JPH0592180A - Apparatus and method for treating garbage - Google Patents

Apparatus and method for treating garbage

Info

Publication number
JPH0592180A
JPH0592180A JP3099117A JP9911791A JPH0592180A JP H0592180 A JPH0592180 A JP H0592180A JP 3099117 A JP3099117 A JP 3099117A JP 9911791 A JP9911791 A JP 9911791A JP H0592180 A JPH0592180 A JP H0592180A
Authority
JP
Japan
Prior art keywords
drying
food waste
dryer
air
garbage
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.)
Granted
Application number
JP3099117A
Other languages
Japanese (ja)
Other versions
JP3485189B2 (en
Inventor
Koji Nakayama
仲山浩司
Hidehiro Sakate
坂手英博
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.)
SEKIYU SANGYO KASSEIKA CENTER
Tonen General Sekiyu KK
Japan Petroleum Energy Center JPEC
Original Assignee
SEKIYU SANGYO KASSEIKA CENTER
Petroleum Energy Center PEC
Tonen Corp
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 SEKIYU SANGYO KASSEIKA CENTER, Petroleum Energy Center PEC, Tonen Corp filed Critical SEKIYU SANGYO KASSEIKA CENTER
Priority to JP09911791A priority Critical patent/JP3485189B2/en
Publication of JPH0592180A publication Critical patent/JPH0592180A/en
Application granted granted Critical
Publication of JP3485189B2 publication Critical patent/JP3485189B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To reduce the volume and amount of garbage while preventing the spoilage thereof and to reutilize the garbage as a raw material for fertilizer or feed. CONSTITUTION:A garbage treatment apparatus has a garbage grinding and dehydrating device 3, a dryer 4 drying the ground and dehydrated garbage, the drying blow pipe 15 and drying exhaust pipe 16 connected to the dryer 4 and a heat exchanger 10 for heating the air flowing through the drying blow pipe 15 by the air heated by a burner 11 and combustion quantity is controlled on the basis of the temp. in the drying blow pipe 15 and the water activity of garbage is controlled on the basis of the temp. in the drying exhaust pipe 16 to grasp a drying state.

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、食品工場、ホテル、飲
食店、集合住宅等から出る生ごみの減容化、減量化を図
るとともに生ごみの腐敗を防止し、また、生ごみを肥
料、飼料等の原料に再利用可能にするための生ごみ処理
装置および処理方法に関する。
[Field of Industrial Application] The present invention aims to reduce the volume and quantity of food waste produced from food factories, hotels, restaurants, apartments, etc., prevent spoilage of the food waste, and fertilize the food waste. The present invention relates to a food waste processing device and a processing method for making it reusable as a raw material such as feed.

【0002】[0002]

【従来の技術】近年、食品工場、ホテル、飲食店、集合
住宅等から出る生ごみは、ユーザ側においては、腐敗の
発生、ごみ置き場面積の増加、処理業者の引き取り手数
量の増加等の問題を有し、処理業者側においては、収
集、運搬コストの増大、人手不足等の問題を有し、自治
体側においては焼却炉及び埋立地対策等の問題を有し、
生ごみの減容化、減量化が大きな課題となっている。そ
のために、従来、簡単な構造によりユーザ側で処理する
装置として、例えば、生ごみを粉砕、脱水、袋詰めにす
ることにより、衛生的な手段でかつ減容化する装置が開
発されている。
2. Description of the Related Art In recent years, food waste generated from food factories, hotels, restaurants, multi-dwelling houses, etc. has caused problems on the user side such as the occurrence of decay, an increase in the garbage storage area, and an increase in the amount of waste collected by processors. Yes, the treatment company side has problems such as collection, transportation cost increase, labor shortage, etc., and the local government side has problems such as incinerator and landfill measures,
Reducing the volume and quantity of raw garbage has become a major issue. For this reason, conventionally, as a device to be processed by a user with a simple structure, for example, a device for crushing, dehydrating, and bagging food waste has been developed which is a hygienic means and reduces the volume.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記従
来の生ごみ処理装置においては、生ごみ中の水分の存在
のために、重量が重く輸送コストが減少しないという問
題や、生ごみが腐敗しやすいために環境的に悪影響を与
えるという問題を有している。また、これらの問題のた
めに、肥料、飼料等の原料に再利用可能にすることが困
難であった。
However, in the above-mentioned conventional food waste processing apparatus, the weight of the food waste is heavy and the transportation cost is not reduced due to the presence of water in the food waste, and the food waste is easily decomposed. Therefore, there is a problem that the environment is adversely affected. Further, because of these problems, it has been difficult to make them reusable as raw materials such as fertilizers and feeds.

