JP2000018547A - Gasification incinerating device and control method of operation of the same - Google Patents

Gasification incinerating device and control method of operation of the same

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Publication number
JP2000018547A
JP2000018547A JP10176892A JP17689298A JP2000018547A JP 2000018547 A JP2000018547 A JP 2000018547A JP 10176892 A JP10176892 A JP 10176892A JP 17689298 A JP17689298 A JP 17689298A JP 2000018547 A JP2000018547 A JP 2000018547A
Authority
JP
Japan
Prior art keywords
combustion chamber
primary
temperature
incineration
air supply
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
JP10176892A
Other languages
Japanese (ja)
Inventor
Terunobu Suzuki
照伸 鈴木
Katsumi Kawabata
勝美 川端
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric 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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP10176892A priority Critical patent/JP2000018547A/en
Publication of JP2000018547A publication Critical patent/JP2000018547A/en
Pending legal-status Critical Current

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  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the generation of black smoke by controlling the optimum amount of air. SOLUTION: The inside temperature of a secondary combustion chamber 6 is detected by a secondary temperature detector 9 while the changing rate per time of the inside temperature of the secondary combustion chamber 6, which is detected by the secondary temperature detector 9, is calculated by changing rate of secondary temperature per time operating means 24. In this case, when the changing rate of inside temperature of secondary combustion chamber 6 per time, which is calculated by the changing rate of secondary temperature per time operating means 24, is higher than a predetermined value, the supplying amount of secondary air, supplied by a secondary air supplying device 8, is increased forcibly.

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】この発明は、ガス化焼却装置
およびガス化焼却装置の運転制御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 gasification and incineration apparatus and a method for controlling the operation of the gasification and incineration apparatus.

【0002】[0002]

【従来の技術】図4は、従来のガス化燃焼炉の構成を示
している。従来のガス化燃焼炉は、焼却物が投入される
1次燃焼室(ガス化炉、乾溜炉)1と、1次燃焼室1に
おける焼却物の着火を行う1次着火装置(1次バーナ)
2と、焼却物の熱分解に必要な空気を1次燃焼室1に供
給する1次空気供給装置3と、1次燃焼室1の室内温度
を検出する1次温度検出器(熱電対)4と、1次燃焼室
1の室内圧を検出する圧力検出器5と、1次燃焼室1内
での焼却物の熱分解により発生した可燃性ガスを完全燃
焼させる2次燃焼室(ガス燃焼炉)6と、2次燃焼室6
に導入された可燃性ガスが燃焼するのに必要な温度を維
持する2次温度維持装置(2次バーナ)7と、可燃性ガ
スの燃焼に必要な空気を2次燃焼室6に供給する2次空
気供給装置8と、2次燃焼室6の室内温度を検出する2
次温度検出器(熱電対)9と、排ガスの温度を検出する
排ガス温度検出器(熱電対)10、煙突11と、1次着
火装置2および2次温度維持装置7のオン/オフ制御と
1次空気供給装置3による1次空気供給量および2次空
気供給装置8による2次空気供給量を制御する制御手段
12とを有している。
2. Description of the Related Art FIG. 4 shows a configuration of a conventional gasification combustion furnace. The conventional gasification combustion furnace includes a primary combustion chamber (gasification furnace, dry distillation furnace) 1 into which incineration material is charged, and a primary ignition device (primary burner) for igniting the incineration material in the primary combustion chamber 1.
2, a primary air supply device 3 for supplying air required for the thermal decomposition of incineration to the primary combustion chamber 1, and a primary temperature detector (thermocouple) 4 for detecting the indoor temperature of the primary combustion chamber 1 A pressure detector 5 for detecting the indoor pressure of the primary combustion chamber 1; and a secondary combustion chamber (gas combustion furnace) for completely combusting the combustible gas generated by the thermal decomposition of the incineration in the primary combustion chamber 1. ) 6 and secondary combustion chamber 6
Secondary temperature maintaining device (secondary burner) 7 for maintaining the temperature required for the combustible gas introduced into the combustion chamber to burn, and supplying air necessary for combustion of the combustible gas to the secondary combustion chamber 6 2 A secondary air supply device 8 for detecting the indoor temperature of the secondary combustion chamber 6
Secondary temperature detector (thermocouple) 9, exhaust gas temperature detector (thermocouple) 10 for detecting the temperature of exhaust gas, chimney 11, on / off control of primary ignition device 2 and secondary temperature maintaining device 7, and 1 A controller 12 for controlling the amount of primary air supplied by the secondary air supply device 3 and the amount of secondary air supplied by the secondary air supply device 8.

【0003】制御手段12は、1次温度検出器4により
検出された温度と圧力検出器5により検出された圧力と
2次温度検出器9により検出された温度と排ガス温度検
出器10により検出された温度により、1次空気供給装
置3による1次空気供給量と、2次空気供給装置8によ
る2次空気供給量を各々演算決定する。
The control means 12 detects the temperature detected by the primary temperature detector 4, the pressure detected by the pressure detector 5, the temperature detected by the secondary temperature detector 9, and the temperature detected by the exhaust gas temperature detector 10. Based on the temperature, the primary air supply amount by the primary air supply device 3 and the secondary air supply amount by the secondary air supply device 8 are calculated and determined.

【0004】つぎに、上述のような構成による従来のガ
ス化燃焼炉の動作について説明する。1次燃焼室1に投
入された焼却物は、1次バーナ2により着火され、1次
空気供給装置3によって1次燃焼室1に熱分解に必要な
空気が供給される。以降、1次燃焼室1の室内温度(以
下、1次温度という)は1次バーナ2の火力と供給空気
量の制御によって、所定値、例えば400〜500℃に
保たれる。着火された燃焼物はある部分が燃焼し、その
燃焼熱によりある部分は熱分解を始める。この熱分解に
よって1次燃焼室1では可燃性ガスが発生し、この可燃
性ガスは2次燃焼室6に送られる。
Next, the operation of the conventional gasification and combustion furnace having the above-described configuration will be described. The incineration material charged into the primary combustion chamber 1 is ignited by a primary burner 2 and air required for thermal decomposition is supplied to the primary combustion chamber 1 by a primary air supply device 3. Thereafter, the room temperature of the primary combustion chamber 1 (hereinafter, referred to as the primary temperature) is maintained at a predetermined value, for example, 400 to 500 ° C. by controlling the thermal power of the primary burner 2 and the amount of supplied air. A portion of the ignited combustion material burns, and the heat of combustion causes a portion to start pyrolysis. By this thermal decomposition, combustible gas is generated in the primary combustion chamber 1, and this combustible gas is sent to the secondary combustion chamber 6.

【0005】2次燃焼室6では、可燃性ガスを燃焼させ
るために、2次バーナ7により2次燃焼室6の室内温度
(以下、2次温度という)が、例えば800〜900℃
に保たれ、2次燃焼室6には2次空気供給装置8により
燃焼に必要な空気量が供給される。通常、2次温度を、
例えば800℃以上にしておくために、焼却物に着火す
る前に2次バーナ7を作動させ、2次温度を上昇させる
ための2次燃焼室予熱期間が設けられる。燃焼した可燃
性ガスは、排ガスとして煙突11より大気中に排出され
る。
In the secondary combustion chamber 6, in order to burn combustible gas, the indoor temperature (hereinafter referred to as secondary temperature) of the secondary combustion chamber 6 is set to, for example, 800 to 900.degree.
The secondary combustion chamber 6 is supplied with an amount of air required for combustion by a secondary air supply device 8. Usually, the secondary temperature is
For example, in order to keep the temperature at 800 ° C. or higher, a secondary combustion chamber preheating period is provided for operating the secondary burner 7 and raising the secondary temperature before igniting the incinerated material. The burnable combustible gas is discharged into the atmosphere from the chimney 11 as exhaust gas.

【0006】このようなガス化焼却炉においては、燃焼
過程を、2次温度を800℃等の所定温度以上に上昇さ
せるための2次燃焼室予熱期間と、1次燃焼室1の焼却
物を着火して熱分解により可燃性ガスを発生させ、2次
燃焼室6にて可燃性ガスを燃焼させるガス化燃焼期間
と、ガス化が終了して炭化した焼却物を1次燃焼室1で
燃焼灰化させる炭化燃焼期間と、炭化燃焼が衰えて灰化
が進み冷却してゆく冷却期間というように区分すること
がある。
[0006] In such a gasification incinerator, the combustion process includes a preheating period for the secondary combustion chamber for raising the secondary temperature to a predetermined temperature such as 800 ° C. or more, and the incineration of the primary combustion chamber 1 Combustion gas is generated by ignition and pyrolysis to generate a combustible gas, and the combustible gas is burned in the secondary combustion chamber 6, and the incinerated material that has been gasified and carbonized is burned in the primary combustion chamber 1 There are cases where the carbonization combustion period for incineration is divided into a cooling period in which carbonization combustion is attenuated and ashing proceeds and cools down.

【0007】つぎに、各部の制御方法について説明す
る。1次バーナ2は、1次温度により例えば500℃で
オフ、400℃で低下すれば再びオンというようにオン
/オフ制御される。通常、1次バーナ2は焼却物の着火
を行い、例えば500℃に一旦達すれば、以降1次バー
ナ2が再びオンすることはほとんどない。2次バーナ7
も同様で、2次温度により、例えば900℃でオフ、8
00℃に低下すれば再びオンというようにオン/オフ制
御される。2次燃焼室を800℃以上に保つことによ
り、可燃性ガスは着火手段によらずとも自己燃焼する。
従って通常、2次バーナ7についても、ガス化燃焼期間
が始まれば、オフすることになる。
Next, a control method of each unit will be described. The primary burner 2 is on / off controlled such that the primary burner 2 is turned off at, for example, 500 ° C. depending on the primary temperature, and turned on again when the temperature drops at 400 ° C. Usually, the primary burner 2 ignites the incinerated material, and once it reaches, for example, 500 ° C., the primary burner 2 hardly turns on again thereafter. Secondary burner 7
Similarly, depending on the secondary temperature, for example, off at 900 ° C., 8
If the temperature drops to 00 ° C., on / off control is performed so as to turn on again. By maintaining the temperature of the secondary combustion chamber at 800 ° C. or higher, the combustible gas self-combustes without using ignition means.
Therefore, the secondary burner 7 is normally turned off when the gasification combustion period starts.

【0008】ここで、1次空気供給装置3による1次空
気供給量は、ガス化が安定して行われるよう制御される
必要があり、2次空気供給装置8による2次空気供給量
は可燃性ガスを完全燃焼させる適量の空気を供給するよ
う制御される必要がある。
Here, the amount of primary air supplied by the primary air supply device 3 needs to be controlled so that gasification is performed stably, and the amount of secondary air supplied by the secondary air supply device 8 is flammable. It needs to be controlled to supply an appropriate amount of air to completely burn the reactive gas.

【0009】これらの空気量制御は、従来、過去の運転
データや作業者の勘といった経験則による方法、1次温
度または2次温度より燃焼状態を概略推定して制御する
方法、あるいは可燃性ガス、または排ガスの成分分析が
できるガスセンサを設け、その結果により必要な空気量
を判定する方法等がとられている。
Conventionally, such air amount control is based on empirical rules such as past operating data or operator's intuition, a method of roughly estimating a combustion state from a primary temperature or a secondary temperature, or a method of controlling flammable gas. Alternatively, a method is provided in which a gas sensor capable of analyzing the components of exhaust gas is provided, and the required amount of air is determined based on the result.

【0010】以上に述べた制御の一部もしくは全部は、
通常、焼却物のガス化が終了した時点で終了する。
[0010] Part or all of the control described above is
Usually, the process ends when the gasification of the incinerated material ends.

【0011】[0011]

【発明が解決しようとする課題】従来のガス化燃焼炉で
は、1次バーナによって焼却物の着火を行った直後は、
2次燃焼室における2次空気供給量が不足するため、黒
煙が発生する可能性がある。また、ガス化燃焼過程にお
いて、2次燃焼室の温度が上昇し過ぎ、2次燃焼室の温
度が2次燃焼室の耐火レンガ等の許容温度を超える可能
性があるため、炉の耐久性が低下する。
In the conventional gasification combustion furnace, immediately after the incineration is ignited by the primary burner,
Since the secondary air supply amount in the secondary combustion chamber is insufficient, black smoke may be generated. Further, in the gasification combustion process, the temperature of the secondary combustion chamber rises too much, and the temperature of the secondary combustion chamber may exceed the allowable temperature of the refractory bricks and the like of the secondary combustion chamber. descend.

