatus capable of heating a floor of a decomposition treatment chamber at a uniform temperature. It is to provide an organic waste treatment apparatus which is disposed in a line and can transport and decompose organic waste.

本発明は前記課題を解決するためになされたものであって、請求項1に記載の発明は、有機性排出物分解装置を配置してなる有機性排出物処理装置であって、排水により有機性排出物を有機性排出物処理装置本体内に導入する有機性排出物流入管の排出端部の下流に、流量を調整する流量調整堰と、前記流量調整堰よりも高さの低い溢流板と、排水から有機性排出物を分離する回転式スクリーンを2基配置し、前記2基の回転式スクリーンの下流に有機性排出物分解装置を配置してなり、前記有機性排出物分解装置は、有機性排出物を微生物により分解する分解処理室と前記分解処理室の床全体を均一に加熱する床暖房手段とからなり、前記分解処理室は有機性排出物とこれを分解する微生物とを混合する攪拌手段を備え、攪拌手段は2つの回転軸とこの回転軸から軸径方向外方に突出する攪拌ロッドの先端部に鋭角な斜面を有する斜角錐体台の掻き揚げ羽根を設けてなり、2つの回転軸における掻き揚げ羽根は攪拌領域が一部重複するように取り付けられており、前記分解処理室の床は掻き揚げ羽根の回転軌跡に沿うように円弧状に形成されており、表面全体が断熱材で覆われていることを特徴とする有機性排出物処理装置である。 The present invention has been made in order to solve the above-mentioned problems, and the invention according to claim 1 is an organic waste treatment apparatus in which an organic waste decomposition apparatus is arranged, and is organic by waste water. Downstream of the discharge end of the organic waste inflow pipe for introducing the organic waste into the organic waste treatment apparatus main body, and the overflow plate having a height lower than that of the flow rate control weir And two rotary screens for separating the organic discharge from the waste water, and an organic discharge decomposition device is arranged downstream of the two rotary screens. A decomposition treatment chamber for decomposing organic waste by microorganisms and a floor heating means for uniformly heating the entire floor of the decomposition treatment chamber, wherein the decomposition treatment chamber contains the organic discharge and microorganisms for decomposing it. It has a stirring means for mixing, and the stirring means has two A rotating blade and a tip of a stirring rod that protrudes outward in the radial direction of the shaft from the rotating shaft are provided with a fringing blade of an oblique pyramid having a sharp slope, and the lifting blade on the two rotating shafts is a stirring region. Are attached so as to partially overlap, the floor of the decomposition chamber is formed in an arc shape along the rotation trajectory of the raking blade, and the entire surface is covered with a heat insulating material. It is an organic waste treatment device .

請求項1に記載の発明によると、排水により有機性排出物を導入する有機性排出物流入管の排出端部の下流に、排水から有機性排出物を分離する2基の回転式スクリーンを配置し、この2基の回転式スクリーンの下流に有機性排出物分解装置を配置したことにより、従来、回転式スクリーンの下流に必要であった破砕機や脱水機が不要となり、メンテナンスの簡素化、省コスト化が図れる。また、流量調整堰よりも高さの低い溢流板を設けることにより、常に一定量の混合液が回転スクリーンで処理される。 According to the first aspect of the present invention, two rotary screens for separating the organic waste from the wastewater are disposed downstream of the discharge end of the organic waste inflow pipe for introducing the organic waste by the wastewater. By arranging the organic waste decomposition device downstream of these two rotary screens, the conventional crusher and dehydrator required downstream of the rotary screen are no longer required, simplifying and saving maintenance. Cost can be reduced. Further, by providing an overflow plate having a height lower than that of the flow control weir, a constant amount of the mixed liquid is always processed by the rotating screen.

また、前記有機性排出物分解装置とすることによって、被処理物を少量処理する場合に適した攪拌手段とすることができる。 Moreover, it can be set as the stirring means suitable when processing a small amount of to-be-processed objects by setting it as the said organic waste decomposition device.

また、請求項に記載の発明は、分解処理室が有機性排出物とこれを分解する微生物とを混合する攪拌手段を備えたことにより、微生物が有機性排出物の分解作用を発揮するのに最適な温度と微生物に餌さとなる有機性排出物を十分に供給できるため有機性排出物の分解処理速度が向上する。 Further, in the invention according to claim 1 , since the decomposition treatment chamber is provided with a stirring means for mixing the organic effluent and the microorganism for decomposing the organic effluent, the microorganism exhibits the decomposition action of the organic effluent. Therefore, the organic waste can be sufficiently supplied and the organic waste that feeds the microorganisms can be supplied sufficiently.

請求項に記載の発明は、床暖房手段が、前記分解処理室の床全体を液体の加熱媒体により直接加熱する床暖房室と、この床暖房室内に前記液体を供給・排出する液体給排手段と、前記液体を床暖房室内で加熱して前記加熱媒体とするヒータとから構成されている請求項に記載の有機性排出物処理装置である。 According to a second aspect of the present invention, the floor heating means directly heats the entire floor of the decomposition treatment chamber with a liquid heating medium, and supplies and discharges the liquid into and out of the floor heating chamber. 2. The organic waste treatment apparatus according to claim 1 , wherein the organic waste treatment apparatus includes a means and a heater that heats the liquid in a floor heating chamber and uses the liquid as the heating medium.

請求項に記載の発明によると、前記床暖房手段を、前記床全体を液体の加熱媒体により直接加熱する床暖房室と、この床暖房室内に供給・排出する給排手段と、前記液体を床暖房室内で加熱して前記加熱媒体とするヒータとから構成することにより、分解処理室の床全体を液体の加熱媒体で加熱することができるので床のどこの位置でも一定の温度で加熱することができる。 According to the invention described in claim 2 , the floor heating means includes a floor heating chamber that directly heats the entire floor with a liquid heating medium, a supply / discharge unit that supplies and discharges the floor heating chamber, and the liquid. By comprising a heater that is heated in the floor heating chamber and used as the heating medium, the entire floor of the decomposition processing chamber can be heated with a liquid heating medium, so that it is heated at a constant temperature anywhere on the floor. be able to.

