JPS6343123B2 - - Google Patents

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Publication number
JPS6343123B2
JPS6343123B2 JP58189242A JP18924283A JPS6343123B2 JP S6343123 B2 JPS6343123 B2 JP S6343123B2 JP 58189242 A JP58189242 A JP 58189242A JP 18924283 A JP18924283 A JP 18924283A JP S6343123 B2 JPS6343123 B2 JP S6343123B2
Authority
JP
Japan
Prior art keywords
filtration
filter paper
water
filter
winding
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.)
Expired
Application number
JP58189242A
Other languages
Japanese (ja)
Other versions
JPS6082113A (en
Inventor
Yoshimi Oshitari
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP58189242A priority Critical patent/JPS6082113A/en
Priority to FR8415414A priority patent/FR2553297A1/en
Priority to DE19843436911 priority patent/DE3436911A1/en
Priority to GB08425744A priority patent/GB2147821A/en
Priority to NL8403095A priority patent/NL8403095A/en
Priority to IT48993/84A priority patent/IT1178129B/en
Publication of JPS6082113A publication Critical patent/JPS6082113A/en
Publication of JPS6343123B2 publication Critical patent/JPS6343123B2/ja
Granted legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 本発明は液体中の粒子を長時間連続的に効率よ
く除去できる小型な液体濾過装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a small-sized liquid filtration device that can efficiently remove particles in a liquid continuously for a long period of time.

LSIなどの半導体装置の製造に当つて、丸棒状
の半導体素材を薄い厚みで順次切り落して多数の
薄い円板状基板を作り、各円板状基板上には多数
の微小長方形区画に区切られた各区画のそれぞれ
に半導体素子回路を形成したのち、各区画に切断
分離して作ることが行われている。ところでこの
場合切断部に水を掛けながら切断を行うが、切断
に使用された水の中には、切断によつて生じた
0.3〜1μ程度の径をもつ半導体素材の切屑が多量
に含まれ、これに加えて半導体基板の材料がカリ
ウム砒素のような場合、有害物質を含むため、直
接排水することができない。
In manufacturing semiconductor devices such as LSI, a round bar-shaped semiconductor material is successively cut into thin pieces to create many thin disk-shaped substrates, and each disk-shaped substrate is divided into many small rectangular sections. After forming a semiconductor element circuit in each section, the semiconductor device is cut and separated into each section. By the way, in this case, cutting is done while pouring water on the cut part, but the water used for cutting contains the
It contains a large amount of semiconductor material chips with a diameter of about 0.3 to 1 μm, and in addition, if the semiconductor substrate material is potassium arsenic, it contains harmful substances and cannot be directly drained.

そこで対策として従来から凝集沈澱法による水
処理が行われているが、この方法によつては処理
が不充分であるなどの欠点がある。そこでこれに
代えて処理が簡単であり、しかも最近濾過性能の
向上が著しく、0.3μ以下の微粒子の除去も容易で
ある耐水性濾紙を用いる方法が実施されている。
この方法は例えば第1図aに示すように、波形に
折曲げた紙状濾材1(以下濾紙と称す)を環状と
なるようにケース2内に支持して、例えばその外
周側から被処理水を通して濾過する所謂カートリ
ツジ方式と呼ばれる方法である。また他の例は第
1図bに示すように、ロール状に巻込んだ濾紙1
の一部を通水部に位置させ、こゝに切断屑が堆積
したとき濾紙1をロール3に巻取つて、常に新し
い濾紙により濾過を行う方法である。
As a countermeasure, water treatment by coagulation and sedimentation has conventionally been carried out, but this method has drawbacks such as insufficient treatment. Therefore, instead of this, a method using water-resistant filter paper is being implemented, which is easy to process, and has recently seen a remarkable improvement in filtration performance, and which can easily remove fine particles of 0.3 μm or less.
In this method, for example, as shown in Fig. 1a, a paper-like filter medium 1 (hereinafter referred to as filter paper) folded into a corrugated shape is supported in a case 2 so as to form an annular shape, and the to-be-treated water is This is a so-called cartridge method in which the liquid is filtered through a filter. Another example is a filter paper 1 rolled up into a roll, as shown in FIG.
In this method, a part of the filter paper 1 is placed in a water passage section, and when cutting debris accumulates there, the filter paper 1 is wound up on a roll 3, and filtration is always performed using a new filter paper.

