JPH0757894B2 - Cleaning method of main exhaust gas of sintering machine - Google Patents
Cleaning method of main exhaust gas of sintering machineInfo
- Publication number
- JPH0757894B2 JPH0757894B2 JP29344890A JP29344890A JPH0757894B2 JP H0757894 B2 JPH0757894 B2 JP H0757894B2 JP 29344890 A JP29344890 A JP 29344890A JP 29344890 A JP29344890 A JP 29344890A JP H0757894 B2 JPH0757894 B2 JP H0757894B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- sintering machine
- main exhaust
- temperature
- bag filter
- 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
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- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、粉鉱石を予備処理する焼結機の主排気ガスの
バグフィルターを用いた清浄方法に関する。TECHNICAL FIELD The present invention relates to a cleaning method using a bag filter for main exhaust gas of a sintering machine for pretreating powdered ore.
一般に、粉鉱石の予備処理のための焼結機は、第10図に
示すように焼結機1の風箱をメインダクト20と連結し、
このメインダクト20に設けられた主排風機4により点火
炉9で点火後の焼結機1を経て各風箱から排ガスを吸引
することにより、焼結機上の水分を含んだ原料粉鉱石を
焼き固める。この排ガスは、原料性状、操業条件、設備
条件等により変わるが、一例を示すと第1〜3表のよう
な性状を有する。Generally, a sintering machine for pretreatment of powdered ore has a wind box of the sintering machine 1 connected to a main duct 20 as shown in FIG.
By sucking exhaust gas from each air box through the sintering machine 1 after ignition in the ignition furnace 9 by the main exhauster 4 provided in this main duct 20, raw material ore containing water on the sintering machine is obtained. Bake. This exhaust gas has properties as shown in Tables 1 to 3 as an example, though it varies depending on properties of raw materials, operating conditions, equipment conditions and the like.
かつては、主排風機4前に設けた乾式サイクロン19で除
塵したのち消音機5,乾式電気集塵機10を経て煙突6から
放散されていたが、その後放散ガス中の含塵量を更に低
減させるため乾式電気集塵機等のガス清浄装置が代替と
して設置されたり、又は増設されるようになった。そし
て近年、硫黄酸化物、窒素酸化物等の有害ガスの煙突か
らの放散規制が厳しくなり、脱硫装置、脱硝装置等のガ
ス処理装置がこの主排気ラインに設置又は増設されるよ
うになった(特開平1−68429号公報)。 In the past, dust was removed by a dry cyclone 19 provided in front of the main exhauster 4, and then was emitted from the chimney 6 via the silencer 5 and the dry electrostatic precipitator 10, but to further reduce the dust content in the emitted gas. A gas cleaning device such as a dry type electrostatic precipitator has been installed or added as an alternative. In recent years, regulations on the emission of harmful gases such as sulfur oxides and nitrogen oxides from stacks have become stricter, and gas treatment devices such as desulfurization devices and denitration devices have been installed or expanded in this main exhaust line ( JP-A-1-68429).
ここ数年来、上記の有害ガスの規制に加えて、製鉄所周
辺の住民から洗濯物の汚れ防止、農作物の汚染防止等の
生活環境向上の要請が日増しに強くなり、煙突からの降
下媒塵量の抑制が強く叫ばれるようになってきた。とこ
ろが、従来から使用されている乾式サイクロン、乾式電
気集塵機等においては焼結排ガスに対して限界があり、
降下媒塵量の抑制が充分とはいい難い状況になってき
た。ここで考えられるのが、比較的設備が安価で、尚且
つ集塵性能が著しく良好で、煙突からの排出媒塵量の低
減可能なバグフィルターを導入することである。Over the past few years, in addition to the above harmful gas regulations, residents around the steelworks have been increasingly demanding improvements in the living environment such as preventing soiling of laundry and pollution of agricultural products. The suppression of quantity has come to be screamed strongly. However, conventional dry cyclones, dry electrostatic precipitators, etc. have limitations on sintering exhaust gas,
It has become difficult to say that the amount of dust fall is sufficiently suppressed. What is considered here is to introduce a bag filter that is relatively inexpensive in equipment, has extremely good dust collection performance, and can reduce the amount of dust discharged from the chimney.
しかし、焼結機の主排気ガスにはバグフィルター使用上
下記の問題があり、これまでこの焼結機の主排気ライン
にはバグフィルターが使用されなかった。However, the main exhaust gas of the sintering machine has the following problems in using the bag filter, and so far, the main exhaust line of this sintering machine has not used the bag filter.
(1) 焼結機の起動時、排ガス温度が低く、焼結原料
から持ち込まれた水分がメインダクト、ガス清浄機等の
ガス流停滞域で結露し、排ガス中に含まれているアルカ
リ系をはじめとするダストや硫黄酸化物等の腐食性成分
と結合及び化合し、メインダクト、ガス清浄機等の構成
物に付着したり、又それらの構成物を腐食する。したが
って、バグフィルター使用の場合、濾布の目詰りによる
圧損増加、濾布や濾布取付け金具の腐食劣化をおこすお
それが多分にある。(1) When the sintering machine is started up, the exhaust gas temperature is low, and the moisture introduced from the sintering raw material condenses in the gas flow stagnation area of the main duct, gas purifier, etc. It binds to and combines with corrosive components such as dust and sulfur oxides, and adheres to components such as main ducts and gas purifiers, or corrodes those components. Therefore, when a bag filter is used, there is a possibility that pressure loss will increase due to clogging of the filter cloth, and that the filter cloth and the filter cloth fitting will be corroded and deteriorated.
