JP2000297390A - Continuous pickling method and continuous pickling apparatus - Google Patents

Continuous pickling method and continuous pickling apparatus

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Publication number
JP2000297390A
JP2000297390A JP11104366A JP10436699A JP2000297390A JP 2000297390 A JP2000297390 A JP 2000297390A JP 11104366 A JP11104366 A JP 11104366A JP 10436699 A JP10436699 A JP 10436699A JP 2000297390 A JP2000297390 A JP 2000297390A
Authority
JP
Japan
Prior art keywords
pickling
continuous
tank
acid
acid concentration
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.)
Granted
Application number
JP11104366A
Other languages
Japanese (ja)
Other versions
JP3591366B2 (en
Inventor
Koichi Takeuchi
孝一 武内
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP10436699A priority Critical patent/JP3591366B2/en
Publication of JP2000297390A publication Critical patent/JP2000297390A/en
Application granted granted Critical
Publication of JP3591366B2 publication Critical patent/JP3591366B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To raise the acid concn. in pickling liquid held in pickling vessels to a prescribed value while suppressing the acid concn. in the pickling liquid from the last pickling vessel to 12% or less. SOLUTION: A predicted value of the acid consumption in the pickling liquid held in a third vessel 11c and the last vessel 11d of a continuous pickling apparatus 10 at the pickling time is calculated with a control unit 14. On the basis of the calculated prediction value, acid liquid supplying quantities into the third vessel 11c and the last vessel 11d are decided and the acid liquid is supplied from an acid liquid supplying system 12. Then, the acid concns. in the pickling liquid held in the third vessel 11c and the last vessel 11d supplied with the acid liquid are continuously measured with an acid concn. continuous measuring instruments 13c, 13d, respectively. On the basis of the continuous measured values of the acid concns., the acid liquid is supplied into the third vessel 11c and the last vessel 11d from the acid liquid supplying system 12 so that the acid concns. of the pickling liquid held in the third vessel 11c and the last vessel 11d correspond to each of the target values, respectively.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、連続酸洗方法およ
び連続酸洗装置に関し、より具体的には、例えば、熱間
圧延を終了した鋼帯の表面に生成したスケールを除去す
るための連続酸洗方法および連続酸洗装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous pickling method and a continuous pickling apparatus, and more particularly to, for example, a continuous pickling method for removing scale formed on the surface of a steel strip after hot rolling. The present invention relates to a pickling method and a continuous pickling apparatus.

【0002】[0002]

【従来の技術】周知のように、熱間圧延を行われた鋼帯
の表面には、酸化物からなるスケールが生成される。こ
のスケールは、一般的に、鋼帯を例えば塩酸等からなる
酸洗液に連続的に浸漬させる酸洗を行われることによっ
て、除去される。この酸洗は、通常、3槽〜5槽程度の
酸洗槽を備える連続酸洗装置を用いて行われる。
2. Description of the Related Art As is well known, oxide scale is generated on the surface of a hot-rolled steel strip. This scale is generally removed by performing pickling in which the steel strip is continuously immersed in a pickling solution such as hydrochloric acid. This pickling is usually performed using a continuous pickling apparatus having about 3 to 5 pickling tanks.

【0003】図4は、4槽の酸洗槽2a〜2dを備える連続
酸洗装置1を模式的に示す説明図である。同図に示すよ
うに、連続酸洗装置1の第1槽2a、第2槽2b、第3槽2c
および第4槽(最終槽)2dに、鋼帯3を順次連続的に通
板させることにより、酸洗が行われる。各酸洗槽2a〜2d
に収容される酸洗液は、鋼帯3との反応や鋼帯3による
持ち出しにより、徐々に減少する。そのため、この連続
酸洗装置1では、最終槽2dに酸液供給装置4から酸液を
供給し、隣接する各酸洗槽2a〜2dの間に設けられた酸液
輸送配管5a〜5cにより、酸洗液を下流側の酸洗槽から上
流側に隣接する酸洗槽へ順次輸送する。そして、第1槽
2aからオーバーフローする酸洗液を、回収装置6に送っ
て回収し、再利用する。
FIG. 4 is an explanatory view schematically showing a continuous pickling apparatus 1 having four pickling tanks 2a to 2d. As shown in the figure, the first tank 2a, the second tank 2b, and the third tank 2c of the continuous pickling apparatus 1
And pickling is performed by continuously passing the steel strip 3 through the fourth tank (final tank) 2d. Each pickling tank 2a-2d
The pickling liquid contained in the steel strip 3 gradually decreases due to the reaction with the steel strip 3 and the removal by the steel strip 3. Therefore, in the continuous pickling apparatus 1, an acid solution is supplied from the acid solution supply device 4 to the final tank 2d, and the acid solution transport pipes 5a to 5c provided between the adjacent pickling tanks 2a to 2d are used. The pickling liquid is sequentially transported from the pickling tank on the downstream side to the pickling tank adjacent on the upstream side. And the first tank
The pickling liquid overflowing from 2a is sent to the collecting device 6 to be collected and reused.

【0004】連続酸洗装置1では、酸洗液をこのように
各酸洗槽2a〜2d間で循環させるため、各酸洗槽2a〜2dに
収容される酸洗液の酸濃度は異なる。例えば、最終槽2d
では12%程度であり、第1槽2aでは3%程度である。ま
た、第2槽2b、第3槽2cでは、最終槽2dと第1槽2aとの
中間の濃度となる。
In the continuous pickling apparatus 1, since the pickling solution is circulated between the pickling tanks 2a to 2d in this manner, the acid concentrations of the pickling solutions contained in the pickling tanks 2a to 2d are different. For example, the final tank 2d
In the first tank 2a, it is about 3%. In the second tank 2b and the third tank 2c, the concentration is intermediate between the final tank 2d and the first tank 2a.

【0005】この連続酸洗装置1では、最終槽2dへの酸
液の供給量を決定するには、少なくとも最終槽2dに収容
された酸洗液の酸濃度を測定する必要がある。しかし、
これまでの酸濃度測定技術では、酸洗液の酸濃度を短時
間で測定することはできなかった。例えば、公知の滴定
式分析計を用いて最終槽2dに収容された酸洗液の酸濃度
を測定すると、試薬導入からデータ出力までの1回のサ
ンプリングに約15分間を要してしまう。このため、最終
槽2dへの酸液の供給が大幅に遅れてしまい、この間に過
渡的に鋼帯に酸洗不良が発生してしまう。
In the continuous pickling apparatus 1, in order to determine the supply amount of the acid solution to the final tank 2d, it is necessary to measure at least the acid concentration of the pickling liquid contained in the final tank 2d. But,
With the conventional acid concentration measurement technology, the acid concentration of the pickling solution cannot be measured in a short time. For example, when the acid concentration of the pickling solution contained in the final tank 2d is measured using a known titration analyzer, it takes about 15 minutes for one sampling from the introduction of the reagent to the output of the data. For this reason, the supply of the acid solution to the final tank 2d is greatly delayed, and during this time, pickling failure occurs transiently in the steel strip.

【0006】そこで、酸洗液の酸濃度を短時間で測定で
きないことを補償するために、例えば、特開昭57−1744
73号公報には、酸洗液の酸濃度を測定せずに鋼帯の寸法
や材質等に基づいて酸液の供給量を演算により求める発
明が、また特開平7−54175号公報には、酸洗液の酸濃
度を測定せずに酸洗の前後における鋼帯の板厚の測定値
に基づいて酸液の供給量を演算により求める発明が、そ
れぞれ提案されている。これらの従来の技術によれば、
酸液を供給される酸洗槽(図4の連続酸洗装置1では最
終槽2d)に収容された酸洗液の酸濃度を、目標値に制御
することができる。
In order to compensate for the inability to measure the acid concentration of the pickling solution in a short time, for example, Japanese Patent Application Laid-Open No.
No. 73 discloses an invention in which the supply amount of an acid solution is calculated by calculation based on the dimensions and materials of a steel strip without measuring the acid concentration of the pickling solution. Each invention has been proposed in which the supply amount of the acid solution is calculated by calculation based on the measured value of the thickness of the steel strip before and after the pickling without measuring the acid concentration of the pickling solution. According to these conventional techniques,
The acid concentration of the pickling solution contained in the pickling tank (the last tank 2d in the continuous pickling apparatus 1 in FIG. 4) to which the acid solution is supplied can be controlled to a target value.

【0007】[0007]

【発明が解決しようとする課題】しかし、これらの従来
の技術では、酸液を供給される酸洗槽以外の酸洗槽に収
容される酸洗液の酸濃度を高くすることができないた
め、連続酸洗装置1を備える酸洗工程の生産性を向上さ
せること、つまり酸洗速度を向上させることができな
い。
However, these conventional techniques cannot increase the acid concentration of the pickling liquid contained in the pickling tank other than the pickling tank to which the acid liquid is supplied. It is not possible to improve the productivity of the pickling step including the continuous pickling apparatus 1, that is, to improve the pickling speed.

【0008】すなわち、連続酸洗装置1の酸洗速度を向
上するには、酸液を供給される最終槽2dへの酸液の供給
量を増加して、各酸洗槽2a〜2dに収容される酸洗液の酸
濃度を高める必要がある。しかし、最終槽2dの酸洗液の
酸濃度が約12%を越えると、酸洗液である塩酸の蒸気圧
が高くなり、最終槽2dにおいて蒸発による塩酸の消費量
が増加し、酸洗液に要するコストが著しく増加してしま
う。このため、最終槽2d以外の各酸洗槽2a〜2cに収容さ
れる酸洗液の酸濃度を高めることができず、酸洗速度を
向上することができない。
That is, in order to increase the pickling speed of the continuous pickling apparatus 1, the supply amount of the acid solution to the final tank 2d to which the acid solution is supplied is increased, and the acid solution is accommodated in each of the pickling tanks 2a to 2d. It is necessary to increase the acid concentration of the pickling solution to be used. However, when the acid concentration of the pickling liquid in the final tank 2d exceeds about 12%, the vapor pressure of the hydrochloric acid, which is the pickling liquid, increases, and the consumption of hydrochloric acid by evaporation in the final tank 2d increases. The cost required for this increases significantly. For this reason, the acid concentration of the pickling liquid contained in each of the pickling tanks 2a to 2c other than the final tank 2d cannot be increased, and the pickling speed cannot be improved.

