JPH07233931A - Reduced-pressure drying garbage incinerator and treating method of combustion exhaust gas - Google Patents

Reduced-pressure drying garbage incinerator and treating method of combustion exhaust gas

Info

Publication number
JPH07233931A
JPH07233931A JP6066380A JP6638094A JPH07233931A JP H07233931 A JPH07233931 A JP H07233931A JP 6066380 A JP6066380 A JP 6066380A JP 6638094 A JP6638094 A JP 6638094A JP H07233931 A JPH07233931 A JP H07233931A
Authority
JP
Japan
Prior art keywords
chamber
garbage
combustion
drying chamber
drying
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.)
Pending
Application number
JP6066380A
Other languages
Japanese (ja)
Inventor
Koichi Nakayama
紘一 中山
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP6066380A priority Critical patent/JPH07233931A/en
Publication of JPH07233931A publication Critical patent/JPH07233931A/en
Pending legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2204/00Supplementary heating arrangements
    • F23G2204/20Supplementary heating arrangements using electric energy
    • F23G2204/203Microwave

Landscapes

  • Drying Of Solid Materials (AREA)
  • Air Supply (AREA)
  • Incineration Of Waste (AREA)

Abstract

PURPOSE:To obtain a reduced-pressure drying garbage incinerator and a treating method of combustion exhaust gas which make it possible to incinerate garbage efficiently, to reduce the volume thereof and to put the exhaust gas in a state of being free from soot dust, smoke and odor. CONSTITUTION:Stock garbage 1a is assorted and charged sequentially as cut-out garbage 1b to be processed subsequently, into a drying chamber 3a and a combustion chamber 3b partitioned by an opening-closing door in the main body 31 of an incinerator inside a reduced- pressure chamber 23 and it is dried by reduced-pressure microwave heating in the drying chamber 3a and then subjected to oxygen incineration in the combustion chamber 3b. A combustion gas thus produced is led to the drying chamber 3a through a communication pipe 49 for auxiliary heating of garbage 1c in the drying chamber and water is vaporized from the garbage by the effect of this heating and the reduced-pressure microwave heating. Both the water vapor thus obtained and the combustion gas are led to a cooling trap 52 by a vacuum pump 54 and the water vapor is condensed by cooling and made to drop into the cooling trap 52 to be subjected to water-vapor separation. In the process of condensation of the water vapor, soot dust, smoke, a hazardous gas and odor are washed and exhausted. Incineration ashes are discharged from an ash discharge door 24 through an ash box 70.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、業務用厨房内や家庭
で発生する生ごみの焼却処理を、減圧下でマイクロ波加
熱乾燥し、酸素焼却を行う生ごみ減圧乾燥焼却装置およ
び燃焼排ガス処理方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a food waste vacuum drying / incinerator and a combustion exhaust gas treatment for incinerating food waste generated in commercial kitchens and households by microwave heating and drying under reduced pressure. It is about the method.

【0002】[0002]

【従来の技術】従来、生ごみの焼却は、焼却炉に一度に
その処理全量を投入し、大気圧下で、油もしくはガスバ
ーナーによる燃焼炎によって焼却を行っている。
2. Description of the Related Art Conventionally, when incinerating food waste, the entire amount of the garbage is put into an incinerator at a time, and the incinerator is incinerated by a combustion flame from an oil or gas burner under atmospheric pressure.

【0003】[0003]