(2) 一方、焼結機の突発停止時、あるいは一般的操
業においても排ガス温度が200℃以上の異常高温になる
ことがあり、焼結原料から来る可燃物、焼結機のシール
用のグリース等が燃焼する恐れもある。したがって、バ
グフィルターの場合、この排ガス温度の高温と可燃物の
燃焼により濾布に引火し、焼損を招く恐れが多分にあっ
た。(2) On the other hand, the exhaust gas temperature may reach an abnormally high temperature of 200 ° C or more even when the sintering machine is suddenly stopped or during general operation. Combustible substances coming from the sintering raw material, grease for sealing the sintering machine There is also a risk of burning. Therefore, in the case of a bag filter, there is a possibility that the filter cloth may be ignited by the high exhaust gas temperature and the burning of combustibles, resulting in burning.
本発明は、焼結機の主排気ラインにバグフィルターを使
用する場合において、前記バグフィルター使用上の問題
点を解決して、主排気ラインのバグフィルター使用によ
るガス清浄度の高い清浄方法を提供する。The present invention provides a cleaning method with a high gas cleanliness by using a bag filter in the main exhaust line by solving the problems in using the bag filter in the case of using the bag filter in the main exhaust line of the sintering machine. To do.
本発明は、焼結機の主排気ガスの清浄ラインにガス清浄
装置としてバグフィルターを使用する焼結機の主排気ガ
スの清浄方法であり、焼結機操業初期の主排気ガス温度
が低い場合におけるバグフィルター濾布への結露を防止
して濾布の目詰りを防止し、焼結機停止時等の異常昇温
によるバグフィルター濾布の焼損を防止する。必要に応
じて、主排気ガスラインをバグフィルター使用ラインと
乾式電気集塵機使用ラインとの2ラインで構成して使い
分け、更には、焼結機の主排気ガスの清浄ラインにおい
てガス清浄と同時に脱硫、排熱回収を行う。The present invention is a method for cleaning a main exhaust gas of a sintering machine, which uses a bag filter as a gas cleaning device in a main exhaust gas cleaning line of the sintering machine, when the temperature of the main exhaust gas is low at the beginning of the operation of the sintering machine. In this case, the dew condensation on the bag filter filter cloth is prevented to prevent the filter cloth from being clogged and prevent the bag filter filter cloth from being burned due to an abnormal temperature rise such as when the sintering machine is stopped. If necessary, the main exhaust gas line consists of two lines, a bag filter use line and a dry electrostatic precipitator use line, and used properly. Furthermore, in the main exhaust gas cleaning line of the sintering machine, desulfurization is performed simultaneously with gas cleaning. Exhaust heat recovery.
結露はメインダクト、バグフィルターのガス流停滞域で
起こることが多く、その時期は主排気ガス温度が低い焼
結機操業開始から約30〜60分の間である。従って、この
時期に主排気ガス温度を水蒸気飽和温度以上にすること
によって結露を防止することができる。Condensation often occurs in the gas flow stagnation area of the main duct and bag filter, which is about 30 to 60 minutes after the start of operation of the sintering machine where the temperature of the main exhaust gas is low. Therefore, dew condensation can be prevented by making the temperature of the main exhaust gas equal to or higher than the steam saturation temperature at this time.
この時期は主排気ガス温度を水蒸気飽和温度以上にする
ためには次の手段がある。At this time, the following means are available to raise the main exhaust gas temperature to the steam saturation temperature or higher.
(1) バグフィルター上流側のメインダクト内に別設
した加熱炉から高温の燃焼ガスを吹き込み、これを焼結
機の主排気ガスと混合することにより昇温する。(1) A high temperature combustion gas is blown from a heating furnace separately provided in the main duct upstream of the bag filter, and this is mixed with the main exhaust gas of the sintering machine to raise the temperature.
(2) バグフィルター本体及びバグフィルター前のメ
インダクトをスチームトレースする。(2) Steam trace the bag filter body and the main duct in front of the bag filter.
(3) 焼結機操業開始前に焼結点火炉で燃料ガス(コ
ークス炉ガス等)を燃焼し、メインダクトを経由して主
排風機で吸引し、メインダクト、バグフィルターを予熱
してから焼結機操業を開始する。(3) Before starting the operation of the sintering machine, burn the fuel gas (such as coke oven gas) in the sintering ignition furnace, suck it in with the main exhaust fan through the main duct, and preheat the main duct and bag filter. Started operation of the sintering machine.
(4) バグフィルターの上流のメインダクトに複数の
バーナーを固設してバーナーで燃焼火炎を生成し、この
燃焼火炎によりメインダクト内の排ガスを昇温する。(4) A plurality of burners are fixedly installed in the main duct upstream of the bag filter to generate combustion flames, and the combustion flames raise the temperature of the exhaust gas in the main ducts.
又、焼結機操業初期の主排気ガス温度の低い時期には、
バグフィルターによるガス清浄ラインを用いない手段と
して、以下のものがある。Also, when the temperature of the main exhaust gas is low at the beginning of the operation of the sintering machine,
The following are means for not using a gas cleaning line with a bag filter.
(5) 焼結機主排気ラインを硫黄酸化物高濃度ライン
(乾式電気集塵機と湿式脱硫装置を設置するライン)と
硫黄酸化物低濃度ライン(バグフィルターを設置するラ
イン)の2ラインに分け、焼結機操業初期の主排気ガス
温度が低い時期は硫黄酸化物高濃度ラインのみを稼働
し、主排気ガス温度が上昇してバグフィルター、濾布の
目詰りの心配がなくなってから両ラインを稼働する。(5) The main exhaust line of the sintering machine is divided into two lines, a high sulfur oxide concentration line (a line for installing a dry electrostatic precipitator and a wet desulfurizer) and a low sulfur oxide concentration line (a line for installing a bag filter). During the period when the main exhaust gas temperature is low at the beginning of the operation of the sintering machine, only the sulfur oxide high concentration line is operated, and both lines are removed after the main exhaust gas temperature rises and there is no concern about clogging of bag filters and filter cloths. Get up and running.
