JP2002349827A - Method for controlling dust feeding amount in incinerator - Google Patents

Method for controlling dust feeding amount in incinerator

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Publication number
JP2002349827A
JP2002349827A JP2001152485A JP2001152485A JP2002349827A JP 2002349827 A JP2002349827 A JP 2002349827A JP 2001152485 A JP2001152485 A JP 2001152485A JP 2001152485 A JP2001152485 A JP 2001152485A JP 2002349827 A JP2002349827 A JP 2002349827A
Authority
JP
Japan
Prior art keywords
dust
amount
operation speed
supply
furnace
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001152485A
Other languages
Japanese (ja)
Other versions
JP3850228B2 (en
Inventor
Yoshiaki Takahata
義明 高畠
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.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP2001152485A priority Critical patent/JP3850228B2/en
Publication of JP2002349827A publication Critical patent/JP2002349827A/en
Application granted granted Critical
Publication of JP3850228B2 publication Critical patent/JP3850228B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To realize a dust feeding amount controlling method to properly control an amount of refuse fed in a furnace F by a refuse feeding means 11, in an incinerator 10 to incinerate and dispose of refuse in the furnace F. SOLUTION: A process wherein the refuse feeding efficiency of the refuse feeding means 11 is calculated; a process wherein from the calculated refuse feeding efficiency, a heating value per a unit amount of refuse, and a target heating amount in the furnace F, a reference operation speed of the refuse feeding means 11 is calculated; and a process wherein the operation speed of the refuse feeding means 11 is set to an operation speed where a given additional amount is added to a reference operation speed are executed.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、火炉内でゴミを焼
却処理する焼却炉において、前記給塵手段による前記火
炉内への前記ゴミの供給量を制御する給塵量制御方法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling the amount of dust supplied to the furnace by the dust supply means in an incinerator for incinerating dust in a furnace.

【0002】[0002]

【従来の技術】従来、ゴミ焼却設備は、火炉にゴミを供
給する給塵手段としての給塵機構を備え、火炉の出口温
度検出と火炉から排出される排ガスの酸素濃度検出等に
より、火炉における発熱量を算出し、その発熱量が目標
発熱量付近で安定するように、給塵機構の動作速度を調
整して、火炉へのゴミの供給量を制御するように構成さ
れることがある。即ち、2〜3時間の所定時間内におけ
る算出した発熱量の移動平均と、同じく所定時間内にお
けるクレーン等により給塵機構へ投入したゴミの重量の
移動平均とから、ゴミの単位重量あたりの発熱量所謂ゴ
ミ質を推測し、このゴミ質と目標発熱量とから、ゴミの
単位時間あたりの目標焼却量を求め、さらに、上記所定
時間内の給塵機構へ投入したゴミの重量と給塵機構の動
作速度とから、給塵機構の動作速度に対するゴミの供給
重量である給塵効率を求め、給塵機構によるゴミの供給
量がこの目標焼却量となるように、上記目標焼却量と上
記給塵効率とを基に、給塵機構の動作速度を設定するの
である。
2. Description of the Related Art Conventionally, a refuse incineration system is provided with a dust supply mechanism as dust supply means for supplying refuse to the furnace, and detects the temperature at the exit of the furnace and the oxygen concentration of the exhaust gas discharged from the furnace, and so on. In some cases, the calorific value is calculated, and the operation speed of the dust supply mechanism is adjusted so that the calorific value is stabilized near the target calorific value, thereby controlling the amount of dust supplied to the furnace. That is, based on the moving average of the calorific value calculated within a predetermined time of 2 to 3 hours and the moving average of the weight of dust input to the dust supply mechanism by the crane or the like within the same predetermined time, the heat generation per unit weight of the dust is calculated. The amount of so-called dust is estimated, the target incineration amount per unit time of the dust is determined from the dust quality and the target calorific value. From the operation speed of the dust supply mechanism, the dust supply efficiency, which is the weight of the dust with respect to the operation speed of the dust supply mechanism, is obtained. The target incineration amount and the supply amount are set so that the supply amount of the dust by the dust supply mechanism becomes the target incineration amount. The operation speed of the dust supply mechanism is set based on the dust efficiency.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記従来のゴ
ミ焼却設備のゴミの供給量の制御においては、実際に給
塵機構により供給されたゴミ質と、上記のように算出し
た火炉における発熱量から推測したゴミ質との間には、
誤差が生じる場合があり、次のような問題を招いてい
た。例えば、ゴミの含水率や嵩密度が急激に変化した場
合には、火炉内に供給されたゴミの発熱量が急激に変化
するが、このことで火炉の出口温度に変化が生じた時点
でのゴミの供給量のフィードバック制御を行っても、対
応が遅くなることがある。
However, in the control of the amount of refuse supplied to the conventional refuse incineration equipment, the quality of the refuse actually supplied by the dust supply mechanism and the amount of heat generated in the furnace as calculated above are controlled. Between the garbage quality estimated from
An error may occur, causing the following problem. For example, when the moisture content and bulk density of the refuse change rapidly, the calorific value of the refuse supplied into the furnace changes rapidly. Even if feedback control of the supply amount of garbage is performed, the response may be delayed.

