JPWO2003099417A1 - High viscosity fluid filter unit and spinning pack - Google Patents

High viscosity fluid filter unit and spinning pack Download PDF

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JPWO2003099417A1
JPWO2003099417A1 JP2004506937A JP2004506937A JPWO2003099417A1 JP WO2003099417 A1 JPWO2003099417 A1 JP WO2003099417A1 JP 2004506937 A JP2004506937 A JP 2004506937A JP 2004506937 A JP2004506937 A JP 2004506937A JP WO2003099417 A1 JPWO2003099417 A1 JP WO2003099417A1
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filter unit
filter
viscosity fluid
fluid filter
pleated
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JP4423186B2 (en
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敏 石川
敏 石川
睦彦 西畑
睦彦 西畑
英昭 谷川
英昭 谷川
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Kansai Wire Netting Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/10Filter screens essentially made of metal
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/20Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/20Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2027Metallic material
    • B01D39/2041Metallic material the material being filamentary or fibrous
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D1/00Treatment of filament-forming or like material
    • D01D1/10Filtering or de-aerating the spinning solution or melt
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D1/00Treatment of filament-forming or like material
    • D01D1/10Filtering or de-aerating the spinning solution or melt
    • D01D1/106Filtering

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • Textile Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Filtering Materials (AREA)
  • Filtration Of Liquid (AREA)

Abstract

高粘性の溶融有機高分子化合物や高分子溶液などに含まれる異物のろ過に使用するプリーツタイプのフィルターユニットである。ろ過される高粘性流体がフィルター周縁部からリークしたり、高いろ過圧によってフィルターが変形しないように構成する。シート状フィルター(1)の両面に支持部材(2)を重ね、ジグザグに折り畳んでプリーツ加工する。プリーツ状にされた盤状体の周縁部(4)をつば状に形成し、両面に軟質金属製または金属不織布製のリングシート類(5)を重ね、金属薄板(6)を被せて圧着し、周縁部4における高粘性流体リークを防止する。折りひだ(7)は、先端部分をふくらませ、隣り合う折りひだの先端部と互いに近接又は部分的に接触するように形成する。プリーツフィルターの信頼性と利点とが引き出され、合成繊維、合成フィルムなどの有機高分子化合物成形品の製造工程に好適である。It is a pleated type filter unit used for filtering foreign substances contained in highly viscous molten organic polymer compounds or polymer solutions. The high-viscosity fluid to be filtered does not leak from the peripheral edge of the filter, or the filter is not deformed by a high filtration pressure. The support member (2) is overlapped on both surfaces of the sheet filter (1), folded in a zigzag manner, and pleated. The peripheral part (4) of the pleated plate-like body is formed into a collar shape, ring sheets (5) made of soft metal or metal non-woven fabric are overlapped on both sides, and a thin metal plate (6) is put on and crimped. , Preventing high-viscosity fluid leakage at the peripheral edge 4. The fold fold (7) is formed such that the tip end portion is inflated and the tip end portions of adjacent fold folds are close to or partially in contact with each other. The reliability and advantages of the pleated filter are derived, and it is suitable for the manufacturing process of organic polymer compound molded articles such as synthetic fibers and synthetic films.

