JP2000189834A - Method and apparatus for purifying cleaning liquid - Google Patents

Method and apparatus for purifying cleaning liquid

Info

Publication number
JP2000189834A
JP2000189834A JP10367138A JP36713898A JP2000189834A JP 2000189834 A JP2000189834 A JP 2000189834A JP 10367138 A JP10367138 A JP 10367138A JP 36713898 A JP36713898 A JP 36713898A JP 2000189834 A JP2000189834 A JP 2000189834A
Authority
JP
Japan
Prior art keywords
sludge
cleaning liquid
container
pickling
valve
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
JP10367138A
Other languages
Japanese (ja)
Inventor
Toshihiro Mori
俊博 森
Koichi Takeuchi
孝一 武内
Toru Matsuhashi
透 松橋
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 JP10367138A priority Critical patent/JP2000189834A/en
Publication of JP2000189834A publication Critical patent/JP2000189834A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To separate and remove sludge with a simple apparatus without corrosion even when a cleaning liquid such as a pickling liquid is treated and to circulate the cleaning liquid to be used by installing a nonmagnetic container which is arranged in a separation tank and makes sludge adhere to the container and a sludge removing apparatus. SOLUTION: Inlet side piping 1a for supplying a pickling liquid before sludge separation treatment and outlet side piping 1b for discharging the pickling liquid after separation treatment are connected to a separation tank 2. A nonmagnetic container 3 is installed in the separation tank 2, a magnetism generator 4 is installed in the container 3, sludge is made to adhere to the surface of the container by magnetic force, and the corrosion of the generator 4 is prevented. A sludge removing apparatus 9 is installed in the tank 2, and sludge adherent to the surface of the container and the coating surface of the generator 4. An inlet side valve 5a, an outlet side valve 5b, and a sludge discharge valve 7 are installed to prevent the mixing of the separated sludge into a pickling liquid.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、容器や鋼材の洗浄
工程において循環利用される洗浄液の浄化装置ならびに
浄化方法に関する。特に、鋼材の酸洗処理で酸洗液に含
まれるスケールを分離し、酸洗液を環流使用する際に用
いる酸洗液の浄化装置ならびに酸洗液の浄化方法に好適
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cleaning apparatus and a cleaning method for a cleaning liquid circulated in a cleaning process for containers and steel materials. In particular, the present invention is suitable for a pickling solution purifying apparatus and a method for purifying a pickling solution which is used when a pickling solution is refluxed by separating scales contained in the pickling solution by pickling treatment of a steel material.

【0002】[0002]

【従来の技術】板、棒、管等の鉄鋼製品の製造工程にお
いて、熱間加工や焼鈍等の熱処理によって鋼表面に生成
するスケ−ルを除去する方法としては、アルカリ溶融塩
処理や中性塩電解処理のようにスケール自体を溶解して
除去する方法と、酸洗によってスケール直下の地金を溶
解して剥離する方法がある。
2. Description of the Related Art In the manufacturing process of steel products such as plates, rods, pipes, etc., as a method of removing scale generated on the steel surface by heat treatment such as hot working or annealing, there are alkali molten salt treatment and neutral method. There are a method of dissolving and removing the scale itself as in a salt electrolytic treatment, and a method of dissolving and peeling the metal immediately below the scale by pickling.

【0003】一般に、前者の方法はスケールが薄い場合
に適用されることが多く、例えばステンレス鋼帯の仕上
げ連続焼鈍酸洗ラインにおいて多用されている。 一
方、後者の方法は熱延後の炭素鋼鋼板のように、スケ−
ルが比較的厚い場合に用いられることが多く、この場合
には剥離したスケールが酸洗液中に蓄積し、酸洗槽の底
部にヘドロ状に堆積する。この堆積物をスラッジとい
う。このスラッジは放置すると固化し、また酸洗液と反
応して酸洗液を劣化させる。このため、定期的にスラッ
ジを酸洗槽外に排出する作業が必要となるが、酸による
薬害の恐れだけでなく、操業を停止しなければならない
ので酸洗の能率が低下する。
[0003] In general, the former method is often applied when the scale is thin, and is often used, for example, in a finish continuous annealing and pickling line for a stainless steel strip. On the other hand, the latter method has a scale like carbon steel sheet after hot rolling.
In many cases, the scale is used in the case where the thickness is relatively thick. In this case, the exfoliated scale accumulates in the pickling solution and accumulates like a sludge at the bottom of the pickling tank. This deposit is called sludge. The sludge solidifies on standing and reacts with the pickling solution to deteriorate the pickling solution. For this reason, it is necessary to periodically discharge the sludge to the outside of the pickling tank, but not only the risk of acid damage due to acid, but also the operation must be stopped, so that the efficiency of pickling is reduced.

【0004】このスラッジを連続的に除去する方法とし
ては、例えば特公平2−10874号公報、特公平7−
126876号公報に、酸洗槽外に酸洗液と共にスラッ
ジを排出し、沈殿槽でスラッジと酸洗液とを分離する設
備が開示されている。
As a method of continuously removing the sludge, for example, Japanese Patent Publication No. 2-10874 and Japanese Patent Publication No.
JP 126876 discloses a facility for discharging sludge together with a pickling liquid outside a pickling tank and separating the sludge and the pickling liquid in a settling tank.

【0005】また、特開平7−213941号公報に
は、磁気力を有する回転円盤とマグネットロールを洗浄
液に浸漬し、円盤とマグネットロールに吸着したスラッ
ジをスクレーパで掻き取り分離する設備が提示されてい
る。
Japanese Patent Application Laid-Open No. 7-213941 discloses a facility in which a rotating disk having a magnetic force and a magnet roll are immersed in a cleaning liquid, and sludge adsorbed on the disk and the magnet roll is scraped off by a scraper and separated. I have.