【0012】また、1次燃焼室の温度上昇により可燃性
ガスの発生が増加して行く時点で、液体の可燃物が蒸発
と同時に燃焼した場合には、可燃性ガスが急激に発生
し、1次燃焼室が異常高温になることがあるため、炉の
耐久性が低下する。
Further, when the generation of combustible gas increases due to a rise in the temperature of the primary combustion chamber and the combustible liquid material burns simultaneously with the evaporation, the combustible gas is rapidly generated, and Since the temperature of the next combustion chamber may become abnormally high, the durability of the furnace is reduced.

【0013】また、なかには、空気供給量を燃焼過程
(ガス化燃焼過程、炭化燃焼過程)に従って自動的に変
化させる機能を有したものもあるが、一時的な停電等に
よる運転停止後に再起動したとき、固定パターンに再復
帰させることは非常に困難であった。
[0013] Some of them have a function of automatically changing an air supply amount in accordance with a combustion process (a gasification combustion process, a carbonization combustion process), but are restarted after the operation is stopped due to a temporary power failure or the like. Sometimes it was very difficult to return to the fixed pattern.

【0014】また、各機器の故障、特に2次バーナの故
障時には、2次燃焼室を800℃以上に保つことができ
なくなるため、ガス化燃焼過程では緊急停止させる必要
があるが、従来のものでは、この対策がなされておら
ず、障害発生時の自動緊急停止が行われない。
[0014] In addition, when each device fails, especially when the secondary burner fails, the secondary combustion chamber cannot be maintained at 800 ° C or higher, so it is necessary to make an emergency stop in the gasification combustion process. Does not take this measure and does not perform an automatic emergency stop when a failure occurs.

【0015】この発明は、上述のような問題点を解消す
るためになされたもので、最適な空気量制御によって黒
煙の発生と燃焼室の異常高温化を防止し、また障害発生
時の自動緊急停止を適切に行い、また一時的な停電等に
よる運転停止後に再起動を行う際に通常の燃焼過程に速
やかに復帰できるガス化焼却装置およびガス化焼却装置
の運転制御方法を得ることを目的としている。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and it is possible to prevent the generation of black smoke and abnormally high temperatures in a combustion chamber by optimal air amount control, and to automatically control the occurrence of a failure. The purpose of the present invention is to provide a gasification incinerator and an operation control method for the gasification and incineration device which can perform an emergency stop appropriately and can quickly return to a normal combustion process when restarting after an operation stop due to a temporary power failure or the like. And

【0016】[0016]

【課題を解決するための手段】上述の目的を達成するた
めに、この発明による焼却装置は、焼却物を投入される
1次燃焼室と、前記1次燃焼室内の焼却物の着火を行う
1次着火装置と、1次燃焼室に投入された焼却物の熱分
解に必要な空気を前記1次燃焼室に供給する1次空気供
給装置と、前記1次燃焼室内での焼却物の熱分解により
発生して可燃性ガスを燃焼させる2次燃焼室と、2次燃
焼室に導入された可燃性ガスが燃焼するのに必要な温度
を維持するための2次温度維持装置と、2次燃焼室に導
入された可燃性ガスが燃焼するのに必要な空気を前記2
次燃焼室に供給する2次空気供給装置とを有するガス化
焼却装置において、 前記2次燃焼室の室内温度を検出
する2次温度検出器と、前記2次温度検出器により検出
された前記2次燃焼室の室内温度の時間変化率を演算す
る2次温度時間変化率演算手段を有し、前記2次温度時
間変化率演算手段により演算される前記2次燃焼室の室
内温度の時間変化率が所定値以下であれば、前記2次空
気供給装置による2次空気供給量を強制的に増加する制
御手段とを有しているものである。
In order to achieve the above-mentioned object, an incinerator according to the present invention comprises: a primary combustion chamber into which incineration material is charged; and an ignition device for igniting the incineration material in the primary combustion chamber. A secondary ignition device, a primary air supply device for supplying air required for the thermal decomposition of the incinerated material put into the primary combustion chamber to the primary combustion chamber, and a thermal decomposition of the incinerated material in the primary combustion chamber Secondary combustion chamber for combusting the combustible gas generated by the combustion, a secondary temperature maintaining device for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber, and secondary combustion The air necessary for the combustible gas introduced into the chamber to burn is
In a gasification and incineration device having a secondary air supply device for supplying to a secondary combustion chamber, a secondary temperature detector for detecting an indoor temperature of the secondary combustion chamber, and the secondary temperature detector detected by the secondary temperature detector A secondary temperature temporal change rate calculating means for calculating a temporal change rate of the room temperature of the secondary combustion chamber, and a temporal change rate of the room temperature of the secondary combustion chamber calculated by the secondary temperature temporal change rate calculating means; Control means for forcibly increasing the amount of secondary air supplied by the secondary air supply device if is less than or equal to a predetermined value.

【0017】つぎの発明によることガス化焼却装置は、
焼却物を投入される1次燃焼室と、前記1次燃焼室内の
焼却物の着火を行う1次着火装置と、1次燃焼室に投入
された焼却物の熱分解に必要な空気を前記1次燃焼室に
供給する1次空気供給装置と、前記1次燃焼室内での焼
却物の熱分解により発生して可燃性ガスを燃焼させる2
次燃焼室と、2次燃焼室に導入された可燃性ガスが燃焼
するのに必要な温度を維持するための2次温度維持装置
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な空気を前記2次燃焼室に供給する2次空気供給装
置とを有するガス化焼却装置において、前記1次燃焼室
の室内温度を検出する1次温度検出器と、前記1次温度
検出器により検出された前記1次燃焼室の室内温度の時
間変化率を演算する1次温度時間変化率演算手段を有
し、前記1次温度時間変化率演算手段により演算される
前記1次燃焼室の室内温度の時間変化率が所定値以上で
あれば、前記1次空気供給装置による1次空気供給量を
強制的に低減する制御手段とを有しているものである。
According to the next invention, the gasification and incineration apparatus
A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber, and air required for thermal decomposition of the incineration material charged into the primary combustion chamber, A primary air supply device for supplying to the secondary combustion chamber, and a combustible gas generated by pyrolysis of incinerated material in the primary combustion chamber;
A secondary combustion chamber, a secondary temperature maintaining device for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber, and combustible gas introduced into the secondary combustion chamber A gasification and incineration system having a secondary air supply device for supplying air required for the secondary combustion chamber to the secondary combustion chamber, a primary temperature detector for detecting an indoor temperature of the primary combustion chamber, and the primary temperature A primary temperature temporal change rate calculating means for calculating a temporal change rate of the room temperature of the primary combustion chamber detected by a detector, wherein the primary combustion calculated by the primary temperature temporal change rate calculating means; A control means for forcibly reducing a primary air supply amount by the primary air supply device when a temporal change rate of the room temperature of the room is equal to or more than a predetermined value.

【0018】つぎの発明によることガス化焼却装置は、
焼却物を投入される1次燃焼室と、前記1次燃焼室内の
焼却物の着火を行う1次着火装置と、1次燃焼室に投入
された焼却物の熱分解に必要な空気を前記1次燃焼室に
供給する1次空気供給装置と、前記1次燃焼室内での焼
却物の熱分解により発生して可燃性ガスを燃焼させる2
次燃焼室と、2次燃焼室に導入された可燃性ガスが燃焼
するのに必要な温度を維持するための2次温度維持装置
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な空気を前記2次燃焼室に供給する2次空気供給装
置とを有するガス化焼却装置において、前記1次燃焼室
の室内圧を検出する圧力検出器と、前記圧力検出器によ
り検出された前記1次燃焼室の室内圧の時間変化率を演
算する圧力時間変化率演算手段を有し、前記圧力時間変
化率演算手段により演算される前記1次燃焼室の室内圧
の時間変化率が所定値以上であれば、前記1次空気供給
装置による1次空気供給量を強制的に低減する制御手段
とを有しているものである。
According to the next invention, the gasification and incineration apparatus comprises:
A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber, and air required for thermal decomposition of the incineration material charged into the primary combustion chamber, A primary air supply device for supplying to the secondary combustion chamber, and a combustible gas generated by pyrolysis of incinerated material in the primary combustion chamber;
A secondary combustion chamber, a secondary temperature maintaining device for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber, and combustible gas introduced into the secondary combustion chamber In a gasification and incineration device having a secondary air supply device for supplying air required for the secondary combustion chamber to the secondary combustion chamber, a pressure detector for detecting an indoor pressure of the primary combustion chamber and a pressure detector for detecting the indoor pressure of the primary combustion chamber A pressure time change rate calculating means for calculating the time change rate of the room pressure of the primary combustion chamber, and a time change rate of the indoor pressure of the primary combustion chamber calculated by the pressure time change rate calculating means. Control means for forcibly reducing the amount of primary air supplied by the primary air supply device if is greater than or equal to a predetermined value.

【0019】つぎの発明によることガス化焼却装置は、
焼却物を投入される1次燃焼室と、前記1次燃焼室内の
焼却物の着火を行う1次着火装置と、1次燃焼室に投入
された焼却物の熱分解に必要な空気を前記1次燃焼室に
供給する1次空気供給装置と、前記1次燃焼室内での焼
却物の熱分解により発生して可燃性ガスを燃焼させる2
次燃焼室と、2次燃焼室に導入された可燃性ガスが燃焼
するのに必要な温度を維持するための2次温度維持装置
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な空気を前記2次燃焼室に供給する2次空気供給装
置とを有するガス化焼却装置において、前記2次燃焼室
の室内温度を検出する2次温度検出器と、前記2次温度
検出器により検出された前記2次燃焼室の室内温度が所
定値以上であれば、前記2次空気供給装置による2次空
気供給量を強制的に増加する制御手段とを有しているも
のである。
According to the next invention, the gasification and incineration apparatus comprises:
A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber, and air required for thermal decomposition of the incineration material charged into the primary combustion chamber, A primary air supply device for supplying to the secondary combustion chamber, and a combustible gas generated by pyrolysis of incinerated material in the primary combustion chamber;
A secondary combustion chamber, a secondary temperature maintaining device for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber, and combustible gas introduced into the secondary combustion chamber A secondary air supply device for supplying air required for the second combustion chamber to the secondary combustion chamber, a secondary temperature detector for detecting a room temperature of the secondary combustion chamber, and the secondary temperature detector. Control means for forcibly increasing the amount of secondary air supplied by the secondary air supply device if the room temperature of the secondary combustion chamber detected by the detector is equal to or higher than a predetermined value. is there.

【0020】つぎの発明によることガス化焼却装置は、
焼却物を投入される1次燃焼室と、前記1次燃焼室内の
焼却物の着火を行う1次着火装置と、1次燃焼室に投入
された焼却物の熱分解に必要な空気を前記1次燃焼室に
供給する1次空気供給装置と、前記1次燃焼室内での焼
却物の熱分解により発生して可燃性ガスを燃焼させる2
次燃焼室と、2次燃焼室に導入された可燃性ガスが燃焼
するのに必要な温度を維持するための2次温度維持装置
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な空気を前記2次燃焼室に供給する2次空気供給装
置とを有するガス化焼却装置において、前記2次温度維
持装置の故障を検出する故障検出手段と、前記故障検出
手段により前記2次温度維持装置の故障が1次着火装置
の着火前の2次燃焼室予熱過程で検出されれば異常警報
を出力し、ガス化燃焼終了前であれば1次空気量を強制
的に減少して焼却物の燃焼を停止し、ガス化燃焼終了後
で炭化燃焼終了前であれば通常の空気量制御を続行する
制御手段とを有しているものである。
According to the next invention, the gasification and incineration apparatus comprises:
A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber, and air required for thermal decomposition of the incineration material charged into the primary combustion chamber, A primary air supply device for supplying to the secondary combustion chamber, and a combustible gas generated by pyrolysis of incinerated material in the primary combustion chamber;
A secondary combustion chamber, a secondary temperature maintaining device for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber, and combustible gas introduced into the secondary combustion chamber A gasification and incineration device having a secondary air supply device for supplying air required for the secondary combustion chamber to the secondary combustion chamber, wherein a failure detection means for detecting a failure of the secondary temperature maintaining device; If a failure of the secondary temperature maintenance device is detected in the secondary combustion chamber preheating process before the primary ignition device is ignited, an abnormal alarm is output, and if the gasification combustion is not completed, the primary air amount is forcibly reduced. Control means for stopping combustion of the incinerated material and continuing normal air amount control after the end of gasification combustion and before the end of carbonization combustion.

