JPS5848805B2 - Natural draft heating furnace - Google Patents
Natural draft heating furnaceInfo
- Publication number
- JPS5848805B2 JPS5848805B2 JP1451778A JP1451778A JPS5848805B2 JP S5848805 B2 JPS5848805 B2 JP S5848805B2 JP 1451778 A JP1451778 A JP 1451778A JP 1451778 A JP1451778 A JP 1451778A JP S5848805 B2 JPS5848805 B2 JP S5848805B2
- Authority
- JP
- Japan
- Prior art keywords
- damper
- damper opening
- draft
- oxygen concentration
- heating furnace
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
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- Regulation And Control Of Combustion (AREA)
Description
【発明の詳細な説明】
本発明は自然通風型加熱炉に関し、特に燃焼状態を良好
かつ安全に維持すると共に燃料経済性を高めた加熱炉に
関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a natural draft heating furnace, and particularly to a heating furnace that maintains good and safe combustion conditions and improves fuel economy.
石油化学工場等で広く用いられている自然通風型加熱炉
では、バーナの空気導入口から炉内に自然通風される燃
焼用空気の供給量を排気流出口に取り付けたダンバを開
度制御して微調整している。In natural draft heating furnaces, which are widely used in petrochemical factories, etc., the amount of combustion air that is naturally ventilated into the furnace from the burner air inlet is controlled by the opening of a damper attached to the exhaust outlet. It's being fine-tuned.
この場合、炉内への空気供給量が不必要に多過ぎると燃
焼に供しない空気によって炉内が冷却されその分無駄々
加熱が行なわれるため燃費が悪化し不経済となる。In this case, if the amount of air supplied into the furnace is unnecessarily large, the inside of the furnace will be cooled by the air that is not used for combustion, and the furnace will be heated accordingly, resulting in poor fuel consumption and uneconomical performance.
即ち、燃焼用空気量は被加熱体の加熱熱量に要求される
だけの量を供給することが好ましく、このためには炉内
のドラフト圧力(通風圧力)を大気圧に近い微小な負圧
に維持し必要最小限の空気量を供給するのがよい。In other words, it is preferable to supply the amount of combustion air required for the amount of heating heat of the object to be heated, and for this purpose, the draft pressure (ventilation pressure) in the furnace must be reduced to a minute negative pressure close to atmospheric pressure. It is best to maintain and supply the minimum amount of air required.
しかし、一方にかいて、自然通風型加熱炉ではドラフト
圧力が炉内で局部的に増減することがあり必ずしも炉内
の空気量即ち酸素量に対応しないことがある。However, in a natural draft heating furnace, on the other hand, the draft pressure may locally increase or decrease within the furnace, and may not necessarily correspond to the amount of air, ie, the amount of oxygen, within the furnace.
このためドラフト圧力を大気圧に近い微小な負圧に維持
して供給空気量を最小限に抑えようとする場合、局部的
に測定されたドラフト圧力が正常値を示していても炉内
全体の酸素量は不足していて不完然燃焼を起こすことが
あり、又この後空気供給量が瞬間的に急増すると爆発的
に燃焼し加熱炉破壊に至る危険性を有している。Therefore, when trying to minimize the amount of supplied air by maintaining the draft pressure at a minute negative pressure close to atmospheric pressure, even if the locally measured draft pressure shows a normal value, the overall Insufficient amount of oxygen may cause incomplete combustion, and if the amount of air supplied increases suddenly thereafter, there is a risk of explosive combustion and destruction of the heating furnace.
したがってかかる酸素量不足時には一時的にダンパ開度
を大きくしてやる必要がある。Therefore, when the amount of oxygen is insufficient, it is necessary to temporarily increase the damper opening.
ところで、従来の自然通風型加熱炉にかけるダンパ開度
制御はドラフト圧力計を見ながら指示圧力に応じてダン
パ開度を適宜手動により制御する方式か(圧力指示メー
タは制御室にかかれ、ここで遠隔制御する場合が多い)
、又はドラフト圧力計により検出したドラフト圧力に対
応してダンパが設定開度に連動される自動制御方式等が
ある。By the way, the conventional method of controlling the opening of the damper applied to a natural draft heating furnace is to manually control the opening of the damper according to the indicated pressure while watching the draft pressure gauge (the pressure indicating meter is installed in the control room, (often controlled remotely)
Alternatively, there is an automatic control method in which a damper is linked to a set opening degree in response to draft pressure detected by a draft pressure gauge.
