JP2007031791A - Cleaning method for pickled steel strip in continuous pickling treatment line and cleaning apparatus - Google Patents

Cleaning method for pickled steel strip in continuous pickling treatment line and cleaning apparatus Download PDF

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JP2007031791A
JP2007031791A JP2005218155A JP2005218155A JP2007031791A JP 2007031791 A JP2007031791 A JP 2007031791A JP 2005218155 A JP2005218155 A JP 2005218155A JP 2005218155 A JP2005218155 A JP 2005218155A JP 2007031791 A JP2007031791 A JP 2007031791A
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steel strip
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Koichi Kanbara
宏一 蒲原
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Nippon Steel Nisshin Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G3/00Apparatus for cleaning or pickling metallic material
    • C23G3/02Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously
    • C23G3/024Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously by a combination of dipping and spraying

Abstract

<P>PROBLEM TO BE SOLVED: To provide a cleaning method and apparatus for a pickled steel strip by which a satisfactory cleaning effect can be obtained even during low-speed running and line stop by using water not containing a discoloration preventing agent as cleaning water. <P>SOLUTION: A plurality of stages of rinsing tanks (8<SB>1</SB>, 8<SB>2</SB>, 8<SB>3</SB>, 8<SB>4</SB>) having spray nozzles (4<SB>1</SB>. 4<SB>2</SB>, 4<SB>3</SB>, 4<SB>4</SB>) are provided with cleaning water storage pits (10<SB>1</SB>, 10<SB>2</SB>, 10<SB>3</SB>, 10<SB>4</SB>) partitioned by weirs (9<SB>1</SB>, 9<SB>2</SB>, 9<SB>3</SB>), and circulating spray cleaning circuits (13<SB>1</SB>, 13<SB>2</SB>, 13<SB>3</SB>, 13<SB>4</SB>) are arranged. During steady operation, the cleaning water (circulation cleaning water) of the storage pits is sprayed by the circulating spray cleaning circuits to the steel strip. The contamination of the circulation cleaning water is diluted by replenishing the fresh cleaning water from a feedwater nozzle (12) of the rinsing tank of the final stage (received in the pit 10<SB>4</SB>of the final stage and flowing into the respective pits 10<SB>3</SB>, 10<SB>2</SB>, 10<SB>1</SB>as cascade flow overflowing the weirs 9<SB>1</SB>, 9<SB>2</SB>, 9<SB>3</SB>) and is held at required clarity. During the low-speed or line stop, the spray cleaning is performed by the fresh cleaning water in fresh spray cleaning circuits (15<SB>1</SB>, 15<SB>2</SB>, 15<SB>3</SB>, 15<SB>4</SB>) in place of the circulating spray cleaning. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、鋼帯を連続移送しながら鋼帯の表面スケールを酸液で溶解除去する酸洗処理につづいて、鋼帯表面の酸液の残留による変色を防止するために酸洗処理部の出側において鋼帯の残留酸液を洗浄水で除去する酸洗鋼帯の洗浄方法及び洗浄装置に関する。   In the present invention, in order to prevent discoloration due to the residual acid solution on the surface of the steel strip, the pickling treatment is performed to remove the surface scale of the steel strip with an acid solution while continuously transporting the steel strip. The present invention relates to a method and apparatus for cleaning a pickled steel strip that removes residual acid solution from the steel strip with cleaning water on the outlet side.

鋼帯を連続移送しながら鋼帯の表面スケール(酸化物)を除去する連続酸洗処理ラインは、酸洗装置とその出側に設置された洗浄装置とを有する。鋼帯は、酸洗浴槽の酸液(濃度調整された塩酸等)の浴中を通過することにより表面スケールを溶解除去され、ついで洗浄装置内を通過することにより、鋼帯表面に残留する酸液を洗い流される。洗浄処理の形態には、洗浄液をスプレーノズルから鋼帯表面に吹き付けるスプレー洗浄と、リンス浴槽に貯えた洗浄液の浴中を浸漬通板させる浸漬洗浄(浸漬リンス)とがあり、一般的に両者を併用した洗浄処理が行われる。   A continuous pickling treatment line that removes the surface scale (oxide) of the steel strip while continuously transporting the steel strip has a pickling device and a cleaning device installed on the outlet side thereof. The steel strip is removed by dissolving the surface scale by passing through the bath of acid solution (concentrated hydrochloric acid, etc.) in the pickling bath, and then passing through the cleaning device to remove the acid remaining on the steel strip surface. The liquid is washed away. There are two types of cleaning processes: spray cleaning in which cleaning liquid is sprayed from the spray nozzle to the steel strip surface, and immersion cleaning (immersion rinse) in which the cleaning liquid stored in the rinsing bath is immersed in a bath. The combined cleaning process is performed.

図2は、洗浄装置の構成例を示している。酸洗装置(I)の出側に設置された洗浄装置(II)は、鋼帯(S)のパスライン(通板ライン)に沿ってスプレーノズル(4)を配列したスプレー洗浄部と、リンス浴槽(5)を有する浸漬リンス部とを備えている。酸洗浴槽(1)の酸液浴(2)中を浸漬移送された鋼帯(S)は、リンガーロール(絞りロール)(3)で鋼帯表面の酸液を絞り取られた後、洗浄装置(II)のスプレー洗浄部のスプレーノズル(4)による洗浄液の吹付け(スプレー洗浄)とリンス浴槽(5)の洗浄液浴(6)中を通過する浸漬リンスとが施され、洗浄された鋼帯は、ついで表面の洗浄液を乾燥除去されて次工程に送り出される。   FIG. 2 shows a configuration example of the cleaning apparatus. The cleaning device (II) installed on the outlet side of the pickling device (I) includes a spray cleaning unit in which spray nozzles (4) are arranged along a pass line (passing plate line) of the steel strip (S), and a rinse. An immersion rinse section having a bathtub (5). The steel strip (S) immersed and transferred in the acid bath (2) of the pickling tub (1) is washed after the acid solution on the surface of the steel strip is squeezed out by a ringer roll (squeezing roll) (3). Steel which has been subjected to spraying of cleaning liquid (spray cleaning) by spray nozzle (4) of spray cleaning section of apparatus (II) and immersion rinsing passing through cleaning liquid bath (6) of rinse bath (5) and cleaned Then, the surface cleaning liquid is removed by drying and sent to the next process.

連続酸洗・洗浄ラインにおける鋼帯の移送運転は、酸洗装置の入側で行われる鋼帯の溶接施工(先行鋼帯と後行鋼帯との溶接)や、洗浄装置の下流側の次工程ライン(例えばスキンパス圧延ライン)でのロール取替え等により、低速移送ないし移送停止等の運転モードの切り替えが定期又は不定期に実施される。所定のライン速度で鋼帯を移送する定常運転と異なって、低速移送や移送停止等の非定常運転状態においては、酸洗鋼帯の表面を十分に洗浄することが困難となり、鋼帯表面に酸液の残留による変色(黄色化)が生じ易くなる。
この対策として、変色防止剤、変色除去剤等と称される洗浄用薬剤、例えば有機カルボン酸塩等のキレート剤などが使用されており、洗浄装置入側のリンガーロール部を通過する鋼帯表面に、洗浄用薬剤を含む溶液を塗布する洗浄処理(特許文献1,特許文献2)や、洗浄用薬剤含有溶液でスプレー洗浄する方法(特許文献3)等が提案されている。
特開2000−178775 特開2003−231983 特開2003−193275
The steel strip transfer operation in the continuous pickling / cleaning line involves welding of the steel strip (welding of the preceding steel strip and the subsequent steel strip) performed on the inlet side of the pickling device and the downstream of the cleaning device. Switching of operation modes such as low-speed transfer or transfer stop is performed regularly or irregularly by roll replacement in a process line (for example, a skin pass rolling line). Unlike the steady operation in which the steel strip is transferred at a predetermined line speed, it becomes difficult to sufficiently clean the surface of the pickled steel strip in an unsteady operation state such as low-speed transfer or transfer stop. Discoloration (yellowing) due to the remaining acid solution tends to occur.
As a countermeasure, a cleaning agent called a discoloration preventing agent, a discoloration removing agent or the like, for example, a chelating agent such as an organic carboxylate, is used, and the surface of the steel strip that passes through the ringer roll portion on the inlet side of the cleaning device In addition, a cleaning process (Patent Document 1, Patent Document 2) for applying a solution containing a cleaning drug, a spray cleaning method using a cleaning drug-containing solution (Patent Document 3), and the like have been proposed.
JP 2000-178775 A JP2003-231983 JP 2003-193275 A

洗浄用薬剤の使用は、洗浄効果を高め鋼帯表面の変色の抑制・防止に著効を奏するが、洗浄廃液のCOD(化学的酸素要求量)の増加により環境汚染対策として廃液処理コストの大幅な負担増を余儀なくされる。別法として、工業用水等の清澄水を大量に使用してスプレー洗浄等を徹底させれば、洗浄用薬剤を用いずに変色を抑制防止することも可能と考えられるが、この場合も洗浄水の大量消費に伴う洗浄処理コストの大幅な増加を避けることができない。
そこで本発明は、変色防止剤等の洗浄用薬剤を使用することなく、しかも洗浄水として工業用水の使用量とその排出量を可及的に抑制しつつ、鋼帯移送の低速運転や運転停止等の非定常運転状態においても十分な洗浄効果を確保し、鋼帯表面の変色を防止し得るようにした酸洗鋼帯の洗浄方法及び洗浄装置を提供するものである。
The use of cleaning chemicals is effective in increasing the cleaning effect and suppressing or preventing discoloration of the steel strip surface. However, as the COD (chemical oxygen demand) of the cleaning waste liquid increases, the waste liquid treatment cost is greatly increased as a measure against environmental pollution. Will be forced to increase the burden. As another method, it is considered possible to suppress and prevent discoloration without using a cleaning agent by thoroughly using a large amount of clarified water such as industrial water and thoroughly performing spray cleaning. A large increase in the cost of the cleaning process due to the large amount of consumption is unavoidable.
Therefore, the present invention does not use a cleaning agent such as a discoloration prevention agent, and further suppresses the amount of industrial water used and the amount discharged as cleaning water, and at a low speed operation or shutdown of steel strip transfer. The present invention provides a pickling steel strip cleaning method and a cleaning device that ensure a sufficient cleaning effect even in an unsteady operation state such as the above, and can prevent discoloration of the steel strip surface.

