JPS5939447Y2 - Solid-liquid separator - Google Patents

Solid-liquid separator

Info

Publication number
JPS5939447Y2
JPS5939447Y2 JP1980102725U JP10272580U JPS5939447Y2 JP S5939447 Y2 JPS5939447 Y2 JP S5939447Y2 JP 1980102725 U JP1980102725 U JP 1980102725U JP 10272580 U JP10272580 U JP 10272580U JP S5939447 Y2 JPS5939447 Y2 JP S5939447Y2
Authority
JP
Japan
Prior art keywords
liquid
solid
mesh
cylinder
tube
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
JP1980102725U
Other languages
Japanese (ja)
Other versions
JPS5725710U (en
Inventor
幸造 山口
Original Assignee
大日本スクリ−ン製造株式会社
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 大日本スクリ−ン製造株式会社 filed Critical 大日本スクリ−ン製造株式会社
Priority to JP1980102725U priority Critical patent/JPS5939447Y2/en
Publication of JPS5725710U publication Critical patent/JPS5725710U/ja
Application granted granted Critical
Publication of JPS5939447Y2 publication Critical patent/JPS5939447Y2/en
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は、工場処理液中の固液分離装置に関し、殊に、
金属の精密加工法の1つであるフ第1・エツチング法に
よって処理された液中の膜固型を連続分離する装置に関
する。
[Detailed description of the invention] The present invention relates to a solid-liquid separation device for factory processing liquid, and in particular,
The present invention relates to an apparatus for continuously separating membrane solids in a liquid processed by the first etching method, which is one of metal precision processing methods.

一般に、プリント基板等を製作する工程において、まず
基板へのフ第1・レジスト膜の塗布付着し焼付、現像液
導電性膜をエツチング後、このフォトレジスト膜の剥離
を行う。
Generally, in the process of manufacturing a printed circuit board or the like, a first resist film is first coated on the board, adhered, and baked, a developer conductive film is etched, and then this photoresist film is peeled off.

このフ第1・レジスト膜の剥離においては剥離液によっ
て膨潤させて剥離するが、この剥離したいわゆる膜固型
と剥離液とを分離する際上記の固液分離装置が用いられ
る。
In this first stripping of the resist film, it is swollen with a stripping solution and then stripped, and the above-mentioned solid-liquid separator is used to separate the peeled so-called solid film from the stripping solution.

この種の固液分離装置で、200☆/min程度の処理
能力の従来技術は、前記処理能力以下であればタンク内
での沈澱分離法が、能力アップさせる場合は回転式遠心
分離法や、メツシュベルトによるベルI・掛は方式分離
法がある。
With this type of solid-liquid separator, the conventional technology with a processing capacity of about 200☆/min is the sedimentation separation method in a tank if the processing capacity is below the above-mentioned processing capacity, and the rotary centrifugal separation method if the capacity is to be increased. There is a method separation method for Bell I/Kake by Metschwert.

いずれも人手を要し、使い難いところがあった。All of them required manpower and were difficult to use.

即ち、沈澱分離法ではタンクを必要とし、ごく少量処理
については適しているが、処理量が」−ると沈澱タンク
が大きくなり、場所をとる等不適当であり、遠・じ・分
離法は連続式にすれば、装置が大きく高価になり、小型
では膜固形分を度々人手にて取除く手間がかかる。
In other words, the precipitation separation method requires a tank and is suitable for processing very small amounts, but if the amount of processing is large, the precipitation tank becomes large and takes up space, making it unsuitable. If a continuous system is used, the equipment will be large and expensive, and if it is small, it will take time and effort to manually remove the solid content from the membrane.

また、メツシュベルトによるベルト掛は方式分離法は、
メンシュベルトによる濾過に過ぎず、分離能力に難点が
ある。
In addition, the belt hanging method using Metsch belt is separated by
It is only a filtration method using a menschbelt, and its separation ability is difficult.

一方、大量処理の汚物の混じった水道用水など処理する
場合、回転式筒状のメツシュン濾過筒は従来より使われ
ているが、メツシュに付着した固型分を取除くには、清
浄水を部外より吹き付けて行ない分離水と清浄水とが混
合してもよく且つ構造複雑でもあった。
On the other hand, rotary cylindrical mesh filtration tubes have traditionally been used when processing tap water mixed with filth in large quantities, but in order to remove solid matter adhering to the mesh, it is necessary to partially remove clean water. Separated water and clean water may be mixed by spraying from the outside, and the structure is complicated.

かがる機構を本考案のような工場処理液の再利用システ
ムの一環にそのまま転用することは、はなはだ高価につ
く。
It would be very expensive to directly use the darning mechanism as part of a factory treatment liquid reuse system like the one proposed in this invention.

