JPH09262740A - Purifying equipment - Google Patents

Purifying equipment

Info

Publication number
JPH09262740A
JPH09262740A JP7205296A JP7205296A JPH09262740A JP H09262740 A JPH09262740 A JP H09262740A JP 7205296 A JP7205296 A JP 7205296A JP 7205296 A JP7205296 A JP 7205296A JP H09262740 A JPH09262740 A JP H09262740A
Authority
JP
Japan
Prior art keywords
main body
liquid
purified
oil
flow passage
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
JP7205296A
Other languages
Japanese (ja)
Inventor
Hiroyuki Miwa
弘行 三輪
Shuzo Yamamoto
修三 山本
Genichi Sato
嚴一 佐藤
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.)
Toyota Motor Corp
Original Assignee
Toyota Motor Corp
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 Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP7205296A priority Critical patent/JPH09262740A/en
Priority to CN 97104543 priority patent/CN1164455A/en
Publication of JPH09262740A publication Critical patent/JPH09262740A/en
Pending legal-status Critical Current

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  • Auxiliary Devices For Machine Tools (AREA)
  • Removal Of Floating Material (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a purifying device capable of eliminating both oil content and small dust by a single device. SOLUTION: An inclined plate 2 is arranged in a body 1 to form a zigzag flow passage 3, an oil flow passage 4 is formed on an upper end part of a rising flow passage 3a of the zigzag flow passage 3, a sediment flow passage 5 is formed on a lower end part of a descending flow passage 3b of the zigzag flow passage 3, a flow-out port of the purified liquid is provided on the downstream side of the zigzag flow passage 3, and a discharge port 13 of the sediment is provided on the upstream side of the zigzag flow passage 3.

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、固体、液体の少な
くとも一方の不純物を含む被浄化液から不純物を除去し
て洗浄された被浄化液とする浄化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a purification apparatus for removing impurities from a liquid to be purified containing at least one of solid and liquid impurities to obtain a cleaned liquid to be purified.

【0002】[0002]

【従来の技術】加工ラインでは、水溶性洗浄液やクーラ
ントを使用しているが、その液中に、 前工程からの持込み、またはマシンの潤滑油等の洩れ
により油が混入する、切粉や糸クズの微小ゴミが混入
する、という問題がある。これらは液の性能を劣化させ
るので、除去する必要があり、種種の装置が使用されて
いる。たとえば、特開平4−122463号公報は、切
粉など不純物を含む切削液に対して切粉を下方へ沈澱さ
せ、切削液を上方へサイクロン状態で昇出させて、切削
液を浄化する浄化装置を開示している。
2. Description of the Related Art A water-soluble cleaning liquid or coolant is used in a processing line. However, if the liquid is brought in from the previous process or oil leaks from the machine such as lubricating oil in the machine, chips or threads There is a problem that small dust particles are mixed in. These degrade the performance of the liquid and therefore need to be removed and various devices are used. For example, Japanese Unexamined Patent Publication No. 4-122346 discloses a purifying device for purifying the cutting fluid by precipitating the cutting fluid downward with respect to the cutting fluid containing impurities such as cutting dust and elevating the cutting fluid upward in a cyclone state. Is disclosed.

【0003】[0003]

【発明が解決しようとする課題】しかし、従来のサイク
ロン方式の浄化装置には、被洗浄液が油分を含んでいる
場合、その油分を除去できない、という問題がある。ま
た、油分を除去しようとすれば、ゴミ除去装置と別別に
油分除去装置を設けなければならず、装置の大型化を伴
なう。さらに、サイクロン方式の浄化装置は、ゴミを分
離、除去しにくく、ごみ除去がより確実なフィルター式
にすると、フィルターの定期的交換が必要になるという
問題もある。本発明の目的は、別別の装置とせずにゴミ
と油分の両方を除去できる浄化装置を提供することにあ
る。
However, the conventional cyclone type purifying apparatus has a problem that if the liquid to be cleaned contains oil, the oil cannot be removed. Further, if the oil content is to be removed, an oil content removing device must be provided separately from the dust removing device, which causes an increase in the size of the device. Further, the cyclone type purification device has a problem that it is difficult to separate and remove dust, and if the filter type is more reliable for dust removal, the filter needs to be replaced regularly. An object of the present invention is to provide a purification device that can remove both dust and oil without using a separate device.