【0004】本発明は上記問題を解決するものであっ
て、生ごみの減容化、減量化を図るとともに腐敗を防止
し、また、肥料、飼料等の原料に再利用可能にするため
の生ごみ処理装置および処理方法を提供することを目的
とする。
The present invention solves the above problems and aims to reduce the volume and amount of food waste, prevent spoilage, and reuse raw materials for fertilizers, feeds, etc. It is an object to provide a waste treatment device and a treatment method.

【0005】[0005]

【課題を解決するための手段】そのために本発明の生ご
み処理装置は、生ごみを破砕脱水する破砕脱水装置3
と、破砕脱水された生ごみを乾燥する乾燥機4と、乾燥
機4に接続される乾燥用送風管15および乾燥用排出管
16と、バーナー11により加熱された空気により乾燥
用送風管15を流れる空気を加熱するための熱交換器1
0とを有することを特徴とする。
To this end, the apparatus for treating food waste according to the present invention is a crushing and dehydrating device 3 for crushing and dehydrating food waste.
The dryer 4 for drying the crushed and dehydrated food waste, the drying air blow pipe 15 and the drying air discharge pipe 16 connected to the dryer 4, and the drying air blow pipe 15 by the air heated by the burner 11. Heat exchanger 1 for heating flowing air
It is characterized by having 0 and.

【0006】また、本発明の生ごみ処理方法は、生ごみ
を破砕脱水する破砕脱水装置3と、破砕脱水された生ご
みを乾燥する乾燥機4と、乾燥機4に接続される乾燥用
送風管15および乾燥用排出管16と、バーナー11に
より加熱された空気により乾燥用送風管15を流れる空
気を加熱するための熱交換器10とを有し、乾燥用送風
管15内の温度で燃焼量を制御し、乾燥用排出管16内
の温度により生ごみの水分活性を制御し乾燥状態を把握
することを特徴とする。
[0006] The method of treating food waste according to the present invention comprises a crushing / dewatering device 3 for crushing and dehydrating food waste, a dryer 4 for drying the crushed and dehydrated food waste, and a blowing air for drying connected to the dryer 4. It has a pipe 15 and a discharge pipe 16 for drying, and a heat exchanger 10 for heating the air flowing through the drying blower pipe 15 by the air heated by the burner 11, and burns at the temperature in the drying blower pipe 15. It is characterized by controlling the amount and controlling the water activity of food waste by the temperature in the drying discharge pipe 16 to grasp the dry state.

【0007】なお、上記構成に付加した番号は、理解を
容易にするために図面と対比させるためのもので、これ
により本発明の構成が何ら限定されるものではない。
It should be noted that the numbers added to the above configuration are for comparison with the drawings for easy understanding, and the configuration of the present invention is not limited by this.

