JP3777769B2 - 厨 芥 Processing machine - Google Patents

厨 芥 Processing machine Download PDF

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JP3777769B2
JP3777769B2 JP36467597A JP36467597A JP3777769B2 JP 3777769 B2 JP3777769 B2 JP 3777769B2 JP 36467597 A JP36467597 A JP 36467597A JP 36467597 A JP36467597 A JP 36467597A JP 3777769 B2 JP3777769 B2 JP 3777769B2
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water
condensing unit
gas
drainage channel
water level
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JPH11169822A (en
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敏宏 小林
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パロマ工業株式会社
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Priority to JP36467597A priority Critical patent/JP3777769B2/en
Priority to US09/207,265 priority patent/US6076271A/en
Priority to CN98123298A priority patent/CN1115287C/en
Priority to EP98123828A priority patent/EP0924488B1/en
Priority to ES98123828T priority patent/ES2210652T3/en
Priority to DE69819459T priority patent/DE69819459T2/en
Priority to KR10-1998-0055509A priority patent/KR100492866B1/en
Priority to TW087120947A priority patent/TW533098B/en
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Description

【0001】
【発明の属する技術分野】
本発明は生ゴミ等の厨芥を乾燥処理する厨芥処理機に関する。
【0002】
【従来の技術】
従来から、生ゴミ等の厨芥を乾燥状態にして腐敗しないようにすると共に、処理中に発生する臭い成分を脱臭処理するといった厨芥処理機が知られている。一般にこのような厨芥処理機は、厨芥を加熱して発生した水蒸気を脱臭して排出する構成となっている。
【0003】
生ゴミは主にキッチンで発生することから、厨芥処理機を室内に設置すると使い勝手がよいが、臭気の漏れ、水蒸気の排出による湿度上昇、熱源による温度上昇といった室内環境を悪化させる要因が多く、室内設置が困難であった。そのため本願出願人は、厨芥を加熱する加熱室と、外部のファンからの送風により水蒸気を冷却して凝縮させる凝縮室とを備え、厨芥を加熱して発生した水蒸気により加熱室と凝縮室との連通する空間に存在する空気を押し出した状態でこの空間を密閉し、水蒸気の凝縮量を多くすることでこの密閉空間内を負圧にして乾燥処理するといった発明を先に提案している。このような構成では、負圧により蓋とのシール部からの臭気漏れを防止できると共に、沸点を低下させて加熱量を低減させることができる。しかも厨芥から発生した臭い成分を凝縮した水と共に下水管に排水することで臭気や水蒸気を排出する必要がなく、室内で使用することができる。
【0004】
【発明が解決しようとする課題】
このような構成では、厨芥から発生した水蒸気を効率よく凝縮させることが重要となるが、冷却効率を高くするために外部からファンにより送風すると構造が複雑となりコストが高くなってしまうといった問題があった。
本発明の厨芥処理機は上記課題を解決し、安価な構成で水蒸気の冷却効率を向上させることを目的とする。
【0005】
【課題を解決するための手段】
上記課題を解決する本発明の請求項1記載の厨芥処理機は、
生ゴミ等の厨芥を加熱する加熱部と、
上記加熱部と連通され上記厨芥から発生した水蒸気を含む気体を冷却する凝縮部と、
上記凝縮部で凝縮した水を外部に排水する排水路と
上記凝縮部から排水路への流路に水を溜める凝縮水溜まりを形成し、該凝縮水溜まりに溜まった水が所定の密閉水位を越えた状態で該水により上記凝縮部と上記排水路とを遮断すると共に、上記密閉水位より高い所定の排水水位を越えた分の水を上記排水路に排水する遮断排水部を備える厨芥処理機であって、
上記凝縮部の圧力が上記排水路の圧力に比べて低くなり上記凝縮水溜まりにおける上記排水路側の水位が所定の密閉水位まで下降したときに、排水路側の空気が凝縮部側に吸入される構成とするとともに、
上記凝縮部を、少なくとも一方の板に凹みを設けた2枚の板を重ね合わせ該板の周囲をシールし鉛直となるように設置して内部に空間を生じさせるとともに、該空間内に、下端のみを開口した下端開口隔壁と、上下両端を共に開口してその下端位置を上記下端開口隔壁の下端位置よりも低くした両端開口隔壁とを交互に形成し、凝縮内部の空気を蛇行させて流通させるものとしたことを特徴とする厨芥処理機。
【0011】
更に、縮部から排水路への流路に水を溜める凝縮水溜まりを形成し、凝縮水溜まりに溜まった水が所定の密閉水位を越えた状態でその水により凝縮部の気体と排水路の気体とが連通する流路を遮断することで、加熱室と凝縮室との連通空間を密封する。この密封空間内で厨芥の加熱及び発生した水蒸気の凝縮を行ない、凝縮されない水蒸気がそのまま外部に排出されてしまうことを防止する。また、凝縮水溜まりには凝縮部で凝縮された水が送られてくるが、凝縮水溜まりに溜まった水は所定の排水水位を越えた分が排水路から外部(例えば下水管)に排水されるため増え続けることがない。また、密閉空間内が排水路に比べて負圧となると凝縮水溜まりの排水路側の水位が下降すると共に凝縮部側の水位が上昇するが、排水路側の水位が所定の密閉水位まで下降することで排水路側の空気が密閉空間内に吸入されるため、凝縮部側の水位が上昇しすぎることを防ぐことができる。
【0008】
上記課題を解決する本発明の請求項記載の厨芥処理機は、請求項1載の厨芥処理機において、
上記凝縮部で冷却した気体を上記加熱部に強制的に送り返す返還手段と、