【発明が解決しようとする課題】業務用厨房内や家庭で
生ずる生ごみは、一般の可燃性廃棄物に比べてその含有
水分量が大変多いため、着火や燃焼が困難であり、燃焼
可能な乾燥状態にする際に、発生する生ごみの処理全量
を一括投入した状態では、生ごみの深部からの水分蒸発
エネルギー効率が悪く、乾燥が不充分となり、燃焼に際
して不完全燃焼を生じ、煤塵、煙、悪臭も多く、食品容
器プラスチックなどの混入によっては有害ガスの発生も
生じ、また、生ごみの処理量に比例し焼却炉の大型化を
余儀なくされ、焼却炉および周辺の安全管理も問題とな
っている。この発明は、上記課題を解決するもので、発
生する生ごみを効率よく焼却処理できるよう、減圧チャ
ンバー内に焼却装置を設置し、生ごみを一定量毎に分別
し、乾燥工程と、燃焼工程とをそれぞれに効率よく行う
ことによって、焼却炉を小型化し安全性の高い生ごみの
焼却装置を提供することを目的としている。
Since garbage contained in commercial kitchens and households has a much higher water content than general combustible waste, it is difficult to ignite or burn it, and combustible. In the dry state, when the total amount of raw garbage generated is put in at one time, the energy efficiency of water evaporation from the deep part of the raw garbage is poor, the drying becomes insufficient, incomplete combustion occurs during combustion, soot, There is a lot of smoke and bad odor, and harmful gas may be generated due to the mixing of food container plastic, etc. Also, the incinerator must be upsized in proportion to the amount of food waste treated, and safety management of the incinerator and its surroundings becomes a problem. Has become. This invention is to solve the above-mentioned problems, in order to efficiently incinerate the generated garbage, an incinerator is installed in the decompression chamber, the garbage is separated into fixed amounts, a drying step and a combustion step. The purpose of the present invention is to provide a highly safe incinerator for food waste by downsizing the incinerator by efficiently performing the above steps.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するため
に、本発明の焼却装置においては、生ごみを収容する生
ごみストック部(1)と、焼却炉本体部を内蔵設置する
減圧チャンバー部(2)、および、焼却装置部(3)に
よって大別構成され、生ごみストック部(1)として
は、ストックホッパー(11)と、ホッパー蓋(12)
と、ストック生ごみ(1a)から所定量を分別し次処理
切出し生ごみ(1b)とする切出しシャッター(13)
と、これを開閉駆動するシャッター駆動シリンダー(1
4)と、処理すべき生ごみの有無を検知する物有無確認
センサー(15)からなり、この生ごみストック部
(1)を、減圧チャンバー部(2)の上部に設置する。
減圧チャンバー部(2)は、チャンバー投入口密閉扉
(21)と、これを開閉駆動する密閉扉開閉シリンダー
(22)と、チャンバー(23)と、灰排出扉(24)
からなり、チャンバー投入口密閉扉(21)と灰排出扉
(24)を閉じて、チャンバー(23)の側面に設けた
チャンバー排気配管(51)から真空ポンプ(54)で
排気を行うとチャンバー(23)内が減圧される。チャ
ンバー投入口密閉扉(21)は、生ごみストック部
(1)の底扉の機能を兼ねて開閉される。チャンバー
(23)内に、焼却炉本体(31)が焼却炉脚(38)
で支持設置され、焼却炉本体(31)に、乾燥室上扉
(32)とその開閉用に上扉開閉シリンダー(33)、
中間扉(34)とその開閉用に中間扉開閉シリンダー
(35)、燃焼室下扉(36)とその開閉用に下扉開閉
シリンダー(37)が設けられ、上室を乾燥室(3a)
とし、下室を燃焼室(3b)とする。切出しシャッター
(13)を閉じて、チャンバー投入口密閉扉(21)と
の間に仕切られる生ごみを次処理切出し生ごみ(1b)
として、焼却炉本体(31)の中間扉(34)を閉じ
て、乾燥室上扉(32)を開け、次いでチャンバー投入
口密閉扉(21)を開け、次処理切出し生ごみ(1b)
を乾燥室(3a)に落下投入し、乾燥室生ごみ(1c)
とし、乾燥室上扉(32)とチャンバー投入口密閉扉
(21)を閉じる。生ごみストック部(2)は、次の処
理準備として切出しシャッター(13)を開け、ストッ
ク生ごみ(1a)を自重降下させ、物有無確認センサー
(15)によって次処理切出し生ごみ(1b)の有無を
確認し待機する。真空ポンプ(54)作動によって、チ
ャンバー(21)内部の気体がチャンバー排気配管(5
1)から冷却トラップ(52)を経て排気されて減圧チ
ャンバー部(2)の内部が減圧され、同時に乾燥室(3
a)および連通間(49)を介して燃焼室(3b)内部
の気体が乾燥室排気配管(50)から冷却トラップ(5
2)を経て排気され減圧される。焼却炉本体(31)の
乾燥室部側面には加熱用にマイクロ波の導波管(42)
とマグネトロン(41)が設けられ、導波管(42)の
乾燥室接続部にはマイクロ波透過材でできた導波管蓋
(43)を取り付ける。また乾燥室排気配管(50)の
接続部と、連通管(49)の乾燥室接続部に、金属製の
ネット状で通気性の有る蓋をそれぞれ排気管蓋(4
5)、連通管蓋(44)として取り付ける。乾燥室生ご
み(1c)を減圧下でマイクロ波加熱すると、マイクロ
波が、生ごみ内部で吸収され熱に変り内部蒸気圧を高め
て生ごみ内部の水分を外部に移行するとともに、水分は
飽和蒸気圧に対応した低温度で蒸発を始める。蒸発水蒸
気は真空ポンプ(54)の作動により乾燥室排気配管
(50)から冷却トラップ(52)へ吸引排出される。
乾燥室(3a)の湿度センサー(46)によって、乾燥
室生ごみ(1c)の乾燥状態をセンシングして湿度変化
から乾燥を検知した後、中間扉(34)を開き、燃焼室
(3b)へ乾燥後の生ごみを落下投入し、中間扉(3
4)を閉じて、燃焼室生ごみ(1d)とする。生ごみス
トック部(1)から次処理切出し生ごみ(1b)を再
び、前述の動作で乾燥室(3a)に、落下投入し乾燥室
生ごみ(1c)とする。これによって乾燥室生ごみ(1
c)と燃焼室生ごみ(1d)がそれぞれの処理室に収容
されて、以後、乾燥と燃焼とを同時進行ですすめる。燃
焼室(3b)に酸素ガス発生装置から酸素用逆止弁(5
8)と、酸素供給配管(57)を経て酸素を供給し、着
火バーナー(47)で、燃焼室生ごみ(1d)に着火
し、酸素を供給することにより生ごみを自燃させる。真
空ポンプ(54)の作動により燃焼室(3b)の燃焼ガ
スは燃焼室と乾燥室を結ぶ連通管(49)を通り乾燥室
(3a)へ吸引され、乾燥室蒸発水蒸気とともに乾燥室
排気配管(50)から冷却トラップ(52)へ吸引排出
され、冷却トラップ(52)内で冷却され、蒸発水蒸気
は凝結し滴下し、気水分離する。燃焼ガスは冷却トラッ
プ(52)から真空ポンプ配管(53)を経て排気され
る。真空ポンプ(54)の排気速度能力を、乾燥室蒸発
水蒸気量と、燃焼室への供給酸素量と、燃焼ガス発生量
との加算量より充分大きく選定し、処理中の減圧状態を
維持する。燃焼室内の生ごみの燃焼状態は、温度センサ
ー(48)でセンシングし、温度センサー(48)の温
度変化によって燃焼完了を検知した後、酸素供給を停止
し、燃焼室下扉(36)を開き、焼却された生ごみ灰を
灰受箱(70)に落下収容する。次いで、燃焼室下扉
(36)を閉じ次の処理に対応する。灰受箱(70)
は、焼却炉(31)を支持する四隅の焼却炉脚(38)
の間に、燃焼室下扉(36)の下方になるよう配置す
る。上記の乾燥工程および燃焼工程を繰り返し行って、
乾燥室(3a)に生ごみの無くなった状態では、つま
り、処理すべき生ごみを、順次、乾燥・焼却処理してき
て最後の燃焼室生ごみ(1d)を焼却する時、乾燥室
(3a)に水用バルブ(63)を開いて、水用逆止弁
(62)を経て、給水配管(61)より適量の給水を行
って、マイクロ波加熱し、乾燥室(3a)に水蒸気を発
生し、乾燥室に吸引される燃焼ガスとともに乾燥室排気
配管(50)から冷却トラップ(52)へ排出され、冷
却トラップ(52)内で冷却され、蒸発水蒸気は凝結し
滴下し、気水分離する。燃焼ガスは冷却トラップ(5
2)から真空ポンプ配管(53)を経て排気される。生
ごみストック部(1)内の生ごみの全量を焼却処理した
後、焼却灰を収容した灰受箱(70)を、チャンバー
(23)の下部側面に設けた灰排出扉(24)から排出
する。本発明は、以上の構成よりなる生ごみ減圧乾燥焼
却装置および燃焼排ガス処理方法である。
In order to achieve the above object, in the incinerator according to the present invention, a garbage stock section (1) for containing garbage and a decompression chamber section for internally installing an incinerator main body section are provided. (2) and the incinerator unit (3), which are roughly classified, and the food waste stock unit (1) includes a stock hopper (11) and a hopper lid (12).
And a cutting shutter (13) for separating a predetermined amount from the stock garbage (1a) to obtain the next processed cut garbage (1b)
And a shutter drive cylinder (1
4) and an object presence / absence confirmation sensor (15) for detecting the presence / absence of food waste to be processed. The food waste stock section (1) is installed above the decompression chamber section (2).
The decompression chamber part (2) includes a chamber inlet closed door (21), a closed door opening / closing cylinder (22) for opening and closing the door, a chamber (23), and an ash discharge door (24).
The chamber inlet closing door (21) and the ash discharge door (24) are closed, and the chamber exhaust pipe (51) provided on the side surface of the chamber (23) is evacuated by the vacuum pump (54). 23) The inside pressure is reduced. The chamber inlet hermetically closed door (21) is also opened and closed with the function of the bottom door of the food waste stock section (1). Inside the chamber (23), the incinerator body (31) has the incinerator legs (38).
The upper door (32) of the drying chamber and the upper door opening / closing cylinder (33) for opening and closing the drying chamber upper door (32)
An intermediate door (34) and an intermediate door opening / closing cylinder (35) for opening / closing thereof, a combustion chamber lower door (36) and a lower door opening / closing cylinder (37) for opening / closing thereof are provided, and the upper chamber is a drying chamber (3a).
And the lower chamber is the combustion chamber (3b). Close the cut-out shutter (13), and the raw garbage that is partitioned between the closing door (21) for closing the chamber inlet is next processed. Cut-out raw garbage (1b)
As a result, the intermediate door (34) of the incinerator body (31) is closed, the drying chamber upper door (32) is opened, then the chamber inlet closing door (21) is opened, and the next-processing cut-out garbage (1b) is opened.
Drop into the drying room (3a) and dry in the drying room (1c)
Then, the drying chamber upper door (32) and the chamber inlet closing door (21) are closed. The raw garbage stock section (2) opens the cutting shutter (13) as the preparation for the next treatment, lowers the stock garbage (1a) by its own weight, and the sensor for detecting the presence / absence of the object (15) detects the raw garbage (1b) for the next processing. Check the presence and wait. By operating the vacuum pump (54), the gas inside the chamber (21) is moved to the chamber exhaust pipe (5).
The inside of the decompression chamber part (2) is decompressed by being exhausted from the cooling trap (52) from the (1), and at the same time, the drying chamber (3
a) and the gas inside the combustion chamber (3b) through the communication space (49) from the drying chamber exhaust pipe (50) to the cooling trap (5).
After 2), it is exhausted and decompressed. A microwave waveguide (42) for heating is provided on the side surface of the drying chamber of the incinerator body (31).
And a magnetron (41), and a waveguide lid (43) made of a microwave transparent material is attached to the drying chamber connecting portion of the waveguide (42). Further, a metal net-like air-permeable lid is attached to the exhaust pipe lid (4) at the connecting portion of the drying chamber exhaust pipe (50) and the connecting portion of the communicating pipe (49), respectively.
5), as a connecting pipe lid (44). When microwave (1c) in the drying room is heated under reduced pressure, microwaves are absorbed inside the garbage and turned into heat, increasing internal vapor pressure and transferring moisture inside the garbage to the outside, while moisture is saturated steam. Start evaporation at a low temperature corresponding to the pressure. The evaporated water vapor is sucked and discharged from the drying chamber exhaust pipe (50) to the cooling trap (52) by the operation of the vacuum pump (54).
The humidity sensor (46) of the drying chamber (3a) senses the dry state of the drying chamber garbage (1c) to detect the drying based on the change in humidity, and then the intermediate door (34) is opened to dry the combustion chamber (3b). After that, throw in the garbage and put in the middle door (3
4) is closed and it becomes the combustion chamber garbage (1d). The raw garbage (1b) cut out from the raw garbage stock section (1) is dropped again into the drying chamber (3a) by the above-mentioned operation to form the drying chamber raw garbage (1c). As a result, the dry room garbage (1
c) and the combustion chamber food waste (1d) are stored in the respective processing chambers, and thereafter, drying and combustion are performed simultaneously. From the oxygen gas generator to the combustion chamber (3b), the check valve for oxygen (5
8) and oxygen through the oxygen supply pipe (57), the combustion burner (47) ignites the combustion chamber garbage (1d), and supplies oxygen to cause the garbage to self-burn. Due to the operation of the vacuum pump (54), the combustion gas in the combustion chamber (3b) is sucked into the drying chamber (3a) through the communication pipe (49) connecting the combustion chamber and the drying chamber, and the drying chamber exhaust pipe (as well as the evaporation vapor in the drying chamber) ( 50) is sucked and discharged into the cooling trap (52), cooled in the cooling trap (52), and the evaporated water vapor is condensed and dropped to separate water and water. Combustion gas is exhausted from the cooling trap (52) through the vacuum pump pipe (53). The evacuation speed capability of the vacuum pump (54) is selected to be sufficiently larger than the sum of the amount of evaporated water vapor in the drying chamber, the amount of oxygen supplied to the combustion chamber, and the amount of combustion gas generated, and the depressurized state during processing is maintained. The combustion state of the garbage in the combustion chamber is sensed by the temperature sensor (48), and after the completion of combustion is detected by the temperature change of the temperature sensor (48), the oxygen supply is stopped and the lower door (36) of the combustion chamber is opened. The incinerated food waste ash is dropped and stored in the ash receiving box (70). Then, the lower door of the combustion chamber (36) is closed to handle the next process. Ash receiving box (70)
Is an incinerator leg (38) at the four corners that supports the incinerator (31)
Between them and below the lower door (36) of the combustion chamber. Repeating the above drying process and burning process,
When there is no food waste in the drying chamber (3a), that is, when the food waste to be treated is sequentially dried and incinerated and the last combustion chamber food waste (1d) is incinerated, it goes to the drying chamber (3a). The water valve (63) is opened, an appropriate amount of water is supplied from the water supply pipe (61) through the water check valve (62), microwave heating is performed, and steam is generated in the drying chamber (3a). Along with the combustion gas sucked into the drying chamber, it is discharged from the drying chamber exhaust pipe (50) to the cooling trap (52) and cooled in the cooling trap (52). Combustion gas is cooled trap (5
It is exhausted from 2) through the vacuum pump pipe (53). After incinerating the total amount of food waste in the food waste stock section (1), the ash receiving box (70) containing the incinerated ash is discharged from the ash discharge door (24) provided on the lower side surface of the chamber (23). To do. The present invention is a food waste reduced pressure dry incineration apparatus and a combustion exhaust gas treatment method having the above-mentioned configurations.