【0004】さらに、通常15〜20分程度の周期でク
レーンにてホッパにゴミが投入されるが、その投入され
たゴミがホッパ内で落下せずにホッパのレベルが下がら
ないブリッジが発生すると、ゴミの投入周期が長くなる
場合がある。また、手動でクレーンを操作している場
合、クレーンの操作員のゴミの投入が、何らかの理由で
遅れた場合、ゴミのホッパへの投入周期が長くなり、さ
らに、その反動でその後はゴミの投入周期が短くなる。
このため、実際の給塵機構の給塵効率が変動し、火炉内
へ供給されたゴミの発熱量に基づく給塵機構の動作速度
の制御が追いつかず、ゴミ切れ等が発生する虞がある。
Further, dust is usually thrown into the hopper by a crane at a cycle of about 15 to 20 minutes. If a bridge occurs in which the thrown dust does not fall in the hopper and the hopper level does not decrease, There is a case that the garbage input cycle becomes longer. In addition, when the crane is operated manually, if the input of dust by the operator of the crane is delayed for some reason, the input cycle of the dust into the hopper becomes longer, The cycle becomes shorter.
For this reason, the actual dust supply efficiency of the dust supply mechanism fluctuates, and the control of the operation speed of the dust supply mechanism based on the calorific value of the dust supplied into the furnace may not catch up, and the dust may run out.

【0005】従って、本発明は、上記の事情に鑑みて、
火炉内でゴミを焼却処理する焼却炉において、給塵手段
による火炉内への前記ゴミの供給量を適切に制御するこ
とができる給塵量制御方法を実現することを目的とす
る。
Accordingly, the present invention has been made in view of the above circumstances,
It is an object of the present invention to realize a dust supply amount control method capable of appropriately controlling a supply amount of the dust into the furnace by a dust feeding unit in an incinerator for incinerating dust in a furnace.

【0006】[0006]

【課題を解決するための手段】〔構成1〕本発明に係る
給塵量制御方法は、請求項1に記載したごとく、火炉内
でゴミを焼却処理する焼却炉において、給塵手段による
前記火炉内への前記ゴミの供給量を制御する給塵量制御
方法であって、前記給塵手段の動作速度に対する前記ゴ
ミの供給量である給塵効率を算出する給塵効率算出工程
と、前記給塵効率算出工程で算出された給塵効率と、前
記ゴミの単位量あたりの発熱量と、前記火炉における目
標発熱量とから、前記給塵手段の基準動作速度を算出す
る基準動作速度算出工程と、前記給塵手段の動作速度
を、前記基準動作速度算出工程で算出された基準動作速
度に所定の上乗せ量を加算した動作速度に設定する動作
速度設定工程とを実行することを特徴とする。
According to a first aspect of the present invention, there is provided a dust supply amount control method according to the first aspect of the present invention, wherein in the incinerator for incinerating garbage in a furnace, the dust is supplied by the dust supply means. A dust supply amount control method for controlling a supply amount of the dust to the inside, wherein a dust supply efficiency calculating step of calculating a dust supply efficiency which is a supply amount of the dust with respect to an operation speed of the dust supply means; A dust supply efficiency calculated in the dust efficiency calculation step, a calorific value per unit amount of the dust, and a target calorific value in the furnace, a reference operation speed calculation step of calculating a reference operation speed of the dust supply means, And an operation speed setting step of setting the operation speed of the dust supply means to an operation speed obtained by adding a predetermined additional amount to the reference operation speed calculated in the reference operation speed calculation step.