【0006】[0006]

【発明が解決しようとする課題】特公平2−10874
号公報や特公平7−126876号公報に開示された設
備は、スラッジを酸洗槽から除去することはできるが、
いずれもスラッジと酸洗液の分離に重力沈殿法を用いて
いる。この沈殿法は、スラッジの沈降速度が遅いうえ、
粉状のスケールは沈殿しにくいため沈殿することなく酸
洗槽に環流されるといった問題がある。
[Problems to be Solved by the Invention]
The equipment disclosed in Japanese Patent Publication No. 7-126876 and Japanese Patent Publication No. 7-126876 can remove sludge from the pickling tank,
In each case, gravity sedimentation is used to separate sludge and pickling liquid. This sedimentation method has a slow sludge settling speed,
Since the powdery scale hardly precipitates, there is a problem that the scale is returned to the pickling tank without settling.

【0007】また、特開平7−213941号公報に開
示された方法は、洗浄液が酸溶液やアルカリ溶液などの
場合には、円盤やマグネットロールが腐食するといった
問題があり、酸洗液の浄化装置としては使用することが
できない。また、円盤やスクレーパなどの摩耗によりス
ラッジの掻き取りが充分でないといった問題もある。
The method disclosed in Japanese Patent Application Laid-Open No. 7-213941 has a problem that when the cleaning solution is an acid solution or an alkaline solution, the disk or the magnet roll is corroded. As can not be used. Another problem is that the sludge is not sufficiently scraped off due to abrasion of the disk or scraper.

【0008】本発明の課題は、簡単な設備で、特に酸洗
液などの洗浄液であっても腐食することなくスラッジを
速やかに分離除去し、洗浄液を環流使用することができ
る浄化装置ならびに浄化方法を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a purification apparatus and a purification method capable of quickly separating and removing sludge without corrosion even with a cleaning liquid such as an pickling liquid, and using the cleaning liquid at reflux, with simple equipment. Is to provide.

【0009】[0009]

【課題を解決するための手段】本発明は、上記課題を解
決するものであり、その要旨は以下の(1) 〜(6) のとお
りである。
The present invention solves the above-mentioned problems, and the gist thereof is as follows (1) to (6).

【0010】(1) 洗浄液に混入した鉄分を含むスラッジ
を磁気力により分離する洗浄液の浄化装置であって、分
離前の洗浄液を供給する入側バルブを備えた入側配管と
分離後の洗浄液を排出する出側バルブを備えた出側配管
とを接続した分離槽と、該分離槽の内部に配設されスラ
ッジを付着させる非磁性の容器と、該容器に挿入され磁
気力を有する磁力発生装置と、上記分離槽内部に設けら
れ上記容器の表面に付着したスラッジを除去するスラッ
ジ除去装置と、上記分離槽に接続され除去されたスラッ
ジを排出するスラッジ排出バルブとを設けたことを特徴
とする洗浄液浄化装置。
(1) A cleaning liquid purifying apparatus for separating sludge containing iron contained in a cleaning liquid by magnetic force, comprising an inlet pipe provided with an inlet valve for supplying the cleaning liquid before separation, and a cleaning liquid after separation. A separation tank connected to an outlet pipe having an outlet valve for discharging, a non-magnetic container disposed inside the separation tank for attaching sludge, and a magnetic force generator inserted into the container and having a magnetic force And a sludge removal device provided inside the separation tank for removing sludge attached to the surface of the container, and a sludge discharge valve connected to the separation tank for discharging the removed sludge. Cleaning liquid purifier.

【0011】(2) 磁力発生装置を容器に挿脱する昇降機
構を設けたことを特徴とする上記(1) 項に記載の洗浄液
浄化装置。
(2) The cleaning liquid purifying apparatus according to the above (1), further comprising an elevating mechanism for inserting and removing the magnetic force generating device from the container.

【0012】(3) 洗浄液に混入した鉄分を含むスラッジ
を磁気力により分離する洗浄液の浄化装置であって、分
離前の洗浄液を供給する入側バルブを備えた入側配管と
分離後の洗浄液を排出する出側バルブを備えた出側配管
とを接続した分離槽と、該分離槽の内部に配設され外面
を非磁性の被覆部で覆われた磁気力を有する磁力発生装
置と、上記分離槽内部に設けられ上記被覆部の表面に付
着したスラッジを除去するスラッジ除去装置と、上記分
離槽に接続され除去されたスラッジを排出するスラッジ
排出バルブとを設けたことを特徴とする洗浄液浄化装
置。
(3) A cleaning liquid purifying apparatus for separating sludge containing iron contained in the cleaning liquid by magnetic force, comprising an inlet pipe provided with an inlet valve for supplying the cleaning liquid before separation, and a cleaning liquid after separation. A separation tank connected to an outlet pipe provided with an outlet valve for discharging, a magnetic force generating device having a magnetic force disposed inside the separation tank and having an outer surface covered with a non-magnetic covering portion; A cleaning liquid purifying apparatus comprising: a sludge removing device provided inside a tank for removing sludge adhering to the surface of the coating portion; and a sludge discharging valve connected to the separation tank for discharging the removed sludge. .

【0013】(4) 上記(1) または(2) 項に記載の洗浄液
浄化装置を用い、容器の表面にスラッジを付着させた
後、入側バルブと出側バルブで洗浄液の供給と排出を停
止し、次いでスラッジ除去装置で上記容器の表面に付着
したスラッジを除去し、除去したスラッジをスラッジ排
出バルブから排出することを特徴とする洗浄液の浄化方
法。
(4) After using the cleaning liquid purifying apparatus described in the above (1) or (2) to attach sludge to the surface of the container, supply and discharge of the cleaning liquid are stopped by the inlet valve and the outlet valve. Removing the sludge adhering to the surface of the container with a sludge removing device, and discharging the removed sludge from a sludge discharge valve.