しかし、前者の手動制御方式は精度性に劣シ十分な燃料
経済性が満たされず、又後者は前記した炉内の一時的な
酸素不足に対処することができず安全性に問題があるた
め実際には余り使用されてい女い。However, the former manual control method has poor accuracy and does not have sufficient fuel economy, and the latter cannot deal with the above-mentioned temporary oxygen shortage in the reactor, resulting in safety problems. It's not used to much by women.
本発明に、かかる従来の欠点に鑑み為されたものでドラ
フト圧カダンパ開度、排気中酸素濃度、被加熱体の流量
及び加熱炉出入口での温度等を定時間毎に測定し、ドラ
フト圧力測定値の現測定値を含む適数回の平均値に対応
したダンバ開度に制御する高精度かつ安定性に霧れた主
制御系に加え、ドラフト圧力、ダンバ開度の異常測定値
に対して番主上記ドラフト圧力によるダンパ開度制御が
正常に行なわれないためこれを停止させ、又排気中酸素
濃度が異常に低下したときには炉内の酸素不足につなが
るためドラフト圧力にかかわシなくダンパを開動作させ
る補助制御系を備えたダンパ開度制御装置を設けた自然
通風型加熱炉を提供することを第1の目的とする。The present invention has been developed in view of these conventional drawbacks, and measures the draft pressure damper opening, the oxygen concentration in the exhaust gas, the flow rate of the heated object, the temperature at the entrance and exit of the heating furnace, etc. at regular intervals, and measures the draft pressure. In addition to a highly accurate and stable main control system that controls the damper opening corresponding to the average value of an appropriate number of times, including the current measured value, it also has a main control system that controls the damper opening according to the average value of a suitable number of times, including the current measured value. The damper opening control based on the draft pressure mentioned above is not performed normally, so it is stopped, and when the oxygen concentration in the exhaust air drops abnormally, the damper is opened regardless of the draft pressure, as this leads to a lack of oxygen in the furnace. A first object of the present invention is to provide a natural draft heating furnace equipped with a damper opening degree control device equipped with an auxiliary control system for operation.
さらに、加熱炉の熱負荷が増加中には空気供給量も増加
する必要があるためドラフト圧力が低下してもダレパを
閉じたいようにした補助制御系を上記ダンバ制御装置に
加えた自然通風型加熱炉を提供することを第2の目的と
する。Furthermore, since it is necessary to increase the air supply amount when the heat load of the heating furnace increases, we added an auxiliary control system to the damper control device to close the damper even if the draft pressure decreases. The second purpose is to provide a furnace.
以下に本発明を原油常圧蒸留装置に適用した実施例を図
面に基づいて説明する。An example in which the present invention is applied to a crude oil atmospheric distillation apparatus will be described below based on the drawings.
第1図に釦いて1は加熱炉本体であり、底部に取り付け
たバーナ2によって炉内を通過する被加熱体をその流通
管3管壁の加熱を介して一定温度に高めるようになって
いる。In Fig. 1, 1 is the heating furnace main body, and a burner 2 attached to the bottom raises the heated object passing through the furnace to a constant temperature by heating the wall of the flow pipe 3. .
流通管3の本体1人口部には流量計4及び入口部温度計
5が取り付けられ、本体1出口部には出口部温度計6が
取り付けられている。A flow meter 4 and an inlet thermometer 5 are attached to the inlet portion of the main body 1 of the flow pipe 3, and an outlet thermometer 6 is attached to the outlet portion of the main body 1.
該出口部温度計6によって測定された被加熱体の加熱後
の温度に応じてバーナ2に通じる燃料供給管Tに介装さ
れた流量制御弁8が自動的に開度制御され、被加熱体の
要求加熱熱量に応じた燃料量がバーナ2に供給されるよ
うにしてある。Depending on the temperature of the heated object measured by the outlet thermometer 6, the opening degree of the flow control valve 8 installed in the fuel supply pipe T leading to the burner 2 is automatically controlled, and the opening of the flow control valve 8 is automatically controlled. The amount of fuel is supplied to the burner 2 according to the required amount of heating heat.
本体1上部に開口された排気流出口1aには排気流量を
制御して本体1に導入される空気量を制御するためのダ
ンパ9が取り付けられている。A damper 9 for controlling the amount of air introduced into the main body 1 by controlling the exhaust flow rate is attached to the exhaust outlet 1a opened at the upper part of the main body 1.