【0008】[0008]

【作用】本発明においては、例えば、図1に示すよう
に、生ごみは、破砕脱水装置3にて破砕脱水され乾燥機
4内に送られ、一方、送風用ファン12により外気は、
燃焼用送風管14を経てバーナー11に送られると共
に、乾燥用送風管15を経て熱交換器10に送られ、バ
ーナー11にて加熱された高温空気は、排気管17を経
て熱交換器10に送られ、乾燥用送風管15を流れる空
気を加熱し、加熱された空気を乾燥容器5内に送り生ご
みを加熱し、生ごみの水分を吸収した湿り空気は、乾燥
用排出管16を経てバーナー11に送られ燃焼用空気と
して用いられる。そして、水分活性をある所定値まで乾
燥するために、乾燥用送風管15における温度検出器T
C1の温度で燃焼量を制御し、乾燥用排出管16におけ
る温度検出器TC2の温度で生ごみの水分活性を制御し
乾燥状態を把握するものである。
In the present invention, for example, as shown in FIG. 1, raw garbage is crushed and dehydrated by the crushing and dehydrating device 3 and sent to the dryer 4, while the outside air is blown by the blower fan 12
The high-temperature air sent to the burner 11 via the combustion blower pipe 14 and to the heat exchanger 10 via the drying blower pipe 15 and heated by the burner 11 is sent to the heat exchanger 10 via the exhaust pipe 17. The air sent and heated in the drying blower pipe 15 is heated, the heated air is sent into the drying container 5 to heat the food waste, and the moist air which has absorbed the moisture of the food waste passes through the drying discharge pipe 16. It is sent to the burner 11 and used as combustion air. Then, in order to dry the water activity to a predetermined value, the temperature detector T in the drying blower pipe 15
The amount of combustion is controlled at the temperature of C1 and the water activity of the food waste is controlled at the temperature of the temperature detector TC2 in the drying discharge pipe 16 to grasp the dry state.

【0009】[0009]

【実施例】以下本発明の実施例を図面を参照しつつ説明
する。図1は本発明の生ごみ処理装置の一実施例を示す
構成図である。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a block diagram showing an embodiment of the food waste processing apparatus of the present invention.

【0010】図中、1は生ごみ投入用のホッパー、3は
破砕脱水装置、4は乾燥機で乾燥容器5の周囲に熱風通
路6を有し、内部にモータにより駆動される回転軸21
と回転軸21に設けられる切断刃22とを有する攪拌装
置7を備えている。8は開閉装置、9はごみ収納容器ま
たは収集袋、10は熱交換器、11はバーナー、12は
送風用ファンである。
In the figure, 1 is a hopper for throwing food waste, 3 is a crushing dehydrator, 4 is a dryer having a hot air passage 6 around a drying container 5, and a rotary shaft 21 driven by a motor therein.
And a stirring device 7 having a cutting blade 22 provided on the rotary shaft 21. Reference numeral 8 is an opening / closing device, 9 is a waste container or collection bag, 10 is a heat exchanger, 11 is a burner, and 12 is a blower fan.

【0011】送風用ファン12は、燃焼用送風管14に
よりバーナー11に接続されると共に、乾燥用送風管1
5により熱交換器10を経て乾燥容器5の下部に接続さ
れる。乾燥容器5の上部とバーナー11との間には、乾
燥用排出管16が接続され、バーナー11に接続されて
いる。バーナー11の排気管17は熱交換器10を経て
排気されるように接続され、また、乾燥用送風管15と
乾燥用排出管16には、それぞれ温度検出器TC1、T
C2が配設されている。
The blower fan 12 is connected to the burner 11 by a combustion blower pipe 14 and also the drying blower pipe 1
5 is connected to the lower part of the drying container 5 via the heat exchanger 10. A discharge pipe 16 for drying is connected between the upper portion of the drying container 5 and the burner 11, and is connected to the burner 11. The exhaust pipe 17 of the burner 11 is connected so as to be exhausted via the heat exchanger 10, and the drying blower pipe 15 and the drying discharge pipe 16 are respectively provided with temperature detectors TC1 and T1.
C2 is provided.

