JPH0321605B2 - - Google Patents
Info
- Publication number
- JPH0321605B2 JPH0321605B2 JP58105627A JP10562783A JPH0321605B2 JP H0321605 B2 JPH0321605 B2 JP H0321605B2 JP 58105627 A JP58105627 A JP 58105627A JP 10562783 A JP10562783 A JP 10562783A JP H0321605 B2 JPH0321605 B2 JP H0321605B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- valve
- switching
- bell
- pressure
- 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 - Lifetime
Links
- 230000001052 transient effect Effects 0.000 claims description 8
- 239000002184 metal Substances 0.000 claims description 4
- 238000012856 packing Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 66
- 239000000428 dust Substances 0.000 description 9
- 238000007664 blowing Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000002123 temporal effect Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000012718 dry electrostatic precipitator Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/38—Removal of waste gases or dust
- C21C5/40—Offtakes or separating apparatus for converter waste gases or dust
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Control Of Fluid Pressure (AREA)
- Flow Control (AREA)
- Chimneys And Flues (AREA)
Description
【発明の詳細な説明】
本発明は、1つのガス導入口と2つのガス排出
口、作動装置を備えた遮断装置、並びに計測およ
び制御装置をそれぞれ具備したハウジングから成
ると共に、過渡的圧力変動を伴わずにガス焼却塔
からガス溜におよびその逆に転炉から出るガス流
を切換える装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention consists of a housing with one gas inlet and two gas outlets, a shutoff device with an actuating device, and a measuring and control device, and which is capable of suppressing transient pressure fluctuations. The present invention relates to a device for switching the flow of gas leaving a converter from a gas incinerator to a gas reservoir and vice versa without combustion.
転炉の運転において、吹練段階の間に、
8000kJ/Nm3またはそれ以上の熱量をもつたCO
含有ガスが発生し、このガスは適当にクリーニン
グされた後、別の利用のためにガス溜めに集めら
れる。他方、吹練段階の初期及び末期並びに吹練
停止期間においては、可燃制成分が少ないため、
又は大気中の空気を含有するため、他に利用でき
ないガスが発生し、このガスはやはりクリーニン
グされてガス焼却塔から大気中へ排出される。そ
してこれら2種類のガスに対応するため、排ガス
導管内には切換装置を設ける必要がある。 In converter operation, during the blowing stage,
CO with a calorific value of 8000kJ/ Nm3 or more
Contained gas is generated which, after suitable cleaning, is collected in a gas reservoir for further use. On the other hand, at the beginning and end of the blowing stage and during the stopping period of blowing, there are few flammable control components;
Or, because it contains atmospheric air, an otherwise unusable gas is generated, which is also cleaned and discharged from the gas incinerator to the atmosphere. In order to handle these two types of gas, it is necessary to provide a switching device within the exhaust gas conduit.
また排ガスは、転炉の操業中にその組成が全サ
イクルを通じて変化するだけではなく、その量も
また変化する。したがつてこの排ガスの量に送風
機の出力を合わせる必要も生じる。 Also, during the operation of the converter, the exhaust gas not only changes in its composition throughout the cycle, but also in its quantity. Therefore, it becomes necessary to adjust the output of the blower to the amount of exhaust gas.
排気ガスのクリーニングには、いわゆるスクラ
ツバーを使用することができるが、ガス焼却操作
の間にスクラツバーによる圧力損失が約200ミリ
バールに達する。これに対して、乾式電気集塵装
置は、ガス焼却操作の間の圧力損失がわずかに約
20ミリバールであるという利点がある。 For exhaust gas cleaning, so-called scrubbers can be used, but during gas incineration operations the pressure loss through the scrubber reaches approximately 200 mbar. Dry electrostatic precipitators, on the other hand, have a pressure drop of only approx.
It has the advantage of being 20 mbar.