以上のような事情に鑑み本考案は案出されたもので、フ
ォトエツチング法の如き、精密加工の処理液の固液分離
に適する小型で安価且つ取扱い容易な装置を提供する。
The present invention was devised in view of the above circumstances, and provides a small, inexpensive, and easy-to-handle device suitable for solid-liquid separation of processing liquids in precision processing such as photoetching.

これを図面に示す実施例につき説明すれば、第1図は一
部破断正面図、第2図は一部破1新側面図を示すが、1
は底板2を有する密閉筐体で、該筐体1内に、一方を開
[」3した円筒状のメツシュン濾過筒4を液投入用管5
によって片持ち支持で且つ回転自在に横架している。
To explain this with reference to the embodiment shown in the drawings, Fig. 1 shows a partially broken front view, and Fig. 2 shows a partially broken side view.
is a closed housing having a bottom plate 2, and inside the housing 1, a cylindrical mesh filter cylinder 4 with one side open [3] is inserted into a liquid injection pipe 5.
It is cantilever supported and rotatably suspended horizontally.

詳しく云えば、該液投入用管5は筐体1外壁に固着され
たボス6を貫通してお・す、該ボス6は複数のブラケッ
ト板7′で補強支持されている。
Specifically, the liquid injection pipe 5 passes through a boss 6 fixed to the outer wall of the housing 1, and the boss 6 is reinforced and supported by a plurality of bracket plates 7'.

また、該ボス6と前記液栓入管5との間に管軸7を遊嵌
し、該管軸7の一端は前記メツシュ濾過筒4の鏡板8に
固定され、その他端は筐体1の底板2下に内蔵した駆動
モータ9によってチェノを介して1〜10rpm程度で
回転するスプロケット(図示せず)が設けられており、
モータ9によって管軸7を介してメツシュ濾過筒4はゆ
っくり回転される。
Further, a tube shaft 7 is loosely fitted between the boss 6 and the liquid stopper inlet tube 5, one end of the tube shaft 7 is fixed to the end plate 8 of the mesh filtration tube 4, and the other end is fixed to the bottom plate of the housing 1. A sprocket (not shown) is provided, which is rotated at a speed of about 1 to 10 rpm via a chain by a drive motor 9 built in below the sprocket.
The mesh filter cylinder 4 is slowly rotated by the motor 9 via the tube shaft 7.

液投入用管5の外端は、フランジ10を設け、所要の処
理現場と連結できるようになっており、また、11はチ
ェン覆いを示す。
The outer end of the liquid injection pipe 5 is provided with a flange 10 so that it can be connected to a desired processing site, and 11 indicates a chain cover.

次に、メツシュ濾過筒4はステンレス製の30メツシユ
金網で構成され、前記のように一方は開に13し、他方
は鏡板8で壁を作っている。
Next, the mesh filtration tube 4 is composed of a 30-mesh wire mesh made of stainless steel, and as described above, one side is open 13 and the other side is made of a wall with a mirror plate 8.

メツシュ濾過筒4の内周には筒軸方向に沿って、かつ、
径方向に向いた板状のフィン12を多数内側に植設し、
これによって内周を浅い区割室に形成し、回転するメツ
シュ濾過筒4内に溜った膜固型分をトhに迄持ち卜げる
ようにしている。
On the inner periphery of the mesh filter cylinder 4, along the cylinder axis direction, and
A large number of plate-shaped fins 12 facing in the radial direction are planted inside,
As a result, the inner periphery is formed into a shallow compartment, and the membrane solid content accumulated in the rotating mesh filtration cylinder 4 can be carried out to a depth h.

メツシュ濾過筒4の外上方にはエアパイプ13をメツシ
ュン濾過筒4の軸方向と平行に横架味読エアパイプ13
に多数の圧縮空気孔14を約15mm間隔で穿設し、空
気を噴出し所謂エアナイフの役目をするようにしでいる
An air pipe 13 is installed on the outer upper side of the mesh filter cylinder 4, and a horizontal air pipe 13 is installed parallel to the axial direction of the mesh filter cylinder 4.
A large number of compressed air holes 14 are bored at intervals of about 15 mm in the hole, so that air is blown out and acts as a so-called air knife.

該エアパイプ13はバルブ15を介してコンプレッサに
連結するようにしている。
The air pipe 13 is connected to a compressor via a valve 15.

