JP3616485B2 - Drying furnace wall surface processing object penetration part sealing device - Google Patents

Drying furnace wall surface processing object penetration part sealing device Download PDF

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JP3616485B2
JP3616485B2 JP29602997A JP29602997A JP3616485B2 JP 3616485 B2 JP3616485 B2 JP 3616485B2 JP 29602997 A JP29602997 A JP 29602997A JP 29602997 A JP29602997 A JP 29602997A JP 3616485 B2 JP3616485 B2 JP 3616485B2
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gas
opening
drying furnace
pressure
seal box
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JPH11132661A (en
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律 中谷
洸 塩崎
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ジャパン・エア・ガシズ株式会社
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Description

【0001】
【発明の属する技術分野】
本発明は、乾燥炉内雰囲気ガスを不活性ガスで実質的に置換し、且つ乾燥炉内の溶剤濃度を高濃度に保持したイナート乾燥炉において、被処理体が貫通し得る乾燥炉の開口部からの外気の侵入および炉内ガスの漏洩を効率良く抑え、不活性雰囲気を保持するためのシール装置に関する。
【0002】
【従来の技術】
従来より、溶剤を含有する被処理体(例えば、顔料等の固形成分を溶剤中に分散させた塗工液を塗布した基材など)を帯状ウェブ式、または連続コンベア式などの搬送手段により連続的に乾燥炉に導入し、塗工液中の溶剤を加熱して蒸発させる乾燥装置が、種々の産業分野において広範囲に使用されている。
【0003】
このような乾燥装置において、一般に溶剤含有被処理体を空気中で乾燥する方式(エアーモード)により乾燥を行なっているが、他方、特公昭55−36389号公報に記載のように、乾燥炉内の雰囲気を窒素ガス等の不活性ガスで置換し、酸素濃度を低下することにより、蒸発した溶剤ガスの爆発・燃焼の発生を防止しながら、雰囲気中の溶剤濃度を安全に上昇させる乾燥炉が開示されている。
【0004】
ところで、乾燥炉には内部雰囲気を外気と連通した被処理体が貫通する開口部を有する(以下乾燥炉開口部とする)。
【0005】
したがって、前記不活性ガス雰囲気(イナートモード)方式の乾燥炉において、開口部からの外気侵入による酸素濃度の上昇は、高濃度の有機溶剤ガスによる爆発・燃焼の危険を伴う。
【0006】
したがって、イナート方式の乾燥炉は、乾燥炉開口部の間隙をスライド板等により出来るだけ狭くし外気の侵入を抑え、また乾燥炉開口部の被処理体に窒素ガスをスリット状に吹き付けることにより、内部のガスと外気とを遮断するシール装置も考案されている。一方、乾燥炉内の乾燥用及び被処理体搬送(フローティング)用のための吹出しノズルからの吹出しガスが被処理体の表面に沿って移動するガスの動圧を抑えるために、吹出しノズルから乾燥炉開口部までの距離をとり動圧を緩衝する空間(バッファーゾーン)を乾燥炉開口部に設けたり、またその他種々のシール構造が考案されている。
【0007】
この様に窒素ガスによりイナート化された乾燥炉内の空間は、吹出しノズルからの乾燥風発生用のガスの循環による圧力バランスの影響で、乾燥炉開口部からのガスの出入りが発生する。イナート方式の乾燥炉は、基本的に密閉循環系による溶剤の回収を組み込むため物質収支的に均一であり、一方の乾燥炉開口部よりガスが出ると反対側の乾燥炉開口部よりガスを吸込むような乾燥炉内でのガスの流れが発生し、その結果乾燥炉内のガスの吸込み側から酸素濃度が上昇し、反対側の乾燥炉開口部より溶剤を含んだ窒素ガスが吹き出す状態となる。
【0008】
通常、イナート雰囲気が維持される空間では、乾燥炉開口部に設けたシール装置に供給される窒素ガス量と、乾燥炉の出入りガス量との質量バランスを確立させているが、ガスの流れが大きい場合はイナート雰囲気の維持が困難となる。
【0009】
また、一般にイナート方式の乾燥炉は、溶剤濃度を爆発下限界(LEL)を越えて運転しても爆発や燃焼の危険がないので、密閉循環系溶剤回収方式(特公平3−25228号公報に記載)における溶剤ガスの凝縮回収を効率良く行うために、乾燥炉内の溶剤濃度は、ある程度高い濃度(LEL〜約30モル%の範囲内)で運転される。従って、このような高濃度の溶剤ガスを含んだ窒素ガスが乾燥炉開口部より流出した場合、周辺の換気が不十分であると作業環境を悪化させたり、最悪の場合、滞留した溶剤ガスにより爆発の危険がある。
【0010】
この対策として特公平8−7025号公報には、被処理体に接近させて先端を炉内側に折り曲げたシール板により、乾燥炉開口部から被処理体表面に沿って乾燥炉外に流出するガスの吹出しを抑えるシール構造が開示されている。しかしこの方法では、シール板を被処理体にかなり接近させなければ効果が現れないが、吹出しノズルからの乾燥風吹出しによる被処理体の波打ちに対し、シール板が接触しないようにある程度の間隙を設けなければならない。特に上下の吹出しノズルからの吹出しにより被処理体をフローティングさせる形状のものは、この間隙をより大きくとる必要が有る。このように、シール板によるシール構造では、漏洩ガスを充分に抑える事は困難である。
【0011】
