JP4057469B2 - Garbage processing machine - Google Patents

Garbage processing machine Download PDF

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Publication number
JP4057469B2
JP4057469B2 JP2003158800A JP2003158800A JP4057469B2 JP 4057469 B2 JP4057469 B2 JP 4057469B2 JP 2003158800 A JP2003158800 A JP 2003158800A JP 2003158800 A JP2003158800 A JP 2003158800A JP 4057469 B2 JP4057469 B2 JP 4057469B2
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air
garbage
heat exchanger
path
drying container
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JP2004358335A (en
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直樹 横尾
朋之 小武内
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Dainichi Co Ltd
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Dainichi Co Ltd
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Description

【0001】
【発明が属する技術分野】
本発明は、工場、飲食店、ホテル、一般家庭等から出る生ごみを加熱乾燥処理して減量化を計る生ごみ処理機に関するものである。
【0002】
【従来の技術】
生ごみを加熱乾燥処理する生ごみ処理機としては、電気ヒータで高温に加熱する方式や、ガスまたは灯油等の液体燃料をバーナで燃焼させ、その燃焼熱と熱交換して得られる高温空気を生ごみに吹き付けて乾燥させる等の方式があるが、本出願人は灯油等の液体燃料をバーナで燃焼させる方式の生ごみ処理機として、図8に示すようなものを発明した。
【0003】
図8を説明すると、乾燥容器50に投入された生ごみを加熱乾燥するための燃焼熱を生成するバーナ51の下流に、臭い空気燃焼室52、脱臭触媒53、直交熱交換器54、排気経路55を配置している。そして、この直交熱交換器54は一方の経路を脱臭触媒53および排気経路55と連通し、他の経路を乾燥容器50内の空気を循環させる循環ダクト56および高温空気ダクト57と連通させた構成としたものである。つまり、乾燥容器50、循環ダクト56、直交熱交換器54,高温空気ダクト57から成る内部空気循環経路58を形成している。また、59は臭い空気吸引手段で乾燥容器50内部からの臭い空気を臭い空気燃焼室52に導入するものである。
【0004】
この構成によれば、生ごみの加熱乾燥処理に伴い、臭い空気吸引手段59により乾燥容器50内部から吸引された臭い空気は臭い空気燃焼室52へ流入する。そして、臭い空気の臭気成分はバーナ51の燃焼火炎により臭い空気燃焼室52にて加熱分解され、加熱分解されなかった臭気成分も、バーナ51の燃焼熱にて活性化した脱臭触媒53により、酸化分解されてほとんど臭気成分が無い空気として排気経路55から外部に放出されることになる。
【0005】
また、乾燥容器50内の空気は循環ダクト56を通って直交熱交換器54へも流入する。バーナ51の燃焼熱により脱臭触媒53の下流に配置した直交熱交換器54も加熱されることから、循環ダクト56により直交熱交換器54に導入された乾燥容器50内の空気は、直交熱交換器54を通過する間に高温空気となり、高温空気ダクト57を介して再度乾燥容器50に入り生ごみを加熱乾燥する。このように乾燥容器50内では、内部空気循環経路58を介して高温空気が拡散するため効率よく生ごみを乾燥でき、さらに、生ごみの乾燥時に発生する臭気成分も臭い空気燃焼室52及び脱臭触媒53にて分解されるため、臭気の少ない生ごみ乾燥機を供給できることになる。
【0006】
【特許文献1】
特開2001−104910号公報
【0007】
【発明が解決しようとする課題】
しかしながら、従来の生ごみ処理機では、投入する生ごみの種類によっては乾燥が進むと生ごみの一部が粉塵となる場合がある。乾燥容器内の空気は循環ダクトを経由して直交熱交換器を通過し、高温空気となって高温空気ダクトから再び乾燥容器に導入されているため、上記の粉塵も循環する空気と一緒に直交熱交換器を通過することになる。さらに直交熱交換器はバーナの燃焼熱を循環する空気に効率よく熱交換するため空気との接触面積を多くしており、空気が通過する開口部は狭い構造となっている。したがって、粉塵は直交熱交換器の吸い込み側に時間経過とともに堆積することになる。すると、直交熱交換器を通過する空気量が減少して高温空気ダクトから乾燥容器に導入される温風温度は上昇し、生ごみの焦げ付きや発火に至る可能性がある。
【0008】
また、直交熱交換器を通過する空気の流れは、排気経路側に比べて脱臭触媒側では高温となっているため、粉塵が堆積し直交熱交換器を通過する空気量が少ない状態では、脱臭触媒側の温風温度が局部的に高温となるため、さらに生ごみの焦げ付きや発火に至る可能性が高くなるという問題があった。
【0009】
また、生ごみの乾燥処理を効率的に行うため内部空気循環経路によって循環される空気量を出来る限り大きくする必要があり、さらに、脱臭触媒の活性化を保持するように脱臭触媒の温度を高温に保つためには、臭い空気吸引手段によって吸引される空気量を最小限にとどめることが必要である。したがって、内部空気循環経路の内圧が排気経路の内圧に比べて大きくなる構造となっている。
【0010】
このように内部空気循環経路と排気経路の内圧に差が生じる構造では、例えば直交熱交換器に微細な穴があったり、生ごみ処理機に直交熱交換器を組み付ける際のパッキンなどのばらつきによりシール性が悪かった場合には、内部空気循環経路の空気が直交熱交換器を通過する際に、内圧の小さい排気経路に漏れ出ることがある。したがって、排気経路を通過する空気は脱臭触媒を通過して無臭化された空気であるが、この空気に脱臭処理されていない臭気成分を含む空気が混入することになり、混入した臭気成分により使用者や周辺環境に悪影響を及ぼすという問題があった。
【0011】
本発明は上記課題を解決するためのもので、乾燥容器に導入される温風温度を均一化できるため、生ごみの焦げ付きや発火を防止して乾燥状態を均一化できるとともに、生ごみ処理機内部から臭気成分が漏れ出ることを防止できる生ごみ処理機を提供することを目的とする。
【0012】
【課題を解決するための手段】
請求項1記載の発明は、生ごみを乾燥する乾燥容器と、燃料を燃焼させ燃焼熱を生成するバーナ部と、前記バーナ部の下流に設けた脱臭触媒と、前記乾燥容器内の空気を内部空気循環手段により循環させる内部空気循環経路と、一方の通路を前記脱臭触媒に連通し、他方の通路を前記内部空気循環経路に連通する直交熱交換器とを有し、前記バーナ部の燃焼熱にて前記脱臭触媒を加熱して前記乾燥容器からの臭い空気を脱臭処理するとともに、前記乾燥容器内の空気を前記内部空気循環経路を介して前記直交熱交換器で加熱昇温させながら循環させて生ごみを乾燥処理する生ごみ処理機において、前記直交熱交換器をバイパスして前記乾燥容器内の空気を循環させる内部空気循環バイパス経路を備えたことを特徴とする生ごみ処理機である。
