JPH0642726A - Combustion amount detecting device and combustion control device for fluidized bed type furnace - Google Patents

Combustion amount detecting device and combustion control device for fluidized bed type furnace

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Publication number
JPH0642726A
JPH0642726A JP5200058A JP20005893A JPH0642726A JP H0642726 A JPH0642726 A JP H0642726A JP 5200058 A JP5200058 A JP 5200058A JP 20005893 A JP20005893 A JP 20005893A JP H0642726 A JPH0642726 A JP H0642726A
Authority
JP
Japan
Prior art keywords
furnace
fluidized bed
brightness
combustion
detecting
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
JP5200058A
Other languages
Japanese (ja)
Inventor
Takeyuki Naito
剛行 内藤
Yoshiki Kuroda
芳喜 黒田
Yutaka Yoshida
吉田  裕
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.)
Ebara Corp
Original Assignee
Ebara 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 Ebara Corp filed Critical Ebara Corp
Priority to JP5200058A priority Critical patent/JPH0642726A/en
Publication of JPH0642726A publication Critical patent/JPH0642726A/en
Pending legal-status Critical Current

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  • Incineration Of Waste (AREA)

Abstract

PURPOSE:To enable an instantaneous accurate sensing of a combustion state within a fluidized bed type furnace to be carried out by a method wherein a brightness within the furnace is detected and the combustion amount of incinerated item within the furnace is detected. CONSTITUTION:A brightness sensing sensor 14-1 may detect brightness within a furnace 1 caused by combustion of ignited item A fed from a supplying feeder 12 into the furnace 1. Due to this fact, its fixing position is located at a place where it is sufficiently above an air nozzle 8 for blowing air into an upper part spacing of a fluidized bed 2 as well as in a secondary air feeding pipe 18 and an entire cross sectional surface of the furnace 1 can be seen. An adjustor 13 may adjust a degree of opening of a control valve 7 in response to a measured value of the brightness sensing sensor 14-1 for use in sensing brightness within the furnace 1. That is, as brightness within the furnace 1 is increased, the adjuster 13 releases the control valve 7, bypasses a part of the air amount blown from an air chamber 6 and blows it from the air nozzle 8 into the upper spacing of the fluidized bed 2 through a pipe 16. In this way, it is possible to perform an accurate measurement of the combustion amount within the furnace.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、砂等の流動媒体を炉床
下部から送り込む空気により流動させながら焼却物を焼
却する流動床炉において、炉内に投入される焼却物の燃
焼状態を検出する流動床炉の燃焼量検出装置及び燃焼制
御装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention detects the combustion state of the incineration material that is put into the furnace in a fluidized bed furnace that incinerates the incinerated material while flowing the fluidized medium such as sand from the lower part of the hearth with air. The present invention relates to a combustion amount detection device and a combustion control device for a fluidized bed furnace.

【0002】[0002]

【従来技術】従来、流動床焼却炉は都市ゴミの焼却等に
使用されており、都市ゴミをこの流動床焼却炉で燃焼す
る場合はゴミを連続的に流動床焼却炉に投入するが、都
市ゴミはその性質上互いに絡まり、大きな塊となった状
態で瞬間的に大量に投入される場合が度々ある。流動床
焼却炉は焼却炉として燃焼速度の極めて速い炉であり、
非常に良く燃えるという利点があるが、これが逆に欠点
となる場合がある。即ち、燃焼性能が良いため流動床に
燃焼物を投入すると早いものは僅か数秒で燃えてしま
う。そのため、焼却物を炉内に供給するフィーダの定量
性が悪いと、焼却物の投入量のバラツキはそのまま燃焼
ガス中の酸素濃度のバラツキにつながるという問題があ
る。
2. Description of the Related Art Conventionally, a fluidized bed incinerator has been used for incineration of city refuse, and when burning city refuse in this fluidized bed incinerator, the garbage is continuously fed to the fluidized bed incinerator. Garbage is often entangled with each other due to its nature, and is often thrown into a large lump in a moment. The fluidized bed incinerator is an incinerator with an extremely high burning rate,
It has the advantage of burning very well, but this can be a drawback on the contrary. That is, since the combustion performance is good, when a combustion product is put into the fluidized bed, a fast product burns in just a few seconds. Therefore, if the quantitativeness of the feeder that supplies the incinerator into the furnace is poor, there is a problem that the variation of the input amount of the incineration directly leads to the variation of the oxygen concentration in the combustion gas.

【0003】流動床焼却炉の形式にもよるが、燃焼排ガ
ス中の酸素濃度が約5%近辺以下となると一酸化炭素と
か、メタン、エチレン、プロピレン、アセチレン、ベン
ゼンといった炭化水素等が燃焼しきれずに排出されるこ
とになる。また、塩化アンモン、水酸化アンモンといっ
た物質も生成されるので煙突より白煙が出ることにな
る。
Depending on the type of fluidized bed incinerator, carbon monoxide and hydrocarbons such as methane, ethylene, propylene, acetylene and benzene cannot be completely burned when the oxygen concentration in the flue gas falls below approximately 5%. Will be discharged to. In addition, since substances such as ammonium chloride and ammonium hydroxide are also produced, white smoke will be emitted from the chimney.

