JPS6363808B2 - - Google Patents

Info

Publication number
JPS6363808B2
JPS6363808B2 JP56215789A JP21578981A JPS6363808B2 JP S6363808 B2 JPS6363808 B2 JP S6363808B2 JP 56215789 A JP56215789 A JP 56215789A JP 21578981 A JP21578981 A JP 21578981A JP S6363808 B2 JPS6363808 B2 JP S6363808B2
Authority
JP
Japan
Prior art keywords
amount
value
furnace
garbage
air
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
Application number
JP56215789A
Other languages
Japanese (ja)
Other versions
JPS58115215A (en
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 filed Critical
Priority to JP56215789A priority Critical patent/JPS58115215A/en
Publication of JPS58115215A publication Critical patent/JPS58115215A/en
Publication of JPS6363808B2 publication Critical patent/JPS6363808B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/02Regulating fuel supply conjointly with air supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2225/00Measuring
    • F23N2225/08Measuring temperature
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2233/00Ventilators
    • F23N2233/06Ventilators at the air intake
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2235/00Valves, nozzles or pumps
    • F23N2235/02Air or combustion gas valves or dampers
    • F23N2235/06Air or combustion gas valves or dampers at the air intake
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2239/00Fuels
    • F23N2239/02Solid fuels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N5/00Systems for controlling combustion
    • F23N5/18Systems for controlling combustion using detectors sensitive to rate of flow of air or fuel

Description

【発明の詳細な説明】 本発明は、都市ごみ、塵芥やそれに類似した廃
棄物を焼却処理するためのボイラ付ごみ焼却炉に
おいて燃焼を安定化させ効果的に処理する焼却炉
の運転方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an incinerator operating method for stabilizing combustion and effectively treating municipal waste, garbage, and similar waste in a boiler-equipped garbage incinerator. It is.

一般にごみ焼却炉においては、最近、発生する
熱エネルギーの有効利用を行なうために廃熱利用
の組合方式として排熱ボイラを設置し、発生した
蒸気を利用することが多くなつた。しかしこの焼
却炉に供給されるごみの性状、発熱量が刻々変化
するために発生量が変化し、蒸気発生量が大巾に
変動することが多い。この蒸気発生量が変動する
と蒸気の利用計画を立てる時に、変動する蒸気量
の最低値で計画せざるを得ないから、発生した蒸
気の一部しか有効に利用できないので問題があ
る。
In general, waste heat boilers have recently been installed in garbage incinerators as a combination system for waste heat utilization in order to effectively utilize the heat energy generated, and the steam generated has become increasingly used. However, because the properties and calorific value of the waste supplied to this incinerator change from moment to moment, the amount generated changes, and the amount of steam generated often fluctuates widely. If this amount of steam generation fluctuates, when planning the use of steam, the plan must be based on the lowest value of the fluctuating amount of steam, which poses a problem because only a portion of the steam generated can be used effectively.

また、蒸気量を一定にすることは焼却炉の熱出
力を安定にすることにもなり、蒸気の有効利用と
燃焼の安定化を行なう上で、蒸気発生量を一定に
制御することは非常に重要なことである。
Furthermore, keeping the amount of steam constant also stabilizes the thermal output of the incinerator, so controlling the amount of steam generated at a constant level is extremely important for effective use of steam and stabilization of combustion. It's important.

従来は、蒸気流量を検知して、蒸気発生量が一
定になるように燃焼空気量を調整してそれとは別
に、炉内温度が高温になり過ぎると炉壁のレンガ
が損傷するので炉温が設定値以上になると炉冷送
風機により炉冷空気を炉内に送つて、常に炉温が
設定値以下になるように制御している。
Conventionally, the flow rate of steam was detected and the amount of combustion air was adjusted to keep the amount of steam generated constant. When the temperature exceeds the set value, the furnace cooling air blower sends cold air into the furnace to control the furnace temperature so that it is always below the set value.