【0004】[0004]

【課題を解決するための手段】上記目的を達成する本発
明の装置はつぎの通りである。中空の本体内に互いに間
隔をおいて傾斜し、かつ、上端と下端が前記本体と間隙
を有して配置された複数枚の傾斜プレートと、前記本体
下部に設けられ不純物を含む被浄化液を前記本体内に供
給する被浄化液供給装置と、前記本体下部に設けられ前
記本体下部に沈澱した不純物を排出する沈澱物排出口
と、前記本体上部の前記傾斜プレート下端側に開口する
浄化された前記被浄化液を前記本体から流出させる流出
口と、前記本体上部の前記傾斜プレート上端側に開口す
る前記本体上部に浮上した不純物を排出する浮上物排出
口と、を備えた浄化装置。
The device of the present invention for achieving the above object is as follows. A plurality of inclined plates that are inclined in a hollow body at a distance from each other and that are arranged with an upper end and a lower end having a gap with the main body; and a liquid to be purified that is provided in the lower portion of the main body and contains impurities. A liquid to be purified supply device to be supplied into the main body, a precipitate discharge port provided in the lower part of the main body for discharging impurities precipitated in the lower part of the main body, and a purified liquid having an opening at the lower end side of the inclined plate in the upper part of the main body A purification device comprising: an outlet for letting out the liquid to be purified from the main body; and a floating material outlet for discharging impurities floating on the upper portion of the main body, which is open to the upper end side of the inclined plate on the upper portion of the main body.

【0005】本発明の浄化装置では、被浄化液供給装置
から供給された被浄化液が本体内で複数の傾斜プレート
の間を流れる際に、浄化液より比重の軽い不純物は傾斜
プレートの上端側の間隙を通り抜けて上方に浮上し、本
体上部まで浮上した後に浮上物排出口から排出され、浄
化液より比重の重い不純物は傾斜プレートの下端側の間
隙を通り抜けて下方に沈降し、本体下部まで沈降した後
に沈澱物排出口から排出される。浮上物と沈澱物が除去
された被浄化液は本体上部の流出口から流出する。した
がって、単一の装置で、浮上物と沈澱物の両方を除去で
きる。
In the purifying device of the present invention, when the liquid to be purified supplied from the liquid to be purified supply device flows between the plurality of inclined plates in the main body, impurities having a specific gravity lower than that of the liquid to be purified are on the upper end side of the inclined plate. After passing through the gap of the above, it floats up to the upper part of the main body and is then discharged from the floating material discharge port, and impurities with a specific gravity higher than that of the purification liquid pass through the gap on the lower end side of the inclined plate and settle down to the lower part of the main body. After settling, it is discharged from the sediment discharge port. The liquid to be purified from which the floating substances and the precipitates have been removed flows out from the outlet on the upper part of the main body. Thus, a single device can remove both floats and precipitates.

【0006】[0006]

【発明の実施の形態】本発明実施例の浄化装置は、図1
に示すように、中空の筐体からなる本体1を有する。図
は、筐体が円筒形である場合を示しているが、直方体な
ど任意の形状をとることができる。本体1内には、複数
枚の傾斜プレート2が互いに間隔をおいて水平から傾け
られて配置されている。傾斜プレート2は、本体1の上
下方向壁から斜め下方に向かって延びるプレートの間
に、斜め上方に向かって延びる(図示例では本体1の中
央部から半径方向外側に斜め上方に向かって延びる)プ
レートをその上端と本体1の上下方向壁との間に流路の
一部となる間隙を残して、配置することにより、本体1
内にジグザグ状流路3を形成している。
BEST MODE FOR CARRYING OUT THE INVENTION A purifying apparatus according to an embodiment of the present invention is shown in FIG.
As shown in FIG. 1, it has a main body 1 made of a hollow casing. Although the figure shows the case where the housing is cylindrical, it may have any shape such as a rectangular parallelepiped. In the main body 1, a plurality of inclined plates 2 are arranged at intervals from each other and inclined from the horizontal. The inclined plate 2 extends obliquely upward between the plates extending obliquely downward from the vertical wall of the main body 1 (in the illustrated example, it extends obliquely upward outward in the radial direction from the central portion of the main body 1). By disposing a plate between the upper end of the plate and the vertical wall of the main body 1 with a gap that forms a part of the flow path, the main body 1
A zigzag-shaped flow path 3 is formed therein.