【0012】上記構成からなる本発明の生ごみ処理方法
について説明する。生ごみは、ホッパー1に投入され破
砕脱水装置3にて破砕脱水される。次に生ごみは乾燥機
4内に送られ、乾燥容器5内で攪拌装置7により攪拌さ
れる。乾燥容器5内で乾燥された生ごみは、開閉装置8
を開くことによりごみ収納容器または収集袋9に収納さ
れる。
The food waste processing method of the present invention having the above-mentioned structure will be described. The garbage is put into the hopper 1 and crushed and dehydrated by the crushing and dehydrating apparatus 3. Next, the food waste is sent into the dryer 4 and stirred by the stirring device 7 in the drying container 5. The food waste dried in the drying container 5 is opened and closed by the opening / closing device 8
The container is stored in the garbage container or the collection bag 9 by opening.

【0013】一方、送風用ファン12により外気は、燃
焼用送風管14を経てバーナー11に送られると共に、
乾燥用送風管15を経て熱交換器10に送られる。バー
ナー11にて加熱された高温空気は、排気管17を経て
熱交換器10に送られ、乾燥用送風管15を流れる空気
を加熱し、加熱された空気を乾燥容器5内に送る。この
高温空気は、乾燥容器5内で生ごみと接触することによ
り断熱冷却され、定常状態では乾燥機4の出口空気温度
は一定となる。生ごみが加熱され水分活性が低下すると
共に乾燥機4の出口空気温度は上昇し、生ごみの水分を
吸収した湿り空気は、乾燥用排出管16を経てバーナー
11に送られ燃焼用空気として用いられると共に、空気
中に含まれる臭気は殆どバーナー11により加熱分解さ
れた後、外部に排出される。なお、排気系に脱臭装置を
設け、排気を脱臭装置にて脱臭させるようにしてもよ
い。
On the other hand, the outside air is sent by the blower fan 12 to the burner 11 through the combustion blower pipe 14, and
It is sent to the heat exchanger 10 via the drying blower pipe 15. The high-temperature air heated by the burner 11 is sent to the heat exchanger 10 via the exhaust pipe 17, heats the air flowing through the drying blast pipe 15, and sends the heated air into the drying container 5. The hot air is adiabatically cooled by coming into contact with food waste in the drying container 5, and the outlet air temperature of the dryer 4 becomes constant in a steady state. The food waste is heated to lower the water activity, the outlet air temperature of the dryer 4 rises, and the moist air that has absorbed the water content of the food waste is sent to the burner 11 via the discharge pipe 16 for drying and used as combustion air. At the same time, most of the odor contained in the air is decomposed by heating by the burner 11 and then discharged to the outside. Note that a deodorizing device may be provided in the exhaust system so that the exhaust gas is deodorized by the deodorizing device.

【0014】ところで、生ごみは各種食品の混合物であ
り、その腐敗、臭気発生の要因は、各食品毎の水分活性
aw により異なる。ここで水分活性awは、 aw =食品の示す水蒸気圧/空気の飽和水蒸気圧 である。この水分活性aw を0.2〜0.6程度にする
ように乾燥するのがよいとされている。水分活性が少な
すぎると脂質の酸化により変質が促進されるからであ
る。従って、水分活性をある所定値となるように乾燥す
るために、本発明においては、乾燥用送風管15におけ
る温度検出器TC1の温度で燃焼量を制御し、乾燥用排
出管16における温度検出器TC2の温度で乾燥状態を
把握することを特徴としている。
By the way, the food waste is a mixture of various foods, and the factors of spoilage and odor generation thereof differ depending on the water activity aw of each food. Here, the water activity aw is aw = water vapor pressure of food / saturated water vapor pressure of air. It is said that it is preferable to dry so that the water activity aw becomes about 0.2 to 0.6. This is because if the water activity is too low, the deterioration of the lipid is promoted by the oxidation of the lipid. Therefore, in order to dry the water activity to a predetermined value, in the present invention, the combustion amount is controlled by the temperature of the temperature detector TC1 in the drying blower pipe 15, and the temperature detector in the drying discharge pipe 16 is controlled. The feature is that the dry state is grasped at the temperature of TC2.

