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JP3240844B2 - Garbage processing equipment - Google Patents
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JP3240844B2 - Garbage processing equipment - Google Patents

Garbage processing equipment

Info

Publication number
JP3240844B2
JP3240844B2 JP18458394A JP18458394A JP3240844B2 JP 3240844 B2 JP3240844 B2 JP 3240844B2 JP 18458394 A JP18458394 A JP 18458394A JP 18458394 A JP18458394 A JP 18458394A JP 3240844 B2 JP3240844 B2 JP 3240844B2
Authority
JP
Japan
Prior art keywords
gas
garbage
deodorizing
catalyst
outside air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP18458394A
Other languages
Japanese (ja)
Other versions
JPH0849975A (en
Inventor
博史 西田
修三 徳満
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Corp
Panasonic Holdings Corp
Original Assignee
Panasonic Corp
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Panasonic Corp, Matsushita Electric Industrial Co Ltd filed Critical Panasonic Corp
Priority to JP18458394A priority Critical patent/JP3240844B2/en
Publication of JPH0849975A publication Critical patent/JPH0849975A/en
Application granted granted Critical
Publication of JP3240844B2 publication Critical patent/JP3240844B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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  • Processing Of Solid Wastes (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は一般家庭や業務用として
使用される、生ゴミ等の厨芥を乾燥処理する厨芥処理装
置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a garbage disposal apparatus for drying garbage such as garbage, which is used for general households and businesses.

【0002】[0002]

【従来の技術】従来では、台所で発生した厨芥を粉砕し
てそのまま下水へ流すディスポ−ザ−や、厨芥を粉砕脱
水して回収する生ゴミ脱水機、マイクロ波やヒータや蒸
気などの加熱手段を用いて厨芥を完全に焼却処理あるい
は乾燥処理して回収する厨芥処理装置を使用していた。
2. Description of the Related Art Conventionally, a disposer for crushing kitchen waste generated in a kitchen and flowing it to sewage as it is, a garbage dewatering machine for crushing and dewatering kitchen waste, and a heating means such as a microwave, a heater or steam are used. A garbage disposal device that completely incinerates or dries the garbage using the garbage collection system has been used.

【0003】[0003]

【発明が解決しようとする課題】これら従来の厨芥処理
装置は以下のような課題を有している。ディスポーザー
は処理排水のBODが著しく高く、下水処理場に負担を
かけることになる。日本の下水道の普及率が低い現状を
考えると、適当な処理方法とは言えない。
These conventional garbage disposal apparatuses have the following problems. Disposers have a significantly higher BOD for treated effluents, placing a burden on sewage treatment plants. Given the current low sewerage penetration in Japan, this is not an appropriate treatment method.

【0004】生ゴミ脱水機は、回収した粉砕厨芥に処理
を施していないので腐敗し易く、悪臭の原因、または害
虫や病原菌の発生の原因となるおそれがある。
[0004] The garbage dewatering machine does not treat the collected crushed garbage, so that it is liable to rot and may cause a bad smell or a pest or a pathogen.

【0005】加熱手段を用いた厨芥処理装置は、焼却や
乾燥によって無害化、無臭化、減量化処理を施し、前記
の腐敗等の問題を解決してはいるが、屋内に設置するこ
とが非常に困難であるという問題を残している。なぜな
ら、第一に、焼却処理する場合、この処理を行う為に機
器は高温に耐える構成が必要があり、極めて高い耐久性
と安全性が必要で、屋内に設置するには危険が伴う。第
二に、乾燥処理する場合においても、加熱処理時には一
時的に厨芥から臭気とともに大量の蒸気が発生し、その
ような高湿度下の脱臭処理は通常より困難であり、処理
をする度に悪臭が発生する恐れがあるからである。
[0005] Garbage disposal equipment using heating means has been detoxified, deodorized and reduced by incineration and drying to solve the above-mentioned problems such as decay, but it is very difficult to install it indoors. The problem remains that it is difficult. First, in the case of incineration, the equipment must have a configuration that can withstand high temperatures in order to perform this incineration, and must have extremely high durability and safety, and it is dangerous to install the apparatus indoors. Secondly, even in the case of drying treatment, a large amount of steam is generated together with odor from kitchen garbage during heat treatment, and it is more difficult to deodorize under such high humidity than usual. This is because there is a risk of occurrence.

【0006】以上のように加熱手段を用いた厨芥処理装
置は屋外にしかその設置の可能性は少なく、台所等で発
生した厨芥を屋外までわざわざ運搬しなければならず、
仮に屋内設置するとしても排気設備が不可欠となり大が
かりな設備機器となってしまい、コストが高く非常に使
い勝手が悪くなっている。
As described above, there is little possibility of installing a garbage disposal apparatus using a heating means only outdoors, and the garbage generated in a kitchen or the like must be transported to the outdoors.
Even if it is installed indoors, exhaust equipment is indispensable and it becomes a large-scale equipment, and the cost is high and the usability is very poor.