上記加熱部に送り返した気体を厨芥に向かって吹き付ける吹き付けノズルとを備えたことを要旨とする。
【0009】
上記構成を有する本発明の請求項1記載の厨芥処理機は、加熱部にて生ゴミ等の厨芥を加熱して厨芥に含まれる水分を蒸発させ、加熱部と連通される凝縮部で気体を冷却して水蒸気を凝縮させる。この凝縮部は、少なくとも一方の板に凹みを設けた2枚の板を重ね合わせ、板の周囲をシールして内部に空間を生じさせると共に、空間内に複数の隔壁を形成して気体を蛇行させて導くように形成される。そのため、加熱部からの気体は凝縮部で蛇行して導かれ、板の内面と水蒸気とが接触しやすくなり冷却効率を高くすることができる。また、厨芥から発生した臭気のほとんどは、凝縮した水と共に外部(例えば下水管)に排水することができる。
【0010】
またが鉛直となるように設置して気体を上下方向に蛇行させて導くようにされているため、外部の空気を板の外面に沿ってドラフト力により上方に流れやすくすることができ冷却効率を高くすることができる。また、蛇行する流路で水蒸気が凝縮して水となると鉛直面を伝って直ちに下に流れ落ちる。ここで、単に蛇行流路を形成しただけでは流路の下部に水が溜まって気体流路が塞がれてしまうが、下端のみが開口した下端開口隔壁と、上下端が共に開口し下端位置が下端開口隔壁より低い両端開口隔壁とを交互に形成した構成により下部に連通空間が形成されるため、蛇行流路から流れ落ちる水を一箇所に溜めて排水路に導くことができると共に、下部に溜まった水の水位が両端開口隔壁の下端より高くなっている状態では連通空間から気体が流れることを防いで蛇行して導くことができる。
【0012】
に、上記構成を有する本発明の請求項記載の厨芥処理機は、凝縮部で冷却した気体を加熱部に強制的に送り返す。そのため、加熱部内の水蒸気を多く含んだ気体が凝縮部にスムーズに流れ、また凝縮部で冷却されて水蒸気の含有量が少なくなった気体がスムーズに加熱部に流れ、厨芥に含まれる水分が効率良く蒸発すると共にその水蒸気が効率良く凝縮される。また、加熱部に送り返した気体を厨芥に向かって吹き付けることで、厨芥に含まれる水分の蒸発が促進される。
【0013】
【発明の実施の形態】
以上説明した本発明の構成・作用を一層明らかにするために、以下本発明の厨芥処理機の好適な実施例について説明する。
図1は、本発明の一実施例としての厨芥処理機の概略構成図である。この厨芥処理機は大別して、生ゴミAを加熱する加熱部10と、生ゴミAから発生した水蒸気を凝縮させる凝縮部20と、凝縮部20と下水管1とを連通して排水すると共に溜水の状態に応じて通気を遮断する遮断排水部30と、凝縮部20で冷却した気体を再び加熱部10に送り返す返還部40とからなる。
【0014】
加熱部10は、生ゴミAを収納する処理槽11と、処理槽11を加熱する処理槽用ヒータ12と、これらを収納する断熱構造の加熱室13とにより構成される。また加熱室13の上部には、処理槽11を出し入れするために開閉する蓋13aが形成される。
【0015】
凝縮部20は、図2に示すように所定形状の凹みを設けた2枚の金属板21,22を重ね合わせ、その金属板21,22の周囲をシーム溶接によりシールして内部に空間を生じさせると共に、その空間内に、下端のみが開口した下端開口隔壁23,23,…と、上下端が共に開口した両端開口隔壁24,24,…とを交互に形成したものである。両端開口隔壁24,24,…の下端は下端開口隔壁23,23,…の下端に比べ低い位置まで形成されており、内部空間に水位Lまで水が溜まることにより両端開口隔壁24,24,…の下端開口のみが塞がれ、気体を上下方向に蛇行させて導く流路が形成される。また、下部の連通スペースの底面は遮断排水部30に向かって下り傾斜となっており、水を流れやすくしている。
【0016】
また、金属板21,22が縦向きとなるように設置することで、外部の空気がドラフト力により外面に沿って上方にスムーズに流れるため、冷却効率を高くすることができる。更に、上下方向に蛇行させる隔壁を形成しているため、流路内で結露した水が鉛直面により下に流れ落ちやすい。ここで、下部に連通スペースを設けず単純に上下方向に蛇行させる流路のみを形成した場合、流路内で凝縮した水が溜まって増加することにより気体流路を塞いでしまうが、下部に連通スペースを形成することで流路内で結露した水を遮断排水部30側に送ることができ、しかも溜まった水によりその連通スペースを塞ぐことで、気体を蛇行して流すことができる。
【0017】
遮断排水部30は、水を溜めるタンク31と、タンク31の底面に臨んで垂下し凝縮部20からの水を下方に流す凝縮水排出管32と、タンク31の上方側面と下水管1とを連通してタンク31内の所定水位dを越えた分の水を下水管1に排水する排水管33とにより構成される。このような構成により、タンク31内の水が凝縮水排出管32の下端開口面である水位eより高くなっている状態で、加熱室13と凝縮部20との気体の連通する空間を外部に対して密閉する。
【0018】
返還部40は、凝縮部20の下流側と加熱室13とを連通する返還管41を形成し、この返還管41には凝縮部20から加熱室13の方向に気体を流すファン42と、ファン42の下流側で気体を加熱する気体用ヒータ43と、下流側端部から加熱室13内の生ゴミAに向けて気体を噴射するノズル44とが設けられる。
【0019】
次に、この厨芥処理機の動作について説明する。処理槽11内に生ゴミAが投入されて乾燥処理の開始操作がされると、処理槽用ヒータ12により処理槽11の加熱を開始する。そのため、処理槽11及び加熱室13内の温度が上昇し、生ゴミAに含まれる水分が蒸発して、加熱室13及び凝縮部20の気体の連通する空間内の圧力が上昇する。そして、凝縮水排出管32の水が下端開口面である水位eまで下降すると、図3に示すように加熱室13及び凝縮部20に存在していた空気が下水管1側に押し出されるため、タンク31と凝縮水排出管32との水位差により決まる圧力までしか増加しない。一方、処理槽ヒータ12により加熱を開始してから所定時間が経過すると、返還部40のファン42及び気体用ヒータ43を作動させる。そのため、加熱室13内の水蒸気を多く含んだ気体は凝縮部20に流れ、蛇行して流れる際に冷却され、返還管41を通って加熱室13に送り返される。その際、加熱室13から凝縮部20に送られた気体は冷却されて露点が下がるため、気体に含まれる水蒸気が凝縮して水となり凝縮部下部に溜まり、凝縮水排出管32に流れ落ちる。そして、加熱室13で与える熱量を凝縮部20で奪う熱量より小さくして水蒸気の凝縮量を増やすことで、加熱室13及び凝縮部20の圧力が低下し、タンク31に水が溜まっていく。そのため、加熱室13と凝縮部20との気体の連通する空間が外部に対して密閉状態となり、運転開始時に存在していた空気の一部を下水管1側に押し出したことから密閉空間内を負圧にすることができる。
【0020】
