JP6052208B2 - Steel strip continuous pickling apparatus and steel strip manufacturing method - Google Patents

Steel strip continuous pickling apparatus and steel strip manufacturing method Download PDF

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JP6052208B2
JP6052208B2 JP2014043845A JP2014043845A JP6052208B2 JP 6052208 B2 JP6052208 B2 JP 6052208B2 JP 2014043845 A JP2014043845 A JP 2014043845A JP 2014043845 A JP2014043845 A JP 2014043845A JP 6052208 B2 JP6052208 B2 JP 6052208B2
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steel strip
heat exchanger
pickling
dam
acid solution
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JP2015168843A (en
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雅史 森枝
雅史 森枝
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JFE Steel Corp
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Description

本発明は、鋼帯を連続的に酸洗する連続式酸洗装置に関するものである。   The present invention relates to a continuous pickling apparatus for continuously pickling steel strips.

冷間圧延鋼板や珪素鋼板などの鋼帯の表面スケールを除去するために、鋼帯を連続的に酸洗する連続式酸洗装置が用いられている。   In order to remove the surface scale of a steel strip such as a cold rolled steel plate or a silicon steel plate, a continuous pickling apparatus for continuously pickling the steel strip is used.

図6は、その続式酸洗装置の基本的な構成を示すものである。図6に示すように、連続式酸洗装置10は、酸洗液(酸液)2が満たされた酸洗槽6を備えており、酸洗槽6は複数のダム1により鋼帯3の進行方向d1に分割されている(ここでは、酸洗槽6a、6b、6c、6dの4個に分割)。そして、酸洗によって消耗した酸液2を補給するために、ダム1の高さを鋼帯進行方向d1に向かって順に高くし、酸液を鋼帯進行方向d1とは逆に、鋼帯3の出口側から順次各ダム1をオーバーフローさせて鋼帯進行方向d1上流側の酸洗槽に供給している(ここでは、酸洗槽6d→6c→6b→6aの順)。   FIG. 6 shows the basic structure of the continuous pickling apparatus. As shown in FIG. 6, the continuous pickling apparatus 10 includes a pickling tank 6 filled with a pickling solution (acid solution) 2, and the pickling tank 6 is formed of a steel strip 3 by a plurality of dams 1. It is divided in the traveling direction d1 (here, divided into four pickling tanks 6a, 6b, 6c, 6d). Then, in order to replenish the acid solution 2 consumed by pickling, the height of the dam 1 is increased in order toward the steel strip traveling direction d1, and the acid solution is opposite to the steel strip traveling direction d1, and the steel strip 3 Each dam 1 is sequentially overflowed from the outlet side of the steel plate and supplied to the pickling tank upstream of the steel strip traveling direction d1 (here, pickling tank 6d → 6c → 6b → 6a).

このような連続式酸洗装置10においては、通常、酸液2として、硫酸、塩酸などの希釈液が用いられ、酸洗効率を上げるために、その温度を80〜90℃程度に保っている。   In such a continuous pickling apparatus 10, a dilute solution such as sulfuric acid or hydrochloric acid is usually used as the acid solution 2, and the temperature is maintained at about 80 to 90 ° C. in order to increase the pickling efficiency. .

そして、酸液2を昇温保持するために、図3に示すように、蒸気パイプ7により直接蒸気を酸液2中に投入したり、図4、図5に示すように、蒸気を用いた側面設置型の熱交換器8もしくは底面設置型の熱交換器5を設置したりしている(例えば、特許文献1、特許文献2)。   In order to maintain the temperature of the acid solution 2 at a high temperature, as shown in FIG. 3, the steam is directly injected into the acid solution 2 through the steam pipe 7, or the steam is used as shown in FIGS. A side-mounted heat exchanger 8 or a bottom-mounted heat exchanger 5 is installed (for example, Patent Document 1 and Patent Document 2).

なお、図5に示した底面設置型熱交換器5においては、鋼帯3と側面設置型熱交換器5の接触を防止するために、上端が底面設置型熱交換器5の上端より高くかつ酸液2の液面より低い保護ダム9を設置している。   In the bottom surface installation type heat exchanger 5 shown in FIG. 5, the upper end is higher than the upper end of the bottom surface installation type heat exchanger 5 in order to prevent contact between the steel strip 3 and the side surface installation type heat exchanger 5. A protective dam 9 lower than the level of the acid solution 2 is installed.