排気流出口1aにはダンバ9の上流及び下流に夫々ドラ
フト圧力計10及び酸素濃度計11を取り付け、ダンバ
9にはその開度計12及び該ダンパ9を回転駆動させる
駆動機13を連結する。A draft pressure gauge 10 and an oxygen concentration meter 11 are attached to the exhaust outlet 1a upstream and downstream of the damper 9, respectively, and the damper 9 is connected to an opening gauge 12 thereof and a drive machine 13 for rotationally driving the damper 9.
そして、前記被加熱体の流量計4、温度計5,6及びド
ラフト圧力計10、酸素濃度計11から発せられる夫々
の測定信号をコンピュータ14に定時間毎に入力させ、
コンピュータ14は該入力信号に応じて計算されたダン
パ開度制御信号を前記駆動機13に送信してこれを駆動
させダンパ9を適当な開度に制御する。Then, the measurement signals emitted from the flow meter 4, thermometers 5, 6, draft pressure gauge 10, and oxygen concentration meter 11 of the heated body are input into the computer 14 at regular intervals,
The computer 14 transmits a damper opening degree control signal calculated according to the input signal to the driver 13 to drive it and control the damper 9 to an appropriate opening degree.
又、コンピュータ14は後述するように制御途中で各測
定値に異常を検出した時、該情報をテレビ15及びタイ
ブライタ16に送信して異常を伝達する。Further, as will be described later, when the computer 14 detects an abnormality in each measured value during control, it transmits the information to the television 15 and tie writer 16 to notify the abnormality.
かかる構成からなる燃焼制御システムの制御プログラム
を第2図によって説明する。A control program for the combustion control system having such a configuration will be explained with reference to FIG.
各測定計による測定信号は3分毎にコンピュータ14に
入力され、現測定値と前回及び前々回の測定値が入力ご
とに更新されデータ処理部にセットされる。Measurement signals from each measuring meter are input to the computer 14 every three minutes, and the current measurement value, the previous measurement value, and the measurement value before the previous measurement are updated each time they are input and set in the data processing section.
そして入力開始後2回目lではダンバ開度を現状に維持
する。Then, at the second time l after the start of input, the damper opening degree is maintained at the current level.
入力開始後3回目からの制御プログラムは以下の如く進
行する。The control program from the third time after the start of input progresses as follows.
まず酸素濃度計11の異常をチェックする。First, check for abnormalities in the oxygen concentration meter 11.
排気中酸素濃度の現測定値が3〜9%の範囲内にあるか
、又、現測定値と前回測定値との差が±1φ以内である
かどうか判別し、これらのいずれかが満たされない場合
には酸素濃度計が異常であると判定し、これをテレビ1
5及びタイブライタ16を介してモニタに通報し(以下
テレビ、タイプライタを介しての通報は“通報する“と
略記する)、後述する排気中酸素濃度測定値と目標酸素
濃度との比較は行なわすダンパ開度及びドラフト圧力の
異常を調べた上でドラフト圧力によるダンバ開度制御を
行なう。Determine whether the current measured value of the oxygen concentration in exhaust gas is within the range of 3 to 9%, and whether the difference between the current measured value and the previous measured value is within ±1φ, and if either of these is not satisfied. In this case, it is determined that the oxygen concentration meter is abnormal, and this is detected on TV 1.
5 and the typewriter 16 (hereinafter, notifications via the TV or typewriter will be abbreviated as "report"), and the measured value of the oxygen concentration in the exhaust gas and the target oxygen concentration will be compared as described below. After checking for abnormalities in the damper opening and draft pressure, the damper opening is controlled using the draft pressure.
次に、排気中酸素濃度の現測定値が例えば3.5多以下
であるかどうか判別し、3.5%以下である場合には該
測定値と目標酸素濃度との比較を行なった上でダンパ9
を例えば3%開動作(ダンハ開度はダンバ全開時の排気
流出口断面積を100条としたときの断面積割合に対応
して示す)したときの開度を算出し、該算出開度が設定
下限開度以上であるときは算出開度に、設定下限開度を
下まわるときは該下限開度にダンパ9を制御する。Next, it is determined whether the current measured value of the oxygen concentration in the exhaust gas is, for example, 3.5% or less, and if it is 3.5% or less, the measured value is compared with the target oxygen concentration. Damper 9
For example, calculate the opening when the damper is opened by 3% (the damper opening is shown corresponding to the cross-sectional area ratio when the cross-sectional area of the exhaust outlet when the damper is fully open is 100), and the calculated opening is The damper 9 is controlled to the calculated opening degree when the opening degree is greater than or equal to the lower limit opening degree, and to the lower limit opening degree when the opening degree is less than the lower limit opening degree.
