JP2005041761A - Garbage biological disposing apparatus corresponding to c/n ratio control - Google Patents

Garbage biological disposing apparatus corresponding to c/n ratio control Download PDF

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JP2005041761A
JP2005041761A JP2003303657A JP2003303657A JP2005041761A JP 2005041761 A JP2005041761 A JP 2005041761A JP 2003303657 A JP2003303657 A JP 2003303657A JP 2003303657 A JP2003303657 A JP 2003303657A JP 2005041761 A JP2005041761 A JP 2005041761A
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JP4196275B2 (en
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Yutaka Tsuchiya
豊 土屋
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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
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    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
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    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Abstract

<P>PROBLEM TO BE SOLVED: To provide a disposing apparatus in which garbage is biologically regenerated without depending on incineration to be recycled by converting a base material to a form to be usable repeatedly in municipality or a treated medium is regenerated by washing inorganic components accumulated in the treated medium with water. <P>SOLUTION: In the garbage biological disposing apparatus in which a C/N ratio control mode to convert the base material fermented at a high temperature of ≥80°C to have C/N ratio of 18-25 which is usable in municipality repeatedly and various controls using the phase lag arising by the change of the load on a motor as control information when primary fermentation and secondary fermentation are carried out with a virtual C/N ratio are performed. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

発明の詳細な説明Detailed Description of the Invention

この発明は、生ゴミを効率よく分解すると共にアンモニア臭の発生を伴わない微生物処理装置に関するものであり、装置単体での使用はもちろん、特に家庭から排出される生ゴミを再生利用して自治体で何度も同一基材で使用可能な形態に変換する方法、及びそれに適したC/N比率管理による生ゴミの微生物処理方法に使用できる微生物処理装置に関するものである。  The present invention relates to a microbial treatment apparatus that efficiently decomposes garbage and does not generate ammonia odor. Of course, the apparatus can be used alone, and in particular, municipalities can recycle and recycle garbage discharged from homes. The present invention relates to a method for converting to a form that can be used repeatedly on the same base material, and a microorganism treatment apparatus that can be used for a method for treating microorganisms of garbage by C / N ratio management suitable for the method.

特開平4−330979号公報には、発酵室を複数の室に分離し核複数の発酵室を、集中投入室と発酵専念室として使用することにより、発酵速度を速くし、投入量は減らすことの無いように構成された発明が提案されている。発酵周期を自由に設定できるため、従来の未発酵のコンポストに新しい生ゴミを追加する弊害が防げる優れた方法である。しかし、複数の室に分離しているため発酵状態に差が現れる。また、回動軸が同一のため片側の室の攪拌を停止することができない問題点がある。  In Japanese Patent Laid-Open No. 4-330979, a fermentation chamber is separated into a plurality of chambers, and a plurality of nuclear fermentation chambers are used as a concentrated input chamber and a dedicated fermentation chamber, thereby increasing the fermentation rate and reducing the input amount. There has been proposed an invention configured so as to eliminate the above. Since the fermentation cycle can be set freely, it is an excellent method that can prevent the harmful effect of adding new garbage to conventional unfermented compost. However, since it is separated into a plurality of chambers, a difference appears in the fermentation state. Moreover, since the rotation axis is the same, there is a problem that stirring of the chamber on one side cannot be stopped.

特開平11−192473号公報には、加熱手段は、攪拌槽の内部の上方に配置され前記攪拌槽に充填した食品加工残差を直接的に加熱する遠赤外線ヒータにて形成した発明が提案されている。直接加熱のため従来の方法より熱吸収率がよく優れた方法である。しかし、空気中に熱放射する方法のため部分加熱には使用できない問題点がある。  Japanese Patent Laid-Open No. 11-192473 proposes an invention in which the heating means is formed by a far-infrared heater that is disposed above the inside of the stirring tank and directly heats the food processing residual filled in the stirring tank. ing. Because of direct heating, this method has a better heat absorption rate than conventional methods. However, there is a problem that it cannot be used for partial heating because of the method of radiating heat into the air.

特開2002−126686号公報には、「ご飯モード」では例えば25分攪拌停止/5分攪拌のように、攪拌停止時間が攪拌時間に比べ長く設定されており、攪拌を停止させて加熱を行う時間を長くすることで、生ごみ(主にご飯)の表面を乾燥した状態にし餅化しにくくする発明が提案されている。しかし、熱源との位置関係は制御されないため加熱処理の最適化がなされていない問題点がある。  In Japanese Patent Laid-Open No. 2002-126686, in the “rice mode”, the stirring stop time is set to be longer than the stirring time, for example, 25 minutes stirring stopped / 5 minutes stirring, and heating is performed by stopping stirring. An invention has been proposed in which the surface of raw garbage (mainly rice) is dried to make it difficult to hatch by lengthening the time. However, since the positional relationship with the heat source is not controlled, there is a problem that the heat treatment is not optimized.

特開2002−136954号公報には、水道から供給される水をコントローラで調整してメッシュ状の底部の貫通穴に水を噴射し貫通穴の詰まりを解消する発明が提案されている。しかし、貫通穴の詰まりを解消するのに水道水を供給しなければならない問題点や貫通穴に対する位置が不特定多数である問題点がある。また、生ゴミ処理装置から排出される排水を再び生ゴミ処理装置に戻すループ機構の発明が提案されている。しかし、排水のpHが変動しているため排水を未処理で戻すことにより、異常発酵や発酵停止に陥る問題点がある。  Japanese Patent Application Laid-Open No. 2002-136554 proposes an invention in which water supplied from a water supply is adjusted by a controller to inject water into a through-hole at the bottom of the mesh to eliminate clogging of the through-hole. However, there is a problem that tap water must be supplied to eliminate clogging of the through hole and a problem that the positions with respect to the through hole are unspecified. Further, an invention of a loop mechanism for returning waste water discharged from the garbage processing apparatus to the garbage processing apparatus has been proposed. However, since the pH of the wastewater is fluctuating, there is a problem that abnormal fermentation or fermentation stoppage is caused by returning the wastewater to an untreated state.

実開平6−79730号公報には、排出される生ゴミ残飯等を給水用シャワーの水分と共に細かく粉砕させた後、加温された処理媒体中へ投入し泥状の生ゴミ残飯等を液化肥料と化す発明が提案されている。また、特開2002−136954号公報には、必要に応じて水分を補給する散水管を備えた発明が提案されている。どちらも微生物が活動するのに最適な環境に整えるのが目的であり、処理媒体中に発酵により蓄積した無機物質を水洗浄する課題は提案されていない。  In Japanese Utility Model Laid-Open No. 6-79730, discharged garbage is pulverized finely together with water from a shower for water supply, and then poured into a heated treatment medium to liquefy fertilizer. An invention has been proposed. Japanese Patent Application Laid-Open No. 2002-136554 proposes an invention including a watering pipe that replenishes moisture as necessary. In both cases, the objective is to prepare an optimum environment for the activity of microorganisms, and no problem has been proposed for washing inorganic substances accumulated by fermentation in the treatment medium.

特開平7−313957号公報には、担体及び有機物を収納する処理槽内の湿度を湿度センサによって、また温度を温度センサによって検出し、処理槽内の湿度と温度に応じて処理槽内の空気を送風機により排気し発酵条件を改善する発明が提案されている。しかし、内部の温度や湿度は外部の温度や湿度の影響を受ける問題点や湿度センサーが有機質の汚水に弱い問題点ある。  In JP-A-7-313957, the humidity in the treatment tank containing the carrier and the organic substance is detected by a humidity sensor and the temperature is detected by a temperature sensor, and the air in the treatment tank is determined according to the humidity and temperature in the treatment tank. An invention has been proposed in which fermentation conditions are improved by exhausting the air with a blower. However, the internal temperature and humidity are affected by the external temperature and humidity, and the humidity sensor is vulnerable to organic sewage.

特開平11−10119号公報には、排気の湿度が所定値以上となった場合に、制御手段によって処理槽内に流入する外気を加温し、処理槽内の水分制御を行い得るとともに、排気フィルタよりも下流側に排気湿度検出手段を配設して挨や結露に弱い排気湿度検出手段を確実に保護し、湿度センサーの使用寿命を改善する発明が提案されている。しかし、湿度センサーが有機質の汚水に弱いため抜本的改善が望まれている。  Japanese Patent Laid-Open No. 11-10119 discloses that when the humidity of the exhaust gas exceeds a predetermined value, the outside air flowing into the processing tank can be heated by the control means to control the moisture in the processing tank, and An invention has been proposed in which exhaust humidity detection means is disposed downstream of the filter to reliably protect the exhaust humidity detection means that is sensitive to dust and condensation, and to improve the service life of the humidity sensor. However, drastic improvement is desired because the humidity sensor is vulnerable to organic sewage.

特開平6−247785号公報には、発酵槽を上段に配置し、乾燥槽を下段に配し、発酵槽において発酵処理した処理物を開口部のシャッターを開いて乾燥槽に落下せしめるが、該開口部の周縁に堰を設けて、該堰によって該処理物の一部を受止して発酵槽に残存させ、次回の発酵工程の種とする発明が提案されている。しかし、上段と下段の2槽を有するため投入が困難になる問題点や処理槽の面積が2倍必要となる問題点がある。  In JP-A-6-247785, the fermenter is arranged in the upper stage, the drying tank is arranged in the lower stage, and the processed material fermented in the fermenter is dropped into the drying tank by opening the shutter of the opening. There has been proposed an invention in which a weir is provided at the periphery of the opening, a part of the processed product is received by the weir and left in the fermenter, and used as a seed for the next fermentation step. However, since there are two tanks, an upper stage and a lower stage, there are problems that it is difficult to input and that the area of the processing tank is doubled.

