JP2955436B2 - Method of detecting moisture content of garbage in garbage incinerator - Google Patents
Method of detecting moisture content of garbage in garbage incineratorInfo
- Publication number
- JP2955436B2 JP2955436B2 JP4326350A JP32635092A JP2955436B2 JP 2955436 B2 JP2955436 B2 JP 2955436B2 JP 4326350 A JP4326350 A JP 4326350A JP 32635092 A JP32635092 A JP 32635092A JP 2955436 B2 JP2955436 B2 JP 2955436B2
- Authority
- JP
- Japan
- Prior art keywords
- garbage
- combustion
- detecting
- zone
- dust
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Incineration Of Waste (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、投入されたゴミを搬送
しながら乾燥させる乾燥帯と乾燥されたゴミを搬送しな
がら燃焼させる燃焼帯とを段差部を介して連設してある
ゴミ焼却炉におけるゴミの含水量検出方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refuse incineration system in which a drying zone for drying the conveyed dust while transporting it and a combustion zone for conveying the dried refuse and burning it through a step. The present invention relates to a method for detecting the moisture content of refuse in a furnace.
【0002】[0002]
【従来の技術】この種の焼却炉は、生ゴミ等の水分を含
んだゴミを極力乾燥させた状態で燃焼させるように乾燥
帯を設けて、さらに段差部から燃焼帯にゴミを落下させ
て粉砕することにより乾燥、燃焼を促進するように構成
しているが、燃焼帯上のゴミの乾燥度合いが焼却効率に
重大な影響を及ぼすために、ゴミの乾燥度合いにより乾
燥帯や燃焼帯におけるゴミの搬送速度や、燃焼用空気の
供給量を調節する必要がある。しかし、従来、高温の乾
燥帯上にあるゴミの含水量等の性状そのものを検出する
ことが困難であったために、前記燃焼帯における燃焼温
度等を検出して、間接的にゴミの含水量等の性状を推定
するものや、ゴミの表面から放射される赤外線エネルギ
ーを乾燥帯の上方から検出するものがあった(特願平4
−26342号)。2. Description of the Related Art An incinerator of this kind is provided with a drying zone so that garbage containing water such as garbage is dried as much as possible and burns the garbage from the step to the combustion zone. Drying and burning are promoted by crushing.However, since the degree of drying of the garbage on the combustion zone has a significant effect on the incineration efficiency, the garbage in the drying zone or the combustion zone depends on the degree of garbage drying. It is necessary to adjust the conveying speed of the air and the supply amount of the combustion air. However, conventionally, it has been difficult to detect the property itself such as the water content of the garbage on the high-temperature drying zone. Therefore, the combustion temperature or the like in the combustion zone is detected to indirectly detect the water content of the garbage. Some estimated the properties of the garbage and others detected infrared energy emitted from the surface of the trash from above the drying zone (Japanese Patent Application No. Hei 4
-26342).
【0003】[0003]
【発明が解決しようとする課題】しかし、上述の燃焼温
度等を検出するものでは、現在燃焼中のゴミの含水量等
の性状を推定するものであり、その後に搬送されるゴミ
の含水量等が大きく変化しないとの前提のもとに推定す
るものであったため、ゴミ質が急変した場合には、乾燥
帯や燃焼帯におけるゴミの搬送速度や、燃焼用空気の供
給量を適切に調節できず焼却効率が低下することがあっ
た。また、ゴミの表面から放射される赤外線エネルギー
を乾燥帯の上方から検出するものでは、表面温度は検出
できても、乾燥帯上に約1mもの厚さで搬送されるゴミ
内部の含水量等の性状まで正確に検出できるものではな
かった。本発明の目的は、ゴミが燃焼帯に搬送される以
前に、ゴミ内部の含水量を正確に検出することができる
ゴミ焼却炉におけるゴミの含水量検出方法を提供するこ
とにある。However, in the above-described apparatus for detecting the combustion temperature and the like, the properties such as the water content of the garbage currently burning are estimated, and the water content and the like of the garbage conveyed thereafter are estimated. In the case of a sudden change in the quality of garbage, it is possible to appropriately adjust the garbage transport speed and the supply amount of combustion air in the drying zone and combustion zone. The incineration efficiency was sometimes reduced. In the case of detecting infrared energy radiated from the surface of the garbage from above the drying zone, even if the surface temperature can be detected, the water content inside the garbage conveyed with a thickness of about 1 m on the drying zone can be detected. The properties could not be accurately detected. An object of the present invention is to provide a method for detecting the water content of refuse in a refuse incinerator that can accurately detect the water content inside the refuse before the refuse is conveyed to the combustion zone.