ただし、図3に示した蒸気パイプ7による方法は、蒸気を直接酸液2中に投入するため、図4、図5に示した側面設置型熱交換器8や底面設置型熱交換器5に比べて廃液が増加するという欠点がある。   However, in the method using the steam pipe 7 shown in FIG. 3, since the steam is directly put into the acid solution 2, the side-mounted heat exchanger 8 and the bottom-mounted heat exchanger 5 shown in FIGS. 4 and 5 are used. There is a drawback that the amount of waste liquid increases.

また、図4に示した側面設置型熱交換器8は、耐酸性の樹脂チューブなどを用いて熱交換を行うため廃液の増加は無いが、酸洗槽6の側面からの張り出し寸法が蒸気パイプでは80mm程度で有るのに比べ250mm程度が必要であり、鋼帯3の蛇行などによって熱交換器8を破損する事故が多く発生し、維持管理に多大の費用を要すると共に操業に悪影響を与えている。   The side-mounted heat exchanger 8 shown in FIG. 4 performs heat exchange using an acid-resistant resin tube or the like, so that there is no increase in waste liquid, but the overhang dimension from the side surface of the pickling tank 6 is a steam pipe. In this case, about 250 mm is required compared to about 80 mm, and many accidents that damage the heat exchanger 8 due to the meandering of the steel strip 3 occur, which requires a large expense for maintenance and adversely affects the operation. Yes.

これに対して、図5に示した底面設置型熱交換器5は、酸洗槽6の側面には酸洗槽6の底面に位置する底面設置型熱交換器5へ蒸気を導くチューブを配するのみであるので、酸洗槽6の側面からの張り出し寸法は蒸気パイプ7と同等の80mm程度とすることができるため、鋼帯3の蛇行による熱交換器5の破損が発生しにくい。   On the other hand, in the bottom surface installation type heat exchanger 5 shown in FIG. 5, a tube for introducing steam to the bottom surface installation type heat exchanger 5 located on the bottom surface of the pickling tank 6 is arranged on the side surface of the pickling tank 6. Therefore, since the overhang dimension from the side surface of the pickling tank 6 can be about 80 mm, which is the same as that of the steam pipe 7, the heat exchanger 5 is hardly damaged due to the meandering of the steel strip 3.

このように、図5に示した底面設置型熱交換器5を設置する方法は、図3に示した蒸気パイプ7により直接蒸気を投入する方法や図4に示した側面設置型熱交換器8を設置する方法に比べて優れている。   As described above, the method of installing the bottom surface installation type heat exchanger 5 shown in FIG. 5 includes the method of directly injecting steam through the steam pipe 7 shown in FIG. 3 and the side installation type heat exchanger 8 shown in FIG. It is superior to the method of installing.

しかし、底面設置型熱交換器5を設置する方法は、操業異常時等の鋼帯3の張力低下時に鋼帯3の高さ位置が下がることで底面設置型熱交換器5と接触する可能性がある。そのため、上述したように、上端が底面設置型熱交換器5の上端より高くかつ酸液2の液面より低い保護ダム9を設置して鋼帯3の接触を防いでいるが、鋼帯3の随伴流がダム1に衝突した際に発生する下方への酸液2の流れが保護ダム9により底面設置型熱交換器5周辺で滞り、酸洗により除去されたスケールが底面設置型熱交換器5に堆積して、底面設置型熱交換器5の性能が低下する等といった問題がある。   However, the method of installing the bottom surface installation type heat exchanger 5 is likely to come into contact with the bottom surface installation type heat exchanger 5 by lowering the height position of the steel strip 3 when the tension of the steel strip 3 is lowered when the operation is abnormal. There is. Therefore, as described above, the upper end of the protective dam 9 that is higher than the upper end of the bottom surface installed heat exchanger 5 and lower than the liquid level of the acid solution 2 is installed to prevent the steel strip 3 from contacting. The downward flow of the acid solution 2 generated when the accompanying flow collides with the dam 1 is stagnated around the bottom-mounted heat exchanger 5 by the protective dam 9, and the scale removed by pickling is the bottom-mounted heat exchange. There is a problem that it accumulates in the vessel 5 and the performance of the bottom-mounted heat exchanger 5 deteriorates.

