JPH04332307A - Refuse disposal device - Google Patents
Refuse disposal deviceInfo
- Publication number
- JPH04332307A JPH04332307A JP10072091A JP10072091A JPH04332307A JP H04332307 A JPH04332307 A JP H04332307A JP 10072091 A JP10072091 A JP 10072091A JP 10072091 A JP10072091 A JP 10072091A JP H04332307 A JPH04332307 A JP H04332307A
- Authority
- JP
- Japan
- Prior art keywords
- garbage
- heat
- waste
- cooling air
- container
- 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
Links
- 238000009833 condensation Methods 0.000 claims abstract description 19
- 230000005494 condensation Effects 0.000 claims abstract description 19
- 238000001816 cooling Methods 0.000 claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 38
- 239000002699 waste material Substances 0.000 claims description 29
- 230000003247 decreasing effect Effects 0.000 claims description 3
- 239000000498 cooling water Substances 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims 1
- 238000001035 drying Methods 0.000 abstract description 11
- 238000000034 method Methods 0.000 description 7
- 239000003054 catalyst Substances 0.000 description 5
- 239000000428 dust Substances 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
- 239000012780 transparent material Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、厨房,病院等で発生す
るごみを簡便に処理する装置に利用される。ごみは現在
自治体で埋め立てあるいは焼却処分されている。埋め立
て用地不足のためごみ処理は焼却処分に頼らざるをえな
いが、焼却処分も輸送時の衛生問題,焼却場立地難とい
う課題を持っている。本発明はごみを発生した場所で軽
量化,減容化し、かつ衛生的なものとする装置に関する
もので、この課題を解決できるものである。本発明は家
庭,料理店,食料品店等のごみ処理に利用される。FIELD OF INDUSTRIAL APPLICATION The present invention is applied to an apparatus for easily disposing of waste generated in kitchens, hospitals, etc. Garbage is currently disposed of in landfills or incinerated by local governments. Due to a lack of land for landfill, waste disposal has no choice but to rely on incineration, but incineration also poses issues such as hygiene issues during transportation and difficulty in locating an incinerator. The present invention relates to a device that reduces the weight and volume of waste at the place where it is generated, and makes it sanitary, and can solve this problem. The present invention can be used for waste disposal in homes, restaurants, grocery stores, etc.
【0002】0002
【従来の技術】ごみを衛生的に処理するための乾燥もし
くは焼却する方法がとられる。大規模な設備に適したも
のは各種あるが、小型の機器に適した物としてはマイク
ロ波を用いてごみを乾燥あるいは燃焼する方式が提案さ
れている。この方式は乾燥速度が早く、ごみは腐敗しな
い衛生的なものとなる。また、軽量化し廃棄が容易とな
る。2. Description of the Related Art Drying or incineration methods are used to hygienically dispose of waste. There are various methods suitable for large-scale equipment, but a method that uses microwaves to dry or burn waste has been proposed as a method suitable for small-sized equipment. This method dries quickly and the waste is sanitary and does not rot. In addition, it is lightweight and easy to dispose of.
【0003】0003
【発明が解決しようとする課題】しかしながら、上記従
来の方法では、水の蒸発潜熱が大きいため、ごみを乾燥
するには多大な電力を必要とする問題点を有していた。
又、一方でごみから蒸発した水蒸気が凝縮した後の水は
凝縮熱を有したまま外部へ排出しており、熱の有効利用
がはかれていなかった。However, the conventional method described above has the problem of requiring a large amount of electric power to dry the waste because the latent heat of vaporization of water is large. On the other hand, after the water vapor evaporated from the garbage is condensed, the water is discharged to the outside while retaining the heat of condensation, and the heat is not used effectively.
【0004】本発明のごみ処理装置は上記問題を解決す
るものでごみから発生する水蒸気を凝縮する際の熱をご
み乾燥用に再利用することで、乾燥効率のアップをはか
り、少ない消費電力でごみを乾燥できるごみ処理装置の
実現を目的とする。The garbage disposal device of the present invention solves the above problem, and by reusing the heat generated when condensing water vapor generated from garbage for drying garbage, it improves drying efficiency and consumes less power. The aim is to create a garbage disposal device that can dry garbage.