【0004】[0004]

【発明が解決しようとする課題】上記のように流動床焼
却炉の燃焼速度が極めて速いという利点が逆に欠点とな
るという問題に対処し、上記問題が発生しない燃焼制御
を行なうには、流動床焼却炉内の燃焼量(単位時間当た
りの焼却物の燃焼量)を瞬時に検出し、その燃焼状態に
合った、例えば一次空気量や二次空気量の供給制御を行
なう必要がある。しかしながら、従来、流動床焼却炉内
の燃焼状態を瞬時に正確に検出する手段がなく、特に都
市ゴミ等を焼却する流動床焼却炉において、燃焼ガス中
の酸素濃度のバラツキが無く、煙突から白煙が出ないよ
うにする燃焼制御を的確に行なうことが困難であった。
In order to deal with the problem that the advantage of the extremely high burning rate of the fluidized bed incinerator is a drawback, and to perform the combustion control without causing the above problem, the It is necessary to instantaneously detect the combustion amount in the floor incinerator (combustion amount of incineration material per unit time) and perform supply control of, for example, the primary air amount or the secondary air amount suitable for the combustion state. However, conventionally, there is no means for instantaneously and accurately detecting the combustion state in a fluidized bed incinerator, and especially in a fluidized bed incinerator that incinerates municipal solid waste, there is no variation in the oxygen concentration in the combustion gas, and there is no whiteness from the chimney. It was difficult to accurately control the combustion so that no smoke was emitted.

【0005】本発明は上述の点に鑑みてなされたもの
で、流動床炉内の燃焼状態を瞬時に正確に検出できる流
動床炉の燃焼量検出装置及び燃焼制御装置を提供するこ
とを目的とする。
The present invention has been made in view of the above points, and an object thereof is to provide a combustion amount detection device and a combustion control device for a fluidized bed furnace capable of instantaneously and accurately detecting the combustion state in the fluidized bed furnace. To do.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するため
本発明は、流動床下部から送り込む空気により流動媒体
を流動させ、炉内に投入される焼却物を燃焼させる流動
床炉の炉内の燃焼量を検出する燃焼量検出装置であっ
て、炉内の明るさを検出する明るさ検出手段を設け、該
明るさ検出手段の出力から炉内の焼却物の燃焼量を検出
することを特徴とする。
In order to solve the above problems, the present invention is directed to the inside of the furnace of a fluidized bed furnace in which the fluidized medium is made to flow by the air sent from the lower part of the fluidized bed, and the incinerator charged into the furnace is burned. A combustion amount detecting device for detecting a combustion amount, comprising brightness detecting means for detecting brightness in a furnace, and detecting a combustion amount of incineration material in the furnace from an output of the brightness detecting means. And

【0007】また、前記明るさ検出手段は炉の横断面全
面が見渡せる位置に設けたことを特徴とする。
Further, the brightness detecting means is provided at a position overlooking the entire cross section of the furnace.

【0008】また、前記明るさ検出手段は流動媒体や炉
壁等による明るさに影響されない位置に設けたことを特
徴とする。
Further, the brightness detecting means is provided at a position which is not affected by the brightness due to the fluid medium or the furnace wall.

【0009】また、前記明るさ検出手段炉は頂又は炉頂
近傍に設けたことを特徴とする。
Further, the brightness detecting means furnace is provided at or near the top of the furnace.

【0010】また、前記明るさ検出手段を二次空気吹き
込み位置より上方に設けたことを特徴とする。
Further, the brightness detecting means is provided above the secondary air blowing position.

【0011】また、流動床下部から送り込む空気により
流動媒体を流動させ、炉内に投入される焼却物を燃焼さ
せる流動床炉の炉内の燃焼量を検出する燃焼量検出装置
であって、炉内の明るさを検出する明るさ検出手段及び
排ガス中酸素濃度、炉内圧力、炉内に投入される焼却物
の性状や形状や嵩及び量を検出する検出手段を設け、該
明るさ検出手段及び排ガス中酸素濃度、炉内圧力、炉内
に投入される焼却物の性状や形状や嵩及び量を検出する
検出手段のうちいずれか大きい方で炉内の燃焼量を検出
することを特徴とする。
Further, there is provided a combustion amount detecting device for detecting the combustion amount in the furnace of a fluidized bed furnace in which the fluidized medium is made to flow by the air sent from the lower part of the fluidized bed to combust the incinerated substances thrown into the furnace. The brightness detection means for detecting the brightness in the interior and the detection means for detecting the oxygen concentration in the exhaust gas, the pressure in the furnace, and the property, shape, volume and amount of the incineration material thrown into the furnace are provided. And a detection means for detecting the oxygen concentration in the exhaust gas, the pressure in the furnace, and the property, shape, volume and amount of the incinerator that is put into the furnace, whichever is larger. To do.

【0012】また、上記いずれか1つに記載の燃焼量検
出装置の出力を流動床炉の燃焼制御装置の制御信号とし
て用いることを特徴とする。
Also, the output of the combustion amount detecting device described in any one of the above is used as a control signal of the combustion control device of the fluidized bed furnace.