【0014】(5) 上記(3) 項に記載の洗浄液浄化装置を
用い、被覆部の表面にスラッジを付着させた後、入側バ
ルブと出側バルブで洗浄液の供給と排出を停止し、次い
でスラッジ除去装置で上記被覆部の表面に付着したスラ
ッジを除去し、除去したスラッジをスラッジ排出バルブ
から排出することを特徴とする洗浄液の浄化方法。
(5) Using the cleaning liquid purifying apparatus described in the above item (3), after depositing sludge on the surface of the coating portion, supply and discharge of the cleaning liquid are stopped by the inlet valve and the outlet valve, and then A method for purifying a cleaning liquid, comprising removing sludge adhering to the surface of the coating portion with a sludge removing device, and discharging the removed sludge from a sludge discharge valve.

【0015】(6) 上記(1) 〜(3) 項のいずれかに記載の
洗浄液浄化装置を用い、鋼材の酸洗槽内の酸洗液を循環
処理して酸洗液中のスケールを除去分離し、除去分離後
の酸洗液を環流使用することを特徴とする鋼材の酸洗方
法。
(6) Using the cleaning liquid purifying apparatus according to any one of the above (1) to (3), the pickling liquid in the pickling tank for steel is circulated to remove scale in the pickling liquid. A method for pickling steel, wherein the pickling liquid after separation and removal is used under reflux.

【0016】[0016]

【発明の実施の形態】以下、本発明の態様は、鋼材を酸
洗液に浸漬して鋼材表面のスケールを除去する酸洗方法
において、スケールを含有したスラッジが混入した酸洗
液の浄化を例に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention is directed to a pickling method for removing scale from the surface of a steel material by immersing the steel material in a pickling solution, the method comprising purifying a pickling solution mixed with sludge containing scale. An example is described.

【0017】図1は、本発明装置の一例を模式的に示す
概要図である。図2は、本発明の別の装置の一例を模式
的に示す概要図である。なお、図1、2で、符号1a、
1bはそれぞれ入側配管と出側配管、2は分離槽、3は
容器、4は磁気発生装置、5a、5bはそれぞれ入側バ
ルブと出側バルブ、6は空気抜きバルブ、7はスラッジ
排出バルブ、8はスラッジ処理装置、9はスラッジ除去
装置、10はスラッジ除去バルブ、11は昇降装置、1
2は上蓋、13は液抜きバルブ、14は被覆部である。
FIG. 1 is a schematic diagram schematically showing an example of the apparatus of the present invention. FIG. 2 is a schematic diagram schematically showing an example of another apparatus of the present invention. In addition, in FIG.
1b is an inlet pipe and an outlet pipe, 2 is a separation tank, 3 is a container, 4 is a magnetic generator, 5a and 5b are inlet and outlet valves respectively, 6 is an air vent valve, 7 is a sludge discharge valve, 8 is a sludge treatment device, 9 is a sludge removal device, 10 is a sludge removal valve, 11 is a lifting device, 1
2 is an upper lid, 13 is a drain valve, and 14 is a covering part.

【0018】図1、図2に示すように、本発明によれ
ば、スラッジの分離処理前の酸洗液を供給する入側配管
1aと分離処理後の酸洗液を排出する出側配管1bを分
離槽2に接続したことにより、酸洗液の連続処理が可能
となる。すなわち、図示していない酸洗槽に入側配管1
aと出側配管1bを接続することにより、酸洗槽内の酸
洗液を分離槽2に供給し、分離槽内で分離処理した酸洗
液を酸洗槽に環流させることができる。
As shown in FIGS. 1 and 2, according to the present invention, an inlet pipe 1a for supplying pickling liquid before sludge separation processing and an outlet pipe 1b for discharging pickling liquid after sludge separation processing. Is connected to the separation tank 2 so that the pickling solution can be continuously processed. That is, the inlet pipe 1 is placed in the pickling tank (not shown).
By connecting a to the outlet pipe 1b, the pickling liquid in the pickling tank can be supplied to the separation tank 2, and the pickling liquid separated in the separation tank can be returned to the pickling tank.

【0019】図1に示すように、本発明の装置によれ
ば、分離槽2内部に非磁性の容器3とその容器の内部に
磁気発生装置4を設けたことにより、磁気発生装置と酸
洗液との接触を防止して、磁気発生装置の磁気力の作用
により容器3の表面にスラッジを付着させることができ
るので、磁気発生装置の腐食を防止することができ、ま
た、後述するスラッジ除去装置によるスラッジ除去が容
易となる。この容器の材質は非磁性であればよく、特に
限定するものでないが、耐食性に優れた材質を選択する
ことができる。例えば、塩化ビニール、FRP(繊維強
化プラスチック)やガラスなどとすることができる。ま
た、容器の厚さは、容器の損耗や磁気力の減衰などの観
点から0.5〜3.0mm程度とするのがよい。
As shown in FIG. 1, according to the apparatus of the present invention, a non-magnetic container 3 is provided inside the separation tank 2 and a magnetic generator 4 is provided inside the container. Sludge can be adhered to the surface of the container 3 by the action of the magnetic force of the magnetic generator by preventing contact with the liquid, so that corrosion of the magnetic generator can be prevented, and sludge removal, which will be described later. Sludge removal by the device becomes easy. The material of the container is not particularly limited as long as it is non-magnetic, and a material having excellent corrosion resistance can be selected. For example, vinyl chloride, FRP (fiber reinforced plastic), glass, or the like can be used. Further, the thickness of the container is preferably about 0.5 to 3.0 mm from the viewpoints of wear of the container and attenuation of the magnetic force.