このような方法では、炉温が設定値以下になつ
て炉冷空気が送入されなくなると、当然蒸気発生
量は減少し燃焼空気量を増すことになるが、その
応答は炉内のごみ量、厚さ等の状態で異なる。従
つて炉内にごみが燃えやすい状態で十分に存在す
る時は燃焼空気量を増すとすぐにごみに火がつく
から炉温も上昇し蒸気量を多くなるから蒸気量制
御が行なわれる。しかし、炉内に存在するごみ量
が少なくなつた時に燃焼空気量を増しても過剰空
気となつて炉温を更に下げてしまい、蒸気量も減
少し、制御不能となる。このようなことにならな
いように通常は炉内のごみを観察して、ごみが少
なくなつたらごみ送り速度を速くしてごみを多く
送り、ごみ量が多くなつたらごみ送り速度を遅く
するが、炉温が低くなつた時にごみ送り速度を速
くしても、炉内温度が低い影響で乾燥速度が遅
く、炉温が上昇するまでかなり時間がかかる。し
かもその時に過剰空気を入れ過ぎると炉温が更に
下がり消火する危険すらあるなど操業性の上で問
題があるばかりか燃焼処理の不安定化となつて効
率不良と廃熱利用にも支障となる欠点があつた。
In this method, when the furnace temperature falls below the set value and the furnace cold air is no longer fed, the amount of steam generated naturally decreases and the amount of combustion air increases, but the response depends on the amount of garbage in the furnace. , thickness, etc. Therefore, when a sufficient amount of trash exists in the furnace in a combustible state, increasing the amount of combustion air will quickly ignite the trash, raising the furnace temperature and increasing the amount of steam, so steam amount control is performed. However, even if the amount of combustion air is increased when the amount of dust present in the furnace decreases, the excess air becomes excess and further lowers the furnace temperature, and the amount of steam also decreases, making control uncontrollable. To prevent this from happening, normally we observe the garbage in the furnace, and when there is less garbage, we increase the garbage feeding speed to feed more garbage, and when the amount of garbage increases, we slow down the garbage feeding speed. Even if the waste feeding speed is increased when the furnace temperature is low, the drying speed is slow due to the low temperature inside the furnace, and it takes a considerable amount of time for the furnace temperature to rise. Moreover, if too much air is introduced at that time, the furnace temperature will drop further and there is a risk of extinguishing the fire, which not only causes problems in terms of operability, but also destabilizes the combustion process, resulting in poor efficiency and hindering the utilization of waste heat. There were flaws.

本発明は、これら従来の諸欠点を適確に除去し
ようとするもので、炉温の低下をなくし、蒸発量
制御が不能とならないようにごみ送り速度を制御
して燃焼を安定化させ効果的に焼却処分を可能に
し、且つ操業性も著しく向上しうる経済的な方法
を提供することを目的としたものである。
The present invention aims to accurately eliminate these conventional drawbacks, and effectively stabilizes combustion by eliminating the drop in furnace temperature and controlling the waste feeding speed so as not to make it impossible to control the amount of evaporation. The purpose of this project is to provide an economical method that allows for incineration and significantly improves operability.

本発明はごみ類を焼却炉内の燃焼室で燃焼空気
を供給しつつ燃焼するボイラ付ごみ焼却炉におい
て、炉冷空気が常に炉内に送入されている状態を
保ちながら、該炉冷空気量の増減で炉温を一定に
制御し、かつ前記燃焼空気の燃焼空気量の増減で
前記ボイラの蒸気発生量を制御するに際し、前記
炉冷空気量が単位時間内に設定上限値以上又は、
設定下限値以下になつたときごみ送り速度を調節
して運転することを特徴としたごみ焼却炉の運転
制御方法である。
The present invention provides a waste incinerator with a boiler that burns garbage while supplying combustion air in a combustion chamber in the incinerator, and the furnace cooled air is constantly supplied into the furnace. When controlling the furnace temperature to a constant value by increasing or decreasing the amount of combustion air, and controlling the steam generation amount of the boiler by increasing or decreasing the amount of combustion air, the amount of furnace cooling air is equal to or higher than a set upper limit within a unit time, or
This is a method for controlling the operation of a waste incinerator, which is characterized in that the waste incinerator is operated by adjusting the waste feeding speed when the value falls below a set lower limit value.