一方、水蒸気の含有量が少なくなった気体は返還管41を流れる際に気体用ヒータ43によって高温に加熱された後、ノズル44により処理槽11内の生ゴミAに噴射される。このように気体用ヒータ43により加熱して相対湿度の低くなった気体を生ゴミAに直接噴射することで、生ゴミAに含まれる水分の蒸発が促進され、また返還管41内での結露も防止される。しかも、加熱室13内が負圧であるため沸点が低下し、低い温度で水分を蒸発させることが可能となり、また臭い成分を蓋13aとの隙間から外部に漏れにくくすることができる。
【0021】
タンク31には凝縮部20から流れ落ちる水が溜まっていくが、タンク31の水が水位dを越えた分は排水管33を介して下水管1に流れるため、水が増え続けることがなく水位が安定する。そして、生ゴミAから発生した臭い成分のほとんどはタンク31に溜まった水に溶け込み下水管1に排水される。また、凝縮水排出管32とタンク31との水の水位差は密閉空間内と下水管1内との圧力差により決まるため、密閉空間内の圧力が負圧値となっている状態では凝縮水排出管32或いは凝縮部20の水の水位はタンク31の水の水位より高い水位Cで安定する。この水位Cが、図1に示すように両端開口隔壁24の下端となる水位Lより高くなることで、気体を蛇行させて案内する流路が形成される。
【0022】
一方、密閉空間内の圧力が減少し続けると、凝縮部20の水とタンク31の水との水位差が大きくなっていく。そして、凝縮部20の水が下端開口隔壁23の下端となる水位Hより高くなると気体の流路が遮断されてしまうが、タンク31の水が減少して水位eまで下降すると、図4に示すようにタンク31側の空気が凝縮水排出管32側に吸引されて、密閉空間内の圧力が減少しすぎることが防止される。従って、凝縮部20の水の水位が上昇しすぎることを防ぐことができる。
【0023】
以上説明したように、本実施例の厨芥処理機によれば、凝縮部20を板21,22が鉛直となるように設置することで、外気をドラフト力により外面に沿って上方に流れやすくし、また気体を蛇行させて導くことで気体に含まれる水蒸気を板21,22の内面に接触しやすくして冷却効率を高くすることができ、しかも2枚の金属板21,22を重ね合わせた簡単な構造であるため低コストで実現できる。また、上下に蛇行させると共に下部に連通スペースを設けることで、流路内で凝縮した水により流路が塞がれてしまうことを防ぐことができ、しかも溜まった水により連通スペースを塞ぐことで気体は連通させずに蛇行させて流すことができる。更に、密閉空間内の圧力が減少してタンク31の水が水位eまで下降するとタンク31側の空気が凝縮水排出管32側に吸引される構成により、凝縮部20内の水の水位が上昇しすぎることにより気体流路が塞がれてしまうことを防ぐことができる。また、凝縮部20で冷却した気体を加熱室13に送り返すための返還管41を設け、密閉空間内の気体をファン42により強制的に循環させることで、水蒸気を多く含んだ気体が凝縮部20にスムーズに流れると共に、凝縮部20で冷却されて水蒸気の含有量の少なくなった気体がスムーズに加熱室13に流れるため、生ゴミAに含まれる水の蒸発及び発生した水蒸気の凝縮を効率良く行なうことができ、乾燥性能を高くすることができる。更に、返還管41を介して加熱室13に送られる気体を加熱することで、相対湿度の低くなった気体を生ゴミAに直接噴射して水分の蒸発を促進させることができると共に、返還管41で水蒸気が結露してしまうことを防ぐことができる。加えて、タンク31に溜まった水により凝縮部20から下水管1への気体の連通する流路を遮断する構成により、電磁弁等の開閉弁を用いることなく加熱室13及び凝縮部20を含む空間を外部に対して密閉することができるため安価に構成することができ、しかもタンク31の水が水位dを越えた分は排水管33を介して下水管1に流れるため、密閉空間を維持しつつ排水することができる。
【0024】
また、加熱した生ゴミAから発生した水蒸気を凝縮して臭気と共に排水する構成により、臭気漏れや湿度上昇を防止することができるため、室内環境の悪化を防ぐことができる。更に、加熱室13内が負圧となることで蓋13aとの隙間からの臭気漏れを防ぐことができるため、シール性能を過剰に高くする必要がなく、しかも沸点が低下して低い温度で乾燥処理することができるため、加熱に要するエネルギーを減らして消費電力を低減させることができると共に室内の温度上昇を低減させることができる。加えて、加熱室13内を負圧にするために真空ポンプ等高価な装置を設ける必要がなく、しかも脱臭装置や水蒸気排出装置等を設ける必要がないため、構造を簡単にしてコストを低減することができる。
【0025】
尚、本実施例では、ファン42及び気体用ヒータ43を処理槽用ヒータ12により加熱を開始してから所定時間経過後に作動させたが、これに限ったものではなく、例えば凝縮部20内や加熱室13内の温度や湿度や圧力等、或いは遮断排水部30における水位等を検出し、その検出値に基づいて作動させてもよく、また処理槽用ヒータ12と同時に作動させてもよい。
また、遮断排水部は本実施例の様な構造に限ったものではなく、例えば図5に示すように、凝縮部20からの水を下方に流す下り流路52と、下り流路52から一旦上る上り流路53と、上り流路53から再び下り下水管1に連通する排水流路54とを形成するS字管51としてもよい。また、水により遮断する構成に限らず、電磁弁等の開閉弁を用いて流路を遮断する構成としてもよい。
また、生ゴミAは処理槽用ヒータ12により加熱する構成に限ったものではなく、例えばガスバーナやマイクロ波等により加熱する構成であってもよい。
また、本実施例では返還管41を流れる気体を気体用ヒータ43により加熱したが、加熱しない構成であってもよい。また、処理槽用ヒータ12を用いずに気体用ヒータ43によって加熱した熱風により生ゴミAに含まれる水分を蒸発させる構成であってもよい。また、凝縮部20から加熱室13に気体を送り返さない構成であってもよい。
また、例えば図6に示すように、凝縮部20内の水は両端開口隔壁24の下端となる水位Lよりも高い所定水位を越えた分だけタンク31に流す構成にしてもよい。このような構成によれば、凝縮部20の圧力やタンク31の水の量に関係なく下部に気体流路が連通することを防いで常時気体を蛇行して流すことができる。
また、本実施例では加熱室13及びフィンチューブ21を含む空間を密閉状態にすると共に負圧にしたが、負圧にしない構成であってもよく、密閉状態にしない構成であってもよい。
【0026】
以上本発明の実施例について説明したが、本発明はこうした実施例に何等限定されるものではなく、本発明の要旨を逸脱しない範囲において、種々なる態様で実施し得ることは勿論である。
【0027】
【発明の効果】
以上詳述したように、本発明の請求項1記載の厨芥処理機によれば、水蒸気を含む気体を蛇行させて導くことにより、水蒸気と板の内面とを接触しやすくして冷却効率を高くすることができ、しかも2枚の板を重ね合わせた簡単な構造により低コストで実現できる。
【0028】