特開平9−150135号公報には、投入口を備えた一次処理槽と取出口を備えた二次処理槽を水平方向に連接して開口部により連通し、一次処理槽及び二次処理槽に開口部を挟んで平行に且つ回転軸心を水平方向に指向させて夫々軸支した一次攪拌軸及び二次攪拌軸に夫々一次攪拌具及び二次攪拌具を取付けて設け、これら一次攪拌具及び二次攪拌具を回転させる一次駆動モータ及び二次駆動モータを設け、有機廃棄物を処理する際に一次攪拌具及び二次攪拌具を互いに逆方向に回転させるよう一次駆動モータ及び二次駆動モータに電源を供給するとともに、一次処理槽の有機廃棄物を開口部を介して二次処理槽へ移送する際に一次攪拌具を有機廃棄物を処理する際の回転方向と逆方向に回転させるよう一次駆動モータに電源を供給する発明が提案されている。しかし、処理槽の面積が2倍必要となる問題点がある。  In JP-A-9-150135, a primary treatment tank provided with an inlet and a secondary treatment tank provided with an outlet are connected in a horizontal direction and communicated by an opening, and are connected to the primary treatment tank and the secondary treatment tank. A primary stirrer and a secondary stirrer are respectively attached to a primary stirrer shaft and a secondary stirrer shaft that are supported in parallel with the opening interposed in parallel and with the rotation axis oriented in the horizontal direction. A primary drive motor and a secondary drive motor provided with a primary drive motor and a secondary drive motor for rotating the secondary stirrer so that the primary stirrer and the secondary stirrer are rotated in opposite directions when treating organic waste Power is supplied to the primary processing tank and the primary stirrer is rotated in the direction opposite to the rotation direction when the organic waste is processed when the organic waste in the primary processing tank is transferred to the secondary processing tank through the opening. Supplying power to the primary drive motor There has been proposed. However, there is a problem that the area of the treatment tank is required twice.

特開平8−24825号公報には、モータにて回転駆動される攪拌羽根が納められている処理槽内に、水分調整用であり且つ微生物の担体であるおがくずや木粉からなる調整材をいれた生ゴミ処理機の上記攪拌羽根の回転数を検出する検出手段を備え、この検出手段で検出された回転数に基づいてモータの制御や分解促進用の加熱手段の制御を行う制御回路を備えている。生ゴミの投入量が多かったり、調整材も分解されてしまったために調整材による水分調整機能が十分作用しない状態となった時、あるいはモータロックが生じた時、攪拌羽根の回転数からこれらを検出して、対応する処理に移ることができる発明が提案されている。しかし、回転数の検出による制御では精度の要求には対応できない問題点がある。  In JP-A-8-24825, an adjustment material made of sawdust or wood powder, which is used for moisture adjustment and is a carrier of microorganisms, is placed in a processing tank in which a stirring blade that is rotationally driven by a motor is contained. And a control circuit for controlling the motor and the heating means for promoting decomposition based on the number of rotations detected by the detection means. ing. When the amount of raw garbage input is large or the adjustment material is also disassembled, the moisture adjustment function by the adjustment material does not work sufficiently, or when the motor lock occurs, these are determined from the rotation speed of the stirring blade. An invention has been proposed that can detect and move to a corresponding process. However, there is a problem that the control based on the detection of the rotational speed cannot meet the accuracy requirement.

特開2002−355571号公報には使用目的は違うが、駆動モータに連動する粉砕機構により生ごみを粉砕するディスポーザの粉砕終了検知装置であって、粉砕終了検知装置は、駆動モータに供給された電流の位相を検出する電流位相検出回路と、商用電源の交流電圧の電圧位相を検出する電圧位相検出回路と、電流位相検出回路により検出された電流位相と、電圧位相検出回路により検出された電圧位相の位相差を算出する乗算回路とを備え、乗算回路により算出された位相差と、駆動モータの予め設定された粉砕終了時の電流の基準値を比較し、該位相差が該基準値を超えたとき粉砕終了を判定する発明が提案されている。しかし、駆動モータに供給された電流の位相を検出する電流位相検出回路では、電流値が基準であり全電流から負荷変動に現れる部分の電流の部分検出を要求されるため、両波の整流によるクリップや電流位相検出信号の部分検出プログラムが必要となり、駆動モータの容量の違いや使用目的違いで対応できない問題点がある。  Japanese Patent Laid-Open No. 2002-355571 has a different purpose of use, but is a disposer crushing end detection device for crushing garbage by a crushing mechanism linked to a drive motor. The crushing end detection device is supplied to a drive motor Current phase detection circuit for detecting the phase of current, voltage phase detection circuit for detecting the voltage phase of the AC voltage of the commercial power supply, current phase detected by the current phase detection circuit, and voltage detected by the voltage phase detection circuit A multiplication circuit that calculates a phase difference between the phases, and compares the phase difference calculated by the multiplication circuit with a preset reference value of the current at the end of grinding of the drive motor, and the phase difference determines the reference value. There has been proposed an invention for determining the end of pulverization when exceeding. However, in the current phase detection circuit that detects the phase of the current supplied to the drive motor, the current value is the reference, and partial detection of the current that appears in the load fluctuation from the total current is required. A partial detection program for clips and current phase detection signals is required, and there is a problem that cannot be dealt with due to differences in drive motor capacity and purpose of use.

発明が解決しようとする課題Problems to be solved by the invention

従来の技術は、高効率発酵を目指すもので多くの設備で技術革新の報告がなされている。しかし、各技術は対処療法的な応用が多く常に最良の結果が得られていない欠点があった。また、一度生ゴミを投入すると所定の処理時間を必要とし、連続的に発生する生ゴミを処理するには非常に不便であった。また、周囲の環境に対応する配慮が少なく悪臭や不要成分を含む水蒸気を撒き散らすものも現存する。このような事態を鑑み高効率発酵は基より、悪臭や不要成分を含む水蒸気を処理でき、安全で清潔なC/N比率管理対応の生ゴミ微生物処理装置を提供することを目的とする。  Conventional technology is aimed at high-efficiency fermentation, and technical innovations have been reported in many facilities. However, each technique has many drawbacks, such as coping therapy, and the best results are not always obtained. In addition, once garbage is thrown in, it requires a predetermined processing time, and it is very inconvenient to process continuously generated garbage. In addition, there are some that disperse water vapor containing bad odors and unnecessary components with little consideration for the surrounding environment. In view of such circumstances, the purpose of high-efficiency fermentation is to provide a safe, clean C / N ratio management-compatible garbage microorganism treatment apparatus that can treat malodors and steam containing unnecessary components.

課題を解決するための手段Means for solving the problem

上記の目的を達成するために請求項1に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、C/N比率管理対応による単体処理モードと、生ゴミ投入回数や攪拌機構の負荷率を履歴管理する連続投入モードの制御が可能な管理制御を備えたことを特徴とするC/N比率管理対応の生ゴミ微生物処理装置である。  In order to achieve the above object, a first aspect of the present invention provides a microbial treatment of garbage including a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and management control. The apparatus is provided with management control capable of controlling a single processing mode corresponding to C / N ratio management and a continuous charging mode for history management of the number of times of throwing away garbage and the load factor of the stirring mechanism. It is a garbage microbe processing device that supports ratio management.

この発明は、発明者らが同時期に出願する特許願の整理番号P2003−CN1に記載する有機物を堆肥化するにあたり、全原料の水分率を60±5%、炭素と窒素の重量比(C/N)を25〜40、pH8で発酵を開始し1日で80度以上の発酵温度に上昇させることを特徴とする、C/N比率管理による生ゴミの微生物処理方法。再利用の戻し堆肥は、全原料の水分率を60±5%、炭素と窒素の重量比(C/N)を18〜25、pH8で発酵を開始し1日で80度以上の発酵温度に上昇させることを特徴とする、C/N比率管理による生ゴミの微生物処理方法。再利用後の再生は、炭素原(C)を補充して炭素と窒素の重量比の更正で行うことを特徴とする、C/N比率管理による生ゴミの微生物処理方法。有機物の発酵時のpH管理は、初期値pH8、中期値pH7〜8、後期値pH6.5〜7であることを特徴とするC/N比率管理による生ゴミの微生物処理方法を実行する単体処理モードと、生ゴミ投入回数や攪拌機構を駆動するモータの負荷変動により変化する駆動コイルの自己インダクタンス(L)の変化で生じる位相の遅れを、供給する商用電源の位相と比較して得た数値を制御情報として演算処理して、攪拌機構の負荷率を履歴管理する連続投入モードとを制御が可能なため、装置単体での使用はもちろん、特に家庭から排出される生ゴミを再生利用して自治体で何度も同一基材で使用可能な形態に変換する方法、及びそれに適したC/N比率管理による生ゴミの微生物処理方法に使用できる。  When composting the organic matter described in the serial number P2003-CN1 of the patent application filed by the inventors at the same time, the present invention has a moisture content of 60 ± 5% and a weight ratio of carbon and nitrogen (C / N) is started at 25 to 40 and pH 8, and is raised to a fermentation temperature of 80 ° C. or more in one day. A method for treating microorganisms of garbage by C / N ratio management. Reusable recycled compost is fermented at a moisture content of 60 ± 5%, carbon / nitrogen weight ratio (C / N) of 18-25, pH 8, and a fermentation temperature of 80 ° C or more per day. A method for treating microorganisms of garbage by C / N ratio management, characterized in that it is increased. Recycling after recycling is carried out by supplementing the carbon source (C) and correcting the weight ratio of carbon and nitrogen, and a method for treating microorganisms of garbage by C / N ratio management. Single substance treatment for performing a microorganism treatment method for garbage by C / N ratio management, wherein pH control during fermentation of organic matter is an initial value of pH 8, an intermediate value of pH 7-8, and a late value of pH 6.5-7 A numerical value obtained by comparing the phase delay caused by the mode and the change in the self-inductance (L) of the drive coil, which changes due to fluctuations in the load of the motor that drives the agitation mechanism, with the number of thrown garbage, and the phase of the commercial power supply Can be processed as control information, and the continuous charging mode that controls the load factor of the stirring mechanism can be controlled, so that it can be used not only as a single unit but also recycled from household waste. It can be used in a method of converting to a form that can be used repeatedly on the same base material in local governments, and a method for treating microorganisms of garbage by C / N ratio management suitable for it.

請求項2に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、仕切のない1つの発酵槽に生ゴミ投入口を左右に独立して設け、攪拌手が左右に独立して回動可能な攪拌機構を備え、生ゴミ投入口それぞれに対応する攪拌手が独立回動する手段と、生ゴミ投入口と関係なく同期回動する手段とを備え、投入条件を判断し投入可能な生ゴミ投入口を指示するランプとを備えたことを特徴とするC/N比率管理対応の生ゴミ微生物処理装置である。  According to a second aspect of the present invention, there is provided a garbage microbial treatment apparatus including a garbage input port, a compost outlet, a stirring mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and a management control. The fermenter is provided with a garbage inlet independently on the left and right, provided with a stirring mechanism in which the stirrer can be rotated independently on the left and right, and a stirrer corresponding to each of the garbage inlets independently rotates, A garbage that corresponds to C / N ratio management, comprising a means for rotating synchronously irrespective of the garbage input, and a lamp for determining an input condition and instructing an inputable garbage input. It is a microbial treatment apparatus.