【0007】本発明は従来の課題を解決しようとするも
のであって、特に、乾燥処理を行う厨芥処理装置が有す
る脱臭処理の困難性を解決するものであり、屋内に設置
できる使い勝手の良い厨芥処理装置を提供することを目
的としている。
SUMMARY OF THE INVENTION The present invention is intended to solve the conventional problems, and in particular, to solve the difficulty of the deodorization treatment of a kitchen waste treatment apparatus which performs a drying treatment, and which is easy to use and can be installed indoors. It is intended to provide a processing device.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
の本発明の第一の手段は、厨芥を乾燥させる加熱手段
と、乾燥させる厨芥を収納する乾燥室と、前記乾燥室内
の厨芥を撹拌する撹拌手段と、厨芥の乾燥中に発生する
ガスを脱臭する脱臭手段とを備え、前記脱臭手段から排
出されるガスが外気へ排出されるまでの間に一定量以上
の貯留空間を設けるとともに、前記貯留空間の容積を前
記乾燥室の容積の1/250倍以上とし 脱臭手段に触
媒酸化方式を用い、脱臭手段の排出部から外気に至るま
での貯留空間に断熱材を設けたものである。
A first means of the present invention for achieving the above object is a heating means for drying garbage, a drying room for storing the garbage to be dried, and a stirrer for the garbage in the drying room. Agitating means, comprising a deodorizing means for deodorizing the gas generated during drying of the garbage, while providing a storage space of a certain amount or more until the gas discharged from the deodorizing means is discharged to the outside air, the volume of the storage space and above 1/250 times the volume of the drying chamber, touch the deodorizing means
Use a medium oxidation method to remove air from the exhaust port of the deodorizing means to the outside air.
Insulation material is provided in the storage space at

【0009】また第二の手段は、第一の手段に加え、貯
留空間を脱臭手段の排出部から外気に至るまでの通路で
構成し、この通路の長さを前記通路の任意の断面の短径
の8倍以上としたものである。
In the second means, in addition to the first means, the storage space is constituted by a passage from the discharge portion of the deodorizing means to the outside air, and the length of the passage is set to be shorter than an arbitrary cross section of the passage. It is eight times or more the diameter.

【0010】また第三の手段は、第一の手段及び第二の
手段に加え、脱臭の前段階にガス中に含まれる水蒸気を
凝縮して除湿する凝縮手段を設けるものである。
[0010] A third means is to provide a condensing means for condensing water vapor contained in the gas and dehumidifying it before deodorization, in addition to the first means and the second means.

【0011】[0011]

【作用】本発明の第一の手段によれば、脱臭手段の排出
側に貯留空間を設けているので、脱臭されたガスがすぐ
に外気へ排出されることが無く、一度内部に留まる。一
方、乾燥室では加熱手段と撹拌手段により厨芥が乾燥さ
れ、臭いと水蒸気を含むガスが発生しているが、瞬間的
なガスの発生量は一定なものではないので乾燥室内の圧
力は絶えず変動している。つまり発生ガスは往復の脈動
を繰り返し、脱臭行程から排気されるガスも出たり入っ
たりを繰り返しながら外気へ出ていくことになる。よっ
て、前記のように脱臭されたガスがすぐに外気へ排出さ
れること無く一度内部に留まる構成ならば、一度脱臭行
程を通過したガスは、外気へ排気される前に再度脱臭行
程へ吸引され再び脱臭されることになる。そしてさら
に、排出されるときにも脱臭行程を通過するので、少な
くとも3回は脱臭されることになり、脱臭効率が高くな
る。また、厨芥を乾燥させるときに発生するガスを触媒
酸化方式で脱臭することになる。そのような臭気ガスは
主に有機系のガスであり、加熱された触媒で酸化するこ
とにより炭酸ガスと水となり無臭ガスになる。一方前述
のように、加熱された触媒から排出されたガスは、何度
か再び触媒へ戻ることになる。この時、排気ガスは熱交
換され高温になっている。高温のガスが触媒へ戻るとい
うことは、潜在的に脱臭されやすいガスが脱臭行程へ戻
るので脱臭効果が高く、一方で熱ロスが少ないというこ
とである。よって、非常に効率がよくなる。 また、加熱
された触媒より排出されたガスは断熱材により放熱が抑
えられ、再び吸引されるときも高温を保ったまま脱臭手
段へ再回収されることになる。つまり、さらに熱ロスが
少なく脱臭効果も高くなる。
According to the first means of the present invention, since the storage space is provided on the discharge side of the deodorizing means, the deodorized gas does not immediately discharge to the outside air, but stays inside once. On the other hand, kitchen waste is dried by the heating means and stirring means in the drying room, and gas containing odor and water vapor is generated, but the instantaneous gas generation is not constant, so the pressure in the drying room constantly fluctuates. are doing. In other words, the generated gas repeats a reciprocating pulsation, and the gas exhausted from the deodorization process also goes out and out while repeating going in and out. Therefore, if the deodorized gas stays inside once without being immediately discharged to the outside air as described above, the gas once passed through the deodorization process is sucked into the deodorization process again before being exhausted to the outside air. It will be deodorized again. Further, since the waste gas passes through the deodorization process when it is discharged, it is deodorized at least three times, and the deodorization efficiency is increased. In addition, the gas generated when drying kitchen garbage is used as a catalyst.
It will be deodorized by the oxidation method. Such odorous gas
It is mainly an organic gas that can be oxidized by a heated catalyst.
As a result, carbon dioxide gas and water become odorless gas. On the other hand
Gas discharged from the heated catalyst
Or will return to the catalyst again. At this time, the exhaust gas
It has been replaced by high temperature. When hot gas returns to the catalyst
This means that potentially deodorizable gases return to the deodorization process.
Therefore, the deodorizing effect is high, while the heat loss is small.
And Therefore, the efficiency is extremely improved. Also heating
The heat emitted from the exhausted catalyst is suppressed by the heat insulating material.
Deodorizing hand while maintaining high temperature even when sucked again
It will be recollected to the step. In other words, further heat loss
The deodorizing effect is high.