また、乾燥炉内空間の質量バランスをある一定条件で維持することが出来ても、乾燥炉内の圧力バランスに変化が生じたり、開口部周辺の外気の圧力に変化が生じた場合には、乾燥炉内空間の質量バランスの維持が崩れる。
【0012】
また、被処理体の処理速度(走行速度)が速い(例えば、100m/分以上)の場合は、被処理体表面の摩擦力(ドラグ力)による慣性で、被処理体とともに乾燥炉内空間に同伴される空気により、乾燥装置内の圧力バランスが変化しイナート雰囲気の維持が崩れることがある。
【0013】
特に、処理速度の大幅な変化や、被処理体材質の変更により表面摩擦力による同伴ガス移動量の変化に伴う圧力バランスの変化に追従できない問題がある。
【0014】
結果的に、このような圧力バランスの変化により、乾燥炉内に外部空気中の酸素が入り込み、イナート雰囲気の維持のために、過剰な窒素ガスの供給を余儀なくされているケースが有り、窒素ガスの消費によるランニングコストのアップを引き起こす。
【0015】
前記した特公平8−7025号公報には、乾燥炉壁面の乾燥炉開口部に連通するシールボックスを設け、該シールボックスに排気路および不活性ガス供給路を設けると共に、シールボックスから乾燥炉内への循環路を設けた構成が開示されているが、この循環路は単に過剰なガスを乾燥炉内に戻すためのものであり、前記したように乾燥炉内の圧力バランスの変化に追従できないという問題が依然として残っている。
【0016】
【発明が解決しようとする課題】
本発明は上記問題点を解決するためになされたものであり、その目的とするところは、上記乾燥炉内の圧力バランスの変化に対して、バランスの矯正を行なうためのシール装置により、窒素ガスの供給量の低減と高濃度の溶剤を含んだガスの放出の低減を行なうことができる乾燥炉壁面の被処理体貫通部シール装置を提供することにある。
【0017】
【課題を解決するための手段】
本発明の乾燥炉壁面の被処理体貫通部シール装置は、乾燥炉の壁面に設けられた被処理体が貫通し得る第1の開口部を通るガスの流通を減少するための、乾燥炉壁面の被処理体貫通部シール装置であって、該乾燥炉の該第1の開口部に連通して設けられており、該被処理体が貫通し得る第2の開口部を有するシールボックスと、該シールボックスの外側に配設された第3の開口部を有する圧力調整室と、該シールボックス内に不活性ガスを供給する手段と、該第1の開口部を通るガスの流通を検知する手段と、検知したガスの流通量を低減するための該圧力調整室の圧力調整手段と、を具備し、そのことにより上記目的が達成される。
【0018】
また、本発明の他の乾燥炉壁面の被処理体貫通部シール装置は、乾燥炉の壁面に設けられた被処理体が貫通し得る第1の開口部を通るガスの流通を減少するための、乾燥炉壁面の被処理体貫通部シール装置であって、該乾燥炉の該第1の開口部に連通して設けられており、該被処理体が貫通し得る第2の開口部を有するシールボックスと、該シールボックス内に設けられており、該被処理体が貫通し得る該第2の開口部を共有する圧力調整空間と、該シールボックス内に不活性ガスを供給する手段と、該圧力調整空間内に空気を供給および/または排除する手段と、該第1の開口部を通るガスの流通を検知する手段と、検知したガスの流通量を低減するための該圧力調整空間の圧力調整手段と、を具備し、そのことにより上記目的が達成される。
【0019】
一つの実施態様では、前記第1の開口部を流通するガスの流通を検知する手段が、前記シールボックス内の第1の開口部側と圧力調整室内との圧力差信号または乾燥炉内の入口側及び出口側の酸素濃度計測定値の偏差信号により行われる。
【0020】
一つの実施態様では、前記第1の開口部を流通するガスの流通を検知する手段が、前記シールボックス内と前記圧力調整空間内の圧力差信号または乾燥炉内の入口側及び出口側の酸素濃度計測定値の偏差信号により行われる。
【0021】
一つの実施態様では、前記ガス流通量の調整手段が、前記圧力調整室内または圧力調整空間内への空気の供給手段に設けられた給気調整弁および/または排除手段に設けられた排気調整弁の開閉により行われる。
【0022】
一つの実施態様では、前記ガス流通量の調整手段が、前記シールボックス内のガスをファンで乾燥炉内に戻す配管に設置した吸引ガス調整弁で圧力を調整することにより行われる。
【0023】
一つの実施態様では、前記ガス流通量の調整手段が、乾燥炉に接続されたイナート方式による溶剤回収装置におけるシールボックスヘのガスの流出入量調整手段である。
【0024】
次に、本発明の作用について説明する。
【0025】
通常、気体は圧力の高い方より低い方へ移動する。そのため乾燥炉内の圧力が外部の圧力より高い場合は、乾燥炉開口部を通って内部より外部に向かってガスが流出し、逆の場合は逆方向にガス(一般には、外部空気)が流れる。この圧力差が例えば、1mmAqであれば、約4m/secの流速でガスが移動し、この圧力差はガスの流速の2乗に比例する。一般に、イナート雰囲気の維持を行なうためには、被処理体上下の開口間隙を10mm(間隙は出来るだけ狭い方が好ましい)に仕切った場合のガス移動量が1m/sec以下(好ましくは0.5m/sec以下)にする必要が有る。
【0026】
したがって、これに見合った圧力差以下にバランスを維持する事により、乾燥炉開口部への少量の窒素ガス供給でイナート雰囲気を維持することが出来る。
【0027】
第1の発明においては、シールボックスの外側に設けた圧力調整室内に不活性ガスを供給しつつ、乾燥炉の第1の開口部を通るガスの流通を検知手段で検知して、そのガスの流通量を調整手段によって低減するようにすることにより、乾燥炉内の圧力バランスを所定の値以下に維持する事ができ、乾燥炉開口部への少量の窒素ガス供給でイナート雰囲気を維持することが出来る。
【0028】
また、第2の発明においては、シールボックス内に不活性ガスを供給し、第1の開口部を通るガスの流通を検知手段で検知してそのガスの流通量を低減するための調整手段によって、圧力調整空間内に空気を供給および/または排除することにより、乾燥炉内の圧力バランスを所定の値以下に維持する事ができ、乾燥炉開口部への少量の窒素ガス供給でイナート雰囲気を維持することが出来る。
【0029】
【発明の実施の形態】
(実施例1)
本発明を実施例に基づいて具体的に説明する。
