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JP6299334B2 - Coke oven electric dust collector operation management method - Google Patents
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JP6299334B2 - Coke oven electric dust collector operation management method - Google Patents

Coke oven electric dust collector operation management method Download PDF

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JP6299334B2
JP6299334B2 JP2014068497A JP2014068497A JP6299334B2 JP 6299334 B2 JP6299334 B2 JP 6299334B2 JP 2014068497 A JP2014068497 A JP 2014068497A JP 2014068497 A JP2014068497 A JP 2014068497A JP 6299334 B2 JP6299334 B2 JP 6299334B2
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coke oven
electric dust
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electrostatic precipitator
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高志 平川
高志 平川
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Nippon Steel Corp
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Description

本発明は、コークス炉が排出する副生ガス(以下「コークス炉ガス」という。)からタールミストを除去する電気集塵機の運転管理方法に関する。   The present invention relates to an operation management method for an electrostatic precipitator that removes tar mist from a by-product gas discharged from a coke oven (hereinafter referred to as “coke oven gas”).

コークス炉ガスは、タールミスト、スラッジ、ナフタリン、硫化水素、アンモニア等を除去して精製し、例えば、燃料として使用される。スラッジは、スラッジ沈降槽で除去し、ナフタリン、硫化水素、アンモニア等の化合物は、冷却、吸収等の操作で除去する。タールミストは、通常、回転籠型のタール除去機、又は、電気集塵機で除去する。   Coke oven gas is purified by removing tar mist, sludge, naphthalene, hydrogen sulfide, ammonia and the like, and is used as, for example, fuel. Sludge is removed in a sludge settling tank, and compounds such as naphthalene, hydrogen sulfide, and ammonia are removed by operations such as cooling and absorption. Tar mist is usually removed by a rotary saddle type tar remover or an electric dust collector.

図1に、電気集塵機の断面を模式的に示す。コークス炉ガスGが、電気集塵機1の底部流入口10aから流入し、多孔板8から、放電線4aと集塵板4bの間を通過し、頂部流出口10bから流出する間、直流電源11に高電圧ケーブル12を介して接続されている放電線4aから高電圧がコークス炉ガスGに印加されてタールミストが帯電し、集塵板4bに捕集される。   FIG. 1 schematically shows a cross section of the electrostatic precipitator. While the coke oven gas G flows in from the bottom inlet 10a of the electrostatic precipitator 1, passes through the perforated plate 8 between the discharge wire 4a and the dust collector 4b, and flows out of the top outlet 10b, the DC power source 11 is supplied. A high voltage is applied to the coke oven gas G from the discharge wire 4a connected via the high voltage cable 12, and the tar mist is charged and collected on the dust collecting plate 4b.

しかし、電気集塵機1を長時間使用していると、当然に、内部はタールミストで汚れるが、高電圧ケーブル12を絶縁して支持する支持碍子3aや貫通碍子3bを収容している碍子塔3の内部が汚れると、絶縁抵抗が低下するか、又は、放電線4aと集塵板4bが短絡する。なお、図1中、9は、集塵物(タールミスト)を取り出すマンホールである。   However, when the electrostatic precipitator 1 is used for a long time, the inside is naturally contaminated with tar mist. However, the insulator tower 3 accommodating the supporting insulator 3a and the penetrating insulator 3b for insulating and supporting the high voltage cable 12 is used. When the inside of the container becomes dirty, the insulation resistance decreases, or the discharge wire 4a and the dust collecting plate 4b are short-circuited. In FIG. 1, reference numeral 9 denotes a manhole for taking out the collected dust (tar mist).