これに対して、酸液の流れの滞留および熱交換器の損傷への対策として、特許文献3では、上端が酸液の液面より高くかつ開口部を備えた邪魔壁をダムの前に設け、その邪魔壁とダムの間に熱交換器を設置することによって、邪魔壁の開口部によって酸液の流れの滞留を回避しながら、邪魔壁により熱交換器と鋼帯の接触を防止するようにしている。   On the other hand, as a countermeasure against the stay of the acid liquid flow and damage to the heat exchanger, in Patent Document 3, a baffle wall having an upper end higher than the liquid surface of the acid liquid and having an opening is provided in front of the dam. By installing a heat exchanger between the baffle wall and the dam, the baffle wall prevents contact with the heat exchanger and the steel strip while avoiding stagnation of the flow of the acid solution by the opening of the baffle wall. I have to.

また、堆積したスケールによる熱交換器の性能低下等の対策として、特許文献4では、熱交換器に圧縮空気または酸液を吹き付けることによって、熱交換器に堆積したスケールを洗い流すようにしている。   In addition, as a countermeasure against the deterioration of the performance of the heat exchanger due to the accumulated scale, in Patent Document 4, the scale accumulated in the heat exchanger is washed away by spraying compressed air or acid solution on the heat exchanger.

実開昭61−102308号公報Japanese Utility Model Publication No. 61-102308 実開昭62−106965号公報Japanese Utility Model Publication No. 62-106965 実開昭64−37469号公報Japanese Utility Model Publication No. 64-37469 特開2003−213466号公報JP 2003-213466 A

上述したように、鋼帯の連続式酸洗装置において、酸洗槽の底面に熱交換器を設置し、その熱交換器と鋼帯が接触するのを防止すために保護ダムを設置した場合、その保護ダムにより熱交換器周辺の酸液の流れが滞り、酸洗により除去されたスケールが堆積するという問題がある。   As mentioned above, in a continuous pickling device for steel strip, when a heat exchanger is installed on the bottom of the pickling tank, and a protective dam is installed to prevent the heat exchanger from contacting the steel strip The protective dam causes a problem that the flow of the acid solution around the heat exchanger stagnates and the scale removed by pickling accumulates.

この対策として、特許文献3のように、上端が酸液の液面より高くかつ開口部を備えた邪魔壁をダムの前に設け、その邪魔壁とダムの間に熱交換器を設置することによって、酸液の流れの滞留を回避しながら、邪魔壁により熱交換器と鋼帯の接触を防止することや、特許文献4のように、熱交換器に圧縮空気や酸液を吹き付けることによって、熱交換器に付着したスケールを洗い流すことが考えられる。   As a countermeasure, as in Patent Document 3, a baffle wall whose upper end is higher than the level of the acid solution and has an opening is provided in front of the dam, and a heat exchanger is installed between the baffle wall and the dam. By preventing the stagnation of the flow of the acid solution while preventing contact between the heat exchanger and the steel strip by the baffle wall, or by blowing compressed air or acid solution on the heat exchanger as in Patent Document 4 It is conceivable to wash away the scale attached to the heat exchanger.

しかしながら、特許文献3のように、上端が酸液の液面より高い邪魔壁をダムの前に設けた場合、構造上、ダムの前で鋼帯が酸液中から露出するため、邪魔壁を設置しない場合に比べて鋼帯の酸液通過長さが減少し、酸洗効率が悪化するという問題がある。   However, as in Patent Document 3, when a baffle wall whose upper end is higher than the liquid surface of the acid solution is provided in front of the dam, the steel strip is exposed from the acid solution in front of the dam, so the baffle wall is Compared with the case where it is not installed, there is a problem that the acid solution passage length of the steel strip is reduced and the pickling efficiency is deteriorated.