【0007】〔作用効果〕本構成の給塵量制御方法によ
れば、先ず、給塵効率算出工程において、所定の単位時
間内における給塵手段の動作速度と、同じく所定の単位
時間内における給塵手段による火炉へのゴミの供給量と
から給塵手段の上記給塵効率を算出し、次に、基準動作
速度算出工程において、火炉において目標発熱量を達成
するための給塵手段の動作速度である上記基準動作速度
を算出する。そして、本発明の給塵制御方法は、動作速
度設定工程において、給塵手段の動作速度を、上記基準
動作速度に所定の上乗せ量を加算した値、好ましくは、
基準動作速度に対して5〜15%程度の割合の上乗せ量
を基準動作速度に加算した値に設定する。このように、
給塵手段の動作速度を、火炉において目標発熱量を達成
する値に対して若干大きい値に設定して、火炉へのゴミ
の供給を、火炉の能力の範囲内において若干過剰気味と
することで、火炉へ供給されるゴミ質の急激な低下等
や、給塵手段の給塵効率の急激な低下が発生しても、火
炉のゴミ切れを発生することなく、火炉において常に目
標発熱量を確保することができる。
According to the dust supply amount control method of this configuration, first, in the dust supply efficiency calculation step, the operation speed of the dust supply means within a predetermined unit time and the operation speed of the dust supply unit within the predetermined unit time are also determined. The above-mentioned dust-supplying efficiency of the dust-supplying means is calculated from the amount of refuse supplied to the furnace by the dusting means, and then, in the reference operation speed calculating step, the operating speed of the dust-supplying means for achieving the target heating value in the furnace. Is calculated. In the dust supply control method of the present invention, in the operation speed setting step, the operation speed of the dust supply means is a value obtained by adding a predetermined additional amount to the reference operation speed, preferably,
An additional amount of about 5 to 15% of the reference operation speed is set to a value obtained by adding to the reference operation speed. in this way,
By setting the operation speed of the dust supply means to a value slightly larger than the value that achieves the target calorific value in the furnace, the supply of dust to the furnace is slightly excessive within the range of the capability of the furnace. Even if the quality of refuse supplied to the furnace suddenly decreases or the dust supply efficiency of the dust supply means drops sharply, the furnace does not run out of refuse and always keeps the target heating value in the furnace. can do.

【0008】〔構成2〕本発明に係る給塵量制御方法
は、請求項2に記載したごとく、上記構成1の給塵量制
御方法の構成に加えて、前記基準動作速度に対する前記
上乗せ量の割合が、前記ゴミの単位量あたりの発熱量が
大きいほど小さく設定されていることを特徴とする。
[0010] According to a second aspect of the present invention, in addition to the configuration of the dust supply amount control method of the first aspect, the dust supply amount control method according to the present invention further comprises the addition of the additional amount to the reference operation speed. The ratio is set to be smaller as the calorific value per unit amount of the dust is larger.

【0009】〔作用効果〕本構成の給塵量制御方法によ
れば、例えば、過去の所定時間内にクレーン等により給
塵手段に投入されたゴミの量の移動平均値と、同じく過
去の所定時間内に火炉内で発生した発熱量の移動平均値
とから自動的に求めることができる火炉内へ供給される
ゴミの単位量あたりの発熱量、又は手動により入力され
たゴミの単位量あたりの発熱量を受付け、その受付た発
熱量が大きいほど上記上乗せ量を小さく設定すること
で、本発明の給塵量制御方法において、給塵手段の動作
速度を若干過剰気味に設定しても、排ガス処理設備等の
上限能力を上回らないように、火炉内における発熱量の
過剰上昇を抑制することができる。
According to the dust supply amount control method of this configuration, for example, the moving average value of the amount of dust introduced into the dust supply means by a crane or the like within a predetermined time in the past is the same as that in the past. The heating value per unit amount of garbage supplied to the furnace, which can be automatically calculated from the moving average value of the heating value generated in the furnace within the time, or the unit amount of garbage manually input In the dust supply amount control method of the present invention, even if the operation speed of the dust supply unit is set to be slightly excessive, exhaust gas is received by receiving the heat generation amount and setting the additional amount to be smaller as the received heat generation amount is larger. Excessive rise in the calorific value in the furnace can be suppressed so as not to exceed the upper limit capacity of the processing equipment or the like.