これらの方法は従来の凝集沈澱法に比べて操作
が簡単であり、濾過性能において大きく勝る。し
かしこれらの方法では濾過に使用される濾紙が薄
いために生ずる濾過効率の低下、即ち第1図のよ
うに表面に捕捉された大部分の切断屑4のうち、
濾紙1の通気細孔より小さい径の切断屑の一部が
水圧により濾紙1を通して排水側に出て、濾過効
率を低下するのをまぬがれ得ないため、予定した
濾過性能を得られない共通した欠点がある。また
これに加えて第1図aに示した方法即ちカートリ
ツジ方式では、濾紙1を波形に折曲げて濾過容積
を大にするように考慮されているが、それでも得
られる濾過容積は小さいため、しばしばカートリ
ツジを交換しなければならない。このため長時間
連続的な濾過を行うことができないばかりか、面
倒な交換作業を必要とし、それだけ半導体装置の
製造コストを上昇させる。
These methods are easier to operate than conventional coagulation-sedimentation methods and are significantly superior in filtration performance. However, in these methods, the filtration efficiency decreases due to the thinness of the filter paper used for filtration, that is, most of the cutting debris 4 trapped on the surface as shown in FIG.
A common drawback is that the expected filtration performance cannot be obtained because some of the cut debris with a diameter smaller than the ventilation pores of the filter paper 1 comes out through the filter paper 1 to the drainage side due to water pressure, reducing the filtration efficiency. There is. In addition, in the method shown in Figure 1a, that is, the cartridge method, the filter paper 1 is folded into a corrugated shape to increase the filtration volume, but the filtration volume obtained is still small, so it is often Cartridge must be replaced. For this reason, not only cannot continuous filtration be performed for a long period of time, but also troublesome replacement work is required, which increases the manufacturing cost of the semiconductor device.

本発明は以上の如き従来方法の欠点を一掃した
高い濾過効率を維持しながら、長時間連続的に濾
過作業を行うことができる小型な液体濾過装置の
提供を目的としてなされたもので、次に図面を用
いてその詳細を説明する。
The present invention has been made for the purpose of providing a compact liquid filtration device that can perform continuous filtration work for a long time while maintaining high filtration efficiency that eliminates the drawbacks of the conventional methods. The details will be explained using drawings.

本発明の特徴とするところは次の点にある。即
ち本発明においては第2図或いは第3図に示す平
面図のように、中心に空胴部5aを作るようにロ
ール状に多層に濾紙1を巻込んだ濾過胴5を作つ
て、図中矢印Aのようにその内周面から外周面の
方向に被処理水を通して、濾過を行うようにする
と同時に、濾過胴5の空胴部5a内に濾紙の一端
が固定された巻取軸6を設ける。そして濾過胴5
の内径寸法と巻取軸6の外径寸法を、常に濾過胴
5と濾紙を巻取つた巻取軸6との間に、被処理水
の流入空間を作るようにして、濾過胴5の内周面
から外周面に被処理水を通して濾過を行うと同時
に、切断屑4が内周面に堆積して通水圧力が増大
したとき、最後に後備濾過層Fを残すように巻取
軸6により切断屑堆積部分即ち一層分宛濾紙1を
巻取るようにしたことを特徴とするものである。
The features of the present invention are as follows. That is, in the present invention, as shown in the plan view of FIG. 2 or FIG. At the same time, the water to be treated is passed from the inner circumferential surface to the outer circumferential surface in the direction of the outer circumferential surface as shown by arrow A to perform filtration. establish. and filter cylinder 5
The inner diameter of the filter drum 5 and the outer diameter of the winding shaft 6 are adjusted such that an inflow space for the water to be treated is always created between the filter drum 5 and the winding shaft 6 on which the filter paper is wound. While filtering the water to be treated by passing it from the peripheral surface to the outer peripheral surface, when cutting waste 4 accumulates on the inner peripheral surface and the water flow pressure increases, the winding shaft 6 is used to leave a backup filtration layer F at the end. The filter paper 1 is characterized in that the filter paper 1 is wound up for the portion where cutting waste is accumulated, that is, for one layer.