【0030】
図1は、本発明の基本的実施態様を示した、乾燥炉出口側の被処理体貫通部における、シール装置の一実施例の断面図である。
【0031】
本実施例のシール装置は、乾燥炉2の壁面に設けられた、被処理体1が貫通し得る第1の開口部4から炉内ガスの流通を減少するためのものであり、該シール装置は、該乾燥炉2の該第1の開口部4に連通するよう、該乾燥炉2の壁面に設けられたシールボックス5と、該シールボックス5の下流側に設けられた圧力調整室9、を有する。該圧力調整室9はシールボックス5を覆うようにシールボックス5の外側に配設されている。
【0032】
該シールボックス5には被処理体1が貫通し得る第2の開口部37が、上記乾燥炉2の第1の開口部4と対応して形成され、また圧力調整室9にも同様に被処理体1が貫通し得る第3の開口部18が形成されている。
【0033】
該シールボックス5内に不活性ガスを供給する手段として、窒素ガス供給配管6がシールボックス5に接続されている。また、該シールボックス5内部には、被処理体1の表面、裏面に向けてその走行方向に対し任意の角度で吹き付けるためのオリフィス7a,7bが上下にそれぞれ設けられている。さらに、シールボックス5の外側には、第2の開口部37を開閉し得るスライド板8a,8bが上下に設けられている。これらのスライド板8a,8bによって、被処理体1の走行に影響が出ない範囲で出来るだけ第2の開口部37の間隙を狭めることが好ましい。
【0034】
また、圧力調整室9内に空気を供給および排除する手段として、給気調整弁16を有する給気管10と、排気調整弁17を有する排気管11が該圧力調整室9にそれぞれ接続されている。
【0035】
そして、該シールボックス5内に配置された圧力検知部12と、圧力調整室9内に配置された圧力検知部13における両圧力の差圧を差圧計14にて測定し、その信号と制御部15に設定した値(基本的に設定差圧は0)との偏差により、給気調整弁16と排気調整弁17を操作して流量を調整し(給気又は排気のどちらか一方の調整でも可能)、圧力調整室9内の圧力をコントロールし、シールボックス5の第2の開口部37からのガスの吹出し(もしくは空気吸込み)を抑えるように構成されている。
【0036】
この圧力調整室9においても給気、排気により圧力調整を行なうため、被処理体1が貫通し得る第3の開口部18の断面積を小さくすることが好ましく、シールボックス5と同様にその開口部18にスライド板19a,19bが開閉可能に設けられている。
【0037】
上記構成のシール装置を備えたイナート方式の乾燥装置において、被処理体1は、窒素ガスによりイナート化された乾燥炉2内の吹出しノズル3より吹出すガスにより、表面に塗布された塗工液の乾燥を行い、第1の開口部4より図右側(矢印方向)に搬送され、シールボックス5の第2の開口部37及び圧力調整室9の第3の開口部18を貫通する。イナート方式の乾燥炉2を密閉循環系として溶剤を含むガスを循環させると共に該循環系にコンデンサー等の溶剤回収装置を設けることにより、雰囲気中の溶剤を回収することができる。
【0038】
ここで、上記シールボックス5においては、上記したように窒素ガス供給配管6より窒素ガスが供給され該シールボックス5内部の上下のオリフィス7a,7bより、被処理体1の表面、裏面の走行方向に対し任意の角度で吹き付ける。シールボックス5内部の圧力12と、圧力調整室9内の圧力13の差圧を差圧計14にて測定し、その信号と制御部15に設定した値(基本的に設定差圧は0)との偏差により、給気調整弁16と排気調整弁17により流量を調整し(給気又は排気のどちらか一方の調整でも可能)、圧力調整室9内の圧力をコントロールすることにより、つまりシールボックス5内の圧力と圧力調整室9内の圧力とをほぼ等しく設定することにより、シールボックス5の第2の開口部37からのガスの吹出し(もしくは吸込み)が抑えられる。
【0039】
上記実施例は、乾燥炉2の出口側の第1の開口部4について説明したが、同様な構成のシール装置を乾燥炉2の入口側に設ける事も可能である。
【0040】
(実施例2)
図2に、上記の図1に示した実施例に改良を加えた第2の実施例について説明する。
【0041】
図2の実施例の特徴は、図1の圧力調整室9による圧力調整機能をシールボックス5内に組み込んだ点である。図2は乾燥炉2の入口側、出口側のシール装置の断面構造を示したものである。
【0042】
被処理体1は、窒素ガスによりイナート化された乾燥炉2内を左側から右側に移動する間に、吹出しノズル3から吹出されるガスにより乾燥される。
【0043】
該乾燥炉2の入口側および出口側の壁面には、雰囲気のイナート状態を維持するためにそれぞれ第1の開口部4と連通するようシールボックス5が設置されている。
【0044】
該シールボックス5には、乾燥炉2の第1の開口部4側に乾燥炉2内の吹出しノズル3の吹出しによる動圧を緩衝し弱めるための、緩衝空間20が設けられている。緩衝空間20内には動圧の緩衝を効率良く行なうために複数枚の仕切板21が、被処理体1に出来るだけ間隙を狭めた状態で設置されている(動圧に対して抵抗をつける事で弱める)。その外側には、シール用窒素ガスの吹出しオリフィス7a,7bが設置されたシール用窒素ガス空間部40が形成されている。またシールボックス5の外側に図1の圧力調整室9に相当する圧力調整空間22が設けられ、空気供給配管10より圧力を加える事が出来るようになっている。
【0045】
この構成のシール装置におけるイナート雰囲気維持のバランスの調整方法は、緩衝空間20内に設置された圧力検知部12による圧力測定と、圧力調整空間22内に設置された圧力検知部13による圧力測定の差圧を差圧計14により測定し、その信号と制御部15との偏差による信号で、乾燥炉2の入口側と出口側の圧力調整空間22へ供給する空気の量を給気調整弁16aの開閉操作により調整する。例えば、差圧計14が、緩衝空間20内の圧力の方が圧力調整空間22内の圧力に比べて高いことを示す場合は、乾燥炉の開口部4近傍のガスが第1の開口部4を通って外に向かって吹出すので、圧力調整空間22内の圧力を上げるために空気調整弁16aが開き空気を圧力調整空間22内へ供給する。一方、逆に圧力調整空間22内の圧力が高い場合には、圧力調整空間22内の圧力を下げるために給気調整弁16aが閉まる方向に作動する。
