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JPS6023169B2 - How to clean the gas cooler of vacuum degassing equipment - Google Patents
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JPS6023169B2 - How to clean the gas cooler of vacuum degassing equipment - Google Patents

How to clean the gas cooler of vacuum degassing equipment

Info

Publication number
JPS6023169B2
JPS6023169B2 JP9410278A JP9410278A JPS6023169B2 JP S6023169 B2 JPS6023169 B2 JP S6023169B2 JP 9410278 A JP9410278 A JP 9410278A JP 9410278 A JP9410278 A JP 9410278A JP S6023169 B2 JPS6023169 B2 JP S6023169B2
Authority
JP
Japan
Prior art keywords
vacuum
gas
degassing
gas cooler
dust
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP9410278A
Other languages
Japanese (ja)
Other versions
JPS5521554A (en
Inventor
敬之 小谷野
正之 半明
勝 石川
稔 北村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Engineering Corp
Original Assignee
Nippon Kokan Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Kokan Ltd filed Critical Nippon Kokan Ltd
Priority to JP9410278A priority Critical patent/JPS6023169B2/en
Publication of JPS5521554A publication Critical patent/JPS5521554A/en
Publication of JPS6023169B2 publication Critical patent/JPS6023169B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/10Handling in a vacuum

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Steel In Its Molten State (AREA)

Description

【発明の詳細な説明】 本発明は、溶鋼等の脱ガスを行うための真空脱ガス装置
のガス・クーラーに堆積する凝集ダストの洗液方法に係
わる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for washing agglomerated dust deposited in a gas cooler of a vacuum degassing apparatus for degassing molten steel or the like.

従来、溶鋼等の真空脱ガス処理方法は、概ね第1図に示
される設備系統によって、以下に述べられる如く実施さ
れていた。
Conventionally, vacuum degassing treatment methods for molten steel and the like have been carried out as described below using the equipment system generally shown in FIG.

図において実線部が従来の方法の系統を示し、1は処理
される溶鋼を収容する取鍋、2は脱ガスのための真空槽
(脱ガス槽)、3は溶鋼に添加する合金の投入装置、4
はダスト・セ/fレーター、5はガス・クーラー、6は
多段式蒸気ェジェクター(図示せず)によって構成され
ている真空排気系、7は操業用真空度計、8は復圧用不
活性ガス導入管である。脱ガス処理において、真空槽2
は真空排気系6によって排気減圧され、敬鍋1中の溶鋼
は脱ガスされる。真空槽よりの排ガスは、ガス・クーラ
ー5が設けられている場合はこれを通過して、ダスト・
セパレーター4内にて蒸発金属のダストを沈降分離させ
た後、真空排気系を通過して排出される。脱ガス処理は
通常一1k9/均Gに近い真空下で行われるが、1ヒー
トの処理が終れば、真空排気系の運転を停止し、復圧用
不活性ガス導入管8を通じて冷却内に不活性ガスを導入
して大気圧で復圧することが行われている。これは、真
空排気系の運転を停止しても、尚真空槽内には10mo
n以下の低圧が保持されているために、これを大気圧力
と同等に復圧しないと次の工程に入る操作が出来ないた
めである。前記の如く従来の方法においては、真空排気
系6内に使用される蒸気ェジェクターは、高真空度を得
る必要から多段配置されており、そのために動力源とし
て使用される蒸気の容積が増加して、大気側のェジェク
ターに要求される能力が大きなものとなるので、通常は
脱ガス装置にコンデンサー(図示せず)を配設して排気
容積の縮小をはかっているが、脱ガス操業中には、溶鋼
は真空処理を受けるので、大気中では起らない金属蒸気
の蒸発が起り、特に蒸気圧の高いMn等が蒸発し、これ
らが真空排気系へ排出されると、前記コンデンサー中で
凝集し、コンデンサーの冷却水中に混入して流出するこ
とになる。
In the figure, the solid line indicates the system of the conventional method, where 1 is a ladle for storing molten steel to be processed, 2 is a vacuum tank for degassing (degassing tank), and 3 is a charging device for alloy added to molten steel. , 4
is a dust separator, 5 is a gas cooler, 6 is a vacuum exhaust system consisting of a multi-stage steam ejector (not shown), 7 is a vacuum gauge for operation, and 8 is an inert gas introduction for return pressure. It's a tube. In the degassing process, vacuum chamber 2
is evacuated and depressurized by a vacuum exhaust system 6, and the molten steel in the ladle 1 is degassed. Exhaust gas from the vacuum chamber passes through a gas cooler 5, if one is provided, and collects dust and
After the evaporated metal dust is sedimented and separated in the separator 4, it is discharged through a vacuum exhaust system. Degassing treatment is usually carried out under a vacuum close to -1k9/G, but once one heat treatment is completed, the operation of the vacuum evacuation system is stopped and inert gas is introduced into the cooling chamber through the inert gas introduction pipe 8 for repressurization. Gas is introduced and the pressure is restored to atmospheric pressure. This means that even if the operation of the vacuum evacuation system is stopped, there will still be 10 mo in the vacuum chamber.
This is because a low pressure of n or less is maintained, and the next step cannot be performed unless this pressure is restored to the same level as atmospheric pressure. As mentioned above, in the conventional method, the steam ejectors used in the vacuum evacuation system 6 are arranged in multiple stages due to the need to obtain a high degree of vacuum, which increases the volume of steam used as a power source. Since the capacity required of the ejector on the atmospheric side is large, normally a condenser (not shown) is installed in the degassing device to reduce the exhaust volume, but during degassing operation Since molten steel is subjected to vacuum treatment, evaporation of metal vapor that does not occur in the atmosphere occurs, especially Mn etc. with high vapor pressure evaporates, and when these are discharged to the vacuum evacuation system, they condense in the condenser. , it gets mixed into the cooling water of the condenser and leaks out.