【0005】[0005]

【作用】上記のように構成された生ごみの焼却装置を稼
働すると、処理生ごみの全量から、一定量毎、順次、乾
燥処理、燃焼焼却処理が行われる。生ごみは含有水分が
大変多いが、一定処理量毎に、減圧下でマイクロ波加熱
されると、真空度によって水分蒸発が飽和蒸気圧に対応
した低温度で始まり、マイクロ波が生ごみ表面から内部
にまで浸透し、そのエネルギーは直接水分子に吸収され
熱に変るので、内部蒸気圧を高め内部の水分を外部に移
行する作用が有る。マイクロ波加熱の効率は、対象物の
量により大きく変化することが知られており、処理量を
一定量とすることにより高効率のマイクロ波活用ができ
る。また、燃焼室での生ごみ燃焼によって、乾燥室(3
a)に燃焼室(3b)の燃焼ガスが吸引流入されるので
燃焼ガスによっても乾燥室生ごみ(1c)の加熱がなさ
れ水分蒸発を促進する。この燃焼ガスは乾燥室内の蒸発
水蒸気と接触し混合状態となり、真空ポンプ(54)に
より乾燥室排気配管(50)から冷却トラップ(52)
に吸引排気され、燃焼ガスの流入・排気が気流となり、
乾燥室の蒸発水蒸気の排出を効果的に行うことができる
のである。乾燥室の湿度センサー(46)により乾燥状
態をセンシングし、乾燥を検知し、制御系によりマイク
ロ波の照射を停止し過剰照射を防止することができる。
乾燥した後、焼却室(3b)に投入された生ごみを減圧
下で酸素を供給し、着火すると、酸素供給量に応じた燃
焼速度で自燃する。燃焼ガスは、連通管(49)から吸
引排気されるので、酸素供給量制御により燃焼速度のコ
ントロールが可能となる。燃焼室温度センサー(48)
により燃焼室温度をセンシングし、燃焼完了を検知し、
制御系により酸素の供給を停止し過剰供給を防止する。
このように、乾燥工程と、燃焼工程を分けて、同時進行
処理を行うことにより、生ごみ焼却が効率よく行われ焼
却灰として著しく減容化できる。燃焼室で発生する燃焼
ガスは、前記のごとく、乾燥室内へ吸引され減圧マイク
ロ波加熱による蒸発水蒸気と接触混合状態となり、燃焼
ガスは蒸発水蒸気により冷却されながら、乾燥室(3
a)から乾燥室排気配管(50)内を通って蒸発水蒸気
とともに、冷却トラップ(52)へ吸引されて冷却トラ
ップ(52)内で冷却され、蒸発水蒸気と燃焼ガスの接
触混合状態から蒸発水蒸気が冷えて凝結し水滴となり冷
却トラップ(52)の底部に溜まる。燃焼ガスは、蒸発
水蒸気の凝結がなされる過程で燃焼ガスに含まれた煤塵
や煙や有害ガスや臭気が洗浄される。冷却トラップ(5
2)内で、水蒸気と気水分離された洗浄後の燃焼ガス
は、真空ポンプ配管(53)から真空ポンプ(54)、
ミストトラップ(55)を経て排気され燃焼排ガス処理
がなされる。冷却トラップ(52)内の溜水はドレーン
バルブ(56)より適宜排出できる。本発明の装置は、
処理生ごみの全量から、一定量毎、順次、乾燥処理、焼
却処理が行われので、乾燥室(3a)・燃焼室(3b)
を構成する焼却炉本体(31)を小形化することができ
る。また、焼却炉本体(31)が、減圧チャンバー部
(2)内に設置され、減圧によって、チャンバー(2
3)内の気体が希薄となりチャンバー素材への対流伝熱
が少なくなるので、減圧チャンバー部(2)の温度上昇
が低減され、焼却装置設置場所周辺への安全性も高いも
のである。
When the food waste incinerator configured as described above is operated, drying treatment and combustion incineration treatment are sequentially performed from the total amount of the treated food waste for every fixed amount. Food waste contains a large amount of water, but when it is heated in a microwave under reduced pressure for each fixed amount of processing, evaporation of water starts at a low temperature corresponding to the saturated vapor pressure due to the degree of vacuum, and microwaves start from the surface of the food waste. It penetrates to the inside, and its energy is directly absorbed by water molecules and converted into heat, which has the effect of increasing the internal vapor pressure and transferring the internal moisture to the outside. It is known that the efficiency of microwave heating varies greatly depending on the amount of the object, and the microwave can be utilized with high efficiency by keeping the treatment amount constant. In addition, by burning food waste in the combustion chamber, the drying chamber (3
Since the combustion gas in the combustion chamber (3b) is sucked into the a), the combustion chamber gas also heats the drying chamber garbage (1c) to accelerate the evaporation of water. This combustion gas comes into contact with vaporized water vapor in the drying chamber and enters a mixed state, and a vacuum pump (54) is used to cool the trap (52) from the drying chamber exhaust pipe (50).
Are sucked and exhausted into the
The vaporized water vapor in the drying chamber can be effectively discharged. The humidity sensor (46) in the drying chamber can detect the dry state to detect the dry state, and the control system can stop the microwave irradiation to prevent the excessive irradiation.
After being dried, oxygen is supplied to the food waste put in the incinerator (3b) under reduced pressure, and when ignited, the food waste self-combusts at a burning rate according to the oxygen supply amount. Since the combustion gas is sucked and exhausted from the communication pipe (49), the combustion rate can be controlled by controlling the oxygen supply amount. Combustion chamber temperature sensor (48)
Senses the temperature of the combustion chamber, detects the completion of combustion,
The control system stops the supply of oxygen to prevent excess supply.
As described above, by performing the simultaneous process by dividing the drying process and the combustion process, the incineration of food waste is efficiently performed, and the volume of incinerated ash can be significantly reduced. As described above, the combustion gas generated in the combustion chamber is sucked into the drying chamber and brought into a contact mixing state with the vaporized water vapor by the depressurized microwave heating.
From a), it is sucked into the cooling trap (52) and cooled in the cooling trap (52) together with the evaporative steam through the drying chamber exhaust pipe (50), and the evaporative steam is evaporated from the contact mixed state of the evaporative steam and the combustion gas. It cools and condenses into water droplets that collect on the bottom of the cooling trap (52). The combustion gas is cleaned of soot dust, smoke, harmful gas and odor contained in the combustion gas in the process of condensing the evaporated water vapor. Cooling trap (5
The combustion gas after cleaning, which is separated from water vapor and steam in 2), is transferred from the vacuum pump pipe (53) to the vacuum pump (54),
The exhaust gas is exhausted through the mist trap (55) and treated as combustion exhaust gas. The accumulated water in the cooling trap (52) can be appropriately discharged through the drain valve (56). The device of the present invention is
From the total amount of processed food waste, a fixed amount is sequentially dried and incinerated, so the drying chamber (3a) and combustion chamber (3b)
It is possible to downsize the incinerator body (31) constituting the. In addition, the incinerator body (31) is installed in the decompression chamber part (2), and the chamber (2
Since the gas in 3) is diluted and the convective heat transfer to the chamber material is reduced, the temperature rise in the decompression chamber section (2) is reduced, and the safety around the installation site of the incinerator is high.

