JP2012219358A - Dry type dust collection system and dry type gas collection method for furnace gas in blast furnace - Google Patents

Dry type dust collection system and dry type gas collection method for furnace gas in blast furnace Download PDF

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JP2012219358A
JP2012219358A JP2011089005A JP2011089005A JP2012219358A JP 2012219358 A JP2012219358 A JP 2012219358A JP 2011089005 A JP2011089005 A JP 2011089005A JP 2011089005 A JP2011089005 A JP 2011089005A JP 2012219358 A JP2012219358 A JP 2012219358A
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furnace top
top gas
heat
heat exchanger
heat medium
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Noriaki Fujii
紀彰 藤井
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Nippon Steel Engineering Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

PROBLEM TO BE SOLVED: To provide a dry type dust collection system for furnace gas in a blast furnace, stably performing temperature rising of furnace gas in a starting operation from the stopping of blasting in a blast furnace, with an inexpensive constitution and capable of increasing a power recovery amount by a TRT.SOLUTION: A furnace gas temperature adjustment means 6 adjusting the temperature of furnace gas G includes: a furnace gas heat exchanger 61 provided in furnace gas piping 721; a furnace gas temperature measuring means 62 measuring the temperature of the furnace gas G before heat exchange in the furnace gas heat exchanger 61; and a heating medium switching means 67 switching a heating state, where a heated heating medium flowing out from an exhaust gas heat exchanger 51 is flowed in the furnace gas heat exchanger 61 and the furnace gas G is heated by heat exchange with the heated heating medium flowed in, and a cooling state, where the cooled heating medium flowing out from a fuel gas heat exchanger 52 and a combustion air heat exchanger 53 is flowed in the furnace gas heat exchanger 61 and the furnace gas G is cooled by heat exchange with the cooled heating medium flowed in.

Description

本発明は、高炉炉頂ガスの乾式集塵システムおよび乾式集塵方法に関する。   The present invention relates to a dry dust collection system for a blast furnace top gas and a dry dust collection method.

高炉には、高炉炉頂ガスの持つ温度および圧力エネルギーを電力として回収するための炉頂圧力回収タービン(TRT)と、高炉炉頂ガス中のダストを除去する集塵設備とが設置されている。集塵設備には、乾式集塵機と湿式集塵機の2種類がある。
ところで、集塵設備として乾式集塵機を用いる場合には、以下のような問題が発生するおそれがある。
The blast furnace is equipped with a top pressure recovery turbine (TRT) for recovering the temperature and pressure energy of the blast furnace top gas as electric power, and a dust collection facility for removing dust in the blast furnace top gas. . There are two types of dust collection equipment: dry dust collectors and wet dust collectors.
By the way, when using a dry dust collector as dust collection equipment, the following problems may occur.

高炉休風立ち上がり時や高炉冷え込み時には、炉頂ガス温度が低く、後続設置している乾式集塵機内で結露する温度(60℃程度)以下になる場合、前記結露の発生により乾式集塵機の濾布にダストが付着して、ガスの流路が塞がれてしまう。このため、乾式集塵機の集塵能力が低下してしまう。
また、高炉の吹抜け時において、炉頂ガス温度が高く濾布を焼損させる温度(200℃程度)以上になる場合、濾布が焼損して乾式集塵機自体が機能しなくなる。
When the blast furnace rest wind rises or the blast furnace cools down, if the furnace top gas temperature is low and falls below the temperature (about 60 ° C) in the dry dust collector installed afterwards, the condensation will occur on the filter cloth of the dry dust collector. Dust adheres and the gas flow path is blocked. For this reason, the dust collection capacity of the dry dust collector is reduced.
In addition, when the blast furnace is blown through, if the furnace top gas temperature is higher than the temperature at which the filter cloth is burned (about 200 ° C.), the filter cloth is burned out and the dry dust collector itself does not function.

両ケースとも、最悪の場合には高炉の休風に至ることが想定される。
また、高炉が冷え込みや吹き抜け状態になると、通常操業状態に回復させるのが難しく、場合によっては何日、何カ月といったオーダーで非常事態が続く可能性がある。
そこで、このような乾式集塵機における問題を解決するための検討がなされている(例えば、特許文献1,2参照)。
In both cases, in the worst case, it is assumed that the blast furnace will be closed.
In addition, when the blast furnace is cooled or blown through, it is difficult to restore the normal operation state, and in some cases, an emergency may continue on the order of days or months.
Then, examination for solving the problem in such a dry type dust collector is made (for example, refer to patent documents 1 and 2).

特許文献1では、炉頂ガスを昇温させるための専用のガス燃焼炉を設置し、前記炉頂ガス温度が低温になった場合、このガス燃焼炉で温めたガスを乾式集塵機の前流側に設置した熱交換器に導いて炉頂ガスを昇温させている。この昇温後の炉頂ガスを乾式集塵機に導いて、乾式集塵機内での結露を防止している。また、炉頂ガス温度が高温の場合には、乾式集塵機の前流側で炉頂ガスに液体噴射器で冷却水を噴射することで、炉頂ガス温度を下げている。   In Patent Document 1, a dedicated gas combustion furnace for raising the temperature of the furnace top gas is installed, and when the temperature of the furnace top gas becomes low, the gas heated in this gas combustion furnace is supplied to the upstream side of the dry dust collector. The furnace top gas is heated up by being led to a heat exchanger installed in the factory. The furnace top gas after this temperature rise is led to a dry dust collector to prevent condensation in the dry dust collector. When the furnace top gas temperature is high, the furnace top gas temperature is lowered by injecting cooling water into the furnace top gas with a liquid injector on the upstream side of the dry dust collector.

特許文献2では、熱媒式の熱交換器を乾式集塵機の前後に設置するとともに、熱媒配管途中に蓄熱体を設置している。蓄熱体に蓄熱された熱を利用して、炉頂ガスを昇温したり、冷却したりすることで、炉頂ガスの温度を適切に制御している。また、このような構成を用いることにより、従来、前記炉頂ガス温度の異常高低温時の緊急用として併設されている湿式集塵機を廃止し、乾式集塵機のみで集塵している。   In patent document 2, while installing a heat-medium type heat exchanger before and behind a dry-type dust collector, the thermal storage body is installed in the middle of the heat-medium piping. The temperature of the furnace top gas is appropriately controlled by heating or cooling the furnace top gas using the heat stored in the heat storage body. Further, by using such a configuration, conventionally, the wet dust collector provided for emergency when the furnace top gas temperature is abnormally high or low is abolished, and dust is collected only by the dry dust collector.

実開平3−18500号公報Japanese Utility Model Publication No. 3-18500 特開2007−46113号公報JP 2007-46113 A

しかしながら、特許文献1のような構成では、ガス燃焼炉用のガス管を新たに架設する必要がある。さらに、ガスにより熱交換器を昇温させているため、熱交換器まで太い配管を架設する必要がある。このようなことから、経済的に合理的でない。   However, in the configuration as in Patent Document 1, it is necessary to newly construct a gas pipe for a gas combustion furnace. Furthermore, since the temperature of the heat exchanger is raised by gas, it is necessary to construct a thick pipe up to the heat exchanger. For this reason, it is not economically reasonable.

一方、特許文献2のような構成では、操業状況により蓄熱体の必要容量が変わり、さらに蓄熱体からの放散熱もあるため、蓄熱体の容量決定が難しい。
また、操業状態により炉頂ガスの昇温に必要な供給熱量や冷却に必要な奪熱量が変化してしまう。このような変化する状況においては、蓄熱体が絶えず放熱していることもあり、操業状況によっては、必要熱量を確保できない可能性が出てくる。
そのため、蓄熱体の容量不足になる可能性があり、依然として湿式集塵機の併設が必要となり、さらに湿式集塵機使用のためにTRTによる電力回収量の低下を招いてしまう。
On the other hand, in the configuration as in Patent Document 2, the required capacity of the heat storage body changes depending on the operation status, and further, there is also heat dissipated from the heat storage body, so it is difficult to determine the capacity of the heat storage body.
In addition, the amount of heat supplied for raising the temperature of the furnace top gas and the amount of heat removed for cooling change depending on the operating state. In such a changing situation, the heat storage body may radiate heat continuously, and depending on the operation situation, there is a possibility that the necessary amount of heat cannot be secured.
Therefore, there is a possibility that the capacity of the heat storage body is insufficient, and it is still necessary to install a wet dust collector, and further, the amount of power recovered by TRT is reduced due to the use of the wet dust collector.

本発明の目的は、高炉炉頂ガスの異常高低温時の対策を安価な構成で安定的に実施し、TRTによる電力回収量の増加を図ることができる高炉炉頂ガスの乾式集塵システムおよび乾式集塵方法を提供することである。   An object of the present invention is to provide a dry dust collection system for blast furnace top gas that can stably implement measures for abnormally high and low temperatures of blast furnace top gas with an inexpensive configuration and increase the amount of power recovered by TRT, and It is to provide a dry dust collection method.

本発明の乾式集塵システムは、高炉と、前記高炉に熱風を供給する熱風炉と、前記熱風炉に燃料ガスおよび燃焼空気を供給する燃料ガス供給手段および燃焼空気供給手段と、前記熱風炉からの排気ガスを再利用する排熱再利用システムと、前記高炉から発生する炉頂ガスの温度を調整する炉頂ガス温度調整手段と、前記炉頂ガス中のダストを除去する乾式集塵機と、前記乾式集塵機からの炉頂ガスにより駆動する炉頂圧回収タービンと、を少なくとも備え、前記排熱再利用システムは、前記熱風炉からの排ガス配管に設けられ、流入する熱媒体と排気ガスの間で熱交換を行って、加熱後の熱媒体を流出させる排ガス熱交換器と、前記燃料ガス供給手段と前記熱風炉とを連結する燃料ガス配管および前記燃焼空気供給手段と前記熱風炉とを連結する燃焼空気配管に各々設けられ、前記排ガス熱交換器で加熱された熱媒体との間で熱交換を行って燃料ガスおよび燃焼空気を加熱し、冷却後の熱媒体を前記排ガス熱交換器へと流入させる燃料ガス熱交換器および燃焼空気熱交換器と、から構成される高炉炉頂ガスの乾式集塵システムにおいて、前記炉頂ガス温度調整手段は、前記高炉と前記乾式集塵機とを連結する炉頂ガス配管に設けられ、流入する熱媒体と炉頂ガスとの間で熱交換を行って、当該熱媒体を流出させる炉頂ガス熱交換器と、前記炉頂ガス熱交換器での熱交換前の炉頂ガスの温度を測定する炉頂ガス温度測定手段と、前記炉頂ガス熱交換器における熱媒体の流入元および熱媒体の流出先を切り替える熱媒体切替手段と、を備え、前記熱媒体切替手段は、前記炉頂ガス温度測定手段での測定結果に基づいて、前記排ガス熱交換器から流出する加熱後の熱媒体を前記炉頂ガス熱交換器へ流入させて、この流入させた加熱後の熱媒体との熱交換により炉頂ガスを加熱し、奪熱された熱媒体を前記排ガス熱交換器へ流出させる加熱状態と、前記燃料ガス熱交換器および前記燃焼空気熱交換器から流出する奪熱後の熱媒体を前記炉頂ガス熱交換器へ流入させて、この流入させた奪熱後の熱媒体との熱交換により炉頂ガスを冷却し、加熱された熱媒体を前記燃料ガス熱交換器および前記燃焼空気熱交換器へ流出させる冷却状態と、を切り替え可能に構成されていることを特徴とする。   The dry dust collection system of the present invention includes a blast furnace, a hot blast furnace for supplying hot blast to the blast furnace, fuel gas supply means and combustion air supply means for supplying fuel gas and combustion air to the hot blast furnace, and the hot blast furnace. An exhaust heat reuse system for reusing the exhaust gas of the above, a furnace top gas temperature adjusting means for adjusting the temperature of the furnace top gas generated from the blast furnace, a dry dust collector for removing dust in the furnace top gas, and A furnace top pressure recovery turbine driven by furnace top gas from a dry dust collector, and the exhaust heat reuse system is provided in an exhaust gas pipe from the hot stove, between the inflowing heat medium and the exhaust gas Exhaust gas heat exchanger for exchanging heat and allowing the heated heat medium to flow out, fuel gas piping connecting the fuel gas supply means and the hot stove, and connecting the combustion air supply means and the hot stove Provided in each combustion air pipe and heat-exchanged with the heat medium heated by the exhaust gas heat exchanger to heat the fuel gas and combustion air, and the cooled heat medium to the exhaust gas heat exchanger In the dry dust collection system for blast furnace top gas composed of a fuel gas heat exchanger and a combustion air heat exchanger to be introduced, the top gas temperature adjusting means connects the blast furnace and the dry dust collector A furnace top gas heat exchanger that is provided in the furnace top gas pipe and performs heat exchange between the inflowing heat medium and the furnace top gas and flows out the heat medium, and heat in the furnace top gas heat exchanger Furnace top gas temperature measuring means for measuring the temperature of the furnace top gas before replacement, and heat medium switching means for switching the heat medium inflow source and the heat medium outflow destination in the furnace top gas heat exchanger, The heat medium switching means measures the furnace top gas temperature. On the basis of the measurement results of the means, the heated heat medium flowing out from the exhaust gas heat exchanger is caused to flow into the furnace top gas heat exchanger, and the furnace is exchanged with the heated heat medium that has been introduced. A heating state in which the top gas is heated and the deprived heat medium flows out to the exhaust gas heat exchanger, and the deprived heat medium flowing out from the fuel gas heat exchanger and the combustion air heat exchanger is removed from the furnace. The gas is introduced into the top gas heat exchanger, and the furnace top gas is cooled by heat exchange with the heat medium after deprived heat that has flowed in, and the heated heat medium is exchanged with the fuel gas heat exchanger and the combustion air heat exchange. It is configured to be switchable between a cooling state to be discharged to the vessel.