また、特許文献4のように、熱交換器に圧縮空気や酸液を吹き付けた場合、圧縮空気分の原単位の悪化や鋼帯への気泡の付着による酸洗ムラの発生という問題や、吹き付け用ポンプなどが必要となり、設備の維持管理に多大な労力と費用がかかるという問題がある。   In addition, as in Patent Document 4, when compressed air or acid solution is sprayed on the heat exchanger, problems such as deterioration of the basic unit of compressed air or occurrence of pickling unevenness due to adhesion of bubbles to the steel strip, or spraying For example, there is a problem that a large amount of labor and cost are required for maintenance and management of equipment.

本発明は、上記のような事情に鑑みてなされたものであり、鋼帯の連続式酸洗装置において、酸洗槽の底面に熱交換器を設置した場合に、酸洗効率の悪化や設備維持管理の煩雑化を招くことなく、熱交換器と鋼帯の接触防止と熱交換器へのスケールの堆積抑止を効率的に行うことができる、鋼帯の連続式酸洗装置を提供することを目的とするものである。   The present invention has been made in view of the above circumstances, and in a steel strip continuous pickling apparatus, when a heat exchanger is installed on the bottom surface of the pickling tank, deterioration of pickling efficiency and equipment To provide a steel strip continuous pickling apparatus that can efficiently prevent contact between the heat exchanger and the steel strip and suppress the accumulation of scale on the heat exchanger without complicating maintenance. It is intended.

上記課題を解決するために、本発明は以下の特徴を有する。   In order to solve the above problems, the present invention has the following features.

[1]鋼帯を連続的に酸洗する連続式酸洗装置であって、ダムにより鋼帯進行方向に分割された酸洗槽と、前記酸洗槽の底面に設置された熱交換器と、前記ダムとで前記熱交換器を挟み込むように設置された保護ダムとを備え、
前記保護ダムは、上端が前記熱交換器の上端より高くかつ前記酸洗槽内の酸液の液面より低くなっているとともに、酸液が通過可能なスリットを有するスリット構造付き保護ダムであることを特徴とする鋼帯の連続式酸洗装置。
[1] A continuous pickling apparatus for continuously pickling steel strip, a pickling tank divided by a dam in the steel strip traveling direction, and a heat exchanger installed on the bottom surface of the pickling tank, A protective dam installed to sandwich the heat exchanger with the dam,
The protective dam is a protective dam with a slit structure having a slit whose upper end is higher than the upper end of the heat exchanger and lower than the level of the acid solution in the pickling tub and through which the acid solution can pass. A continuous pickling apparatus for steel strips.

[2]前記[1]に記載の鋼帯の連続式酸洗装置を用いて鋼帯を連続的に酸洗することにより、鋼帯を製造することを特徴とする鋼帯の製造方法。   [2] A method for producing a steel strip, comprising producing a steel strip by continuously pickling the steel strip using the continuous pickling apparatus for steel strip according to [1].

本発明では、鋼帯の連続式酸洗装置において、酸洗槽の底面に熱交換器を設置した場合に、前記熱交換器を保護する保護ダムとして、上端が前記熱交換器の上端より高くかつ前記酸洗槽内の酸液の液面より低くなっているとともに、酸液が通過可能なスリットを有するスリット構造付き保護ダムを備えるようにしているので、鋼帯が酸液中から露出することがほぼ無いため、操業異常時等の鋼帯の張力低下時に鋼帯の高さ位置が下った場合でも、酸洗効率の悪化を招くことなく、熱交換器と鋼帯の接触を防止できるとともに、鋼帯の随伴流がダムに衝突した際に発生する下方への酸液の流れがスリット内を通るため、ダムとで保護ダムで挟み込まれた熱交換器周辺の酸液の流れを速めることになり、設備維持管理の煩雑化を招くことなく、熱交換器へのスケールの堆積が抑止できる。   In the present invention, in the continuous pickling apparatus for steel strip, when a heat exchanger is installed on the bottom surface of the pickling tank, the upper end is higher than the upper end of the heat exchanger as a protective dam for protecting the heat exchanger. And since it is lower than the level of the acid solution in the pickling tank and a protective dam with a slit structure having a slit through which the acid solution can pass, the steel strip is exposed from the acid solution. Therefore, even if the height of the steel strip drops when the steel strip tension drops due to abnormal operation, contact between the heat exchanger and the steel strip can be prevented without deteriorating the pickling efficiency. At the same time, the downward flow of the acid solution generated when the accompanying flow of the steel strip collides with the dam passes through the slit, so the flow of the acid solution around the heat exchanger sandwiched between the protective dam and the dam is accelerated. As a result, heat is maintained without complicating equipment maintenance. Scale of the deposition of the exchanger can be suppressed.