【0013】[0013]

【作用】本発明は上記構成を採用することにより、流動
床に焼却物が投入され、該焼却物が流動床でガス化さ
れ、該ガスが燃焼すると火炎が発生する。この火炎輝度
は燃焼量に応じて瞬時に変化するから該火炎輝度を明る
さ検出手段で検出することにより、流動床焼却炉内の燃
焼量を瞬時に正確に測定することができる。
According to the present invention, by adopting the above construction, the incinerated matter is put into the fluidized bed, the incinerated matter is gasified in the fluidized bed, and when the gas burns, a flame is generated. Since the flame intensity changes instantaneously according to the combustion amount, the combustion amount in the fluidized bed incinerator can be instantly and accurately measured by detecting the flame intensity with the brightness detecting means.

【0014】また、炉内の明るさを検出する明るさ検出
手段の他に炉内の圧力を検出する圧力検出手段を設け、
明るさ検出手段及び圧力検出手段の出力のうちいずれか
大きい方で炉内の燃焼量を検出することにより、炉内圧
は燃焼量に応じて燃焼量が大きいと高く、小さいと低く
なるから、例えば炉内に煙が発生し暗くなり、明るさ検
出手段が正確な燃焼量を検出できない場合でも、圧力検
出器がそれを補う作用を奏することになる。
In addition to the brightness detecting means for detecting the brightness in the furnace, a pressure detecting means for detecting the pressure in the furnace is provided.
By detecting the combustion amount in the furnace by the larger one of the outputs of the brightness detection means and the pressure detection means, the in-furnace pressure becomes high when the combustion amount is large and becomes low when the combustion amount is small. Even if smoke is generated in the furnace and it becomes dark and the brightness detection means cannot detect the accurate combustion amount, the pressure detector has a function of compensating for it.

【0015】[0015]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。流動床焼却炉においては、燃焼対象物の燃焼量を
直接測定することは極めて困難である。この燃焼量(単
位時間当たりの燃焼量)は炉内の明るさ、排ガス中の酸
素濃度、炉内圧力に密接に関係する。図1の(A),
(B),(C)は流動床焼却炉における燃焼量を代表す
る炉内の明るさL、排ガス中の酸素濃度E、炉内圧力P
の関係を示す図である。図中横軸は時間t(1目盛は5
秒)を示す。図示するように流動床焼却炉においては、
燃焼量の変動に応じて炉内の明るさL、排ガス中の酸素
濃度E及び炉内圧力Pが変化する。特に炉内の明るさL
は忠実に瞬時に燃焼量に反映する。そこで本願発明は、
明るさ検出センサを設けこの炉内の明るさLを検出し
て、その出力より流動床焼却炉内の燃焼量を推測するこ
とにより燃焼量を瞬時に検出できる燃焼量検出装置であ
る。また、明るさ検出センサの他に炉内の圧力を検出す
る圧力検出センサを設け、該圧力検出センサの出力で明
るさ検出センサの補完を行なわせる。これによりより精
度良く燃焼量を検出できる。
Embodiments of the present invention will be described below with reference to the drawings. In a fluidized bed incinerator, it is extremely difficult to directly measure the combustion amount of the combustion target. This combustion amount (combustion amount per unit time) is closely related to the brightness in the furnace, the oxygen concentration in the exhaust gas, and the furnace pressure. 1 (A),
(B) and (C) are the brightness L in the furnace, which represents the combustion amount in the fluidized bed incinerator, the oxygen concentration E in the exhaust gas, and the furnace pressure P.
It is a figure which shows the relationship of. In the figure, the horizontal axis is time t (1 scale is 5
Seconds). As shown in the figure, in a fluidized bed incinerator,
The brightness L in the furnace, the oxygen concentration E in the exhaust gas, and the furnace pressure P change according to the fluctuation of the combustion amount. Especially the brightness L in the furnace
Faithfully reflects the amount of combustion instantly. Therefore, the present invention is
This is a combustion amount detection device capable of instantaneously detecting the combustion amount by providing a brightness detection sensor, detecting the brightness L in the furnace, and estimating the combustion amount in the fluidized bed incinerator from its output. In addition to the brightness detection sensor, a pressure detection sensor for detecting the pressure inside the furnace is provided, and the brightness detection sensor is complemented by the output of the pressure detection sensor. Thereby, the combustion amount can be detected more accurately.

【0016】図2は本発明の燃焼量検出装置を取り付け
た燃焼制御を行なう流動床焼却炉の概略構成を示す図で
ある。図において、1は炉であり、該炉1の内部には砂
等の流動媒体が流動する流動床2が形成されている。流
動床2の下部にはエアチャンバー6が設けられており、
配管5を通して流動用ブロワ(図示せず)より流動空気
を該エアチャンバー6を介して炉1内に送り込むことに
より、流動媒体を流動させている。このブロワは例えば
遠心ブロワであり、運転中は望ましくは風量が一定にな
るように制御されている。
FIG. 2 is a diagram showing a schematic construction of a fluidized bed incinerator for controlling combustion equipped with a combustion amount detecting device of the present invention. In the figure, reference numeral 1 is a furnace, and inside the furnace 1, a fluidized bed 2 in which a fluid medium such as sand flows is formed. An air chamber 6 is provided below the fluidized bed 2,
The fluidized medium is made to flow by sending fluidized air from a flow blower (not shown) through the pipe 5 into the furnace 1 through the air chamber 6. This blower is, for example, a centrifugal blower, and is preferably controlled so that the air volume becomes constant during operation.