【0013】
また、請求項2記載の発明は、生ごみを乾燥する乾燥容器と、前記乾燥容器から臭い空気を吸引する臭い空気吸引手段と、液体燃料を燃焼させ燃焼熱を生成するバーナと、前記バーナの下流に設け前記臭い吸引手段により前記乾燥容器から吸引した臭い空気を前記バーナの燃焼火炎にて加熱分解する臭い空気燃焼室と、前記臭い空気燃焼室の下流に設けた脱臭触媒と、前記脱臭触媒を通過した空気を外部に排出する排気経路と、前記乾燥容器に循環ファンを介して連通する循環ダクトと前記バーナの燃焼熱により加熱された空気を前記乾燥容器内に吹き込む温風吹出口ダクトを有する内部空気循環経路と、一方の通路を前記排気経路と前記脱臭触媒に連通し、他方の通路を前記内部空気循環経路に連通する直交熱交換器とを有し、前記乾燥容器内から前記臭い空気吸引手段により吸引された臭い空気を前記臭い空気燃焼室と前記脱臭触媒にて脱臭処理するとともに、前記乾燥容器内の空気を前記内部空気循環経路を介して前記直交熱交換器にて加熱昇温させながら循環させて生ごみを乾燥処理する生ごみ処理機において、前記循環ダクトと前記温風吹出口ダクトとの間に前記直交熱交換器をバイパスして前記乾燥容器内の空気を循環させる内部空気循環バイパス経路を備えたことを特徴とする生ごみ処理機である。
【0014】
すなわち、請求項1及び請求項2記載の発明では、循環ダクトから直交熱交換器を通過して温風吹出口ダクトに至る内部空気循環経路と、循環ダクトから直交熱交換器を通過しないで温風吹出口ダクトに至る内部空気循環バイパス経路の2つの経路構成としたので、直交熱交換器が粉塵等によって閉塞し直交熱交換器を通過する空気量が減少してこの空気の温度が上昇した場合には、内部空気循環バイパス経路を通過する空気量がその分多くなり温風吹出口ダクトで混合され乾燥容器に導入されることから温風温度を均一化できるため、生ごみの焦げ付きや発火を防止して生ごみの乾燥状態を均一化できる。
【0015】
請求項3記載の発明は、温風吹出口ダクトにおいて、内部空気循環バイパス経路から導入される空気量は、直交熱交換器の低温側より高温側に多く導入されることを特徴とする請求項2記載の生ごみ処理機である。
【0016】
すなわち、請求項3記載の発明では、温風吹出口ダクト内において直交熱交換器の高温側には内部空気循環バイパス経路からの空気量を多くして、低温側には空気量を少なくする構成としたので、乾燥容器に導入される温風温度を均一化できるため、生ごみの焦げ付きや発火を防止して生ごみの乾燥状態を均一化できる。
【0017】
請求項4記載の発明は、内部空気循環経路の内圧が排出経路の内圧より小さいことを特徴とする請求項2乃至請求項3記載の生ごみ処理機である。
【0018】
すなわち、請求項4記載の発明では、乾燥容器内の空気は直交熱交換器を通過する内部空気循環経路と直交熱交換器を通過しない内部空気循環バイパス経路を循環する構成としたことから、内部空気循環経路の内圧が排気経路の内圧より低くなるため、臭気成分を含む内部空気循環経路の空気が直交熱交換器を通過する際に排気経路側に漏れ出ること確実に防止できる。
【0019】
【発明の実施の形態】
以下、本発明の実施の一形態を図面に基づいて説明する。
【0020】
図1は生ごみ処理機の外観傾視図、図2は側面構成図、図3は正面構成図である。まず、図1より1は生ごみ処理機の本体、2は本体1に生ごみを投入するための開閉自在の扉である。また、3は生ごみ処理機の運転を制御するための操作部であり、この操作部3の下部には本体1内で乾燥処理された乾燥処理物を受けるための容器を格納する処理物容器収納部4を有している。
【0021】
次に、図2より、5は本体1内に収納され生ごみを乾燥処理する乾燥容器、6は生ごみを乾燥するために必要な燃焼熱を生成するバーナ部、7は乾燥容器5から排出される臭気成分をバーナ部6の燃焼火炎にて加熱分解する臭い空気燃焼室である。8はバーナ部6の燃焼熱により活性化し臭気成分を酸化分解する脱臭触媒であり、この脱臭触媒8の下流に直交熱交換器9を配設し、その下流に排気筒10を有する排気経路11を連通している。
【0022】
また、図3より、乾燥容器5底部付近には生ごみを撹拌する撹拌手段12が内設され、外部に撹拌手段12を駆動する撹拌駆動手段13を配設している。14は生ごみの乾燥処理物を排出するための排出口、15は排出口14からの乾燥処理物を収容する処理物容器である。16は排出口14を開閉するための排出口開閉手段であり、モーターにより排出口14の開閉を行うようにしている。
【0023】
さらに、乾燥容器5内の上部には、乾燥容器5から臭い空気を吸引し臭い空気燃焼室7へ送風する臭い空気吸引手段としての臭い空気吸引ファン17を外側に配設した臭い空気吸入口18を設け、この臭い空気吸入口18と臭い空気燃焼室7は臭い空気ダクト19を介して連通している。つまり、乾燥容器5からの臭い空気は臭い空気燃焼室7で加熱分解された後、脱臭触媒8を通過して完全に脱臭処理され、直交熱交換器9を通過して排気筒10を有する排気経路11から無臭の空気として外部に排出される構成としている。
【0024】
また、図3より循環空気吸入口20の外側には内部空気循環手段としての循環ファン21を配設し、この循環ファン21を介して循環空気吸入口20と循環ダクト22を連通し、この循環ダクト22は脱臭触媒8と直交熱交換器9の周囲に空気の通路となる空隙を形成するように設けられた箱体23と連通している。そして、24は乾燥容器5内に高温空気を導入するための温風吹出口ダクトである。また、25は箱体23に設けられた内部空気循環バイパス口である。
【0025】
つまり、図4、図5に示すように、循環ダクト22、直交熱交換器9、温風吹出口ダクト24から構成された内部空気循環経路26(実線矢印)と、直交熱交換器9を通過しないで内部空気循環バイパス口25を通過して温風吹出口ダクト24に至る内部空気循環バイパス経路27(破線矢印)の2つの循環経路を有し、循環ダクト22からの空気は、直交熱交換器9を通過してバーナ部6の燃焼熱により高温空気となった空気と、直交熱交換器9を通過しないで内部空気循環バイパス口25を通過した空気が、温風吹出口ダクト24で混合され乾燥容器5へ導入されるようになっている。
【0026】
また、図6に示すように、内部空気循環バイパス口25を通過した空気は、直交熱交換器9からの高温空気との混合の際、直交熱交換器9の低温側より高温側に多く流入されるように仕切板28により制御されている。尚、本実施例の仕切板28では高温側の切り欠きを大きくした形状としているが、要は高温側に空気が多く流入できれば良いのであり、本実施例の形状に限定されるものではない。
【0027】
バーナ部6は、図7に示すように、燃焼ファン29、バーナ30、バーナ30に燃料の気化ガスを噴出供給する気化器31からなっている。また、バーナ30の下流には二次空気噴出用の二次空気孔32を多数穿設した二次空気噴出板33が火口34の両側に対向立設し、さらに、臭い空気燃焼室7は臭い空気ダクト19と連通する周縁通路を外方に備えた二重構造をなし、その内外は対向壁面に多数穿設された臭い空気噴出孔35を介して連通している。
【0028】
次に上記構成における動作を説明する。本体1の扉2を開けて乾燥容器5に生ごみを投入し操作部3にて運転操作を行うと、気化器31を予熱する等の燃焼準備に入る。予熱が完了すると、図示しない送油ポンプが始動して気化器31に灯油が流入し、加熱気化した気化ガスがバーナ30に噴出する。その一方で燃焼ファン29も低回転始動し一次空気がバーナ30に流入する。
【0029】
