JPH0581275U - Steel strip pickling device with waste acid recovery tank - Google Patents

Steel strip pickling device with waste acid recovery tank

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Publication number
JPH0581275U
JPH0581275U JP2955592U JP2955592U JPH0581275U JP H0581275 U JPH0581275 U JP H0581275U JP 2955592 U JP2955592 U JP 2955592U JP 2955592 U JP2955592 U JP 2955592U JP H0581275 U JPH0581275 U JP H0581275U
Authority
JP
Japan
Prior art keywords
tank
pickling
acid
upstream
rinse
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.)
Pending
Application number
JP2955592U
Other languages
Japanese (ja)
Inventor
季男 信原
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 JP2955592U priority Critical patent/JPH0581275U/en
Publication of JPH0581275U publication Critical patent/JPH0581275U/en
Pending legal-status Critical Current

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Abstract

(57)【要約】 【目的】 最終酸洗槽とリンス槽間に設けたリンガーロ
ールから流出する酸洗液を、リンス廃水として処理する
ことなく回収する。 【構成】 複数の酸洗槽1とリンス槽9からなる横型酸
洗装置の最終酸洗槽1とリンス槽9の間に酸液濃度計2
4を有する排酸回収槽22を設けると共に、排酸回収槽
22と上流各酸洗槽1あるいは上流各酸液貯留槽2とを
接続する導管23に制御弁25、26を設け、酸液濃度
計24の酸濃度に応じて上流各酸洗槽1あるいは上流各
酸液貯留槽2の制御弁25、26の開閉を制御する制御
部27を設ける。 【効果】 最終酸洗槽から流出する酸洗液を回収して再
使用することができ、酸洗液の原単位の低減、中和処理
コストの低減を図ることができる。
(57) [Summary] [Purpose] The pickling solution that flows out from the ringer roll provided between the final pickling tank and the rinsing tank is recovered as rinse wastewater without being treated. [Structure] An acid concentration meter 2 is provided between a final pickling tank 1 and a rinse tank 9 of a horizontal pickling apparatus including a plurality of pickling tanks 1 and a rinse tank 9.
4 is provided, and control valves 25 and 26 are provided in a conduit 23 that connects the waste acid recovery tank 22 and each upstream pickling tank 1 or each upstream acid solution storage tank 2 to control the acid solution concentration. A control unit 27 is provided to control the opening and closing of the control valves 25 and 26 of the upstream pickling tanks 1 or the upstream acid solution storage tanks 2 according to the total acid concentration of 24. [Effect] The pickling solution flowing out from the final pickling tank can be recovered and reused, and the unit consumption of the pickling solution and the cost of the neutralization treatment can be reduced.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

この考案は、熱間圧延工程等で鋼帯表面に生成した酸化スケール皮膜を連続的 に酸洗除去する複数の酸洗槽とリンス槽からなる横型酸洗装置に関する。 The present invention relates to a horizontal pickling apparatus including a plurality of pickling tanks and a rinse tank for continuously pickling and removing an oxide scale film formed on the surface of a steel strip in a hot rolling process or the like.

【0002】[0002]

【従来の技術】[Prior Art]

鋼帯を塩酸や硫酸等の酸洗液に通して表面の酸化スケール皮膜を除去する酸洗 装置には、各種の型式があるが、最近は熱エネルギー節減の観点から、酸洗槽の 槽深さが浅いローバス型、シャロ型等の浅浴浸漬式や、槽深さが浅くて、かつ槽 内の酸洗液を撹拌させることにより酸洗処理時間の短縮を図ったタービュランス 型、噴流型等の噴流撹拌式の酸洗装置が広く使用されつつある。 There are various types of pickling equipment that removes the oxide scale film on the surface by passing the steel strip through a pickling solution such as hydrochloric acid or sulfuric acid, but recently, from the viewpoint of saving heat energy, the depth of the pickling tank is deep. Shallow bath immersion type such as low bath type, charo type, etc., turbulence type, jet type, etc. that has a shallow bath depth and agitates the pickling solution in the bath to shorten the pickling time. The jet agitation type pickling device is widely used.

【0003】 鋼帯酸洗装置の一例としてタービュランス型を例に挙げて説明する。タービュ ランス型酸洗装置は、図4、図5に示すとおり、酸洗槽31が通常3〜5槽(図 4では3槽)連設されており、酸液貯留槽32内の酸洗液がポンプ33によって 加圧され、メインヘッダー34およびサイドヘッダー35から各酸洗槽31内を 通過する鋼帯36に噴射され、鋼帯36表面の酸化スケール皮膜が除去される。 各酸洗槽31内に噴射された酸洗液は、それぞれ戻り配管37を通って各酸液貯 留槽32へ戻り、再び各酸洗槽31内に噴射される。A turbulence type will be described as an example of the steel strip pickling apparatus. As shown in FIG. 4 and FIG. 5, the turbulence type pickling device is normally provided with 3 to 5 pickling tanks 31 (three tanks in FIG. 4) connected in series. Is pressurized by the pump 33 and is sprayed from the main header 34 and the side header 35 onto the steel strip 36 passing through each of the pickling tanks 31, and the oxide scale film on the surface of the steel strip 36 is removed. The pickling solution sprayed into each pickling tank 31 returns to each pickling solution storage tank 32 through each return pipe 37, and is again sprayed into each pickling tank 31.