【0004】[0004]
【課題を解決するための手段】この目的を達成するため
本発明によるゴミ焼却炉におけるゴミの含水量検出方法
の特徴構成は、乾燥帯上のゴミのうち、前記段差部から
前記燃焼帯への落下により生じる断面部分における厚み
方向の温度分布を、その断面部分から放射される赤外線
エネルギーを検出して求め、その温度分布に基づいてゴ
ミの含水量を推定する点にある。上述の構成において、
赤外線エネルギーが3.9μmを中心波長とする帯域の
ものであれば好ましい。また、前記断面部分における厚
み方向の温度分布が急激に低下した時期を、ゴミの前記
燃焼帯への落下時期と判別して、その直後の温度分布を
検出することにより、ゴミ落下後の前記断面部分の温度
を 検出するものであればより好ましい。 In order to achieve this object, a characteristic structure of the method for detecting the water content of refuse in a refuse incinerator according to the present invention is as follows. The point is that the temperature distribution in the thickness direction in the cross section caused by the fall is determined by detecting infrared energy radiated from the cross section, and the moisture content of the dust is estimated based on the temperature distribution. In the above configuration,
Infrared energy has a center wavelength of 3.9 μm.
Is preferred. In addition, the thickness in the cross section
The time when the temperature distribution in the direction of
Judging when it is time to drop into the combustion zone, the temperature distribution immediately after
By detecting, the temperature of the cross section after dust falls
It is more preferable to detect the following.
【0005】[0005]
【作用】乾燥帯上のゴミのうち、前記段差部から前記燃
焼帯への落下により生じる断面部分から放射される赤外
線エネルギーを検出して求まる厚み方向の温度分布は、
図2に示すように、一般に上方から下方にかけて低下す
るように分布するが、これは、下方のゴミの含水量が上
方のゴミの含水量よりも多いためである。従って、上方
から下方にかけて温度が低下する度合いからゴミの含水
量が推定できるのである。前記赤外線エネルギーが3.
9μmを中心波長とする帯域のものであれば好ましい。
これは、前記燃焼帯上で発生する火炎中のCO,CO
2 ,NOX,SOX、さらにはH 2 Oによる赤外線エネ
ルギー吸収帯域を回避するためである。従って、3.9
μmを中心波長とする帯域の赤外線エネルギーを測定す
ることにより、燃焼排ガスから輻射される特徴的な赤外
線波長領域を避け、燃焼排ガスの輻射が無い赤外線のみ
の輻射強度を測定できる。また、前記断面部分における
厚み方向の温度分布が急激に低下した時期を、ゴミの前
記燃焼帯への落下時期と判別して、その直後の温度分布
を検出することにより、ゴミ落下後の前記断面部分の温
度を検出するものであればより好ましい。これは、ゴミ
の落下後の断面部分の温度は、前記燃焼帯での燃焼熱に
より次第に上昇するためである。従って、ゴミの前記燃
焼帯への落下時期を判別して、ゴミ落下後の前記断面部
分の温度を検出できるのである。 [Function] Of the refuse on the drying zone, the fuel
Infrared radiated from the cross section caused by falling into the burnt zone
The temperature distribution in the thickness direction obtained by detecting the line energy is
Generally, as shown in FIG.
The lower the garbage, the higher the moisture content.
This is because it is larger than the water content of the garbage. Therefore, upward
From the degree to which the temperature drops from
The amount can be estimated.The infrared energy is 3.
A band having a center wavelength of 9 μm is preferable.