よって、気化ガスと一次空気の予混合気が火口34より噴出し、図示しない着火装置により着火し燃焼開始となる。さらに燃焼火炎に二次空気噴出板33から二次空気が強制的に供給されて完全燃焼する。そして、この燃焼排ガスの燃焼熱は、臭い空気燃焼室7、脱臭触媒8、直交熱交換器9を加熱した後、排気筒10より外部に排気される。
【0030】
また、燃焼開始と相前後して撹拌駆動手段13により撹拌手段12が回転し、生ごみを粉砕・撹拌して表面積を大きくすることで乾燥効率を高める。さらに撹拌・粉砕時において、撹拌駆動手段13は正逆回転することで、乾燥容器5内で生ごみが片寄らないようにしている。
【0031】
さらに、燃焼開始とほぼ同時に循環ファン21が始動すると、乾燥容器5内の空気は循環空気吸入口20より循環ダクト22に流入して箱体23に送られ、図4、図5の矢印に示すように箱体23内の空隙を通り直交熱交換器9にほとんどの空気が流入する一方で、内部空気循環バイパス口25からも温風吹出口ダクト24へ流入する。ここで、直交熱交換器9を通過する空気はバーナ部6の燃焼熱と熱交換するが、脱臭触媒8側では高温の温風となり、排気筒10側は脱臭触媒8側より低温の温風となるため、直交熱交換器9を通過した空気の温風温度は不均一となってしまう。
【0032】
しかし、内部空気循環バイパス口25から流入した空気は、直交熱交換器9を通過しないため温風温度は不均一とならず、さらに温風吹出口ダクト24の仕切板28により直交熱交換器9の高温側からの高温空気と多く混合されるため温風吹出口ダクト24から乾燥容器5へ流入する温風温度を均一化することができ、生ごみの焦げ付きをなくして粉砕・撹拌されて表面積の拡大した生ごみを効率よく乾燥することができるため乾燥状態を均一化できる。
【0033】
また、投入する生ごみの種類によっては乾燥が進むと生ごみの一部が粉塵となり、この粉塵が直交熱交換器9の吸い込み側に時間経過とともに堆積した場合には、直交熱交換器9を通過する空気量が減少して温風吹出口ダクト24から乾燥容器5に導入される温風温度は上昇し、生ごみの焦げや発火に至る可能性があった。
【0034】
しかし、循環ダクト22から直交熱交換器9を通過しないで内部空気循環バイパス口25から温風吹出口ダクト24に至る内部空気循環バイパス経路27を設けているので、直交熱交換器9を通過する空気量が減少しても、内部空気循環バイパス経路27を通過する空気量がその分多くなり、温風吹出口ダクト24にて直交熱交換器9からの高温空気と混合されるため、温風吹出口ダクト24から乾燥容器5に導入される空気の温度上昇を防止でき、生ごみの焦げ付きをなくして乾燥状態を均一化できるのである。尚、直交熱交換器9に一定以上の粉塵が堆積しないように、直交熱交換器9を通過する温風温度を検知して温風温度が所定温度以上になった場合には生ごみ処理機の運転を停止するようにしている。
【0035】
さらに、乾燥容器5に連通する内部空気循環経路26と内部空気循環バイパス経路27を介して循環している空気は、乾燥容器5内で生ごみから発生した臭気成分を多く含む臭い空気であるが、排気経路11を通過する空気は臭い空気燃焼室7と脱臭触媒8により完全に脱臭処理されるため無臭の空気である。この臭い空気と無臭の空気が直交熱交換器9の各経路を通過する際、排気経路11の内圧が内部空気循環経路26の内圧より小さければ、例えば直交熱交換器9に微細な穴があったり、直交熱交換器9のシール性が悪かった場合には、内部空気循環経路26の臭い空気が内圧の小さい排気経路11に漏れ出ることになる。
【0036】
しかし、内部空気循環経路26に内部空気循環バイパス経路27を設けているため、内部空気循環経路26の内圧が排気経路11の内圧より小さくなるため、直交熱交換器9に微細な穴があったりシール性が悪かった場合でも、排気経路11へ臭い空気が漏れ出ることはなく、排気経路11から内部空気循環経路26へ無臭の空気が漏れることになるだけである。したがって、排気経路11を介して生ごみ処理機の本体1外部に臭気成分が漏れ出ることはなく、臭気成分により使用者や周辺環境に悪影響を及ぼすということを防止できるのである。
【0037】
一方、乾燥容器5内部の臭い空気は、臭い空気吸引ファン17により臭い空気吸入口18から臭い空気ダクト19を通って臭い空気燃焼室7に噴出されるため、臭い空気の臭気成分は、バーナ部6の燃焼火炎によって加熱分解され、さらに、臭い空気燃焼室7で加熱分解されずに残った臭気成分は、臭い空気燃焼室7下流の脱臭触媒8に流入し完全に酸化分解されることになる。
【0038】
上記の如く生ごみの乾燥が進み、乾燥容器5内部の水分が残り少なくなると、徐々に乾燥容器5上部より徐々に温度が上昇してくる。そして、乾燥容器5内に設けられた温度センサが所定温度を検出すると生ごみの乾燥完了と判断し、バーナ30の燃焼火力を下げ、所定時間運転した後バーナ30を消火する。この後、循環ファン21、臭い空気吸引ファン17及び撹拌手段12を所定時間運転させ乾燥容器5及び乾燥処理物を冷却し生ごみの乾燥処理を完了する。
【0039】
乾燥処理が完了すると、排出口開閉手段16のモーターが作動して乾燥容器5に設けられた排出口14が開き、撹拌手段12を撹拌駆動手段13で一定方向に回転させ、生ごみの乾燥処理物は排出口14から処理物容器15に排出されることになる。
【0040】
【発明の効果】
以上に説明したように本発明の請求項1及び請求項2記載の発明によれば、循環ダクトから直交熱交換器を通過して温風吹出口ダクトに至る内部空気循環経路と、循環ダクトから直交熱交換器を通過しないで温風吹出口ダクトに至る内部空気循環バイパス経路の2つの経路構成としたので、直交熱交換器が粉塵によって閉塞し直交熱交換器を通過する空気量が減少してこの空気の温度が上昇した場合には、内部空気循環バイパス経路を通過する空気量がその分多くなり温風吹出口ダクトで混合され乾燥容器に導入されることから温風温度を均一化できるため、生ごみの焦げ付きや発火を防止して生ごみの乾燥状態を均一化できる。
【0041】
また、本発明の請求項3記載の発明によれば、温風吹出口ダクト内において、直交熱交換器の高温側には内部空気循環バイパス経路からの空気量を多くして、低温側には空気量を少なくする構成としたので、乾燥容器に導入される温風温度を均一化できるため、生ごみの焦げ付きや発火を防止して生ごみの乾燥状態を均一化できる。
【0042】
また、本発明の請求項4記載の発明によれば、乾燥容器内の空気は直交熱交換器を通過する内部空気循環経路と直交熱交換器を通過しない内部空気循環バイパス経路を循環する構成としたことから、内部空気循環経路の内圧が排気経路の内圧より低くなるため、臭気成分を含む内部空気循環経路の空気が直交熱交換器を通過する際に排気経路側に漏れ出ることを確実に防止できるため、臭気成分により使用者や周辺環境に悪影響を及ぼすということを防止できる。
【図面の簡単な説明】
【図1】本発明の実施例を示す生ごみ処理機の外観傾視図である。
【図2】本発明の実施例を示す生ごみ処理機の側面構成図である。
【図3】本発明の実施例を示す生ごみ処理機の正面構成図である。
【図4】本発明の実施例の直交熱交換器、箱体の拡大傾斜図である。
【図5】本発明の実施例の直交熱交換器、箱体、温風吹出口ダクトの側面構成図である。
【図6】本発明の実施例の温風吹出口ダクトの傾視図である。
【図7】本発明の実施例のバーナ部、臭い空気燃焼室の構成図である。
【図8】従来の実施例を示す生ごみ処理機の側面の構成図である。
【符号の説明】
5 乾燥容器
6 バーナ部
7 臭い空気燃焼室
8 脱臭触媒
9 直交熱交換器
11 排気経路
17 臭い空気吸引ファン(臭い空気吸引手段)
21 循環ファン(内部空気循環手段)
22 循環ダクト
24 温風吹出口ダクト
26 内部空気循環経路