特許文献1には、碍子塔の内部へのタールミストの侵入を抑制し、高電圧ケーブルの絶縁を確保した電気集塵機が提案されている。しかし、電気集塵機の運転管理は従来どおりであり、碍子塔の内部の汚染は抑制できても、タールミストの除去効率は向上しない。   Patent Document 1 proposes an electrostatic precipitator that suppresses intrusion of tar mist into the inside of an insulator tower and ensures insulation of a high-voltage cable. However, the operation management of the electrostatic precipitator is the same as before, and even if the contamination inside the insulator tower can be suppressed, the removal efficiency of tar mist is not improved.

コークス炉ガス中のタールミストを、電気集塵機で効率的に除去するためには、電気集塵機を、比較的高度に運転管理する必要がある。しかし、現状は、計器室での電流監視、又は、オペレーターの経験と勘に頼る計測作業及び巡回監視で運転管理を行っていて、タールミストの除去は効率的でない。   In order to efficiently remove tar mist in coke oven gas with an electric dust collector, the electric dust collector needs to be operated and managed at a relatively high level. However, at present, operation management is performed by current monitoring in the instrument room or measurement work and patrol monitoring depending on the experience and intuition of the operator, and removal of tar mist is not efficient.

特開2004−043534号公報JP 2004-043534 A

通常、数機の電気集塵機を備えた電気集塵系統にコークス炉ガスを流し、タールミストを除去するが、コークス炉ガスの流量が不均等になり、電気集塵機に堆積するタールミストの量(除去量)が不均等になる。結局、電気集塵機の集塵能力に差が生じ、電気集塵系統の全体的な集塵効率は低下する。   Normally, coke oven gas is flowed through an electrostatic precipitator system equipped with several electrostatic precipitators to remove tar mist, but the flow rate of coke oven gas becomes uneven and the amount of tar mist that accumulates in the electrostatic precipitator (removal) Amount) becomes uneven. Eventually, a difference occurs in the dust collection capacity of the electrostatic precipitator, and the overall dust collection efficiency of the electrostatic precipitator system is reduced.

本発明は、数機の電気集塵機を備えた電気集塵系統にコークス炉ガスを流し、タールミストを除去する場合において、電気集塵系統の全体的な集塵効率を向上させることを課題とし、該課題を解決する電気集塵機の管理方法を提供することを目的とする。   The present invention aims to improve the overall dust collection efficiency of the electric dust collection system when flowing coke oven gas through an electric dust collection system equipped with several electric dust collectors and removing tar mist. An object of the present invention is to provide a method for managing an electrostatic precipitator that solves this problem.

本発明者らは、上記課題を解決する手法について鋭意検討した。その結果、コークス炉ガスからタールミストを、複数の電気集塵機を備えた集塵系統で除去する場合、(x)電気集塵系統に流入するコークス炉ガスの量を、個々の電気集塵機の集塵量が等しくなるように調整すると、電気集塵系統の全体的な集塵効率が向上することが判明した。   The present inventors diligently studied a method for solving the above problems. As a result, when removing tar mist from coke oven gas with a dust collection system equipped with a plurality of electrostatic precipitators, (x) the amount of coke oven gas flowing into the electrostatic precipitator system, It has been found that adjusting the amount to be equal improves the overall dust collection efficiency of the electric dust collection system.

また、(y)電気集塵機の電圧を経時的に監視し、不規則な電圧変動が生じた電気集塵機への電圧印加を停止するとともに、電気集塵系統に流入するコークス炉ガスの量を、残る個々の電気集塵機の集塵量が等しくなるように調整すると、電気集塵系統の全体的な集塵効率が向上することが判明した。   In addition, (y) the voltage of the electrostatic precipitator is monitored over time, the voltage application to the electrostatic precipitator in which irregular voltage fluctuation has occurred is stopped, and the amount of coke oven gas flowing into the electrostatic precipitator system remains. It has been found that the overall dust collection efficiency of the electric dust collection system is improved by adjusting the dust collection amounts of the individual electric dust collectors to be equal.

本発明は、上記知見に基づいてなされたもので、その要旨は以下のとおりである。   This invention was made | formed based on the said knowledge, and the summary is as follows.