本発明の連続酸洗処理ラインにおける酸洗鋼帯の洗浄処理方法(請求項1)は、
鋼帯の連続移送下に、酸洗処理部において鋼帯の表面スケールを酸液で溶解除去する酸洗処理の後、鋼帯表面の酸液の残留による変色を防止するための、前記酸洗処理部の出側に設置された洗浄装置において洗浄用薬剤を含まない水で残留酸液を除去する酸洗鋼帯の洗浄方法であって、
鋼帯のパスラインに沿ってスプレーノズルが配列された複数段のリンス槽のそれぞれに、スプレーノズルから鋼帯表面に吹付けられる洗浄水を受容する洗浄水貯留ピットを槽底に設け、各洗浄水貯留ピットに、洗浄用薬剤を含まない水を洗浄水として貯留する共に、洗浄水を適時補給することにより、各洗浄水貯留ピットの洗浄水を所定の清浄度に保持し、
鋼帯が所定のライン速度で移送される定常運転状態においては、各段のリンス槽ごとに、洗浄水貯留ピットの洗浄水をポンプアップしてスプレーノズルから鋼帯表面に吹付ける循環スプレー洗浄処理を行い、鋼帯の低速移送又は移送停止の非定常運転状態においては、上記循環スプレー洗浄処理を停止すると共に、洗浄用薬剤を含まない未使用の新洗浄水を、上記スプレーノズルに供給し鋼帯表面に吹付ける新水スプレー洗浄処理を施すことを特徴としている。
The washing treatment method for the pickled steel strip in the continuous pickling treatment line of the present invention (Claim 1)
The pickling for preventing discoloration due to the acid solution remaining on the surface of the steel strip after the pickling treatment in which the surface scale of the steel strip is dissolved and removed by the acid solution in the pickling treatment section under the continuous transfer of the steel strip. In the cleaning apparatus installed on the outlet side of the processing unit, a method for cleaning a pickled steel strip that removes residual acid solution with water that does not contain cleaning chemicals,
A wash water storage pit that receives the wash water sprayed from the spray nozzle to the steel strip surface is provided at the bottom of each of the multiple-stage rinse tanks in which spray nozzles are arranged along the steel strip pass line. In the water storage pit, water that does not contain cleaning chemicals is stored as cleaning water, and the cleaning water in each cleaning water storage pit is maintained at a predetermined cleanliness by replenishing the cleaning water in a timely manner.
In the steady operation state in which the steel strip is transferred at a predetermined line speed, the circulating spray cleaning process in which the cleaning water in the cleaning water storage pit is pumped up and sprayed from the spray nozzle onto the surface of the steel strip for each rinsing tank In the unsteady operation state of low-speed transfer or stop of the steel strip, the circulating spray cleaning process is stopped, and unused fresh cleaning water not containing a cleaning chemical is supplied to the spray nozzle. It is characterized by a new water spray cleaning process that sprays on the surface of the belt.

上記スプレー洗浄処理において、非定常運転状態における循環スプレー洗浄から新水スプレー洗浄への切り替えは、必ずしも複数段のリンス槽のすべてにおいて行なう必要はなく、ライン上流側のリンス槽においてのみ新水スプレー洗浄への切り替えを行ない、下流側のリンス槽は循環スプレー洗浄のままとすることもできる(請求項2)。 また、鋼帯の移送停止(ライン停止)の非定常運転状態においては、ライン停止の状態が比較的長い時間つづく場合、一定時間の経過により所要の洗浄処理がなされた時点で、新水スプレー洗浄処理を停止し、循環スプレー洗浄処理に復帰させることができる(請求項3)。   In the above spray cleaning process, switching from the circulating spray cleaning to the fresh water spray cleaning in the unsteady operation state is not necessarily performed in all of the rinsing tanks in the plurality of stages, and the fresh water spray cleaning is performed only in the rinse tank upstream of the line. The downstream rinse tank can be kept in the circulation spray cleaning (Claim 2). Also, in the unsteady operation state of steel strip transfer stop (line stop), if the line stop state lasts for a relatively long time, the new water spray cleaning is performed when the required cleaning process is performed after a certain period of time. The process can be stopped and returned to the circulating spray cleaning process (claim 3).

本発明に係る酸洗鋼帯の洗浄装置(請求項4)は、
鋼帯の連続移送下に、酸洗処理装置で鋼帯の表面スケールを酸液で溶解除去する酸洗処理の後、酸洗処理部の出側において、洗浄用薬剤を含まない水で鋼帯表面の酸液を除去することにより鋼帯の変色を防止する酸洗鋼帯の洗浄装置であって、
i) 鋼帯の移送方向に連接する複数段のリンス槽8(8,8,8…)内の鋼帯パスラインに沿って洗浄水スプレーノズル4 (4,4,4…)を配列し、
ii) 隣合うリンス槽とリンス槽との間に位置して、鋼帯パスラインを挟んで上下に対向するリンガーロール3(3,3,3…)を配置すると共に、鋼帯移送方向と直交する向きの堰9(9,9…)を槽底に設けてそれぞれの槽底を洗浄水貯留ピット10(10,10,10…)とし、前記堰(9,9…)は、ライン終端側の洗浄水貯留ピットから始端側の洗浄水貯留ピットにかけて各堰(9,9…)を順次溢流する洗浄水のカスケード流が形成されるように、ライン終端側の堰から始端側の堰へと段階的に低くなる堰高さとし、
The pickling steel strip cleaning device according to the present invention (Claim 4)
The steel strip is washed with water that does not contain cleaning chemicals on the exit side of the pickling section after the pickling treatment where the surface scale of the steel strip is dissolved and removed with an acid solution in a pickling treatment device under continuous transfer of the steel strip. A pickling steel strip cleaning device that prevents discoloration of the steel strip by removing the acid solution on the surface,
i) Cleaning water spray nozzles 4 (4 1 , 4 2 , 4 3 ) along the steel strip pass line in the multiple-stage rinsing tanks 8 (8 1 , 8 2 , 8 3 ...) connected in the direction of steel strip transfer. ...)
ii) The ringer rolls 3 (3 2 , 3 3 , 3 4 ...) that are positioned between the adjacent rinsing tanks and that face each other across the steel strip pass line are arranged and the steel strips are transferred. Weirs 9 (9 1 , 9 2 ...) Orthogonal to the direction are provided at the tank bottoms, and the tank bottoms are used as washing water storage pits 10 (10 1 , 10 2 , 10 3 ...), And the weirs (9 1 , 9 2 ..., So that a cascade flow of wash water that sequentially overflows each weir (9 1 , 9 2 ...) From the wash water storage pit on the line end side to the wash water storage pit on the start end side is formed. The weir height that gradually decreases from the weir on the line end side to the weir on the start end side,

iii) 上記洗浄水貯留ピット10に貯留される洗浄水として洗浄用薬剤を含まない水を、鋼帯パスライン終端側のリンス槽に開口する給水ノズル12より供給し、終端側の洗浄水貯留ピットから前記カスケード流により始端側の洗浄水貯留ピットに到る各洗浄水貯留ピットのそれぞれに洗浄水を貯留せしめると共に、前記給水管から洗浄水を適時補給し洗浄水貯留ピット10の余剰水量は始端側の洗浄水貯留ピットから排出することにより、洗浄水貯留ピット内の洗浄水を常時所定の清浄度に保持し、
iv) 各洗浄水貯留ピット10 の洗浄水をポンプアップして各リンス槽のスプレーノズル(4,4,4…)から鋼帯表面に吹付ける循環スプレー洗浄回路13(13,13,13…)を各リンス槽(8,8,8…)ごとに設けると共に、洗浄用薬剤を含まない未使用の新洗浄水を各リンス槽のスプレーノズル4(4,4,4…) から鋼帯表面に吹付ける新水スプレー洗浄回路15(15,15,15…)を設け、
鋼帯が所定のライン速度で移送される定常運転時は循環スプレー洗浄回路13による洗浄処理とし、鋼帯の低速移送又は移送停止の非定常運転時は新水スプレー洗浄回路15による洗浄処理とする洗浄処理回路の切り替えが行なわれるように構成されている。
iii) Water that does not contain cleaning chemicals as cleaning water stored in the cleaning water storage pit 10 is supplied from the water supply nozzle 12 that opens to the rinsing tank on the end side of the steel strip pass line, and the cleaning water storage pit on the end side From the cascade flow, the wash water is stored in each of the wash water storage pits to the wash water storage pit on the start end side, and the wash water is replenished from the water supply pipe in a timely manner, so that the surplus water amount in the wash water storage pit 10 is By discharging from the cleaning water storage pit on the side, the cleaning water in the cleaning water storage pit is always kept at a predetermined cleanliness,
iv) Circulating spray cleaning circuit 13 (13 1 , 13) that pumps up the cleaning water in each cleaning water storage pit 10 and sprays it on the steel strip surface from the spray nozzles (4 1 , 4 2 , 4 3 ...) of each rinsing tank 2 , 13 3 ... Are provided for each rinsing tank (8 1 , 8 2 , 8 3 ...), And unused new washing water that does not contain cleaning chemicals is added to the spray nozzles 4 (4 1 , 4,. 4 2, 4 3 ...) fresh water spray cleaning circuit 15 sprayed on the steel strip surface (15 1, 15 2, 15 3 ...) provided from,
During the steady operation in which the steel strip is transferred at a predetermined line speed, the cleaning process is performed by the circulating spray cleaning circuit 13, and when the steel strip is transferred at a low speed or when the transfer is stopped, the cleaning process is performed by the fresh water spray cleaning circuit 15. The cleaning processing circuit is configured to be switched.