【0017】14−1は炉1内の炉頂又は炉頂近傍に取
り付けられた明るさを検出する明るさ検出センサであ
る。該明るさ検出センサ14−1の取り付け位置はこの
炉頂又は炉頂近傍に限定されるものではなく、流動媒体
や炉壁等による明るさに影響されないで、供給フィーダ
12から炉1内に投入される焼却物Aの燃焼による炉1
内の明るさを検出できるように、二次空気送入配管18
や流動床2の上部空間に空気を吹き込むための空気ノズ
ル8より充分上方で且つ炉1の横断面全面が見渡せる位
置に取り付ける。
Reference numeral 14-1 is a brightness detection sensor attached to the furnace top in the furnace 1 or mounted near the furnace top to detect the brightness. The mounting position of the brightness detection sensor 14-1 is not limited to the furnace top or the vicinity of the furnace top, and is supplied from the supply feeder 12 into the furnace 1 without being affected by the brightness due to the fluid medium or the furnace wall. Furnace 1 for burning incinerated waste A
Secondary air inlet piping 18 so that the brightness inside can be detected
It is installed at a position sufficiently above the air nozzle 8 for blowing air into the upper space of the fluidized bed 2 and overlooking the entire cross section of the furnace 1.

【0018】13は炉1内の明るさを検出する明るさ検
出センサの測定値をもとに制御弁7の開度を調節する調
節器である。11は都市ゴミ等の焼却物を投入する焼却
物投入ホッパーであり、該焼却物投入ホッパー11の下
部には焼却物を炉1内に供給するための供給フィーダ1
2が設けられている。また、図1において、EGは排ガ
ス出口部から排出される排ガスを示し、ASは灰出口部
から排出される灰を示す。
Reference numeral 13 is an adjuster for adjusting the opening of the control valve 7 based on the measured value of the brightness detecting sensor for detecting the brightness in the furnace 1. Reference numeral 11 denotes an incineration material input hopper for inputting incineration material such as municipal waste, and a supply feeder 1 for supplying the incineration material into the furnace 1 below the incineration material input hopper 11.
Two are provided. Further, in FIG. 1, EG represents exhaust gas discharged from the exhaust gas outlet portion, and AS represents ash discharged from the ash outlet portion.

【0019】上記構成の流動床焼却炉において、供給フ
ィーダ12から炉1内に投入される焼却物Aは流動床2
上で熱分解されガス化され燃焼し、火炎を発する。この
火炎により炉1内が明るくなるから、この明るさを検出
することにより、炉1内の燃焼量、即ち燃焼量を検出す
ることが可能となる。しかも燃焼と火炎の発生は略同時
であるから、明るさ検出センサ14−1で炉1内の明る
さを検出することは、炉1内の燃焼量を瞬時に検出でき
ることになる。
In the fluidized bed incinerator having the above-mentioned structure, the incinerated material A introduced into the furnace 1 from the supply feeder 12 is the fluidized bed 2
Above it is pyrolyzed, gasified and burned, producing a flame. Since the flame makes the inside of the furnace 1 brighter, it is possible to detect the combustion amount in the furnace 1, that is, the combustion amount by detecting the brightness. Moreover, since the combustion and the generation of the flame are substantially simultaneous, detecting the brightness in the furnace 1 by the brightness detection sensor 14-1 makes it possible to instantaneously detect the combustion amount in the furnace 1.

【0020】上記流動床焼却炉の燃焼制御は、炉1内の
焼却物の燃焼量を上記供給フィーダ12から投入される
焼却物Aの量にかかわりなく、所定量に維持する制御を
行なっている。以下、その動作を説明する。供給フィー
ダ12から投入される焼却物Aが通常より大きい場合、
該焼却物Aの燃焼量(単位時間当り)が大きくなるか
ら、炉1内が通常より明るくなり、明るさ検出センサ1
4−1の出力が大きくなる。炉1内の明るさが大きくな
ると調節器13は制御弁7を開放し、エアチャンバー6
から吹き込む空気量の一部をバイパスし配管16を通し
て、空気ノズル8から流動床2の上部空間に吹き込む。
The combustion control of the fluidized bed incinerator is such that the combustion amount of the incineration material in the furnace 1 is maintained at a predetermined amount regardless of the amount of the incineration material A fed from the supply feeder 12. . The operation will be described below. When the incineration A input from the supply feeder 12 is larger than usual,
Since the combustion amount (per unit time) of the incinerated material A becomes large, the inside of the furnace 1 becomes brighter than usual, and the brightness detection sensor 1
The output of 4-1 becomes large. When the brightness inside the furnace 1 becomes large, the controller 13 opens the control valve 7 and opens the air chamber 6
A part of the amount of air blown from is bypassed and blown into the upper space of the fluidized bed 2 from the air nozzle 8 through the pipe 16.