、次に、16はメツシュよりなる引出状受皿で、所定時
間、装置内に装着しているので、該受皿16内に落下し
た膜固型分中の水分を滴下可能としているもので゛あっ
て、メツシュン濾過筒4内周に付着[7て回転により上
方に迄持ち運ばれた膜固型分を自由落下させると共に、
場合によっては、圧縮空気によって該受皿16内に吹き
落とすが、前記フィン12が膜固型群を区割した状態に
なっているので膜固型物が重力によるころがりかその区
割内において出て集合しゃすくうまく受肌にだんご状に
なって落る。
Next, reference numeral 16 is a drawer-shaped tray made of mesh, which is installed in the apparatus for a predetermined period of time, so that the moisture in the membrane solid content that has fallen into the tray 16 can be dripped. , adhering to the inner periphery of the mesh filter cylinder 4 [7] While allowing the membrane solids carried upward by the rotation to fall freely,
In some cases, compressed air is used to blow it down into the tray 16, but since the fins 12 divide the membrane solids into sections, the membrane solids will not roll due to gravity or come out within the divisions. It collects well and falls on the receiving skin in a dumpling shape.

なお、該受皿16には外端に取手17を設けており、そ
の支持は、筐体1の壁部ど前記静止液投入用管5の外周
によって支持されている。
A handle 17 is provided at the outer end of the tray 16, and the handle 17 is supported by the outer periphery of the static liquid injection tube 5, such as the wall of the housing 1.

18は液排出管で、底板2上にのぞませており、また、
19は排気「1で吹き込まれた圧縮空気及び液のガス等
を上方に排出し、処理液の漏出を防いでいる。
18 is a liquid discharge pipe, which is visible on the bottom plate 2, and
19 is an exhaust gas which discharges the compressed air and liquid gas blown in in step 1 upward to prevent leakage of the processing liquid.

上記のように、膜固型・剥離液の混合処理排液を液投入
用管5に流入させると、読管5がメツシュ濾過筒4の中
央部にのぞんでいるので、混合処理排液は、メツシュ濾
過筒の中央部で放出されでメツシュを透過し液排串管1
8に流下されでゆく。
As mentioned above, when the mixed treated waste liquid of the membrane solid and the stripping liquid is allowed to flow into the liquid input tube 5, since the reading tube 5 extends into the center of the mesh filtration cylinder 4, the mixed treated waste liquid is The liquid is discharged from the center of the mesh filtration tube and passes through the mesh to the drain pipe 1.
8 is carried away.

そして、処理液は回収されて再び膜剥離行程へ送られる
The processing liquid is then collected and sent to the membrane stripping process again.

一方、メツシュ濾過筒4内に残存したj膜固型分は、筒
4内に植設されたフィン12にすくわれ且つメツシュに
張付いた状態で上方に迄持ち一七げられながら重力の影
響でメツシュからはがれ、だんご状にかたまり、上方位
置で受皿16内に落される。
On the other hand, the J-membrane solids remaining in the mesh filtration tube 4 are scooped up by the fins 12 installed in the tube 4 and stuck to the mesh as they are lifted upwards and are subject to the influence of gravity. It peels off from the mesh, clumps into a ball, and falls into the saucer 16 at an upper position.

また時に1.15じてメツシュに部分的に張付いて残っ
た膜は、エアナイフからのFF、縮空□tで吹き落され
る。
Also, at 1.15 pm, the remaining film partially stuck to the mesh is blown off by FF and air contraction □t from the air knife.

このようにして処理液の固液分離は連続的に行われ、時
々受刑16を人手によって取り出し膜固型を放てきする
In this way, the solid-liquid separation of the treatment liquid is carried out continuously, and from time to time the prisoner 16 is manually taken out and the membrane solid is released.

■ 回転するメツシュ浜過筒4内周にフィン12を多数
植設したので、これらフィン12によって濾過すべき泥
上状膜を分割できて、だんご状に形成できるので、該膜
の固形分が回転メツシュ濾過筒4の内壁に付着したまま
降下することなく、上方位置迄持ち1′、ぼられ、そこ
で丁度固体受皿16上に落下することができ、しかも固
体受111L16をni欠的に抜き差しする作業(例え
ば1「1につき1間)に都合よくマツチしていて、固形
分の筒内からの取り出しを受皿の位置が高いことと相俟
って容易に行うことができる。
■ Since a large number of fins 12 are installed on the inner periphery of the rotating mesh filter tube 4, the mud-like membrane to be filtered can be divided by these fins 12 and formed into a dumpling shape, so that the solid content of the membrane can be rotated. The mesh filtration tube 4 does not fall while adhering to the inner wall, but is lifted up to the upper position 1', where it falls exactly onto the solid tray 16, and the work involves inserting and removing the solid tray 111L16 intermittently. (for example, 1" for 1"), and together with the high position of the saucer, it is possible to easily take out the solids from the cylinder.