【0015】これを図2により説明する。図2は湿り空
気線図を示し、tは乾球温度℃、xは絶対湿度、ψは相
対湿度を示している。
This will be described with reference to FIG. FIG. 2 shows a moist air diagram, where t is the dry-bulb temperature ° C, x is the absolute humidity, and ψ is the relative humidity.

【0016】生ごみの水分活性を0.3まで乾燥するの
であれば、乾燥容器5から排出される乾燥用排出管16
内の湿り空気の相対湿度を30%にすればよい。例え
ば、外気の温度が30℃、相対湿度が80%(図のA
点)とすれば、これを熱交換器10で等絶対湿度線Bに
沿って120℃まで加熱し(図のC点)、乾燥容器5内
では、断熱冷却線Dにそって冷却され定常状態では40
℃のE点で飽和空気となる。生ごみが加熱され水分活性
が低下すると、出口空気温度は上昇し相対湿度が30%
と交わる点Fの温度62℃が、乾燥用排出管16におけ
る温度検出器TC2の温度となる。すなわち、生ごみの
水分活性を0.3とするには、温度検出器TC2の温度
が62℃となるように、バーナー11の燃焼量を温度検
出器TC1の温度で制御すればよいことになる。
If the water activity of food waste is to be dried up to 0.3, the discharge pipe 16 for drying is discharged from the drying container 5.
The relative humidity of the moist air inside may be set to 30%. For example, the temperature of outside air is 30 ° C and the relative humidity is 80% (A in the figure
Point), this is heated to 120 ° C. along the iso-absolute humidity line B in the heat exchanger 10 (point C in the figure), and is cooled along the adiabatic cooling line D in the drying container 5 in a steady state. Then 40
It becomes saturated air at point E in ° C. When food waste is heated and the water activity decreases, the outlet air temperature rises and the relative humidity becomes 30%.
The temperature of 62 ° C. at the point F intersecting with the temperature becomes the temperature of the temperature detector TC2 in the drying discharge pipe 16. That is, in order to set the water activity of raw garbage to 0.3, the combustion amount of the burner 11 should be controlled by the temperature of the temperature detector TC1 so that the temperature of the temperature detector TC2 becomes 62 ° C. ..

【0017】図3および図4は本発明の生ごみ処理装置
の他の実施例を示し、図3は乾燥機用のファン12と燃
焼用ファン12´を別々に設けた例を示し、図4はバー
ナー11への燃焼用空気を乾燥機4のみから送る例を示
している。
3 and 4 show another embodiment of the food waste processing apparatus of the present invention, FIG. 3 shows an example in which a fan 12 for a dryer and a combustion fan 12 'are provided separately, and FIG. Shows an example in which combustion air to the burner 11 is sent only from the dryer 4.

【0018】図5、図6及び図7は、図1の実施例にお
ける実験結果を示している。図5は乾燥機入口温度と熱
効率との関係を示している。ここで言う熱効率とは、乾
燥機入口における全熱量に対する乾燥機出口における蒸
発潜熱量の比である。これによれば、乾燥機入口温度が
100〜300℃、好ましくは200℃程度で熱効率が
高く、従って、乾燥時間が早くなることが判明した。温
度を高くすると熱効率が低下する理由は、壁面からの熱
損失が多くなるためである。
FIGS. 5, 6 and 7 show the experimental results in the embodiment of FIG. FIG. 5 shows the relationship between the dryer inlet temperature and the thermal efficiency. The thermal efficiency here is the ratio of the latent heat of vaporization at the dryer outlet to the total heat at the dryer inlet. According to this, it was found that the thermal efficiency is high when the dryer inlet temperature is 100 to 300 ° C., preferably about 200 ° C., and therefore the drying time is shortened. The reason why the thermal efficiency decreases with increasing temperature is that the heat loss from the wall surface increases.