上記酸洗装置は、非定常運転状態におけるスプレー洗浄回路の切り替えを、所望により、ライン上流側のリンス槽と下流側のリンス槽とに分け、上流側のリンス槽において循環スプレー洗浄から新水スプレー洗浄への切り替えを行ない、下流側のリンス槽は循環スプレー洗浄処理をそのまま継続する構成(請求項5)、及び/又は鋼帯の移送停止(ライン停止)の非定常運転状態において、一定時間の経過により所要の洗浄処理がなされた時点で、新水スプレー洗浄処理を停止し、循環スプレー洗浄処理に復帰させる構成(請求項6)が適宜採用される。   In the pickling apparatus, switching of the spray cleaning circuit in the unsteady operation state is divided into a rinse tank on the upstream side of the line and a rinse tank on the downstream side as desired, and in the upstream rinse tank, from the circulating spray cleaning to the fresh water spray. The rinsing tank on the downstream side is switched to cleaning, and the circulation spray cleaning process is continued as it is (Claim 5) and / or in the unsteady operation state of the steel strip transfer stop (line stop) for a certain period of time. A configuration (Claim 6) is adopted as appropriate in which the fresh water spray cleaning process is stopped and returned to the circulating spray cleaning process when the required cleaning process is performed.

本発明はリンス槽を鋼帯移送方向(ライン方向)に連接した複数段の槽(8,8,8…)からなる多段構成とし、各段のリンス槽における洗浄形態をすべてスプレー洗浄とすると共に、そのスプレー洗浄をラインの運転状態(a:定常運転状態、b:非定常運転状態)に対応する2つの形態に分けている。そして所定のライン速度で鋼帯移送を行う定常運転においては、各段のリンス槽(8,8,8…)の洗浄水貯留ピット(10,10,10…)に貯留されている洗浄水を循環使用することにより洗浄水の消費量を抑えている。
また定常運転時に循環使用される洗浄水貯留ピットの洗浄水の汚染(循環使用下の鋼帯通板量の増加と共に酸液の混入による汚染が進む)に対し、新たな洗浄水が適宜補給(汚染の希釈化)されることにより汚染濃度が所定値以下に保持される。これにより定常運転における鋼帯表面の変色防止に必要な洗浄効果が安定に維持される。 他方、鋼帯の移送を低速移送もしくは移送停止(ライン停止)とする非定常運転においては、洗浄水貯留ピット(10,10,10…)の洗浄水を循環使用する上記循環スプレー洗浄に代え、未使用の洗浄水(新洗浄水)を使用するスプレー洗浄(新水スプレー洗浄)に切り替えられ、これにより非定常運転でのスプレー洗浄効果が確保される。
In the present invention, the rinsing tank has a multi-stage configuration (8 1 , 8 2 , 8 3 ...) Connected in the steel strip transfer direction (line direction), and all cleaning modes in each stage rinsing tank are spray-cleaned. In addition, the spray cleaning is divided into two forms corresponding to the operation state of the line (a: steady operation state, b: unsteady operation state). In the steady operation in which the steel strip is transferred at a predetermined line speed, it is stored in the wash water storage pits (10 1 , 10 2 , 10 3 ...) Of the rinsing tanks (8 1 , 8 2 , 8 3 ...) Of each stage. The consumption of washing water is reduced by circulating the washing water used.
In addition, cleaning water in the cleaning water storage pit that is circulated during steady operation (contamination due to mixing of the acid solution with the increase in the amount of steel strip through circulation) will be replenished with new cleaning water as appropriate ( Dilution of contamination) keeps the contamination concentration below a predetermined value. As a result, the cleaning effect necessary for preventing discoloration of the steel strip surface during steady operation is stably maintained. On the other hand, in the unsteady operation in which the steel strip is transferred at a low speed or stopped (line stop), the above circulating spray cleaning using the cleaning water in the cleaning water storage pits (10 1 , 10 2 , 10 3 ...) Is circulated. Instead of switching to spray cleaning (new water spray cleaning) using unused cleaning water (new cleaning water), the spray cleaning effect in unsteady operation is ensured.

このように洗浄水貯留ピット(10,10,10…)の洗浄水を、定常運転において循環使用し、新たに供給される洗浄水は、洗浄水貯留ピットの洗浄水(循環使用される)の汚染を希釈するために補給される水量と、非定常運転時の新水スプレー洗浄に使用される水量とに限定されており、従って洗浄水の総消費量を抑制しつつ、ラインの定常運転と非定常運転との変更・切り替えに対応した洗浄処理が達成される。 洗浄水の総消費量が抑制されることにより、洗浄コストの低減及び洗浄装置から排出される廃棄水量とその処理コストの削減効果が得られる。 In this way, the wash water in the wash water storage pits (10 1 , 10 2 , 10 3 ...) Is circulated and used in the steady operation, and the newly supplied wash water is the wash water (circulation used in the wash water storage pit). The amount of water replenished to dilute the contamination of the water and the amount of water used for fresh water spray cleaning during non-steady operation is limited to the total The cleaning process corresponding to the change / switch between the steady operation and the unsteady operation is achieved. By suppressing the total consumption of cleaning water, it is possible to reduce the cleaning cost and to reduce the amount of waste water discharged from the cleaning device and the treatment cost.

また上記非定常運転(低速移送又はライン停止)となった時の新水スプレー洗浄への切り替えは、下流側のリンス槽では必ずしも必要としないので(後記)、上流側のリンス槽だけを新水スプレー洗浄に切替える(下流側のリンス槽は循環スプレー洗浄をそのまま継続する)ことにより、新洗浄水の消費量をより削減することができる。更に移送停止(ライン停止)の非定常運転状態が比較的長くつづく場合、その間の新水スプレー洗浄で鋼帯表面の洗浄処理が達成されれば、その時点で新水スプレー洗浄から循環スプレー洗浄に復帰させてよく、新洗浄水の消費量をよりいっそう節減することができる。
しかも、使用される洗浄水は、ライン運転状態のいかんに拘わらず、定常運転又は非定常運転時のいずれにおいても、洗浄用薬剤を含まない水(工業用水等)であるから、洗浄用薬剤を使用する洗浄処理に比べ、廃棄洗浄水の汚染(COD増加)及び環境負荷もそれだけ低減し、廃液処理に要するコスト負担が少なくなる。
Also, switching to fresh water spray cleaning when the above-mentioned unsteady operation (low speed transfer or line stop) is not always necessary in the downstream rinse tank (described later), so only the upstream rinse tank is treated with fresh water. By switching to spray cleaning (the rinsing tank on the downstream side continues circulation spray cleaning as it is), the consumption of new cleaning water can be further reduced. Furthermore, if the unsteady operation state of the transfer stop (line stop) continues for a relatively long time, if the cleaning process of the steel strip surface is achieved by the new water spray cleaning in the meantime, the water spray is changed from the new water spray cleaning to the circulating spray cleaning at that time. It can be restored and the consumption of new washing water can be further reduced.
In addition, the cleaning water used is water that does not contain cleaning chemicals (industrial water, etc.) in both steady operation and non-steady operation regardless of the line operation state. Compared with the cleaning process to be used, the waste cleaning water contamination (COD increase) and the environmental load are reduced accordingly, and the cost burden required for the waste liquid processing is reduced.

以下本発明について図面を参照して説明する。
図1において、酸洗装置(I)の出側に設置された洗浄装置(II)は、鋼帯移送方向に連接する複数のリンス槽(8)(8,8,8,8)からなる多段構成を有する。各段のリンス槽は、鋼帯パスラインに沿ってスプレーノズル(4)(4,4,4,4)が配列され、槽底には堰(9)(9,9,9)が設けられている。各リンス槽(8,8,8,8)のそれぞれは、堰(9,9,9)で区分される洗浄水貯留ピット(10)(10,10,10,10)を有し、隣合うリンス槽との間には、鋼帯表面の付着液を除去(液切り)するためのリンガーロール(3)(3,3,3)が配設されている。またスプレー洗浄効果を高めるための補助的手段として、鋼帯表面に回転摺接するブラシロール(7)が適宜個所に配設される。
以下の説明では、リンス槽(8)(8)(8)(8)のそれぞれを、ライン始端側から終端側に向って、第1段、第2段、第3段、第4段(又は最終段)リンス槽と指称し、また洗浄水貯留ピット(10)(10)(10)(10)のそれぞれに対し、同様の段数符号を付して指称することもある。
The present invention will be described below with reference to the drawings.
In FIG. 1, the cleaning device (II) installed on the outlet side of the pickling device (I) includes a plurality of rinse tanks (8) (8 1 , 8 2 , 8 3 , 8 4 ) connected in the steel strip transfer direction. ). In each rinsing tank, spray nozzles (4) (4 1 , 4 2 , 4 3 , 4 4 ) are arranged along the steel strip pass line, and weirs (9) (9 1 , 9 2 are arranged at the bottom of the tank. , 9 3 ). Each rinse tank (8 1 , 8 2 , 8 3 , 8 4 ) has a wash water storage pit (10) (10 1 , 10 2 , 10) separated by a weir (9 1 , 9 2 , 9 3 ). 3 , 10 4 ), and between adjacent rinsing tanks, there is a ringer roll (3) (3 2 , 3 3 , 3 4 ) for removing (draining) the adhered liquid on the surface of the steel strip It is arranged. Further, as an auxiliary means for enhancing the spray cleaning effect, a brush roll (7) that is in rotational sliding contact with the surface of the steel strip is disposed at an appropriate place.
In the following description, each of the rinsing tanks (8 1 ) (8 2 ) (8 3 ) (8 4 ) is arranged in the first, second, third, Designate a 4-stage (or final-stage) rinse tank, and designate the wash water storage pits (10 1 ) (10 2 ) (10 3 ) (10 4 ) with the same stage number code. There is also.

