[go: up one dir, main page]

JPS59197712A - Nox controller for incinerator - Google Patents

Nox controller for incinerator

Info

Publication number
JPS59197712A
JPS59197712A JP7268383A JP7268383A JPS59197712A JP S59197712 A JPS59197712 A JP S59197712A JP 7268383 A JP7268383 A JP 7268383A JP 7268383 A JP7268383 A JP 7268383A JP S59197712 A JPS59197712 A JP S59197712A
Authority
JP
Japan
Prior art keywords
nox
burner
bias ratio
value
combustion
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
JP7268383A
Other languages
Japanese (ja)
Inventor
Masataka Yamaguchi
正隆 山口
Nobuo Shimada
島田 信雄
Norio Sato
則夫 佐藤
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.)
Toyota Motor Corp
Original Assignee
Toyota Motor 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 Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP7268383A priority Critical patent/JPS59197712A/en
Publication of JPS59197712A publication Critical patent/JPS59197712A/en
Pending legal-status Critical Current

Links

Landscapes

  • Regulation And Control Of Combustion (AREA)

Abstract

PURPOSE:To suppress the value of NOX contained in a waste gas to a defined value range in the entire region of a combustion load by controlling the bias ratio between respective burners responsive to the combustion state. CONSTITUTION:An adjusting operator 8 is set to store beforehand an NOX exhaustion defined value 9, and compares a flow quantity signal 17 from a fuel meter 15 and an NOX signal 6 from an NOX meter 4 with the NOX exhaustion defined value 9. The adjusting operator 8 further determines the bias ratio between respective burners so that the NOX value within the waste gas assumes a value which is less than the NOX exhaustion defined value 9, so as to set the opening degrees of bias ratio control valves 16a, 16b and 16c to the bias ratio.

Description

【発明の詳細な説明】 本発明は、複数のバーナを備えた燃焼炉のNOx制御装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a NOx control device for a combustion furnace equipped with a plurality of burners.

ボイラー等に使用している燃焼炉の廃ガス中の窒素酸化
物(NOx )は、公害対策」−できる限り抑制するこ
とが重重しい。ところで、燃焼炉のなかには複数のバー
ナを備え、燃焼負荷に応じて燃焼バーナの数を切替える
ようにしたものがあるが、従来この複数のバーナを備え
た燃焼炉においては前記NOxを抑制する方法として、
各バーナに供給する燃料の分配比即ちバイアス比を変え
ることにより燃料リッチ炎のバーナと空気リッチ炎のバ
ーナとを形成し、これによってNOxの発生を規制値以
下となるように抑制していた。このようなNOx抑制効
果はバイアス比を変えることによって変化することが知
られているが、従来の燃焼炉においてはバーナの初期燃
焼調整時にバイアス比を固定的に設定しておリ、燃焼の
変化或は燃料中の窒素(N)分の変化によるNOxの変
化に充分対応することができず、残存酸素濃度の高い過
剰燃焼、規制値以上の高濃度のNOxの排出などを招来
し、公害防止や省エネルギ一対策の点で未だ問題があっ
た。
It is important to suppress nitrogen oxides (NOx) in the waste gas from combustion furnaces used in boilers and the like as much as possible as a pollution control measure. By the way, some combustion furnaces are equipped with a plurality of burners, and the number of combustion burners is changed according to the combustion load. Conventionally, in combustion furnaces equipped with a plurality of burners, there is a method for suppressing the NOx. ,
By changing the distribution ratio, that is, the bias ratio, of the fuel supplied to each burner, a burner with a fuel-rich flame and a burner with an air-rich flame are formed, thereby suppressing the generation of NOx to below a regulation value. It is known that this NOx suppression effect changes by changing the bias ratio, but in conventional combustion furnaces, the bias ratio is fixed at the time of initial combustion adjustment of the burner. Alternatively, changes in NOx due to changes in the nitrogen (N) content in the fuel cannot be adequately addressed, leading to excessive combustion with high residual oxygen concentrations and the emission of NOx at concentrations higher than the regulation value, making it difficult to prevent pollution. There were still problems in terms of energy conservation and energy conservation measures.