【0046】
さらに、給気調整弁16aが全閉になってもまだ圧力調整空間22内の圧力が高い場合は、乾燥炉2の反対側の乾燥炉開口部のシールボックス5の給気調整弁16bが開く方向に移動し圧力調整を行なう。
【0047】
なお、乾燥炉のシール装置部分で窒素ガスの流通が生じているか否かを検出する方法として、上記シールボックス5と圧力調整空間22の差圧を検出する方法以外に、乾燥炉内の酸素濃度により実施する事も可能である。
【0048】
乾燥炉2の入口側に酸素濃度計23を設置し、その濃度計23の検出出力と、出口側に設置した酸素濃度計24の検出出力との偏差よって、制御部25から所定の信号を給気調整弁16a、16bに送り開度調整を行なう。この場合においても、上記差圧による圧力の調整と同様に、乾燥炉2の入口側の酸素濃度が高い場合は、乾燥炉2の出口側の圧力調整空間22の圧力を上げる方向に給気調整弁16aが作動し、反対に出口側の酸素濃度が高い場合は逆動作となる。
【0049】
(実施例3)
図3に示す実施例3の特徴は、実施例2(図2)に記載の圧力調整機能を、緩衝空間20からの吸引ガスにより行なう点である。
【0050】
シールボックス5の緩衝空間20と乾燥炉2の下流側とは、ファン26および吸引ガス調整弁28を有する戻り配管27によって接続されており、シールボックス5内のガスをファン26で吸引して乾燥炉2内ヘガスを戻す事により、緩衝空間20内の圧力を低下させる事ができる。
【0051】
これによるイナート雰囲気維持の圧力バランス調整方法は、基本的に実施例2(図2)での説明と同様で、差圧計14の測定値より、緩衝空間20内の圧力が圧力調整空間22の内圧より高い場合は、緩衝空間20の圧力を下げるために、戻り配管27のファン26の吐出側に設置した吸引ガス調整弁28が開き、緩衝空間20からの吸引量を増加し、圧力の調整を行なう。逆に、緩衝空間20内の圧力が低い場合は、吸引ガス量の減少と反対側開口部4のシールボックス5の吸引量増加により調整する。
【0052】
また、酸素濃度の偏差による圧力バランス調整については、前記の実施例2と同じであるためここでは省略する。
【0053】
(実施例4)
図4に示す実施例4の特徴は、特公平3−25228号公報に記載の、イナート方式による溶剤回収方法である、乾燥炉内の溶剤蒸気を含んだガスの一部をコンデンサーに導入し、冷熱により溶剤蒸気を凝縮回収し、残りのガスを乾燥炉内に戻す密閉循環系を構成する溶剤回収装置システムにおいて、この密閉循環系のガスを利用し、シールボックス5内の圧力調整を行なう点である。
【0054】
窒素ガスによりイナート雰囲気が構成された乾燥炉2内のガスは、ファン29と排気管30によりコンデンサー31へ送られ、ここで冷却し溶剤蒸気を凝縮回収する。そして残りのガスは戻り配管32により再び乾燥炉2へ戻される循環系を構成する。乾燥炉2の壁面に形成された被処理体1が貫通する第1の開口部4の外側に設置されたシールボックス5には、窒素ガス供給配管6よりオリフィス7a,7bに窒素ガスを供給し、先端部より吹出す。また、圧力調整空間22には、戻り配管32からのガスの一部を供給するための、戻りガス供給配管33と、流量を調整するための戻りガス調整弁34が設けられている。一方、緩衝空間20からは、排気管30ヘガスが吸引できるように、吸引配管35と流量を調整するための吸引ガス調整弁36を設けられている。
【0055】
イナート雰囲気維持のバランス調整方法は、基本的に図2,図3の実施例2及び3に示した方法により行う。差圧計14からの圧力信号又は酸素濃度計23,24の偏差信号により、戻りガス調整弁34と吸引ガス調整弁36の流量調整により行なう事が出来る。
【0056】
【発明の効果】
本発明の乾燥炉の被処理体貫通部のシール装置により、乾燥炉内のイナート雰囲気を維持するための圧力バランスの調整に効果が認められた。それにより、シール用の窒素ガス流量の低減と、外部への高濃度溶剤蒸気を含んだ雰囲気ガスの漏洩を防止する事が出来、ランニングコストの低減と、環境保全の改善が認められる。
【0057】
特に、乾燥炉内の圧力バランスの変動を、差圧計または酸素濃度計により検知する事によって自動的に圧力によるバランス調整が行えるため、運転中に乾燥炉内の圧力バランスに変動を来す場合(例えば、吹出しノズルの風速の変化や、被処理体の走行速度の変化等)、特に効果がある。
【図面の簡単な説明】
【図1】乾燥炉内雰囲気の圧力バランス調整を、圧力調整室の圧力調整により行なった本発明のシール装置の一実施例の要部断面図である。
【図2】乾燥炉雰囲気の圧力バランス調整を、シールボックス内の圧力調整空間の空気供給量調整により行なった本発明のシール装置の他の実施例を示す要部断面図である。
【図3】乾燥炉雰囲気の圧力バランス調整を、シールボックス内緩衝空間からのガス吸引量調整により行なった本発明のシール装置のさらに他の実施例を示す一部切欠断面図である。
【図4】乾燥炉雰囲気の圧力バランス調整を、密閉循環系溶剤回収装置における、シールボックスヘのガス出入り量の調整により行なった本発明のシール装置のさらに他の実施例を示す要部の断面図である。
【符号の説明】
1 被処理体
2 乾燥炉
3 吹出しノズル
4 第1の開口部
5 シールボックス
6 窒素ガス供給配管
7a,7b オリフィス
8a,8b スライド板
9 圧力調整室
10 給気管
11 排気管
12 シールボックス内の圧力検知部
13 圧力調整室内の圧力検知部
14 差圧計
15 制御部
16,16a,16b 給気調整弁
17 排気調整弁
18 圧力調整室の第3の開口部
19a,19b スライド板
20 緩衝空間
21 仕切板
22 圧力調整空間
23 入口側酸素濃度計
24 出口側酸素濃度計
25 制御部
26 ファン
27 ガス戻り配管
28 吸引ガス調整弁
29 ファン
30 抽気配管
31 コンデンサー
32 戻り配管
33 戻りガス供給配管
34 戻りガス調整弁
35 吸引配管
36 吸引ガス調整弁
37 第2の開口部
40 シール用窒素ガス空間部
[0001]
BACKGROUND OF THE INVENTION