Description

技術分野
本発明は、高粘性流体用フィルターユニット及び紡糸パックに関する。高粘性の溶融有機高分子化合物や高分子溶液などに含まれる夾雑物やゲル状物のろ過、分離に好適である。
背景技術
流体中の固体異物をろ過して分離、除去する目的で製作されているフィルターユニットは、電子工業、精密工業、製薬工業、水処理などのあらゆる産業分野に広く利用されており、その技術的レベルは極めて高度なものであって、かつ使いやすくなっている。しかし、そのろ過対象は空気や水などの低粘度物質を中心に開発されてきた。
一方、有機高分子化合物を原料とするプラスチック成形加工業や一部の食品工業分野などにおいても、フィルターユニットが使用されて高粘度流体中の固形異物をろ過、分離している。たとえば、合成繊維、合成フィルムやその他の有機高分子化合物成形品は、それぞれ紡糸、製膜、成形などの工程を経て製造されているが、これらの工程においては原料ポリマーを加熱溶融したり溶剤に溶解して液体化し、フィルターユニットを装着したろ過装置や紡糸パック等によって混在する異物やゲル化物をろ過、分離している。これらのろ過操作は、前記の空気や水のろ過操作とは異なり、原料の有機高分子化合物やその溶液の粘度が極めて高いので、ろ過速度が遅く非能率的である。そこで、ろ過速度を上げるために前記の低粘度物質に較べて数十倍、数百倍のろ過圧力を付与したり、フィルターのろ過面積を可能な限り大きくするなどの努力がなされているものの、現在に至るまで十分な成果を得るに至っていない。
フィルターのろ過面積を増加する手段として、例えば特開昭60−058208号には、ろ過膜をネット支持体で補強し、それらを合わせて折り畳み、プリーツ状にしたものを円筒状にしたフィルターユニットが開示されている。この方式はろ過圧の小さな気体や粘性の小さな液体のろ過には適当であるが、円筒状であるため、高いろ過圧力を要する高粘度流体をろ過するには耐圧設計などの点で限界がある。また、高いろ過圧力を要するケースにプリーツ状フィルターを使用しようとするとフィルター周縁部からのリークが問題になる。この問題を解決する手段が特開平10−211411号公報に開示されているが、接着剤を利用するために、高温度溶融ポリマーをろ過するには耐熱性の点で不適当である。また、特開2002−266152公報には、金属線フィルターと金属線不織布とを重ねて波形形状に形成し、外周部を金属リムで挟持した溶融紡糸パック用のフィルターユニットが開示されている。しかし、高圧力損失を伴う粘弾性流体のろ過に対する、フィルター部の変形対策やろ過液のリーク防止に課題を残していた。
さて、前記の高温度溶融ポリマーのろ過工程では、原料や操作条件によって異なるが高粘性流体を効率的にろ過するには10〜30MPa程度のろ過圧力を要することも少なくない。このろ過圧力を下げるために、フィルター形状に工夫を加えて、例えば、紡糸パック1個当たりのろ過面積を増やす試みがなされている。しかし、ろ過される筈の高粘性流体がフィルター周縁部からフィルターをバイパスして漏出し、製品の品質低下や操業トラブルの原因になったり、操業時間の経過とともにろ過圧が高くなってフィルターが変形し、所要のろ過面積を維持できないなどの課題が発生している。
本発明は、合成繊維の紡糸工程や合成フィルムの製膜工程などにおける高粘性流体の高圧ろ過に際し、ろ過しようとする高粘性流体がフィルターをバイパスして漏出することを阻止し、かつ、ろ過圧力によってフィルターの形状が変形するのを防止して、コンパクトで長い期間、継続、安定してろ過操作のできる、信頼性の高い高粘性流体用フィルターユニットを課題に、研究と試作とを行った結果、完成されたものである。
発明の開示
本発明について第1図及び第2図を参照して説明する。本発明は、シート状フィルター1に支持部材2を重ねてジグザグに折り畳まれた複層からなるプリーツ状の盤状体3であって、盤状体の周縁部4が平たくつば状に形成され、かつ、前記つば状部分4の少なくとも片面には軟質金属製又は金属不織布製のリングシート類5を重ね、さらに金属薄板6を被せ、つば状部分4において重ねられたフィルター、支持部材、リングシート類及び被せられた金属薄板を圧着することにより、周縁部において高粘性被ろ過流体がフィルター1をバイパスして漏出するのが防止されていることを特徴とする高粘性流体用フィルターユニットを開示する。プリーツの折りひだ7の先端部分は、ふくらんで、隣り合う折りひだの先端部と互いに近接し、又は部分的に接触していることが望ましい。
上記の高粘性流体用フィルターユニットは、高粘性流体の種類やろ過条件によっては、第8図に示されるように、使用中にろ液流出側の折りひだ81の先端部が変形し、ろ液の円滑な流れが阻害されることがある。このようなケースにおいては、第3図に示されるように、フィルター31のろ液流出側Bに2枚の支持部材32b、32cを重ね、ジグザグに折り畳んだ4層からなるプリーツ状の盤状体を用いることによって、ろ液の円滑な流れを維持できる。さらに、支持部材41に金属線材42を織成した金網を用いるに当たっては、金属線材42が折りひだの長手方向43に対してバイアス(斜交)方向になるように重ねるとよい(第4図)。
また、本発明フィルターユニットでは、第6図に示されるように、ろ液の流路を安定的に維持するため、盤状体の片面又は両面の折りひだ61の間に通液性のスペーサー62を挿入してもよい。その場合、前記盤状体の両表面又は一方の表面にスペーサーの離脱を防止するため、通液性の金網63などを取り付けておくとよい。
あるいは、前記つば状部分71において、片面にのみに軟質金属製又は金属不織布製のリングシート類72を重ねて足りるケースもある(第7図)。
さらに本発明は、紡糸パックのケーシング91中に、紡糸液の吐出側92から順に、少なくとも紡糸口金93、フィルターユニットを支持する耐圧板94、前記したいずれかの高粘性流体用フィルターユニット95、前段のフィルター96及び高粘性流体分配板97を含んで取り付けられていることを特徴とする紡糸パック(第9図)を開示する。なお、本発明においてフィルターユニットは、フィルターを装置等に装着、交換しやすいなど、使用に便利なように付属部材とともに組み立てられたユニットをいう。
発明を実施するための最良の形態
本発明の理解を容易にするため、第1図及び第2図を参照しつつ本発明に係る高粘性流体用フィルターユニットを、便宜上、一般的な製作手順に従って順次に説明するが、本発明フィルターユニットは、製作手順によって限定されるものではない。