ところでガス溜への供給操作に切換えることに
よつて、湿式法及び乾式法のいずれの集塵装置の
場合も、圧力損失は例えば20ミリバールである。
このために、湿式機械的集塵装置を備えたプラン
トの場合、送風機が打ちかつべき圧力差は約10%
に過ぎないが、乾式集塵装置(この集塵装置は所
要動力が実質的に少ない点では好ましい)を備え
たプラントの場合、圧力損失の変化が約100%に
達する。かくして湿式集塵装置を備えたプラント
では、乾式集塵装置を備えたプラントの場合に比
べて、ガス焼却塔からガス溜への切換えおよびそ
の逆への切換えが制御技術的に難しくないという
ことは容易に理解されるであろう。前者の場合、
集塵装置は絞りのように作用するので、切換えに
起因する過渡的圧力変動の影響は、流れの上流に
おいて、転炉上の吸引フードの領域までほとんど
達し得ない。これに反して、後者の場合は、切換
装置を本質的に注意深く設計する必要があり、吸
引フードの領域における圧力関係の乱れを排除し
ようとする場合、送風機の制御装置を一層正確に
作動させねばならない。 However, by switching to the supply operation to the gas reservoir, the pressure loss is, for example, 20 mbar in both wet and dry dust collectors.
For this reason, in plants with wet mechanical dust collectors, the pressure difference that the blower has to overcome is approximately 10%.
However, for plants equipped with dry dust collectors (which are preferred since they require substantially less power), the change in pressure drop amounts to approximately 100%. Thus, in a plant equipped with a wet dust collector, switching from a gas incinerator to a gas reservoir and vice versa is less difficult in terms of control technology than in a plant equipped with a dry dust collector. It will be easily understood. In the former case,
Since the dust collector acts like a throttle, the effects of transient pressure fluctuations due to switching can hardly reach upstream of the flow in the region of the suction hood above the converter. In the latter case, on the other hand, the switching device essentially has to be carefully designed and the control device of the blower has to be operated more precisely if disturbances in the pressure relationship in the area of the suction hood are to be eliminated. No.
ドイツ特許公告(DE−AS)第1433688号には、
酸素上吹き転炉からの未燃焼排気ガスを回収する
ための装置が開示されており、その装置において
は、排気ガスが吸出し送風機によつて吸引され、
選択的に、一部分がガス溜めに供給され、一部分
が大気中に吹出される。その際、ガス溜に通じる
導管の内部と、大気中に吹出させるための吹出し
導管の内部とには、互いに逆方向に移動するよう
に連結された切換え用のちよう形弁が設けられ、
さらに上記吹出し導管内には、ガス流の方向に離
れて1つのちよう形弁が設けられている。また上
記吹出し導管内のガス流の方向に見え遠く離れた
ちよう形弁は、制御器を介して、送風導管と、2
個のちよう形弁の間にある吹出し導管とに接続さ
れた差圧計に連結されている。この装置は、ガス
の吹出しの場合と切換えとの際に差圧計で測定し
た圧力差がゼロに維持されるように、そして、2
個の連結したちよう弁の切換えが最初はゆつくり
と、ついで次第に速く行なわれるように制御され
る。 German Patent Publication (DE-AS) No. 1433688 states:
An apparatus for recovering unburned exhaust gas from an oxygen top-blown converter is disclosed, in which the exhaust gas is sucked by a suction blower;
Optionally, a portion is fed into a gas reservoir and a portion is blown into the atmosphere. At this time, the inside of the conduit leading to the gas reservoir and the inside of the blowout conduit for blowing out into the atmosphere are provided with switching valves connected so as to move in opposite directions,
Furthermore, a chimney valve is provided in the outlet conduit spaced apart in the direction of the gas flow. Further, a flute-shaped valve visible in the direction of gas flow in the blow-off conduit and distant from the blow-off conduit is connected to the blow-off conduit through a controller.
It is connected to a differential pressure gauge connected to a discharge conduit located between the individual chimney valves. This device is designed so that the pressure difference measured by the differential pressure gauge is maintained at zero during gas blow-off and switching;
The switching of the individual connected flow valves is controlled to occur slowly at first and then progressively faster.
この公知の切換装置は比較的高価で、かつ複雑
である。その欠点はなかんずく、制御特性が劣つ
ているということである。この公知の装置は、乾
式集塵装置を備えたプラント用としては不適当で
ある。その理由は、切換過程において必らず過渡
的圧力の変動が生じること、そしてさらに、操作
条件下でのガス圧力とガス流量とが十分に制御で
きないことである。 This known switching device is relatively expensive and complex. Their disadvantages are, among other things, poor control characteristics. This known device is unsuitable for use in plants with dry dust collectors. The reason for this is that transient pressure fluctuations necessarily occur during the switching process and, furthermore, that the gas pressure and gas flow rate under operating conditions cannot be well controlled.