(1)請求項1に記載の発明によれば、従来、回転式スクリーンの下流に必要であった破砕機や脱水機が不要となり、メンテナンスの簡素化、省コスト化が図れる。また、分解処理室内の被処理物が局部加熱されて微生物が死滅することがなくなるので、有機性排出物の分解速度が向上する。また、微生物が有機性排出物の分解作用を発揮するのに最適な温度と微生物に餌さとなる有機性排出物を十分に供給できる。  (1) According to the first aspect of the present invention, a crusher and a dehydrator that have been conventionally required downstream of the rotary screen become unnecessary, and maintenance can be simplified and cost can be reduced. In addition, since the object to be processed in the decomposition treatment chamber is not locally heated and the microorganisms are not killed, the decomposition rate of the organic waste is improved. In addition, it is possible to sufficiently supply the organic effluent serving as a feed to the microorganism and the optimal temperature for the microorganism to exert the decomposition action of the organic effluent.
(2)請求項2に記載の発明によれば、分解処理室の床全体を液体の加熱媒体で加熱することができるので床のどこの位置でも一定の温度で加熱することができる。  (2) According to the invention described in claim 2, since the entire floor of the decomposition treatment chamber can be heated with the liquid heating medium, it can be heated at a constant temperature anywhere on the floor.

本発明に係る有機性排出物処理装置について説明する。  The organic waste treatment apparatus according to the present invention will be described.
最初に、本発明に係る有機性排出物処理装置に配設する第1実施形態の有機性排出物分解装置について図面を参照しながら説明する。  First, the organic waste decomposition apparatus according to the first embodiment disposed in the organic waste treatment apparatus according to the present invention will be described with reference to the drawings.
図1及び図3に示すように、有機性排出物分解装置1は、上部の分解処理室11と下部の床暖房室12とから主要部が構成される。有機性排出物分解装置全体は箱型をしており、キャスタつきの架台の上に設置されている。    As shown in FIGS. 1 and 3, the organic waste decomposition apparatus 1 is composed of an upper decomposition treatment chamber 11 and a lower floor heating chamber 12. The entire organic waste decomposition device is box-shaped and installed on a caster-mounted base.

分解処理室11と床暖房室12は、分解処理室11の下部及び床暖房室12の上部にそれぞれ設けられたフランジ18,18同士をボルト・ナットで締結されている。前記フランジ18,18の間には、分解処理室11の床13の外周端部を挟持されている。分解処理室11の床13は、図3に示すように、攪拌手段20,21それぞれの攪拌翼22,22--の回転軌跡に沿うように円弧状に形成されている。  The decomposition processing chamber 11 and the floor heating chamber 12 are fastened with bolts and nuts between flanges 18 and 18 provided at the lower portion of the decomposition processing chamber 11 and the upper portion of the floor heating chamber 12, respectively. Between the flanges 18 and 18, an outer peripheral end portion of the floor 13 of the decomposition processing chamber 11 is sandwiched. As shown in FIG. 3, the floor 13 of the decomposition processing chamber 11 is formed in an arc shape so as to follow the rotation trajectories of the stirring blades 22, 22-of the stirring means 20, 21.
このように床13を円弧状に形成することで、床を平坦にしたときよりも被処理物を加熱する伝熱面積を大きくすることができる。  By forming the floor 13 in an arc shape in this way, the heat transfer area for heating the object to be processed can be made larger than when the floor is flattened.

このように、前記床暖房室12を、前記床13に対してボルト・ナットにより着脱自在に構成したことにより、床暖房室12の装着・取り外しが簡単にできるようになり、有機性排出物分解装置全体の点検・メンテナンスが容易となる。As described above, the floor heating chamber 12 is configured to be detachable from the floor 13 with bolts and nuts, so that the floor heating chamber 12 can be easily attached and detached, and organic waste decomposition is achieved. Inspection and maintenance of the entire device becomes easy.
尚、分解処理室11の天井19には、図示しない開閉自在の有機性排出物の投入口と内部点検口とが設けられている。  The ceiling 19 of the decomposition processing chamber 11 is provided with an openable / closable organic discharge inlet and an internal inspection port (not shown).

分解処理室11の内部には、図1〜図3に示すような1組の攪拌手段20,21が備えられている。攪拌手段20,21は、分解処理室内に水平に配設された2つの回転軸23,24とこの回転軸23,24から軸径方向外方へ突出する複数の攪拌翼22,22--とから構成される。攪拌翼22、22は、図3に示すように、全長にわたり一定の幅を有する攪拌ロッド25と、前記攪拌ロッド25の先端部に設けられる鋭角の斜面を有する斜角錐体台(横断面が台形)の掻き揚げ羽根26とから形成されている。掻き揚げ羽根26は、台形の下底面(掻き揚げ羽根26の横断面が台形なので便宜上こう呼ぶことにする)が分解処理室11の床側となるように設けられている。A set of stirring means 20 and 21 as shown in FIGS. 1 to 3 are provided inside the decomposition processing chamber 11. The agitating means 20 and 21 include two rotating shafts 23 and 24 disposed horizontally in the decomposition processing chamber, and a plurality of stirring blades 22 and 22-- protruding outward in the axial radial direction from the rotating shafts 23 and 24. Consists of As shown in FIG. 3, the stirring blades 22, 22 have a stirring rod 25 having a constant width over the entire length, and an oblique pyramid base (having a trapezoidal cross section) having an acute slope provided at the tip of the stirring rod 25. ) Of the raking blades 26). The raking blade 26 is provided such that the lower bottom surface of the trapezoid (which will be referred to as a convenience for the reason that the horizontal section of the raking blade 26 is trapezoidal) is the floor side of the decomposition processing chamber 11.
また、掻き揚げ羽根26の尖端は、攪拌手段20,21の回転方向と同じ方向に向くように設けられている。  Further, the tip of the scraping blade 26 is provided so as to face the same direction as the rotation direction of the stirring means 20 and 21.

攪拌翼22,22……は、図1及び図2に示すように、攪拌ロッド25,25……の中心線と掻き揚げ羽根26,26--の下底面(掻き揚げ羽根の横断面が台形なので便宜上こう呼ぶことにする)とが交わった点を結んだ曲線が、回転軸23,24の周りを囲繞する螺旋を描くように取り付けられている。また、攪拌翼22,22……の攪拌領域が一部重複するように、それぞれの攪拌翼22の取り付け位置を、回転軸23,24の回転方向に互いに等角度間隔ずらした状態となるように取り付けられている(図3参照)。As shown in FIGS. 1 and 2, the stirring blades 22, 22... Are centered on the stirring rods 25, 25... And the lower bottom surfaces of the lifting blades 26, 26-- Therefore, a curve connecting the intersections of the rotation axis 23 and 24 is attached so as to draw a spiral surrounding the rotation axes 23 and 24. Further, the mounting positions of the stirring blades 22 are shifted from each other at equal angular intervals in the rotation direction of the rotary shafts 23 and 24 so that the stirring regions of the stirring blades 22, 22. It is attached (see FIG. 3).