フィルター1には、通常、必要とするろ過レベルに応じ、細かい目を構成する金属不織布製シート状の精密ろ過用フィルターなどを適宜に選択して用いるが、目的によっては細かい目の金網、合成繊維不織布などを用いてもよい。例えば、合成繊維の紡糸パックに組み込むためのフィルターユニットを製作する場合には、一般に目開きが40μm以下のフィルターを使用する。
シート状フィルター1には、形状を保持するための支持部材2を重ね、ろ過面積を広くするためにジグザグに折り畳んでプリーツ加工して、両面に折りひだ7を平行に形成し、プリーツ状盤状体3として用いる。盤状体3の折りひだ7に直角方向の断面形状は、両面において先端が尖った従来のジグザグなプリーツ状でもよい。しかし、好ましくは第1図に例示されるように、シート状フィルター1の両面に支持部材2を重ね3層にしてプリーツ加工し、両面ともに折りひだ7の先端部分を丸くふくらませて、隣り合う折りひだ7の先端部と互いに近接し、又は部分的に接触したプリーツ状の盤状体3に加工する。折りひだ7の間は、ろ液の流路8になるので流れを保つため間隙を設ける。加工には、金網用のプリーツ加工機を利用すればよい。プリーツ加工時には、フィルター1と支持部材2との間は固定されていないので、フィルター1に無理な応力が作用することはなく容易に加工できる。
支持部材2には、強度を考慮して直径が0.17mm以上の金属線材を用いて織成または編成された、比較的目の粗い金網が好ましく用いられる。このほか、金属線材を用いた不織布等を利用してもよい。線材にはステンレス鋼線を用い、平織、綾織、畳織(Dutch weave )の金網を用いることが多い。プリーツの深さ及びピッチは、ろ過圧、所要ろ過面積、取付条件などにより適宜に決めることができる。紡糸ヘッドに装着することを目的にする場合には、一般に盤状体3の厚さを5〜10mm程度、折りひだのピッチを3〜5mm程度の範囲で設計し、製作するとよい。支持部材は、例えば、ろ過の圧力損失が小さく長期の使用においてプリーツ面の変形が無視できるような場合には、ろ過時の受圧方向を考慮し支持部材をフィルターの片面のみに配置することも可能ではあるが、合成繊維の紡糸パックに組み込むことを目的にする場合などでは、両面に重ねることが望ましい。
さて、本発明のフィルターユニットは、かなり大きなろ過圧力を受けるので、紡糸パックなどでは、通常、フィルターユニットを支持する耐圧板(第9図:94)上に装着される。高粘性流体のろ過操作がはじまり、ろ過された異物が次第にフィルター面に蓄積され、ろ過圧が上昇してくると、フィルターユニットは、ろ過される高粘性流体と耐圧板との間に挟まれて大きな圧縮力を受け、折りひだが押圧されて変形しやすくなる。折りひだが変形するとフィルターのろ過面積が減少し、また、ろ過される高粘性流体の円滑な流れが阻害されて所要のろ過性能を維持できなくなる。そこで、本発明のフィルターユニットでは、折りひだ7の先端部分を丸くふくらませて隣り合う折りひだの先端部と互いに近接し、又は部分的に接触させ、押圧による変形を起こりにくく、また、たとえ変形を生じても高粘性流体の流路8を確保し、長期にわたりろ過性能を維持できるようにするのである。
実際に、本発明高粘性流体用フィルターユニットを紡糸パックに取り付けて実地試験した結果、ろ過液のリークがなくなって品質が向上し、従来のフラットタイプのフィルターユニットに較べて目詰まり等によるろ過圧力の上昇速度は1/3程度にまで減少した。
しかし、ろ過するポリマーの種類やろ過条件によっては、使用開始後、次第にろ過圧力が増大し、従来のフラットタイプフィルターと大差のない状態になった。解体調査の結果、第8図に示されるように、ろ液流出側Bの折りひだ81の先端部が変形して、使用前5mmであった折りひだ81の高さHが4.2ないし4.5mmになり、また、折りひだ81が互いに密着し、ろ液の流出側流路82が塞がれた状態になっていた。結局、実質的なろ過面積がフラットフィルターと変わらない状態になったものと考えられる。
上記問題を検討の結果、有効な解決手段を見出したので説明する。なお、説明順は効果や有利さとは無関係である。一つの手段は、第3図に示されるように、支持部材を2枚重ね、上流側Aから下流側Bに向かって支持部材31/フィルター32/支持部材33/支持部材34の順に積層し、積極的にろ液の流路を確保するものである。支持部材を強化して変形を防止し、また、支持部材自身の隙間をろ液流路に利用するものである。
たて方向とよこ方向の線材が直交する前記平織等の金網を支持部材41として使用する場合、最も簡単な手段は、第4図に示されるように、折りひだの長手方向43に対して支持部材41を構成する線材42をバイアス(斜交)方向に重ねるものである。従来は第5図に示されるように一般に一方の線材51の方向を折りひだの長手方向53と平行にして加工されていた。しかし、線材52が折りひだの方向53に平行に重ねられていると、折りひだ先端側部の変形により、隣り合う折りひだの線材が、互いに密着し、あるいは噛み合ってろ液の流れを阻害しやすい傾向がおおきい。バイアス角度は折りひだ長手方向に対して60度又は30度程度が好ましい。折り返された線材のバイアス角度が30度になるので、線材同士が密着したり、支持部材が噛み合う可能性が少なくなる。
ろ過圧力によるフィルターの変形を防止する他の手段として、第6図に例示されるように、折りひだ61と折りひだ61との間に金網、スパイラル線材、金属粒子、金属繊維やセラミック粒子など、あるいはこれらの焼結多孔質成形体などの、高粘性流体が通過しやすい通液性のスペーサー62を挿入し、あるいは充填することができる。スペーサー62は、通常、フィルターユニットの両面側に挿入する。さらに、挿入、充填したスペーサー62が脱離しないようにフィルターユニットの両面に金網シート63などを当てて固定しておくとよい。前記したいずれの方法が適当であるかは、その状況によって前記いずれかの手段を選択し、あるいは組み合わせて用いればよい。
ついで、前記盤状体を所要の平面形状に切断する。製作手順は、フィルター及び支持部材を所要の形状に切断、積層してからプリーツ加工を行ってもよい。盤状体3は、所要の平面形状にした後、周縁部4をつば状に圧縮成形する。つば4の幅は、通常3〜5mm程度が適当である。そして、成形したつば状部分4の両面に、軟質金属製または金属不織布製のリングシート類(金属製Oリングを含む)5を積層する。前記の軟質金属としては、アルミニウム、銅、鉛、これらの合金類、軟鋼などの中から、ろ過流体による腐食などを考慮して、適宜、選択し使用する。条件によっては、リングシートを片面に重ねたもので足りることも少なくない。第7図にはリングシート71を片面に重ねた例が示されている。
さらに、つば状部分4に周縁側から金属薄板6(第7図では72)を被せて加圧し、つば状部分においてフィルター1、支持部材2、リングシート類5および被せた金属薄板6を圧着せしめ、フィルターユニットを完成させる。この結果、フィルター1周縁部での高粘性流体のバイパス漏出を防止することができる。
高粘性流体の供給側には大きなろ過圧力が加えられるので、所要の部材などとともに耐圧ハウジング等の中に取り付けて使用される。