なお第2図の例は固定した濾過胴5の空胴部5
aの中心に、回転されるようにした巻取軸6を設
けると同時に、ばね体7により圧接力を得るよう
にした圧接片8により、濾過胴5の濾紙1の巻込
みが緩むことのないように濾紙送出部の位置を規
制しながら、巻取りを行うようにしたものであ
る。また第3図の例は巻取軸6がばね体9によ
り、濾過胴5の内周面に圧接されるように設けて
濾過胴5を回転することにより、濾過胴5の内周
面と巻取軸6との間の摩擦を利用して、巻込みが
緩むことなく濾紙1の巻取りを行うようにしたも
のである。
Note that the example in FIG. 2 shows the cavity 5 of a fixed filter cylinder 5.
A winding shaft 6 that can be rotated is provided at the center of a, and at the same time, a pressure contact piece 8 that obtains pressure contact force by a spring body 7 prevents the winding of the filter paper 1 in the filter cylinder 5 from loosening. Winding is performed while regulating the position of the filter paper delivery section. Further, in the example shown in FIG. 3, the winding shaft 6 is provided so as to be pressed against the inner peripheral surface of the filtration drum 5 by a spring body 9, and by rotating the filtration drum 5, the winding shaft 6 is brought into contact with the inner peripheral surface of the filtration drum 5. The filter paper 1 is wound up by utilizing the friction between it and the take-up shaft 6 without loosening the winding.

本発明のように濾紙1を多層に巻いた濾過胴5
により濾過を行うようにすれば、第1層目の濾紙
により捕捉されることなく通過した切断屑4は第
2層目の濾紙の表面に堆積し、これでも捕捉され
ずに通過したものは第3層によつて捕捉される。
そして以下同一要領により次々と捕捉が行われ
る。従つて後備濾過層Fの積層数の選定により、
排水側への切断屑4の流出をほゞ完全に防いで濾
過でき、第1図a,bの方法における共通の欠点
は一掃される。また本発明においては濾紙を複数
層巻込んで濾過胴を形成しているため、第1図a
によつて前記したカートリツジ方式のものに比べ
て、濾紙の総面積を著しく多くできる。従つて連
続的に濾過できる時間を著しく長くでき、濾紙の
交換に要する時間と手数を激減できる。例えばカ
ートリツジ方式において長さ5m、幅0.5mの濾紙
を外径が0.5mになるように巻込んだ場合、濾紙
の面積は2.5m2である。これに対し本発明では同
じ大きさの濾紙を平均径0.3mで1000回巻いた場
合、その総面積は約471m2となり、カートリツジ
方式に比べて単純に比較しても約188倍となる。
また一般に濾紙一枚の厚さは0.2mm前後であるか
ら、1000回巻いたとしてもその巻厚は0.2mであ
る。従つて平均径0.3mの上にこの厚みがのると
考えても、その外径はほゞカートリツジ方式の外
径と同じ程度となり、ほゞ同じ径の容器内に収容
して形成できる。また、更に第1図bに示したロ
ール状に巻込んだ濾紙を通水部を通して巻込んで
濾過するものでは、濾紙の巻込み部と通水部およ
び巻取り部が直列となつており、しかも巻取り部
に巻込まれた場合、そのロールの外径は濾過開始
当初における巻込み部の外径と同じ大きさとな
り、同一スペースを必要とする。従つて装置が大
型となるが、本発明では濾過胴内において巻取軸
によつて巻取るようにしており、濾過胴の外径は
常に一定であるため、小型に形成できる利点があ
る。
A filter cylinder 5 in which filter paper 1 is wound in multiple layers as in the present invention
If filtration is performed by filtration, the cutting debris 4 that has passed without being captured by the first layer of filter paper will accumulate on the surface of the second layer of filter paper, and the debris that has passed without being captured will be deposited on the surface of the second layer of filter paper. Captured by 3 layers.
Then, capture is performed one after another in the same manner. Therefore, by selecting the number of layers of the backup filtration layer F,
The cutting waste 4 can be filtered while being almost completely prevented from flowing out to the drainage side, and the common drawbacks of the methods shown in FIGS. 1a and 1b are eliminated. In addition, in the present invention, since the filter cylinder is formed by rolling up multiple layers of filter paper, the
As a result, the total area of the filter paper can be significantly increased compared to the above-mentioned cartridge type. Therefore, the time during which continuous filtration can be carried out can be significantly extended, and the time and labor required for replacing filter paper can be drastically reduced. For example, in a cartridge system, when a filter paper with a length of 5 m and a width of 0.5 m is rolled up so that the outer diameter is 0.5 m, the area of the filter paper is 2.5 m 2 . On the other hand, in the present invention, if the same size filter paper is wound 1000 times with an average diameter of 0.3 m, the total area will be about 471 m2 , which is about 188 times as much as the cartridge method.
Furthermore, since the thickness of one sheet of filter paper is generally around 0.2 mm, even if it is rolled 1000 times, the thickness of the roll is 0.2 m. Therefore, even if this thickness is considered to be on top of the average diameter of 0.3 m, its outer diameter will be approximately the same as the outer diameter of the cartridge system, and it can be formed by being accommodated in a container with approximately the same diameter. Furthermore, in the filter paper rolled into a roll shown in FIG. 1b, which is rolled through a water passage section and filtered, the filter paper winding section, water passage section, and winding section are in series, Moreover, when wound up in the winding section, the outer diameter of the roll is the same as the outside diameter of the winding section at the beginning of filtration, and the same space is required. Therefore, the apparatus becomes large-sized, but in the present invention, the filter is wound up by a winding shaft within the filter cylinder, and the outer diameter of the filter cylinder is always constant, so there is an advantage that it can be made compact.