【0021】つぎの発明によることガス化焼却装置は、
焼却物を投入される1次燃焼室と、前記1次燃焼室内の
焼却物の着火を行う1次着火装置と、1次燃焼室に投入
された焼却物の熱分解に必要な空気を前記1次燃焼室に
供給する1次空気供給装置と、前記1次燃焼室内での焼
却物の熱分解により発生して可燃性ガスを燃焼させる2
次燃焼室と、2次燃焼室に導入された可燃性ガスが燃焼
するのに必要な温度を維持するための2次温度維持装置
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な空気を前記2次燃焼室に供給する2次空気供給装
置とを有するガス化焼却装置において、運転開始時にお
ける1次燃焼室1の燃焼状態を判別し、燃焼状態に応じ
て2次燃焼室予熱過程、ガス化燃焼過程、炭化燃焼過程
と云う一連のシーケンス動作の起動過程を選択設定する
制御手段を有しているものである。
According to the next invention, the gasification and incineration apparatus
A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber, and air required for thermal decomposition of the incineration material charged into the primary combustion chamber, A primary air supply device for supplying to the secondary combustion chamber, and a combustible gas generated by pyrolysis of incinerated material in the primary combustion chamber;
A secondary combustion chamber, a secondary temperature maintaining device for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber, and combustible gas introduced into the secondary combustion chamber In the gasification and incineration system having a secondary air supply device for supplying air necessary for the above to the secondary combustion chamber, the combustion state of the primary combustion chamber 1 at the start of operation is determined, and It has a control means for selectively setting a start-up process of a series of sequence operations such as a pre-heating process of the next combustion chamber, a gasification combustion process, and a carbonization combustion process.

【0022】また、上述の目的を達成するために、この
発明による焼却装置は、ガス化焼却装置の運転制御方法
において、ガス化焼却装置の運転制御方法に焼却物を投
入される1次燃焼室と、前記1次燃焼室内の焼却物の着
火を行う1次着火装置と、1次燃焼室に投入された焼却
物の熱分解に必要な空気を前記1次燃焼室に供給する1
次空気供給装置と、前記1次燃焼室内での焼却物の熱分
解により発生して可燃性ガスを燃焼させる2次燃焼室
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な温度を維持するための2次温度維持装置と、2次
燃焼室に導入された可燃性ガスが燃焼するのに必要な空
気を前記2次燃焼室に供給する2次空気供給装置とを有
するガス化焼却装置の運転制御方法において、2次温度
検出器により前記2次燃焼室の室内温度を検出し、前記
2次温度検出器により検出された前記2次燃焼室の室内
温度の時間変化率を演算し、演算された前記2次燃焼室
の室内温度の時間変化率が所定値以下であれば、前記2
次空気供給装置による2次空気供給量を強制的に増加す
るものである。
According to another aspect of the present invention, there is provided an incinerator according to the present invention, wherein the incineration material is charged into the operation control method of the gasification incinerator. A primary igniter for igniting the incineration in the primary combustion chamber, and supplying air necessary for thermal decomposition of the incineration into the primary combustion chamber to the primary combustion chamber 1
A secondary air supply device, a secondary combustion chamber for combusting combustible gas generated by thermal decomposition of the incineration in the primary combustion chamber, and a combustible gas introduced into the secondary combustion chamber for combustion. A secondary temperature maintaining device for maintaining a required temperature, and a secondary air supply device for supplying air necessary for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber. In the operation control method for a gasification and incineration apparatus, a room temperature of the secondary combustion chamber is detected by a secondary temperature detector, and a time change of the room temperature of the secondary combustion chamber detected by the secondary temperature detector Rate, and if the calculated time rate of change of the room temperature of the secondary combustion chamber is equal to or less than a predetermined value,
This is to forcibly increase the amount of secondary air supplied by the secondary air supply device.

【0023】つぎの発明による焼却装置は、焼却物を投
入される1次燃焼室と、前記1次燃焼室内の焼却物の着
火を行う1次着火装置と、1次燃焼室に投入された焼却
物の熱分解に必要な空気を前記1次燃焼室に供給する1
次空気供給装置と、前記1次燃焼室内での焼却物の熱分
解により発生して可燃性ガスを燃焼させる2次燃焼室
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な温度を維持するための2次温度維持装置と、2次
燃焼室に導入された可燃性ガスが燃焼するのに必要な空
気を前記2次燃焼室に供給する2次空気供給装置とを有
するガス化焼却装置の運転制御方法において、1次温度
検出器により前記1次燃焼室の室内温度を検出し、前記
1次温度検出器により検出された前記1次燃焼室の室内
温度の時間変化率を演算し、演算された1次燃焼室の室
内温度の時間変化率が所定値以上であれば、前記1次空
気供給装置による1次空気供給量を強制的に低減するも
のである。
The incinerator according to the next invention comprises a primary combustion chamber into which the incinerated material is charged, a primary ignition device for igniting the incinerated material in the primary combustion chamber, and an incineration charged into the primary combustion chamber. Supply air necessary for the thermal decomposition of material to the primary combustion chamber 1
A secondary air supply device, a secondary combustion chamber for combusting combustible gas generated by thermal decomposition of the incineration in the primary combustion chamber, and a combustible gas introduced into the secondary combustion chamber for combustion. A secondary temperature maintaining device for maintaining a required temperature, and a secondary air supply device for supplying air necessary for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber. In the operation control method for a gasification and incineration apparatus, a primary temperature detector detects a room temperature of the primary combustion chamber, and a temporal change in the room temperature of the primary combustion chamber detected by the primary temperature detector. The rate is calculated, and if the calculated time change rate of the room temperature of the primary combustion chamber is equal to or more than a predetermined value, the amount of primary air supplied by the primary air supply device is forcibly reduced.

【0024】つぎの発明による焼却装置は、焼却物を投
入される1次燃焼室と、前記1次燃焼室内の焼却物の着
火を行う1次着火装置と、1次燃焼室に投入された焼却
物の熱分解に必要な空気を前記1次燃焼室に供給する1
次空気供給装置と、前記1次燃焼室内での焼却物の熱分
解により発生して可燃性ガスを燃焼させる2次燃焼室
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な温度を維持するための2次温度維持装置と、2次
燃焼室に導入された可燃性ガスが燃焼するのに必要な空
気を前記2次燃焼室に供給する2次空気供給装置とを有
するガス化焼却装置の運転制御方法において、圧力検出
器により前記1次燃焼室の室内圧を検出し、前記圧力検
出器により検出された前記1次燃焼室の室内圧の時間変
化率を演算し、演算された前記1次燃焼室の室内圧の時
間変化率が所定値以上であれば、前記1次空気供給装置
による1次空気供給量を強制的に低減するものである。
The incinerator according to the next invention comprises a primary combustion chamber into which the incinerated material is charged, a primary ignition device for igniting the incinerated material in the primary combustion chamber, and an incineration charged into the primary combustion chamber. Supply air necessary for the thermal decomposition of material to the primary combustion chamber 1
A secondary air supply device, a secondary combustion chamber for combusting combustible gas generated by thermal decomposition of the incineration in the primary combustion chamber, and a combustible gas introduced into the secondary combustion chamber for combustion. A secondary temperature maintaining device for maintaining a required temperature, and a secondary air supply device for supplying air necessary for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber. In the operation control method for a gasification and incineration apparatus, a pressure detector detects the indoor pressure of the primary combustion chamber, and calculates a temporal change rate of the indoor pressure of the primary combustion chamber detected by the pressure detector. If the calculated time change rate of the indoor pressure of the primary combustion chamber is equal to or greater than a predetermined value, the primary air supply amount by the primary air supply device is forcibly reduced.

【0025】つぎの発明による焼却装置は、焼却物を投
入される1次燃焼室と、前記1次燃焼室内の焼却物の着
火を行う1次着火装置と、1次燃焼室に投入された焼却
物の熱分解に必要な空気を前記1次燃焼室に供給する1
次空気供給装置と、前記1次燃焼室内での焼却物の熱分
解により発生して可燃性ガスを燃焼させる2次燃焼室
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な温度を維持するための2次温度維持装置と、2次
燃焼室に導入された可燃性ガスが燃焼するのに必要な空
気を前記2次燃焼室に供給する2次空気供給装置とを有
するガス化焼却装置の運転制御方法において、2次温度
検出器により前記2次燃焼室の室内温度を検出し、前記
2次温度検出器により検出された前記2次燃焼室の室内
温度が所定値以上であれば、前記2次空気供給装置によ
る2次空気供給量を強制的に増加するものである。
The incinerator according to the next invention comprises a primary combustion chamber into which the incinerated material is charged, a primary ignition device for igniting the incinerated material in the primary combustion chamber, and an incineration charged into the primary combustion chamber. Supply air necessary for the thermal decomposition of material to the primary combustion chamber 1
A secondary air supply device, a secondary combustion chamber for combusting combustible gas generated by thermal decomposition of the incineration in the primary combustion chamber, and a combustible gas introduced into the secondary combustion chamber for combustion. A secondary temperature maintaining device for maintaining a required temperature, and a secondary air supply device for supplying air necessary for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber. In the operation control method for a gasification and incineration apparatus, a room temperature of the secondary combustion chamber is detected by a secondary temperature detector, and the room temperature of the secondary combustion chamber detected by the secondary temperature detector is a predetermined value. Above, the secondary air supply amount by the secondary air supply device is forcibly increased.

【0026】つぎの発明による焼却装置は、焼却物を投
入される1次燃焼室と、前記1次燃焼室内の焼却物の着
火を行う1次着火装置と、1次燃焼室に投入された焼却
物の熱分解に必要な空気を前記1次燃焼室に供給する1
次空気供給装置と、前記1次燃焼室内での焼却物の熱分
解により発生して可燃性ガスを燃焼させる2次燃焼室
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な温度を維持するための2次温度維持装置と、2次
燃焼室に導入された可燃性ガスが燃焼するのに必要な空
気を前記2次燃焼室に供給する2次空気供給装置とを有
するガス化焼却装置の運転制御方法において、故障検出
手段により前記2次温度維持装置の故障を検出し、前記
故障検出手段により前記2次温度維持装置の故障が1次
着火装置の着火前の2次燃焼室予熱過程で検出されれば
異常警報を出力し、ガス化燃焼終了前であれば1次空気
量を強制的に減少して焼却物の燃焼を停止し、ガス化燃
焼終了後で炭化燃焼終了前であれば通常の空気量制御を
続行するものである。
The incinerator according to the next invention comprises a primary combustion chamber into which the incinerated material is charged, a primary ignition device for igniting the incinerated material in the primary combustion chamber, and an incineration charged into the primary combustion chamber. Supply air necessary for the thermal decomposition of material to the primary combustion chamber 1
A secondary air supply device, a secondary combustion chamber for combusting combustible gas generated by thermal decomposition of the incineration in the primary combustion chamber, and a combustible gas introduced into the secondary combustion chamber for combustion. A secondary temperature maintaining device for maintaining a required temperature, and a secondary air supply device for supplying air necessary for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber. In the operation control method for a gasification and incineration apparatus, a failure of the secondary temperature maintenance device is detected by failure detection means, and the failure of the secondary temperature maintenance device is detected by the failure detection means. If it is detected in the pre-heating process of the secondary combustion chamber, an abnormal alarm is output. If it is before the end of gasification combustion, the amount of primary air is forcibly reduced to stop burning incinerated materials, and carbonization is performed after the end of gasification combustion. If the combustion is not completed, normal air volume control is continued.