【0005】[0005]
【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1の手段として、加熱によりごみから発生
する水蒸気を冷却用空気で強制冷却する凝縮部を設ける
とともに、上記凝縮部で発生した凝縮熱及び凝縮水の潜
熱を上記冷却用空気に伝達する熱交換壁と冷却用空気流
動用の送風機を備えた。[Means for Solving the Problems] As a first means of the present invention to achieve the above object, a condensing section is provided for forcibly cooling water vapor generated from garbage by heating with cooling air, and the condensing section It is equipped with a heat exchange wall that transfers the generated condensation heat and the latent heat of condensed water to the cooling air, and a blower for flowing the cooling air.
【0006】又、第2の手段として、冷却用空気が熱交
換壁を通過する際に上記凝縮水の流下する方向とは逆に
流れ、ごみ容器を通過した後に排気されることとした。Furthermore, as a second means, when the cooling air passes through the heat exchange wall, it flows in the opposite direction to the direction in which the condensed water flows down, and is exhausted after passing through the waste container.
【0007】さらに、第3の手段として、マイクロ波を
用いるとともに、マイクロ波加熱手段と送風機の出力の
増減を交互にすることとした。Furthermore, as a third means, microwaves are used and the outputs of the microwave heating means and the blower are alternately increased and decreased.
【0008】[0008]
【作用】上記構成における本発明の作用を以下に説明す
る。[Operation] The operation of the present invention in the above configuration will be explained below.
【0009】水分を多く含むごみを加熱することにより
水蒸気を発生する。水蒸気は周囲で凝縮して凝縮熱を出
し凝縮水となる。[0009] Water vapor is generated by heating waste containing a large amount of moisture. Water vapor condenses in its surroundings, releasing heat of condensation and becoming condensed water.
【0010】この凝縮水は流下して排気口より外部に排
出されるが、送風機によりこの凝縮水の流下方向と反対
方向に空気を送り、熱交換壁を介して凝縮熱及び潜熱を
受け取る。高温化した空気がごみに送り込まれ、乾燥を
促進する。[0010] This condensed water flows down and is discharged to the outside from the exhaust port, but a blower sends air in a direction opposite to the direction in which this condensed water flows down, and receives condensation heat and latent heat through a heat exchange wall. Hot air is pumped into the waste to accelerate drying.
【0011】さらに、マイクロ波により加熱している時
は送風機の出力を弱めているため、ごみ容器内部が十分
高温になり水分の蒸発が活発に行われるものである。[0011]Furthermore, since the output of the blower is weakened when heating is performed using microwaves, the inside of the waste container reaches a sufficiently high temperature and moisture evaporates actively.
【0012】0012
【実施例】以下第1項の本発明の一実施例を添付図面に
基づいて説明する。図1において1はプラスチック,セ
ラミック,ガラス,紙等のマイクロ波透過材料で作られ
たごみ容器である。ごみ容器1は袋状でもコップ状でも
よく孔2が複数個設けてある。ごみ容器1が紙袋である
場合は繊維間の隙間がこの孔2の役目をする。マイクロ
波反射材料で作られた桶状の収納部3に入れられたごみ
容器1の開口4は枠体5で拡げられ収納部3の係止部6
に保持されているとともに内蓋7で閉じられている。DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention described in item 1 will be described below with reference to the accompanying drawings. In FIG. 1, 1 is a garbage container made of a microwave transparent material such as plastic, ceramic, glass, or paper. The garbage container 1 may be bag-shaped or cup-shaped and has a plurality of holes 2. When the garbage container 1 is a paper bag, the gaps between the fibers serve as the holes 2. The opening 4 of the garbage container 1 placed in a bucket-shaped storage section 3 made of a microwave reflective material is widened by a frame 5, and the locking section 6 of the storage section 3 is opened.
and is closed with an inner lid 7.