【0007】ジグザグ状流路3は上昇流路部分3aと下
降流路部分3bを有する。ジグザグ状流路3のうち上昇
流路部分3aから下降流路部分3bへの変化部分3cの
すぐ上の傾斜プレートと本体1との接続部近傍には、油
分を浮力で上方に通過させる油通路4が形成されてい
る。油通路4は、たとえば傾斜プレート2を点溶接で本
体1に固定したときに傾斜プレート2の上端と本体1の
内面との間に形成される約1〜3mmの隙間など(傾斜
プレート2に小孔を設けたものでもよい)から構成され
る。ジグザグ状流路3のうち下降流路部分3bから上昇
流路部分3aへの変化部分3dのすぐ下の傾斜プレート
には、沈澱物を沈澱物の自重で通過させる、開閉可能な
沈澱物通路5が形成されている。沈澱物通路5は、沈澱
物通路5を開閉する弁体6を取りつけた支持棒7を駆動
シリンダー8など(モータの回転を上下動に変換した機
構でもよい)により上下させることにより開閉される。
The zigzag channel 3 has an ascending channel portion 3a and a descending channel portion 3b. In the zigzag flow path 3, an oil passage for passing oil upward by buoyancy is provided in the vicinity of the connecting portion between the inclined plate and the main body 1 immediately above the changing portion 3c from the ascending flow path portion 3a to the descending flow path portion 3b. 4 are formed. The oil passage 4 is, for example, a gap of about 1 to 3 mm formed between the upper end of the inclined plate 2 and the inner surface of the main body 1 when the inclined plate 2 is fixed to the main body 1 by spot welding. It may be provided with holes). An openable and closable sediment passage 5 for allowing the sediment to pass by its own weight is provided on the inclined plate immediately below the changing portion 3d in the zigzag-like flow passage 3 from the descending passage portion 3b to the ascending passage portion 3a. Are formed. The sediment passage 5 is opened and closed by moving a support rod 7 having a valve body 6 for opening and closing the sediment passage 5 up and down by a drive cylinder 8 or the like (a mechanism in which the rotation of a motor is converted into vertical movement may be used).

【0008】被浄化液供給装置は本体1のジグザグ状流
路3より上流側の部分に開口する供給口9を有してお
り、供給口9から固体(切粉などの沈澱する物19)、
液体(油分18など)の少なくとも一方の不純物を含む
被浄化液10(洗浄液、クーラントなど)が本体1内に
供給される。本体1のジグザグ状流路3より下流側の部
分には、浄化された被浄化液を本体1から流出させる流
出口11が設けられている。また、本体1のジグザグ状
流路3より下流側でかつ被浄化液流出口11と離れた部
位には、油排出口12が設けられている。油排出口12
は、望ましくは油通路4の真上の設けられる。本体1は
中央部から外周部に向かって斜め上方に傾斜する天井壁
を有しており、この天井壁の中央部に被浄化液流出口1
1が設けられ、天井壁の外周部に油排出口12が設けら
れている。一方、本体1の沈澱物通路5の下方に位置す
る部分には、沈澱物排出口13が設けられている。望ま
しくは、本体1はテーパ状の底壁を有し、その最下部に
沈澱物排出口13が設けられている。この沈澱物排出口
13には沈澱物排出口13を開閉するバルブ14が設け
られている。
The liquid to be purified supply device has a supply port 9 which is opened in a portion upstream of the zigzag-shaped flow path 3 of the main body 1, and from the supply port 9 a solid (a substance 19 such as chips that precipitates),
A liquid to be purified 10 (cleaning liquid, coolant, etc.) containing at least one impurity of liquid (oil 18 or the like) is supplied into the main body 1. An outlet 11 is provided in a portion of the main body 1 on the downstream side of the zigzag-shaped flow path 3 to let the purified liquid to be purified flow out from the main body 1. Further, an oil discharge port 12 is provided at a portion of the main body 1 downstream of the zigzag flow path 3 and away from the liquid to be purified outlet 11. Oil outlet 12
Is preferably provided directly above the oil passage 4. The main body 1 has a ceiling wall that is inclined obliquely upward from the central portion toward the outer peripheral portion, and the liquid to be purified outlet 1 is provided at the central portion of the ceiling wall.
1 is provided, and the oil discharge port 12 is provided at the outer peripheral portion of the ceiling wall. On the other hand, a sediment discharge port 13 is provided in a portion of the main body 1 located below the sediment passage 5. Desirably, the main body 1 has a tapered bottom wall, and the sediment discharge port 13 is provided at the lowermost portion thereof. The deposit discharge port 13 is provided with a valve 14 that opens and closes the deposit discharge port 13.