洗浄装置(II)の入口側(「ライン始端側」)から出口側(「ライン終端側」)に到る各段の洗浄水貯留ピット(10,10,10,10)に貯えられる洗浄水(w)(w,w,w,w)は、洗浄用薬剤を含まない水(代表的には工業用水)である。その洗浄水は、洗浄水供給源(11)から給水管路(15)を介して、ライン終端側の第4段リンス槽(8)に開口するノズル(12)により供給され、その供給/停止の切替えは、バルブ(16)の開閉制御により行われる。この洗浄水供給ノズル(12)からの新洗浄水の補給は、ライン運転過程において適宜実施される(後記)。
また、リンス槽(8)の槽底を仕切る堰(9,9,9)は、ライン終端側の堰(9)から始端側の堰(9)にかけて、段階的に低くなる堰高さが与えられている。これは前記洗浄水供給ノズル(12)から供給される洗浄水を、終端側の洗浄水貯留ピット(10)から始端側に向かって(鋼帯の移送方向とは逆向きに)、堰(9,9,9)を順次溢流(オーバーフロー)するカスケード流として、洗浄水貯留ピット(10,10,10)のそれぞれに流入させるためである。
Store in the wash water storage pits (10 1 , 10 2 , 10 3 , 10 4 ) of each stage from the inlet side (“line start side”) to the outlet side (“line end side”) of the cleaning device (II) The washing water (w) (w 1 , w 2 , w 3 , w 4 ) to be obtained is water (typically industrial water) that does not contain a cleaning agent. The cleaning water is supplied from the cleaning water supply source (11) through the water supply pipe (15 0 ) by the nozzle (12) opened to the fourth-stage rinse tank (8 4 ) on the line end side. / switching stop is performed by opening and closing control of the valve (16 0). The replenishment of new washing water from the washing water supply nozzle (12) is appropriately performed during the line operation process (described later).
In addition, the weirs (9 1 , 9 2 , 9 3 ) that partition the bottom of the rinse tank (8) gradually decrease from the weir (9 3 ) on the line end side to the weir (9 1 ) on the start end side. Weir height is given. This is because the washing water supplied from the washing water supply nozzle (12) is moved from the washing water storage pit (10 4 ) on the end side toward the start end side (opposite to the direction of transport of the steel strip), This is because 9 3 , 9 2 , 9 1 ) are caused to flow into the wash water storage pits (10 3 , 10 2 , 10 1 ) as cascade flows that sequentially overflow (overflow).

リンス槽(8,8,8,8)の各段は、相互に独立した循環スプレー洗浄回路(13)(13, 13,13,13)を備えている。洗浄水貯留ピット(10,10,10,10)の洗浄水(w,w,w,w)は、それぞれの循環スプレー洗浄回路(13,13,13,13)により、それぞれのスプレーノズル(4,4,4,4)から、そこを通過する鋼帯(S)に吹付けられる。すなわちリンス槽を通過する鋼帯のスプレー洗浄は、各段のリンス槽(8,8,8,8)ごとにその洗浄水(w,w,w,w)を循環使用することにより行われる。この洗浄水を以下の説明では「循環洗浄水」と称することもある。この循環スプレー洗浄は、鋼帯移送を所定のライン速度で行なう定常運転状態のもとにおいて実施される。 Each stage of the rinse tank (8 1 , 8 2 , 8 3 , 8 4 ) is provided with a mutually independent circulation spray cleaning circuit (13) (13 1 , 13 2 , 13 3 , 13 4 ). The washing water (w 1 , w 2 , w 3 , w 4 ) of the washing water storage pit (10 1 , 10 2 , 10 3 , 10 4 ) is supplied to each circulation spray washing circuit (13 1 , 13 2 , 13 3 , 13 4 ) is sprayed from each spray nozzle (4 1 , 4 2 , 4 3 , 4 4 ) to the steel strip (S) passing therethrough. That is, spray cleaning of the steel strip passing through the rinsing tank is carried out by using the washing water (w 1 , w 2 , w 3 , w 4 ) for each stage of the rinsing tank (8 1 , 8 2 , 8 3 , 8 4 ). This is done by recirculating use. This cleaning water may be referred to as “circulating cleaning water” in the following description. This circulating spray cleaning is performed under a steady operation state in which the steel strip is transferred at a predetermined line speed.

リンス槽(8,8,8,8)は、上記循環スプレー洗浄回路(13,13,13,13)と共に新水スプレー洗浄回路(15)(15,15,15,15)を備えている。これは、循環洗浄水とは異なる未使用の洗浄水(新洗浄水)を洗浄水供給源(11)から供給し、スプレーノズル(4,4,4,4)により鋼帯の表面に吹付けるものである。該洗浄水供給源(11)から供給される新洗浄水は、前記のように洗浄用薬剤を含まない水(工業用水等)である。この新洗浄水を使用するスプレー洗浄を、前記循環スプレー洗浄と区別して、以下の説明では「新水スプレー洗浄」と称する。新水スプレー洗浄は非定常運転状態において実施される。 The rinsing tank (8 1 , 8 2 , 8 3 , 8 4 ) has a fresh water spray cleaning circuit (15) (15 1 , 15 2 ) together with the circulating spray cleaning circuit (13 1 , 13 2 , 13 3 , 13 4 ). , 15 3 , 15 4 ). This is because unused cleaning water (new cleaning water) different from circulating cleaning water is supplied from the cleaning water supply source (11), and the steel strip is sprayed by the spray nozzle (4 1 , 4 2 , 4 3 , 4 4 ). It sprays on the surface. The new cleaning water supplied from the cleaning water supply source (11) is water (industrial water or the like) that does not contain a cleaning chemical as described above. This spray cleaning using the new cleaning water is referred to as “new water spray cleaning” in the following description, in distinction from the circulation spray cleaning. The fresh water spray cleaning is performed in an unsteady operation state.

前記の循環スプレー洗浄と新水スプレー洗浄との切り替え操作は、循環スプレー洗浄回路(13)のバルブ(14,14,14,14)の開閉とポンプ(p,p,p,p)のON・OFF操作および新水供給スプレー洗浄回路のバルブ(16,16,16,16)の開閉操作より行われる。この切替え操作については、所望により、上流側のリンス槽(例えばリンス槽8,8)だけを、循環スプレー洗浄から新水スプレー洗浄に切り替え、下流側のリンス槽(リンス槽8,8)は循環スプレー洗浄をそのまま継続させる構成とすることもできる。
また移送停止(ライン停止)における新水スプレー洗浄については、新水スプレー洗浄の継続時間に上限を設け、タイマー設定により、一定時間を経過した時点で、新水スプレー洗浄からもとの循環スプレー洗浄に復帰させる構成を採用することもできる(後記)。
The switching operation between the circulating spray cleaning and the fresh water spray cleaning is performed by opening / closing the valves (14 1 , 14 2 , 14 3 , 14 4 ) of the circulating spray cleaning circuit (13) and the pumps (p 1 , p 2 , p 3 , p 4 ) and ON / OFF operation of the fresh water supply spray cleaning circuit (16 1 , 16 2 , 16 3 , 16 4 ). For this switching operation, if desired, only the upstream rinse tank (for example, rinse tanks 8 1 , 8 2 ) is switched from circulating spray cleaning to fresh water spray cleaning, and downstream rinse tanks (rinse tanks 8 3 , 8). 4 ) may be configured to continue the circulating spray cleaning as it is.
In addition, with regard to fresh water spray cleaning when the transfer is stopped (line stop), an upper limit is set for the duration of the new water spray cleaning, and when a certain period of time elapses due to the timer setting, the original circulating spray cleaning from the new water spray cleaning is performed. It is also possible to adopt a configuration for returning to (see below).

なお、新水スプレー供給回路(15)には、所望により、鎖線で示した新洗浄水供給支管(1511,1521,1531,1541)を設け、リンガーロール(3,3,3,3)の出側直近のスプレーノズルを循環スプレー洗浄回路から切り離した構成が採用される。この場合、新洗浄水供給支管(1511,1521,1531,1541) のそれぞれに連結されたスプレーノズル(411,421,431,441)(リンガーロールの出側直近のノズル)からは、常時(定常及び非定常運転において)新洗浄水がスプレーされるので、リンガーロール(3,3,3,3)の各ロール表面を、より清浄な状態に保持することができ、酸洗鋼帯の洗浄効果を高位安定に保つのに有効である。 The new water spray supply circuit (15) is provided with new washing water supply branches (15 11 , 15 21 , 15 31 , 15 41 ) indicated by chain lines as desired, and ringer rolls (3 1 , 3 2 , A configuration in which the spray nozzle closest to the outlet side of 3 3 , 3 4 ) is separated from the circulation spray cleaning circuit is adopted. In this case, new cleaning water supply branch pipes (15 11, 15 21, 15 31, 15 41) spray nozzle connected to each of (4 11, 4 21, 4 31, 4 41) (Ringer roll exit side of the last Since the new washing water is sprayed from the nozzles at all times (steady and unsteady operation), the surface of each ringer roll (3 1 , 3 2 , 3 3 , 3 4 ) is kept in a cleaner state. This is effective for keeping the cleaning effect of the pickled steel strip highly stable.