The present invention provides an opening of a drying furnace through which a workpiece can penetrate in an inert drying furnace in which the atmosphere gas in the drying furnace is substantially replaced with an inert gas and the solvent concentration in the drying furnace is maintained at a high concentration. The present invention relates to a sealing device for efficiently suppressing intrusion of outside air from the inside and leakage of gas in the furnace and maintaining an inert atmosphere.
[0002]
[Prior art]
Conventionally, an object to be treated containing a solvent (for example, a substrate coated with a coating liquid in which a solid component such as a pigment is dispersed in a solvent) is continuously conveyed by a belt-like web type or continuous conveyor type conveying means. In general, drying apparatuses that are introduced into a drying furnace and heat and evaporate a solvent in a coating liquid are widely used in various industrial fields.
[0003]
In such a drying apparatus, in general, drying is performed by a method (air mode) of drying a solvent-containing object to be processed in air. On the other hand, as described in JP-B-55-36389, A drying furnace that safely increases the solvent concentration in the atmosphere while substituting the atmosphere with an inert gas such as nitrogen gas and reducing the oxygen concentration to prevent the explosion and combustion of the evaporated solvent gas. It is disclosed.
[0004]
By the way, the drying furnace has an opening through which an object to be processed communicated with the outside air through the internal atmosphere (hereinafter referred to as a drying furnace opening).
[0005]
Accordingly, in the inert gas atmosphere (inert mode) type drying furnace, an increase in oxygen concentration due to intrusion of outside air from the opening is accompanied by a risk of explosion and combustion due to a high concentration organic solvent gas.
[0006]
Therefore, the inert type drying furnace narrows the gap of the opening of the drying furnace as much as possible by a slide plate or the like, suppresses intrusion of outside air, and blows nitrogen gas into the object to be processed in the opening of the drying furnace in a slit shape, A sealing device that shuts off the internal gas and the outside air has also been devised. On the other hand, in order to suppress the dynamic pressure of the gas blown from the blow nozzle for drying in the drying furnace and for conveying the workpiece (floating), it is dried from the blow nozzle. A space (buffer zone) for buffering dynamic pressure by taking a distance to the furnace opening is provided in the drying furnace opening, and various other sealing structures have been devised.