(6) 焼結主排気ラインにバグフィルターと乾式電気
集塵機を並列に設け、焼結機操業初期の主排気ガス温度
が低い時期は乾式電気集塵機ラインを稼働し、主排気ガ
ス温度が上昇した時点でバグフィルターラインに切り換
える。(6) A bag filter and a dry electrostatic precipitator are installed in parallel in the sintering main exhaust line, and when the temperature of the main exhaust gas is low at the beginning of the operation of the sintering machine, the dry electrostatic precipitator line is activated and the main exhaust gas temperature rises. Switch to the bag filter line with.
バグフィルターの結露防止の他の方法、脱硫、熱回収機
能の付加方法として、以下のものがある。Other methods for preventing condensation on the bag filter and methods for adding desulfurization and heat recovery functions are as follows.
(7) バグフィルターの上硫のメインダクトに粉体供
給装置を設け、焼結機操業開始に際して予めその粉体供
給装置から粉体をバグフィルターに供給し、バグフィル
ターの濾布表面に1次濾過層を形成する(所謂、プレコ
ート方法)。(7) A powder supply device is installed in the main duct of the vulcanization of the bag filter, and the powder is supplied from the powder supply device to the bag filter before starting the operation of the sintering machine. A filtration layer is formed (a so-called precoat method).
プレコート用の粉体は吸湿効果の高い消石灰粉、粉コー
クス、焼結環境集塵ダスト等が好ましい。特に、消石灰
粉は焼結操業中常時使用すると脱硫効果も期待できる。
しかし、ここでの捕集ダストの利用性は低下するので、
脱硫効果と供にダクトの利用性も向上させるために以下
の手段がある。The powder for precoating is preferably slaked lime powder, powder coke, sintering environment dust collection dust or the like, which has a high hygroscopic effect. In particular, slaked lime powder can be expected to have a desulfurizing effect if it is constantly used during the sintering operation.
However, the availability of collected dust here is reduced, so
The following measures are available to improve the desulfurization effect as well as the duct availability.
(8) 焼結主排気ラインを硫黄酸化物高濃度ラインと
硫黄酸化物低濃度ラインの2ラインに分け、各々バグフ
ィルターを設け、尚且つ硫黄酸化物高濃度ラインにはガ
ス加熱炉、ボイラー、粉体供給装置を設け、焼結機操業
初期の排ガスの結露防止対策としてガス加熱炉を使用
し、通常操業時にはボイラーで熱回収し、又粉体供給装
置から供給された消石灰粉で脱硫する。(8) The main sintering exhaust line is divided into a sulfur oxide high-concentration line and a sulfur oxide low-concentration line, each provided with a bag filter, and the sulfur oxide high-concentration line is equipped with a gas heating furnace, a boiler, and A powder supply device is provided, and a gas heating furnace is used as a measure to prevent condensation of exhaust gas at the beginning of the operation of the sintering machine. During normal operation, heat is recovered by a boiler and desulfurized with slaked lime powder supplied from the powder supply device.
この場合、硫黄酸化物高濃度ラインのバグフィルターダ
ストは硫黄酸化物と消石灰との反応生成物が含まれるた
め、利用性は低いので廃棄し、硫黄酸化物低濃度ライン
のバグフィルターダクトは再利用出来る。一方、排ガス
の温度上昇防止、即ちバグフィルターの濾布焼損防止対
策としては以下の手段がある。In this case, the bag filter dust on the high concentration line of sulfur oxide contains the reaction product of sulfur oxide and slaked lime, so it is not available and is discarded.The bag filter duct on the low concentration line of sulfur oxide is reused. I can. On the other hand, there are the following means for preventing the temperature rise of the exhaust gas, that is, for preventing the filter cloth from being burnt out of the bag filter.
(9) 焼結機停止時、焼結機と連動し、主排風機前ダ
ンパーの開度を小さくする。(9) When the sintering machine is stopped, it works in conjunction with the sintering machine to reduce the opening of the damper in front of the main exhauster.
(10) 焼結機操業時、バグフィルター前排ガス温度を
管理し、例えば、ある上限温度以上となればメインダク
ト端部から冷風(常温空気)を導入し、排ガス温度をあ
る上限温度以下に維持する。(10) When operating the sintering machine, control the exhaust gas temperature before the bag filter. For example, if the temperature exceeds a certain upper limit temperature, cool air (normal temperature air) is introduced from the end of the main duct to maintain the exhaust gas temperature below the certain upper limit temperature. To do.
(11) 焼結操業時常にバグフィルター前排ガス温度を
管理し、140℃〜160℃であれば焼結原料のうちの可燃物
(炭材)の量を減少させ、160℃以上であれば焼結機を
停止し、主排風機前ダンパーの開度を小さくする。(11) Always control the exhaust gas temperature before the bag filter during the sintering operation, reduce the amount of combustible material (carbonaceous material) in the sintering raw material at 140 ° C to 160 ° C, and burn it at 160 ° C or higher. Stop the binding and reduce the opening of the damper in front of the main exhaust fan.
上記(1)〜(11)の実施に当たっては、各対策の一つ
あるいは複数を採用する事によって、焼結機の主排気ガ
スの清浄ラインにバグフィルターを使用した場合のバグ
フィルター濾布への目詰りによるガス清浄特性の低下を
抑制すると共にバグフィルター濾布の焼損を防止してバ
グフィルター寿命を延長し、併せて脱硫、熱回収等も有
利に行うことができる。In carrying out the above (1) to (11), by adopting one or more of each measure, it is possible to apply a bag filter to the filter cloth when the bag filter is used in the main exhaust gas cleaning line of the sintering machine. It is possible to prevent deterioration of the gas cleaning property due to clogging, prevent burning of the bag filter filter cloth, extend the life of the bag filter, and also perform desulfurization, heat recovery, etc. advantageously.
以下、図面を参照しながら本発明の実施例を説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第1図は、別設したガス燃焼炉からの高温燃焼ガスを焼
結排ガス中に混合してその温度を上昇させることによっ
てメインダクト、バグフィルターにおける結露を防止す
る例のフロー図である。FIG. 1 is a flow chart of an example of preventing dew condensation in a main duct and a bag filter by mixing high temperature combustion gas from a separately provided gas combustion furnace into sintering exhaust gas and raising its temperature.