したがつて、冒頭に述べた種類の装置であつ
て、前記の諸欠点がなく、その上、乾式集塵装置
を備えたプラントにおいても過渡的圧力変動を伴
なわずに切換えが可能である装置を作製すること
が課題である。この装置は可能な限り簡単かつ安
価で、適当な制御特性を有し、それぞれガス焼却
塔及びガス溜めへ通じるガス導管の完全な密封遮
断を交互に確実に行なうものでなければならな
い。 Therefore, there is a need for a device of the type mentioned at the outset, which does not have the above-mentioned disadvantages and which, moreover, can be switched without transient pressure fluctuations even in plants equipped with dry dust collectors. The challenge is to create one. This device should be as simple and inexpensive as possible and should have suitable control characteristics to ensure alternately complete and sealed shut-off of the gas lines leading to the gas incinerator and the gas reservoir, respectively.
この課題は、本発明に従つて、上記ガス焼却塔
と、上記ガス溜とにそれぞれ連なる2つの排出口
が、互いに独立に働く作動装置を備えると共に、
特性が互いにほぼ同一なベル形弁を遮断装置とし
てそれぞれ具備している前述した種類の装置によ
つて解決される。 This problem is solved according to the present invention, in which two exhaust ports connected to the gas incineration tower and the gas reservoir are provided with operating devices that operate independently of each other, and
The solution is provided by devices of the type described above, each of which is equipped as a shut-off device with a bell-shaped valve whose characteristics are essentially identical to each other.
上記ベル形弁はほぼ同じ大きさの流れ断面を有
するのが好ましい。またベル形弁は、金属と金属
パツキンとから成りかつ上記ガス溜の圧力の少な
くとも3倍の閉鎖圧に、堪えることが好ましい。 Preferably, the bell-shaped valves have flow cross-sections of approximately the same size. Preferably, the bell valve is made of metal and metal packing and can withstand a closing pressure of at least three times the pressure of the gas reservoir.
ところで本発明の装置は、切換え操作を同時に
調整して2つの排出導管を交互に確実に閉塞する
たつた2つの制御要素が必要であるという利点を
有する。 However, the device according to the invention has the advantage that only two control elements are required, which simultaneously adjust the switching operation and reliably block the two discharge conduits alternately.
すなわち転炉のガス流は互いに同一の特性を持
つベル形弁の形状のお蔭で、圧力変動を伴うこと
なく前記2場合について切換えられる。また上記
ベル形弁に属する互いに独立な作動装置のお蔭
で、ガス溜導管内の静圧と並んで、必要とされる
動圧の増加の制御も保証される。なおこれは、上
記切換操作中に転炉上の吸引フードからガスが溢
出するのを回避するための前提である。 In other words, the gas flow of the converter can be switched between the two cases without pressure fluctuations, thanks to the shape of the bell valve, which has mutually identical properties. Thanks to the mutually independent actuating devices belonging to the bell valve, control of the required dynamic pressure increase as well as the static pressure in the gas reservoir conduit is also ensured. Note that this is a premise for avoiding overflow of gas from the suction hood on the converter during the above switching operation.
図面に示した具体例に基づいて本発明の装置の
詳細及び利点を述べる。 The details and advantages of the device according to the invention will be described based on the specific example shown in the drawings.
第1図において、ハウジングが10で示されて
いて、ガス導管4がこのハウジングに開口し、ま
た、このハウジングから2本のガス導管7及び8
が延びている。転炉からのガスは送風機3によつ
てハウジング10に供給され、ベル形弁1及び2
の開度に応じて、導管7を経てガス溜めへ、又
は、導管8を経てガス焼却塔9へさらに送られ
る。ベル形弁1及び2の作動装置はそれぞれ5及
び6で示されている。 In FIG. 1, a housing is indicated at 10, into which a gas conduit 4 opens, and from which two gas conduits 7 and 8 are opened.
is extending. Gas from the converter is supplied to the housing 10 by a blower 3 and bell valves 1 and 2
Depending on the degree of opening, it is further sent via conduit 7 to a gas reservoir or via conduit 8 to gas incineration tower 9. The actuating devices for bell valves 1 and 2 are designated 5 and 6, respectively.