【0013】ごみ容器1の中へごみ8は内蓋7および収
納部3の上部の開閉する扉9を開いて入れられる。マグ
ネトロン10で発振したマイクロ波は導波管11によっ
て収納部3のごみ8に照射される構成となっている。導
波管11の開口はマイクロ波透過性の蓋12により覆わ
れている。The garbage 8 is put into the garbage container 1 by opening the inner lid 7 and the door 9 at the top of the storage section 3, which opens and closes. Microwaves oscillated by the magnetron 10 are configured to be irradiated onto the dust 8 in the storage section 3 through a waveguide 11. The opening of the waveguide 11 is covered with a microwave transparent lid 12.
【0014】収納部3のごみ容器1の周囲は凝縮部13
で、収納部3の下部には排水管14がある。さらに排水
管14の下流は蒸気排出管15とドレン管16に分流す
る。送風機17により収納部3の外周に形成された冷却
経路18に取入れられた空気は冷却経路18、ごみ容器
1の外壁である熱交換壁21及びごみ容器1を通り蒸気
と混合して吸引され、蒸気排出管15とヒータ20で加
熱されている触媒22を通して室外に排出される。A condensing section 13 surrounds the garbage container 1 in the storage section 3.
A drain pipe 14 is provided at the bottom of the storage section 3. Furthermore, the downstream side of the drain pipe 14 is divided into a steam exhaust pipe 15 and a drain pipe 16 . The air introduced into the cooling path 18 formed around the outer periphery of the storage section 3 by the blower 17 passes through the cooling path 18, the heat exchange wall 21 which is the outer wall of the garbage container 1, and the garbage container 1, and is mixed with steam and sucked. The steam is discharged outside through the steam exhaust pipe 15 and the catalyst 22 heated by the heater 20.
【0015】蒸気排出管15と触媒22に温度検知部2
3,24が設けられている。ドレン管16の下部はトラ
ップ25,下水管26である。上記構成の本発明の動作
を以下に説明する。[0015] A temperature detecting section 2 is installed in the steam exhaust pipe 15 and the catalyst 22.
3 and 24 are provided. A trap 25 and a sewer pipe 26 are located below the drain pipe 16. The operation of the present invention having the above configuration will be explained below.
【0016】扉9よりごみはごみ容器1の中に投入され
る。ごみ容器1は収納部3の内部に着脱自在に設けられ
た扉9より出し入れできる。このような状態でマグネト
ロン10がマイクロ波を発振するとごみ8は温度上昇し
水蒸気を発生する。マイクロ波透過性のごみ容器1は温
度上昇しないが、マイクロ波浸透性の良いごみ8は放熱
のない中央部より温度上昇する傾向を持つ。したがって
水蒸気はまずごみ8の中央で発生し、周りのごみの熱破
壊による遊離水を外に押し出しつつ表面よりでることと
なる。押し出された遊離水は他のごみ8の周りを通りご
み容器1の下部の孔2より流下し、排水管14より外部
に排出される。Garbage is thrown into the garbage container 1 through the door 9. The garbage container 1 can be taken in and taken out through a door 9 that is detachably provided inside the storage section 3. When the magnetron 10 oscillates microwaves in this state, the temperature of the dust 8 rises and generates water vapor. The temperature of the waste container 1 which is permeable to microwaves does not rise, but the temperature of the waste 8 which is permeable to microwaves tends to rise more than the central part where there is no heat dissipation. Therefore, water vapor is first generated in the center of the waste 8, and comes out from the surface while pushing out the free water due to thermal destruction of the surrounding waste. The pushed out free water passes around other garbage 8, flows down through the hole 2 at the bottom of the garbage container 1, and is discharged to the outside through the drain pipe 14.
【0017】水蒸気はごみ容器1の孔2を通り収納部3
のごみ容器1外の凝縮部13に充満し、送風機17の空
気で冷却されているので、収納部3の内壁で凝縮して排
水管14へ排出される。水蒸気の凝縮水は蒸留過程を経
ているので比較的有機物が少なくスムーズに流下し速や
かに排出されるため、水滴がマイクロ波を吸収すること
もないうえ収納部3の底部も比較的清潔に保たれる。Water vapor passes through the hole 2 of the garbage container 1 and enters the storage section 3.