This is because CO, CO in the flame generated on the combustion zone
Two , NOX, SOX, and H Two Infrared energy by O
This is to avoid the energy absorption band. Therefore, 3.9
Measures infrared energy in the band centered at μm
Characteristic infrared radiation emitted from the combustion exhaust gas
Infrared ray only, avoiding the emission wavelength region and no emission of combustion exhaust gas
Radiation intensity can be measured. Also, in the cross section
The time when the temperature distribution in the thickness direction suddenly decreases
Judgment of the fall time to the combustion zone and the temperature distribution immediately after
Detecting the temperature of the cross section after the dust falls.
It is more preferable to detect the degree. This is garbage
The temperature of the cross section after falling of the combustion zone depends on the heat of combustion in the combustion zone.
This is because it will rise gradually. Therefore, the combustion of garbage
Determine the timing of falling to the burn zone, and the cross section after the dust falls
The temperature of the minute can be detected.
【0006】[0006]
【発明の効果】本発明によれば、ゴミが燃焼帯に搬送さ
れる以前に、ゴミの内部の含水量までを正確に検出する
ことができるゴミ焼却炉におけるゴミの含水量検出方法
を提供することができるので、これにより、乾燥帯や燃
焼帯におけるゴミの搬送速度や、燃焼用空気の供給量を
適切に調節して焼却炉の燃焼効率を向上することができ
るようになった。また、前記赤外線エネルギーが3.9
μmを中心波長とする帯域のものであれば、より正確
に、ゴミの内部の含水量までを検出することが可能であ
る。また、前記断面部分における厚み方向の温度分布が
急激に低下した時期を、ゴミの前記燃焼帯への落下時期
と判別して、その直後の温度分布を検出することによ
り、ゴミ落下後の前記断面部分の温度を検出するもので
あれば、より正確に、前記乾燥帯から前記燃焼帯への段
落ちでのゴミの切り出し面の表面温度を把握することが
可能である。 According to the present invention, there is provided a method for detecting the water content of garbage in a refuse incinerator, which can accurately detect the water content inside the refuse before the refuse is conveyed to the combustion zone. As a result, it has become possible to improve the combustion efficiency of the incinerator by appropriately adjusting the conveying speed of the refuse in the drying zone and the combustion zone and the supply amount of the combustion air. The infrared energy is 3.9.
More accurate if the band is centered on μm
In addition, it is possible to detect even the moisture content inside the garbage.
You. Further, the temperature distribution in the thickness direction in the cross section is
The time when the garbage drops sharply is the time when the garbage falls into the combustion zone.
By detecting the temperature distribution immediately after
It detects the temperature of the cross section after dust falls.
If present, more precisely the step from the drying zone to the combustion zone
It is possible to grasp the surface temperature of the cut surface of garbage when falling
It is possible.
【0007】[0007]
【実施例】以下に実施例を説明する。ゴミ焼却炉は、図
3に示すように、被焼却物であるゴミを収容するホッパ
3と、ゴミを焼却する燃焼室2と、焼却済みの灰を集め
る灰ピット4等を設けて構成してある。前記燃焼室2
は、前記ホッパ3の下端部に設けられたプッシャ5によ
り投入されたゴミを乾燥させ着火点近傍まで加熱する乾
燥帯6と、乾燥ゴミを燃焼させる燃焼帯7と、その燃焼
帯7で燃焼したゴミを灰化する後燃焼帯8とを上方から
下方に段階的に配置して構成してある。前記乾燥帯6と
燃焼帯7の境界、及び前記燃焼帯7と後燃焼帯8との境
界には約1mの段差部d1,d2を設けてあり、それぞ
れの底部には斜め上下姿勢に配置された火格子Gを油圧
シリンダC1,C2,C3で斜め上下方向に摺動させて
ゴミを攪拌しながら前記灰ピット4へ搬送するストーカ
方式の搬送手段Sを設けてある。前記プッシャ5は油圧
シリンダC4による往復駆動で前記燃焼室2にゴミを押
し出し投入する。前記後燃焼帯8で灰化したゴミは灰押
し出し装置10に落下し、灰出しコンベア11により前
記灰ピット4に搬送集積される。前記燃焼帯7は前部燃
焼帯7Aと後部燃焼帯7Bの二領域で構成してあり、後
述の燃焼制御装置によりゴミは前部燃焼帯7Aで主に燃
焼した後、後部燃焼帯7Bで完全に燃焼するように制御
される。前記燃焼室2下部には、送風機16により送ら
れた加熱空気を乾燥・燃焼用の空気として前記燃焼室2
に供給する供給路17を設けてあり、前記乾燥帯6、燃
焼帯7、後燃焼帯8に各別に供給量を調節するダンパD
を設けてある。前記燃焼室2で発生した燃焼ガスは、排
熱ボイラ12によって発電機13のエネルギィとして利
用すべく熱エネルギィが蒸気の形で取り出され場外に供