ークス炉が排出する副生ガスからタールミストを除去する電気集塵機の運転管理方法において、
(i)(i-1)複数の電気集塵機を備える電気集塵系統に流入するコークス炉ガスの量を、個々の電気集塵機の集塵量が等しくなるように調整するとともに、(i-2)電気集塵機へ印加する電圧を経時的に監視し、
(ii)(ii-1)上記電圧に不規則な電圧変動が生じた電気集塵機への電圧印加を停止してコークス炉ガスの流入を遮断するとともに、(ii-2)残る複数の電気集塵機を備える電気集塵系統に流入するコークス炉ガスの量を、個々の電気集塵機での集塵量が等しくなるように、再度、調整する
ことを特徴とするコークス炉の電気集塵機の運転管理方法。
In operation management method for an electro-precipitator coke furnace to remove tar mist from by-product gas to be discharged,
(I) (i-1) While adjusting the amount of coke oven gas flowing into an electric dust collector system having a plurality of electric dust collectors so that the individual dust collectors have the same dust collection amount, (i-2) Monitor the voltage applied to the electrostatic precipitator over time,
(Ii) (ii-1) Stops the application of voltage to the electrostatic precipitator in which irregular voltage fluctuation has occurred in the above voltage to shut off the inflow of coke oven gas, and (ii-2) the remaining multiple electrostatic precipitators An operation management method for an electric dust collector of a coke oven, wherein the amount of coke oven gas flowing into the electric dust collector system is adjusted again so that the amount of dust collected in each electric dust collector becomes equal.

本発明によれば、数機の電気集塵機を備えた電気集塵系統にコークス炉ガスを流し、タールミストを除去する場合において、電気集塵系統の全体的な集塵効率が向上する。   According to the present invention, when the coke oven gas is allowed to flow through an electric dust collection system equipped with several electric dust collectors and tar mist is removed, the overall dust collection efficiency of the electric dust collection system is improved.

電気集塵機の断面を模式的に示す図である。It is a figure which shows typically the cross section of an electric dust collector. 2系統の電気集塵系統を示す図である。It is a figure which shows two electric dust collection systems. 電気集塵機の電圧特性の経時変化を示す図である。It is a figure which shows the time-dependent change of the voltage characteristic of an electrostatic precipitator.

本発明のコークス炉の電気集塵機の運転管理方法(以下「本発明方法」ということがある。)は、コークス炉が排出する副生ガスからタールミストを除去する電気集塵機の運転管理方法において、
(i)(i-1)複数の電気集塵機を備える電気集塵系統に流入するコークス炉ガスの量を、個々の電気集塵機の集塵量が等しくなるように調整するとともに、(i-2)電気集塵機へ印加する電圧を経時的に監視し、
(ii)(ii-1)上記電圧に不規則な電圧変動が生じた電気集塵機への電圧印加を停止してコークス炉ガスの流入を遮断するとともに、(ii-2)残る複数の電気集塵機を備える電気集塵系統に流入するコークス炉ガスの量を、個々の電気集塵機での集塵量が等しくなるように、再度、調整する
ことを特徴とする。
The operation management method of the electric dust collector of the coke oven of the present invention (hereinafter sometimes referred to as “the method of the present invention”) is an operation management method of the electric dust collector that removes tar mist from the by-product gas discharged from the coke oven .
(I) (i-1) While adjusting the amount of coke oven gas flowing into an electric dust collector system having a plurality of electric dust collectors so that the individual dust collectors have the same dust collection amount, (i-2) Monitor the voltage applied to the electrostatic precipitator over time,
(Ii) (ii-1) Stops the application of voltage to the electrostatic precipitator in which irregular voltage fluctuation has occurred in the above voltage to shut off the inflow of coke oven gas, and (ii-2) the remaining multiple electrostatic precipitators The amount of coke oven gas flowing into the electric dust collection system provided is adjusted again so that the amount of dust collection in each electric dust collector becomes equal.