本発明は、特許請求の範囲に記載した構成のNOx制御
装置により上述問題を解決したもので、各バーナ間のバ
イアス比を燃焼状態に応じてコントロールするととによ
り廃ガス中のNOx値を燃焼負荷の全領域において規制
値内に抑えることのできる燃焼炉のNOx制御装置を提
供するものである。
The present invention solves the above-mentioned problems by using a NOx control device having the structure described in the claims.The present invention is an attempt to solve the above-mentioned problems by controlling the bias ratio between each burner according to the combustion state, thereby controlling the NOx value in the exhaust gas under the combustion load. The purpose of the present invention is to provide a combustion furnace NOx control device that can suppress NOx within the regulation value in the entire range.

以下、図面に基づき本発明の詳細な説明する。Hereinafter, the present invention will be described in detail based on the drawings.

第1図及び第2図は本発明を3本のバーナを備えた燃焼
炉に適用した場合の1例を示し、1は3本のバーナ2a
、2b、2cを備えた燃焼炉の本体であシ、該燃焼炉1
の廃ガス経路3途中には廃ガス中のNOx!度を測定す
るNOx計4と02c度を測定する02計5とを設け、
該NOx信号6と02信号7を調節演算器8へ入力して
いる。
FIG. 1 and FIG. 2 show an example in which the present invention is applied to a combustion furnace equipped with three burners.
, 2b, 2c, the combustion furnace 1
NOx in the waste gas! A NOx meter 4 for measuring the degree of NOx and a total of 5 for measuring the degree of 02C are installed.
The NOx signal 6 and the 02 signal 7 are input to the adjustment calculator 8.

他方、燃焼炉1のバーナボックス10に−は燃料供給系
11と空気供給系12とが取付けられている。燃料供給
系11には、噴射ポンプ13゜主燃料制御弁14.燃料
流量計15が設けられていると共に、該流量計15の下
流側経路は三分岐され、バイアス比コン゛トロール弁1
6 a 。
On the other hand, a fuel supply system 11 and an air supply system 12 are attached to the burner box 10 of the combustion furnace 1. The fuel supply system 11 includes an injection pump 13 and a main fuel control valve 14 . A fuel flow meter 15 is provided, and the downstream path of the flow meter 15 is branched into three, with a bias ratio control valve 1
6 a.

16b、16cの合弁を介してバーナ2a、2b、2c
へ接続されている。そして、前記燃料流量計15の流量
信号17は調節演算器8へ入力され、また調節演算器8
からはバイアス比コントロール信号18,19.20が
パイナス比コントロール弁16a、16b、16cへ入
力されている。
Burner 2a, 2b, 2c through joint venture of 16b, 16c
connected to. Then, the flow rate signal 17 of the fuel flow meter 15 is inputted to the adjustment calculator 8.
From there, bias ratio control signals 18, 19, and 20 are input to the negative ratio control valves 16a, 16b, and 16c.

調節演算器8は、NOx排出規制値9を予め記憶設定さ
れており、燃料流量計15からの流量信号17と、N0
xit4からのNOx信号6と、NOx排出規制値9と
を比較し、廃ガス中のNOx値が前記NOx排出規制値
9以下となるような各バーナ間のバイアス比を決定し、
バイアス比コントロール弁16 a 、 1.6 b 
、 16 cの開度を該バイアス比に設定するものであ
る。なお、第1図中性号21は煙突である。
The adjustment calculator 8 has the NOx emission regulation value 9 stored in advance, and receives the flow rate signal 17 from the fuel flow meter 15 and the NOx emission regulation value 9.
Compare the NOx signal 6 from the xit 4 and the NOx emission regulation value 9, and determine the bias ratio between each burner such that the NOx value in the waste gas is equal to or less than the NOx emission regulation value 9,
Bias ratio control valve 16a, 1.6b
, 16c is set to the bias ratio. Note that the neutral number 21 in Figure 1 is a chimney.