【0004】 また、最終酸洗槽31の後部には、プレリンス槽38と複数のリンス槽39が 接続され、鋼帯36表面に残存する酸洗液を洗い流すために、ポンプ40で加圧 されたリンス水がスプレーヘッダー41から噴射される。プレリンス槽38内で 噴射されて酸洗液を含んだリンス廃水は、配管42を介して槽外へ排出される。 各酸洗槽31、31の間、最終酸洗槽31とプレリンス槽38の間およびプレ リンス槽38とリンス槽39の間には、酸洗液やリンス水が各槽間を移動するの を防止するため、上下一対のリンガーロール43、44および45が設けられて いる。 さらに、最終酸洗槽31の酸液貯留槽32には、補給配管46を介して新しい 酸洗液が供給され、最終酸洗槽31から順次上流の酸洗槽31にカスケードポン プ47により補給量に見合う量の酸洗液が供給され、この間に鋼帯36表面の酸 化スケールと反応し、廃酸となった酸洗液は、最上流酸洗槽31からポンプ48 により図示しない酸回収装置に送給され、再生されたの補給配管46を介して最 終酸洗槽31の酸液貯留槽32に返送される。A pre-rinse tank 38 and a plurality of rinse tanks 39 are connected to the rear part of the final pickling tank 31, and a pump 40 pressurizes the pickling solution remaining on the surface of the steel strip 36. The rinse water is sprayed from the spray header 41. The rinse wastewater that has been sprayed in the pre-rinse tank 38 and contains the pickling solution is discharged to the outside of the tank through the pipe 42. Between the respective pickling tanks 31, 31, the final pickling tank 31 and the pre-rinse tank 38, and the pre-rinse tank 38 and the rinse tank 39, pickling solution and rinse water are moved between the respective tanks. To prevent this, a pair of upper and lower ringer rolls 43, 44 and 45 are provided. Further, a new pickling solution is supplied to the pickling solution storage tank 32 of the final pickling tank 31 via a replenishment pipe 46, and the final pickling tank 31 is sequentially replenished to the pickling tank 31 upstream by a cascade pump 47. An amount of pickling solution corresponding to the amount is supplied, and during this time, the pickling solution which has reacted with the acid scale on the surface of the steel strip 36 and becomes waste acid is recovered from the most upstream pickling tank 31 by a pump 48, not shown. It is sent to the apparatus and returned to the acid solution storage tank 32 of the final pickling tank 31 through the regenerated supply pipe 46.

【0005】[0005]

【考案が解決しようとする課題】[Problems to be solved by the device]

上記従来の酸洗装置においては、最終酸洗槽31とプレリンス槽38の間に設 けられたリンガーロール44によって、酸洗液のプレリンス槽38への流出(移 動)を防止しているが、その流出量は、リンガーロール44の表面状況や鋼帯通 過速度により大きく左右され、一定ではない。すなわち、酸洗液の流出量は、リ ンガーロール44の損耗が進行するにつれ、また鋼帯通過速度が高速になるに連 れて増加し、プレリンス槽38から排出されるリンス廃水の酸濃度が高くなる。 このような条件下で排出されるリンス廃水は、酸洗液を多量に含有しており、 まだ十分使用し得る状態にある。したがって、このリンス廃水を中和処理して投 棄したのでは、酸洗液原単位および中和処理コストの増大を招くこととなり多大 の損失となる。 また、スプレーヘッダー41から噴霧されたリンス水は、最終酸洗槽31内に 流入し、最終酸洗槽31の酸液濃度が確保できず、濃度確保のため多量の酸液を 投入するため、酸液原単位が悪化する。 In the above-mentioned conventional pickling apparatus, the ringer roll 44 provided between the final pickling tank 31 and the pre-rinsing tank 38 prevents the pickling solution from flowing out (moving) to the pre-rinsing tank 38. The outflow amount is not constant because it largely depends on the surface condition of the ringer roll 44 and the steel strip passing speed. That is, the outflow amount of the pickling solution increases as the wear of the ringer roll 44 progresses and as the steel strip passing speed increases, and the acid concentration of the rinse waste water discharged from the pre-rinse tank 38 becomes high. Become. The rinse wastewater discharged under such conditions contains a large amount of pickling solution and is still in a state in which it can be sufficiently used. Therefore, if this rinse wastewater is neutralized and discarded, the cost of the pickling solution and the cost of neutralization will increase, resulting in a large loss. Further, the rinse water sprayed from the spray header 41 flows into the final pickling tank 31, the acid solution concentration in the final pickling tank 31 cannot be secured, and a large amount of acid solution is added to secure the concentration. The basic unit of acid liquid deteriorates.