すなわち、本発明によって、酸洗効率の悪化や設備維持管理の煩雑化を招くことなく、熱交換器と鋼帯の接触防止と熱交換器へのスケールの堆積抑止を効率的に行うことができる。   That is, according to the present invention, it is possible to efficiently prevent contact between the heat exchanger and the steel strip and suppress accumulation of scale on the heat exchanger without causing deterioration of pickling efficiency and complication of equipment maintenance management. .

本発明の一実施形態を示す側面図である。It is a side view which shows one Embodiment of this invention. 図1におけるA−A矢視断面図である。It is AA arrow sectional drawing in FIG. 従来技術を示す図である。It is a figure which shows a prior art. 従来技術を示す図である。It is a figure which shows a prior art. 従来技術を示す図である。It is a figure which shows a prior art. 鋼帯の連続式酸洗装置の基本的な構成を示す図である。It is a figure which shows the basic composition of the continuous pickling apparatus of a steel strip.

本発明一実施形態を図面に基づいて説明する。   An embodiment of the present invention will be described with reference to the drawings.

図1は、本発明一実施形態における鋼帯の連続式酸洗装置10Aを示す側面図であり、図2は、図1におけるA−A矢視断面図である。   FIG. 1 is a side view showing a steel strip continuous pickling apparatus 10A according to an embodiment of the present invention, and FIG. 2 is a cross-sectional view taken along line AA in FIG.

まず、本発明一実施形態における鋼帯の連続式酸洗装置10Aの基本的な構成は、前述した図6に示した連続式酸洗装置10と同様である。   First, the basic configuration of a steel strip continuous pickling apparatus 10A according to an embodiment of the present invention is the same as that of the continuous pickling apparatus 10 shown in FIG.

すなわち、この実施形態における連続式酸洗装置10Aは、酸洗液(酸液)2が満たされた酸洗槽6を備えており、酸洗槽6は複数のダム1により鋼帯3の進行方向d1に分割されている。そして、酸洗によって消耗した酸液2を補給するために、ダム1の高さを鋼帯進行方向d1に向かって順に高くし、酸液を鋼帯進行方向d1とは逆に、鋼帯3の出口側から順次各ダム1をオーバーフローさせて、鋼帯進行方向d1上流側の酸洗槽に供給している。   That is, the continuous pickling apparatus 10 </ b> A in this embodiment includes a pickling tank 6 filled with a pickling solution (acid solution) 2, and the pickling tank 6 is advancing the steel strip 3 by a plurality of dams 1. It is divided in the direction d1. Then, in order to replenish the acid solution 2 consumed by pickling, the height of the dam 1 is increased in order toward the steel strip traveling direction d1, and the acid solution is opposite to the steel strip traveling direction d1, and the steel strip 3 Each dam 1 is sequentially overflowed from the outlet side of the steel sheet and supplied to the pickling tank upstream of the steel strip traveling direction d1.

そして、図1は、鋼帯進行方向d1に分割されている酸洗槽6の一部分を抽出して示した図である。   And FIG. 1 is the figure which extracted and showed a part of the pickling tank 6 divided | segmented into the steel strip advancing direction d1.

図1、図2に示すように、この連続式酸洗装置10Aは、ダム1の鋼帯進行方向d1上流側に近接して、酸洗槽6の底面に底面設置型熱交換器5が設置されており、さらに、その底面設置型熱交換器5を保護するための保護ダム4が底面設置型熱交換器5をダム1とで挟み込むように設置されている。   As shown in FIGS. 1 and 2, the continuous pickling apparatus 10 </ b> A is provided with a bottom-installed heat exchanger 5 on the bottom surface of the pickling tank 6 near the upstream side d <b> 1 in the steel strip traveling direction of the dam 1. Furthermore, a protective dam 4 for protecting the bottom surface installation type heat exchanger 5 is installed so as to sandwich the bottom surface installation type heat exchanger 5 with the dam 1.