即ち排気中酸素濃度が低過ぎる場合炉内の酸素量が不足
していることが多く前記したように不完全燃焼を生じた
り爆発的な燃焼を生じたりし易いため一時的にダンパ開
度を大きくして炉内への空気供給量を増大させる。In other words, if the oxygen concentration in the exhaust gas is too low, the amount of oxygen in the furnace is often insufficient, and as mentioned above, incomplete combustion or explosive combustion is likely to occur, so temporarily increase the damper opening. to increase the amount of air supplied into the furnace.
この構成は詳細には上記状態を初めて検出したときにダ
ンパ9を開動作させるが、次回入力時の測定値が連続し
て3.5%を下まわるときにはもう1回即ち3分開様子
をみるためそのときのダンパ開度に保ち、さらに3回連
続して同状態が継続したときには再度ダンパ9を3多開
動作させる。In detail, this configuration causes the damper 9 to open when the above condition is detected for the first time, but when the measured value at the next input is continuously below 3.5%, the damper 9 is opened once more, that is, for 3 minutes. The damper opening degree is maintained at that time, and when the same state continues three times in a row, the damper 9 is again opened three times.
そして、かかるダンパ開度制御にもかかわらず同状態が
4回以上連続したときには、該酸素濃度測定値の異常は
酸素濃度計11の異常が原因であると判定し該情報を通
報し後述するドラフト圧力によるダンバ開度制御を行な
う構成とする。If the same condition occurs four or more times in a row despite the damper opening control, it is determined that the abnormality in the oxygen concentration measurement value is caused by an abnormality in the oxygen concentration meter 11, and the information is reported to the draft controller, which will be described later. The damper opening degree is controlled by pressure.
このようにすれば酸素濃度計11の異常により誤ってダ
ンパ9が長時間開度大に保たれ実際の酸素濃度が異常上
昇し燃料経済性が悪化することを防止できる。In this way, it is possible to prevent the damper 9 from being erroneously kept at a large opening for a long time due to an abnormality in the oxygen concentration meter 11, thereby preventing the actual oxygen concentration from increasing abnormally and deteriorating fuel economy.
次に被加熱体の流量と加熱炉出入口の温度差から被加熱
体の加熱に要する熱量即ち加熱炉の熱負荷を計算し、予
め定められた熱負荷と排気中酸素濃度との関係式から目
標酸素濃度を割り出し記憶部にセットする。Next, the amount of heat required to heat the heated object, that is, the heat load of the heating furnace, is calculated from the flow rate of the heated object and the temperature difference between the entrance and exit of the heating furnace, and the target value is calculated from the predetermined relational expression between the heat load and the oxygen concentration in the exhaust gas. Determine the oxygen concentration and set it in the memory.
そして排気中酸素濃度の測定値が目標酸素濃度より0.
5%以上低い状態が12時間以上継続した場合には該目
標酸素濃度を所定量減じた値(目標酸素濃度式の定数項
を例えば0.2%減じる)を新たな目標酸素濃度として
セットし、逆に目標酸素濃度がo.s%以上高い状態が
2時間以上継続した場合にはこの状態を通報し、バーナ
2の空気導入口開度を小さくして空気供給量を減少させ
るように指示する。Then, the measured value of the oxygen concentration in the exhaust gas is 0.0% lower than the target oxygen concentration.
If the condition continues to be lower than 5% for 12 hours or more, a value obtained by subtracting the target oxygen concentration by a predetermined amount (for example, by reducing the constant term of the target oxygen concentration formula by 0.2%) is set as a new target oxygen concentration, Conversely, if the target oxygen concentration is o. If the condition remains high for more than s% for two hours or more, this condition is reported and an instruction is given to reduce the air inlet opening of the burner 2 to reduce the air supply amount.
即ち酸素濃度の測定値が目標酸素濃度に比べ所定時間以
上継続して低いときは目標酸素濃度が高過ぎると判定し
て自動的に目標酸素濃度が切り下げられ、測定値が切り
下げられた目標酸素濃度の設定範囲内に納まればこれが
新た々目標酸素濃度となる。In other words, when the measured value of oxygen concentration is lower than the target oxygen concentration for a predetermined period of time or more, it is determined that the target oxygen concentration is too high, and the target oxygen concentration is automatically lowered, and the target oxygen concentration is the target oxygen concentration that the measured value is lowered. If it falls within the set range, this becomes the new target oxygen concentration.