本発明高粘性流体用フィルターユニットは、種々の高分子高粘性流体をろ過して紡糸する紡糸パックの主要部品として口金と共に一体に組み立てるのに好適である。一例を第9図に示した。本紡糸パックは、ケーシング91中に、紡糸液の吐出側92から順に、少なくとも紡糸口金93、フィルターユニットを支持する耐圧板94、前記本発明に係る高粘性流体用フィルターユニット95、前段のフィルター96及び高粘性流体分配板97を含んで取り付けられている。前段のフィルター96にはサンドフィルターを用いることが多い。
前記した本発明高粘性流体用フィルタユニットは、その周縁部からの紡糸原液のリーク問題を解消して、プリーツタイプフィルターユニットの信頼性を高め、フィルターの変形が防止されて流路閉塞や目詰まりによるフィルターの昇圧速度を激減させて、広いろ過面積を活用することを実質的に可能にするという、大きな効果を奏する。その結果、本発明フィルターユニットを組み込んだ紡糸パックは、安心してプリーツタイプフィルターユニットの優位性を享受することができる。
産業上の利用可能性
本発明フィルターユニットは、フィルターがプリーツ状に加工されて、例えば紡糸ヘッド1個当たりのろ過面積を大きく、かつ、高粘性流体ろ過に特有の高いろ過圧力に対し、変形しにくい形状、構造に製作されているので、長期間安定したろ過操作が可能である。さらに、フィルター周縁部が圧着され、高粘性流体がフィルターをバイパスできない構造になっており、異物混入によって生じるトラブルの発生がなく、大きなろ過面積の耐圧フィルターをコンパクトに構成することができる。
従って、合成繊維、合成フィルムやその他の有機高分子化合物成形品の製造工程において加熱溶融したり溶剤に溶解したポリマーに混在する異物やゲル化物をろ過、除去するのに好適である。とくに紡糸パックとしての利用性が高い。
【図面の簡単な説明】
第1図は、本発明に係る高粘性流体用フィルターユニットの実施形態の一例を示す、折りひだに直角方向の断面図(部分図)であり、第2図は、第1図の平面図である。第3図、第6図、第7図は、本発明高粘性流体用フィルターユニットの他の実施形態を例示する、折りひだに直角方向の断面図(部分図)である。第4図は、平織金網を支持部材として金網の線材方向を折りひだの方向とバイアスに、第5図は、線材方向を折りひだの方向に平行に配したフィルターユニットの斜視図(部分図)である。第8図は、流出側の折りひだ先端部が変形し、ろ液の流路が閉塞された様子を示す断面図である。また、第9図は、本発明高粘性流体用フィルターユニットを組み込んだ紡糸パックの一例を示す模式的な断面図である。
TECHNICAL FIELD The present invention relates to a high viscosity fluid filter unit and a spin pack. It is suitable for filtration and separation of impurities and gels contained in highly viscous molten organic polymer compounds and polymer solutions.
BACKGROUND ART Filter units manufactured for the purpose of filtering and separating solid foreign substances in fluids are widely used in various industrial fields such as the electronics industry, precision industry, pharmaceutical industry, and water treatment. The target level is extremely advanced and easy to use. However, the filtration target has been developed mainly for low-viscosity substances such as air and water.
On the other hand, filter units are used to filter and separate solid foreign substances in high-viscosity fluids in the plastic molding processing industry using organic polymer compounds as raw materials and in some food industries. For example, synthetic fibers, synthetic films, and other organic polymer compound molded products are manufactured through processes such as spinning, film formation, and molding. In these processes, the raw material polymer is heated and melted or used as a solvent. It is dissolved and liquefied, and foreign substances and gelled substances are filtered and separated by a filtration device equipped with a filter unit or a spinning pack. These filtration operations, unlike the above-described filtration operations of air and water, are very inefficient because the organic polymer compound as a raw material and the solution thereof have a very high viscosity. Therefore, in order to increase the filtration speed, efforts have been made such as applying a filtration pressure several tens of times or hundreds of times higher than that of the low-viscosity material, or increasing the filtration area of the filter as much as possible. Until now, it has not achieved sufficient results.
