JPH0465910B2 - - Google Patents
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- Publication number
- JPH0465910B2 JPH0465910B2 JP19359487A JP19359487A JPH0465910B2 JP H0465910 B2 JPH0465910 B2 JP H0465910B2 JP 19359487 A JP19359487 A JP 19359487A JP 19359487 A JP19359487 A JP 19359487A JP H0465910 B2 JPH0465910 B2 JP H0465910B2
- Authority
- JP
- Japan
- Prior art keywords
- acid
- pickling
- acid solution
- tank
- tanks
- 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
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- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、種類が異なる2種以上の酸液を使用
して鋼帯、線材等を酸洗処理する際、酸液の切換
え並びに酸洗槽及び配管系の洗浄を容易に行うこ
とができる連続酸洗ラインの酸液切換えシステム
に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a method for changing acid solutions and pickling when pickling steel strips, wire rods, etc. using two or more different types of acid solutions. This invention relates to an acid solution switching system for a continuous pickling line that allows easy cleaning of tanks and piping systems.
熱間圧延によつて製造された鋼帯等の鋼材の表
面には、酸化スケールが厚い被膜となつて存在す
る。この熱延鋼材を、冷間圧延等の後続工程にお
いて処理するためには、その表面にある酸化スケ
ールを取り除くことが必要とされる。
Oxidized scale exists in the form of a thick film on the surface of steel materials such as steel strips manufactured by hot rolling. In order to process this hot-rolled steel material in subsequent steps such as cold rolling, it is necessary to remove the oxide scale on its surface.
このスケール除去の代表的な方法としては、鋼
材を塩酸、硫酸等の酸液中に浸漬する酸洗が採用
されている。ここで使用される酸液は、鋼材の材
質によつて使用する酸液の種類及び/又は濃度を
変えたり、酸洗の進行過程に応じて酸液の種類を
変更するような場合もある。 A typical method for removing scale is pickling, in which the steel material is immersed in an acid solution such as hydrochloric acid or sulfuric acid. The type and/or concentration of the acid solution used here may be changed depending on the material of the steel material, or the type of acid solution may be changed depending on the progress of pickling.
このような各種の酸洗作業を行うため、酸洗槽
1槽に対して酸液貯留タンクを1基以上用意し、
酸洗槽への酸液供給は目的とする材質に適合した
種類及び濃度のものを酸液貯留タンクからポンプ
によつて送り込むことにより行われる。また、異
なる酸液を使用して酸洗を実施する場合、以上の
ような1ラインによる酸液の切換え操業を行わず
に、普通鋼用、ステンレス鋼用等の鋼種に合わせ
て設けた専用ラインを使用した酸洗処理が行われ
ている。たとえば、特開昭59−83784号公報では、
複数種類の酸液貯留タンクから任意の酸液を酸洗
ラインの酸洗槽に装入することができる多目的連
続酸洗装置が提案されている。 In order to carry out various types of pickling work, one or more acid solution storage tanks are prepared for each pickling tank.
The acid solution is supplied to the pickling tank by pumping the acid solution of the type and concentration suitable for the target material from the acid solution storage tank. In addition, when pickling is performed using different acid solutions, instead of switching the acid solution in one line as described above, a dedicated line is set up according to the steel type, such as for ordinary steel or stainless steel. A pickling treatment using For example, in Japanese Patent Application Laid-open No. 59-83784,
A multipurpose continuous pickling device has been proposed that can charge any acid solution from a plurality of types of acid solution storage tanks into a pickling tank of a pickling line.