【0027】つぎの発明による焼却装置は、焼却物を投
入される1次燃焼室と、前記1次燃焼室内の焼却物の着
火を行う1次着火装置と、1次燃焼室に投入された焼却
物の熱分解に必要な空気を前記1次燃焼室に供給する1
次空気供給装置と、前記1次燃焼室内での焼却物の熱分
解により発生して可燃性ガスを燃焼させる2次燃焼室
と、2次燃焼室に導入された可燃性ガスが燃焼するのに
必要な温度を維持するための2次温度維持装置と、2次
燃焼室に導入された可燃性ガスが燃焼するのに必要な空
気を前記2次燃焼室に供給する2次空気供給装置とを有
するガス化焼却装置の運転制御方法において、運転開始
時における1次燃焼室1の燃焼状態を判別し、燃焼状態
に応じて2次燃焼室予熱過程、ガス化燃焼過程、炭化燃
焼過程と云う一連のシーケンス動作の起動過程を選択設
定するものである。
The incinerator according to the next invention comprises a primary combustion chamber into which the incinerated material is charged, a primary ignition device for igniting the incinerated material in the primary combustion chamber, and an incineration charged into the primary combustion chamber. Supply air necessary for the thermal decomposition of material to the primary combustion chamber 1
A secondary air supply device, a secondary combustion chamber for combusting combustible gas generated by thermal decomposition of the incineration in the primary combustion chamber, and a combustible gas introduced into the secondary combustion chamber for combustion. A secondary temperature maintaining device for maintaining a required temperature, and a secondary air supply device for supplying air necessary for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber. In the operation control method of the gasification and incineration apparatus, the combustion state of the primary combustion chamber 1 at the start of operation is determined, and a series of a preheating process, a gasification combustion process, and a carbonization combustion process are performed according to the combustion state. Of the sequence operation is selectively set.

【0028】[0028]

【発明の実施の形態】以下に添付の図を参照してこの発
明に係る焼却装置および焼却装置の運転制御方法の実施
の形態を詳細に説明する。なお、以下に説明するこの発
明の実施の形態において、上述の従来例と同一構成の部
分は、上述の従来例に付した符号と同一の符号を付して
説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of an incinerator and an operation control method of the incinerator according to the present invention will be described below in detail with reference to the accompanying drawings. In the embodiments of the present invention described below, portions having the same configurations as those of the above-described conventional example will be described with the same reference numerals as those of the above-described conventional example.

【0029】図1はこの発明による焼却装置の一つの実
施の形態を示している。ガス化燃焼炉は、焼却物が投入
される1次燃焼室1と、1次燃焼室1における焼却物の
着火を行う1次バーナ2と、焼却物の熱分解に必要な空
気を1次燃焼室1に供給する1次空気供給装置3と、1
次燃焼室1の室内温度を検出する1次温度検出器4と、
1次燃焼室1の室内圧を検出する圧力検出器5と、1次
燃焼室1内での焼却物の熱分解により発生した可燃性ガ
スを完全燃焼させる2次燃焼室6と、2次燃焼室6に導
入された可燃性ガスが燃焼するのに必要な温度を維持す
る2次バーナ7と、可燃性ガスの燃焼に必要な空気を2
次燃焼室6に供給する2次空気供給装置8と、2次燃焼
室6の室内温度を検出する2次温度検出器9と、排ガス
の温度を検出する排ガス温度検出器10、煙突11と、
2次バーナ7の故障(未着火)を検出するフレームアイ
等による2次バーナ故障検出器20と、1次バーナ2お
よび2次温度維持装置7のオン/オフ制御と1次空気供
給装置3による1次空気供給量および2次空気供給装置
8による2次空気供給量を制御する制御手段21とを有
している。
FIG. 1 shows an embodiment of the incinerator according to the present invention. The gasification combustion furnace includes a primary combustion chamber 1 into which incineration material is charged, a primary burner 2 for igniting the incineration material in the primary combustion chamber 1, and a primary combustion of air required for thermal decomposition of the incineration material. A primary air supply device 3 for supplying to the chamber 1;
A primary temperature detector 4 for detecting the indoor temperature of the secondary combustion chamber 1,
A pressure detector 5 for detecting the indoor pressure of the primary combustion chamber 1, a secondary combustion chamber 6 for completely combusting the combustible gas generated by the thermal decomposition of the incineration material in the primary combustion chamber 1, and a secondary combustion A secondary burner 7 for maintaining a temperature required for the combustible gas introduced into the chamber 6 to burn;
A secondary air supply device 8 for supplying the secondary combustion chamber 6, a secondary temperature detector 9 for detecting the indoor temperature of the secondary combustion chamber 6, an exhaust gas temperature detector 10 for detecting the temperature of the exhaust gas, and a chimney 11;
A secondary burner failure detector 20 based on a flame eye or the like for detecting a failure (non-ignition) of the secondary burner 7, an on / off control of the primary burner 2 and the secondary temperature maintaining device 7, and a primary air supply device 3 And a control unit 21 for controlling the primary air supply amount and the secondary air supply amount by the secondary air supply device 8.

【0030】制御手段21は、1次温度検出器4により
検出される1次燃焼室1の室内温度より1次温度の時間
変化率を演算する1次温度時間変化率演算器22と、圧
力検出器5により検出される1次燃焼室1の室内圧より
1次燃焼室1の室内圧の時間変化率を演算する圧力時間
変化率演算器23と、2次温度検出器9により検出され
る2次燃焼室6の室内温度より2次温度の時間変化率を
演算する2次温度時間変化率演算器24とを有してい
る。
The control means 21 comprises a primary temperature temporal change rate calculator 22 for calculating a temporal change rate of the primary temperature based on the room temperature of the primary combustion chamber 1 detected by the primary temperature detector 4; Pressure time change rate calculator 23 for calculating the time change rate of the indoor pressure of the primary combustion chamber 1 from the indoor pressure of the primary combustion chamber 1 detected by the heater 5, and 2 detected by the secondary temperature detector 9. A secondary temperature temporal change rate calculator 24 for calculating a temporal change rate of the secondary temperature from the room temperature of the secondary combustion chamber 6.

【0031】制御手段21は、つぎのような制御を行
う。 (1)2次温度時間変化率演算器24により演算された
2次燃焼室6の室内温度の時間変化率(上昇率)が所定
値以下であるか否かの判定を行い、2次燃焼室6の室内
温度の時間変化率が所定値以下であれば、2次空気供給
装置8による2次空気供給量を強制的に増加させる制御
を行う。
The control means 21 performs the following control. (1) It is determined whether or not the temporal change rate (increase rate) of the room temperature of the secondary combustion chamber 6 calculated by the secondary temperature temporal change rate calculator 24 is equal to or less than a predetermined value, and the secondary combustion chamber is determined. If the time change rate of the room temperature in Step 6 is equal to or less than a predetermined value, control is performed to forcibly increase the amount of secondary air supplied by the secondary air supply device 8.

【0032】これにより、2次燃焼室予熱過程完了後
に、1次バーナ2により1次燃焼室1の焼却物の着火を
行う時点で、2次燃焼室6の室内温度の上昇が遅いこと
により、2次燃焼室6の室内温度の時間変化率が所定値
以下であると、2次空気供給装置8による2次空気供給
量が強制的に増加される。この2次空気供給量の増加に
より、煙突11から黒煙が排出されることが防止され
る。
Thus, at the time when the incineration material in the primary combustion chamber 1 is ignited by the primary burner 2 after the completion of the preheating process of the secondary combustion chamber, the rise in the indoor temperature of the secondary combustion chamber 6 is slow. When the time rate of change of the room temperature of the secondary combustion chamber 6 is equal to or less than a predetermined value, the amount of secondary air supplied by the secondary air supply device 8 is forcibly increased. This increase in the amount of secondary air supply prevents black smoke from being discharged from the chimney 11.

【0033】(2)1次温度時間変化率演算器22によ
り演算された1次燃焼室1の室内温度の時間変化率(上
昇率)が所定値以上であるか否かの判定を行い、1次燃
焼室1の室内温度の時間変化率が所定値以上であれば、
1次空気供給装置3による1次空気供給量を強制的に減
少させる制御を行う。
(2) It is determined whether or not the time change rate (increase rate) of the room temperature of the primary combustion chamber 1 calculated by the primary temperature time change rate calculator 22 is equal to or more than a predetermined value. If the time change rate of the room temperature of the next combustion chamber 1 is equal to or more than a predetermined value,
Control for forcibly reducing the primary air supply amount by the primary air supply device 3 is performed.

【0034】これにより、1次燃焼室1の温度上昇によ
り可燃性ガスの発生が増加して行く過程で、液体の可燃
物が蒸発と同時に燃焼したことで、1次燃焼室1の室内
温度の時間変化率が所定値以上になると、1次空気供給
装置3による1次空気供給量が強制的に減少される。こ
の1次空気供給量の減少により、急激な可燃性ガスの発
生が防止され、急激な可燃性ガスの増加による異常燃焼
が防止される。
Thus, in the process in which the generation of flammable gas increases due to the rise in the temperature of the primary combustion chamber 1, the combustible liquid material burns at the same time as the evaporation, and the temperature of the room of the primary combustion chamber 1 decreases. When the time rate of change exceeds a predetermined value, the primary air supply amount by the primary air supply device 3 is forcibly reduced. Due to the decrease in the primary air supply amount, rapid generation of combustible gas is prevented, and abnormal combustion due to rapid increase of combustible gas is prevented.

【0035】(3)圧力時間変化率演算器23により演
算された1次燃焼室1の室内圧の時間変化率(上昇率)
が所定値以上であるか否かの判定を行い、1次燃焼室1
の室内圧の時間変化率が所定値以上であれば、1次空気
供給装置3による1次空気供給量を強制的に減少させる
制御を行う。
(3) Temporal change rate (increase rate) of the indoor pressure of the primary combustion chamber 1 calculated by the pressure time change rate calculator 23
Is determined to be equal to or greater than a predetermined value, and the primary combustion chamber 1
If the time change rate of the indoor pressure is equal to or more than the predetermined value, control is performed to forcibly reduce the amount of primary air supplied by the primary air supply device 3.

【0036】これにより、1次燃焼室1の温度上昇によ
り可燃性ガスの発生が増加して行く過程で、液体の可燃
物が蒸発と同時に燃焼したことで、1次燃焼室1の室内
圧時間変化率が所定値以上になると、1次空気供給装置
3による1次空気供給量が強制的に減少される。この1
次空気供給量の減少により、急激な可燃性ガスの発生が
防止され、急激な可燃性ガスの増加による異常燃焼が防
止される。
Thus, in the process in which the generation of combustible gas increases due to the rise in temperature of the primary combustion chamber 1, the liquid combustible material is burned at the same time as the vaporization of the liquid. When the rate of change exceeds a predetermined value, the primary air supply amount by the primary air supply device 3 is forcibly reduced. This one
Due to the decrease in the supply amount of the secondary air, rapid generation of combustible gas is prevented, and abnormal combustion due to rapid increase of combustible gas is prevented.

【0037】(4)2次温度検出器9によって検出され
た2次燃焼室6の室内温度が所定値以上であるか否かの
判定を行い、2次燃焼室6の室内温度が所定値以上であ
れば、2次空気供給装置8による2次空気供給量を強制
的に増加させる制御を行う。
(4) It is determined whether or not the room temperature of the secondary combustion chamber 6 detected by the secondary temperature detector 9 is higher than a predetermined value, and the room temperature of the secondary combustion chamber 6 is higher than a predetermined value. If so, the control for forcibly increasing the secondary air supply amount by the secondary air supply device 8 is performed.

【0038】これにより、ガス化燃焼中において、2次
燃焼室6の温度が上昇し、耐火レンガ等の許容温度を超
える可能性がある場合には、2次燃焼室6の室内温度が
所定値以上に達し、2次空気供給装置8による2次空気
供給量が強制的に増加される。この2次空気供給量の増
加により、2次燃焼室6の温度上昇が抑制され、2次燃
焼室6の温度が耐火レンガ等の許容温度を超えることが
回避される。
Accordingly, during the gasification combustion, if the temperature of the secondary combustion chamber 6 rises and may exceed the allowable temperature of refractory bricks or the like, the indoor temperature of the secondary combustion chamber 6 is increased to a predetermined value. At this point, the secondary air supply amount by the secondary air supply device 8 is forcibly increased. Due to the increase in the amount of the secondary air supplied, a rise in the temperature of the secondary combustion chamber 6 is suppressed, and the temperature of the secondary combustion chamber 6 is prevented from exceeding the allowable temperature of refractory bricks or the like.