【0010】〔構成3〕本発明に係る給塵量制御方法
は、請求項3に記載したごとく、上記構成1又は2の給
塵量制御方法の構成に加えて、前記給塵効率算出工程
が、所定時間内における前記給塵手段の動作速度と、同
じく所定時間内における前記給塵手段へのゴミの投入量
とから、前記給塵効率を算出する工程であることを特徴
とする。
[Structure 3] In the dust supply amount control method according to the present invention, in addition to the structure of the dust supply amount control method according to the above structure 1 or 2, the dust supply efficiency calculating step may be carried out. Calculating the dust supply efficiency from the operation speed of the dust supply unit within a predetermined time and the amount of dust input to the dust supply unit within the predetermined time.

【0011】〔作用効果〕本構成のごとく、上記給塵効
率算出工程において、上記給塵効率を算出するに、動作
速度設定工程で設定される給塵手段の動作速度と、給塵
手段にゴミを投入するクレーン等により計測されるゴミ
の投入量との、所定時間内における夫々の移動平均値等
から、容易に、上記給塵手段の給塵効率を算出すること
ができる。
[Effects] As in the present configuration, in the dust supply efficiency calculating step, the operation speed of the dust supply means set in the operation speed setting step is determined by calculating the dust supply efficiency. It is possible to easily calculate the dust-supply efficiency of the dust-supply unit from the moving average value and the like within a predetermined time with the amount of dust that is measured by a crane or the like that throws the dust.

【0012】〔構成4〕本発明に係る給塵量制御方法
は、請求項4に記載したごとく、上記構成1から3の何
れかの給塵量制御方法の構成に加えて、前記動作速度設
定工程において、前記給塵手段の動作速度を設定する
に、前記火炉内の発熱量が前記目標発熱量以上となった
ときには、前記給塵手段の動作速度を一時的に所定の量
を低下させることを特徴とする。
[Structure 4] According to a fourth aspect of the present invention, in addition to the configuration of the dust supply amount control method of any one of the first to third aspects, the dust supply amount control method according to the present invention further comprises the operation speed setting method. In the step, when the operation speed of the dust supply unit is set, the operation speed of the dust supply unit is temporarily reduced by a predetermined amount when the heat generation amount in the furnace becomes equal to or more than the target heat generation amount. It is characterized by.

【0013】〔作用効果〕本構成の給塵量制御方法によ
れば、動作速度設定工程において、給塵手段の動作速度
を、通常は、基準動作速度に対して若干過剰気味に設定
するのであるが、火炉内の発熱量が目標発熱量以上とな
ったときは、給塵手段の動作速度を過剰気味に設定する
と火炉の能力以上の発熱量が発生する危険性があるとし
て、給塵手段の動作速度を、一時的に、通常の動作速度
に対して例えば50%程度以上急激に低減した値に設定
することで、上記のような火炉の能力を逸脱する発熱量
が発生することを抑制することができる。
[Operation and Effect] According to the dust supply amount control method of this configuration, in the operation speed setting step, the operation speed of the dust supply means is usually set to be slightly excessive with respect to the reference operation speed. However, when the calorific value in the furnace exceeds the target calorific value, it is considered that if the operation speed of the dust supply means is set to an excessive degree, there is a risk that a calorific value exceeding the capacity of the furnace may occur, and By temporarily setting the operating speed to a value that is sharply reduced by, for example, about 50% or more with respect to the normal operating speed, the generation of the heat generation that deviates from the furnace capability as described above is suppressed. be able to.

【0014】[0014]