この発明は、処理槽を1槽のままで効率よく発酵が開始されるように、生ゴミ投入口を左右に独立して設け、攪拌手が左右に独立して回動可能な攪拌機構を備え、従来の未発酵のコンポストに新しい生ゴミを追加する弊害を時間差投入により防止する。また、請求項3と、請求項5の動作が強調して行われ発酵槽の面積を増やすことなく処理できるのである。そして、過去の投入履歴と発酵物の回転負荷の条件を判断し投入可能な生ゴミ投入口を指示するランプを備えているため投入ミスが防止されるのである。  This invention includes a stirring mechanism in which a garbage input port is provided independently on the left and right sides and a stirring hand can be rotated independently on the left and right sides so that fermentation can be efficiently started with one processing tank remaining. Preventing the harmful effects of adding new garbage to conventional unfermented compost by introducing time difference. Further, the operations of claims 3 and 5 are emphasized and can be processed without increasing the area of the fermenter. In addition, since a lamp for judging the past loading history and the rotational load condition of the fermented product and instructing a garbage loading port that can be loaded is provided, a loading error is prevented.

請求項3に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、攪拌部位の先端が真の垂直方向から水平方向へ時計回りに45度進んだ位置にオイルを充填した保温装置を配し、攪拌部位の先端が真の垂直方向から水平方向へ反時計回りに45度遅れた位置に処理済みのコンポスト取り出し口を設け、制御により各位置に適宜停止することを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置である。  According to a third aspect of the present invention, there is provided a microbial treatment apparatus for garbage, comprising a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and a management control. A heat retaining device filled with oil is arranged at a position 45 degrees clockwise from the true vertical direction to the horizontal direction, and the tip of the stirring portion is positioned 45 degrees counterclockwise from the true vertical direction to the horizontal direction. 2. The garbage microorganism treatment apparatus for C / N ratio management according to claim 1, wherein a treated compost outlet is provided, and is appropriately stopped at each position by control.

この発明は、投入された生ゴミを指定された角度まで移動し効率よく保温や排出作業を行うものである。保温動作では、投入された生ゴミを45度進んだ位置に移動させ局部保温による効率的発酵を促進する。この局部保温に当たってはオイルヒータの原理を応用し放熱効率を向上させ省エネを実現している。コンポスト排出作業においては、45度遅れた位置までコンポストをすくい上げて停止させることで、それぞれの作業を効率よく実現できるのである。  According to the present invention, the input garbage is moved to a specified angle to efficiently perform heat insulation and discharge work. In the heat retaining operation, the input garbage is moved to a position advanced 45 degrees to promote efficient fermentation by local heat retaining. In this local heat insulation, the principle of the oil heater is applied to improve heat dissipation efficiency and realize energy saving. In the compost discharge work, each work can be efficiently realized by scooping up and stopping the compost to a position delayed by 45 degrees.

請求項4に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、排気処理機構と加温処理機構とを制御し、乾燥処理や加湿処理や除湿処理を行うことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置である。  According to a fourth aspect of the present invention, there is provided a garbage disposal apparatus comprising a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and management control. 2. The garbage microorganism treatment apparatus according to claim 1, which controls a temperature treatment mechanism and performs a drying process, a humidifying process, and a dehumidifying process.

この発明は、排気処理機構と加温処理機構とを制御し、乾燥処理では発酵熱に、加温処理機構によるブロアー内に組み込まれたヒータの発熱を加算し、空気と加温による乾燥に加え、蒸散した水蒸気を排出する排気処理機構を効率的に制御して行う。加湿処理では、加温処理機構と処理槽を結ぶ貯留室内に設けられたノズルに清水化された水を供給しブロアーの圧縮空気と共に処理槽内へ供給する。除湿処理では加温処理機構内のブロアーの回転速度を減じて、主に排気処理機構の水蒸気を排出する動作を優先する。この最適制御により各処理が高効率で行われるのである。  This invention controls the exhaust treatment mechanism and the warming treatment mechanism. In the drying process, the heat generated by the heater built into the blower by the warming treatment mechanism is added to the heat of fermentation, in addition to the drying by air and warming. Efficiently controls the exhaust treatment mechanism that discharges the evaporated water vapor. In the humidification process, the purified water is supplied to a nozzle provided in a storage chamber connecting the heating processing mechanism and the processing tank, and supplied into the processing tank together with the compressed air of the blower. In the dehumidifying process, priority is given mainly to the operation of discharging the water vapor of the exhaust processing mechanism by reducing the rotational speed of the blower in the heating processing mechanism. Each process is performed with high efficiency by this optimal control.

請求項5に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、一次発酵行程と二次発酵行程を攪拌部位の停止角度と回転の制御で行うことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置である。  According to a fifth aspect of the present invention, there is provided a microbial treatment apparatus for garbage comprising a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and management control. 2. The garbage microorganism treatment apparatus for C / N ratio management according to claim 1, wherein the next fermentation process is performed by controlling the stop angle and rotation of the stirring portion.

この発明は、粗攪拌のC/N比率が高い状態で高効率の一次発酵処理をし、充分に攪拌した状態で二次発酵を行うため、請求項3の生ゴミを45度進んだ位置に移動させ局部保温(移動完了後20時間以上停止)による一次発酵と、攪拌混合(5分動作)した二次発酵を行い攪拌混合率の違いで変化する仮装C/N比を用いて発酵させるため効率よく発酵が進み臭気の発生が抑制されるのである。  This invention performs high-efficiency primary fermentation with a high C / N ratio of coarse agitation, and performs secondary fermentation with sufficient agitation, so that the garbage of claim 3 is advanced 45 degrees. In order to ferment by using a temporary C / N ratio that changes depending on the difference in the stirring and mixing ratio, by performing primary fermentation by moving and keeping the local temperature (stopped for 20 hours or more after completion of movement) and secondary fermentation by stirring and mixing (operation for 5 minutes) The fermentation proceeds efficiently and the generation of odor is suppressed.

請求項6に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、攪拌部位の中心部先端と後端部をずらし、生ゴミの移動と、混合と、攪拌が行える攪拌手を備えたことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置である。  The invention according to claim 6 is a microbial treatment apparatus for garbage, comprising a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and management control. 2. The garbage microorganism treatment apparatus according to claim 1, further comprising a stirring hand capable of moving, mixing, and stirring the garbage by shifting the front end and the rear end. is there.

この発明は、投入された生ゴミに対して、攪拌部位の中心部先端が生ゴミを培養床に押し込む作用と空けられた空間に生ゴミを落とす作用を起こす。そして、遅れて到着する後端部により粗攪拌と共に生ゴミ混在部が移動する。このように攪拌部位の中心部先端と後端部の位置をずらしたことにより移動と混合が適度に行われるのである。  According to the present invention, an action of pushing the raw garbage into the culture bed and an action of dropping the raw garbage into the vacated space are caused with respect to the input raw garbage. And the garbage mixing part moves with rough stirring by the rear end part which arrives late. Thus, the movement and mixing are appropriately performed by shifting the positions of the front end and the rear end of the central portion of the stirring portion.

請求項7に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、攪拌機構を駆動するモータの負荷変動で変わる自己インダクタンス(L)の変化を位相変化として捉え商用電源の交流波形の位相と比較して、水分率コントロールやモータ異常検出やコンポスト完了を判定する判定手段を備えることを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置である。  A seventh aspect of the present invention drives a stirring mechanism in a garbage microbe treatment apparatus having a garbage input port, a compost outlet, a stirring mechanism, an exhaust processing mechanism, a heating processing mechanism, and a management control. It is characterized by having a judgment means for judging the moisture content control, motor abnormality detection and compost completion by comparing the change of the self-inductance (L) which changes with the load fluctuation of the motor as a phase change and comparing it with the phase of the AC waveform of the commercial power supply. It is a garbage microbe processing apparatus corresponding to the C / N ratio management of Claim 1.

この発明は、攪拌機構を駆動するモータの負荷変動により変化する駆動コイルの自己インダクタンス(L)の変化で生じる位相の遅れを、供給する商用電源の交流波形の位相と比較しているため、無負荷から全負荷の位相変化全てを用いることが可能となり、位相変化で得た数値を制御情報として演算処理し、水分率コントロールやモータ異常検出やコンポスト完了を判定するため手段としているため、1つの情報源からモータの保護はもちろん、負荷率の平均値から精度の高い制御が可能となり、位相変化で得た数値を演算処理して水分率を判断することが可能なため湿度センサーを排除でき、正回転・逆回転の適正動作や、コンポスト完了判定までの処理が可能となった。  The present invention compares the phase delay caused by the change of the self-inductance (L) of the drive coil, which changes due to the load fluctuation of the motor that drives the stirring mechanism, with the phase of the AC waveform of the commercial power supply to be supplied. Since it is possible to use all phase changes from the load to the entire load, the numerical value obtained by the phase change is processed as control information, and it is used as a means for determining moisture content control, motor abnormality detection and compost completion. In addition to protecting the motor from the information source, it is possible to control with high accuracy from the average value of the load factor, and it is possible to eliminate the humidity sensor because it can judge the moisture content by calculating the numerical value obtained by phase change, Appropriate forward / reverse operation and processing up to the completion of composting are now possible.

請求項8に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、発酵により蓄積した無機物質量の判定手段により、処理媒体中に蓄積した無機物質成分を水洗浄する水洗シャワーノズルを備えることを特徴とする、請求項1または7記載のC/N比率管理対応の生ゴミ微生物処理装置である。  The invention according to claim 8 is an inorganic material accumulated by fermentation in a microbial treatment apparatus for garbage, comprising a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and management control. 8. The garbage microorganism treatment apparatus for C / N ratio management according to claim 1 or 7, further comprising a washing shower nozzle for washing the inorganic substance component accumulated in the treatment medium with water by means of mass determination. is there.

この発明は、請求項7のコンポスト完了を判定する判定手段の信号を基に、発酵により蓄積した無機物質量を推定し、水洗シャワーノズルに給水する洗浄水の量をコントロールすることで、処理媒体中に蓄積した無機物質成分を水洗浄し処理媒体の負荷を軽くしたり、処理媒体を再生したりするのである。  The present invention estimates the amount of inorganic substance accumulated by fermentation based on the signal of the judging means for judging completion of composting according to claim 7, and controls the amount of washing water supplied to the washing shower nozzle in the processing medium. The inorganic substance component accumulated in the substrate is washed with water to lighten the load on the processing medium or to regenerate the processing medium.

請求項9に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、加温処理機構内と処理槽を結ぶ貯留室内に送風口清掃と加湿をする多機能ノズルを設けたことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置である。  The invention according to claim 9 is a microorganism disposal apparatus for garbage, comprising a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and management control. 2. The garbage microorganism processing apparatus for C / N ratio management according to claim 1, wherein a multi-function nozzle for cleaning and humidifying the air blowing port is provided in a storage chamber connecting the processing tank.