この金属を含んでいることから、工業的に冷却水の水処
理の問題が生じて来る。よって、上記の金属を含む冷却
水の流出を防止する目的を以つて、真空排気系6の前に
、真空槽(脱ガス槽)2において発生するダストを凝集
分離するためのダスト・セパレーター4が配設されたも
のであるが、その集塵効率を上げるために、ダスト・セ
パレーター4内に間接冷却式のガス・クーラー5が配置
されることがある。
The presence of this metal causes problems in the industrial treatment of cooling water. Therefore, in order to prevent the cooling water containing the metals from flowing out, a dust separator 4 is installed before the vacuum exhaust system 6 to coagulate and separate the dust generated in the vacuum tank (degassing tank) 2. However, in order to improve the dust collection efficiency, an indirect cooling type gas cooler 5 may be disposed within the dust separator 4.

(この場合、冷却効果上、真空槽とダクト・セパレータ
ーを連絡するダストに面したセパレーター入口部に設け
ることが好ましい。)然して、従来の方法においては、
操業用真空度計7をダスト・セパレーターの排出側のダ
クトに配置して真空度を測定し、その測定値を脱ガス装
置の脱ガス効果を代表するものとみなして操業が行なわ
れていたものである。
(In this case, in terms of cooling effect, it is preferable to provide the separator inlet facing the dust that connects the vacuum chamber and the duct separator.) However, in the conventional method,
An operational vacuum gauge 7 was placed in the duct on the discharge side of the dust separator to measure the degree of vacuum, and the operation was carried out by assuming that the measured value was representative of the degassing effect of the degassing device. It is.