【0006】 この考案の目的は、最終酸洗槽とリンス槽間に設けたリンガーロールから流出 する酸洗液を、リンス廃水として処理することなく回収できる酸洗装置を提供す ることにある。An object of the present invention is to provide a pickling apparatus capable of recovering a pickling solution flowing out from a ringer roll provided between a final pickling tank and a rinse tank without treating it as rinse wastewater.

【0007】[0007]

【課題を解決するための手段】[Means for Solving the Problems]

本考案者らは、上記目的を達成すべく鋭意検討を重ねた。その結果、最終酸洗 槽とプレリンス槽との間に排酸回収槽を設け、該排酸回収槽と低濃度酸洗液を貯 留する上流酸洗槽または上流酸洗液貯留槽を導管によって接続することにより、 最終酸洗槽とプレリンス槽間に設けたリンガーロールから流出する酸洗液を、リ ンス廃水として処理することなく回収できるとの結論に至り、この考案に到達し た。 The present inventors have conducted extensive studies to achieve the above object. As a result, an exhausted acid recovery tank is provided between the final pickling tank and the pre-rinse tank, and the exhausted acid recovery tank and the upstream pickling tank or the upstream pickling solution storage tank for storing the low-concentration pickling solution are provided by conduits. It was concluded that the connection makes it possible to recover the pickling solution flowing out from the ringer roll provided between the final pickling tank and the pre-rinsing tank without treating it as a rinse wastewater, and arrived at the present invention.

【0008】 すなわちこの考案は、複数の酸洗槽とリンス槽からなる横型酸洗装置において 、最終酸洗槽とリンス槽の間に排酸回収槽を設けると共に、排酸回収槽と上流酸 洗槽あるいは上流酸液貯留槽とを導管で接続してなる排酸回収槽を備えた鋼帯酸 洗装置である。That is, the present invention provides a horizontal pickling apparatus including a plurality of pickling tanks and a rinsing tank, which is provided with an exhausted acid recovery tank between the final pickling tank and the rinse tank, This is a steel strip pickling device equipped with a waste acid recovery tank that is connected to a tank or an upstream acid solution storage tank by a conduit.

【0009】 また、複数の酸洗槽とリンス槽からなる横型酸洗装置の最終酸洗槽とリンス槽 の間に酸液濃度計を有する排酸回収槽を設けると共に、排酸回収槽と上流各酸洗 槽あるいは上流各酸液貯留槽とを接続する導管に制御弁を設け、酸液濃度計の酸 濃度に応じて上流各酸洗槽あるいは上流各酸液貯留槽の制御弁の開閉を制御する 制御部を設けてなる排酸回収槽を備えた鋼帯酸洗装置である。Further, an exhaust acid recovery tank having an acid concentration meter is provided between the final pickling tank and the rinse tank of the horizontal pickling apparatus including a plurality of pickling tanks and a rinse tank, and the exhaust acid recovery tank and the upstream side are provided. A control valve is installed in the conduit that connects each pickling tank or each upstream acid solution storage tank, and opens or closes the control valve of each upstream pickling tank or each upstream acid solution storage tank according to the acid concentration of the acid solution concentration meter. It is a steel strip pickling apparatus equipped with a waste acid recovery tank provided with a control unit for controlling.

【0010】 さらに、複数の酸洗槽とリンス槽からなる横型酸洗装置の最終酸洗槽とリンス 槽の間に排酸回収槽を設けると共に、排酸回収槽と上流酸洗槽あるいは上流酸液 貯留槽とを導管で接続した鋼帯酸洗装置において、最終酸洗槽とプレリンス槽と を区画する仕切り壁とプレリンス槽水スプレーノズル間にリンガーロールを設け 、該リンガーロールの上流側にライン速度が所定値以下の状態に連動して水を噴 射するスプレーノズルを設けてなる排酸回収槽を備えた鋼帯酸洗装置である。Further, an exhaust acid recovery tank is provided between the final pickling tank and the rinse tank of the horizontal pickling apparatus including a plurality of pickling tanks and a rinse tank, and the exhaust acid recovery tank and the upstream pickling tank or the upstream pickling tank are provided. In a steel strip pickling device that connects a liquid storage tank with a conduit, a ringer roll is provided between the partition wall that divides the final pickling tank and the pre-rinse tank and the water spray nozzle of the pre-rinse tank, and a line is provided upstream of the ringer roll. It is a steel strip pickling device equipped with an exhaust acid recovery tank provided with a spray nozzle that sprays water in conjunction with a state where the speed is below a predetermined value.