次に本発明の具体例について説明する。第4図
a,bは本発明の一実施例を示す部分縦断面図お
よびそのA―A′面に沿う矢視断面図であつて、
図において10は密閉容器、10aは被処理水の
入口、10bは清浄になつた水の出口、10cは
濾過胴交換用の蓋で、ボルトナツトにより着脱で
きるように形成されている。5は濾過胴で、中心
に空胴部5aを作るように濾紙を巻いて形成さ
れ、またその上下両端面には濾紙の巻取りを阻害
しない程度の厚さで接着剤層5bを設けて、濾過
胴5の内周面側のみから被処理水が入るように形
成される。11は多数の穴を有する円筒状のパン
チング、メタル板で、その上下両端部は密閉容器
10の内壁面に水密に熔接されて固定される。1
2は外周辺部がパンチングメタル板11の下端に
水密に連結された円環状の下部支持板、13はパ
ンチングメタル板11に着脱自在に水密にねじ止
めされる円環状の上部支持板である。そして上下
両端の外周面に水密パツキン5cを接着した濾過
胴5をパンチングメタル板11内に差込んだの
ち、上部支持板13をパンチングメタル板11の
上返部にねじ止めして、濾過胴5を上下から挟み
こむことにより、被処理水が上下部支持板12,
13と濾過胴5の間の隙間から、パンチングメタ
ル板11を介して清浄水の出口側に流出しないよ
うに濾過胴5を支持する。6は巻取軸、14は上
部軸受円板で蓋10cと共に固定される。15は
下部水密軸受で巻取軸6は電動機16により減速
機17を介して回転される。8は圧接片、18,
19は圧接片の上下支持体で、巻取軸6の上下に
固定される。そして圧接片8は第4図bのよう
に、その上下端を設けた支持穴8a,8b内に差
込まれた上下支持体18,19により動き得るよ
うに支持され、かつばね体7により上下支持体1
2,13に設けた半径方向の長穴12a,13a
内を、濾紙の巻取りに伴い外周方向に動いて、常
に濾過胴5の内周面に圧接され、濾過胴5に巻込
まれた濾紙が緩まないように濾紙1の巻取り位置
を規制する。そして入口10aから送りこまれた
被処理水を、図中矢印のように濾過胴5の内周面
側から外周面側に通して濾過を行い、パンチング
メタル板11と出口10bを介して清浄となつた
水を出口10bから排出する。20は圧力検出
器、21は電子スイツチで、圧力検出器20は濾
過胴5の被処理水の流入側の圧力上昇を検出し
て、これが例えば第5図に示す操作過程図中のA
のように2〜3Kg/cm2になつたとき信号を送出し
て、電子スイツチ21をオンとすることにより電
動機16を駆動して、巻取軸6により濾紙1の巻
取りを行わせる。そして切断屑4の堆積部分が巻
取られ、圧力が第5図Bのように元の値に戻ると
信号の送出を停止して、電動機16による濾紙1
の巻取りを停止させる動作を行い、以下圧力が上
昇する毎に以上の動作を繰返して、新しい濾紙1
を被処理水の流入面に位置させる。22は巻取り
規制スイツチ例えばリードスイツチであつて、そ
のリード線は密閉容器10を水密に貫通して引出
される。22aはその作動子、23は信号発生回
路であつて、圧接片8の下端に設けられている。
そして濾紙1の巻取軸6による巻取りにより、濾
過胴5の厚さが或る厚さになつたとき、電子スイ
ツチ21をオフとしてそれ以上電動機16による
巻取りが行われないようにして、必らず排出側に
切断屑4を流出させない厚さをもつ後備濾紙層F
を残す。従つてこのまゝ濾過を継続すれば、濾過
胴5の内周面には切断屑4はたまる一方である。
24はタイマー、25は電磁切換弁、26は本発
明による他の一台の液体濾過装置であつて、タイ
マー24は上記のように切断屑4がたまる一方の
状態となつて、圧力検出器20が第5図のC点の
圧力、例えば2〜3Kg/cm2以上の圧力を一定時間
連続的に検出したとき動作して出力を送出する。
そして電磁切換弁25を液体濾過装置26側に切
換えて、濾過が継続して行われるようにする。2
7は切断装置からの排水の流入口であつて、この
実施例装置による実験によれば、濾過された被処
理水は高い清浄度をもちしかも長い連続処理可能
時間をもつことが明らかにされた。
Next, specific examples of the present invention will be explained. FIGS. 4a and 4b are a partial longitudinal cross-sectional view showing an embodiment of the present invention and a cross-sectional view taken along the plane A-A',
In the figure, 10 is a closed container, 10a is an inlet for water to be treated, 10b is an outlet for purified water, and 10c is a lid for replacing the filter cylinder, which can be attached and detached using bolts and nuts. Reference numeral 5 denotes a filter cylinder, which is formed by winding a filter paper so as to form a cavity 5a in the center, and an adhesive layer 5b is provided on both upper and lower end surfaces of the cylinder to a thickness that does not impede winding of the filter paper. The filter body 5 is formed so that the water to be treated enters only from the inner peripheral surface side. Reference numeral 11 is a cylindrical punched metal plate having a large number of holes, and its upper and lower ends are welded and fixed to the inner wall surface of the closed container 10 in a watertight manner. 1
2 is an annular lower support plate whose outer peripheral portion is watertightly connected to the lower end of the punched metal plate 11, and 13 is an annular upper support plate which is detachably screwed to the punched metal plate 11 in a watertight manner. Then, after inserting the filter cylinder 5 with watertight gaskets 5c adhered to the outer peripheral surfaces of both upper and lower ends into the punched metal plate 11, the upper support plate 13 is screwed to the upside down part of the punched metal plate 11, and the filter cylinder 5 is By sandwiching them from above and below, the water to be treated can be transferred to the upper and lower support plates 12,