【0020】図2に示すように、本発明の別の装置によ
れば、磁気発生装置4を分離槽2内部に設け、この磁気
発生装置4の外面を覆う被覆部14により、磁気発生装
置4と酸洗液との接触を防止して、磁気発生装置4の磁
気力の作用により前記被覆部14の表面(以下、「被覆
面」ともいう)にスラッジを付着させることができるの
で、磁気発生装置4の腐食を防止することができ、ま
た、後述するスラッジ除去装置9によるスラッジ除去が
容易となる。被覆部の材質は非磁性であればよく、特に
限定するものでないが、例えば、塩化ビニール、FRP
(繊維強化プラスチック)、ガラスやゴムなどとするこ
とができる。また、被覆部の厚さは、0.5〜3.0m
m程度とするのがよい。
As shown in FIG. 2, according to another apparatus of the present invention, a magnetic generator 4 is provided inside the separation tank 2, and a coating portion 14 covering the outer surface of the magnetic generator 4 is used. And the pickling solution is prevented from contacting the sludge with the magnetic force of the magnetic generator 4, thereby allowing sludge to adhere to the surface of the cover 14 (hereinafter, also referred to as “covered surface”). Corrosion of the device 4 can be prevented, and sludge removal by a sludge removing device 9 described later becomes easy. The material of the covering portion is not particularly limited as long as it is non-magnetic, and is, for example, vinyl chloride or FRP.
(Fiber reinforced plastic), glass, rubber, and the like. In addition, the thickness of the covering portion is 0.5 to 3.0 m.
m.

【0021】図1、図2に示すように、スラッジ除去装
置9を分離槽2に設けたことにより、容器3や磁気発生
装置4を外すことなく容器の表面や磁気発生装置の被覆
面に付着したスラッジを除去することができる。スラッ
ジ除去装置としては、水などの液体または液体と気体や
固体との混合物を噴射するノズルが好適である。その
他、ブラシ、板などで機械的に除去してもよい。
As shown in FIGS. 1 and 2, the sludge removing device 9 is provided in the separation tank 2, so that the sludge removing device 9 adheres to the surface of the container and the coating surface of the magnetic generating device without removing the container 3 and the magnetic generating device 4. Sludge can be removed. As the sludge removing device, a nozzle that ejects a liquid such as water or a mixture of a liquid and a gas or a solid is suitable. In addition, you may remove mechanically with a brush, a board, etc.

【0022】図1、図2に示すように、入側バルブ5a
と出側バルブ5b、ならびにスラッジを排出するスラッ
ジ排出バルブ7を設けたことにより、磁気力により酸洗
液から分離されスラッジ除去装置9で除去されたスラッ
ジが酸洗液に混入するのを防止することができる。すな
わち、入側バルブ5aと出側バルブ5bでそれぞれ酸洗
液の供給と排出を停止し、次いでスラッジ排出バルブ7
を開いてスラッジ除去装置9で除去したスラッジをスラ
ッジ処理装置8に排出することにより、出側バルブ5b
から排出され酸洗槽に環流する酸洗液へのスラッジ混入
を防止することができる。
As shown in FIGS. 1 and 2, the inlet valve 5a
And the discharge side valve 5b and the sludge discharge valve 7 for discharging sludge prevent the sludge separated from the pickling liquid by magnetic force and removed by the sludge removing device 9 from being mixed into the pickling liquid. be able to. That is, supply and discharge of the pickling solution are stopped by the inlet valve 5a and the outlet valve 5b, respectively.
Is opened and the sludge removed by the sludge removal device 9 is discharged to the sludge treatment device 8, whereby the outlet valve 5b
Sludge mixed into the pickling liquid discharged from the tank and returned to the pickling tank can be prevented.

【0023】図3は、図1および図2に示す磁気発生装
置の構造の一例を模式的に示す縦断面図である。符号1
5は永久磁石、16は鉄芯、17は固定ナットで、図
1、2と同じ要素は同一の符号で示す。
FIG. 3 is a longitudinal sectional view schematically showing an example of the structure of the magnetic generator shown in FIG. 1 and FIG. Sign 1
5 is a permanent magnet, 16 is an iron core, 17 is a fixing nut, and the same elements as those in FIGS.

【0024】図3に示すように、磁気発生装置4は、鉄
芯16と永久磁石15を交互に配置した構造で、上蓋1
2と固定ナット17で固定され、鉄芯16を挟んで永久
磁石15のN極同士、S極同士が向き合うように配置さ
れる。磁気発生装置4で生じる磁気力は、図1の容器3
の表面または図2の被覆部14の表面で、1000〜6
000ガウス程度以上あればよい。上限は特に限定しな
いが、磁気発生装置が大型化するので通常15000ガ
ウス以下とするのがよい。なお、図3では、永久磁石1
5を用いる場合を示したが、電磁石を用いてもよい。
As shown in FIG. 3, the magnetic generator 4 has a structure in which iron cores 16 and permanent magnets 15 are alternately arranged.
2 and a fixing nut 17, and are arranged such that the N poles and the S poles of the permanent magnet 15 face each other with the iron core 16 interposed therebetween. The magnetic force generated by the magnetism generating device 4
2 or the surface of the covering portion 14 in FIG.
It may be about 2,000 Gauss or more. Although the upper limit is not particularly limited, it is usually preferable to set the upper limit to 15,000 gauss or less because the size of the magnetic generator increases. In FIG. 3, the permanent magnet 1
5 is used, but an electromagnet may be used.

【0025】図1に示すように、磁気発生装置4を容器
3に挿脱する昇降機構11を設けたことにより、磁気発
生装置4を容器3から外して容器3を開磁することがで
き、スラッジ除去装置9の除去能力を小さくすることが
できる。なお、昇降機構は、エアシリンダや油圧シリン
ダなどでよいが、昇降できれば他の手段であってもよ
い。
As shown in FIG. 1, the provision of the elevating mechanism 11 for inserting and removing the magnetic generator 4 from the container 3 allows the magnetic generator 4 to be removed from the container 3 and the container 3 to be opened. The removal ability of the sludge removal device 9 can be reduced. The lifting mechanism may be an air cylinder, a hydraulic cylinder, or the like, but may be other means as long as it can be raised and lowered.

【0026】なお、図1、図2に示すように、液抜きバ
ルブ13を分離槽2に接続して設けるのが好ましい。ス
ラッジ排出バルブ7からスラッジを排出する前に液抜き
バルブ13から分離槽内の酸洗液を排出し回収すること
ができるので、酸洗液のコストが低減する。
As shown in FIGS. 1 and 2, a drain valve 13 is preferably connected to the separation tank 2. Before the sludge is discharged from the sludge discharge valve 7, the pickling liquid in the separation tank can be discharged and collected from the liquid drain valve 13, so that the cost of the pickling liquid can be reduced.