【発明の実施の形態】上記本発明のゴミ焼却炉における
給塵量制御方法の実施の形態について、以下に、図面を
参照しながら説明する。図1に示すように、本発明の給
塵量制御方法を適用可能なゴミ焼却設備には、ゴミ焼却
炉10の二次燃焼室13からの排ガスを煙突19に導く
煙道Dに、前記排ガスの熱、即ち前記火床上で焼却され
るゴミの焼却生成熱を回収して蒸気を発生する廃熱ボイ
ラ15と、前記排ガスから除塵するバグフィルタ16
と、除塵した後の排ガスを無害化処理する排ガス処理装
置17と、無害化処理した後の排ガスを前記煙突に向け
て送り出す誘引送風機18とが順に配置されている。こ
のゴミ焼却炉10には、炉内の燃焼量を所定の条件下で
制御するための燃焼制御機構20を設けてあり、この燃
焼制御機構20には、火炉Fの出口に温度検出端7aを
配置して、炉出口における燃焼排ガスの温度を検出する
炉出口温度検出手段7と、前記バグフィルタ16の入口
側の煙道Dにその検出端8aが配置され、排ガスの温度
を検出する排ガス温度検出手段8と、前記バグフィルタ
16の出口側の煙道Dに酸素検出端6aを配置して、排
ガス中の酸素濃度を検出する酸素濃度検出手段6とを夫
々備えている。前記廃熱ボイラ15で生成する蒸気は、
タービンを回転駆動して発電する発電装置50の駆動源
等として利用される。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the method for controlling the amount of dust supplied to a refuse incinerator according to the present invention will be described below with reference to the drawings. As shown in FIG. 1, a refuse incineration facility to which the dust supply amount control method of the present invention can be applied includes a flue D from a secondary combustion chamber 13 of a refuse incinerator 10, Waste heat boiler 15 that collects the heat of the waste, that is, the heat generated by incineration of the refuse incinerated on the grate, and generates steam, and a bag filter 16 that removes dust from the exhaust gas
And an exhaust gas treatment device 17 for detoxifying the exhaust gas after dust removal, and an induction blower 18 for sending the exhaust gas after the detoxification toward the chimney. The refuse incinerator 10 is provided with a combustion control mechanism 20 for controlling the amount of combustion in the furnace under predetermined conditions. The combustion control mechanism 20 has a temperature detection end 7a at the outlet of the furnace F. Furnace outlet temperature detecting means 7 for detecting the temperature of the flue gas at the furnace outlet, and a detecting end 8a for the flue D on the inlet side of the bag filter 16 for detecting the temperature of the exhaust gas. The apparatus is provided with a detecting means 8 and an oxygen concentration detecting means 6 for arranging an oxygen detecting end 6a in the flue D on the outlet side of the bag filter 16 to detect the oxygen concentration in the exhaust gas. The steam generated by the waste heat boiler 15 is
It is used as a drive source of a power generation device 50 that generates power by rotating a turbine.

【0015】また、ゴミ焼却炉10には、火炉F内にゴ
ミを投入する給塵機構11と、前記火炉F内に一次空気
を供給する一次空気供給機構12と、前記火炉F内での
前記ゴミの焼却処理に伴い生成した燃焼ガスを二次燃焼
させる二次燃焼空間Sを形成した二次燃焼室13と、前
記二次燃焼室13内に二次空気を供給する二次空気供給
機構14とを設けてある。その燃焼制御機構20には、
給塵機構11による前記火炉F内へのゴミの供給量を、
その燃焼発熱量に対し目標発熱量を設定して制御する給
塵量制御手段25が設けられている。
The refuse incinerator 10 includes a dust supply mechanism 11 for introducing refuse into the furnace F, a primary air supply mechanism 12 for supplying primary air into the furnace F, and a A secondary combustion chamber 13 that forms a secondary combustion space S for secondary combustion of combustion gas generated by the incineration of garbage; and a secondary air supply mechanism 14 that supplies secondary air into the secondary combustion chamber 13 Are provided. The combustion control mechanism 20 includes:
The amount of refuse supplied into the furnace F by the dust supply mechanism 11 is
Dust supply amount control means 25 is provided for setting and controlling a target heat generation amount with respect to the combustion heat generation amount.

【0016】燃焼制御機構20には、前記二次燃焼空間
Sの下流側の煙道Dに、前記二次燃焼空間S出口におけ
る排ガス中の酸素濃度を検出する酸素濃度検出手段6が
設けられている。さらに、燃焼制御機構20は、その酸
素濃度検出手段6で検出する排ガス中の酸素濃度と、前
記一次空気供給機構12と前記二次空気供給機構14と
により供給された総燃焼空気量とを基に、前記火炉F内
に投入されたゴミの燃焼発熱量を演算導出する燃焼発熱
量演算手段21を備え、さらに、このように演算された
燃焼発熱量と、クレーン(図示せず)等により給塵機構
11に投入されたゴミの重量とを基に、火炉Fに供給さ
れたゴミの単位重量あたりの発熱量をゴミ質として推定
するゴミ発熱量推定手段22を備える。
The combustion control mechanism 20 is provided with an oxygen concentration detecting means 6 for detecting the oxygen concentration in the exhaust gas at the outlet of the secondary combustion space S in the flue D downstream of the secondary combustion space S. I have. Further, the combustion control mechanism 20 determines the oxygen concentration in the exhaust gas detected by the oxygen concentration detecting means 6 and the total amount of combustion air supplied by the primary air supply mechanism 12 and the secondary air supply mechanism 14. The combustion heating value calculating means 21 for calculating and deriving the combustion heating value of the refuse charged into the furnace F is provided. Further, the combustion heating value calculated in this manner is supplied by a crane (not shown) or the like. A dust heating value estimating means 22 for estimating a heating value per unit weight of the dust supplied to the furnace F as dust quality based on the weight of the dust input to the dust mechanism 11.