本発明は上記構成になるものであって、燃焼炉1の燃焼
負荷に応じ主燃料制御弁14の開度を調整し、燃料供給
系11から重油等の燃料を供給すると共に、空気供給系
12から空気を供給し、燃焼を行なう。
The present invention has the above configuration, in which the opening degree of the main fuel control valve 14 is adjusted according to the combustion load of the combustion furnace 1, fuel such as heavy oil is supplied from the fuel supply system 11, and the air supply system 12 is supplied with fuel such as heavy oil. Air is supplied from the combustion chamber to carry out combustion.

この時、燃料流量計15は燃料供給系11を流れる燃料
流量を検出し、これを流量信号1.7として調節演算器
8へ送る。まだ、NOx計4及び02計5は廃ガス経路
3を流れる廃ガス中のNOx値と02値を検出し、とれ
をNOx信号6及び02信号7として調節演算器8へ送
る。
At this time, the fuel flow meter 15 detects the fuel flow rate flowing through the fuel supply system 11 and sends this to the adjustment calculator 8 as a flow rate signal 1.7. Still, the NOx meter 4 and the 02 meter 5 detect the NOx value and the 02 value in the waste gas flowing through the waste gas path 3, and send the values as the NOx signal 6 and the 02 signal 7 to the adjustment calculator 8.

調節演算器8は、第3図に例示するように、燃料流量(
燃焼負荷)の犬Jhに応じて1本バーナ使用域、2本バ
ーナ使用域、3本バーナ使用域が予め設定されており、
例えば、1本バーナ使用域の燃料流量の場合にはバーナ
2b1本のみを用いて燃焼し、2本バーナ使用域の燃ネ
4流量の場合にはバニナ2b、2cの2本を用いて燃焼
し、3本バーナ使用域の場合にはバーナ2a、2b、2
cの全部を用いて燃焼するよう設定されている。そして
、このそれぞれの使用域において、NOx計4の検出す
るNOx値とNOx排量規制値9とを比較しながら、以
下に述べるようにして、廃ガス中のNOx値がNOx排
出規制値9を超えることのないように各バーナ間のバイ
アス比を決定し、それぞれのバーナ開度を該バイアス比
に設定するものである。
The adjustment calculator 8, as illustrated in FIG.
One burner usage range, two burner usage range, and three burner usage range are preset according to the dog Jh of combustion load).
For example, if the fuel flow rate is in the one-burner usage range, only one burner 2b is used for combustion, and if the two-burner usage range is four fuel flows, two burners 2b and 2c are used for combustion. , burners 2a, 2b, 2 in the case of a three-burner usage area.
It is set to burn using all of c. Then, in each usage area, while comparing the NOx value detected by the NOx meter 4 and the NOx emission regulation value 9, it is determined that the NOx value in the waste gas exceeds the NOx emission regulation value 9 as described below. The bias ratio between each burner is determined so as not to exceed the bias ratio, and the opening degree of each burner is set to the bias ratio.

1例として、3本バーナ使用域の燃料流量の場合のバイ
アス比の決定の仕方について述べる。
As an example, a method of determining the bias ratio in the case of a fuel flow rate in a three-burner usage range will be described.

調節演算器8は燃料流量計15からの流量信号1γを受
け、3本バーナ使用域の燃料流量と判断する。そして、
調節演算器8はまず第15階トシテ、バイアス比コント
ロール弁16 a 。
The adjustment calculator 8 receives the flow rate signal 1γ from the fuel flow meter 15 and determines that the fuel flow rate is in the three burner usage range. and,
The adjustment calculator 8 is first located on the 15th floor, the bias ratio control valve 16a.