【0019】図6は乾燥容器5の容積当りの風量と熱効
率との関係を示し、これによれば、容積当りの風量(m
3 /hm3 )が1.2×103 〜3.0×103 、好ま
しくは1.7×103 程度で熱効率が高いことが判明し
た。
FIG. 6 shows the relationship between the air volume per volume of the drying container 5 and the thermal efficiency. According to this, the air volume per volume (m
It has been found that the thermal efficiency is high when 3 / hm 3 ) is 1.2 × 10 3 to 3.0 × 10 3 , preferably about 1.7 × 10 3 .

【0020】図7は攪拌回転数と乾燥機熱交換効率及び
電動機出力との関係を示し、これによれば、攪拌回転数
が60rpm以下になると熱交換効率が低下することが
判明した。攪拌回転数を上げると電動機出力も増大する
ので、電動機の容量に合わせて攪拌回転数を60rpm
以上とすることが良い。
FIG. 7 shows the relationship between the agitation rotation speed, the dryer heat exchange efficiency and the motor output, and it was found that the heat exchange efficiency decreases when the agitation rotation speed becomes 60 rpm or less. If the stirring speed is increased, the motor output also increases, so adjust the stirring speed to 60 rpm according to the capacity of the motor.
It is good to be above.

【0021】その他種々の実験の結果、生ごみとして残
飯の乾燥が最も困難であることが判明した。これは、残
飯を乾燥機内に入れて攪拌すると、残飯が餅状又は糊状
となって乾燥機内面に固着してしまったり、表面のみが
焦げ付いてしまい内部が乾燥できなくなってしまうため
である。そこで、前記した乾燥機出口温度を検出して乾
燥状態を把握する制御を採用し、かつ、乾燥機出口温度
を見ながら少量ずつ分割投入する方法を試みた。
As a result of various other experiments, it was found that it is the most difficult to dry the leftover food as raw garbage. This is because when the leftover rice is put in the dryer and stirred, the leftover rice becomes a rice cake-like or pasty-like substance and sticks to the inner surface of the dryer, or only the surface is scorched so that the inside cannot be dried. Therefore, an attempt was made to adopt the above-mentioned control for detecting the dryer outlet temperature and grasping the dried state, and to carry out the stepwise addition while watching the dryer outlet temperature.

【0022】表1は生ごみとして残飯を用い、残飯を乾
燥機内に一括投入する場合と、乾燥機出口温度により少
量ずつ分割投入する場合との実験結果を示し、分割投入
を採用した場合には、攪拌動力が小さいと共に熱効率が
高く、かつ、残飯が餅状又は糊状となって乾燥機内面に
固着してしまったり、表面のみが焦げ付いてしまい内部
が乾燥できなくなるということがなくなる。
Table 1 shows the experimental results of the case where the leftover rice is used as raw garbage and the leftover rice is put into the dryer all at once, and the case where the leftover rice is divided into small portions depending on the outlet temperature of the dryer. In addition, the stirring power is small and the thermal efficiency is high, and the leftover rice does not become sticky or pasty and stick to the inner surface of the dryer, or only the surface is scorched so that the inside cannot be dried.

【0023】[0023]

【表1】 [Table 1]

【0024】[0024]

【発明の効果】以上説明から明らかなように本発明によ
れば、乾燥の前処理として生ごみを破砕脱水するため、
生ごみ表面への付着水が除去されると共に表面積が増加
し、乾燥の省エネルギー化、効率化を図ることができ
る。また、生ごみの減容化、減量化を図ることができる
ため、運搬コストおよび保管スペースを低減させること
ができる。
As is apparent from the above description, according to the present invention, since food waste is crushed and dehydrated as a pretreatment for drying,
Water adhering to the surface of food waste is removed and the surface area is increased, so that energy saving and efficiency of drying can be achieved. Further, since it is possible to reduce the volume and the amount of garbage, it is possible to reduce the transportation cost and the storage space.