【0005】[0005]

【実施例】以下、本発明の実施例について説明する。こ
の焼却装置は、生ごみを収容する生ごみストック部
(1)と、焼却炉本体部を内蔵設置する減圧チャンバー
部(2)、および、焼却装置部(3)によって大別構成
され、処理生ごみの全量から、一定量毎分別し、順次、
乾燥処理、燃焼焼却処理を行っていき、その生ごみ全量
の焼却を完了する。生ごみストック部(1)は、ストッ
クホッパー(11)と、ホッパー蓋(12)と、ストッ
ク生ごみ(1a)から所定量を分別し次処理切出し生ご
み(1b)とする切出しシャッター(13)と、これを
開閉駆動するシャッター駆動シリンダー(14)と、処
理すべき生ごみの有無を検知する物有無確認センサー
(15)からなり、この生ごみストック部(1)を、減
圧チャンバー部(2)のチャンバー投入口密閉扉(2
1)をストックホッパー(11)の底扉を兼ねるように
してその上部に設置する。減圧チャンバー部(2)は、
チャンバー投入口密閉扉(21)と、これを開閉駆動す
る密閉扉開閉シリンダー(22)と、チャンバー(2
3)と、灰排出扉(24)からなり、チャンバー投入口
密閉扉(21)と灰排出扉(24)を閉じて、チャンバ
ー(23)の側面に設けたチャンバー排気配管(51)
から真空ポンプ(54)で排気を行うとチャンバー(2
3)内が減圧される。チャンバー投入口密閉扉(21)
は、生ごみストック部(1)の底扉の機能を兼ねて開閉
される。チャンバー(23)内に、焼却炉本体(31)
が焼却炉脚(38)で支持設置され、焼却炉本体(3
1)に、乾燥室上扉(32)とその開閉用に上扉開閉シ
リンダー(33)、中間扉(34)とその開閉用に中間
扉開閉シリンダー(35)、燃焼室下扉(36)とその
開閉用に下扉開閉シリンダー(37)が設けられ、上室
を乾燥室(3a)とし、下室を燃焼室(3b)とする。
切出しシャッター(13)を閉じて、チャンバー投入口
密閉扉(21)との間に仕切られる生ごみを次処理切出
し生ごみ(1b)として、焼却炉本体(31)の中間扉
(34)を閉じて、乾燥室上扉(32)を開け、次いで
チャンバー投入口密閉扉(21)を開け、次処理切出し
生ごみ(1b)を乾燥室(3a)に落下投入し、乾燥室
生ごみ(1c)とし、乾燥室上扉(32)とチャンバー
投入口密閉扉(21)を閉じる。生ごみストック部
(2)は、次の処理準備として切出しシャッター(1
3)を開け、ストック生ごみ(1a)を自重降下させ、
物有無確認センサー(15)によって次処理切出し生ご
み(1b)の有無を確認し待機する。真空ポンプ(5
4)作動によって、減圧チャンバー部(2)内部の気体
がチャンバー排気配管(51)から冷却トラップ(5
2)と真空ポンプ配管(53)を経て排気されて減圧チ
ャンバー部(2)の内部が減圧され、同時に乾燥室(3
a)および連通間(49)を介して燃焼室(3b)内部
の気体が乾燥室排気配管(50)から冷却トラップ(5
2)と真空ポンプ配管(53)を経て排気され減圧され
る。乾燥室排気配管(50)のチャンバー(23)側板
の貫通部は気密を保てるよう溶接接合をする。金属製の
焼却炉本体(31)の乾燥室部側面に加熱用にマイクロ
波の導波管(42)とマグネトロン(41)が設けら
れ、導波管(42)の乾燥室内接続部にはマイクロ波透
過材でできた導波管蓋(43)を取り付ける。また乾燥
室排気配管(50)の接続部と、連通管(49)の乾燥
室内接続部に、金属製のネット状で通気性の有る蓋をそ
れぞれ排気管蓋(45)、連通管蓋(44)として取り
付ける。乾燥室生ごみ(1c)を減圧下でマイクロ波加
熱すると、真空度によって水分蒸発が飽和蒸気圧に対応
した低温度で始まり、マイクロ波が、生ごみ表面から内
部まで浸透し、マイクロ波エネルギーは直接水分子に吸
収され熱に変るので、内部蒸気圧を高めて生ごみ内部の
水分をも外部に移行するとともに、水分は飽和蒸気圧に
対応した低温度で蒸発を始め、生ごみ温度を高めるほど
蒸発が盛んに行なわれる。マイクロ波加熱の効率は、対
象物の量により大きく変化することが知られており、処
理量を一定量とすることにより高効率のマイクロ波活用
ができる。蒸発水蒸気は真空ポンプ(54)の作動によ
り乾燥室排気配管(50)から冷却トラップ(52)へ
排出される。乾燥室(3a)の湿度センサー(46)に
よって、乾燥室生ごみ(1c)の乾燥状態をセンシング
して湿度変化から乾燥を検知した後、中間扉(34)を
開き、燃焼室(3b)へ乾燥後の生ごみを落下投入し、
中間扉(34)を閉じて、燃焼室生ごみ(1d)とす
る。湿度センサー(46)と制御系によって、マイクロ
波の照射を制御し過剰照射を防止する。生ごみストック
部(1)から次処理切出し生ごみ(1b)を再び、前述
の動作で乾燥室(3a)に、落下投入し乾燥室生ごみ
(1c)とする。これによって乾燥室生ごみ(1c)と
燃焼室生ごみ(1d)がそれぞれの処理室に収容され
て、以後、乾燥処理と燃焼焼却処理とを同時進行ですす
める。燃焼室(3b)に酸素ガス発生装置から酸素用逆
止弁(58)と、酸素供給配管(57)を経て、減圧下
で、酸素を供給し、着火バーナー(47)で、燃焼室生
ごみ(1d)に着火し、酸素を供給することにより生ご
みを自燃させ、燃焼ガスを真空ポンプ(54)の作動に
より、燃焼室と乾燥室を結ぶ連通管(49)を通して乾
燥室(3a)の蒸発水蒸気とともに乾燥室排気配管(5
0)から冷却トラップ(52)へ排出する。この時、燃
焼ガスの乾燥室(3a)への流入・排気が気流となっ
て、乾燥室(3a)の蒸発水蒸気の排出を効果的に行う
ことができる。燃焼室(3b)の燃焼室生ごみ(1d)
の燃焼速度は酸素供給量制御でコントロールができる。
酸素供給配管(57)のチャンバー(23)側板の貫通
部は、気密性が保てるよう溶接接合とする。燃焼室内の
生ごみの燃焼状態は、温度センサー(48)でセンシン
グし、温度センサー(48)の温度変化によって燃焼完
了を検知した後、酸素供給を停止し、燃焼室下扉(3
6)を開き、焼却された生ごみ灰を灰受箱(70)に落
下収容する。次いで、燃焼室下扉(36)を閉じ次の処
理に対応する。灰受箱(70)は、焼却炉(31)を支
持する四隅の焼却炉脚(38)の間に、燃焼室下扉(3
6)の下方になるよう配置する。真空ポンプ(54)の
排気速度能力を、乾燥室蒸発水蒸気量と、燃焼室への供
給酸素量と、燃焼ガス発生量との加算量より充分大きく
選定し、処理中の減圧状態を維持する。上記の乾燥工程
および燃焼工程を繰り返し行って、乾燥室(3a)に生
ごみの無くなった状態では、つまり、処理すべき生ごみ
を、順次、乾燥・焼却処理してきて最後の燃焼室生ごみ
(1d)を焼却する時、乾燥室(3a)に水用バルブ
(63)を開いて、水用逆止弁(62)を経て、給水配
管(61)より適量の給水を行って、マイクロ波加熱
し、乾燥室(3a)に水蒸気を発生し、乾燥室に吸引さ
れる燃焼ガスとともに乾燥室排気配管(50)から冷却
トラップ(52)へ排出する。給水配管(61)のチャ
ンバー(23)側板の貫通部は、気密性が保てるように
溶接接合とする。生ごみストック部(1)内の生ごみの
全量を焼却処理した後、焼却灰を収容した灰受箱(7
0)を、チャンバー(23)の下部側面に設けた灰排出
扉(24)から排出する。このように、乾燥工程と、燃
焼工程を分けて、同時進行処理を行うことにより、生ご
み焼却が効率よく行われ焼却灰として著しく減容化され
る。燃焼室で発生する燃焼ガスは、前記のごとく、乾燥
室内へ吸引され減圧マイクロ波加熱による蒸発水蒸気と
接触混合状態となる。燃焼ガスは蒸発水蒸気により冷却
されながら、乾燥室排気配管(50)から蒸発水蒸気と
ともに、冷却トラップ(52)へ吸引されて冷却され、
水蒸気が冷えて凝結し気水分離され、水滴となり、冷却
トラップ内の底部に溜まる。溜水はドレーンバルブ(5
6)より適宜、排出できる。生ごみに食品容器などのプ
ラスチックが一部混入することも有り、排出ガスの洗浄
も配慮を要する。燃焼ガスは、減圧マイクロ波加熱によ
る蒸発水蒸気とともに、乾燥室(3a)から排出され、
冷却トラップ(52)内での冷却によって、蒸発水蒸気
の凝結がなされる過程で燃焼ガスに含まれた煤塵や煙や
有害ガスや臭気が洗浄される。洗浄後の燃焼ガスは冷却
トラップ(52)から真空ポンプ配管(53)、真空ポ
ンプ(54)、ミストトラップ(55)を経て排気され
る。本発明の装置は、処理生ごみの全量から、一定量毎
分別し、順次、乾燥処理、焼却処理が行われので、乾燥
室(3a)・燃焼室(3b)を構成する焼却炉本体(3
1)を小形化することができる。また、焼却炉本体(3
1)が、減圧チャンバー部(2)内に設置され、減圧に
よって、チャンバー(23)内の気体が希薄となりチャ
ンバー素材への対流伝熱が少なくなるので、減圧チャン
バー部(2)の温度上昇が低減され、焼却装置設置場所
周辺へ影響も少なく、安全性を高めることができる。
EXAMPLES Examples of the present invention will be described below. This incinerator is roughly divided into a food waste stock section (1) for storing food waste, a decompression chamber section (2) having a main body of an incinerator installed therein, and an incinerator section (3). From the total amount of trash, a certain amount of waste is sorted and sorted,
Drying and combustion incineration will be carried out to complete the incineration of all the garbage. The raw garbage stock part (1) is a stock hopper (11), a hopper lid (12), and a cutting shutter (13) that separates a predetermined amount from the stock garbage (1a) to obtain the next processed raw garbage (1b). And a shutter drive cylinder (14) for opening and closing this, and an object presence / absence confirmation sensor (15) for detecting the presence or absence of food waste to be processed. This food waste stock section (1) is connected to the decompression chamber section (2). ) Chamber inlet closed door (2
1) is installed on the upper part of the stock hopper (11) so that it also serves as the bottom door. The decompression chamber part (2) is
The chamber inlet closed door (21), the closed door opening / closing cylinder (22) for opening and closing the door, and the chamber (2
3) and an ash discharge door (24), the chamber inlet sealing door (21) and the ash discharge door (24) are closed, and a chamber exhaust pipe (51) provided on the side surface of the chamber (23).
From the chamber (2
3) The inside pressure is reduced. Chamber entrance closed door (21)
Is opened and closed with the function of the bottom door of the food waste stock section (1). In the incinerator body (31) in the chamber (23)
Are supported and installed on the incinerator legs (38), and the incinerator body (3
1), a drying chamber upper door (32) and an upper door opening / closing cylinder (33) for opening / closing thereof, an intermediate door (34) and an intermediate door opening / closing cylinder (35) for opening / closing thereof, and a combustion chamber lower door (36). A lower door opening / closing cylinder (37) is provided for opening and closing the upper chamber as a drying chamber (3a) and a lower chamber as a combustion chamber (3b).
The cutting shutter (13) is closed, and the garbage separated from the chamber inlet closed door (21) is used as the next processing cutting garbage (1b), and the intermediate door (34) of the incinerator body (31) is closed. , The drying chamber upper door (32) is opened, the chamber inlet closing door (21) is then opened, and the next-processed cut-out garbage (1b) is dropped into the drying chamber (3a) to form the drying chamber garbage (1c). , The drying chamber upper door (32) and the chamber inlet closing door (21) are closed. The raw garbage stock section (2) uses the cutting shutter (1
3) Open and let the stock garbage (1a) drop by its own weight.
The presence / absence confirmation sensor (15) confirms the presence / absence of the raw garbage (1b) to be processed next, and stands by. Vacuum pump (5
4) By the operation, the gas inside the decompression chamber part (2) is cooled by the cooling trap (5) from the chamber exhaust pipe (51).
2) and the vacuum pump pipe (53) are evacuated to reduce the pressure inside the decompression chamber section (2), and at the same time, the drying chamber (3
a) and the gas inside the combustion chamber (3b) through the communication space (49) from the drying chamber exhaust pipe (50) to the cooling trap (5).