【0012】本発明の第二の手段によれば、第一手段に
加え、貯留空間を通路で構成し、一定以上の細長い形状
としているので、通路の排出方向への拡散を極力抑える
ことができる。前述のように、通路の中のガスは往復の
脈動を繰り返しているので、排出方向への拡散が少ない
ということは通路の脱臭手段の排出部に近いガスほど脱
臭行程へ再び戻りやすく、脱臭手段の排出部から遠くて
外気に近い通路内のガスは何度も往復して脱臭され、外
気へと排出されることになるので、結果的に脱臭効率は
非常に高くなる。
[0012] According to the second means of the present invention, in addition to the first means, the storage space is constituted by a passage and is formed to have an elongated shape of a certain size or more, so that diffusion of the passage in the discharge direction can be suppressed as much as possible. . As described above, since the gas in the passage repeats reciprocating pulsation, the fact that diffusion in the discharge direction is small means that the gas closer to the discharge portion of the deodorizing means in the passage is more likely to return to the deodorizing step again, and the deodorizing means Since the gas in the passage far from the discharge portion and close to the outside air is reciprocated many times, it is deodorized and discharged to the outside air, and as a result, the deodorization efficiency is very high.

【0013】本発明の第三の手段によれば、脱臭しよう
とするガスは水蒸気が凝縮され除湿されている。水蒸気
を多量に含む臭気ガスは脱臭が困難であり、脱臭行程の
前に除湿を行うこと脱臭効率が高まることになる。一
方、前述のように乾燥室内では、蒸気が発生し圧力が高
まり、撹拌によってその圧力は変動している。その一方
で凝縮を行っているのでガスの圧力が下がる方向にな
り、その結果、乾燥室内の圧力変動が増幅されて、より
一層往復の脈動が激しくなり、脱臭行程を臭気ガスが頻
繁に出入りして脱臭されることになり、脱臭効果がさら
に高くなる。
According to the third means of the present invention, the gas to be deodorized is dehumidified by condensation of water vapor. It is difficult to deodorize an odor gas containing a large amount of water vapor, and if dehumidification is performed before the deodorization process, the deodorization efficiency is increased. On the other hand, as described above, in the drying chamber, steam is generated and the pressure increases, and the pressure fluctuates due to stirring. On the other hand, since the gas is condensed, the pressure of the gas decreases, and as a result, the pressure fluctuation in the drying chamber is amplified, the reciprocating pulsation becomes more intense, and the odorous gas frequently enters and leaves the deodorization process. As a result, the deodorizing effect is further enhanced.

【0014】[0014]

【実施例】以下、本発明の一実施例を図1に基づいて説
明する。図1において、1は乾燥室であり、内部に厨芥
をいれるゴミ容器2を配している。ゴミ容器2の内底部
には撹拌羽根3を設け、ゴミ容器2内の厨芥を撹拌する
構成である。乾燥室1の上部には蓋4を配し、蓋4に設
けたパッキンによって乾燥室1上部を密閉する構成であ
る。前記ゴミ容器2の底部の撹拌羽根3はモータ5と軸
6によって駆動回転し、厨芥を撹拌する。また、軸6と
撹拌羽根3は脱着可能であり、ゴミ容器2は撹拌羽根3
と共に乾燥室1より取り出せる構造をなしている。7は
加熱ヒータであり、ゴミ容器2を加熱し、内部の厨芥を
加熱乾燥する。
An embodiment of the present invention will be described below with reference to FIG. In FIG. 1, reference numeral 1 denotes a drying room, in which a garbage container 2 for storing kitchen waste is disposed. A stirring blade 3 is provided on the inner bottom of the trash container 2 to stir the garbage in the trash container 2. A lid 4 is arranged on the upper part of the drying chamber 1, and the upper part of the drying chamber 1 is sealed by packing provided on the lid 4. The stirring blade 3 at the bottom of the trash container 2 is driven and rotated by a motor 5 and a shaft 6 to stir the garbage. The shaft 6 and the stirring blade 3 are detachable, and the trash container 2 is
Together with the drying chamber 1. Reference numeral 7 denotes a heater for heating the trash container 2 and heating and drying the garbage inside.