ところが、従来の酸液の供給及び排出系統にお
いては、酸液の流れが酸洗槽からと酸液貯留タン
クからとでは逆方向になるため、一つの配管系統
によつて行うことができなかつた。このため、酸
液供給用及び酸液排出用のそれぞれに配管及び耐
酸ポンプを必要としていた。そのため、装置が複
雑となり、設備費の高騰を招いていた。また、酸
液貯留タンクが酸洗槽より低く配置されている場
合には、酸洗槽から酸液貯留タンクへの排液は自
重落下するので耐酸ポンプの必要はないが、酸液
貯留タンクから酸洗槽への給液用として専用のポ
ンプが設置されている。この場合でも、配管系を
2系統設けることが必要となる。
However, in conventional acid solution supply and discharge systems, the flow of acid solution from the pickling tank and from the acid solution storage tank is in opposite directions, making it impossible to perform this process using a single piping system. . Therefore, piping and acid-resistant pumps were required for supplying acid liquid and for discharging acid liquid. As a result, the equipment has become complicated, leading to a rise in equipment costs. In addition, if the acid solution storage tank is located lower than the pickling tank, there is no need for an acid-resistant pump because the drained liquid from the pickling tank to the acid solution storage tank will fall under its own weight. A dedicated pump is installed to supply liquid to the pickling tank. Even in this case, it is necessary to provide two piping systems.
また、酸洗槽内には、酸洗の進行に伴つて鋼材
から剥離されたスケールがスラツジとして槽の底
部に堆積しており、また酸洗槽の内張りであるれ
んがも剥離して屑となつて槽内に堆積することも
ある。このような異物があるとき、従来の酸洗設
備においては、サイホンを使用した上抜き方式に
よる酸洗槽の液抜き、スラツジ除去、槽内洗浄等
の工程を含む酸液切換えが行われている。このた
め、槽底部の残留酸液、スラツジの完全除去や槽
内洗浄液の排出は非常に困難であつた。 In addition, in the pickling tank, the scale that was peeled off from the steel as the pickling progressed was deposited as sludge at the bottom of the tank, and the bricks that lined the pickling tank were also peeled off and turned into scraps. It may also accumulate in the tank. When such foreign matter is present, in conventional pickling equipment, acid solution switching is performed, which includes processes such as draining the pickling tank using a top drain method using a siphon, removing sludge, and cleaning the inside of the tank. . For this reason, it has been extremely difficult to completely remove the residual acid solution and sludge at the bottom of the tank and to drain the cleaning solution inside the tank.
そこで、本発明は、このような酸洗槽に対する
酸液の供給及び排出のための設備を簡単な構造の
ものとし、しかも酸洗槽及び配管系の洗浄を良好
に行うことができる酸液切換えシステムを提供す
ることを目的とする。 Therefore, the present invention aims to simplify the structure of equipment for supplying and discharging acid solution to and from such a pickling tank, and to provide an acid solution switching system that can effectively clean the pickling tank and piping system. The purpose is to provide a system.
本発明の酸液切換えシステムは、その目的を達
成するため、酸洗槽と酸液貯留タンクとを結ぶ配
管の途中を2つの流路に分岐させて、この分岐し
た流路を相互に接続する連絡流路を形成し、該連
絡流路に耐酸ポンプを設け、且つ前記連絡流路が
前記2つの流路に接続された上流側及び下流側の
それぞれにバルブを介在させ、これらバルブの開
閉操作により前記酸洗槽から前記酸液貯留タンク
及び前記酸液貯留タンクから前記酸洗槽への酸液
が常に1方向の流れとなつて前記耐酸ポンプを通
過することを特徴とする。
In order to achieve the purpose of the acid liquid switching system of the present invention, the piping connecting the pickling tank and the acid liquid storage tank is branched into two flow paths, and these branched flow paths are interconnected. A communicating channel is formed, an acid-resistant pump is provided in the communicating channel, and valves are interposed on each of the upstream and downstream sides where the communicating channel is connected to the two channels, and the valves are opened and closed. Accordingly, the acid solution from the pickling tank to the acid solution storage tank and from the acid solution storage tank to the pickling tank always flows in one direction and passes through the acid-resistant pump.
〔作用〕
本発明においては、2種類以上の酸を切替えて
酸洗槽に供給することにより、普通鋼の他、ステ
ンレス鋼等種々の材質のコイルを酸洗処理する。[Function] In the present invention, coils made of various materials such as ordinary steel and stainless steel are pickled by switching between two or more types of acids and supplying them to the pickling tank.