【0009】本発明の目的は、酸液を供給される酸洗槽
からの酸洗液の蒸発量をできるだけ抑制しながら、各酸
洗槽に収容された酸洗液の酸濃度を高めて所望の値に近
づけ、これにより、酸洗の生産性を向上することができ
る連続酸洗方法および連続酸洗装置を提供することであ
る。また、本発明の目的は、このような連続酸洗方法お
よび連続酸洗装置を、既存の連続酸洗設備をできるだけ
改造することなく提供することである。
An object of the present invention is to increase the acid concentration of the pickling liquid contained in each pickling tank while minimizing the evaporation of the pickling liquid from the pickling tank to which the acid liquid is supplied. And to provide a continuous pickling method and a continuous pickling apparatus that can improve the productivity of pickling. Another object of the present invention is to provide such a continuous pickling method and a continuous pickling apparatus without modifying existing continuous pickling equipment as much as possible.

【0010】[0010]

【課題を解決するための手段】本発明は、連続酸洗装置
を構成する複数の酸洗槽のうちの2以上の酸洗槽にそれ
ぞれ収容された酸洗液の酸洗時における酸消費量の予測
値を、酸洗時の酸洗条件に基づいて算出し、算出した予
測値に基づいて2以上の酸洗槽それぞれへの酸液供給量
を決定して酸液を供給し、酸液を供給された2以上の酸
洗槽にそれぞれ収容される酸洗液の酸濃度を連続的に測
定し、測定された酸濃度の連続的な測定値に基づいて、
2以上の酸洗槽にそれぞれ収容された酸洗液の酸濃度が
目標値に一致するように、2以上の酸洗槽への酸液供給
量を制御することを特徴とする連続酸洗方法である。
According to the present invention, there is provided an acid pickling solution for pickling a pickling solution contained in at least two pickling tanks among a plurality of pickling tanks constituting a continuous pickling apparatus. Is calculated based on the pickling conditions at the time of pickling, and based on the calculated predicted value, the supply amount of the acid solution to each of the two or more pickling tanks is determined, and the acid solution is supplied. The acid concentration of the pickling liquid contained in each of the two or more pickling tanks supplied is continuously measured, and based on the continuously measured values of the measured acid concentration,
A continuous pickling method characterized by controlling the supply amount of an acid solution to two or more pickling tanks so that the acid concentration of the pickling liquid stored in each of the two or more pickling tanks matches a target value. It is.

【0011】この本発明にかかる連続酸洗方法では、
(i) 2以上の酸洗槽が少なくとも最終酸洗槽を含むこ
と、(ii)連続酸洗装置が、下流側の酸洗槽に収容された
酸洗液を上流側に隣接する酸洗槽へ順次オーバーフロー
させる型の連続酸洗装置、または下流側の酸洗槽に収容
された酸洗液を上流側に隣接する酸洗槽へ順次輸送する
型の連続酸洗装置であること、(iii) 酸濃度の連続的な
測定値が、少なくとも、2以上の酸洗槽にそれぞれ設け
られた酸洗液循環流路に配置された密度計からの連続的
な出力値を用いて、測定されることが例示される。特
に、この(iii) 項の場合には、酸濃度の連続的な測定値
が、酸洗槽または酸洗液循環流路に配置された温度計お
よび導電率計それぞれからの連続的な出力値を用いて測
定されることが、さらに例示される。
In the continuous pickling method according to the present invention,
(i) the two or more pickling tanks include at least a final pickling tank; (ii) a continuous pickling apparatus, wherein the pickling liquid contained in the downstream pickling tank is adjacent to the pickling tank on the upstream side. A continuous pickling apparatus of a type that sequentially overflows to the pickling tank, or a continuous pickling apparatus of a type that sequentially transports the pickling liquid stored in the pickling tank on the downstream side to the pickling tank adjacent to the upstream side, (iii) ) A continuous measurement value of the acid concentration is measured using at least continuous output values from a densitometer disposed in a pickling liquid circulation channel provided in each of two or more pickling tanks. Is exemplified. In particular, in the case of this paragraph (iii), the continuous measurement value of the acid concentration is the continuous output value from each of the thermometer and the conductivity meter arranged in the pickling tank or the pickling liquid circulation channel. Is further exemplified.

【0012】また、別の観点からは、本発明は、連続酸
洗装置を構成する複数の酸洗槽のうちの2以上の酸洗槽
と、2以上の酸洗槽へそれぞれ酸液を供給する酸液供給
系と、2以上の酸洗槽にそれぞれ収容された酸洗液の酸
濃度をそれぞれ連続的に測定する酸濃度連続測定装置
と、2以上の酸洗槽にそれぞれ収容された酸洗液の酸洗
時における酸消費量の予測値を、酸洗時の酸洗条件から
それぞれ算出し、算出した予測値に基づいて酸液供給量
を決定して酸液供給系へ酸液供給信号を出力するととも
に、酸液供給系から2以上の酸洗槽へ酸液が供給された
後に酸濃度連続測定装置から出力される酸濃度の連続的
な測定値に基づいて、2以上の酸洗槽にそれぞれ収容さ
れた酸洗液の酸濃度が目標値になるように、酸液供給系
へ酸液供給信号を出力する制御装置とを組み合わせて備
えることを特徴とする連続酸洗装置である。
Further, from another viewpoint, the present invention provides an acid pickling tank comprising two or more pickling tanks constituting a continuous pickling apparatus and supplying an acid solution to the two or more pickling tanks. Acid supply system, an acid concentration continuous measuring device for continuously measuring the acid concentration of each of the pickling liquids contained in the two or more pickling tanks, and the acid contained in the two or more pickling tanks, respectively. The predicted value of the acid consumption during the pickling of the washing solution is calculated from the pickling conditions during the pickling, and the acid solution supply amount is determined based on the calculated predicted value to supply the acid solution to the acid solution supply system. A signal is output and, based on the continuous measurement of the acid concentration output from the acid concentration continuous measuring device after the acid solution is supplied from the acid solution supply system to the two or more pickling tanks, two or more acids are measured. An acid solution supply signal is output to the acid solution supply system so that the acid concentration of the pickling solution stored in each of the washing tanks becomes the target value. A continuous pickling apparatus, characterized in that it comprises a combination of a control device for.

【0013】この本発明にかかる連続酸洗装置では、(i
v)2以上の酸洗槽が少なくとも最終酸洗槽を含むこと、
(v) 連続酸洗装置が、下流側の酸洗槽に収容された酸洗
液を上流側に隣接する酸洗槽へ順次オーバーフローさせ
る型の連続酸洗装置、または下流側の酸洗槽に収容され
た酸洗液を上流側に隣接する酸洗槽へ順次輸送する型の
連続酸洗装置であること、(vi)酸濃度連続測定装置が、
酸洗槽に接続され、酸洗槽から取り出された酸洗液の流
路の一部に設けられた本体と、この本体の内部を流れる
酸洗液の密度を測定する密度計と、流路または酸洗槽に
おける酸洗液の温度を測定する温度計と、流路または酸
洗槽における酸洗液の導電率を測定する導電率計と、密
度、温度計および導電率計それぞれの測定結果に基づい
て流路の一部を流れる酸洗液の酸濃度を演算する演算装
置とを組み合わせて備えることが、いずれも例示され
る。
In the continuous pickling apparatus according to the present invention, (i)
v) the two or more pickling tanks include at least a final pickling tank;
(v) A continuous pickling apparatus in which a pickling solution contained in a downstream pickling tank overflows sequentially to an adjacent pickling tank on the upstream side, or a pickling tank on the downstream side. It is a continuous pickling apparatus of a type that sequentially transports the contained pickling liquid to an adjacent pickling tank on the upstream side, and (vi) a continuous acid concentration measuring apparatus,
A main body connected to the pickling tank and provided in a part of the flow path of the pickling liquid taken out of the pickling tank; a density meter for measuring the density of the pickling liquid flowing inside the main body; Or a thermometer that measures the temperature of the pickling solution in the pickling tank, a conductivity meter that measures the conductivity of the pickling solution in the flow path or the pickling tank, and the measurement results of the density, thermometer, and conductivity meter, respectively. And a calculation device for calculating the acid concentration of the pickling solution flowing through a part of the flow path based on the above.

【0014】[0014]

【発明の実施の形態】以下、本発明にかかる連続酸洗方
法および連続酸洗装置の実施の形態を、添付図面を参照
しながら詳細に説明する。なお、以降の実施の形態の説
明では、酸洗液が塩酸であるとともに、後述する図2に
示す酸濃度連続測定装置13を用いた場合を例にとる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of a continuous pickling method and a continuous pickling apparatus according to the present invention will be described below in detail with reference to the accompanying drawings. In the following description of the embodiment, a case where the pickling liquid is hydrochloric acid and a continuous acid concentration measuring device 13 shown in FIG.

【0015】図1は、本実施形態の連続酸洗装置10の構
成を模式的に示す説明図である。同図に示すように、こ
の連続酸洗装置10は、酸洗槽11a 〜11d と、酸液供給系
12と、酸濃度連続測定装置13c 、13d と、制御装置14と
を備える。以下、これらの構成要素について、順次説明
する。
FIG. 1 is an explanatory view schematically showing a configuration of a continuous pickling apparatus 10 of the present embodiment. As shown in FIG. 1, the continuous pickling apparatus 10 includes pickling tanks 11a to 11d and an acid solution supply system.
12, a continuous acid concentration measuring device 13c, 13d, and a control device 14. Hereinafter, these components will be sequentially described.