またが鉛直となるように設置することで、外気をドラフト力により外面に沿って上方に流れやすくして、冷却効率を高くすることができる。また、流路で凝縮した水を下部で連通させることで溜まった水により流路が塞がれてしまうことを防止できると共に、気体は連通させずに蛇行させて流すことで冷却効率を高くすることができる。
【0029】
更に、閉空間内の圧力が低下して凝縮水溜まりの排水路側の水位が所定の密閉水位まで下降すると排水路側の空気が密閉空間内に吸引される構成により、凝縮部内の水の水位が上昇しすぎることにより気体流路が塞がれてしまうことを防ぐことができる。
【0030】
に、本発明の請求項記載の厨芥処理機によれば、加熱部内の水蒸気を多く含んだ気体を凝縮部にスムーズに流すと共に、凝縮部で冷却されて水蒸気の含有量が少なくなった気体を再び加熱部に送り返すことで、厨芥に含まれる水分を効率良く蒸発させることができると共に、その水蒸気を効率良く凝縮させることができるため、乾燥性能を高くすることができる。また、水蒸気の含有量が少なくなった気体を厨芥に吹き付けることで、水分の蒸発を促進させることができる。
【図面の簡単な説明】
【図1】一実施例としての厨芥処理機の概略構成図である。
【図2】凝縮部の説明図である。
【図3】凝縮部及び遮断排水部の水位を示す説明図である。
【図4】凝縮部及び遮断排水部の水位を示す説明図である。
【図5】別例としての厨芥処理機の概略構成図である。
【図6】別例としての厨芥処理機の概略構成図である。
【符号の説明】
10…加熱部、 13…加熱室、 20…凝縮部、 21,22…金属板、
23…下端開口隔壁、 24…両端開口隔壁、 30…遮断排水部、
31…タンク、 40…返還部、 41…返還管。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a soot processing machine for drying soot such as raw garbage.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, a soot processing machine has been known in which the soot such as raw garbage is dried to prevent it from being spoiled and the odor component generated during the processing is deodorized. In general, such a soot treating machine is configured to deodorize and discharge water vapor generated by heating the soot.
[0003]
Since garbage is generated mainly in the kitchen, it is convenient to install a slag treatment machine indoors, but there are many factors that worsen the indoor environment such as odor leakage, increased humidity due to discharge of water vapor, and increased temperature due to heat sources, Indoor installation was difficult. Therefore, the applicant of the present application includes a heating chamber that heats the soot and a condensing chamber that cools and condenses the steam by blowing air from an external fan, and the heating chamber and the condensing chamber are heated by the steam generated by heating the soot. An invention has been proposed in which the space is sealed in a state where air existing in the communicating space is pushed out, and the amount of condensation of water vapor is increased to dry the sealed space with a negative pressure. In such a configuration, odor leakage from the sealing portion with the lid can be prevented by negative pressure, and the heating amount can be reduced by lowering the boiling point. Moreover, it is not necessary to discharge odor and water vapor by draining the odorous components generated from the soot into the sewer pipe together with the condensed water, and can be used indoors.
[0004]
[Problems to be solved by the invention]
In such a configuration, it is important to efficiently condense the water vapor generated from the soot, but there is a problem that if the air is blown by a fan from the outside in order to increase the cooling efficiency, the structure becomes complicated and the cost increases. It was.
An object of the soot treating machine of the present invention is to solve the above-mentioned problems and to improve the cooling efficiency of water vapor with an inexpensive configuration.