また、本発明の乾式集塵方法は、高炉と、前記高炉に熱風を供給する熱風炉と、前記熱風炉に燃料ガスおよび燃焼空気を供給する燃料ガス供給手段および燃焼空気供給手段と、前記熱風炉からの排気ガスを再利用する排熱再利用システムと、前記炉頂ガス中のダストを除去する乾式集塵機と、前記乾式集塵機からの炉頂ガスにより駆動する炉頂圧回収タービンと、を少なくとも備え、前記排熱再利用システムは、前記熱風炉からの排ガス配管に設けられ、流入する熱媒体と排気ガスの間で熱交換を行って、加熱後の熱媒体を流出させる排ガス熱交換器と、前記燃料ガス供給手段と前記熱風炉とを連結する燃料ガス配管および前記燃焼空気供給手段と前記熱風炉とを連結する燃焼空気配管に各々設けられ、前記排ガス熱交換器で加熱された熱媒体との間で熱交換を行って燃料ガスおよび燃焼空気を加熱し、冷却後の熱媒体を前記排ガス熱交換器へと流入させる燃料ガス熱交換器および燃焼空気熱交換器と、から構成される高炉炉頂ガスの乾式集塵システムを利用する乾式集塵方法であって、前記乾式集塵システムに、前記高炉と前記乾式集塵機とを連結する炉頂ガス配管に設けられ、流入する熱媒体と炉頂ガスとの間で熱交換を行って、当該熱媒体を流出させる炉頂ガス熱交換器と、前記炉頂ガス熱交換器での熱交換前の炉頂ガスの温度を測定する炉頂ガス温度測定手段と、前記炉頂ガス熱交換器における熱媒体の流入元および熱媒体の流出先を切り替える熱媒体切替手段と、を設け、前記炉頂ガス温度測定手段で測定された温度が予め設定された下限値未満であると判断すると、前記排ガス熱交換器から流出する加熱後の熱媒体を前記炉頂ガス熱交換器へ流入させて、この流入させた加熱後の熱媒体との熱交換により炉頂ガスを加熱し、奪熱された熱媒体を前記排ガス熱交換器へ流出させる加熱状態に設定し、予め設定された上限値以上であると判断すると、前記燃料ガス熱交換器および前記燃焼空気熱交換器から流出する奪熱後の熱媒体を前記炉頂ガス熱交換器へ流入させて、この流入させた奪熱後の熱媒体との熱交換により炉頂ガスを冷却し、加熱された熱媒体を前記燃料ガス熱交換器および前記燃焼空気熱交換器へ流出させる冷却状態に設定することを特徴とする。   The dry dust collection method of the present invention includes a blast furnace, a hot blast furnace for supplying hot air to the blast furnace, fuel gas supply means for supplying fuel gas and combustion air to the hot blast furnace, combustion air supply means, and the hot air An exhaust heat recycling system that reuses exhaust gas from the furnace, a dry dust collector that removes dust in the furnace top gas, and a furnace top pressure recovery turbine that is driven by the furnace top gas from the dry dust collector. The exhaust heat reuse system is provided in an exhaust gas pipe from the hot stove, and an exhaust gas heat exchanger for exchanging heat between the inflowing heat medium and the exhaust gas and causing the heated heat medium to flow out. , A fuel gas pipe connecting the fuel gas supply means and the hot stove, and a combustion air pipe connecting the combustion air supply means and the hot stove, respectively, and heated by the exhaust gas heat exchanger A fuel gas heat exchanger and a combustion air heat exchanger that heat the fuel gas and the combustion air with each other and heat the cooled heat medium into the exhaust gas heat exchanger. A dry dust collection method using a dry dust collection system for a blast furnace top gas, wherein the dry dust collection system is provided in a furnace top gas pipe connecting the blast furnace and the dry dust collector; A furnace top gas heat exchanger that exchanges heat with the furnace top gas and flows out the heat medium, and a furnace top gas that measures the temperature of the furnace top gas before heat exchange in the furnace top gas heat exchanger. Gas temperature measuring means and heat medium switching means for switching the heat medium inflow source and the heat medium outflow destination in the furnace top gas heat exchanger are provided, and the temperature measured by the furnace gas temperature measuring means is previously measured. If it is determined that it is less than the set lower limit, The heated heating medium flowing out from the exhaust gas heat exchanger was caused to flow into the furnace top gas heat exchanger, and the furnace top gas was heated by heat exchange with the heated heating medium that was introduced, and was deprived of heat. When the heating medium is set to a heating state that flows out to the exhaust gas heat exchanger and is determined to be equal to or higher than a preset upper limit value, after the heat removal flowing out from the fuel gas heat exchanger and the combustion air heat exchanger A heat medium is caused to flow into the furnace top gas heat exchanger, the furnace top gas is cooled by heat exchange with the heat medium that has been deprived, and the heated heat medium is converted into the fuel gas heat exchanger and The cooling state is set to flow out to the combustion air heat exchanger.

以上のような本発明によれば、高炉に熱風を供給する熱風炉の排気ガス、燃料ガス、および、燃焼空気を利用して、炉頂ガスの温度を調整する。具体的に、炉頂ガスの温度を上げたい場合には、燃料ガスと燃焼空気との熱交換により加熱された熱媒体を利用して、炉頂ガスの温度を上げる。一方で、炉頂ガスの温度を下げたい場合には、排気ガスとの熱交換に利用される加熱されていない熱媒体を利用して、炉頂ガスの温度を下げる。
このため、高炉の操業中には常に運転している熱風炉の排気ガスを使用しているため、炉頂ガスの温度調整をいつでも行うことができ、安定的に炉頂ガスの昇温や冷却を行うことができる。従って、湿式集塵機が不要となり、乾式集塵機のみを使用することができるので、TRTによる電力回収量の低下を防止できる。また、排熱再利用システムを利用して炉頂ガスの温度調整を行っているため、炉頂ガス配管に炉頂ガス熱交換器を設けるとともに、排熱再利用システムで循環させている熱媒体を炉頂ガス熱交換器に供給する経路を設けるだけでよい。さらに、熱媒体を循環させるための配管として比較的小さいサイズのものを用いることができる。よって、設備費の増加を抑制できる。
According to the present invention as described above, the temperature of the top gas is adjusted using the exhaust gas, the fuel gas, and the combustion air of the hot air furnace that supplies the hot air to the blast furnace. Specifically, when it is desired to increase the temperature of the furnace top gas, the temperature of the furnace top gas is increased using a heat medium heated by heat exchange between the fuel gas and the combustion air. On the other hand, when it is desired to lower the temperature of the furnace top gas, the temperature of the furnace top gas is lowered using an unheated heat medium used for heat exchange with the exhaust gas.
For this reason, since the exhaust gas from the hot stove that is always in operation is used during the operation of the blast furnace, the temperature of the furnace top gas can be adjusted at any time, and the temperature rise and cooling of the furnace top gas can be performed stably. It can be performed. Therefore, a wet dust collector is not required, and only a dry dust collector can be used, so that it is possible to prevent a reduction in power recovery amount due to TRT. In addition, because the temperature of the furnace top gas is adjusted using the exhaust heat reuse system, a furnace top gas heat exchanger is provided in the furnace top gas piping, and the heat medium circulated in the exhaust heat reuse system It is only necessary to provide a path for supplying the gas to the furnace top gas heat exchanger. Furthermore, a relatively small size pipe can be used for circulating the heat medium. Therefore, an increase in equipment cost can be suppressed.

本発明の乾式集塵システムでは、前記熱媒体切替手段は、前記排ガス熱交換器から流出し前記炉頂ガス熱交換器に流入する加熱後の熱媒体の流量を調整する第1熱媒体流入弁と、前記燃料ガス熱交換器および前記燃焼空気熱交換器から流出し前記炉頂ガス熱交換器に流入する奪熱後の熱媒体の流量を調整する第2熱媒体流入弁と、前記炉頂ガス熱交換器から流出し前記排ガス熱交換器に流入する奪熱後の熱媒体の流量を調整する第1熱媒体流出弁と、前記炉頂ガス熱交換器から流出し前記燃料ガス熱交換器および前記燃焼空気熱交換器に流入する加熱後の熱媒体の流量を調整する第2熱媒体流出弁と、を備え、前記炉頂ガス温度調整手段は、前記炉頂ガス熱交換器での熱交換前の炉頂ガスの流量を測定する炉頂ガス流量測定手段と、前記第1熱媒体流入弁に流入する加熱後の熱媒体の温度および流量を測定する第1熱媒体測定手段と、前記第2熱媒体流入弁に流入する冷却後の熱媒体の温度および流量を測定する第2熱媒体測定手段と、を備えることが好ましい。   In the dry dust collection system of the present invention, the heat medium switching means adjusts the flow rate of the heated heat medium flowing out from the exhaust gas heat exchanger and flowing into the furnace top gas heat exchanger. A second heat medium inlet valve that adjusts the flow rate of the heat medium after heat removal flowing out of the fuel gas heat exchanger and the combustion air heat exchanger and flowing into the furnace top gas heat exchanger, and the furnace top A first heat medium outlet valve for adjusting the flow rate of the heat medium after heat removal flowing out from the gas heat exchanger and flowing into the exhaust gas heat exchanger; and the fuel gas heat exchanger flowing out from the furnace top gas heat exchanger And a second heat medium outlet valve that adjusts the flow rate of the heated heat medium flowing into the combustion air heat exchanger, and the furnace top gas temperature adjusting means is configured to heat the heat in the furnace top gas heat exchanger. A furnace top gas flow rate measuring means for measuring a flow rate of the furnace top gas before replacement; First heat medium measuring means for measuring the temperature and flow rate of the heated heat medium flowing into the medium inflow valve, and second temperature for measuring the temperature and flow rate of the cooled heat medium flowing into the second heat medium inflow valve It is preferable to include a heat medium measuring unit.