【0021】これにより、エアチャンバー6から流動床
2に送り込まれる空気量が減少するから、流動床2の流
動媒体の流動が緩慢となり、流動媒体から焼却物Aへの
伝熱量が減り焼却物Aのガス化速度が遅くなる。即ち燃
焼速度が遅くなる。この時、エアーチャンバー6からの
空気量を減らすことで、流動床2の酸素量は減少し、そ
の分未燃ガスが増えるが、空気ノズル8から吹き込む空
気量を増大させることで、フリーボード部9等の流動床
2の上部空間でのこの未燃ガスは燃焼することになる。
As a result, the amount of air sent from the air chamber 6 to the fluidized bed 2 is reduced, the flow of the fluidized medium in the fluidized bed 2 is slowed, the amount of heat transferred from the fluidized medium to the incinerated material A is reduced, and the incinerated material A is reduced. The gasification rate of is slowed. That is, the burning speed becomes slow. At this time, by reducing the amount of air from the air chamber 6, the amount of oxygen in the fluidized bed 2 is reduced, and unburned gas is increased accordingly. However, by increasing the amount of air blown from the air nozzle 8, the freeboard portion is increased. This unburned gas in the upper space of the fluidized bed 2, such as 9, will burn.

【0022】流動床焼却炉においては、燃焼量と炉内圧
力は図1の(C)に示すように、密接な関係がある。即
ち、燃焼量が増大すれば炉内圧が高くなり、燃焼量が減
少すれば炉内圧が低くなる。図3は燃焼物の燃焼量を炉
1内の圧力を検出して燃焼制御を行なう流動床焼却炉の
概略構成を示す図である。図3において、図2と同一符
号を付した部分は同一又は相当部分を示す。図示するよ
うに、流動床2の上部に炉1内の圧力を検出する圧力検
出センサ14−2を設け、該圧力検出センサ14−2の
出力を調節器13に入力している。
In the fluidized bed incinerator, the combustion amount and the in-furnace pressure have a close relationship as shown in FIG. 1 (C). That is, as the combustion amount increases, the furnace pressure increases, and when the combustion amount decreases, the furnace pressure decreases. FIG. 3 is a diagram showing a schematic configuration of a fluidized bed incinerator that performs combustion control by detecting the combustion amount of combustion products by detecting the pressure in the furnace 1. In FIG. 3, the same reference numerals as those in FIG. 2 indicate the same or corresponding portions. As shown in the figure, a pressure detection sensor 14-2 that detects the pressure inside the furnace 1 is provided above the fluidized bed 2, and the output of the pressure detection sensor 14-2 is input to the controller 13.

【0023】上記流動床焼却炉において、炉1内に投入
された焼却物Aの量が多い場合は、焼却物Aの燃焼量
(単位時間当り)が多くなるから、排ガスの発生量が増
大して、炉1の内圧は図1(C)からも分かるように高
くなり、圧力検出センサ14−2の出力も大きくなる。
この炉1の内圧が大きくなると調節器13は制御弁7を
開放して、空気ノズル8から流動床2の上部空間に吹き
込む空気量を増大させる。これによる作用は上記図2の
場合と同一であるから説明は省略する。
In the above fluidized bed incinerator, when the amount of the incinerated material A put in the furnace 1 is large, the combustion amount of the incinerated material A (per unit time) is large, so that the amount of exhaust gas generated is increased. Then, as can be seen from FIG. 1C, the internal pressure of the furnace 1 becomes high, and the output of the pressure detection sensor 14-2 also becomes large.
When the internal pressure of the furnace 1 increases, the controller 13 opens the control valve 7 to increase the amount of air blown from the air nozzle 8 into the upper space of the fluidized bed 2. The operation by this is the same as in the case of FIG.

【0024】上記図2、図3に示す流動床焼却炉の例で
は炉1の焼却物の燃焼量を明るさ検出センサ14−1、
圧力検出センサ14−2で検出し、制御する例である
が、それ以外に図4に示すように、明るさ検出センサ1
4−1の出力値PVO1を符号aを付した演算器YO1によ
り、例えば明るさの信号に対して係数k(0〜2.0)
を乗ずることにより明るさに比例した出力信号yO1で制
御弁7の開度調整を行なう方法もある。
In the example of the fluidized bed incinerator shown in FIGS. 2 and 3, the brightness detection sensor 14-1, which detects the combustion amount of the incinerator in the furnace 1,
This is an example in which the pressure detection sensor 14-2 detects and controls, but other than that, as shown in FIG.
The output value PV O1 of 4-1 is given by a calculator Y O1 to which a symbol a is added, for example, a coefficient k (0 to 2.0) for the brightness signal.
There is also a method in which the opening of the control valve 7 is adjusted by multiplying by the output signal y O1 proportional to the brightness.

【0025】この場合都市ゴミ等の焼却物が炉内に連続
的に供給されている場合は問題はないが、都市ゴミの性
質上絡みつきによる所謂「ドカ落ち」により大量のゴミ
が投入され、急激な燃焼による煙等が発生し、燃焼が盛
んになったにもかかわらず炉内が暗くなったりし、明る
さ検出センサ14−1から燃焼が不活発であるという誤
った信号を出力し、制御弁7の開度調整に不調を来すこ
とがある。
In this case, there is no problem when the incinerated materials such as municipal waste are continuously supplied into the furnace, but due to the nature of the municipal waste, a large amount of garbage is thrown in due to the so-called "falling shavings" due to entanglement, and sudden Smoke etc. generated due to various combustion, the inside of the furnace gets dark even though combustion is active, and the brightness detection sensor 14-1 outputs an erroneous signal indicating that combustion is inactive, and controls The opening degree of the valve 7 may be out of order.