[0005]
[Means for Solving the Problems]
The soot treating machine according to claim 1 of the present invention for solving the above-mentioned problems is
A heating section for heating straw such as raw garbage;
A condensing unit that communicates with the heating unit and cools a gas containing water vapor generated from the soot;
A drainage channel for draining the water condensed in the condensing unit to the outside ;
A condensate pool is formed to store water in the flow path from the condensing unit to the drainage channel, and the condensate unit and the drainage channel are blocked by the water when the water accumulated in the condensate pool exceeds a predetermined sealed water level. And a dredger with a shut-off drain that drains the amount of water that exceeds a predetermined drainage water level higher than the sealed water level to the drainage channel,
When the pressure in the condensing unit is lower than the pressure in the drainage channel and the water level on the drainage channel side in the condensate pool is lowered to a predetermined sealed water level, the air on the drainage channel side is sucked into the condensing unit side. And
The condensing unit is installed so that at least one plate is provided with a dent, and the periphery of the plate is sealed so as to be vertical so as to create a space inside. The lower end opening partition walls that are open only and the both end opening partition walls that are open at both upper and lower ends and whose lower end position is lower than the lower end position of the lower end opening partition wall are alternately formed, and the air inside the condensate is circulated to circulate A cocoon treatment machine characterized by the fact that
[0011]
Furthermore, coagulation in the flow path from the reduced portion to the drainage to form a condensed puddle for storing water, gas drainage and gas condenser portion by the water while the water collected in the condensate puddle exceeds a predetermined sealing level The communication space between the heating chamber and the condensing chamber is sealed by blocking the flow path that communicates with the heating chamber. In this sealed space, the soot is heated and the generated water vapor is condensed to prevent the uncondensed water vapor from being discharged to the outside as it is. In addition, water condensed in the condensing unit is sent to the condensate pool, but the water accumulated in the condensate pool is drained from the drainage channel to the outside (for example, sewer pipes) beyond the predetermined drainage water level. It will not continue to increase. In addition, when the pressure in the sealed space becomes negative compared to the drainage channel, the water level on the drainage channel side of the condensate pool falls and the water level on the condensing unit side rises, but the water level on the drainage channel side falls to a predetermined sealed water level. Since the air on the drainage channel side is sucked into the sealed space, it is possible to prevent the water level on the condensing unit side from rising too much.
[0008]
Garbage disposer according to claim 2 of the present invention to solve the above problems is the garbage disposer of claim 1 Symbol placement,
A return means forcibly returning the gas cooled in the condensing unit to the heating unit;
The gist is provided with a spray nozzle that blows the gas sent back to the heating unit toward the ridge.
[0009]
In the soot treating machine according to claim 1 of the present invention having the above-described configuration, the soot such as garbage is heated in the heating unit to evaporate water contained in the soot, and the gas is produced in the condensing unit communicated with the heating unit. Cool and condense the water vapor. This condensing part overlaps at least one plate with two dents, seals the periphery of the plate to create a space inside, and forms a plurality of partition walls in the space to meander the gas To be guided. Therefore, the gas from the heating unit is meandered and guided in the condensing unit, and the inner surface of the plate and the water vapor are easily brought into contact with each other, so that the cooling efficiency can be increased. Moreover, most of the odor generated from the soot can be drained to the outside (for example, a sewer pipe) together with the condensed water.
[0010]
Moreover, because it is installed so the plate is vertical to guide by meandering gas in the vertical direction, it is possible to easily flow upward through the draft force along the external air to the outer surface of the plate, Cooling efficiency can be increased. Further, when water vapor condenses in the meandering flow path and becomes water, it immediately flows down along the vertical plane. Here, simply forming a meandering channel causes water to accumulate in the lower part of the channel and block the gas channel. Since the communication space is formed in the lower part by the structure in which the both end opening partition walls are lower than the lower end opening partition wall, the water flowing down from the meandering channel can be collected in one place and guided to the drainage channel, and In the state where the water level of the accumulated water is higher than the lower end of the both-end opening partition wall, the gas can be guided by meandering while preventing the gas from flowing from the communication space.
[0012]
In the following, garbage disposer according to claim 2 of the present invention having the above structure, forcing back the cooled gas in the condensing section to the heating section. For this reason, a gas containing a large amount of water vapor in the heating part flows smoothly to the condensing part, and a gas cooled by the condensing part and having a reduced water vapor content flows smoothly to the heating part. The water vapor evaporates well and the water vapor is condensed efficiently. Moreover, evaporation of the water | moisture content contained in a soot is accelerated | stimulated by blowing the gas sent back to the heating part toward the soot.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
In order to further clarify the configuration and operation of the present invention described above, preferred embodiments of the soot treating machine of the present invention will be described below.
FIG. 1 is a schematic configuration diagram of a soot processing machine as an embodiment of the present invention. This dredging machine is roughly divided into a heating unit 10 for heating the garbage A, a condensing unit 20 for condensing water vapor generated from the garbage A, a condensing unit 20 and the sewage pipe 1 communicating with each other for drainage and storage. It consists of a blocking drainage unit 30 that blocks ventilation according to the state of water, and a return unit 40 that sends the gas cooled by the condensing unit 20 back to the heating unit 10 again.
[0014]
The heating unit 10 includes a processing tank 11 that stores the garbage A, a processing tank heater 12 that heats the processing tank 11, and a heating chamber 13 that has a heat insulating structure that stores these. In addition, a lid 13 a that opens and closes in order to take in and out the processing tank 11 is formed in the upper part of the heating chamber 13.
[0015]
As shown in FIG. 2, the condensing unit 20 overlaps two metal plates 21 and 22 each having a recess having a predetermined shape, and seals the periphery of the metal plates 21 and 22 by seam welding to create a space inside. In this space, lower end opening partition walls 23, 23,... Having only the lower end opened and both end opening partition walls 24, 24,. The lower ends of the both-end open partition walls 24, 24,... Are formed at positions lower than the lower ends of the lower-end open partition walls 23, 23,. Only the lower end opening is closed, and a flow path for guiding the gas by meandering in the vertical direction is formed. Further, the bottom surface of the lower communication space is inclined downward toward the shut-off drain portion 30 to facilitate the flow of water.