又、測定値が修正された目標酸素濃度より所定時間以上
継続して高くなった時通報によって空気供給量が減量制
御されるため結局酸素濃度は目標酸素濃度に設定範囲内
に納まる結果となり排気中の酸素濃度を低濃度に安定さ
せひいては燃料経済性をより高めることができる。In addition, when the measured value continues to be higher than the corrected target oxygen concentration for a predetermined period of time or more, the air supply amount is controlled to be reduced by notification, so the oxygen concentration ends up within the set range of the target oxygen concentration and the exhaust gas is being pumped out. It is possible to stabilize the oxygen concentration at a low concentration and further improve fuel economy.
次にダンバ開度計12の異常を判別し、ダンパ開度が設
定下限開度である60φを下まわるとき又は現測定値と
前回測定値との差が±5%以上あるときにはダンバ開度
計12が異常であると判定し、該異常状態を通報すると
共にドラフト圧力によるダンパ開度制御は行なわすダン
パ開度を現状に維持する。Next, it is determined whether there is an abnormality in the damper opening degree meter 12, and if the damper opening degree is less than the set lower limit opening of 60φ or the difference between the current measurement value and the previous measurement value is ±5% or more, the damper opening degree meter 12 is detected. 12 is determined to be abnormal, the abnormal state is notified, and the damper opening is controlled by the draft pressure to maintain the damper opening at the current state.
続いて、ドラフト圧力計10の異常を調べ、現測定値が
設定圧力範囲例えば−4〜3 trrm Aqから外れ
ているとき又は現測定値と前回測定値との圧力差が例え
ば±2 tan A q以上あるときには前記と同様ダ
ンパ開度を現状に維持する。Next, check for abnormalities in the draft pressure gauge 10, and check if the current measured value is outside the set pressure range, for example -4 to 3 trrm Aq, or if the pressure difference between the current measured value and the previous measured value is, for example, ±2 tan Aq. If the above condition exists, the damper opening degree is maintained at the current level as described above.
そして、これら異常項目にかいて異常が通報された場合
には速やかに異常箇所を点検又は手動制御によって正常
状態に修正する。When an abnormality is reported in any of these abnormal items, the abnormality is promptly inspected or corrected to a normal state by manual control.
次に、上記ダンパ開度、ドラフト開度が正常であると判
定された場合又は排気中酸素濃度の異常測定値が酸素濃
度計11の異常が原因である場合には主たる制御である
ドラフト圧力によるダンパ開度制御を行なう。Next, if it is determined that the damper opening degree and the draft opening degree are normal, or if the abnormal measured value of the oxygen concentration in the exhaust gas is caused by an abnormality in the oxygen concentration meter 11, the main control is the draft pressure. Controls the damper opening.
まず、ドラフト圧力の現測定値と前回及び前々回測定値
の3回の平均値Pmを求め、次にPm ) 1. O
mAq (以下単位省略)のときダンバ9を2.0%開
、O(Pm≦1.0では1.1%開としてダンパ開度を
算出し、該算出開度が下限開度のときには算出開度に、
下限開度を下まわるときには下限開度に制御する。First, calculate the average value Pm of the current measured value of the draft pressure and the previous and two previous measured values, and then calculate Pm.1. O
mAq (unit omitted below), the damper opening degree is calculated by opening the damper 9 by 2.0%, O (if Pm≦1.0, opening is 1.1%, and when the calculated opening degree is the lower limit opening degree, the damper opening degree is calculated by opening the damper 9 by 2.0%. At times,
When the opening degree falls below the lower limit opening degree, the opening degree is controlled to the lower limit opening degree.
次いでPm≦0.0に釦いて被加熱体の流量及び加熱炉
出入口での温度差に基づき加熱炉の熱負荷が増加中か否
かを調へ増加中の場合にはダンパ9をその現状開度が下
眼開度以上のときは現状開度に、下限開度を下まわると
きには下限開度に制御する。Next, press Pm≦0.0 to check whether the heat load of the heating furnace is increasing based on the flow rate of the object to be heated and the temperature difference at the entrance and exit of the heating furnace. When the opening degree is equal to or higher than the lower eye opening degree, the opening degree is controlled to the current opening degree, and when it is below the lower limit opening degree, the opening degree is controlled to the lower limit opening degree.
即ち、熱負荷増加中には空気供給量が増加する過程にあ
るからPm≦0.0の場合でもダンパ開度を閉動作しな
いようにする。That is, since the air supply amount is in the process of increasing while the heat load is increasing, the damper opening degree is set not to close even if Pm≦0.0.