次に上記洗浄装置による鋼帯のスプレー洗浄操作を説明する。
酸洗装置(I)の出側の酸洗槽(1)から導出される鋼帯(S)は、洗浄装置(II)の入側のリンガーロール(3)で表面の付着酸液を絞り取られてリンス槽(8)に導入され、始端側の第1のリンス槽(8)から終端側の第4のリンス槽(8)に到る各リンス槽で順次循環スプレー洗浄処理を受ける。鋼帯(S)が、隣合うリンス槽同士の境界部を通過する際にはそこに設置されたリンガーロール(3,3,3)で表面に付着残留した洗浄水を絞り取られ、また各段の洗浄水貯留ピット(10,10,10,10)は堰(9,9,9)で相互に仕切られている。このため、上流側のリンス槽の洗浄水(循環洗浄水)が下流側のリンス槽に持ち込まれる量(鋼帯の移送に付随する循環洗浄水の移動量)は極く少量である。そして、鋼帯表面の酸液残留は、各段のリンス槽を通過するごとに順次減少していくので、洗浄水貯留ピット(10,10,10,10)のそれぞれにおける循環洗浄水の汚染濃度は、上流側から下流側に向って段階的に希薄となる濃度勾配を示す。
Next, the steel strip spray cleaning operation by the cleaning apparatus will be described.
The steel strip (S) led out from the pickling tank (1) on the exit side of the pickling device (I) is squeezed on the surface with the ringer roll (3 1 ) on the inlet side of the cleaning device (II). It is taken and introduced into the rinsing tank (8), and the circulation spray cleaning process is sequentially performed in each rinsing tank from the first rinsing tank (8 1 ) on the start end side to the fourth rinsing tank (8 4 ) on the end side. receive. When the steel strip (S) passes through the boundary between adjacent rinsing tanks, the washing water adhering to the surface is squeezed out by the ringer roll (3 2 , 3 3 , 3 4 ) installed there. The wash water storage pits (10 1 , 10 2 , 10 3 , 10 4 ) of each stage are separated from each other by weirs (9 1 , 9 2 , 9 3 ). For this reason, the amount of cleaning water (circulated cleaning water) in the upstream rinsing tank brought into the downstream rinsing tank (the amount of movement of the circulating cleaning water accompanying the transfer of the steel strip) is very small. Since the acid solution residue on the surface of the steel strip gradually decreases as it passes through the rinsing tanks of each stage, the circulating cleaning in each of the cleaning water storage pits (10 1 , 10 2 , 10 3 , 10 4 ) The contamination concentration of water shows a concentration gradient that gradually decreases from the upstream side toward the downstream side.

各段の洗浄水貯留ピット(10,10,10,10)に貯えられた循環洗浄水の汚染濃度は、鋼帯洗浄操業の進行(鋼帯通板量の経時的増加)に伴って漸次上昇する。所要の洗浄効果(鋼帯表面の変色を防止し得る酸液除去効果)を安定に確保するには、各段の循環洗浄水のそれぞれが、常時一定の清浄度に維持されていること(酸液による汚染濃度が許容上限値を越えないこと)を要する。そのための汚染濃度の希釈は、洗浄水供給ノズル(12)から新洗浄水を補給することにより行われる。洗浄水供給ノズル(12)から新洗浄水を補給すると、最終段のリンス槽の洗浄水貯留ピット(10)から始端側のリンス槽の洗浄水貯留ピット(10)に向って、槽底の堰(9)(9)(9)を順次溢流(オーバーフロー)する洗浄水のカスケード流が形成される。新洗浄水の補給に伴なう循環洗浄水の増量分(洗浄水貯留ピット10の貯水量を越える水量)は始端側の洗浄水貯留ピット(10)に設けられた排液口(17)から廃液として排出される。廃液は廃液処理装置(図示せず)に送り込まれ所定の処理に付される。 Contamination concentration of circulating wash water stored in the wash water storage pits (10 1 , 10 2 , 10 3 , 10 4 ) at each stage is due to the progress of the steel strip cleaning operation (increase in the amount of steel strip passage over time) Ascending gradually. To ensure the required cleaning effect (acid solution removal effect that can prevent discoloration of the steel strip surface) stably, each stage of the circulating cleaning water must be maintained at a constant cleanliness (acid The contamination concentration by the liquid must not exceed the allowable upper limit). For this purpose, the contamination concentration is diluted by supplying new cleaning water from the cleaning water supply nozzle (12). When new cleaning water is replenished from the cleaning water supply nozzle (12), the bottom of the tank moves from the cleaning water storage pit (10 4 ) of the final stage rinsing tank toward the cleaning water storage pit (10 1 ) of the rinsing tank on the start side. A cascade flow of washing water is formed which sequentially overflows (overflows) the weirs (9 3 ), (9 2 ) and (9 1 ). The increased amount of the circulating cleaning water accompanying the replenishment of the new cleaning water (the amount of water exceeding the amount stored in the cleaning water storage pit 10) is the drainage port (17) provided in the cleaning water storage pit (10 1 ) on the start side. Discharged as waste liquid. The waste liquid is sent to a waste liquid processing apparatus (not shown) and subjected to a predetermined process.

従って、各洗浄水貯留ピット(10,10,10,10)の循環洗浄水の汚染状況を適時検出し、その汚染の進み具合に応じて、洗浄水供給ノズル(12)から新洗浄水の補給を適宜実施することにより、洗浄水貯留ピット(10,10,10,10)内の循環洗浄水を常時所要の清浄度(許容汚染濃度の範囲内)に維持し、定常運転における洗浄効果を確保する。各洗浄水貯留ピット(10,10,10,10)の清浄度(汚染濃度)は、例えばpH測定により管理される。具体例として、第1段ピット(10)のpH:1.8以上、第2段ピット(10)のpH:3.0以上、第3段ピット(10)のpH:5.0以上、第4段ピット(10)のpH:6.3以上、にそれぞれ調整される。そのpH測定値が管理限界値から外れるような異常が検出される場合は、その異常状態を解消する措置としてリンガーロール(3)の不具合(鋼帯表面付着液の液切り不良)の点検、循環洗浄水の更新等の措置が適宜実施される。
リンス槽(8,8,8,8)を順次通過して表面の酸液を洗い落とされた鋼帯(S)は、最終段リンス槽(8)の終端部に設置されたリンガーロール(3)で表面の付着洗浄液を搾り取られて洗浄装置から送り出される。
Therefore, the contamination status of the circulating cleaning water in each cleaning water storage pit (10 1 , 10 2 , 10 3 , 10 4 ) is detected in a timely manner, and a new one is supplied from the cleaning water supply nozzle (12) according to the progress of the contamination. By appropriately supplying cleaning water, the circulating cleaning water in the cleaning water storage pit (10 1 , 10 2 , 10 3 , 10 4 ) is always maintained at the required cleanliness (within the allowable contamination concentration range). , Ensure the cleaning effect in steady operation. The cleanliness (contamination concentration) of each wash water storage pit (10 1 , 10 2 , 10 3 , 10 4 ) is managed by, for example, pH measurement. As specific examples, the pH of the first stage pit (10 1 ): 1.8 or more, the pH of the second stage pit (10 2 ): 3.0 or more, the pH of the third stage pit (10 3 ): 5.0 or more, the fourth stage pit The pH of (10 4 ) is adjusted to 6.3 or more. If an abnormality is detected that causes the pH measurement value to deviate from the control limit value, check or circulate the ringer roll (3) malfunction (defective liquid removal from the surface of the steel strip) as a measure to eliminate the abnormal condition. Measures such as cleaning water renewal will be implemented as appropriate.
The steel strip (S), which has passed through the rinsing tanks (8 1 , 8 2 , 8 3 , 8 4 ) and washed away the acid solution on the surface, is installed at the end of the final stage rinsing tank (8 4 ). The attached cleaning liquid on the surface is squeezed out by the ringer roll (3 5 ) and sent out from the cleaning device.

他方、定常運転と異なって、鋼帯移送を低速移送又は移送停止(ライン停止)とする非定常運転での洗浄処理は、前記循環スプレー洗浄から新水スプレー洗浄に切替えられる。新水スプレー洗浄は、各リンス槽ごとに配設された新水スプレー洗浄回路(15,15,15,15)を介して、洗浄新洗浄水供給源(11)からの新洗浄水をスプレーノズル(4,4,4,4)で鋼帯表面に吹付ける洗浄処理である。新洗浄水供給源(11)から供給される新洗浄水は未使用の清澄な水(工業用水等)であり、循環スプレー洗浄で使用される循環洗浄水に比し高い洗浄作用を有し、非定常運転に対する鋼帯の変色防止に必要な洗浄効果を奏する。新水スプレー洗浄に使用した新洗浄水は洗浄水貯留ピット(10,10,10,10)に受容され、循環洗浄水の希釈(汚染濃度の低減)にも寄与し、洗浄水貯留ピット(10)の貯留容量を越える余剰量は始端側の洗浄水貯留ピット(10)の排水口(17)から排出される。 On the other hand, unlike the steady operation, the cleaning process in the non-steady operation in which the steel strip is transferred at a low speed or stopped (line stop) is switched from the circulating spray cleaning to the fresh water spray cleaning. The new water spray cleaning is performed by a new water spray source (11) from a new cleaning water supply source (11) through a new water spray cleaning circuit (15 1 , 15 2 , 15 3 , 15 4 ) arranged for each rinsing tank. This is a cleaning process in which water is sprayed onto the surface of the steel strip with a spray nozzle (4 1 , 4 2 , 4 3 , 4 4 ). New cleaning water supplied from the new cleaning water supply source (11) is unused clear water (industrial water, etc.), and has a higher cleaning action than circulating cleaning water used in circulating spray cleaning, Provides the cleaning effect necessary to prevent discoloration of the steel strip for unsteady operation. The new cleaning water used for the new water spray cleaning is accepted in the cleaning water storage pit (10 1 , 10 2 , 10 3 , 10 4 ) and contributes to the dilution (reduction of contamination concentration) of the circulating cleaning water. Excess amount exceeding the storage capacity of the storage pit (10) is discharged from the drain port (17) of the washing water storage pit (10 1 ) on the start end side.

