JP3767801B2 - Garbage disposal method and apparatus - Google Patents

Garbage disposal method and apparatus Download PDF

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Publication number
JP3767801B2
JP3767801B2 JP2001163631A JP2001163631A JP3767801B2 JP 3767801 B2 JP3767801 B2 JP 3767801B2 JP 2001163631 A JP2001163631 A JP 2001163631A JP 2001163631 A JP2001163631 A JP 2001163631A JP 3767801 B2 JP3767801 B2 JP 3767801B2
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Prior art keywords
garbage
cooling means
heat
treatment tank
heating
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JP2002355634A (en
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孝徳 山本
洋城 吉村
孝紀 望月
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Takagi Industrial Co Ltd
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Takagi Industrial Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、生ごみを加熱して乾燥処理する生ごみ処理方法及びその装置に関する。
【0002】
【従来の技術】
最近、厨房等より発生する生ごみは多量の水分等を含んでおり、その水分等を除去すれば、その減量化を図ることができる。乾燥させた生ごみは、通常の可燃ごみとして廃棄、又は、肥料等の再利用が可能である。
【0003】
【発明が解決しようとする課題】
ところで、生ごみの乾燥処理では、乾燥中に多量の油脂分が蒸気化して冷却手段であるラジエータ側に流れ、冷却によってラジエータ内で凝固すると、ラジエータの機能を低下させ、処理槽で発生した蒸気の冷却循環を妨げるおそれがある。その結果、処理槽内の内圧を上昇させ、乾燥処理を困難にするおそれがある。固化した油脂分を洗浄等で除去することは、ラジエータの構造からしても非常に厄介である。
【0004】
そこで、本発明は、油脂分の凝縮による不都合を防止した生ごみ処理方法及びその装置を提供することを課題とする。
【0005】
【課題を解決するための手段】
本発明の生ごみ処理方法は、処理槽内で加熱される生ごみから発生する蒸気を冷却手段に循環させて冷却して凝縮水と分離させた後、前記処理槽に戻す生ごみ処理方法であって、前記冷却手段に隣接して配設された加熱手段を発熱させ、この加熱手段の発熱により、前記生ごみの加熱処理前、加熱処理中又は加熱処理後に前記冷却手段を油脂溶解温度以上に加熱することを特徴とする。即ち、処理槽内で発生した蒸気には生ごみの水分とともに油脂分が含まれており、このような蒸気が冷却手段に流れて冷却されて凝縮すると、その油脂分が固化することになる。そこで、冷却手段を油脂溶解温度以上に加熱することにより、固化している油脂分は軟化して流動化し、容易に排出することができる。この場合、冷却手段の加熱時期は、生ごみの加熱処理前、加熱処理中又は加熱処理後の何れを選択してもよく、また、併用してもよい。
【0006】
本発明の生ごみ処理装置は、生ごみを収容して加熱する処理槽と、この処理槽に発生した蒸気を冷却する冷却手段と、この冷却手段に前記処理槽で発生した前記蒸気を導き、前記冷却手段で凝縮させ、凝縮水と分離させた後、前記処理槽に戻す循環手段と、前記冷却手段に併設され、前記生ごみの加熱処理前、加熱処理中又は加熱処理後に前記冷却手段を油脂溶解温度以上に加熱する加熱手段とを備えたことを特徴とする。即ち、加熱によって処理槽内の生ごみから発生した蒸気中の油脂分は、循環手段を通じて処理槽から冷却手段に流れて冷却され、凝縮する。そこで、加熱手段によって冷却手段を油脂溶解温度以上に加熱すれば、固化している油脂分は軟化して流動化し、容易に排出することができる。この場合、冷却手段の加熱時期は、生ごみの加熱処理前、加熱処理中又は加熱処理後の何れを選択してもよく、また、併用してもよい。
【0007】
本発明の生ごみ処理装置は、生ごみを収容する処理槽と、この処理槽の前記生ごみを加熱する加熱手段と、前記処理槽に発生した蒸気を冷却する冷却手段とを備え、前記生ごみの加熱処理前、加熱処理中又は加熱処理後に前記冷却手段を油脂溶解温度以上に加熱する熱源に前記加熱手段を用いたことを特徴とする。即ち、冷却手段を油脂溶解温度以上に加熱する熱源には、処理槽側の加熱手段の熱を用いることができ、冷却手段内の油脂分を軟化させて流動化させ、容易に排出させることができる。
【0008】
本発明の生ごみ処理装置において、前記冷却手段に放熱ファン(50)を備え、前記冷却手段の加熱時、前記放熱ファンを停止させることを特徴とする。即ち、冷却手段には放熱手段として放熱ファンが備えられるが、この放熱ファンを停止させることで放熱を抑え、冷却手段の加熱を促進することができる。
【0009】
本発明の生ごみ処理装置において、前記冷却手段に放熱ファンを備え、前記冷却手段の加熱時、前記放熱ファンを回転させることにより、熱風を前記冷却手段に流すことを特徴とする。即ち、冷却手段には放熱手段として放熱ファンが備えられるが、この放熱ファンを回転させて熱風を通流させることにより、冷却手段の加熱を促進させることができる。
【0010】
本発明の生ごみ処理方法は、処理槽内で加熱される生ごみから発生する蒸気を冷却手段に循環させて冷却して凝縮水と分離させた後、前記処理槽に戻す生ごみ処理方法であって、前記冷却手段に対する前記蒸気の循環量を制御して前記冷却手段を加熱することを特徴とする。即ち、蒸気が持つ熱を熱源に用いて冷却手段の加熱を行うことができ、油脂分の溶解、流動化による排出が可能となる。
【0011】
【発明の実施の形態】
図1及び図2は本発明の生ごみ処理方法及びその装置の第1実施例を示し、図1は生ごみ処理装置、図2はその制御装置を示している。
【0012】