2) and the vacuum pump pipe (53) to evacuate and reduce the pressure. The penetration portion of the chamber (23) side plate of the drying chamber exhaust pipe (50) is welded so as to keep airtightness. A microwave waveguide (42) and a magnetron (41) are provided for heating on the side surface of the drying chamber of the metal-made incinerator body (31), and a microwave is connected to the drying chamber connecting portion of the waveguide (42). Attach a waveguide lid (43) made of wave transparent material. Further, a metal net-like and air-permeable lid is connected to the connecting portion of the drying chamber exhaust pipe (50) and the connecting portion of the communicating pipe (49) to the exhaust pipe lid (45) and the communicating pipe lid (44), respectively. ) To install. When microwave oven food waste (1c) is heated under reduced pressure, moisture evaporation starts at a low temperature corresponding to the saturated vapor pressure due to the degree of vacuum, microwaves penetrate from the garbage surface to the inside, and microwave energy is directly transmitted. Since it is absorbed by water molecules and converted to heat, the internal vapor pressure is increased and the moisture inside the food waste is also transferred to the outside, and the moisture starts to evaporate at a low temperature corresponding to the saturated vapor pressure, and the higher the food waste temperature is. Evaporation is active. It is known that the efficiency of microwave heating varies greatly depending on the amount of the object, and the microwave can be utilized with high efficiency by keeping the treatment amount constant. The vaporized water vapor is discharged from the drying chamber exhaust pipe (50) to the cooling trap (52) by the operation of the vacuum pump (54). The humidity sensor (46) of the drying chamber (3a) senses the dry state of the drying chamber garbage (1c) to detect the drying based on the change in humidity, and then the intermediate door (34) is opened to dry the combustion chamber (3b). Drop the garbage afterwards,
The intermediate door (34) is closed to form the combustion chamber garbage (1d). A humidity sensor (46) and a control system control the irradiation of microwaves to prevent excessive irradiation. The raw garbage (1b) cut out from the raw garbage stock section (1) is dropped again into the drying chamber (3a) by the above-mentioned operation to form the drying chamber raw garbage (1c). As a result, the dry room garbage (1c) and the combustion room garbage (1d) are stored in the respective processing chambers, and thereafter, the drying process and the combustion incineration process are simultaneously advanced. Oxygen is supplied to the combustion chamber (3b) from the oxygen gas generator through the oxygen check valve (58) and the oxygen supply pipe (57) under reduced pressure, and the ignition burner (47) supplies the combustion chamber garbage ( 1d) is ignited, oxygen is supplied to cause the garbage to self-combust, and the combustion gas is evaporated by the vacuum pump (54) through the communication pipe (49) connecting the combustion chamber and the drying chamber to the drying chamber (3a). Exhaust pipe (5) with drying chamber
0) to the cooling trap (52). At this time, the inflow / exhaust of the combustion gas into the drying chamber (3a) becomes an air flow, and the evaporated water vapor in the drying chamber (3a) can be effectively discharged. Combustion chamber garbage (1d) in the combustion chamber (3b)
The combustion rate of can be controlled by controlling the oxygen supply.
The penetrating portion of the side plate of the chamber (23) of the oxygen supply pipe (57) is welded to maintain airtightness. The combustion state of the garbage in the combustion chamber is sensed by the temperature sensor (48), and after the completion of combustion is detected by the temperature change of the temperature sensor (48), the oxygen supply is stopped, and the combustion chamber lower door (3
6) is opened, and the incinerated food waste ash is dropped and stored in the ash receiving box (70). Then, the lower door of the combustion chamber (36) is closed to handle the next process. The ash receiving box (70) has a lower combustion chamber door (3) between the incinerator legs (38) at four corners supporting the incinerator (31).
Place it so that it is below 6). The evacuation speed capability of the vacuum pump (54) is selected to be sufficiently larger than the sum of the amount of evaporated water vapor in the drying chamber, the amount of oxygen supplied to the combustion chamber, and the amount of combustion gas generated, and the depressurized state during processing is maintained. By repeating the above-mentioned drying process and combustion process, when there is no food waste in the drying chamber (3a), that is, the food waste to be processed is sequentially dried and incinerated, and the last combustion chamber food waste (1d ) Is incinerated, the water valve (63) is opened in the drying chamber (3a), an appropriate amount of water is supplied from the water check valve (62) through the water supply pipe (61), and microwave heating is performed. The steam is generated in the drying chamber (3a) and is discharged from the drying chamber exhaust pipe (50) to the cooling trap (52) together with the combustion gas sucked in the drying chamber. The penetrating portion of the side plate of the chamber (23) of the water supply pipe (61) is welded so as to maintain airtightness. After incineration of all the garbage in the garbage stock section (1), the ash receiving box (7) containing the incinerated ash
0) is discharged from the ash discharge door (24) provided on the lower side surface of the chamber (23). In this way, by performing the simultaneous progress treatment by dividing the drying process and the combustion process, the incineration of food waste is efficiently performed and the volume of incinerated ash is remarkably reduced. As described above, the combustion gas generated in the combustion chamber is sucked into the drying chamber and brought into a contact mixing state with the vaporized water vapor generated by the reduced pressure microwave heating. While the combustion gas is cooled by the evaporative steam, the combustion gas is sucked into the cooling trap (52) together with the evaporative steam from the drying chamber exhaust pipe (50) and cooled,
The water vapor cools, condenses, and is separated into air and water to form water droplets, which accumulate at the bottom of the cooling trap. Drain valve (5
It can be appropriately discharged from 6). Since some plastics such as food containers may be mixed in the garbage, it is necessary to consider the cleaning of exhaust gas. The combustion gas is discharged from the drying chamber (3a) together with the vaporized water vapor generated by the reduced pressure microwave heating,
By cooling in the cooling trap (52), soot dust, smoke, harmful gas, and odor contained in the combustion gas are washed away in the process of condensation of evaporated water vapor. The combustion gas after cleaning is exhausted from the cooling trap (52) through the vacuum pump pipe (53), the vacuum pump (54) and the mist trap (55). The apparatus of the present invention separates a fixed amount of the total amount of the treated food waste into a fixed amount and sequentially performs the drying process and the incineration process. Therefore, the incinerator main body (3) that configures the drying chamber (3a) and the combustion chamber (3b).
1) can be miniaturized. In addition, the incinerator body (3
1) is installed in the decompression chamber part (2), and the decompression reduces the gas in the chamber (23) and reduces the convective heat transfer to the chamber material, so that the temperature rise in the decompression chamber part (2). It is reduced, the impact around the installation site of the incinerator is small, and the safety can be improved.