The filter cylinder 5 is supported so that clean water does not flow out from the gap between the filter cylinder 13 and the filter cylinder 5 through the punched metal plate 11 to the outlet side. Reference numeral 6 indicates a winding shaft, and 14 indicates an upper bearing disc which is fixed together with the lid 10c. 15 is a lower watertight bearing, and the winding shaft 6 is rotated by an electric motor 16 via a reduction gear 17. 8 is a pressure welding piece, 18,
Reference numeral 19 denotes upper and lower supports for the pressure contact piece, which are fixed above and below the winding shaft 6. As shown in FIG. 4b, the pressure contact piece 8 is movably supported by upper and lower supports 18 and 19 inserted into support holes 8a and 8b provided at its upper and lower ends, and is supported vertically by a spring body 7. Support 1
Radial long holes 12a and 13a provided in 2 and 13
As the filter paper is wound up, the inside moves in the outer circumferential direction and is always in pressure contact with the inner peripheral surface of the filter cylinder 5, regulating the winding position of the filter paper 1 so that the filter paper wound around the filter cylinder 5 does not loosen. Then, the water to be treated sent from the inlet 10a is filtered by passing from the inner peripheral surface side to the outer peripheral surface side of the filter cylinder 5 as shown by the arrow in the figure, and becomes clean through the punched metal plate 11 and the outlet 10b. The water is discharged from the outlet 10b. 20 is a pressure detector, 21 is an electronic switch, and the pressure detector 20 detects the pressure increase on the inflow side of the water to be treated of the filter barrel 5, and this detects, for example, A in the operation process diagram shown in FIG.
When the pressure reaches 2 to 3 kg/cm 2 , a signal is sent out and the electronic switch 21 is turned on to drive the electric motor 16 and cause the winding shaft 6 to wind up the filter paper 1. When the accumulated part of the cutting waste 4 is wound up and the pressure returns to the original value as shown in FIG.
1. Repeat the above operation every time the pressure rises to remove a new filter paper 1.
is located on the inflow surface of the water to be treated. Reference numeral 22 denotes a winding regulation switch, such as a reed switch, whose lead wire passes through the closed container 10 in a watertight manner and is drawn out. Reference numeral 22a denotes an actuator thereof, and 23 denotes a signal generating circuit, which are provided at the lower end of the pressure contact piece 8.
When the thickness of the filter drum 5 reaches a certain level due to the winding of the filter paper 1 by the winding shaft 6, the electronic switch 21 is turned off to prevent further winding by the electric motor 16. A back-up filter paper layer F having a thickness that does not necessarily allow cutting waste 4 to flow out to the discharge side
leave. Therefore, if the filtration continues as it is, the cutting debris 4 will continue to accumulate on the inner circumferential surface of the filter cylinder 5.
24 is a timer, 25 is an electromagnetic switching valve, and 26 is another liquid filtration device according to the present invention. When the pressure at point C in FIG. 5, for example, a pressure of 2 to 3 kg/cm 2 or more is continuously detected for a certain period of time, it operates and sends out an output.
Then, the electromagnetic switching valve 25 is switched to the liquid filtration device 26 side so that filtration continues. 2
7 is an inlet for wastewater from the cutting device, and experiments using this example device revealed that the filtered water to be treated has a high degree of cleanliness and can be continuously treated for a long time. .