【0027】また、図1および図2において、磁気発生
装置4を通過する酸洗液の速度は、速すぎると一旦付着
したスラッジが剥離しスラッジの分離効率が低下するた
め、1m/s程度以下がよい。好ましくは0.5m/s
以下である。
In FIGS. 1 and 2, if the speed of the pickling solution passing through the magnetic generator 4 is too high, the sludge that has once adhered is separated and the efficiency of separating the sludge is reduced, so that the speed of the pickling solution is reduced to about 1 m / s or less. Is good. Preferably 0.5 m / s
It is as follows.

【0028】図4は、本発明装置の他の例を模式的に示
す断面図である。図1と同じ要素は同一の符号で示す。
図5は、本発明の別の装置の他の例を模式的に示す断面
図である。図2と同じ要素は同一の符号で示す。図4に
示すように、磁気発生装置4を備えた複数個の非磁性の
容器3を分離槽2内に配設し、また 図5に示すよう
に、外面を非磁性の被覆部14で覆われた複数個の磁気
発生装置4を分離槽2内に配設することにより、スラッ
ジの分離能力が向上し、洗浄液の浄化能力を高めること
ができる。図4、5では、分離槽2の長手方向(図面の
左右方向)に複数個配設する例を示したが、分離槽の幅
方向(図面の垂直方向)または幅方向と長手方向に複数
個配設してもよい。
FIG. 4 is a sectional view schematically showing another example of the apparatus of the present invention. 1 are denoted by the same reference numerals.
FIG. 5 is a cross-sectional view schematically showing another example of another apparatus of the present invention. 2 are denoted by the same reference numerals. As shown in FIG. 4, a plurality of non-magnetic containers 3 each having a magnetic generator 4 are disposed in the separation tank 2, and the outer surface is covered with a non-magnetic covering portion 14, as shown in FIG. By disposing the plurality of magnetic generators 4 separated in the separation tank 2, the sludge separation ability is improved, and the cleaning liquid purification ability can be enhanced. 4 and 5 show an example in which a plurality of the separation tanks are arranged in the longitudinal direction (horizontal direction in the drawing), but a plurality of separation tanks are arranged in the width direction (vertical direction in the drawing) or in the width direction and the longitudinal direction. It may be provided.

【0029】次ぎに、本発明の浄化方法を酸洗槽内の酸
洗液の浄化を例に説明する。図1、図2において、図示
していない酸洗槽内の酸洗液は入側配管1aから分離槽
2内を通過して出側配管1bを経て酸洗槽槽内に環流す
る。酸洗液が分離槽内を通過する際、磁気発生装置4の
磁気作用で酸洗液中のスラッジは、図1では容器3の表
面に、図2では被覆部14の表面に付着する。分離槽2
内に酸洗液を所定時間供給した後(この時間を「通液時
間」という)、入側バルブ5aと出側バルブ5bを閉め
て酸洗液の供給と排出を停止する。なお、通液時間は、
スラッジの吸着効率の観点から通常1〜10分程度でよ
い。
Next, the purification method of the present invention will be described with reference to the purification of a pickling solution in a pickling tank as an example. In FIG. 1 and FIG. 2, the pickling liquid in the pickling tank (not shown) flows from the inlet pipe 1a through the separation tank 2 and returns to the pickling tank via the outlet pipe 1b. When the pickling solution passes through the separation tank, the sludge in the pickling solution adheres to the surface of the container 3 in FIG. 1 and to the surface of the coating portion 14 in FIG. Separation tank 2
After the pickling liquid is supplied for a predetermined period of time (this time is referred to as "liquid passing time"), the inlet valve 5a and the outlet valve 5b are closed to stop the supply and discharge of the pickling liquid. The flow time is
From the viewpoint of sludge adsorption efficiency, it is usually about 1 to 10 minutes.

【0030】次いで、空気抜きバルブ6とスラッジ排出
バルブ7を開け、その後、スラッジ除去装置9を用い
て、例えば水噴射することで、図1では容器3の表面、
図2では被覆部14の表面に付着したスラッジを除去し
スラッジ処理装置8に排出する。なお、スラッジを排出
する前に、液抜きバルブ13を開け分離槽内の酸洗液を
排出し回収するのが望ましい。また、図1において、ス
ラッジを除去する際、磁気発生装置4を容器3から引き
抜くことが好ましく、スラッジの除去効率を高めること
ができる。
Next, the air release valve 6 and the sludge discharge valve 7 are opened, and thereafter, for example, water is sprayed by using a sludge removing device 9, so that the surface of the container 3 in FIG.
In FIG. 2, sludge adhering to the surface of the coating portion 14 is removed and discharged to the sludge treatment device 8. Before discharging the sludge, it is desirable to open the liquid drain valve 13 and discharge and collect the pickling liquid in the separation tank. Also, in FIG. 1, when removing sludge, it is preferable to pull out the magnetic generator 4 from the container 3, so that sludge removal efficiency can be increased.

【0031】スラッジを排出した後、スラッジ排出バル
ブ7を閉じて、入側バルブ1aおよび出側バルブ1bを
開いて、分離槽2への通液を開始し、容器3あるいは被
覆部14の表面にスラッジを吸着させる。このような操
作を繰り返しておこなうことにより酸洗液のスラッジが
分離除去され、酸洗液を連続処理して浄化することがで
きる。
After the sludge is discharged, the sludge discharge valve 7 is closed, the inlet valve 1a and the outlet valve 1b are opened, and the liquid is started to flow into the separation tank 2, and the sludge is discharged to the surface of the container 3 or the coating portion 14. Adsorb sludge. By repeating such an operation, sludge of the pickling liquid is separated and removed, and the pickling liquid can be continuously treated and purified.