16b、16cの開度をバイアス比コントロール信号1
8,19.20を通じて3本バーナ使用域における予め
与えられた基準バイアス比にセットする。いまとの基準
バイアス比を40=30:30とすると、バイアス比コ
ントロールル弁16 bを3 (J%HK、バイアス比
コントロール弁16cを30%開度に設定し、該バイア
ス比で各バーナ2a、2b、2cがら燃料を噴射して燃
焼させる。次いで、第2段階として、バーナ2bの開度
を前記30%開度に固定し、この状態において、NOx
計4で検出するNOx値とNOx排出規制値9とを比較
しながら廃ガス中のNOx値が前記NOx排出規制値9
以下となるように他のバーナ2a、2cのバイアス比を
調節する。この調節の結果、バーナ2a:バーナ2C−
45:20のバイアス比を得たとする。次いて、第3段
階として、バーナ2cのバイアス比を前記第2段階で得
られた20%開度に固定し、この状態において、NOx
計4で検出するNOx値と 會NOx排出規制値9とを
比較しながら廃ガス中のNOx値が前記NOx排出規制
値9以下となるように他のバーナ2a、2bのバイアス
比を調節する。この調節の結果、バーナ2a:バーナ2
b=55:25のバイアス比を得たとする。
Bias ratio control signal 1 controls the opening degrees of 16b and 16c.
8, 19. Set to a pre-given reference bias ratio in the three burner usage range through 20. If the current reference bias ratio is 40 = 30:30, the bias ratio control valve 16b is set to 3 (J%HK), the bias ratio control valve 16c is set to 30% opening, and each burner 2a is opened at this bias ratio. , 2b, 2c and burns the fuel.Next, in the second stage, the opening degree of the burner 2b is fixed at the 30% opening degree, and in this state, NOx
While comparing the NOx value detected in Total 4 with the NOx emission regulation value 9, the NOx value in the waste gas is determined to be the NOx emission regulation value 9.
The bias ratios of the other burners 2a and 2c are adjusted as follows. As a result of this adjustment, burner 2a: burner 2C-
Suppose we obtain a bias ratio of 45:20. Next, in the third stage, the bias ratio of the burner 2c is fixed at the 20% opening degree obtained in the second stage, and in this state, NOx
The bias ratios of the other burners 2a and 2b are adjusted so that the NOx value in the waste gas becomes less than or equal to the NOx emission regulation value 9 while comparing the NOx value detected in step 4 with the association NOx emission regulation value 9. As a result of this adjustment, burner 2a: burner 2
Assume that a bias ratio of b=55:25 is obtained.

調節演算器8は上記第3段階までの演算を実行し、該第
3段階で得られたバイアス比、即ちバーナ2a:バーナ
2b:バーナ2C=55:25:20の値を、その時の
燃料流量(燃焼負荷)において所定のNOx排出基準値
9以下のNOx一度を力える各バーナ間のバイアス比と
して決定する。そして、調節演算器8は、バーナ2aの
燃滓−1量を規制するバイアス比コントロール弁16a
に対して55%開度信号を、バーナ2bの燃料量を規制
するバイアス比コントロール弁16bに対して25φ開
度信号を、バーナ2cの燃料量を規制するバイアス比コ
ントロール弁16cに対して20%開度信号をそれぞれ
送出し、各バーナ2a、2b、2cのバイアス比を前記
最良比に設定し、燃焼を行なわせるものである。
The adjustment calculator 8 executes the calculations up to the third stage, and uses the bias ratio obtained in the third stage, that is, the value of burner 2a:burner 2b:burner 2C=55:25:20, as the fuel flow rate at that time. (combustion load) is determined as a bias ratio between each burner that outputs NOx once below a predetermined NOx emission standard value of 9. The adjustment calculator 8 also controls a bias ratio control valve 16a that regulates the amount of slag -1 in the burner 2a.
a 55% opening signal for the burner 2b, a 25φ opening signal for the bias ratio control valve 16b that regulates the fuel amount of the burner 2b, and a 20% opening signal for the bias ratio control valve 16c that regulates the fuel amount of the burner 2c. Opening signals are sent to each burner, the bias ratio of each burner 2a, 2b, and 2c is set to the above-mentioned best ratio, and combustion is performed.