例えば10c.c.当り約30000〜50000箇の切断屑を含
む切断装置からの排出水を、流量25/minで濾
過したところ、排水中の切断屑の数は10c.c.当り
100〜300箇であり、排出粒子の粒径は0.3μ〜1μで
あつた。また500時間連続的に運転しても濾過性
能は殆ど変ることがなかつた。また一般に半導体
切断装置は1台当り25/分の水(工業用水又は
純水)を必要とし、一工場当り30台の切断装置を
備えて24時間連続作業することがよく行われる。
従つて30日当りの水の量は一台当り25×60×24×
30=1080t即ち月当り1080×30トンの極めて大量
となり、水代金も多額になる。しかし本発明によ
る濾過は極めてよく行われ、しかも処理のために
薬品を使用しないことから、排水の再利用を行う
ことができ、水を大きく節約できる。
For example, when waste water from a cutting device containing about 30,000 to 50,000 pieces of cutting waste per 10 c.c. is filtered at a flow rate of 25/min, the number of cutting pieces in the waste water is
There were 100 to 300 particles, and the particle size of the discharged particles was 0.3 μ to 1 μ. Furthermore, even after continuous operation for 500 hours, there was almost no change in filtration performance. Generally, each semiconductor cutting device requires 25/min of water (industrial water or pure water), and it is common for one factory to have 30 cutting devices and operate continuously for 24 hours.
Therefore, the amount of water per 30 days is 25 x 60 x 24 x per unit.
30 = 1080 tons, that is, 1080 x 30 tons per month, which is an extremely large amount, and the water bill will be large. However, since the filtration according to the invention is very efficient and no chemicals are used for the treatment, the waste water can be reused and water can be saved significantly.