【0017】そして、燃焼制御機構20は、このように
推定された単位重量あたりのゴミの発熱量と、予め設定
されるゴミの目標焼却量等とを基に、前記給塵機構11
と、前記一次空気供給機構12と、前記二次空気供給機
構14とをそれぞれ調節するのである。
The combustion control mechanism 20 then controls the dust supply mechanism 11 based on the heat generation amount of dust per unit weight estimated in this way and a preset target incineration amount of dust.
Then, the primary air supply mechanism 12 and the secondary air supply mechanism 14 are adjusted.

【0018】また、給塵量制御手段25は、給塵機構1
1の動作速度に対するゴミの供給量である給塵効率を算
出する給塵効率算出工程を実行するための給塵効率算出
手段26を備えており、給塵効率算出手段25は、2〜
3時間の所定時間内における給塵機構11の動作速度の
移動平均値と、同じく所定時間内におけるクレーン等か
ら給塵機構11へのゴミの投入重量の移動平均値とを基
に、給塵効率を算出する。
The dust supply amount control means 25 includes a dust supply mechanism 1.
1 is provided with a dust supply efficiency calculating means 26 for executing a dust supply efficiency calculating step of calculating a dust supply efficiency which is a supply amount of dust with respect to the operation speed of 1;
The dusting efficiency is determined based on the moving average value of the operating speed of the dust supply mechanism 11 within a predetermined time of 3 hours and the moving average value of the weight of dust input from the crane or the like to the dust supply mechanism 11 within the predetermined time period. Is calculated.

【0019】また、給塵量制御手段25は基準動作速度
算出手段27を備えており、基準動作速度算出手段27
は、給塵効率算出手段26で算出された給塵効率と、ゴ
ミ発熱量推定手段22で推定されたゴミの単位重量あた
りの発熱量と、予め設定されているゴミの目標焼却量か
ら求められる、火炉Fにおける単位時間あたりの目標発
熱量とを基に、給塵機構11により目標発熱量を発する
ゴミを火炉Fに供給することができる給塵機構11の基
準動作速度を算出する基準動作速度算出工程を実行す
る。
The dust supply amount control means 25 includes a reference operation speed calculation means 27.
Is calculated from the dust-supply efficiency calculated by the dust-supply efficiency calculating means 26, the heat value per unit weight of dust estimated by the dust heat value estimating means 22, and the preset target incineration amount of dust. A reference operation speed for calculating a reference operation speed of the dust supply mechanism 11 capable of supplying dust generating the target heat generation amount to the furnace F based on the target heat generation amount per unit time in the furnace F based on the target heat generation amount per unit time. Execute the calculation process.

【0020】そして、給塵制御手段25は、このように
算出した基準動作速度に基づいて給塵機構11の動作速
度を設定する動作速度設定手段28を備えており、動作
速度設定手段28は、給塵機構11の動作速度を、基準
動作速度算出手段27で算出された基準動作速度に所定
の上乗せ量を加算した値、好ましくは、基準動作速度に
対して5〜15%程度の割合の上乗せ量を基準動作速度
に加算した値に設定する動作速度設定工程を実行し、給
塵機構11の動作速度を、火炉Fにおいて目標発熱量を
達成することができると推定される値よりも若干大きい
値に設定して、急激な給塵効率の低下やゴミ質の低下等
が発生しても、火炉Fのゴミ切れの発生を抑制すること
ができる。
The dust supply control means 25 includes an operation speed setting means 28 for setting the operation speed of the dust supply mechanism 11 based on the reference operation speed calculated as described above. The operation speed of the dust supply mechanism 11 is a value obtained by adding a predetermined additional amount to the reference operation speed calculated by the reference operation speed calculation means 27, preferably, a ratio of about 5 to 15% of the reference operation speed. An operation speed setting step of setting the amount to a value obtained by adding the amount to the reference operation speed is performed, and the operation speed of the dust supply mechanism 11 is slightly larger than the value estimated to be able to achieve the target heating value in the furnace F. When the value is set to a value, even if a sudden decrease in dust supply efficiency or a decrease in dust quality occurs, it is possible to prevent the furnace F from running out of dust.