■ 基板用膜及び剥離液の混合処理液は連続的に供給す
るが、分離された膜は固体受肌にて間欠的に取り出す固
液分離装置であるから、明らかなうに、ドロドロした固
形分の呈の割には液分の多い混合処理液に対し、都合よ
く分離できるばかりではなく、本装置の操作用動力は、
回転メツシュ濾過筒のみですみ、これど液栓入管5をメ
ツシュ濾過筒4四転支持と兼用して部品点数を少なくし
たことと相俟って、且つ、固体受皿16の支持も液栓入
管5で一端を支持しておることからも構造がきわめて簡
素化でき、半自動固液分離装置として、安価な相応しい
ものとすることができるし、該濾過筒4周辺より特には
み出し部材もなく場所もとらない。
■ The mixed processing solution of the substrate film and stripping solution is continuously supplied, but the separated film is taken out intermittently on the solid receiving surface, so it is clear that the solid content is Not only can it conveniently separate mixed processing liquids that have a relatively large liquid content, but the operating power of this device is
Only the rotating mesh filtration tube is required, and the liquid stopper inlet tube 5 is also used as a four-way support for the mesh filtration tube 4, reducing the number of parts. Since one end is supported by the filtration tube 4, the structure can be extremely simplified, making it suitable for use as a semi-automatic solid-liquid separator at low cost, and there are no parts protruding from the periphery of the filter cylinder 4, so it does not take up much space. .

■ 殊に、プリント基板等を製作する工程で、各種膜と
その剥離液の混合液が生じ、該液中の剥離液再利用のた
め、固液分離操作が必要となってくるが、液量に対し、
フォトレジスト等膜の量は少ないので、固体受皿に蓄積
される量は、1目に1回又は数回の取り出し量ですむこ
とから、連続操作の固液分離装置は必要でなく、いわば
半自動的な装置で充分その機能を果している。
■ In particular, in the process of manufacturing printed circuit boards, etc., a mixed solution of various films and their stripping solutions is generated, and in order to reuse the stripping solution in the solution, a solid-liquid separation operation is required. For,
Since the amount of film such as photoresist is small, the amount accumulated in the solid tray only needs to be taken out once or several times, so there is no need for a continuous solid-liquid separator, so it can be used semi-automatically. The equipment performs its function satisfactorily.

したがって、この種の装置には簡素で且つ安価なものが
好ましいニーズが存在し、そのニーズに合致した前記■
■の処理物に特有の効果を奏することができる。
Therefore, there is a need for this type of device to be simple and inexpensive, and the above-mentioned
Effects specific to the treated product (2) can be achieved.

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

第1図は正面図、第2図は側面図を示す。 3・・・・・・開ト−1,4・・・・・・メツシュ濾過
筒、5・・・・・・液栓入管、12・・・・・・フィン
、16・・・・・・受皿。
FIG. 1 shows a front view, and FIG. 2 shows a side view. 3...Open-1, 4...Mesh filtration cylinder, 5...Liquid stopper entry pipe, 12...Fin, 16... saucer.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 回転メツシュ沢過筒4の少くとも一方を開口3し、該メ
ツシュ沢過筒4内周にフィンを筒軸芯方向に多数植設し
、該筒4を片持支持する液栓入管5より筒4内に放流し
た混合液中の泥土状固形分を前上方に持ち1″、げるよ
うにし、前記開口3にて抜き差し自在で且つ前記液栓入
管5で一端を支持した固体受■旧6上に落すようにし、
固形分を間欠的に取り出すようにした基板用膜及びその
剥離液分離装置。
At least one side of the rotating mesh overflow tube 4 is opened 3, and a large number of fins are installed on the inner periphery of the mesh overflow tube 4 in the direction of the axis of the cylinder, and the liquid stopper inlet tube 5 that supports the cylinder 4 in a cantilever manner is inserted into the cylinder. A solid receiver 6 holds the mud-like solid content in the mixed liquid discharged into the liquid mixture 6 in the front upward direction so that it extends 1 inch, can be freely inserted and removed through the opening 3, and has one end supported by the liquid stopper entry pipe 5. Let it fall on top,
A substrate membrane and its stripping liquid separation device that extracts solid content intermittently.
JP1980102725U 1980-07-19 1980-07-19 Solid-liquid separator Expired JPS5939447Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1980102725U JPS5939447Y2 (en) 1980-07-19 1980-07-19 Solid-liquid separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1980102725U JPS5939447Y2 (en) 1980-07-19 1980-07-19 Solid-liquid separator

Publications (2)

Publication Number Publication Date
JPS5725710U JPS5725710U (en) 1982-02-10
JPS5939447Y2 true JPS5939447Y2 (en) 1984-11-05

Family

ID=29464144

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1980102725U Expired JPS5939447Y2 (en) 1980-07-19 1980-07-19 Solid-liquid separator

Country Status (1)

Country Link
JP (1) JPS5939447Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5233982Y2 (en) * 1973-01-23 1977-08-03

Also Published As

Publication number Publication date
JPS5725710U (en) 1982-02-10

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