給され、電気集塵機等からなる排ガス処理設備14によ
りばいじんや有害ガスを除去して排気される。Embodiments will be described below. As shown in FIG. 3, the refuse incinerator is provided with a hopper 3 for storing refuse, which is an incineration object, a combustion chamber 2 for incinerating refuse, an ash pit 4 for collecting incinerated ash, and the like. is there. The combustion chamber 2
Are a drying zone 6 for drying dust heated by a pusher 5 provided at a lower end portion of the hopper 3 and heating the dust to near an ignition point, a combustion zone 7 for burning dry dust, and a dust zone burned in the combustion zone 7. And the post-combustion zone 8 for incineration of ash are arranged stepwise from above to below. At the boundary between the drying zone 6 and the combustion zone 7 and at the boundary between the combustion zone 7 and the post-combustion zone 8, there are provided steps d1 and d2 of about 1 m. A stoker-type transfer means S is provided which slides the fire grate G obliquely up and down by hydraulic cylinders C1, C2 and C3 and transfers the dust to the ash pit 4 while stirring the dust. The pusher 5 pushes dust into the combustion chamber 2 by reciprocating drive by a hydraulic cylinder C4. The refuse incinerated in the post-combustion zone 8 falls into the ash extruder 10, and is conveyed and collected in the ash pit 4 by the ash conveyer 11. The combustion zone 7 is composed of two regions, a front combustion zone 7A and a rear combustion zone 7B. The refuse is mainly combusted in the front combustion zone 7A by a combustion control device described later, and then completely separated in the rear combustion zone 7B. It is controlled so as to burn. In the lower part of the combustion chamber 2, the heated air sent by the blower 16 is used as air for drying and combustion.
And a damper D for adjusting the supply amounts to the drying zone 6, the combustion zone 7, and the post-combustion zone 8, respectively.
Is provided. The combustion gas generated in the combustion chamber 2 is extracted from the combustion gas by the exhaust heat boiler 12 in the form of steam so as to be used as energy of the generator 13 and supplied to the outside of the plant. And harmful gases are removed and exhausted.
【0008】前記燃焼室2には、燃焼状態をモニタする
ために、乾燥帯6上のゴミの温度を検出する放射温度検
出手段1、燃焼帯7の温度を検出する熱電対でなる炉出
口温度検出手段15、燃焼空気量を検出する圧力検出手
段(図示せず)等を設けてあり、前記焼却炉には、前記
各種のセンサ検出値を入力する入力手段18A、入力手
段18Aからの入力データに基づき燃焼室2の燃焼状態
を評価する評価手段18B、評価手段18Bによる評価
結果に基づきプッシャ5によるゴミの投入速度、ストー
カ手段Sによるゴミの搬送速度、ダンパの開度等の調節
を行い適正な燃焼状態に調節維持する燃焼制御手段18
Cとを備えたマイクロコンピュータを搭載してなる燃焼
制御装置18を設けてある。The combustion chamber 2 has a radiation temperature detecting means 1 for detecting the temperature of dust on the drying zone 6 and a furnace outlet temperature comprising a thermocouple for detecting the temperature of the combustion zone 7 in order to monitor the combustion state. Detecting means 15, pressure detecting means (not shown) for detecting the amount of combustion air, etc. are provided. The incinerator has input means 18A for inputting the various sensor detection values, and input data from input means 18A. Means 18B for evaluating the combustion state of the combustion chamber 2 on the basis of the evaluation results, the dust input speed by the pusher 5, the dust transfer speed by the stoker means S, the opening of the damper, etc. Combustion control means 18 for adjusting and maintaining a stable combustion state
C is provided with a combustion control device 18 equipped with a microcomputer equipped with C.