本発明の実施例につき図面を参照して説明する
と、投入ホツパー1内のごみは投入プツシヤー2
により焼却炉A内へ送入し、ストーカ駆動装置3
でストーカBを動かすことによりごみを送る。こ
のごみ送りの速度は、ごみ送り速度調節器により
投入プツシヤー2およびストーカBの単位時間当
りの稼動回数を変えることにより変更される 前記焼却炉Aに連結配備される燃焼空気送風機
4を出た空気は、燃焼空気ダンパ6によりボイラ
8の蒸気発生量を一定に制御するように調節計1
2例えば蒸気流量調節計で調節されて焼却炉A内
に送入される。又焼却炉の炉温を一定に制御する
ように調節計13例えば電子式温度指示調節計の
指示で炉冷空気ダンパ7を開閉して、炉冷空気送
風機5からの炉冷空気量を調節する。
An embodiment of the present invention will be described with reference to the drawings.
into the incinerator A, and the stoker drive device 3
The garbage is sent by moving stoker B. The speed of this waste feeding is changed by changing the number of operations per unit time of the input pusher 2 and the stoker B using the waste feeding speed regulator. Air exiting the combustion air blower 4 connected to the incinerator A. The controller 1 is configured to control the steam generation amount of the boiler 8 at a constant level by the combustion air damper 6.
2. For example, the steam is regulated by a steam flow rate controller and sent into the incinerator A. Further, in order to control the furnace temperature of the incinerator at a constant level, the amount of furnace cooling air from the furnace cooling air blower 5 is adjusted by opening and closing the furnace cooling air damper 7 according to instructions from a controller 13, for example, an electronic temperature indicating controller. .

一方、炉冷空気量に上限と下限の設定値を設け
差圧式記録流量計14を介して演算器9により単
位時間毎に炉冷空気量が上限以上になつた時間お
よび下限以下になつた時間を各々積算する。あら
かじめ設定時間を決めると共に前記ストーカBの
ごみ送り速度の設定値を速い値と遅い値の2通り
決める。
On the other hand, upper and lower limit set values are set for the amount of furnace cooling air, and the time when the amount of furnace cooling air exceeds the upper limit and the time when it falls below the lower limit for each unit time is determined by the calculator 9 via the differential pressure recording flow meter 14. Accumulate each. The setting time is determined in advance, and the setting value of the garbage feeding speed of the stoker B is determined in two ways: a fast value and a slow value.

そして単位時間内に炉冷空気量が下限以下にな
つた積算時間が設定時間以上になつた時に、ごみ
送り速度を速い値に変え、炉冷空気量が上限以上
になつた積算時間が設定時間以上になつた時にご
み送り速度を遅い値に変えるように制御するよう
にしてある。
Then, when the cumulative time during which the amount of furnace cooled air is below the lower limit within a unit time exceeds the set time, the garbage feed speed is changed to a faster value, and the cumulative time during which the amount of furnace cooled air is above the upper limit exceeds the set time. When the value exceeds this value, the garbage feeding speed is controlled to be changed to a slower value.

このようにした場合、焼却炉A内の熱出力が大
きくなると、炉温を一定にするために炉冷空気量
が多くなり、ボイラ8の蒸気発生量を一定にする
ために燃焼空気量は逆に少なくなる。又焼却炉A
内の熱出力が小さくなると、炉冷空気量が少なく
なり、燃焼空気量は多くなる。このように炉冷空
気量と燃焼空気量は正反対の動きをするから、炉
冷空気量と燃焼空気量を加えたものは或る程度の
範囲内で一定となる。
In this case, when the heat output in the incinerator A increases, the amount of furnace cooling air increases to keep the furnace temperature constant, and the amount of combustion air increases in order to keep the amount of steam generated in the boiler 8 constant. will decrease. Also incinerator A
As the heat output within the furnace decreases, the amount of furnace cooling air decreases and the amount of combustion air increases. Since the amount of furnace cooling air and the amount of combustion air move in opposite directions in this way, the sum of the amount of furnace cooling air and the amount of combustion air remains constant within a certain range.

さらに炉内の熱出力が大きく低下すると、炉冷
空気量がゼロになり、炉温が下がり蒸気量制御が
できなくなる。油やガス等の燃料であれば、熱出
力が低下した時に燃料を供給してすぐに復帰でき
るが、ごみ焼却炉では、ごみ送り速度を速くして
も、すぐには燃焼しないために、熱出力が回復す
るのに時間がかかるが、前記の通り炉冷空気量に
下限設定値を設けて下限以下になつた積算時間が
多くなるとごみ送り速度を速くすると、炉冷空気
量がゼロとなることを事前に回避できる。
Furthermore, when the thermal output inside the furnace decreases significantly, the amount of furnace cooling air becomes zero, and the furnace temperature drops, making it impossible to control the amount of steam. With fuels such as oil and gas, when the heat output decreases, fuel can be supplied to quickly recover, but in garbage incinerators, even if the garbage feeding speed is increased, it does not burn immediately, so the heat output is reduced. It takes time for the output to recover, but as mentioned above, if a lower limit is set for the amount of furnace cooling air, and the cumulative amount of time that the amount is below the lower limit increases, increasing the garbage feed rate will cause the amount of furnace cooling air to drop to zero. This can be avoided in advance.