この例においては焼結機1の風箱をメインダクト20と連
結し、このメインダクト20に設けられたバグフィルター
2の後の主排風機4により点火炉9で点火後の焼結機1
を経て各風箱から排ガスを吸引する焼結主排気ラインに
おいて、バグフィルター2前のメインダクト20近くにガ
ス加熱炉7を設け、焼結機操業初期の主排気ガス温度が
低い時期に、このガス加熱炉7で例えば高炉ガスを燃焼
し、この高温の燃焼ガスを昇圧してバグフィルター2の
上硫側のメインダクト20内に吹き込んで主排気ガスと混
合し、これを結露の心配のない温度まで上昇させる。こ
の場合、この時期における主排気ガスの水分、流量、温
度の変化を考慮して、バグフィルターへの導入温度が結
露温度以上になるようにガス加熱炉7からの高温燃焼ガ
スの吹き込み条件を設定する。In this example, the air box of the sintering machine 1 is connected to the main duct 20, and the main exhaust fan 4 after the bag filter 2 provided in the main duct 20 ignites the sintering machine 1 in the ignition furnace 9.
A gas heating furnace 7 is provided near the main duct 20 in front of the bag filter 2 in the sintering main exhaust line that sucks the exhaust gas from each wind box through the air conditioner, and when the temperature of the main exhaust gas is low at the beginning of the operation of the sintering machine, For example, blast furnace gas is combusted in the gas heating furnace 7, and this high temperature combustion gas is pressurized and blown into the main duct 20 on the vulcanization side of the bag filter 2 and mixed with the main exhaust gas, so that there is no fear of dew condensation. Raise to temperature. In this case, in consideration of the changes in the water content, flow rate, and temperature of the main exhaust gas at this time, the conditions for blowing the high-temperature combustion gas from the gas heating furnace 7 are set so that the temperature introduced into the bag filter becomes the condensation temperature or higher. To do.
なお、加熱炉を設けないで、例えば別系から高温ガスを
導入するようにしても良い。Note that, for example, a high temperature gas may be introduced from another system without providing a heating furnace.
第2図は、焼結操業開始に先立って焼結機点火炉で燃料
ガスを燃焼させ、この燃焼ガスによってメインダクト、
バグフィルターを予熱して結露を防止する例のフロー図
である。この例においては、点火炉9で焼結機1の操業
開始に燃料ガスを燃焼し、メインダクト20を経由して主
排風機4で吸引し、メインダクト20、バグフィルター2
の表面温度が例えば120〜160℃程度になるまで予熱した
後に焼結操業を開始させることによって、操業初期の温
度の低い主排気ガスをバクフィルターに導入しても結露
を生じないようにしている。この予熱条件は、予め容易
に設定することができる。第3図は、焼結機の主排気ガ
スの清浄ラインを2つのラインで構成し、この2つのラ
インを使い分けることによってバグフィルターにおける
結露を防止する例のフロー図である。この例において
は、焼結機の主排気ラインを硫黄酸化物高濃度ライン
(排拡側からの排ガス吸引ラインで乾式電気集塵機10と
湿式脱硫装置11を持つ)と硫黄酸化物低濃度ライン(給
拡側からの排ガス吸引ラインでバグフィルター2を持
つ)の2つのラインに分け、焼結機操業初期の主排気ガ
ス温度が低い時期は硫黄酸化物高濃度ラインのみでガス
清浄を行い、主排気ガス温度が上昇し結露の心配が解消
された時点でバグフィルターを使用する硫黄酸化物低濃
度ラインによるガス清浄も開始し、両ラインでガス清浄
を行う。この場合、硫黄酸化物低濃度ラインのガス清浄
を開始する時期は予め操業条件に応じて設定しておいて
も良いし、主排気ガスの温度を測定して主排気ガスが所
定温度以上になったことを確認した時点としても良い。FIG. 2 shows that the fuel gas is burned in the sinter ignition furnace prior to the start of the sintering operation, and the combustion gas causes the main duct,
It is a flowchart of the example which preheats a bag filter and prevents dew condensation. In this example, fuel gas is burned in the ignition furnace 9 to start the operation of the sintering machine 1, and is sucked by the main exhauster 4 via the main duct 20, and the main duct 20 and the bag filter 2 are sucked.
By preheating until the surface temperature of the product reaches, for example, 120 to 160 ° C, the sintering operation is started to prevent dew condensation even when the main exhaust gas with a low temperature in the initial operation is introduced into the back filter. . This preheating condition can be easily set in advance. FIG. 3 is a flow chart of an example in which the main exhaust gas cleaning line of the sintering machine is composed of two lines and these two lines are used properly to prevent dew condensation on the bag filter. In this example, the main exhaust line of the sintering machine is a sulfur oxide high concentration line (the exhaust gas suction line from the exhaust expansion side has the dry electrostatic precipitator 10 and the wet desulfurization device 11) and the sulfur oxide low concentration line (supply The exhaust gas suction line from the expansion side is divided into two lines (having a bag filter 2), and when the temperature of the main exhaust gas is low at the beginning of the sintering machine operation, gas purification is performed only with the sulfur oxide high-concentration line. When the gas temperature rises and the concern about dew condensation is resolved, the gas cleaning with the sulfur oxide low-concentration line using the bag filter will be started, and the gas cleaning will be performed on both lines. In this case, the timing for starting the gas cleaning of the sulfur oxide low-concentration line may be set in advance according to the operating conditions, or the temperature of the main exhaust gas may be measured and the main exhaust gas may reach a predetermined temperature or higher. It may be the time when it is confirmed.