非定常運転(低速移送又はライン停止)は、酸洗装置(I)の入側(図示省略)での鋼帯溶接施工や、洗浄装置(II)の下流側(図示省略)の次工程(例えば鋼帯のスキンパスライン)におけるロール取替え等の種々の事由により定期又は不定期に発生する。非定常運転状態の継続時間の長短や、低速運転の具体的な移送速度は、それぞれの発生事由により異なる。 循環スプレー洗浄(定常運転)と新水スプレー洗浄(非定常運転)との切り替えはライン速度を基準として行なう。ライン速度は、洗浄装置の具体的な構成・仕様、鋼帯の材種等により異なるが、概ね30m/minを基準とし、それ以上の移送速度を定常運転とみなして循環スプレー洗浄を適用し、それより低い移送速度に減速される場合を低速運転として新水スプレー洗浄に切り替えて効率よく洗浄処理を遂行することができる。   Unsteady operation (low-speed transfer or line stop) can be performed by steel strip welding on the entry side (not shown) of the pickling device (I), or on the downstream side (not shown) of the washing device (II) (for example, It occurs regularly or irregularly due to various reasons such as roll change in the steel band skin pass line). The duration of the unsteady operation state and the specific transfer speed in the low-speed operation differ depending on the respective occurrence reasons. Switching between circulating spray cleaning (steady operation) and fresh water spray cleaning (unsteady operation) is performed based on the line speed. The line speed varies depending on the specific configuration and specifications of the cleaning device, the steel strip material type, etc., but generally 30m / min is used as a reference, and the higher spraying speed is regarded as a steady operation, and circulating spray cleaning is applied. When the speed is reduced to a lower transfer speed, it is possible to perform the cleaning process efficiently by switching to the new water spray cleaning as a low speed operation.

各段リンス槽(8,8,8,8)のスプレーノズル(4,4,4,4)は、循環スプレー洗浄(定常運転)と新水スプレー洗浄(非定常運転)との両方に共用されるが、新水スプレー洗浄の洗浄水(新洗浄水)は、循環洗浄水に比し高い洗浄作用を有することから、その吹付け流量を、循環スプレー洗浄の吹付け流量に比べて少ない量に抑えることができる。例えば循環スプレー洗浄の吹付け流量が約60m/minに設定されたラインにおいて、新水スプレー洗浄では約10m/minないしそれ以下の低い流量に設定して所期の洗浄効果を得ることができる。鋼板に対する洗浄水の吹付け流量の調節は、各スプレーノズルのそれぞれにバルブ(図示省略)を取り付けて、スプレーノズルごとの開閉制御による選択使用(スプレーノズルの間引き使用)やその噴射圧力の高低調整等により任意に行なうことができる。 Each stage rinsing tank spray nozzle (8 1, 8 2, 8 3, 8 4) (4 1, 4 2, 4 3, 4 4) is Shinmizu spray cleaning (unsteady and circulating spray cleaning (steady operation) However, since the cleaning water for new water spray cleaning (new cleaning water) has a higher cleaning action than the circulating cleaning water, the spray flow rate of The amount can be reduced compared to the attached flow rate. For example, in a line where the spraying flow rate for circulating spray cleaning is set to about 60 m 3 / min, it is possible to obtain the desired cleaning effect by setting the flow rate to about 10 m 3 / min or less for fresh water spray cleaning. it can. The flow rate of cleaning water sprayed onto the steel sheet is adjusted by attaching a valve (not shown) to each spray nozzle, and selectively using the spray nozzle by opening / closing control (spraying of the spray nozzle) or adjusting the injection pressure. It can be performed arbitrarily.

非定常運転における新水スプレー洗浄は、必ずしも全段のリンス槽(8,8,8,8)を対象として実施する必要はなく、上流側のリンス槽(例えばリンス槽8,8)のみを新水スプレー洗浄に切り替え、下流側のリンス槽(リンス槽8,8)は、定常運転時の循環スプレー洗浄をそのまま継続させることもできる。下流側の鋼帯は、上流側のリンス槽(ここではリンス槽8,8)を通過する際の循環スプレー洗浄を既に受けており、それだけ鋼帯表面の酸液残留が少なくなっているからである。ここにいう上流側,下流側という区別は相対的であり、例えばリンス槽(8)が5段に連接された構成では、第1と第2段を上流側、第3〜第5段を下流側とする仕分け、または第1〜第3段を上流側とし、第4,第5段を下流側としてそれぞれのスプレー洗浄を切り替えるようにしてもよい。 上記のように下流側のリンス槽(例えばリンス槽8,8)における新水スプレー洗浄への切替えが必要でない場合は、該リンス槽の新水スプレー洗浄回路(今の例では新水スプレー洗浄回路15,15)の設置を省略してよい。 The fresh water spray cleaning in the non-steady operation is not necessarily performed for the rinsing tanks in all stages (8 1 , 8 2 , 8 3 , 8 4 ), and the upstream rinsing tank (for example, the rinsing tank 8 1 , Only the 8 2 ) can be switched to the fresh water spray cleaning, and the downstream rinsing tank (rinsing tanks 8 3 and 8 4 ) can continue the circulating spray cleaning during the steady operation as it is. The steel strip on the downstream side has already undergone circulation spray cleaning when passing through the upstream rinsing tank (in this case, the rinsing tanks 8 1 , 8 2 ), and the acid solution residue on the steel strip surface is reduced accordingly. Because. The distinction between the upstream side and the downstream side here is relative. For example, in a configuration in which the rinsing tank (8) is connected in five stages, the first and second stages are upstream, and the third to fifth stages are downstream. Alternatively, the spray cleaning may be switched with the first or third stage being the upstream side and the fourth and fifth stages being the downstream side. If it is not necessary to switch to the fresh water spray cleaning in the downstream rinsing tank (for example, the rinsing tanks 8 3 and 8 4 ) as described above, the new water spray cleaning circuit (in this example, the new water spray is used). Installation of the cleaning circuits 15 3 and 15 4 ) may be omitted.

また、ライン停止の非定常運転状態が比較的長い時間にわたる場合は、ライン停止の全時間に亘って新水スプレー洗浄を継続させる必要はない。新水スプレー洗浄の実施で、変色防止に必要な洗浄効果が達成されれば、新水スプレー洗浄をそれ以上続ける必要はないからである。従って新水スプレー洗浄の開始に際して、その洗浄時間をタイマー設定しておき、所定時間を経過した時点で、循環スプレー洗浄に戻すようにしてよい。例えば、新水スプレー洗浄の開始から数分(例えば6分)を経過した時点で、なおライン停止状態が続くような場合は、新水スプレー洗浄からもとの循環スプレー洗浄に復帰させてよく、これにより新洗浄水の消費量をより節減することができる。
なお、ラインの定期修理のように、製品鋼帯に代えてダミーコイル鋼帯が通板される場合は、その間のスプレー洗浄は不要であるから、製品鋼帯の通板運転が再開されるまでの間、循環スプレー洗浄及び新水スプレー洗浄ともに休止される。
Moreover, when the unsteady operation state of the line stop is for a relatively long time, it is not necessary to continue the fresh water spray cleaning over the entire time of the line stop. This is because if the cleaning effect necessary for preventing discoloration is achieved by performing the new water spray cleaning, it is not necessary to continue the new water spray cleaning. Therefore, at the time of starting the fresh water spray cleaning, the cleaning time may be set as a timer, and when the predetermined time has elapsed, it may be returned to the circulating spray cleaning. For example, when a line stop state continues after several minutes (for example, 6 minutes) have passed since the start of new water spray cleaning, it is possible to return from the new water spray cleaning to the original circulating spray cleaning, Thereby, consumption of new washing water can be further reduced.
In addition, when the dummy coil steel strip is passed through instead of the product steel strip as in periodic repairs of the line, spray cleaning during that time is unnecessary, so the product steel strip passing operation is resumed. During this period, both the circulating spray cleaning and the fresh water spray cleaning are suspended.

図1の洗浄装置を備えた連続酸洗ラインにおいて、酸洗装置(I)の酸液浴槽(1)(酸液浴:HCl約10vol%水溶液)から導出される鋼帯を洗浄装置(II)(リンス槽の段数4、全長24m)に導入しスプレー洗浄処理を施す。循環スプレー洗浄(定常運転)及び新水スプレー洗浄(非定常運転)のための洗浄水供給源(11)から供給される洗浄水は洗浄用薬剤を含まない清澄な工業用水である。   In the continuous pickling line equipped with the cleaning device of FIG. 1, the steel strip derived from the acid bath (1) of the pickling device (I) (acid bath: about 10 vol% HCl solution) is cleaned with the cleaning device (II). Introduce into the rinsing tank (4 stages, total length 24 m) and perform spray cleaning treatment. The cleaning water supplied from the cleaning water supply source (11) for circulating spray cleaning (steady operation) and fresh water spray cleaning (unsteady operation) is clear industrial water that does not contain cleaning chemicals.

[スプレー洗浄操業]
各段リンス槽の洗浄水貯留ピット(10,10,10,10)に貯留される循環洗浄水の清澄度(汚染濃度)を管理するために 各洗浄水貯留ピットにpH測定計を配置してそれぞれの循環洗浄水のpH値を検出すると共に、検出されるpH値の変動に対応して、新洗浄水供給ノズル(12)から新洗浄水を適宜補給することにより、各リンス槽の循環洗浄水のpH値を下記の範囲に保持してスプレー洗浄処理を行った。
[Spray cleaning operation]
To manage the clarification (contamination concentration) of circulating wash water stored in the wash water storage pits (10 1 , 10 2 , 10 3 , 10 4 ) of each stage rinse tank Is arranged to detect the pH value of each of the circulating cleaning water and to appropriately replenish the new cleaning water from the new cleaning water supply nozzle (12) in response to the change in the detected pH value. Spray cleaning treatment was performed while maintaining the pH value of the circulating cleaning water in the tank within the following range.