【0039】(5)2次バーナ故障検出器20により2
次バーナ7の故障(未着火)が検出されると、1次バー
ナ2の着火前(2次燃焼室予熱過程)であれば異常警報
を出力、ガス化燃焼終了前であれば1次空気量を強制的
に減少して焼却物の燃焼を停止、ガス化燃焼終了後で炭
化燃焼終了前であれば通常の空気量制御を続行する。
(5) The secondary burner failure detector 20
If a failure (non-ignition) of the secondary burner 7 is detected, an abnormal alarm is output if the primary burner 2 is not ignited (secondary combustion chamber preheating process), and if the primary burner is not yet finished, the primary air amount is output. , The combustion of the incinerated material is stopped, and if the gasification combustion is completed but before the carbonization combustion is completed, the normal air amount control is continued.

【0040】つぎに、2次バーナ故障検出処理について
図2に示すフローチャートを参照して説明する。運転が
開始されると、制御手段21が故障検出器20の出力を
時間割込により取り込み、2次バーナ7の状態を監視す
る(ステップS10)。
Next, the secondary burner failure detection processing will be described with reference to the flowchart shown in FIG. When the operation is started, the control means 21 takes in the output of the failure detector 20 by time interruption and monitors the state of the secondary burner 7 (step S10).

【0041】2次バーナ7の故障が検出されると(ステ
ップS10肯定)、現時点が1次バーナ2の着火後であ
るか否かの判別を行う(ステップS20)。1次バーナ
2の着火前であれば(ステップS20否定)、焼却物に
は火が着いていないので、2次バーナ7が故障している
ことを表す異常警報を出力し(ステップS30)、故障
状態を記録し(ステップS80)シーケンス動作を終了
する。
When the failure of the secondary burner 7 is detected (Yes at Step S10), it is determined whether or not the current time is after the ignition of the primary burner 2 (Step S20). If the primary burner 2 is not ignited (No at Step S20), the incinerated material is not ignited, so that an abnormal alarm indicating that the secondary burner 7 is out of order is output (Step S30). The state is recorded (step S80), and the sequence operation ends.

【0042】着火後の場合には(ステップS20肯
定)、ガス化燃焼終了であるか否かの確認を行う(ステ
ップS40)。ガス化燃焼終了前であれば(ステップS
40否定)、1次空気量を強制的に減少し、焼却物の燃
焼を停止させる。
If the ignition has been completed (Yes at Step S20), it is confirmed whether or not the gasification combustion has ended (Step S40). Before the end of gasification combustion (step S
40 No) The amount of primary air is forcibly reduced to stop the burning of the incineration.

【0043】これに対し、ガス化燃焼終了後の場合には
(ステップS40肯定)、つぎに炭化燃焼終了であるか
否かの確認を行う(ステップS60)。炭化燃焼終了前
であれば(ステップS60否定)、通常の空気量コント
ロールを続行し(ステップS70)、炭化燃焼を終了さ
せる。炭化燃焼終了後の場合には(ステップS60肯
定)、故障状態を記録し(ステップS80)、シーケン
ス動作を終了する。
On the other hand, when the gasification combustion has been completed (Yes at Step S40), it is checked whether the carbonization combustion has been completed (Step S60). If the carbonization combustion has not been completed (No at Step S60), the normal air amount control is continued (Step S70), and the carbonization combustion is terminated. If the carbonization combustion has ended (Yes at Step S60), the failure state is recorded (Step S80), and the sequence operation ends.

【0044】(6)運転開始時における1次燃焼室1の
燃焼状態(ガス化燃焼完了前、ガス化燃焼完了後)によ
り、シーケンス動作(2次燃焼室予熱過程→ガス化燃焼
過程→炭化燃焼過程)の起動過程を選択設定する。
(6) The sequence operation (secondary combustion chamber preheating process → gasification combustion process → carbonization combustion) depends on the combustion state of the primary combustion chamber 1 at the start of operation (before the completion of gasification combustion and after the completion of gasification combustion). Select and set the starting process of step).

【0045】通常の運転開始時には、2次燃焼室予熱過
程から始まり、ガス化燃焼過程、炭化燃焼過程を順に実
行するが、停電後の再起動には1次燃焼室1の温度およ
び2次燃焼室6の温度、さらにそれらの時間的温度変化
率から燃焼状態をガス化燃焼前かガス化燃焼後かを判断
し、ガス化燃焼前であれば、ガス化燃焼過程からシーケ
ンス動作を開始し、ガス化燃焼後であれば、炭化燃焼過
程からシーケンス動作を開始する。
At the start of normal operation, the gasification combustion process and the carbonization combustion process are sequentially performed starting from the secondary combustion chamber preheating process, but the temperature of the primary combustion chamber 1 and the secondary combustion It is determined whether the combustion state is before gasification combustion or after gasification combustion based on the temperature of the chamber 6 and the temporal temperature change rate. If it is before gasification combustion, a sequence operation is started from the gasification combustion process, After the gasification combustion, the sequence operation is started from the carbonization combustion process.

【0046】つぎに、運転開始制御について図3に示す
フローチャートを参照して説明する。運転が開始される
と、シーケンス選択により、1次燃焼室1の着火状態を
確認し(ステップS100)、着火していない状態であ
れば(ステップS100否定)、通常の起動過程である
2次燃焼室予熱過程からスタートする。この場合には、
2次燃焼室予熱(ステップS110)、1次燃焼室1の
着火、2次空気供給量強制増加(ステップS120)、
ガス化燃焼過程に適合した1次、2次空気量調整(ステ
ップS130)、ガス化燃焼の終了確認(ステップS1
40)、炭化燃焼過程に適合した1次、2次空気量調整
(ステップS150)、炭化燃焼の終了確認(ステップ
S160)を通常通り、順に実行する。
Next, the operation start control will be described with reference to the flowchart shown in FIG. When the operation is started, the ignition state of the primary combustion chamber 1 is confirmed by sequence selection (step S100), and if it is not ignited (step S100: No), the secondary combustion which is a normal startup process is performed. Start from the room preheating process. In this case,
Secondary combustion chamber preheating (step S110), ignition of primary combustion chamber 1, secondary air supply forced increase (step S120),
Primary and secondary air amount adjustment suitable for the gasification combustion process (Step S130), completion confirmation of gasification combustion (Step S1)
40), the adjustment of the primary and secondary air amounts suitable for the carbonization combustion process (step S150), and the completion confirmation of the carbonization combustion (step S160) are sequentially executed as usual.

【0047】これに対し、1次燃焼室1が着火していれ
ば(ステップS100肯定)、1次燃焼室の温度および
2次燃焼室の温度、これらの時間的温度変化率から、燃
焼状態がガス化燃焼前かガス化燃焼後かを判断し(ステ
ップS170)、ガス化燃焼前であれば、ステップS1
30へジャンプしてガス化燃焼過程を実行し、ガス化燃
焼後であれば、ステップS150へジャンプして炭化燃
焼過程を実行する。
On the other hand, if the primary combustion chamber 1 is ignited (Yes at step S100), the combustion state is determined from the temperature of the primary combustion chamber, the temperature of the secondary combustion chamber, and the temporal temperature change rate. It is determined whether before gasification combustion or after gasification combustion (step S170). If it is before gasification combustion, step S1 is performed.
The process jumps to step 30 to execute the gasification combustion process. If it is after the gasification combustion, the process jumps to step S150 to execute the carbonization combustion process.

【0048】これにより、停電等による途中中断後に、
再起動を行う際に通常の燃焼状態に速やかに復帰でき
る。
As a result, after an interruption due to a power failure or the like,
When restarting, it can quickly return to the normal combustion state.

【0049】[0049]

【発明の効果】以上のように、この発明によるガス化焼
却装置によれば、2次温度時間変化率演算手段により演
算される2次燃焼室の室内温度の時間変化率が所定値以
下であれば、2次空気供給装置による2次空気供給量を
強制的に増加するから、2次燃焼室予熱過程完了後に、
1次着火装置(1次バーナ)により1次燃焼室1の焼却
物の着火を行う時点で、2次燃焼室の室内温度の上昇が
遅いことにより、2次燃焼室の室内温度の時間変化率が
所定値以下であると、2次空気供給装置による2次空気
供給量が強制的に増加され、この2次空気供給量の増加
により、着火直後の空気量不足による黒煙の排出が防止
される。
As described above, according to the gasification and incineration apparatus of the present invention, the time change rate of the room temperature of the secondary combustion chamber calculated by the time change rate calculation means of the secondary temperature is not more than a predetermined value. For example, since the secondary air supply amount by the secondary air supply device is forcibly increased, after the secondary combustion chamber preheating process is completed,
When the incineration material in the primary combustion chamber 1 is ignited by the primary ignition device (primary burner), the temperature rise in the secondary combustion chamber is slow due to the slow rise in the indoor temperature in the secondary combustion chamber. Is less than or equal to a predetermined value, the amount of secondary air supplied by the secondary air supply device is forcibly increased, and the increase in the amount of secondary air supplied prevents black smoke from being discharged due to a shortage of air immediately after ignition. You.

【0050】つぎの発明によるガス化焼却装置によれ
ば、1次温度時間変化率演算手段により演算される1次
燃焼室の室内温度の時間変化率が所定値以上であれば、
1次空気供給装置による1次空気供給量を強制的に低減
するから、1次燃焼室の温度上昇により可燃性ガスの発
生が増加して行く過程で、液体の可燃物が蒸発と同時に
燃焼したことで、1次燃焼室の室内温度の時間変化率が
所定値以上になると、1次空気供給装置による1次空気
供給量が強制的に減少され、この1次空気供給量の減少
により、急激な可燃性ガスの発生が防止され、急激な可
燃性ガスの増加による異常燃焼が防止され、炉の耐久性
が向上する。
According to the gasification and incineration apparatus of the next invention, if the time change rate of the room temperature of the primary combustion chamber calculated by the primary temperature time change rate calculating means is equal to or more than a predetermined value,
Since the amount of primary air supplied by the primary air supply device is forcibly reduced, in the process of increasing the generation of flammable gas due to an increase in the temperature of the primary combustion chamber, liquid combustibles burned simultaneously with evaporation. Thus, when the time change rate of the room temperature of the primary combustion chamber becomes equal to or more than a predetermined value, the amount of primary air supplied by the primary air supply device is forcibly reduced. The generation of flammable gas is prevented, abnormal combustion due to a rapid increase in flammable gas is prevented, and the durability of the furnace is improved.

【0051】つぎの発明によるガス化焼却装置によれ
ば、圧力時間変化率演算手段により演算される1次燃焼
室の室内圧の時間変化率が所定値以上であれば、1次空
気供給装置による1次空気供給量を強制的に低減するか
ら、1次燃焼室の温度上昇により可燃性ガスの発生が増
加して行く過程で、液体の可燃物が蒸発と同時に燃焼し
たことで、1次燃焼室の室内温度の時間変化率が所定値
以上になると、1次空気供給装置による1次空気供給量
が強制的に減少され、この1次空気供給量の減少によ
り、急激な可燃性ガスの発生が防止され、急激な可燃性
ガスの増加による異常燃焼が防止され、炉の耐久性が向
上する。
According to the gasification and incineration apparatus of the next invention, if the time change rate of the indoor pressure of the primary combustion chamber calculated by the pressure time change rate calculating means is equal to or more than a predetermined value, the primary air supply apparatus is used. Since the primary air supply amount is forcibly reduced, the primary combustible material burns at the same time as the liquid combustible evaporates in the process of increasing the generation of combustible gas due to the temperature rise of the primary combustion chamber. When the temporal change rate of the room temperature of the room becomes equal to or more than a predetermined value, the primary air supply amount by the primary air supply device is forcibly reduced, and the decrease in the primary air supply amount causes rapid generation of combustible gas. Is prevented, abnormal combustion due to a rapid increase in combustible gas is prevented, and the durability of the furnace is improved.