Since the condensation section 13 outside the garbage container 1 is filled with the waste and is cooled by the air from the blower 17, it condenses on the inner wall of the storage section 3 and is discharged to the drain pipe 14. Since the condensed water of steam has undergone a distillation process, it has relatively little organic matter and flows down smoothly and is quickly discharged, so water droplets do not absorb microwaves and the bottom of the storage compartment 3 is kept relatively clean. It will be done.
【0018】水蒸気が凝縮する際の凝縮熱及び凝縮水の
潜熱は収納部3の外周の冷却経路18の空気を熱交換壁
21を介して加熱している。熱交換壁21には凹凸を設
けることで熱交換性を高めている。凝縮熱を回収するた
め冷却空気は凝縮水の流下する方向と逆方向に流れ、ま
ずごみ容器1の下方にある低温の凝縮水の顕熱を受け取
った後、高温凝縮水の顕熱を受取り、さらに水蒸気の凝
縮熱を受取り高温の空気となる。The heat of condensation when the water vapor condenses and the latent heat of the condensed water heat the air in the cooling path 18 on the outer periphery of the storage section 3 via the heat exchange wall 21. Heat exchange performance is improved by providing unevenness on the heat exchange wall 21. In order to recover the heat of condensation, the cooling air flows in the opposite direction to the direction in which the condensed water flows, and first receives the sensible heat of the low-temperature condensed water located below the garbage container 1, and then receives the sensible heat of the high-temperature condensed water. Furthermore, it receives the heat of condensation from water vapor and becomes high-temperature air.
【0019】この高温の空気は蓋9の手前でUターンし
てごみ容器1のごみ8の中を通過しごみ8の乾燥を促進
されることとなる。この加熱された空気はごみ8を冷却
しにくいので乾燥を促進し、かつ触媒20で臭気の酸化
に必要な酸素を供給している(乾燥の進行と共にごみ8
が若干量の分解ガスを発生する。これは臭気の原因とな
るが予めヒータ20で活性化温度になるように温度検知
部24で保たれている触媒22で酸化され無臭化される
)。ごみを通過して含湿した空気は再び凝縮空間で脱水
し外部に排出される。この乾燥の進行と終了は温度検知
部23の温度が低下する、あるいはマグネトロン10の
温度が上昇する、あるいはごみ8の重量変化、等の手段
で検出されることとなる。This high-temperature air makes a U-turn before the lid 9 and passes through the waste 8 in the waste container 1, thereby promoting the drying of the waste 8. This heated air is difficult to cool the garbage 8, so it accelerates drying, and the catalyst 20 supplies oxygen necessary for oxidizing the odor (as the drying progresses, the garbage 8
generates some amount of decomposition gas. This causes odor, but it is oxidized and rendered odorless by the catalyst 22, which is maintained in advance by the temperature detection unit 24 so as to reach the activation temperature by the heater 20). The moist air that has passed through the garbage is dehydrated again in the condensation space and discharged to the outside. The progress and completion of this drying is detected by means such as a decrease in the temperature of the temperature detection section 23, an increase in the temperature of the magnetron 10, or a change in the weight of the dust 8.
【0020】ごみ8は乾燥収縮してごみ容器1の下部に
溜るが乾燥しているのでそのまま保管しても腐敗するこ
とはなく、ごみ容器1が一杯になるまで繰り返し処理で
きる。The garbage 8 shrinks when dry and accumulates at the bottom of the garbage container 1, but since it is dry, it will not rot even if stored as is, and can be repeatedly disposed of until the garbage container 1 is full.