攪拌翼22,22……をこのように取り付けたことで、被処理物を破砕・混合する場合、回転方向に小さな動力を与えることになるので、被処理物を少量処理する場合(被処理物の厚みが薄い場合)に適した攪拌手段20,21となる。By attaching the stirring blades 22, 22... In this way, when crushing and mixing the object to be processed, a small amount of power is applied in the rotational direction. The agitating means 20 and 21 are suitable for the case where the thickness is small.

このような有機性排出物とこれを分解する微生物とを破砕・混合する攪拌手段20,21を備えたことにより、微生物の餌さとなる有機性排出物を微生物に十分に供給できるため、有機性排出物の分解処理速度が向上する。By providing the agitation means 20 and 21 for crushing and mixing such organic effluent and the microorganisms that decompose the organic effluent, the organic effluent serving as a food for the microorganism can be sufficiently supplied to the microorganism. The decomposition processing speed of the emission is improved.
尚、上記攪拌手段20,21を駆動する駆動機構は、回転軸23,24の端部に取り付けられて互いに歯合する従動歯車と一方の従動歯車を駆動歯車を介して駆動する減速機付きのモータ4とから構成される。攪拌手段20,21の回転方向は正逆どちらでも回転できるようになっている。  The drive mechanism for driving the agitating means 20 and 21 includes a driven gear attached to the ends of the rotary shafts 23 and 24 and meshing with each other and a driven gear with one of the driven gears via the drive gear. And a motor 4. The rotating directions of the stirring means 20 and 21 can be rotated either forward or reverse.

また、有機性排出物分解装置1の床暖房手段は、図3及び図4に示すように、分解処理室11の床全体を液体の加熱媒体、例えば温水により直接加熱するための床暖房室12と、この床暖房室12内に液体として水を供給・排出する水給排手段である給水口30、排水口31と、前記水を床暖房室12内で加熱して温水とするヒータ32とから構成される。Further, as shown in FIGS. 3 and 4, the floor heating means of the organic waste decomposition apparatus 1 is a floor heating chamber 12 for directly heating the entire floor of the decomposition treatment chamber 11 with a liquid heating medium, for example, hot water. A water supply port 30 and a water discharge port 31 that are water supply / discharge means for supplying and discharging water as liquid in the floor heating chamber 12, and a heater 32 that heats the water in the floor heating chamber 12 to make hot water Consists of

このように、前記床暖房手段を、前記床全体を温水により直接加熱する床暖房室12と、この床暖房室12に水を供給・排出する給水口30・排水口31と、水を床暖房室内で加熱して温水とするヒータ32とから構成することにより、従来行っていた床や床下の空気をヒータで加熱する場合と比較して、分解処理室11の床全体を比熱の大きい温水で加熱するので床13のどこの位置でも一定の温度で加熱することができる。In this way, the floor heating means includes a floor heating chamber 12 that directly heats the entire floor with hot water, a water supply port 30 and a drain port 31 that supply and discharge water to the floor heating chamber 12, and floor heating the water. By comprising the heater 32 that is heated indoors to produce hot water, the entire floor of the decomposition treatment chamber 11 is heated with hot water having a large specific heat, compared to the conventional case where the floor and the air under the floor are heated by the heater. Therefore, it can be heated at a constant temperature anywhere on the floor 13.

また、有機性排出物を微生物により分解する分解処理室11の床全体を均一に加熱する床暖房手段を備えたことにより、分解処理室内の被処理物が局部加熱されて有機性排出物を分解するのに有効な微生物が死滅することがなくなるので、有機性排出物の分解速度が向上する。Further, by providing a floor heating means for uniformly heating the entire floor of the decomposition treatment chamber 11 for decomposing the organic emission by microorganisms, the object to be treated in the decomposition treatment chamber is locally heated to decompose the organic emission. Since the microorganisms effective to do so are not killed, the decomposition rate of the organic effluent is improved.
尚、通常有機性排出物を分解するための加熱温度としては、この発明では30〜50℃(好ましくは35〜40℃)程度の温度で加熱するので、加熱媒体としては比熱の小さい(冷めやすい)気体よりも比熱の大きい(冷めにくい)液体のほうが一定の温度を保持しやすいので液体を利用するのが望ましい。加温温度を50℃以下とすることにより臭気抑制が可能となり、これによって発生臭気対策はきわめて容易になる。  In addition, as the heating temperature for decomposing the organic effluent, it is heated at a temperature of about 30 to 50 ° C. (preferably 35 to 40 ° C.) in the present invention, so that the heating medium has a small specific heat (easy to cool). ) It is desirable to use a liquid because a liquid having a larger specific heat (harder to cool) than a gas tends to maintain a constant temperature. By setting the heating temperature to 50 ° C. or less, it becomes possible to suppress odors, which makes it very easy to take measures against generated odors.

また、本実施形態では、分解処理室11で被処理物を分解するときに発生する熱量に対して有機性排出物分解装置1の装置表面積が大きいので、外部への放散熱量の割合が大きくなるため、図3に示すように、装置の表面全体を断熱材35で厳重に覆って放散する熱量を少なくしている。特に床暖房室12の底部では、厚さの厚い断熱材39をチャンバ36に充填して保温を確実に行っている。Moreover, in this embodiment, since the apparatus surface area of the organic waste decomposition | disassembly apparatus 1 is large with respect to the calorie | heat amount generate | occur | produced when decomposing | disassembling a to-be-processed object in the decomposition | disassembly process chamber 11, the ratio of the amount of heat dissipated outside becomes large. Therefore, as shown in FIG. 3, the entire surface of the apparatus is strictly covered with the heat insulating material 35 to reduce the amount of heat dissipated. In particular, at the bottom of the floor heating chamber 12, the heat insulation material 39 having a large thickness is filled into the chamber 36 to ensure heat insulation.