【0021】さらに、動作速度設定手段28は、図2に
示すように、先ず、ゴミ発熱量推定手段22で推定した
ゴミの単位重量あたりの発熱量が設計基準となる基準ゴ
ミ発熱量以下であるときは、基準動作速度に加算する上
記上乗せ量の基準動作速度に対する割合である上乗せ率
を10%程度に維持し、上記ゴミの単位重量あたりの発
熱量が上記基準ゴミ発熱量以上且つ予め設定された高質
ゴミ発熱量以下であるときは、上記上乗せ率を10%か
ら5%の範囲内でゴミの単位重量あたりの発熱量が大き
いほど小さくなるように設定し、さらに、ゴミの単位重
量あたりの発熱量が高質ゴミ発熱量以上であるときは、
上記上乗せ率を5%に維持する。このように、動作速度
設定手段28は、単位重量あたりの発熱量が大きい高質
のゴミが火炉Fに投入された場合に、給塵機構11の動
作速度の過剰程度を低めに設定して、火炉F内における
発熱量の過剰上昇を抑制するのである。
Further, as shown in FIG. 2, the operating speed setting means 28 first determines that the heat value per unit weight of dust estimated by the dust heat value estimating means 22 is equal to or smaller than a reference dust heat value as a design standard. At this time, the rate of addition of the additional amount to the reference operation speed, which is the ratio of the additional amount to the reference operation speed, is maintained at about 10%, and the heat generation amount per unit weight of the dust is equal to or more than the reference heat generation amount and is set in advance. When the heat generation amount is less than the high-quality garbage, the additional rate is set in the range of 10% to 5% so that the heat generation amount per unit weight of the garbage becomes smaller as the heat generation amount becomes larger. If the calorific value of the
The above addition rate is maintained at 5%. In this way, the operation speed setting means 28 sets the excessive degree of the operation speed of the dust supply mechanism 11 low when high-quality dust having a large heat value per unit weight is put into the furnace F, This suppresses an excessive increase in the calorific value in the furnace F.

【0022】さらにまた、動作速度設定手段28は、通
常は、基準動作速度に対して若干過剰気味に設定するの
であるが、火炉F内の発熱量が目標発熱量以上となった
ときは、給塵機構11の動作速度を過剰気味に維持して
おくと、火炉Fの能力の上限以上の発熱量が発生する危
険性があるとして、給塵機構11の動作速度を、一時的
に通常の動作速度に対して例えば50%程度以上低減し
た値に設定し、さらに、この一時的な動作速度の低減を
適正状態に復帰するまでパルス的に行うように構成され
ている。
Further, the operating speed setting means 28 normally sets the operating speed to be slightly excessive with respect to the reference operating speed. However, when the calorific value in the furnace F exceeds the target calorific value, If the operating speed of the dust mechanism 11 is maintained at an excessive level, there is a danger that a heating value exceeding the upper limit of the capacity of the furnace F may be generated. For example, the speed is set to a value reduced by about 50% or more with respect to the speed, and further, the temporary reduction of the operating speed is performed in a pulsed manner until the speed returns to an appropriate state.

【0023】以上ように構成されたゴミ焼却設備におい
て、発熱量の安定性の確認のために、上記給塵機構11
の動作速度の上記上乗せ率を15%に設定して廃熱ボイ
ラ15から発生する水蒸気量を計測した結果、水蒸気量
は90%以上の頻度で±5%以内に収まっており、火炉
Fの発熱量が安定していることが判る。
In the garbage incineration system configured as described above, the dust supply mechanism 11 is used to confirm the stability of the calorific value.
As a result of measuring the amount of water vapor generated from the waste heat boiler 15 by setting the above-mentioned addition rate of the operation speed of the furnace to 15%, the amount of water vapor was within ± 5% at a frequency of 90% or more, and the heat generation of the furnace F It can be seen that the amount is stable.

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

【図1】ゴミ焼却設備の概略構成図FIG. 1 is a schematic configuration diagram of a garbage incineration facility.