【0011】[0011]

【作用】[Action]

この考案においては、最終酸洗槽とリンス槽の間に排酸回収槽を設けると共に 、排酸回収槽と上流酸洗槽あるいは上流酸液貯留槽とを導管で接続したから、最 終酸洗槽とプレリンス槽との間のリンガーロールで阻止できずに流出した酸洗液 は、一部リンス水によって希釈されるが、大部分が排酸回収槽内に落下し、リン ス廃水とは別に、上流側の低濃度酸洗槽または酸液貯留槽へ回収され、再使用に 供される。 In this invention, an exhaust acid recovery tank is provided between the final pickling tank and the rinsing tank, and the exhaust acid recovery tank and the upstream pickling tank or the upstream acid solution storage tank are connected by a conduit. The pickling solution that could not be blocked by the Ringer roll between the tank and the pre-rinse tank was partially diluted with the rinse water, but most of it was dropped into the waste acid recovery tank and separated from the rinse waste water. , And is collected in the upstream low-concentration pickling tank or acid solution storage tank for reuse.

【0012】 また、最終酸洗槽とリンス槽の間に酸液濃度計を有する排酸回収槽を設けると 共に、排酸回収槽と上流各酸洗槽あるいは上流各酸液貯留槽とを接続する導管に 制御弁を設け、酸液濃度計の酸濃度に応じて上流各酸洗槽あるいは上流各酸液貯 留槽の制御弁の開閉を制御する制御部を設けたから、操業条件等によって変動す る回収酸洗液濃度を測定し、最適な濃度条件の上流酸洗槽あるいは上流酸液貯留 槽へ送液されるため、酸洗液の再使用効率を更に高めることができる。Further, an exhaust acid recovery tank having an acid solution concentration meter is provided between the final pickling tank and the rinse tank, and the exhaust acid recovery tank is connected to each upstream pickling tank or each upstream acid solution storage tank. A control valve is installed in the conduit to control the opening and closing of the control valve of each upstream pickling tank or each upstream acid solution storage tank according to the acid concentration of the acid concentration meter. Since the concentration of the recovered pickling solution is measured and sent to the upstream pickling tank or the upstream pickling solution storage tank under the optimum concentration condition, the reuse efficiency of the pickling solution can be further increased.

【0013】 さらに、最終酸洗槽とプレリンス槽とを区画する仕切り壁とプレリンス槽水ス プレーノズル間にリンガーロールを設けたから、リンス水の排酸回収槽への混入 が抑制されて酸洗液濃度の低下が防止でき、再利用価値を高めることができる。 また、該リンガーロールの上流側にライン速度が所定値以下の状態(例えばライ ン停止または一定速度以下、具体的には20〜30m/min以下)に連動して 水を噴射するスプレーノズルを設けたから、ライン速度が所定値以下となるとこ れに連動してスプレーノズル水が噴射され、リンガーロールとリンガーロール間 の鋼帯表面の乾燥による酸洗変色を防止することができる。Furthermore, since the ringer roll is provided between the partition wall that divides the final pickling tank and the pre-rinse tank and the water spray nozzle of the pre-rinse tank, the rinse water is suppressed from mixing into the waste acid recovery tank, and the pickling solution is It is possible to prevent the concentration from decreasing and to enhance the reuse value. Further, a spray nozzle for injecting water is provided on the upstream side of the ringer roll in conjunction with a state where the line speed is a predetermined value or less (for example, line stop or a certain speed or less, specifically 20 to 30 m / min or less). Therefore, when the line speed falls below a predetermined value, the spray nozzle water is sprayed in tandem with this, and it is possible to prevent pickling discoloration due to the drying of the steel strip surface between the ringer rolls.

【0014】[0014]

【実施例】【Example】

以下にこの考案について、実施の一例を示す図1ないし図3に基いて詳述する 。図1はこの考案を実施したタービュランス型噴流撹拌方式の横型酸洗装置の一 例を示す横断面図、図3は排酸回収槽部分の詳細横断面図、図3は最終酸洗槽の リンガーロールとプレリンス槽のリンス水スプレーノズル間にリンガーロールと ライン停止に連動して水を噴射するスプレーノズルを設けた場合の排酸回収槽部 分の詳細横断面図である。 This invention will be described in detail below with reference to FIGS. Fig. 1 is a cross-sectional view showing an example of a turbulence-type jet agitation type horizontal pickling apparatus according to the present invention, Fig. 3 is a detailed cross-sectional view of a waste pickling tank, and Fig. 3 is a ringer of the final pickling tank. FIG. 3 is a detailed cross-sectional view of the waste acid recovery tank part when a ringer roll and a spray nozzle that sprays water in conjunction with line stop are provided between the roll and the rinse water spray nozzle of the pre-rinse tank.

