JP2900283B2 - Control method of exhaust gas ventilator of flue gas desulfurization unit - Google Patents

Control method of exhaust gas ventilator of flue gas desulfurization unit

Info

Publication number
JP2900283B2
JP2900283B2 JP2224216A JP22421690A JP2900283B2 JP 2900283 B2 JP2900283 B2 JP 2900283B2 JP 2224216 A JP2224216 A JP 2224216A JP 22421690 A JP22421690 A JP 22421690A JP 2900283 B2 JP2900283 B2 JP 2900283B2
Authority
JP
Japan
Prior art keywords
exhaust gas
ventilator
flue gas
flue
boiler
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 - Lifetime
Application number
JP2224216A
Other languages
Japanese (ja)
Other versions
JPH04106308A (en
Inventor
照雄 杉谷
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.)
CHODA KAKO KENSETSU KK
Original Assignee
CHODA KAKO KENSETSU KK
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 CHODA KAKO KENSETSU KK filed Critical CHODA KAKO KENSETSU KK
Priority to JP2224216A priority Critical patent/JP2900283B2/en
Publication of JPH04106308A publication Critical patent/JPH04106308A/en
Application granted granted Critical
Publication of JP2900283B2 publication Critical patent/JP2900283B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treating Waste Gases (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ボイラなどの燃焼設備からの排ガス中の硫
黄酸化物を低減する排煙脱硫装置の排ガス通風機の制御
方法に関するものである。
Description: TECHNICAL FIELD The present invention relates to a method for controlling an exhaust gas ventilator of a flue gas desulfurization device that reduces sulfur oxides in exhaust gas from combustion equipment such as a boiler.

〔従来の技術〕[Conventional technology]

従来の排煙脱硫装置では、第3図に示すように、ボイ
ラ送風機6によりボイラ1などの燃焼設備に送風して、
ボイラ1内で燃焼を行ない、ボイラ1から排出した未処
理の排ガスを、排ガス送風機4で誘引した後、ガス・ガ
スヒータの熱回収器7を通して温度を降下させた後、排
煙脱硫装置である脱硫槽8に送り、そこで脱硫した処理
ずみの排ガスをガス・ガスヒータの再加熱器7′に通し
て高温の未処理の排ガスと熱交換し、昇温した処理ずみ
の排ガスを煙突2から排出するようにしている。
In a conventional flue gas desulfurization apparatus, as shown in FIG. 3, a boiler blower 6 blows air to a combustion facility such as the boiler 1,
After burning in the boiler 1 and untreated exhaust gas discharged from the boiler 1 is attracted by the exhaust gas blower 4, the temperature is lowered through the heat recovery unit 7 of the gas / gas heater, and then, the desulfurization as the flue gas desulfurization device is performed. It is sent to a tank 8 where the desulfurized treated exhaust gas is passed through a reheater 7 ′ of a gas heater to exchange heat with high-temperature untreated exhaust gas, and the heated treated exhaust gas is discharged from the chimney 2. I have to.

これにより、ボイラ1などの燃焼設備からの排ガス中
の硫黄酸化物を一定レベルにまで低減し、かつ煙突2か
ら排出したときに白煙が生ずるのを防止している。
As a result, sulfur oxides in exhaust gas from combustion equipment such as the boiler 1 are reduced to a certain level, and the generation of white smoke when discharged from the chimney 2 is prevented.

さらに、この排煙脱硫装置の事故が発生したような緊
急の場合に備えて、未処理の排ガスが煙突2へ直接排出
するバイパスダクト3を設けている。
Further, in case of an emergency such as when an accident of the flue gas desulfurization device occurs, a bypass duct 3 for discharging untreated exhaust gas directly to the chimney 2 is provided.