【0009】被浄化液供給装置は、被浄化液が入れられ
たタンク15と、タンク15内の被浄化液に浮かぶ油分
や微小ゴミを含む液を選択的に流れ込ます、タンク15
内の被浄化液に浮かべられたフロート装置16と、フロ
ート装置16からの被浄化液を供給口9に送って本体1
内に供給するポンプ17(またはバキューム装置で吸引
したり、タンク15を高所に置いて液の自重で流下させ
てもよい)と、を備えている。
The purification liquid supply device selectively flows a tank 15 containing the purification liquid and a liquid containing oil and fine dust floating in the purification liquid in the tank 15, the tank 15
The float device 16 floated on the liquid to be purified inside, and the liquid to be purified from the float device 16 is sent to the supply port 9 and the main body 1
A pump 17 (or a vacuum device may be used for suction or a tank 15 may be placed at a high place to allow the liquid to flow down by its own weight).

【0010】つぎに、浄化作用について説明する。油
分、微小ゴミは液の表面に浮上しやすいので、フロート
装置16はタンク15内の被洗浄液のうち油分、微小ゴ
ミを多く含む表面近傍の液を選択的に流れこませ、被浄
化液を供給口9に送って本体1内に供給する。これによ
り、洗浄効率は上がる。
Next, the purifying action will be described. Since oil and minute dust easily float on the surface of the liquid, the float device 16 selectively causes the liquid near the surface containing a large amount of oil and minute dust among the liquids to be cleaned in the tank 15 to supply the liquid to be purified. It is sent to the mouth 9 and supplied into the main body 1. This improves the cleaning efficiency.

【0011】供給口9から本体1内に流れ込んだ被洗浄
液は、傾斜プレート2に沿ってジグザグ状流路3内を流
れる。この時、油粒18は軽いため上昇流路部分3aか
ら下降流路部分3bへの変化部分3c(本体1内の外周
部分に位置している)に溜り、そのすぐ上の傾斜プレー
ト2に設けられた油通路4を通り抜けて本体1の内壁面
に沿って上方に浮上し、他の油粒とくっつき粗粒化(粒
のサイズアップ)していき、これを最上部の流路まで繰
り返した後、油通路4の上方にある油排出口12から選
択的に排出される。
The liquid to be cleaned flowing from the supply port 9 into the main body 1 flows in the zigzag flow path 3 along the inclined plate 2. At this time, since the oil particles 18 are light, they are collected in the changing portion 3c (located on the outer peripheral portion in the main body 1) from the ascending flow path portion 3a to the descending flow path portion 3b, and are provided on the inclined plate 2 immediately above it. The oil passes through the oil passage 4 and floats upward along the inner wall surface of the main body 1 and sticks to other oil particles to become coarse particles (size increase of particles), and this is repeated up to the uppermost flow path. After that, the oil is selectively discharged from the oil discharge port 12 above the oil passage 4.