乾燥処理すべき生ごみ2を収容する処理槽4には例えば、底面側を半円筒状とした容器が用いられ、この処理槽4内には生ごみ2を攪拌する攪拌手段としての攪拌羽根車であるスクレーパ6が設けられている。このスクレーパ6は、例えば、回転軸8に放射状に突設した複数のアーム10の先端に攪拌羽根12を取り付けたものであり、回転軸8の両端が処理槽4の側面に設けられた軸受14によって回転可能に支持されている。回転軸8には、攪拌モータ16からの回転力を受けるためのプーリ18が取り付けられ、このプーリ18と攪拌モータ16側の駆動プーリ20との間には、駆動チェーン22が懸け回されている。即ち、スクレーパ6には攪拌モータ16により矢印A、Bで示すように、所望の回転、連続回転、断続回転、正逆回転等の回転パターンを持つ回転が付与される。このスクレーパ6の回転により、処理槽4内の生ごみ2が攪拌されるとともに粉砕される。この実施例では、スクレーパ6の回転駆動手段として攪拌モータ16を用いているが、エンジン等の駆動手段を用いてもよく、回転伝達手段にはプーリ18及び駆動プーリ20に代えてスプロケットホイール及びチェーンでもよく、また、ギア機構等を用いてもよい。
【0013】
この処理槽4の上部側には、生ごみ2を処理槽4内に装填するための投入口24が形成されているとともに、この投入口24を開閉する扉26がヒンジ28で開閉可能に取り付けられている。即ち、扉26は把手30を持って開閉可能であり、閉止状態では図示しないパッキン等の封止手段によって処理槽4を密封状態に維持するものである。
【0014】
また、この処理槽4の底面部には第1の加熱手段として、処理槽4内の生ごみ2を加熱するヒータ32が設置されているとともに、ヒータ32の発熱温度を検出する第1の温度検出手段として温度センサ34が設置されている。この実施例にあっては、処理槽4の湾曲面に沿ってヒータ32が設置されている。加熱手段としては、燃料ガスを燃焼させるバーナ等を用いてもよい。また、処理槽4内の処理温度を検出する第2の温度検出手段として温度センサ35が処理槽4の外壁に取り付けられている。
【0015】
そして、処理槽4で発生した蒸気36を冷却させて凝縮する冷却手段ないし凝縮手段としてラジエータ38が設置され、このラジエータ38と処理槽4との間には蒸気36を循環させるための循環手段として循環路40が設けられており、この循環路40は往管42及び戻管44で構成されている。即ち、処理槽4内で気化した油脂分は蒸気36とともにラジエータ38に流れる。このラジエータ38は、蒸気36を分流させて通流する複数の細管46を備えるとともにその細管46に放熱フィン48を取り付けたものである。このラジエータ38には放熱手段として例えば、放熱ファン50が設けられ、この放熱ファン50は駆動手段であるモータ52によって駆動される。この放熱ファン50の回転によって流通する冷却空気Cの通流により、ラジエータ38の放熱が促進され、ラジエータ38内を通過する蒸気36が放熱、冷却され、凝縮水54を生じるが、蒸気36内の油脂分はその冷却によって固化し、ラジエータ38の細管46内に滞留するおそれがある。そこで、この油脂分を除去する第2の加熱手段としてヒータ56が設置されている。このヒータ56によってラジエータ38の細管46等に滞留する油脂分を流動化させることができる。
【0016】
この実施例にあっては、ラジエータ38は放熱面を水平方向にした縦置型であり、その底面側に設けられた気水分離部58に蒸気36の冷却により発生する凝縮水54が導かれる。この気水分離部58には排水管60が連結されており、この排水管60の中途部には臭気止めとしてU字トラップ62が設けられている。
【0017】
往管42が接続されているラジエータ38の入側には冷却前の蒸気温度を検出する第3の温度検出手段として、ラジエータ38の入側温度を検出する温度センサ64、気水分離部58には冷却後の蒸気温度を検出する第4の温度検出手段として、温度センサ66が設けられている。また、戻管44には蒸気36を強制的に循環させる手段として循環ファン68が取り付けられ、この循環ファン68は駆動手段であるモータ70によって駆動される。
【0018】
そして、運転スイッチ72からの運転指令、温度センサ34、35、64、66等の制御情報により攪拌モータ16の回転制御やヒータ32、56の駆動及び温度制御を行う制御手段として制御装置74が設けられている。この制御装置74は、例えば、図2に示すように、マイクロプロセッサ等で構成される演算制御部76が設けられ、この演算制御部76には、運転を指令する運転スイッチ72、温度センサ34、35、64、66から入力信号が加えられるとともに、この演算制御部76から出力された駆動出力は、攪拌モータ16、モータ52、70、ヒータ32、56等に加えられる。
【0019】
次に、生ごみ処理方法及びその装置の動作を図3に示すフローチャートを参照して説明する。
【0020】
第1段階のルーチン(ステップS1〜S2)は、生ごみ2の加熱処理前のラジエータ38のクリーニング処理を示すルーチン、第2段階のルーチン(ステップS3〜S4)は生ごみ2の加熱乾燥処理を示すルーチン、第3段階のルーチン(ステップS5〜S6)は、生ごみ2の加熱乾燥処理後のラジエータ38のクリーニング処理を示すルーチンである。
【0021】
ステップS1では、扉26を開き、処理槽4に生ごみ2を装填した後、運転スイッチ72を投入すると、ラジエータクリーニング処理モードが実行される。即ち、制御装置74を通してヒータ56に通電され、ヒータ56によってラジエータ38の加熱が開始され、ステップS2に移行する。即ち、この加熱処理は所定時間が継続して行われる。このような加熱処理において、ラジエータ38の内部に油脂分が残留していれば、その加熱によって溶解、流動化した油脂分が凝縮水54と同様に、気水分離部58に滴下し、排水管60に排出される。
【0022】
そして、所定時間が経過すると、ステップS3に移行し、生ごみ2の加熱乾燥処理が開始される。この処理では、攪拌モータ16、モータ52、70を回転させるとともに、ヒータ32に通電し、処理槽4内の生ごみ2の加熱とともにスクレーパ6の回転によって生ごみ2の攪拌及びその攪拌による粉砕が行われる。加熱が進み、生ごみ2から発生した蒸気36は処理槽4から循環路40の往管42を通してラジエータ38に流れ、放熱によって冷却される。この冷却により発生した凝縮水54は気体分と分離されて気水分離部58に滴下し、排水管60を通して外部に排水される。この凝縮水54と分離された蒸気36は戻管44を通じて処理槽4に戻るが、凝縮した分だけ体積が減ることから、処理槽4の内部圧力が抑制され、処理槽4からの臭気漏れが防止されている。
【0023】
この生ごみ乾燥処理において、ラジエータ38の入側温度T1 は温度センサ64によって検出され、また、その出側温度T2 は温度センサ66によって検出される。これらの検出温度T1 、T2 は、生ごみ2の乾燥が進行するに従って変化し、検出温度T1 、T2 の温度差ΔT(=T1 〜T2 )が所定値に上昇したとき、生ごみ2の乾燥が完了する。即ち、蒸気36の水分が減少すると、検出温度T1 が上昇し、検出温度T2 が低下する結果、温度差ΔTが大きくなるので、その比較値Tmを設定し、この比較値Tmまで温度差ΔTが到達したとき、生ごみ2の乾燥を終了する。