この発明は、加温処理機構と処理槽を結ぶ貯留室内に設けられたノズルに、排気処理機構のオゾン処理により清水化された水を加えて貯留室内の送風口清掃や処理槽内の湿度をコントロールする。この動作により送風能力の低下や湿度の低下が防止できるのである。  In this invention, water purified by ozone treatment of the exhaust treatment mechanism is added to a nozzle provided in the storage chamber connecting the heating treatment mechanism and the treatment tank, and the humidity in the storage tank is adjusted to clean the air blowing port in the storage chamber. To control. This operation can prevent a decrease in blowing capacity and a decrease in humidity.

請求項10に記載の発明は、生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、生ゴミ投入口を清掃するノズルを設けたことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置である。  According to a tenth aspect of the present invention, there is provided a garbage disposal device including a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating processing mechanism, and a management control. 2. The garbage microbe processing apparatus for C / N ratio management according to claim 1, wherein a nozzle for cleaning is provided.

この発明は、生ゴミ投入口に残留する処理物を生ゴミ投入口上面に設けられたノズルに圧縮空気や、排気処理機構のオゾン処理により清水化された水を加えて自動的に清掃するので常に清潔に投入口が保たれるのである。  According to the present invention, the processed material remaining in the garbage input port is automatically cleaned by adding compressed air or water purified by ozone treatment of the exhaust processing mechanism to the nozzle provided on the upper surface of the garbage input port. The inlet is always kept clean.

そして、この発明で使用している排気処理機構は、発明者らが同時期に出願する特許願の整理番号P2003−D1に記載する吸気管を備えた貯水槽内に、悪臭を含む排出ガスと水を吸入しながら攪拌するポンプと溶解筒を配設すると共に、オゾンガスと水を吸入しながら攪拌するポンプと水の改質筒との2系統の処理筒が配設され、処理水のpH管理調整器を設けた脱臭装置において、悪臭を含む排出ガスの温度を下げる放熱板を設けた吸気管と、悪臭を含む排出ガスを吸引する吸入パイプを設けたポンプと、旋回流を発生する機構を設けた溶解筒とが互いに連通し配設され、オゾンガスを吸引する吸入パイプを設けたポンプと、旋回流を発生する機構を設けた水の改質筒が貯水槽内で同居し、悪臭を含む排出ガスの溶解と水の改質を同時に行うことを特徴とする脱臭装置を、排気処理機構として使用している。  The exhaust treatment mechanism used in the present invention includes an exhaust gas containing bad odor in a water tank provided with an intake pipe described in the patent application serial number P2003-D1 filed at the same time by the inventors. A pump and a dissolving cylinder that stir while sucking water are arranged, and two treatment cylinders, a pump that stirs while sucking ozone gas and water and a water reforming cylinder, are arranged, and pH control of the treated water In a deodorizing apparatus provided with a regulator, an intake pipe provided with a heat sink that lowers the temperature of exhaust gas containing bad odor, a pump provided with a suction pipe that sucks exhaust gas containing bad odor, and a mechanism that generates a swirling flow The dissolving cylinder provided is connected to each other, the pump provided with the suction pipe for sucking ozone gas, and the water reforming cylinder provided with the mechanism for generating the swirling flow coexist in the water tank and contain bad odor. Simultaneous dissolution of exhaust gas and water reforming The deodorizing apparatus characterized by performing, are used as exhaust treatment system.

次に本発明の実施の形態を図1〜図12を参照して詳細に説明する。図1は本発明によるC/N比率管理対応の生ゴミ微生物処理装置の一実施例を示す一部切欠正面図、図2は側面断面図、図3は処理説明図、図4は攪拌部先端図、図5は判定手段の回路図、図6は判定手段の波形図、図7は水洗シャワーノズル図、図8は多機能ノズル詳細図、図9は気体と液体の流れ図、図10は排気処理機構正面断面図、図11は発酵曲線図、図12はC/N比率管理のフローチャート図を示す。  Next, an embodiment of the present invention will be described in detail with reference to FIGS. FIG. 1 is a partially cutaway front view showing an embodiment of a garbage microbe processing apparatus for C / N ratio management according to the present invention, FIG. 2 is a side sectional view, FIG. 3 is a process explanatory view, and FIG. FIG. 5, FIG. 5 is a circuit diagram of the determination means, FIG. 6 is a waveform diagram of the determination means, FIG. 7 is a flush shower nozzle diagram, FIG. 8 is a detailed diagram of a multifunction nozzle, FIG. 9 is a flow diagram of gas and liquid, and FIG. FIG. 11 is a fermentation curve diagram, and FIG. 12 is a flowchart of C / N ratio management.

図1、図2に示す生ゴミ微生物処理装置1外部には、左右に設けた生ゴミ投入口2と、左右に設けたコンポスト取り出し口3と、排気処理機構へ接続するパイプ4−1(4−2)あるいは5−1(5−2)と、加温処理機構6と、投入指示ランプ7が設けられている。生ゴミ微生物処理装置1内部には、処理槽8と、左右に設けた攪拌機構9と、左右に設けた駆動モータ10と、保温装置11と、水洗シャワーノズル12と、多機能ノズル13と、貯留室14と清掃ノズル15が設けられている。  1 and FIG. 2, outside the garbage microorganism treatment apparatus 1, the garbage input ports 2 provided on the left and right, the compost outlet 3 provided on the left and right, and the pipe 4-1 (4) connected to the exhaust treatment mechanism. -2) or 5-1 (5-2), a heating processing mechanism 6, and a closing instruction lamp 7. Inside the garbage microbe treatment apparatus 1, a treatment tank 8, a stirring mechanism 9 provided on the left and right, a drive motor 10 provided on the left and right, a heat retaining device 11, a washing shower nozzle 12, a multifunction nozzle 13, A storage chamber 14 and a cleaning nozzle 15 are provided.

生ゴミの経路は図3に示すごとく、生ゴミ投入口2を開けた状態で生ゴミ16を矢印17方向へ投入する。投入が完了し生ゴミ投入口2を図2の状態に閉めると、図示しないスイッチが動作し運転が開始され攪拌機構9が矢印18の方向に回転し、炭素原19と粗く攪拌され保温装置11の真上に生ゴミ20を形成し一次発酵し、一次発酵が完了すると全攪拌が行われ二次発酵に移行する。数ヶ月間運転を繰り返し発酵が完了した処理物は外扉21を開け、コンポスト取り出し口3を開放して矢印22の方向へ取り出す。  As shown in FIG. 3, the path of the garbage is input in the direction of the arrow 17 with the garbage input port 2 opened. When the charging is completed and the garbage inlet 2 is closed to the state shown in FIG. 2, a switch (not shown) is operated to start operation, and the stirring mechanism 9 rotates in the direction of the arrow 18 to be roughly stirred with the carbon raw material 19 to be kept warm. The raw garbage 20 is formed immediately above the primary fermentation, and the primary fermentation is completed. When the primary fermentation is completed, the entire agitation is performed, and the secondary fermentation is started. After the operation has been repeated for several months and the fermentation is completed, the outer door 21 is opened, the compost outlet 3 is opened, and the processed product is taken out in the direction of the arrow 22.

処理水の経路は図9に示すごとく、排気処理機構から接続パイプ5−1を経由して清水化された水23−1を導入する。図示しない電磁弁を開放することにより、水洗シャワーノズル12と清掃ノズル15より霧状の水23−2と23−3を必要に応じて噴霧する。役目を果たした水は、処理槽8の底部に設置された図8に示す多機能ノズル13の隙間を通り、24−1、24−2、24−3のように流れ貯留室14に貯まる。貯留室14に貯まった水23−4は接続パイプ5−2を経由して排気処理機構に戻される。  As shown in FIG. 9, the treated water path introduces purified water 23-1 from the exhaust treatment mechanism via the connection pipe 5-1. By opening an electromagnetic valve (not shown), mist-like water 23-2 and 23-3 are sprayed as necessary from the washing shower nozzle 12 and the cleaning nozzle 15. The water which played the role passes through the clearance gap between the multifunctional nozzles 13 shown in FIG. 8 installed at the bottom of the treatment tank 8 and flows into the storage chamber 14 like 24-1, 24-2 and 24-3. The water 23-4 stored in the storage chamber 14 is returned to the exhaust treatment mechanism via the connection pipe 5-2.

処理槽内空気の経路は図9に示すごとく、処理槽8の上部の空気25−1を加温処理機構6が吸引し、空気25−2を経由して加熱部26で必要に応じて暖められ、25−3、25−4を経由して貯留室14に貯められる。貯留室14に貯められた空気は図8に示す多機能ノズル13の隙間を通り、処理水とは逆に24−3、24−2、24−1を経由して処理槽8の内部へ空気25−5として放出される。  As shown in FIG. 9, the air path in the upper part of the processing tank 8 is sucked by the heating processing mechanism 6 and heated by the heating unit 26 via the air 25-2, as shown in FIG. 9. And stored in the storage chamber 14 via 25-3 and 25-4. The air stored in the storage chamber 14 passes through the gap between the multi-function nozzles 13 shown in FIG. 8 and flows into the inside of the processing tank 8 via 24-3, 24-2 and 24-1 contrary to the processing water. Released as 25-5.

外気の吸入経路は図9に示すごとく、排気処理機構でオゾンガス発生時に使用され、オゾン反応で元の状態に戻された酸素27−1を、接続パイプ4−2を経由して空気25−4の流れに乗せ貯留室14に導入する。貯留室14に導入された酸素27−1は図8に示す多機能ノズル13の隙間を通り、空気25−4と共に24−3、24−2、24−1を経由して処理槽8の内部へ酸素27−3として放出され微生物の活動を活発にする。使用後の排気27−2は接続パイプ4−1を経由して排気処理機構に戻される。  As shown in FIG. 9, the outside air intake path is used when ozone gas is generated by the exhaust treatment mechanism, and oxygen 27-1 returned to the original state by the ozone reaction is supplied to the air 25-4 via the connection pipe 4-2. And introduced into the storage chamber 14. The oxygen 27-1 introduced into the storage chamber 14 passes through the gap between the multifunctional nozzles 13 shown in FIG. 8 and passes through the air 25-4 along with 24-3, 24-2 and 24-1 to the inside of the processing tank 8. It is released as oxygen 27-3 and activates the activity of microorganisms. The exhaust 27-2 after use is returned to the exhaust treatment mechanism via the connection pipe 4-1.