【0015】 図1および図2において、3槽の酸洗槽1が連設されており、各酸洗槽1には 各酸液貯留槽2の酸洗液がポンプ3によって加圧され、メインヘッダー4および サイドヘッダー5から各酸洗槽1内を通過する鋼帯6に噴射され、鋼帯6表面の 酸化スケール皮膜が除去される。各酸洗槽1内に噴射された酸洗液は、それぞれ 戻り配管7を通って各酸液貯留槽2へ戻り、再び各酸洗槽1内に噴射される。 また、最終酸洗槽1の後部には、プレリンス槽8と仕切り壁21によって区切 られ排酸回収槽22、プレリンス槽8および複数のリンス槽9(図面では1槽の み)が接続され、鋼帯6表面に残存する酸洗液を洗い流すために、ポンプ10で 加圧されたリンス水がスプレーヘッダー11から噴射される。プレリンス槽8内 で噴射されて酸洗液を含んだリンス廃水は、配管12を介して槽外へ排出される 。In FIG. 1 and FIG. 2, three pickling tanks 1 are connected in series, and the pickling solution in each pickling solution storage tank 2 is pressurized by a pump 3 in each pickling tank 1. It is sprayed from the header 4 and the side header 5 onto the steel strip 6 passing through each pickling tank 1, and the oxide scale film on the surface of the steel strip 6 is removed. The pickling solution sprayed into each pickling tank 1 returns to each pickling solution storage tank 2 through the return pipe 7 and is again sprayed into each pickling tank 1. Further, in the rear part of the final pickling tank 1, a pre-rinse tank 8 and a partition wall 21 are connected, and an exhaust acid recovery tank 22, a pre-rinse tank 8 and a plurality of rinse tanks 9 (only one tank in the drawing) are connected to each other. Rinse water pressurized by the pump 10 is sprayed from the spray header 11 in order to wash away the pickling solution remaining on the surface of the strip 6. The rinse wastewater that has been sprayed in the pre-rinse tank 8 and contains the pickling solution is discharged to the outside of the tank through the pipe 12.

【0016】 各酸洗槽1、1の間、最終酸洗槽1と排酸回収槽22の間およびプレリンス槽 8とリンス槽9の間には、酸洗液やリンス水が各槽間を移動するのを防止するた め、上下一対のリンガーロール13、14および15が設けられている。 さらに、最終酸洗槽1には、補給配管16を介して所定の濃度(例えばHCl :12〜15%)に調整された新酸洗液が供給され、最終酸洗槽1から順次上流 の酸洗槽1にカスケードポンプ17により供給量に見合う量の酸洗液が移送され 、この間に鋼帯6表面の酸化スケールと反応し、廃酸となった酸洗液は、最上流 酸洗槽1からポンプ18により図示しない酸回収装置に送給され、再生されたの 供給管16を介して最終酸洗槽1に返送される。Between the pickling tanks 1 and 1, between the final pickling tank 1 and the waste acid recovery tank 22, and between the pre-rinsing tank 8 and the rinse tank 9, pickling solution and rinse water are passed between the tanks. In order to prevent the movement, a pair of upper and lower ringer rolls 13, 14 and 15 are provided. Further, the final pickling tank 1 is supplied with a new pickling solution adjusted to a predetermined concentration (for example, HCl: 12 to 15%) via the replenishment pipe 16, and the pickling solution from the final pickling tank 1 is sequentially supplied to the upstream pickling solution. The amount of pickling solution commensurate with the supply amount is transferred to the washing tank 1 by the cascade pump 17, and during this period, the pickling solution which has reacted with the oxide scale on the surface of the steel strip 6 and becomes waste acid is the most upstream pickling tank 1. Is sent from a pump 18 to an acid recovery device (not shown), and is returned to the final pickling tank 1 via the regenerated supply pipe 16.

