JPS60210316A - Device for purifying drawing liquid of drawing mill - Google Patents
Device for purifying drawing liquid of drawing millInfo
- Publication number
- JPS60210316A JPS60210316A JP6633484A JP6633484A JPS60210316A JP S60210316 A JPS60210316 A JP S60210316A JP 6633484 A JP6633484 A JP 6633484A JP 6633484 A JP6633484 A JP 6633484A JP S60210316 A JPS60210316 A JP S60210316A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- tank
- sludge
- cyclone
- purified
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Cyclones (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Metal Extraction Processes (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は伸線機の引抜きダイスに供給される伸線液の浄
化装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for purifying wire drawing fluid supplied to a drawing die of a wire drawing machine.
周知の如く伸線液には引抜き時に発生するスラッジを含
み、そのま\使゛用するときは引抜き線条に疵を生じ、
かつダイスの寿命を縮める等の問題があり、浄化する必
要がある。このため例えば第1図に示す如く沈澱槽1を
オリ用し、スラッジの自然沈降による浄化手段が用いら
れている。図中2は伸線機の伸線液受槽(図示省略)に
接続される戻り液供給管、8はスラッジポンプ、4は浄
化された液を伸線機に送り出す供給ポンプ、6は沈澱槽
l内に設けられ、液流を迂回させる仕切板である。As is well known, wire drawing fluid contains sludge generated during drawing, and if used as is, it may cause defects in the drawn wire.
In addition, there are problems such as shortening the life of the dice, so it is necessary to purify them. For this reason, for example, as shown in FIG. 1, a settling tank 1 is used as a purification means by natural settling of the sludge. In the figure, 2 is a return liquid supply pipe connected to the wire drawing liquid receiving tank (not shown) of the wire drawing machine, 8 is a sludge pump, 4 is a supply pump that sends purified liquid to the wire drawing machine, and 6 is a settling tank l. This is a partition plate installed inside the tank to divert the liquid flow.
この浄化手段によるときは、檜の容量は犬となり、広い
設置面積が必要である。また使用する液量は大となり、
液の交換時には多量の廃油処理を必要とし、油化、タン
ク清掃費等のメンテナンス費用が高価となる等の欠点が
ある。When using this purification method, the capacity of the Japanese cypress is limited, and a large installation area is required. Also, the amount of liquid used is large,
When replacing the liquid, it is necessary to dispose of a large amount of waste oil, and there are drawbacks such as high maintenance costs such as oil conversion and tank cleaning costs.
更に伸線液には潤滑性を増すために植物性油が混入され
る場合があり、この場合には長期使用時嫌気性バクテリ
ヤが発生し、液が腐敗する等のおそれがある。Furthermore, vegetable oil may be mixed into the wire drawing fluid to increase lubricity, and in this case, there is a risk that anaerobic bacteria will develop during long-term use, causing the fluid to rot.
また他の液中のスラッジ除去手段としては、ホフマン式
コンベヤータンクとして槽内の液を攪拌する等により泡
立たせ、浮遊物を該気泡に吸着させ、吸着した気泡を掻
出す方式も採られているが、伸線液の種類によっては発
泡性が低く、或いは発泡性を抑えているので70−テー
シヨンの効果か出ずかつ大型のスラッジの吸着除去は困
難である等の問題がある。Another method for removing sludge from liquid is a Hoffman conveyor tank, which stirs the liquid in the tank to create bubbles, adsorbs suspended matter to the bubbles, and scrapes out the adsorbed bubbles. However, depending on the type of wire drawing liquid, the foaming property is low or the foaming property is suppressed, so there are problems such as not being as effective as a 70-station and making it difficult to adsorb and remove large sludge.
本発明はかかる点に鑑み、自然沈降とサイクロンによる
強制分離とを組合わせ、比較的小型の浄化装置により効
果的に伸線液中のスラッジを分離除去することを目的と
する。In view of this, an object of the present invention is to combine natural sedimentation and forced separation using a cyclone to effectively separate and remove sludge in a wire drawing liquid using a relatively small purification device.
更に本発明は、上記サイクロンを利用し曝気効果により
液の腐敗を防止することを目的とする。A further object of the present invention is to use the above-mentioned cyclone to prevent liquid spoilage through the aeration effect.