【0025】また、乾燥状態を把握するためのパラメー
タとして水分活性を用いることにより、乾燥品質を簡便
な方法で正確に把握することができると共に、生ごみの
水分活性を適正値に処理するので、生ごみの腐敗、臭気
の発生を防止し、生ごみの保管を容易にし、また、肥
料、飼料等の原料に再利用可能とすることができる。
Further, by using the water activity as a parameter for ascertaining the dry state, it is possible to accurately ascertain the dry quality by a simple method, and the water activity of raw garbage is processed to an appropriate value. It is possible to prevent spoilage and odor generation of food waste, facilitate the storage of food waste, and make it reusable as a raw material such as fertilizer and feed.

【0026】また、乾燥熱源として、熱交換器を用いる
ことにより各部のガス温度状態を自由に設定することが
できる。
By using a heat exchanger as the drying heat source, the gas temperature state of each part can be freely set.

【0027】さらに、乾燥機から排出される空気は、バ
ーナーに送られ燃焼用空気として用いられるため、空気
中に含まれる臭気は殆どバーナーにより加熱分解される
ため、脱臭装置が不要となる。
Further, since the air discharged from the dryer is sent to the burner and used as combustion air, most of the odor contained in the air is thermally decomposed by the burner, so that the deodorizing device is unnecessary.

【0028】さらに、生ごみの分割投入を採用した場合
には、攪拌動力が小さいと共に熱効率が高く、かつ、残
飯が餅状又は糊状となって乾燥機内面に固着してしまっ
たり、表面のみが焦げ付いてしまい内部が乾燥できなく
なるということがなくなる。
Further, in the case of adopting the divided input of raw garbage, the stirring power is small and the thermal efficiency is high, and the leftover rice becomes sticky or pasty and sticks to the inner surface of the dryer, or only the surface. No longer sticks to the inside and cannot be dried inside.

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

【図1】本発明の生ごみ処理装置の一実施例を示す構成
FIG. 1 is a configuration diagram showing an embodiment of a food waste processing device of the present invention.

【図2】生ごみ処理方法を説明するための湿り空気線図FIG. 2 is a moist air diagram for explaining the method of treating food waste.

【図3】本発明の生ごみ処理装置の他の実施例を示す構
成図
FIG. 3 is a configuration diagram showing another embodiment of the garbage processing device of the present invention.

【図4】本発明の生ごみ処理装置の他の実施例を示す構
成図
FIG. 4 is a configuration diagram showing another embodiment of the garbage processing device of the present invention.

【図5】本発明による実験結果を説明するための図FIG. 5 is a diagram for explaining an experimental result according to the present invention.

【図6】本発明による実験結果を説明するための図FIG. 6 is a diagram for explaining an experimental result according to the present invention.

【図7】本発明による実験結果を説明するための図FIG. 7 is a diagram for explaining an experimental result according to the present invention.

【符号の説明】[Explanation of symbols]

1…ホッパー、3…破砕脱水装置、4…乾燥機、5…乾
燥容器、7…攪拌装置 8…開閉装置、9…ごみ収納容器または収集袋、10…
熱交換器 11…バーナー、12…送風用ファン、14…燃焼用送
風管 15…乾燥用送風管、16…乾燥用排出管、17…排気
管、21…回転軸 22…切断刃、TC1、TC2…温度検出器
DESCRIPTION OF SYMBOLS 1 ... Hopper, 3 ... Crushing dehydrator, 4 ... Dryer, 5 ... Drying container, 7 ... Stirring device 8 ... Opening / closing device, 9 ... Garbage storage container or collection bag, 10 ...
Heat exchanger 11 ... Burner, 12 ... Blower fan, 14 ... Combustion blast pipe 15 ... Drying blast pipe, 16 ... Drying exhaust pipe, 17 ... Exhaust pipe, 21 ... Rotating shaft 22 ... Cutting blade, TC1, TC2 ... Temperature detector

