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JP3724294B2 - Garbage disposal equipment - Google Patents
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JP3724294B2 - Garbage disposal equipment - Google Patents

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Publication number
JP3724294B2
JP3724294B2 JP33071999A JP33071999A JP3724294B2 JP 3724294 B2 JP3724294 B2 JP 3724294B2 JP 33071999 A JP33071999 A JP 33071999A JP 33071999 A JP33071999 A JP 33071999A JP 3724294 B2 JP3724294 B2 JP 3724294B2
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Japan
Prior art keywords
flow path
exhaust
garbage
heat
temperature side
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JP33071999A
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Japanese (ja)
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JP2001145864A (en
Inventor
浩之 大村
悦郎 藤野
尚治 中川
弘典 片山
浩通 森北
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Panasonic Electric Works Co Ltd
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Matsushita Electric Works Ltd
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Priority to JP33071999A priority Critical patent/JP3724294B2/en
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Description

【0001】
【発明の属する技術分野】
本発明は、微生物の力を利用して生ごみの分解処理を行う生ごみ処理装置に関し、詳しくは生ごみ処理装置における吸気、排気の構造に関するものである。
【0002】
【従来の技術】
近年、微生物の力を利用して有機物及び水分を有する生ごみを環境に影響を与えない程度に分解発酵することが行われており、この生ごみ処理を行うための生ごみ処理装置が知られている。この生ごみ処理装置は、生ごみ処理槽内にバイオチップと称される木質細片などの担体を生ごみ処理材として充填してある。生ごみ処理槽に設けた生ごみ投入口から生ごみを生ごみ処理槽内に投入し、生ごみ処理材に生息する微生物の働きで生ごみを発酵させて分解処理するようになっている。
【0003】
この種の生ごみ処理装置では、生ごみ処理槽からの排気は、生ごみ処理槽内部で有機物の分解に伴って発生する臭気を含んでおり、これをそのまま排気した場合、臭気が周囲に漂い、周辺環境の悪化を引き起こす可能性がある。そこで、従来では、生ごみ処理槽からの排気が導かれる排気流路の途中に加熱脱臭部を配置し、加熱脱臭部にて脱臭した後に外気へ放出するようにしている。
【0004】
【発明が解決しようとする課題】
ところが、従来のように生ごみ処理槽からの排気を加熱脱臭する方式にあっては、外気に放出される排気の温度が高くなる。例えば触媒燃焼式の加熱脱臭装置の場合、触媒出口温度を200℃〜400℃にする必要があり、そのために、生ごみ処理装置の設置場所に制限を受けるなどの問題があった。
【0005】
本発明は、上記の従来例の問題点に鑑みて発明したものであって、その目的とするところは、脱臭性能を維持したままで、外気に放出される排気の温度を下げることができ、設置場所に制限を受けずに排気が可能になると共に、運転コストの低下を図ることができ、さらに外気に放出される排気の放熱分を有効利用して加熱脱臭部における加熱負荷の軽減を図ることができる生ごみ処理装置を提供するにある。
【0006】
【課題を解決するための手段】
上記課題を解決するために本発明は、内部に微生物が生息した生ごみ処理材を収容し、生ごみと共に攪拌して発酵分解処理を行う生ごみ処理槽1を備え、生ごみ処理槽1からの排気を加熱脱臭部22により加熱脱臭した後に処理機本体の排気口9から外気に放出する生ごみ処理装置において、生ごみ処理槽1の内部に、上流側流路22aと下流側流路22bとを有する第1の熱交換部23と、低温側流路70bと高温側流路70aとを有する第2の熱交換部70とを備え、生ごみ処理槽1内の排気が、第2の熱交換部70の低温側流路70bから第1の熱交換部23の上流側流路22aを介して加熱脱臭部22に流れ、加熱脱臭部22で脱臭された排気が第1の熱交換部23の下流側流路22bから第2の熱交換部70の高温側流路70aを介して排気口9に排気され、上記第1の熱交換部23において上流側流路22aを流れる排気ニと下流側流路22bを流れる排気とが熱交換され、上記第2の熱交換部70において低温側流路70bを流れる排気ルと高温側流路70aを流れる排気ヲとが熱交換されるように構成されることを特徴としており、このように構成することで、外気に放出される排気の放熱分を、加熱脱臭部22に導入される前の排気への予熱として有効利用することができる。これにより、外気に放出される排気の熱を回収して生ごみ処理槽1からの排気温度を上昇させることができるので、加熱脱臭部22における加熱負荷を軽減することができると共に、加熱脱臭部22による脱臭性能を維持したままで、熱ロスを少なくでき、さらに、外気に放出される排気の温度を下げることができる。