【0017】 また、前記排酸回収槽22は、各上流側酸液貯留槽2と導管23によって接続 されている。さらに、導管23には、酸液濃度計24が設けられ、測定した酸液 濃度に応じて特定の酸液貯留槽2または酸洗槽1へ送液するための開閉弁25、 26が導管23中の酸液濃度計24以降に設けられている。 酸液濃度計24で測定された酸液濃度は、開閉弁25、26の制御部27に出 力される。制御部27は、酸液濃度計24から入力される酸液濃度に応じて、酸 液濃度が5〜7%以下ならば最上流側酸液貯留槽2へ、酸液濃度が7%以上なら ば最上流の次の酸液貯留槽2へ回収された排酸を導くよう開閉弁25、26を開 閉制御するよう構成されている。Further, the discharged acid recovery tank 22 is connected to each upstream acid solution storage tank 2 by a conduit 23. Further, the conduit 23 is provided with an acid solution concentration meter 24, and opening / closing valves 25, 26 for delivering the solution to a specific acid solution storage tank 2 or a pickling tank 1 are provided in the conduit 23 according to the measured acid solution concentration. It is provided after the inside of the acid concentration meter 24. The acid solution concentration measured by the acid solution concentration meter 24 is output to the control unit 27 of the opening / closing valves 25 and 26. According to the acid solution concentration input from the acid solution concentration meter 24, the control unit 27 sends to the uppermost stream side acid solution storage tank 2 if the acid solution concentration is 5 to 7% or less, and if the acid solution concentration is 7% or more. For example, the on-off valves 25 and 26 are controlled to be opened and closed so as to guide the recovered waste acid to the next highest acid solution storage tank 2.

【0018】 さらに、図3に示すとおり、プレリンス槽8のスプレーヘッダー11と仕切り 壁21との間に、さらにリンガーロール28を設けると共に、リンガーロール2 8とリンガーロール14との間にライン停止に連動して水をスプレーするスプレ ーノズル29を設け、ラインが停止すれば、スプレーノズル29から鋼帯6の表 面に水が噴霧されるよう構成する。Further, as shown in FIG. 3, a ringer roll 28 is further provided between the spray header 11 and the partition wall 21 of the pre-rinse tank 8, and the line is stopped between the ringer roll 28 and the ringer roll 14. A spray nozzle 29 for spraying water is provided in conjunction with the spray nozzle 29. When the line is stopped, water is sprayed from the spray nozzle 29 onto the surface of the steel strip 6.

【0019】 上記のとおり構成したから、最終酸洗槽1のリンガーロール14で捕捉できず に流出する比較的高濃度の酸洗液は、排酸回収槽22内に収容され、導管23を 通って比較的低濃度の上流側酸液貯留槽2へと導入される。 排酸回収槽22で回収される酸洗液の酸濃度は、操業条件によって変化するが 、導管23の途中に設けた酸液濃度計24によって測定され、開閉制御部27に 出力され、酸液濃度に応じて開閉弁25、26を開閉制御し、酸液濃度が5〜7 %以下ならば最上流側酸液貯留槽2へ、酸液濃度が7%以上ならば最上流の次の 酸液貯留槽2へ回収された排酸が導入される。 この結果、従来リンス廃水として中和処理されていた最終酸洗槽1から流出し た比較的高濃度の酸洗液は、回収して再使用することができるから、酸洗液の原 単位の低減、中和処理コストの低減を図ることができる。With the above-described structure, the relatively high-concentration pickling solution that cannot be captured by the Ringer roll 14 of the final pickling tank 1 and is discharged is stored in the waste acid recovery tank 22 and passes through the conduit 23. And is introduced into the upstream acid solution storage tank 2 having a relatively low concentration. Although the acid concentration of the pickling solution recovered in the waste acid recovery tank 22 changes depending on the operating conditions, it is measured by an acid solution concentration meter 24 provided in the middle of the conduit 23 and output to the opening / closing control unit 27. The on-off valves 25 and 26 are controlled to open and close according to the concentration, and if the acid solution concentration is 5 to 7% or less, it goes to the most upstream acid solution storage tank 2. If the acid solution concentration is 7% or more, the next most upstream acid solution is used. The recovered waste acid is introduced into the liquid storage tank 2. As a result, the relatively high-concentration pickling solution discharged from the final pickling tank 1, which was conventionally neutralized as rinse wastewater, can be recovered and reused. It is possible to reduce the cost of the neutralization treatment.

【0020】 さらに、プレリンス槽8のスプレーヘッダー11と仕切り壁21との間に、さ らにリンガーロール28を設けたから、スプレーヘッダー11からのリンス水が 排酸回収槽22へ混入するのが抑制される。また、リンガーロール28とリンガ ーロール14との間にライン停止に連動して水をスプレーするスプレーノズル2 9を設けたから、ラインが停止すれば、スプレーノズル29から鋼帯6の表面に 水が噴霧され、ライン停止時におけるリンガーロール28とリンガーロール14 間の鋼帯6表面の乾燥による酸洗変色を防止することができる。Further, since the ringer roll 28 is further provided between the spray header 11 and the partition wall 21 of the pre-rinse tank 8, it is possible to prevent the rinse water from the spray header 11 from mixing into the waste acid recovery tank 22. To be done. Further, since the spray nozzle 29 for spraying water is provided between the ringer roll 28 and the ringer roll 14 in conjunction with the line stop, if the line is stopped, the water is sprayed from the spray nozzle 29 onto the surface of the steel strip 6. Therefore, it is possible to prevent discoloration due to pickling due to drying of the surface of the steel strip 6 between the Ringer roll 28 and the Ringer roll 14 when the line is stopped.