然し、本発明の発明者らは、実操業の精密な検を通じて
、脱ガス処理中に真空槽中で発生するダストが前記ガス
・クーラーに付着堆積し、次第にクーラーの抵抗を増大
し、このダスト堆積が排気経路の圧損に大きく影響して
、操業用真空度計の良好な真空度指示にもかかわらず、
脱ガスの効果を低下させており、操業用真空度計の指示
値が脱ガスの効果を代表するものでないことを見出した
。即ち、本発明の発明者らは、従来蒸発ガスの存在によ
り圧力測定が困難とされていた真空槽に試験真空度計9
(第1図の点線の部分)を取付け、従来の操業用真空度
計7との、脱ガス処理中における真空度指示値の比較を
行なった結果、従来の操業用真空度計では安定した低い
気圧を指示していても、真空槽の正確な真空度を示す試
験真空度計では測定値が大きく変動していることを見出
した。その状態は第2図に示される如きもので、従来の
操業用真空度計によれば真空度は0.3mbar前後で
一見安定しているが、真空槽の気圧を正確に示す試験真
空度計によれば、真空度は約1.5〜5.仇hbarと
広い範囲に変動しており、従来の操業用真空度計の測定
値が正しく真空槽の真空度を示すものでなく、これによ
って脱ガス効果を判定し得ないことがわかる。従来は、
操業用真空度計の指示が低い気圧に安定している限り、
真空槽内の真空度も良好なものとして、ガス・クーラー
の抵抗増大による脱ガス装置の低下に対して十分な対策
をとることが出来ていなかったと言ってよい。前記の如
く真空槽内の真空度の変動(従って脱ガス効果の変動)
が間接式ガス・クーラーに堆積するダストによる抵抗の
増大に起因することを解明し本発明の発明者らは、次に
そのダスト洗糠方法の研究に着手し、装置の内部がガス
・クーラー入側において1000qo前後という高温で
、且真空設備の密閉構造内で行なわなければならないと
いう困難な問題を解決し、従来の設備に大きな付加を行
なうことなく、ガス・クーラーを洗液する方法を発明し
た。
However, through detailed inspection of actual operations, the inventors of the present invention discovered that dust generated in the vacuum chamber during degassing treatment adheres and accumulates on the gas cooler, gradually increasing the resistance of the cooler, and causing this dust to accumulate. The accumulation greatly affects the pressure drop in the exhaust path, and despite the good vacuum indication from the operational vacuum gauge,
It was found that the degassing effect was reduced, and the reading on the operating vacuum gauge was not representative of the degassing effect. That is, the inventors of the present invention installed a test vacuum gauge 9 in a vacuum chamber, where pressure measurement was conventionally difficult due to the presence of evaporative gas.
(dotted line in Figure 1) and compared the vacuum level readings during degassing with the conventional operating vacuum gauge 7. It was discovered that even if the test vacuum gauge indicated the atmospheric pressure, the measured value fluctuated greatly, indicating the exact degree of vacuum in the vacuum chamber. The situation is as shown in Figure 2.According to conventional operational vacuum gauges, the vacuum level is seemingly stable at around 0.3 mbar, but a test vacuum gauge that accurately shows the pressure in the vacuum chamber According to the company, the degree of vacuum is approximately 1.5 to 5. It can be seen that the measured value of the conventional operational vacuum gauge does not accurately indicate the vacuum degree of the vacuum chamber, and that the degassing effect cannot be determined due to this. conventionally,
As long as the operating vacuum gauge indicates a stable low pressure,
Assuming that the degree of vacuum in the vacuum chamber was good, it can be said that sufficient measures were not taken to prevent deterioration of the degassing device due to increased resistance of the gas cooler. As mentioned above, fluctuations in the degree of vacuum in the vacuum chamber (and therefore fluctuations in the degassing effect)
The inventors of the present invention discovered that this was caused by an increase in resistance due to dust deposited on indirect gas coolers, and the inventors of the present invention then began research on a dust washing method. The company solved the difficult problem of having to clean gas coolers at high temperatures of around 1000 qo on the side and in a sealed structure of vacuum equipment, and invented a method for cleaning gas coolers without making any major additions to conventional equipment. .

本発明の方法は、ガス・クーラー入側に面した複数のガ
ス吹付用ノズルを配置し、これによって、従来ダスト・
セパレーターの排出側のダクトに設けられた導入管を通
じて脱ガス装置の復圧のために導入されていた不活性ガ
スを「ガス・クーラーに吹付けることによって、脱ガス
装置の復圧と同時にガス・クーラーに堆積したダストを
ガスにより洗練する方法である。
The method of the present invention arranges a plurality of gas blowing nozzles facing the inlet side of the gas cooler, thereby eliminating the conventional dust
By blowing the inert gas that had been introduced into the gas cooler through the inlet pipe installed in the duct on the discharge side of the separator to restore the pressure in the degasser, the gas can be restored at the same time as the pressure in the degasser is restored. This method uses gas to refine the dust that has accumulated in the cooler.

本発明の方法を実施するための装置の1例は、第3図に
示される如く構成され、図において、1は取鍋、2は真
空槽、4はダスト・セパレーター、5はガス・クーラー
、.は真空排気系、7は操業用真空度計、1川ま不活性
ガスをガス・クーラーに吹付けるための不活性ガス吹付
ノズル、11は吹付ガス配管、12は不活性ガス吹付時
に真空槽を閉じるためのシール弁である。
An example of an apparatus for carrying out the method of the present invention is constructed as shown in FIG. 3, in which 1 is a ladle, 2 is a vacuum chamber, 4 is a dust separator, 5 is a gas cooler, .. 1 is the vacuum exhaust system, 7 is the vacuum gauge for operation, 1 is the inert gas spray nozzle for spraying inert gas into the gas cooler, 11 is the spray gas piping, and 12 is the vacuum chamber when spraying the inert gas. It is a seal valve for closing.