【0024】
そこで、ステップS4では、温度差ΔTが比較値Tmに到達したか否かによって生ごみ乾燥終了か否かを判定し、到達するまで乾燥処理を持続させ、温度差ΔTが比較値Tmに到達したとき、生ごみ乾燥を終了する。この生ごみ乾燥が終了すると、ヒータ32の通電を解除し、攪拌モータ16、モータ52、70を停止させるとともに、表示器78に乾燥終了を表示する。
【0025】
この生ごみ乾燥終了の後、ステップS5に移行し、再度、ラジエータクリーニング処理モードが実行される。即ち、ヒータ56に通電され、ヒータ56によってラジエータ38の加熱が開始され、ステップS6に移行する。即ち、この加熱処理が所定時間継続して行われる。このような加熱処理において、乾燥処理で発生した蒸気36により、ラジエータ38の内部に油脂分が残留していれば、その加熱によって溶解、流動化した油脂分が凝縮水54と同様に、気水分離部58に滴下し、排水管60に排出される。
【0026】
このように、生ごみ2の乾燥処理によって生じる油脂分の蒸発、ラジエータ38内での油脂分の固化による閉塞状態を解消させることができ、ラジエータ38の機能低下を防止することができるとともに、生ごみ2の乾燥処理の効率化を図ることができ、乾燥処理後のラジエータ38のメンテナンスや清掃処理が不要となり、乾燥処理前の準備も簡略化することができる。
【0027】
なお、この実施例では、生ごみ乾燥処理の前後にラジエータ加熱処理を行っているが、生ごみ2の加熱処理前又は加熱処理後、何れか一方を選択して行ってもよく、また、生ごみ乾燥処理途上にラジエータ加熱処理を介在させてもよい。即ち、生ごみ乾燥処理を中断させ、又は生ごみ乾燥処理と並行してラジエータ加熱処理を行えば、生ごみ2の加熱処理途上で発生する油脂分を流動化させて排出することができ、ラジエータ38の機能低下による不都合を防止することができ、生ごみ乾燥処理の効率化を図ることができる。
【0028】
次に、図4は、本発明の生ごみ処理方法及びその装置の第2実施例を示している。
【0029】
この実施例は、ラジエータ38の加熱手段としてヒータ32を熱源に用いるものである。即ち、処理槽4の底面側に蓄熱手段としてのカバー80が取り付けられてヒータ32が包囲され、カバー80から導熱パイプ82を介してラジエータ38の細管46側に導くようにしたものである。導熱パイプ82には開閉弁84が設置されているとともに、導熱ファン86が設置され、導熱ファン86はモータ88によって駆動される。また、ラジエータ38の近傍には、外気温度を検出する温度センサ90が設置されている。
【0030】
前記実施例と同様に制御装置74が設けられ、この制御装置74には温度センサ90等の検出温度が制御情報として入力されており、この制御装置74が発生する制御出力がモータ52、70、開閉弁84及びモータ88等に加えられている。
【0031】
この実施例の生ごみ処理方法及びその装置では、生ごみ2の加熱処理前、加熱処理中又は加熱処理後の何れか又はこれらから選択される時期に開閉弁84を開き、導熱ファン86を回転させれば、カバー80内の蓄熱によって熱風92が得られ、その熱風92をラジエータ38に送り込むことで、ラジエータ38を加熱し、残留している油脂分を溶解及び流動化させ、排水管60に排出することができる。その他の動作は、第1実施例と同様である。
【0032】
そして、ラジエータ38側の外気温度を温度センサ90で検出し、外気温度が高い場合には、放熱ファン50の回転数を上昇させる等、その検出温度に応じて放熱ファン50の回転制御を行うようにしてもよい。その検出温度によって蒸気36の循環量を制御してもよい。また、外気温度が低い時には、導熱ファン86を動作させてラジエータ38を加熱してもよい。
【0033】
また、第1及び第2実施例では、ラジエータ38の加熱処理にヒータ56又はヒータ32を用いているが、蒸気36が持つ熱を利用してもよい。即ち、ラジエータ38の放熱手段である放熱ファン50を停止すると、ラジエータ38の温度が蒸気36が持つ熱によって上昇することになる。そこで、温度センサ64によって検出されるラジエータ38の入側温度が所定温度、例えば、60℃に上昇するまで放熱ファン50の回転を停止させ、ラジエータ38の温度上昇による加熱を以て油脂分を溶解及び流動化させることができ、排水管60に排出することができる。この処理の後、放熱ファン50を回転させ、蒸気36を凝縮させ、凝縮水54を流すことにより、処理槽4内の内圧を安定化させることができる。
【0034】
そして、ラジエータ38の入側温度と出側温度との温度差ΔTが所定温度に到達したとき、再び、放熱ファン50を所定時間だけ停止させ、蒸気36が持つ熱によってラジエータ38を加熱し、油脂分を溶解及び流動化させてラジエータ38外に除去することができる。
【0035】
また、生ごみの乾燥処理中にヒータ32、ヒータ32とともに設置され又はヒータ32に代えて設置される他の加熱源を所定の時間間隔で間欠駆動させ、生ごみ処理中の油脂分を溶解して排出させ、油脂分の蓄積を防止してもよい。また、この実施例では、ラジエータ38の加熱源としてその近傍にヒータ56を配置したが、ラジエータ38内にヒータ等の加熱源を設置してラジエータ38をその内部から加熱してもよい。
【0036】
また、放熱ファン50を停止状態又は回転状態で、循環ファン68の回転を上昇させると、多量の蒸気36をラジエータ38に流すことができ、蒸気36が持つ熱によってラジエータ38を加熱することができる。そこで、循環ファン68の回転の増減によりラジエータ38に対する蒸気36の循環量を制御すれば、蒸気36の熱を熱源に用いてラジエータ38を加熱することができ、同様にラジエータ38内の油脂分を溶解又は流動化させ、ラジエータ38から除去することができる。
【0037】
なお、第1実施例において、ラジエータ38側に外気温度を検出する温度センサ90を設置し、ラジエータ38の放熱量の制御、蒸気36の循環量、ヒータ32、56の発熱制御を行うようにしてもよい。これらヒータ32、56の発熱制御について、例えば、外気温度が低い場合には発熱量を高く、外気温度が高い場合には発熱量を低くする等、外気温度に応じて発熱量を制御すれば、効率的な発熱制御を行うことができる。
【0038】
また、放熱ファン50の上流側にラジエータ38の加熱手段としてヒータを設置し、ラジエータ38の加熱時、そのヒータ及び放熱ファン50を動作させて熱風をラジエータ38に供給すれば、同様に、ラジエータ38内の油脂分を溶解及び流動化させてラジエータ38外に排出することができる。
【0039】
【発明の効果】
以上説明したように、本発明によれば、次の効果が得られる。
a 生ごみに含まれるラード等の油脂分が冷却手段内で凝固しても、冷却手段を加熱することにより、その油脂分を溶解及び流動化させるので、冷却手段から容易に除去でき、冷却手段の機能低下を防止できるとともに、寿命低下を防止できる。