調節演算器8は、上述の制御動作を燃焼炉1の燃焼状態
の変動のたびに実行し、これにより燃焼炉1の廃ガス中
のNOx濃度を常に規制値以下になるように自動的に制
御するものである。
The adjustment calculator 8 executes the above-mentioned control operation every time the combustion state of the combustion furnace 1 changes, thereby automatically controlling the NOx concentration in the waste gas of the combustion furnace 1 to always be below the regulation value. It is something to do.

なお、2本バーナ使用域の燃料流量の場合にd、前記し
た如くバーナ2b、2cのみが使用される。従って、該
2つのバーナ2b、2cのバイアス比は前記第2段階ま
での演算動作によって決定されるので、前記第3段階の
演算動作は不要となる。−!た、1本バーナ使用域の燃
料流量の場合にはバーナ2bのみが使用されるので、こ
の場合にはバーナ2bを100饅開度に設定しておけば
よく、バイアス比を決定する必要はない。以上述べた本
発明に基づく制御による燃料流量(燃焼負荷)とNOx
濃度及び02C度との関係を第3図に例示する。図中、
実線は本発明の場合を、また点線は従来のバイアス比固
定式の場合をそれぞれ示す。図示するところから明らか
なように、本発明によるときは燃料流量の全領域におい
て廃ガス中のNoXS度を規制値以下に抑制できるが、
従来のバイアス比固定式によるときは初期燃焼時にバイ
アス比を固定的に設定しだま捷であるため、燃焼状態の
変化に正確に追随できず、規制値以上のNOxが排出さ
れる。更に、本発明によるときは、燃焼状態の変化に応
じてバイアス比が制御されるため燃焼が良好となり、第
3図中に示すように廃ガス中の02(774度も低くな
り、廃ガス損失も小さくなる。
In addition, in the case of the fuel flow rate in the two-burner usage range d, only burners 2b and 2c are used as described above. Therefore, since the bias ratio of the two burners 2b and 2c is determined by the calculation operations up to the second stage, the calculation operations in the third stage are unnecessary. -! In addition, if the fuel flow rate is in the single burner usage range, only burner 2b is used, so in this case, burner 2b can be set to 100 degrees of opening, and there is no need to determine the bias ratio. . Fuel flow rate (combustion load) and NOx by control based on the present invention described above
The relationship between concentration and 02C degree is illustrated in FIG. In the figure,
The solid line shows the case of the present invention, and the dotted line shows the case of the conventional fixed bias ratio type. As is clear from the diagram, according to the present invention, the NoXS degree in the exhaust gas can be suppressed to below the regulation value in the entire fuel flow range, but
When using the conventional fixed bias ratio type, the bias ratio is fixedly set during initial combustion, which makes it impossible to accurately follow changes in combustion conditions, and NOx exceeding the regulation value is emitted. Furthermore, according to the present invention, since the bias ratio is controlled according to changes in the combustion state, combustion is improved, and as shown in FIG. will also become smaller.

なお、上述実施例においては02計5によって廃ガス中
のOza度を測定し、調節演算器8へ入力しているが、
この02et度を測定する理由は、公害関係においては
02換算によるNOx値を規制対象として採用している
ためである。例えば、ボイラー等の場合には廃ガス中の
02濃度4係換算時のNOx値を規制対象としており、
該4%換算NOx値は、次式によって計算される。
In the above embodiment, the Oza degree in the waste gas is measured by the 02 total 5 and inputted to the adjustment calculator 8.
The reason for measuring this 02et degree is that in pollution-related matters, the NOx value based on 02 conversion is adopted as a regulation target. For example, in the case of boilers, etc., the NOx value when converting the 02 concentration in waste gas to 4 factors is subject to regulation.
The 4% equivalent NOx value is calculated by the following formula.

