JPS62280320A - Exhaust gas pressure control device for refining furnace - Google Patents
Exhaust gas pressure control device for refining furnaceInfo
- Publication number
- JPS62280320A JPS62280320A JP12378086A JP12378086A JPS62280320A JP S62280320 A JPS62280320 A JP S62280320A JP 12378086 A JP12378086 A JP 12378086A JP 12378086 A JP12378086 A JP 12378086A JP S62280320 A JPS62280320 A JP S62280320A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- pressure
- furnace
- flow rate
- control device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Manufacture Of Iron (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Abstract
Description
【発明の詳細な説明】
3、発明の詳細な説明
[a業上の利用分野]
この発明は精錬炉の排ガス圧力制御装置、特にその排ガ
ス圧力の高圧化及びその圧力制御の自動化に関するもの
である。[Detailed Description of the Invention] 3. Detailed Description of the Invention [Field of Application in Industry A] This invention relates to an exhaust gas pressure control device for a refining furnace, particularly to increasing the exhaust gas pressure and automating the pressure control. .
[従来の技術]
ガスの圧力が低いので、この排ガスを利用する場合は、
この排ガスを高圧にする排ガス処理装置が必要であフた
。そして、炉口から排出される排ガスは高温であるため
、通常の排ガス処理装置では高圧化か困難であり、この
ため、特別な排ガス処理装置を必要としていた。即ち、
排ガスを一旦冷却した後昇圧し、次工程が流動予熱装置
等のように加熱を必要とする場合には、部分燃焼により
、ガス温度を上昇させる必要があった。[Conventional technology] Since the gas pressure is low, when using this exhaust gas,
An exhaust gas treatment device was required to pressurize this exhaust gas. Since the exhaust gas discharged from the furnace mouth is at a high temperature, it is difficult to increase the pressure using a normal exhaust gas treatment device, and therefore a special exhaust gas treatment device is required. That is,
If the exhaust gas is once cooled and then pressurized, and the next step requires heating, such as in a fluidized preheater, it is necessary to raise the gas temperature by partial combustion.
[発明が解決しようとする問題点]
上記のような従来の排ガス処理装置では、装置か複雑に
なり、無駄な操作が多くなり、熱エネルギーか無駄にな
っているという問題点があった。[Problems to be Solved by the Invention] The conventional exhaust gas treatment device as described above has problems in that the device is complicated, there are many unnecessary operations, and thermal energy is wasted.
この発明は、かかる問題点を解決するためになされたも
ので、排ガスの保有する熱エネルギーを無駄にすること
なく、簡単な装置て排ガスを高圧化できる精錬炉の排ガ
ス圧力ホIJ御装置を得ることを目的とする。This invention was made to solve this problem, and provides an exhaust gas pressure IJ control device for a refining furnace that can increase the pressure of exhaust gas with a simple device without wasting the thermal energy possessed by the exhaust gas. The purpose is to
[問題点を解決するための手段]
この発明に係る精錬炉の排ガス圧力制御装置は、精錬炉
から炉外の排ガス利用設備に排ガスを供給する密閉構造
の煙道と、該徘ガス利用設備の徘ガス出口に設けられた
流量調節装置と、該流量調節装置を駆動する駆動装置と
、該精錬炉の出湯口に取り付けられた圧力検出装置と、
該圧力検出装置の出力によって該駆動装置の駆動量、す
なわち、該流量調節装置の絞り蚤を制御して排ガス圧力
を一定にする制御装置とからなるものである。[Means for Solving the Problems] The exhaust gas pressure control device for a refining furnace according to the present invention includes a flue of a closed structure that supplies exhaust gas from the refining furnace to exhaust gas utilization equipment outside the furnace, and a flue of the stray gas utilization equipment. A flow rate adjustment device provided at the wandering gas outlet, a drive device for driving the flow rate adjustment device, and a pressure detection device attached to the outlet of the refining furnace.
It is comprised of a control device that controls the amount of drive of the drive device, that is, the throttle flap of the flow rate adjustment device, based on the output of the pressure detection device to keep the exhaust gas pressure constant.