【0032】[0032]

【実施例】(実施例1)図1に示す基本構成の試験装置
を製作し、酸洗液中のスラッジを分離し浄化する試験を
おこなった。図1で、上記試験装置は、外径125m
m、高さ230mmの円筒型の分離槽2の内部に外径7
6.3mm、高さ220mmの円筒型の容器3を設け、
エアシリンダ11により外径70mm、高さ210mm
の磁気発生装置4をその容器に挿脱可能とした構造と
し、分離槽内部にスケール除去装置として水噴射ノズル
9を設けた。分離槽側面には、入側バルブ5aと出側バ
ルブ5bをそれぞれ備えた入側配管1aと出側配管1b
とを接続し、分離槽下部にスラッジ排出バルブ7を取り
付けた。磁気発生装置4は、図3に示すように、外径7
0mmの永久磁石9枚と鉄芯を積層した構造で、磁気力
は容器の表面で、2000〜6000ガウスであった。
なお、容器3の材質は塩化ビニールで、その厚さは2.
5mmとした。
EXAMPLES (Example 1) A test apparatus having a basic structure shown in FIG. 1 was manufactured, and a test for separating and purifying sludge in an acid pickling solution was performed. In FIG. 1, the test device has an outer diameter of 125 m.
m, an outer diameter of 7 mm inside a cylindrical separation tank 2 having a height of 230 mm.
A cylindrical container 3 having a height of 6.3 mm and a height of 220 mm is provided.
Outer diameter 70mm, height 210mm by air cylinder 11
The magnetic generator 4 of the above was configured to be insertable into and removable from the container, and a water jet nozzle 9 was provided inside the separation tank as a scale removing device. An inlet pipe 1a and an outlet pipe 1b having an inlet valve 5a and an outlet valve 5b, respectively, on the side of the separation tank.
And a sludge discharge valve 7 was attached to the lower part of the separation tank. As shown in FIG. 3, the magnetic generator 4 has an outer diameter of 7 mm.
With a structure in which nine 0 mm permanent magnets and an iron core were laminated, the magnetic force was 2000 to 6000 Gauss on the surface of the container.
The material of the container 3 is vinyl chloride, and the thickness thereof is 2.
5 mm.

【0033】酸洗槽からスラッジを回収してスラッジ濃
度0.24%、粒子径20μm以下が70〜80%含有
する酸洗液を作り、この液を100リットル/minで
入側配管を介して分離槽に供給し、磁気発生装置でスラ
ッジを捕捉し、酸洗液は出側配管から排出した。所定時
間通液した後、分離槽内部の酸洗液を排出し、その後、
磁気発生装置を容器に挿入した状態で水噴射ノズルによ
り水圧0.3kg/cm2 の条件で水を噴射して容器の
表面に付着したスラッジを洗い出し、スラッジ排出バル
ブからスラッジを排出し、スラッジの量を測定した。な
お、容器の表面に付着したスラッジは水噴射により容易
に除去することができた。
The sludge is recovered from the pickling tank to produce a pickling solution having a sludge concentration of 0.24% and a particle diameter of 20 μm or less containing 70 to 80%, and this solution is supplied at a rate of 100 liter / min through an inlet pipe. The mixture was supplied to a separation tank, sludge was captured by a magnetic generator, and the pickling solution was discharged from an outlet pipe. After passing the solution for a predetermined time, the pickling solution inside the separation tank is discharged, and then
With the magnetic generator inserted into the container, water is injected by a water injection nozzle at a water pressure of 0.3 kg / cm 2 to wash out sludge attached to the surface of the container, and the sludge is discharged from a sludge discharge valve. The amount was measured. In addition, sludge adhering to the surface of the container could be easily removed by water injection.

【0034】スラッジ量は、乾燥重量で通液時間30秒
で9g、1分間で15gであり、1分間の浄化効率(ス
ラッジ分離除去量/酸洗液中のスラッジ量)は、6.2
5%(15g/240g×100)であった。
The sludge amount was 9 g in dry weight and 30 g in 30 minutes, and 15 g in 1 minute. Purification efficiency (sludge separation amount / sludge amount in pickling solution) per minute was 6.2.
It was 5% (15 g / 240 g × 100).

【0035】(実施例2)図2に示す基本構成の試験装
置を製作し、酸洗液中のスラッジを分離し浄化する試験
をおこなった。試験装置の仕様は、容器を用いず、磁気
発生装置に塩化ビニールを厚1.5mmで被覆した以外
は表1と同様である。実施例1で説明したと同様の条件
で通液し、磁気発生装置の被覆面に付着したスラッジを
除去し、その重量を測定した。
(Example 2) A test apparatus having the basic configuration shown in FIG. 2 was manufactured, and a test for separating and purifying sludge in the pickling solution was performed. The specifications of the test apparatus were the same as in Table 1 except that the container was not used and the magnetic generator was coated with vinyl chloride to a thickness of 1.5 mm. The solution was passed under the same conditions as described in Example 1, sludge attached to the coating surface of the magnetic generator was removed, and the weight was measured.

【0036】スラッジ量は、乾燥重量で通液時間1分間
で23gであり、浄化効率は9.5%(23g/240
g×100)であった。
The amount of sludge was 23 g per 1 minute in a dry weight, and the purification efficiency was 9.5% (23 g / 240 g).
g × 100).

【0037】[0037]

【発明の効果】本発明によれば、簡単な設備で、特に酸
洗の洗浄液であっても腐食することなくスラッジを速や
かに分離除去し、洗浄液を環流使用することが可能とな
り、洗浄液の原単位が向上する。既存の酸洗槽などに配
管を接続するだけで適用が可能であり、スラッジ除去作
業の低減や除去作業による操業停止時間の短縮など経済
的価値が大きい。
According to the present invention, sludge can be separated and removed quickly with simple equipment without corrosive even with a pickling cleaning liquid, and the cleaning liquid can be used under reflux. The unit improves. It can be applied simply by connecting a pipe to an existing pickling tank, etc., and has great economic value such as reduction of sludge removal work and shortening of operation stoppage time due to removal work.