以下、本発明を第2図以下に示す実施側番と基づいて詳
細に説明する。Hereinafter, the present invention will be explained in detail based on the implementation numbers shown in FIG. 2 and below.
図に複数台、例えば4台の伸線機AI 、A2 。The figure shows multiple wire drawing machines, for example four wire drawing machines AI and A2.
A8.A4(以下総称するときは単にAという)に対し
1台の浄化装置1oにより伸線液を浄化する例を示すも
ので、第2図は該浄化装置の概略作動説明図である。該
浄化装置1oは、各伸線機At、A2・・・の伸線液受
槽a1.a2゜as、a4(以下総称するときは単にa
という)に連なる戻り油回路11a、llb、lie。A8. This shows an example of purifying the wire drawing liquid for A4 (hereinafter generically referred to as simply A) using one purifying device 1o, and FIG. 2 is a schematic explanatory diagram of the operation of the purifying device. The purifying device 1o includes wire drawing liquid receiving tanks a1. of each wire drawing machine At, A2... a2゜as, a4 (hereinafter referred to collectively as simply a)
Return oil circuits 11a, llb, lie connected to
11(1(以下総称するときは単に11という)と、該
戻り油回路11により送り込まれる伸線液を収納する処
理槽18並びにサイクロン14を備える。処理槽18は
第8図に示す如く、第1次貯槽16と゛、該第1次貯槽
16よりも小容量の第2次貯槽16並ひに浄化液槽17
とを備え、第1次貯槽16と第2次貯槽16とは後部を
開放した隔壁18により区分され、両槽16゜16の下
部にはそれぞれスラッジ掻出し用スクレーパー(ゴム張
)はコンベア20.20’が敷設されている。また浄化
液槽17は上記第1次、第2次貯槽15,16に対し隔
壁21により区画され、該隔壁21には浄化液槽17か
ら第1次貯槽16に対しオーバーフロー用地22が形成
されている。堰の途中適所にはバランス板22aが取付
けられ、ポンプ28が故障した場合、第1次、第2次貯
槽115.16の液部が高くなり水圧で液が浄化液槽1
7に流れ込むようになっている。但し正常運転時は浄化
液槽17の水圧が高いためバランス板22aは閉成状態
で第1次、第2次貯槽15.16との流通は遮断されて
いる。11 (hereinafter simply referred to as 11), a processing tank 18 for storing the wire drawing liquid sent by the return oil circuit 11, and a cyclone 14. A primary storage tank 16, a secondary storage tank 16 with a smaller capacity than the primary storage tank 16, and a purification liquid tank 17.
The primary storage tank 16 and the secondary storage tank 16 are separated by a partition wall 18 with an open rear part, and a scraper (rubber-lined) for scraping out sludge is installed at the bottom of both tanks 16 and 16, respectively, and a conveyor 20. 20' has been installed. Further, the septic liquid tank 17 is divided from the primary and secondary storage tanks 15 and 16 by a partition 21, and an overflow area 22 is formed in the partition 21 from the septic liquid tank 17 to the primary storage tank 16. There is. A balance plate 22a is installed at a suitable location in the middle of the weir, and if the pump 28 fails, the liquid portions of the primary and secondary storage tanks 115 and 16 will become high and the liquid will flow to the clarification liquid tank 1 due to water pressure.
7. However, during normal operation, the water pressure in the purification liquid tank 17 is high, so the balance plate 22a is closed and communication with the primary and secondary storage tanks 15 and 16 is cut off.
22bは処理槽16.16−17の全体の液面が上昇し
た時、槽上面から液が溢れないように槽の上位適所に取
付けたオーバーフロ一部でこのオーバーフロ一部22b
より液を処理槽外に導くようにする。22b is an overflow part installed at a suitable position above the tank to prevent the liquid from overflowing from the top surface of the tank when the overall liquid level of the processing tank 16.16-17 rises.This overflow part 22b
The liquid should be guided to the outside of the processing tank.