【0007】[0007]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。処
理生ごみの全量から、一定量毎に分別し、乾燥処理およ
び、燃焼焼却処理を順次行うことができるので、乾燥処
理条件と、燃焼焼却処理条件のそれぞれを、最適に選定
でき、効率良く、安定的に生ごみの焼却処理が遂行でき
得る。マイクロ波加熱の効率は対象物の誘電損失係数と
その量により大きく変化するが処理生ごみの量を一定量
毎とすることにより、生ごみの平均的構成素材を基に、
高効率の照射条件の選択が出来ることから、エネルギー
ロスを小さくできる。減圧マイクロ波加熱で生ごみの乾
燥を行う時、減圧真空度によって、飽和蒸気圧に対応し
た低温度で水分蒸発が始まり、生ごみ温度が高くなる
程、活発に蒸発する。マイクロ波エネルギーが生ごみ内
部まで浸透し、直接水分子に吸収されて熱に変るので、
内部蒸気圧を高めて生ごみ内部の水分をも外部に移行す
る。故に、生ごみの深部まで急速に加熱されて低温度で
急速乾燥ができる。燃焼室の燃焼ガスを乾燥室を経由し
て排気するので、乾燥室生ごみの加熱効果が有り、且
つ、燃焼ガスの流入・流出の気流が、乾燥室の蒸発水蒸
気の排出を促進する。燃焼ガスは蒸発水蒸気と混合状態
で冷却とラップに吸引排出され、冷却トラップ内で冷却
され、蒸発水蒸気の凝結がなされる過程で燃焼ガスに含
まれた煤塵や煙や有害ガスや臭気が洗浄されて、その
後、真空ポンプを経て、ミストトラップのフィルターを
透して清浄にして排気することが出来る。生ごみは酸素
焼却による充分な燃焼が行われるので減容化効果が大き
い。一定量毎に分別処理するので、焼却炉本体が小形化
でき、焼却装置全体としての小形化が可能となる。発熱
部である焼却炉本体が減圧チャンバー部の中に設置され
るので、焼却装置の外郭となる減圧チャンバー部表面の
温度を低く押さえることが出来る。減圧チャンバー部表
面の温度が低く、焼却装置設置場所周辺への影響が少な
く、安全性が高い焼却装置を提供することができる。
Since the present invention is constructed as described above, it has the following effects. From the total amount of treated food waste, it is possible to sort by a fixed amount, and the drying treatment and the combustion incineration treatment can be performed sequentially, so that each of the drying treatment condition and the combustion incineration treatment condition can be optimally selected and efficiently, It is possible to stably incinerate food waste. The efficiency of microwave heating varies greatly depending on the dielectric loss coefficient of the object and its amount, but by setting the amount of treated garbage to a fixed amount, based on the average constituent material of garbage,
Energy loss can be reduced because high-efficiency irradiation conditions can be selected. When the raw garbage is dried by the reduced pressure microwave heating, the evaporation of water starts at a low temperature corresponding to the saturated vapor pressure due to the vacuum degree of the reduced pressure, and the higher the temperature of the raw garbage, the more vigorous the evaporation. Microwave energy penetrates into the garbage and is directly absorbed by water molecules and converted into heat.
By increasing the internal vapor pressure, the water inside the food waste is also transferred to the outside. Therefore, it is rapidly heated to the deep part of the garbage and can be rapidly dried at a low temperature. Since the combustion gas in the combustion chamber is exhausted through the drying chamber, there is a heating effect for the garbage in the drying chamber, and the inflow / outflow air flow of the combustion gas promotes the discharge of evaporated water vapor in the drying chamber. Combustion gas is sucked and discharged into a cooling wrap in a mixed state with vaporized steam, cooled in a cooling trap, and soot, smoke, harmful gas and odor contained in the combustion gas are washed in the process of condensation of vaporized steam. Then, after passing through the vacuum pump, the filter of the mist trap can be passed through to be cleaned and exhausted. Since garbage is burned sufficiently by incineration with oxygen, it has a large volume reduction effect. As the incinerator body can be miniaturized because it is separated and processed for each fixed amount, it is possible to miniaturize the incinerator as a whole. Since the incinerator body, which is the heat generating part, is installed in the decompression chamber part, the temperature of the surface of the decompression chamber part, which is the outer shell of the incinerator, can be kept low. The temperature of the surface of the decompression chamber is low, there is little influence on the surroundings of the installation location of the incinerator, and the incinerator with high safety can be provided.