ここで、例えば、炉頂ガスの温度を目的温度までの上昇させる時間を、炉頂ガスの温度によらず一定にする場合、炉頂ガスの流量が多いほど、炉頂ガスに与える単位時間あたりの熱量を多くする必要がある。
この発明によれば、炉頂ガス熱交換器に流入させる熱媒体の温度に応じて、第1熱媒体流入弁を調整することで、炉頂ガスとの熱交換に利用される熱媒体の流量を調整することができる。すなわち、炉頂ガスに与える単位時間あたりの熱量を調整できる。従って、温度調整対象の炉頂ガスの流量にあわせた必要な熱量を、炉頂ガスに与えることができ、炉頂ガスの温度によらず、炉頂ガスの温度を目的温度まで上昇させる時間を一定にできる。
Here, for example, when the time for raising the temperature of the furnace top gas to the target temperature is made constant regardless of the temperature of the furnace top gas, the higher the flow rate of the furnace top gas, the more per unit time given to the furnace top gas. It is necessary to increase the amount of heat.
According to this invention, the flow rate of the heat medium used for heat exchange with the furnace top gas by adjusting the first heat medium inlet valve according to the temperature of the heat medium flowing into the furnace top gas heat exchanger. Can be adjusted. That is, the amount of heat per unit time given to the furnace top gas can be adjusted. Therefore, the necessary amount of heat according to the flow rate of the furnace top gas to be temperature-adjusted can be given to the furnace top gas, and the time for raising the temperature of the furnace top gas to the target temperature regardless of the temperature of the furnace top gas. Can be constant.

本発明の乾式集塵システムでは、前記炉頂ガス温度調整手段は、前記炉頂ガス温度測定手段で測定された温度が予め設定された下限値未満であると判断すると、前記熱媒体切替手段を前記加熱状態に設定し、予め設定された上限値以上であると判断すると、前記熱媒体切替手段を前記冷却状態に設定する熱媒体制御手段を備え、前記熱媒体制御手段は、前記炉頂ガス流量測定手段、前記第1熱媒体測定手段、および、前記第2熱媒体測定手段での測定結果に基づいて、前記第1熱媒体流入弁、前記第2熱媒体流入弁、前記第1熱媒体流出弁、および、前記第2熱媒体流出弁を制御することで、前記炉頂ガス熱交換器に流入する熱媒体の流量を調整することが好ましい。   In the dry dust collection system of the present invention, when the furnace top gas temperature adjusting means determines that the temperature measured by the furnace top gas temperature measuring means is less than a preset lower limit value, the heat medium switching means is When the heating state is set and it is determined that it is equal to or higher than a preset upper limit value, the heating medium switching means sets the heating medium switching means to the cooling state, and the heating medium control means includes the furnace top gas Based on the measurement results of the flow rate measuring means, the first heat medium measuring means, and the second heat medium measuring means, the first heat medium inflow valve, the second heat medium inflow valve, and the first heat medium. It is preferable to adjust the flow rate of the heat medium flowing into the furnace top gas heat exchanger by controlling the outflow valve and the second heat medium outflow valve.

この発明によれば、熱媒体制御手段による自動制御により炉頂ガスの温度を適切に調整できるため、対応が瞬時にタイミングよくでき、作業者の負荷を低減できる。   According to the present invention, since the temperature of the furnace top gas can be appropriately adjusted by automatic control by the heat medium control means, the response can be instantly performed and the load on the operator can be reduced.

本発明の乾式集塵システムでは、前記炉頂ガス配管は、前記炉頂ガス熱交換器が設置された熱交換器設置管と、前記熱交換器設置管における前記炉頂ガス熱交換器よりも前記高炉側と前記炉頂ガス熱交換器よりも前記乾式集塵機側とを連結するバイパス管と、を備え、前記炉頂ガス温度調整手段は、前記熱交換器設置管に炉頂ガスを流通させて当該炉頂ガスの熱交換を行う熱交換状態と、前記バイパス管に炉頂ガスを流通させて当該炉頂ガスの熱交換を行わない非熱交換状態と、を切り替える熱交換状態切替手段を備えることが好ましい。   In the dry dust collection system of the present invention, the furnace top gas pipe is more than a heat exchanger installation pipe in which the furnace top gas heat exchanger is installed, and the furnace top gas heat exchanger in the heat exchanger installation pipe. A bypass pipe that connects the blast furnace side and the dry dust collector side with respect to the furnace top gas heat exchanger, and the furnace top gas temperature adjusting means distributes the furnace top gas to the heat exchanger installation pipe. Heat exchange state switching means for switching between a heat exchange state in which heat exchange of the furnace top gas is performed and a non-heat exchange state in which the furnace top gas is circulated through the bypass pipe and heat exchange of the furnace top gas is not performed. It is preferable to provide.

この発明によれば、熱交換状態切替手段により、排気ガスの熱交換を行う熱交換状態と、熱交換を行わない非熱交換状態とを切り替えることにより、必要な場合のみ炉頂ガス熱交換器を使用することができ、炉頂ガス熱交換器の長寿命化を図ることができる。   According to the present invention, the furnace top gas heat exchanger is switched only when necessary by switching between the heat exchange state in which the heat exchange of the exhaust gas is performed and the non-heat exchange state in which the heat exchange is not performed by the heat exchange state switching means. Can be used, and the life of the furnace top gas heat exchanger can be extended.

本発明の乾式集塵システムでは、前記炉頂ガス温度調整手段は、前記炉頂ガス温度測定手段で測定された温度が予め設定された下限値未満、又は、予め設定された上限値以上であると判断すると、前記熱交換状態切替手段を前記熱交換状態に設定し、前記下限値以上且つ前記上限値未満であると判断すると、前記熱交換状態切替手段を前記非熱交換状態に設定する熱交換制御手段を備えることが好ましい。   In the dry dust collection system of the present invention, the furnace top gas temperature adjusting means is such that the temperature measured by the furnace top gas temperature measuring means is less than a preset lower limit value or more than a preset upper limit value. The heat exchange state switching means is set to the heat exchange state, and if it is determined that the heat exchange state switching means is less than the upper limit value and less than the upper limit value, the heat exchange state switching means is set to the non-heat exchange state. It is preferable to provide an exchange control means.

この発明によれば、熱交換制御手段による自動制御により、炉頂ガスの熱交換を行うか否かを適切に調整できるため、対応が瞬時にタイミングよくでき、作業者の負荷を低減できる。   According to the present invention, it is possible to appropriately adjust whether or not the heat exchange of the furnace top gas is performed by automatic control by the heat exchange control means. Therefore, it is possible to instantly cope with the situation and reduce the load on the operator.

本発明の一実施形態に係る高炉炉頂ガスの乾式集塵システムを示す模式図。The schematic diagram which shows the dry dust collection system of the blast furnace top gas which concerns on one Embodiment of this invention. 前記乾式集塵システムの炉頂ガス温度調整手段の要部を示すブロック図。The block diagram which shows the principal part of the furnace top gas temperature adjustment means of the said dry-type dust collection system. 前記乾式集塵システムにおける立ち上げの際の作用を示す説明図。Explanatory drawing which shows the effect | action at the time of starting in the said dry-type dust collection system. 前記乾式集塵システムにおける炉頂ガス温度を上げるときの作用を示す説明図。Explanatory drawing which shows an effect | action when raising the furnace top gas temperature in the said dry-type dust collection system. 前記乾式集塵システムにおける炉頂ガス温度を下げるときの作用を示す説明図。Explanatory drawing which shows an effect | action when lowering the furnace top gas temperature in the said dry-type dust collection system.

以下、本発明の実施形態を図面に基づいて説明する。
[乾式集塵システムの構成]
図1において、乾式集塵システム1は、高炉2と、この高炉2に熱風を供給する2基の熱風炉3と、この熱風炉3に燃料を供給する燃料供給手段4と、熱媒体を循環させることで煙突31から発生する排気ガスEの熱を再利用する排熱再利用システム5と、高炉2から発生する炉頂ガスGの温度を調整する炉頂ガス温度調整手段6と、熱風炉3で温度が調整された炉頂ガスG中の固体粒子を除去する集塵設備7と、この集塵設備7で固体粒子が除去された炉頂ガスGで駆動するTRT8とを備える。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[Configuration of dry dust collection system]
In FIG. 1, a dry dust collection system 1 includes a blast furnace 2, two hot blast furnaces 3 for supplying hot air to the blast furnace 2, fuel supply means 4 for supplying fuel to the hot blast furnace 3, and a heat medium. The exhaust heat reuse system 5 for reusing the heat of the exhaust gas E generated from the chimney 31, the furnace top gas temperature adjusting means 6 for adjusting the temperature of the furnace top gas G generated from the blast furnace 2, and the hot stove 3, a dust collection facility 7 that removes solid particles in the furnace top gas G whose temperature has been adjusted in 3, and a TRT 8 that is driven by the furnace top gas G from which solid particles have been removed by the dust collection equipment 7.

熱風炉3は、それぞれ図示しない燃焼室と、蓄熱室とを備える。
燃焼室は、燃料供給手段4から供給される燃料ガスおよび燃焼空気を混合して燃焼させる。
蓄熱室では、燃焼室での燃焼ガスから生ずる熱を蓄え、蓄熱後の排気ガスEを煙突31から排出する。一方で、蓄熱室では、蓄熱が終了した後、この蓄えた熱を送風機32から導入される空気に伝えて熱風Wを生成し、高炉2の羽口に供給する。なお、熱風炉3の数は、3基以上であっても良い。
The hot stove 3 includes a combustion chamber (not shown) and a heat storage chamber.
The combustion chamber mixes and burns fuel gas and combustion air supplied from the fuel supply means 4.
In the heat storage chamber, heat generated from the combustion gas in the combustion chamber is stored, and the exhaust gas E after the heat storage is discharged from the chimney 31. On the other hand, in the heat storage chamber, after the heat storage is completed, the stored heat is transmitted to the air introduced from the blower 32 to generate hot air W, which is supplied to the tuyere of the blast furnace 2. In addition, the number of the hot stove 3 may be three or more.