以下、図1〜図4を参照して第1実施形態の有機性排出物分解装置の作用について説明する。Hereinafter, with reference to FIGS. 1-4, the effect | action of the organic waste decomposition | disassembly apparatus of 1st Embodiment is demonstrated.
最初に床暖房室内へ給水口30から水を供給する。所定量が供給されたかの水量は液面計37で確認する。水が所定量供給できたらヒータ32のスイッチをONさせる。床暖房室内の水温が常に30〜50℃(好ましくは35〜40℃)となるようにヒータ32の電力供給量を制御する。  First, water is supplied from the water supply port 30 to the floor heating room. The amount of water as to whether a predetermined amount has been supplied is confirmed with a liquid level gauge 37. When a predetermined amount of water can be supplied, the heater 32 is turned on. The power supply amount of the heater 32 is controlled so that the water temperature in the floor heating room is always 30 to 50 ° C. (preferably 35 to 40 ° C.).
ここで温水の温度の制御方法として、例えば分解処理室内の(a)被処理物の温度、(b)酸素濃度、(c)排気中の水分を凝縮させた液のpH値、(d)相対湿度等を測定して被処理物の分解状況を把握し、分解状況に基づいてフランジヒータ32への電力供給量を制御するようにしても良い。  Here, as a method of controlling the temperature of the hot water, for example, (a) the temperature of the object to be processed in the decomposition chamber, (b) the oxygen concentration, (c) the pH value of the liquid condensed with the moisture in the exhaust, (d) relative You may make it grasp | ascertain the decomposition | disassembly condition of a to-be-processed object by measuring humidity etc. and control the electric power supply amount to the flange heater 32 based on a decomposition | disassembly condition.

次いで、攪拌手段20,21の駆動を開始する。その後、排気ブロワ3を起動し、分解処理室内へ新鮮な空気を導入する。これで準備が完了する。分解処理室11には、例えば、有機性排出物10L、微生物として有機性排出物分解酵素10L、水分調整材としてもみ殻80Lを分解処理室11の天井19の図示しない投入口から分解処理室内へ投入する。Next, the drive of the stirring means 20 and 21 is started. Thereafter, the exhaust blower 3 is activated to introduce fresh air into the decomposition chamber. This completes the preparation. In the decomposition chamber 11, for example, an organic discharge 10 L, an organic discharge decomposing enzyme 10 L as a microorganism, and a rice husk 80 L as a moisture adjusting material are introduced from a not-shown inlet of the ceiling 19 of the decomposition chamber 11 into the decomposition chamber. throw into.
尚、水分調整材は、必要に応じて添加したり、しなかったりするものなので添加しないこともある。有機性排出物投入時の被処理物の水分値としては特に限定しないが、処理機能力と被処理物の投入量の調整によって、分解工程での水分値が60%から65%の範囲となるように調整することが望ましい。  Note that the moisture adjusting material may or may not be added because it may or may not be added as necessary. Although there is no particular limitation on the moisture value of the object to be treated at the time of introducing the organic waste, the moisture value in the decomposition step is in the range of 60% to 65% by adjusting the processing function power and the amount of the object to be treated. It is desirable to adjust so that.

分解処理室11に投入された被処理物は、互いに内側に回転する攪拌手段20,21の攪拌翼22,22……の間で破砕・混合されながら微生物の分解作用を受ける。このとき攪拌ロッド25,25--の先端部に設けられた掻き揚げ羽根26,26、……の斜面に沿って被処理物が掻き揚げられ落下するので、被処理物の上下方向の攪拌と空気との接触が促進される。また、被処理物が床13の一箇所に留まった状態になる事がなくなるため被処理物全体を万遍なく加熱することができる。The object to be processed put into the decomposition chamber 11 is subjected to a microorganism decomposing action while being crushed and mixed between the stirring blades 22, 22. At this time, since the object to be treated is scraped and dropped along the slopes of the lifting blades 26, 26,... Provided at the tips of the stirring rods 25, 25-- Contact with air is promoted. Further, since the object to be processed does not stay in one place on the floor 13, the entire object to be processed can be heated uniformly.

このようにして有機性排出物を分解する微生物にとって必要な最適な温度と空気と水とが十分に確保されるため有機性排出物の分解速度が向上する。ここに、発酵分解による発熱により被処理物内の余剰な水分を蒸散させることで、被処理物内水分値を60%から65%に調整可能となるほか、発酵熱が床暖房室内の液体を加温する働きをするため、床暖房室内の液体の加温エネルギーを削減する効果が得られる。さらに、分解発熱による被処理物内の水分を蒸散させることで、処理室内の温度を微生物が育成・繁殖しやすい温度帯に安定維持できるという効果が得られる。In this way, the optimum temperature, air, and water necessary for the microorganisms that decompose the organic discharge are sufficiently secured, so that the decomposition rate of the organic discharge is improved. Here, by evaporating excess water in the object to be processed by heat generated by fermentation decomposition, the moisture value in the object to be processed can be adjusted from 60% to 65%. Since it works to warm, the effect of reducing the heating energy of the liquid in the floor heating room can be obtained. Furthermore, by evaporating the water in the object to be processed due to decomposition heat generation, it is possible to stably maintain the temperature in the processing chamber in a temperature range in which microorganisms can be easily grown and propagated.
尚、分解処理中は被処理物の温度が最大80℃近くまで昇温する。このように高温になることで有機性排出物を分解するのに有効な微生物以外の病原性の微生物やハエの卵等を死滅させることができる。その結果、良質の最終処理物が得られる。  During the decomposition process, the temperature of the object to be processed is raised to a maximum of nearly 80 ° C. In this way, it becomes possible to kill pathogenic microorganisms, fly eggs, and the like other than microorganisms effective for decomposing organic effluents due to the high temperature. As a result, a high quality final processed product is obtained.