【0009】前記放射温度検出手段1は、前記後燃焼帯
8のさらに下流側から前記乾燥帯6を臨むように取り付
けてあり、図4に示すような黒体輻射エネルギーを検出
するもので、図1及び図5に示すように、前記燃焼帯7
上で発生する火炎中のCO,CO2 ,NOX,SOX、
さらにはH2Oによる赤外線エネルギー吸収帯域を回避
すべく、波長が約3.9(3.6〜4)μmのフィルタ
を設けた赤外線カメラ1aと、赤外線カメラ1aによる
検出画像を解析する画像処理手段1b等で構成してあ
り、前記乾燥帯6上に堆積した約1mの厚さのゴミのう
ち、前記段差部d1から前記燃焼帯7への落下により生
じる断面部分における厚み方向の温度分布を検出する。
詳述すると、ゴミの落下後の断面部分の温度は、前記燃
焼帯7での燃焼熱により次第に上昇するため、前記画像
処理手段1bは、前記放射温度検出手段1による前記断
面部分の検出温度が急激に低下した時期を前記燃焼帯7
への落下時期と判別して、その直後の温度分布を検出す
る。図2に示すように、温度分布は前記断面部分の上方
から下方にかけて次第に低下するように分布しており、
その程度によりゴミの含水量を推定する。つまり、ゴミ
の含水量が多ければ前記乾燥帯6での乾燥が不十分で前
記断面部分の下方における温度が低くなり、ゴミの含水
量が少なければ前記乾燥帯6での乾燥が十分で前記断面
部分の下方における温度はそれほど低下しない点に着目
して、上部と下部の温度勾配の程度、及び、ゴミ厚さに
基づいてゴミの含水量を推定する。The radiation temperature detecting means 1 is mounted so as to face the drying zone 6 from a further downstream side of the post-combustion zone 8 and detects black body radiation energy as shown in FIG. As shown in FIG. 1 and FIG.
CO, CO 2 , NOX, SOX in the flame generated above
Furthermore in order to avoid infrared energy absorption bands due to H 2 O, and the infrared camera 1a whose wavelength is provided about 3.9 (3.6 to 4) [mu] m filter, the image processing for analyzing the detected image by the infrared camera 1a The temperature distribution in the thickness direction of a cross section generated by dropping from the step portion d1 to the combustion zone 7 among the garbage having a thickness of about 1 m deposited on the drying zone 6 To detect.
More specifically, since the temperature of the cross section after the fall of the dust gradually increases due to the combustion heat in the combustion zone 7, the image processing unit 1b determines that the temperature detected by the radiation temperature detection unit 1 at the cross section is lower. The time when the combustion zone 7 suddenly drops
Then, the temperature distribution immediately after that is determined. As shown in FIG. 2, the temperature distribution is distributed so as to gradually decrease from above to below the cross section.
The water content of the garbage is estimated based on the degree. In other words, if the moisture content of the dust is high, the drying in the drying zone 6 is insufficient and the temperature below the cross-sectional portion is low. If the moisture content of the dust is low, the drying in the drying zone 6 is sufficient and the cross-section is insufficient. Paying attention to the fact that the temperature below the portion does not decrease so much, the moisture content of the dust is estimated based on the degree of the temperature gradient between the upper portion and the lower portion and the thickness of the dust.