【0015】8は乾燥室断熱材であり、乾燥室1の放熱
を防ぐ。9は乾燥室1とガス導入管10によって通気さ
れた凝縮部であり、内部には放熱フィン、クロスフロー
ファン(図示せず)などで構成されており、乾燥室1で
発生したガスの水蒸気を凝縮して除湿を行う。凝縮した
凝縮水は下部の凝縮水容器11に捕集される。12は脱
臭部であり、触媒加熱用ヒータ13及びハニカム状の触
媒14で構成され、前記凝縮部9で除湿された臭気ガス
がこの脱臭部12内で脱臭される。脱臭されたガスは、
一定以上の容量と一定の形状を有する貯留部を構成する
排気管15を通って、排気口16から外気へ排出され
る。17は排気管断熱材であり、排気管15の放熱を防
ぐ。
Reference numeral 8 denotes a drying room heat insulating material, which prevents the drying room 1 from radiating heat. Reference numeral 9 denotes a condensing section which is ventilated by the drying chamber 1 and the gas introduction pipe 10, and is internally constituted by radiating fins, a cross flow fan (not shown) and the like. Condensate and dehumidify. The condensed condensed water is collected in the condensed water container 11 at the lower part. Reference numeral 12 denotes a deodorizing section, which is constituted by a catalyst heating heater 13 and a honeycomb-shaped catalyst 14. The odor gas dehumidified in the condenser section 9 is deodorized in the deodorizing section 12. The deodorized gas is
The gas is discharged from the exhaust port 16 to the outside air through an exhaust pipe 15 constituting a storage part having a certain capacity or more and a certain shape. Reference numeral 17 denotes an exhaust pipe heat insulating material, which prevents the exhaust pipe 15 from radiating heat.

【0016】以下、本実施例の主要動作について、図1
に基づいて説明する。使用者がゴミ容器2に厨芥を入れ
乾燥室1に図1のような状態でセットする。このゴミ容
器2は本機器とは脱着可能であり、使用者は厨芥を本機
器まで運ぶ必要はなく、厨芥の発生する場所でこのゴミ
容器2に厨芥を投入してから本機器にセットできるので
使い勝手がよい。使用者が蓋4を閉じた後、図示してい
ないスイッチをオンすると、図示していない制御装置が
作用して、モータ5、加熱ヒータ7及び触媒加熱用ヒー
タ13に通電され、それぞれ撹拌や加熱を開始する。こ
の加熱によって厨芥が加熱され乾燥される。
Hereinafter, the main operation of the present embodiment will be described with reference to FIG.
It will be described based on. The user puts the garbage in the trash container 2 and sets it in the drying chamber 1 as shown in FIG. The garbage container 2 can be detached from the apparatus, and the user does not need to carry the garbage to the apparatus. The user can put the garbage into the garbage container 2 at a place where the garbage is generated and then set the garbage on the apparatus. Easy to use. When the user turns on a switch (not shown) after the user closes the lid 4, a control device (not shown) operates to energize the motor 5, the heater 7, and the catalyst heater 13 to stir or heat the respective components. To start. The garbage is heated and dried by this heating.

【0017】また、モータ5の駆動が軸6を介して撹拌
羽根3に伝わり回転し、厨芥を撹拌する。この撹拌によ
って厨芥が均一に乾燥される。乾燥によって生じた発生
ガスはガス導入管10を通って、凝縮部9へと導入され
る。凝縮部9では放熱フィン、クロスフローファンなど
で発生ガスを冷却(凝縮)し、除湿を行う。この時凝縮
された水は凝縮水容器11に貯まり、除湿されたガスは
脱臭部12へと導入される。ここで除湿を行わなけれ
ば、脱臭すべきガスは水蒸気を多量に含んだガスとな
り、このようなガスの脱臭は非常に困難であり、また、
かりに脱臭されても排気ガスには水蒸気が含まれたまま
であるので、屋内にこの機器を設置した場合、部屋に結
露するなどして問題が生じる。
Further, the drive of the motor 5 is transmitted to the stirring blade 3 via the shaft 6 and rotates to stir the garbage. By this stirring, the kitchen waste is uniformly dried. The generated gas generated by the drying is introduced into the condenser 9 through the gas introduction pipe 10. In the condenser 9, the generated gas is cooled (condensed) by a radiation fin, a cross flow fan, or the like, and dehumidified. The water condensed at this time is stored in the condensed water container 11, and the dehumidified gas is introduced into the deodorizing section 12. If dehumidification is not performed here, the gas to be deodorized is a gas containing a large amount of water vapor, and it is very difficult to deodorize such a gas.
Even if the exhaust gas is deodorized, the exhaust gas still contains water vapor. Therefore, when this equipment is installed indoors, a problem occurs such as dew condensation in a room.