【0016】〔酸洗槽11a 〜11d 〕この連続酸洗装置10
は、4つの酸洗槽11a 〜11d を有する。酸洗槽11a が第
1槽であり、酸洗槽11b が第2槽であり、酸洗槽11c が
第3槽であり、さらに酸洗槽11d が最終槽である。
[Pickling tanks 11a to 11d] This continuous pickling apparatus 10
Has four pickling tanks 11a to 11d. The pickling tank 11a is a first tank, the pickling tank 11b is a second tank, the pickling tank 11c is a third tank, and the pickling tank 11d is a final tank.

【0017】酸洗される鋼帯15は、第1槽11a 、第2槽
11b 、第3槽11c および最終槽11dの順に、各酸洗槽11a
〜11d に収容された酸洗液に浸漬される。そして、最
終槽11d を出た鋼帯15は、次工程に送られる。
The steel strip 15 to be pickled is supplied to a first tank 11a and a second tank 11a.
11b, the third tank 11c and the final tank 11d in this order.
It is immersed in the pickling liquid stored in ~ 11d. Then, the steel strip 15 that has left the final tank 11d is sent to the next step.

【0018】また、この連続酸洗装置10では、下流側の
酸洗槽に収容された酸洗液が上流側に隣接する酸洗槽へ
順次オーバーフローする。すなわち、最終槽11d に収容
された酸洗液が第3槽11c へオーバーフローし、第3槽
11c に収容された酸洗液が第2槽11b へオーバーフロー
し、第2槽11b に収容された酸洗液が第1槽11a へオー
バーフローする。そして、第1槽11a からオーバーフロ
ーする酸洗液は、図示しない回収装置に送られて回収さ
れ、再利用される。本実施形態の酸洗槽11a 〜11d は、
以上のように構成される。
In the continuous pickling apparatus 10, the pickling liquid contained in the downstream pickling tank sequentially overflows to the pickling tank adjacent on the upstream side. That is, the pickling liquid contained in the final tank 11d overflows to the third tank 11c,
The pickling liquid contained in 11c overflows to the second tank 11b, and the pickling liquid contained in the second tank 11b overflows to the first tank 11a. Then, the pickling solution overflowing from the first tank 11a is sent to a collecting device (not shown) to be collected and reused. The pickling tanks 11a to 11d of the present embodiment include:
The configuration is as described above.

【0019】〔酸液供給系12〕本実施形態の連続酸洗装
置10は、酸液供給系12を有する。本実施形態の酸液供給
系12は、第3槽11c に酸液を供給する第3槽酸液供給装
置12c と、最終槽11dに酸液を供給する最終槽酸液供給
装置12d とにより構成される。第3槽酸液供給装置12c
および最終槽酸液供給装置12d は、いずれも、電磁式の
ダイヤフラム弁16を介して、図示しない酸液供給源に接
続されている。第3槽酸液供給装置12cおよび最終槽酸
液供給装置12d にそれぞれ設けられたダイヤフラム弁16
は、いずれも、後述する制御装置14に接続されており、
制御装置14から出力される酸液供給信号によって弁の開
度が制御される。これにより、第3槽酸液供給装置12c
から第3槽11c への酸液の供給量と、最終槽酸液供給装
置12d から最終槽11d への酸液の供給量とが、個別に制
御される。
[Acid Solution Supply System 12] The continuous pickling apparatus 10 of the present embodiment has an acid solution supply system 12. The acid solution supply system 12 of the present embodiment includes a third tank acid solution supply device 12c that supplies an acid solution to the third tank 11c, and a final tank acid solution supply device 12d that supplies an acid solution to the final tank 11d. Is done. Third tank acid solution supply device 12c
In addition, the final tank acid solution supply device 12d is connected to an acid solution supply source (not shown) via an electromagnetic diaphragm valve 16. The diaphragm valves 16 provided in the third tank acid solution supply device 12c and the final tank acid solution supply device 12d, respectively.
Are connected to the control device 14 described below,
The opening degree of the valve is controlled by the acid solution supply signal output from the control device 14. Thereby, the third tank acid solution supply device 12c
And the supply amount of the acid solution from the final tank acid solution supply device 12d to the final tank 11d is individually controlled.

【0020】なお、本実施形態では第3槽11c および最
終槽11d に酸液を供給するようにしているが、第2槽11
b やさらには第1槽11a にも、第3槽酸液供給装置12c
および最終槽酸液供給装置12d と同様の酸液供給装置を
それぞれ設けて、酸液を個別に供給するようにしてもよ
い。本実施形態の酸液供給系12は、以上のように構成さ
れる。
In this embodiment, the acid solution is supplied to the third tank 11c and the final tank 11d.
b and also the first tank 11a, the third tank acid solution supply device 12c
Alternatively, an acid solution supply device similar to the final tank acid solution supply device 12d may be provided to supply the acid solution individually. The acid solution supply system 12 of the present embodiment is configured as described above.

【0021】〔酸濃度連続測定装置13c 、13d 〕本実施
形態では、第3槽11c には酸濃度連続測定装置13c が設
けられるとともに、最終槽11d には酸濃度連続測定装置
13d が設けられる。酸濃度連続測定装置13c および酸濃
度連続測定装置13d は、同一のものであるため、以降の
説明では酸濃度連続測定装置13d を例にとって説明す
る。
[Continuous Acid Concentration Measurement Apparatus 13c, 13d] In this embodiment, the third tank 11c is provided with a continuous acid concentration measurement apparatus 13c, and the final tank 11d is provided with a continuous acid concentration measurement apparatus.
13d is provided. Since the acid concentration continuous measurement device 13c and the acid concentration continuous measurement device 13d are the same, the following description will be made using the acid concentration continuous measurement device 13d as an example.

【0022】図2は、本実施形態の酸濃度連続測定装置
13d の内部構造を示す説明図である。図2中の破線矢印
は酸洗液の流れを示す。図2に示すように、この酸濃度
連続測定装置13d は、ポンプ17d により最終槽11d から
圧送された酸洗液を連続的に一方向へ流すための循環流
路18d の一部を内蔵する筒状の酸濃度連続測定装置本体
19d と、循環流路18d の一部を流れる酸洗液を連続的に
測定する密度計20d 、温度計21d および導電率計22d と
を備える。
FIG. 2 shows a continuous acid concentration measuring apparatus according to this embodiment.
It is explanatory drawing which shows the internal structure of 13d. The broken arrows in FIG. 2 indicate the flow of the pickling solution. As shown in FIG. 2, the acid concentration continuous measuring device 13d is a cylinder having a part of a circulation channel 18d for continuously flowing the pickling solution pumped from the final tank 11d in one direction by a pump 17d. Acid concentration continuous measurement device main body
19d, a density meter 20d, a thermometer 21d, and a conductivity meter 22d for continuously measuring the pickling liquid flowing through a part of the circulation channel 18d.

【0023】本実施形態における酸濃度連続測定装置本
体19d は、筒型状のものであってサンプルである酸洗液
を最終槽11d から連続的に流して最終槽11d へ戻すこと
ができる構造であればよく、特定の構造には限定されな
い。
The main body 19d of the apparatus for continuously measuring acid concentration in this embodiment has a cylindrical shape and has a structure in which a pickling liquid as a sample can be continuously flowed from the final tank 11d and returned to the final tank 11d. It is sufficient if it is provided, and it is not limited to a specific structure.

【0024】酸濃度連続測定装置本体19d の材質は、酸
洗液に浸食されない程度の耐酸性を有するものであれば
よく、本実施形態ではポリプロピレン製とした。また、
酸濃度連続測定装置本体19d の内部に形成される循環流
路18d の一部は、できるだけエルボ等の流速低下部が少
ないストレート状に形成してある。これにより、酸濃度
連続測定装置本体19d の内部において、酸洗液の流れが
低下することによる詰まりの発生が可及的抑制される。
The material of the acid concentration continuous measuring device main body 19d may be any material having an acid resistance such that it is not eroded by the pickling solution. In this embodiment, the material is made of polypropylene. Also,
A part of the circulation flow path 18d formed inside the acid concentration continuous measurement device main body 19d is formed in a straight shape with a reduced flow velocity portion such as an elbow as much as possible. As a result, the occurrence of clogging due to a decrease in the flow of the pickling liquid inside the acid concentration continuous measuring device main body 19d is suppressed as much as possible.

【0025】さらに、循環流路18d の一部を流れる酸洗
液の流速は、密度計20d 、温度計21d および導電率計22
d それぞれの測定精度を維持するために、2m/sec 以下
であることが望ましい。本実施形態の酸濃度連続測定装
置13d の酸濃度連続測定装置本体19d の内部では、下方
に位置する循環流路18d が、排出用配管23d と略同じ高
さ位置に形成されている。これにより、ポンプ17d によ
り圧送されてきた酸洗液は、図中の破線矢印で示すよう
に、酸濃度連続測定装置本体19d の内部における最底部
付近において一旦滞留してから、排出用配管23d へと導
かれる。このため、本実施形態の酸濃度連続測定装置19
d では、循環流路18d を流れる酸洗液の流速を、密度計
20d 、温度計21d および導電率計22d の測定精度の観点
から望ましい流速である2m/sec 以下に容易に設定・管
理し、測定精度の向上を図ることができる。本実施形態
では、酸洗液の流速が1m/sec になるように、酸濃度連
続測定装置本体19d の各部寸法を設定した。
Further, the flow rate of the pickling liquid flowing through a part of the circulation channel 18d is controlled by a density meter 20d, a thermometer 21d and a conductivity meter 22d.
d In order to maintain the accuracy of each measurement, it is desirable that it be 2 m / sec or less. Inside the acid concentration continuous measuring device main body 19d of the acid concentration continuous measuring device 13d of the present embodiment, a lower circulation channel 18d is formed at substantially the same height as the discharge pipe 23d. As a result, the pickling solution pumped by the pump 17d temporarily stays in the vicinity of the bottom in the acid concentration continuous measuring device main body 19d as shown by the broken arrow in the figure, and then flows to the discharge pipe 23d. It is led. For this reason, the acid concentration continuous measurement device 19 of the present embodiment
In d, the flow rate of the pickling liquid flowing through the circulation passage 18d is
From the viewpoint of the measurement accuracy of the thermometer 20d, the thermometer 21d and the conductivity meter 22d, it is possible to easily set and manage the flow velocity to 2 m / sec or less, which is a desirable flow rate, thereby improving the measurement accuracy. In the present embodiment, the dimensions of each part of the acid concentration continuous measuring device main body 19d are set such that the flow rate of the pickling solution is 1 m / sec.