【0026】上記問題を解決するため、燃焼が盛んにな
った際、炉内圧力が上昇する傾向にあるので、図5に示
すように明るさ検出センサ14−1と圧力検出センサ1
4−2を組み合わせ、符号bを付した演算器YO2により
炉内圧力に対応する圧力検出センサ14−2の出力値P
O2がある設定値以上になったら、いままで最小開度で
あった制御弁7の開度を一定開度まで開放するような出
力信号yO2を出力する。ここで炉内圧力は通常制御され
ているので、直ちに低下し設定値以下となる。圧力検出
センサ14−2の出力信号値PVO2が低下し、ある設定
値以下が所定時間継続したならば、制御弁への最小開度
の出力信号値yO2を出力する。出力信号値yO1とyO2
符号cを付した演算器YO3により比較され、大きな値の
信号値を出力信号値yO3として出力し、制御弁7は出力
信号yO3により開度調整される。このような制御を行な
うことにより、煙等が発生し、炉1内が暗くなった場合
でも制御弁7が一定開度に開放され有効に働くので、望
ましい燃焼制御が可能となる。
In order to solve the above problem, the pressure in the furnace tends to rise when combustion becomes vigorous, so that the brightness detection sensor 14-1 and the pressure detection sensor 1 as shown in FIG.
The output value P of the pressure detection sensor 14-2 corresponding to the pressure in the furnace is calculated by the calculator Y O2 having a combination of 4-2 and the symbol b.
When V O2 exceeds a certain set value, an output signal y O2 is output to open the opening of the control valve 7 which has been the minimum opening until now to a fixed opening. Since the pressure inside the furnace is normally controlled here, it immediately drops and falls below the set value. When the output signal value PV O2 of the pressure detection sensor 14-2 decreases and remains below a certain set value for a predetermined time, the output signal value y O2 of the minimum opening to the control valve is output. The output signal values y O1 and y O2 are compared by the computing unit Y O3 with the reference sign c, and a large signal value is output as the output signal value y O3 , and the opening of the control valve 7 is adjusted by the output signal y O3. It By performing such control, even if smoke or the like is generated and the inside of the furnace 1 becomes dark, the control valve 7 is opened to a constant opening and works effectively, so that desirable combustion control is possible.

【0027】なお、上記実施例では明るさ検出センサ1
4−1の出力で炉1内の燃焼量を検出し、エアチャンバ
ー6から流動床2に送り込む空気量を制御弁7を介して
制御する例を示したが、本発明の燃焼量検出装置は、炉
1内の明るさを検出し、燃焼量を瞬時に検出できるか
ら、該燃焼量検出装置は上記燃焼制御に限定されるもの
ではなく、流動床焼却炉の炉1内の燃焼量を瞬時に検出
したデータを必要とする制御には有効に利用できること
は当然である。
In the above embodiment, the brightness detection sensor 1
An example in which the amount of combustion in the furnace 1 is detected by the output of 4-1 and the amount of air sent from the air chamber 6 to the fluidized bed 2 is controlled via the control valve 7 has been shown. Since the brightness in the furnace 1 can be detected and the combustion amount can be instantaneously detected, the combustion amount detection device is not limited to the above combustion control, and the combustion amount in the furnace 1 of the fluidized bed incinerator can be instantaneously detected. Naturally, it can be effectively used for the control that requires the data detected in the above.

【0028】また、明るさ検出センサ14−1は1個に
限定されるものではなく、炉1内の適当な箇所に複数個
設け、その中から何らかの基準、例えば最も大きい出力
のものを1つ選択するようにすることにより、より精度
のよい燃焼量を検出することが可能となる。
The number of brightness detection sensors 14-1 is not limited to one, but a plurality of brightness detection sensors 14-1 may be provided at appropriate locations in the furnace 1, and one of them may be one of the criteria, for example, one having the highest output. By making the selection, it becomes possible to detect the combustion amount with higher accuracy.

【0029】また、上記実施例では炉内の明るさを検出
する明るさ検出手段の他に炉内の圧力を検出する炉内圧
力検出手段を用いる例を示したが、明るさ検出手段以外
の燃焼量検出する手段としてはこれに限定されるもので
はなく、排ガス中の酸素濃度を検出する排ガス中酸素濃
度検出手段、炉内に投入される焼却物の性状や形状や嵩
及び量を検出する検出手段を設け、これら明るさ検出手
段及び排ガス中酸素濃度、炉内に投入される焼却物の性
状や形状や嵩及び量を検出する検出手段のうちいずれか
大きい方で炉内の燃焼量を検出するようにしても良いこ
とは当然である。
Further, in the above embodiment, an example in which the furnace pressure detecting means for detecting the pressure in the furnace is used in addition to the brightness detecting means for detecting the brightness in the furnace has been shown. The means for detecting the amount of combustion is not limited to this, but the means for detecting the oxygen concentration in the exhaust gas for detecting the oxygen concentration in the exhaust gas, and the properties, shape, volume and amount of the incineration material thrown into the furnace are detected. A detection means is provided, and the combustion amount in the furnace is determined by the greater of the brightness detection means, the oxygen concentration in the exhaust gas, and the detection means for detecting the property, shape, volume, and amount of the incinerator put into the furnace. Of course, it may be detected.