[作用]
この発明においては、圧力検出装置か精錬炉の圧力を検
出し、この検出された結果が制御装置に出力され、この
制御装置は駆動装置の駆動量、すなわち、流量調節装置
の絞り量を調節し、排ガス利用設備の排ガス圧力を自動
的に一定値に制御する。[Operation] In this invention, the pressure of the refining furnace is detected by the pressure detection device, and the detected result is output to the control device, and this control device controls the amount of drive of the drive device, that is, the amount of throttling of the flow rate adjustment device. and automatically control the exhaust gas pressure of the exhaust gas utilization equipment to a constant value.
[実施例]
第1図はこの発明の一実施例を示す説明図であり、図に
おいて、(1)は溶融還元炉、(2)は溶融還元炉(1
)の側部に設けられた出湯口、(3)は溶融還元炉(1
)の外に設けられた流動予熱装置(排ガス利用設備)、
(4)は溶融還元炉(1)から流動予熱装置(3)に排
ガスを供給する密閉構造の煙道、(5)は流動予熱装置
(3)の出口に設けられた流量調節装置、(6)は流量
調節装置(5)を駆動する駆動装置、(7)は圧力検出
装置、(8)は出湯口(2)に挿入された圧力センサー
、(9)は圧力検出装置(7)の出力装置、(10)は
出力装置(9)の出力によって駆動装置(6)の駆動量
、すなわち、流量調節装置(5)の絞り量を調節する制
御装置である。[Example] Fig. 1 is an explanatory diagram showing an example of the present invention. In the figure, (1) shows a melting reduction furnace, and (2) shows a melting reduction furnace (1
), (3) is the melting reduction furnace (1).
) installed outside the fluid preheating device (exhaust gas utilization equipment),
(4) is a flue with a closed structure that supplies exhaust gas from the melting reduction furnace (1) to the fluidized preheating device (3), (5) is a flow rate adjustment device provided at the outlet of the fluidized preheating device (3), and (6) ) is the drive device that drives the flow rate adjustment device (5), (7) is the pressure detection device, (8) is the pressure sensor inserted in the outlet (2), and (9) is the output of the pressure detection device (7). The device (10) is a control device that adjusts the drive amount of the drive device (6), that is, the throttle amount of the flow rate adjustment device (5), based on the output of the output device (9).
上記のように構成された精錬炉の排ガス圧力制御装面に
おいては、圧力検出装置(7)の圧力センサー(8)か
溶融還元炉(1)の圧力を検出し、この検出された結果
か出力装置(9)によって制御装置(10)に出力され
、制御筒装置(10)は駆動装置(6)の駆動量、すな
わち、流量調節装置(5)の絞り二を調節し、その結果
、流動予熱装置(3)の排ガス圧力か自動的に一定値に
制御されることになる。In the exhaust gas pressure control system of the refining furnace configured as described above, the pressure sensor (8) of the pressure detection device (7) or the pressure of the smelting reduction furnace (1) is detected, and the detected result is output. The device (9) outputs an output to the control device (10), and the control tube device (10) adjusts the drive amount of the drive device (6), that is, the throttle of the flow rate adjustment device (5), and as a result, the flow preheating The exhaust gas pressure of the device (3) is automatically controlled to a constant value.
この実施例によれは、炉内圧1〜5 Kg/cm2を達
成し1.二の排ガス圧力の上昇により、次工程すなゎち
流動予熱装置での還元反応か促進され9排ガス利用が容
易となり、排ガス量の減少も含め、設備がコンパクトに
なった。According to this example, a furnace internal pressure of 1 to 5 Kg/cm2 was achieved. The increase in exhaust gas pressure promotes the next process, that is, the reduction reaction in the fluidized preheater, making it easier to use the exhaust gas, reducing the amount of exhaust gas, and making the equipment more compact.
ところで上記説明では、この発明を溶融還元炉に利用す
る場合について述べたが、その他の精錬炉にい利用でき
ることはいうまでもない。Incidentally, in the above explanation, the case where the present invention is applied to a smelting reduction furnace has been described, but it goes without saying that it can be applied to other refining furnaces.