[0016]
In addition, by installing the metal plates 21 and 22 so as to be vertically oriented, external air smoothly flows upward along the outer surface by the draft force, so that the cooling efficiency can be increased. Furthermore, since the partition wall meandering in the vertical direction is formed, the water condensed in the flow path tends to flow down by the vertical surface. Here, when only a flow path that is meandered in the vertical direction without providing a communication space in the lower part is formed, water condensed in the flow path accumulates and increases, thereby blocking the gas flow path. By forming the communication space, water condensed in the flow path can be sent to the blocking drainage unit 30 side, and by closing the communication space with the accumulated water, gas can meander and flow.
[0017]
The cutoff drainage unit 30 includes a tank 31 for storing water, a condensed water discharge pipe 32 that hangs down on the bottom surface of the tank 31 and flows the water from the condensation unit 20 downward, and an upper side surface of the tank 31 and the sewage pipe 1. A drain pipe 33 that drains water in a tank 31 that exceeds a predetermined water level d to the sewer pipe 1. With such a configuration, in a state where the water in the tank 31 is higher than the water level e which is the lower end opening surface of the condensed water discharge pipe 32, the space where the gas communicates between the heating chamber 13 and the condensing unit 20 is exposed to the outside. Seal against.
[0018]
The return unit 40 forms a return pipe 41 that communicates the downstream side of the condensing unit 20 and the heating chamber 13, and the return pipe 41 includes a fan 42 that allows gas to flow from the condensing unit 20 toward the heating chamber 13, and a fan A gas heater 43 that heats the gas on the downstream side of 42 and a nozzle 44 that injects the gas from the downstream end toward the garbage A in the heating chamber 13 are provided.
[0019]
Next, the operation of this soot processor will be described. When the garbage A is put into the treatment tank 11 and the drying operation is started, the treatment tank 11 is heated by the treatment tank heater 12. Therefore, the temperature in the processing tank 11 and the heating chamber 13 rises, the moisture contained in the garbage A evaporates, and the pressure in the space where the gas in the heating chamber 13 and the condensing unit 20 communicates rises. And when the water of the condensed water discharge pipe 32 descends to the water level e which is the lower end opening surface, as shown in FIG. 3, the air present in the heating chamber 13 and the condensing part 20 is pushed out to the sewer pipe 1 side. The pressure increases only to a pressure determined by the water level difference between the tank 31 and the condensed water discharge pipe 32. On the other hand, when a predetermined time elapses after the heating by the treatment tank heater 12 is started, the fan 42 and the gas heater 43 of the return unit 40 are operated. Therefore, the gas containing a large amount of water vapor in the heating chamber 13 flows into the condensing unit 20, is cooled when flowing meanderingly, and is sent back to the heating chamber 13 through the return pipe 41. At that time, since the gas sent from the heating chamber 13 to the condensing unit 20 is cooled and the dew point is lowered, the water vapor contained in the gas is condensed and becomes water, and accumulates in the lower part of the condensing unit and flows down to the condensed water discharge pipe 32. Then, the amount of heat given by the heating chamber 13 is made smaller than the amount of heat taken by the condensing unit 20 to increase the amount of water vapor condensation, so that the pressure in the heating chamber 13 and the condensing unit 20 decreases, and water is accumulated in the tank 31. Therefore, the gas communication space between the heating chamber 13 and the condensing unit 20 is in a sealed state with respect to the outside, and a part of the air that was present at the start of operation is pushed out to the sewer pipe 1 side. Negative pressure can be set.
[0020]
On the other hand, the gas whose water vapor content is reduced is heated to a high temperature by the gas heater 43 when flowing through the return pipe 41, and then sprayed to the garbage A in the treatment tank 11 by the nozzle 44. By directly injecting the gas having a low relative humidity by being heated by the gas heater 43 directly to the garbage A, evaporation of moisture contained in the garbage A is promoted, and dew condensation in the return pipe 41 is achieved. Is also prevented. Moreover, since the inside of the heating chamber 13 has a negative pressure, the boiling point is lowered, it is possible to evaporate water at a low temperature, and it is possible to make it difficult for odorous components to leak out from the gap with the lid 13a.
[0021]
The water that flows down from the condensing unit 20 accumulates in the tank 31, but since the water in the tank 31 exceeds the water level d flows to the sewer pipe 1 through the drain pipe 33, the water level does not continue to increase. Stabilize. And most of the odorous components generated from the garbage A are dissolved in the water accumulated in the tank 31 and drained to the sewer pipe 1. In addition, since the water level difference between the condensed water discharge pipe 32 and the tank 31 is determined by the pressure difference between the sealed space and the sewage pipe 1, the condensed water is used when the pressure in the sealed space is a negative pressure value. The water level in the discharge pipe 32 or the condensing unit 20 is stabilized at a water level C higher than the water level in the tank 31. As the water level C becomes higher than the water level L which is the lower end of the both-end opening partition wall 24 as shown in FIG. 1, a flow path for guiding gas in a meandering manner is formed.
[0022]
On the other hand, if the pressure in the sealed space continues to decrease, the water level difference between the water in the condensing unit 20 and the water in the tank 31 increases. And if the water of the condensation part 20 becomes higher than the water level H which becomes the lower end of the lower end opening partition wall 23, the gas flow path will be interrupted, but when the water in the tank 31 decreases and falls to the water level e, it is shown in FIG. Thus, the air on the tank 31 side is sucked to the condensed water discharge pipe 32 side, and the pressure in the sealed space is prevented from being excessively reduced. Therefore, it is possible to prevent the water level of the condensing unit 20 from rising too much.