以下、本発明方法について、図面に基づいて説明する。   Hereinafter, the method of the present invention will be described with reference to the drawings.

図2に、2系統の電気集塵系統を示す。ガス流本管2から、流入管2aと流入管2bが枝分かれして、流入管2aには、3機の電気集塵機1a、1b、1cが並列に接続され、流入管2bには、同じく、3機の電気集塵機1d、1e、1fが並列に接続され、2系統の電気集塵系統が構成されている。   FIG. 2 shows two electric dust collection systems. An inflow pipe 2a and an inflow pipe 2b are branched from the gas flow main pipe 2, and three electrostatic precipitators 1a, 1b, 1c are connected in parallel to the inflow pipe 2a. The electric dust collectors 1d, 1e, and 1f of the machine are connected in parallel to form two electric dust collection systems.

ガス流本管2には、流入管2aへ流入するコークス炉ガスの流量を調整する調整弁7aと、流入管2bへ流入するコークス炉ガスの流量を調整する調整弁7bの間に、コークス炉ガスの流量を測定する流量計5と、該流量を調整するダンパー6が配置(図では、流量計の上流側と下流側に配置)されている。流量計5で測定した測定値(流量値)に基づいて、制御演算装置(図示なし)で、ダンパー6の開度が調整される。   The gas flow main pipe 2 includes a coke oven between an adjustment valve 7a for adjusting the flow rate of the coke oven gas flowing into the inflow pipe 2a and an adjustment valve 7b for adjusting the flow rate of the coke oven gas flowing into the inflow pipe 2b. A flow meter 5 for measuring the gas flow rate and a damper 6 for adjusting the flow rate are arranged (in the drawing, arranged on the upstream side and the downstream side of the flow meter). Based on the measured value (flow value) measured by the flow meter 5, the opening degree of the damper 6 is adjusted by a control arithmetic device (not shown).

コークス炉ガスは、流入管2a及び流入管2bのそれぞれに接続した電気集塵機1a、1b、1c及び電気集塵機1d、1e、1fに、底部の流入口から流入し、タールミストが除去された後、電気集塵機の頂部の流出口から、それぞれ流出管2a’及び流出管2b’へ流出する。   The coke oven gas flows into the electrostatic precipitators 1a, 1b, 1c and the electrostatic precipitators 1d, 1e, 1f connected to the inflow pipe 2a and the inflow pipe 2b, respectively, from the bottom inlet, and after tar mist is removed, Outflow from the outlet at the top of the electric dust collector to the outflow pipe 2a 'and the outflow pipe 2b', respectively.

流入管2aには、電気集塵機へ流入するコークス炉ガスの流量を測定する流量計5aと、該流量を調整するダンパー6aが配置されている。流量計5aで測定した測定値(流量値)に基づいて、制御演算器(図示なし)で、ダンパー6aの開度が調整され、電気集塵機1a、1b、1cへ流入するコークス炉ガスの流量が制御される。   In the inflow pipe 2a, a flow meter 5a for measuring the flow rate of the coke oven gas flowing into the electric dust collector and a damper 6a for adjusting the flow rate are arranged. Based on the measured value (flow rate value) measured by the flow meter 5a, the opening degree of the damper 6a is adjusted by a control calculator (not shown), and the flow rate of the coke oven gas flowing into the electrostatic precipitators 1a, 1b, 1c is determined. Be controlled.

流入管2bには、電気集塵機へ流入するコークス炉ガスの流量を測定する流量計5bと、該流量を調整するダンパー6bが配置されている。流量計5bで測定した測定値(流量値)に基づいて、制御演算器(図示なし)で、ダンパー6bの開度が調整され、電気集塵機1d、1e、1fへ流入するコークス炉ガスの流量が制御される。   The inflow pipe 2b is provided with a flow meter 5b for measuring the flow rate of the coke oven gas flowing into the electric dust collector and a damper 6b for adjusting the flow rate. Based on the measured value (flow value) measured by the flow meter 5b, the opening of the damper 6b is adjusted by a control calculator (not shown), and the flow rate of the coke oven gas flowing into the electrostatic precipitators 1d, 1e, 1f is determined. Be controlled.