分解処理室11で被処理物を分解するときに発生したガスは、排気ブロワ3で分解処理室11から排ガス処理装置、例えば生物脱臭装置へと導かれ、生物脱臭装置で浄化されたガスは大気へと放出される。一方、分解処理室内の最終処理物は、一旦ホッパ等に貯留・保管されて安定化させた後、袋詰めにされて土壌改良材や有機肥料としてリサイクルされる。The gas generated when the object to be processed is decomposed in the decomposition treatment chamber 11 is guided from the decomposition treatment chamber 11 to the exhaust gas treatment device, for example, a biological deodorization device by the exhaust blower 3, and the gas purified by the biological deodorization device is the atmosphere. Is released. On the other hand, the final treated product in the decomposition treatment chamber is once stored and stored in a hopper or the like, stabilized, then packed into a bag and recycled as a soil conditioner or organic fertilizer.
尚、有機性排出物中に無機成分がない場合には、殆どの固体有機物が二酸化炭素や水、アンモニア等に変換されるので、分解処理室内には残渣が発生しない。  When there are no inorganic components in the organic discharge, most solid organic matter is converted into carbon dioxide, water, ammonia, etc., and no residue is generated in the decomposition chamber.

このような構成と作用を有する第1実施形態の有機性排出物分解装置によれば、According to the organic waste decomposition apparatus of the first embodiment having such a configuration and action,
(1)分解処理室の床を温水を使って加熱するようにしたので、床全体を均一に加熱できる。従って、分解処理室内の被処理物が局部加熱されて有機性排出物を分解するのに有効な微生物が死滅することがないので有機性排出物の分解効率が向上する。  (1) Since the floor of the decomposition treatment chamber is heated using hot water, the entire floor can be heated uniformly. Therefore, since the processing object in the decomposition treatment chamber is locally heated and microorganisms effective for decomposing the organic discharge are not killed, the decomposition efficiency of the organic discharge is improved.
(2)床暖房室を分解処理室の床に対してボルト・ナットで着脱自在に構成したことにより、床暖房室の装着・取り外しが簡単にできるようになり、有機性排出物分解装置全体の点検・メンテナンスが容易となる。  (2) Since the floor heating room is detachable from the floor of the decomposition chamber with bolts and nuts, the floor heating room can be easily installed and removed, and the entire organic waste decomposition system Inspection and maintenance become easy.

次に、第2実施形態の有機性排出物分解装置について図面を参照しながら説明する。  Next, the organic waste decomposition apparatus of 2nd Embodiment is demonstrated, referring drawings.
図5〜図8に示すように、第2実施形態の有機性排出物分解装置10が第1実施形態の有機性排出物分解装置と構成が異なる点は、  As shown in FIGS. 5 to 8, the organic waste decomposition apparatus 10 of the second embodiment is different in configuration from the organic waste decomposition apparatus of the first embodiment.
(1)分解処理室内上部の空間をできるだけ小さくして、分解処理室41で発生したガスを早く外部へ排気しやすい構造にしている点である。  (1) The space in the upper part of the decomposition chamber is made as small as possible so that the gas generated in the decomposition chamber 41 can be easily exhausted to the outside quickly.
(2)また、床暖房室42の容積をできるだけ小さくし、床暖房室内の水をヒータ43で加熱し、万が一床暖房室内の圧力が必要以上に上昇してしまった場合には、リリーフ弁44を介して床暖房室内の過剰な圧力を系外へ逃がせるように構成した点である。  (2) Further, when the volume of the floor heating chamber 42 is made as small as possible and the water in the floor heating chamber is heated by the heater 43, and the pressure in the floor heating chamber rises more than necessary, the relief valve 44 It is the point which comprised so that the excess pressure in a floor-heating room could be escaped outside via system.
(3)そして攪拌手段45,46の攪拌軸47,48に取り付けられる攪拌翼49,49……の取り付け位置が大きく異なる点である。  (3) And the attachment positions of the stirring blades 49, 49... Attached to the stirring shafts 47, 48 of the stirring means 45, 46 are greatly different.

以下、これらのうち特に第1実施形態の有機性排出物分解装置と大きく異なる構成である攪拌手段45,46の構成と作用について図面を参照しながら説明する。  Hereinafter, the configuration and operation of the stirring means 45 and 46, which are particularly different from the organic waste decomposition apparatus of the first embodiment, will be described with reference to the drawings.
尚、第1実施形態の有機性排出物分解装置と同じ構成や作用については説明を省略する。  In addition, description is abbreviate | omitted about the same structure and effect | action as the organic waste decomposition | disassembly apparatus of 1st Embodiment.

図6に示すように、第2実施形態の有機性排出物分解装置10の攪拌翼49,49……は、回転軸の軸線方向に等間隔にかつ攪拌翼間の距離を半ピッチずらした180度反対側の位置にも攪拌翼49,49……を軸線方向に等間隔に取り付けている。そして、回転軸47,48を回転したときに、攪拌領域が一部重複するように、それぞれの取り付け位置を回転軸47,48の周りに互いに90度ずつ等角度間隔ずらした状態で取り付けられている。攪拌翼49,49……をこのように取り付けたことで、被処理物を攪拌・混合する場合、回転方向に大きな動力を与えることができるので、被処理物を大量処理する場合(被処理物の厚みが厚い場合)に適した攪拌手段45,46となる。   As shown in FIG. 6, the stirring blades 49, 49... Of the organic waste decomposition apparatus 10 of the second embodiment are equally spaced in the axial direction of the rotating shaft and the distance between the stirring blades is shifted by a half pitch. At the opposite side, stirring blades 49, 49,... Are attached at equal intervals in the axial direction. Then, when the rotation shafts 47 and 48 are rotated, the respective attachment positions are attached around the rotation shafts 47 and 48 at an equal angular interval by 90 degrees so that the stirring regions partially overlap. Yes. Since the stirring blades 49, 49,... Are attached in this manner, when stirring and mixing the workpiece, a large amount of power can be applied in the rotational direction. The agitation means 45 and 46 are suitable for the case where the thickness is large.

このように構成した第2実施形態の有機性排出物分解装置によれば、  According to the organic waste decomposition apparatus of the second embodiment configured as described above,
(1)分解処理室内で大量にガスが発生しても分解処理室内からすぐに排気されてしまうので新鮮な空気がすぐに供給され有機性排出物の分解速度が向上する。  (1) Even if a large amount of gas is generated in the decomposition treatment chamber, it is immediately exhausted from the decomposition treatment chamber, so that fresh air is immediately supplied and the decomposition rate of the organic emission is improved.
(2)床暖房室内を加圧した温水により加熱できる構造としたため床の加熱能力を大きくでき、床暖房室を小さくすることができる。  (2) Since the floor heating room can be heated by pressurized hot water, the floor heating capacity can be increased and the floor heating room can be reduced.
従って、有機性排出物の処理量が大きくなっても有機性排出物分解装置を必要以上に大きくしないですむ。  Therefore, it is not necessary to enlarge the organic waste decomposition device more than necessary even if the amount of organic waste processed increases.