前記サイクロン14は第2次貯槽16上に配備され、第
1次貯槽16の上澄液は供給用ポンプ28により供給管
24を介して該サイクロン14に送り込まれる。該サイ
クロン14は第4図に示す如く複数サイクロン(処理液
量に応じた連数例えは8群4個の12連のマルチサイク
ロン)が好ましく、該複合サイクロン14は高圧分配マ
ニホルド14aと、複数のサイクロン本体14bと、低
圧集合マニホルド140を主体として構成される(但し
第2図は単体のサイクロン14として示す)。このサイ
クロン14によりスラッジと分離された浄化液は排出管
25を介して浄化液槽17に導かれ、一方分離濃縮され
少量の排液を含むスラッジは、コーン状部の下方排出口
X+Z(第す図)から第2次貯槽16に排出される。The cyclone 14 is disposed on a secondary storage tank 16, and the supernatant liquid of the primary storage tank 16 is fed into the cyclone 14 via a supply pipe 24 by a supply pump 28. As shown in FIG. 4, the cyclone 14 is preferably a plurality of cyclones (for example, 12 multicyclones in 8 groups, 4 in series) depending on the amount of liquid to be treated, and the composite cyclone 14 includes a high pressure distribution manifold 14a and a plurality of cyclones. It is mainly composed of a cyclone body 14b and a low-pressure collecting manifold 140 (however, FIG. 2 shows it as a single cyclone 14). The purified liquid separated from the sludge by this cyclone 14 is led to the purified liquid tank 17 via the discharge pipe 25, while the separated and concentrated sludge containing a small amount of waste liquid is sent to the lower discharge port X+Z (first (Fig.) is discharged to the secondary storage tank 16.
浄化液槽17には、心安により温度センサ26並びに冷
却手段27およびヒーター29を備える。浄化液槽17
に設けられた温度センサ26により液温を検知し、液温
か高い時は熱交換機60を介して液を冷却して液温を下
げる。The purification liquid tank 17 is equipped with a temperature sensor 26, a cooling means 27, and a heater 29 for peace of mind. Purification liquid tank 17
The liquid temperature is detected by a temperature sensor 26 installed in the tank, and when the liquid temperature is high, the liquid is cooled via a heat exchanger 60 to lower the liquid temperature.
また冬期において浄化装置を休日休憩により長時間運転
休止した後再運転する場合、液温が一定温度以下の時は
製品に不良が発生するため加熱ヒーター29で液を一定
温度まで加熱昇温せしめる等の温度コントロール装置を
設ける。In addition, when restarting the purification equipment after a long suspension of operation due to a holiday break in winter, if the liquid temperature is below a certain temperature, product defects may occur, so the heating heater 29 is used to heat the liquid to a certain temperature. A temperature control device shall be provided.
冷却手段27は周知構造の冷却液送り出しポンプ28並
びに熱交換機5o及び冷却塔51、冷却水循環ポンプ6
2、配管68、切換バルプ54にて構成される。そして
浄化され、かつ所定温度に冷却又は加熱された伸線液は
送り出しポンプ80a、80b、80c 、80d(以
下総称するときは単に80という)により戻し回路81
a、81b、81c、81d(以下総称するときは単に
81という)を経てそれぞれの伸線機A 1 、A2・
・・に供給される。The cooling means 27 includes a cooling liquid delivery pump 28 of a known structure, a heat exchanger 5o, a cooling tower 51, and a cooling water circulation pump 6.
2, piping 68, and switching valve 54. The purified wire drawing liquid, which has been cooled or heated to a predetermined temperature, is returned to a return circuit 81 by sending pumps 80a, 80b, 80c, and 80d (hereinafter collectively referred to simply as 80).
a, 81b, 81c, and 81d (hereinafter collectively referred to as simply 81) to the respective wire drawing machines A 1 , A2.
...is supplied to...
図中、Hは前記掻出し用コンベア20により掻出される
スラッジを収納し搬送するスラッジ運搬台車である。In the figure, H is a sludge transport vehicle that stores and conveys the sludge scraped out by the scraping conveyor 20.
上記構成において、戻り油回路11を介して送り出され
るスラッジを含んだ伸線液は第1次貯槽16に収納され
、重いスラッジは沈降し、下部に集積し、掻出し用コン
ベア20により外部に掻き出される。軽い浮遊したスラ
ッジを含む上澄液は供給用ポンプ28によりサイクロン
14に送り込まれ、該サイクロン14において遠心力に
よりスラッジは強制的に液から分離濃縮され少量の排液
と共にサイクロン下部の排出口148から第2仄貯槽1
6に落下排出され、一方濾過された浄化液はす゛イタロ
ン14の送り出し口14d(第6図)から排出管26を
介して浄化液槽17に送り込まれる。In the above configuration, the wire drawing liquid containing sludge sent out via the return oil circuit 11 is stored in the primary storage tank 16, and the heavy sludge settles and accumulates in the lower part, and is scraped out to the outside by the scraping conveyor 20. Served. The supernatant liquid containing light suspended sludge is sent to the cyclone 14 by the supply pump 28, and in the cyclone 14, the sludge is forcibly separated and concentrated from the liquid by centrifugal force, and is discharged from the outlet 148 at the bottom of the cyclone along with a small amount of waste liquid. Second storage tank 1
6, and the filtered purification liquid is sent into the purification liquid tank 17 from the outlet 14d (FIG. 6) of the Suitaron 14 via the discharge pipe 26.