排気処理経路は図9、図10に示すごとく、排気処理機構28の吸気管29と接続された接続パイプ4−1の排気は、ポンプ30に吸引され処理タンク31内の水と気液混合され、溶解筒32で水に吸収され、排気成分を含んだ水33となる。一方、オゾンガス吸気管34には酸素発生器に接続したオゾン生成器が接続されていて、ポンプ35に吸引され処理タンク31内の排気成分を含んだ水33と気液混合され、溶解筒36でオゾンガスにより酸化改質され清水化された水37となる。その他、接続パイプ4−2は排気処理機構28の圧力放出口38と、接続パイプ5−2はポンプを経由して排気処理機構28の注水口39と、接続パイプ5−1もポンプを経由して排気処理機構28の排水口40と接続されている。  As shown in FIGS. 9 and 10, the exhaust treatment path is exhausted by the connection pipe 4-1 connected to the intake pipe 29 of the exhaust treatment mechanism 28 and is sucked by the pump 30 and mixed with water in the treatment tank 31. The water is absorbed by the dissolution cylinder 32 and becomes water 33 containing exhaust components. On the other hand, an ozone generator connected to an oxygen generator is connected to the ozone gas intake pipe 34, and it is sucked into the pump 35 and mixed with water 33 containing exhaust components in the treatment tank 31, It becomes water 37 that has been oxidized and reformed by ozone gas. In addition, the connection pipe 4-2 is connected to the pressure discharge port 38 of the exhaust treatment mechanism 28, the connection pipe 5-2 is connected to the water injection port 39 of the exhaust treatment mechanism 28 via a pump, and the connection pipe 5-1 is also connected to the connection pipe 5-1. And connected to the drain port 40 of the exhaust treatment mechanism 28.

制御の情報処理はモード設定の選択や、生ゴミ投入口2の開閉状況や、図示しない温度計の温度推移や、積算加温時間や、排気処理機構28の運転時間や、攪拌機構9を駆動する駆動モータ10の位相情報により得られた情報を元に実行される。特に攪拌機構9を駆動する駆動モータ10の位相情報は、部分検出を必要としない無負荷から全負荷の位相変化の全てを用いることが可能な、駆動コイルの自己インダクタンス(L)の変化で生じる位相の遅れを、供給する商用電源の交流波形の位相と比較する方式のため、1つの情報源からモータの保護はもちろん、水分率を判断することや、正回転・逆回転の適正動作や、コンポスト完了判定までの処理が可能となる。  The information processing of the control selects the mode setting, the open / close state of the garbage input port 2, the temperature transition of a thermometer (not shown), the accumulated heating time, the operating time of the exhaust processing mechanism 28, and the stirring mechanism 9 This is executed based on information obtained from the phase information of the driving motor 10 to be operated. In particular, the phase information of the drive motor 10 that drives the stirring mechanism 9 is generated by a change in the self-inductance (L) of the drive coil that can use all of the phase changes from no load to full load that do not require partial detection. Because it is a method that compares the phase lag with the phase of the AC waveform of the commercial power supply that is supplied, not only protects the motor from one information source, but also determines the moisture content, proper operation of forward and reverse rotation, Processing up to the completion of composting is possible.

図5の回路は、商用電源の交流電圧をアイソレーションし電子回路に入力できるように設けた電圧変成トランス41と、駆動モータ10に直列に接続された自己インダクタンス検出トランス42により構成されている。回路の作用は電圧変成トランス41では、電子回路の入力電圧に適合する値に調整された出力波形の位相は商用電源の位相と同じで固定です。しかし、駆動モータ10の駆動コイルには磁束が生じます。そこで、導線に交差する鎖交磁束数Φ=駆動コイルの自己インダクタンスL×回路電流1が成立しますので、負荷率が変化すれば駆動コイルの自己インダクタンスLも変化することになります。  The circuit shown in FIG. 5 includes a voltage transformation transformer 41 provided so that an AC voltage of a commercial power supply can be isolated and input to an electronic circuit, and a self-inductance detection transformer 42 connected in series to the drive motor 10. In the voltage transformation transformer 41, the phase of the output waveform adjusted to a value that matches the input voltage of the electronic circuit is the same as that of the commercial power supply and is fixed. However, magnetic flux is generated in the drive coil of the drive motor 10. Therefore, the number of flux linkages intersecting the conductor Φ = self-inductance L of the drive coil x circuit current 1 is established, so if the load factor changes, the self-inductance L of the drive coil will also change.

交流電流の変化に対して、駆動モータ10の駆動コイルには磁束数の変化を阻止する作用が生じます。これは駆動モータ10の駆動コイルの両端電圧の発生で知ることができますが、交流電源に駆動モータ10を接続した状態では交流電源の位相しか検出できません。そこで、駆動モータ10のコイルの一部としてトランス42の一次コイルを作用させれば、トランス42の二次側には自己誘導で発生する電圧を確保できます。自己誘導で発生する電圧波形が駆動モータ10の駆動コイルの両端に発生する電圧波形と位相的には同相であるため、アイソレーションされた駆動モータ10の出力波形の位相として捉えることが可能となる。  In response to the change in AC current, the drive coil of the drive motor 10 acts to prevent the change in the number of magnetic fluxes. This can be known from the generation of the voltage across the drive coil of the drive motor 10, but only the phase of the AC power supply can be detected when the drive motor 10 is connected to the AC power supply. Therefore, if the primary coil of the transformer 42 is operated as a part of the coil of the drive motor 10, a voltage generated by self-induction can be secured on the secondary side of the transformer 42. Since the voltage waveform generated by self-induction is in phase with the voltage waveform generated at both ends of the drive coil of the drive motor 10, it can be understood as the phase of the output waveform of the isolated drive motor 10. .

図5の電圧変成トランス41でアイソレーションされた商用電源の交流電圧の出力1の波形が図6で示す波形43で、駆動モータ10の自己インダクタンス検出トランス42でアイソレーションされた交流電圧の出力2の波形が図6で示す波形44や波形45となる。負荷率の違いで生じる位相の変化はt1やt2のような時間の変化に置き換えることができる。  The waveform 1 of the AC voltage output 1 of the commercial power source isolated by the voltage transformation transformer 41 of FIG. 5 is the waveform 43 shown in FIG. 6 and the output 2 of the AC voltage isolated by the self-inductance detection transformer 42 of the drive motor 10. Are the waveform 44 and the waveform 45 shown in FIG. A change in phase caused by a difference in load factor can be replaced with a change in time such as t1 or t2.

本発明の生ゴミ微生物処理装置1により、図12示すC/N比率管理対応による単体処理モード1(A1)の処理を図11のC/N比40(E)で実行する場合は、全原料の水分率を60±5%、炭素と窒素の重量比(C/N)を40(E)、pH値を8に原料調整し、処理槽8の全容量分を一度に投入して発酵を開始し1日で80度以上の発酵温度に上昇させる。  When the processing in the single processing mode 1 (A1) corresponding to the C / N ratio management shown in FIG. 12 is executed with the C / N ratio 40 (E) in FIG. The raw material is adjusted to a moisture content of 60 ± 5%, carbon to nitrogen weight ratio (C / N) of 40 (E), and a pH value of 8, and the entire volume of the treatment tank 8 is added at a time for fermentation. Start and raise to a fermentation temperature of 80 degrees or more in one day.

単体処理モード1では、図示しない温度調節器を発酵温度80度にセットし、加温処理機構6内の加熱部26を動作させ発酵処理を行う。図11のC/N比40(E)での発酵では、運転開始直後に加熱部26が働くが、夏場10時間、冬場20時間程度で所定の発酵温度に達するため加熱部26への通電はOFFされる。しかし、菌体の状態や酸素不足や外気温が異常に低下した場合は通電が開始され80度以上の発酵温度は保たれる。  In the single processing mode 1, a temperature controller (not shown) is set to a fermentation temperature of 80 degrees, and the heating unit 26 in the heating processing mechanism 6 is operated to perform a fermentation process. In the fermentation at the C / N ratio of 40 (E) in FIG. 11, the heating unit 26 works immediately after the start of operation. However, since the predetermined fermentation temperature is reached in the summer 10 hours and the winter 20 hours, It is turned off. However, when the bacterial cell state, oxygen shortage, or outside temperature is abnormally decreased, energization is started and the fermentation temperature of 80 ° C. or higher is maintained.

攪拌は酸素供給や温度分布や発酵状態を均一にするため、5rpmで2分間実施し24時間置きに1回行う。最初の攪拌方向は左右に設けた攪拌機構9が双方共に正回転し、次のサイクルでは右の攪拌機構9が逆回転で左の攪拌機構9が正回転し、次のサイクルでは攪拌機構9が双方共に逆回転し、次のサイクルでは右の攪拌機構9が正回転で左の攪拌機構9が逆回転し、次のサイクルで元の回転方向に戻る攪拌サイクルを繰り返す。この反転動作を伴う攪拌により、短時間の攪拌でも原料が充分に攪拌され均一な発酵が可能となる。  Stirring is performed at 5 rpm for 2 minutes and once every 24 hours in order to make the oxygen supply, temperature distribution, and fermentation state uniform. In the first agitating direction, both the agitating mechanisms 9 provided on the left and right rotate in the forward direction. In the next cycle, the agitating mechanism 9 on the right rotates in the reverse direction and the agitating mechanism 9 on the left rotates in the forward direction. Both of them rotate in the reverse direction, and in the next cycle, the right stirring mechanism 9 rotates forward and the left stirring mechanism 9 rotates reversely, and in the next cycle, the stirring cycle returning to the original rotation direction is repeated. Due to the agitation accompanied by the reversal operation, the raw materials are sufficiently agitated even in a short period of time and uniform fermentation is possible.

温度調節と攪拌が実行され継続発酵A2を経由して約45日目には、処理された部材のC/Nが15〜20で窒素1%程度で水分率40%程度の値を示します。A3での測定C/N比が25を超えている場合は、再度継続発酵A2へ移行しC/Nの低下を促進する。  On the 45th day after temperature control and agitation and continuous fermentation A2, the C / N of the processed material is 15 to 20, the nitrogen content is about 1%, and the moisture content is about 40%. When the measured C / N ratio at A3 exceeds 25, the process proceeds to continuous fermentation A2 again to promote the reduction of C / N.

A3での測定C/N比が15〜25であれば再利用原料A4の完成である。この再利用原料A4の水分率を調整し、調整後のC/N比が18〜25であるかA6で測定する。A6での測定C/N比が18を下まわっている場合は再度、調整A5へ移行する。  If the measured C / N ratio at A3 is 15 to 25, the recycled material A4 is completed. The water content of the reused raw material A4 is adjusted, and whether the C / N ratio after adjustment is 18 to 25 is measured by A6. If the measured C / N ratio at A6 is less than 18, the process proceeds to adjustment A5 again.