燃料供給手段4は、燃料ガスを熱風炉3に供給する燃料ガス供給手段41と、燃料ガスに対して所定の比率となるような燃焼空気を熱風炉3に供給する燃焼空気供給手段42とを備える。
また、燃料ガス供給手段41から延びる燃料ガス配管411、燃焼空気供給手段42から延びる燃焼空気配管421、煙突31へと延びる排ガス配管311、送風機32から延びる配管321、および、高炉2の図示しない羽口へと延びる配管201は、それぞれ2個に分岐しており、2基の熱風炉3にそれぞれ接続されている。また、燃料ガス配管411、燃焼空気配管421、排ガス配管311、配管321、配管201における分岐点よりも熱風炉3側には、それぞれ弁43、弁44、弁33、弁34、弁21が設けられている。
The fuel supply means 4 includes a fuel gas supply means 41 for supplying fuel gas to the hot stove 3 and a combustion air supply means 42 for supplying combustion air to the hot stove 3 at a predetermined ratio to the fuel gas. Prepare.
Further, a fuel gas pipe 411 extending from the fuel gas supply means 41, a combustion air pipe 421 extending from the combustion air supply means 42, an exhaust gas pipe 311 extending to the chimney 31, a pipe 321 extending from the blower 32, and a blade (not shown) of the blast furnace 2 Each of the pipes 201 extending to the mouth is branched into two and connected to the two hot stoves 3. Further, a valve 43, a valve 44, a valve 33, a valve 34, and a valve 21 are provided on the hot stove 3 side of the branch point in the fuel gas pipe 411, the combustion air pipe 421, the exhaust gas pipe 311, the pipe 321, and the pipe 201, respectively. It has been.

排熱再利用システム5は、排ガス熱交換器51と、燃料ガス熱交換器52と、燃焼空気熱交換器53と、熱媒体貯槽54と、膨張タンク55とを備える。なお、以下において、加熱されていない低温の熱媒体を低温媒体Lと言い、加熱された高温の熱媒体を高温媒体Hと言う場合がある。   The exhaust heat reuse system 5 includes an exhaust gas heat exchanger 51, a fuel gas heat exchanger 52, a combustion air heat exchanger 53, a heat medium storage tank 54, and an expansion tank 55. In the following, a low-temperature heat medium that is not heated may be referred to as a low-temperature medium L, and a heated high-temperature heat medium may be referred to as a high-temperature medium H.

排ガス熱交換器51、燃料ガス熱交換器52、および、燃焼空気熱交換器53は、排ガス配管311、燃料ガス配管411、および、燃焼空気配管421における、分岐点よりも煙突31側、燃料ガス供給手段41側、および、燃焼空気供給手段42側に、それぞれ設けられている。
排ガス熱交換器51の出口から延びる高温管511は、2個に分岐しており、燃料ガス熱交換器52、燃焼空気熱交換器53の入口にそれぞれ接続されている。また、排ガス熱交換器51の入口から延びる低温管512も、2個に分岐しており、燃料ガス熱交換器52、燃焼空気熱交換器53の出口にそれぞれ接続されている。低温管512には、熱媒体を循環させる循環ポンプ56が設けられている。
The exhaust gas heat exchanger 51, the fuel gas heat exchanger 52, and the combustion air heat exchanger 53 are arranged on the chimney 31 side of the exhaust gas pipe 311, the fuel gas pipe 411, and the combustion air pipe 421, the fuel gas. Provided on the supply means 41 side and the combustion air supply means 42 side, respectively.
The high temperature pipe 511 extending from the outlet of the exhaust gas heat exchanger 51 is branched into two, and is connected to the inlets of the fuel gas heat exchanger 52 and the combustion air heat exchanger 53, respectively. A cryogenic pipe 512 extending from the inlet of the exhaust gas heat exchanger 51 is also branched into two and connected to the outlets of the fuel gas heat exchanger 52 and the combustion air heat exchanger 53, respectively. The cryogenic pipe 512 is provided with a circulation pump 56 for circulating the heat medium.

熱媒体貯槽54は、配管541を介して低温管512に接続されている。配管541には、熱媒体貯槽54に貯蔵された熱媒体を低温管512に供給する供給ポンプ57が設けられている。
膨張タンク55は、配管551を介して低温管512に接続され、低温管512内の熱媒体が膨張した際に、この膨張分の熱媒体を吸収する。
The heat medium storage tank 54 is connected to the cryogenic pipe 512 via a pipe 541. The pipe 541 is provided with a supply pump 57 that supplies the heat medium stored in the heat medium storage tank 54 to the cryogenic pipe 512.
The expansion tank 55 is connected to the low-temperature pipe 512 via the pipe 551, and absorbs the heat medium corresponding to the expansion when the heat medium in the low-temperature pipe 512 expands.

集塵設備7は、除塵器71と、乾式集塵機72とを備える。
乾式集塵機72は、炉頂ガス配管721を介して除塵器71に接続され、配管724を介してTRT8に接続されている。乾式集塵機72は、図示しない濾布を備える。そして、乾式集塵機72は、炉頂ガスGのダストを濾布で除去してTRT8へ供給する。なお、炉頂ガス配管721は、除塵器71と乾式集塵機72とを連結し後述する炉頂ガス熱交換器61が設置される熱交換器設置管722と、熱交換器設置管722における炉頂ガス熱交換器61よりも除塵器71側と乾式集塵機72側とを連結するバイパス管723とを備える。
The dust collector 7 includes a dust remover 71 and a dry dust collector 72.
The dry dust collector 72 is connected to the dust remover 71 via the furnace top gas pipe 721 and connected to the TRT 8 via the pipe 724. The dry dust collector 72 includes a filter cloth (not shown). Then, the dry dust collector 72 removes the dust of the furnace top gas G with a filter cloth and supplies it to the TRT 8. The furnace top gas pipe 721 connects the dust remover 71 and the dry dust collector 72 and has a heat exchanger installation pipe 722 in which a furnace top gas heat exchanger 61 described later is installed, and a furnace top in the heat exchanger installation pipe 722. A bypass pipe 723 that connects the dust remover 71 side and the dry dust collector 72 side to the gas heat exchanger 61 is provided.

ここで、炉頂ガスGの温度が高すぎると、乾式集塵機72が有する濾布が焼損してしまい、前記温度が低すぎると、濾布が結露して乾式集塵機72の集塵性能が低下してしまうため、炉頂ガスGの温度を適切に制御する必要がある。
炉頂ガス温度調整手段6は、このような不具合を解消するためのものであり、炉頂ガス熱交換器61と、炉頂ガス温度測定手段62と、炉頂ガス流量測定手段63と、第1熱媒体測定手段64と、第2熱媒体測定手段65と、熱交換状態切替手段66と、熱媒体切替手段67と、熱交換後ガス温度測定手段68と、制御装置69(図2参照)とを備える。
Here, if the temperature of the furnace top gas G is too high, the filter cloth of the dry dust collector 72 is burned out. If the temperature is too low, the filter cloth is condensed and the dust collection performance of the dry dust collector 72 is lowered. Therefore, it is necessary to appropriately control the temperature of the furnace top gas G.
The furnace top gas temperature adjusting means 6 is for eliminating such problems, and the furnace top gas heat exchanger 61, the furnace top gas temperature measuring means 62, the furnace top gas flow rate measuring means 63, the first 1 heat medium measuring means 64, second heat medium measuring means 65, heat exchange state switching means 66, heat medium switching means 67, gas temperature measuring means 68 after heat exchange, and control device 69 (see FIG. 2) With.

炉頂ガス熱交換器61は、熱交換器設置管722に設置され、排熱再利用システム5で循環させる熱媒体と、炉頂ガスGとの間で熱交換を行う。この炉頂ガス熱交換器61の入口には、入口配管611が接続され、出口には、出口配管612が接続されている。入口配管611は、2個に分岐しており、この分岐の先端が高温管511と低温管512とにそれぞれ連結されている。また、出口配管612も2個に分岐しており、この分岐の先端が高温管511と低温管512とにそれぞれ連結されている。なお、高温管511における入口配管611との連結点は、出口配管612との連結点よりも上流側に位置している。また、低温管512における入口配管611との連結点は、出口配管612との連結点よりも下流側に位置している。   The furnace top gas heat exchanger 61 is installed in the heat exchanger installation pipe 722 and performs heat exchange between the heat medium circulated in the exhaust heat reuse system 5 and the furnace top gas G. An inlet pipe 611 is connected to the inlet of the furnace top gas heat exchanger 61, and an outlet pipe 612 is connected to the outlet. The inlet pipe 611 is branched into two, and the leading ends of the branches are connected to the high temperature pipe 511 and the low temperature pipe 512, respectively. Further, the outlet pipe 612 is also branched into two, and the tips of the branches are connected to the high temperature pipe 511 and the low temperature pipe 512, respectively. In addition, the connection point with the inlet pipe 611 in the high temperature pipe 511 is located upstream from the connection point with the outlet pipe 612. Further, the connection point of the cryogenic pipe 512 with the inlet pipe 611 is located downstream of the connection point with the outlet pipe 612.

炉頂ガス温度測定手段62および炉頂ガス流量測定手段63は、配管711に設置されている。炉頂ガス温度測定手段62は、炉頂ガス熱交換器61での熱交換前の炉頂ガスGの温度を測定し、炉頂ガス流量測定手段63は、炉頂ガス熱交換器61での熱交換前の炉頂ガスGの流量を測定する。そして、炉頂ガス温度測定手段62および炉頂ガス流量測定手段63は、その測定結果を制御装置69へ出力する。   The furnace top gas temperature measuring means 62 and the furnace top gas flow rate measuring means 63 are installed in the pipe 711. The furnace top gas temperature measuring means 62 measures the temperature of the furnace top gas G before heat exchange in the furnace top gas heat exchanger 61, and the furnace top gas flow rate measuring means 63 is measured by the furnace top gas heat exchanger 61. The flow rate of the top gas G before heat exchange is measured. Then, the furnace top gas temperature measuring means 62 and the furnace top gas flow rate measuring means 63 output the measurement results to the control device 69.

第1熱媒体測定手段64は、高温管511における入口配管611との接続点よりも上流側に、第2熱媒体測定手段65は、低温管512における入口配管611との接続点よりも上流側に、それぞれ設けられている。第1熱媒体測定手段64は、高温管511を流通する熱媒体の温度を測定する熱媒体温度測定手段641と、当該熱媒体の流量を測定する熱媒体流量測定手段642とを備える。また、第2熱媒体測定手段65も同様に、低温管512を流通する熱媒体の温度および流量をそれぞれ測定する熱媒体温度測定手段651と、熱媒体流量測定手段652とを備える。そして、第1熱媒体測定手段64および第2熱媒体測定手段65は、熱媒体温度測定手段641、熱媒体温度測定手段651、熱媒体流量測定手段642、熱媒体流量測定手段652での測定結果を制御装置69へ出力する。   The first heat medium measuring means 64 is upstream of the connection point with the inlet pipe 611 in the high temperature pipe 511, and the second heat medium measurement means 65 is upstream of the connection point with the inlet pipe 611 in the low temperature pipe 512. Are provided respectively. The first heat medium measuring means 64 includes a heat medium temperature measuring means 641 that measures the temperature of the heat medium flowing through the high temperature pipe 511 and a heat medium flow measuring means 642 that measures the flow rate of the heat medium. Similarly, the second heat medium measuring means 65 includes a heat medium temperature measuring means 651 that measures the temperature and flow rate of the heat medium flowing through the cryogenic pipe 512, and a heat medium flow rate measuring means 652, respectively. The first heat medium measuring means 64 and the second heat medium measuring means 65 are the measurement results of the heat medium temperature measuring means 641, the heat medium temperature measuring means 651, the heat medium flow measuring means 642, and the heat medium flow measuring means 652. Is output to the control device 69.