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成3年5月20日[Submission date] May 20, 1991

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】図面[Document name to be corrected] Drawing

【補正対象項目名】図1[Name of item to be corrected] Figure 1

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【図1】 [Figure 1]

【手続補正2】[Procedure Amendment 2]

【補正対象書類名】図面[Document name to be corrected] Drawing

【補正対象項目名】図5[Name of item to be corrected] Figure 5

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【図5】 [Figure 5]

【手続補正3】[Procedure 3]

【補正対象書類名】図面[Document name to be corrected] Drawing

【補正対象項目名】図6[Name of item to be corrected] Figure 6

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【図6】 [Figure 6]

【手続補正4】[Procedure amendment 4]

【補正対象書類名】図面[Document name to be corrected] Drawing

【補正対象項目名】図7[Name of item to be corrected] Figure 7

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【図7】 [Figure 7]

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】生ごみを破砕脱水する破砕脱水装置と、該
破砕脱水された生ごみを乾燥する乾燥機と、該乾燥機に
接続される乾燥用送風管および乾燥用排出管と、バーナ
ーにより加熱された空気により前記乾燥用送風管を流れ
る空気を加熱するための熱交換器とを有することを特徴
とする生ごみ処理装置。
1. A crushing and dehydrating apparatus for crushing and dehydrating food waste, a dryer for drying the crushed and dehydrated food waste, a drying blower pipe and a drying discharge pipe connected to the dryer, and a burner. And a heat exchanger for heating the air flowing through the drying blower pipe with heated air.
【請求項2】生ごみを破砕脱水する破砕脱水装置と、破
砕脱水された生ごみを乾燥する乾燥機と、乾燥機に接続
される乾燥用送風管および乾燥用排出管と、バーナーに
より加熱された空気により乾燥用送風管を流れる空気を
加熱するための熱交換器とを有し、乾燥用送風管内の温
度で前記バーナーの燃焼量を制御し、乾燥用排出管内の
温度により生ごみの水分活性を制御し乾燥状態を把握す
ることを特徴とする生ごみ処理方法。
2. A crushing and dehydrating apparatus for crushing and dehydrating food waste, a dryer for drying the crushed and dehydrated food waste, a drying blower pipe and a drying discharge pipe connected to the dryer, and a heater for heating. It has a heat exchanger for heating the air flowing through the drying blast pipe with the air, and controls the combustion amount of the burner by the temperature inside the drying blast pipe, and the moisture in the food waste depending on the temperature inside the drying discharge pipe. A method for treating food waste, which comprises controlling the activity and grasping the dry state.
JP09911791A 1990-10-23 1991-04-30 Garbage disposal method Expired - Fee Related JP3485189B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP09911791A JP3485189B2 (en) 1990-10-23 1991-04-30 Garbage disposal method

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2-285244 1990-10-23
JP28524490 1990-10-23
JP09911791A JP3485189B2 (en) 1990-10-23 1991-04-30 Garbage disposal method

Publications (2)

Publication Number Publication Date
JPH0592180A true JPH0592180A (en) 1993-04-16
JP3485189B2 JP3485189B2 (en) 2004-01-13

Family

ID=26440262

Family Applications (1)

Application Number Title Priority Date Filing Date
JP09911791A Expired - Fee Related JP3485189B2 (en) 1990-10-23 1991-04-30 Garbage disposal method

Country Status (1)

Country Link
JP (1) JP3485189B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130067763A1 (en) * 2010-05-12 2013-03-21 Woongjin Coway Co., Ltd. Method of controlling the finishing of operation of a drying furnace assembly in a food waste disposer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130067763A1 (en) * 2010-05-12 2013-03-21 Woongjin Coway Co., Ltd. Method of controlling the finishing of operation of a drying furnace assembly in a food waste disposer

Also Published As

Publication number Publication date
JP3485189B2 (en) 2004-01-13

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