第1A図に示された弁開度においては、導管8
へ通じる、従つてガス焼却塔へ通じるガス排出口
は全開されており、一方、弁1を経て導管7へ通
じるガス排出口は閉鎖されている。このような弁
開度は第3図における段階1に対応する。 At the valve opening shown in FIG. 1A, the conduit 8
The gas outlet leading to and thus to the gas incineration tower is fully open, while the gas outlet leading via valve 1 to conduit 7 is closed. Such a valve opening corresponds to stage 1 in FIG.
第1B図には切換過程の開始が示されていて、
弁1はまだ全閉されており、弁2は幾分閉じられ
ている。第1C図においては、弁2はさらに閉じ
られており、弁1は既に幾分開かれている。これ
ら第1B図及び第1C図はいずれも第3図に示し
た切換段階2の間におけるある瞬間的な状態を示
すものである。 FIG. 1B shows the beginning of the switching process,
Valve 1 is still fully closed and valve 2 is somewhat closed. In FIG. 1C, valve 2 is further closed and valve 1 is already somewhat open. Both FIGS. 1B and 1C show certain instantaneous conditions during switching phase 2 shown in FIG.
第1D図において、弁2は全閉されており、一
方、今度は弁1が全開されている。この結果、導
管8へ通じる、従つてガス焼却塔9へ通じるガス
排出口は閉鎖され、一方、導管7へ通じる、従つ
てガス溜めへ通じるガス排出口は全開されてい
る。それぞれベル形弁1及び2のための作動装置
5及び6は互いに独立に作動するので、過渡的圧
力変動を全く生じることなく切換装置の2つの作
動状態の間での移行が可能となる。 In FIG. 1D, valve 2 is fully closed, while valve 1 is now fully opened. As a result, the gas outlet leading to conduit 8 and thus to gas incineration tower 9 is closed, while the gas outlet leading to conduit 7 and thus to the gas reservoir is fully open. The actuating devices 5 and 6 for the bell valves 1 and 2 respectively operate independently of each other, so that a transition between the two operating states of the switching device is possible without any transient pressure fluctuations.
2個のベル形弁1及び2は、第2A図に拡大図
で示されているように、特殊な外形を有する。第
2B図にはその制御特性が示されていて、特性値
kvが弁開度に対してプロツトされている。2個
のベル形弁の制御特性がほぼ同一で、かつこれら
の弁が互いに独立に作動するため、予期されるす
べての作動条件下において、上記2場合間の満足
できる切換えが可能となる。 The two bell-shaped valves 1 and 2 have a special external shape, as shown in an enlarged view in FIG. 2A. Figure 2B shows its control characteristics, and the characteristic value
kv is plotted against valve opening. Since the control characteristics of the two bell-shaped valves are substantially identical and they operate independently of each other, satisfactory switching between the two cases is possible under all expected operating conditions.
第3図には、切換過程が時間(段階)の関数と
して示されている。第3B図には、曲線V1及び
V2によつて、ガス焼却操作(段階1)の間、切
換え(段階2)の間及びガス溜めへの供給操作
(段階3)の間におけるベル形弁1及び2の弁開
度が示されている。なおこの場合の圧力関係は第
3A図に示されている。 FIG. 3 shows the switching process as a function of time (steps). FIG. 3B shows curves V 1 and
V 2 designates the valve opening of the bell valves 1 and 2 during the gas incineration operation (stage 1), during the switching (stage 2) and during the supply operation to the gas reservoir (stage 3). ing. Note that the pressure relationship in this case is shown in FIG. 3A.