【0026】また、本実施形態では、密度計20d には、
二つの検出部20d-1 、20d-2 を有する公知の差圧センサ
ー方式の密度計を用いた。二つの検出部20d-1 、20d-2
は、所望の密度測定精度を確保するために、循環流路18
d の一部の形成方向に関する距離d1 が少なくとも500m
m となるように離して、酸濃度連続測定装置本体19dの
長手方向略中央の胴部に設置される。
In this embodiment, the density meter 20d includes:
A known differential pressure sensor type densitometer having two detectors 20d-1 and 20d-2 was used. Two detectors 20d-1 and 20d-2
In order to ensure the desired density measurement accuracy,
At least 500m distance d 1 of a portion of the formation direction of the d
The main body 19d is installed at a substantially central body in the longitudinal direction of the main body 19d of the continuous acid concentration measuring device so as to be m.

【0027】また、検出部20d-1 、20d-2 の設置部で
は、酸洗液の流通方向と直交する方向(図2における左
右方向) に関する分流部の突出量d2 を、できるだけ小
さく設定してある。これにより、分流部における酸洗液
の滞留が抑制され、酸洗液の詰まりが確実に防止され
る。
Further, in the installation of the detection unit 20d-1, 20d-2 is a projection amount d 2 of diverter with respect to the direction (horizontal direction in FIG. 2) perpendicular to the flow direction of the pickling solution, and set as small as possible It is. Thereby, the stagnation of the pickling liquid in the branch part is suppressed, and the clogging of the pickling liquid is reliably prevented.

【0028】本実施形態では、温度計21d には公知の白
金抵抗体式の温度計を用いた。また、導電率計22d にも
公知の電磁誘導型の導電率計を用いた。温度計21d およ
び導電率計22d は、ともに、循環流路18d の一部の出側
で測定を行うことができるように、酸濃度連続測定装置
本体19d の底部に設置される。
In this embodiment, a known platinum resistor type thermometer is used as the thermometer 21d. A known electromagnetic induction type conductivity meter was also used as the conductivity meter 22d. Both the thermometer 21d and the conductivity meter 22d are installed at the bottom of the acid concentration continuous measuring device main body 19d so that the measurement can be performed at a part of the outlet side of the circulation channel 18d.

【0029】なお、本実施形態では、温度計21d および
導電率計22d は、いずれも、酸濃度連続測定装置本体19
d に設けた。これは、温度計21d および導電率計22d を
ともに密度計20d の近傍に配置することにより、測定誤
差を可及的低減するためである。しかし、温度計21d 、
導電率計22d は、必ずしも酸濃度連続測定装置本体19d
に配置する必要はない。温度計21d 、導電率計22d を、
最終槽11d の内部または、最終槽11d と酸濃度連続測定
装置本体19d との間の循環流路18d を構成する配管等に
設置して、循環する酸洗液の温度、導電率を測定するこ
ととしてもよい。この場合、密度計20d の設置部近傍に
おける温度、導電率の値と、温度計21d、導電率計22d
の設置部における測定データとの偏差を予め求めてお
き、これらの偏差を用いて温度計21d 、導電率計22d の
設置部における測定データを補正すればよい。これによ
り、温度計21d および導電率計22d を密度計20d の近傍
に配置しなくとも、測定誤差が可及的低減される。
In the present embodiment, both the thermometer 21d and the conductivity meter 22d are provided with the acid concentration continuous measuring device main body 19d.
d. This is because the measurement error can be reduced as much as possible by arranging both the thermometer 21d and the conductivity meter 22d near the density meter 20d. However, thermometer 21d,
The conductivity meter 22d is not necessarily the acid concentration continuous measurement device main body 19d.
You do not need to place them. Thermometer 21d, conductivity meter 22d,
The temperature and conductivity of the circulating pickling liquid should be measured by installing the inside of the final tank 11d or in a pipe or the like constituting the circulation flow path 18d between the final tank 11d and the acid concentration continuous measuring device main body 19d. It may be. In this case, the values of the temperature and conductivity near the installation portion of the density meter 20d and the thermometer 21d and the conductivity meter 22d
Deviations from the measurement data at the installation portion of the thermometer 21d and the conductivity data at the installation portion of the conductivity meter 22d may be corrected using these deviations. Thereby, the measurement error can be reduced as much as possible without disposing the thermometer 21d and the conductivity meter 22d near the density meter 20d.

【0030】この酸濃度連続測定装置13d は、本実施形
態では、最終槽11d の外壁面近傍に設置される。そし
て、酸濃度連続測定装置13d は、最終槽11d の近傍に設
置したポンプ17d により最終槽11d に収容された酸洗液
を一方向へ流す。これにより、酸濃度連続測定装置13d
は、連続的に酸洗液の密度、温度および導電率をいずれ
も測定することが可能である。
In this embodiment, the acid concentration continuous measuring device 13d is installed near the outer wall surface of the final tank 11d. The acid concentration continuous measuring device 13d allows the pickling liquid contained in the final tank 11d to flow in one direction by a pump 17d installed near the final tank 11d. Thereby, the acid concentration continuous measuring device 13d
Can continuously measure the density, temperature and conductivity of the pickling liquid.

【0031】このように、本実施形態の酸濃度連続測定
装置13d で用いる密度計20d 、温度計21d および導電率
計22d には、いずれも、高い使用実績を有する公知の工
業計器を使用する。このため、本実施形態の酸濃度連続
測定装置13d は、極めて高い精度で正確に、酸洗液の密
度、温度および導電率を求めることができる。
As described above, as the density meter 20d, the thermometer 21d and the conductivity meter 22d used in the acid concentration continuous measuring device 13d of the present embodiment, all known industrial instruments having a high track record of use are used. For this reason, the acid concentration continuous measuring device 13d of the present embodiment can accurately and accurately determine the density, temperature, and conductivity of the pickling liquid.

【0032】また、本実施形態の酸濃度連続測定装置13
d の近傍には、密度計20d により連続的に測定された密
度と、温度計21d により連続的に測定された温度と、導
電率計22d により連続的に測定された導電率とに基づい
て、酸洗液の酸濃度を演算する演算装置 (図示しない)
が設置される。この演算装置により酸洗液の酸濃度が連
続的に演算される。この演算装置による演算結果は、後
述する制御装置14へ入力される。
Further, the acid concentration continuous measuring device 13 of the present embodiment
In the vicinity of d, based on the density continuously measured by the density meter 20d, the temperature continuously measured by the thermometer 21d, and the conductivity continuously measured by the conductivity meter 22d, An arithmetic unit (not shown) that calculates the acid concentration of the pickling solution
Is installed. The arithmetic unit continuously calculates the acid concentration of the pickling solution. The calculation result by this calculation device is input to the control device 14 described later.

【0033】なお、本実施形態の酸濃度連続測定装置13
d による「連続的な測定」とは、例えば公知の滴定式分
析計を用いた場合の測定ピッチ(約15分間)に比べて極
めて短い測定ピッチでの測定を意味しており、例えば、
測定ピッチが1分間以下、望ましくは10秒間以下である
酸濃度測定を意味する。
It should be noted that the acid concentration continuous measuring device 13 of the present embodiment
"Continuous measurement" by d means, for example, measurement at a measurement pitch that is extremely short as compared to the measurement pitch (about 15 minutes) when using a known titration analyzer, for example,
It refers to acid concentration measurement where the measurement pitch is 1 minute or less, preferably 10 seconds or less.

【0034】また、本実施形態の酸濃度連続測定装置13
d では、酸濃度連続測定装置本体19d を筒型状単管式と
する。このため、以下に列記する効果(i) 〜(vii) が奏
せられる。
The acid concentration continuous measuring device 13 of the present embodiment
In d, the acid concentration continuous measurement device main body 19d is a cylindrical single tube type. Therefore, the following effects (i) to (vii) can be obtained.

【0035】(i) 循環流路18d の形状をできるだけ直線
状とするとともに、距離d2 をできるだけ小さく設定す
る。このため、循環流路18d 内、特に密度計20d 、温度
計21dおよび導電率計22d それぞれの近傍における酸洗
液の滞留が防止され、酸洗液を連続的に流すことができ
る。
(I) The shape of the circulation channel 18d is made as straight as possible, and the distance d 2 is set as small as possible. This prevents the pickling solution from staying in the circulation flow path 18d, particularly in the vicinity of each of the density meter 20d, the thermometer 21d, and the conductivity meter 22d, and allows the pickling solution to flow continuously.

【0036】(ii)酸洗液は、循環流路18d 内を連続的に
流れる。このため、循環流路18d 内における酸洗液の偏
析が防止され、別々に採取した複数種の酸洗液をも同一
条件で正確に測定することができる。
(Ii) The pickling liquid flows continuously in the circulation channel 18d. For this reason, segregation of the pickling liquid in the circulation channel 18d is prevented, and a plurality of types of pickling liquid separately collected can be accurately measured under the same conditions.

【0037】(iii) ポンプ17d により酸洗液を常時流す
ため、酸濃度連続測定装置本体19d のメンテナンス性お
よび内部洗浄性がいずれも著しく向上し、酸洗液の詰ま
りを解消しながら連続測定を行うことができる。
(Iii) Since the pickling solution is constantly flowed by the pump 17d, both the maintainability and the internal cleanability of the acid concentration continuous measuring device main body 19d are significantly improved, and continuous measurement can be performed while eliminating clogging of the pickling solution. It can be carried out.