【0030】[0030]

【発明の効果】以上説明したように、本発明によれば下
記のような優れた効果が得られる。 (1)流動床に焼却物が投入され、該焼却物が流動床で
ガス化され、該ガスが燃焼して発生する火炎による炉内
の明るさを検出するので、炉内の燃焼量、即ち燃焼量を
瞬時に正確に測定することができる。
As described above, according to the present invention, the following excellent effects can be obtained. (1) The incinerated matter is put into the fluidized bed, the incinerated matter is gasified in the fluidized bed, and the brightness in the furnace due to the flame generated by the combustion of the gas is detected. The amount of combustion can be measured instantaneously and accurately.

【0031】(2)炉内の明るさを検出する明るさ検出
手段の他に炉内の圧力を検出する圧力検出手段を設け、
明るさ検出手段及び圧力検出手段の出力のうちいずれか
大きい方で炉内の燃焼量を検出することにより、例えば
炉内に煙が発生し暗くなり、明るさ検出手段が正確な燃
焼量を検出できない場合でも、圧力検出手段はそれを補
う作用を奏する。
(2) In addition to the brightness detecting means for detecting the brightness in the furnace, a pressure detecting means for detecting the pressure in the furnace is provided.
By detecting the combustion amount in the furnace by the larger one of the outputs of the brightness detection means and the pressure detection means, for example, smoke is generated in the furnace and it becomes dark, and the brightness detection means detects the accurate combustion amount. Even if it is not possible, the pressure detecting means has a function of compensating for it.

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

【図1】流動床焼却炉における炉内の明るさL、排ガス
中の酸素濃度E、炉内圧力Pの関係を示す図である。
FIG. 1 is a diagram showing a relationship among a brightness L in a furnace, an oxygen concentration E in exhaust gas, and a furnace pressure P in a fluidized bed incinerator.

【図2】本発明の燃焼量検出装置を取り付けて燃焼制御
を行なう流動床焼却炉の概略構成を示す図である。
FIG. 2 is a diagram showing a schematic configuration of a fluidized bed incinerator in which a combustion amount detection device of the present invention is attached to perform combustion control.

【図3】燃焼物の燃焼量を炉内の圧力を検出して燃焼制
御を行う流動床焼却炉の概略構成を示す図である。
FIG. 3 is a diagram showing a schematic configuration of a fluidized bed incinerator that performs combustion control by detecting the combustion amount of combustion products by detecting the pressure inside the furnace.

【図4】本発明の燃焼量検出装置の構成例を示す図であ
る。
FIG. 4 is a diagram showing a configuration example of a combustion amount detection device of the present invention.

【図5】本発明の燃焼量検出装置の構成例を示す図であ
る。
FIG. 5 is a diagram showing a configuration example of a combustion amount detection device of the present invention.

【符号の説明】[Explanation of symbols]

1 炉 2 流動床 5 配管 6 エアチャンバー 7 制御弁 8 空気ノズル 9 フリーボード 11 焼却物投入ホッパー 12 供給フィーダ 13 調節器 14−1 明るさ検出センサ 14−2 圧力検出センサ 16 配管 18 二次空気送入配管 1 Furnace 2 Fluidized Bed 5 Piping 6 Air Chamber 7 Control Valve 8 Air Nozzle 9 Freeboard 11 Incinerator Input Hopper 12 Supply Feeder 13 Regulator 14-1 Brightness Detection Sensor 14-2 Pressure Detection Sensor 16 Piping 18 Secondary Air Delivery Inlet piping