ガス・クーラー及び不活性ガス吹付ノズルの配置関係の
詳細は第4図に示され、不活性ガス吹付ノズルの1型式
が第5図に示される。ガス・クーラーは縦型多管式のも
のが、ダストが比較的付着しもこく〈且洗瓶これ易いと
いう点から横型のものよりも好ましく、第4図において
aはガス・クーラー側面、bは背面を示し、図において
13はガス・クーラーの給排水ダクト、14は冷却管、
15は真空槽とダスト・セパレーターを連絡するダクト
で、吹付ガス配管11を分岐して複数の不活性ガス吹付
ノズルを取付けるへッダー部となるものであるが、図面
を見易くするためにaには不活性ガス吹付ノズル、bに
は吹付ガス配管のみを示してある。
The details of the arrangement of the gas cooler and the inert gas blowing nozzle are shown in FIG. 4, and one type of inert gas blowing nozzle is shown in FIG. A vertical multi-tube type gas cooler is preferable to a horizontal type because dust is relatively hard to adhere to and bottles can easily be washed away. In Figure 4, a is the side of the gas cooler, and b is The back side is shown, and in the figure, 13 is the gas cooler's supply and drainage duct, 14 is the cooling pipe,
15 is a duct that connects the vacuum chamber and the dust separator, and serves as a header part where the blowing gas piping 11 is branched and multiple inert gas blowing nozzles are attached; Only the inert gas blowing nozzle and the blowing gas piping are shown in b.

不活性ガス吹付ノズルはガス・クーラーの前面(真空槽
に面する側)に配置される。第5図においては16はノ
ズルのへツダー部、17はノズルの吹出管部を示す。不
活性ガス吹付洗練は通常1ヒートの真空脱ガス処理を終
った後、従来方法における脱ガス装置の復圧時に行なわ
れ、ガス・クーラーの冷却管のノズルから不活性ガスを
吹付けることにより、冷却管に堆積したダストはガスの
圧力によって洗総され(吹落され)、ダストの堆積によ
り増加したクーラーの抵抗が除去されると同時に脱ガス
装置の復圧が行なわれる。
The inert gas blowing nozzle is placed at the front of the gas cooler (the side facing the vacuum chamber). In FIG. 5, reference numeral 16 indicates a header portion of the nozzle, and reference numeral 17 indicates a blowout pipe portion of the nozzle. Inert gas spray refinement is usually carried out after one heat of vacuum degassing treatment and when the degasser is repressurized in the conventional method, by spraying inert gas from the nozzle of the cooling pipe of the gas cooler. The dust accumulated in the cooling pipe is washed away (blown off) by the pressure of the gas, and the resistance of the cooler increased by the accumulation of dust is removed, and at the same time, the pressure in the degasser is restored.

本発明によれば、1ヒート毎にダストの洗糠が容易に行
なわれるので、ガス・クーラーの抵抗は殆ど増加するこ
となく、常に概ね装置の新しいときの状態を保つことが
出来、脱ガスの対果も平均的に良好に保たれる。
According to the present invention, since the dust is easily washed off after each heat, the resistance of the gas cooler hardly increases, and the equipment can always be kept in the same state as when it was new. The results are also kept good on average.

不活性ガス吹付にあっては、ダストが真空排気に逃げな
いように、ダスト・セパレーターの出口のシール弁12
を閉じる。尚、不活性ガスによるガス・クーラー洗練は
、通常1ヒート終了毎に行われるが、脱ガス処理中にお
いても抵抗除去の必要があれば随時行うことが出来、こ
れによって操業用真空度計の指示値に近い安定した真空
槽の真空度を以て操業を行うことが出来る。次に本発明
の実施による抵抗除去、脱ガス効果の向上について、実
施例によって説明する。
When spraying with inert gas, a seal valve 12 at the outlet of the dust separator is installed to prevent dust from escaping into the vacuum.
Close. Note that gas cooler refinement with inert gas is normally performed after each heat, but it can be performed at any time during the degassing process if there is a need to remove resistance. It is possible to operate with a stable vacuum degree of the vacuum chamber close to the above value. Next, the improvement of resistance removal and degassing effect by carrying out the present invention will be explained with reference to examples.