[0023]
As described above, according to the soot processor of the present embodiment, the condensing unit 20 is installed so that the plates 21 and 22 are vertical, so that the outside air can easily flow upward along the outer surface by the draft force. Further, by introducing the gas in a meandering manner, the water vapor contained in the gas can be easily brought into contact with the inner surfaces of the plates 21 and 22 to increase the cooling efficiency, and the two metal plates 21 and 22 are overlapped. Since it has a simple structure, it can be realized at low cost. In addition, meandering up and down and providing a communication space at the bottom can prevent the flow path from being blocked by water condensed in the flow path, and by blocking the communication space with accumulated water The gas can meander and flow without being communicated. Furthermore, when the pressure in the sealed space decreases and the water in the tank 31 falls to the water level e, the water level in the condensing unit 20 rises due to the configuration in which the air on the tank 31 side is sucked into the condensed water discharge pipe 32 side. It is possible to prevent the gas flow path from being blocked by being too much. In addition, a return pipe 41 for sending the gas cooled in the condensing unit 20 back to the heating chamber 13 is provided, and the gas in the sealed space is forcibly circulated by the fan 42 so that the gas containing a large amount of water vapor is condensed in the condensing unit 20. Since the gas which has been smoothly cooled and cooled in the condensing unit 20 and has a reduced water vapor content flows smoothly into the heating chamber 13, the evaporation of water contained in the garbage A and the condensation of the generated water vapor can be efficiently performed. This can be done and the drying performance can be increased. Furthermore, by heating the gas sent to the heating chamber 13 via the return pipe 41, the gas having a low relative humidity can be directly injected onto the garbage A to promote the evaporation of moisture, and the return pipe 41 can prevent water vapor from condensing. In addition, the structure in which the flow of gas from the condensing unit 20 to the sewer pipe 1 is blocked by the water accumulated in the tank 31 includes the heating chamber 13 and the condensing unit 20 without using an on-off valve such as an electromagnetic valve. Since the space can be sealed with respect to the outside, it can be constructed at low cost, and since the water in the tank 31 exceeds the water level d flows into the sewer pipe 1 through the drain pipe 33, the sealed space is maintained. It can be drained while.
[0024]
Moreover, since the water vapor | steam generated from the heated garbage A is condensed and drained with an odor, since an odor leak and a humidity rise can be prevented, deterioration of the indoor environment can be prevented. Furthermore, since the inside of the heating chamber 13 has a negative pressure, odor leakage from the gap with the lid 13a can be prevented, so that it is not necessary to increase the sealing performance excessively, and the boiling point is lowered and drying is performed at a low temperature. Since it can process, the energy required for a heating can be reduced and power consumption can be reduced, and the temperature rise in a room | chamber can be reduced. In addition, it is not necessary to provide an expensive device such as a vacuum pump in order to make the inside of the heating chamber 13 have a negative pressure, and it is not necessary to provide a deodorizing device, a water vapor discharging device, etc., so that the structure is simplified and the cost is reduced. be able to.
[0025]
In this embodiment, the fan 42 and the gas heater 43 are operated after a lapse of a predetermined time since the heating by the processing tank heater 12 was started. However, the present invention is not limited to this. The temperature, humidity, pressure, etc. in the heating chamber 13 or the water level in the shut-off drain part 30 may be detected and operated based on the detected value, or may be operated simultaneously with the treatment tank heater 12.
Further, the cutoff drainage part is not limited to the structure as in the present embodiment. For example, as shown in FIG. It is good also as the S-shaped pipe | tube 51 which forms the going up flow path 53 and the drainage flow path 54 which communicates from the up flow path 53 to the down sewer 1 again. Moreover, it is good also as a structure which interrupts | blocks a flow path not only using the structure interrupted | blocked with water but using on-off valves, such as a solenoid valve.
Further, the garbage A is not limited to the configuration heated by the processing tank heater 12, and may be configured to be heated by, for example, a gas burner or a microwave.
Further, in this embodiment, the gas flowing through the return pipe 41 is heated by the gas heater 43, but it may be configured not to be heated. Moreover, the structure which evaporates the water | moisture content contained in the garbage A with the hot air heated with the gas heater 43 without using the heater 12 for process tanks may be sufficient. Moreover, the structure which does not send gas back from the condensation part 20 to the heating chamber 13 may be sufficient.
Further, for example, as shown in FIG. 6, the water in the condensing unit 20 may flow into the tank 31 by an amount exceeding a predetermined water level higher than the water level L that is the lower end of the both-end opening partition wall 24. According to such a configuration, the gas can be constantly meandered and flowed by preventing the gas flow path from communicating with the lower part regardless of the pressure of the condensing unit 20 and the amount of water in the tank 31.
Further, in the present embodiment, the space including the heating chamber 13 and the fin tube 21 is sealed and negative pressure is set, but a configuration without negative pressure may be used, or a configuration without sealing may be used.
[0026]
Although the embodiments of the present invention have been described above, the present invention is not limited to these embodiments, and it is needless to say that the present invention can be implemented in various modes without departing from the gist of the present invention.
[0027]
【The invention's effect】
As described above in detail, according to the soot treating machine according to claim 1 of the present invention, the gas containing water vapor is meandered and guided, whereby the water vapor and the inner surface of the plate can be easily brought into contact with each other to increase the cooling efficiency. Moreover, it can be realized at a low cost by a simple structure in which two plates are overlapped.
[0028]
Moreover , by installing the plate so as to be vertical, the outside air can easily flow upward along the outer surface by the draft force, and the cooling efficiency can be increased. In addition, it is possible to prevent the flow path from being blocked by water accumulated in the lower part of the water condensed in the flow path, and to increase the cooling efficiency by causing the gas to meander and flow without communicating. be able to.
[0029]
Further, the configuration in which the water level of the drainage path side of the condensation puddles and the pressure drops in the between-tight closed space of air and drainage roadside lowered to a predetermined sealing level is sucked into the sealed space, the water level of the water in the condensing part rises It is possible to prevent the gas flow path from being blocked by being too much.