第1A図、第3A図および第3B図に示す段階
1の状態において、ベル形弁1の手前側の圧力は
第3A図に示すごとく周囲圧力よりも例えば2ミ
リバール高くなつている。また上記ガス溜への供
給操作の間、すなわち第1D図、第3A図および
第3B図に示す段階3の状態では、例えば40ミリ
バールガス溜圧力より例えば5ミリバール高くな
つている。 In the state of stage 1 shown in FIGS. 1A, 3A and 3B, the pressure in front of the bell valve 1 is, for example, 2 mbar higher than the ambient pressure, as shown in FIG. 3A. Also, during the supply operation to the gas reservoir, ie in the state of stage 3 shown in FIGS. 1D, 3A and 3B, the reservoir pressure is, for example, 5 mbar higher than, for example, 40 mbar.
次にその間の第3A図および第3B図に示す段
階2においては、弁1に掛る圧力が上記所定値に
達するような位置まで弁2が閉じると、弁1が開
き始めて上記ガス溜への供給が始まる。そのあと
は第3B図に示すように、弁1が一定の速さで開
き、弁2は引き続いて全閉の方向に移動する。そ
して弁2は、弁1が全開位置に達すると完全に閉
鎖する。なおガス焼却操作への切換えの際は、ま
ず弁1が全閉位置まで移動し、全閉すると同時に
弁2が開く。 Then, in the intervening stage 2 shown in FIGS. 3A and 3B, when the valve 2 closes to a position where the pressure applied to the valve 1 reaches the predetermined value, the valve 1 begins to open and the supply to the gas reservoir is interrupted. begins. Thereafter, as shown in FIG. 3B, valve 1 opens at a constant speed, and valve 2 continues to move in the fully closed direction. Valve 2 then closes completely when valve 1 reaches its fully open position. Note that when switching to the gas incineration operation, first the valve 1 moves to the fully closed position, and at the same time as the valve 1 is fully closed, the valve 2 opens.
本発明の装置を用いることによつて、転炉から
のガス流のガス焼却操作からガス溜め供給操作へ
の切換え及びその逆方向への切換えを、過渡的圧
力変動を伴なうことなく、迅速かつ確実に行なう
ことができる。この装置は比較的構造が簡単であ
り、制御機能と密封機能とを同時に果たす。 By using the device of the present invention, the gas flow from the converter can be quickly switched from gas incineration operation to gas reservoir supply operation and vice versa without any transient pressure fluctuations. And it can be done reliably. This device is relatively simple in construction and performs control and sealing functions at the same time.
本発明を要約して述べると、転炉からの排気ガ
ス流を、過渡的圧力変動を伴なうことなく、ガス
焼却操作からガス溜め供給操作へ及びその逆方向
へ切換えるための装置が提案され、この装置は
又、乾式集塵装置を備えたプラントに特に適して
いる。 To summarize the invention, an apparatus is proposed for switching the exhaust gas flow from a converter from a gas incineration operation to a gas reservoir supply operation and vice versa without transient pressure fluctuations. , this device is also particularly suitable for plants equipped with dry dust collectors.
この装置は、1つのガス導入口と2つのガス排
出口とを備えたハウジングを有し、この2つのガ
ス排出口には、互いに独立に作動する作動装置を
備えかつ特性が互いにほぼ同一なベル形弁がそれ
ぞれ設けられている。 The device has a housing with a gas inlet and two gas outlets, each of which is equipped with an actuator that operates independently of the other and has substantially identical characteristics. A shaped valve is provided for each.
第1A図〜第1D図は、異なる作動状態にある
2個のベル形弁の開度を示す概略図、第2A図は
ベル形弁の構造を示す簡略図、第2B図は前記ベ
ル形弁の特性曲線、第3A図は、切換過程の間に
おける圧力関係の時間的変化、及び第3B図はベ
ル形弁開度の時間的変化を示す図である。
なお、図面に用いられた符号において、1,2
……ベル形弁(遮断装置)、3……送風機、4…
…ガス導管(ガス導入口)、5,6……作動装置、
7,8……ガス導管(ガス排出口)、9……ガス
焼却塔、10……ハウジングである。
Figures 1A to 1D are schematic diagrams showing the opening degrees of two bell-shaped valves in different operating states, Figure 2A is a simplified diagram showing the structure of the bell-shaped valve, and Figure 2B is the bell-shaped valve. FIG. 3A shows the temporal variation of the pressure relationship during the switching process, and FIG. 3B shows the temporal variation of the bell valve opening. In addition, in the symbols used in the drawings, 1, 2
...Bell-shaped valve (shutoff device), 3...Blower, 4...