【0038】(iv)酸洗液の密度、温度および導電率を連
続的に測定するため、酸洗液の酸濃度を連続的に測定す
ることができる。これにより、この酸濃度連続測定装置
13d を、例えば連続酸洗設備の最終酸洗槽の酸濃度に関
するフィードバック制御、または、フィードバック制御
およびフィードフォワード制御と組合せることにより、
最終酸洗槽の酸濃度を連続的かつ高精度で自動制御する
ことも可能となる。
(Iv) Since the density, temperature and conductivity of the pickling solution are continuously measured, the acid concentration of the pickling solution can be continuously measured. With this, this acid concentration continuous measurement device
By combining 13d with, for example, feedback control on the acid concentration of the final pickling tank of a continuous pickling facility, or feedback control and feedforward control,
It is also possible to automatically control the acid concentration in the final pickling tank continuously and with high accuracy.

【0039】(v) 酸濃度連続測定装置13d は、図1およ
び図2に示すように、極めて簡単な外部形状を有する。
このため、例えば連続酸洗設備等への設置の自由度が高
い。
(V) The acid concentration continuous measuring device 13d has an extremely simple external shape as shown in FIGS.
For this reason, there is a high degree of freedom in installation in, for example, a continuous pickling facility.

【0040】(vi)酸濃度連続測定装置13d の内部は、図
2に示すように、簡単な内部構造を有する。このため、
循環流路18d を流れる酸洗液の流速を、密度計20d 、温
度計21d および導電率計22d の測定精度の観点から望ま
しい流速である2m/sec 以下に、容易に設定・管理する
ことができる。したがって、酸濃度連続測定装置13d
は、測定精度の維持が容易である。
(Vi) The inside of the continuous acid concentration measuring device 13d has a simple internal structure as shown in FIG. For this reason,
The flow rate of the pickling liquid flowing through the circulation channel 18d can be easily set and controlled to be 2 m / sec or less, which is a desirable flow rate from the viewpoint of the measurement accuracy of the density meter 20d, the thermometer 21d, and the conductivity meter 22d. . Therefore, the acid concentration continuous measurement device 13d
Is easy to maintain the measurement accuracy.

【0041】(vii) 酸濃度連続測定装置13d は簡単な構
造であるため、酸洗槽の近傍に容易に設置することがで
きる。このため、酸洗槽から酸洗液を分流させる循環流
路18dを構成する配管の長さを可及的短くすることがで
きる。これにより、酸洗液が酸洗槽を出てから酸濃度連
続測定装置13d に到達して測定されるまでの間のタイム
ロスを可及的短縮することができる。このため、酸濃度
連続測定装置13d は、制御精度の低下を抑制できる。
(Vii) Since the acid concentration continuous measuring device 13d has a simple structure, it can be easily installed near the pickling tank. For this reason, the length of the pipe constituting the circulation flow path 18d for diverting the pickling solution from the pickling tank can be shortened as much as possible. As a result, the time loss between the time when the pickling solution leaves the pickling tank and the time when it reaches the acid concentration continuous measuring device 13d and is measured can be reduced as much as possible. For this reason, the acid concentration continuous measurement device 13d can suppress a decrease in control accuracy.

【0042】なお、本実施形態では、第3槽11c および
最終槽11d にそれぞれ酸濃度連続測定装置13c 、13d を
設けたが、図1に図示するように、第2槽11b にも酸濃
度連続測定装置13b を設け、さらに必要に応じて第1槽
11a にも酸濃度連続測定装置13a を設け、これらの出力
値も制御装置14に入力するように構成してもよい。本実
施形態の酸濃度連続測定装置13c 、13d は、以上のよう
に構成される。
In this embodiment, the continuous acid concentration measuring devices 13c and 13d are provided in the third tank 11c and the final tank 11d, respectively. However, as shown in FIG. A measuring device 13b is provided, and if necessary, a first tank
A continuous acid concentration measuring device 13a may be provided in 11a, and these output values may also be input to the control device 14. The continuous acid concentration measuring devices 13c and 13d of the present embodiment are configured as described above.

【0043】〔制御装置14〕本実施形態の連続酸洗装置
10は、制御装置14を有する。この制御装置14は、第3槽
11c に収容された酸洗液の酸洗時における酸消費量と、
最終槽11d に収容された酸洗液の酸洗時における酸消費
量とを、いずれも、近似式を用いて算出する。第3槽11
c および最終槽11d それぞれにおける酸消費量の予測計
算は、酸洗ライン制御装置24から入力される、鋼帯15の
材質や寸法、通板速度、酸液組成、酸液温度さらには各
槽の寸法等といった酸洗時の酸洗条件に基づいて行われ
るが、特定の手段には限定されない。公知の手段により
予測計算を行えばよい。
[Control unit 14] Continuous pickling apparatus of this embodiment
10 has a control device 14. This control device 14 is a third tank
Acid consumption during pickling of the pickling solution contained in 11c,
The acid consumption of the pickling solution contained in the final tank 11d during pickling is calculated using an approximate expression. Third tank 11
The prediction calculation of the acid consumption in each of c and the final tank 11d is based on the material and dimensions of the steel strip 15, the passing speed, the acid solution composition, the acid solution temperature, and the It is performed based on pickling conditions at the time of pickling, such as dimensions, but is not limited to a specific means. The prediction calculation may be performed by a known means.

【0044】例えば、単位面積当たりの減少量(本明細
書では「酸洗減量値」という。)を時間に対して1次式
を用いて近似する場合、酸洗時間と酸洗減量値との関係
は比例関係になる。図3は、この関係の一例を示すグラ
フである。
For example, when the amount of reduction per unit area (hereinafter, referred to as “pickling weight loss value”) is approximated by a linear equation with respect to time, the pickling time and the pickling weight loss value are calculated. The relationship is proportional. FIG. 3 is a graph showing an example of this relationship.

【0045】図3にグラフで示すように、酸洗時間と酸
洗減量値との関係は、原点Oを起点とする直線関係とな
る。すなわち、第1槽11a を通過する時刻t1における酸
洗減量値m1、第2槽11b を通過する時刻t2における酸洗
減量値m2、第3槽11c を通過する時刻t3における酸洗減
量値m3、および最終槽11d を通過する時刻t4における酸
洗減量値m4は、いずれも、同一の直線上に位置し、酸洗
が完了した時刻t4以降は酸洗減量値が一定となる。この
直線の傾きが酸洗速度を示し、酸洗される鋼帯15の材質
や、酸洗条件 (酸洗液の温度や組成等) により規定され
る。
As shown in the graph of FIG. 3, the relationship between the pickling time and the pickling weight loss value is a linear relationship starting from the origin O. That is, the pickling weight loss value m 1 at the time t 1 passing through the first tank 11 a, the pickling weight loss value m 2 at the time t 2 passing through the second tank 11 b, and the acid value at the time t 3 passing through the third tank 11 c. Both the washing loss value m 3 and the pickling loss value m 4 at time t 4 when passing through the final tank 11 d are on the same straight line, and after the time t 4 at which the pickling is completed, the pickling weight loss value Becomes constant. The slope of this straight line indicates the pickling speed, and is defined by the material of the steel strip 15 to be pickled and the pickling conditions (temperature, composition, etc. of the pickling solution).

【0046】したがって、各酸洗槽11a 〜11d における
酸消費量は、各酸洗槽11a 〜11d それぞれを通過するの
に要した時間と、図3のグラフの直線の傾きと、鋼帯15
の寸法 (幅) とを掛け合わせた値として、求められる。
このようにして、各酸洗槽11a 〜11d それぞれにおける
酸洗液の消費量を算出することができる。なお、本実施
形態のように、酸洗時間と酸洗減量値との関係を直線で
近似するのではなく、図3に一点鎖線で示すように、実
際の酸洗曲線に近いS字状曲線により近似すれば、より
高精度に各酸洗槽11a 〜11d における酸消費量を算出す
ることができる。
Therefore, the amount of acid consumed in each of the pickling tanks 11a to 11d depends on the time required to pass through each of the pickling tanks 11a to 11d, the slope of the straight line in the graph of FIG.
It is obtained as a value multiplied by the dimension (width) of
In this way, the consumption of the pickling solution in each of the pickling tanks 11a to 11d can be calculated. Note that, as in the present embodiment, the relationship between the pickling time and the pickling weight loss value is not approximated by a straight line, but as shown by a dashed line in FIG. 3, an S-shaped curve close to the actual pickling curve is used. By approximation, the acid consumption in each of the pickling tanks 11a to 11d can be calculated with higher accuracy.

【0047】また、制御装置14は、このようにして算出
した第3槽11c および最終槽11d それぞれにおける酸消
費量の予測値に基づいて、第3槽11c および最終槽11d
それぞれへの酸液供給量を決定する。そして、制御装置
14は、酸液供給系12のダイヤフラム弁16へ酸液供給信号
を出力して、必要供給量の酸液を、第3槽11c および最
終槽11d それぞれへ供給する。
Further, the controller 14 controls the third tank 11c and the final tank 11d based on the predicted values of the acid consumption in the third tank 11c and the final tank 11d calculated in this way.
The supply amount of the acid solution to each is determined. And the control device
The unit 14 outputs an acid solution supply signal to the diaphragm valve 16 of the acid solution supply system 12 to supply a required amount of the acid solution to each of the third tank 11c and the final tank 11d.

【0048】さらに、制御装置14は、第3槽酸液供給装
置12c から第3槽11c へ酸液を供給するとともに最終槽
酸液供給装置12d から最終槽11d へ酸液を供給した後
に、酸濃度連続測定装置13c 、13d から出力される酸濃
度の連続的な測定値に基づいて、酸液供給系12へ酸液供
給信号を再度出力して、第3槽11c および最終槽11d に
それぞれ収容された酸洗液の酸濃度が目標値に一致する
ように、微調整する。
Further, the control device 14 supplies the acid solution from the third tank acid solution supply device 12c to the third tank 11c and supplies the acid solution from the final tank acid solution supply device 12d to the final tank 11d. An acid solution supply signal is output again to the acid solution supply system 12 based on the continuous measurement of the acid concentration output from the concentration measuring devices 13c and 13d, and the acid solution is stored in the third tank 11c and the final tank 11d, respectively. Fine adjustment is made so that the acid concentration of the pickled solution matches the target value.