【0007】
また上記第2の熱交換部70における高温側流路70aを低温側流路70bの内側に配置して、低温側流路70bを流れる排気ルと高温側流路70aを流れる排気ヲとが熱交換されるようにするのが好ましく、この場合、流通する空気温度が高い場合には、生ごみ処理材の低温発火が発生しないようにすることができる。
【0008】
また上記第2の熱交換部70における高温側流路70aの一部又は全体を、低温側流路70bの一部又は全体の外側に配置して、低温側流路70bを流れる排気ルと高温側流路70aを流れる排気ヲとが熱交換されるようにするのが好ましく、この場合、熱効率が向上する。
【0009】
また上記生ごみ処理槽1の内部に、加熱脱臭部22の一部又は全体を収容し、生ごみ処理槽1からの排気を加熱脱臭部22へ導く低温側流路70bと上記収容された加熱脱臭部22との間で熱交換を行う別の熱交換部を構成するのが好ましく、この場合、加熱脱臭部22の放熱分も生ごみ処理槽1内に回収でき、熱効率が一層向上する。
【0010】
【発明の実施の形態】
以下、本発明を添付図面に示す実施形態に基づいて説明する。
【0011】
本実施形態の生ごみ処理装置Aは、図1に示すように、ハウジング18内に、生ごみ投入口19を有する生ごみ処理槽1を備えており、この生ごみ処理槽1内部には、微生物の寄生した生ごみ処理材が収容され、生ごみ処理材を生ごみと共に攪拌して発酵分解処理を行うように構成されている。図1中のgは生ごみや生ごみ処理材等を示し、Fは隙間空間71内に導入された吸気に排気ダクト31の放熱分を回収する熱回収部を示している。
【0012】
すなわち図2に示すように、生ごみ処理槽1内には撹拌羽根16aを有する撹拌軸16bが架設してあり、モータ100により撹拌軸16bが回転するようになっている。そして、この撹拌羽根16a、撹拌軸16bにより撹拌機構16が構成してある。撹拌の目的は、生ごみ処理材とを混合すること、大型の生ごみを粉砕すること、また、水分蒸発を促進すること等である。生ごみ処理槽1内には微生物が生息したバイオチップと称されるおが屑状の木質細片のような担体よりなる生ごみ処理材が充填してある。またハウジング18の上面には生ごみ投入口19が設けてあり、生ごみ投入口19に開閉自在な蓋30が設けてあり、蓋30を開けて生ごみ投入口19から生ごみ処理槽1の上開口を経て生ごみ処理槽1内に生ごみを投入することができるようになっている。生ごみ処理槽1の一側部の上部には生ごみ処理槽1の排気を排出するための排気部10が設けてある。
【0013】
生ごみ処理槽1の排気部10の出口側の流路には、集塵フィルタ等からなるフィルタ2(図1)が設けられている。フィルタ2よりも下流側の流路には、第2の熱交換部70と、加熱脱臭部22と第1の熱交換部23とを備えた脱臭装置24とが設けてある。
【0014】
第2の熱交換部70は、生ごみ処理槽1の内部に設けられている。この第2の熱交換部70は、図3、図4に示すように、生ごみ処理槽1内の排気を流す低温側流路70bと、加熱脱臭部22で脱臭された排気を排出する高温側流路70aとにより構成してある。ここでは、第2の熱交換部70において、低温側流路70bを流れる排気ルと高温側流路70aを流れる排気ヲとは、図1に示すように、互い逆方向の流れ、つまり、対向流となるように配置されている。尚、図4の破線矢印イは熱の伝達を示している。
【0015】
加熱脱臭部22は、図6に示すように、ヒータ3と、白金触媒のような脱臭触媒を添着したハニカム構造の脱臭ハニカム4とを有している。
【0016】
第1の熱交換部23は、生ごみ処理槽1内の排気を加熱脱臭部22に排気を流す上流側流路22aと、加熱脱臭部22で脱臭された排気を排出する下流側流路22bとにより構成してある。ここでは、第1の熱交換部23において上流側流路22aを流れる排気ニと下流側流路22bを流れる排気ヘとは図6に示すように互いに逆方向の流れ、つまり、対向流となるように配置されている。なお図6中の矢印ホは熱の伝達を示している。なお第1の熱交換部23の構造は一例であって、これに限定されるものではない。
【0017】
図5、図6に示す例では、ヒータ3と脱臭ハニカム4とを上下に並べて配置すると共に、ヒータ3と脱臭ハニカム4の前方に連通室5を形成し、この連通室5をケーシング8外部から取り付けられる蓋板6により開閉可能としてある。ここでは第1の熱交換部23のケーシング8の前面部を前方に大きく突出させ、その内部にヒータ3と脱臭ハニカム4とを伝熱板7を介して上下に配置し、且つその前方に連通室5を設けている。図6中の42は取付具、44はシール部材であり、取付具42を取り外すことで脱臭ハニカム4を出し入れ自在に収納できるようになっている。
【0018】
上記加熱脱臭部22と第1の熱交換部23とを備えた脱臭装置24は、図2に示すように、ハウジング18と生ごみ処理槽1の上部との間の隙間空間71内に配置してある。ハウジング18の底板18aには、ハウジング18と生ごみ処理槽1の側部との間の隙間空間71に開口する外気取り入れ口34が設けてある。
【0019】
これにより、外気取り入れ口34→ハウジング18と生ごみ処理槽1の側部との間の隙間空間71→ハウジング18と生ごみ処理槽1の上部との間の隙間空間72→生ごみ処理槽1入口36という順路で生ごみ処理装置Aの外部から生ごみ処理槽1内に新鮮な外部空気が供給されるようになり、このような外気取り入れ口34→隙間空間71→隙間空間72→生ごみ処理槽1入口36という一連の流路が吸気経路となっている。
【0020】
一方、生ごみ処理槽1からの排気は、生ごみ処理槽1の排気部10→第2の熱交換部70の低温側流路70b→第1の熱交換部23の上流側流路22a→ヒータ3→脱臭ハニカム4→第1の熱交換部23の下流側流路22b→第2の熱交換部70の高温側流路70a→図2の排気ダクト31→排気ファン25→排気ダクト31→消音ボックス40を経て、排気口9から外気に放出されるようになっている。