b 冷却手段の加熱は、生ごみの加熱処理前、加熱処理中又は加熱処理後の何れでもよく、又はこれらの時期の複数であってもよく、冷却手段の機能低下防止により、生ごみ乾燥処理の迅速化を図ることができる。
c 冷却手段の加熱に処理槽の加熱手段が発生する熱を併用すれば、特別な加熱手段を用いる必要がなく、冷却手段の機能低下防止を図ることができる。
d 冷却手段の放熱ファンを停止させて放熱量を抑制することで、冷却手段の加熱を促進することができる。
e 冷却手段の放熱ファンを回転させて熱風を通流させることで、冷却手段の加熱を促進することができる。
f 冷却手段に流れる蒸気の循環量を制御して冷却手段を加熱すれば、特別な熱源を用いることなく、冷却手段から油脂分を溶解及び流動化させ、排出することができる。
【図面の簡単な説明】
【図1】本発明の生ごみ処理方法及びその装置の第1実施例を示す図である。
【図2】その制御装置を示すブロック図である。
【図3】生ごみ乾燥処理及びラジエータの加熱制御を示すフローチャートである。
【図4】本発明の生ごみ処理方法及びその装置の第2実施例を示す図である。
【符号の説明】
2 生ごみ
4 処理槽
32 ヒータ(加熱手段)
36 蒸気
38 ラジエータ(冷却手段)
40 循環路(循環手段)
50 放熱ファン
54 凝縮水
56 ヒータ(加熱手段)
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a garbage disposal method and apparatus for heating and drying garbage.
[0002]
[Prior art]
Recently, garbage generated from kitchens or the like contains a large amount of water and the like, and if the water and the like are removed, the amount can be reduced. Dried garbage can be discarded as normal combustible waste or reused as fertilizer.
[0003]
[Problems to be solved by the invention]
By the way, in the drying process of garbage, a large amount of oil and fat is vaporized during drying and flows to the radiator side, which is a cooling means, and solidifies in the radiator by cooling, thereby reducing the function of the radiator and generating steam generated in the treatment tank. There is a risk of hindering the cooling circulation. As a result, there is a possibility that the internal pressure in the treatment tank is increased and the drying process becomes difficult. It is very troublesome to remove the solidified fats and oils by washing or the like even from the structure of the radiator.
[0004]
Then, this invention makes it a subject to provide the garbage processing method and its apparatus which prevented the inconvenience by condensation of fats and oils.
[0005]
[Means for Solving the Problems]
The garbage treatment method of the present invention is a garbage treatment method in which steam generated from the garbage heated in the treatment tank is circulated through a cooling means, cooled and separated from condensed water, and then returned to the treatment tank. The heating means disposed adjacent to the cooling means generates heat, and the heat generated by the heating means causes the garbage to be heated above the oil dissolution temperature before, during or after the heat treatment of the garbage. It is characterized by heating. That is, the steam generated in the treatment tank contains oil and fat together with the moisture of the garbage, and when such steam flows to the cooling means and is cooled and condensed, the oil and fat is solidified. Therefore, by heating the cooling means to a temperature equal to or higher than the fat dissolving temperature , the solidified fat and oil can be softened and fluidized and easily discharged. In this case, the heating timing of the cooling means may be selected before, during or after the heat treatment of garbage, or may be used in combination.