なお以上においては半導体装置における切断装
置の排水について説明したが、原子力プラントに
おける排水処理などの他の排水処理にも適用でき
ることは勿論であつて、この場合排水中の粒子径
により使用する濾紙の濾過効率を定めればよい。
また以上の実施例では排出側に必らず後備濾過層
Fを残して巻取るようにしたが、この後備濾過層
Fを別に作つて濾過胴5の外周にはめこみ、濾過
胴5の濾紙を最後まで巻取るようにしてもよい。
この方法によれば、リードスイツチ22など濾過
層Fを残して巻取るための装置を省略できるので
装置を簡単化できる。
Although the above description has been about wastewater from cutting equipment in semiconductor devices, it is of course applicable to other wastewater treatments such as wastewater treatment in nuclear power plants. All you have to do is determine the efficiency.
Furthermore, in the above embodiment, the back-up filtration layer F was always left on the discharge side and the back-up filtration layer F was wound up, but this back-up filtration layer F was made separately and fitted around the outer periphery of the filtration drum 5, so that the filter paper of the filtration drum 5 was finally It is also possible to wind it up to the maximum length.
According to this method, it is possible to omit a device such as the reed switch 22 for winding up the filtration layer F while leaving it behind, thereby simplifying the device.

また以上では紙状の濾材を巻いて濾過胴を形成
したが、糸例えば2〜20μの繊維を外径が3〜8
mmになるように束ねて作つた長い糸を、第6図に
示す斜視図のように、一つの層を形成する糸28
aと次の層を形成する糸28bとが交叉するよう
に巻いて濾過胴5を作り、この糸28を巻取軸6
により切断屑が堆積する毎に巻取るように構成し
てもよい。なおこの場合糸と糸との空隙、更には
糸を形成する繊維間の空隙などが濾過作用を行
う。従つて所要の濾過効率を得るように、糸の巻
き方、巻き間隔、糸の種類などを選定すればよ
い。
In addition, in the above description, the filter body was formed by winding paper-like filter media, but threads such as fibers of 2 to 20 μm with an outer diameter of 3 to 8
As shown in the perspective view in Fig. 6, long threads made by bundling them to a length of
A and a thread 28b forming the next layer are wound to intersect with each other to form a filter cylinder 5, and this thread 28 is wound around a winding shaft 6.
It may also be configured to wind up cutting waste each time it accumulates. In this case, the voids between the threads, as well as the voids between the fibers forming the threads, perform a filtration action. Therefore, the method of winding the thread, the winding interval, the type of thread, etc. may be selected in order to obtain the required filtration efficiency.