次に、第1実施形態の有機性排出物分解装置を有機性排出物処理ラインに組み込んだ一実施形態の有機性排出物処理装置について図9〜図12を参照して説明する。  Next, an organic waste treatment apparatus according to an embodiment in which the organic waste decomposition apparatus according to the first embodiment is incorporated in an organic waste treatment line will be described with reference to FIGS.

本発明に係る有機性排出物処理装置50は、図9及び図12に示すように、レストランやホテル、食品加工工場等から排出される有機性排出物(主として固体有機廃棄物)を含んだ排水とトイレ排水等の生活排水との混合液を有機性排出物処理装置本体50aに導入するための2本の流入管51a,51bと、前記流入管51a,51bの後段に設けられ混合液の流量を調整する流量調整堰52と、前記流量調整堰52で調整された混合液から夾雑物(し渣)を除去する2基の回転式スクリーン53a,53bと、前記回転式スクリーン53a,53bで分離された夾雑物(し渣)を微生物の分解作用により処理する有機性排出物分解装置54と、これら全体を収納する有機性排出物処理装置本体50aとから主要部が構成される。As shown in FIGS. 9 and 12, the organic waste treatment apparatus 50 according to the present invention is a wastewater containing organic waste (mainly solid organic waste) discharged from restaurants, hotels, food processing factories, and the like. And two inflow pipes 51a, 51b for introducing a mixed liquid of domestic wastewater such as toilet wastewater into the organic waste treatment apparatus main body 50a, and a flow rate of the mixed liquid provided in the subsequent stage of the inflow pipes 51a, 51b Is separated by two rotary screens 53a and 53b for removing impurities from the mixed liquid adjusted by the flow rate control weir 52, and the rotary screens 53a and 53b. The main part is composed of an organic waste decomposition apparatus 54 for treating the contaminated waste (sediment) by the decomposition action of microorganisms and an organic waste treatment apparatus main body 50a for storing the whole.

流入管51a,51bは、有機性排出物処理装置本体50aの室内上部の一端に、2本並行に壁を貫通して設けられ、本体室内での配管は水平方向に対して90度下方に曲げられている。  The inflow pipes 51a and 51b are provided at one end of the organic upper part of the organic waste treatment apparatus main body 50a so as to penetrate two walls in parallel, and the piping in the main body room is bent downward by 90 degrees with respect to the horizontal direction. It has been.
流入管51a,51bの排出端では、上下を開口した箱(バッフル板)51cが流入管51a,51bの排出端の周りを囲うように配設されている。  At the discharge ends of the inflow pipes 51a and 51b, a box (baffle plate) 51c that is open at the top and bottom is disposed so as to surround the discharge ends of the inflow pipes 51a and 51b.

流量調整堰52は、図11に示すように、矩形の板の上部に、2枚の堰板52a,52bを鉛直方向に挿脱自在に設けることができるように、堰板52a,52bを案内するガイド溝を対向させて設けた門柱52bを2組(4本)立設したものである。As shown in FIG. 11, the flow control weir 52 guides the weir plates 52a and 52b so that the two weir plates 52a and 52b can be inserted and removed in the vertical direction at the upper part of the rectangular plate. Two sets (four) of gate columns 52b provided with guide grooves facing each other are erected.
以下、このような流量調整堰52を設けて後段の回転式スクリーン53への流量を調節する流量調節機構について図10及び図12を参照しながら説明する。  Hereinafter, a flow rate adjusting mechanism that provides such a flow rate adjusting weir 52 and adjusts the flow rate to the subsequent rotary screen 53 will be described with reference to FIGS.

通常、有機性排出物処理装置50は、図10に示すように、流量調整堰52の一側に堰板52aを一枚挿着し、堰が開口している第2回転式スクリーン53b側で混合液を処理している。第1回転式スクリーン53aは、何かトラブルを発生したときの予備機として設けられている。すなわち、運転している第2回転式スクリーン53bに目詰まり等が発生し、第2回転式スクリーン53bへ混合液の供給ができなくなったときには、流量調整堰52の堰板52aの挿着する位置を隣接する他側に切り換えて予備の第1回転式スクリーン53aで混合液を処理できるようにしている。Normally, as shown in FIG. 10, the organic waste treatment apparatus 50 has a single weir plate 52a inserted on one side of the flow rate adjusting weir 52 and the second rotary screen 53b side where the weir is open. The mixture is being processed. The first rotary screen 53a is provided as a spare machine when something goes wrong. That is, when clogging or the like occurs in the operating second rotary screen 53b and the liquid mixture cannot be supplied to the second rotary screen 53b, the position where the weir plate 52a of the flow rate adjusting weir 52 is inserted. Is switched to the adjacent other side so that the mixed liquid can be processed by the spare first rotary screen 53a.

また、第2回転式スクリーン53bの処理能力に対して混合液の供給量が多すぎる場合には、図12に示すように、堰板52aの高さをHとし、溢流板51dの高さをhとすると、H>hとなるように形成することにより、過剰分の液が溢流板51dを溢流して溢流管51eから外部へ排出され、常に一定量の混合液が第2回転式スクリーン53bで処理できるようになっている。  Further, when the supply amount of the mixed liquid is too much for the processing capability of the second rotary screen 53b, the height of the weir plate 52a is set to H and the height of the overflow plate 51d as shown in FIG. If h is set to H> h, excess liquid overflows the overflow plate 51d and is discharged to the outside from the overflow pipe 51e, so that a constant amount of the mixed liquid always rotates in the second rotation. It can be processed by the expression screen 53b.

回転式スクリーン53a,53bは、混合液中の夾雑物(し渣)を液中から分離するための固液分離装置であり、ここでは金網のベルトコンベアを用いた回転式スクリーンを使用している。通常は夾雑物(し渣)の捕捉効率を上げるため金網のバケットつきの回転式スクリーンを使用している。尚、回転式スクリーンとして微細目のバー回転式スクリーンも使用することもできる。  The rotary screens 53a and 53b are solid-liquid separators for separating impurities in the liquid mixture from the liquid, and here, a rotary screen using a wire mesh belt conveyor is used. . Normally, a rotating screen with a wire mesh bucket is used to increase the trapping efficiency of impurities. A fine bar rotary screen can also be used as the rotary screen.