酸液を切り換えることにより、多鋼種の材料の
酸洗処理を行う際、酸洗槽の酸液は、オフライン
に設置した酸液貯留タンクに排液し、別の酸液貯
留タンクから、酸洗槽に酸液を供給する。このと
き、酸洗槽と酸液貯留タンクとを結ぶ配管の途中
に設けた切換え機構によつて、常に同一方向で酸
液が耐酸ポンプを通過するため、酸洗槽〜酸液貯
留タンク間の酸液の給排液が1系統の配管、耐酸
ポンプにより行われる。 When pickling multi-steel materials by switching the acid solution, the acid solution in the pickling tank is drained to an acid solution storage tank installed offline, and the pickling is carried out from another acid solution storage tank. Supply acid solution to the tank. At this time, the switching mechanism installed in the middle of the piping connecting the pickling tank and the acid solution storage tank allows the acid solution to always pass through the acid-resistant pump in the same direction, so that Acid liquid is supplied and drained using one system of piping and an acid-resistant pump.
以下、図面を参照しながら、実施例により本発
明の特徴を具体的に説明する。
Hereinafter, the features of the present invention will be specifically explained using examples with reference to the drawings.
第1図は、本実施例の酸洗ラインにおける酸液
切換え装置の全体図を示す。 FIG. 1 shows an overall view of the acid liquid switching device in the pickling line of this embodiment.
鋼帯等の酸洗処理される鋼材は、酸洗槽に浸漬
される。図示の例においては、酸洗槽1a,1
b,1cの3層式となつており、鋼材は酸洗槽1
a,1b,1cを逐次通板される。そして、酸洗
槽1a,1b,1cのそれぞれに、酸液を貯留す
るタンク2a,2b,2cが接続されている。こ
れらタンク2a,2b,2cは、対応する酸洗槽
1a,1b,1cの酸液を全量収容する能力を有
している。 A steel material to be pickled, such as a steel strip, is immersed in a pickling tank. In the illustrated example, pickling tanks 1a, 1
It is a three-layer system of b and 1c, and the steel material is pickled in the pickling tank 1.
A, 1b, and 1c are sequentially threaded. Tanks 2a, 2b, and 2c for storing acid liquid are connected to the pickling tanks 1a, 1b, and 1c, respectively. These tanks 2a, 2b, 2c have the ability to accommodate the entire amount of acid solution in the corresponding pickling tank 1a, 1b, 1c.
酸液貯留タンク2a,2b,2cは、図示の例
においては、2種類の酸液A,Bを切り換えて使
用するので、それぞれ2基のタンクを有してい
る。 In the illustrated example, the acid liquid storage tanks 2a, 2b, and 2c each have two tanks because two types of acid liquids A and B are used selectively.
これら酸洗槽1a,1b,1cと酸液貯留タン
ク2a,2b,2cとを接続する配管3a,3
b,3cの途中には、それぞれの酸洗槽1a,1
b,1cに送り込まれる酸液A,Bの種類を切り
換えるための切換え機構4a,4b,4cが設け
られている。 Pipes 3a, 3 connecting these pickling tanks 1a, 1b, 1c and acid solution storage tanks 2a, 2b, 2c
In the middle of b, 3c, there are pickling tanks 1a, 1, respectively.
Switching mechanisms 4a, 4b, and 4c are provided for switching the types of acid solutions A and B sent to the buffers b and 1c.
第2図は、この切換え機構の詳細を示す図であ
る。酸洗槽1a,1b,1cから酸液貯留タンク
2a,2b,2cに酸液を排出する場合には、バ
ルブ21,22を開き、チエツクバルブ23を通
り、バルブ24,25を閉じる。これによつて、
各酸洗槽1a,1b,1cからの酸液は、バルブ
21、耐酸ポンプ26、チエツクバルブ23及び
バルブ22を経由する点線で示した経路に沿つ
て流れ、対応するタンクに送り込まれる。他方、
タンク2a,2b,2cから酸洗槽1a,1b,
1cに酸液を送り込む場合には、バルブ24,2
5を開き、チエツクバルブ23を通り、バルブ2
1,22を閉じる。これにより、各タンク2a,
2b,2cからの酸液は、バルブ25、耐酸ポン
プ26、チエツクバルブ23及びバルブ24を経
由する一点鎖線で示した経路に沿つて流れ、各
酸洗槽1a,1b,1cに送り込まれる。 FIG. 2 is a diagram showing details of this switching mechanism. When discharging the acid solution from the pickling tanks 1a, 1b, 1c to the acid solution storage tanks 2a, 2b, 2c, the valves 21, 22 are opened, the acid solution passes through the check valve 23, and the valves 24, 25 are closed. By this,
The acid solution from each pickling tank 1a, 1b, 1c flows along a path shown by a dotted line via a valve 21, an acid-proof pump 26, a check valve 23, and a valve 22, and is sent to the corresponding tank. On the other hand,
From tanks 2a, 2b, 2c to pickling tanks 1a, 1b,
When sending acid solution to 1c, valves 24 and 2
5, pass through check valve 23, and then open valve 2.