そこで、排ガス送風機4の誘引量が多い場合はリサイ
クル量が増加し、各装置が大型化すると共に、誘引量が
少ない場合はバイパスダクト3によりショートパスする
ので、性能上に問題が生じるため、そのバイパスダクト
3にバイパスダンパ5を介設している。
Therefore, when the amount of the exhaust gas blower 4 attracted is large, the amount of recycling increases, and the size of each device is increased. When the amount of attracted air is small, a short pass is performed by the bypass duct 3, which causes a problem in performance. A bypass damper 5 is provided in the bypass duct 3.

さらに、バイパスダンパ5は、緊急時に必ず全開にな
らなければならないが、ダストの摺動部への堆積によ
り、動作しないこともあり、このため、運転中に開閉試
験をある頻度で行なうことになる。
Further, the bypass damper 5 must be fully opened in an emergency, but may not operate due to accumulation of dust on the sliding portion. Therefore, the open / close test is performed at a certain frequency during operation. .

ここで、ボイラ1の内圧はボイラ1の燃焼状態などに
より±5〜20mm水柱の範囲で振れるので、そのため、密
閉性の高いバイパスダンパ5を設けるか、排ガス通風機
入口設定圧力をリークの無い範囲で未処理の排ガス路側
を低圧にする必要がある。
Here, since the internal pressure of the boiler 1 fluctuates within a range of ± 5 to 20 mm water column depending on the combustion state of the boiler 1, a bypass damper 5 having a high hermeticity is provided, or the set pressure of the exhaust gas ventilator inlet is set to a range without leakage. Therefore, it is necessary to reduce the pressure of the untreated exhaust gas path side.

排ガス通風機4の制御は、排ガス通風機4入口圧力ま
たは排ガス流量またはバイパスダンパ5の差圧で行な
う。
The exhaust gas ventilator 4 is controlled based on the inlet pressure of the exhaust gas ventilator 4, the exhaust gas flow rate, or the differential pressure of the bypass damper 5.

さらに、ボイラ送風機6かボイラ誘引ファンの信号を
先行信号として使用することもある。
Further, the signal of the boiler blower 6 or the boiler induction fan may be used as a preceding signal.

このうち、排ガス通風機4入口圧力を用いる方法は外
気温により煙突ドラフトが変化するため排ガス通風機4
の選定が大きくなり、運転時の通風機効率を悪くする。
Among these methods, the method using the exhaust gas ventilator 4 inlet pressure is different because the chimney draft changes depending on the outside air temperature.
Selection increases, and the ventilation efficiency during operation deteriorates.

これを解消するため、バイパスダンパ5の差圧で制御
するのが一般的である。
In order to solve this, it is common to control by the differential pressure of the bypass damper 5.

排ガス流量を用いる方法は季節的外気温の変化により
同一ボイラ負荷でも排ガス流量が変化し、さらに石炭を
燃料とする場合、石炭成分によっても排ガス流量が変化
するため、ショートパスやリサイクルによる設備の大型
化等が懸念される。
In the method using the exhaust gas flow rate, the exhaust gas flow rate changes even with the same boiler load due to seasonal changes in the outside temperature, and when coal is used as fuel, the exhaust gas flow rate also changes depending on the coal component, so large equipment using short paths and recycling Is concerned.

しかし、従来は密封性の低いバイパスダンパ5を用い
るか、全く用いずリサイクルをかけて排ガス通風機4を
流量で制御するのが多くみられる。
However, conventionally, it is often seen that the exhaust gas ventilator 4 is controlled at a flow rate by using a bypass damper 5 having a low hermeticity or by not using the bypass damper 5 at all.

一方、第3図のごとく、排ガス通風機4が複数台ある
場合は、ファン性能に若干でも性能の差異があったり、
ダクト配置が異なることがある。
On the other hand, as shown in FIG. 3, when there are a plurality of exhaust gas ventilators 4, there may be a slight difference in fan performance,
Duct arrangement may be different.