(表1)
−洗浄水貯留ピットの循環洗浄水の汚染濃度管理−
第1ピット(10 ) 第2ピット(10 ) 第3ピット(10 ) 第4ピット(10 )
pH 1.8以上 3.0以上 5.0以上 6.3以上
(Table 1)
-Control of contamination concentration of circulating cleaning water in cleaning water storage pit-
1st pit (10 1 ) 2nd pit (10 1 ) 3rd pit (10 1 ) 4th pit (10 1 )
pH 1.8 or more 3.0 or more 5.0 or more 6.3 or more

この連続酸洗ラインにおける鋼帯移送は、下流側のスキンパスラインのロール取替え時に減速運転に切替えられる。ライン速度30m/min以上の鋼帯移送を定常運転(循環スプレー洗浄)、それより低速の移送運転を非定常運転としてスプレー洗浄を実施した。循環スプレー洗浄(a)と新水スプレー洗浄(b)との切り替えは、循環スプレー洗浄回路(13,13,13,13)のバルブ開/閉及びポンプの起動/停止と、これに対応する新水スプレー洗浄回路(15,15,15,15)のバルブの開/閉操作により行なった。
スプレー洗浄操業条件を表2及び表3に示す(表2: 循環スプレー洗浄、表3:新水スプレー洗浄)。
Steel strip transfer in this continuous pickling line is switched to deceleration operation when the roll of the downstream skin pass line is replaced. Spray cleaning was carried out with steel strip transfer at a line speed of 30 m / min or more as steady operation (circulating spray cleaning), and transfer operation at a lower speed as unsteady operation. Switching between circulating spray cleaning (a) and fresh water spray cleaning (b) is performed by opening / closing the valve of the circulating spray cleaning circuit (13 1 , 13 2 , 13 3 , 13 4 ) and starting / stopping the pump. It was performed by opening / closing the valves of the new water spray cleaning circuit (15 1 , 15 2 , 15 3 , 15 4 ) corresponding to.
The spray cleaning operation conditions are shown in Tables 2 and 3 (Table 2: Circulating spray cleaning, Table 3: Fresh water spray cleaning).

(表2)

[a:定常運転(ライン速度≧30m/min)における循環スプレー洗浄]
ヘッダー数 ノズル数 吹付け圧力(MPa) 吹付け液量(m /min)
第1リンス槽 12 90 0.15 60
第2リンス槽 12 90 0.15 60
第3リンス槽 8 60 0.15 60
第4リンス槽 8 60 0.15 60
* 吹付け圧力は最大値を示す
(Table 2)

[a: Circulating spray cleaning in steady operation (line speed ≧ 30m / min)]
Number of headers Number of nozzles Spray pressure (MPa) * Spray fluid volume (m 3 / min)
First rinsing tank 12 90 0.15 60
Second rinse tank 12 90 0.15 60
Third rinsing tank 8 60 0.15 60
4th rinse tank 8 60 0.15 60
* Spray pressure shows maximum value

(表3)
[b:非定常運転(ライン速度<30m/min)における新水スプレー洗浄]
ヘッダー数 ノズル数 吹付け圧力(MPa) 吹付け液量(m /min)
第1リンス槽 12 16 0.15 6
第2リンス槽 12 14 0.10 6
第3リンス槽 8 16 0.10 6
第4リンス槽 8 14 0.10 6
* 吹付け圧力は最大値を示す
(Table 3)
[b: New water spray cleaning in non-steady operation (line speed <30m / min)]
Number of headers Number of nozzles Spray pressure (MPa) * Spray fluid volume (m 3 / min)
First rinse tank 12 16 0.15 6
Second rinse tank 12 14 0.10 6
Third rinse tank 8 16 0.10 6
4th rinse tank 8 14 0.10 6
* Spray pressure shows maximum value

定期又は不定期に非定常運転が反復される条件下に、ライン運転の変動に対応してスプレー洗浄の運転モード(循環スプレー洗浄と新水スプレー洗浄)の切り替えを実施することにより、定常及び非定常運転のライン運転を通して、良好な洗浄効果を確保することができ、従来の洗浄処理に比し鋼帯の変色防止効果を各段に改善し得ることが認められた。
また、鋼帯の移送停止(ライン停止)の場合について、新水スプレー洗浄の上限時間を6分に設定し、それを越える時点で新水スプレー洗浄から、循環スプレー洗浄に復帰する運転モードの切り替えを行った場合にも、上記と同様の良好な洗浄効果が得られることが認められた。なお、新水スプレー洗浄の実施による新洗浄水の消費量の増加分は、5m以下(新水スプレー洗浄1回当たり)であり、そのコスト負担の増加は、洗浄効果の向上(洗浄不良に起因する損失の大幅な減少)により十分に補うことができる。
By switching the spray cleaning operation mode (circulating spray cleaning and fresh water spray cleaning) in response to fluctuations in line operation under conditions where unsteady operation is repeated regularly or irregularly, It was confirmed that a good cleaning effect can be ensured through the line operation of the steady operation, and the anti-discoloration effect of the steel strip can be improved in each stage as compared with the conventional cleaning treatment.
Also, in case of steel strip transfer stop (line stop), the upper limit time of fresh water spray cleaning is set to 6 minutes, and when it exceeds that time, the operation mode is switched from fresh water spray cleaning to circulating spray cleaning. It was confirmed that the same good cleaning effect as described above was obtained even when the above was performed. Incidentally, the new new washing water consumption increase in accordance with the practice of the water spray washing, a 5 m 3 or less (fresh water spray cleaning per), the increase in the cost burden, improve the cleaning effect (cleaning poor This can be fully compensated for by a significant reduction in the resulting loss).

本発明によれば、定常運転及び非定常運転の変動に拘わらず、洗浄用薬剤を含まない洗浄水を使用するスプレー洗浄により、酸洗鋼帯の酸液残留を効果的に洗浄除去して、変色を生じない改良された鋼帯表面品質を得ることができる。そのスプレー洗浄を、定常運転と非定常運転とに対応させて循環スプレー洗浄と新水スプレー洗浄とに分けて運転モードの切り替えを行う構成としているので、新洗浄水の消費量を削減しながら所定の洗浄効果を得ることができ、新洗浄水のコスト負担も軽微である。洗浄装置から排出される廃液は、洗浄用薬剤を含まないので、環境負荷も少なく、廃液処理仁要するコスト負担も軽減され、酸洗鋼帯の洗浄処理法として工業的に極めて有用な価値を有するものである。   According to the present invention, regardless of fluctuations in steady operation and non-steady operation, the remaining acid solution of the pickled steel strip is effectively washed away by spray cleaning using cleaning water that does not contain cleaning chemicals. An improved steel strip surface quality that does not cause discoloration can be obtained. The spray cleaning is divided into cyclic spray cleaning and fresh water spray cleaning corresponding to steady operation and non-steady operation, and the operation mode is switched. The cleaning effect can be obtained, and the cost burden of new cleaning water is small. Since the waste liquid discharged from the cleaning equipment does not contain cleaning chemicals, the environmental impact is small, the cost burden required for waste liquid treatment is reduced, and it has industrially very useful value as a cleaning treatment method for pickling steel strips. Is.

本発明の酸洗鋼帯の洗浄処理を実施する洗浄装置の実施例を示す図である。It is a figure which shows the Example of the washing | cleaning apparatus which implements the washing process of the pickled steel strip of this invention. 従来の一般的な洗浄装置を示す図である。It is a figure which shows the conventional general washing | cleaning apparatus.

符号の説明Explanation of symbols

1 :酸洗浴槽
2 :酸液浴
3(3,3,3,3,3):リンガーロール
4(4,4,4,4) :スプレーノズル
5 :リンス浴槽
6 :リンス液浴
7 :ブラシロール
8(8,8,8,8) :リンス槽
9(9,9,9) :堰
1: Acid bath 2: Acid bath
3 (3 1 , 3 2 , 3 3 , 3 4 , 3 5 ): Ringer roll 4 (4 1 , 4 2 , 4 3 , 4 4 ): Spray nozzle 5: Rinse tub 6: Rinse liquid bath 7: Brush roll 8 (8 1 , 8 2 , 8 3 , 8 4 ): Rinse tank 9 (9 1 , 9 2 , 9 3 ): Weir

10(10,1010,10):洗浄水貯留ピット
11 :新洗浄水供給源
12 :新洗浄水供給ノズル
13(13,13,13,13):循環スプレー洗浄回路
14(14,14,14,14):開閉バルブ
15(15,15,15,15):新水スプレー洗浄回路
1511,1521,1531,1541:新水供給支管
16(16,16,16,16):バルブ
17 :排水口
1,p,p,p :ポンプ
I :酸洗装置
II :洗浄装置
S :鋼帯
10 (10 1 , 10 2 10 3 , 10 4 ): Wash water storage pit 11: New wash water supply source 12: New wash water supply nozzle 13 (13 1 , 13 2 , 13 3 , 13 4 ): Circulating spray washing Circuit 14 (14 1 , 14 2 , 14 3 , 14 4 ): Open / close valve 15 (15 1 , 15 2 , 15 3 , 15 4 ): New water spray cleaning circuit
15 11 , 15 21 , 15 31 , 15 41 : New water supply branch 16 (16 1 , 16 2 , 16 3 , 16 4 ): Valve 17: Drain port p 1 , p 2 , p 3 , p 4 : Pump I : Pickling equipment
II: Cleaning device S: Steel strip

Claims (6)