尚、硫黄酸化物低濃度ラインの主排気ガスは硫黄酸化物
低濃度ラインの排ガスより温度が高いので、乾式電気集
塵機10の前に排ガス温度計21とダンパー12を設けると共
に硫黄酸化物低濃度ラインのバグフィルター2の前に排
ガス温度計22とダンパー13を設け、水蒸気結露開始温度
以上に常に維持するように温度調節装置23でバンパー1
2、ダンパー13の開度を自動調整しても良い。すなわ
ち、硫黄酸化物低濃度ラインの主排気ガス温度が低い場
合に、硫黄酸化物高濃度ラインの温度の高い主排気ガス
硫黄酸化物低濃度ラインの主排気ガスに混合して硫黄酸
化物低濃度ラインの主排気ガスを増加させると共に、そ
の温度をある程度上昇させることができる。Since the main exhaust gas of the sulfur oxide low concentration line has a higher temperature than the exhaust gas of the sulfur oxide low concentration line, an exhaust gas thermometer 21 and a damper 12 are provided in front of the dry electrostatic precipitator 10 and the sulfur oxide low concentration line is also provided. An exhaust gas thermometer 22 and a damper 13 are installed in front of the bag filter 2 of No. 1, and a bumper 1 is provided with a temperature control device 23 so as to always maintain the temperature above the steam condensation start temperature.
2. The opening of the damper 13 may be automatically adjusted. That is, when the temperature of the main exhaust gas in the low sulfur oxide concentration line is low, the main exhaust gas with a high temperature in the high sulfur oxide concentration line is mixed with the main exhaust gas in the low sulfur oxide concentration line to reduce the low sulfur oxide concentration. The main exhaust gas of the line can be increased and its temperature can be raised to some extent.
第4図は、焼結機の主清浄ガスの洗浄ラインにバグフィ
ルター2と乾式電気集塵機10を並列に設けて切り替え使
用する例のフロー図である。この例においては、乾式電
気集塵機10を持ったラインとバグフィルター2を持った
ラインとを並列ラインとし、焼結機操業初期の排ガス温
度が低い時期は乾式電気集塵機10ラインでガス清浄を行
い、排ガス温度が上昇した時点でバグフィルター2ライ
ンでのガス清浄に切り替える。この切り替えの時期は、
予め操業条件に応じてタイマー設定しても良く、又、主
排気ガス温度を測定して所定の温度になった時点で切り
替えるようにしても良い。FIG. 4 is a flow chart of an example in which the bag filter 2 and the dry electrostatic precipitator 10 are provided in parallel in the cleaning line of the main clean gas of the sintering machine and are switched and used. In this example, the line having the dry electrostatic precipitator 10 and the line having the bag filter 2 are parallel lines, and gas cleaning is performed by the dry electrostatic precipitator 10 line when the exhaust gas temperature is low at the beginning of the operation of the sintering machine. When the exhaust gas temperature rises, switch to gas cleaning in the bag filter 2 line. The timing of this switch is
A timer may be set in advance according to the operating conditions, or the main exhaust gas temperature may be measured and switched when the temperature reaches a predetermined temperature.
第5図は、焼結機主排気ガスの清浄ラインのバグフィル
ターの濾布の漏れを防止することによって結露の影響を
軽減する例のフロー図である。この例においては、バグ
フィルター2上硫のメインダクト20の近くに粉体供給装
置16を設け、焼結機起動前に粉体供給装置16から粉体を
メインダクト20内に吹き込んで主排風機で吸引すること
によって、第9図に示すようにバグフィルター2の濾布
24の表面に一次濾過層25を形成する。ここで、粉体とし
ては主として吸湿性のある脱硫性もある安価な消石灰
等、カルシウム系のものが用いられる。FIG. 5 is a flow chart of an example of reducing the influence of dew condensation by preventing the filter cloth from leaking from the bag filter in the main exhaust gas cleaning line of the sintering machine. In this example, a powder supply device 16 is provided near the main duct 20 of the bag filter 2 and the main air blower blows powder into the main duct 20 from the powder supply device 16 before starting the sintering machine. As shown in FIG. 9, the filter cloth of the bag filter 2 is sucked by
A primary filtration layer 25 is formed on the surface of 24. Here, as the powder, a calcium-based powder such as inexpensive slaked lime that is hygroscopic and desulfurizing is mainly used.
第6図は、第1図、第3図、第5図に示される焼結機の
主排気ガスの清浄ラインを折哀的に組合せた例のフロー
図である。この例においては、焼結機主排気ラインを硫
黄酸化物高濃度ラインと硫黄酸化物濃度ラインの2ライ
ンに分け、各々バグフィルター2を設け、尚且つ硫黄酸
化物高濃度ラインにはガス加熱炉7,ボイラー26,粉体供
給装置16を設け、焼結機操業初期の排ガスの結露防止対
策としてガス加熱炉7を使用し、通常操業時にはボイラ
ー26で熱回収し、又粉体供給装置16から供給された消石
灰粉で脱硫する等、主排気ガスの清浄以外の機能を付与
している。一方、硫黄酸化物低濃度ラインにおいては通
常操業状態で主排気ガス清浄のみを行う。FIG. 6 is a flow chart of an example in which the cleaning lines for the main exhaust gas of the sintering machine shown in FIGS. In this example, the main exhaust line of the sintering machine is divided into a sulfur oxide high-concentration line and a sulfur oxide high-concentration line, each provided with a bag filter 2, and the sulfur oxide high-concentration line has a gas heating furnace. 7, Boiler 26, Powder supply device 16 is installed, and gas heating furnace 7 is used as a measure to prevent condensation of exhaust gas at the beginning of the operation of the sintering machine. During normal operation, heat is recovered by the boiler 26, and from the powder supply device 16 It has functions other than cleaning the main exhaust gas, such as desulfurization with the supplied slaked lime powder. On the other hand, in the sulfur oxide low-concentration line, only the main exhaust gas is cleaned during normal operation.