電気集塵機でタールミストが除去された後のコークス炉ガスは、電気集塵機の頂部の流出口から、それぞれ、流出管2a’及び流出管2b’へ流出する。本発明方法においては、個々の電気集塵機の集塵量が等しくなるように、電気集塵系統に流入するコークス炉ガスの量を、流量計とダンパーで調整する。   The coke oven gas after the tar mist is removed by the electric dust collector flows out from the outlet at the top of the electric dust collector to the outflow pipe 2a 'and the outflow pipe 2b', respectively. In the method of the present invention, the amount of coke oven gas flowing into the electric dust collection system is adjusted by a flow meter and a damper so that the dust collection amount of each electric dust collector becomes equal.

コークス炉ガス中のタールダストを除去するため、個々の電気集塵機に高電圧を負荷するが、稼働中、個々の電気集塵機の電圧特性を測定し、稼動状態を、常時、監視する。   In order to remove tar dust in coke oven gas, high voltage is applied to each electrostatic precipitator. During operation, the voltage characteristics of each electrostatic precipitator are measured, and the operating state is constantly monitored.

図3に、電気集塵機の電圧特性の経時変化を示す。電気集塵機が正常に稼動している間は、電圧は略一定のV0で推移するが、電気集塵機に異常な兆候が現れると電圧は上昇し始める。   In FIG. 3, the time-dependent change of the voltage characteristic of an electrostatic precipitator is shown. While the electrostatic precipitator is operating normally, the voltage changes at a substantially constant V0, but when an abnormal sign appears in the electrostatic precipitator, the voltage starts to rise.

図3では、時間t0の時点から電圧が上昇し始めている。即ち、電気集塵機が、時間t0の時点から異常な稼動状態になり始めたことを意味している。電圧の上昇傾向が時間T1(t1−t0)の間継続し、電気集塵機が異常の状態(タールミストが限界量まで堆積し放電電極との短絡)に達すると、電圧は不規則に大きく変動し始める(図中、T2(=t2−t1)の区間)。電圧変動が、所定の時間T2継続した後、電圧は0まで降下する。   In FIG. 3, the voltage starts to increase from time t0. That is, it means that the electrostatic precipitator has started to be in an abnormal operating state from time t0. When the rising trend of voltage continues for time T1 (t1-t0) and the electrostatic precipitator reaches an abnormal state (tar mist accumulates to the limit amount and short-circuits with the discharge electrode), the voltage fluctuates randomly Start (interval of T2 (= t2-t1) in the figure). After the voltage fluctuation continues for a predetermined time T2, the voltage drops to zero.

そこで、本発明方法では、特定の電気集塵機の電圧に不規則な電圧変動が生じた場合、電圧が0まで降下するのを待たずに、電圧印加を停止して、コークス炉ガスの流入を遮断し、残る電気集塵機でタールミストの除去を継続する。このとき、残る電気集塵機に過大な負荷がかからない範囲で、電気集塵系統に流入するコークス炉ガスの量を、個々の電気集塵機での集塵量が等しくなるように、再度、流量計とダンパーで調整する。   Therefore, in the method of the present invention, when irregular voltage fluctuation occurs in the voltage of a specific electrostatic precipitator, the voltage application is stopped and the inflow of coke oven gas is shut off without waiting for the voltage to drop to zero. Continue to remove tar mist with the remaining electrostatic precipitator. At this time, the amount of coke oven gas flowing into the electrostatic precipitator system is again adjusted so that the amount of dust collected by each electrostatic precipitator becomes equal, within a range where the excessive load is not applied to the remaining electrostatic precipitator. Adjust with.