熱交換状態切替手段66は、炉頂ガスGを炉頂ガス熱交換器61において熱交換を行う熱交換状態と、熱交換を行わない非熱交換状態とを切り替える。この熱交換状態切替手段66は、熱交換器設置管722における炉頂ガス熱交換器61よりも除塵器71側および乾式集塵機72側にそれぞれ設けられた一対の熱切替弁661と、バイパス管723に設けられたバイパス弁662とを備える。熱切替弁661およびバイパス弁662は、制御装置69の制御により、開度を連続的に調整可能に構成されている。   The heat exchange state switching means 66 switches between a heat exchange state in which the furnace top gas G performs heat exchange in the furnace top gas heat exchanger 61 and a non-heat exchange state in which heat exchange is not performed. The heat exchange state switching means 66 includes a pair of heat switching valves 661 provided on the dust remover 71 side and the dry dust collector 72 side of the furnace top gas heat exchanger 61 in the heat exchanger installation pipe 722, and a bypass pipe 723. And a bypass valve 662 provided in The heat switching valve 661 and the bypass valve 662 are configured such that the opening degree can be continuously adjusted under the control of the control device 69.

熱媒体切替手段67は、炉頂ガス熱交換器61に流入させる熱媒体を切り替えるとともに、当該熱媒体の流量を調整する。この熱媒体切替手段67は、第1熱媒体流入弁671と、第2熱媒体流入弁672と、第1熱媒体流出弁673と、第2熱媒体流出弁674とを備える。
第1熱媒体流入弁671は、入口配管611における分岐点よりも高温管511側に設置され、第2熱媒体流入弁672は、当該分岐点よりも低温管512側に設置されている。また、第1熱媒体流出弁673は、出口配管612における分岐点よりも低温管512側に設置され、第2熱媒体流出弁674は、当該分岐点よりも高温管511側に設置されている。第1熱媒体流入弁671、第2熱媒体流入弁672、第1熱媒体流出弁673、第2熱媒体流出弁674は、制御装置69の制御により、開度を連続的に調整可能に構成されている。
熱交換後ガス温度測定手段68は、炉頂ガス配管721における炉頂ガス熱交換器61の後流側に設けられ、熱媒体との熱交換後の炉頂ガスの温度を測定し、その測定結果を制御装置69へ出力する。
The heat medium switching means 67 switches the heat medium flowing into the furnace top gas heat exchanger 61 and adjusts the flow rate of the heat medium. The heat medium switching means 67 includes a first heat medium inflow valve 671, a second heat medium inflow valve 672, a first heat medium outflow valve 673, and a second heat medium outflow valve 674.
The first heat medium inflow valve 671 is installed closer to the high temperature pipe 511 than the branch point in the inlet pipe 611, and the second heat medium inflow valve 672 is installed closer to the cold pipe 512 than the branch point. Further, the first heat medium outflow valve 673 is installed closer to the low temperature pipe 512 than the branch point in the outlet pipe 612, and the second heat medium outflow valve 674 is installed closer to the high temperature pipe 511 than the branch point. . The first heat medium inflow valve 671, the second heat medium inflow valve 672, the first heat medium outflow valve 673, and the second heat medium outflow valve 674 are configured such that the opening degree can be continuously adjusted under the control of the control device 69. Has been.
The post-heat exchange gas temperature measuring means 68 is provided on the downstream side of the furnace top gas heat exchanger 61 in the furnace top gas pipe 721, measures the temperature of the furnace top gas after heat exchange with the heat medium, and measures the temperature. The result is output to the control device 69.

制御装置69は、いわゆるコンピュータであり、図示しない記憶手段に記憶されたプログラムおよびデータをCPU(Central Processing Unit)が処理することにより構成される熱風炉制御手段691と、熱交換制御手段692と、熱媒体制御手段693とを備える。
熱風炉制御手段691は、2基の熱風炉3を必要に応じて稼働させ、熱風Wを高炉2に供給させたり、炉頂ガスGの温度調整に利用するために排気ガスEを排出させたりする。
熱交換制御手段692は、熱交換状態切替手段66を制御して、炉頂ガスGの加熱又は冷却を行う熱交換状態と、加熱および冷却の両方を行わない非熱交換状態とを切り替える。
熱媒体制御手段693は、熱媒体切替手段67を制御して、炉頂ガスGを加熱する加熱状態と、炉頂ガスGを冷却する冷却状態とを切り替える。
The control device 69 is a so-called computer, and a hot stove control means 691 configured by a CPU (Central Processing Unit) processing a program and data stored in a storage means (not shown), a heat exchange control means 692, A heat medium control means 693.
The hot stove control means 691 operates the two hot stoves 3 as necessary to supply hot air W to the blast furnace 2 or exhaust the exhaust gas E for use in adjusting the temperature of the top gas G. To do.
The heat exchange control unit 692 controls the heat exchange state switching unit 66 to switch between a heat exchange state in which the furnace top gas G is heated or cooled and a non-heat exchange state in which neither heating nor cooling is performed.
The heat medium control unit 693 controls the heat medium switching unit 67 to switch between a heating state in which the furnace top gas G is heated and a cooling state in which the furnace top gas G is cooled.

[乾式集塵システムの作用]
次に、乾式集塵システム1の作用について説明する。なお、以下において、熱媒体のうち高温状態の熱媒体を高温媒体Hと、低温状態の熱媒体を低温媒体Lという場合がある。
[Operation of dry dust collection system]
Next, the operation of the dry dust collection system 1 will be described. In the following description, a high-temperature heat medium may be referred to as a high-temperature medium H, and a low-temperature heat medium may be referred to as a low-temperature medium L.

まず、乾式集塵システム1の立ち上げの際、制御装置69の熱風炉制御手段691は、図1に示すように、全ての弁21と弁34とを閉じ、全ての弁43と弁44と弁33とを開く。そして、燃料ガス供給手段41から図1中下の熱風炉3に燃料ガスを供給し、燃焼空気供給手段42から熱風炉3に燃焼空気を供給して、熱風炉3の燃焼室での燃焼を開始する。
一方、制御装置69の熱交換制御手段692は、第1熱媒体流入弁671、第2熱媒体流入弁672、第1熱媒体流出弁673、第2熱媒体流出弁674を閉じて、循環ポンプ56を回転させて熱媒体を低温管512に供給し、この熱媒体を低温管512と高温管511を介して、排ガス熱交換器51と燃料ガス熱交換器52との間、および、排ガス熱交換器51と燃焼空気熱交換器53との間で循環させる。
また、制御装置69の熱媒体制御手段693は、熱切替弁661を閉じ、バイパス弁662を開けて、炉頂ガスGがバイパス管723を流通可能な非熱交換状態に設定する。
First, when the dry dust collection system 1 is started up, the hot stove control means 691 of the control device 69 closes all the valves 21 and 34 and closes all the valves 43 and 44 as shown in FIG. Open the valve 33. Then, the fuel gas is supplied from the fuel gas supply means 41 to the hot stove 3 in the lower part of FIG. 1, and the combustion air is supplied from the combustion air supply means 42 to the hot stove 3 so that the combustion in the combustion chamber of the hot stove 3 is performed. Start.
On the other hand, the heat exchange control means 692 of the control device 69 closes the first heat medium inflow valve 671, the second heat medium inflow valve 672, the first heat medium outflow valve 673, and the second heat medium outflow valve 674, and the circulation pump 56 is rotated to supply a heat medium to the low temperature pipe 512, and this heat medium is supplied between the exhaust gas heat exchanger 51 and the fuel gas heat exchanger 52 via the low temperature pipe 512 and the high temperature pipe 511, and the exhaust gas heat. Circulation is performed between the exchanger 51 and the combustion air heat exchanger 53.
Further, the heat medium control means 693 of the control device 69 closes the heat switching valve 661 and opens the bypass valve 662 to set the non-heat exchange state in which the top gas G can flow through the bypass pipe 723.

熱風炉制御手段691は、熱風炉3の燃焼室での温度が十分に上昇したことを検出すると、図3に示すように、図3中上の熱風炉3に対応する弁34と弁21とを開け、当該熱風炉3に対応する弁33を閉じて、送風機32からの空気を燃焼室に導入し、燃焼室で昇熱された熱風Wを高炉2の羽口に供給する。
一方、昇温中の図3中下の熱風炉3で発生する排気ガスEは、排ガス配管311を介して排ガス熱交換器51内に導入される。この排気ガスEは、排ガス熱交換器51において低温管512から供給される低温媒体Lとの熱交換により熱を奪われた後、煙突31から排出される。
When the hot stove control means 691 detects that the temperature in the combustion chamber of the hot stove 3 has risen sufficiently, as shown in FIG. 3, the valves 34 and 21 corresponding to the hot stove 3 in FIG. Is opened, the valve 33 corresponding to the hot stove 3 is closed, the air from the blower 32 is introduced into the combustion chamber, and the hot air W heated in the combustion chamber is supplied to the tuyere of the blast furnace 2.
On the other hand, the exhaust gas E generated in the hot stove 3 in the lower part of FIG. 3 during the temperature rise is introduced into the exhaust gas heat exchanger 51 through the exhaust gas pipe 311. The exhaust gas E is exhausted from the chimney 31 after heat is removed from the exhaust gas heat exchanger 51 by heat exchange with the low-temperature medium L supplied from the low-temperature pipe 512.

低温管512から排ガス熱交換器51に流入する低温媒体Lは、排気ガスEとの熱交換により加熱されて、高温媒体Hとして高温管511に流出する。この高温媒体Hは、燃料ガス熱交換器52と燃焼空気熱交換器53にそれぞれ流入し、燃料ガスと燃焼空気との熱交換により熱を奪われた後、低温媒体Lとして低温管512に流出する。この低温媒体Lは、排ガス熱交換器51に再度流入し、上述したような排気ガスEとの熱交換に利用される。
一方、燃料ガスと燃焼空気は、燃料ガス熱交換器52および燃焼空気熱交換器53における高温媒体Hとの熱交換により加熱される。この加熱された燃料ガスと燃焼空気が熱風炉3に導入されることで、燃焼室での燃焼が促進される。
The low temperature medium L flowing into the exhaust gas heat exchanger 51 from the low temperature pipe 512 is heated by heat exchange with the exhaust gas E, and flows out to the high temperature pipe 511 as the high temperature medium H. The high temperature medium H flows into the fuel gas heat exchanger 52 and the combustion air heat exchanger 53, and after heat is taken away by heat exchange between the fuel gas and the combustion air, flows out into the low temperature pipe 512 as the low temperature medium L. To do. This low-temperature medium L flows into the exhaust gas heat exchanger 51 again and is used for heat exchange with the exhaust gas E as described above.
On the other hand, the fuel gas and the combustion air are heated by heat exchange with the high-temperature medium H in the fuel gas heat exchanger 52 and the combustion air heat exchanger 53. By introducing the heated fuel gas and combustion air into the hot stove 3, combustion in the combustion chamber is promoted.

高炉2では、羽口に導入された熱風Wを利用して、銑鉄が製造される。この製造の際に生成される炉頂ガスGは、配管711およびバイパス管723を介して除塵器71および乾式集塵機72に導入され、ダストが除去される。そして、ダストが除去された炉頂ガスGは、TRT8に導入され、TRT8の駆動に利用される。   In the blast furnace 2, pig iron is manufactured using hot air W introduced into the tuyere. The top gas G generated during the production is introduced into the dust remover 71 and the dry dust collector 72 through the pipe 711 and the bypass pipe 723, and the dust is removed. The furnace top gas G from which the dust has been removed is introduced into the TRT 8 and used for driving the TRT 8.