[発明の効果コ
この発明は以上説明したとおり、圧力検出装置が精錬炉
の圧力を検出し、この検出された結果が制御装置に出力
され、この制御装置は駆動装置の駆動量、すなわち、流
ユ調節装置の絞り量を調節し、排ガス利用設備の排ガス
圧力を自動的に一定値に制御するようにしたので、排ガ
ス利用が容易となり、排ガス量の減少も含め、設備かコ
ンパクトになるという効果がある。[Effects of the Invention] As explained above, in this invention, the pressure detection device detects the pressure in the refining furnace, the detected result is output to the control device, and this control device determines the drive amount of the drive device, that is, the flow rate. The exhaust gas pressure in the exhaust gas usage equipment is automatically controlled to a constant value by adjusting the throttle amount of the exhaust gas adjustment device, making it easier to use the exhaust gas, reducing the amount of exhaust gas, and making the equipment more compact. There is.
纂1図はこの発明の一実施例を示す説明図である。 FIG. 1 is an explanatory diagram showing an embodiment of the present invention.
Claims (1)
閉構造の煙道と、該排ガス利用設備の排ガス出口に設け
られた流量調節装置と、該流量調節装置を駆動する駆動
装置と、該精錬炉の出湯口に取り付けられた圧力検出装
置と、該圧力検出装置の出力によって該駆動装置の駆動
量、すなわち、該流量調節装置の絞り量を制御して排ガ
ス圧力を一定にする制御装置とからなる精錬炉の排ガス
圧力制御装置。A flue with a closed structure that supplies exhaust gas from the refining furnace to exhaust gas utilization equipment outside the furnace, a flow rate adjustment device provided at the exhaust gas outlet of the exhaust gas utilization equipment, a drive device that drives the flow rate adjustment device, and the smelting process. A pressure detection device attached to the outlet of the furnace, and a control device that controls the drive amount of the drive device, that is, the throttling amount of the flow rate adjustment device, using the output of the pressure detection device to keep the exhaust gas pressure constant. Exhaust gas pressure control device for smelting furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12378086A JPS62280320A (en) | 1986-05-30 | 1986-05-30 | Exhaust gas pressure control device for refining furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12378086A JPS62280320A (en) | 1986-05-30 | 1986-05-30 | Exhaust gas pressure control device for refining furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS62280320A true JPS62280320A (en) | 1987-12-05 |
Family
ID=14869103
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12378086A Pending JPS62280320A (en) | 1986-05-30 | 1986-05-30 | Exhaust gas pressure control device for refining furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62280320A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01220710A (en) * | 1988-01-29 | 1989-09-04 | Uk Atomic Energy Authority | Fluid device |
| JPH03173711A (en) * | 1989-12-04 | 1991-07-29 | Nkk Corp | Method for adjusting gas flow for preliminary reduction in smelting reduction equipment equipped with preliminary reduction furnace |
| JPH06279823A (en) * | 1992-07-21 | 1994-10-04 | Mas Fab Koeppern Gmbh & Co Kg | Steel making method |
| JPH0711317A (en) * | 1991-11-20 | 1995-01-13 | Kawasaki Heavy Ind Ltd | Smelting reduction device |
| CN106756182A (en) * | 2016-12-20 | 2017-05-31 | 江苏豪然喷射成形合金有限公司 | A kind of alloy refining device |
-
1986
- 1986-05-30 JP JP12378086A patent/JPS62280320A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01220710A (en) * | 1988-01-29 | 1989-09-04 | Uk Atomic Energy Authority | Fluid device |
| JPH03173711A (en) * | 1989-12-04 | 1991-07-29 | Nkk Corp | Method for adjusting gas flow for preliminary reduction in smelting reduction equipment equipped with preliminary reduction furnace |
| JPH0711317A (en) * | 1991-11-20 | 1995-01-13 | Kawasaki Heavy Ind Ltd | Smelting reduction device |
| JPH06279823A (en) * | 1992-07-21 | 1994-10-04 | Mas Fab Koeppern Gmbh & Co Kg | Steel making method |
| CN106756182A (en) * | 2016-12-20 | 2017-05-31 | 江苏豪然喷射成形合金有限公司 | A kind of alloy refining device |
| CN106756182B (en) * | 2016-12-20 | 2018-06-29 | 江苏豪然喷射成形合金有限公司 | A kind of alloy refining device |
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