【0021】
しかして、加熱脱臭部22への入り側の通気を加熱脱臭部22からの出側の通気により加熱するための第2の熱交換部70を、生ごみ処理槽1内に収容したことによって、外気に放出される排気の放熱分を、加熱脱臭部22に導入される前の排気への予熱として有効利用することができる。つまり、外気に放出される排気の熱を回収して生ごみ処理槽1からの排気温度を上昇させることによって、加熱脱臭部22における加熱負荷を軽減することができる。しかも、加熱脱臭部22による脱臭性能を維持したままで、熱ロスを少なくして、運転コストの低下を図ることができる。さらに、外気に放出される排気の温度を下げることができるので、設置場所にも制限を受けなくてすむという利点もある。
【0022】
また、図3、図4に示すように、第2の熱交換部における高温側流路70aを低温側流路70bの内側に配置してある。ちなみに、流通する空気温度が高すぎると、生ごみ処理槽1内のバイオチップと称される木質細片が生ごみ処理材で混合される際に低温発火するおそれがある。そこで、流通する空気温度が高い場合には、第2の熱交換部からの熱回収量を少なくすることで、低温発火が発生しないようにすることができる。
【0023】
図7、図8では、高温側流路70aと低温側流路70bとを図3、図4の場合とは逆になるように配置した場合を示している。つまり、高温側流路70aを低温側流路70bの外側に配置することにより、高温側流路70aの放熱分を生ごみ処理槽1内に回収でき、熱効率が向上する。従って、流通する空気温度が低い場合に、熱交換性能の向上を図ることができる。なお、高温側流路70aを低温側流路70bの外側に配置するにあたって、高温側流路70a全体を低温側流路70b全体の外側に配置する場合、或いは、高温側流路70aの一部を低温側流路70b全体或いは一部の外側に配置する場合など、適宜変更可能である。これにより、生ごみ処理槽1内に回収される高温側流路70aからの熱回収量をコントロールできるようになり、流通する空気温度に適した状態に容易に対応できるものとなる。
【0024】
図9は、生ごみ処理槽1の内部に、第2の熱交換部70を収容すると共に、脱臭装置24全体を収容した場合を示している。他の構成は図1と同様であり、異なる点だけを述べる。本例では、生ごみ処理槽1からの排気を加熱脱臭部22へ導く低温側流路70bと、生ごみ処理槽1内に収容された脱臭装置24との間で熱交換を行う別の熱交換部が構成されている。つまり、脱臭装置24を構成する加熱脱臭部22及び第1の熱交換部23の放熱分も生ごみ処理槽1内に回収でき、さらに熱効率が向上するという利点がある。なお、脱臭装置24全体を生ごみ処理槽1内に収容する場合には限らず、例えば加熱脱臭部22のみ、或いは第1の熱交換部23のみを収容してもよいものである。
【0025】
【発明の効果】
上述のように請求項1記載の発明にあっては、内部に微生物が生息した生ごみ処理材を収容し、生ごみと共に攪拌して発酵分解処理を行う生ごみ処理槽を備え、生ごみ処理槽からの排気を加熱脱臭部により加熱脱臭した後に処理機本体の排気口から外気に放出する生ごみ処理装置において、生ごみ処理槽の内部に、上流側流路と下流側流路とを有する第1の熱交換部と、低温側流路と高温側流路とを有する第2の熱交換部とを備え、生ごみ処理槽内の排気が、第2の熱交換部の低温側流路から第1の熱交換部の上流側流路を介して加熱脱臭部に流れ、加熱脱臭部で脱臭された排気が第1の熱交換部の下流側流路から第2の熱交換部の高温側流路を介して排気口に排気され、上記第1の熱交換部において上流側流路を流れる排気と下流側流路を流れる排気とが熱交換され、上記第2の熱交換部において低温側流路を流れる排気と高温側流路を流れる排気とが熱交換されるように構成したので、外気に放出される排気の放熱分を、加熱脱臭部に導入される前の排気への予熱として有効利用することができる。従って、外気に放出される排気の熱を回収して生ごみ処理槽からの排気温度を上昇させることができ、加熱脱臭部における加熱負荷を軽減することができると共に、脱臭性能を維持したままで、熱ロスを少なくして、運転コストの低下を図ることができる。さらに、外気に放出される排気の温度を下げることができるので、設置場所に制限を受けずに排気が可能となる。
【0026】
また請求項2記載の発明は、請求項1記載の効果に加えて、第2の熱交換部における高温側流路を低温側流路の内側に配置して、低温側流路を流れる排気と高温側流路を流れる排気とが熱交換されるようにしたので、熱交換からの熱回収量を少なくでき、例えば流通する空気温度が高い場合には、生ごみ処理材の低温発火が発生しないようにすることができる。
【0027】
また請求項3記載の発明は、請求項1記載の効果に加えて、第2の熱交換部における高温側流路の一部又は全体を、低温側流路の一部又は全体の外側に配置して、低温側流路を流れる排気と外側高温側流路を流れる排気とが熱交換されるようにしたので、熱効率が向上する。従って、流通する空気温度が低い場合には、熱交換性能の向上を図ることができる。
【0028】
また請求項4記載の発明は、請求項1乃至請求項3のいずれかに記載の効果に加えて、生ごみ処理槽の内部に、加熱脱臭部の一部又は全体を収容し、生ごみ処理槽からの排気を加熱脱臭部へ導く低温側流路と上記収容された加熱脱臭部との間で熱交換を行う別の熱交換部を構成したので、加熱脱臭部の放熱分も生ごみ処理槽内に回収でき、熱効率が一層向上する。
【図面の簡単な説明】
【図1】本発明の実施形態の一例を示す模式図である。
【図2】同上の生ごみ処理槽の概略斜視図である。
【図3】同上の第2の熱交換部の斜視図である。
【図4】同上の第2の熱交換部の内部構造の概略図である。
【図5】同上の第1の熱交換部の斜視図である。
【図6】図5の第1の熱交換部の内部構造の概略図である。
【図7】同上の第2の熱交換部の他の実施形態の斜視図である。
【図8】図7の第2の熱交換部の内部構造の概略図である。
【図9】他の実施形態の模式図である。
【符号の説明】
A 生ごみ処理装置
1 生ごみ処理槽
9 排気口
22 加熱脱臭部
70 熱交換部