[0006]
The garbage processing apparatus of the present invention is a treatment tank that accommodates and heats garbage, a cooling means that cools the steam generated in the treatment tank, and the steam generated in the treatment tank is guided to the cooling means, The cooling means is condensed by the cooling means and separated from the condensed water and then returned to the treatment tank, and is provided in the cooling means, and the cooling means is disposed before, during or after the heating treatment of the garbage. And a heating means for heating to a temperature equal to or higher than the oil / fat dissolution temperature . That is, the fat and oil in the steam generated from the garbage in the treatment tank by heating flows from the treatment tank to the cooling means through the circulation means, and is cooled and condensed. Therefore, if the cooling means is heated to a temperature equal to or higher than the fat dissolving temperature by the heating means, the solidified fat and oil can be softened and fluidized and easily discharged. In this case, the heating timing of the cooling means may be selected before, during or after the heat treatment of garbage, or may be used in combination.
[0007]
The garbage processing apparatus of the present invention comprises a treatment tank for containing garbage, a heating means for heating the garbage in the treatment tank, and a cooling means for cooling the steam generated in the treatment tank, The heating means is used as a heat source for heating the cooling means to a temperature equal to or higher than the oil dissolution temperature before, during or after the heat treatment of the waste. That is, the heat source for heating the cooling means or fat melting temperature can be used the heat of the heating means of the processing tank side, to soften the grease in the cooling means is fluidized, it is easily discharged it can.
[0008]
In the garbage processing apparatus of the present invention, the cooling means includes a heat radiating fan (50), and the heat radiating fan is stopped when the cooling means is heated. That is, the cooling means is provided with a heat radiating fan as the heat radiating means. By stopping the heat radiating fan, the heat radiating can be suppressed and heating of the cooling means can be promoted.
[0009]
In the garbage processing apparatus of the present invention, the cooling means is provided with a heat radiating fan, and when the cooling means is heated, the heat radiating fan is rotated to flow hot air to the cooling means. In other words, the cooling means is provided with a heat radiating fan as the heat radiating means. By rotating the heat radiating fan and flowing hot air, heating of the cooling means can be promoted.
[0010]
The garbage treatment method of the present invention is a garbage treatment method in which steam generated from the garbage heated in the treatment tank is circulated through a cooling means, cooled and separated from condensed water, and then returned to the treatment tank. And the cooling means is heated by controlling a circulation amount of the steam to the cooling means. That is, the heat of the steam can be used as a heat source to heat the cooling means, and the oil and fat can be discharged and discharged by fluidization.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
1 and 2 show a first embodiment of a garbage disposal method and apparatus according to the present invention, FIG. 1 shows a garbage disposal apparatus, and FIG. 2 shows a control apparatus thereof.
[0012]
For example, a container having a bottom-side semi-cylindrical shape is used as the treatment tank 4 for storing the garbage 2 to be dried, and a stirring impeller as a stirring means for stirring the garbage 2 is used in the treatment tank 4. A scraper 6 is provided. The scraper 6 is, for example, one in which stirring blades 12 are attached to the tips of a plurality of arms 10 projecting radially on the rotating shaft 8, and both ends of the rotating shaft 8 are provided on bearings 14 provided on the side surfaces of the processing tank 4. Is supported rotatably. A pulley 18 for receiving a rotational force from the stirring motor 16 is attached to the rotating shaft 8, and a drive chain 22 is suspended between the pulley 18 and the driving pulley 20 on the stirring motor 16 side. . That is, as shown by arrows A and B, the scraper 6 is provided with a rotation having a rotation pattern such as desired rotation, continuous rotation, intermittent rotation, and forward / reverse rotation, as indicated by arrows A and B. By the rotation of the scraper 6, the garbage 2 in the treatment tank 4 is stirred and pulverized. In this embodiment, the agitation motor 16 is used as the rotation drive means of the scraper 6. However, a drive means such as an engine may be used, and the rotation transmission means is replaced with the pulley 18 and the drive pulley 20 by using a sprocket wheel and chain. Alternatively, a gear mechanism or the like may be used.
[0013]
An inlet 24 for loading the garbage 2 into the processing tank 4 is formed on the upper side of the processing tank 4, and a door 26 for opening and closing the inlet 24 is attached by a hinge 28 so as to be opened and closed. It has been. That is, the door 26 can be opened and closed with the handle 30 and, in the closed state, the processing tank 4 is maintained in a sealed state by a sealing means such as packing (not shown).
[0014]
A heater 32 for heating the garbage 2 in the treatment tank 4 is installed as a first heating means on the bottom surface of the treatment tank 4 and a first temperature for detecting the heat generation temperature of the heater 32 is provided. A temperature sensor 34 is installed as detection means. In this embodiment, a heater 32 is installed along the curved surface of the processing tank 4. As the heating means, a burner or the like for burning fuel gas may be used. A temperature sensor 35 is attached to the outer wall of the processing tank 4 as second temperature detection means for detecting the processing temperature in the processing tank 4.