27 内部空気循環バイパス経路
30 バーナ
[0001]
[Technical field to which the invention belongs]
The present invention relates to a garbage processing machine that measures the weight reduction by heating and drying the garbage from a factory, a restaurant, a hotel, a general household, and the like.
[0002]
[Prior art]
As a garbage processing machine that heats and drys garbage, a method of heating to high temperature with an electric heater or high temperature air obtained by burning liquid fuel such as gas or kerosene with a burner and exchanging heat with the combustion heat is used. Although there is a method of spraying and drying garbage, the present inventor has invented a garbage processing machine of the type shown in FIG. 8 that burns liquid fuel such as kerosene with a burner.
[0003]
Referring to FIG. 8, an odor air combustion chamber 52, a deodorizing catalyst 53, an orthogonal heat exchanger 54, an exhaust path are provided downstream of a burner 51 that generates combustion heat for heating and drying raw garbage put into the drying container 50. 55 is arranged. The orthogonal heat exchanger 54 is configured such that one path communicates with the deodorizing catalyst 53 and the exhaust path 55 and the other path communicates with a circulation duct 56 and a high-temperature air duct 57 that circulate the air in the drying container 50. It is what. That is, an internal air circulation path 58 including the drying container 50, the circulation duct 56, the orthogonal heat exchanger 54, and the high temperature air duct 57 is formed. Reference numeral 59 denotes odor air suction means for introducing odor air from the inside of the drying container 50 into the odor air combustion chamber 52.
[0004]
According to this configuration, the odorous air sucked from the inside of the drying container 50 by the odorous air suction means 59 flows into the odorous air combustion chamber 52 along with the heat drying process of the garbage. The odor component of the odor air is thermally decomposed in the odor air combustion chamber 52 by the combustion flame of the burner 51, and the odor component that is not thermally decomposed is also oxidized by the deodorization catalyst 53 activated by the combustion heat of the burner 51. As a result of being decomposed and having almost no odor component, the air is discharged to the outside from the exhaust passage 55.
[0005]
The air in the drying container 50 also flows into the orthogonal heat exchanger 54 through the circulation duct 56. Since the orthogonal heat exchanger 54 disposed downstream of the deodorizing catalyst 53 is also heated by the combustion heat of the burner 51, the air in the drying vessel 50 introduced into the orthogonal heat exchanger 54 by the circulation duct 56 is orthogonally heat exchanged. While passing through the vessel 54, it becomes hot air, enters the drying container 50 again via the high-temperature air duct 57, and heats and drys the garbage. As described above, in the drying container 50, the high temperature air diffuses through the internal air circulation path 58, so that the garbage can be efficiently dried. Further, the odor component generated when the garbage is dried also has the odor air combustion chamber 52 and the deodorization. Since it is decomposed by the catalyst 53, a garbage dryer with less odor can be supplied.