【0049】本実施形態の制御装置14は、以上のように
構成される。次に、4つの酸洗槽11a 〜11d と、酸液供
給系12と、酸濃度連続測定装置13c、13d と、制御装置1
4とを備える本実施形態の連続酸洗装置10により、鋼帯1
5に酸洗を行う状況を経時的に説明する。
The control device 14 of this embodiment is configured as described above. Next, four pickling tanks 11a to 11d, an acid solution supply system 12, an acid concentration continuous measuring devices 13c and 13d, and a control device 1
4 and the continuous pickling apparatus 10 of the present embodiment,
The situation of pickling is described with reference to FIG.

【0050】〔酸消費量の予測計算〕図1に示す連続酸
洗装置10により、鋼帯15に酸洗が行われている。ここ
で、制御装置14により、第3槽11c および最終槽11d に
それぞれ収容された酸洗液の酸消費量の予測値が、酸洗
ライン制御装置24から入力される前述した酸洗条件に基
づいて、算出される。
[Estimation Calculation of Acid Consumption] Pickling is performed on the steel strip 15 by the continuous pickling apparatus 10 shown in FIG. Here, the controller 14 calculates the predicted value of the acid consumption of the pickling liquid stored in the third tank 11c and the final tank 11d based on the aforementioned pickling conditions input from the pickling line controller 24. Is calculated.

【0051】ここで、予測計算の種類にかかわらず、こ
の算出値には、必ず実際の酸消費量に対する誤差が存在
する。そこで、本実施形態では、後述するように、酸濃
度の連続的な測定値を用いて酸液の供給量を制御するこ
とにより、この誤差を可及的に低減する。
Here, regardless of the type of prediction calculation, the calculated value always has an error with respect to the actual acid consumption. Therefore, in the present embodiment, as will be described later, the error is reduced as much as possible by controlling the supply amount of the acid solution using a continuous measurement value of the acid concentration.

【0052】〔算出値に基づく酸液の供給〕次に、制御
装置14により、このようにして予測した第3槽11c およ
び最終槽11d にそれぞれ収容された酸洗液の酸消費量に
基づいて、第3槽11c および最終槽11d それぞれへの酸
液供給量が決定される。
[Supply of Acid Solution Based on Calculated Value] Next, the controller 14 calculates the acid consumption of the pickling solution contained in the third tank 11c and the final tank 11d, respectively, as predicted in this manner. The supply amount of the acid solution to each of the third tank 11c and the final tank 11d is determined.

【0053】そして、制御装置14から、第3槽酸液供給
系12c および最終槽酸液供給系12dそれぞれのダイヤフ
ラム弁16、16へ酸液供給信号が出力され、第3槽11c お
よび最終槽11d それぞれへ、決定された供給量の酸液が
供給される。
Then, the controller 14 outputs an acid solution supply signal to the diaphragm valves 16 and 16 of the third tank acid solution supply system 12c and the final tank acid solution supply system 12d, respectively. Each of them is supplied with the determined supply amount of the acid solution.

【0054】〔酸濃度の連続測定〕このようにして、第
3槽11c および最終槽11d それぞれへ、決定された供給
量の酸液が供給された後に、酸濃度連続測定装置13c に
より第3槽11c に収容された酸洗液の酸濃度が連続的に
測定されるとともに、酸濃度連続測定装置13d により最
終槽11d に収容された酸洗液の酸濃度が連続的に測定さ
れる。これらの連続的な測定値は、制御装置14に送られ
る。
[Continuous Measurement of Acid Concentration] After the determined supply amount of the acid solution is supplied to each of the third tank 11c and the final tank 11d, the third tank 11c is continuously measured by the acid concentration continuous measuring apparatus 13c. The acid concentration of the pickling liquid stored in the final tank 11d is continuously measured by the acid concentration continuous measuring device 13d while the acid concentration of the pickling liquid stored in the pickling liquid 11c is continuously measured. These continuous measurements are sent to the controller 14.

【0055】〔連続測定結果に基づく酸液の供給〕制御
装置14では、これらの連続的な測定値と、第3槽11c お
よび最終槽11d にそれぞれ収容された酸洗液の酸濃度の
目標値との偏差が求められる。そして、この偏差が零に
なるように、制御装置14から第3槽酸液供給系12c およ
び最終槽酸液供給系12d それぞれのダイヤフラム弁16、
16へ酸液供給信号が出力され、第3槽11c および最終槽
11d それぞれに対する酸液の供給量が制御される。
[Supply of Acid Solution Based on Continuous Measurement Results] In the control device 14, these continuous measurement values and the target value of the acid concentration of the pickling solution stored in the third tank 11c and the final tank 11d, respectively. Is determined. Then, the control device 14 controls the diaphragm valves 16 of the third tank acid solution supply system 12c and the final tank acid solution supply system 12d so that this deviation becomes zero.
An acid solution supply signal is output to 16 and the third tank 11c and the final tank
11d The supply amount of the acid solution for each is controlled.

【0056】これにより、第3槽11c および最終槽11d
それぞれへの酸液供給量の予測計算結果が有する誤差が
補正され、第3槽11c および最終槽11d のみならず、第
2槽11b に収容された酸洗液の酸濃度を、目標値に迅速
かつ正確に近づけることができる。
Thus, the third tank 11c and the final tank 11d
The error in the prediction calculation result of the supply amount of the acid solution to each is corrected, and the acid concentration of the pickling solution contained in the second tank 11b as well as the third tank 11c and the final tank 11d is quickly adjusted to the target value. And it can be approached accurately.

【0057】本実施形態において、最終槽11d だけでな
く第3槽11c にも酸液を供給するのは、このように、第
3槽11c や第2槽11b にそれぞれ収容された酸洗液の酸
濃度を高め、目標値に近づけるためである。したがっ
て、第4槽が最終槽11d となる本実施形態では、最終槽
11d および第3槽11c に酸液を供給したが、例えば第5
槽が最終槽となる連続酸洗装置の場合には、最終槽およ
び第3槽それぞれに酸液を供給することが望ましい。
In the present embodiment, the acid solution is supplied not only to the final tank 11d but also to the third tank 11c, as described above, because the pickling liquid contained in the third tank 11c and the second tank 11b is supplied. This is for increasing the acid concentration to approach the target value. Therefore, in this embodiment in which the fourth tank is the final tank 11d, the final tank
The acid solution was supplied to the tank 11d and the third tank 11c.
In the case of a continuous pickling apparatus in which the tank is the final tank, it is desirable to supply an acid solution to each of the final tank and the third tank.

【0058】本実施形態では、連続測定結果に基づく酸
液の供給を、最終槽11d だけでなく第3槽11c に対して
も行うため、最終槽11d に収容された酸洗液の酸濃度を
12%超に上昇させることなく、第3槽11c に収容された
酸洗液の酸濃度を高めて目標値に近づけることができ
る。このため、最終槽11d からの酸洗液の蒸発を防止し
ながら、第3槽11c に収容された酸洗液の酸濃度を高め
て目標値に近づけることができる。このため、各酸洗槽
11a 〜11d それぞれの酸洗能力をいずれも充分に発揮さ
せて、鋼帯15の酸洗を行うことができる。したがって、
本実施形態によれば、連続酸洗装置10の全体の生産性を
向上することができる。
In this embodiment, the supply of the acid solution based on the result of the continuous measurement is performed not only in the final tank 11d but also in the third tank 11c.
The acid concentration of the pickling liquid contained in the third tank 11c can be increased to approach the target value without increasing to more than 12%. For this reason, the acid concentration of the pickling liquid contained in the third tank 11c can be increased to approach the target value while preventing the pickling liquid from evaporating from the final tank 11d. For this reason, each pickling tank
Pickling of the steel strip 15 can be performed by fully exhibiting each of the pickling abilities of 11a to 11d. Therefore,
According to the present embodiment, the overall productivity of the continuous pickling apparatus 10 can be improved.

【0059】また、本実施形態は、既存の連続酸洗装置
の第3槽11c および最終槽11d の近傍に酸濃度連続測定
装置13c 、13d を設け、これらの酸濃度連続測定装置13
c 、13d からの出力信号を制御装置14へ送るとともに、
制御装置14のソフトを一部変更するだけで、実施するこ
とができる。このため、既存の連続酸洗設備をできるだ
け改造せずに実施できる。このように、本実施形態によ
れば、従来の生産設備を大幅に改良することなく、不良
率の低減と生産性の向上とをともに図ることができる。
In this embodiment, the continuous acid concentration measuring devices 13c and 13d are provided in the vicinity of the third tank 11c and the final tank 11d of the existing continuous pickling device.
The output signals from c and 13d are sent to the controller 14,
The present invention can be implemented by only partially changing the software of the control device 14. For this reason, the existing continuous pickling equipment can be implemented as little as possible. As described above, according to the present embodiment, it is possible to reduce both the defect rate and improve the productivity without significantly improving the conventional production equipment.

【0060】[0060]

【実施例】さらに、本発明を実施例を参照しながら、よ
り具体的に説明する。図1に示す連続酸洗装置1 (各酸
洗槽13a 〜13d の容量:50m3、酸洗液の温度:90℃)を
用い、本発明にかかる連続酸洗方法と、比較例の連続酸
洗方法とを用いて、鋼帯15の酸洗を1ヵ月間行った。な
お、この型の連続酸洗装置を用いた酸洗では、通常、本
実施例における操業期間の1ヵ月間に、操業条件の様々
な変動が殆ど全て発生するため、本発明の有用性を評価
するには充分な期間である。
EXAMPLES The present invention will be described more specifically with reference to examples. Using the continuous pickling apparatus 1 shown in FIG. 1 (the capacity of each of the pickling tanks 13a to 13d: 50 m 3 , the temperature of the pickling liquid: 90 ° C.), the continuous pickling method according to the present invention and the continuous pickling Using the washing method, the steel strip 15 was pickled for one month. In the pickling using this type of continuous pickling apparatus, usually, almost all various changes in the operating conditions occur during one month of the operating period in the present embodiment, so that the usefulness of the present invention is evaluated. That's enough time to do it.