[0030]
In the following, according to the garbage disposer according to claim 2 of the present invention, laden gas steam in the heating unit together smoothly flow into the condensing section, is cooled in the condensing section has decreased content of water vapor By returning the gas to the heating unit again, the moisture contained in the soot can be efficiently evaporated and the water vapor can be efficiently condensed, so that the drying performance can be enhanced. Moreover, evaporation of moisture can be promoted by blowing a gas having a reduced water vapor content on the soot.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram of a soot processing machine as an embodiment.
FIG. 2 is an explanatory diagram of a condensing unit.
FIG. 3 is an explanatory diagram showing water levels in a condensing unit and a shut-off drain unit.
FIG. 4 is an explanatory diagram showing water levels in a condensing unit and a shut-off drain unit.
FIG. 5 is a schematic configuration diagram of a soot processing machine as another example.
FIG. 6 is a schematic configuration diagram of a soot processing machine as another example.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 10 ... Heating part, 13 ... Heating chamber, 20 ... Condensing part, 21, 22 ... Metal plate,
23 ... A lower end opening partition, 24 ... Both ends opening partition, 30 ... Shut off drainage part,
31 ... Tank, 40 ... Return part, 41 ... Return pipe.

Claims (2)

生ゴミ等の厨芥を加熱する加熱部と、
上記加熱部と連通され上記厨芥から発生した水蒸気を含む気体を冷却する凝縮部と、
上記凝縮部で凝縮した水を外部に排水する排水路と、
上記凝縮部から排水路への流路に水を溜める凝縮水溜まりを形成し、該凝縮水溜まりに溜まった水が所定の密閉水位を越えた状態で該水により上記凝縮部と上記排水路とを遮断すると共に、上記密閉水位より高い所定の排水水位を越えた分の水を上記排水路に排水する遮断排水部を備える厨芥処理機であって、
上記凝縮部の圧力が上記排水路の圧力に比べて低くなり上記凝縮水溜まりにおける上記排水路側の水位が所定の密閉水位まで下降したときに、排水路側の空気が凝縮部側に吸入される構成とするとともに、
上記凝縮部を、少なくとも一方の板に凹みを設けた2枚の板を重ね合わせ該板の周囲をシールし鉛直となるように設置して内部に空間を生じさせるとともに、該空間内に、下端のみが開口した下端開口隔壁と、上下両端が共に開口してその下端位置を上記下端開口隔壁の下端位置よりも低くした両端開口隔壁とを交互に形成し、凝縮内部の空気を蛇行させて流通させるものとしたことを特徴とする厨芥処理機。
A heating section for heating straw such as raw garbage;
A condensing unit that communicates with the heating unit and cools a gas containing water vapor generated from the soot;
A drainage channel for draining the water condensed in the condensing unit to the outside;
A condensate pool is formed to store water in the flow path from the condensing unit to the drainage channel, and the condensate unit and the drainage channel are blocked by the water when the water accumulated in the condensate pool exceeds a predetermined sealed water level. And a dredger with a shut-off drain that drains the amount of water that exceeds a predetermined drainage water level higher than the sealed water level to the drainage channel,
When the pressure in the condensing unit is lower than the pressure in the drainage channel and the water level on the drainage channel side in the condensate pool is lowered to a predetermined sealed water level, the air on the drainage channel side is sucked into the condensing unit side. And
The condensing unit is installed so that at least one plate is provided with a dent, and the periphery of the plate is sealed so as to be vertical so as to create a space inside. The lower end opening partition wall that is open only and the both end opening partition walls that are open at both upper and lower ends and whose lower end position is lower than the lower end position of the lower end opening partition wall are alternately formed, and the air inside the condensate is circulated to circulate garbage processor, characterized in that it is assumed to be.
上記凝縮部で冷却した気体を上記加熱部に強制的に送り返す返還手段と、
上記加熱部に送り返した気体を厨芥に向かって吹き付ける吹き付けノズルとを備えたことを特徴とする請求項1記載の厨芥処理機。
A return means forcibly returning the gas cooled in the condensing unit to the heating unit;
The soot processing machine according to claim 1, further comprising a spray nozzle for spraying the gas sent back to the heating unit toward the soot.
JP36467597A 1997-12-16 1997-12-17 厨 芥 Processing machine Expired - Fee Related JP3777769B2 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
JP36467597A JP3777769B2 (en) 1997-12-17 1997-12-17 厨 芥 Processing machine
US09/207,265 US6076271A (en) 1997-12-16 1998-12-09 Garbage disposer
CN98123298A CN1115287C (en) 1997-12-16 1998-12-11 Refuse treatment device for kitchen
ES98123828T ES2210652T3 (en) 1997-12-16 1998-12-15 DEVICE FOR THE DISPOSAL OF GARBAGE.
EP98123828A EP0924488B1 (en) 1997-12-16 1998-12-15 Garbage disposer
DE69819459T DE69819459T2 (en) 1997-12-16 1998-12-15 A garbage disposer
KR10-1998-0055509A KR100492866B1 (en) 1997-12-16 1998-12-16 Food Waste Treatment
TW087120947A TW533098B (en) 1997-12-16 1998-12-16 Garbage disposal machine
HK99105889A HK1020933A1 (en) 1997-12-16 1999-12-15 Kitchen garbage disposal apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP36467597A JP3777769B2 (en) 1997-12-17 1997-12-17 厨 芥 Processing machine

Publications (2)

Publication Number Publication Date
JPH11169822A JPH11169822A (en) 1999-06-29
JP3777769B2 true JP3777769B2 (en) 2006-05-24

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP36467597A Expired - Fee Related JP3777769B2 (en) 1997-12-16 1997-12-17 厨 芥 Processing machine

Country Status (1)

Country Link
JP (1) JP3777769B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113104437A (en) * 2021-03-30 2021-07-13 广州恩华特环境技术有限公司 Garbage disposal device and garbage disposal system

Also Published As

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JPH11169822A (en) 1999-06-29

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