熱負荷増加中でない場合には−1(Pm≦0.0ではダ
ンパ開度を現状維持、−2(Pm≦−1.0では1.1
%閉、Pmく−2では2.0%閉として算出し、該算出
開度が下限開度以上では算出開度に下限開度を下まわる
ときには下限開度に制御する。If the heat load is not increasing, -1 (if Pm≦0.0, the damper opening is maintained as it is, -2 (if Pm≦-1.0, the damper opening is 1.1)
% closed, Pm -2 is calculated as 2.0% closed, and when the calculated opening is greater than or equal to the lower limit opening, the calculated opening is controlled to the lower limit when the opening is less than the lower limit.
このように、基本的な制御としてはドラフト圧力の増減
に応じてダンパを閉又は開動作して炉内への空気供給量
が適量となるように調整するものである。As described above, the basic control is to adjust the amount of air supplied into the furnace to be an appropriate amount by closing or opening the damper in response to an increase or decrease in draft pressure.
原油常圧蒸留装置の加熱炉にかける制御例では本発明装
置の場合、ドラフト圧力の設定値をO〜− 2 waA
qとしたときドラフト圧力の実測平均値が−1.1 2
1IaILAqとなり、従来の手動ダンバ制御方式ドラ
フト圧力の管理目標を同様にO〜−2tmAqとしたと
きの実測平均値−1.76mmAqに比べて一段と正圧
に近い負圧が得られた。In the example of control applied to the heating furnace of crude oil atmospheric distillation equipment, in the case of the equipment of the present invention, the set value of the draft pressure is set to O~-2 waA.
When q, the measured average value of draft pressure is -1.1 2
1IaILAq, and a negative pressure much closer to positive pressure was obtained than the actual measured average value -1.76 mmAq when the draft pressure management target of the conventional manual damper control system was similarly set to O~-2 tmAq.
さらにドラフト圧力の設定値を0〜−1mAqとしたと
きには実測平均値は−(16 1 ttan Aqにま
で低下し、この場合でも正圧となることは殆んど女かっ
た。Further, when the set value of the draft pressure was set from 0 to -1 mAq, the actual measured average value decreased to -(16 1 ttan Aq), and even in this case, positive pressure was almost never achieved.
この結果を燃料経済性の指標となる燃料原単位[”/,
)(被加熱体1Bを所定温度加熱するのに要する燃料の
t量)に換算すると加熱炉の稼動率90%では第3図に
示すように前記実測平均値− 1−1 2mm▲q(ド
ラフト圧力の設定値O〜−2m7ILAq)のとき8.
0 7 ( 1/Kl〕(図示B点)、実測平均値−0
.6 1mAq (設定値0〜−IWanAq)のとき
8. 6 5 ( ’/kl〕(図示C点)となジ、手
動制御方式の−1.7 6mmAq (ドラフト圧力管
理目標値O〜−2閤Aq )のときの8.75[”イ’
H3 (図示A点)に比べ夫々0.6%及び1.1条減
少している。This result is used as a fuel consumption index [”/,
) (amount of fuel required to heat the heated object 1B to a predetermined temperature) When the operating rate of the heating furnace is 90%, the actual measured average value - 1-1 2 mm▲q (draft 8. When the pressure setting value is O~-2m7ILAq).
0 7 (1/Kl) (point B in the diagram), measured average value -0
.. 6 When 1mAq (setting value 0 to -IWanAq) 8. 6 5 ('/kl) (point C in the figure) and 8.75 ["I'" when -1.76 mmAq (draft pressure management target value O ~ -2 Aq) of manual control method.
Compared to H3 (point A in the diagram), the number of threads is reduced by 0.6% and 1.1, respectively.
即ち燃費をこれだけ減少することができ特にこの種加熱
炉のように長時間運転し続けるものでは経済的有利性が
大きい。That is, the fuel consumption can be reduced to this extent, which is economically advantageous, especially in a furnace of this kind that is operated continuously for a long time.
以上説明したように本発明によれば、主たる空気供給量
制御が現在及び過去数回のドラフト圧力測定値の平均値
に基づいたダンパ開度に制御することによって行なわれ
るので一時的なドラフト圧力上昇による影響を受けるこ
とが少なく安定した燃焼性が保たれかつ燃料経済性が大
幅に向上する。As explained above, according to the present invention, the main air supply amount control is performed by controlling the damper opening based on the average value of the current and past several draft pressure measurements, so the draft pressure increases temporarily. Stable combustibility is maintained, and fuel economy is greatly improved.