[0006]
[Patent Document 1]
Japanese Patent Laid-Open No. 2001-104910
[Problems to be solved by the invention]
However, in a conventional garbage processing machine, depending on the type of garbage to be input, part of the garbage may become dust when drying progresses. The air inside the drying container passes through the orthogonal heat exchanger via the circulation duct and becomes high-temperature air and is again introduced into the drying container from the high-temperature air duct. Therefore, the dust is also orthogonal to the circulating air. It will pass through the heat exchanger. Furthermore, the orthogonal heat exchanger increases the contact area with the air in order to efficiently exchange heat with the air that circulates the combustion heat of the burner, and the opening through which the air passes has a narrow structure. Therefore, dust accumulates over time on the suction side of the orthogonal heat exchanger. Then, the amount of air passing through the orthogonal heat exchanger decreases, and the temperature of the hot air introduced into the drying container from the high-temperature air duct rises, which may lead to burnt garbage or ignition.
[0008]
In addition, since the flow of air passing through the orthogonal heat exchanger is higher on the deodorization catalyst side than on the exhaust path side, the deodorization is performed when dust is accumulated and the amount of air passing through the orthogonal heat exchanger is small. Since the hot air temperature on the catalyst side is locally high, there is a further problem that the possibility of scorching or igniting garbage becomes high.
[0009]
In addition, in order to efficiently dry garbage, it is necessary to increase the amount of air circulated through the internal air circulation path as much as possible, and the temperature of the deodorization catalyst is increased so as to maintain the activation of the deodorization catalyst. Therefore, it is necessary to minimize the amount of air sucked by the odorous air sucking means. Therefore, the internal pressure of the internal air circulation path is larger than the internal pressure of the exhaust path.
[0010]
In such a structure in which the internal pressure of the internal air circulation path and the exhaust path is different, for example, there are fine holes in the orthogonal heat exchanger, or due to variations in packing etc. when assembling the orthogonal heat exchanger in the garbage treatment machine When the sealing performance is poor, the air in the internal air circulation path may leak into the exhaust path with a small internal pressure when passing through the orthogonal heat exchanger. Therefore, the air that passes through the exhaust path is air that has not been brominated by passing through the deodorizing catalyst, but this air contains air that contains odor components that have not been deodorized, and is used by the mixed odor components. There was a problem of adversely affecting the people and the surrounding environment.
[0011]
The present invention is for solving the above-mentioned problems, and since the temperature of the hot air introduced into the drying container can be made uniform, it is possible to make the dry state uniform by preventing the burning and burning of the garbage, and the garbage processing machine. An object of the present invention is to provide a garbage disposal machine capable of preventing leakage of odor components from the inside.
[0012]
[Means for Solving the Problems]
The invention according to claim 1 includes a drying container for drying garbage, a burner section for burning fuel to generate combustion heat, a deodorization catalyst provided downstream of the burner section, and air in the drying container. An internal air circulation path that is circulated by an air circulation means; an orthogonal heat exchanger that communicates one passage with the deodorization catalyst and communicates the other passage with the internal air circulation path; and combustion heat of the burner section The deodorizing catalyst is heated to deodorize the odorous air from the drying container, and the air in the drying container is circulated while being heated and heated by the orthogonal heat exchanger via the internal air circulation path. In the garbage processing machine for drying the garbage, an internal air circulation bypass path for circulating the air in the drying container by bypassing the orthogonal heat exchanger is provided. .
[0013]
Further, the invention according to claim 2 is a drying container for drying garbage, odor air suction means for sucking odor air from the drying container, a burner for combusting liquid fuel to generate combustion heat, An odor air combustion chamber that is provided downstream and thermally decomposes the odor air sucked from the drying container by the odor suction means with a combustion flame of the burner, a deodorization catalyst provided downstream of the odor air combustion chamber, and the deodorization catalyst An exhaust path for discharging the air passing through the outside, a circulation duct communicating with the drying container via a circulation fan, and a hot air outlet duct for blowing air heated by the combustion heat of the burner into the drying container. An internal air circulation path, an orthogonal heat exchanger that communicates one passage with the exhaust passage and the deodorization catalyst, and communicates the other passage with the internal air circulation path, and The odor air sucked from the inside by the odor air suction means is deodorized by the odor air combustion chamber and the deodorization catalyst, and the air in the drying container is passed through the internal air circulation path to the orthogonal heat exchanger. In the garbage processing machine that circulates while raising the temperature by heating in the garbage processing machine, the orthogonal heat exchanger is bypassed between the circulation duct and the hot air outlet duct to air in the drying container It is a garbage processing machine provided with the internal air circulation bypass path which circulates.
[0014]
That is, according to the first and second aspects of the invention, the internal air circulation path from the circulation duct through the orthogonal heat exchanger to the hot air outlet duct, and the hot air blowing from the circulation duct without passing through the orthogonal heat exchanger. Since the internal air circulation bypass path leading to the outlet duct has two paths, the orthogonal heat exchanger is blocked by dust and the amount of air passing through the orthogonal heat exchanger decreases and the temperature of this air rises. Since the amount of air passing through the internal air circulation bypass path is increased by that amount and mixed in the hot air outlet duct and introduced into the drying container, the temperature of the hot air can be made uniform, thus preventing burning of the garbage and ignition. This makes it possible to make the garbage dry.
[0015]
The invention described in claim 3 is characterized in that, in the hot air outlet duct, the amount of air introduced from the internal air circulation bypass path is introduced more on the high temperature side than on the low temperature side of the orthogonal heat exchanger. It is a garbage disposal machine described.
[0016]
That is, in the invention described in claim 3, in the hot air outlet duct, the amount of air from the internal air circulation bypass path is increased on the high temperature side of the orthogonal heat exchanger, and the amount of air is decreased on the low temperature side. Therefore, since the temperature of the hot air introduced into the drying container can be made uniform, it is possible to prevent the kitchen garbage from being burnt and ignited, and to make the kitchen garbage dry.
[0017]
According to a fourth aspect of the present invention, there is provided the garbage processing machine according to any one of the second to third aspects, wherein the internal pressure of the internal air circulation path is smaller than the internal pressure of the discharge path.