またごみ送り速度を速くしたままだと、熱出力
が大きくなつてきて炉冷空気が最大量になつても
炉温が上がることになるから、炉冷空気量が上限
以上になつた積算時間が多くなつたらごみ送り速
度を遅くすることにより、ごみ送り速度の切りか
えが自動となつて燃焼を安定化できるのである。
In addition, if the waste feed rate remains high, the heat output will increase and the furnace temperature will rise even when the amount of furnace cooling air reaches the maximum amount, so the cumulative time when the amount of furnace cooling air exceeds the upper limit will increase. By slowing down the garbage feed rate when the amount increases, the garbage feed rate can be switched automatically and combustion can be stabilized.

この上限、下限の設定値としては、上限が炉冷
空気量の最大値の80%、下限が同じく最大値の20
%とするのが最適である。
The upper and lower limit settings are such that the upper limit is 80% of the maximum furnace cooling air amount, and the lower limit is 20% of the maximum value.
It is best to set it as %.

ごみ送り速度の別の制御方法として、ごみ送り
速度の設定値を速い値、中間の値、遅い値の3通
り決め、単位時間内に炉冷空気量が下限以下にな
つた積算時間が設定時間以上の間は速い値とし、
炉冷空気量が上限以上になつた積算時間が設定時
間以上の間は遅い値で、それら以外の時は中間の
値で運転するのも効果的な結果が得られる。
Another way to control the waste feed speed is to set the waste feed speed in three settings: fast, medium, and slow, and then calculate the cumulative time during which the amount of furnace cooling air falls below the lower limit within a unit time. For the above, it is considered a fast value,
Effective results can also be obtained by operating at a slow value while the cumulative time during which the amount of furnace cooling air exceeds the upper limit is longer than the set time, and at other times at an intermediate value.

なおごみ送り速度が速い値と遅い値の2通りの
場合、速度の変更が急激すぎるのでつねに速度の
変更をくり返し燃焼状態が不安定になりやすい
が、3通りの値の場合ほとんどの時間は中間の値
で運転し、かつ、速度の変更の頻度が少ないの
で、燃焼はより安定する。
Note that when the garbage feeding speed is set to two values, one fast and one slow, the speed changes are too sudden, causing the combustion state to become unstable due to constant speed changes. Since the engine operates at a value of , and the speed changes less frequently, combustion is more stable.

本発明はボイラ付ごみ焼却炉において、炉冷空
気が常に炉内に送入されている状態を保ちなが
ら、該炉冷空気量の増域で炉温を一定に制御し、
かつ前記燃焼空気の燃焼空気量の増減で前記ボイ
ラの蒸気発生量を制御するに際し、前記炉冷空気
量が単位時間内に設定上限値以上又は、設定下限
値以下になつたときごみ送り速度を調節して運転
することにより、常に炉内炉温を一定に保ち、燃
焼空気により蒸気発生量を一定に制御することが
可能であり簡単な方法でごみ送り速度を制御して
炉内に存在するごみ量を適正な範囲に収めること
で蒸気発生量量が制御不能となる不具合な事態を
未然に防止して燃焼の安定化を確実にし焼却処理
の効率を著しく向上し、その操業性も良好経済的
にでき、熱エネルギーの有効利用も大巾に改善で
きる等の利益がある。
The present invention provides a waste incinerator with a boiler that controls the furnace temperature to a constant level by increasing the amount of furnace cooling air while keeping the furnace cooling air constantly being fed into the furnace.
and when controlling the steam generation amount of the boiler by increasing or decreasing the amount of combustion air, when the amount of furnace cooling air becomes more than a set upper limit value or less than a set lower limit value within a unit time, the garbage feeding rate is adjusted. By adjusting the operation, it is possible to keep the furnace temperature constant at all times and control the amount of steam generated by the combustion air to a constant level. By keeping the amount of waste within an appropriate range, we can prevent malfunctions in which the amount of steam generated becomes uncontrollable, ensure stable combustion, and significantly improve the efficiency of incineration processing, resulting in good operability and economy. It has the advantage of being able to improve the efficiency of heat energy and the effective use of thermal energy.