又、排気中酸素濃度が設定濃度を下まわシ炉内の酸素量
が不足傾向にあるときはドラフト圧力にかカワリなくダ
ンバを開動作させるので不完全燃焼及び爆発燃焼を防止
でき、さらにドラフト圧力及びダンパ開度の異常時には
ドラフト圧力によるダンバ開度制御を停止させるので異
常測定値に基づく誤った制御を防止することができる。In addition, when the oxygen concentration in the exhaust gas falls below the set concentration and the amount of oxygen in the furnace tends to be insufficient, the damper is opened without worrying about the draft pressure, which prevents incomplete combustion and explosive combustion. Also, when the damper opening degree is abnormal, the damper opening degree control using the draft pressure is stopped, so that erroneous control based on the abnormal measured value can be prevented.
さらに熱負荷増加中にドラフト圧力が低下していてもダ
ンバを閉じない構成とした場合には、該熱負荷増大に伴
なう要求空気量の増加を満たすことができ炉内の酸素量
不足を防止することができる。Furthermore, if the damper is configured not to close even if the draft pressure decreases during an increase in heat load, it is possible to satisfy the increase in the amount of air required due to the increase in heat load, and to prevent a lack of oxygen in the furnace. It can be prevented.
第1図は本発明の一実施例装置を示す構成図、第2図A
,B,Cは同装置の制御プログラム図、第3図は同装置
の制御方式と手動制御方式に釦けるドラフト圧力一燃料
原単位の関係を示すグラフである。
1・・・加熱炉本体、4・・・流量計、5・・・入口部
温度計、6・・・出口部温度計、9・・・ダンパ、10
・・・ドラフト圧力計、11・・・酸素濃度計、12・
・・ダンパ開度計、14・・・コンピュータ。Fig. 1 is a configuration diagram showing an embodiment of the device of the present invention, Fig. 2A
, B, and C are control program diagrams of the same device, and FIG. 3 is a graph showing the relationship between draft pressure and fuel consumption rate for the control method and manual control method of the same device. DESCRIPTION OF SYMBOLS 1... Heating furnace main body, 4... Flow meter, 5... Inlet part thermometer, 6... Outlet part thermometer, 9... Damper, 10
...Draft pressure gauge, 11...Oxygen concentration meter, 12.
...Damper opening gauge, 14...Computer.
Claims (1)
出口に取り付けたダンパを開度制御することによって調
整する自然通風型加熱炉において、加熱炉内のドラフト
圧力、排気中酸素濃度、ダンパ開度の夫々の測定値を定
時間毎に入力し、ドラフト圧力及びダンパ開度の各測定
値が正常であり、かつ、排気中酸素濃度が設定下限濃度
以上ある時にはドラフト圧力の現在及び過去適数回の測
定値を平均し該平均値を大気圧に近い圧力に近づけるよ
うにダンパ開度を制御する第1制御系と、ドラフト圧力
及びダンパ開度の各測定値が正常であり、かつ、排気中
酸素濃度が前記設定下限濃度よシ下まわるときドラフト
圧力にかかわり々くダンパを所定量開動作させる第2制
御系と、ドラフト圧力及びダンバ開度の少なくとも一方
の測定値が異常であるとき無条件にダンバ開度を現状に
維持する第3制御系とからなるダンパ開度制御装置を設
けたことを特徴とする自然通風型加熱炉。 2 第1制御系はドラフト圧力の現測定値と前回及び前
々回の測定値の3回の測定値の平均値に応じてダンパ開
度を制御してなる特許請求の範囲第1項記載の自然通風
型加熱炉。 3 炉内に自然通風される燃焼用空気の供給量を排気流
出口に取シ付けたダンパを開度制御することによって調
整する自然通風型加熱炉に訃いて、加熱炉内のドラフト
圧力、排気中酸素濃度、ダンパ開度、被加熱体流量、被
加熱体の加熱炉出入口温度の夫々の測定値を定時間毎に
入力し、ドラフト圧力及びダンパ開度の各測定値が正常
であう、かつ、排気中酸素濃度が設定下限濃度以上ある
時にはドラフト圧力の現在及び過去適数回の測定値を平
均し該平均値を大気圧に近い圧力に近づけるようにダン
バ開度を制御する第1制御系と、ドラフト圧力及びダン
パ開度の各測定値が正常であり、かつ、排気中酸素濃度
が前記設定下限濃度より下回るときドラフト圧力にかか
わりなくダンバを所定量開動作させる第2制御系と、ド
ラフト圧力及びダンパ開度の少なくとも一方の測定値が
異常であるとき無条件にダンパ開度を現状に維持する第
3制御系と、前記第1制御系が作動する条件下で前記ド
ラフト圧力の平均値が負圧であり、かつ、被加熱体の流
量及び加熱炉出入口における温度差に基づき検出される
加熱炉の熱負荷が増大中である時には、ダンパ開度を閉
じ女いようにする第4制御系とからなるダンパ開度制御
装置を設けたことを特徴とする自然通風型加熱炉。[Claims] 1. In a natural draft heating furnace in which the supply amount of combustion air naturally ventilated into the furnace is adjusted by controlling the opening of a damper attached to an exhaust outlet, the draft pressure in the heating furnace is , input the measured values of exhaust oxygen concentration and damper opening at regular intervals, and if the measured values of draft pressure and damper opening are normal and the exhaust oxygen concentration is above the set lower limit concentration. A first control system that controls the damper opening so that the current and past measurements of the draft pressure are averaged and the average value approaches atmospheric pressure, and each measured value of the draft pressure and the damper opening. a second control system that opens the damper by a predetermined amount regardless of the draft pressure when the exhaust oxygen concentration is normal and the oxygen concentration in the exhaust falls below the set lower limit concentration; and at least one of the draft pressure and the damper opening degree. A natural draft heating furnace comprising a damper opening control device comprising a third control system that unconditionally maintains the damper opening at the current state when a measured value is abnormal. 