70a 高温側流路
70b 低温側流路
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a garbage processing apparatus that performs decomposition processing of garbage using the force of microorganisms, and more particularly to a structure of intake and exhaust air in the garbage processing apparatus.
[0002]
[Prior art]
In recent years, garbage containing organic matter and moisture has been decomposed and fermented to the extent that it does not affect the environment using the power of microorganisms, and a garbage treatment apparatus for performing this garbage treatment is known. ing. In this garbage disposal apparatus, a garbage disposal tank is filled with a carrier such as a wood chip called a biochip as a garbage disposal material. Garbage is introduced into the garbage treatment tank from the garbage input port provided in the garbage treatment tank, and the garbage is fermented and decomposed by the action of microorganisms that inhabit the garbage treatment material.
[0003]
In this type of garbage processing equipment, the exhaust from the garbage processing tank contains odors generated by the decomposition of organic matter inside the garbage processing tank, and if this is exhausted as it is, the odors drift around. , May cause deterioration of the surrounding environment. Therefore, conventionally, a heating deodorization unit is arranged in the middle of an exhaust passage through which exhaust from the garbage treatment tank is guided, and is deodorized by the heating deodorization unit and then released to the outside air.
[0004]
[Problems to be solved by the invention]
However, in the conventional method of heating and deodorizing the exhaust from the garbage treatment tank, the temperature of the exhaust discharged to the outside air becomes high. For example, in the case of a catalytic combustion type heating and deodorizing apparatus, it is necessary to set the catalyst outlet temperature to 200 ° C. to 400 ° C. Therefore, there is a problem that the installation place of the garbage disposal apparatus is restricted.
[0005]
The present invention was invented in view of the problems of the above-described conventional example, and the object of the present invention is to reduce the temperature of the exhaust gas released to the outside air while maintaining the deodorizing performance. Exhaust can be performed without restriction on the installation location, and the operating cost can be reduced. Furthermore, the heat radiation of the exhaust discharged to the outside air can be effectively used to reduce the heating load in the heating deodorization section. It is in providing the garbage processing apparatus which can.