【0018】一方、この時、乾燥室1内でおこる乾燥は
定常的なものではなく、水蒸気及び臭気を含んだガスの
発生は瞬間的には不均一なものであり、乾燥室1内の圧
力は非常に変動している。また、凝縮部9での凝縮は圧
力を下げる方向にあり、乾燥室1内の圧力変動を打ち消
すのではなく増幅することになる。つまり凝縮部9から
脱臭部12へ向かうガスは行ったり来たりの往復の脈動
を繰り返す。
On the other hand, at this time, the drying in the drying chamber 1 is not stationary, and the generation of gas containing water vapor and odor is non-uniform instantaneously. Is very variable. In addition, the condensation in the condensation section 9 is in the direction of decreasing the pressure, and the pressure fluctuation in the drying chamber 1 is amplified rather than canceled out. In other words, the gas flowing from the condenser 9 to the deodorizer 12 repeats the reciprocating pulsation back and forth.

【0019】脱臭部へ達したガスは触媒加熱用ヒータ1
3で加熱された触媒14によって、その臭気成分が脱臭
される。この臭気成分は触媒酸化方式で脱臭することが
最も好ましい。なぜなら厨芥から発生する臭気成分はほ
とんどと言っていいほど有機物であり、この有機物は酸
化すると水と二酸化炭素に分解され、無臭で無害の気体
に変わるからである。本実施例では前記触媒14の材質
として白金族金属を活性アルミナなどに担持したハニカ
ム形状のものを使用したが、特に触媒の種類を限定する
ものではない。
The gas that has reached the deodorizing section is a heater 1 for catalyst heating.
The odor component is deodorized by the catalyst 14 heated in 3. This odor component is most preferably deodorized by a catalytic oxidation method. This is because most of the odor components generated from kitchen garbage are organic substances, and when this organic substance is oxidized, it is decomposed into water and carbon dioxide, turning into odorless and harmless gas. In the present embodiment, as the material of the catalyst 14, a honeycomb-shaped catalyst having a platinum group metal supported on activated alumina or the like is used, but the type of the catalyst is not particularly limited.

【0020】また、触媒の温度も触媒の種類によって異
なるので、本発明では特に詳しく言及しないが、本実施
例では触媒加熱用ヒータ13によって加熱される触媒1
4の温度を約400〜450℃で管理を行った。
Although the temperature of the catalyst also differs depending on the type of the catalyst, it is not described in detail in the present invention. However, in this embodiment, the catalyst 1 heated by the catalyst heater 13 is used.
4 was controlled at about 400 to 450 ° C.

【0021】前述したように脱臭部12へ導入されるガ
スは、往復の脈動を繰り返している。よって、脱臭部1
2から排出されるガスも出たり入ったりの排出と吸引を
繰り返す。もし、脱臭部12の下流側がすぐに外気であ
ると、脱臭部12から排出されたガスはその慣性で外気
に混ざってしまい、次に吸引されるときには、外気を吸
引して、脱臭されるガスは一度しか触媒14を通らず、
吸引時には脱臭する必要の無い外気を触媒14内に取り
入れてしまう。この脱臭部12から、外気に触れる排気
口16までの間に一定量以上の容積の空間を設けること
は、一度脱臭部12を出たガスを再び脱臭部12へと戻
して、再びさらに触媒酸化反応を起こし脱臭するため
に、非常に有効な手段である。つまり、例えば99.9
%の脱臭浄化率を求められた時、一度の脱臭部の通過で
その浄化率を達成するよりも、排出、吸引、再排出とい
った3度の通過では一度の通過で90%の脱臭浄化率が
99.9%を達成できるわけである((1−0.9)3
=1−0.999)。
As described above, the gas introduced into the deodorizing section 12 repeats reciprocating pulsation. Therefore, deodorizing section 1
The gas exhausted from 2 also repeats exhausting and sucking in and out. If the downstream side of the deodorizing section 12 is immediately outside air, the gas discharged from the deodorizing section 12 will be mixed with the outside air due to its inertia. Passes through the catalyst 14 only once,
At the time of suction, outside air that does not need to be deodorized is taken into the catalyst 14. Providing a space having a certain volume or more between the deodorizing section 12 and the exhaust port 16 that comes into contact with the outside air can be achieved by returning the gas that has once exited the deodorizing section 12 to the deodorizing section 12 and further oxidizing the catalyst again. It is a very effective means for initiating the reaction and deodorizing. That is, for example, 99.9
When a deodorization purification rate of 90% is required, 90% of the deodorization purification rate can be achieved in one pass in three passes such as discharge, suction, and re-discharge, rather than achieving the purification rate in one pass through the deodorization section. 99.9% can be achieved ((1-0.9) 3
= 1-0.999).