【0010】前記燃焼制御装置18は、前記放射温度検
出手段1により、ゴミの含水量が大であると判別された
場合、乾燥帯6に対応するダンパDの開度を大に調節し
て乾燥を促進しつつ、燃焼帯7での燃焼を促進すべく前
記燃焼帯7での搬送速度を低下するとともに、前記プッ
シャ5によるゴミの投入量や前記乾燥帯6の搬送量を低
減し、前記放射温度検出手段1により、ゴミの含水量が
少であると判別された場合、乾燥帯6に対応するダンパ
Dの開度を現状維持か若干絞り、燃焼帯7での燃焼をさ
らに促進すべく前記燃焼帯7での搬送速度を上昇すると
ともに、前記プッシャ5によるゴミの投入量や前記乾燥
帯6の搬送量を増す。When the radiant temperature detecting means 1 determines that the water content of the dust is large, the combustion control device 18 adjusts the opening of the damper D corresponding to the drying zone 6 to a large value to dry the dust. The transport speed in the combustion zone 7 is reduced to promote the combustion in the combustion zone 7 while promoting the combustion in the combustion zone 7, and the amount of refuse introduced by the pusher 5 and the transport amount in the drying zone 6 are reduced. If the temperature detection means 1 determines that the water content of the dust is small, the opening of the damper D corresponding to the drying zone 6 is maintained at the current level or slightly reduced to further promote the combustion in the combustion zone 7. The transport speed in the combustion zone 7 is increased, and the amount of dust input by the pusher 5 and the transport amount of the drying zone 6 are increased.
【0011】以下に別実施例を説明する。先の実施例で
説明した放射温度検出手段1の検出結果に基づき燃焼制
御装置18により実行される燃焼制御は、上述のものに
限定するものではなく、乾燥帯6上でのゴミの厚さや、
他の温度センサ等の検出情報に基づいて適切な制御を行
うことができる。Another embodiment will be described below. The combustion control executed by the combustion control device 18 based on the detection result of the radiation temperature detecting means 1 described in the previous embodiment is not limited to the above-described one, and the thickness of the dust on the drying zone 6 and
Appropriate control can be performed based on detection information from another temperature sensor or the like.
【0012】尚、特許請求の範囲の項に図面との対照を
便利にする為に符号を記すが、該記入により本発明は添
付図面の構成に限定されるものではない。In the claims, reference numerals are provided for convenience of comparison with the drawings, but the present invention is not limited to the configuration shown in the attached drawings.
【図1】要部の説明図FIG. 1 is an explanatory view of a main part.
【図2】断面部分の温度分布図FIG. 2 is a temperature distribution diagram of a cross-sectional portion.
【図3】焼却炉の概略構成図FIG. 3 is a schematic configuration diagram of an incinerator.
【図4】黒体輻射エネルギーの波長特性図FIG. 4 is a wavelength characteristic diagram of black body radiation energy.
【図5】大気の透過率の特性図FIG. 5 is a characteristic diagram of the transmittance of the atmosphere.
6 乾燥帯 7 燃焼帯 d1 段差部 6 Dry zone 7 Combustion zone d1 Step
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F23G 5/50 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 6 , DB name) F23G 5/50
Claims (3)
る乾燥帯(6)と乾燥されたゴミを搬送しながら燃焼さ
せる燃焼帯(7)とを段差部(d1)を介して連設して
あるゴミ焼却炉におけるゴミの含水量検出方法であっ
て、 前記乾燥帯(6)上のゴミのうち、前記段差部(d1)
から前記燃焼帯(7)への落下により生じる断面部分に
おける厚み方向の温度分布を、その断面部分から放射さ
れる赤外線エネルギーを検出して求め、その温度分布に
基づいてゴミの含水量を推定するゴミ焼却炉におけるゴ
ミの含水量検出方法。1. A drying zone (6) for drying while transporting input dust and a combustion zone (7) for burning while transporting the dried dust are connected via a step (d1). A method for detecting the water content of garbage in a garbage incinerator, wherein the step portion (d1) of the trash on the drying zone (6)
The temperature distribution in the thickness direction in the cross-section caused by falling from the surface to the combustion zone (7) is determined by detecting the infrared energy radiated from the cross-section, and the moisture content of the dust is estimated based on the temperature distribution. A method for detecting the water content of garbage in garbage incinerators.