【0008】[0008]

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

【図1】本発明の生ごみ減圧乾燥焼却装置の実施例を示
す要部縦断面と機器構成を示す構成図
FIG. 1 is a configuration diagram showing a longitudinal cross section and a device configuration of a main part showing an embodiment of a reduced-pressure drying and incinerating apparatus for raw garbage of the present invention.

【図2】生ごみストック部の実施例を示す縦断面図FIG. 2 is a vertical cross-sectional view showing an embodiment of a food waste stock section.

【図3】減圧チャンバー部の実施例を示す縦断面図FIG. 3 is a vertical cross-sectional view showing an example of a decompression chamber section.

【図4】焼却装置部の実施例を示す焼却炉本体縦断面と
機器構成を示す構成図
FIG. 4 is a configuration diagram showing a vertical cross-section of the incinerator body showing an embodiment of an incinerator unit and a device configuration.

【符号の説明】[Explanation of symbols]

1 生ごみストック部 2 減圧チャン
バー部 3 焼却装置部 1a ストック生ごみ 1b 次処理切出
し生ごみ 1c 乾燥室生ごみ 1d 燃焼室生ご
み 1e 焼却灰 11 ストックホッパー 12 ホッパー蓋 13 切出しシャッター 14 シャッター
駆動シリンダー 15 物有無確認センサー 21 チャンバー
投入口密閉扉 22 密閉扉開閉シリンダー 23 チャンバー 24 灰排出扉 3a 乾燥室 3b 燃焼室 31 焼却炉本体 32 乾燥室上扉 33 上扉開閉シリンダー 34 中間扉 35 中間扉開閉シリンダー 36 焼却室下扉 37 下扉開閉シリンダー 38 焼却炉脚 41 マグネトロン 42 導波管 43 導波管蓋 44 連通管蓋 45 排気管蓋 46 湿度センサ
ー 47 着火バーナー 48 温度センサ
ー 49 連通管 50 乾燥室排気
配管 51 チャンバー排気配管 52 冷却トラッ
プ 53 真空ポンプ配管 54 真空ポンプ 55 ミストトラップ 56 ドレーンバ
ルブ 57 酸素供給配管 58 酸素用逆止
弁 59 酸素ガス発生装置 61 給水配管 62 水用逆止弁 63 水用バルブ 70 灰受箱
1 Garbage stock part 2 Decompression chamber part 3 Incinerator part 1a Stock garbage 1b Next processing cut out garbage 1c Drying room garbage 1d Combustion chamber garbage 1e Incineration ash 11 Stock hopper 12 Hopper lid 13 Cutting out shutter 14 Shutter drive cylinder 15 Presence or absence of objects Confirmation sensor 21 Chamber inlet closed door 22 Sealed door open / close cylinder 23 Chamber 24 Ash discharge door 3a Drying chamber 3b Combustion chamber 31 Incinerator body 32 Drying chamber upper door 33 Upper door opening / closing cylinder 34 Intermediate door 35 Intermediate door opening / closing cylinder 36 Incinerator chamber Lower door 37 Lower door opening / closing cylinder 38 Incinerator leg 41 Magnetron 42 Waveguide 43 Waveguide lid 44 Communication pipe lid 45 Exhaust pipe lid 46 Humidity sensor 47 Ignition burner 48 Temperature sensor 49 Communication pipe 50 Drying chamber exhaust pipe 51 Chamber exhaust Pipe 52 cooling trap 53 Vacuum pump pipe 54 vacuum pump 55 mist trap 56 drain valve 57 oxygen supply pipe 58 oxygen check valve 59 the oxygen gas generator 61 feed water pipe 62 water check valve 63 for water valve 70 ash receiving boxes

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F25D 7/00 ZAB Z F26B 21/00 K ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI technical display location F25D 7/00 ZAB Z F26B 21/00 K