[0018]
That is, in the invention according to claim 4, since the air in the drying container circulates through the internal air circulation path that passes through the orthogonal heat exchanger and the internal air circulation bypass path that does not pass through the orthogonal heat exchanger, Since the internal pressure of the air circulation path is lower than the internal pressure of the exhaust path, it is possible to reliably prevent the air in the internal air circulation path containing odor components from leaking to the exhaust path side when passing through the orthogonal heat exchanger.
[0019]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of the present invention will be described with reference to the drawings.
[0020]
1 is an external perspective view of a garbage disposal machine, FIG. 2 is a side configuration diagram, and FIG. 3 is a front configuration diagram. First, as shown in FIG. 1, reference numeral 1 denotes a main body of the garbage processing machine, and 2 denotes an openable / closable door for putting the garbage into the main body 1. Reference numeral 3 denotes an operation unit for controlling the operation of the garbage processing machine, and a processed product container for storing a container for receiving a dried processed product in the main body 1 below the operation unit 3. A storage unit 4 is provided.
[0021]
Next, from FIG. 2, 5 is a drying container stored in the main body 1 for drying the garbage, 6 is a burner section for generating combustion heat necessary for drying the garbage, and 7 is discharged from the drying container 5. This is an odor air combustion chamber in which the odor component to be heated is decomposed by the combustion flame of the burner section 6. Reference numeral 8 denotes a deodorization catalyst that is activated by the combustion heat of the burner unit 6 to oxidatively decompose odor components. An orthogonal heat exchanger 9 is disposed downstream of the deodorization catalyst 8, and an exhaust path 11 having an exhaust cylinder 10 downstream thereof. Is communicated.
[0022]
Further, as shown in FIG. 3, a stirring means 12 for stirring the garbage is provided in the vicinity of the bottom of the drying container 5, and a stirring driving means 13 for driving the stirring means 12 is provided outside. Reference numeral 14 denotes a discharge port for discharging the garbage processed waste, and reference numeral 15 denotes a processed product container for storing the dried processed product from the discharge port 14. Reference numeral 16 denotes a discharge port opening / closing means for opening and closing the discharge port 14, and the discharge port 14 is opened and closed by a motor.
[0023]
Further, in the upper part of the drying container 5, an odor air suction port 18, which is provided with an odor air suction fan 17 as an odor air suction means for sucking odor air from the drying container 5 and sending it to the odor air combustion chamber 7. The odorous air inlet 18 and the odorous air combustion chamber 7 communicate with each other via an odorous air duct 19. That is, the odorous air from the drying container 5 is thermally decomposed in the odorous air combustion chamber 7 and then completely deodorized through the deodorizing catalyst 8, passes through the orthogonal heat exchanger 9, and has the exhaust cylinder 10. It is set as the structure discharged | emitted outside from the path | route 11 as odorless air.
[0024]
Further, as shown in FIG. 3, a circulation fan 21 as an internal air circulation means is disposed outside the circulation air suction port 20, and the circulation air suction port 20 and the circulation duct 22 are communicated with each other via the circulation fan 21. The duct 22 communicates with a box body 23 provided so as to form a gap serving as an air passage around the deodorizing catalyst 8 and the orthogonal heat exchanger 9. Reference numeral 24 denotes a hot air outlet duct for introducing hot air into the drying container 5. Reference numeral 25 denotes an internal air circulation bypass port provided in the box body 23.
[0025]
That is, as shown in FIGS. 4 and 5, the internal air circulation path 26 (solid arrow) configured by the circulation duct 22, the orthogonal heat exchanger 9, and the hot air outlet duct 24 does not pass through the orthogonal heat exchanger 9. The internal air circulation bypass passage 25 passes through the internal air circulation bypass port 25 to reach the hot air outlet duct 24, and the internal air circulation bypass route 27 (broken arrow) has two circulation paths. The air from the circulation duct 22 passes through the orthogonal heat exchanger 9 The air that has passed through the air and becomes high-temperature air due to the combustion heat of the burner unit 6 and the air that has passed through the internal air circulation bypass port 25 without passing through the orthogonal heat exchanger 9 are mixed in the hot air outlet duct 24 and dried. 5 is introduced.
[0026]
Further, as shown in FIG. 6, the air that has passed through the internal air circulation bypass port 25 flows more into the high temperature side than the low temperature side of the orthogonal heat exchanger 9 when mixing with the high temperature air from the orthogonal heat exchanger 9. In this way, it is controlled by the partition plate 28. Although the partition plate 28 of the present embodiment has a shape in which the notch on the high temperature side is increased, the point is that a large amount of air can flow into the high temperature side, and is not limited to the shape of the present embodiment.
[0027]
As shown in FIG. 7, the burner unit 6 includes a combustion fan 29, a burner 30, and a carburetor 31 that ejects fuel vaporized gas to the burner 30. Further, downstream of the burner 30, a secondary air ejection plate 33 in which a large number of secondary air holes 32 for ejecting secondary air are provided so as to be opposed to both sides of the crater 34, and the odorous air combustion chamber 7 is odorous. A double structure having an outer peripheral passage communicating with the air duct 19 is formed on the outside, and the inside and outside communicate with each other via a scented air injection hole 35 formed in a large number on the opposing wall surface.
[0028]
Next, the operation in the above configuration will be described. When the door 2 of the main body 1 is opened and the garbage is put into the drying container 5 and the operation unit 3 is operated, the combustion preparation such as preheating the vaporizer 31 is started. When preheating is completed, an oil supply pump (not shown) is started, kerosene flows into the vaporizer 31, and the vaporized gas that has been heated and vaporized is ejected to the burner 30. On the other hand, the combustion fan 29 also starts to rotate at a low speed, and the primary air flows into the burner 30.
[0029]
Therefore, the premixed gas of vaporized gas and primary air is ejected from the crater 34, ignited by an ignition device (not shown), and combustion starts. Further, secondary air is forcibly supplied from the secondary air ejection plate 33 to the combustion flame, and complete combustion is performed. And the combustion heat of this combustion exhaust gas heats the odor air combustion chamber 7, the deodorization catalyst 8, and the orthogonal heat exchanger 9, and then is exhausted to the outside from the exhaust cylinder 10.
[0030]
Also, the stirring means 12 is rotated by the stirring driving means 13 before and after the start of combustion, and the garbage is crushed and stirred to increase the surface area, thereby increasing the drying efficiency. Further, at the time of agitation / pulverization, the agitation drive means 13 rotates in the forward and reverse directions so that the garbage is not displaced in the drying container 5.