有機性排出物分解装置54は、第1実施形態の有機性排出物分解装置1を配置しているが、第2実施形態の有機性排出物分解装置10を配置してもよい。有機性排出物分解装置54は、前段の第2回転式スクリーン53bで分離された夾雑物(し渣)をホッパ53dから供給され、微生物の分解作用により被処理物を分解処理するものである。  Although the organic waste decomposition apparatus 54 arrange | positions the organic waste decomposition | disassembly apparatus 1 of 1st Embodiment, you may arrange | position the organic waste decomposition | disassembly apparatus 10 of 2nd Embodiment. The organic waste decomposition apparatus 54 is supplied with the trash (seed) separated by the second rotary screen 53b in the previous stage from the hopper 53d, and decomposes the object to be processed by the decomposition action of microorganisms.

有機性排出物処理装置本体50aは、上述した主要部を構成する機器・配管をその内部に収納する箱体である。尚、2本の流入管51a,51bを設けた側壁と対向する側壁には、コンテナ式の出入口56が設けられている。また、有機性排出物処理装置本体50aの下部には、架台57が設けられている。  The organic waste disposal apparatus main body 50a is a box that accommodates the equipment and piping that constitute the main part described above. A container-type doorway 56 is provided on the side wall opposite to the side wall provided with the two inflow pipes 51a and 51b. Further, a gantry 57 is provided below the organic waste treatment apparatus main body 50a.

以下、図9〜図12を参照して有機性排出物処理装置50の作用について説明する。Hereinafter, the operation of the organic waste treatment apparatus 50 will be described with reference to FIGS.
レストランやホテル、食品加工工場等から排出される有機性排出物(主として固体有機廃棄物)を含んだ排水とトイレ排水等の生活排水との混合液が流入管51a,51bから有機性排出物処理装置本体50aへと供給される。流入管51a,51bから有機性排出物処理装置本体50aへ供給された混合液は、流入管51a,51bの周りを囲繞したバッフル板51cと衝突して、周囲に飛散することなく下方へと供給される。  A mixture of wastewater containing organic waste (mainly solid organic waste) discharged from restaurants, hotels, food processing factories, etc. and domestic wastewater such as toilet wastewater is treated with organic waste from the inflow pipes 51a and 51b. It is supplied to the apparatus main body 50a. The mixed liquid supplied from the inflow pipes 51a and 51b to the organic waste treatment apparatus main body 50a collides with the baffle plate 51c surrounding the inflow pipes 51a and 51b, and is supplied downward without being scattered around. Is done.

さらに、混合液は、流量調整堰52の堰板520が挿着されていない側を通流し第2回転式スクリーン53bへと流れていく。第2回転式スクリーン53bでは、混合液中の夾雑物(し渣)が分離される。このとき分離水は流出管53cを通じて排水処理装置へと導入され、浄化された分離水は河川に放流される。Further, the mixed liquid flows through the side of the flow rate adjusting weir 52 where the dam plate 520 is not inserted and flows to the second rotary screen 53b. In the second rotary screen 53b, impurities (sediment) in the mixed liquid are separated. At this time, the separated water is introduced into the waste water treatment apparatus through the outflow pipe 53c, and the purified separated water is discharged into the river.

第2回転式スクリーン53bで分離された夾雑物(し渣)は、一旦ホッパ53dで受けた後、有機性排出物分解装置54の投入口から有機性排出物分解装置54へと供給される。有機性排出物分解装置54に供給された夾雑物(し渣)は、攪拌手段により破砕・混合され、分解処理室内で微生物の分解作用を活性化するのに必要な温度、空気、水分が十分に確保される。その結果、有機性排出物分解処理室の中で被処理物は好適に分解処理される。  The contaminants separated by the second rotary screen 53b are once received by the hopper 53d, and then supplied from the inlet of the organic waste decomposition device 54 to the organic waste decomposition device 54. The impurities supplied to the organic waste decomposition device 54 are crushed and mixed by the stirring means, and sufficient temperature, air and moisture are required to activate the decomposition action of microorganisms in the decomposition treatment chamber. Secured. As a result, the object to be processed is suitably decomposed in the organic emission decomposition processing chamber.

このような構成と作用を有する一実施形態の有機性排出物処理装置によれば、According to the organic waste treatment apparatus of one embodiment having such a configuration and action,
(1)第1実施形態の有機性排出物分解装置を有機性排出物処理ラインに配設することにより、有機性排出物の搬送と分解が可能な有機性排出物処理装置を提供することができる。尚、有機性排出物処理ラインに第2実施形態の有機性排出物分解装置を組み込んでも同様な効果が得られる。  (1) To provide an organic waste disposal apparatus capable of transporting and decomposing organic waste by disposing the organic waste decomposition apparatus of the first embodiment in an organic waste treatment line. it can. The same effect can be obtained even if the organic waste decomposition apparatus of the second embodiment is incorporated in the organic waste treatment line.
(2)従来、スクリーンの後段で必要であった夾雑物(し渣)の破砕機や脱水機が不要になるため、省スペース、省コストが図れる。  (2) Since there is no need for a crusher or dehydrator for dust that was conventionally required in the latter stage of the screen, space and cost can be saved.
(3)回転式スクリーンでの混合液の処理量が常に一定となるように回転式スクリーン用の流量調整機構を設けたので、安定して処理ができる。  (3) Since the flow rate adjusting mechanism for the rotary screen is provided so that the processing amount of the mixed liquid on the rotary screen is always constant, processing can be performed stably.