As a means for increasing the filtration area of the filter, for example, Japanese Patent Application Laid-Open No. 60-058208 discloses a filter unit in which a filtration membrane is reinforced with a net support, folded together, and formed into a pleated shape into a cylindrical shape. It is disclosed. This method is suitable for filtration of gas with low filtration pressure or liquid with low viscosity, but because it is cylindrical, there is a limit in terms of pressure resistance design etc. to filter high viscosity fluids that require high filtration pressure. . In addition, if a pleated filter is used in a case that requires a high filtration pressure, leakage from the filter periphery becomes a problem. Means for solving this problem is disclosed in Japanese Patent Application Laid-Open No. 10-211411. However, since an adhesive is used, it is unsuitable in terms of heat resistance to filter a high temperature molten polymer. Japanese Patent Application Laid-Open No. 2002-266152 discloses a filter unit for a melt spinning pack in which a metal wire filter and a metal wire non-woven fabric are overlapped to form a corrugated shape and the outer peripheral portion is sandwiched between metal rims. However, problems remain in measures against deformation of the filter part and prevention of leakage of the filtrate with respect to the filtration of viscoelastic fluid with high pressure loss.
In the filtration process of the high temperature molten polymer, although it varies depending on the raw materials and operating conditions, it is not rare that a filtration pressure of about 10 to 30 MPa is required to efficiently filter a highly viscous fluid. In order to lower the filtration pressure, attempts have been made to increase the filtration area per spin pack, for example, by modifying the filter shape. However, the highly viscous fluid of the soot to be filtered leaks out from the filter periphery, bypassing the filter, causing product quality degradation and operational troubles, and the filtration pressure increases with the passage of time and the filter is deformed. However, the problem that the required filtration area cannot be maintained has occurred.
The present invention prevents high-viscosity fluid to be filtered from leaking out by bypassing the filter during high-pressure filtration of high-viscosity fluid in the spinning process of synthetic fibers or the film-forming process of synthetic film, and the filtration pressure As a result of research and trial production on the subject of a highly reliable high-viscosity fluid filter unit that prevents the shape of the filter from being deformed by the filter and that can be stably and stably filtered for a long period of time. It has been completed.
Disclosure of the Invention The present invention will be described with reference to FIGS. 1 and 2. FIG. The present invention is a pleated plate-like body 3 composed of a plurality of layers folded in a zigzag manner by superposing a support member 2 on a sheet-like filter 1, and the peripheral edge 4 of the plate-like body is formed into a flat brim shape, Further, at least one surface of the collar portion 4 is overlapped with a ring sheet 5 made of a soft metal or a metal non-woven fabric, and further covered with a thin metal plate 6, and the filter, support member, and ring sheets overlapped on the collar portion 4. A high-viscosity fluid filter unit is disclosed in which the high-viscosity fluid to be filtered is prevented from leaking out of the filter 1 at the peripheral edge by pressure-bonding the covered metal thin plate. It is desirable that the tip portion of the pleat fold fold 7 is inflated and in close proximity to or in partial contact with the tip of adjacent fold folds.
Depending on the type of high-viscosity fluid and the filtration conditions, the above-mentioned filter unit for high-viscosity fluid may deform the tip of the fold 81 on the filtrate outflow side during use as shown in FIG. Smooth flow may be hindered. In such a case, as shown in FIG. 3, a pleated disk-shaped body consisting of four layers folded in a zigzag manner, with two support members 32b and 32c overlapped on the filtrate outflow side B of the filter 31. By using, a smooth flow of the filtrate can be maintained. Furthermore, when using a wire mesh in which the metal wire 42 is woven on the support member 41, the metal wire 42 is preferably stacked so as to be in a bias (oblique) direction with respect to the longitudinal direction 43 of the folds (FIG. 4).
Further, in the filter unit of the present invention, as shown in FIG. 6, in order to stably maintain the flow path of the filtrate, a liquid-permeable spacer 62 is provided between the folds 61 on one or both sides of the disk-like body. May be inserted. In that case, a liquid-permeable wire mesh 63 or the like is preferably attached to both surfaces or one surface of the disk-shaped body in order to prevent the spacer from being detached.
Alternatively, in the collar portion 71, there may be a case where a ring sheet 72 made of a soft metal or a metal nonwoven fabric is overlapped only on one side (FIG. 7).
Further, in the present invention, in the spinning pack casing 91, in order from the spinning solution discharge side 92, at least the spinneret 93, the pressure plate 94 for supporting the filter unit, any of the above-described high-viscosity fluid filter units 95, and the preceding stage. A spin pack (FIG. 9) is disclosed, which is mounted to include a filter 96 and a highly viscous fluid distribution plate 97. In the present invention, the filter unit refers to a unit assembled together with an accessory member so as to be convenient for use, for example, it is easy to attach and replace the filter to an apparatus or the like.
BEST MODE FOR CARRYING OUT THE INVENTION In order to facilitate understanding of the present invention, a filter unit for a highly viscous fluid according to the present invention will be described in accordance with a general manufacturing procedure for convenience, with reference to FIGS. Although sequentially described, the filter unit of the present invention is not limited by the manufacturing procedure.
For the filter 1, a metal non-woven sheet-like fine filter for fine filtration is usually selected and used depending on the required filtration level. You may use a nonwoven fabric etc. For example, when a filter unit to be incorporated into a synthetic fiber spinning pack is manufactured, a filter having an opening of 40 μm or less is generally used.