[0031]
Further, when the circulation fan 21 is started almost simultaneously with the start of combustion, the air in the drying container 5 flows into the circulation duct 22 from the circulation air suction port 20 and is sent to the box body 23, as indicated by the arrows in FIGS. As described above, most of the air flows into the orthogonal heat exchanger 9 through the gap in the box body 23, and also flows into the warm air outlet duct 24 from the internal air circulation bypass port 25. Here, the air passing through the orthogonal heat exchanger 9 exchanges heat with the combustion heat of the burner section 6, but becomes hot air having a high temperature on the deodorizing catalyst 8 side, and hot air having a lower temperature on the exhaust tube 10 side than the deodorizing catalyst 8 side. Therefore, the warm air temperature of the air that has passed through the orthogonal heat exchanger 9 becomes non-uniform.
[0032]
However, since the air flowing in from the internal air circulation bypass port 25 does not pass through the orthogonal heat exchanger 9, the hot air temperature does not become non-uniform, and further, the partition plate 28 of the hot air outlet duct 24 causes the orthogonal heat exchanger 9 to Because it is mixed with a lot of high-temperature air from the high-temperature side, the temperature of the hot air flowing into the drying container 5 from the hot-air outlet duct 24 can be made uniform, and the surface area can be increased by eliminating the burning of the garbage and crushing and stirring. The dried garbage can be efficiently dried, so that the dried state can be made uniform.
[0033]
Depending on the type of garbage to be thrown in, when drying progresses, part of the garbage becomes dust, and when this dust accumulates on the suction side of the orthogonal heat exchanger 9 over time, the orthogonal heat exchanger 9 is The amount of air passing therethrough has decreased, and the temperature of the hot air introduced from the hot air outlet duct 24 into the drying container 5 has risen, which may lead to burning of the garbage and ignition.
[0034]
However, since the internal air circulation bypass path 27 from the internal air circulation bypass port 25 to the hot air outlet duct 24 is provided without passing through the orthogonal heat exchanger 9 from the circulation duct 22, air passing through the orthogonal heat exchanger 9 is provided. Even if the amount decreases, the amount of air passing through the internal air circulation bypass path 27 increases correspondingly and is mixed with the hot air from the orthogonal heat exchanger 9 in the hot air outlet duct 24, so the hot air outlet duct The temperature rise of the air introduced into the drying container 5 from 24 can be prevented, and the dry state can be made uniform without burning of the garbage. It should be noted that when the hot air temperature passing through the orthogonal heat exchanger 9 is detected and the hot air temperature exceeds a predetermined temperature so that dust of a certain level or more does not accumulate on the orthogonal heat exchanger 9, a garbage disposal machine The operation is stopped.
[0035]
Further, the air circulated through the internal air circulation path 26 and the internal air circulation bypass path 27 communicating with the drying container 5 is odorous air containing a lot of odor components generated from garbage in the drying container 5. The air passing through the exhaust path 11 is odorless air because it is completely deodorized by the odorous air combustion chamber 7 and the deodorizing catalyst 8. When the odorous air and odorless air pass through each path of the orthogonal heat exchanger 9, if the internal pressure of the exhaust path 11 is smaller than the internal pressure of the internal air circulation path 26, for example, the orthogonal heat exchanger 9 has fine holes. If the sealing performance of the orthogonal heat exchanger 9 is poor, the odorous air in the internal air circulation path 26 leaks into the exhaust path 11 having a low internal pressure.
[0036]
However, since the internal air circulation bypass path 27 is provided in the internal air circulation path 26, the internal pressure of the internal air circulation path 26 is smaller than the internal pressure of the exhaust path 11, so there are fine holes in the orthogonal heat exchanger 9. Even if the sealing performance is poor, odorous air does not leak into the exhaust path 11, and only odorless air leaks from the exhaust path 11 to the internal air circulation path 26. Therefore, the odor component does not leak to the outside of the main body 1 of the garbage disposal machine through the exhaust path 11, and it is possible to prevent the odor component from adversely affecting the user and the surrounding environment.
[0037]
On the other hand, since the odorous air inside the drying container 5 is ejected from the odorous air intake port 18 through the odorous air duct 19 to the odorous air combustion chamber 7 by the odorous air suction fan 17, 6, and the odor component remaining without being thermally decomposed in the odor air combustion chamber 7 flows into the deodorization catalyst 8 downstream of the odor air combustion chamber 7 and is completely oxidized and decomposed. .
[0038]
As the garbage is dried as described above and the moisture in the drying container 5 is reduced, the temperature gradually rises from the upper part of the drying container 5. And if the temperature sensor provided in the drying container 5 detects predetermined temperature, it will judge that drying of garbage has been completed, the combustion thermal power of the burner 30 will be lowered | hung, and after operating for a predetermined time, the burner 30 will be extinguished. Thereafter, the circulation fan 21, the odorous air suction fan 17 and the stirring means 12 are operated for a predetermined time to cool the drying container 5 and the dried product and complete the drying process of the garbage.
[0039]
When the drying process is completed, the motor of the discharge port opening / closing means 16 is actuated to open the discharge port 14 provided in the drying container 5, and the stirring means 12 is rotated in a fixed direction by the stirring drive means 13 to dry the garbage. The material is discharged from the discharge port 14 to the processed material container 15.
[0040]
【The invention's effect】
As described above, according to the first and second aspects of the present invention, the internal air circulation path from the circulation duct through the orthogonal heat exchanger to the hot air outlet duct, and the orthogonal from the circulation duct Since the internal air circulation bypass path that leads to the hot air outlet duct without passing through the heat exchanger is used, the orthogonal heat exchanger is blocked by dust and the amount of air passing through the orthogonal heat exchanger is reduced. When the temperature of the air rises, the amount of air passing through the internal air circulation bypass path is increased by that amount and mixed in the hot air outlet duct and introduced into the drying container. The dry state of garbage can be made uniform by preventing garbage from burning and igniting.
[0041]
According to the third aspect of the present invention, in the hot air outlet duct, the amount of air from the internal air circulation bypass path is increased on the high temperature side of the orthogonal heat exchanger, and the air is Since the amount is reduced, the temperature of the hot air introduced into the drying container can be made uniform, so that the garbage can be kept in a dry state by preventing scorching and ignition of the garbage.
[0042]
According to the invention described in claim 4 of the present invention, the air in the drying container circulates through an internal air circulation path that passes through the orthogonal heat exchanger and an internal air circulation bypass path that does not pass through the orthogonal heat exchanger; As a result, the internal pressure of the internal air circulation path is lower than the internal pressure of the exhaust path, so that it is ensured that the air in the internal air circulation path containing odor components leaks to the exhaust path side when passing through the orthogonal heat exchanger. Therefore, it is possible to prevent the odor component from adversely affecting the user and the surrounding environment.