[0006]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, the present invention includes a garbage treatment tank 1 that contains a garbage treatment material inhabited by microorganisms and that is stirred together with the garbage to perform a fermentation decomposition treatment. In the garbage processing apparatus that discharges the exhaust gas from the exhaust port 9 of the processing machine body to the outside air after being heated and deodorized by the heating and deodorizing unit 22, the upstream flow path 22a and the downstream flow path 22b are disposed inside the garbage processing tank 1. And a second heat exchange section 70 having a low temperature side flow path 70b and a high temperature side flow path 70a, and the exhaust in the garbage treatment tank 1 is second Exhaust gas that has flowed from the low temperature side flow path 70b of the heat exchange section 70 to the heating deodorization section 22 through the upstream flow path 22a of the first heat exchange section 23 and deodorized by the heating deodorization section 22 is the first heat exchange section. 23 from the downstream flow path 22b of the second heat exchange section 70 to the high temperature side flow path 70a. Then, the exhaust gas exhausted to the exhaust port 9 is subjected to heat exchange between the exhaust gas flowing through the upstream flow path 22a and the exhaust gas flowing through the downstream flow path 22b in the first heat exchange unit 23, and the second heat exchange unit 70 is replaced. The exhaust gas flowing through the low temperature side flow path 70b and the exhaust gas flowing through the high temperature side flow path 70a are heat-exchanged . In this way, the exhaust gas is discharged to the outside. The heat released from the exhaust can be effectively used as preheating to the exhaust before being introduced into the heating deodorization unit 22. Thereby, since the heat of the exhaust gas discharged into the outside air can be recovered and the exhaust gas temperature from the garbage treatment tank 1 can be raised, the heating load in the heating deodorization unit 22 can be reduced, and the heating deodorization unit The heat loss can be reduced while maintaining the deodorizing performance of No. 22, and the temperature of the exhaust gas released to the outside air can be lowered.
[0007]
Further, the high temperature side flow path 70a in the second heat exchange section 70 is disposed inside the low temperature side flow path 70b, and the exhaust gas flowing through the low temperature side flow path 70b and the exhaust gas flowing through the high temperature side flow path 70a are heated. In this case, when the temperature of the circulating air is high, it is possible to prevent low temperature ignition of the garbage treatment material.
[0008]
Further, a part or the whole of the high temperature side channel 70a in the second heat exchanging unit 70 is arranged outside a part or the whole of the low temperature side channel 70b, and the exhaust gas flowing through the low temperature side channel 70b and the high temperature It is preferable to exchange heat with the exhaust gas flowing through the side flow path 70a . In this case, the thermal efficiency is improved.
[0009]
Further, a part or the whole of the heating and deodorizing unit 22 is accommodated inside the garbage processing tank 1, and the low-temperature channel 70 b that guides exhaust from the garbage processing tank 1 to the heating and deodorizing unit 22 and the stored heating. It is preferable to configure another heat exchange unit that exchanges heat with the deodorization unit 22, and in this case, the heat radiation of the heating deodorization unit 22 can also be collected in the garbage treatment tank 1, and the thermal efficiency is further improved.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described based on embodiments shown in the accompanying drawings.
[0011]
As shown in FIG. 1, the garbage processing apparatus A of the present embodiment includes a garbage processing tank 1 having a garbage input port 19 in a housing 18, and inside the garbage processing tank 1, A food waste treatment material infested with microorganisms is accommodated, and the food waste treatment material is stirred together with the food waste and subjected to fermentation decomposition treatment. In FIG. 1, “g” represents garbage, garbage disposal material, and the like, and “F” represents a heat recovery unit that recovers the heat radiation of the exhaust duct 31 to the intake air introduced into the gap space 71.
[0012]
That is, as shown in FIG. 2, a stirring shaft 16 b having stirring blades 16 a is installed in the garbage treatment tank 1, and the stirring shaft 16 b is rotated by the motor 100. And the stirring mechanism 16 is comprised by this stirring blade 16a and the stirring shaft 16b. The purpose of the agitation is to mix with the garbage processing material, to pulverize large garbage, to promote moisture evaporation, and the like. The garbage treatment tank 1 is filled with a garbage treatment material made of a carrier such as sawdust-like wood chips called biochip inhabited by microorganisms. Further, a garbage input port 19 is provided on the upper surface of the housing 18, and a lid 30 that can be opened and closed is provided at the garbage input port 19. The lid 30 is opened and the garbage processing tank 1 is opened from the garbage input port 19. Garbage can be put into the garbage processing tank 1 through the upper opening. An exhaust unit 10 for exhausting the exhaust from the garbage treatment tank 1 is provided on the upper side of one side of the garbage treatment tank 1.
[0013]
A filter 2 (FIG. 1) made of a dust collection filter or the like is provided in the flow path on the outlet side of the exhaust unit 10 of the garbage treatment tank 1. A flow path on the downstream side of the filter 2 is provided with a second heat exchange unit 70, and a deodorization device 24 including a heating deodorization unit 22 and a first heat exchange unit 23.