A6での測定C/N比が、18〜25であれば自治体で使用可能な戻し堆肥A7の完成である。この戻し堆肥A7を自治体で使用する小型の簡易コンポスター(自然発酵式)で培養床として使い生ゴミの微生物処理をする。  If the measured C / N ratio at A6 is 18 to 25, the return compost A7 that can be used by the local government is completed. The returned compost A7 is used as a culture bed in a small simple poster (natural fermentation type) used in local governments for microbial treatment of garbage.

A8では発生臭気を官能的に評価して、回収業者にリサイクル資材A9を引き渡す。リサイクル資材A9は自治体での使用でC/N比が変化するため、分解、発酵、などの堆肥としての品質が低下しC/N比8程度になっているので、炭素原を補充して炭素と窒素の重量比の更正と水分率の更正A10を行う。  In A8, the generated odor is sensuously evaluated, and the recycled material A9 is delivered to the collection company. Since the C / N ratio of recycled material A9 changes when used in local governments, the quality of compost, such as decomposition and fermentation, is reduced to a C / N ratio of about 8. And nitrogen weight ratio correction and moisture content correction A10.

本発明の生ゴミ微生物処理装置1により、図12示すC/N比率管理対応による単体処理モード2(A11)の再生発酵処理の更正A10の更正値を図11のC/N比25(D)で実行する場合は、全原料の水分率を60±5%、pH値を8に原料調整し、処理槽8の全容量分を一度に投入して発酵を開始し1日で80度以上の発酵温度に上昇させる。  By the garbage microbe processing apparatus 1 of the present invention, the correction value A10 of the regenerative fermentation process in the single processing mode 2 (A11) corresponding to the C / N ratio management shown in FIG. 12 is set to the C / N ratio 25 (D) in FIG. , The raw material is adjusted to a moisture content of 60 ± 5% and a pH value of 8, and the entire volume of the treatment tank 8 is charged at a time to start fermentation, and the temperature of 80 ° C. or more is increased in one day. Increase to fermentation temperature.

温度調節と攪拌が単体処理モード1と同様に実行され、調整発酵A12を経由し、約17日目には処理された部材のC/Nが15〜20で窒素1%程度で水分率40%程度の値を示します。A13での測定C/N比が25を超えている場合は、再度継続発酵A12へ移行する。単体処理モード2の再生発酵処理では、同じ機械化プロセスで再生発酵A11を行い、自治体で使用するC/N比18〜25の戻し堆肥A7に再生するのである。  Temperature control and agitation are carried out in the same manner as in the unit treatment mode 1, and after about 17 days, the C / N of the treated member is 15 to 20 and the nitrogen content is about 1% and the moisture content is 40% via the adjusted fermentation A12. Indicates the degree value. When the measured C / N ratio at A13 exceeds 25, the process proceeds to continuous fermentation A12 again. In the regenerative fermentation process in the single-unit treatment mode 2, regenerative fermentation A11 is performed by the same mechanized process and regenerated to return compost A7 having a C / N ratio of 18 to 25 used in the local government.

本例では単体処理モード1で図11のC/N比40(E)での処理と、単体処理モード2でC/N比25(D)で再生発酵処理を実行する場合を述べているが、C/N比50(F)の発酵処理では、自己発酵熱による発酵温度が1日で80度以上の温度に上昇させることが不可能であった。これは、窒素原不足のため微生物の活動エネルギーが不足するためと推察される。このC/N比でも、加熱部26の熱エネルギーを加えれば、発酵温度を1日で80度以上の温度に上昇させることが可能なため、限定条件付きなら発酵処理は成立する。以上のことから自治体で使用するC/N比18〜25の戻し堆肥A7に再生する条件は、C/N比25〜C/N比50の範囲が発酵処理の適合条件である。  In this example, the case where the processing at the C / N ratio 40 (E) in FIG. 11 in the single processing mode 1 and the regeneration fermentation processing at the C / N ratio 25 (D) in the single processing mode 2 is executed is described. In the fermentation process with a C / N ratio of 50 (F), it was impossible to increase the fermentation temperature by self-fermentation heat to a temperature of 80 ° C. or more in one day. This is presumed to be due to the lack of microbial activity energy due to the lack of nitrogen source. Even with this C / N ratio, if the heat energy of the heating unit 26 is applied, the fermentation temperature can be raised to a temperature of 80 ° C. or more in one day. From the above, the conditions for regeneration to the return compost A7 having a C / N ratio of 18 to 25 used in the local government are in the range of the C / N ratio 25 to 50 of the C / N ratio are suitable conditions for fermentation treatment.

単体処理モード1と2では、処理槽8の全容量分を一度に投入して発酵完了まで処理するため、投入指示ランプ7と保温装置11は使用しない。また、排気処理機構28は水分を補給する加湿動作には必要に応じて使用されるが、除湿動作は使用しないため急激な湿度の変化は起こらない。  In the single processing modes 1 and 2, since the entire capacity of the processing tank 8 is charged at a time until the fermentation is completed, the charging instruction lamp 7 and the heat retaining device 11 are not used. Further, the exhaust treatment mechanism 28 is used as needed for the humidifying operation for replenishing moisture, but since the dehumidifying operation is not used, a rapid change in humidity does not occur.

本発明の生ゴミ微生物処理装置1により日々の生ゴミを処理する連続投入モードで実行する場合は、図3に示すごとく炭素原19を予め培養床としてセットし、コンポスト取り出し口3も図2の位置に固定されている状態で使用する。この炭素原19は、木材チップ、モミ殻、稲わら、麦わら、落葉、樹皮などから適宜選択される。  When the processing is performed in a continuous charging mode in which daily garbage is processed by the garbage microorganism processing apparatus 1 of the present invention, the carbon source 19 is set as a culture bed in advance as shown in FIG. 3, and the compost outlet 3 is also shown in FIG. Use with fixed position. The carbon source 19 is appropriately selected from wood chips, fir shells, rice straw, straw, fallen leaves, bark, and the like.

生ゴミ16が投入され生ゴミ投入口2を閉めると、図示しない検出機構が動作し、連動して図示しない電磁弁を開放し清掃ノズル15より霧状の水23−3をセットされた時間(0〜15秒)噴霧し投入口付近に残った生ゴミを洗い流す。同時期に攪拌機構9が矢印18の方向に回転し、図4に示す攪拌部先端図の攪拌棒46が生ゴミを培養床に押し込む作用と、空けられた空間にゴミを落とす作用を発揮する。そして、遅れて到着する攪拌棒47、48がすくい板49と協調して移動と攪拌と混合を実行する。  When the garbage 16 is introduced and the garbage inlet 2 is closed, a detection mechanism (not shown) is operated, and a solenoid valve (not shown) is opened in conjunction with the time when the atomized water 23-3 is set from the cleaning nozzle 15 ( (0 to 15 seconds) Spray to wash away any garbage left near the inlet. At the same time, the stirring mechanism 9 rotates in the direction of the arrow 18, and the stirring rod 46 in the tip of the stirring unit shown in FIG. 4 exerts the action of pushing the garbage into the culture bed and the action of dropping the garbage into the vacated space. . Then, the stirring rods 47 and 48 that arrive late are moved, stirred and mixed in cooperation with the rake plate 49.

炭素原19と粗く攪拌され保温装置11の真上にC/N比の低い状態の生ゴミ20を形成し一次発酵を開始する。この一次発酵はオイルを充填した保温装置11の局部保温と、加温処理機構6の加熱部26より発生する熱で加温された空気25−5(図9参照)と協調して高速高温発酵を可能にする。  A raw agglomerate 20 having a low C / N ratio is formed just above the carbon source 19 and agitated roughly, and the primary fermentation is started. In this primary fermentation, high-speed and high-temperature fermentation is performed in cooperation with the local heat retention of the heat retention device 11 filled with oil and the air 25-5 (see FIG. 9) heated by the heat generated from the heating unit 26 of the heat treatment mechanism 6. Enable.

この一次発酵の時間は、プログラムの選択により4時間〜24時間の設定が可能であり、一次発酵が完了すると全攪拌が5rpmで5分動作し二次発酵に移行する。このように、攪拌機構の一時停止と全攪拌による攪拌混合率の違いで変化する仮装C/N比を用いて一次発酵や二次発酵させるため効率よく発酵が進み臭気の発生が抑制される。  The primary fermentation time can be set from 4 hours to 24 hours depending on the selection of the program. When the primary fermentation is completed, the total agitation is performed at 5 rpm for 5 minutes, and the secondary fermentation is started. Thus, since primary fermentation and secondary fermentation are performed using the temporary C / N ratio that changes depending on the difference in the stirring and mixing ratio due to the temporary suspension of the stirring mechanism and the total stirring, the fermentation proceeds efficiently and the generation of odor is suppressed.

連続投入モードでは左右の投入口2を使い分ける。左右の投入口2の投入指示は投入指示ランプ7により行われ、1日置に投入指示が変わるモード1と1週間置きに投入指示が変わるモード2と1ヶ月置に投入指示が変わるモード3を備えている。このモード切替は、投入される生ゴミの量や内容物の分解特性を考慮して選択する。野菜類が中心で塩分を含まない生ゴミではモード1を、畜産の骨などが含まれる場合はモード2を、畜産の骨や塩分過多の食材の残渣を含む生ゴミではモード3を選択する。  In the continuous input mode, the left and right input ports 2 are used properly. The insertion instruction of the left and right insertion ports 2 is performed by the insertion instruction lamp 7, and includes a mode 1 in which the insertion instruction changes every other day, a mode 2 where the insertion instruction changes every other week, and a mode 3 where the insertion instruction changes every other month. ing. This mode switching is selected in consideration of the amount of garbage to be introduced and the decomposition characteristics of the contents. Mode 1 is selected for raw garbage that is mainly made of vegetables and does not contain salt, mode 2 is selected when livestock bones and the like are included, and mode 3 is selected for raw garbage that includes livestock bones and residues of excessive salt.