即ち、前記調節演算器8は、NOx信号6と02信号7
から前記式によって直ちに換算NOx値を算出するもの
である。当然のことながら調節演算器8はマイクロコン
ピュータによっても構成できる。なお、02換算による
NOx値を採用しない燃焼炉の場合には、前記02計5
は不要となしうる。丑だ、上述実施例においては独立し
たバイアス比コントロール弁16a、16b、16Cを
設けた場合について示したが、バーナ2a。
That is, the adjustment calculator 8 outputs the NOx signal 6 and the 02 signal 7.
The converted NOx value is immediately calculated from the above formula. Naturally, the adjustment calculator 8 can also be constituted by a microcomputer. In addition, in the case of a combustion furnace that does not adopt the NOx value based on 02 conversion, the above 02 total 5
can be considered unnecessary. In the above embodiment, the case where independent bias ratio control valves 16a, 16b, and 16C were provided was shown, but the burner 2a.

21) 、 2 cのそれぞれに電磁開閉弁が付設され
ている場合には、該電磁開閉弁をバイアス比コントロー
ル弁として利用することができ、上述バイアス比コント
ロール弁16a、16b。
When an electromagnetic on-off valve is attached to each of 21) and 2c, the electromagnetic on-off valve can be used as a bias ratio control valve, and the above-mentioned bias ratio control valves 16a and 16b.

16cを特別に設ける必要はない。There is no need to specially provide 16c.

本発明は、以」二説明した如き構成、作用になるもので
、各バーナ間のバイアス比を燃焼状態に応じて自動的に
コントロールすることにょシ燃焼炉の燃焼の変化や燃料
中の窒素(N)分の変化等に対して廃ガス中のNOx濃
度を常に規制値以内に抑えると共に、燃焼炉内の空気バ
ランスも良好とでき、公害防止及び省エネルギーに多大
に資するという著効を奏するものである。
The present invention has the configuration and operation as explained below, and it is possible to automatically control the bias ratio between each burner according to the combustion state, and to control changes in the combustion of the combustion furnace and nitrogen (nitrogen) in the fuel. This has the remarkable effect of keeping the NOx concentration in the exhaust gas within the regulated value at all times against changes in N) and maintaining a good air balance within the combustion furnace, greatly contributing to pollution prevention and energy conservation. be.

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

第1図は本発明の1実施例の構成図、第2図は同上バー
ナ部の略示拡大図、第3図は燃料流量に対する排出NO
x濃度と排出02 e度の関係を示すグラフである。 1:燃焼炉、2a、2b、2c:バーナ、3:廃ガス経
路、4 : NOx計、5:02計、6 : NOx信
号、7:02信号、8:調節演算器、9 : NOx排
出基準値、11:燃料供給系、12:空気供給系、14
:主燃料制御弁、15:燃料流量計、16a、16b、
16c:バイアス比’j7トロール弁、17:流量信号
、18,19,20:ハイアス比コントロール信号。
Fig. 1 is a configuration diagram of one embodiment of the present invention, Fig. 2 is a schematic enlarged view of the same burner section, and Fig. 3 is a diagram showing the exhaust NO in relation to the fuel flow rate.
It is a graph showing the relationship between x concentration and discharge 02 e degree. 1: Combustion furnace, 2a, 2b, 2c: Burner, 3: Waste gas path, 4: NOx meter, 5: 02 meter, 6: NOx signal, 7: 02 signal, 8: Adjustment calculator, 9: NOx emission standard Value, 11: Fuel supply system, 12: Air supply system, 14
: Main fuel control valve, 15: Fuel flow meter, 16a, 16b,
16c: Bias ratio 'j7 troll valve, 17: Flow rate signal, 18, 19, 20: High ass ratio control signal.