制御装置69の熱交換制御手段692は、炉頂ガス温度測定手段62での測定結果に基づいて、高炉2から排出される炉頂ガスGの温度が予め設定された下限値(例えば、70℃)未満と判断した場合、炉頂ガスGの温度を上げるために、熱切替弁661を開け、バイパス弁662を閉じて、図4に示すように、炉頂ガスGが熱交換器設置管722を流通可能な熱交換状態に設定する。
また、制御装置69の熱媒体制御手段693は、炉頂ガスGの温度を上げるために、熱媒体切替手段67を加熱状態に切り替える。具体的に、第1熱媒体流入弁671と第1熱媒体流出弁673とを開く。この切り替えにより、高温管511を流通する高温媒体Hが入口配管611にも流入する。そして、熱交換器設置管722を流通する炉頂ガスGは、炉頂ガス熱交換器61において高温媒体Hとの熱交換により加熱される。この加熱により適切な温度に調整された炉頂ガスGが乾式集塵機72に流入するため、乾式集塵機72の濾布が結露してしまうという不具合が抑制される。
The heat exchange control means 692 of the control device 69 has a preset lower limit value (for example, 70 ° C.) based on the measurement result of the furnace top gas temperature measuring means 62, the temperature of the furnace top gas G discharged from the blast furnace 2. ) To increase the temperature of the furnace top gas G, the heat switching valve 661 is opened, the bypass valve 662 is closed, and the furnace top gas G is transferred to the heat exchanger installation pipe 722 as shown in FIG. Is set to a heat exchange state that allows circulation.
Further, the heat medium control means 693 of the control device 69 switches the heat medium switching means 67 to a heating state in order to increase the temperature of the furnace top gas G. Specifically, the first heat medium inflow valve 671 and the first heat medium outflow valve 673 are opened. By this switching, the high temperature medium H flowing through the high temperature pipe 511 also flows into the inlet pipe 611. The furnace top gas G flowing through the heat exchanger installation pipe 722 is heated by heat exchange with the high-temperature medium H in the furnace top gas heat exchanger 61. Since the furnace top gas G adjusted to an appropriate temperature by this heating flows into the dry dust collector 72, the problem that the filter cloth of the dry dust collector 72 is condensed is suppressed.

ここで、熱媒体制御手段693は、炉頂ガス温度測定手段62、炉頂ガス流量測定手段63、第1熱媒体測定手段64での測定結果に基づいて、第1熱媒体流入弁671の開度を調節することで、炉頂ガスGを目的温度まで上昇させる所要時間を、炉頂ガスGの温度によらずほぼ同じにする。   Here, the heat medium control means 693 opens the first heat medium inlet valve 671 based on the measurement results of the furnace top gas temperature measuring means 62, the furnace top gas flow rate measuring means 63, and the first heat medium measuring means 64. By adjusting the degree, the time required for raising the furnace top gas G to the target temperature is made substantially the same regardless of the temperature of the furnace top gas G.

熱交換制御手段692は、高炉2から排出される炉頂ガスGの温度が予め設定された上限値(例えば、180℃)以上と判断した場合、炉頂ガスGの温度を下げるために、図5に示すように、熱交換状態切替手段66を熱交換状態に設定する。
また、熱媒体制御手段693は、炉頂ガスGの温度を下げるために、熱媒体切替手段67を冷却状態に切り替える。具体的に、第2熱媒体流入弁672と第2熱媒体流出弁674とを開くことで、低温管512を流通する低温媒体Lを入口配管611に流入させる。そして、熱交換器設置管722を流通する炉頂ガスGは、炉頂ガス熱交換器61において低温媒体Lとの熱交換により適切な温度まで冷却され、乾式集塵機72に流入する。これにより、乾式集塵機72の濾布が焼損してしまうという不具合が抑制される。
When the temperature of the top gas G discharged from the blast furnace 2 is determined to be equal to or higher than a preset upper limit value (for example, 180 ° C.), the heat exchange control unit 692 As shown in FIG. 5, the heat exchange state switching means 66 is set to the heat exchange state.
Further, the heat medium control means 693 switches the heat medium switching means 67 to the cooling state in order to lower the temperature of the furnace top gas G. Specifically, by opening the second heat medium inflow valve 672 and the second heat medium outflow valve 674, the low temperature medium L flowing through the low temperature pipe 512 is caused to flow into the inlet pipe 611. The furnace top gas G flowing through the heat exchanger installation pipe 722 is cooled to an appropriate temperature by heat exchange with the low temperature medium L in the furnace top gas heat exchanger 61 and flows into the dry dust collector 72. Thereby, the malfunction that the filter cloth of the dry dust collector 72 will burn out is suppressed.

ここで、熱媒体制御手段693は、炉頂ガス温度測定手段62、炉頂ガス流量測定手段63、第2熱媒体測定手段65での測定結果に基づいて、第2熱媒体流入弁672の開度を調節することで、炉頂ガスGを目的温度まで下降させる所要時間を、炉頂ガスGの温度によらずほぼ同じにする。
また、熱風炉制御手段691は、熱交換後ガス温度測定手段68で測定された、炉頂ガス熱交換器61の後流側での温度に基づいて、燃料ガスおよび燃焼空気の流量を調整して、熱風炉3内で必要な燃焼カロリーを確保する。
Here, the heat medium control means 693 opens the second heat medium inflow valve 672 based on the measurement results of the furnace top gas temperature measuring means 62, the furnace top gas flow rate measuring means 63, and the second heat medium measuring means 65. By adjusting the degree, the time required for lowering the furnace top gas G to the target temperature is made substantially the same regardless of the temperature of the furnace top gas G.
The hot stove control means 691 adjusts the flow rates of the fuel gas and the combustion air based on the temperature at the downstream side of the furnace top gas heat exchanger 61 measured by the gas temperature measuring means 68 after heat exchange. Thus, necessary calorie calories are secured in the hot stove 3.

[乾式集塵システムの効果]
このように、本実施形態では、高炉2に熱風を供給する熱風炉3からの排気ガスEを使用して、乾式集塵機72の集塵能力が落ちないように炉頂ガスGの温度を調整している。
このため、高炉2の操業中には常に運転している熱風炉3の排気ガスEを使用しているため、炉頂ガスGの温度調整が必要なときには、安定的に炉頂ガスGの昇温や冷却を行うことができる。従って、湿式集塵機が不要となり、乾式集塵機72のみを使用することができるので、TRT8による電力回収量の低下を防止できる。特に、乾式集塵システム1を新設する場合には、湿式集塵機の設置費用を削減でき、安価に新設できる。また、排熱再利用システム5を利用して炉頂ガスGの温度調整を行っているため、炉頂ガス配管721に炉頂ガス熱交換器61を設けるとともに、排熱再利用システム5で循環させている熱媒体を炉頂ガス熱交換器61に供給する経路を設けるだけでよい。さらに、熱媒体の循環により炉頂ガスGの温度調整を行うため、熱媒体を循環させるための入口配管611および出口配管612として比較的小さいサイズのものを用いることができる。よって、設備費の増加を抑制できる。
[Effect of dry dust collection system]
Thus, in this embodiment, the exhaust gas E from the hot blast furnace 3 that supplies hot blast to the blast furnace 2 is used to adjust the temperature of the furnace top gas G so that the dust collection capacity of the dry dust collector 72 does not decrease. ing.
For this reason, since the exhaust gas E of the hot stove 3 that is always in operation is used during the operation of the blast furnace 2, when the temperature adjustment of the furnace top gas G is necessary, the rise of the furnace top gas G is stably performed. Temperature and cooling can be performed. Accordingly, the wet dust collector is not required, and only the dry dust collector 72 can be used, so that it is possible to prevent the power recovery amount from being reduced by the TRT 8. In particular, when the dry dust collection system 1 is newly installed, the installation cost of the wet dust collector can be reduced and can be newly installed at low cost. In addition, since the temperature of the furnace top gas G is adjusted using the exhaust heat reuse system 5, a furnace top gas heat exchanger 61 is provided in the furnace top gas pipe 721 and is circulated in the exhaust heat reuse system 5. It is only necessary to provide a path for supplying the heated heat medium to the furnace top gas heat exchanger 61. Furthermore, since the temperature of the furnace top gas G is adjusted by circulation of the heat medium, a relatively small size can be used as the inlet pipe 611 and the outlet pipe 612 for circulating the heat medium. Therefore, an increase in equipment cost can be suppressed.

炉頂ガスGの流量を測定する炉頂ガス流量測定手段63と、入口配管611に流入させる高温媒体Hおよび低温媒体Lの温度および流量を測定する第1熱媒体測定手段64および第2熱媒体測定手段65と、入口配管611に流入させる高温媒体Hおよび低温媒体Lの流量をそれぞれ調整する第1熱媒体流入弁671および第2熱媒体流入弁672とを設けている。
このため、例えば高温媒体Hの温度に応じて炉頂ガス熱交換器61に供給する高温媒体Hの流量を調整することで、温度調整対象の炉頂ガスGの流量にあわせた必要な熱量を、炉頂ガスGに与えることができる。
A furnace top gas flow measuring means 63 for measuring the flow rate of the furnace top gas G, and a first heat medium measuring means 64 and a second heat medium for measuring the temperature and flow rate of the hot medium H and the cold medium L flowing into the inlet pipe 611. A measuring means 65 and a first heat medium inflow valve 671 and a second heat medium inflow valve 672 for adjusting the flow rates of the high temperature medium H and the low temperature medium L flowing into the inlet pipe 611 are provided.
For this reason, for example, by adjusting the flow rate of the high-temperature medium H supplied to the furnace top gas heat exchanger 61 according to the temperature of the high-temperature medium H, a necessary amount of heat corresponding to the flow rate of the furnace top gas G to be temperature-adjusted can be obtained. , Can be supplied to the top gas G.

熱交換状態切替手段66を設けて、炉頂ガスGの熱交換を行う熱交換状態と、熱交換を行わない非熱交換状態とを切り替え可能に構成している。このため、必要な場合のみ炉頂ガス熱交換器61を使用することができ、炉頂ガス熱交換器61の長寿命化を図ることができる。   The heat exchange state switching means 66 is provided so as to be switchable between a heat exchange state in which the heat exchange of the furnace top gas G and a non-heat exchange state in which no heat exchange is performed. For this reason, the top gas heat exchanger 61 can be used only when necessary, and the life of the top gas heat exchanger 61 can be extended.

熱媒体制御手段693による自動制御により熱媒体切替手段67を調整し、熱交換制御手段692による自動制御により熱交換状態切替手段66を調整しているため、瞬時にタイミングよく対応でき作業者の負荷を低減できる。   Since the heat medium switching means 67 is adjusted by the automatic control by the heat medium control means 693 and the heat exchange state switching means 66 is adjusted by the automatic control by the heat exchange control means 692, the load on the operator can be dealt with instantly and with good timing. Can be reduced.