以上、本発明について、図2に示す2系統の電気集塵系統に基づいて説明したが、本発明方法は、2系統の電気集塵系統に限られない。電気集塵系統は1系統でもよく、3系統以上でもよい。本発明方法においては、電気集塵系統の系統数によらず、全体の集塵率が顕著に向上する。   As mentioned above, although this invention was demonstrated based on the two electric dust collection systems shown in FIG. 2, this invention method is not restricted to two electric dust collection systems. The electric dust collection system may be one system or three or more systems. In the method of the present invention, the overall dust collection rate is remarkably improved regardless of the number of electric dust collection systems.

次に、本発明の実施例について説明するが、実施例での条件は、本発明の実施可能性及び効果を確認するために採用した一条件例であり、本発明は、この一条件例に限定されるものではない。本発明は、本発明の要旨を逸脱せず、本発明の目的を達成する限りにおいて、種々の条件を採用し得るものである。   Next, examples of the present invention will be described. The conditions in the examples are one example of conditions used for confirming the feasibility and effects of the present invention, and the present invention is based on this one example of conditions. It is not limited. The present invention can adopt various conditions as long as the object of the present invention is achieved without departing from the gist of the present invention.

(実施例)
図2に示す電気集塵系統で、コークス炉ガスを、流入管2aに100,000Nm3/hr、流入管2bに100,000Nm3/hr流し、それぞれ、3機の電気集塵機で、コークス炉ガス中のタールミストを除去した。個々の電気集塵機の電圧特性を測定して稼動状態を監視し、集塵量を一定時間毎に測定した。電圧特性は略一定で良好に推移し、集塵量も略等しかった。
(Example)
In the electric dust collection system shown in FIG. 2, coke oven gas is supplied to the inflow pipe 2a at 100,000 Nm 3 / hr and to the inflow pipe 2b at 100,000 Nm 3 / hr. Inside tar mist was removed. The voltage characteristics of each electrostatic precipitator were measured to monitor the operating state, and the amount of dust collected was measured at regular intervals. The voltage characteristics were almost constant and good, and the amount of dust collected was almost equal.

電気集塵機1cの電圧特性に不規則な変動が現れたので、直ちに電圧負荷を停止し、コークス炉ガスの流入を遮断した。同時に、ダンパーを調節し、流入管2aの流量を100,000Nm3/hrから80,000Nm3/hrに変更し、流入管2bの流量を100,000Nm3/hrから120,000Nm3/hrに変更した。 Since irregular fluctuations appeared in the voltage characteristics of the electrostatic precipitator 1c, the voltage load was immediately stopped and the inflow of coke oven gas was shut off. At the same time, the damper is adjusted to change the flow rate of the inflow pipe 2a from 100,000 Nm 3 / hr to 80,000 Nm 3 / hr, and the flow rate of the inflow pipe 2b from 100,000 Nm 3 / hr to 120,000 Nm 3 / hr. changed.

流量の変更後も、個々の電気集塵機の電圧特性を測定して稼動状態を監視し、集塵量を一定時間毎に測定した。電圧特性は略一定で良好に推移し、集塵量も略等しかった。   Even after the flow rate was changed, the voltage characteristics of each electrostatic precipitator were measured to monitor the operating state, and the dust collection amount was measured at regular intervals. The voltage characteristics were almost constant and good, and the amount of dust collected was almost equal.

電気集塵機1cの修理後、再稼動するとともに、ダンパーを調節し、流入管2aの流量を80,000Nm3/hrから100,000Nm3/hrに変更し、流入管2bの流量を120,000Nm3/hrから100,000Nm3/hrに変更した。 After repairing the electrostatic precipitator 1c, it is restarted, the damper is adjusted, the flow rate of the inflow pipe 2a is changed from 80,000 Nm 3 / hr to 100,000 Nm 3 / hr, and the flow rate of the inflow pipe 2b is 120,000 Nm 3. / Hr was changed to 100,000 Nm 3 / hr.