【0052】つぎの発明によるガス化焼却装置によれ
ば、2次温度検出器により検出された前記2次燃焼室の
室内温度が所定値以上であれば、前記2次空気供給装置
による2次空気供給量を強制的に増加するから、ガス化
燃焼中において、2次燃焼室の温度が上昇し、耐火レン
ガ等の許容温度を超える可能性がある場合には、2次燃
焼室の室内温度が所定値以上に達し、2次空気供給装置
による2次空気供給量が強制的に増加され、この2次空
気供給量の増加により、2次燃焼室6の温度上昇が抑制
され、2次燃焼室6の温度が耐火レンガ等の許容温度を
超えることが回避され、炉の耐久性が向上する。
According to the gasification and incineration device of the next invention, if the room temperature of the secondary combustion chamber detected by the secondary temperature detector is equal to or higher than a predetermined value, the secondary air supplied by the secondary air supply device is used. Since the supply amount is forcibly increased, during the gasification combustion, if the temperature of the secondary combustion chamber rises and may exceed the allowable temperature of refractory bricks or the like, the indoor temperature of the secondary combustion chamber may be increased. When the temperature reaches a predetermined value or more, the amount of secondary air supplied by the secondary air supply device is forcibly increased, and the increase in the amount of secondary air supplied suppresses a rise in the temperature of the secondary combustion chamber 6, thereby reducing the temperature of the secondary combustion chamber. The temperature of No. 6 is prevented from exceeding the allowable temperature of the refractory brick or the like, and the durability of the furnace is improved.

【0053】つぎの発明によるガス化焼却装置によれ
ば、故障検出手段により2次温度維持装置の故障が1次
着火装置の着火前の2次燃焼室予熱過程で検出されれば
異常警報を出力し、ガス化燃焼終了前であれば1次空気
量を強制的に減少して焼却物の燃焼を停止し、ガス化燃
焼終了後で炭化燃焼終了前であれば通常の空気量制御を
続行するから、障害発生時の自動緊急停止が無駄なく適
切に行われる。
According to the gasification and incineration system of the next invention, if a failure of the secondary temperature maintaining device is detected in the secondary combustion chamber preheating process before the ignition of the primary ignition device by the failure detection means, an abnormality alarm is output. If the gasification combustion is not yet completed, the primary air amount is forcibly reduced to stop burning the incinerated material, and if the gasification combustion is completed and the carbonization combustion is not completed, the normal air amount control is continued. Therefore, the automatic emergency stop in the event of a failure is appropriately performed without waste.

【0054】つぎの発明によるガス化焼却装置によれ
ば、運転開始時における1次燃焼室1の燃焼状態を判別
し、燃焼状態に応じて2次燃焼室予熱過程、ガス化燃焼
過程、炭化燃焼過程と云う一連のシーケンス動作の起動
過程を選択設定するから、一時的な停電等による運転停
止後に再起動を行う際に通常の燃焼過程に速やかに復帰
することができる。
According to the gasification and incineration apparatus according to the next invention, the combustion state of the primary combustion chamber 1 at the start of operation is determined, and the secondary combustion chamber preheating step, gasification combustion step, carbonization combustion is performed according to the combustion state. Since the starting process of a series of sequence operations called the process is selected and set, it is possible to quickly return to the normal combustion process when restarting after an operation stop due to a temporary power failure or the like.

【0055】つぎの発明によるガス化焼却装置の運転制
御方法によれば、2次温度検出器により検出された前記
2次燃焼室の室内温度の時間変化率を演算し、演算され
た前記2次燃焼室の室内温度の時間変化率が所定値以下
であれば、2次空気供給装置による2次空気供給量を強
制的に増加するから、2次燃焼室予熱過程完了後に、1
次着火装置(1次バーナ)により1次燃焼室1の焼却物
の着火を行う時点で、2次燃焼室の室内温度の上昇が遅
いことにより、2次燃焼室の室内温度の時間変化率が所
定値以下であると、2次空気供給装置による2次空気供
給量が強制的に増加され、この2次空気供給量の増加に
より、着火直後の空気量不足による黒煙の排出が防止さ
れる。
According to the operation control method of the gasification incinerator according to the next invention, the time change rate of the room temperature of the secondary combustion chamber detected by the secondary temperature detector is calculated, and the calculated secondary temperature is calculated. If the time change rate of the room temperature of the combustion chamber is equal to or less than a predetermined value, the amount of secondary air supplied by the secondary air supply device is forcibly increased.
At the time when the incineration material in the primary combustion chamber 1 is ignited by the secondary ignition device (primary burner), the temporal change rate of the indoor temperature of the secondary combustion chamber is reduced due to the slow rise in the indoor temperature of the secondary combustion chamber. If it is less than the predetermined value, the secondary air supply amount by the secondary air supply device is forcibly increased, and the increase in the secondary air supply amount prevents black smoke from being discharged due to insufficient air amount immediately after ignition. .

【0056】つぎの発明によるガス化焼却装置の運転制
御方法によれば、1次温度検出器により検出された1次
燃焼室の室内温度の時間変化率を演算し、演算された1
次燃焼室の室内温度の時間変化率が所定値以上であれ
ば、前記1次空気供給装置による1次空気供給量を強制
的に低減するから、1次燃焼室の温度上昇により可燃性
ガスの発生が増加して行く過程で、液体の可燃物が蒸発
と同時に燃焼したことで、1次燃焼室の室内温度の時間
変化率が所定値以上になると、1次空気供給装置による
1次空気供給量が強制的に減少され、この1次空気供給
量の減少により、急激な可燃性ガスの発生が防止され、
急激な可燃性ガスの増加による異常燃焼が防止され、炉
の耐久性が向上する。
According to the operation control method of the gasification incinerator according to the next invention, the time change rate of the room temperature of the primary combustion chamber detected by the primary temperature detector is calculated, and the calculated 1 is calculated.
If the temporal change rate of the room temperature of the secondary combustion chamber is equal to or more than a predetermined value, the primary air supply amount by the primary air supply device is forcibly reduced. During the process of increasing the generation, when the time change rate of the room temperature of the primary combustion chamber becomes equal to or more than a predetermined value due to the combustion of the liquid combustible simultaneously with the evaporation, the primary air supply device supplies the primary air. The primary air supply is reduced to prevent the rapid generation of combustible gas,
Abnormal combustion due to a rapid increase in combustible gas is prevented, and the durability of the furnace is improved.

【0057】つぎの発明によるガス化焼却装置の運転制
御方法によれば、圧力検出器により検出された1次燃焼
室の室内圧の時間変化率を演算し、演算された1次燃焼
室の室内圧の時間変化率が所定値以上であれば、1次空
気供給装置による1次空気供給量を強制的に低減するか
ら、1次燃焼室の温度上昇により可燃性ガスの発生が増
加して行く過程で、液体の可燃物が蒸発と同時に燃焼し
たことで、1次燃焼室の室内温度の時間変化率が所定値
以上になると、1次空気供給装置による1次空気供給量
が強制的に減少され、この1次空気供給量の減少によ
り、急激な可燃性ガスの発生が防止され、急激な可燃性
ガスの増加による異常燃焼が防止され、炉の耐久性が向
上する。
According to the operation control method of the gasification and incineration apparatus according to the next invention, the temporal change rate of the indoor pressure of the primary combustion chamber detected by the pressure detector is calculated, and the calculated room of the primary combustion chamber is calculated. If the time rate of change of the pressure is equal to or more than the predetermined value, the primary air supply amount by the primary air supply device is forcibly reduced, so that the generation of combustible gas increases due to a rise in the temperature of the primary combustion chamber. In the process, when the time change rate of the room temperature of the primary combustion chamber becomes equal to or more than a predetermined value due to the combustion of the liquid combustible simultaneously with the evaporation, the primary air supply amount by the primary air supply device is forcibly reduced. Then, due to the decrease in the primary air supply amount, rapid generation of combustible gas is prevented, abnormal combustion due to rapid increase of combustible gas is prevented, and durability of the furnace is improved.

【0058】つぎの発明によるガス化焼却装置の運転制
御方法によれば、2次温度検出器により検出された2次
燃焼室の室内温度が所定値以上であれば、2次空気供給
装置による2次空気供給量を強制的に増加するから、ガ
ス化燃焼中において、2次燃焼室の温度が上昇し、耐火
レンガ等の許容温度を超える可能性がある場合には、2
次燃焼室の室内温度が所定値以上に達し、2次空気供給
装置による2次空気供給量が強制的に増加され、この2
次空気供給量の増加により、2次燃焼室6の温度上昇が
抑制され、2次燃焼室6の温度が耐火レンガ等の許容温
度を超えることが回避され、炉の耐久性が向上する。
According to the operation control method of the gasification and incineration apparatus according to the next invention, if the room temperature of the secondary combustion chamber detected by the secondary temperature detector is equal to or higher than a predetermined value, the secondary air supply system is used. Since the secondary air supply is forcibly increased, if the temperature of the secondary combustion chamber rises during gasification combustion and may exceed the allowable temperature of refractory bricks, etc.
When the room temperature of the secondary combustion chamber reaches a predetermined value or more, the amount of secondary air supplied by the secondary air supply device is forcibly increased.
The increase in the amount of the secondary air supply suppresses a rise in the temperature of the secondary combustion chamber 6, prevents the temperature of the secondary combustion chamber 6 from exceeding the allowable temperature of refractory bricks or the like, and improves the durability of the furnace.

【0059】つぎの発明によるガス化焼却装置の運転制
御方法によれば、故障検出手段により2次温度維持装置
の故障が1次着火装置の着火前の2次燃焼室予熱過程で
検出されれば異常警報を出力し、ガス化燃焼終了前であ
れば1次空気量を強制的に減少して焼却物の燃焼を停止
し、ガス化燃焼終了後で炭化燃焼終了前であれば通常の
空気量制御を続行するから、障害発生時の自動緊急停止
が無駄なく適切に行われる。
According to the operation control method of the gasification incinerator according to the next invention, if the failure detecting means detects a failure of the secondary temperature maintaining device in the secondary combustion chamber preheating process before the ignition of the primary ignition device. Outputs an abnormal alarm and forcibly reduces the amount of primary air to stop the burning of incinerated material before the end of gasification combustion, and normal air amount after the end of gasification combustion and before the end of carbonization combustion. Since the control is continued, the automatic emergency stop when a failure occurs is appropriately performed without waste.

【0060】つぎの発明によるガス化焼却装置の運転制
御方法によれば、運転開始時における1次燃焼室1の燃
焼状態を判別し、燃焼状態に応じて2次燃焼室予熱過
程、ガス化燃焼過程、炭化燃焼過程と云う一連のシーケ
ンス動作の起動過程を選択設定するから、一時的な停電
等による運転停止後に再起動を行う際に通常の燃焼過程
に速やかに復帰することができる。
According to the operation control method of the gasification incinerator according to the next invention, the combustion state of the primary combustion chamber 1 at the start of operation is determined, and the secondary combustion chamber preheating process, gasification combustion Since the start-up process of a series of sequence operations called the process and the carbonization combustion process is selected and set, it is possible to quickly return to the normal combustion process when restarting after an operation stop due to a temporary power failure or the like.

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

【図1】 この発明によるガス化焼却装置の一つの実施
の形態を示す全体構成図である。
FIG. 1 is an overall configuration diagram showing one embodiment of a gasification and incineration apparatus according to the present invention.

【図2】 この発明によるガス化焼却装置の運転制御方
法を示すフローチャート(故障検出)である。
FIG. 2 is a flowchart (failure detection) showing an operation control method of the gasification incinerator according to the present invention.

【図3】 この発明によるガス化焼却装置の運転制御方
法を示すフローチャート(シーケンス選択)である。
FIG. 3 is a flowchart (sequence selection) showing an operation control method of the gasification and incineration apparatus according to the present invention.

【図4】 従来におけるガス化焼却炉の構成を示す全体
構成図である。
FIG. 4 is an overall configuration diagram showing a configuration of a conventional gasification incinerator.