そのため、バイパス差圧で制御すると、排ガス量にア
ンバランスを生じて、その差異が大幅になることもあ
り、高容量の排ガスを処理する場合では、その脱硫、冷
却、熱回収等に性能上の問題を生じる一方、低負荷時の
低容量の排ガスを処理するときには、その排ガス通風機
4や脱硫槽8等の制御性に問題を生じることになる。
Therefore, if controlled by the bypass differential pressure, the amount of exhaust gas will be unbalanced, and the difference may be large.When processing high-capacity exhaust gas, it is difficult to perform desulfurization, cooling, heat recovery, etc. On the other hand, when processing a low-capacity exhaust gas under a low load, a problem occurs in the controllability of the exhaust gas ventilator 4, the desulfurization tank 8, and the like.

〔発明の解決しようとする課題〕[Problem to be solved by the invention]

本発明は、前記従来の問題点を解決するためになされ
たものであり、複数の排ガス通風機を備えた場合のファ
ン性能の相違やダクトの配置にとらわれずに排ガスの流
量を同量にして、安定した排煙脱硫装置の運用を行ない
うる排煙脱硫装置の排ガス通風機の制御方法を提供する
ことを解決課題としたものである。
The present invention has been made in order to solve the conventional problems, and the same flow rate of the exhaust gas without regard to the difference in fan performance and the arrangement of the duct when a plurality of exhaust gas ventilators are provided. It is an object of the present invention to provide a method for controlling an exhaust gas ventilator of a flue gas desulfurization device capable of stably operating the flue gas desulfurization device.

〔課題を解決するための手段〕 上記の課題を解決するための手段として、本発明の排
煙脱硫装置の排ガス通風機の制御方法は、ボイラなどの
燃焼設備から排出された未処理の排ガス路と脱硫槽など
の排煙脱硫装置から出た処理ずみ排ガス路との間を、バ
イパスダンパを介設したバイパスダクトで接続し、その
ボイラなどから脱硫槽などへ未処理の排ガスを送る複数
の排ガス通風機に対し、上記バイパスダンパの前後の差
圧を、未処理の排ガス路側を処理ずみ排ガス路側より5
から50mm水柱低く制御し、さらに各排ガス通風機4の流
量、または各排ガス通風機への出力信号の差を排ガス通
風機の制御に加算、減算することにより構成される。
[Means for Solving the Problems] As a means for solving the above problems, a method for controlling an exhaust gas ventilator of a flue gas desulfurization apparatus according to the present invention comprises an untreated exhaust gas passage discharged from a combustion facility such as a boiler. A plurality of flue gas that connects untreated flue gas discharged from a flue gas desulfurization unit such as a desulfurization tank with a bypass duct interposed with a bypass damper and sends untreated flue gas from the boiler etc. to the desulfurization tank etc. For the ventilator, the differential pressure before and after the bypass damper is increased by 5% from the exhaust gas path side after the untreated exhaust gas path side is processed.
, And the flow rate of each exhaust gas ventilator 4 or the difference between the output signals to each exhaust gas ventilator is added to or subtracted from the control of the exhaust gas ventilator.

〔実施例〕〔Example〕

以下図面を参照して本発明の実施例を説明するが、本
発明の制御方法を適用する排煙脱硫装置の実施例として
は、第3図にて説明したとほぼ同様の構成及び機能を有
するボイラ1、2台の排ガス通風機4、ガス・ガスヒー
タの熱回収器7及び再加熱器7′、脱硫槽8、煙突2な
どからなり、未処理の排ガス路と処理ずみ排ガス路との
間を、バイパスダンパ5を介設したバイパスダクト3で
接続したものであり、その作用は前述の説明と同様であ
るのでここでは省略する。
Hereinafter, an embodiment of the present invention will be described with reference to the drawings. An embodiment of a flue gas desulfurization apparatus to which the control method of the present invention is applied has substantially the same configuration and function as that described with reference to FIG. It comprises a boiler 1, two exhaust gas ventilators 4, a gas / gas heater heat recovery unit 7 and a reheater 7 ', a desulfurization tank 8, a chimney 2, etc., and connects between an untreated exhaust gas passage and a treated exhaust gas passage. , Connected by a bypass duct 3 provided with a bypass damper 5 interposed therebetween, and the operation thereof is the same as that described above, and will not be described here.