【0021】マイクロ波の熱は水の蒸気潜熱と空気の顕
熱と装置からの放熱として消費されている。よって送風
機17の制御で送風量を略停止しごみ8を加熱乾燥する
と、器外に逃げる熱はほとんどなく効率よく水蒸気の凝
縮熱又は凝縮熱の潜熱となる。この点に着眼し本発明で
はごみ容器を袋としたほかマイクロ波を間欠動作するこ
とを行う。すなわち収納室3あるいはごみ容器1が凝縮
熱で所定の温度まで昇温したことを検知部27で検知し
てマグネトロン10を停止し、同時に送風機17の送風
量を増加して装置の凝縮熱をごみ容器8に搬送し温風乾
燥する。ごみ8は乾燥した温風で乾燥しつつ潜熱により
冷却される。所定の温度まで低下した時マイクロ波を照
射し再び送風量を減少させる。この繰り返しにより装置
外への熱の無駄な流出は少ないものとなる。すなわち、
収納部3あるいはごみ容器1は実質的に蓄熱材として機
能するので熱伝導のロスはなくなるものである。[0021] The heat of the microwave is consumed as vapor latent heat of water, sensible heat of air, and heat radiated from the device. Therefore, when the blower 17 is controlled to substantially stop the amount of air blown and the waste 8 is heated and dried, almost no heat escapes to the outside of the container and efficiently becomes condensation heat of water vapor or latent heat of condensation heat. Focusing on this point, the present invention uses a bag as the garbage container and uses microwaves intermittently. That is, the detection unit 27 detects that the temperature of the storage chamber 3 or the waste container 1 has risen to a predetermined temperature due to the heat of condensation, the magnetron 10 is stopped, and at the same time, the amount of air blown by the blower 17 is increased to transfer the heat of condensation from the device to the waste. Transferred to container 8 and dried with warm air. The garbage 8 is cooled by latent heat while being dried by the dry warm air. When the temperature drops to a predetermined level, microwaves are irradiated and the amount of air blown is reduced again. By repeating this process, wasteful outflow of heat to the outside of the device is reduced. That is,
Since the storage section 3 or the garbage container 1 essentially functions as a heat storage material, there is no loss in heat conduction.
【0022】またマイクロ波がごみを中心から加熱する
傾向を持つのに対して、温風は外表面のみ加熱乾燥する
ので両者を交互に操作することで乾燥は速くなる。Furthermore, while microwaves tend to heat the dust from the center, warm air heats and dries only the outer surface, so drying can be speeded up by alternately operating the two.
【0023】なお本実施例はマイクロ波を加熱手段とし
ているが請求第1項の実施を赤外線ヒータ,電気抵抗線
ヒータ等を用いて行っても同一の効果は得られるもので
ある。Although microwaves are used as the heating means in this embodiment, the same effect can be obtained even if the method described in claim 1 is carried out using an infrared heater, an electric resistance wire heater, or the like.
【0024】[0024]
【発明の効果】上記実施例より明らかなように、ごみか
ら蒸発する水蒸気を冷却空気により冷却する凝縮部と、
この冷却空気の送風手段及び排気口と、凝縮水の排出手
段とを有し上記冷却空気は、水蒸気及び凝縮水と熱交換
壁を介して接するとともに上記凝縮水と逆方向に流れる
構成としたことにより、水蒸気の凝縮熱及び凝縮水の潜
熱を再利用してごみを乾燥することができる。Effects of the Invention As is clear from the above embodiments, a condensing section that cools water vapor evaporated from garbage with cooling air;
The cooling air has a blowing means and exhaust port for the cooling air, and a condensed water discharge means, and the cooling air is in contact with steam and condensed water through a heat exchange wall and flows in the opposite direction to the condensed water. This makes it possible to reuse the heat of condensation of water vapor and the latent heat of condensed water to dry waste.
【0025】すなわち、加熱手段からごみに加えられた
熱が、凝縮水の排出により外部へ逃げることが少なく、
非常に熱効率の良いごみ処理装置を実現できるものであ
る。In other words, the heat applied to the waste from the heating means is less likely to escape to the outside due to the discharge of condensed water.
This makes it possible to realize a garbage treatment device with extremely high thermal efficiency.
【0026】さらに、マイクロ波加熱手段と送風機の出
力の増減を交互にすることで、熱効率の向上が計れ、経
済的なごみ処理装置を実現できるものである。Furthermore, by alternately increasing and decreasing the output of the microwave heating means and the blower, thermal efficiency can be improved and an economical garbage disposal apparatus can be realized.