【0012】一方、微小ゴミは沈降する性質があり、そ
の沈澱(沈降)物19は下降流路部分3bから上昇流路
部分3aへの変化部分3dに沈澱し、そのすぐ下の傾斜
プレート2に設けられた沈澱物通路5が開となった時に
沈澱物通路5を通り抜けて下方に移行し、これを最下部
の流路まで繰り返した後、沈澱物排出口13から排出さ
れる。油分と沈澱物を除去された浄化された被浄化液は
流出口11から流出する。
On the other hand, the fine dust has a property of settling, and its precipitate (sedimentation) 19 is settled on the changing portion 3d from the descending flow path portion 3b to the ascending flow path portion 3a, and on the inclined plate 2 immediately below it. When the provided sediment passage 5 is opened, it passes through the sediment passage 5 and moves downward, and this is repeated up to the lowermost passage, and then discharged from the sediment discharge port 13. The purified liquid to be purified from which the oil content and the precipitate have been removed flows out from the outlet 11.

【0013】したがって、傾斜プレート2およびジグザ
グ状流路3の部分は、油分18と沈澱物19の両方を液
からの分離し除去する機能を有し、しかも単一の装置内
でこれを達成する。この場合、下降流路部分3bの下端
側を微小ゴミの沈澱部としてあるので、流れによって微
小ゴミに与えられる慣性力によっても微小ゴミが液体か
ら効果的に分離してそのまま沈澱部に溜り、溜まった所
が沈澱物通路5となっているので、溜まった沈澱物が再
び流れにのりにくいという利点もある。しかも、流路3
はジグザグ状のため長く、かつ層状になっているので、
小さなスペースで大きな分離、除去効果がある。この浄
化装置はフィルターをもたないので、フィルターの交換
をする必要がない。また、サイクロンを利用したり遠心
力を利用するものでないので、大きな速度が不要であ
り、しかも分離効率が高い。
Therefore, the part of the inclined plate 2 and the zigzag-shaped flow path 3 has a function of separating and removing both the oil component 18 and the precipitate 19 from the liquid, and achieves this in a single apparatus. . In this case, since the lower end side of the descending flow path portion 3b is used as a settling portion for the fine dust, the fine dust is effectively separated from the liquid by the inertial force applied to the fine dust by the flow, and the fine dust is directly collected in the settling portion and accumulated. Since the sediment passage 5 is provided at a different place, there is also an advantage that the accumulated sediment is less likely to flow again. Moreover, the flow path 3
Is long and layered due to the zigzag shape,
Has a large separation and removal effect in a small space. This purifier does not have a filter, so there is no need to replace the filter. Moreover, since a cyclone or a centrifugal force is not used, a large speed is unnecessary and the separation efficiency is high.

【0014】[0014]

【発明の効果】本発明の装置は、中空の本体内に互いに
間隔をおいて傾斜し、かつ、上端と下端が本体と間隙を
有して配置された複数枚の傾斜プレートと、本体下部に
設けられ不純物を含む被浄化液を本体内に供給する被浄
化液供給装置と、本体下部に設けられ本体下部に沈澱し
た不純物を排出する沈澱物排出口と、本体上部の傾斜プ
レート下端側に開口する浄化された被浄化液を本体から
流出させる流出口と、本体上部の傾斜プレート上端側に
開口する本体上部に浮上した不純物を排出する浮上物排
出口と、を備えているので、被浄化液供給装置から供給
された被浄化液が本体内で複数の傾斜プレートの間を流
れる際に、浄化液より比重の軽い不純物は傾斜プレート
の上端側の間隙を通り抜けて上方に浮上し、本体上部ま
で浮上した後に浮上物排出口から排出され、浄化液より
比重の重い不純物は傾斜プレートの下端側の間隙を通り
抜けて下方に沈降し、本体下部まで沈降した後に沈澱物
排出口から排出され、浮上物と沈澱物が除去された被浄
化液は本体上部の流出口から流出する。したがって、単
一の装置で、浮上物と沈澱物の両方を除去できる。
The apparatus of the present invention comprises a plurality of inclined plates which are inclined in a hollow body at a distance from each other and whose upper and lower ends are spaced apart from the body, and the lower plate of the body. A liquid to be purified supply device for supplying a liquid to be purified containing impurities to the main body, a precipitate discharge port provided at the lower part of the main body for discharging impurities settled at the lower part of the main body, and an opening at the lower end side of the inclined plate at the upper part of the main body Since the purified liquid to be purified is discharged from the main body, and the floating substance discharge port for discharging impurities floating on the upper portion of the main body, which is open to the upper end side of the inclined plate on the upper portion of the main body, the liquid to be purified is When the liquid to be purified supplied from the supply device flows between the multiple inclined plates in the main body, impurities with a specific gravity lower than that of the purified liquid pass through the gap on the upper end side of the inclined plate and float up to the upper part of the main body. Float after ascending Impurities that are discharged from the substance discharge port and have a higher specific gravity than the purified liquid pass through the gap on the lower end side of the inclined plate and settle down to the bottom of the main body, and then are discharged from the sediment discharge port. The removed liquid to be purified flows out from the outlet on the upper part of the main body. Thus, a single device can remove both floats and precipitates.