そこで、第1図は上記の一実施例における排煙脱硫装
置の排ガス通風機4の制御回路のブロック図であり、2
台の排ガス通風機4について、脱硫槽8入側の未処理の
排ガス路側を、脱硫槽8の出側の処理ずみ排ガス路側よ
り5〜50mm水柱低くなるようにバイパスダンパ5の差圧
DPを制御しており、さらに2台の排ガス通風機4の排ガ
ス流量1及び排ガス流量2を比例・積分調節器21に送
り、各排ガス通風機4の排ガス流量の差を演算し、その
流量差補正信号を加算器16に送り、各排ガス通風機4の
制御に適宜加算と減算とを施すようにしている。
Therefore, FIG. 1 is a block diagram of a control circuit of the exhaust gas ventilator 4 of the flue gas desulfurization apparatus according to the embodiment, and FIG.
Pressure difference of the bypass damper 5 so that the untreated exhaust gas passage side on the inlet side of the desulfurization tank 8 is lower than the treated exhaust gas passage side on the exit side of the desulfurization tank 8 by 5 to 50 mm water column.
And controlling the D P, further feeding the exhaust gas flow rate 1 of the two exhaust gas ventilator 4 and the exhaust gas flow 2 in the proportional-integral controller 21, calculates a difference of the exhaust gas flow rate of each gas ventilator 4, the flow rate The difference correction signal is sent to the adder 16 so that the control of each exhaust gas ventilator 4 is appropriately added and subtracted.

一方、2台のボイラ送風機6の各開度信号を関係変換
器15に送って各排ガス通風機4のコントロールドライブ
量を決定し、上記加算器16と、2台の排ガス通風機4の
それぞれの制御器1及び制御器2のバイパスダンパ5の
差圧DPの信号が送られる比例・積分調節器21の加算器17
の一方に送る。
On the other hand, each opening signal of the two boiler blowers 6 is sent to the related converter 15 to determine the control drive amount of each exhaust gas ventilator 4, and the adder 16 and each of the two exhaust gas ventilators 4 are controlled. adder 17 of the proportional plus integral controller 21 to signal the pressure difference D P of the bypass damper 5 of the controller 1 and the controller 2 is sent
Send to one of

これにより、一方の排ガス送風機4の排ガス流量1の
出力信号を基準として、他方の排ガス送風機4の排ガス
流量2の信号との差を補正信号として加減するようにし
ている。
Thereby, the difference between the output signal of the exhaust gas blower 4 and the signal of the exhaust gas flow 2 of the other exhaust gas blower 4 is used as a reference, and the difference is adjusted as a correction signal.

次に、第2図に示す他の実施例では、2台の排ガス送
風機4への出力信号の差を排ガス通風機4の制御に加減
するものであり、第1図の実施例とほぼ同様な機能を有
するものであり、同じ部品は同じ部品番号で示してい
る。
Next, in another embodiment shown in FIG. 2, the difference between the output signals to the two exhaust gas blowers 4 is added to or subtracted from the control of the exhaust gas blowers 4, which is almost the same as the embodiment shown in FIG. They have functions and the same parts are indicated by the same part numbers.

〔発明の効果〕〔The invention's effect〕

以上に説明した本発明の排煙脱硫装置の排ガス通風機
の制御方法によれば、複数の排ガス通風機の性能の相違
や、ダクトの配置にとらわれずに、排ガス流量を同量と
できるので、排煙脱硫装置の全設備が安全運用できると
いう効果がある。
According to the control method of the exhaust gas ventilator of the flue gas desulfurization apparatus of the present invention described above, the exhaust gas flow rate can be the same, regardless of the difference in performance between the plurality of exhaust gas ventilators and the arrangement of the ducts. There is an effect that all the facilities of the flue gas desulfurization device can be safely operated.