Close 1 and 22. As a result, each tank 2a,
The acid solution from 2b and 2c flows along the path shown by the dashed line via the valve 25, acid-resistant pump 26, check valve 23, and valve 24, and is sent to each pickling tank 1a, 1b, and 1c.
すなわち、酸洗槽1a,1b,1cから酸液を
排出する場合、及び酸液貯留タンク2a,2b,
2cから酸液を酸洗槽1a,1b,1cに送り込
む場合のいずれにあつても、バルブ21,22,
24,25の切換えによつて、耐酸ポンプ26及
びチエツクバルブ23を含む管路における酸液の
流れは常に一定の方向となる。したがつて、一台
の耐酸ポンプ26及び配管系によつて、給液及び
排液の両方を行うことができる。この切換えシス
テムによつて、耐酸ポンプ及び配管系統を一つに
まとめることができる。 That is, when discharging the acid solution from the pickling tanks 1a, 1b, 1c, and when discharging the acid solution from the acid solution storage tanks 2a, 2b,
2c to the pickling tanks 1a, 1b, 1c, the valves 21, 22,
By switching 24 and 25, the flow of the acid solution in the pipe line including the acid-resistant pump 26 and the check valve 23 is always in a constant direction. Therefore, both liquid supply and liquid drainage can be performed using one acid-resistant pump 26 and piping system. This switching system allows the acid-resistant pump and piping system to be combined into one.
なお、酸洗槽1a,1b,1cを酸液貯留タン
ク2a,2b,2cに結ぶ配管3a,3b,3c
の途中に、異物除去用のフイルター14a,14
b,14cを設ける必要がある。このときに、酸
洗槽1a,1b,1cからバルブ18a,18
b,18c及び管路15a,15b,15cを経
て配管3a,3b,3cに直接至るフイルターバ
イパス経路及び管路16a,16b,16c及び
フイルター14a,14b,14cを経由して配
管3a,3b,3cに至る管路とが設けられる。
そして、酸液貯留タンク2a,2b,2cから酸
洗槽1a,1b,1cに酸液を送るときは、切換
え機構4a,4b,4c、配管3a,3b,3
c、管路15a,15b,15c及びバルブ18
a,18b,18cの経路を使用する。他方、酸
洗槽1a,1b,1cからタンク2a,2b,2
cに酸液を送るときは、バルブ18a,18b,
18c、管路16a,16b,16c、フイルタ
ー14a,14b,14c、バルブ16−1a,
16−1b,16−1c及び配管3a,3b,3
cを使用する。 In addition, piping 3a, 3b, 3c connects the pickling tanks 1a, 1b, 1c to the acid solution storage tanks 2a, 2b, 2c.
Filters 14a, 14 for removing foreign matter are installed in the middle of the
b, 14c must be provided. At this time, from the pickling tanks 1a, 1b, 1c, the valves 18a, 18
b, 18c and pipes 15a, 15b, 15c to directly reach pipes 3a, 3b, 3c, and pipes 16a, 16b, 16c and filters 14a, 14b, 14c to pipes 3a, 3b, 3c. A conduit leading to the pipe is provided.