本発明に係る有機性排出物処理装置に配設する第1実施形態の有機性排出物分解装置の正面部分断面図である。It is a front fragmentary sectional view of the organic waste decomposition | disassembly apparatus of 1st Embodiment arrange | positioned at the organic waste processing apparatus which concerns on this invention. 本発明に係る有機性排出物処理装置に配設する第1実施形態の有機性排出物分解装置の平面図である。It is a top view of the organic waste decomposition | disassembly apparatus of 1st Embodiment arrange | positioned at the organic waste processing apparatus which concerns on this invention. 図1のA−A断面図である。It is AA sectional drawing of FIG. 床暖房手段を説明するための図である。It is a figure for demonstrating a floor heating means. 本発明に係る有機性排出物処理装置に配設する第2実施形態の有機性排出物分解装置の正面部分断面図である。It is a front fragmentary sectional view of the organic waste decomposition | disassembly apparatus of 2nd Embodiment arrange | positioned at the organic waste processing apparatus which concerns on this invention. 本発明に係る有機性排出物処理装置に配設する第2実施形態の有機性排出物分解装置の平面図である。It is a top view of the organic waste decomposition | disassembly apparatus of 2nd Embodiment arrange | positioned at the organic waste processing apparatus which concerns on this invention. 図5のB−B断面図である。It is BB sectional drawing of FIG. 床暖房手段を説明するための図である。It is a figure for demonstrating a floor heating means. 本発明に係る一実施形態の有機性排出物処理装置の正面部分断面図である。It is a front fragmentary sectional view of the organic waste disposal device of one embodiment concerning the present invention. 本発明に係る一実施形態の有機性排出物処理装置の平面図である。It is a top view of the organic waste disposal apparatus of one embodiment concerning the present invention. 流量調整用堰の外形図である。It is an external view of the weir for flow rate adjustment. 回転式スクリーンの流量調整機構を説明するための図である。It is a figure for demonstrating the flow volume adjustment mechanism of a rotary screen.

符号の説明Explanation of symbols

1、10:有機性排出物分解装置
11、41:分解処理室
12:床暖房室
13:床
17;リリーフ弁
18:フランジ
19:天井
20:第1攪拌手段
21:第2攪拌手段
22:撹拌翼
23,24:回転軸
25:撹拌ロッド
26:掻き揚げ羽根
30:吸水口
31:排水口
32:ヒータ
35:断熱材
36:チャンバ
44:リリース弁
45,46:撹拌手段
47,48:撹拌軸
49:撹拌翼
50:有機性排出物処理装置
53a:第1回転式スクリーン
53b: 第2回転式スクリーン
DESCRIPTION OF SYMBOLS 1, 10: Organic waste decomposition device 11, 41: Decomposition processing room 12: Floor heating room 13: Floor
17: Relief valve 18: Flange 19: Ceiling 20: First stirring means 21: Second stirring means 22: Stirring blades 23, 24: Rotating shaft 25: Stirring rod 26: Raising blade 30: Water inlet 31: Drain port 32 : Heater 35: Heat insulating material 36: Chamber 44: Release valve 45, 46: Stirring means 47, 48: Stirring shaft 49: Stirring blade 50: Organic waste treatment apparatus 53a: First rotary screen 53b: Second rotary type screen

Claims (2)

有機性排出物分解装置を配置してなる有機性排出物処理装置であって、排水により有機性排出物を有機性排出物処理装置本体内に導入する有機性排出物流入管の排出端部の下流に、流量を調整する流量調整堰と、前記流量調整堰よりも高さの低い溢流板と、排水から有機性排出物を分離する回転式スクリーンを2基配置し、前記2基の回転式スクリーンの下流に有機性排出物分解装置を配置してなり、前記有機性排出物分解装置は、有機性排出物を微生物により分解する分解処理室と前記分解処理室の床全体を均一に加熱する床暖房手段とからなり、前記分解処理室は有機性排出物とこれを分解する微生物とを混合する攪拌手段を備え、攪拌手段は2つの回転軸とこの回転軸から軸径方向外方に突出する攪拌ロッドの先端部に鋭角な斜面を有する斜角錐体台の掻き揚げ羽根を設けてなり、2つの回転軸における掻き揚げ羽根は攪拌領域が一部重複するように取り付けられており、前記分解処理室の床は掻き揚げ羽根の回転軌跡に沿うように円弧状に形成されており、表面全体が断熱材で覆われていることを特徴とする有機性排出物処理装置。  An organic waste treatment device having an organic waste decomposition device disposed downstream of the discharge end of an organic waste inflow pipe that introduces organic waste into the body of the organic waste treatment device by drainage In addition, two flow adjusting weirs for adjusting the flow rate, an overflow plate having a height lower than that of the flow adjusting weir, and two rotary screens for separating the organic discharge from the waste water are arranged, and the two rotary type An organic waste decomposition device is disposed downstream of the screen, and the organic waste decomposition device uniformly heats the decomposition treatment chamber in which the organic waste is decomposed by microorganisms and the entire floor of the decomposition treatment chamber. The decomposition treatment chamber comprises an agitating means for mixing the organic discharge and the microorganisms that decompose the organic waste, and the agitating means protrudes outward in the axial radial direction from the two rotation shafts. A sharp slope on the tip of the stirring rod The slanting cone pyramid fraying blades are provided, and the fisting blades on the two rotating shafts are attached so that the stirring areas partially overlap, and the floor of the decomposition treatment chamber is the rotation trajectory of the filing blades The organic waste treatment apparatus is characterized in that it is formed in an arc shape so as to extend along the surface, and the entire surface is covered with a heat insulating material. 床暖房手段が、前記分解処理室の床全体を液体の加熱媒体により直接加熱する床暖房室と、この床暖房室内に前記液体を供給・排出する液体給排手段と、前記液体を床暖房室内で加熱して前記加熱媒体とするヒータとから構成されている請求項1に記載の有機性排出物処理装置。A floor heating means directly heats the entire floor of the decomposition treatment chamber with a liquid heating medium, a liquid supply / discharge means for supplying and discharging the liquid to and from the floor heating room, and the liquid to the floor heating room. The organic waste treatment apparatus according to claim 1, wherein the organic waste treatment apparatus is configured by a heater that is heated at a temperature as the heating medium.
JP2004131356A 2004-04-27 2004-04-27 Organic waste treatment equipment Expired - Fee Related JP3995662B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101469832B1 (en) * 2014-07-04 2014-12-09 코오롱이엔지니어링 주식회사 Disposal system for adulterated matter of food waste

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CN105693310B (en) * 2016-04-20 2022-04-19 常州市苏风机械有限公司 Stirring device of ultrahigh-temperature organic fertilizer fermentation equipment
CN105712756B (en) * 2016-04-20 2022-06-14 常州市苏风机械有限公司 Ultrahigh-temperature organic fertilizer fermentation equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101469832B1 (en) * 2014-07-04 2014-12-09 코오롱이엔지니어링 주식회사 Disposal system for adulterated matter of food waste

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