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

【図1】本発明の実施例の浄化装置の断面図である。FIG. 1 is a cross-sectional view of a purification device according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 本体 2 傾斜プレート 3 ジグザグ状流路 3a 上昇流路部分 3b 下降流路部分 4 油通路 5 沈澱物通路 9 供給口 10 被浄化液 11 被浄化液流出口 12 油排出口 13 沈澱物排出口 15 タンク 16 フロート装置 18 油分 19 沈澱物 1 Main Body 2 Inclined Plate 3 Zigzag Flow Path 3a Upflow Flow Path Part 3b Downflow Flow Path Part 4 Oil Passage 5 Sediment Passage 9 Supply Port 10 Purified Liquid 11 Purified Liquid Outlet 12 Oil Discharge Port 13 Precipitate Discharge Port 15 Tank 16 Float device 18 Oil 19 Deposit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 佐藤 嚴一 愛知県名古屋市名東区貴船一丁目204番地 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Koichi Sato 1-204 Kibune, Meito-ku, Nagoya, Aichi Prefecture

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 中空の本体内に互いに間隔をおいて傾斜
し、かつ、上端と下端が前記本体と間隙を有して配置さ
れた複数枚の傾斜プレートと、 前記本体下部に設けられ不純物を含む被浄化液を前記本
体内に供給する被浄化液供給装置と、 前記本体下部に設けられ前記本体下部に沈澱した不純物
を排出する沈澱物排出口と、 前記本体上部の前記傾斜プレート下端側に開口する浄化
された前記被浄化液を前記本体から流出させる流出口
と、 前記本体上部の前記傾斜プレート上端側に開口する前記
本体上部に浮上した不純物を排出する浮上物排出口と、
を備えた浄化装置。
1. A plurality of inclined plates, which are inclined in a hollow body at a distance from each other, and whose upper and lower ends are spaced from the body, and an impurity provided in a lower portion of the body. A liquid to be purified supply device that supplies the liquid to be purified into the main body, a precipitate discharge port that is provided in the lower part of the main body to discharge impurities that have precipitated in the lower part of the main body, and a lower end side of the inclined plate above the main body An outlet for discharging the purified liquid to be purified out of the main body, and a floating material outlet for discharging impurities floating on the upper portion of the main body, which is open to the upper end side of the inclined plate on the upper portion of the main body,
Purification device equipped with.
JP7205296A 1996-03-27 1996-03-27 Purifying equipment Pending JPH09262740A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP7205296A JPH09262740A (en) 1996-03-27 1996-03-27 Purifying equipment
CN 97104543 CN1164455A (en) 1996-03-27 1997-03-25 Apparatus for purifying liquid containing impurities

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7205296A JPH09262740A (en) 1996-03-27 1996-03-27 Purifying equipment

Publications (1)

Publication Number Publication Date
JPH09262740A true JPH09262740A (en) 1997-10-07

Family

ID=13478233

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7205296A Pending JPH09262740A (en) 1996-03-27 1996-03-27 Purifying equipment

Country Status (2)

Country Link
JP (1) JPH09262740A (en)
CN (1) CN1164455A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20130132472A (en) * 2010-12-14 2013-12-04 시티즌홀딩스 코리미티드 Workpiece separation device

Also Published As

Publication number Publication date
CN1164455A (en) 1997-11-12

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