【符号の説明】[Explanation of symbols]

1 1次燃焼室、2 1次着火装置(1次バーナ)、3
1次空気供給装置、4 1次温度検出器、5 圧力検
出器、6 2次燃焼室、7 2次温度維持装置(2次バ
ーナ)、8 2次空気供給装置、9 2次温度検出器、
10 排ガス温度検出器、11 煙突、21 故障検出
器、21 制御装置、22 1次温度時間変化率演算
器、23 圧力時間変化率演算器、24 2次温度時間
変化率演算器。
1 Primary combustion chamber, 2 Primary ignition device (primary burner), 3
Primary air supply device, 4 Primary temperature detector, 5 Pressure detector, 6 Secondary combustion chamber, 7 Secondary temperature maintenance device (Secondary burner), 8 Secondary air supply device, 9 Secondary temperature detector,
Reference Signs List 10 exhaust gas temperature detector, 11 chimney, 21 failure detector, 21 control device, 22 primary temperature temporal change rate calculator, 23 pressure temporal change rate calculator, 24 secondary temperature temporal change rate calculator.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F23G 5/16 ZAB F23G 5/16 ZABE ZABB Fターム(参考) 3K061 AA24 AB02 AC01 AC19 BA02 BA06 FA21 FA25 3K062 AA24 AB02 AC01 AC19 BA02 CA01 CB03 DA01 DA11 DB06 DB08 3K078 AA02 AA06 BA03 CA02 CA12──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat ゛ (Reference) F23G 5/16 ZAB F23G 5/16 ZABE ZABB F term (Reference) 3K061 AA24 AB02 AC01 AC19 BA02 BA06 FA21 FA25 3K062 AA24 AB02 AC01 AC19 BA02 CA01 CB03 DA01 DA11 DB06 DB08 3K078 AA02 AA06 BA03 CA02 CA12

Claims (12)