Claims (1)

【特許請求の範囲】[Claims] 複数のバーナを備えだ燃焼炉において、燃焼炉に供給さ
れる燃料流量を測定する燃料流量計と、廃ガス中のNO
x値を測定するNOx計と、予め装置内に記憶設定され
たNOx排出規制値と前記測定された燃料流量とNOx
値とを比較し、廃ガス中のNOx値が前記NOx排出規
制値以下となるように各バーナー間のバイアス比を決定
し、各バーナの燃料流量比を該バイアス比に設定する調
節演算器とを設けたことを特徴とする燃焼炉のNOx制
御装置。
In a combustion furnace equipped with multiple burners, there is a fuel flow meter that measures the fuel flow rate supplied to the combustion furnace, and a fuel flow meter that measures the NO in the waste gas.
A NOx meter that measures x value, NOx emission regulation value stored in advance in the device, the measured fuel flow rate, and NOx
an adjustment calculator that compares the values with the values, determines a bias ratio between each burner so that the NOx value in the waste gas is equal to or less than the NOx emission regulation value, and sets the fuel flow rate ratio of each burner to the bias ratio; A NOx control device for a combustion furnace, characterized in that it is provided with:
JP7268383A 1983-04-25 1983-04-25 Nox controller for incinerator Pending JPS59197712A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7268383A JPS59197712A (en) 1983-04-25 1983-04-25 Nox controller for incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7268383A JPS59197712A (en) 1983-04-25 1983-04-25 Nox controller for incinerator

Publications (1)

Publication Number Publication Date
JPS59197712A true JPS59197712A (en) 1984-11-09

Family

ID=13496417

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7268383A Pending JPS59197712A (en) 1983-04-25 1983-04-25 Nox controller for incinerator

Country Status (1)

Country Link
JP (1) JPS59197712A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5538463A (en) * 1978-09-13 1980-03-17 Mitsubishi Heavy Ind Ltd Burner apparatus
JPS5666607A (en) * 1979-11-05 1981-06-05 Babcock Hitachi Kk Combustion method with low nox

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5538463A (en) * 1978-09-13 1980-03-17 Mitsubishi Heavy Ind Ltd Burner apparatus
JPS5666607A (en) * 1979-11-05 1981-06-05 Babcock Hitachi Kk Combustion method with low nox

Similar Documents

Publication Publication Date Title
US20010047650A1 (en) Method of operating a gas-turbine chamber with gaseous fuel
US7513117B2 (en) Method for operating a furnace
CA2642980C (en) Assured compliance mode of operating a combustion system
CA1240916A (en) Gas burner
US20040255831A1 (en) Combustion-based emission reduction method and system
US4531905A (en) Optimizing combustion air flow
JPH0461169B2 (en)
JPS59197712A (en) Nox controller for incinerator
JP3023948B2 (en) Sewage sludge fluidized bed incinerator
JPS58145820A (en) Method for controlling air flow rate when boiler is operated under low load
JPH06241416A (en) Gas fuel low oxygen burner and control method thereof
JPS62138607A (en) Burning equipment
JPS62276322A (en) Nitrogen oxide reducing device
JPH07280256A (en) Combustion furnace pressure control method
JPS59195029A (en) Controller of nox of burning furnace
JP4463220B2 (en) Exhaust reburning burner device
JP2622482B2 (en) Combustor
JPH0517444B2 (en)
JPS5981420A (en) Pressure controlling method of automizing medium
SU1719796A1 (en) Method of combustion automatic control
JPS6267241A (en) Control device of gas turbine
JP2675105B2 (en) Burner automatic control device
JPH0419445B2 (en)
JPH0510505A (en) Air ratio controller of burner at start-up time of boiler
JPH0220896B2 (en)