[0007]
In this manner, the space in the drying furnace inerted with nitrogen gas causes gas to enter and exit from the opening of the drying furnace due to the effect of pressure balance due to the circulation of the gas for generating the drying air from the blowing nozzle. The inert type drying furnace is basically uniform in mass balance because it incorporates solvent recovery by a closed circulation system, and when gas comes out from one drying furnace opening, gas is sucked from the other drying furnace opening. As a result, a gas flow occurs in the drying furnace, and as a result, the oxygen concentration increases from the gas suction side in the drying furnace, and nitrogen gas containing a solvent is blown out from the opening on the opposite side of the drying furnace. .
[0008]
Normally, in a space where an inert atmosphere is maintained, a mass balance is established between the amount of nitrogen gas supplied to the sealing device provided at the opening of the drying furnace and the amount of gas entering and leaving the drying furnace. If it is large, it will be difficult to maintain the inert atmosphere.
[0009]
In general, an inert drying furnace has no danger of explosion or combustion even if the solvent concentration exceeds the lower explosion limit (LEL). Therefore, a closed circulation system solvent recovery system (Japanese Patent Publication No. 3-25228) In order to efficiently perform the condensation recovery of the solvent gas in the description), the solvent concentration in the drying furnace is operated at a somewhat high concentration (in the range of LEL to about 30 mol%). Therefore, when nitrogen gas containing such a high concentration of solvent gas flows out from the opening of the drying furnace, the surrounding environment is insufficient if the ventilation is insufficient, or in the worst case, the retained solvent gas causes There is a risk of explosion.
[0010]
As a measure against this, Japanese Patent Publication No. 8-7025 discloses a gas that flows out of the drying furnace along the surface of the object to be processed from the opening of the drying furnace by means of a sealing plate that is brought close to the object to be processed and whose tip is bent inside the furnace. A seal structure that suppresses the blow-out is disclosed. However, in this method, the effect does not appear unless the seal plate is brought close to the object to be processed.However, a certain amount of gap is provided so that the seal plate does not come into contact with the undulation of the object to be processed by blowing dry air from the blowing nozzle. Must be provided. In particular, a shape in which the workpiece is floated by blowing from the upper and lower blowing nozzles needs to have a larger gap. As described above, it is difficult to sufficiently suppress the leaked gas in the seal structure using the seal plate.
[0011]
Also, even if the mass balance of the drying furnace space can be maintained under a certain condition, if the pressure balance in the drying furnace changes, or if the pressure of the outside air around the opening changes, Maintaining the mass balance of the drying furnace space is disrupted.
[0012]
In addition, when the processing speed (traveling speed) of the object to be processed is high (for example, 100 m / min or more), the inertia due to the frictional force (drag force) on the surface of the object to be processed and the space in the drying furnace together with the object to be processed Entrained air may change the pressure balance in the drying apparatus and disrupt the maintenance of the inert atmosphere.
[0013]
In particular, there is a problem in that it cannot follow a change in pressure balance accompanying a change in the amount of entrained gas movement due to a surface friction force due to a significant change in the processing speed or a change in the material to be processed.
[0014]
As a result, there are cases where oxygen in the external air enters the drying furnace due to such a change in pressure balance, and in order to maintain the inert atmosphere, there is a case where an excessive supply of nitrogen gas is forced. Increases running costs due to consumption.
[0015]
In the above-mentioned Japanese Patent Publication No. 8-7025, a seal box communicating with a drying furnace opening on the wall surface of the drying furnace is provided, and an exhaust passage and an inert gas supply passage are provided in the seal box. Although a configuration with a circulation path is disclosed, this circulation path is merely for returning excess gas into the drying furnace, and as described above, it cannot follow the change in the pressure balance in the drying furnace. The problem still remains.
[0016]
[Problems to be solved by the invention]
The present invention has been made to solve the above-mentioned problems, and the object of the present invention is to provide nitrogen gas by means of a sealing device for correcting the balance against changes in the pressure balance in the drying furnace. An object of the present invention is to provide an apparatus for sealing an object to be processed on the wall of a drying furnace capable of reducing the supply amount of gas and reducing the release of gas containing a high-concentration solvent.
[0017]
[Means for Solving the Problems]
A drying object wall surface sealing device for a drying furnace wall surface according to the present invention has a drying furnace wall surface for reducing the flow of gas through a first opening through which a processing object provided on the wall surface of the drying furnace can pass. A to-be-processed object through-portion sealing device, which is provided in communication with the first opening of the drying furnace and has a second opening through which the object to be processed can pass, A pressure adjusting chamber having a third opening disposed outside the seal box; means for supplying an inert gas into the seal box; and detecting a gas flow through the first opening. Means, and pressure adjusting means of the pressure adjusting chamber for reducing the detected gas flow rate, whereby the above object is achieved.
[0018]
Moreover, the other object penetration part sealing device of the drying furnace wall surface of this invention is for reducing the distribution | circulation of the gas through the 1st opening part which the to-be-processed object provided in the wall surface of the drying furnace can penetrate. An apparatus for sealing an object to be processed through the drying furnace wall, the apparatus being provided in communication with the first opening of the drying furnace, and having a second opening through which the object to be processed can penetrate. A seal box, a pressure adjusting space provided in the seal box and sharing the second opening through which the object can pass, and means for supplying an inert gas into the seal box; Means for supplying and / or removing air into the pressure adjustment space, means for detecting the flow of gas through the first opening, and the pressure adjustment space for reducing the flow rate of the detected gas. Pressure adjusting means, whereby the above object is achieved. .
[0019]
In one embodiment, the means for detecting the flow of the gas flowing through the first opening is a pressure difference signal between the first opening side in the seal box and the pressure adjustment chamber, or an inlet in the drying furnace. This is done by the deviation signal of the oximeter measurement values on the side and outlet side.