従来の方法により、ガス・クーラーのダストの洗膝を行
わないで、真空脱ガス処理を数ヒート継続して行った場
合と、本発明の方法によって1ヒート毎にダスト洗糠を
行った場合の、真空槽の真空度及び脱ガス処理後の漆鋼
中の水素含有量(脱ガス効果を示す)との比較を行った
。その結果は第6図に示される。図に於てAo,A,は
夫々従来方法及び本発明の方法による真空槽の真空度を
示し、B。,B,は夫々従来方法及び本発明の方法によ
る脱ガス後の港鋼中の水素含有量(鋳型内の坪m)の下
限を示し、Co,C,は同じく上限を示す。横軸の座標
の1は新しい状態のガス・クーラーにより操業を開始し
た真空脱ガス処理の第1ヒートを示し、以下順次第2〜
第6ヒートを示す。第6図に示される如く、従釆の方法
によれば、真空槽中の真空度は、脱ガス処理の回を重ね
るに従って次第に気圧上昇の傾向を示し、又脱ガス処理
後の溶鋼中の水素含有量は上下限共(特に上限において
)回を重ねるに従って増大する。これに対して本発明の
方法により1ヒートの処理毎にガス・クーラーの洗膝を
行った場合は、真空槽の真空度は新しいガス・クーラー
使用時と殆ど変らず安定して良好であり、脱ガス処理後
の溶鋼内の水素含有量も毎ヒート殆ど変らず上昇があっ
ても極めて僅少であり、従来方法に比べて脱ガス効果の
優れていることがわかる。本発明の方法の実施により、
真空度は従来上限値で靴舷r以上を記録することがあっ
たものが、2.5hbar以下に安常的に管理可能とな
り、又脱ガス処理後の溶鋼水素含有量も従来上限値で2
.5〜3.岬叫〆上を記録していたものが1.跡岬〆下
に安定するに至った。以上述べたように、本発明のガス
・クーラー洗膝方法は、脱ガス装置の復圧用の不活性ガ
スをダスト洗終に利用する方法であるので、大きな設備
の付加を要せず、又操業のための経費も増加することな
く、脱ガス装置の真空度を安定、良好ならしめて脱ガス
効果を高く維持する極めて優れた方法である。
A case where the vacuum degassing treatment was performed continuously for several heats without washing the dust of the gas cooler by the conventional method, and a case where the dust was washed every heat by the method of the present invention. A comparison was made between the vacuum degree of the vacuum chamber and the hydrogen content in lacquered steel after degassing treatment (indicating the degassing effect). The results are shown in FIG. In the figure, Ao and A indicate the degree of vacuum of the vacuum chamber according to the conventional method and the method of the present invention, respectively, and B. , B, respectively indicate the lower limit of the hydrogen content (tsubo m in the mold) in the port steel after degassing by the conventional method and the method of the present invention, and Co, C, similarly indicate the upper limit. The coordinate 1 on the horizontal axis indicates the first heat of the vacuum degassing process that started operation with the gas cooler in a new state, and the following heats are 2 to 2 in order.
Showing the 6th heat. As shown in Figure 6, according to the conventional method, the degree of vacuum in the vacuum chamber shows a tendency for the pressure to gradually increase as the degassing process is repeated, and the hydrogen in the molten steel after the degassing process shows a tendency to gradually increase. The content increases as the number of times increases at both the upper and lower limits (especially at the upper limit). On the other hand, when the gas cooler is cleaned every heat treatment using the method of the present invention, the degree of vacuum in the vacuum chamber is stable and good, with almost no difference from when using a new gas cooler. The hydrogen content in the molten steel after degassing treatment hardly changes from heat to heat, and even if there is an increase, it is extremely small, indicating that the degassing effect is superior to that of the conventional method. By carrying out the method of the invention,
The degree of vacuum, which used to be recorded at the upper limit of more than 2.5 hbar, can now be safely managed to 2.5 hbar or less, and the hydrogen content of molten steel after degassing treatment has also been reduced to 2.
.. 5-3. The one that recorded the end of the cape was 1. It reached a stable level at Cape Atomisaki. As described above, the gas cooler knee cleaning method of the present invention is a method that uses the inert gas for restoring the pressure of the degassing device at the end of dust cleaning, so it does not require the addition of large equipment, and it This is an extremely excellent method for keeping the degree of vacuum in the degassing device stable and good and maintaining a high degassing effect without increasing the cost.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の真空脱ガス方法を図式化して示す図、第
2図は従来の操業用真空度計の指示値と試験真空度計が
示す真空槽の真空度との比較を示すグラフ、第3図は本
発明の方法を図式的に示す図、第4図aは本発明の方法
に使用されるガス・クーラーと不活性ガス吹付ノズルの
配置図(側面)、bは同じく配置図背面、第5図は不活
性ガス吹付ノズルの詳細図である。 第6図は本発明の方法によるヒート数と溶鋼水素の関係
を示すグラフ図である。1・・・取鍋、2・・・真空槽
、3・・・合金投入装置、4…ダスト・セパレーター、
5…ガス・クーラー、6・・・真空排気系、7・・・操
業用真空度計、8・・・復圧用ガス導入管、9・・・試
験真空度計、10・・・不活性ガス吹付ノズル、11・
・・吹付ガス配管、13・・・クーラー給排水ダクト、
14・・・冷却管。 第1図 第2図 第3図 第5図 第4図 第6図
Fig. 1 is a diagram schematically showing a conventional vacuum degassing method, Fig. 2 is a graph showing a comparison between the indicated value of a conventional operational vacuum gauge and the vacuum degree of the vacuum chamber indicated by a test vacuum gauge. Figure 3 is a diagram schematically showing the method of the present invention, Figure 4a is a layout diagram (side view) of the gas cooler and inert gas spray nozzle used in the method of the present invention, and b is the rear layout diagram. , FIG. 5 is a detailed view of the inert gas spray nozzle. FIG. 6 is a graph showing the relationship between the number of heats and molten steel hydrogen according to the method of the present invention. 1... Ladle, 2... Vacuum chamber, 3... Alloy charging device, 4... Dust separator,
5... Gas cooler, 6... Vacuum exhaust system, 7... Vacuum gauge for operation, 8... Gas introduction pipe for pressure recovery, 9... Test vacuum gauge, 10... Inert gas Spray nozzle, 11.
...Blow gas piping, 13...Cooler supply and drainage duct,
14...Cooling pipe. Figure 1 Figure 2 Figure 3 Figure 5 Figure 4 Figure 6