[0015]
A radiator 38 is installed as a cooling means or a condensing means for cooling and condensing the steam 36 generated in the treatment tank 4, and as a circulation means for circulating the steam 36 between the radiator 38 and the treatment tank 4. A circulation path 40 is provided, and the circulation path 40 includes an outward pipe 42 and a return pipe 44. That is, the fat and oil vaporized in the treatment tank 4 flows to the radiator 38 together with the steam 36. The radiator 38 includes a plurality of thin tubes 46 through which the steam 36 is divided and flows, and heat radiating fins 48 are attached to the thin tubes 46. The radiator 38 is provided with, for example, a heat dissipation fan 50 as heat dissipation means, and the heat dissipation fan 50 is driven by a motor 52 as drive means. Due to the flow of the cooling air C circulated by the rotation of the heat radiating fan 50, the heat radiation of the radiator 38 is promoted, and the steam 36 passing through the radiator 38 is radiated and cooled to generate condensed water 54. The oil and fat is solidified by the cooling and may stay in the narrow tube 46 of the radiator 38. Therefore, a heater 56 is installed as a second heating means for removing the oil and fat. This heater 56 can fluidize the oil and fat staying in the thin tube 46 of the radiator 38 and the like.
[0016]
In this embodiment, the radiator 38 is of a vertical type in which the heat radiating surface is in the horizontal direction, and the condensed water 54 generated by the cooling of the steam 36 is guided to the steam / water separator 58 provided on the bottom side thereof. A drain pipe 60 is connected to the air / water separator 58, and a U-shaped trap 62 is provided in the middle of the drain pipe 60 as an odor stopper.
[0017]
As a third temperature detecting means for detecting the steam temperature before cooling on the inlet side of the radiator 38 to which the outgoing pipe 42 is connected, a temperature sensor 64 for detecting the inlet temperature of the radiator 38 and a steam / water separator 58 are provided. A temperature sensor 66 is provided as a fourth temperature detecting means for detecting the steam temperature after cooling. A circulation fan 68 is attached to the return pipe 44 as a means for forcibly circulating the steam 36, and the circulation fan 68 is driven by a motor 70 as a drive means.
[0018]
A control device 74 is provided as a control means for performing rotation control of the agitating motor 16, driving of the heaters 32 and 56, and temperature control based on the operation command from the operation switch 72 and control information of the temperature sensors 34, 35, 64, 66, and the like. It has been. For example, as shown in FIG. 2, the control device 74 is provided with a calculation control unit 76 constituted by a microprocessor or the like. Input signals are applied from 35, 64 and 66, and the drive output output from the arithmetic control unit 76 is applied to the stirring motor 16, the motors 52 and 70, the heaters 32 and 56, and the like.
[0019]
Next, the garbage processing method and the operation of the apparatus will be described with reference to the flowchart shown in FIG.
[0020]
The first-stage routine (steps S1 to S2) is a routine showing the cleaning process of the radiator 38 before the heating process of the garbage 2, and the second-stage routine (steps S3 to S4) is the heating and drying process of the garbage 2. The routine shown and the third-stage routine (steps S5 to S6) are routines showing the cleaning process of the radiator 38 after the heating and drying process of the garbage 2.
[0021]
In step S1, when the operation switch 72 is turned on after the door 26 is opened and the garbage 2 is loaded into the processing tank 4, the radiator cleaning processing mode is executed. That is, the heater 56 is energized through the control device 74, and heating of the radiator 38 is started by the heater 56, and the process proceeds to step S2. That is, this heat treatment is performed continuously for a predetermined time. In such a heat treatment, if the oil and fat remains in the radiator 38, the oil and fat dissolved and fluidized by the heating is dripped onto the steam-water separator 58 in the same manner as the condensed water 54, and the drain pipe 60 is discharged.
[0022]
And when predetermined time passes, it will transfer to step S3 and the heat drying process of the garbage 2 will be started. In this process, the agitation motor 16 and the motors 52 and 70 are rotated, the heater 32 is energized, the garbage 2 in the treatment tank 4 is heated, and the scraper 6 is rotated to agitate the garbage 2 and pulverize by the agitation. Done. As the heating progresses, the steam 36 generated from the garbage 2 flows from the treatment tank 4 to the radiator 38 through the outgoing pipe 42 of the circulation path 40 and is cooled by heat radiation. Condensed water 54 generated by this cooling is separated from the gas component and dropped into the steam / water separator 58 and drained to the outside through the drain pipe 60. The vapor 36 separated from the condensed water 54 returns to the treatment tank 4 through the return pipe 44. However, since the volume decreases by the amount of condensation, the internal pressure of the treatment tank 4 is suppressed, and odor leakage from the treatment tank 4 occurs. It is prevented.
[0023]
In the garbage drying process, the inlet temperature T 1 of the radiator 38 is detected by the temperature sensor 64, and the outlet temperature T 2 is detected by the temperature sensor 66. These detected temperatures T 1 and T 2 change as the drying of the garbage 2 proceeds, and when the temperature difference ΔT (= T 1 to T 2 ) between the detected temperatures T 1 and T 2 rises to a predetermined value, The drying of garbage 2 is completed. That is, when the moisture of the steam 36 decreases, the detected temperature T 1 rises and the detected temperature T 2 falls, and as a result, the temperature difference ΔT increases. Therefore, the comparison value Tm is set, and the temperature difference up to this comparison value Tm is set. When ΔT has reached, the drying of the garbage 2 is finished.
[0024]
Therefore, in step S4, it is determined whether or not the garbage drying is finished depending on whether or not the temperature difference ΔT has reached the comparison value Tm. The drying process is continued until the temperature difference ΔT has reached, and the temperature difference ΔT has reached the comparison value Tm. When the garbage drying ends. When the garbage drying is finished, the heater 32 is de-energized, the stirring motor 16 and the motors 52 and 70 are stopped, and the display 78 displays the completion of drying.
[0025]
After the garbage drying is finished, the process proceeds to step S5, and the radiator cleaning process mode is executed again. That is, the heater 56 is energized, and heating of the radiator 38 is started by the heater 56, and the process proceeds to step S6. That is, this heat treatment is continuously performed for a predetermined time. In such a heat treatment, if the oil and fat remains in the radiator 38 due to the steam 36 generated in the drying treatment, the oil and fat dissolved and fluidized by the heating is similar to the condensed water 54 in the air and water. It drops on the separation unit 58 and is discharged to the drain pipe 60.