流量の変更後も、個々の電気集塵機の電圧特性を測定して稼動状態を監視し、集塵量を一定時間毎に測定した。電圧特性は略一定で良好に推移し、集塵量も略等しかった。   Even after the flow rate was changed, the voltage characteristics of each electrostatic precipitator were measured to monitor the operating state, and the dust collection amount was measured at regular intervals. The voltage characteristics were almost constant and good, and the amount of dust collected was almost equal.

前述したように、本発明によれば、数機の電気集塵機を備えた電気集塵系統にコークス炉ガスを流し、タールミストを除去する場合において、電気集塵系統の全体的な集塵効率が向上する。よって、本発明は、コークス製造産業において利用可能性が高いものである。   As described above, according to the present invention, when the coke oven gas is allowed to flow through an electric dust collection system equipped with several electric dust collectors and tar mist is removed, the overall dust collection efficiency of the electric dust collection system is improved. improves. Therefore, the present invention has high applicability in the coke manufacturing industry.

1 電気集塵機
1a、1b、1c 電気集塵機
1d、1e、1f 電気集塵機
2 ガス流本管
2a、2b 流入管
2a’、2b’ 流出管
3 碍子塔
3a 支持碍子
3b 貫通碍子
4a 放電線
4b 集塵板
5、5a、5b 流量計
6、6a、6b ダンパー
7a、7b 調整弁
8 多孔板
9 マンホール
10a 底部流入口
10b 頂部流出口
11 直流電源
12 高電圧ケーブル
E アース
G コークス炉ガス
DESCRIPTION OF SYMBOLS 1 Electric dust collector 1a, 1b, 1c Electric dust collector 1d, 1e, 1f Electric dust collector 2 Gas flow main pipe 2a, 2b Inflow pipe 2a ', 2b' Outflow pipe 3 Insulator tower 3a Support insulator 3b Through insulator 4a Discharge wire 4b Dust collector plate 5, 5a, 5b Flow meter 6, 6a, 6b Damper 7a, 7b Regulating valve 8 Perforated plate 9 Manhole 10a Bottom inlet 10b Top outlet 11 DC power supply 12 High voltage cable E Earth G Coke oven gas

Claims (1)

コークス炉が排出する副生ガスからタールミストを除去する電気集塵機の運転管理方法において、
(i)(i-1)複数の電気集塵機を備える電気集塵系統に流入するコークス炉ガスの量を、個々の電気集塵機の集塵量が等しくなるように調整するとともに、(i-2)電気集塵機へ印加する電圧を経時的に監視し、
(ii)(ii-1)上記電圧に不規則な電圧変動が生じた電気集塵機への電圧印加を停止してコークス炉ガスの流入を遮断するとともに、(ii-2)残る複数の電気集塵機を備える電気集塵系統に流入するコークス炉ガスの量を、個々の電気集塵機での集塵量が等しくなるように、再度、調整する
ことを特徴とするコークス炉の電気集塵機の運転管理方法。
In the operation management method of the electric dust collector that removes tar mist from the by-product gas discharged from the coke oven,
(I) (i-1) While adjusting the amount of coke oven gas flowing into an electric dust collector system having a plurality of electric dust collectors so that the individual dust collectors have the same dust collection amount, (i-2) Monitor the voltage applied to the electrostatic precipitator over time,
(Ii) (ii-1) Stops the application of voltage to the electrostatic precipitator in which irregular voltage fluctuation has occurred in the above voltage to shut off the inflow of coke oven gas, and (ii-2) the remaining multiple electrostatic precipitators An operation management method for an electric dust collector of a coke oven, wherein the amount of coke oven gas flowing into the electric dust collector system is adjusted again so that the amount of dust collected in each electric dust collector becomes equal.
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