[Brief description of the drawings]
FIG. 1 is an external perspective view of a garbage disposal machine according to an embodiment of the present invention.
FIG. 2 is a side view of a garbage disposal apparatus showing an embodiment of the present invention.
FIG. 3 is a front configuration diagram of a garbage disposal machine showing an embodiment of the present invention.
FIG. 4 is an enlarged inclined view of the orthogonal heat exchanger and the box of the embodiment of the present invention.
FIG. 5 is a side configuration diagram of an orthogonal heat exchanger, a box, and a hot air outlet duct according to an embodiment of the present invention.
FIG. 6 is a perspective view of a hot air outlet duct according to an embodiment of the present invention.
FIG. 7 is a configuration diagram of a burner unit and an odorous air combustion chamber according to an embodiment of the present invention.
FIG. 8 is a side view of a garbage disposal apparatus showing a conventional embodiment.
[Explanation of symbols]
5 Drying container 6 Burner section 7 Odor air combustion chamber 8 Deodorization catalyst 9 Orthogonal heat exchanger 11 Exhaust path 17 Odor air suction fan (odor air suction means)
21 Circulation fan (internal air circulation means)
22 Circulating duct 24 Hot air outlet duct 26 Internal air circulation path 27 Internal air circulation bypass path 30 Burner

Claims (4)

生ごみを乾燥する乾燥容器と、燃料を燃焼させ燃焼熱を生成するバーナ部と、前記バーナ部の下流に設けた脱臭触媒と、前記乾燥容器内の空気を内部空気循環手段により循環させる内部空気循環経路と、一方の通路を前記脱臭触媒に連通し、他方の通路を前記内部空気循環経路に連通する直交熱交換器とを有し、前記バーナ部の燃焼熱にて前記脱臭触媒を加熱して前記乾燥容器からの臭い空気を脱臭処理するとともに、前記乾燥容器内の空気を前記内部空気循環経路を介して前記直交熱交換器で加熱昇温させながら循環させて生ごみを乾燥処理する生ごみ処理機において、前記直交熱交換器をバイパスして前記乾燥容器内の空気を循環させる内部空気循環バイパス経路を備えたことを特徴とする生ごみ処理機。A drying container for drying garbage, a burner section for burning fuel to generate combustion heat, a deodorizing catalyst provided downstream of the burner section, and an internal air for circulating air in the drying container by an internal air circulation means A circulation path and an orthogonal heat exchanger that communicates one passage to the deodorization catalyst and communicates the other passage to the internal air circulation path, and heats the deodorization catalyst with combustion heat of the burner section. The odor air from the drying container is deodorized, and the garbage in the drying container is circulated while being heated and heated by the orthogonal heat exchanger through the internal air circulation path. A garbage disposal apparatus, comprising an internal air circulation bypass path for bypassing the orthogonal heat exchanger and circulating the air in the drying container. 生ごみを乾燥する乾燥容器と、前記乾燥容器から臭い空気を吸引する臭い空気吸引手段と、液体燃料を燃焼させ燃焼熱を生成するバーナと、前記バーナの下流に設け前記臭い吸引手段により前記乾燥容器から吸引した臭い空気を前記バーナの燃焼火炎にて加熱分解する臭い空気燃焼室と、前記臭い空気燃焼室の下流に設けた脱臭触媒と、前記脱臭触媒を通過した空気を外部に排出する排気経路と、前記乾燥容器に循環ファンを介して連通する循環ダクトと前記バーナの燃焼熱により加熱された空気を前記乾燥容器内に吹き込む温風吹出口ダクトを有する内部空気循環経路と、一方の通路を前記排気経路と前記脱臭触媒に連通し、他方の通路を前記内部空気循環経路に連通する直交熱交換器とを有し、前記乾燥容器内から前記臭い空気吸引手段により吸引された臭い空気を前記臭い空気燃焼室と前記脱臭触媒にて脱臭処理するとともに、前記乾燥容器内の空気を前記内部空気循環経路を介して前記直交熱交換器にて加熱昇温させながら循環させて生ごみを乾燥処理する生ごみ処理機において、前記循環ダクトと前記温風吹出口ダクトとの間に前記直交熱交換器をバイパスして前記乾燥容器内の空気を循環させる内部空気循環バイパス経路を備えたことを特徴とする生ごみ処理機。A drying container for drying garbage, odor air suction means for sucking odor air from the drying container, a burner for burning liquid fuel to generate combustion heat, and the drying by the odor suction means provided downstream of the burner An odor air combustion chamber for thermally decomposing odor air sucked from a container with a combustion flame of the burner, a deodorization catalyst provided downstream of the odor air combustion chamber, and an exhaust for exhausting air that has passed through the deodorization catalyst to the outside An internal air circulation path having a path, a circulation duct communicating with the drying container via a circulation fan, and a hot air outlet duct for blowing air heated by the combustion heat of the burner into the drying container; The odorous air suction means has an orthogonal heat exchanger that communicates with the exhaust path and the deodorization catalyst and communicates the other path with the internal air circulation path. While the odor air sucked more is deodorized by the odor air combustion chamber and the deodorization catalyst, while the air in the drying container is heated and heated by the orthogonal heat exchanger via the internal air circulation path An internal air circulation bypass for bypassing the orthogonal heat exchanger between the circulation duct and the hot air outlet duct to circulate the air in the drying container in a garbage processing machine for drying and processing the garbage Garbage disposal machine characterized by having a route. 前記温風吹出口ダクトにおいて、前記内部空気循環バイパス経路から導入される空気量は、前記直交熱交換器の低温側より高温側に多く導入されることを特徴とする請求項2記載の生ごみ処理機。The garbage processing according to claim 2, wherein in the hot air outlet duct, an amount of air introduced from the internal air circulation bypass path is introduced more to a high temperature side than a low temperature side of the orthogonal heat exchanger. Machine. 前記内部空気循環経路の内圧が前記排出経路の内圧より小さいことを特徴とする請求項2乃至請求項3記載の生ごみ処理機。4. The garbage processing machine according to claim 2, wherein an internal pressure of the internal air circulation path is smaller than an internal pressure of the discharge path.
JP2003158800A 2003-06-04 2003-06-04 Garbage processing machine Expired - Fee Related JP4057469B2 (en)

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