【図2】ゴミの発熱量と設定される上乗せ率との関係を
示すグラフ図
FIG. 2 is a graph showing the relationship between the amount of heat generated by dust and a set additional rate;

【符号の説明】[Explanation of symbols]

10 焼却炉 11 給塵機構(給塵手段) 20 燃焼制御機構 25 給塵量制御手段 26 給塵効率算出手段 27 基準動作速度算出手段 28 動作速度設定手段 F 火炉 Reference Signs List 10 incinerator 11 dust supply mechanism (dust supply means) 20 combustion control mechanism 25 dust supply amount control means 26 dust supply efficiency calculation means 27 standard operation speed calculation means 28 operation speed setting means F furnace

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 火炉内でゴミを焼却処理する焼却炉にお
いて、給塵手段による前記火炉内への前記ゴミの供給量
を制御する給塵量制御方法であって、 前記給塵手段の動作速度に対する前記ゴミの供給量であ
る給塵効率を算出する給塵効率算出工程と、 前記給塵効率算出工程で算出された給塵効率と、前記ゴ
ミの単位量あたりの発熱量と、前記火炉における目標発
熱量とから、前記給塵手段の基準動作速度を算出する基
準動作速度算出工程と、 前記給塵手段の動作速度を、前記基準動作速度算出工程
で算出された基準動作速度に所定の上乗せ量を加算した
動作速度に設定する動作速度設定工程とを実行する給塵
量制御方法。
1. An incinerator for incinerating garbage in a furnace, comprising: a dust supply amount control method for controlling a supply amount of the refuse into the furnace by a dust supply unit; A dust supply efficiency calculating step of calculating a dust supply efficiency that is a supply amount of the dust with respect to, a dust supply efficiency calculated in the dust supply efficiency calculation step, a calorific value per unit amount of the dust, and A reference operation speed calculation step of calculating a reference operation speed of the dust supply unit from the target heat generation amount, and a predetermined addition of the operation speed of the dust supply unit to the reference operation speed calculated in the reference operation speed calculation step. An operation speed setting step of setting an operation speed to which the amount has been added.
【請求項2】 前記基準動作速度に対する前記上乗せ量
の割合が、前記ゴミの単位量あたりの発熱量が大きいほ
ど小さく設定されている請求項1に記載の給塵量制御方
法。
2. The dust supply amount control method according to claim 1, wherein a ratio of the additional amount to the reference operation speed is set smaller as a heat generation amount per unit amount of the dust is larger.
【請求項3】 前記給塵効率算出工程が、所定時間内に
おける前記給塵手段の動作速度と、同じく所定時間内に
おける前記給塵手段へのゴミの投入量とから、前記給塵
効率を算出する工程である請求項1又は2に記載の給塵
量制御方法。
3. The dust-supply efficiency calculating step includes calculating the dust-supply efficiency from an operation speed of the dust-supply means within a predetermined time and an amount of dust input to the dust-supply means within the same predetermined time. The dust supply amount control method according to claim 1, wherein the dust supply amount is controlled.
【請求項4】 前記動作速度設定工程において、前記給
塵手段の動作速度を設定するに、前記火炉内の発熱量が
前記目標発熱量以上となったときには、前記給塵手段の
動作速度を一時的に所定の量を低下させる請求項1から
3の何れか1項に記載の給塵量制御方法。
4. An operation speed setting step for setting the operation speed of the dust supply unit, wherein the operation speed of the dust supply unit is temporarily set when a heat generation amount in the furnace becomes equal to or more than the target heat generation amount. The dust supply amount control method according to any one of claims 1 to 3, wherein the predetermined amount is reduced.
JP2001152485A 2001-05-22 2001-05-22 Dust supply control method in incinerator Expired - Lifetime JP3850228B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001152485A JP3850228B2 (en) 2001-05-22 2001-05-22 Dust supply control method in incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001152485A JP3850228B2 (en) 2001-05-22 2001-05-22 Dust supply control method in incinerator

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Publication Number Publication Date
JP2002349827A true JP2002349827A (en) 2002-12-04
JP3850228B2 JP3850228B2 (en) 2006-11-29

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ID=18997147

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Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017180971A (en) * 2016-03-31 2017-10-05 日立造船株式会社 Automatic combustion control method for incineration facility

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017180971A (en) * 2016-03-31 2017-10-05 日立造船株式会社 Automatic combustion control method for incineration facility

Also Published As

Publication number Publication date
JP3850228B2 (en) 2006-11-29

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