浄化液槽17は常時オーバフロー用堰22から若干量が
第1次貯槽15側にオーツく−フローする状態に送水量
が設定され、液面に浮遊する微小スラッジは第1次貯槽
15に戻され下方の浄化された伸線液は送り出しポンプ
80により戻し回路81を介して各伸1liI!機Aに
供給される。The amount of water supplied to the clarification liquid tank 17 is set so that a small amount automatically flows from the overflow weir 22 to the primary storage tank 15 side, and the minute sludge floating on the liquid surface is returned to the primary storage tank 15. The purified wire drawing liquid in the lower part is passed through a return circuit 81 by a delivery pump 80 to each drawing 1liI! Supplied to machine A.
この場合、浄化液槽17内の液温が所定値以上になると
、温度センサ26か作動し、冷却手段27が運転され、
所定温度に冷却され、或いは加熱ヒーター29が作動し
所定温度に加熱される。In this case, when the temperature of the liquid in the purification liquid tank 17 exceeds a predetermined value, the temperature sensor 26 is activated and the cooling means 27 is operated.
It is cooled to a predetermined temperature, or the heating heater 29 is activated and heated to a predetermined temperature.
第2次貯槽16は第1次貯槽15より小容量ではあるが
、供給される液量は少なく、従ってスラッジの沈降に充
分な滞留時間が得られ、かつ槽16内のスラッジ濃度は
高いため、凝集性を高めることができ、いわゆる凝集沈
降の効果を高めることができる。Although the secondary storage tank 16 has a smaller capacity than the primary storage tank 15, the amount of liquid supplied is small, so sufficient residence time is obtained for the sludge to settle, and the sludge concentration in the tank 16 is high. It is possible to improve the flocculating property, and it is possible to enhance the effect of so-called flocculation and sedimentation.
更に上記サイクロン14は、下部排出口14111が開
口されており、サイクロン作用に伴なう吸気作用を生じ
、サイクロン14内において液と空気との混合、即ち曝
気作用が行なわれる。Further, the cyclone 14 has a lower discharge port 14111 opened to produce an air suction action accompanying the cyclone action, and mixing of liquid and air, that is, an aeration action is performed within the cyclone 14.
伸線液には潤滑性を増すため植物油等が混合される場合
があり、使用中嫌気性バクテリヤが発生し、液の腐敗を
招くおそれがあるが、上記曝気作用により嫌気性バクテ
リヤを死滅せしめる殺菌効果が得られ、従って液の寿命
の延長を計ることができる。The wire drawing fluid is sometimes mixed with vegetable oil etc. to increase lubricity, which may generate anaerobic bacteria during use and lead to spoilage of the fluid, but the aerobic action described above kills the anaerobic bacteria. effect is obtained, and therefore the life of the liquid can be extended.
以上の如く本発明によるときは、第1次貯槽における自
然沈降と、サイクロンによる強制分離並びに濃縮された
排液に対し第2次貯槽における凝集沈降とによりスラッ
ジを分離するようにしたから、比較的小型の処理槽によ
り効果的に伸線液からスラッジを分離することができる
。As described above, according to the present invention, sludge is separated by natural sedimentation in the primary storage tank, forced separation by a cyclone, and coagulation sedimentation of the concentrated waste liquid in the secondary storage tank. Sludge can be effectively separated from the wire drawing liquid using a small treatment tank.
またスラッジを分離することにより銅イオン量の減少及
び老化物質の量の増加が抑えられ液の劣化防止が図れ液
寿命の延長を計ることができしかも線引用ダイスの摩耗
が少くなり製品の傷、線切れも無くなる等の効果を有す
る。In addition, by separating the sludge, the decrease in the amount of copper ions and the increase in the amount of aging substances are suppressed, preventing the deterioration of the liquid and extending the life of the liquid.In addition, the wear of the drawing die is reduced, resulting in fewer scratches on the product. This has the effect of eliminating line breakage.