また、バイパスダンパの未処理の排ガス路側の圧力を
処理ずみ排ガス路側より低くしたことにより、バイパス
ダンパの開閉試験等においても負荷安定時にそのまま行
なえるという利点もある。
Further, since the pressure on the untreated exhaust gas path side of the bypass damper is made lower than that on the treated exhaust gas path side, there is an advantage that even when the load is stabilized, the opening / closing test of the bypass damper can be performed as it is.

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

第1図は本発明の制御方法を適用する排煙脱硫装置の排
ガス通風機の制御回路の一実施例におけるブロック図、
第2図は第1図と異なる他の実施例におけるブロック
図、第3図は従来の排煙脱硫装置の説明用フロー図であ
る。 1……ボイラ、3……バイパスダクト、4……排ガス通
風機、5……バイパスダンパ、7……熱回収器、7′…
…再加熱器、8……脱硫槽、16,17……加算器、DP……
差圧。
FIG. 1 is a block diagram of one embodiment of a control circuit of an exhaust gas ventilator of a flue gas desulfurization apparatus to which the control method of the present invention is applied,
FIG. 2 is a block diagram of another embodiment different from FIG. 1, and FIG. 3 is a flow chart for explaining a conventional flue gas desulfurization apparatus. 1 boiler 3 bypass duct 4 exhaust gas ventilator 5 bypass damper 7 heat recovery unit 7 ′
… Reheater, 8… desulfurization tank, 16,17 …… adder, D P ……
Differential pressure.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】燃焼設備からの未処理の排ガス路と排煙脱
硫装置で処理した排ガス路との間を、バイパスダンパを
介設したバイパスダクトで接続した排煙脱硫装置へ未処
理の排ガスを送る複数の排ガス通風機について、未処理
の排ガス側を処理ずみ排ガス側より5から50mm水柱低く
するように該バイパスダンパの前後の差圧を制御し、さ
らに各排ガス通風機の流量、または各排ガス通風機への
出力信号の差を排ガス通風機の制御に加算、減算する排
煙脱硫装置の排ガス通風機の制御方法。
An untreated exhaust gas is connected to a flue gas desulfurization device connected between a non-treated flue gas passage from a combustion facility and a flue gas passage treated by a flue gas desulfurization device by a bypass duct provided with a bypass damper. For a plurality of exhaust gas ventilators to be sent, the untreated exhaust gas side is treated and the differential pressure before and after the bypass damper is controlled so that the water column is lower by 5 to 50 mm than the exhaust gas side, and the flow rate of each exhaust gas ventilator or each exhaust gas A method for controlling an exhaust gas ventilator of a flue gas desulfurization device, in which a difference between output signals to the ventilator is added to and subtracted from control of the exhaust gas ventilator.
JP2224216A 1990-08-28 1990-08-28 Control method of exhaust gas ventilator of flue gas desulfurization unit Expired - Lifetime JP2900283B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2224216A JP2900283B2 (en) 1990-08-28 1990-08-28 Control method of exhaust gas ventilator of flue gas desulfurization unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2224216A JP2900283B2 (en) 1990-08-28 1990-08-28 Control method of exhaust gas ventilator of flue gas desulfurization unit

Publications (2)

Publication Number Publication Date
JPH04106308A JPH04106308A (en) 1992-04-08
JP2900283B2 true JP2900283B2 (en) 1999-06-02

Family

ID=16810336

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2224216A Expired - Lifetime JP2900283B2 (en) 1990-08-28 1990-08-28 Control method of exhaust gas ventilator of flue gas desulfurization unit

Country Status (1)

Country Link
JP (1) JP2900283B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102005005801B4 (en) * 2005-02-04 2007-08-09 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Electrostatic deflection system for corpuscular radiation

Also Published As

Publication number Publication date
JPH04106308A (en) 1992-04-08

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