【0022】本実施例では、脱臭部12と排気口16の
間に排気管15を設けた。この排気管15の内容積は5
0cm3あり、それに対し乾燥室は10litterである。各
種実験の結果、脱臭部12から瞬間的に排出されるガス
の最大量は、約40cm3であり、乾燥室1の約1/25
0であった。また乾燥室の容積を変えて行っても、ガス
の最大排出量は乾燥室の約1/250倍分であった。よ
って、脱臭行程終了から外気までの通路の容積が、乾燥
室の容積の1/250倍以上あれば、往復する排気ガス
をうまく脱臭部へ再回収でき、脱臭効率が上がり有効な
手段といえる。
In this embodiment, an exhaust pipe 15 is provided between the deodorizing section 12 and the exhaust port 16. The inner volume of the exhaust pipe 15 is 5
There is 0 cm 3 , whereas the drying room is 10 litters. As a result of various experiments, the maximum amount of gas instantaneously discharged from the deodorizing section 12 is about 40 cm 3, which is about 1/25 that of the drying chamber 1.
It was 0. Even when the drying chamber was changed in volume, the maximum gas emission was about 1/250 times that of the drying chamber. Therefore, if the volume of the passage from the end of the deodorization process to the outside air is 1/250 or more times the volume of the drying chamber, the reciprocating exhaust gas can be successfully collected in the deodorizing section, and the deodorizing efficiency can be improved and it can be said that this is an effective means.

【0023】前述したように本発明では脱臭手段とし
て、触媒酸化方式を用いている。これは加熱され活性化
された触媒が臭気成分との接触により臭気成分を酸化分
解するわけであるが、ここで重要なのは触媒の温度を活
性化温度以上に保つことである。前述のように本発明で
は、脱臭部12を出たガスが効率よく戻る構成を成して
いる。この時、このガスは加熱された触媒により熱交換
され高温を保っている。高温のガスが再び脱臭行程に戻
るということは、加熱された触媒を冷やさないことであ
り、もしこの時、低温の外気が脱臭不12に戻れば触媒
は冷やされてしまい、触媒の出口側の活性が落ちてしま
い、それだけ脱臭効率が下がってしまう。つまり、脱臭
部に触媒酸化方式を用いて、脱臭部を出たガスが効率よ
く戻る構成を併用するということは非常に有効な手段と
いえ、脱臭効率と熱効率を上昇させることになる。
As described above, in the present invention, a catalytic oxidation method is used as a deodorizing means. This means that the heated and activated catalyst oxidizes and decomposes the odor component upon contact with the odor component, but it is important here to keep the temperature of the catalyst at or above the activation temperature. As described above, the present invention has a configuration in which the gas exiting the deodorizing section 12 returns efficiently. At this time, this gas exchanges heat with the heated catalyst and maintains a high temperature. Returning the hot gas to the deodorization step again means not cooling the heated catalyst. At this time, if the low-temperature outside air returns to the deodorizing state 12, the catalyst is cooled and the catalyst exit side is removed. The activity decreases, and the deodorization efficiency decreases accordingly. In other words, it is very effective to use a catalytic oxidation method in the deodorizing section and efficiently return the gas from the deodorizing section together, which increases the deodorizing efficiency and the thermal efficiency.

【0024】逆に、触媒が冷えにくいということは、触
媒を必要以上に高温に保たなくても良いということであ
る。一般的に触媒を構成する担体は熱劣化を起こすもの
であり、温度が高いほどその劣化速度は指数的に大きく
なる。つまり、本発明のように触媒を冷えにくい構成に
するということは、触媒の寿命を長くすることになり、
長期にわたって高い脱臭効果が実現でき、有効な手段と
いえる。
Conversely, the fact that the catalyst is difficult to cool means that the catalyst does not have to be kept at an excessively high temperature. Generally, the carrier constituting the catalyst causes thermal deterioration, and the higher the temperature, the exponentially the deterioration rate increases. In other words, making the catalyst hard to cool down as in the present invention means extending the life of the catalyst,
It can be said to be an effective means that a high deodorizing effect can be realized over a long period.

【0025】また本実施例では、排気管15の内径を1
5mm、排気管の長さを283mmとして、ある程度細長く
した。これはさらに脱臭効果を高める意味で非常に有効
な手段といえる。なぜなら、細長くすることにより、脱
臭行程終了から外気までの通路の長さが長くなり、排出
方向へのガス拡散が抑えられ、それだけ脱臭行程に近い
ガスほど外気へ達し難く、往復の脈動によって再び何度
も脱臭行程に戻りやすく、また外気に近いガスほど何度
も脱臭されているので、外気へと排出されるガスは著し
く浄化されいて、脱臭効率が飛躍的に高くなるからであ
る。また、排出方向の拡散を抑えるということは、排出
方向の熱ロスを抑えることであり、脱臭行程を行き来す
るガスの温度がより高温に保たれたまま脱臭されること
になり、さらに脱臭効果が上がるといえる。また、前述
した理由から触媒の寿命をさらに長くすることにもな
る。
In this embodiment, the inner diameter of the exhaust pipe 15 is set to 1
The length was set to 5 mm, and the length of the exhaust pipe was set to 283 mm, so that it was elongated to some extent. This can be said to be a very effective means in order to further enhance the deodorizing effect. The reason for this is that by making it slender, the length of the passage from the end of the deodorization process to the outside air is lengthened, and gas diffusion in the discharge direction is suppressed. This is because the gas easily returns to the deodorization process, and the gas closer to the outside air is deodorized many times, so that the gas discharged to the outside air is significantly purified, and the deodorization efficiency is dramatically increased. In addition, suppressing diffusion in the discharge direction means suppressing heat loss in the discharge direction, which means that the gas that flows back and forth in the deodorization process is deodorized while being kept at a higher temperature. It can be said that it goes up. Further, for the above-mentioned reason, the life of the catalyst is further extended.