心波長とする帯域のものである請求項1記載のゴミ焼却2. The incineration of garbage according to claim 1, wherein the garbage is in a band having a center wavelength.
炉におけるゴミの含水量検出方法。A method for detecting the water content of refuse in a furnace.
布が急激に低下した時期を、ゴミの前記燃焼帯への落下During the period when the cloth suddenly drops, the garbage falls into the combustion zone.
時期と判別して、その直後の温度分布を検出することにJudging the time and detecting the temperature distribution immediately after
より、ゴミ落下後の前記断面部分の温度を検出する請求The temperature of the cross section after the dust falls
項1〜2記載のゴミ焼却炉におけるゴミの含水量検出方Item 1. Method for detecting water content of garbage in garbage incinerator according to item 1 or 2.
法。Law.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4326350A JP2955436B2 (en) | 1992-12-07 | 1992-12-07 | Method of detecting moisture content of garbage in garbage incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4326350A JP2955436B2 (en) | 1992-12-07 | 1992-12-07 | Method of detecting moisture content of garbage in garbage incinerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06174219A JPH06174219A (en) | 1994-06-24 |
JP2955436B2 true JP2955436B2 (en) | 1999-10-04 |
Family
ID=18186812
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4326350A Expired - Fee Related JP2955436B2 (en) | 1992-12-07 | 1992-12-07 | Method of detecting moisture content of garbage in garbage incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2955436B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6429039B2 (en) * | 2015-12-17 | 2018-11-28 | Jfeエンジニアリング株式会社 | Grate-type waste incinerator and waste incineration method using grate-type waste incinerator |
JP7020299B2 (en) * | 2018-05-31 | 2022-02-16 | Jfeエンジニアリング株式会社 | Waste incinerator and waste incinerator method |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51138077A (en) * | 1975-05-22 | 1976-11-29 | Hitachi Zosen Corp | Control method of garbage incinerator |
JPH02208410A (en) * | 1989-02-03 | 1990-08-20 | Kubota Ltd | Control of combustion in refuse incinerator |
-
1992
- 1992-12-07 JP JP4326350A patent/JP2955436B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH06174219A (en) | 1994-06-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6671326B2 (en) | Combustion control method and waste incinerator | |
JP2704541B2 (en) | Automatic combustion control of rotary incinerator | |
JP2788394B2 (en) | Garbage incinerator | |
JP2955436B2 (en) | Method of detecting moisture content of garbage in garbage incinerator | |
JPH08178247A (en) | Method of detecting nature of refuse in incinerator | |
JP2955431B2 (en) | Incinerator combustion control device | |
JP3669778B2 (en) | Combustion control device for garbage incinerator | |
JP3669779B2 (en) | Combustion control device for garbage incinerator | |
JP2003161420A (en) | Combustion control method and combustion control device of stoker incinerator | |
JP2800871B2 (en) | Incinerator combustion control device | |
JPH0849830A (en) | Waste quality-estimating system of waste incinerator | |
JP3356946B2 (en) | Garbage quality determination method and apparatus, and combustion control device for garbage incinerator | |
JP7384078B2 (en) | Waste incineration equipment and waste incineration method | |
JPH08233241A (en) | Trash character-detecting method for trash incineration furnace | |
JP2889833B2 (en) | Measurement method of combustion flame of garbage incinerator | |
JP2624912B2 (en) | Incinerator combustion control device | |
JP3315036B2 (en) | Combustion control device of garbage incinerator | |
JPH0894055A (en) | Combustion controller | |
JPH06117619A (en) | Burning control device for burning furnace | |
JPH06331120A (en) | Incinerator | |
JP2755539B2 (en) | Combustion control method for refuse incinerator | |
JP2003161421A (en) | Combustion control method and combustion control device of stoker type incinerator | |
JPH08285242A (en) | Incinerator | |
JP3173963B2 (en) | Garbage incineration equipment | |
JP7347339B2 (en) | Grate type waste incinerator and waste incineration method using grate type waste incinerator |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |