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JP5487593B2 - Coke oven flue dust collector startup method - Google Patents
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JP5487593B2 - Coke oven flue dust collector startup method - Google Patents

Coke oven flue dust collector startup method Download PDF

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JP5487593B2
JP5487593B2 JP2008287507A JP2008287507A JP5487593B2 JP 5487593 B2 JP5487593 B2 JP 5487593B2 JP 2008287507 A JP2008287507 A JP 2008287507A JP 2008287507 A JP2008287507 A JP 2008287507A JP 5487593 B2 JP5487593 B2 JP 5487593B2
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dust collector
flue
exhaust gas
chimney
coke oven
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JP2010111824A (en
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有博 菅野
友則 佐藤
辰弘 小林
匡洋 今田
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Nippon Steel Corp
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Nippon Steel and Sumitomo Metal Corp
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Description

本発明はコークス炉用煙道集塵機の立ち上げ方法に関するものである。   The present invention relates to a method for starting a coke oven flue dust collector.

コークス炉の老朽化等に起因してコークス炉内の炭化室と加熱室とを仕切る煉瓦壁のシール性が低下すると、炭化室内に装入された石炭から揮発した燃焼性ガスの一部が加熱室に漏れ、加熱室で不完全燃焼して煤が発生する。このような煤等のダストがコークス炉から排出される排ガス中に含まれる場合、排ガスが黒煙化する。公害等の環境問題の観点から、黒煙対策が必要となる。当該黒煙対策として、従来より、コークス炉から煙突に至る煙道部に電気集塵機やバグフィルターを設置して黒煙を除去する方法が採用されている(例えば、特許文献1)。   If the sealing performance of the brick wall that separates the carbonization chamber and the heating chamber in the coke oven deteriorates due to aging of the coke oven, a part of the combustible gas volatilized from the coal charged in the carbonization chamber is heated. Leaked into the chamber and burned incompletely in the heating chamber, generating soot. When dust such as soot is contained in the exhaust gas discharged from the coke oven, the exhaust gas becomes black smoke. From the viewpoint of environmental problems such as pollution, black smoke countermeasures are necessary. As a measure against the black smoke, conventionally, a method of removing black smoke by installing an electric dust collector or a bag filter in a flue portion from a coke oven to a chimney has been adopted (for example, Patent Document 1).

当該集塵機は、既設のコークス炉の劣化に伴う黒煙対策として設置されるものであるため、コークス炉付近に集塵機の設置スペースが確保できない場合もある。このような場合、コークス炉から集塵機を経て煙突へと排ガスを導く煙道配管が長くなる。煙道配管が長くなると、煙突に導入されるまでに排ガス温度が低下してしまい、ガス比重が高くなる結果、煙突のドラフト力が低下して煙突から速やかにガスが排出されない現象が生じる。煙突から排出されないガスは煙道配管内を循環して煙道圧力を上昇させ、煙道圧力がコークス炉の操業圧力を超過してしまう結果、集塵機を立ち上げることができないという問題を生じていた。
特開昭56−104992号公報
Since the dust collector is installed as a measure against black smoke accompanying deterioration of the existing coke oven, there may be a case where the installation space for the dust collector cannot be secured near the coke oven. In such a case, the flue pipe that leads the exhaust gas from the coke oven to the chimney through the dust collector becomes long. When the flue pipe becomes long, the exhaust gas temperature decreases before being introduced into the chimney, and the gas specific gravity increases. As a result, the draft force of the chimney decreases and a gas is not quickly discharged from the chimney. The gas that is not discharged from the chimney circulates in the flue pipe and raises the flue pressure. As a result of the flue pressure exceeding the operating pressure of the coke oven, the dust collector cannot be started up. .
JP 56-104992 A

本発明の目的は、前記問題を解決し、コークス炉から集塵機を経て煙突へと排ガスを導く煙道配管が長くなった場合でも、煙道圧力がコークス炉の操業圧力を超過することのなく、安定的に立ち上げることのできる煙道集塵機の立ち上げ方法を提供することである。   The object of the present invention is to solve the above problems, and even when the flue pipe leading the exhaust gas from the coke oven to the chimney through the dust collector becomes long, the flue pressure does not exceed the operating pressure of the coke oven, It is to provide a method for starting a flue dust collector that can be started stably.

上記課題を解決するためになされた本発明のコークス炉用煙道集塵機の立ち上げ方法は、排ガスをコークス炉から集塵機を経由せず煙突に導く第一の煙道と排ガスをコークス炉から集塵機を経由して煙突に導く第二の煙道とを有するコークス炉に使用される煙道集塵機の立ち上げ方法であって、第一の煙道には、コークス炉から煙突への排ガス流量を調整する煙道調整弁を備え、第二の煙道には、集塵機から煙突への排ガス流量を調整する集塵機調整弁を備え、煙道集塵機立ち上げ開始時には、煙道調整弁を開状態としつつ、集塵機調整弁を、集塵機入側の排ガス温度上昇と共に、閉状態から徐々に開状態としていき、前記第一の煙道を経由する排ガスと第二の煙道を経由する排ガスを前記煙突下部で合流した合流ガス温度を、該煙突のドラフト圧が担保される排ガス温度に保持することにより、煙道集塵機を立ち上げることを特徴とするものである。 In order to solve the above-mentioned problems, a method for starting a flue dust collector for a coke oven according to the present invention includes a first flue for guiding exhaust gas from a coke oven to a chimney without going through the dust collector, and an exhaust gas from the coke oven to the dust collector. Of a flue dust collector used in a coke oven having a second flue leading to the chimney via the first flue, wherein the exhaust gas flow rate from the coke oven to the chimney is adjusted in the first flue The second flue is equipped with a dust collector adjustment valve that adjusts the exhaust gas flow rate from the dust collector to the chimney, and when the flue dust collector starts up, the flue adjustment valve is opened, As the exhaust gas temperature rises on the dust collector inlet side, the dust collector adjustment valve is gradually opened from the closed state, and the exhaust gas passing through the first flue and the exhaust gas passing through the second flue merge at the lower part of the chimney It was the combined gas temperature, of the chimney de By maintaining the exhaust gas temperature shift pressure is ensured, and is characterized in increasing Rukoto up the flue dust collector.

請求項2記載の発明は、請求項1記載のコークス炉用煙道集塵機の立ち上げ方法であって、前記集塵機入側の排ガス温度T を指標として、T が一定温度に到達ごとに、集塵機調整弁を段階的に開状態としていくことを特徴とするものである。
The invention according to claim 2 is a method for starting up a flue dust collector for a coke oven according to claim 1, wherein the exhaust gas temperature T 0 at the inlet side of the dust collector is used as an index, and when T 0 reaches a certain temperature, The dust collector adjusting valve is opened in stages.

本発明に係る煙道集塵機の立ち上げ方法は、コークス炉の近辺に集塵機を設置するスペースがない場合に、コークス炉から集塵機を経由して煙突に導く第二の煙道配管が長くなり、その結果、集塵機立ち上げ当初に第二の煙道配管を経由する排ガス温度のみでは十分な煙突のドラフト圧を得られずに、煙道圧力が操業圧力を超えて上昇してしまい、集塵機の立ち上げが困難な場合に適用することで、集塵機の立ち上げを可能とする技術である。集塵機の立ち上げ時、集塵機内部及び第二の煙道配管内温度はコークス炉からの排出ガス温度よりも著しく低温となっているため、コークス炉からの排出ガスが第二の煙道配管を通過して煙突の下部に到達するまでの間に、熱エネルギーを吸収され排ガス温度が低下してしまう。本発明によれば、コークス炉から煙突に直接高温の排ガスを導入する第一の煙道と、コークス炉から集塵機を介して煙突に排ガスを導入する第二の煙道の各々から排ガスを導入し、集塵機内温度および第二の煙道配管内温度が十分上昇していない立ち上げ初期過程においては第二の煙道を経由する排ガス量を制限しつつ、第一の煙道を経由する排ガスの有する熱エネルギーによって、煙突下部で合流する排ガス温度を煙突のドラフト圧が担保される範囲とすることにより、第二の煙道配管の長さの如何に関わらず、安定的に集塵機の立ち上げを行うことを可能とした。   When there is no space for installing a dust collector near the coke oven, the second flue pipe leading from the coke oven to the chimney via the dust collector becomes long. As a result, only the exhaust gas temperature via the second flue pipe at the beginning of the dust collector does not provide sufficient chimney draft pressure, and the flue pressure rises above the operating pressure, causing the dust collector to start up. It is a technology that makes it possible to start up a dust collector by applying it when it is difficult. When starting up the dust collector, the temperature inside the dust collector and the second flue pipe is significantly lower than the exhaust gas temperature from the coke oven, so the exhaust gas from the coke oven passes through the second flue pipe. And until it reaches the lower part of the chimney, the heat energy is absorbed and the exhaust gas temperature falls. According to the present invention, exhaust gas is introduced from each of the first flue for introducing high-temperature exhaust gas directly from the coke oven to the chimney and the second flue for introducing exhaust gas from the coke oven to the chimney via a dust collector. In the initial start-up process when the temperature inside the dust collector and the temperature inside the second flue pipe are not sufficiently increased, the amount of exhaust gas passing through the first flue is restricted while limiting the amount of exhaust gas passing through the second flue. By setting the exhaust gas temperature that merges at the lower part of the chimney to a range where the draft pressure of the chimney is secured by the thermal energy that is possessed, the dust collector can be started up stably regardless of the length of the second flue pipe Made it possible to do.

図1には、本発明の集塵機立ち上げ方法に係るコークス炉の排ガスフローを示している。ここで、集塵機の立ち上げとは、集塵機を新たに設置した場合や、集塵機のメンテナンス作業を行った後に、コークス炉から集塵機内を経由して煙突へと抜けてゆく排ガス流路を形成することを言う。煙突から排ガスが排出されるためには、下記の表1に示すような、所定のドラフト圧が必要であり、当該ドラフト圧を得るためには、煙突下部における排ガス温度が所定温度以上必要となる。   FIG. 1 shows an exhaust gas flow of a coke oven according to the dust collector startup method of the present invention. Here, the start-up of the dust collector refers to the formation of an exhaust gas flow path that passes from the coke oven to the chimney through the dust collector after a new dust collector is installed or maintenance work is performed on the dust collector. Say. In order to exhaust the exhaust gas from the chimney, a predetermined draft pressure as shown in Table 1 below is required. In order to obtain the draft pressure, the exhaust gas temperature at the lower part of the chimney is required to be higher than the predetermined temperature. .

Figure 0005487593
Figure 0005487593

集塵機は、コークス炉の老朽化に伴う排ガスの黒煙化対策として、後発的に設置されるものである。従って、常に集塵機をコークス炉の近辺に設置するスペースが確保されるとは限らない。集塵機がコークス炉から離れた場所に設置された場合、排ガスをコークス炉1から集塵機2を経由して煙突3に導く煙道7(本発明では、第二の煙道と呼ぶ)の配管長が100mを超えるケースもある。   The dust collector will be installed later as a countermeasure against the black smoke of exhaust gas accompanying the aging of the coke oven. Therefore, the space for installing the dust collector in the vicinity of the coke oven is not always ensured. When the dust collector is installed at a place away from the coke oven, the pipe length of the flue 7 (referred to as the second flue in the present invention) for guiding the exhaust gas from the coke oven 1 to the chimney 3 via the dust collector 2 is In some cases, the length exceeds 100 m.

例えば、配管長が40m程度の場合の立ち上げ方法は、煙道調整弁5を開状態に保った状態で、集塵機2を起動後した後、集塵機調整弁4を20%程度開放し、コークス炉から排出される排ガスを第二の煙道7に流入させる。配管長が40m程度の場合には、図2に示すように、集塵機調整弁4開放後15分程度で、集塵機2入り側の排ガス温度Tが150〜170℃となるため、その後、集塵機調整弁4を全開として、煙道調整弁5を閉じて立ち上げが完了する。 For example, when the pipe length is about 40 m, the start-up method is that after the dust collector 2 is started up with the flue adjustment valve 5 kept open, the dust collector adjustment valve 4 is opened about 20%, and the coke oven is opened. The exhaust gas discharged from the exhaust gas flows into the second flue 7. When the pipe length is about 40 m, as shown in FIG. 2, the exhaust gas temperature T 0 on the dust collector 2 entrance side becomes 150 to 170 ° C. in about 15 minutes after the dust collector adjustment valve 4 is opened. The valve 4 is fully opened, the flue regulating valve 5 is closed, and the start-up is completed.

一方、配管長が100m以上の場合には、上記同様に煙道調整弁5を開状態に保った状態で、集塵機2を起動後した後、集塵機調整弁4を20%程度開放し、コークス炉から排出される排ガスを第二の煙道7に流入させた場合、100m以上の配管を経由する過程で、排ガス温度が低下し、煙突下部における排ガス温度Tが煙突ドラフト圧を得るために必要な排ガス温度を大きく下回るため、排ガスが煙突から排出されず、煙道圧力が上昇して、集塵機の安全な立ち上げを行うことができない。 On the other hand, when the pipe length is 100 m or more, after starting the dust collector 2 with the flue adjusting valve 5 kept open as described above, the dust collector adjusting valve 4 is opened by about 20%, and the coke oven is opened. When exhaust gas discharged from the exhaust gas flows into the second flue 7, the exhaust gas temperature decreases in the process of passing through a pipe of 100 m or more, and the exhaust gas temperature T 1 at the lower part of the chimney is necessary to obtain the chimney draft pressure. Therefore, the exhaust gas is not discharged from the chimney, the flue pressure rises, and the dust collector cannot be started up safely.

本発明は、このような場合に適用される集塵機立ち上げ方法に関する技術である。本発明では、まず、煙道調整弁5を開状態に保った状態で、集塵機2を起動後した後、集塵機調整弁4を2%程度開放し、コークス炉から排出される高温の排ガスを第二の煙道7に流入させながら、配管および集塵機の昇温を行う。一方、煙道調整弁5の開状態も維持しているため、煙突下部には、第一の煙道から流入する高温(T)の排ガスも流入する。ここで、集塵機調整弁4の開度を煙道調整弁5の開度(100%)に比べて低く抑えることにより、煙突下部に流入する排ガスの割合に占める、第一の煙道から流入する高温(T)の排ガスの割合を大きくとり、煙突下部の合流排ガス温度を煙突ドラフト圧を得るために必要な排ガス温度に保持することができる。
ここで、合流排ガス温度とは下記式により規定される温度をいう。
{(T×第1の煙道経由の排ガス量)+(T×第二の煙道経由の排ガス量)}÷(第1の煙道経由の排ガス量+第二の煙道経由の排ガス量)
The present invention is a technique related to a dust collector startup method applied in such a case. In the present invention, first, after starting the dust collector 2 with the flue adjusting valve 5 kept open, the dust collector adjusting valve 4 is opened by about 2%, and the high temperature exhaust gas discharged from the coke oven is discharged. While flowing into the second flue 7, the pipe and the dust collector are heated. On the other hand, since the open state of the flue adjusting valve 5 is also maintained, the high-temperature (T 2 ) exhaust gas flowing from the first flue also flows into the lower part of the chimney. Here, by suppressing the opening degree of the dust collector adjusting valve 4 to be lower than the opening degree (100%) of the flue adjusting valve 5, it flows from the first flue that occupies the ratio of the exhaust gas flowing into the lower part of the chimney. The ratio of the high-temperature (T 2 ) exhaust gas can be increased, and the combined exhaust gas temperature at the lower part of the chimney can be maintained at the exhaust gas temperature necessary for obtaining the chimney draft pressure.
Here, the combined exhaust gas temperature refers to a temperature defined by the following equation.
{(T 2 × exhaust amount via first flue) + (T 1 × exhaust amount via second flue)} ÷ (exhaust amount via first flue + second flue amount) Exhaust gas amount)

本発明では、このようにして、煙突下部の合流排ガス温度を、煙突ドラフト圧を得るために必要な排ガス温度に保持することにより、第二の煙道配管の長さの如何に関わらず、第二の煙道配管を経由して煙突下部に導入された排ガスを煙突から排出可能とし、低温の排ガスによる煙道圧力上昇の問題を回避可能としている。   In the present invention, the combined exhaust gas temperature at the lower part of the chimney is maintained at the exhaust gas temperature necessary for obtaining the chimney draft pressure in this way, regardless of the length of the second flue pipe. The exhaust gas introduced into the lower part of the chimney via the second flue pipe can be discharged from the chimney, and the problem of the flue pressure rise due to the low temperature exhaust gas can be avoided.

なお、集塵機2入り側の排ガス温度Tは、集塵機2の立ち上げを開始し、高い熱エネルギーを有するコークス炉1からの排ガスを第二の煙道7に流す過程で、時間の経過とともに上昇していく。本発明では、当該集塵機入り側の排ガス温度Tを指標として、Tが一定温度に到達ごとに、段階的に集塵機調整弁4の開度を上げていき、集塵機入り側の排ガス温度Tが150〜170℃となった後、集塵機調整弁4を全開として、煙道調整弁5を閉じて立ち上げを完了することにより、集塵機2を安定的に立ち上げることを可能としている。 The exhaust gas temperature T 0 on the dust collector 2 entry side rises with time in the process of starting the dust collector 2 and flowing the exhaust gas from the coke oven 1 having high thermal energy to the second flue 7. I will do it. In the present invention, the exhaust gas temperature T 0 on the dust collector entrance side is used as an index, and each time T 0 reaches a certain temperature, the opening degree of the dust collector adjustment valve 4 is gradually increased, and the exhaust gas temperature T 0 on the dust collector entrance side is increased. After the temperature reaches 150 to 170 ° C., the dust collector adjusting valve 4 is fully opened, the flue adjusting valve 5 is closed and the start-up is completed, so that the dust collector 2 can be started up stably.