第1図は従来の浄化装置としての沈澱槽の縦断説明図、
第2図乃至第5図は本発明の実施例を示し、第2図は浄
化装置の概略作動説明図、tJs図は処理槽の一部切欠
した平面図、諏4図は一部切欠した処理槽の正面図、第
5図はサイクロンの縦断面図である。
1001.浄化装置
111. 、戻り油回路
1B 11.処理槽
14 、0.サイクロン
150.、第1次貯槽
1600.第2次貯槽
171. 、浄化液槽
200.、掻出し用コンベア
A1.A2.AB、A41.伸線機Figure 1 is a longitudinal cross-sectional diagram of a settling tank as a conventional purification device.
Figures 2 to 5 show embodiments of the present invention, Figure 2 is a schematic explanatory diagram of the operation of the purification device, Figure tJs is a partially cutaway plan view of the treatment tank, and Figure 4 is a partially cutaway treatment tank. A front view of the tank, and FIG. 5 is a longitudinal sectional view of the cyclone. 1001. Purification device 111. , return oil circuit 1B 11. Processing tank 14, 0. Cyclone 150. , primary storage tank 1600. Secondary storage tank 171. , septic tank 200. , scraping conveyor A1. A2. AB, A41. wire drawing machine
Claims (1)
次貯槽に連通される戻り油回路を開口し、上記処理槽は
該第1次貯槽及び第2次貯槽並びに浄化液槽とを備え、
第1次及び第2次貯槽底部にはスラッジ掻出し用コンベ
アが設けられ、かつ第2次貯槽上にはサイクロンが配備
され、該サイクロンには第1次貯槽の上澄液が供給さが
第2次貯槽に落下排出されることを特徴とする伸線機の
伸線液浄化装置。The first processing tank is installed in the wire drawing liquid receiving tank installed in the Shinaiii machine.
opening a return oil circuit that communicates with a secondary storage tank; the treatment tank includes the primary storage tank, the secondary storage tank, and a clarification liquid tank;
A sludge scraping conveyor is provided at the bottom of the primary and secondary storage tanks, and a cyclone is installed above the secondary storage tank, and the cyclone is supplied with the supernatant liquid from the primary storage tank. A wire drawing liquid purifying device for a wire drawing machine, characterized in that the wire is discharged into a secondary storage tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6633484A JPS60210316A (en) | 1984-04-02 | 1984-04-02 | Device for purifying drawing liquid of drawing mill |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6633484A JPS60210316A (en) | 1984-04-02 | 1984-04-02 | Device for purifying drawing liquid of drawing mill |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60210316A true JPS60210316A (en) | 1985-10-22 |
JPH0368767B2 JPH0368767B2 (en) | 1991-10-29 |
Family
ID=13312846
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6633484A Granted JPS60210316A (en) | 1984-04-02 | 1984-04-02 | Device for purifying drawing liquid of drawing mill |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60210316A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006297431A (en) * | 2005-04-19 | 2006-11-02 | Bridgestone Corp | Wet type metal wire drawing method |
CN105526486A (en) * | 2015-12-28 | 2016-04-27 | 江苏兴达钢帘线股份有限公司 | On-line lubricant sedimentation system |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS48102760A (en) * | 1972-04-08 | 1973-12-24 | ||
JPS57136959A (en) * | 1981-02-20 | 1982-08-24 | Oishi Eng:Kk | Purifying device for grinding fluid |
-
1984
- 1984-04-02 JP JP6633484A patent/JPS60210316A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS48102760A (en) * | 1972-04-08 | 1973-12-24 | ||
JPS57136959A (en) * | 1981-02-20 | 1982-08-24 | Oishi Eng:Kk | Purifying device for grinding fluid |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006297431A (en) * | 2005-04-19 | 2006-11-02 | Bridgestone Corp | Wet type metal wire drawing method |
CN105526486A (en) * | 2015-12-28 | 2016-04-27 | 江苏兴达钢帘线股份有限公司 | On-line lubricant sedimentation system |
Also Published As
Publication number | Publication date |
---|---|
JPH0368767B2 (en) | 1991-10-29 |
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