発酵槽は仕切のない一個の発酵槽であるが、左右の投入口2を使い分けることで従来の連続的に発生する生ゴミを処理するには非常に不便であった問題点を解消している。また、左右の投入口2と連動して動作する左右に設けた攪拌機構9が独立回動するため、他方の発酵分解の邪魔をすることはない。また、下記に示す攪拌の反転動作で内容物の相互入れ替えが起こるため、発酵状態に差が現れない利点もある。  Although the fermenter is a single fermenter with no partition, it has solved the problem that was very inconvenient for the conventional continuous processing of garbage by using the left and right inlets 2 properly. . In addition, since the left and right stirring mechanisms 9 that operate in conjunction with the left and right inlets 2 rotate independently, the other fermentation decomposition is not disturbed. In addition, since the contents are interchanged by the reversing operation of stirring shown below, there is also an advantage that no difference appears in the fermentation state.

一次発酵を除く全攪拌での攪拌動作は、5rpmで5分動作し12時間置きに1回行う。最初の攪拌方向は左右に設けた攪拌機構9が双方共に正回転し、次のサイクルでは右の攪拌機構9が逆回転で左の攪拌機構9が正回転し、次のサイクルでは攪拌機構9が双方共に逆回転し、次のサイクルでは右の攪拌機構9が正回転で左の攪拌機構9が逆回転し、次のサイクルで元の回転方向に戻る攪拌サイクルを繰り返す。  The stirring operation in all stirring except the primary fermentation is performed once every 12 hours by operating at 5 rpm for 5 minutes. In the first agitating direction, both the agitating mechanisms 9 provided on the left and right rotate in the forward direction. In the next cycle, the agitating mechanism 9 on the right rotates in the reverse direction and the agitating mechanism 9 on the left rotates in the forward direction. Both of them rotate in the reverse direction, and in the next cycle, the right stirring mechanism 9 rotates forward and the left stirring mechanism 9 rotates reversely, and in the next cycle, the stirring cycle returning to the original rotation direction is repeated.

ご飯類が多量に含まれている場合は、1週間に1回程度の渦乾燥モードを追加する。渦乾燥モードがセットされると直前の駆動モータ10の情報が記憶メモリに退避する。この追加モードでは、加温処理機構6と排気処理機構28の双方を全能力で運転し水分率を一時的に20%程度まで低下させ、ご飯類を乾燥状態に導いた後に30分間、攪拌機構9を5rpmで5分毎に反転動作をして乾燥状態に導いたご飯類を砕き餅化現象を防止する。  If a large amount of rice is included, add a vortex drying mode about once a week. When the vortex drying mode is set, the information of the previous drive motor 10 is saved in the storage memory. In this additional mode, both the heating treatment mechanism 6 and the exhaust treatment mechanism 28 are operated at full capacity, the moisture content is temporarily reduced to about 20%, and the rice is brought into a dry state for 30 minutes. 9 is reversed every 5 minutes at 5 rpm to break the rice that has been brought into a dry state to prevent the hatching phenomenon.

渦乾燥モードの実行後は、図9に示す排気処理機構28から接続パイプ5−1を経由して清水化された水23−1を導入する。図示しない電磁弁を開放することにより、水洗シャワーノズル12より霧状の水23−2を噴霧する。この時、記憶メモリに退避した駆動モータ10の情報に従い、水洗シャワーノズル12より噴霧する霧状の水23−2が放出される。この動作で水分率は渦乾燥モードを実行する直前の状態に戻される。  After execution of the vortex drying mode, purified water 23-1 is introduced from the exhaust treatment mechanism 28 shown in FIG. 9 via the connection pipe 5-1. By opening a solenoid valve (not shown), mist-like water 23-2 is sprayed from the flush shower nozzle 12. At this time, mist-like water 23-2 sprayed from the flush shower nozzle 12 is released in accordance with the information of the drive motor 10 saved in the storage memory. With this operation, the moisture content is returned to the state immediately before the vortex drying mode is executed.

発酵処理が進むにつれて水分率が低下すると、微生物の活性が低下するため水分率を60%程度に保つ必要が生じる。すると総合管理されている制御データーを元に、駆動モータ10の情報を比較演算して投入水分量が計算される。この処理は通常発酵状態を維持するため、排気処理機構28から接続パイプ5−1を経由して清水化された水23−1を図示しない電磁弁を開放することにより、図8に示す多機能ノズル13の噴射口50の穴を通り、加温処理機構6の加熱部26で暖められた空気25−5と共に徐々に放出する。  When the water content decreases as the fermentation process proceeds, the activity of microorganisms decreases, so the water content needs to be maintained at about 60%. Then, based on the control data that is comprehensively managed, the input water amount is calculated by comparing and calculating the information of the drive motor 10. In order to maintain the normal fermentation state in this treatment, the multifunctional shown in FIG. 8 is opened by opening an electromagnetic valve (not shown) of the water 23-1 that has been purified from the exhaust treatment mechanism 28 via the connection pipe 5-1. It passes through the hole of the injection port 50 of the nozzle 13 and is gradually discharged together with the air 25-5 heated by the heating unit 26 of the heating processing mechanism 6.

数ヶ月が過ぎ発酵により蓄積した無機物質量が増えると、コンポスト完了を判定する判定手段の信号を基に、発酵により蓄積した無機物質量を推定し、水洗シャワーノズル12から放出する水23−2と、攪拌機構9を5rpmで30秒毎に反転動作をして、処理媒体中に蓄積した無機物質成分を水洗浄し処理媒体の負荷を軽くしたり、処理媒体を再生したりするのである。役目を果たした水は、処理槽8の底部に設置された図8に示す多機能ノズル13の隙間を通り、24−1、24−2、24−3のように流れ貯留室14に貯まる。貯留室14に貯まった水23−4は接続パイプ5−2を経由して排気処理機構に戻される。  When the amount of inorganic substances accumulated by fermentation increases after several months, the amount of inorganic substances accumulated by fermentation is estimated based on the signal of the determination means for determining completion of composting, and water 23-2 discharged from the washing shower nozzle 12; The stirring mechanism 9 is reversed at 5 rpm every 30 seconds to wash the inorganic substance components accumulated in the processing medium with water to lighten the load on the processing medium or regenerate the processing medium. The water which played the role passes through the clearance gap between the multifunctional nozzles 13 shown in FIG. 8 installed at the bottom of the treatment tank 8 and flows into the storage chamber 14 like 24-1, 24-2 and 24-3. The water 23-4 stored in the storage chamber 14 is returned to the exhaust treatment mechanism via the connection pipe 5-2.

木材チップ、モミ殻、稲わら、麦わら、落葉、樹皮などから適宜選択された炭素原19の培養床も発酵に伴い微生物に消費され減少していく。生ゴミ投入直後のC/N比が20を下回ると、発酵中にアンモニアガスが発生する場合があるため培養床の入れ替え時期である。この培養床の更新時期は、投入物の質や上記の処理媒体を再生する回数で変化するため、温度計の温度推移や、積算加温時間や、排気処理機構28の運転時間や、攪拌機構9を駆動する駆動モータ10の位相情報や過去の履歴から総合的に判断される。培養床の入れ替え時期と判定されると投入指示ランプ7双方が点滅し、培養床の入れ替えを知らせる。  The culture bed of carbon source 19 appropriately selected from wood chips, fir shells, rice straw, wheat straw, defoliation, bark, etc. is also consumed and reduced by microorganisms during fermentation. If the C / N ratio immediately after the input of raw garbage is less than 20, ammonia gas may be generated during fermentation, so it is time to replace the culture bed. Since the renewal time of the culture bed changes depending on the quality of the input and the number of times the above-mentioned treatment medium is regenerated, the temperature transition of the thermometer, the accumulated heating time, the operating time of the exhaust treatment mechanism 28, the stirring mechanism 9 is comprehensively determined from the phase information of the drive motor 10 that drives 9 and the past history. When it is determined that it is time to replace the culture bed, both the loading instruction lamps 7 blink to notify the replacement of the culture bed.

発酵が完了した処理物は図3に示すごとく、外扉21を開けコンポスト取り出し口3を開放して矢印22の方向へ取り出す。このコンポスト取り出し動作は、図4に示す攪拌部先端図の攪拌棒46と、攪拌棒47、48がすくい板49と協調し、水平方向へ反時計回りに45度遅れた位置までコンポストをすくい上げて停止させることでコンポスト取り出し作業を楽にする。  As shown in FIG. 3, the fermented processed product is taken out in the direction of arrow 22 by opening the outer door 21 and opening the compost outlet 3. This compost removal operation is performed by scooping up the compost to a position delayed by 45 degrees counterclockwise in the horizontal direction in cooperation with the scooping plate 49 and the stirrer bars 47 and 48 in the front view of the stirrer shown in FIG. Stop the compost removal work by stopping it.

発明の効果The invention's effect

以上説明したように本発明によれば、C/N比率管理対応による単体処理モード1と単体処理モード2の使用で、家庭から排出される生ゴミを再生利用して自治体で何度も同一基材で使用可能な形態に変換する方法、及びそれに適したC/N比率管理による生ゴミの微生物処理方法が可能になり、焼却処分に頼らない生ゴミの再生利用ができる。  As described above, according to the present invention, by using the single processing mode 1 and the single processing mode 2 corresponding to the C / N ratio management, the same group is repeatedly used by the local government by reclaiming raw garbage discharged from the home. A method of converting to a form that can be used with wood and a method for treating microorganisms of garbage by controlling the C / N ratio suitable for the method become possible, and it is possible to recycle the garbage without depending on incineration.

従来のコンポスト処理方法である日々の生ゴミを処理する連続投入モードでは、C/N比の低い状態を形成し一時停止による一次発酵と、全攪拌による二次発酵を攪拌混合率の違いで変化する仮装C/N比を用いて発酵させ、仕切のない一個の発酵槽で左右の投入口を使い分けることで、従来の連続的に発生する生ゴミを処理するには非常に不便であった問題点を解消することができる。  The continuous composting process, which is a conventional composting process, treats daily garbage, forms a low C / N ratio, and changes between primary fermentation by temporary suspension and secondary fermentation by total agitation depending on the mixing ratio of the agitation It is very inconvenient to treat the raw garbage generated continuously by fermenting using the disguise C / N ratio and using the left and right inlets separately in a single fermenter without partition The point can be solved.

また、生ゴミ投入回数や攪拌機構を駆動するモータの負荷変動により変化する駆動コイルの自己インダクタンス(L)の変化で生じる位相の遅れを、供給する商用電源の位相と比較して得た数値を制御情報として演算処理して履歴管理することにより、水分率の調整や処理媒体中に蓄積した無機物質成分を水洗浄し処理媒体の再生をすることができる。  In addition, the numerical value obtained by comparing the phase delay caused by the change in the self-inductance (L) of the drive coil, which changes due to the load of the garbage driving frequency and the load of the motor driving the stirring mechanism, with the phase of the commercial power supply to be supplied. By calculating and controlling the history as control information, the moisture content can be adjusted and the inorganic substance component accumulated in the processing medium can be washed with water to regenerate the processing medium.