下記の表2に示すシーケンスに従って、集塵機調整弁4の開度を段階的に調整し、図3に示すコークス炉用集塵機の立ち上げを行った結果を図4に示す。   FIG. 4 shows the result of starting up the coke oven dust collector shown in FIG. 3 by adjusting the opening degree of the dust collector adjusting valve 4 stepwise according to the sequence shown in Table 2 below.

Figure 0005487593
Figure 0005487593

図4に示すように、本発明の方法によれば、従来の立ち上げ方法では、立ち上げ困難であった配管長を有する集塵機であっても、安定的に立ち上げることが可能である。   As shown in FIG. 4, according to the method of the present invention, even a dust collector having a pipe length that has been difficult to start up by the conventional start-up method can be started up stably.

本発明の集塵機立ち上げ方法における排ガスフロー図Exhaust gas flow diagram in the dust collector startup method of the present invention 従来手法で集塵機立上げ可能な場合の立上げ時間・T0温度・煙道圧力の関係図Relationship diagram of start-up time, T 0 temperature, and flue pressure when the dust collector can be started up using the conventional method 本発明が適用される配管長を有する集塵機配置の実施例Example of dust collector arrangement having pipe length to which the present invention is applied 図3に示す実施例に本発明を適用した場合の立上げ時間・T0温度・煙道圧力の関係図FIG. 3 is a relationship diagram of the start-up time, T 0 temperature, and flue pressure when the present invention is applied to the embodiment shown in FIG.

符号の説明Explanation of symbols

1 コークス炉
2 集塵機
3 煙突
4 集塵機調整弁
5 煙道調整弁
6 第一の煙道
7 第二の煙道
8 調整弁

DESCRIPTION OF SYMBOLS 1 Coke oven 2 Dust collector 3 Chimney 4 Dust collector adjustment valve 5 Flue adjustment valve 6 First flue 7 Second flue 8 Adjustment valve

Claims (2)

排ガスをコークス炉から集塵機を経由せず煙突に導く第一の煙道と
排ガスをコークス炉から集塵機を経由して煙突に導く第二の煙道と
を有するコークス炉に使用される煙道集塵機の立ち上げ方法であって、
第一の煙道には、コークス炉から煙突への排ガス流量を調整する煙道調整弁を備え、
第二の煙道には、集塵機から煙突への排ガス流量を調整する集塵機調整弁を備え、
煙道集塵機立ち上げ開始時には、煙道調整弁を開状態としつつ、集塵機調整弁を、集塵機入側の排ガス温度上昇と共に、閉状態から徐々に開状態としていき、
前記第一の煙道を経由する排ガスと第二の煙道を経由する排ガスを前記煙突下部で合流した合流ガス温度を、該煙突のドラフト圧が担保される排ガス温度に保持することにより、煙道集塵機を立ち上げることを特徴とする煙道集塵機の立ち上げ方法。
A flue dust collector used in a coke oven having a first flue that leads exhaust gas from the coke oven to the chimney without going through the dust collector and a second flue that leads the exhaust gas from the coke oven to the chimney via the dust collector A startup method,
The first flue is equipped with a flue control valve that adjusts the exhaust gas flow rate from the coke oven to the chimney,
The second flue is equipped with a dust collector adjustment valve that adjusts the exhaust gas flow rate from the dust collector to the chimney,
At the start of flue dust collector start-up, the flue adjustment valve is opened, and the dust collector adjustment valve is gradually opened from the closed state as the exhaust gas temperature rises on the dust collector inlet side.
By maintaining the combined gas temperature of the exhaust gas passing through the first flue and the exhaust gas passing through the second flue at the lower part of the chimney at the exhaust gas temperature at which the draft pressure of the chimney is secured, flue raising of dust collector characterized by raising Rukoto up the road dust collector.
前記集塵機入側の排ガス温度Tを指標として、Tが一定温度に到達ごとに、集塵機調整弁を段階的に開状態としていくことを特徴とする請求項1記載の煙道集塵機の立ち上げ方法。 Wherein as an indicator of exhaust gas temperature T 0 of the dust collector entry side, for each arrival T 0 is a constant temperature, start-up of the flue dust collector of claim 1, wherein the gradually and stepwise opened the dust collector adjustment valve Method.
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