そして、この保護ダム4は、上端が底面設置型熱交換器5の上端より高くかつ酸洗槽6内の酸液2の液面より低くなっているとともに、酸液2が通過可能なスリット4aを有するスリット構造付き保護ダム4となっている。   The protective dam 4 has a slit 4a through which the acid solution 2 can pass while the upper end is higher than the upper end of the bottom surface installation type heat exchanger 5 and lower than the level of the acid solution 2 in the pickling tank 6. It becomes the protection dam 4 with a slit structure which has.

これにより、この連続式酸洗装置10Aにおいては、スリット構造付き保護ダム4の上端が底面設置型熱交換器5の上端より高くかつ酸洗槽6内の酸液2の液面より低くなっているので、鋼帯3が酸液2中から露出することがほぼ無いため、操業異常時等の鋼帯3の張力低下時に鋼帯3の高さ位置が下った場合でも、酸洗効率の悪化を招くことなく、底面設置型熱交換器5と鋼帯3の接触を防止することができる。   Thereby, in this continuous pickling apparatus 10A, the upper end of the protective dam 4 with the slit structure is higher than the upper end of the bottom surface installation type heat exchanger 5 and lower than the liquid level of the acid solution 2 in the pickling tank 6. Therefore, since the steel strip 3 is hardly exposed from the acid solution 2, the pickling efficiency is deteriorated even when the height of the steel strip 3 is lowered when the tension of the steel strip 3 is lowered due to abnormal operation. Without incurring contact with the bottom surface heat exchanger 5 and the steel strip 3.

また、鋼帯3周辺で随伴流f1が発生し、その随伴流f1がダム1と衝突した際に下部への流れf2が発生した場合に、その下部への流れf2がスリット構造付き保護ダム4のスリット4aを通過するため、ダム1とスリット構造付き保護ダム4で挟み込まれた底面設置型熱交換器5周辺の酸液2の流れを速めることになり、設備維持管理の煩雑化を招くことなく、底面設置型熱交換器5へのスケールの堆積を抑止することができる。   Further, when an accompanying flow f1 is generated around the steel strip 3, and when the accompanying flow f1 collides with the dam 1, a downward flow f2 is generated, the downward flow f2 is converted into a protective dam 4 with a slit structure. , The flow of the acid solution 2 around the bottom-mounted heat exchanger 5 sandwiched between the dam 1 and the protective dam 4 with the slit structure is accelerated, resulting in a complicated facility maintenance management. In addition, it is possible to suppress the accumulation of scale on the bottom-mounted heat exchanger 5.

すなわち、この実施形態においては、酸洗効率の悪化や設備維持管理の煩雑化を招くことなく、底面設置型熱交換器5と鋼帯3の接触防止と底面設置型熱交換器5へのスケールの堆積抑止を効率的に行うことができる。   In other words, in this embodiment, the contact between the bottom-mounted heat exchanger 5 and the steel strip 3 is prevented and the scale to the bottom-mounted heat exchanger 5 is obtained without causing deterioration of pickling efficiency and complication of equipment maintenance management. It is possible to efficiently prevent the accumulation of sediment.

図5に示した従来技術による連続式酸洗装置を用いた場合は、3ヶ月程度の使用で、底面設置型熱交換器5へのスケールの堆積によって、熱交換効率の低下や、偏熱の発生による底面設置型熱交換器5の変形・損傷が生じていた。そのため、しばしば、底面設置型熱交換器5の交換等が必要になっていた。   When the continuous pickling apparatus according to the prior art shown in FIG. 5 is used, the heat build-up efficiency is reduced due to the accumulation of the scale on the bottom-mounted heat exchanger 5 after about 3 months of use. Deformation and damage of the bottom-mounted heat exchanger 5 due to the occurrence occurred. For this reason, it is often necessary to replace the bottom-mounted heat exchanger 5 or the like.