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

図面は本発明方法の実施例を示す系統説明図で
ある。 A……焼却炉、B……ストーカ、C……炉下シ
ユート、D……灰出シユート、1……投入ホツパ
ー、2……投入プツシヤー、3……ストーカ駆動
装置、4……燃焼空気送風機、5……炉冷空気送
風機、6,6′……燃焼空気ダンパ、7……炉冷
空気ダンパ、8……ボイラ、9……演算器、10
……ごみ送り速度調節器、11……油圧ユニツ
ト。
The drawing is a system explanatory diagram showing an embodiment of the method of the present invention. A... Incinerator, B... Stoker, C... Under-furnace chute, D... Ash discharge chute, 1... Input hopper, 2... Input pusher, 3... Stoker drive device, 4... Combustion air blower , 5... Furnace cold air blower, 6, 6'... Combustion air damper, 7... Furnace cool air damper, 8... Boiler, 9... Arithmetic unit, 10
...Garbage feed speed regulator, 11...Hydraulic unit.

Claims (1)

【特許請求の範囲】 1 ごみ類の焼却炉内の燃焼室で燃焼空気を供給
しつつ燃焼するボイラ付ごみ焼却炉において、炉
冷空気が常に炉内に送入されている状態を保ちな
がら、該炉冷空気量の増減で炉温を一定に制御
し、かつ前記燃焼空気の燃焼空気量の増減で前記
ボイラの蒸気発生量を制御するに際し、前記炉冷
空気量が単位時間内に設定上限値以上又は設定下
限値以下になつたときごみ送り速度を調節して運
転することを特徴としたごみ焼却炉の運転制御方
法。 2 前記ごみ送り工程が、予め、ごみ送り速度を
速い値、中間の値、遅い値の三種類決めておき、
単位時間内に炉冷空気量が下限設定値以下になつ
た積算時間が設定時間以上の間は、ごみ送り速度
を速い値とし、単位時間内に炉冷空気量が設定上
限値以上になつた積算時間が設定時間以上の間は
ごみ送り速度を遅い値とし、それ以外の時はごみ
送り速度を中間の値で運転するものである特許請
求の範囲第1項記載のごみ焼却炉の運転制御方
法。
[Scope of Claims] 1. In a waste incinerator with a boiler that burns while supplying combustion air in the combustion chamber of the waste incinerator, while maintaining the state in which the furnace cool air is constantly fed into the furnace, When controlling the furnace temperature at a constant level by increasing or decreasing the amount of the furnace cooling air, and controlling the steam generation amount of the boiler by increasing or decreasing the amount of the combustion air, the amount of the furnace cooling air is set at a set upper limit within a unit time. A method for controlling the operation of a waste incinerator, characterized in that the waste incinerator is operated by adjusting the waste feeding speed when the value exceeds a value or falls below a set lower limit value. 2. In the garbage feeding step, three types of garbage feeding speeds are determined in advance: a fast value, an intermediate value, and a slow value,
If the cumulative time during which the amount of cold air in the furnace falls below the lower limit set value within a unit time is greater than or equal to the set time, the garbage feed rate will be set to a higher value, and if the amount of cold air in the furnace exceeds the upper limit set within the unit time. The garbage incinerator operation control according to claim 1, wherein the garbage feeding speed is set to a slow value while the cumulative time is longer than a set time, and the garbage feeding speed is operated at an intermediate value at other times. Method.
JP56215789A 1981-12-28 1981-12-28 Operation controlling method for refuse incinerator Granted JPS58115215A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56215789A JPS58115215A (en) 1981-12-28 1981-12-28 Operation controlling method for refuse incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56215789A JPS58115215A (en) 1981-12-28 1981-12-28 Operation controlling method for refuse incinerator

Publications (2)

Publication Number Publication Date
JPS58115215A JPS58115215A (en) 1983-07-08
JPS6363808B2 true JPS6363808B2 (en) 1988-12-08

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP56215789A Granted JPS58115215A (en) 1981-12-28 1981-12-28 Operation controlling method for refuse incinerator

Country Status (1)

Country Link
JP (1) JPS58115215A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60232413A (en) * 1984-04-27 1985-11-19 Hitachi Zosen Corp Method to control fans in incinerator

Also Published As

Publication number Publication date
JPS58115215A (en) 1983-07-08

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