[0014]
The second heat exchange unit 70 is provided inside the garbage treatment tank 1. As shown in FIGS. 3 and 4, the second heat exchanging unit 70 has a low-temperature channel 70 b through which the exhaust in the garbage treatment tank 1 flows and a high temperature that exhausts the exhaust deodorized by the heating and deodorizing unit 22. It is comprised by the side flow path 70a. Here, in the second heat exchanging section 70, the exhaust gas flowing through the low temperature side flow path 70b and the exhaust gas flowing through the high temperature side flow path 70a flow in opposite directions as shown in FIG. It is arranged to be a flow. In addition, the broken-line arrow a of FIG. 4 has shown heat transfer.
[0015]
As shown in FIG. 6, the heating and deodorizing unit 22 includes a heater 3 and a deodorizing honeycomb 4 having a honeycomb structure to which a deodorizing catalyst such as a platinum catalyst is attached.
[0016]
The first heat exchanging unit 23 includes an upstream flow path 22a for flowing the exhaust gas in the garbage treatment tank 1 to the heating and deodorizing section 22, and a downstream flow path 22b for discharging the exhaust gas deodorized by the heating and deodorizing section 22. It is comprised by. Here, in the first heat exchanging section 23, the exhaust gas flowing through the upstream flow path 22a and the exhaust gas flowing through the downstream flow path 22b are in opposite directions as shown in FIG. Are arranged as follows. Note that an arrow H in FIG. 6 indicates heat transfer. In addition, the structure of the 1st heat exchange part 23 is an example, Comprising: It is not limited to this.
[0017]
In the example shown in FIGS. 5 and 6, the heater 3 and the deodorizing honeycomb 4 are arranged one above the other, and a communication chamber 5 is formed in front of the heater 3 and the deodorizing honeycomb 4, and the communication chamber 5 is formed from the outside of the casing 8. It can be opened and closed by a cover plate 6 attached. Here, the front surface portion of the casing 8 of the first heat exchanging portion 23 is protruded greatly forward, the heater 3 and the deodorizing honeycomb 4 are arranged vertically through the heat transfer plate 7 and communicated with the front thereof. A chamber 5 is provided. In FIG. 6, reference numeral 42 denotes an attachment tool, and 44 denotes a seal member. By removing the attachment tool 42, the deodorized honeycomb 4 can be inserted and removed freely.
[0018]
The deodorizing device 24 having the heating deodorizing unit 22 and the first heat exchanging unit 23 is disposed in a gap space 71 between the housing 18 and the upper part of the garbage treatment tank 1, as shown in FIG. It is. The bottom plate 18 a of the housing 18 is provided with an outside air intake 34 that opens into a gap space 71 between the housing 18 and the side of the garbage disposal tank 1.
[0019]
Accordingly, the gap space 71 between the outside air inlet 34 → the housing 18 and the side of the garbage treatment tank 1 → the gap space 72 between the housing 18 and the upper part of the garbage treatment tank 1 → the garbage treatment tank 1 Fresh external air is supplied into the garbage processing tank 1 from the outside of the garbage processing apparatus A through a route called the inlet 36. Such an outside air inlet 34 → gap space 71 → gap space 72 → garbage A series of flow paths called the treatment tank 1 inlet 36 serves as an intake path.
[0020]
On the other hand, the exhaust from the garbage processing tank 1 is performed in the exhaust section 10 of the garbage processing tank 1 → the low temperature side flow path 70b of the second heat exchange section 70 → the upstream flow path 22a of the first heat exchange section 23 → Heater 3 → deodorizing honeycomb 4 → downstream flow path 22b of the first heat exchange section 23 → high temperature flow path 70a of the second heat exchange section 70 → exhaust duct 31 in FIG. 2 → exhaust fan 25 → exhaust duct 31 → It passes through the muffler box 40 and is discharged from the exhaust port 9 to the outside air.
[0021]
The second heat exchange unit 70 for heating the ventilation on the entry side to the heating deodorization unit 22 by the ventilation on the exit side from the heating deodorization unit 22 is accommodated in the garbage treatment tank 1. The heat radiation of the exhaust discharged to the outside air can be effectively used as preheating to the exhaust before being introduced into the heating deodorization unit 22. That is, the heating load in the heating and deodorizing unit 22 can be reduced by collecting the heat of the exhaust discharged to the outside air and increasing the exhaust temperature from the garbage treatment tank 1. In addition, while maintaining the deodorizing performance by the heating and deodorizing unit 22, it is possible to reduce the heat loss and reduce the operating cost. Furthermore, since the temperature of the exhaust gas discharged to the outside air can be lowered, there is an advantage that the installation location is not restricted.
[0022]
Further, as shown in FIGS. 3 and 4, the high temperature side flow path 70a in the second heat exchange section is arranged inside the low temperature side flow path 70b. Incidentally, if the circulating air temperature is too high, there is a risk of low temperature ignition when the wood chips called biochips in the garbage treatment tank 1 are mixed with the garbage treatment material. Therefore, when the temperature of the circulating air is high, the amount of heat recovered from the second heat exchange unit can be reduced to prevent low temperature ignition from occurring.