The sheet-like filter 1 is overlapped with a support member 2 for holding the shape, and is folded in a zigzag manner to increase the filtration area, and pleats 7 are formed in parallel on both sides to form a pleated disc shape. Used as body 3. The cross-sectional shape in the direction perpendicular to the folds 7 of the plate-like body 3 may be a conventional zigzag pleated shape with sharp tips on both sides. However, preferably, as illustrated in FIG. 1, the support member 2 is overlapped on both sides of the sheet-like filter 1 and is pleated into three layers, and the front ends of the folds 7 are inflated on both sides so as to be folded adjacent to each other. Processing into a pleated disk-shaped body 3 that is close to or partially in contact with the tip of the pleat 7. Between the folds 7, a flow path 8 for the filtrate is formed, so that a gap is provided to keep the flow. For the processing, a pleating machine for wire mesh may be used. Since the filter 1 and the support member 2 are not fixed at the time of pleating, the filter 1 can be easily processed without exerting excessive stress.
The support member 2 is preferably a wire mesh having a relatively coarse mesh woven or knitted using a metal wire having a diameter of 0.17 mm or more in consideration of strength. In addition, you may utilize the nonwoven fabric etc. which used the metal wire. A stainless steel wire is used for the wire, and a wire mesh of plain weave, twill weave or tatami weave is often used. The depth and pitch of the pleats can be appropriately determined depending on the filtration pressure, required filtration area, mounting conditions, and the like. When it is intended to be mounted on the spinning head, it is generally preferable to design and manufacture the disc-like body 3 with a thickness of about 5 to 10 mm and a pitch of folds of about 3 to 5 mm. For example, if the pressure loss of filtration is small and deformation of the pleat surface can be ignored in long-term use, the support member can be placed only on one side of the filter in consideration of the pressure receiving direction during filtration. However, when it is intended to be incorporated into a synthetic fiber spinning pack, it is desirable to overlap both sides.
Now, since the filter unit of the present invention is subjected to a considerably large filtration pressure, the spinning pack or the like is usually mounted on a pressure plate (FIG. 9: 94) that supports the filter unit. When filtration of high-viscosity fluid begins, filtered foreign matter gradually accumulates on the filter surface, and the filtration pressure rises, the filter unit is sandwiched between the high-viscosity fluid to be filtered and the pressure plate. It receives a large compressive force and is easily deformed by being folded and pressed. If the folds are deformed, the filtration area of the filter is reduced, and the smooth flow of the high-viscosity fluid to be filtered is hindered, making it impossible to maintain the required filtration performance. Therefore, in the filter unit of the present invention, the tip portion of the fold fold 7 is inflated so as to be close to or partially in contact with the tip portion of the adjacent fold fold, so that deformation due to pressing is unlikely to occur. Even if it occurs, the flow path 8 of the highly viscous fluid is secured, and the filtration performance can be maintained for a long time.
Actually, the filter unit for high-viscosity fluid of the present invention was attached to a spinning pack, and as a result, the quality of the filtrate was improved by eliminating the leakage of the filtrate, and the filtration pressure due to clogging etc. compared to the conventional flat type filter unit The ascent rate of decreased to about 1/3.
However, depending on the type of polymer to be filtered and the filtration conditions, the filtration pressure gradually increased after the start of use, and there was no significant difference from the conventional flat type filter. As a result of the dismantling investigation, as shown in FIG. 8, the tip of the fold fold 81 on the filtrate outflow side B is deformed, and the height H of the fold fold 81 that was 5 mm before use is 4.2 to 4 Further, the fold folds 81 were in close contact with each other, and the filtrate outflow side flow passage 82 was blocked. Eventually, the substantial filtration area is considered to be in the same state as the flat filter.
As a result of studying the above problem, an effective solution was found, which will be described. The order of explanation is irrelevant to effects and advantages. As shown in FIG. 3, one means is that two support members are stacked and stacked in the order of support member 31 / filter 32 / support member 33 / support member 34 from upstream A to downstream B, The flow path of the filtrate is positively secured. The support member is strengthened to prevent deformation, and the gap of the support member itself is used for the filtrate flow path.
When the wire mesh such as the plain weave in which the wire in the warp direction and the transverse direction is orthogonal is used as the support member 41, the simplest means is the support member with respect to the longitudinal direction 43 of the folds as shown in FIG. The wire 42 which comprises 41 is piled up in a bias (diagonal) direction. Conventionally, as shown in FIG. 5, generally one wire 51 is processed in parallel with the longitudinal direction 53 of the folds. However, when the wire 52 is overlapped in parallel with the fold fold direction 53, the wires of the adjacent folds are likely to be in close contact with each other or mesh with each other due to the deformation of the fold end of the fold. The trend is big. The bias angle is preferably about 60 degrees or 30 degrees with respect to the longitudinal direction of the folds. Since the folded wire has a bias angle of 30 degrees, the possibility that the wires are brought into close contact with each other and the support member is engaged is reduced.