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

【図1】本発明装置の一例を模式的に示す概要図であ
る。
FIG. 1 is a schematic diagram schematically showing an example of the device of the present invention.

【図2】本発明の別の装置の一例を模式的に示す概要図
である。
FIG. 2 is a schematic diagram schematically showing an example of another apparatus of the present invention.

【図3】磁気発生装置の構造の一例を模式的に示す縦断
面図である。
FIG. 3 is a longitudinal sectional view schematically showing an example of the structure of a magnetic generator.

【図4】本発明装置の他の例を模式的に示す断面図であ
る。
FIG. 4 is a cross-sectional view schematically showing another example of the device of the present invention.

【図5】本発明の別の装置の他の例を模式的に示す断面
図である。
FIG. 5 is a cross-sectional view schematically showing another example of another apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1a:入側配管、1b:出側配管、2:分離槽、3:容
器、4:磁気発生装置、5a:入側バルブ、5b:出側
バルブ、6:空気抜きバルブ、7:スラッジ排出バル
ブ、8:スラッジ処理装置、9:スラッジ除去装置(水
噴射バルブ)、10:スラッジ除去バルブ、11:昇降
装置、12:上蓋、13:液抜きバルブ、14:被覆
部、15:永久磁石、16:鉄芯、17:固定ナット。
1a: inlet side pipe, 1b: outlet side pipe, 2: separation tank, 3: container, 4: magnetic generator, 5a: inlet side valve, 5b: outlet side valve, 6: air vent valve, 7: sludge discharge valve, 8: Sludge treatment device, 9: Sludge removal device (water injection valve), 10: Sludge removal valve, 11: Elevating device, 12: Top lid, 13: Drain valve, 14: Coating part, 15: Permanent magnet, 16: Iron core, 17: fixing nut.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 松橋 透 大阪市中央区北浜4丁目5番33号 住友金 属工業株式会社内 Fターム(参考) 3C047 GG13 GG17  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Toru Matsuhashi 4-5-33 Kitahama, Chuo-ku, Osaka-shi Sumitomo Metal Industries Co., Ltd. F-term (reference) 3C047 GG13 GG17

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 洗浄液に混入した鉄分を含むスラッジを
磁気力により分離する洗浄液の浄化装置であって、分離
前の洗浄液を供給する入側バルブを備えた入側配管と分
離後の洗浄液を排出する出側バルブを備えた出側配管と
を接続した分離槽と、該分離槽の内部に配設されスラッ
ジを付着させる非磁性の容器と、該容器に挿入され磁気
力を有する磁力発生装置と、上記分離槽内部に設けられ
上記容器の表面に付着したスラッジを除去するスラッジ
除去装置と、上記分離槽に接続され除去されたスラッジ
を排出するスラッジ排出バルブとを設けたことを特徴と
する洗浄液浄化装置。
An apparatus for purifying a cleaning liquid for separating sludge containing iron contained in the cleaning liquid by magnetic force, comprising an inlet pipe provided with an inlet valve for supplying the cleaning liquid before separation, and discharging the cleaning liquid after separation. A separation tank connected to an outlet pipe having an outlet valve, a non-magnetic container disposed inside the separation tank to attach sludge, and a magnetic force generator inserted into the container and having a magnetic force. A cleaning liquid provided with a sludge removing device provided inside the separation tank for removing sludge adhering to the surface of the container, and a sludge discharge valve connected to the separation tank for discharging the removed sludge. Purification device.
【請求項2】 磁力発生装置を容器に挿脱する昇降機構
を設けたことを特徴とする請求項1に記載の洗浄液浄化
装置。
2. The cleaning liquid purifying apparatus according to claim 1, further comprising an elevating mechanism for inserting and removing the magnetic force generating device from the container.
【請求項3】 洗浄液に混入した鉄分を含むスラッジを
磁気力により分離する洗浄液の浄化装置であって、分離
前の洗浄液を供給する入側バルブを備えた入側配管と分
離後の洗浄液を排出する出側バルブを備えた出側配管と
を接続した分離槽と、該分離槽の内部に配設され外面を
非磁性の被覆部で覆われた磁気力を有する磁力発生装置
と、上記分離槽内部に設けられ上記被覆部の表面に付着
したスラッジを除去するスラッジ除去装置と、上記分離
槽に接続され除去されたスラッジを排出するスラッジ排
出バルブとを設けたことを特徴とする洗浄液浄化装置。
3. A cleaning liquid purifying apparatus for separating sludge containing iron contained in a cleaning liquid by magnetic force, comprising an inlet pipe provided with an inlet valve for supplying the cleaning liquid before separation, and discharging the cleaning liquid after separation. Tank connected to an outlet pipe provided with an outlet valve, a magnetic force generator disposed inside the separation tank and having a magnetic force whose outer surface is covered with a nonmagnetic coating, and the separation tank A cleaning liquid purifying apparatus, comprising: a sludge removing device provided inside for removing sludge adhering to the surface of the coating portion; and a sludge discharging valve connected to the separation tank for discharging the removed sludge.
【請求項4】 請求項1または2に記載の洗浄液浄化装
置を用い、容器の表面にスラッジを付着させた後、入側
バルブと出側バルブで洗浄液の供給と排出を停止し、次
いでスラッジ除去装置で上記容器の表面に付着したスラ
ッジを除去し、除去したスラッジをスラッジ排出バルブ
から排出することを特徴とする洗浄液の浄化方法。
4. Using the cleaning liquid purifying apparatus according to claim 1 or 2, after applying sludge to the surface of the container, supply and discharge of the cleaning liquid are stopped by an inlet valve and an outlet valve, and then the sludge is removed. A method for purifying a cleaning liquid, comprising removing sludge adhering to the surface of the container with an apparatus and discharging the removed sludge from a sludge discharge valve.
【請求項5】 請求項3に記載の洗浄液浄化装置を用
い、被覆部の表面にスラッジを付着させた後、入側バル
ブと出側バルブで洗浄液の供給と排出を停止し、次いで
スラッジ除去装置で上記被覆部の表面に付着したスラッ
ジを除去し、除去したスラッジをスラッジ排出バルブか
ら排出することを特徴とする洗浄液の浄化方法。
5. Using the cleaning liquid purifying apparatus according to claim 3, after applying sludge to the surface of the covering section, supply and discharge of the cleaning liquid are stopped by an inlet valve and an outlet valve, and then the sludge removing apparatus is used. Removing the sludge adhering to the surface of the coating portion and discharging the removed sludge from a sludge discharge valve.
【請求項6】 請求項1〜3のいずれかに記載の洗浄液
浄化装置を用い、鋼材の酸洗槽内の酸洗液を循環処理し
て酸洗液中のスケールを除去分離し、除去分離後の酸洗
液を環流使用することを特徴とする鋼材の酸洗方法。
6. A cleaning liquid purifying apparatus according to claim 1, wherein the pickling liquid in the pickling tank for steel is circulated to remove and separate scales in the pickling liquid. A pickling method for steel materials, wherein the pickling solution is used under reflux.
JP10367138A 1998-12-24 1998-12-24 Method and apparatus for purifying cleaning liquid Pending JP2000189834A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10367138A JP2000189834A (en) 1998-12-24 1998-12-24 Method and apparatus for purifying cleaning liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10367138A JP2000189834A (en) 1998-12-24 1998-12-24 Method and apparatus for purifying cleaning liquid