【0061】本発明例は、制御装置14により、鋼帯15の
材質および酸洗条件 (酸洗液の温度および酸濃度) を用
い、鋼種毎に予め求めた1次近似式に基づいて、第3槽
11cおよび最終槽11d それぞれに収容された酸洗液の消
費量を予測計算し、この結果により第3槽11c および最
終槽11d それぞれに給酸を行うとともに、この給酸後
に、酸濃度連続測定装置13c 、13d からの連続測定値に
基づいて、第3槽11c および最終槽11d それぞれに収容
された酸洗液の酸濃度がいずれも12±0.5 %になるよう
に、第3槽酸液供給系12c および最終槽酸液供給系12d
それぞれのダイヤフラム弁16、16を、いずれもオン/オ
フ制御した。
In the example of the present invention, the controller 14 uses the material of the steel strip 15 and the pickling conditions (the temperature and the acid concentration of the pickling solution) based on a first-order approximation formula previously determined for each steel type. 3 tanks
The consumption of the pickling liquid contained in each of the final tank 11c and the final tank 11d is estimated and calculated, and based on the result, the third tank 11c and the final tank 11d are each supplied with an acid. On the basis of the continuous measurement values from 13c and 13d, the third tank acid solution supply system is set so that the acid concentration of the pickling liquid contained in each of the third tank 11c and the final tank 11d is 12 ± 0.5%. 12c and final tank acid solution supply system 12d
Each of the diaphragm valves 16, 16 was on / off controlled.

【0062】一方、比較例は、最終槽11d のみに給酸を
行い、給酸によりオーバーフローした酸液を第3槽11c
、第2槽11b へ順次輸送し、第1槽11c から廃酸を行
うとともに、最終槽11d に収容された酸洗液の酸濃度が
12±0.5 %になるように、最終槽酸液供給系12d のダイ
ヤフラム弁16を、オン/オフ制御した。
On the other hand, in the comparative example, the acid was supplied only to the final tank 11d, and the acid solution overflowed by the supply was supplied to the third tank 11c.
, And sequentially transported to the second tank 11b, and the waste acid is removed from the first tank 11c, and the acid concentration of the pickling liquid contained in the final tank 11d is reduced.
The on / off control of the diaphragm valve 16 of the final tank acid solution supply system 12d was controlled to 12 ± 0.5%.

【0063】なお、本発明例および比較例ともに、オペ
レータの判断により脱スケール不良が発生しない程度に
通板速度を高めて、酸洗を行った。そして、第2槽11b
〜最終槽11d にそれぞれ収容された酸洗液の酸濃度の変
化幅と、脱スケール不良発生率および生産性を測定し
た。結果を表1にまとめて示す。
In both the present invention example and the comparative example, pickling was performed by increasing the sheet passing speed to such an extent that no descaling failure was generated by the judgment of the operator. And the second tank 11b
-The range of change in the acid concentration of the pickling solution contained in each of the final tanks 11d, the rate of descaling failure occurrence, and the productivity were measured. The results are summarized in Table 1.

【0064】[0064]

【表1】 [Table 1]

【0065】表1から明らかなように、本発明例によ
り、各酸洗槽11a 〜11d にそれぞれ収容された酸洗液の
酸濃度が、目標値を超えない範囲で高まるとともに安定
化した。これにより、脱スケール不良発生率が大幅に低
減され、かつ生産性も顕著に向上した。
As is clear from Table 1, according to the present invention, the acid concentration of the pickling liquid contained in each of the pickling tanks 11a to 11d was increased and stabilized within a range not exceeding the target value. Thereby, the descaling defect occurrence rate was significantly reduced, and the productivity was also significantly improved.

【0066】(変形形態)実施形態および実施例の説明
では、4槽の酸洗槽を備える連続酸洗装置を用いた。し
かし、本発明は、この形態には限定されず、複数の酸洗
槽を備える連続酸洗装置に対して同様に適用される。
(Modification) In the description of the embodiment and the examples, a continuous pickling apparatus having four pickling tanks was used. However, the present invention is not limited to this form, and is similarly applied to a continuous pickling apparatus having a plurality of pickling tanks.

【0067】また、実施形態および実施例の説明では、
第3槽および最終槽に収容された酸洗液の酸消費量を予
測し、これらの酸洗槽に酸液を供給する場合を例にとっ
た。しかし、本発明は、この形態には限定されず、第3
槽および最終槽以外の他の酸洗槽に収容された酸洗液の
酸消費量も予測し、これらの酸洗槽にも酸液を供給する
ようにしてもよい。これにより、各酸洗槽に収容された
酸洗液の酸濃度を、さらに高精度で制御することができ
る。
In the description of the embodiments and examples,
The case where the acid consumption of the pickling liquid stored in the third tank and the final tank is predicted and an acid liquid is supplied to these pickling tanks is taken as an example. However, the present invention is not limited to this mode.
The acid consumption of the pickling liquid contained in the pickling tanks other than the tank and the last tank may also be predicted, and the pickling tank may be supplied with the acid solution. Thereby, the acid concentration of the pickling liquid contained in each pickling tank can be controlled with higher accuracy.

【0068】また、実施形態および実施例の説明では、
図2に示す酸濃度連続測定装置を用いた場合を例にとっ
た。しかし、これはあくまでも酸濃度連続測定装置の例
示であり、本発明は図2に示す酸濃度連続測定装置には
限定されない。本発明は、図2に示す酸濃度連続測定装
置以外でも、酸洗槽にそれぞれ収容された酸洗液の酸濃
度を連続的に測定することができる酸濃度連続測定装置
であれば、同様に適用することができる。
In the description of the embodiments and examples,
The case where the acid concentration continuous measurement device shown in FIG. 2 was used was taken as an example. However, this is merely an example of the acid concentration continuous measurement device, and the present invention is not limited to the acid concentration continuous measurement device shown in FIG. The present invention is not limited to the acid concentration continuous measuring device shown in FIG. 2, but may be any acid concentration continuous measuring device capable of continuously measuring the acid concentration of the pickling solution contained in the pickling tank. Can be applied.

【0069】また、実施形態および実施例の説明では、
少なくとも最終槽に酸液を供給される連続酸洗装置を用
いた。しかし、本発明は、この形態には限定されず、最
終槽には酸液を供給されない連続酸洗装置にも対して
も、同様に適用される。
In the description of the embodiments and examples,
A continuous pickling apparatus in which an acid solution was supplied to at least the final tank was used. However, the present invention is not limited to this mode, and is similarly applied to a continuous pickling apparatus in which an acid solution is not supplied to the final tank.

【0070】また、実施形態および実施例の説明では、
下流側の酸洗槽に収容された酸洗液を上流側に隣接する
酸洗槽へ順次オーバーフローさせる型の連続酸洗装置を
用いた。しかし、本発明は、この形態には限定されず、
複数の酸洗槽を有する連続酸洗装置であれば同様に適用
される。例えば、図4に示すように、下流側の酸洗槽に
収容された酸洗液を上流側に隣接する酸洗槽へ順次輸送
する型の連続酸洗装置に対しても、同様に適用される。
In the description of the embodiments and examples,
A continuous pickling apparatus of a type in which the pickling solution contained in the pickling tank on the downstream side was sequentially overflowed to the pickling tank adjacent on the upstream side was used. However, the invention is not limited to this form,
The same applies to a continuous pickling apparatus having a plurality of pickling tanks. For example, as shown in FIG. 4, the present invention is similarly applied to a continuous pickling apparatus of a type in which a pickling liquid contained in a downstream pickling tank is sequentially transported to an adjacent pickling tank on the upstream side. You.

【0071】さらに、実施形態および実施例の説明で
は、酸液が塩酸である場合を例にとった。しかし、本発
明は、この形態には限定されず、例えば硫酸等の、鋼板
に酸洗処理を行うことはできる酸液であれば、等しく適
用される。
Further, in the description of the embodiments and examples, the case where the acid solution is hydrochloric acid is taken as an example. However, the present invention is not limited to this form, and is equally applicable to any acid solution such as sulfuric acid that can perform a pickling treatment on a steel plate.

【0072】[0072]

【発明の効果】以上詳細に説明したように、本発明によ
り、各酸洗槽からの酸洗液の蒸発量をできるだけ抑制し
ながら、各酸洗槽に収容された酸洗液の酸濃度を、いず
れも高めて目標値に近づけることができ、これにより、
酸洗の生産性を向上することができる連続酸洗方法およ
び連続酸洗装置を、既存の連続酸洗設備をできるだけ改
造せずに、提供できることになった。かかる効果を有す
る本発明の意義は、極めて著しい。
As described above in detail, according to the present invention, the acid concentration of the pickling liquid contained in each pickling tank is reduced while the evaporation amount of the pickling liquid from each pickling tank is suppressed as much as possible. , Both of which can be raised to approach the target value,
It has become possible to provide a continuous pickling method and a continuous pickling apparatus capable of improving the productivity of pickling without modifying existing continuous pickling equipment as much as possible. The significance of the present invention having such an effect is extremely remarkable.

【図面の簡単な説明】[Brief description of the drawings]

【図1】実施形態の連続酸洗装置の構成を模式的に示す
説明図である。
FIG. 1 is an explanatory view schematically showing a configuration of a continuous pickling apparatus according to an embodiment.

【図2】実施形態の酸濃度連続測定装置の内部構造を示
す説明図である。
FIG. 2 is an explanatory diagram showing an internal structure of the continuous acid concentration measuring device of the embodiment.

【図3】酸洗時間と酸洗減量値との関係の一例を示すグ
ラフである。
FIG. 3 is a graph showing an example of the relationship between the pickling time and the pickling weight loss value.

【図4】4槽の酸洗槽を備える従来の連続酸洗装置を模
式的に示す説明図である。
FIG. 4 is an explanatory view schematically showing a conventional continuous pickling apparatus having four pickling tanks.