[0020]
In one embodiment, the means for detecting the flow of the gas flowing through the first opening is a pressure difference signal in the seal box and the pressure adjustment space or oxygen on the inlet side and outlet side in the drying furnace. This is done by the deviation signal of the densitometer measurement value.
[0021]
In one embodiment, the gas flow rate adjusting means includes an air supply adjusting valve provided in an air supply means and / or an exhaust adjusting valve provided in an exhaust means in the pressure adjusting chamber or the pressure adjusting space. It is done by opening and closing.
[0022]
In one embodiment, the gas flow rate adjusting means is performed by adjusting the pressure with a suction gas adjusting valve installed in a pipe for returning the gas in the seal box to the drying furnace with a fan.
[0023]
In one embodiment, the gas flow rate adjusting means is a gas inflow / outflow adjusting means for the seal box in an inert solvent recovery apparatus connected to a drying furnace.
[0024]
Next, the operation of the present invention will be described.
[0025]
Normally, the gas moves to a lower side than a higher one. Therefore, when the pressure in the drying furnace is higher than the external pressure, gas flows out from the inside through the drying furnace opening, and in the opposite case, gas (generally, external air) flows in the opposite direction. . If this pressure difference is 1 mmAq, for example, the gas moves at a flow rate of about 4 m / sec, and this pressure difference is proportional to the square of the gas flow rate. In general, in order to maintain the inert atmosphere, the amount of gas movement when the opening gap above and below the object to be processed is divided into 10 mm (the gap is preferably as narrow as possible) is 1 m / sec or less (preferably 0.5 m). / Sec or less).
[0026]
Therefore, the inert atmosphere can be maintained by supplying a small amount of nitrogen gas to the drying furnace opening by maintaining the balance below the pressure difference corresponding to this.
[0027]
In the first aspect of the invention, the inert gas is supplied into the pressure adjustment chamber provided outside the seal box, and the gas flow through the first opening of the drying furnace is detected by the detection means, and the gas By reducing the flow rate by adjusting means, the pressure balance in the drying furnace can be maintained below a predetermined value, and an inert atmosphere can be maintained by supplying a small amount of nitrogen gas to the opening of the drying furnace. I can do it.
[0028]
In the second invention, an inert gas is supplied into the seal box, and the adjusting means for detecting the gas flow through the first opening by the detecting means and reducing the gas flow rate. By supplying and / or eliminating air in the pressure adjustment space, the pressure balance in the drying furnace can be maintained below a predetermined value, and an inert atmosphere can be created by supplying a small amount of nitrogen gas to the opening of the drying furnace. Can be maintained.
[0029]
DETAILED DESCRIPTION OF THE INVENTION
(Example 1)
The present invention will be specifically described based on examples.
[0030]
FIG. 1 is a cross-sectional view of an example of a sealing device in a workpiece penetration part on the drying furnace outlet side, showing a basic embodiment of the present invention.
[0031]
The sealing device of the present embodiment is for reducing the flow of the gas in the furnace from the first opening 4 provided on the wall surface of the drying furnace 2 through which the workpiece 1 can penetrate, and the sealing device. Is a seal box 5 provided on the wall surface of the drying furnace 2 so as to communicate with the first opening 4 of the drying furnace 2, and a pressure adjustment chamber 9 provided on the downstream side of the seal box 5, Have The pressure adjusting chamber 9 is disposed outside the seal box 5 so as to cover the seal box 5.
[0032]
The seal box 5 is provided with a second opening 37 through which the workpiece 1 can penetrate, corresponding to the first opening 4 of the drying furnace 2, and the pressure adjustment chamber 9 is similarly covered. A third opening 18 through which the processing body 1 can penetrate is formed.
[0033]
A nitrogen gas supply pipe 6 is connected to the seal box 5 as means for supplying an inert gas into the seal box 5. In addition, orifices 7a and 7b for spraying at an arbitrary angle with respect to the traveling direction toward the front surface and the back surface of the object 1 are provided in the seal box 5 respectively. Furthermore, slide plates 8 a and 8 b that can open and close the second opening 37 are provided on the outside of the seal box 5. With the slide plates 8a and 8b, it is preferable to narrow the gap of the second opening 37 as much as possible within a range that does not affect the travel of the object 1 to be processed.
[0034]
Further, as means for supplying and removing air into the pressure adjustment chamber 9, an air supply pipe 10 having an air supply adjustment valve 16 and an exhaust pipe 11 having an exhaust adjustment valve 17 are connected to the pressure adjustment chamber 9. .
[0035]
Then, a differential pressure gauge 14 measures the pressure difference between the pressure detection unit 12 disposed in the seal box 5 and the pressure detection unit 13 disposed in the pressure adjustment chamber 9, and the signal and the control unit are measured. The flow rate is adjusted by operating the air supply adjustment valve 16 and the exhaust adjustment valve 17 according to the deviation from the value set to 15 (basically, the set differential pressure is 0) (Either supply air or exhaust gas can be adjusted). Possible), the pressure in the pressure adjusting chamber 9 is controlled, and the gas blowout (or air suction) from the second opening 37 of the seal box 5 is suppressed.
[0036]
In this pressure adjusting chamber 9 as well, pressure adjustment is performed by supplying and exhausting air. Therefore, it is preferable to reduce the cross-sectional area of the third opening 18 through which the workpiece 1 can penetrate, and the opening is the same as that of the seal box 5. Slide plates 19a and 19b are provided in the portion 18 so as to be openable and closable.