[0023]
7 and 8 show a case where the high temperature side flow path 70a and the low temperature side flow path 70b are arranged so as to be opposite to those in FIGS. That is, by disposing the high temperature side flow path 70a outside the low temperature side flow path 70b, the heat radiation from the high temperature side flow path 70a can be recovered in the garbage treatment tank 1, and the thermal efficiency is improved. Therefore, when the circulating air temperature is low, it is possible to improve the heat exchange performance. In arranging the high temperature side channel 70a outside the low temperature side channel 70b, the entire high temperature side channel 70a is arranged outside the entire low temperature side channel 70b, or a part of the high temperature side channel 70a. Can be appropriately changed, for example, in a case where the liquid crystal is disposed on the entire low temperature side flow path 70b or a part of the outside. Thereby, it becomes possible to control the amount of heat recovered from the high-temperature side flow path 70a recovered in the garbage treatment tank 1, and can easily cope with a state suitable for the temperature of the circulating air.
[0024]
FIG. 9 shows a case where the second heat exchange unit 70 and the entire deodorizing device 24 are accommodated inside the garbage treatment tank 1. Other configurations are the same as those in FIG. 1, and only different points will be described. In this example, another heat for exchanging heat between the low-temperature channel 70 b that guides the exhaust from the garbage treatment tank 1 to the heating deodorization unit 22 and the deodorizer 24 accommodated in the garbage treatment tank 1. An exchange unit is configured. That is, there is an advantage that the heat radiation of the heating and deodorizing unit 22 and the first heat exchanging unit 23 constituting the deodorizing device 24 can also be collected in the garbage treatment tank 1 and the thermal efficiency is further improved. The entire deodorization device 24 is not limited to be accommodated in the garbage treatment tank 1, and for example, only the heating deodorization unit 22 or only the first heat exchange unit 23 may be accommodated.
[0025]
【The invention's effect】
As described above, in the first aspect of the present invention, there is provided a garbage processing tank that accommodates the garbage processing material inhabited by microorganisms and stirs it together with the garbage to perform a fermentation decomposition treatment. In the garbage processing apparatus which discharges the exhaust from the tank to the outside air from the exhaust port of the processing machine body after deodorizing it by the heating deodorization unit, the garbage processing tank has an upstream channel and a downstream channel. A first heat exchanging unit, and a second heat exchanging unit having a low temperature side channel and a high temperature side channel, and the exhaust in the garbage treatment tank is a low temperature side channel of the second heat exchanging unit To the heating deodorization section through the upstream flow path of the first heat exchange section, and the exhaust gas deodorized by the heating deodorization section is heated from the downstream flow path of the first heat exchange section to the high temperature of the second heat exchange section. The exhaust that is exhausted to the exhaust port through the side flow path and flows through the upstream flow path in the first heat exchange section and the downstream flow path The exhaust and is heat exchanged, since it is configured so that the exhaust flowing through the low-temperature side flow passage in the second heat exchange portion and the exhaust gas flowing through the hot-side flow path is a heat exchange, the exhaust gas that is discharged to the outside air The heat radiation can be effectively used as preheating to the exhaust before being introduced into the heating deodorization unit. Therefore, the heat of the exhaust discharged to the outside air can be recovered to raise the exhaust temperature from the garbage treatment tank, the heating load in the heating deodorization part can be reduced, and the deodorizing performance is maintained. The heat loss can be reduced and the operating cost can be reduced. Furthermore, since the temperature of the exhaust discharged to the outside air can be lowered, the exhaust can be performed without being limited by the installation location.
[0026]
Moreover, in addition to the effect of Claim 1, the invention of Claim 2 arrange | positions the high temperature side flow path in a 2nd heat exchange part inside a low temperature side flow path, and the exhaust_gas | exhaustion which flows through a low temperature side flow path, Heat exchange with the exhaust flowing through the high-temperature channel is possible, so the amount of heat recovered from the heat exchange can be reduced. For example, when the temperature of the circulating air is high, the low temperature ignition of the garbage treatment material does not occur Can be.
[0027]
Moreover, in addition to the effect of Claim 1, invention of Claim 3 arrange | positions a part or whole of the high temperature side flow path in a 2nd heat exchange part in the part or whole outside of a low temperature side flow path. Thus, heat exchange is performed between the exhaust gas flowing through the low temperature side flow path and the exhaust gas flowing through the outer high temperature side flow path, so that the thermal efficiency is improved. Therefore, when the circulating air temperature is low, the heat exchange performance can be improved.
[0028]
Moreover, in addition to the effect in any one of Claims 1 thru | or 3, the invention of Claim 4 accommodates a part or whole of a heating deodorizing part in the inside of a garbage processing tank, and treats garbage. Since another heat exchanging part that exchanges heat between the low-temperature side channel that leads the exhaust from the tank to the heating and deodorizing part and the above-mentioned housed heating and deodorizing part is configured, the heat radiation of the heating and deodorizing part is also treated as garbage. It can be recovered in the tank and the thermal efficiency is further improved.