Claims (1)

【特許請求の範囲】[Claims] 1 真空槽、ダスト・セパレーター、該ダスト・セパレ
ーター内に設けられた間接冷却式ガス・クーラー、真空
排気系からなる真空脱ガス装置を用いて溶鋼等の脱ガス
処理を行うに当り、前記ガス・クーラーの真空槽排気流
入口側に対面して、複数の不活性ガス吹付ノズルを配置
し、脱ガス処理の1ヒート終了直後或いは必要に応じて
脱ガス処理中に、前記ガス・クーラーに不活性ガスを吹
付け、該ガス・クーラーに凝集堆積したダストを洗滌す
ると同時に真空脱ガス装置の復圧を行うことを特徴とす
る真空脱ガス装置のガス・クーラーの洗滌方法。
1. When degassing molten steel, etc. using a vacuum degassing device consisting of a vacuum chamber, a dust separator, an indirect cooling type gas cooler installed in the dust separator, and a vacuum exhaust system, the above-mentioned gas and A plurality of inert gas spray nozzles are arranged facing the vacuum chamber exhaust inlet side of the cooler, and inert gas is applied to the gas cooler immediately after one heat of degassing treatment or during degassing treatment as necessary. 1. A method for cleaning a gas cooler of a vacuum degassing device, which comprises blowing gas to wash away dust that has coagulated and deposited on the gas cooler, and at the same time restoring the pressure in the vacuum degassing device.
JP9410278A 1978-08-03 1978-08-03 How to clean the gas cooler of vacuum degassing equipment Expired JPS6023169B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9410278A JPS6023169B2 (en) 1978-08-03 1978-08-03 How to clean the gas cooler of vacuum degassing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9410278A JPS6023169B2 (en) 1978-08-03 1978-08-03 How to clean the gas cooler of vacuum degassing equipment

Publications (2)

Publication Number Publication Date
JPS5521554A JPS5521554A (en) 1980-02-15
JPS6023169B2 true JPS6023169B2 (en) 1985-06-06

Family

ID=14101070

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9410278A Expired JPS6023169B2 (en) 1978-08-03 1978-08-03 How to clean the gas cooler of vacuum degassing equipment

Country Status (1)

Country Link
JP (1) JPS6023169B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5766345A (en) * 1980-10-09 1982-04-22 Hitachi Ltd Inspection device for defect

Also Published As

Publication number Publication date
JPS5521554A (en) 1980-02-15

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