鋼帯の連続移送下に、酸洗処理部において鋼帯の表面スケールを酸液で溶解除去する酸洗処理の後、鋼帯表面の酸液の残留による変色を防止するための、前記酸洗処理部の出側に設置された洗浄装置において洗浄用薬剤を含まない水で残留酸液を除去する酸洗鋼帯の洗浄方法であって、
鋼帯のパスラインに沿ってスプレーノズルが配列された複数段のリンス槽のそれぞれに、スプレーノズルから鋼帯表面に吹付けられる洗浄水を受容する洗浄水貯留ピットを槽底に設け、各洗浄水貯留ピットに、洗浄用薬剤を含まない水を洗浄水として貯留する共に、洗浄水を適時補給することにより、各洗浄水貯留ピットの洗浄水を所定の清浄度に保持し、
鋼帯が所定のライン速度で移送される定常運転状態においては、各段のリンス槽ごとに、洗浄水貯留ピットの洗浄水をポンプアップしてスプレーノズルから鋼帯表面に吹付ける循環スプレー洗浄処理を行い、鋼帯の低速移送又は移送停止の非定常運転状態においては、上記循環スプレー洗浄処理を停止すると共に、洗浄用薬剤を含まない未使用の新洗浄水を、上記スプレーノズルに供給し鋼帯表面に吹付ける新水スプレー洗浄処理を施すことを特徴とする連続酸洗処理ラインにおける酸洗鋼帯の洗浄方法。
The pickling for preventing discoloration due to the acid solution remaining on the surface of the steel strip after the pickling treatment in which the surface scale of the steel strip is dissolved and removed by the acid solution in the pickling treatment section under the continuous transfer of the steel strip. In the cleaning apparatus installed on the outlet side of the processing unit, a method for cleaning a pickled steel strip that removes residual acid solution with water that does not contain cleaning chemicals,
A wash water storage pit that receives the wash water sprayed from the spray nozzle to the steel strip surface is provided at the bottom of each of the multiple-stage rinse tanks in which spray nozzles are arranged along the steel strip pass line. In the water storage pit, water that does not contain cleaning chemicals is stored as cleaning water, and the cleaning water in each cleaning water storage pit is maintained at a predetermined cleanliness by replenishing the cleaning water in a timely manner.
In the steady operation state in which the steel strip is transferred at a predetermined line speed, the circulating spray cleaning process in which the cleaning water in the cleaning water storage pit is pumped up and sprayed from the spray nozzle onto the surface of the steel strip for each rinsing tank In the unsteady operation state of low-speed transfer or stop of the steel strip, the circulating spray cleaning process is stopped, and unused fresh cleaning water not containing a cleaning chemical is supplied to the spray nozzle. A method for cleaning a pickled steel strip in a continuous pickling treatment line, characterized by performing a fresh water spray cleaning treatment to spray the surface of the strip.
非定常運転状態における前記新水スプレー洗浄処理を、鋼帯パスライン上流側のリンス槽において行ない、下流側のリンス槽は循環スプレー洗浄処理をそのまま継続することを特徴とする請求項1に記載の連続酸洗処理ラインにおける酸洗鋼帯の洗浄方法。   2. The fresh water spray cleaning process in an unsteady operation state is performed in a rinse tank on the upstream side of the steel strip pass line, and the downstream rinse tank continues the circulating spray cleaning process as it is. Washing method for pickled steel strip in continuous pickling line. 鋼帯の移送を停止した非定常運転状態において、前記新水スプレー洗浄処理により鋼帯表面の残留酸液が除去された時点で、新洗浄水の供給を停止し、前記循環スプレー洗浄処理に切り替えることを特徴とする請求項1又は請求項2に記載の連続酸洗処理ラインにおける酸洗鋼帯の洗浄方法。   In the unsteady operation state in which the transfer of the steel strip is stopped, when the residual acid solution on the steel strip surface is removed by the new water spray cleaning process, the supply of new cleaning water is stopped and switched to the circulating spray cleaning process. The cleaning method of the pickling steel strip in the continuous pickling processing line of Claim 1 or Claim 2 characterized by the above-mentioned. 鋼帯の連続移送下に、酸洗処理装置で鋼帯の表面スケールを酸液で溶解除去する酸洗処理の後、酸洗処理部の出側において、洗浄用薬剤を含まない水で鋼帯表面の酸液を除去することにより鋼帯の変色を防止する酸洗鋼帯の洗浄装置であって、
i) 鋼帯の移送方向に連接する複数段のリンス槽8(8,8,8…)内の鋼帯パスラインに沿って洗浄水スプレーノズル4 (4,4,4…)を配列し、
ii) 隣合うリンス槽とリンス槽との間に位置して、鋼帯パスラインを挟んで上下に対向するリンガーロール3(3,3,3…)を配置すると共に、鋼帯移送方向と直交する向きの堰9(9,9…)を槽底に設けてそれぞれの槽底を洗浄水貯留ピット10(10,10,10…)とし、前記堰(9,9…)は、ライン終端側の洗浄水貯留ピットから始端側の洗浄水貯留ピットにかけて各堰(9,9…)を順次溢流する洗浄水のカスケード流が形成されるように、ライン終端側の堰から始端側の堰へと段階的に低くなる堰高さとし、
iii) 上記洗浄水貯留ピット10に貯留される洗浄水として洗浄用薬剤を含まない水を、鋼帯パスライン終端側のリンス槽に開口する給水ノズル12より供給し、終端側の洗浄水貯留ピットから前記カスケード流により始端側の洗浄水貯留ピットに到る各洗浄水貯留ピットのそれぞれに洗浄水を貯留せしめると共に、前記給水管から洗浄水を適時補給し洗浄水貯留ピット10の余剰水量は始端側の洗浄水貯留ピットから排出することにより、洗浄水貯留ピット内の洗浄水を常時所定の清浄度に保持し、
iv) 各洗浄水貯留ピット10 の洗浄水をポンプアップして各リンス槽のスプレーノズル(4,4,4…)から鋼帯表面に吹付ける循環スプレー洗浄回路13(13,13,13…)を各リンス槽(8,8,8…)ごとに設けると共に、洗浄用薬剤を含まない未使用の新洗浄水を各リンス槽のスプレーノズル4(4,4,4…) から鋼帯表面に吹付ける新水スプレー洗浄回路15(15,15,15…)を設け、
鋼帯が所定のライン速度で移送される定常運転時は循環スプレー洗浄回路13による洗浄処理とし、鋼帯の低速移送又は移送停止の非定常運転時は新水スプレー洗浄回路15による洗浄処理とする洗浄処理回路の切り替えが行なわれる連続酸洗処理ラインにおける酸洗鋼帯の洗浄装置。
The steel strip is washed with water that does not contain cleaning chemicals on the exit side of the pickling section after the pickling treatment where the surface scale of the steel strip is dissolved and removed with an acid solution in a pickling treatment device under continuous transfer of the steel strip. A pickling steel strip cleaning device that prevents discoloration of the steel strip by removing the acid solution on the surface,
i) Cleaning water spray nozzles 4 (4 1 , 4 2 , 4 3 ) along the steel strip pass line in the multiple-stage rinsing tanks 8 (8 1 , 8 2 , 8 3 ...) connected in the direction of steel strip transfer. ...)
ii) A ringer roll 3 (3 1 , 3 2 , 3 3 ...) that is positioned between the adjacent rinsing tanks and is opposed to the upper and lower sides across the steel strip pass line is disposed and the steel strip is transferred. Weirs 9 (9 1 , 9 2 ...) Orthogonal to the direction are provided at the tank bottoms, and the tank bottoms are used as washing water storage pits 10 (10 1 , 10 2 , 10 3 ...), And the weirs (9 1 , 9 2 ..., So that a cascade flow of wash water that sequentially overflows each weir (9 1 , 9 2 ...) From the wash water storage pit on the line end side to the wash water storage pit on the start end side is formed. The weir height that gradually decreases from the weir on the line end side to the weir on the start end side,
iii) Water that does not contain cleaning chemicals as cleaning water stored in the cleaning water storage pit 10 is supplied from the water supply nozzle 12 that opens to the rinsing tank on the end side of the steel strip pass line, and the cleaning water storage pit on the end side From the above-mentioned cascade flow, the wash water is stored in each of the wash water storage pits that reach the wash water storage pit on the start end side, and the wash water is replenished from the water supply pipe in a timely manner, so that the surplus water amount in the wash water storage pit 10 is By discharging from the cleaning water storage pit on the side, the cleaning water in the cleaning water storage pit is always kept at a predetermined cleanliness,
iv) Circulating spray cleaning circuit 13 (13 1 , 13) that pumps up the cleaning water in each cleaning water storage pit 10 and sprays it on the steel strip surface from the spray nozzles (4 1 , 4 2 , 4 3 ...) of each rinsing tank 2 , 13 3 ... Are provided for each rinsing tank (8 1 , 8 2 , 8 3 ...), And unused new washing water that does not contain cleaning chemicals is added to the spray nozzles 4 (4 1 , 4,. 4 2, 4 3 ...) fresh water spray cleaning circuit 15 sprayed on the steel strip surface (15 1, 15 2, 15 3 ...) provided from,
During the steady operation in which the steel strip is transferred at a predetermined line speed, the cleaning process is performed by the circulating spray cleaning circuit 13, and when the steel strip is transferred at a low speed or when the transfer is stopped, the cleaning process is performed by the fresh water spray cleaning circuit 15. An apparatus for cleaning a pickled steel strip in a continuous pickling line in which the cleaning circuit is switched.
非定常運転状態において、ライン上流側のリンス槽のみ、循環スプレー洗浄処理から新水スプレー洗浄処理への切替えが行なわれ、下流側のリンス槽は循環スプレー洗浄処理が継続されるように構成されている請求項4に記載の連続酸洗処理ラインにおける酸洗鋼帯の洗浄装置。   In the unsteady operation state, only the rinse tank on the upstream side of the line is switched from the circulating spray cleaning process to the fresh water spray cleaning process, and the downstream rinse tank is configured to continue the circulating spray cleaning process. An apparatus for cleaning a pickled steel strip in a continuous pickling treatment line according to claim 4. 鋼帯の移送を停止した非定常運転状態において、前記新水スプレー洗浄処理により鋼帯表面の残留酸液が除去された時点で、前記新水スプレー洗浄処理から前記循環スプレー洗浄処理に切り替えられるように構成されている請求項4又は請求項5に記載の連続酸洗処理ラインにおける酸洗鋼帯の洗浄装置。   In the unsteady operation state in which the transfer of the steel strip is stopped, when the residual acid solution on the surface of the steel strip is removed by the new water spray cleaning process, the fresh water spray cleaning process is switched to the circulating spray cleaning process. The washing apparatus of the pickling steel strip in the continuous pickling processing line of Claim 4 or Claim 5 comprised by these.
JP2005218155A 2005-07-28 2005-07-28 Cleaning method for pickled steel strip in continuous pickling treatment line and cleaning apparatus Withdrawn JP2007031791A (en)

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Effective date: 20081007