...Gas conduit (gas inlet), 5, 6... Actuation device,
7, 8...Gas conduit (gas discharge port), 9...Gas incineration tower, 10...Housing.
Claims (1)
装置を備えた遮断装置、並びに計測および制御装
置をそれぞれ具備したハウジングから成ると共
に、過渡的圧力変動を伴わずにガス焼却塔からガ
ス溜におよびその逆に転炉から出るガス流を切換
える装置において、 互いに独立に働く作動装置を備えかつ特性が互
いにほぼ同一なベル形弁を上記2つのガス排出口
の遮断装置としてそれぞれ具備したガス流を切換
える装置。 2 2つの上記ベル形弁はほぼ同じ大きさの流れ
断面を形成する請求項1記載のガス流を切換える
装置。 3 上記ベル形弁は金属と金属パツキンとから成
りかつ上記ガス溜の圧力の少なくとも3倍の閉鎖
圧を有する請求項1又は2記載のガス流を切換え
る装置。[Scope of Claims] 1. Consists of a housing each equipped with one gas inlet and two gas outlets, a shutoff device with an actuating device, and a measuring and control device, and which allows the gas to flow without transient pressure fluctuations. In a device for switching the flow of gas exiting a converter from an incinerator to a gas reservoir and vice versa, bell-shaped valves having actuators that work independently of each other and having substantially the same characteristics as each other are used as shutoff devices for the two gas outlets. A device that switches the gas flow that each device has. 2. The device for switching gas flow according to claim 1, wherein the two bell-shaped valves form flow cross-sections of approximately the same size. 3. A device for switching gas flow according to claim 1 or 2, wherein said bell valve is made of metal and a metal packing and has a closing pressure of at least three times the pressure of said gas reservoir.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE3222599.7 | 1982-06-16 | ||
| DE19823222599 DE3222599A1 (en) | 1982-06-16 | 1982-06-16 | SWITCHING DEVICE FOR ONE CONVERTER GAS FLOW |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS596312A JPS596312A (en) | 1984-01-13 |
| JPH0321605B2 true JPH0321605B2 (en) | 1991-03-25 |
Family
ID=6166187
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58105627A Granted JPS596312A (en) | 1982-06-16 | 1983-06-13 | Device for switching gas flow from converter |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP0096909B1 (en) |
| JP (1) | JPS596312A (en) |
| DE (2) | DE3222599A1 (en) |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE481132C (en) * | 1929-08-14 | Karl Wolinski | Hydraulically operated valve reversing device for regeneratively heated ovens | |
| GB263165A (en) * | 1925-12-16 | 1927-06-09 | Silica En Ovenbouw Mij Nv | Improvements in distributing valves for regenerative ovens or furnaces heated by gas |
| GB1002585A (en) * | 1961-04-10 | 1965-08-25 | Yawata Iron & Steel Co | Apparatus for selective recovery of waste gas from oxygen top blowing converter |
| FR2458592A1 (en) * | 1979-06-07 | 1981-01-02 | Creusot Loire | STEERING ASSEMBLY FOR THE RECOVERY OF GASES FROM STEEL CONVERTERS |
| DE3043643C2 (en) * | 1980-11-19 | 1983-09-01 | Gottfried Bischoff Bau kompl. Gasreinigungs- und Wasserrückkühlanlagen GmbH & Co KG, 4300 Essen | Plant for converter gas storage |
-
1982
- 1982-06-16 DE DE19823222599 patent/DE3222599A1/en not_active Withdrawn
-
1983
- 1983-05-13 EP EP83200680A patent/EP0096909B1/en not_active Expired
- 1983-05-13 DE DE8383200680T patent/DE3362261D1/en not_active Expired
- 1983-06-13 JP JP58105627A patent/JPS596312A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| EP0096909B1 (en) | 1986-02-26 |
| JPS596312A (en) | 1984-01-13 |
| EP0096909A1 (en) | 1983-12-28 |
| DE3222599A1 (en) | 1983-12-22 |
| DE3362261D1 (en) | 1986-04-03 |
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