本発明の実施形態を示す一部切欠正面図である。It is a partially cutaway front view showing an embodiment of the present invention. 本発明の側面断面図である。It is side surface sectional drawing of this invention. 本発明の処理説明図である。It is processing explanatory drawing of this invention. 本発明の攪拌部先端図である。It is a front end view of the stirring unit of the present invention. 本発明の判定手段の回路図である。It is a circuit diagram of the determination means of this invention. 本発明の判定手段の波形図である。It is a wave form diagram of the determination means of this invention. 本発明の水洗シャワーノズル図である。It is a flush shower nozzle figure of this invention. 本発明の多機能ノズル詳細図である。It is a multifunctional nozzle detailed drawing of this invention. 本発明の気体と液体の流れ図である。It is a flow chart of the gas and liquid of the present invention. 本発明の排気処理機構正面断面図である。It is a front sectional view of the exhaust treatment mechanism of the present invention. 本発明の発酵曲線図である。It is a fermentation curve figure of the present invention. 本発明のC/N比率管理のフローチャート図である。It is a flowchart figure of C / N ratio management of the present invention.

符号の説明Explanation of symbols

1 生ゴミ微生物処理装置
2 生ゴミ投入口
3 コンポスト取り出し口
4−1 接続パイプ
4−2 接続パイプ
5−1 接続パイプ
5−2 接続パイプ
6 加温処理機構
7 投入指示ランプ
8 処理槽
9 攪拌機構
10 駆動モータ
11 保温装置
12 水洗シャワーノズル
13 多機能ノズル
14 貯留室
15 清掃ノズル
16 生ゴミ
17 矢印
18 矢印
19 炭素原
20 生ゴミ
21 外扉
22 矢印
23−1 水
23−2 霧状の水
23−3 霧状の水
23−4 水
24−1 流れ
24−2 流れ
24−3 流れ
25−1 空気
25−2 空気
25−3 空気
25−4 空気
25−5 空気
26 加熱部
27−1 酸素
27−2 排気
27−3 酸素
28 排気処理機構
29 吸気管
30 ポンプ
31 処理タンク
32 溶解筒
33 排気成分を含んだ水
34 オゾンガス吸気管
35 ポンプ
36 溶解筒
37 清水化された水
38 圧力放出口
39 注水口
40 排水口
41 電圧変成トランス
42 自己インダクタンス検出トランス
43 波形
44 波形
45 波形
46 攪拌棒
47 攪拌棒
48 攪拌棒
49 すくい板
50 噴射口
DESCRIPTION OF SYMBOLS 1 Garbage microorganism processing apparatus 2 Garbage input port 3 Compost taking-out port 4-1 Connection pipe 4-2 Connection pipe 5-1 Connection pipe 5-2 Connection pipe 6 Warming treatment mechanism 7 Input instruction lamp 8 Treatment tank 9 Stirring mechanism DESCRIPTION OF SYMBOLS 10 Drive motor 11 Thermal insulation apparatus 12 Washing shower nozzle 13 Multifunctional nozzle 14 Storage chamber 15 Cleaning nozzle 16 Garbage 17 Arrow 18 Arrow 19 Carbon raw material 20 Garbage 21 Outer door 22 Arrow 23-1 Water 23-2 Mist-like water 23 -3 Atomized water 23-4 Water 24-1 Flow 24-2 Flow 24-3 Flow 25-1 Air 25-2 Air 25-3 Air 25-4 Air 25-5 Air 26 Heating unit 27-1 Oxygen 27 -2 Exhaust 27-3 Oxygen 28 Exhaust treatment mechanism 29 Intake pipe 30 Pump 31 Processing tank 32 Dissolving cylinder 33 Water containing exhaust component 34 Ozone gas intake pipe 35 Pump 36 Dissolution Tube 37 Purified water 38 Pressure discharge port 39 Water injection port 40 Drain port 41 Voltage transformation transformer 42 Self-inductance detection transformer 43 Waveform 44 Waveform 45 Waveform 46 Stirring rod 47 Stirring rod 48 Stirring rod 49 Rake plate 50 Injection port

Claims (10)

生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、C/N比率管理対応による単体処理モードと、生ゴミ投入回数や攪拌機構の負荷率を履歴管理する連続投入モードの制御が可能な管理制御を備えたことを特徴とするC/N比率管理対応の生ゴミ微生物処理装置。  In a garbage processing microorganism processing apparatus equipped with a garbage input port, a compost outlet, an agitation mechanism, an exhaust processing mechanism, a heating processing mechanism, and management control, a single processing mode corresponding to C / N ratio management, and garbage A garbage microbe treatment apparatus compatible with C / N ratio management, comprising management control capable of controlling a continuous charging mode for history management of the number of times of charging and the load factor of the stirring mechanism. 生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、仕切のない1つの発酵槽に生ゴミ投入口を左右に独立して設け、攪拌手が左右に独立して回動可能な攪拌機構を備え、生ゴミ投入口それぞれに対応する攪拌手が独立回動する手段と、生ゴミ投入口と関係なく同期回動する手段とを備え、投入条件を判断し投入可能な生ゴミ投入口を指示するランプとを備えたことを特徴とするC/N比率管理対応の生ゴミ微生物処理装置。  Garbage input port, compost take-out port, stirring mechanism, exhaust treatment mechanism, heating treatment mechanism, and garbage processing microorganism treatment equipment with management control. Provided with a stirring mechanism that can be independently rotated to the left and right, and a means for independently rotating the stirring hands corresponding to each of the garbage input ports, and a synchronous rotation regardless of the garbage input ports. A garbage microbe processing apparatus compatible with C / N ratio management, characterized by comprising: a moving means; and a lamp for determining a loading condition and indicating a throwable garbage input port. 生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、攪拌部位の先端が真の垂直方向から水平方向へ時計回りに45度進んだ位置にオイルを充填した保温装置を配し、攪拌部位の先端が真の垂直方向から水平方向へ反時計回りに45度遅れた位置に処理済みのコンポスト取り出し口を設け、制御により各位置に適宜停止することを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置。  In a garbage disposal device equipped with a garbage input port, compost outlet, agitation mechanism, exhaust treatment mechanism, heating treatment mechanism, and management control, the tip of the agitation site is clocked from the true vertical direction to the horizontal direction. A heat retaining device filled with oil is arranged at a position advanced 45 degrees around, and a treated compost outlet is provided at a position where the tip of the stirring portion is delayed 45 degrees counterclockwise from the true vertical direction to the horizontal direction, The garbage microbe processing apparatus corresponding to C / N ratio management according to claim 1, wherein the apparatus is appropriately stopped at each position by control. 生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、排気処理機構と加温処理機構とを制御し、乾燥処理や加湿処理や除湿処理を行うことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置。  Garbage input device, compost outlet, agitation mechanism, exhaust treatment mechanism, warming treatment mechanism, and garbage control microbial treatment equipment with management control, controlling exhaust treatment mechanism and warming treatment mechanism, drying The garbage microorganism treatment apparatus for C / N ratio management according to claim 1, wherein the treatment, the humidification process, and the dehumidification process are performed. 生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、一次発酵行程と二次発酵行程を攪拌部位の停止角度と回転の制御により行うことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置。  Garbage input device, compost outlet, agitation mechanism, exhaust treatment mechanism, heating treatment mechanism, and garbage control microbial treatment equipment with management control, the primary fermentation process and the secondary fermentation process are stopped at the agitation site The garbage microorganism treatment apparatus for C / N ratio management according to claim 1, wherein the treatment is performed by controlling rotation and rotation. 生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、攪拌部位の中心部先端と後端部をずらし、生ゴミの移動と、混合と、攪拌が行える攪拌手を備えたことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置。  In a garbage disposal device equipped with a garbage input port, a compost outlet, a stirring mechanism, an exhaust processing mechanism, a heating processing mechanism, and management control, the center tip and the rear end of the stirring part are shifted, The garbage microorganism treatment apparatus for C / N ratio management according to claim 1, further comprising a stirring hand capable of moving, mixing, and stirring the garbage. 生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、攪拌機構を駆動するモータの負荷変動で変わる自己インダクタンス(L)の変化を位相変化として捉え商用電源の交流波形の位相と比較して、水分率コントロールやモータ異常検出やコンポスト完了を判定する判定手段を備えることを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置。  Self-inductance that changes with load fluctuations of the motor that drives the agitation mechanism in a garbage disposal microorganism treatment apparatus equipped with a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and a management control ( 2. The apparatus according to claim 1, further comprising: a determination unit that recognizes a change in L) as a phase change and compares it with a phase of an AC waveform of a commercial power supply to determine moisture content control, motor abnormality detection, and compost completion. Garbage microorganism treatment equipment that supports C / N ratio management. 生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、発酵により蓄積した無機物質量の判定手段により、処理媒体中に蓄積した無機物質成分を水洗浄する水洗シャワーノズルを備えることを特徴とする、請求項1または7記載のC/N比率管理対応の生ゴミ微生物処理装置。  In a microbial treatment apparatus for garbage that is provided with a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and a management control, the means for judging the amount of inorganic substances accumulated by fermentation in the treatment medium 8. The garbage microorganism treatment apparatus for C / N ratio management according to claim 1 or 7, further comprising a water-washing shower nozzle for washing the inorganic substance component accumulated in the water. 生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、加温処理機構内と処理槽を結ぶ貯留室内に送風口清掃と加湿をする多機能ノズルを設けたことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置。  In a garbage disposal microbial treatment apparatus equipped with a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating treatment mechanism, and management control, air is blown into a storage chamber connecting the inside of the heating treatment mechanism and the treatment tank. The multi-purpose nozzle for cleaning the mouth and humidifying is provided, the garbage microorganism processing apparatus for C / N ratio management according to claim 1. 生ゴミ投入口とコンポスト取り出し口と攪拌機構と、排気処理機構と、加温処理機構と、管理制御を備える生ゴミの微生物処理装置において、生ゴミ投入口を清掃するノズルを設けたことを特徴とする、請求項1に記載のC/N比率管理対応の生ゴミ微生物処理装置。  A garbage disposal device equipped with a garbage input port, a compost outlet, an agitation mechanism, an exhaust treatment mechanism, a heating processing mechanism, and a management control, is provided with a nozzle for cleaning the garbage input port. The garbage microorganism processing apparatus corresponding to C / N ratio management according to claim 1.
JP2003303657A 2003-07-24 2003-07-24 Garbage microbe processing equipment for C / N ratio management Expired - Fee Related JP4196275B2 (en)

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