第7図は、焼結機停止時の主排気ガスの清浄ラインにお
いて排ガス温度が異常上昇した場合、バグフィルターの
焼損を防止する例のフロー図である。この例において
は、焼結機停止時、焼結機1の駆動電動機17の停止信号
により、それと連動し主排風機4前のダンパー3を制御
してその開度を小さくすることにより、主排風機4によ
る主排気ガスの吸引を停止して主排気ガスが異常上昇す
るのを抑制し、バグフィルター2の濾布の焼損を防止す
る。FIG. 7 is a flow chart of an example of preventing burnout of the bag filter when the exhaust gas temperature abnormally rises in the main exhaust gas cleaning line when the sintering machine is stopped. In this example, when the sintering machine is stopped, the damper 3 in front of the main exhauster 4 is controlled in conjunction with the stop signal of the drive motor 17 of the sintering machine 1 to reduce the opening degree of the main exhaust machine 4, The suction of the main exhaust gas by the air blower 4 is stopped to prevent the main exhaust gas from rising abnormally, and the filter cloth of the bag filter 2 is prevented from burning.
第8図は、焼結通常操業時の主排気ガスの清浄ラインに
おける主排気ガス温度が上昇した場合、バグフィルター
の焼損を防止する例のフロー図である。この例において
は、バグフィルター2前の排ガス温度を常時管理し、例
えば、ある上限温度以上となればこの排ガスの流量とそ
の温度等に応じて焼結機下のメインダクト20の端部の冷
風(常温空気)導入装置18から上限温度以下にするため
の所要量の冷風をメインダクト20内に導入し、排ガス温
度を上限温度以下に維持する。FIG. 8 is a flow chart of an example of preventing burning of the bag filter when the temperature of the main exhaust gas in the main exhaust gas cleaning line during normal sintering operation rises. In this example, the exhaust gas temperature in front of the bag filter 2 is constantly controlled. For example, if the exhaust gas temperature exceeds a certain upper limit temperature, the cool air at the end of the main duct 20 under the sintering machine is adjusted according to the flow rate of the exhaust gas and its temperature. (Room temperature air) A required amount of cold air for controlling the temperature below the upper limit temperature is introduced into the main duct 20 from the introduction device 18 to maintain the exhaust gas temperature below the upper limit temperature.
本発明においては、焼結機操業初期の主排気ガス温度の
低い時期に主排気ガス中の水分の結露を未然に防止する
ことが出来、又焼結機停止時、又は通常操業時の主排気
ガス温度の異常上昇も防止することが出来、バグフィル
ターの濾布の目詰り、濾布や濾布の取付け金具の腐食又
は劣化、濾布の焼損又は劣化を起こすことなく、設備費
及びランニングコストが安価で排出媒塵量低減性能を高
位に維持することが出来る。In the present invention, it is possible to prevent dew condensation of water in the main exhaust gas when the temperature of the main exhaust gas is low at the beginning of the operation of the sintering machine, and when the sintering machine is stopped or during the normal operation of the main exhaust gas. It is possible to prevent an abnormal rise in the gas temperature, without clogging of the filter cloth of the bag filter, corrosion or deterioration of the filter cloth or the metal fittings of the filter cloth, burnout or deterioration of the filter cloth, and equipment cost and running cost. However, it is cheap and the performance of reducing the amount of discharged dust can be maintained at a high level.
第1〜6図は本発明の焼結機起動時の結露防止対策のフ
ロー図であり、第7〜8図は本発明の焼結機停止時又は
通常時の排ガス温度上昇防止対策のフロー図であり、第
9図はバグフィルター内部の濾布のプレコート状況を示
す図であり、第10図は従来の焼結主排気ラインのフロー
の一例を示す図である。 1:焼結機 2:バグフィルター 3:ダンパー 4:主排風機 5:消音機 6:煙突 7:ガス加熱炉 8:焼結機装入装置 9:点火炉 10:乾式電気集塵機 11:湿式脱硫装置 12,13:ダンパー 14:昇圧機前ダンパー 15:昇圧機 16:粉体供給装置 17:駆動電動機 18:冷風導入装置 19:乾式サイクロン 20:メインダクト 21,22:排ガス温度計 23:温度調節装置 24:濾布 25:一次濾過層 26:ボイラー1 to 6 are flow charts for preventing dew condensation at the time of starting the sintering machine of the present invention, and FIGS. 7 to 8 are flow charts for preventing exhaust gas temperature rise at the time of stopping the sintering machine of the present invention or during normal times. FIG. 9 is a diagram showing the precoating condition of the filter cloth inside the bag filter, and FIG. 10 is a diagram showing an example of the flow of the conventional sintering main exhaust line. 1: Sintering machine 2: Bag filter 3: Damper 4: Main air exhauster 5: Muffler 6: Chimney 7: Gas heating furnace 8: Sintering machine charging device 9: Ignition furnace 10: Dry electrostatic precipitator 11: Wet desulfurization Equipment 12, 13: Damper 14: Booster front damper 15: Booster 16: Powder supply device 17: Drive motor 18: Cold air introduction device 19: Dry cyclone 20: Main duct 21, 22: Exhaust gas thermometer 23: Temperature control Device 24: Filter cloth 25: Primary filtration layer 26: Boiler
Claims (15)
グフィルターを使用する焼結機の主排気ガスの清浄ライ
ンにあって、焼結機操業初期の主排気ガス温度が低い場
合は、バグフィルターの濾布温度を結露温度以上に上昇
させて濾布への結露を防止し、濾布の目詰りを防止する
ことを特徴とする焼結機の主排気ガスの清浄方法。1. A main exhaust gas cleaning line of a sintering machine which uses a bag filter as a gas cleaning device between the sintering machine and a chimney, and when the temperature of the main exhaust gas is low at the beginning of the operation of the sintering machine. A method for cleaning main exhaust gas of a sintering machine, which comprises raising the filter cloth temperature of a bag filter to a temperature above the condensation temperature to prevent condensation on the filter cloth and preventing clogging of the filter cloth.