【図1】本発明の一実施例におけるごみ処理装置の縦断
面図[Fig. 1] A vertical cross-sectional view of a garbage disposal device in an embodiment of the present invention.
1 ごみ容器 2 孔 3 収納部 13 凝縮部 18 冷却経路 21 触媒 1 Garbage container 2 holes 3 Storage section 13 Condensation section 18 Cooling path 21 Catalyst
Claims (3)
に収納されたごみを加熱する加熱手段と、ごみから蒸発
する水蒸気を冷却用空気で強制冷却する凝縮部と、この
凝縮部で発生する凝縮水を排出する排出口と、上記凝縮
部で発生した凝縮熱を上記冷却用空気に伝達する熱交換
部と、冷却用空気流動用の送風機とを有したごみ処理装
置。Claims: 1. A garbage container for storing garbage, a heating means for heating the garbage stored in the garbage container, a condensing section for forcibly cooling water vapor evaporated from the garbage with cooling air, and water vapor generated in the condensing section. A waste disposal device comprising: a discharge port for discharging condensed water; a heat exchange section for transmitting condensation heat generated in the condensation section to the cooling air; and a blower for flowing the cooling air.
際に凝縮水の流下する方向とは逆に流れ、ごみ容器を通
過した後に排気されることとした請求項1記載のごみ処
理装置。2. The waste according to claim 1, wherein the cooling air flows in the opposite direction to the direction in which the condensed water flows when passing through the heat exchanger, and is exhausted after passing through the waste container. Processing equipment.
に、マイクロ波加熱手段と送風機の出力の増減を交互に
することとした請求項1または2記載のごみ処理装置。3. The waste disposal apparatus according to claim 1, wherein microwaves are used as the heating means, and the outputs of the microwave heating means and the blower are alternately increased and decreased.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10072091A JP2900636B2 (en) | 1991-05-02 | 1991-05-02 | Waste treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10072091A JP2900636B2 (en) | 1991-05-02 | 1991-05-02 | Waste treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04332307A true JPH04332307A (en) | 1992-11-19 |
JP2900636B2 JP2900636B2 (en) | 1999-06-02 |
Family
ID=14281474
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10072091A Expired - Fee Related JP2900636B2 (en) | 1991-05-02 | 1991-05-02 | Waste treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2900636B2 (en) |
-
1991
- 1991-05-02 JP JP10072091A patent/JP2900636B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP2900636B2 (en) | 1999-06-02 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5477623A (en) | Drying apparatus | |
US5335425A (en) | Dry-processing apparatus for heating and drying objects to be processed | |
JP2689798B2 (en) | Garbage disposal equipment | |
JPH04332307A (en) | Refuse disposal device | |
JP2692463B2 (en) | Garbage processing machine | |
KR100480700B1 (en) | waste disposer | |
JP3097194B2 (en) | Garbage disposal equipment | |
JP3087383B2 (en) | Garbage processing machine | |
JP3180354B2 (en) | Operating method of garbage disposal | |
JP3019531B2 (en) | Drying processing equipment | |
KR100455182B1 (en) | Steam circulation apparatus of microwave heating type garbage treatment machine | |
WO2014148807A1 (en) | Drying apparatus with pyrolysis function | |
JP3083394B2 (en) | Garbage disposal equipment | |
JP2943471B2 (en) | Garbage disposal equipment | |
JP2806202B2 (en) | Drying equipment | |
JP2994969B2 (en) | Garbage processing machine | |
JP2809580B2 (en) | Drying equipment | |
JP3241025B2 (en) | Waste treatment equipment | |
JP2742487B2 (en) | Garbage disposal equipment | |
JPH04193382A (en) | Refuse treating device | |
JP2595843B2 (en) | Garbage disposal equipment | |
JPH05275170A (en) | Dry processing device | |
JP3207056B2 (en) | Garbage processing machine | |
JP2579037B2 (en) | Garbage processing equipment | |
JPH0463184A (en) | Garbage treating device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080319 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090319 Year of fee payment: 10 |
|
LAPS | Cancellation because of no payment of annual fees |