[Brief description of the drawings]
FIG. 1 is a schematic diagram showing an example of an embodiment of the present invention.
FIG. 2 is a schematic perspective view of the above garbage disposal tank.
FIG. 3 is a perspective view of the second heat exchanging unit.
FIG. 4 is a schematic view of the internal structure of the second heat exchange unit.
FIG. 5 is a perspective view of the first heat exchange unit.
6 is a schematic view of the internal structure of the first heat exchange unit of FIG. 5;
FIG. 7 is a perspective view of another embodiment of the second heat exchanging unit.
8 is a schematic view of the internal structure of the second heat exchange unit of FIG.
FIG. 9 is a schematic diagram of another embodiment.
[Explanation of symbols]
A Garbage treatment apparatus 1 Garbage treatment tank 9 Exhaust port 22 Heating deodorization part 70 Heat exchange part 70a High temperature side flow path 70b Low temperature side flow path

Claims (4)

内部に微生物が生息した生ごみ処理材を収容し、生ごみと共に攪拌して発酵分解処理を行う生ごみ処理槽を備え、生ごみ処理槽からの排気を加熱脱臭部により加熱脱臭した後に、排気口から外気に放出する生ごみ処理装置において、生ごみ処理槽の内部に、上流側流路と下流側流路とを有する第1の熱交換部と、低温側流路と高温側流路とを有する第2の熱交換部とを備え、生ごみ処理槽内の排気が、第2の熱交換部の低温側流路から第1の熱交換部の上流側流路を介して加熱脱臭部に流れ、加熱脱臭部で脱臭された排気が第1の熱交換部の下流側流路から第2の熱交換部の高温側流路を介して排気口に排気され、上記第1の熱交換部において上流側流路を流れる排気と下流側流路を流れる排気とが熱交換され、上記第2の熱交換部において低温側流路を流れる排気と高温側流路を流れる排気とが熱交換されるように構成したことを特徴とする生ごみ処理装置。It contains a garbage treatment tank that contains garbage treatment material inhabited by microorganisms and that is stirred and fermented and decomposed together with the garbage. The exhaust from the garbage treatment tank is heated and deodorized by the heating deodorization unit, and then exhausted. In the garbage processing apparatus which discharges to the outside air from the mouth , a first heat exchange unit having an upstream channel and a downstream channel, a low temperature channel and a high temperature channel inside the garbage processing tank And a second heat exchanging unit, and the exhaust in the garbage processing tank is heated from the low temperature side channel of the second heat exchanging unit via the upstream side channel of the first heat exchanging unit. The exhaust deodorized in the heating and deodorizing section is exhausted from the downstream flow path of the first heat exchange section to the exhaust port through the high temperature flow path of the second heat exchange section, and the first heat exchange Heat is exchanged between the exhaust flowing in the upstream flow path and the exhaust flowing in the downstream flow path in the second heat exchange section. Garbage disposal apparatus characterized by being configured such that exhaust gas flowing through the hot-side flow path and the exhaust gas flowing through the high-temperature side flow passage is heat exchanged. 請求項1において、第2の熱交換部における高温側流路を低温側流路の内側に配置して、低温側流路を流れる排気と高温側流路を流れる排気とが熱交換されるようにしてなることを特徴とする生ごみ処理装置。 In Claim 1, the high temperature side flow path in the second heat exchanging section is arranged inside the low temperature side flow path so that the exhaust flowing through the low temperature side flow path and the exhaust flowing through the high temperature side flow path are heat-exchanged. is in the garbage disposal apparatus it said. 請求項1において、第2の熱交換部における高温側流路の一部又は全体を、低温側流路の一部又は全体の外側に配置して、低温側流路を流れる排気と高温側流路を流れる排気とが熱交換されるようにしてなることを特徴とする生ごみ処理装置。 2. The exhaust gas and the high temperature side flow according to claim 1, wherein a part or the whole of the high temperature side channel in the second heat exchanging part is disposed outside a part or the whole of the low temperature side channel. garbage disposal apparatus you characterized by comprising as the exhaust gas flowing through the road is heat exchanged. 請求項1乃至請求項3のいずれかにおいて、生ごみ処理槽の内部に、加熱脱臭部の一部又は全体を収容し、生ごみ処理槽からの排気を加熱脱臭部へ導く低温側流路と上記収容された加熱脱臭部との間で熱交換を行う別の熱交換部を構成したことを特徴とする生ごみ処理装置。 The low-temperature side flow path according to any one of claims 1 to 3, wherein a part or the whole of the heating deodorization unit is accommodated inside the garbage processing tank, and exhaust from the garbage processing tank is guided to the heating deodorization unit. garbage disposal apparatus you characterized by being configured to another heat exchange section for exchanging heat between the heating deodorization unit which is the accommodation.
JP33071999A 1999-11-19 1999-11-19 Garbage disposal equipment Expired - Fee Related JP3724294B2 (en)

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