以上の説明から明らかなように、本発明によれ
ば液体中の粒子を長時間連続的に効率よく除去で
きる小型な液体濾過装置を提供し得るもので、実
用上の効果は著しい。
As is clear from the above description, according to the present invention, it is possible to provide a compact liquid filtration device that can efficiently remove particles in a liquid continuously for a long period of time, and the practical effects are remarkable.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図a,bは従来装置の概略説明図、第2
図、第3図は本発明の原理説明図、第4図a,b
は本発明の一実施例を示す部分縦断面図およびそ
のA―A′部における矢視断面図、第5図は操作
過程図、第6図は本発明に用いる濾過胴の他の具
体例を示す斜視図である。 1…濾紙、2…ケース、3…巻取りロール、4
…切断屑、5…濾過胴、5a…接着剤層、5c…
水密パツキン、5a…空胴部、6…巻取軸、F…
後備濾過層、7…ばね体、8…圧接片、8a,8
b…支持穴、9…ばね体、10…密閉容器、10
a…被処理水の入口、10b…清浄水の出口、1
0c…蓋、11…円筒状パンチングメタル板、1
2,13…円環状の上部と下部支持板、12a,
13a…圧接片移動用長穴、14…上部軸受板、
15…下部水密軸受、16…電動機、17…減速
機、18,19…圧接片の上下支持体、20…圧
力検出器、21…電子スイツチ、22…巻取り規
制スイツチ、22a…その作動子、23…制御信
号発生回路、24…タイマー、25…電磁切換
弁、26…本発明による他の一台の液体濾過装
置、27…被処理水源、28…糸、28a,28
b…行きの糸と帰りの糸。
Figures 1a and b are schematic explanatory diagrams of the conventional device;
Figure 3 is an explanatory diagram of the principle of the present invention, Figure 4 a, b
5 is a partial longitudinal cross-sectional view showing one embodiment of the present invention and a cross-sectional view taken along the line A-A', FIG. 5 is an operation process diagram, and FIG. FIG. 1...filter paper, 2...case, 3...take-up roll, 4
... Cutting waste, 5... Filter cylinder, 5a... Adhesive layer, 5c...
Watertight packing, 5a...cavity part, 6...take-up shaft, F...
Backup filtration layer, 7... Spring body, 8... Pressure contact piece, 8a, 8
b...Support hole, 9...Spring body, 10...Airtight container, 10
a... Inlet of treated water, 10b... Outlet of clean water, 1
0c...Lid, 11...Cylindrical punching metal plate, 1
2, 13...Annular upper and lower support plates, 12a,
13a... Elongated hole for moving the pressure welding piece, 14... Upper bearing plate,
DESCRIPTION OF SYMBOLS 15...Lower watertight bearing, 16...Electric motor, 17...Reducer, 18, 19...Upper and lower supports of the pressure contact piece, 20...Pressure detector, 21...Electronic switch, 22...Rewinding regulation switch, 22a...It actuator, 23... Control signal generation circuit, 24... Timer, 25... Solenoid switching valve, 26... Another liquid filtration device according to the present invention, 27... Water source to be treated, 28... Thread, 28a, 28
b...The going thread and the returning thread.

Claims (1)

【特許請求の範囲】[Claims] 1 中心に空胴部をもつように濾材を巻込んで形
成された濾過胴から、濾材を空胴部内に設けた巻
取軸により濾過胴の外周に後備濾過層を残すよう
に巻取るように形成し、濾過胴の内周面から被処
理水を供給して濾過するように構成したことを特
徴とする液体濾過装置。
1. From a filter cylinder formed by winding a filter medium so as to have a hollow part in the center, the filter medium is wound up by a winding shaft provided in the hollow part so as to leave a backup filtration layer on the outer periphery of the filter cylinder. 1. A liquid filtration device characterized in that the water to be treated is supplied from the inner circumferential surface of a filtration drum and filtered.
JP58189242A 1983-10-12 1983-10-12 Liquid filter Granted JPS6082113A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP58189242A JPS6082113A (en) 1983-10-12 1983-10-12 Liquid filter
FR8415414A FR2553297A1 (en) 1983-10-12 1984-10-08 LIQUID FILTER, IN PARTICULAR FOR CONTINUOUS REMOVAL OF PARTICLES CONTAINED IN WATER AFTER CUTTING OF SEMICONDUCTOR DEVICES
DE19843436911 DE3436911A1 (en) 1983-10-12 1984-10-08 LIQUID FILTER
GB08425744A GB2147821A (en) 1983-10-12 1984-10-11 Liquid filter
NL8403095A NL8403095A (en) 1983-10-12 1984-10-11 FLUID FILTER.
IT48993/84A IT1178129B (en) 1983-10-12 1984-10-11 LIQUID FILTER

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58189242A JPS6082113A (en) 1983-10-12 1983-10-12 Liquid filter

Publications (2)

Publication Number Publication Date
JPS6082113A JPS6082113A (en) 1985-05-10
JPS6343123B2 true JPS6343123B2 (en) 1988-08-29

Family

ID=16237992

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58189242A Granted JPS6082113A (en) 1983-10-12 1983-10-12 Liquid filter

Country Status (1)

Country Link
JP (1) JPS6082113A (en)

Also Published As

Publication number Publication date
JPS6082113A (en) 1985-05-10

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