Publications (1)

Publication Number Publication Date
JP2000189834A true JP2000189834A (en) 2000-07-11

Family

ID=18488562

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10367138A Pending JP2000189834A (en) 1998-12-24 1998-12-24 Method and apparatus for purifying cleaning liquid

Country Status (1)

Country Link
JP (1) JP2000189834A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009056553A (en) * 2007-08-31 2009-03-19 Sumco Techxiv株式会社 Device for removing magnetic foreign matters in wire saw slurry
JP2009172572A (en) * 2008-01-21 2009-08-06 Buhmwoo Eco Engineering Co Ltd Apparatus for removing fine iron powder from rolling oil
JP6231240B1 (en) * 2017-05-22 2017-11-15 鹿島建設株式会社 Magnetic separation device and magnetic separation method
CN108607684A (en) * 2018-06-20 2018-10-02 北京建筑材料科学研究总院有限公司 A kind of automatic foreign impurities removing device and the sludge treatment system with the device
JP2020183020A (en) * 2019-05-09 2020-11-12 サンエス工業株式会社 Chip and like separating and removing device
JP7464416B2 (en) 2020-03-17 2024-04-09 株式会社ディスコ Processing powder recovery device

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009056553A (en) * 2007-08-31 2009-03-19 Sumco Techxiv株式会社 Device for removing magnetic foreign matters in wire saw slurry
JP2009172572A (en) * 2008-01-21 2009-08-06 Buhmwoo Eco Engineering Co Ltd Apparatus for removing fine iron powder from rolling oil
JP4665022B2 (en) * 2008-01-21 2011-04-06 株式会社汎宇エコエンジニアリング Equipment for removing fine iron in rolling oil
US8211299B2 (en) 2008-01-21 2012-07-03 Buhmwoo Eco Engineering Co., Ltd. Apparatus for removing iron powder from rolling oil
JP6231240B1 (en) * 2017-05-22 2017-11-15 鹿島建設株式会社 Magnetic separation device and magnetic separation method
JP2018192456A (en) * 2017-05-22 2018-12-06 鹿島建設株式会社 Magnetic separation device and magnetic separation method
CN108607684A (en) * 2018-06-20 2018-10-02 北京建筑材料科学研究总院有限公司 A kind of automatic foreign impurities removing device and the sludge treatment system with the device
JP2020183020A (en) * 2019-05-09 2020-11-12 サンエス工業株式会社 Chip and like separating and removing device
JP7288340B2 (en) 2019-05-09 2023-06-07 サンエス工業株式会社 Separation and removal device for chips, etc.
JP7464416B2 (en) 2020-03-17 2024-04-09 株式会社ディスコ Processing powder recovery device

Similar Documents

Publication Publication Date Title
CA1079004A (en) Non-polluting system for metal surface treatments
JP2000189834A (en) Method and apparatus for purifying cleaning liquid
JP5598841B2 (en) Machining system
CN105593171B (en) Light electrolysis equipment and control method, integrated water treatment device and method for treating water
US6264757B1 (en) Separating contaminants from continuous from surface cleansing solution during continuous strip steel processing
EP0655518B1 (en) System to re-circulate treatment material in processes of surface treatment and finishing
US5830282A (en) Continuous particle separation operation
JP3946287B2 (en) Pickling method for austenitic stainless steel
US6679273B2 (en) Surface cleansing of continuous-strip steel for hot-dip metal coating and apparatus for decreasing surface cleansing solution requirements
KR101897412B1 (en) System for Preventing Air and Water Pollution from Plating Facilities
CN207391565U (en) New-energy automobile Painting Shop degreasing impurity removed system
CN108350576B (en) Treatment device for the acidification and phosphating of metal parts
US5776258A (en) Flat-rolled steel strip continuous cleansing methods
CN212050685U (en) Environment is administered with automatic bonderizing effluent treatment plant
JP2007024816A (en) Vitrification processing method of radioactive waste liquid
US3971539A (en) Method for preventing the adhesive deposition of sludge on the surface of parts of a plant for treating metal surfaces
JP2968069B2 (en) Magnetic separation device
CN210826367U (en) Chemical industry anticorrosive chemical treatment spraying equipment
JP3027789B2 (en) Treatment of pickling liquid
RU2144848C1 (en) Method of regeneration of ion-exchange resins
CN211386066U (en) Treatment equipment for reducing emission
JPS6067897A (en) Method of recovering and treating piping washing material
JP2009106902A (en) Cleaning system
CN105776722A (en) Sewage treatment system
JPH0521199B2 (en)

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050620

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080701

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20081111