2. The natural ventilation according to claim 1, wherein the first control system controls the damper opening degree according to the average value of the current measurement value of the draft pressure, the previous measurement value, and the measurement value before the previous one. Type heating furnace. 3. The amount of combustion air naturally ventilated into the furnace is adjusted by controlling the opening of a damper attached to the exhaust outlet. Input the measured values of medium oxygen concentration, damper opening, flow rate of the heated object, and temperature of the heated object at the entrance and exit of the heating furnace at regular intervals, and make sure that the measured values of draft pressure and damper opening are normal, and a first control system that averages current and past several measured values of draft pressure and controls the damper opening degree so as to bring the average value close to atmospheric pressure when the oxygen concentration in the exhaust gas is higher than a set lower limit concentration; , a second control system that opens the damper by a predetermined amount regardless of the draft pressure when the measured values of the draft pressure and the damper opening degree are normal and the oxygen concentration in the exhaust gas is lower than the set lower limit concentration; and a third control system that unconditionally maintains the damper opening at the current level when at least one of the measured values of the damper opening is abnormal; A fourth control system that closes the damper opening when the pressure is negative and the heat load of the heating furnace is increasing, which is detected based on the flow rate of the heated object and the temperature difference at the entrance and exit of the heating furnace. A natural draft heating furnace characterized by being equipped with a damper opening control device comprising:
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1451778A JPS5848805B2 (en) | 1978-02-10 | 1978-02-10 | Natural draft heating furnace |
US06/009,825 US4262843A (en) | 1978-02-10 | 1979-02-06 | Method of and apparatus for controlling the feed amount of air for combustion in a natural draft-type heating furnace |
DE19792904968 DE2904968A1 (en) | 1978-02-10 | 1979-02-09 | METHOD AND DEVICE FOR CONTROLLING THE AIR SUPPLY OF A STOVE |
FR7903324A FR2417062A1 (en) | 1978-02-10 | 1979-02-09 | METHOD AND APPARATUS FOR CONTROL OF COMBUSTION AIR SUPPLY IN A NATURAL DRAFT TYPE OVEN |
GB7904590A GB2017278B (en) | 1978-02-10 | 1979-02-09 | Method of and apparatus for controlling the feed amount of air for combustion in a natural draft type heating furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1451778A JPS5848805B2 (en) | 1978-02-10 | 1978-02-10 | Natural draft heating furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS54108025A JPS54108025A (en) | 1979-08-24 |
JPS5848805B2 true JPS5848805B2 (en) | 1983-10-31 |
Family
ID=11863274
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1451778A Expired JPS5848805B2 (en) | 1978-02-10 | 1978-02-10 | Natural draft heating furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5848805B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4253404A (en) * | 1980-03-03 | 1981-03-03 | Chevron Research Company | Natural draft combustion zone optimizing method and apparatus |
JPS5777826A (en) * | 1980-10-31 | 1982-05-15 | Idemitsu Petrochem Co Ltd | Heating furnace |
US4574746A (en) * | 1984-11-14 | 1986-03-11 | The Babcock & Wilcox Company | Process heater control |
EP1944999B1 (en) | 2006-06-21 | 2015-01-21 | Panasonic Corporation | Speaker, speaker device using the speaker, and electronic equipment and vehicle using the speaker |
-
1978
- 1978-02-10 JP JP1451778A patent/JPS5848805B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS54108025A (en) | 1979-08-24 |
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