【0026】この排気管15の形状は本実施例では、内
径に対し長さが18倍以上あるが、各種実験によると、
8倍程度からその効果が現れるという結果を得た。この
倍率、つまり長さは長い方が脱臭効果が高くて良いが、
しかしあまり長くすれば、排出方向への抵抗が大きくな
り、乾燥室上部の蓋より発生ガスがリークするという問
題が生じるので、必要以上長くすることはない。しかし
その長さの上限は乾燥室の密閉度によって大きく異なる
ので、本発明ではその長さ(倍率)の上限に付いて明記
するところでない。
In this embodiment, the shape of the exhaust pipe 15 is at least 18 times the inner diameter, but according to various experiments,
The result that the effect appears from about 8 times was obtained. This magnification, that is, the longer the length, the higher the deodorizing effect,
However, if the length is too long, the resistance in the discharge direction increases, and a problem arises in that generated gas leaks from the lid at the top of the drying chamber. Therefore, the length is not increased more than necessary. However, since the upper limit of the length greatly varies depending on the degree of sealing of the drying chamber, the present invention does not specify the upper limit of the length (magnification).

【0027】また排気管15の周囲には排気管断熱材1
7を施した。これは、排気管15の放熱を抑え、その中
のガスの温度を高温に保つためのものであり、こうする
構成によって、前述のように、加熱された触媒をさらに
冷え難くして、脱臭効果をさらに高めるものであって、
触媒寿命にも良いことから、非常に有効な手段といえ
る。
The exhaust pipe heat insulating material 1 is provided around the exhaust pipe 15.
7 was given. This is to suppress the heat radiation of the exhaust pipe 15 and keep the temperature of the gas therein at a high temperature. With such a configuration, as described above, the heated catalyst is more difficult to cool, and the deodorizing effect is obtained. Is further enhanced,
This is a very effective means because of its good catalyst life.

【0028】このようにして排気口16を出たガスは、
臭いは殆ど無臭に近く、THC(総炭化水素;有機系の
ガス成分つまり臭気成分)がメタン換算で1ppm以下
であり、一般の室内空気レベルより下回った結果を得
た。
The gas leaving the exhaust port 16 in this manner is
The odor was almost odorless, and the result was that THC (total hydrocarbons; organic gas components, that is, odor components) was 1 ppm or less in terms of methane, which was lower than a general indoor air level.

【0029】以上のようにして、脱臭しながらの乾燥を
終えると、図示していない温度センサーが乾燥を検知
し、制御装置によってスイッチが切れる。使用者はその
後、前記蓋4を開け、前記ゴミ容器2をとりだし、内部
の乾燥した厨芥を廃棄すれば良い。この乾燥した厨芥
は、もとの厨芥に対して厨芥の種類によって多少誤差は
あるが20%の重量であり、水分がないので腐敗するこ
とがなく体積も減少しているので、本来不快だった厨芥
の取扱いが楽になる。また、凝縮水容器11に貯まった
凝縮水は適宜、下水へ廃棄するだけで良く、煩雑で面倒
だった厨芥の管理が衛生的で簡便なものとなる。
As described above, when the drying while deodorizing is completed, the temperature sensor (not shown) detects the drying, and the switch is turned off by the control device. Then, the user may open the lid 4, take out the garbage container 2, and discard the dried garbage inside. This dried garbage was originally unpleasant because it was 20% of the weight of the original garbage, depending on the type of garbage, but weighed 20%. Handling of kitchen waste becomes easier. Further, the condensed water stored in the condensed water container 11 only needs to be appropriately discarded to the sewage, and the complicated and troublesome management of kitchen waste is sanitary and simple.

【0030】[0030]

【発明の効果】このように本発明の第一の手段によれ
、脱臭効果の高い、臭いの問題の少ない厨芥処理装置
を実現するものであり、屋内設置の可能なものにしてい
る。
As described above , according to the first means of the present invention,
For example , a garbage disposal apparatus having a high deodorizing effect and a small odor problem can be realized, and can be installed indoors.

【0031】また本発明の第二の手段によれば、第一の
手段に加え、さらに脱臭効果の高い、臭いの問題の少な
い厨芥処理装置を実現するものであり、屋内設置の可能
なものにしている。
According to a second means [0031] The present invention, pressurized example the first means, high deodorizing effect in further, which realizes a garbage processing device less odor problems, possible indoor installation What you are doing.