When sending acid solution from acid solution storage tanks 2a, 2b, 2c to pickling tanks 1a, 1b, 1c, switching mechanisms 4a, 4b, 4c, piping 3a, 3b, 3
c, pipe lines 15a, 15b, 15c and valve 18
Routes a, 18b, and 18c are used. On the other hand, from the pickling tanks 1a, 1b, 1c to the tanks 2a, 2b, 2
When sending acid solution to c, valves 18a, 18b,
18c, pipe lines 16a, 16b, 16c, filters 14a, 14b, 14c, valve 16-1a,
16-1b, 16-1c and piping 3a, 3b, 3
Use c.
これにより、酸洗槽1a,1b,1cから酸液
を排出する場合、酸洗槽1a,1b,1c中に浮
遊しているスラツジや槽内壁から剥離したれんが
屑等の異物がフイルター14a,14b,14c
で分離され、耐酸ポンプ26を経て酸液貯留タン
ク2a,2b,2cに送られる。したがつて、耐
酸ポンプ26のライニングがレンガ屑等の異物に
よつて破損されることがなくなり、耐酸ポンプの
寿命延長が図られる。また、実施例では、酸液貯
留タンクにはレンガを使用していないため、タン
クから酸洗槽への給液系統は、フイルターを通さ
ない管路とした。しかし、レンガ張りタンクを使
用する場合は、フイルター14a,14b,14
cを経由する管路(図示せず)とする必要があ
る。 As a result, when the acid solution is discharged from the pickling tanks 1a, 1b, 1c, foreign substances such as sludge floating in the pickling tanks 1a, 1b, 1c and brick chips peeled off from the tank inner wall are removed from the filters 14a, 14b. ,14c
The acid liquid is separated and sent to the acid liquid storage tanks 2a, 2b, and 2c via the acid-resistant pump 26. Therefore, the lining of the acid-resistant pump 26 will not be damaged by foreign objects such as brick chips, and the life of the acid-resistant pump will be extended. Furthermore, in the example, since bricks were not used in the acid solution storage tank, the liquid supply system from the tank to the pickling tank was a pipe line that did not pass through a filter. However, when using a brick-lined tank, the filters 14a, 14b, 14
It is necessary to use a conduit (not shown) via c.
なお、酸洗槽からタンクに排液する場合、液抜
きを槽下部から行うこともできる。たとえば、酸
洗槽1aの場合についていえば、槽下部のバルブ
W−1aからバルブ16−2aを経てフイルター
14aを通りバルブ16−1a、配管3aのルー
トを通すもので、酸洗槽内のスラツジ堆積量が少
ない場合等はこの経路も使用できる。 In addition, when draining the liquid from the pickling tank to the tank, the liquid can also be drained from the bottom of the tank. For example, in the case of pickling tank 1a, the sludge in the pickling tank is routed from valve W-1a at the bottom of the tank, through valve 16-2a, through filter 14a, to valve 16-1a, and to pipe 3a. This route can also be used when the amount of deposition is small.
第1図の例では、各酸洗槽1a,1b,1cご
とに切換え機構4a,4b,4c及び配管3a,
3b,3cを設けている。しかし、これらを集約
して1系統にすることもできる。 In the example shown in FIG. 1, the switching mechanisms 4a, 4b, 4c and the piping 3a,
3b and 3c are provided. However, these can also be aggregated into one system.
第3図は、この集約されたシステム例を示す。
なお、第3図においては、第1図に示した部材等
に相当するものについては、同一の符番で指示
し、その説明を省略した。 FIG. 3 shows an example of this aggregated system.
In FIG. 3, components corresponding to those shown in FIG. 1 are indicated by the same reference numerals, and their explanations are omitted.
この場合、酸液貯留タンク2の設置個数は、使
用する酸液の種類に応じたものとする(図示した
例では、4種類)。 In this case, the number of acid solution storage tanks 2 to be installed is determined according to the type of acid solution used (four types in the illustrated example).