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 生ごみストック部(1)として、ストッ
クホッパー(11)、ホッパー蓋(12)、切出しシャ
ッター(13)、物有無確認センサー(15)を備え、
減圧チャンバー部(2)の上部に設置し、減圧チャンバ
ー部(2)にはチャンバー投入口密閉扉(21)と灰排
出扉(24)を設け、チャンバー投入口密閉扉(21)
を、生ごみストック部(1)の底扉として、切出しシャ
ッター(13)で仕切った次処理切出し生ごみ(1b)
を、減圧チャンバー部(2)内に設置された焼却装置部
(3)の焼却炉本体(31)の乾燥室(3a)に、チャ
ンバー投入口密閉扉(21)と乾燥室上扉(32)を開
いて投入し、閉じて、真空ポンプ(54)の作動にて真
空ポンプ配管(53)、冷却トラップ(52)、チャン
バー排気配管(51)を介して減圧チャンバー部(2)
内の減圧と、乾燥室排気配管(50)を介して乾燥室
(3a)内の減圧とを行いつつ、乾燥室生ごみ(1c)
にマグネトロン(41)のマイクロ波を導波管(42)
を介して、照射加熱し、水分を蒸発させ乾燥し、乾燥室
に設けられた湿度センサー(46)の湿度変化から乾燥
状態を検知した後、中間扉(34)を開いて乾燥室生ご
み(1c)を燃焼室(3b)に落下投入し、燃焼室生ご
み(1d)とし、中間扉(34)を閉じて、乾燥室(3
a)には次処理切出し生ごみ(1b)を再び投入し乾燥
室生ごみ(1c)とし、乾燥を開始しするとともに、燃
焼室(3b)に酸素ガス発生装置(59)から酸素供給
配管(57)を介して酸素を供給しつつ、着火バーナー
(47)にて燃焼室生ごみ(1d)に着火し、自燃さ
せ、燃焼ガスは、燃焼室と乾燥室を結ぶ連通管(49)
により乾燥室(3a)へ吸引排気し、乾燥室蒸発水分と
ともに真空ポンプ(54)により冷却トラップ(52)
へ排出し、冷却トラップ(52)内で冷却し、燃焼ガス
と蒸発水蒸気を気水分離し、燃焼ガスを真空ポンプ配管
(53)を経て排気し、燃焼室内の生ごみの燃焼完了
は、温度センサー(48)の温度変化により検知した
後、燃焼室下扉(36)を開き、焼却された生ごみ灰を
灰受箱(70)に落下収容するようにして、上記の乾燥
工程および燃焼工程を繰り返し行い生ごみストック部
(1)内の生ごみの全量を焼却処理した後、灰排出扉
(24)から排出することを特徴とする生ごみ減圧乾燥
焼却装置。
1. A stock hopper (11), a hopper lid (12), a cutting shutter (13), and an object presence / absence confirmation sensor (15) as a raw garbage stock section (1),
It is installed in the upper part of the decompression chamber part (2), and the decompression chamber part (2) is provided with a chamber inlet closing door (21) and an ash discharging door (24), and the chamber inlet closing door (21).
Is used as the bottom door of the food waste stock section (1) and is divided by the cutting shutter (13) for the next processing cut out food waste (1b)
To the drying chamber (3a) of the incinerator body (31) of the incinerator unit (3) installed in the decompression chamber unit (2), the chamber inlet closing door (21) and the drying chamber upper door (32). Is opened and closed, and the vacuum pump (54) is operated to operate the vacuum pump pipe (53), the cooling trap (52), and the chamber exhaust pipe (51) through the decompression chamber section (2).
While reducing the internal pressure and the internal pressure of the drying chamber (3a) via the drying chamber exhaust pipe (50), the drying chamber garbage (1c)
The microwave of the magnetron (41) to the waveguide (42)
Via irradiation heating to evaporate water to dry, and after detecting the dry state from the humidity change of the humidity sensor (46) provided in the drying chamber, open the intermediate door (34) to open the drying chamber garbage (1c ) Is dropped into the combustion chamber (3b) to form a combustion chamber garbage (1d), the intermediate door (34) is closed, and the drying chamber (3
In step a), the raw garbage (1b) that has been subjected to the next process is put into the drying chamber garbage (1c) again to start drying, and at the same time, the combustion chamber (3b) is supplied with the oxygen supply pipe (57) from the oxygen gas generator (59). ) Via the ignition burner (47) to ignite the combustion chamber garbage (1d) to self-combust, and the combustion gas is a communication pipe (49) connecting the combustion chamber and the drying chamber.
Is sucked and exhausted to the drying chamber (3a) by means of a vacuum pump (54) together with water vapor evaporated in the drying chamber, and a cooling trap (52)
To the cooling trap (52), the combustion gas and vaporized water vapor are separated into water and vapor, and the combustion gas is exhausted through the vacuum pump pipe (53). After detecting the temperature change of the sensor (48), the lower door (36) of the combustion chamber is opened, and the incinerated food waste ash is dropped and stored in the ash receiving box (70). By repeating the above steps to incinerate the total amount of food waste in the food waste stock section (1), the garbage is discharged from the ash discharge door (24).
【請求項2】 乾燥室(3a)と燃焼室(3b)を持つ
焼却装置部(3)において、生ごみを先ず乾燥室(3
a)に投入し乾燥した後、燃焼室(3b)に移送投入し
焼却するようにして、順次、乾燥室(3a)に次処理生
ごみを収容し乾燥した後、燃焼室(3b)に投入し、乾
燥工程と燃焼工程とを同時進行処理をする構成として、
乾燥室(3a)に処理すべき乾燥室生ごみ(1c)の無
くなった時は、給水配管(61)より適量の給水を乾燥
室(3a)に行えるようにして、真空ポンプ(54)に
より乾燥室内の減圧を行いつつ、水分蒸発にマグネトロ
ン(41)によるマイクロ波加熱を行って、同時に燃焼
室(3b)の燃焼室生ごみ(1d)を酸素を供給しつつ
着火し焼却して、発生する燃焼ガスを連通管(49)か
ら乾燥室(3a)に吸引し、乾燥室(3a)の蒸発水蒸
気とともに乾燥室排気配管(50)から冷却トラップ
(52)へ排出し、冷却トラップ(52)内で、蒸発水
蒸気の冷却凝結を行って、気水分離を行い、燃焼ガスを
真空ポンプ(54)によって排気することを特徴とする
燃焼排ガス処理方法。
2. In the incinerator part (3) having a drying chamber (3a) and a combustion chamber (3b), the raw garbage is first dried in the drying chamber (3).
After being put into a) and dried, transferred into the combustion chamber (3b) and incinerated so that the next-treated raw garbage is sequentially stored in the drying chamber (3a) and dried, and then put into the combustion chamber (3b). Then, as a configuration in which the drying process and the combustion process are simultaneously processed,
When the dry room garbage (1c) to be treated in the dry room (3a) is exhausted, an appropriate amount of water can be supplied to the dry room (3a) through the water supply pipe (61), and the dry room is provided by the vacuum pump (54). Combustion gas produced by microwave heating by magnetron (41) while evaporating water while igniting and burning the combustion chamber garbage (1d) in the combustion chamber (3b) while supplying oxygen. Is sucked into the drying chamber (3a) from the communication pipe (49), and is discharged from the drying chamber exhaust pipe (50) to the cooling trap (52) together with the vaporized water vapor in the drying chamber (3a). A method for treating combustion exhaust gas, characterized in that vaporized water vapor is cooled and condensed to separate water and water, and combustion gas is exhausted by a vacuum pump (54).
JP6066380A 1994-02-24 1994-02-24 Reduced-pressure drying garbage incinerator and treating method of combustion exhaust gas Pending JPH07233931A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6066380A JPH07233931A (en) 1994-02-24 1994-02-24 Reduced-pressure drying garbage incinerator and treating method of combustion exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6066380A JPH07233931A (en) 1994-02-24 1994-02-24 Reduced-pressure drying garbage incinerator and treating method of combustion exhaust gas

Publications (1)

Publication Number Publication Date
JPH07233931A true JPH07233931A (en) 1995-09-05

Family

ID=13314173

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6066380A Pending JPH07233931A (en) 1994-02-24 1994-02-24 Reduced-pressure drying garbage incinerator and treating method of combustion exhaust gas

Country Status (1)

Country Link
JP (1) JPH07233931A (en)

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