As another means for preventing the deformation of the filter due to the filtration pressure, as illustrated in FIG. 6, a wire mesh, a spiral wire, metal particles, metal fibers, ceramic particles, etc. between the fold 61 and the fold 61, Alternatively, a liquid-permeable spacer 62 that allows high-viscosity fluid to pass through, such as these sintered porous molded bodies, can be inserted or filled. The spacers 62 are usually inserted on both sides of the filter unit. Furthermore, it is preferable to fix the spacer 62 with both sides of the filter unit so that the inserted and filled spacers 62 are not detached. Which of the above-described methods is appropriate may be selected according to the situation or used in combination.
Next, the disk-like body is cut into a required planar shape. In the manufacturing procedure, the filter and the support member may be cut into a required shape and laminated, and then pleated. The disc-like body 3 is formed into a required planar shape, and then the peripheral edge portion 4 is compression-molded into a collar shape. The width of the collar 4 is usually about 3 to 5 mm. Then, ring sheets (including a metal O-ring) 5 made of a soft metal or a metal nonwoven fabric are laminated on both surfaces of the formed brim-like portion 4. The soft metal is appropriately selected from aluminum, copper, lead, alloys thereof, mild steel and the like in consideration of corrosion caused by a filtering fluid. Depending on the conditions, a ring sheet stacked on one side is often sufficient. FIG. 7 shows an example in which the ring sheet 71 is overlapped on one side.
Further, the collar 4 is covered with a thin metal plate 6 (72 in FIG. 7) from the peripheral side and pressed, and the filter 1, the support member 2, the ring sheets 5 and the covered thin metal plate 6 are crimped on the collar. Complete the filter unit. As a result, high-viscosity fluid bypass leakage at the periphery of the filter 1 can be prevented.
Since a large filtration pressure is applied to the supply side of the high-viscosity fluid, it is used in a pressure-resistant housing or the like together with required members.
The high viscosity fluid filter unit of the present invention is suitable for assembling together with a die as a main part of a spinning pack for filtering and spinning various high viscosity fluids. An example is shown in FIG. The spinning pack includes, in order from the spinning solution discharge side 92, at least a spinneret 93, a pressure plate 94 that supports a filter unit, a high-viscosity fluid filter unit 95 according to the present invention, and a front-stage filter 96. And a high viscosity fluid distribution plate 97. A sand filter is often used as the filter 96 in the previous stage.
The above-described high viscosity fluid filter unit of the present invention solves the problem of spinning stock solution leaking from the peripheral portion thereof, improves the reliability of the pleated type filter unit, prevents the deformation of the filter, and blocks the channel or clogs. The pressure increase speed of the filter is drastically reduced, and it is possible to substantially utilize a wide filtration area. As a result, the spin pack incorporating the filter unit of the present invention can enjoy the advantages of the pleated type filter unit with peace of mind.
Industrial Applicability In the filter unit of the present invention, the filter is processed into a pleated shape, for example, the filtration area per spinning head is large, and the filter unit is deformed with respect to the high filtration pressure specific to high-viscosity fluid filtration. Because it is manufactured in a difficult shape and structure, stable filtration operation is possible for a long time. Further, the filter peripheral edge is pressure-bonded, and the high-viscosity fluid cannot bypass the filter, so that troubles caused by mixing of foreign matters do not occur, and a pressure-resistant filter having a large filtration area can be configured compactly.
Therefore, it is suitable for filtering and removing foreign substances and gelled substances mixed in a polymer melted by heating or dissolving in a solvent in the production process of synthetic fibers, synthetic films and other organic polymer compound molded products. It is particularly useful as a spinning pack.
[Brief description of the drawings]
FIG. 1 is a sectional view (partial view) perpendicular to a fold, showing an example of an embodiment of a filter unit for a highly viscous fluid according to the present invention, and FIG. 2 is a plan view of FIG. is there. FIGS. 3, 6, and 7 are sectional views (partial views) perpendicular to the folds, illustrating another embodiment of the filter unit for a highly viscous fluid of the present invention. 4 is a perspective view (partial view) of a filter unit in which a wire mesh direction is arranged in parallel to the direction of the folds and a bias with a plain woven wire mesh as a support member, and FIG. 5 is a wire unit direction parallel to the direction of the folds. It is. FIG. 8 is a cross-sectional view showing a state in which the leading end of the folded fold is deformed and the flow path of the filtrate is closed. FIG. 9 is a schematic cross-sectional view showing an example of a spin pack incorporating the filter unit for high viscosity fluid of the present invention.