【0021】 なお、上記実施例においては、3槽の酸洗槽1とプレリンス槽8を有するター ビュランス型酸洗装置の例を挙げたが、4槽以上の酸洗槽を有する場合、プレリ ンス槽を装備せず、最終酸洗槽が直接リンス槽に連設する場合、あるいは他の型 式の横型酸洗装置の場合にも適用することができる。 また、導管23に高低差がなく、排酸回収槽22から酸液貯留槽2に回収した 排酸を導入できない場合は、導管23の途中に専用ポンプを設け、圧送すること もできる。In the above-mentioned embodiment, the turbulence type pickling apparatus having the three pickling tanks 1 and the pre-rinsing tank 8 is taken as an example. The present invention can also be applied to the case where the final pickling tank is directly connected to the rinse tank without equipping the tank, or to the case of another type of horizontal pickling device. Further, when there is no difference in height in the conduit 23 and the recovered acid cannot be introduced from the recovered acid recovery tank 22 into the acid solution storage tank 2, a dedicated pump can be provided in the conduit 23 for pressure feeding.

【0022】[0022]

【考案の効果】[Effect of the device]

以上述べたとおり、この考案によれば、最終酸洗槽から流出する酸洗液を回収 して再使用することができ、流出酸洗液を無駄に中和処理していた従来法に比較 し、酸洗液流出量が多少増加しても、大部分が有効に回収できるから、リンガー ロールの維持、管理が容易となる。しかも、酸洗液の原単位の低減、中和処理コ ストの低減を図ることができる。 As described above, according to the present invention, the pickling solution flowing out from the final pickling tank can be collected and reused, and compared with the conventional method in which the flowing pickling solution was wastefully neutralized. However, even if the amount of pickling solution flowing out is increased to a large extent, most of the pickling solution can be effectively recovered, which makes it easy to maintain and manage the ringer roll. Moreover, it is possible to reduce the basic unit of the pickling solution and the cost of the neutralization treatment.

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

【図1】この考案を実施したタービュランス型噴流撹拌
方式の横型酸洗装置の一例を示す横断面図である。
FIG. 1 is a cross-sectional view showing an example of a turbulence type jet agitation type horizontal pickling apparatus according to the present invention.

【図2】排酸回収槽部分の詳細横断面図である。FIG. 2 is a detailed cross-sectional view of an exhaust acid recovery tank portion.

【図3】最終酸洗槽のリンガーロールとプレリンス槽の
リンス水スプレーノズル間にリンガーロールとライン停
止に連動して水を噴射するスプレーノズルを設けた場合
の排酸回収槽部分の詳細横断面図である。
[Fig. 3] Detailed cross section of the waste acid recovery tank when a ringer roll in the final pickling tank and a rinse water spray nozzle in the pre-rinse tank are provided with a ringer roll and a spray nozzle that sprays water in conjunction with the line stop. It is a figure.

【図4】従来のタービュランス型噴流撹拌方式の横型酸
洗装置の一例を示す横断面図である。
FIG. 4 is a cross-sectional view showing an example of a conventional turbulence jet agitation type horizontal pickling apparatus.

【図5】従来のタービュランス型噴流撹拌方式の横型酸
洗装置の最終酸洗槽とプレリンス槽部分の拡大横断面図
である。
FIG. 5 is an enlarged cross-sectional view of a final pickling tank and a pre-rinse tank portion of a conventional turbulence jet agitation type horizontal pickling apparatus.

【符号の説明】[Explanation of symbols]

1,31 酸洗槽 2,32 酸液貯留槽 3,10,18,33,40,48 ポンプ 4,34 メインヘッダー 5,35 サイドヘッダー 6,36 鋼帯 7,37 戻り配管 8,38 プレリンス槽 9,39 リンス槽 11,41 スプレーヘッダー 12,42 配管 13,14,15,28,43,44,45 リンガー
ロール 16,46 補給配管 17,47 カスケードポンプ 21 仕切り壁 22 排酸回収槽 23 導管 24 酸液濃度計 25,26 開閉弁 27 制御部 29 スプレーノズル
1,31 Pickling tank 2,32 Acid solution storage tank 3,10,18,33,40,48 Pump 4,34 Main header 5,35 Side header 6,36 Steel strip 7,37 Return pipe 8,38 Pre-rinse tank 9,39 Rinse tank 11,41 Spray header 12,42 Piping 13,14,15,28,43,44,45 Ringer roll 16,46 Replenishment piping 17,47 Cascade pump 21 Partition wall 22 Waste acid recovery tank 23 Conduit 24 Acid solution concentration meter 25,26 Open / close valve 27 Control unit 29 Spray nozzle