[0026]
As described above, it is possible to eliminate the oil and fat evaporation caused by the drying treatment of the garbage 2 and the clogged state due to the solidification of the oil and fat in the radiator 38, and to prevent the function of the radiator 38 from being deteriorated. The efficiency of the drying process of the garbage 2 can be improved, and the maintenance and the cleaning process of the radiator 38 after the drying process become unnecessary, and the preparation before the drying process can be simplified.
[0027]
In this embodiment, the radiator heat treatment is performed before and after the garbage drying process. However, either or before the heat treatment of the garbage 2 or after the heat treatment may be selected. A radiator heat treatment may be interposed during the waste drying treatment. That is, if the garbage drying process is interrupted or the radiator heating process is performed in parallel with the garbage drying process, the oil and fat generated during the heating process of the garbage 2 can be fluidized and discharged. Therefore, the inconvenience due to the functional degradation of 38 can be prevented, and the efficiency of the garbage drying process can be improved.
[0028]
Next, FIG. 4 shows a second embodiment of the garbage processing method and apparatus of the present invention.
[0029]
In this embodiment, a heater 32 is used as a heat source as a heating means of the radiator 38. That is, a cover 80 as heat storage means is attached to the bottom surface side of the processing tank 4 so as to surround the heater 32 and lead from the cover 80 to the narrow tube 46 side of the radiator 38 through the heat conducting pipe 82. The heat conducting pipe 82 is provided with an on-off valve 84 and a heat conducting fan 86. The heat conducting fan 86 is driven by a motor 88. A temperature sensor 90 that detects the outside air temperature is installed in the vicinity of the radiator 38.
[0030]
A control device 74 is provided in the same manner as in the above embodiment, and the detected temperature of the temperature sensor 90 or the like is input to the control device 74 as control information, and the control output generated by the control device 74 is the motors 52, 70, It is added to the on-off valve 84 and the motor 88.
[0031]
In the garbage processing method and apparatus of this embodiment, the on-off valve 84 is opened before the garbage 2 is heated, during or after the heating, or at a time selected from these, and the heat conduction fan 86 is rotated. Then, the hot air 92 is obtained by the heat storage in the cover 80, and the hot air 92 is sent to the radiator 38, thereby heating the radiator 38, dissolving and fluidizing the remaining fats and oils, and Can be discharged. Other operations are the same as in the first embodiment.
[0032]
Then, the outside air temperature on the radiator 38 side is detected by the temperature sensor 90, and when the outside air temperature is high, the rotation speed of the heat radiating fan 50 is controlled according to the detected temperature, for example, the rotational speed of the heat radiating fan 50 is increased. It may be. The circulation amount of the steam 36 may be controlled by the detected temperature. Further, when the outside air temperature is low, the radiator 38 may be heated by operating the heat conducting fan 86.
[0033]
In the first and second embodiments, the heater 56 or the heater 32 is used for the heat treatment of the radiator 38, but the heat of the steam 36 may be used. That is, when the heat radiating fan 50 that is the heat radiating means of the radiator 38 is stopped, the temperature of the radiator 38 is increased by the heat of the steam 36. Accordingly, the rotation of the radiating fan 50 is stopped until the incoming temperature of the radiator 38 detected by the temperature sensor 64 rises to a predetermined temperature, for example, 60 ° C., and the oil and fat components are dissolved and flowed by heating due to the temperature rise of the radiator 38. And can be discharged to the drain pipe 60. After this processing, the internal pressure in the processing tank 4 can be stabilized by rotating the heat radiating fan 50, condensing the steam 36, and flowing the condensed water 54.
[0034]
When the temperature difference ΔT between the inlet side temperature and the outlet side temperature of the radiator 38 reaches a predetermined temperature, the heat radiating fan 50 is stopped again for a predetermined time, and the radiator 38 is heated by the heat of the steam 36 to Minutes can be dissolved and fluidized and removed outside the radiator 38.
[0035]
Also, during the drying process of the garbage, the heater 32, another heating source installed together with the heater 32 or installed in place of the heater 32 is intermittently driven at a predetermined time interval to dissolve the fat and oil during the garbage treatment. It is possible to prevent accumulation of oil and fat. In this embodiment, the heater 56 is disposed in the vicinity as a heating source for the radiator 38. However, a heating source such as a heater may be installed in the radiator 38 to heat the radiator 38 from the inside.
[0036]
Further, when the rotation of the circulation fan 68 is increased while the heat radiating fan 50 is stopped or rotating, a large amount of the steam 36 can flow to the radiator 38, and the radiator 38 can be heated by the heat of the steam 36. . Therefore, if the circulation amount of the steam 36 with respect to the radiator 38 is controlled by increasing or decreasing the rotation of the circulation fan 68, the radiator 38 can be heated using the heat of the steam 36 as a heat source, and the oil and fat content in the radiator 38 is similarly reduced. It can be dissolved or fluidized and removed from the radiator 38.
[0037]
In the first embodiment, a temperature sensor 90 for detecting the outside air temperature is installed on the radiator 38 side so as to control the heat radiation amount of the radiator 38, the circulation amount of the steam 36, and the heat generation control of the heaters 32 and 56. Also good. Regarding the heat generation control of these heaters 32 and 56, for example, if the heat generation amount is controlled according to the outside air temperature, such as increasing the heat generation amount when the outside air temperature is low and decreasing the heat generation amount when the outside air temperature is high, Efficient heat generation control can be performed.
[0038]
Similarly, if a heater is installed on the upstream side of the heat radiating fan 50 as a heating means for the radiator 38, and when the radiator 38 is heated, the heater and the heat radiating fan 50 are operated to supply hot air to the radiator 38. The oil and fat inside can be dissolved and fluidized and discharged out of the radiator 38.