これに対して、上記の本発明の一実施形態における連続式酸洗装置を用いた場合は、6ヶ月間の使用でも、底面設置型熱交換器5へのスケールの堆積が抑止され、熱交換効率の低下や、偏熱の発生による底面設置型熱交換器5の変形・損傷は生じなかった。   On the other hand, when the continuous pickling apparatus according to one embodiment of the present invention is used, scale build-up on the bottom-mounted heat exchanger 5 is suppressed even after 6 months of use, and heat exchange is performed. Deformation / damage of the bottom-mounted heat exchanger 5 due to the decrease in efficiency and the occurrence of uneven heat did not occur.

このように、本発明の連続式酸洗装置を用いることにより、酸洗効率の悪化や設備維持管理の煩雑化を招くことなく、熱交換器と鋼帯の接触防止と熱交換器へのスケールの堆積抑止を効率的に行うことができる。   Thus, by using the continuous pickling apparatus of the present invention, the contact between the heat exchanger and the steel strip can be prevented and the scale to the heat exchanger can be achieved without deteriorating the pickling efficiency and complication of equipment maintenance management. It is possible to efficiently prevent the accumulation of sediment.

1 ダム
2 酸液
3 鋼帯
4 スリット構造付き保護ダム
4a スリット
5 底面設置型熱交換器
6 酸洗槽
6a、6b、6c、6d 酸洗槽
7 蒸気パイプ
8 側面設置型熱交換器
9 保護ダム
10 連続式酸洗装置
10A 連続式酸洗装置
d1 鋼帯進行方向
f1 鋼帯の随伴流
f2 随伴流がダムに衝突して発生する下方向への流れ
DESCRIPTION OF SYMBOLS 1 Dam 2 Acid liquid 3 Steel strip 4 Protection dam with slit structure 4a Slit 5 Bottom installation type heat exchanger 6 Pickling tank 6a, 6b, 6c, 6d Pickling tank 7 Steam pipe 8 Side installation heat exchanger 9 Protection dam DESCRIPTION OF SYMBOLS 10 Continuous pickling apparatus 10A Continuous pickling apparatus d1 Steel strip traveling direction f1 The accompanying flow of the steel strip f2 The downward flow generated by the accompanying flow colliding with the dam

Claims (2)

鋼帯を連続的に酸洗する連続式酸洗装置であって、ダムにより鋼帯進行方向に分割された酸洗槽と、前記酸洗槽の底面に設置された熱交換器と、前記ダムとで前記熱交換器を挟み込むように設置された保護ダムとを備え、
前記熱交換器は、前記ダムに近接して鋼帯進行方向上流側にのみ設置されており、前記保護ダムは、上端が前記熱交換器の上端より高くかつ前記酸洗槽内の酸液の液面より低くなっているとともに、酸液が通過可能なスリットを有するスリット構造付き保護ダムであることによって、前記熱交換器と前記鋼帯との接触防止と前記熱交換器へのスケールの堆積抑止を行うことを特徴とする鋼帯の連続式酸洗装置。
A continuous pickling apparatus for continuously pickling a steel strip, a pickling tank divided by a dam in the direction of travel of the steel strip, a heat exchanger installed on the bottom surface of the pickling tank, and the dam And a protective dam installed so as to sandwich the heat exchanger,
The heat exchanger is installed only on the upstream side in the steel strip traveling direction in the vicinity of the dam, and the protective dam has an upper end higher than the upper end of the heat exchanger and the acid solution in the pickling tank. By being a protective dam with a slit structure having a slit through which the acid solution can pass while being lower than the liquid level , contact prevention between the heat exchanger and the steel strip and deposition of scale on the heat exchanger A continuous steel pickling device for steel strips characterized by deterrence .
請求項1に記載の鋼帯の連続式酸洗装置を用いて鋼帯を連続的に酸洗することにより、鋼帯を製造することを特徴とする鋼帯の製造方法。   A steel strip is produced by continuously pickling steel strip using the continuous pickling apparatus for steel strip according to claim 1.
JP2014043845A 2014-03-06 2014-03-06 Steel strip continuous pickling apparatus and steel strip manufacturing method Expired - Fee Related JP6052208B2 (en)

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JP6586392B2 (en) 2016-04-27 2019-10-02 Primetals Technologies Japan株式会社 Pickling equipment

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