Claims (12)

シート状フィルター(1)に支持部材(2)を重ねてジグザグに折り畳まれた複層からなるプリーツ状の盤状体(3)であって、前記盤状体の周縁部(4)が平たくつば状に形成され、かつ、前記つば状部分(4)の少なくとも片面には軟質金属製又は金属不織布製のリングシート類(5)を重ね、さらに金属薄板(6)を被せ、つば状部分(4)において重ねられたフィルター、支持部材、リングシート類及び被せられた金属薄板を圧着することにより、周縁部において高粘性被ろ過流体がフィルター(1)をバイパスして漏出するのが防止されていることを特徴とする高粘性流体用フィルターユニット。A pleated plate-like body (3) composed of a plurality of layers folded in a zigzag manner by superposing a support member (2) on a sheet-like filter (1), wherein the peripheral edge (4) of the plate-like body is flat A ring sheet (5) made of a soft metal or a metal non-woven fabric is overlaid on at least one surface of the collar-shaped part (4), and further covered with a thin metal plate (6) to form a collar-shaped part (4 ), The high-viscosity fluid to be filtered is prevented from leaking out of the filter (1) by bypassing the filter (1) at the periphery. A filter unit for high-viscosity fluids. プリーツの折りひだ(7)の先端部分がふくらんで、隣り合う折りひだの先端部と互いに近接し又は部分的に接触していることを特徴とする請求の範囲第1項に記載の高粘性流体用フィルターユニット。2. A highly viscous fluid according to claim 1, wherein the pleat folds (7) have bulging tips and are adjacent to or partially in contact with the tips of adjacent folds. Filter unit. 前記の盤状体が、フィルター(31)のろ液の流出側(33)に2枚の支持部材(32)を重ね、ジグザグに折り畳まれた4層からなるプリーツ状の盤状体であることを特徴とする請求の範囲第1項又は第2項に記載の高粘性流体用フィルターユニット。The disk-shaped body is a pleated disk-shaped body composed of four layers that are folded in a zigzag manner by stacking two support members (32) on the filtrate outflow side (33) of the filter (31). The high viscosity fluid filter unit according to claim 1 or 2, wherein the filter unit is a high viscosity fluid filter unit. 支持部材(41)が金属線材(42)を織成した金網であって、前記の金属線材が折りひだの長手方向(43)に対してバイアス(斜交)方向に重ねられていることを特徴とする請求の範囲第1項又は第2項に記載の高粘性流体用フィルターユニット。The support member (41) is a wire mesh woven with a metal wire (42), and the metal wire is overlapped in the bias (oblique) direction with respect to the longitudinal direction (43) of the folds. The high viscosity fluid filter unit according to claim 1 or 2. 支持部材(41)が金属線材(42)を織成した金網であって、前記の金属線材が折りひだ(43)の長手方向に対してバイアス(斜交)方向に重ねられていることを特徴とする請求の範囲第3項に記載の高粘性流体用フィルターユニット。The support member (41) is a wire mesh woven with a metal wire (42), and the metal wire is overlapped in the bias (oblique) direction with respect to the longitudinal direction of the fold (43). The high viscosity fluid filter unit according to claim 3. 前記盤状体において、折りひだ(61)と折りひだとの間に通液性のスペーサー(62)が挿入されていることを特徴とする請求の範囲第1項に記載の高粘性流体用フィルターユニット。The high viscous fluid filter according to claim 1, wherein a liquid-permeable spacer (62) is inserted between the folds (61) in the plate-like body. unit. 前記盤状体の表面にスペーサーの離脱を防止する通液性のシート(63)が張られていることを特徴とする請求の範囲第6項に記載の高粘性流体用フィルターユニット。The high viscosity fluid filter unit according to claim 6, wherein a liquid-permeable sheet (63) for preventing the spacer from being detached is stretched on the surface of the disk-shaped body. 紡糸パックのケーシング(91)中に、紡糸液の吐出側(92)から順に、少なくとも紡糸口金(93)、フィルターユニットを支持する耐圧板(94)、請求の範囲第1項、第2項又は第6項に記載の高粘性流体用フィルターユニット(95)、前段のフィルター(96)及び高粘性流体分配板(97)を含んで取り付けられていることを特徴とする紡糸パック。In the spinning pack casing (91), in order from the spinning solution discharge side (92), at least the spinneret (93), the pressure plate (94) for supporting the filter unit, the claims 1, 2 or A spinning pack comprising the high-viscosity fluid filter unit (95) according to item 6 and a front-stage filter (96) and a high-viscosity fluid distribution plate (97). 請求の範囲第1項、第2項又は第6項に記載の高粘性流体用フィルタに替え、請求の範囲第3項に記載の高粘性流体用フィルターユニットを含んで取り付けられていることを特徴とする請求の範囲第8項に記載の紡糸パック。The high-viscosity fluid filter unit according to claim 3 is attached in place of the high-viscosity fluid filter according to claim 1, 2 or 6, and is attached. The spin pack according to claim 8. 請求の範囲第1項、第2項又は第6項に記載の高粘性流体用フィルタに替え、請求の範囲第4項に記載の高粘性流体用フィルターユニットを含んで取り付けられていることを特徴とする請求の範囲第8項に記載の紡糸パック。The high viscous fluid filter unit according to claim 4 is attached in place of the high viscous fluid filter according to claim 1, 2, or 6. The spin pack according to claim 8. 請求の範囲第1項、第2項又は第6項に記載の高粘性流体用フィルタに替え、請求の範囲第5項に記載の高粘性流体用フィルターユニットを含んで取り付けられていることを特徴とする請求の範囲第8項に記載の紡糸パック。The high viscous fluid filter unit according to claim 5 is attached instead of the high viscous fluid filter according to claim 1, 2 or 6, and is attached. The spin pack according to claim 8. 請求の範囲第1項、第2項又は第6項に記載の高粘性流体用フィルタに替え、請求の範囲第7項に記載の高粘性流体用フィルターユニットを含んで取り付けられていることを特徴とする請求の範囲第8項に記載の紡糸パック。The high viscous fluid filter unit according to claim 7 is attached in place of the high viscous fluid filter according to claim 1, 2, or 6. The spin pack according to claim 8.
JP2004506937A 2002-05-27 2003-05-27 High viscosity fluid filter unit and spinning pack Expired - Fee Related JP4423186B2 (en)

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