以上に説明したように、本発明の酸液切換えシ
ステムにおいては、酸洗槽に供給される酸液及び
酸洗槽から排出される酸液のいずれもが同一方向
の流れとなつて耐酸ポンプを通過する。このた
め、耐酸ポンプ及び配管系を1酸洗槽に対し1系
統に集約することによつて設備費の削減が図れ
る。したがつて、たとえば酸液の供給及び排出を
それぞれ別系統で行つていた従来のシステムと比
較するとき、ポンプ、配管材等の削減により設備
費が約50%削減できる。また、酸液の切換えが容
易になり、且つポンプによる排液を行うため短時
間の酸液切換えが実施できるため、生産性の向上
も図られる。
As explained above, in the acid liquid switching system of the present invention, both the acid liquid supplied to the pickling tank and the acid liquid discharged from the pickling tank flow in the same direction, and the acid-resistant pump is operated. pass. Therefore, equipment costs can be reduced by consolidating the acid-resistant pump and piping system into one system for one pickling tank. Therefore, for example, when compared with a conventional system in which the supply and discharge of acid solution are performed in separate systems, equipment costs can be reduced by approximately 50% due to the reduction in pumps, piping materials, etc. In addition, it is easy to change the acid liquid, and since the liquid is drained by a pump, the acid liquid can be changed in a short time, so that productivity can be improved.
第1図は本発明第1実施例の酸液切換えシステ
ムの全体構成を示し、第2図は酸洗槽と酸液貯留
タンクとを結ぶ配管の途中に設けた切換え機構を
示し、第3図は第2実施例を示す。
Fig. 1 shows the overall configuration of the acid liquid switching system according to the first embodiment of the present invention, Fig. 2 shows the switching mechanism installed in the middle of the piping connecting the pickling tank and the acid liquid storage tank, and Fig. 3 shows the second embodiment.
Claims (1)
を2つの流路に分岐させて、この分岐した流路を
相互に接続する連絡流路を形成し、該連絡流路に
耐酸ポンプを設け、且つ前記連絡流路が前記2つ
の流路に接続された上流側及び下流側のそれぞれ
にバルブを介在させ、これらバルブの開閉操作に
より前記酸洗槽から前記酸液貯留タンク及び前記
酸液貯留タンクから前記酸洗槽への酸液が常に1
方向の流れとなつて前記耐酸ポンプを通過するこ
とを特徴とする連続酸洗ラインの酸液切換えシス
テム。1. Branch the piping connecting the pickling tank and the acid solution storage tank into two channels, form a communication channel that connects the branched channels, and install an acid-resistant pump in the communication channel. and a valve is interposed on each of the upstream and downstream sides where the communication channel is connected to the two channels, and by opening and closing these valves, the acid solution storage tank and the acid solution are removed from the pickling tank. The acid solution from the storage tank to the pickling tank is always 1
An acid liquid switching system for a continuous pickling line, characterized in that an acid liquid switching system for a continuous pickling line passes through the acid-resistant pump as a directional flow.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19359487A JPS6436780A (en) | 1987-08-01 | 1987-08-01 | Acid liquid changeover system of continuous pickling line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19359487A JPS6436780A (en) | 1987-08-01 | 1987-08-01 | Acid liquid changeover system of continuous pickling line |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6436780A JPS6436780A (en) | 1989-02-07 |
| JPH0465910B2 true JPH0465910B2 (en) | 1992-10-21 |
Family
ID=16310554
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19359487A Granted JPS6436780A (en) | 1987-08-01 | 1987-08-01 | Acid liquid changeover system of continuous pickling line |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6436780A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES2110170T3 (en) * | 1993-11-30 | 1998-02-01 | Danieli Off Mecc | A SYSTEM TO RE-CIRCULATE TREATMENT MATERIAL IN SURFACE TREATMENT AND FINISHING PROCESSES. |
| AT404030B (en) * | 1995-02-15 | 1998-07-27 | Andritz Patentverwaltung | METHOD OF STAINLESSING STEEL MATERIALS, ESPECIALLY STAINLESS STEEL |
| CN104357868A (en) * | 2014-10-23 | 2015-02-18 | 中国二十冶集团有限公司 | Rapid changing method of pickling tank |
| CN110468423B (en) * | 2019-08-07 | 2021-10-22 | 江苏斯德雷特通光光纤有限公司 | A kind of HF residual liquid recovery device of pickling equipment and using method |
-
1987
- 1987-08-01 JP JP19359487A patent/JPS6436780A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6436780A (en) | 1989-02-07 |
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