Claims (3)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 複数の酸洗槽とリンス槽からなる横型酸
洗装置において、最終酸洗槽とリンス槽の間に排酸回収
槽を設けると共に、排酸回収槽と上流酸洗槽あるいは上
流酸液貯留槽とを導管で接続したことを特徴とする排酸
回収槽を備えた鋼帯酸洗装置。
1. A horizontal pickling apparatus comprising a plurality of pickling tanks and a rinsing tank, wherein an exhausted acid recovery tank is provided between the final pickling tank and the rinse tank, and the exhausted acid recovery tank and the upstream pickling tank or upstream. A steel strip pickling apparatus having an exhaust acid recovery tank, characterized in that it is connected to an acid liquid storage tank by a conduit.
【請求項2】 複数の酸洗槽とリンス槽からなる横型酸
洗装置の最終酸洗槽とリンス槽の間に酸液濃度計を有す
る排酸回収槽を設けると共に、排酸回収槽と上流各酸洗
槽あるいは上流各酸液貯留槽とを接続する導管に制御弁
を設け、酸液濃度計の酸濃度に応じて上流各酸洗槽ある
いは上流各酸液貯留槽の制御弁の開閉を制御する制御部
を設けたことを特徴とする排酸回収槽を備えた鋼帯酸洗
装置。
2. A horizontal pickling apparatus comprising a plurality of pickling tanks and a rinsing tank, an exhaust acid recovery tank having an acid concentration meter is provided between the final pickling tank and the rinse tank, and the exhaust acid recovery tank and the upstream side are provided. A control valve is installed in the conduit connecting each pickling tank or each upstream acid solution storage tank, and the control valve of each upstream pickling tank or each upstream acid solution storage tank is opened and closed according to the acid concentration of the acid concentration meter. A steel strip pickling apparatus having an exhaust acid recovery tank, which is provided with a control unit for controlling.
【請求項3】 複数の酸洗槽とリンス槽からなる横型酸
洗装置の最終酸洗槽とリンス槽の間に排酸回収槽を設け
ると共に、排酸回収槽と上流酸洗槽あるいは上流酸液貯
留槽とを導管で接続した鋼帯酸洗装置において、最終酸
洗槽とプレリンス槽とを区画する仕切り壁とプレリンス
槽水スプレーノズル間にリンガーロールを設け、該リン
ガーロールの上流側にライン速度が所定値以下の状態に
連動して水を噴射するスプレーノズルを設けたことを特
徴とする排酸回収槽を備えた鋼帯酸洗装置。
3. An exhaust acid recovery tank is provided between a final pickling tank and a rinse tank of a horizontal pickling apparatus including a plurality of pickling tanks and a rinse tank, and the exhaust acid recovery tank and the upstream pickling tank or the upstream acid is provided. In a steel strip pickling apparatus in which a liquid storage tank is connected by a conduit, a ringer roll is provided between the partition wall that partitions the final pickling tank and the pre-rinse tank and the pre-rinse tank water spray nozzle, and a line is provided on the upstream side of the ringer roll. A steel strip pickling apparatus having an exhaust acid recovery tank, characterized in that a spray nozzle for injecting water is provided in association with a state in which the speed is below a predetermined value.
JP2955592U 1992-04-06 1992-04-06 Steel strip pickling device with waste acid recovery tank Pending JPH0581275U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2955592U JPH0581275U (en) 1992-04-06 1992-04-06 Steel strip pickling device with waste acid recovery tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2955592U JPH0581275U (en) 1992-04-06 1992-04-06 Steel strip pickling device with waste acid recovery tank

Publications (1)

Publication Number Publication Date
JPH0581275U true JPH0581275U (en) 1993-11-05

Family

ID=12279394

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2955592U Pending JPH0581275U (en) 1992-04-06 1992-04-06 Steel strip pickling device with waste acid recovery tank

Country Status (1)

Country Link
JP (1) JPH0581275U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007224356A (en) * 2006-02-23 2007-09-06 Jfe Steel Kk Effluent treatment method in line for pickling steel strip, and effluent treatment facility therefor
CN114622214A (en) * 2022-03-07 2022-06-14 盐城市星凯环保科技股份有限公司 Nickel-iron-chromium electrothermal alloy pickling treatment device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007224356A (en) * 2006-02-23 2007-09-06 Jfe Steel Kk Effluent treatment method in line for pickling steel strip, and effluent treatment facility therefor
CN114622214A (en) * 2022-03-07 2022-06-14 盐城市星凯环保科技股份有限公司 Nickel-iron-chromium electrothermal alloy pickling treatment device
CN114622214B (en) * 2022-03-07 2023-09-05 盐城市星凯环保科技股份有限公司 Nickel-iron-chromium electrothermal alloy pickling treatment device

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