【特許請求の範囲】[Claims] 【請求項1】 焼却物を投入される1次燃焼室と、前記
1次燃焼室内の焼却物の着火を行う1次着火装置と、1
次燃焼室に投入された焼却物の熱分解に必要な空気を前
記1次燃焼室に供給する1次空気供給装置と、前記1次
燃焼室内での焼却物の熱分解により発生して可燃性ガス
を燃焼させる2次燃焼室と、2次燃焼室に導入された可
燃性ガスが燃焼するのに必要な温度を維持するための2
次温度維持装置と、2次燃焼室に導入された可燃性ガス
が燃焼するのに必要な空気を前記2次燃焼室に供給する
2次空気供給装置とを有するガス化焼却装置において、 前記2次燃焼室の室内温度を検出する2次温度検出器
と、 前記2次温度検出器により検出された前記2次燃焼室の
室内温度の時間変化率を演算する2次温度時間変化率演
算手段を有し、前記2次温度時間変化率演算手段により
演算される前記2次燃焼室の室内温度の時間変化率が所
定値以下であれば、前記2次空気供給装置による2次空
気供給量を強制的に増加する制御手段と、 を有していることを特徴とするガス化焼却装置。
1. A primary combustion chamber into which incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying the primary combustion chamber with air necessary for thermal decomposition of the incinerated material charged into the secondary combustion chamber, and a flammable gas generated by thermal decomposition of the incinerated material in the primary combustion chamber A secondary combustion chamber for burning the gas, and a second combustion chamber for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber.
A gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air necessary for combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber; A secondary temperature detector for detecting the indoor temperature of the secondary combustion chamber; and a secondary temperature temporal change rate calculating means for calculating a temporal change rate of the indoor temperature of the secondary combustion chamber detected by the secondary temperature detector. If the time change rate of the room temperature of the secondary combustion chamber calculated by the secondary temperature time change rate calculation means is equal to or less than a predetermined value, the secondary air supply amount by the secondary air supply device is forcibly applied. A gasification and incineration apparatus comprising: a control means for increasing the number of times;
【請求項2】 焼却物を投入される1次燃焼室と、前記
1次燃焼室内の焼却物の着火を行う1次着火装置と、1
次燃焼室に投入された焼却物の熱分解に必要な空気を前
記1次燃焼室に供給する1次空気供給装置と、前記1次
燃焼室内での焼却物の熱分解により発生して可燃性ガス
を燃焼させる2次燃焼室と、2次燃焼室に導入された可
燃性ガスが燃焼するのに必要な温度を維持するための2
次温度維持装置と、2次燃焼室に導入された可燃性ガス
が燃焼するのに必要な空気を前記2次燃焼室に供給する
2次空気供給装置とを有するガス化焼却装置において、 前記1次燃焼室の室内温度を検出する1次温度検出器
と、 前記1次温度検出器により検出された前記1次燃焼室の
室内温度の時間変化率を演算する1次温度時間変化率演
算手段を有し、前記1次温度時間変化率演算手段により
演算される前記1次燃焼室の室内温度の時間変化率が所
定値以上であれば、前記1次空気供給装置による1次空
気供給量を強制的に低減する制御手段と、 を有していることを特徴とするガス化焼却装置。
2. A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying the primary combustion chamber with air necessary for thermal decomposition of the incinerated material charged into the secondary combustion chamber, and a flammable gas generated by thermal decomposition of the incinerated material in the primary combustion chamber A secondary combustion chamber for burning the gas, and a second combustion chamber for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber.
A gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air required for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber; A primary temperature detector for detecting a room temperature of a secondary combustion chamber, and a primary temperature temporal change rate calculating means for calculating a temporal change rate of a room temperature of the primary combustion chamber detected by the primary temperature detector. If the time change rate of the room temperature of the primary combustion chamber calculated by the primary temperature time change rate calculating means is equal to or more than a predetermined value, the primary air supply amount by the primary air supply device is forcibly applied. A gasification incinerator characterized by comprising: control means for reducing the total amount of gasification.
【請求項3】 焼却物を投入される1次燃焼室と、前記
1次燃焼室内の焼却物の着火を行う1次着火装置と、1
次燃焼室に投入された焼却物の熱分解に必要な空気を前
記1次燃焼室に供給する1次空気供給装置と、前記1次
燃焼室内での焼却物の熱分解により発生して可燃性ガス
を燃焼させる2次燃焼室と、2次燃焼室に導入された可
燃性ガスが燃焼するのに必要な温度を維持するための2
次温度維持装置と、2次燃焼室に導入された可燃性ガス
が燃焼するのに必要な空気を前記2次燃焼室に供給する
2次空気供給装置とを有するガス化焼却装置において、 前記1次燃焼室の室内圧を検出する圧力検出器と、 前記圧力検出器により検出された前記1次燃焼室の室内
圧の時間変化率を演算する圧力時間変化率演算手段を有
し、前記圧力時間変化率演算手段により演算される前記
1次燃焼室の室内圧の時間変化率が所定値以上であれ
ば、前記1次空気供給装置による1次空気供給量を強制
的に低減する制御手段と、 を有していることを特徴とするガス化焼却装置。
3. A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying the primary combustion chamber with air necessary for thermal decomposition of the incinerated material charged into the secondary combustion chamber, and a flammable gas generated by thermal decomposition of the incinerated material in the primary combustion chamber A secondary combustion chamber for burning the gas, and a second combustion chamber for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber.
A gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air required for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber; A pressure detector for detecting the indoor pressure of the next combustion chamber; and a pressure time change rate calculating means for calculating a time change rate of the indoor pressure of the primary combustion chamber detected by the pressure detector. Control means for forcibly reducing the primary air supply amount by the primary air supply device, if the time change rate of the indoor pressure of the primary combustion chamber calculated by the change rate calculation means is equal to or more than a predetermined value; A gasification incinerator characterized by having:
【請求項4】 焼却物を投入される1次燃焼室と、前記
1次燃焼室内の焼却物の着火を行う1次着火装置と、1
次燃焼室に投入された焼却物の熱分解に必要な空気を前
記1次燃焼室に供給する1次空気供給装置と、前記1次
燃焼室内での焼却物の熱分解により発生して可燃性ガス
を燃焼させる2次燃焼室と、2次燃焼室に導入された可
燃性ガスが燃焼するのに必要な温度を維持するための2
次温度維持装置と、2次燃焼室に導入された可燃性ガス
が燃焼するのに必要な空気を前記2次燃焼室に供給する
2次空気供給装置とを有するガス化焼却装置において、 前記2次燃焼室の室内温度を検出する2次温度検出器
と、 前記2次温度検出器により検出された前記2次燃焼室の
室内温度が所定値以上であれば、前記2次空気供給装置
による2次空気供給量を強制的に増加する制御手段と、 を有していることを特徴とするガス化焼却装置。
4. A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying the primary combustion chamber with air necessary for thermal decomposition of the incinerated material charged into the secondary combustion chamber, and a flammable gas generated by thermal decomposition of the incinerated material in the primary combustion chamber A secondary combustion chamber for burning the gas, and a second combustion chamber for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber.
A gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air necessary for combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber; A secondary temperature detector for detecting an indoor temperature of the secondary combustion chamber; and if the indoor temperature of the secondary combustion chamber detected by the secondary temperature detector is equal to or higher than a predetermined value, Control means for forcibly increasing the amount of secondary air supplied, and a gasification incinerator characterized by having.
【請求項5】 焼却物を投入される1次燃焼室と、前記
1次燃焼室内の焼却物の着火を行う1次着火装置と、1
次燃焼室に投入された焼却物の熱分解に必要な空気を前
記1次燃焼室に供給する1次空気供給装置と、前記1次
燃焼室内での焼却物の熱分解により発生して可燃性ガス
を燃焼させる2次燃焼室と、2次燃焼室に導入された可
燃性ガスが燃焼するのに必要な温度を維持するための2
次温度維持装置と、2次燃焼室に導入された可燃性ガス
が燃焼するのに必要な空気を前記2次燃焼室に供給する
2次空気供給装置とを有するガス化焼却装置において、 前記2次温度維持装置の故障を検出する故障検出手段
と、 前記故障検出手段により前記2次温度維持装置の故障が
1次着火装置の着火前の2次燃焼室予熱過程で検出され
れば異常警報を出力し、ガス化燃焼終了前であれば1次
空気量を強制的に減少して焼却物の燃焼を停止し、ガス
化燃焼終了後で炭化燃焼終了前であれば通常の空気量制
御を続行する制御手段と、 を有していることを特徴とするガス化焼却装置。
5. A primary combustion chamber into which incineration material is charged, a primary ignition device for igniting the incineration material in said primary combustion chamber,
A primary air supply device for supplying the primary combustion chamber with air necessary for thermal decomposition of the incinerated material charged into the secondary combustion chamber, and a flammable gas generated by thermal decomposition of the incinerated material in the primary combustion chamber A secondary combustion chamber for burning the gas, and a second combustion chamber for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber.
A gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air necessary for combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber; Failure detection means for detecting a failure of the secondary temperature maintenance device; and an abnormality alarm if the failure detection means detects a failure of the secondary temperature maintenance device in a secondary combustion chamber preheating process before ignition of the primary ignition device. If the output is before the end of gasification combustion, the primary air amount is forcibly reduced and the combustion of the incinerated material is stopped, and after the end of gasification combustion and before the end of carbonization combustion, normal air amount control is continued. A gasification and incineration apparatus, comprising:
【請求項6】 焼却物を投入される1次燃焼室と、前記
1次燃焼室内の焼却物の着火を行う1次着火装置と、1
次燃焼室に投入された焼却物の熱分解に必要な空気を前
記1次燃焼室に供給する1次空気供給装置と、前記1次
燃焼室内での焼却物の熱分解により発生して可燃性ガス
を燃焼させる2次燃焼室と、2次燃焼室に導入された可
燃性ガスが燃焼するのに必要な温度を維持するための2
次温度維持装置と、2次燃焼室に導入された可燃性ガス
が燃焼するのに必要な空気を前記2次燃焼室に供給する
2次空気供給装置とを有するガス化焼却装置において、 運転開始時における1次燃焼室1の燃焼状態を判別し、
燃焼状態に応じて2次燃焼室予熱過程、ガス化燃焼過
程、炭化燃焼過程と云う一連のシーケンス動作の起動過
程を選択設定する制御手段、 を有していることを特徴とするガス化焼却装置。
6. A primary combustion chamber into which incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying the primary combustion chamber with air necessary for thermal decomposition of the incinerated material charged into the secondary combustion chamber, and a flammable gas generated by thermal decomposition of the incinerated material in the primary combustion chamber A secondary combustion chamber for burning the gas, and a second combustion chamber for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber.
A gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air necessary for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber, The combustion state of the primary combustion chamber 1 at the time is determined,
Control means for selectively setting a start-up process of a series of sequence operations such as a secondary combustion chamber preheating process, a gasification combustion process, and a carbonization combustion process in accordance with a combustion state. .
【請求項7】 焼却物を投入される1次燃焼室と、前記
1次燃焼室内の焼却物の着火を行う1次着火装置と、1
次燃焼室に投入された焼却物の熱分解に必要な空気を前
記1次燃焼室に供給する1次空気供給装置と、前記1次
燃焼室内での焼却物の熱分解により発生して可燃性ガス
を燃焼させる2次燃焼室と、2次燃焼室に導入された可
燃性ガスが燃焼するのに必要な温度を維持するための2
次温度維持装置と、2次燃焼室に導入された可燃性ガス
が燃焼するのに必要な空気を前記2次燃焼室に供給する
2次空気供給装置とを有するガス化焼却装置の運転制御
方法において、 2次温度検出器により前記2次燃焼室の室内温度を検出
し、前記2次温度検出器により検出された前記2次燃焼
室の室内温度の時間変化率を演算し、演算された前記2
次燃焼室の室内温度の時間変化率が所定値以下であれ
ば、前記2次空気供給装置による2次空気供給量を強制
的に増加することを特徴とするガス化焼却装置の運転制
御方法。
7. A primary combustion chamber into which incineration material is charged, a primary ignition device for igniting the incineration material in said primary combustion chamber,
A primary air supply device for supplying the primary combustion chamber with air necessary for thermal decomposition of the incinerated material charged into the secondary combustion chamber, and a flammable gas generated by thermal decomposition of the incinerated material in the primary combustion chamber A secondary combustion chamber for burning the gas, and a second combustion chamber for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber.
Operation control method of a gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air required for combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber In the above, a room temperature of the secondary combustion chamber is detected by a secondary temperature detector, and a time change rate of the room temperature of the secondary combustion chamber detected by the secondary temperature detector is calculated. 2
An operation control method for a gasification and incineration device, characterized by forcibly increasing the amount of secondary air supplied by the secondary air supply device when the time change rate of the room temperature of the next combustion chamber is equal to or less than a predetermined value.
【請求項8】 焼却物を投入される1次燃焼室と、前記
1次燃焼室内の焼却物の着火を行う1次着火装置と、1
次燃焼室に投入された焼却物の熱分解に必要な空気を前
記1次燃焼室に供給する1次空気供給装置と、前記1次
燃焼室内での焼却物の熱分解により発生して可燃性ガス
を燃焼させる2次燃焼室と、2次燃焼室に導入された可
燃性ガスが燃焼するのに必要な温度を維持するための2
次温度維持装置と、2次燃焼室に導入された可燃性ガス
が燃焼するのに必要な空気を前記2次燃焼室に供給する
2次空気供給装置とを有するガス化焼却装置の運転制御
方法において、 1次温度検出器により前記1次燃焼室の室内温度を検出
し、前記1次温度検出器により検出された前記1次燃焼
室の室内温度の時間変化率を演算し、演算された1次燃
焼室の室内温度の時間変化率が所定値以上であれば、前
記1次空気供給装置による1次空気供給量を強制的に低
減することを特徴とするガス化焼却装置の運転制御方
法。
8. A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying the primary combustion chamber with air necessary for thermal decomposition of the incinerated material charged into the secondary combustion chamber, and a flammable gas generated by thermal decomposition of the incinerated material in the primary combustion chamber A secondary combustion chamber for burning the gas, and a second combustion chamber for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber.
Operation control method of a gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air required for combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber In the above, the primary temperature detector detects the room temperature of the primary combustion chamber, and calculates the time change rate of the room temperature of the primary combustion chamber detected by the primary temperature detector. An operation control method for a gasification and incineration device, characterized by forcibly reducing the amount of primary air supplied by the primary air supply device when the time change rate of the room temperature of the secondary combustion chamber is equal to or more than a predetermined value.
【請求項9】 焼却物を投入される1次燃焼室と、前記
1次燃焼室内の焼却物の着火を行う1次着火装置と、1
次燃焼室に投入された焼却物の熱分解に必要な空気を前
記1次燃焼室に供給する1次空気供給装置と、前記1次
燃焼室内での焼却物の熱分解により発生して可燃性ガス
を燃焼させる2次燃焼室と、2次燃焼室に導入された可
燃性ガスが燃焼するのに必要な温度を維持するための2
次温度維持装置と、2次燃焼室に導入された可燃性ガス
が燃焼するのに必要な空気を前記2次燃焼室に供給する
2次空気供給装置とを有するガス化焼却装置の運転制御
方法において、 圧力検出器により前記1次燃焼室の室内圧を検出し、前
記圧力検出器により検出された前記1次燃焼室の室内圧
の時間変化率を演算し、演算された前記1次燃焼室の室
内圧の時間変化率が所定値以上であれば、前記1次空気
供給装置による1次空気供給量を強制的に低減すること
を特徴とするガス化焼却装置の運転制御方法。
9. A primary combustion chamber into which incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying the primary combustion chamber with air necessary for thermal decomposition of the incinerated material charged into the secondary combustion chamber, and a flammable gas generated by thermal decomposition of the incinerated material in the primary combustion chamber A secondary combustion chamber for burning the gas, and a second combustion chamber for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber.
Operation control method of a gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air required for combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber In the above, the pressure detector detects the indoor pressure of the primary combustion chamber, calculates the time change rate of the indoor pressure of the primary combustion chamber detected by the pressure detector, and calculates the calculated primary combustion chamber. An operation control method for the gasification and incineration device, wherein the primary air supply amount by the primary air supply device is forcibly reduced when the time change rate of the indoor pressure is equal to or more than a predetermined value.
【請求項10】 焼却物を投入される1次燃焼室と、前
記1次燃焼室内の焼却物の着火を行う1次着火装置と、
1次燃焼室に投入された焼却物の熱分解に必要な空気を
前記1次燃焼室に供給する1次空気供給装置と、前記1
次燃焼室内での焼却物の熱分解により発生して可燃性ガ
スを燃焼させる2次燃焼室と、2次燃焼室に導入された
可燃性ガスが燃焼するのに必要な温度を維持するための
2次温度維持装置と、2次燃焼室に導入された可燃性ガ
スが燃焼するのに必要な空気を前記2次燃焼室に供給す
る2次空気供給装置とを有するガス化焼却装置の運転制
御方法において、 2次温度検出器により前記2次燃焼室の室内温度を検出
し、前記2次温度検出器により検出された前記2次燃焼
室の室内温度が所定値以上であれば、前記2次空気供給
装置による2次空気供給量を強制的に増加することを特
徴とするガス化焼却装置の運転制御方法。
10. A primary combustion chamber into which incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying air required for the thermal decomposition of the incineration material injected into the primary combustion chamber to the primary combustion chamber;
A secondary combustion chamber for burning combustible gas generated by thermal decomposition of the incinerated material in the secondary combustion chamber, and for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber. Operation control of a gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air required for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber. In the method, a room temperature of the secondary combustion chamber is detected by a secondary temperature detector, and if the room temperature of the secondary combustion chamber detected by the secondary temperature detector is equal to or higher than a predetermined value, the secondary temperature is detected. A method for controlling operation of a gasification and incineration device, comprising forcibly increasing the amount of secondary air supplied by an air supply device.
【請求項11】 焼却物を投入される1次燃焼室と、前
記1次燃焼室内の焼却物の着火を行う1次着火装置と、
1次燃焼室に投入された焼却物の熱分解に必要な空気を
前記1次燃焼室に供給する1次空気供給装置と、前記1
次燃焼室内での焼却物の熱分解により発生して可燃性ガ
スを燃焼させる2次燃焼室と、2次燃焼室に導入された
可燃性ガスが燃焼するのに必要な温度を維持するための
2次温度維持装置と、2次燃焼室に導入された可燃性ガ
スが燃焼するのに必要な空気を前記2次燃焼室に供給す
る2次空気供給装置とを有するガス化焼却装置の運転制
御方法において、 故障検出手段により前記2次温度維持装置の故障を検出
し、前記故障検出手段により前記2次温度維持装置の故
障が1次着火装置の着火前の2次燃焼室予熱過程で検出
されれば異常警報を出力し、ガス化燃焼終了前であれば
1次空気量を強制的に減少して焼却物の燃焼を停止し、
ガス化燃焼終了後で炭化燃焼終了前であれば通常の空気
量制御を続行することを特徴とするガス化焼却装置の運
転制御方法。
11. A primary combustion chamber into which incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying air required for the thermal decomposition of the incineration material injected into the primary combustion chamber to the primary combustion chamber;
A secondary combustion chamber for burning combustible gas generated by thermal decomposition of the incinerated material in the secondary combustion chamber, and for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber. Operation control of a gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air required for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber. In the method, a failure of the secondary temperature maintenance device is detected by failure detection means, and a failure of the secondary temperature maintenance device is detected by the failure detection means in a secondary combustion chamber preheating process before ignition of the primary ignition device. If this is the case, an abnormal alarm is output.
An operation control method for a gasification and incineration apparatus, characterized in that normal air amount control is continued after the end of gasification combustion and before the end of carbonization combustion.
【請求項12】 焼却物を投入される1次燃焼室と、前
記1次燃焼室内の焼却物の着火を行う1次着火装置と、
1次燃焼室に投入された焼却物の熱分解に必要な空気を
前記1次燃焼室に供給する1次空気供給装置と、前記1
次燃焼室内での焼却物の熱分解により発生して可燃性ガ
スを燃焼させる2次燃焼室と、2次燃焼室に導入された
可燃性ガスが燃焼するのに必要な温度を維持するための
2次温度維持装置と、2次燃焼室に導入された可燃性ガ
スが燃焼するのに必要な空気を前記2次燃焼室に供給す
る2次空気供給装置とを有するガス化焼却装置の運転制
御方法において、 運転開始時における1次燃焼室1の燃焼状態を判別し、
燃焼状態に応じて2次燃焼室予熱過程、ガス化燃焼過
程、炭化燃焼過程と云う一連のシーケンス動作の起動過
程を選択設定することを特徴とするガス化焼却装置の運
転制御方法。
12. A primary combustion chamber into which the incineration material is charged, a primary ignition device for igniting the incineration material in the primary combustion chamber,
A primary air supply device for supplying air required for the thermal decomposition of the incineration material injected into the primary combustion chamber to the primary combustion chamber;
A secondary combustion chamber for burning combustible gas generated by thermal decomposition of the incinerated material in the secondary combustion chamber, and for maintaining a temperature required for burning the combustible gas introduced into the secondary combustion chamber. Operation control of a gasification and incineration device having a secondary temperature maintaining device and a secondary air supply device for supplying air required for burning the combustible gas introduced into the secondary combustion chamber to the secondary combustion chamber. In the method, the combustion state of the primary combustion chamber 1 at the start of operation is determined,
An operation control method for a gasification and incineration apparatus, wherein a start-up process of a series of sequence operations such as a secondary combustion chamber preheating process, a gasification combustion process, and a carbonization combustion process is selectively set according to a combustion state.
JP10176892A 1998-06-24 1998-06-24 Gasification incinerating device and control method of operation of the same Pending JP2000018547A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10176892A JP2000018547A (en) 1998-06-24 1998-06-24 Gasification incinerating device and control method of operation of the same

Publications (1)

Publication Number Publication Date
JP2000018547A true JP2000018547A (en) 2000-01-18

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ID=16021584

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103953931A (en) * 2014-05-19 2014-07-30 张文国 Incineration cracking type innocent garbage treatment device and process
CN114593425A (en) * 2022-03-11 2022-06-07 合肥工业大学 Pyrolysis gas tail gas treatment secondary combustion chamber device and pyrolysis gas tail gas treatment method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103953931A (en) * 2014-05-19 2014-07-30 张文国 Incineration cracking type innocent garbage treatment device and process
CN114593425A (en) * 2022-03-11 2022-06-07 合肥工业大学 Pyrolysis gas tail gas treatment secondary combustion chamber device and pyrolysis gas tail gas treatment method

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