[0039]
【The invention's effect】
As described above, according to the present invention, the following effects can be obtained.
a Even if oils and fats such as lard contained in garbage are solidified in the cooling means, the oil and fats are dissolved and fluidized by heating the cooling means so that they can be easily removed from the cooling means. It is possible to prevent a decrease in the function and a decrease in the service life.
b Heating of the cooling means may be performed before, during or after the heat treatment of the garbage, or may be a plurality of these periods. Can be speeded up.
c If the heat generated by the heating means of the treatment tank is used in combination with the heating of the cooling means, it is not necessary to use a special heating means, and the function of the cooling means can be prevented from lowering.
d Heating of the cooling means can be promoted by stopping the heat dissipating fan of the cooling means to suppress the heat radiation amount.
e Heating of the cooling means can be promoted by rotating the heat dissipating fan of the cooling means to allow hot air to flow.
f If the cooling means is heated by controlling the circulation amount of the steam flowing through the cooling means, the oil and fat can be dissolved and fluidized and discharged from the cooling means without using a special heat source.
[Brief description of the drawings]
FIG. 1 is a diagram showing a first embodiment of a garbage disposal method and apparatus according to the present invention.
FIG. 2 is a block diagram showing the control device.
FIG. 3 is a flowchart showing garbage drying processing and radiator heating control.
FIG. 4 is a view showing a second embodiment of the garbage disposal method and apparatus according to the present invention.
[Explanation of symbols]
2 Garbage 4 Treatment tank 32 Heater (heating means)
36 Steam 38 Radiator (cooling means)
40 Circuit (circulation means)
50 Heat dissipation fan 54 Condensed water 56 Heater (heating means)

Claims (6)

処理槽内で加熱される生ごみから発生する蒸気を冷却手段に循環させて冷却して凝縮水と分離させた後、前記処理槽に戻す生ごみ処理方法であって、
前記冷却手段に隣接して配設された加熱手段を発熱させ、この加熱手段の発熱により、前記生ごみの加熱処理前、加熱処理中又は加熱処理後に前記冷却手段を油脂溶解温度以上に加熱することを特徴とする生ごみ処理方法。
It is a garbage disposal method that circulates steam generated from garbage heated in the treatment tank to the cooling means, cools it and separates it from condensed water, and returns it to the treatment tank,
The heating means disposed adjacent to the cooling means generates heat, and the heat generated by the heating means heats the cooling means to a temperature equal to or higher than the oil dissolution temperature before, during or after the heat treatment of the garbage. The garbage disposal method characterized by the above-mentioned.
生ごみを収容して加熱する処理槽と、
この処理槽に発生した蒸気を冷却する冷却手段と、
この冷却手段に前記処理槽で発生した前記蒸気を導き、前記冷却手段で凝縮させ、凝縮水と分離させた後、前記処理槽に戻す循環手段と、
前記冷却手段に併設され、前記生ごみの加熱処理前、加熱処理中又は加熱処理後に前記冷却手段を油脂溶解温度以上に加熱する加熱手段と、
を備えたことを特徴とする生ごみ処理装置。
A treatment tank for containing and heating garbage;
A cooling means for cooling the steam generated in the treatment tank;
A circulation means for guiding the steam generated in the treatment tank to the cooling means, condensing the cooling means by the cooling means, separating the condensed water, and returning the condensed water to the treatment tank;
A heating unit that is provided in the cooling unit, and heats the cooling unit to a temperature equal to or higher than an oil dissolution temperature before, during, or after the heat treatment of the garbage;
A garbage disposal apparatus characterized by comprising:
生ごみを収容する処理槽と、
この処理槽の前記生ごみを加熱する加熱手段と、
前記処理槽に発生した蒸気を冷却する冷却手段と、
を備え、前記生ごみの加熱処理前、加熱処理中又は加熱処理後に前記冷却手段を油脂溶解温度以上に加熱する熱源に前記加熱手段を用いたことを特徴とする生ごみ処理装置。
A treatment tank for storing garbage;
Heating means for heating the garbage in the treatment tank;
Cooling means for cooling the steam generated in the treatment tank;
And a waste treatment apparatus using the heating means as a heat source that heats the cooling means to a temperature higher than the fat dissolution temperature before, during or after the heat treatment of the garbage.
前記冷却手段に放熱ファンを備え、前記冷却手段の加熱時、前記放熱ファンを停止させることを特徴とする請求項2又は3記載の生ごみ処理装置。  4. The garbage processing apparatus according to claim 2, wherein the cooling means includes a heat radiating fan, and the heat radiating fan is stopped when the cooling means is heated. 前記冷却手段に放熱ファンを備え、前記冷却手段の加熱時、前記放熱ファンを回転させることにより、熱風を前記冷却手段に流すことを特徴とする請求項2又は3記載の生ごみ処理装置。  4. The garbage processing apparatus according to claim 2, wherein the cooling means includes a heat radiating fan, and hot air is caused to flow through the cooling means by rotating the heat radiating fan when the cooling means is heated. 処理槽内で加熱される生ごみから発生する蒸気を冷却手段に循環させて冷却して凝縮水と分離させた後、前記処理槽に戻す生ごみ処理方法であって、
前記冷却手段に対する前記蒸気の循環量を制御して前記冷却手段を加熱することを特徴とする生ごみ処理方法。
It is a garbage disposal method that circulates steam generated from garbage heated in the treatment tank to the cooling means, cools it and separates it from condensed water, and returns it to the treatment tank,
A garbage disposal method, wherein the cooling means is heated by controlling a circulation amount of the steam to the cooling means.
JP2001163631A 2001-05-31 2001-05-31 Garbage disposal method and apparatus Expired - Fee Related JP3767801B2 (en)

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