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 流動床下部から送り込む空気により流動
媒体を流動させ、炉内に投入される焼却物を燃焼させる
流動床炉の炉内の燃焼量を検出する燃焼量検出装置であ
って、 炉内の明るさを検出する明るさ検出手段を設け、該明る
さ検出手段の出力から炉内の焼却物の燃焼量を検出する
ことを特徴とする流動床炉の燃焼量検出装置。
1. A combustion amount detecting device for detecting a combustion amount in a furnace of a fluidized bed furnace in which a fluidized medium is made to flow by air fed from a lower part of the fluidized bed to combust an incinerated substance put into the furnace. A combustion amount detection device for a fluidized bed furnace, comprising brightness detection means for detecting the brightness of the inside, and detecting the combustion quantity of the incinerator in the furnace from the output of the brightness detection means.
【請求項2】 前記明るさ検出手段は炉の横断面全面が
見渡せる位置に設けたことを特徴とする請求項1に記載
の流動床炉の燃焼量検出装置。
2. The combustion amount detecting device for a fluidized bed furnace according to claim 1, wherein the brightness detecting means is provided at a position overlooking the entire cross section of the furnace.
【請求項3】 前記明るさ検出手段は流動媒体や炉壁等
による明るさに影響されない位置に設けたことを特徴と
する請求項1に記載の流動床炉の燃焼量検出装置。
3. The combustion amount detecting device for a fluidized bed furnace according to claim 1, wherein the brightness detecting means is provided at a position that is not affected by the brightness due to the fluid medium or the furnace wall.
【請求項4】 前記明るさ検出手段炉は頂又は炉頂近傍
に設けたことを特徴とする請求項1に記載の流動床炉の
燃焼量検出装置。
4. The combustion amount detecting apparatus for a fluidized bed furnace according to claim 1, wherein the brightness detecting means furnace is provided at or near the top of the furnace.
【請求項5】 前記明るさ検出手段を二次空気吹き込み
位置より上方に設けたことを特徴とする請求項1に記載
の流動床炉の燃焼量検出装置。
5. The combustion amount detecting device for a fluidized bed furnace according to claim 1, wherein the brightness detecting means is provided above a secondary air blowing position.
【請求項6】 流動床下部から送り込む空気により流動
媒体を流動させ、炉内に投入される焼却物を燃焼させる
流動床炉の炉内の燃焼量を検出する燃焼量検出装置であ
って、 炉内の明さを検出する明るさ検出手段及び排ガス中酸素
濃度、炉内圧力、炉内に投入される焼却物の性状や形状
や嵩及び量を検出する検出手段を設け、該明るさ検出手
段及び排ガス中酸素濃度、炉内圧力、炉内に投入される
焼却物の性状や形状や嵩及び量を検出する検出手段のう
ちいずれか大きい方で炉内の燃焼量を検出することを特
徴とする流動床炉の燃焼量検出装置。
6. A combustion amount detecting device for detecting a combustion amount in a furnace of a fluidized bed furnace in which a fluidized medium is made to flow by air fed from a lower part of the fluidized bed to combust an incinerated substance put in the furnace. The brightness detection means for detecting the brightness in the interior and the detection means for detecting the oxygen concentration in the exhaust gas, the pressure in the furnace, and the property, shape, volume and amount of the incineration material thrown into the furnace are provided. And a detection means for detecting the oxygen concentration in the exhaust gas, the pressure in the furnace, and the property, shape, volume and amount of the incinerator that is put into the furnace, whichever is larger. Combustion amount detection device for fluidized bed furnace.
【請求項7】 前記請求項1乃至6に記載のいずれか1
つに記載の燃焼量検出装置の出力を流動床炉の燃焼制御
装置の制御信号として用いることを特徴とする流動床炉
の燃焼制御装置。
7. Any one of claims 1 to 6
A combustion control device for a fluidized bed furnace, wherein the output of the combustion amount detection device according to item 1 is used as a control signal for the combustion control device for the fluidized bed furnace.
JP5200058A 1987-05-01 1993-07-19 Combustion amount detecting device and combustion control device for fluidized bed type furnace Pending JPH0642726A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5200058A JPH0642726A (en) 1987-05-01 1993-07-19 Combustion amount detecting device and combustion control device for fluidized bed type furnace

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP10955287 1987-05-01
JP62-109552 1987-05-01
JP5200058A JPH0642726A (en) 1987-05-01 1993-07-19 Combustion amount detecting device and combustion control device for fluidized bed type furnace

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP63503613A Division JPH0689883B1 (en) 1987-05-01 1988-04-30

Publications (1)

Publication Number Publication Date
JPH0642726A true JPH0642726A (en) 1994-02-18

Family

ID=26449288

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5200058A Pending JPH0642726A (en) 1987-05-01 1993-07-19 Combustion amount detecting device and combustion control device for fluidized bed type furnace

Country Status (1)

Country Link
JP (1) JPH0642726A (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS567915A (en) * 1979-07-02 1981-01-27 Kubota Ltd Combustion control of incinerator
JPS5623630A (en) * 1979-08-02 1981-03-06 Babcock Hitachi Kk Diagnostic method for flame in combustion device
JPS5952105A (en) * 1982-09-20 1984-03-26 Babcock Hitachi Kk Operation of fluidized bed type combustion furnace
JPS59107111A (en) * 1982-12-09 1984-06-21 Ebara Corp Fluidized-bed type incinerating method of refuse
JPS6021622Y2 (en) * 1979-07-23 1985-06-27 石川島播磨重工業株式会社 Fluidized bed incinerator operation control device
JPS60149877A (en) * 1984-01-17 1985-08-07 川崎製鉄株式会社 Method of operating fluidized-bed reactor for reducing chromium ore
JPS6183819A (en) * 1984-09-29 1986-04-28 Mitsubishi Heavy Ind Ltd Burning control of refuse incinerator

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS567915A (en) * 1979-07-02 1981-01-27 Kubota Ltd Combustion control of incinerator
JPS6021622Y2 (en) * 1979-07-23 1985-06-27 石川島播磨重工業株式会社 Fluidized bed incinerator operation control device
JPS5623630A (en) * 1979-08-02 1981-03-06 Babcock Hitachi Kk Diagnostic method for flame in combustion device
JPS5952105A (en) * 1982-09-20 1984-03-26 Babcock Hitachi Kk Operation of fluidized bed type combustion furnace
JPS59107111A (en) * 1982-12-09 1984-06-21 Ebara Corp Fluidized-bed type incinerating method of refuse
JPS60149877A (en) * 1984-01-17 1985-08-07 川崎製鉄株式会社 Method of operating fluidized-bed reactor for reducing chromium ore
JPS6183819A (en) * 1984-09-29 1986-04-28 Mitsubishi Heavy Ind Ltd Burning control of refuse incinerator

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