ターの上流側のメインダクトの周囲に吹き込み装置を設
け、該吹き込み装置から高温燃焼ガスをメインダクト内
に吹き込み主排気ガスに混合して該ガスを昇温し、バグ
フィルターの濾布温度を結露温度以上に上昇させること
を特徴とする焼結機の主排気ガスの清浄方法。2. The method according to claim 1, wherein a blowing device is provided around the main duct upstream of the bag filter, and high temperature combustion gas is blown into the main duct from the blowing device to mix it with the main exhaust gas. A method for cleaning main exhaust gas of a sintering machine, which comprises raising the temperature of gas to raise the temperature of a filter cloth of a bag filter to a temperature above dew condensation temperature.
開始前に焼結点火炉で燃料ガスを燃焼し、この燃焼ガス
をメインダクトを経由して主排風機で吸引し、バグフィ
ルターの濾布温度を結露温度以上に予熱上昇させてから
焼結機を起動することを特徴とする焼結機の主排気ガス
の清浄方法。3. The method according to claim 1, wherein the fuel gas is combusted in a sintering ignition furnace before the operation of the sintering machine is started, and the combustion gas is sucked by a main exhaust fan through a main duct, and a bag filter is used. A method for cleaning main exhaust gas of a sintering machine, which comprises starting the sintering machine after preheating the filter cloth temperature to above the condensation temperature.
ター上流側のメインダクトに複数のバーナーを固設して
バーナーにより燃焼火炎を生成し、該燃焼火炎により、
メインダクト内を通過する主排気ガスを結露温度以上に
上昇させることを特徴とする焼結機の主排気ガスの清浄
方法。4. The method according to claim 1, wherein a plurality of burners are fixedly installed in a main duct upstream of the bag filter, combustion flames are generated by the burners, and the combustion flames generate the combustion flames.
A method for cleaning main exhaust gas of a sintering machine, which comprises raising the temperature of main exhaust gas passing through the main duct to a temperature above dew condensation temperature.
気集塵機と湿式脱硫装置を配設した硫黄酸化物高濃度ラ
インとバグフィルターを配設した硫黄酸化物低濃度ライ
ンとの2ラインに分け、焼結機操業初期の主排気ガス温
度の低い時期は硫黄酸化物高濃度ラインでガス清浄を行
い、主排気ガス温度が上昇してから両ラインでガス清浄
を行うことを特徴とする焼結機の主排気ガスの清浄方
法。5. A main exhaust gas cleaning line of a sintering machine, a dry oxide precipitator and a high-concentration sulfur oxide line equipped with a wet desulfurization device, and a low-concentration sulfur oxide line equipped with a bag filter. It is characterized in that when the temperature of the main exhaust gas is low at the beginning of the operation of the sintering machine, the gas is cleaned with the sulfur oxide high concentration line, and after the temperature of the main exhaust gas rises, the gas is cleaned with both lines. Cleaning method of main exhaust gas of sintering machine.
ィルターラインと乾式電気集塵機ラインを並列に配設
し、焼結機操業初期の主排気ガス温度が低い時期は乾式
電気集塵機ラインでガス清浄を行い、主排気ガス温度が
上昇した時点でバグフィルターラインに切り替えてガス
清浄を行うことを特徴とする焼結機の主排気ガスの清浄
方法。6. A bag filter line and a dry electrostatic precipitator line are arranged in parallel in the main exhaust gas cleaning line of the sintering machine, and the dry electrostatic precipitator line is used when the temperature of the main exhaust gas is low at the beginning of the operation of the sintering machine. A method for cleaning main exhaust gas of a sintering machine, which comprises performing gas cleaning and switching to a bag filter line when the temperature of the main exhaust gas rises to perform gas cleaning.
化物高濃度ラインと硫黄酸化物低濃度ラインとの2ライ
ンに分け、硫黄酸化物高濃度ラインにはバグフィルター
とその上硫側にガス加熱装置とボイラーを配設し、焼結
機操業初期の主排気ガス温度の低い時期はガス加熱装置
からの高温燃焼ガスでメインダクト内の主排気ガスを加
熱、昇温して濾布への結露を防止して濾布の目詰りを防
止し、通常操業時期にはボイラーで熱回収することを特
徴とする焼結機の主排気ガスの清浄方法。7. A main exhaust gas cleaning line of a sintering machine is divided into a sulfur oxide high-concentration line and a sulfur oxide low-concentration line. A gas heating device and a boiler are installed on the side, and when the temperature of the main exhaust gas is low at the beginning of the operation of the sintering machine, the high temperature combustion gas from the gas heating device heats and heats the main exhaust gas in the main duct to filter it. A method for cleaning the main exhaust gas of a sintering machine, which is characterized by preventing condensation on the cloth to prevent clogging of the filter cloth and recovering heat with a boiler during normal operation.
グフィルターを使用する焼結機の主排気ガスの清浄ライ
ンにあって、焼結機の停止等、主排気ガス温度の異常上
昇時はバグフィルターにおける温度上昇を抑制してバグ
フィルターの濾布焼損を防止することを特徴とする焼結
機の主排気ガスの清浄方法。8. A main exhaust gas cleaning line of a sintering machine, which uses a bag filter as a gas cleaning device between the sintering machine and the chimney, and the temperature of the main exhaust gas rises abnormally due to the stop of the sintering machine or the like. A method for cleaning the main exhaust gas of a sintering machine, which is characterized by suppressing the temperature rise in the bag filter to prevent the filter cloth from being burnt out.
止した場合に、焼結機主排風機前ダンパーの開度を小さ
くしてバグフィルターにおける温度上昇を抑制すること
を特徴とする焼結機の主排気ガスの清浄方法。9. The method according to claim 8, wherein when the sintering machine is stopped, the opening of the damper in front of the main exhauster of the sintering machine is reduced to suppress the temperature rise in the bag filter. Cleaning method of main exhaust gas of sintering machine.