【符号の説明】[Explanation of symbols]

10 連続酸洗装置 11c 第3槽 11d 最終槽 12 酸液供給系 13c 、13d 酸濃度連続測定装置 14 制御装置 10 Continuous pickling equipment 11c Third tank 11d Final tank 12 Acid solution supply system 13c, 13d Acid concentration continuous measurement device 14 Controller

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 連続酸洗装置を構成する複数の酸洗槽の
うちの2以上の酸洗槽にそれぞれ収容された酸洗液の酸
洗時における酸消費量の予測値を、該酸洗時の酸洗条件
に基づいて算出し、 算出した前記予測値に基づいて前記2以上の酸洗槽それ
ぞれへの酸液供給量を決定して酸液を供給し、 該酸液を供給された前記2以上の酸洗槽にそれぞれ収容
される酸洗液の酸濃度を連続的に測定し、測定された前
記酸濃度の連続的な測定値に基づいて、前記2以上の酸
洗槽にそれぞれ収容された酸洗液の酸濃度がいずれも目
標値に一致するように、前記2以上の酸洗槽への酸液供
給量を制御することを特徴とする連続酸洗方法。
1. A pickling method according to claim 1, wherein the pickling solution contained in each of two or more of the plurality of pickling tanks constituting the continuous pickling apparatus is estimated at the time of pickling. The amount of the acid solution supplied to each of the two or more pickling tanks was determined based on the calculated predicted value, the acid solution was supplied, and the acid solution was supplied. The acid concentration of the pickling liquid contained in each of the two or more pickling tanks is continuously measured, and based on the continuous measurement values of the measured acid concentrations, A continuous pickling method characterized by controlling the amount of the acid solution supplied to the two or more pickling tanks so that the acid concentrations of the stored pickling solutions all coincide with target values.
【請求項2】 前記2以上の酸洗槽は、少なくとも最終
酸洗槽を含む請求項1に記載された連続酸洗方法。
2. The continuous pickling method according to claim 1, wherein the two or more pickling tanks include at least a final pickling tank.
【請求項3】 前記連続酸洗装置は、下流側の酸洗槽に
収容された酸洗液を上流側に隣接する酸洗槽へ順次オー
バーフローさせる型の連続酸洗装置、または下流側の酸
洗槽に収容された酸洗液を上流側に隣接する酸洗槽へ順
次輸送する型の連続酸洗装置である請求項1または請求
項2に記載された連続酸洗方法。
3. The continuous pickling apparatus according to claim 1, wherein the pickling liquid contained in the downstream pickling tank is successively overflowed to an adjacent pickling tank on the upstream side, or a downstream pickling apparatus. 3. The continuous pickling method according to claim 1, wherein the continuous pickling apparatus is a type of a continuous pickling apparatus that sequentially transports the pickling liquid contained in the washing tank to an adjacent pickling tank on the upstream side.
【請求項4】 前記酸濃度の連続的な測定値は、少なく
とも、前記2以上の酸洗槽にそれぞれ設けられた酸洗液
循環流路に配置された密度計からの連続的な出力値を用
いて、測定される請求項1から請求項3までのいずれか
1項に記載された連続酸洗方法。
4. The continuous measurement value of the acid concentration is at least a continuous output value from a densitometer disposed in a pickling liquid circulation channel provided in each of the two or more pickling tanks. The continuous pickling method according to any one of claims 1 to 3, wherein the method is used and measured.
【請求項5】 前記酸濃度の連続的な測定値は、前記酸
洗槽または前記酸洗液循環流路に配置された温度計およ
び導電率計それぞれからの連続的な出力値を用いて、測
定される請求項4に記載された連続酸洗方法。
5. The continuous measurement value of the acid concentration is obtained by using a continuous output value from each of a thermometer and a conductivity meter arranged in the pickling tank or the pickling liquid circulation channel, The continuous pickling method according to claim 4, which is measured.
【請求項6】 連続酸洗装置を構成する複数の酸洗槽の
うちの2以上の酸洗槽と、 前記2以上の酸洗槽へそれぞれ酸液を供給する酸液供給
系と、 前記2以上の酸洗槽にそれぞれ収容された酸洗液の酸濃
度をそれぞれ連続的に測定する酸濃度連続測定装置と、 前記2以上の酸洗槽にそれぞれ収容された酸洗液の酸洗
時における酸消費量の予測値を、該酸洗時の酸洗条件か
らそれぞれ算出し、算出した前記予測値に基づいて酸液
供給量を決定して前記酸液供給系へ酸液供給信号を出力
するとともに、該酸液供給系から前記2以上の酸洗槽へ
酸液が供給された後に前記酸濃度連続測定装置から出力
される前記酸濃度の連続的な測定値に基づいて、前記2
以上の酸洗槽にそれぞれ収容された酸洗液の酸濃度がい
ずれも目標値に一致するように、前記酸液供給系へ酸液
供給信号を出力する制御装置とを組み合わせて備えるこ
とを特徴とする連続酸洗装置。
6. An acid pickling tank constituting at least two of a plurality of pickling tanks constituting a continuous pickling apparatus; an acid liquid supply system for supplying an acid liquid to each of the two or more pickling tanks; An acid concentration continuous measuring device for continuously measuring the acid concentration of the pickling liquid contained in each of the above pickling tanks; and at the time of pickling the pickling liquid contained in each of the two or more pickling tanks. A predicted value of the acid consumption is calculated from the pickling conditions at the time of the pickling, an acid solution supply amount is determined based on the calculated predicted value, and an acid solution supply signal is output to the acid solution supply system. In addition, based on a continuous measurement of the acid concentration output from the acid concentration continuous measuring device after the acid solution is supplied from the acid solution supply system to the two or more pickling tanks,
A control device for outputting an acid solution supply signal to the acid solution supply system is provided in such a manner that the acid concentration of each of the acid solutions contained in the above-mentioned acid tanks coincides with the target value. And continuous pickling equipment.
【請求項7】 前記2以上の酸洗槽は、少なくとも最終
酸洗槽を含む請求項6に記載された連続酸洗装置。
7. The continuous pickling apparatus according to claim 6, wherein the two or more pickling tanks include at least a final pickling tank.
【請求項8】 前記連続酸洗装置は、下流側の酸洗槽に
収容された酸洗液を上流側に隣接する酸洗槽へ順次オー
バーフローさせる型の連続酸洗装置、または下流側の酸
洗槽に収容された酸洗液を上流側に隣接する酸洗槽へ順
次輸送する型の連続酸洗装置である請求項6または請求
項7に記載された連続酸洗装置。
8. The continuous pickling apparatus according to claim 1, wherein the pickling liquid contained in the downstream pickling tank is sequentially overflowed to the pickling tank adjacent to the upstream side, or a downstream pickling apparatus. The continuous pickling apparatus according to claim 6 or 7, wherein the continuous pickling apparatus is of a type in which the pickling liquid contained in the washing tank is sequentially transported to an adjacent pickling tank on the upstream side.
【請求項9】 前記酸濃度連続測定装置は、 前記酸洗槽に接続され、該酸洗槽から取り出された酸洗
液の流路の一部に設けられた本体と、 該本体の内部を流れる前記酸洗液の密度を測定する密度
計と、 前記流路または前記酸洗槽における酸洗液の温度を測定
する温度計と、 前記流路または前記酸洗槽における酸洗液の導電率を測
定する導電率計と、 前記密度、前記温度計および前記導電率計それぞれの測
定結果に基づいて前記流路の一部を流れる酸洗液の酸濃
度を演算する演算装置とを組み合わせて備える請求項6
から請求項8までのいずれか1項に記載された連続酸洗
装置。
9. The acid concentration continuous measuring device, comprising: a main body connected to the pickling tank and provided in a part of a flow path of a pickling liquid taken out of the pickling tank; A density meter for measuring the density of the flowing pickling liquid; a thermometer for measuring the temperature of the pickling liquid in the flow path or the pickling tank; and a conductivity of the pickling liquid in the flow path or the pickling tank. And a calculating device for calculating an acid concentration of a pickling liquid flowing through a part of the flow path based on the measurement results of the density, the thermometer, and the conductivity meter, respectively. Claim 6
The continuous pickling apparatus according to any one of claims 1 to 8.
JP10436699A 1999-04-12 1999-04-12 Continuous pickling method and continuous pickling apparatus Expired - Fee Related JP3591366B2 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002088426A1 (en) * 2001-04-27 2002-11-07 Sumitomo Metal Industries, Ltd. Continuous pickling method and continuous pickling device
FR2925530A1 (en) * 2007-12-21 2009-06-26 Siemens Vai Metals Tech Sas INSTALLATION AND METHOD FOR CONTINUOUS STRIPPING OF STEEL BANDS
KR101294945B1 (en) 2009-12-30 2013-08-08 주식회사 포스코 Method for continuously removing scale material
CN115044917A (en) * 2022-06-21 2022-09-13 北京首钢冷轧薄板有限公司 Method and device for determining pickling speed of hot-rolled strip steel

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002088426A1 (en) * 2001-04-27 2002-11-07 Sumitomo Metal Industries, Ltd. Continuous pickling method and continuous pickling device
FR2925530A1 (en) * 2007-12-21 2009-06-26 Siemens Vai Metals Tech Sas INSTALLATION AND METHOD FOR CONTINUOUS STRIPPING OF STEEL BANDS
WO2009098401A1 (en) * 2007-12-21 2009-08-13 Siemens Vai Metals Technologies Sas Apparatus and method for the continuous pickling of steel strip
RU2451772C2 (en) * 2007-12-21 2012-05-27 Сименс Фаи Металз Текнолоджиз Сас Apparatus and method for continuous steel strip etching
KR101227282B1 (en) 2007-12-21 2013-01-28 지멘스 바이 메탈스 테크놀로지 에스에이에스 Apparatus and method for the continuous pickling of steel strip
US8834636B2 (en) 2007-12-21 2014-09-16 Siemens Vai Metals Technologies Sas Apparatus and method for the continuous pickling of steel strip
KR101294945B1 (en) 2009-12-30 2013-08-08 주식회사 포스코 Method for continuously removing scale material
CN115044917A (en) * 2022-06-21 2022-09-13 北京首钢冷轧薄板有限公司 Method and device for determining pickling speed of hot-rolled strip steel
CN115044917B (en) * 2022-06-21 2023-10-03 北京首钢冷轧薄板有限公司 Method and device for determining pickling speed of hot rolled strip steel

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