【0032】また本発明の第三の手段によれば、第一の
手段または第二の手段に加え、さらに脱臭効果の高い、
処理中の臭いの問題の少ない機器を実現するものであ
り、屋内設置の可能性を高めるものである。一方、除湿
を行っているので排気ガスに含まれる水蒸気も極力抑え
られたものになっているので、屋内においても結露の問
題も少なく、さらに屋内設置の可能性を高めるものであ
る。
According to a third means [0032] The present invention, pressurized example the first means or the second means, high deodorizing effect in further,
The present invention realizes a device with less odor problem during processing, and enhances the possibility of indoor installation. On the other hand, since the dehumidification is performed, the water vapor contained in the exhaust gas is suppressed as much as possible, so that there is little problem of dew condensation even indoors, and the possibility of indoor installation is further improved.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施例の厨芥処理装置を示す断面図FIG. 1 is a cross-sectional view showing a kitchen waste disposal apparatus according to one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 乾燥室 3 撹拌羽根(撹拌手段) 7 加熱ヒータ(加熱手段) 9 凝縮部(凝縮手段) 12 脱臭部(脱臭手段) 13 触媒加熱用ヒータ 14 触媒 15 排気管(貯留部) 17 排気管断熱材(断熱材) DESCRIPTION OF SYMBOLS 1 Drying room 3 Stirring blade (stirring means) 7 Heater (heating means) 9 Condensing part (condensing means) 12 Deodorizing part (deodorizing means) 13 Heater for catalyst 14 Catalyst 15 Exhaust pipe (storage part) 17 Exhaust pipe heat insulating material (Insulation material)

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平5−319504(JP,A) 特開 平5−146702(JP,A) 特開 平6−159935(JP,A) 特開 平5−39972(JP,A) (58)調査した分野(Int.Cl.7,DB名) B09B 3/00 B09B 3/00 303 B09B 5/00 F26B 1/00 - 25/22 ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-5-319504 (JP, A) JP-A-5-146702 (JP, A) JP-A-6-159935 (JP, A) JP-A-5-159935 39972 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B09B 3/00 B09B 3/00 303 B09B 5/00 F26B 1/00-25/22

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 厨芥を乾燥させる加熱手段と、乾燥させ
る厨芥を収納する乾燥室と、前記乾燥室内の厨芥を撹拌
する撹拌手段と、厨芥の乾燥中に発生するガスを脱臭す
る脱臭手段とを備え、前記脱臭手段から排出されるガス
が外気へ排出されるまでの間に一定量以上の貯留空間を
設けるとともに、前記貯留空間の容積を前記乾燥室の容
積の1/250倍以上とし、脱臭手段に触媒酸化方式を
用い、脱臭手段の排出部から外気に至るまでの貯留空間
に断熱材を設けた厨芥処理装置。
1. A heating means for drying garbage, a drying chamber for storing garbage to be dried, a stirring means for stirring the garbage in the drying chamber, and a deodorizing means for deodorizing gas generated during drying of the garbage. Providing a storage space of a certain amount or more before the gas discharged from the deodorizing means is discharged to the outside air, and making the volume of the storage space 1/250 times or more the volume of the drying chamber , Means of catalytic oxidation
Storage space from the discharge part of the deodorizing means to the outside air
Garbage disposal equipment with heat insulating material .
【請求項2】 貯留空間を脱臭手段の排出部から外気に
至るまでの通路で構成し、この通路の長さを前記通路の
任意の断面の短径の8倍以上とした請求項1記載の厨芥
処理装置。
2. The storage space according to claim 1, wherein the storage space is constituted by a passage from the discharge portion of the deodorizing means to the outside air, and the length of the passage is at least eight times the minor diameter of an arbitrary cross section of the passage. Garbage processing equipment.
【請求項3】 脱臭の前段階にガス中に含まれる水蒸気
を凝縮して除湿する凝縮手段を設けた請求項1または2
記載の厨芥処理装置。
3. A condensing means for condensing water vapor contained in a gas and dehumidifying the gas before deodorization.
A garbage disposal device as described in the above.
JP18458394A 1994-08-05 1994-08-05 Garbage processing equipment Expired - Fee Related JP3240844B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18458394A JP3240844B2 (en) 1994-08-05 1994-08-05 Garbage processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18458394A JP3240844B2 (en) 1994-08-05 1994-08-05 Garbage processing equipment

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2001216364A Division JP2002102825A (en) 2001-07-17 2001-07-17 Garbage processing equipment

Publications (2)

Publication Number Publication Date
JPH0849975A JPH0849975A (en) 1996-02-20
JP3240844B2 true JP3240844B2 (en) 2001-12-25

Family

ID=16155754

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18458394A Expired - Fee Related JP3240844B2 (en) 1994-08-05 1994-08-05 Garbage processing equipment

Country Status (1)

Country Link
JP (1) JP3240844B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108731396B (en) * 2018-05-07 2020-06-16 芜湖良匠机械制造有限公司 Heated air circulation type drying device for glass substrate
CN110207474B (en) * 2019-05-14 2020-10-13 池州中瑞化工有限公司 A chemical raw material heater

Also Published As

Publication number Publication date
JPH0849975A (en) 1996-02-20

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