[変形例]
なお、本発明は前記実施形態に限定されるものではなく、具体的な各部構成などは実施にあたって適宜変形することができる。
すなわち、炉頂ガス熱交換器61で炉頂ガスGに与える熱量や炉頂ガス熱交換器61で炉頂ガスGから回収する熱量にあわせて、炉頂ガス熱交換器61を2個以上設けてもよい。
また、炉頂ガス流量測定手段63、第1熱媒体測定手段64、および、第2熱媒体測定手段65を設けずに、炉頂ガス温度測定手段62での測定結果に基づいて、炉頂ガスGの温度を上げるときに第1熱媒体流入弁671と第1熱媒体流出弁673を全開にし、炉頂ガスGの温度を下げるときに第2熱媒体流入弁672と第2熱媒体流出弁674を全開にしてもよい。
また、熱交換器設置管722、熱切替弁661、バイパス弁662を設けずに、バイパス管723に炉頂ガス熱交換器61を設けてもよい。
そして、熱交換制御手段692を設けずに、作業者が熱切替弁661とバイパス弁662の開閉を行ってもよい。また、熱媒体制御手段693を設けずに、作業者が炉頂ガス温度測定手段62、炉頂ガス流量測定手段63、第1熱媒体測定手段64、第2熱媒体測定手段65での測定結果に基づいて、第1熱媒体流入弁671、第2熱媒体流入弁672、第1熱媒体流出弁673、第2熱媒体流出弁674の開閉を行ってもよい。
[Modification]
In addition, this invention is not limited to the said embodiment, A concrete each part structure etc. can be suitably changed in implementation.
That is, two or more furnace top gas heat exchangers 61 are provided in accordance with the amount of heat given to the furnace top gas G by the furnace top gas heat exchanger 61 and the amount of heat recovered from the furnace top gas G by the furnace top gas heat exchanger 61. May be.
Further, without providing the furnace top gas flow rate measuring means 63, the first heat medium measuring means 64, and the second heat medium measuring means 65, the furnace top gas is measured based on the measurement result of the furnace top gas temperature measuring means 62. When the temperature of G is raised, the first heat medium inflow valve 671 and the first heat medium outflow valve 673 are fully opened, and when the temperature of the furnace top gas G is lowered, the second heat medium inflow valve 672 and the second heat medium outflow valve 674 may be fully opened.
Further, the top gas heat exchanger 61 may be provided in the bypass pipe 723 without providing the heat exchanger installation pipe 722, the heat switching valve 661, and the bypass valve 662.
An operator may open and close the heat switching valve 661 and the bypass valve 662 without providing the heat exchange control means 692. Further, without the heat medium control means 693 being provided, the operator can obtain the measurement results of the furnace top gas temperature measuring means 62, the furnace top gas flow rate measuring means 63, the first heat medium measuring means 64, and the second heat medium measuring means 65. Based on the above, the first heat medium inflow valve 671, the second heat medium inflow valve 672, the first heat medium outflow valve 673, and the second heat medium outflow valve 674 may be opened and closed.

1…乾式集塵システム、2…高炉、3…熱風炉、4…燃料供給手段、5…排熱再利用システム、6…炉頂ガス温度調整手段、7…集塵設備、21…弁、31…煙突、32…送風機、33,34…弁、41…燃料ガス供給手段、42…燃焼空気供給手段、43,44…弁、51…排ガス熱交換器、52…燃料ガス熱交換器、53…燃焼空気熱交換器、54…熱媒体貯槽、55…膨張タンク、56…循環ポンプ、57…供給ポンプ、61…炉頂ガス熱交換器、62…炉頂ガス温度測定手段、63…炉頂ガス流量測定手段、64…第1熱媒体測定手段、65…第2熱媒体測定手段、66…熱交換状態切替手段、67…熱媒体切替手段、68…熱交換後ガス温度測定手段、69…制御装置、71…除塵器、72…乾式集塵機、201…配管、311…排ガス配管、321…配管、411…燃料ガス配管、421…燃焼空気配管、511…高温管、512…低温管、541…配管、551…配管、611…入口配管、612…出口配管、641…熱媒体温度測定手段、642…熱媒体流量測定手段、651…熱媒体温度測定手段、652…熱媒体流量測定手段、661…熱切替弁、662…バイパス弁、671…第1熱媒体流入弁、672…第2熱媒体流入弁、673…第1熱媒体流出弁、674…第2熱媒体流出弁、711…配管、721…炉頂ガス配管、722…熱交換器設置管、723…バイパス管、724…配管、E…排気ガス、G…炉頂ガス、H…高温媒体、L…低温媒体、W…熱風。   DESCRIPTION OF SYMBOLS 1 ... Dry type dust collection system, 2 ... Blast furnace, 3 ... Hot-blast furnace, 4 ... Fuel supply means, 5 ... Waste heat reuse system, 6 ... Furnace top gas temperature adjustment means, 7 ... Dust collection equipment, 21 ... Valve, 31 ... Chimney, 32 ... Blower, 33, 34 ... Valve, 41 ... Fuel gas supply means, 42 ... Combustion air supply means, 43, 44 ... Valve, 51 ... Exhaust gas heat exchanger, 52 ... Fuel gas heat exchanger, 53 ... Combustion air heat exchanger, 54 ... heat medium storage tank, 55 ... expansion tank, 56 ... circulation pump, 57 ... feed pump, 61 ... furnace top gas heat exchanger, 62 ... furnace top gas temperature measuring means, 63 ... furnace top gas Flow rate measuring means, 64 ... first heat medium measuring means, 65 ... second heat medium measuring means, 66 ... heat exchange state switching means, 67 ... heat medium switching means, 68 ... gas temperature measuring means after heat exchange, 69 ... control 71, dust remover, 72 ... dry dust collector, 201 ... piping, 311 ... Gas piping, 321 ... piping, 411 ... fuel gas piping, 421 ... combustion air piping, 511 ... high temperature pipe, 512 ... low temperature pipe, 541 ... piping, 551 ... piping, 611 ... inlet piping, 612 ... outlet piping, 641 ... heat Medium temperature measuring means, 642... Heat medium flow measuring means, 651... Heat medium temperature measuring means, 652... Heat medium flow measuring means, 661... Heat switching valve, 662 .. Bypass valve, 671. 2nd heat medium inflow valve, 673 ... 1st heat medium outflow valve, 674 ... 2nd heat medium outflow valve, 711 ... Piping, 721 ... Furnace top gas piping, 722 ... Heat exchanger installation pipe, 723 ... Bypass pipe, 724 ... pipe, E ... exhaust gas, G ... top gas, H ... high temperature medium, L ... low temperature medium, W ... hot air.

Claims (6)