ルター上流の焼結機の主排気ガスの温度を測定し、該温
度がバグフィルター濾布焼損温度域にある場合はバグフ
ィルター上流のメインダクト内に冷風を吹き込んでバグ
フィルターにおける温度上昇を抑制することを特徴とす
る焼結機の主排気ガスの清浄方法。10. The method according to claim 8, wherein the temperature of the main exhaust gas of the sintering machine upstream of the bag filter is measured, and when the temperature is in the bag filter cloth burning temperature range, the main duct upstream of the bag filter. A method for cleaning main exhaust gas of a sintering machine, characterized in that cool air is blown into the bag filter to suppress temperature rise in a bag filter.
ルター上流の焼結機の主排気ガスの温度を測定し、該温
度が140〜160℃である場合に焼結原料中の可燃物の量を
減少させ、160℃以上の場合には焼結機を停止し、焼結
機主排風機前のダンパー開度を小さくしてバグフィルタ
ーにおける温度上昇を抑制することを特徴とする焼結機
の主排気ガスの清浄方法。11. The method according to claim 8, wherein the temperature of the main exhaust gas of the sintering machine upstream of the bag filter is measured, and when the temperature is 140 to 160 ° C., the amount of combustible material in the sintering raw material. Of the sintering machine, the sintering machine is stopped when the temperature is 160 ° C or higher, and the damper opening in front of the main exhaust machine of the sintering machine is reduced to suppress the temperature rise in the bag filter. How to clean the main exhaust gas.
ィルターによるガス清浄ラインと乾式電気集塵機による
ガス清浄ラインとに分け、焼結機停止時および操業初期
は乾式電気集塵機によるガス清浄ラインで主排気ガスの
清浄を行い、通常操業時にはバグフィルターによるガス
清浄ラインで主排気ガスの清浄を行い結露によるバグフ
ィルター濾布の目詰りおよび温度上昇によるバグフィル
ター濾布の焼損を防止することを特徴とする焼結機の主
排気ガスの清浄方法。12. The main exhaust gas cleaning line of the sintering machine is divided into a gas cleaning line using a bag filter and a gas cleaning line using a dry electrostatic precipitator, and the gas cleaning line using a dry electrostatic precipitator is used when the sintering machine is stopped and at the beginning of operation. The main exhaust gas is cleaned, and during normal operation, the main exhaust gas is cleaned with a bag filter gas cleaning line to prevent clogging of the bag filter cloth due to condensation and burning of the bag filter cloth due to temperature rise. A method for cleaning the main exhaust gas of a sintering machine.
いて、バグフィルターによる焼結機の主排気ガスの清浄
ラインのバグフィルター上流側の主排気ガス中に脱硫剤
を噴射して該主排気ガスの脱硫も行うことを特徴とする
焼結機の主排気ガスの清浄方法。13. The method according to any one of claims 1 to 12, wherein a desulfurizing agent is injected into the main exhaust gas upstream of the bag filter in the main exhaust gas cleaning line of the sintering machine using the bag filter. A method for cleaning the main exhaust gas of a sintering machine, which also desulfurizes the exhaust gas.
ルターによる主排気ガスの清浄ラインのバグフィルター
上流側のメインダクト内に焼結機操業開始に際して先ず
脱硫剤を噴射してバグフィルター濾布に一次濾過層を形
成することを特徴とする焼結機の主排気ガスの清浄方
法。14. The method according to claim 13, wherein a desulfurizing agent is first injected into the main duct on the upstream side of the bag filter in the main exhaust gas cleaning line by the bag filter to inject the desulfurizing agent into the bag filter cloth. A method for cleaning main exhaust gas of a sintering machine, which comprises forming a primary filtration layer.
方法において、バグフィルターの上硫側に熱回収ボイラ
ーを設けてバグフィルターに導入される主排気ガスの熱
回収も行うことを特徴とする焼結機の主排気ガスの清浄
方法。15. The method according to any one of claims 1 to 6 and 8 to 14, wherein a heat recovery boiler is provided on the vulcanization side of the bag filter to recover heat of the main exhaust gas introduced into the bag filter. A method for cleaning the main exhaust gas of a sintering machine, which is characterized by
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29344890A JPH0757894B2 (en) | 1990-10-30 | 1990-10-30 | Cleaning method of main exhaust gas of sintering machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29344890A JPH0757894B2 (en) | 1990-10-30 | 1990-10-30 | Cleaning method of main exhaust gas of sintering machine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04168235A JPH04168235A (en) | 1992-06-16 |
| JPH0757894B2 true JPH0757894B2 (en) | 1995-06-21 |
Family
ID=17794897
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29344890A Expired - Lifetime JPH0757894B2 (en) | 1990-10-30 | 1990-10-30 | Cleaning method of main exhaust gas of sintering machine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0757894B2 (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007245048A (en) * | 2006-03-17 | 2007-09-27 | Sintokogio Ltd | Dust collector |
| JP5465081B2 (en) * | 2010-04-30 | 2014-04-09 | キヤノン株式会社 | Inkjet recording apparatus and method |
| JP5486482B2 (en) * | 2010-12-20 | 2014-05-07 | 株式会社神戸製鋼所 | Exhaust gas control method when the sintering machine is stopped |
| CN102278735B (en) * | 2011-07-01 | 2013-03-20 | 江苏中天能源设备有限公司 | Heat pipe exhaust-heat boiler internally built on big and small flues of sintering machine |
| CN106288834A (en) * | 2016-09-28 | 2017-01-04 | 江苏垦乐节能环保科技有限公司 | A kind of system promoting sintering flue-gas temperature and its implementation |
| CN107913570A (en) * | 2017-09-22 | 2018-04-17 | 广东林顿重工股份有限公司 | A kind of bellows device |
| CN109224832B (en) * | 2018-11-26 | 2024-03-12 | 中冶焦耐(大连)工程技术有限公司 | A coke oven flue gas desulfurization and dust removal system and method |
| CN118816214B (en) * | 2024-07-23 | 2025-01-28 | 扬州永锋工业设备安装有限公司 | An incinerator waste gas treatment and recycling device |
-
1990
- 1990-10-30 JP JP29344890A patent/JPH0757894B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04168235A (en) | 1992-06-16 |
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