高炉と、
前記高炉に熱風を供給する熱風炉と、
前記熱風炉に燃料ガスおよび燃焼空気を供給する燃料ガス供給手段および燃焼空気供給手段と、
前記熱風炉からの排気ガスを再利用する排熱再利用システムと、
前記高炉から発生する炉頂ガスの温度を調整する炉頂ガス温度調整手段と、
前記炉頂ガス中のダストを除去する乾式集塵機と、
前記乾式集塵機からの炉頂ガスにより駆動する炉頂圧回収タービンと、を少なくとも備え、
前記排熱再利用システムは、
前記熱風炉からの排ガス配管に設けられ、流入する熱媒体と排気ガスの間で熱交換を行って、加熱後の熱媒体を流出させる排ガス熱交換器と、
前記燃料ガス供給手段と前記熱風炉とを連結する燃料ガス配管および前記燃焼空気供給手段と前記熱風炉とを連結する燃焼空気配管に各々設けられ、前記排ガス熱交換器で加熱された熱媒体との間で熱交換を行って燃料ガスおよび燃焼空気を加熱し、冷却後の熱媒体を前記排ガス熱交換器へと流入させる燃料ガス熱交換器および燃焼空気熱交換器と、から構成される高炉炉頂ガスの乾式集塵システムにおいて、
前記炉頂ガス温度調整手段は、
前記高炉と前記乾式集塵機とを連結する炉頂ガス配管に設けられ、流入する熱媒体と炉頂ガスとの間で熱交換を行って、当該熱媒体を流出させる炉頂ガス熱交換器と、
前記炉頂ガス熱交換器での熱交換前の炉頂ガスの温度を測定する炉頂ガス温度測定手段と、
前記炉頂ガス熱交換器における熱媒体の流入元および熱媒体の流出先を切り替える熱媒体切替手段と、を備え、
前記熱媒体切替手段は、
前記炉頂ガス温度測定手段での測定結果に基づいて、前記排ガス熱交換器から流出する加熱後の熱媒体を前記炉頂ガス熱交換器へ流入させて、この流入させた加熱後の熱媒体との熱交換により炉頂ガスを加熱し、奪熱された熱媒体を前記排ガス熱交換器へ流出させる加熱状態と、前記燃料ガス熱交換器および前記燃焼空気熱交換器から流出する奪熱後の熱媒体を前記炉頂ガス熱交換器へ流入させて、この流入させた奪熱後の熱媒体との熱交換により炉頂ガスを冷却し、加熱された熱媒体を前記燃料ガス熱交換器および前記燃焼空気熱交換器へ流出させる冷却状態と、を切り替え可能に構成されていることを特徴とする高炉炉頂ガスの乾式集塵システム。
A blast furnace,
A hot air furnace for supplying hot air to the blast furnace;
Fuel gas supply means and combustion air supply means for supplying fuel gas and combustion air to the hot stove;
An exhaust heat reuse system for reusing exhaust gas from the hot stove;
A furnace top gas temperature adjusting means for adjusting the temperature of the furnace top gas generated from the blast furnace;
A dry dust collector for removing dust in the furnace top gas;
A furnace top pressure recovery turbine driven by furnace top gas from the dry dust collector,
The exhaust heat reuse system includes:
An exhaust gas heat exchanger that is provided in the exhaust gas piping from the hot stove, performs heat exchange between the flowing heat medium and the exhaust gas, and flows out the heated heat medium;
A fuel gas pipe connecting the fuel gas supply means and the hot stove, and a combustion air pipe connecting the combustion air supply means and the hot stove, respectively, and a heating medium heated by the exhaust gas heat exchanger; A blast furnace composed of a fuel gas heat exchanger and a combustion air heat exchanger for heating the fuel gas and the combustion air between them to heat the cooled heat medium and flowing the cooled heat medium into the exhaust gas heat exchanger In the dry dust collection system for furnace top gas,
The furnace top gas temperature adjusting means includes:
A furnace top gas heat exchanger that is provided in a furnace top gas pipe that connects the blast furnace and the dry dust collector, performs heat exchange between the inflowing heat medium and the furnace top gas, and causes the heat medium to flow out.
A furnace top gas temperature measuring means for measuring the temperature of the furnace top gas before heat exchange in the furnace top gas heat exchanger;
A heat medium switching means for switching an inflow source of the heat medium and an outflow destination of the heat medium in the furnace top gas heat exchanger,
The heat medium switching means includes
Based on the measurement result of the furnace top gas temperature measuring means, the heated heating medium flowing out from the exhaust gas heat exchanger is caused to flow into the furnace top gas heat exchanger, and the heated heating medium that has been flown in is introduced. A heating state in which the furnace top gas is heated by heat exchange with the exhaust gas, and the deprived heat medium flows out to the exhaust gas heat exchanger, and after the desorption heat that flows out from the fuel gas heat exchanger and the combustion air heat exchanger The heat medium is allowed to flow into the furnace top gas heat exchanger, and the furnace top gas is cooled by heat exchange with the heat medium after deprived heat that has flowed in, and the heated heat medium is converted into the fuel gas heat exchanger. And a dry dust collection system for blast furnace top gas, which is configured to be switchable between a cooling state to flow out to the combustion air heat exchanger.
請求項1に記載の高炉炉頂ガスの乾式集塵システムにおいて、
前記熱媒体切替手段は、
前記排ガス熱交換器から流出し前記炉頂ガス熱交換器に流入する加熱後の熱媒体の流量を調整する第1熱媒体流入弁と、
前記燃料ガス熱交換器および前記燃焼空気熱交換器から流出し前記炉頂ガス熱交換器に流入する奪熱後の熱媒体の流量を調整する第2熱媒体流入弁と、
前記炉頂ガス熱交換器から流出し前記排ガス熱交換器に流入する奪熱後の熱媒体の流量を調整する第1熱媒体流出弁と、
前記炉頂ガス熱交換器から流出し前記燃料ガス熱交換器および前記燃焼空気熱交換器に流入する加熱後の熱媒体の流量を調整する第2熱媒体流出弁と、を備え、
前記炉頂ガス温度調整手段は、
前記炉頂ガス熱交換器での熱交換前の炉頂ガスの流量を測定する炉頂ガス流量測定手段と、
前記第1熱媒体流入弁に流入する加熱後の熱媒体の温度および流量を測定する第1熱媒体測定手段と、
前記第2熱媒体流入弁に流入する冷却後の熱媒体の温度および流量を測定する第2熱媒体測定手段と、を備えることを特徴とする高炉炉頂ガスの乾式集塵システム。
In the blast furnace top gas dry dust collection system according to claim 1,
The heat medium switching means includes
A first heat medium inlet valve that adjusts the flow rate of the heated heat medium that flows out of the exhaust gas heat exchanger and flows into the furnace top gas heat exchanger;
A second heat medium inflow valve for adjusting the flow rate of the heat medium after heat removal flowing out of the fuel gas heat exchanger and the combustion air heat exchanger and flowing into the furnace top gas heat exchanger;
A first heat medium outlet valve that adjusts the flow rate of the heat medium after deprived heat that flows out of the furnace top gas heat exchanger and flows into the exhaust gas heat exchanger;
A second heat medium outlet valve that adjusts the flow rate of the heated heat medium that flows out from the furnace top gas heat exchanger and flows into the fuel gas heat exchanger and the combustion air heat exchanger,
The furnace top gas temperature adjusting means includes:
A furnace top gas flow rate measuring means for measuring a flow rate of the furnace top gas before heat exchange in the furnace top gas heat exchanger;
First heat medium measuring means for measuring the temperature and flow rate of the heated heat medium flowing into the first heat medium inflow valve;
And a second heat medium measuring means for measuring the temperature and flow rate of the cooled heat medium flowing into the second heat medium inflow valve, and a dry dust collection system for blast furnace top gas.
請求項2に記載の高炉炉頂ガスの乾式集塵システムにおいて、
前記炉頂ガス温度調整手段は、
前記炉頂ガス温度測定手段で測定された温度が予め設定された下限値未満であると判断すると、前記熱媒体切替手段を前記加熱状態に設定し、予め設定された上限値以上であると判断すると、前記熱媒体切替手段を前記冷却状態に設定する熱媒体制御手段を備え、
前記熱媒体制御手段は、
前記炉頂ガス流量測定手段、前記第1熱媒体測定手段、および、前記第2熱媒体測定手段での測定結果に基づいて、前記第1熱媒体流入弁、前記第2熱媒体流入弁、前記第1熱媒体流出弁、および、前記第2熱媒体流出弁を制御することで、前記炉頂ガス熱交換器に流入する熱媒体の流量を調整することを特徴とする高炉炉頂ガスの乾式集塵システム。
In the blast furnace top gas dry dust collection system according to claim 2,
The furnace top gas temperature adjusting means includes:
When it is determined that the temperature measured by the furnace top gas temperature measuring means is less than a preset lower limit value, the heating medium switching means is set to the heating state, and is determined to be equal to or higher than a preset upper limit value. Then, comprising a heat medium control means for setting the heat medium switching means in the cooling state,
The heat medium control means includes
Based on the measurement results of the furnace top gas flow rate measuring means, the first heat medium measuring means, and the second heat medium measuring means, the first heat medium inflow valve, the second heat medium inflow valve, Blast furnace top gas dry type, wherein the flow rate of the heat medium flowing into the furnace top gas heat exchanger is adjusted by controlling the first heat medium outflow valve and the second heat medium outflow valve. Dust collection system.
請求項1から請求項3のいずれかに記載の高炉炉頂ガスの乾式集塵システムにおいて、
前記炉頂ガス配管は、
前記炉頂ガス熱交換器が設置された熱交換器設置管と、
前記熱交換器設置管における前記炉頂ガス熱交換器よりも前記高炉側と前記炉頂ガス熱交換器よりも前記乾式集塵機側とを連結するバイパス管と、を備え、
前記炉頂ガス温度調整手段は、前記熱交換器設置管に炉頂ガスを流通させて当該炉頂ガスの熱交換を行う熱交換状態と、前記バイパス管に炉頂ガスを流通させて当該炉頂ガスの熱交換を行わない非熱交換状態と、を切り替える熱交換状態切替手段を備えることを特徴とする高炉炉頂ガスの乾式集塵システム。
In the dry dust collection system of the blast furnace top gas according to any one of claims 1 to 3,
The furnace top gas pipe is
A heat exchanger installation pipe in which the furnace top gas heat exchanger is installed;
A bypass pipe connecting the blast furnace side with respect to the furnace top gas heat exchanger in the heat exchanger installation pipe and the dry dust collector side with respect to the furnace top gas heat exchanger;
The furnace top gas temperature adjusting means includes a heat exchange state in which the furnace top gas is circulated through the heat exchanger installation pipe to exchange heat of the furnace top gas, and the furnace top gas is circulated through the bypass pipe. A dry dust collection system for blast furnace top gas, comprising heat exchange state switching means for switching between a non-heat exchange state in which heat exchange of the top gas is not performed.
請求項4に記載の高炉炉頂ガスの乾式集塵システムにおいて、
前記炉頂ガス温度調整手段は、前記炉頂ガス温度測定手段で測定された温度が予め設定された下限値未満、又は、予め設定された上限値以上であると判断すると、前記熱交換状態切替手段を前記熱交換状態に設定し、前記下限値以上且つ前記上限値未満であると判断すると、前記熱交換状態切替手段を前記非熱交換状態に設定する熱交換制御手段を備えることを特徴とする高炉炉頂ガスの乾式集塵システム。
In the blast furnace top gas dry dust collection system according to claim 4,
When the furnace top gas temperature adjusting means determines that the temperature measured by the furnace top gas temperature measuring means is less than a preset lower limit value or more than a preset upper limit value, the heat exchange state switching A heat exchange control means for setting the heat exchange state switching means to the non-heat exchange state when it is determined that the means is set to the heat exchange state and is not less than the lower limit value and less than the upper limit value. Blast furnace top gas dry type dust collection system.
高炉と、
前記高炉に熱風を供給する熱風炉と、
前記熱風炉に燃料ガスおよび燃焼空気を供給する燃料ガス供給手段および燃焼空気供給手段と、
前記熱風炉からの排気ガスを再利用する排熱再利用システムと、
前記炉頂ガス中のダストを除去する乾式集塵機と、
前記乾式集塵機からの炉頂ガスにより駆動する炉頂圧回収タービンと、を少なくとも備え、
前記排熱再利用システムは、
前記熱風炉からの排ガス配管に設けられ、流入する熱媒体と排気ガスの間で熱交換を行って、加熱後の熱媒体を流出させる排ガス熱交換器と、
前記燃料ガス供給手段と前記熱風炉とを連結する燃料ガス配管および前記燃焼空気供給手段と前記熱風炉とを連結する燃焼空気配管に各々設けられ、前記排ガス熱交換器で加熱された熱媒体との間で熱交換を行って燃料ガスおよび燃焼空気を加熱し、冷却後の熱媒体を前記排ガス熱交換器へと流入させる燃料ガス熱交換器および燃焼空気熱交換器と、から構成される高炉炉頂ガスの乾式集塵システムを利用する乾式集塵方法であって、
前記乾式集塵システムに、
前記高炉と前記乾式集塵機とを連結する炉頂ガス配管に設けられ、流入する熱媒体と炉頂ガスとの間で熱交換を行って、当該熱媒体を流出させる炉頂ガス熱交換器と、
前記炉頂ガス熱交換器での熱交換前の炉頂ガスの温度を測定する炉頂ガス温度測定手段と、
前記炉頂ガス熱交換器における熱媒体の流入元および熱媒体の流出先を切り替える熱媒体切替手段と、を設け、
前記炉頂ガス温度測定手段で測定された温度が予め設定された下限値未満であると判断すると、前記排ガス熱交換器から流出する加熱後の熱媒体を前記炉頂ガス熱交換器へ流入させて、この流入させた加熱後の熱媒体との熱交換により炉頂ガスを加熱し、奪熱された熱媒体を前記排ガス熱交換器へ流出させる加熱状態に設定し、
予め設定された上限値以上であると判断すると、前記燃料ガス熱交換器および前記燃焼空気熱交換器から流出する奪熱後の熱媒体を前記炉頂ガス熱交換器へ流入させて、この流入させた奪熱後の熱媒体との熱交換により炉頂ガスを冷却し、加熱された熱媒体を前記燃料ガス熱交換器および前記燃焼空気熱交換器へ流出させる冷却状態に設定することを特徴とする乾式集塵方法。
A blast furnace,
A hot air furnace for supplying hot air to the blast furnace;
Fuel gas supply means and combustion air supply means for supplying fuel gas and combustion air to the hot stove;
An exhaust heat reuse system for reusing exhaust gas from the hot stove;
A dry dust collector for removing dust in the furnace top gas;
A furnace top pressure recovery turbine driven by furnace top gas from the dry dust collector,
The exhaust heat reuse system includes:
An exhaust gas heat exchanger that is provided in the exhaust gas piping from the hot stove, performs heat exchange between the flowing heat medium and the exhaust gas, and flows out the heated heat medium;
A fuel gas pipe connecting the fuel gas supply means and the hot stove, and a combustion air pipe connecting the combustion air supply means and the hot stove, respectively, and a heating medium heated by the exhaust gas heat exchanger; A blast furnace composed of a fuel gas heat exchanger and a combustion air heat exchanger for heating the fuel gas and the combustion air between them to heat the cooled heat medium and flowing the cooled heat medium into the exhaust gas heat exchanger A dry dust collection method using a dry dust collection system for furnace top gas,
In the dry dust collection system,
A furnace top gas heat exchanger that is provided in a furnace top gas pipe that connects the blast furnace and the dry dust collector, performs heat exchange between the inflowing heat medium and the furnace top gas, and causes the heat medium to flow out.
A furnace top gas temperature measuring means for measuring the temperature of the furnace top gas before heat exchange in the furnace top gas heat exchanger;
A heat medium switching means for switching a heat medium inflow source and a heat medium outflow destination in the furnace top gas heat exchanger,
When it is determined that the temperature measured by the furnace top gas temperature measuring means is less than a preset lower limit value, the heated heating medium flowing out from the exhaust gas heat exchanger is caused to flow into the furnace top gas heat exchanger. Then, the furnace top gas is heated by heat exchange with the heated heating medium that has been allowed to flow, and the heat medium that has been deprived is set to a heating state that flows out to the exhaust gas heat exchanger,
When it is determined that the value is equal to or higher than a preset upper limit value, the heat medium after heat removal flowing out from the fuel gas heat exchanger and the combustion air heat exchanger is caused to flow into the furnace top gas heat exchanger. The furnace top gas is cooled by heat exchange with the deprived heat medium that has been removed, and the heated heat medium is set in a cooling state that flows out to the fuel gas heat exchanger and the combustion air heat exchanger. A dry dust collection method.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114150096A (en) * 2021-12-30 2022-03-08 刘朋川 Waste gas treatment equipment with spraying dust removal structure for smelting blast furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114150096A (en) * 2021-12-30 2022-03-08 刘朋川 Waste gas treatment equipment with spraying dust removal structure for smelting blast furnace

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