[0037]
In the inert type drying apparatus provided with the sealing device having the above-described configuration, the object to be processed 1 is a coating liquid applied to the surface by the gas blown from the blowout nozzle 3 in the drying furnace 2 which has been inerted with nitrogen gas. Is dried and conveyed from the first opening 4 to the right side of the figure (in the direction of the arrow) and passes through the second opening 37 of the seal box 5 and the third opening 18 of the pressure adjusting chamber 9. By circulating a gas containing a solvent using the inert drying furnace 2 as a closed circulation system and providing a solvent recovery device such as a condenser in the circulation system, the solvent in the atmosphere can be recovered.
[0038]
Here, in the seal box 5, as described above, nitrogen gas is supplied from the nitrogen gas supply pipe 6, and the upper and lower orifices 7 a and 7 b inside the seal box 5 are used to travel the front and back surfaces of the workpiece 1. Spray at any angle. A differential pressure between the pressure 12 in the seal box 5 and the pressure 13 in the pressure adjusting chamber 9 is measured by a differential pressure gauge 14 and the value set in the control unit 15 (basically, the set differential pressure is 0) Therefore, the flow rate is adjusted by the air supply adjustment valve 16 and the exhaust adjustment valve 17 (either air supply or exhaust can be adjusted), and the pressure in the pressure adjustment chamber 9 is controlled, that is, the seal box. By setting the pressure in 5 and the pressure in the pressure adjusting chamber 9 to be approximately equal, the blowing (or suction) of gas from the second opening 37 of the seal box 5 is suppressed.
[0039]
Although the said Example demonstrated the 1st opening part 4 by the side of the exit of the drying furnace 2, it is also possible to provide the sealing apparatus of the same structure in the entrance side of the drying furnace 2. FIG.
[0040]
(Example 2)
FIG. 2 illustrates a second embodiment in which the embodiment shown in FIG. 1 is improved.
[0041]
A feature of the embodiment of FIG. 2 is that a pressure adjusting function by the pressure adjusting chamber 9 of FIG. FIG. 2 shows a cross-sectional structure of the sealing device on the inlet side and outlet side of the drying furnace 2.
[0042]
The workpiece 1 is dried by the gas blown from the blowout nozzle 3 while moving from the left side to the right side in the drying furnace 2 that has been inerted with nitrogen gas.
[0043]
Sealing boxes 5 are installed on the wall surfaces on the inlet side and the outlet side of the drying furnace 2 so as to communicate with the first opening 4 in order to maintain the inert state of the atmosphere.
[0044]
The seal box 5 is provided with a buffer space 20 on the first opening 4 side of the drying furnace 2 for buffering and weakening the dynamic pressure due to the blowing of the blowing nozzle 3 in the drying furnace 2. In order to efficiently buffer the dynamic pressure, a plurality of partition plates 21 are provided in the buffer space 20 with the gap as narrow as possible in the object 1 (to add resistance to the dynamic pressure). Weaken by things). A nitrogen gas space 40 for sealing is formed outside the sealing nitrogen gas blowing orifices 7a and 7b. Further, a pressure adjustment space 22 corresponding to the pressure adjustment chamber 9 in FIG. 1 is provided outside the seal box 5 so that pressure can be applied from the air supply pipe 10.
[0045]
The adjustment method of the balance of maintaining the inert atmosphere in the sealing device of this configuration is the pressure measurement by the pressure detection unit 12 installed in the buffer space 20 and the pressure measurement by the pressure detection unit 13 installed in the pressure adjustment space 22. The differential pressure is measured by the differential pressure gauge 14, and the amount of air supplied to the pressure adjustment space 22 on the inlet side and the outlet side of the drying furnace 2 is determined by the difference between the signal and the control unit 15. Adjust by opening and closing. For example, when the differential pressure gauge 14 indicates that the pressure in the buffer space 20 is higher than the pressure in the pressure adjustment space 22, the gas in the vicinity of the opening 4 of the drying furnace passes through the first opening 4. Since the air is blown out through the air, the air regulating valve 16 a is opened to increase the pressure in the pressure regulating space 22 and supply air into the pressure regulating space 22. On the other hand, when the pressure in the pressure adjustment space 22 is high, the air supply adjustment valve 16a is actuated to close in order to reduce the pressure in the pressure adjustment space 22.
[0046]
Further, if the pressure in the pressure adjustment space 22 is still high even when the air supply adjustment valve 16a is fully closed, the air supply adjustment valve 16b of the seal box 5 at the opening of the drying furnace opposite to the drying furnace 2 is opened. Move in the direction and adjust the pressure.
[0047]
In addition, as a method for detecting whether or not nitrogen gas is flowing in the sealing device portion of the drying furnace, the oxygen concentration in the drying furnace is not limited to the method for detecting the differential pressure between the seal box 5 and the pressure adjustment space 22. Can also be implemented.
[0048]
An oxygen concentration meter 23 is installed on the inlet side of the drying furnace 2, and a predetermined signal is supplied from the control unit 25 based on the deviation between the detection output of the concentration meter 23 and the detection output of the oxygen concentration meter 24 installed on the outlet side. A feed opening degree is adjusted to the air regulating valves 16a and 16b. Also in this case, similarly to the pressure adjustment by the differential pressure, when the oxygen concentration on the inlet side of the drying furnace 2 is high, the air supply adjustment is performed in the direction of increasing the pressure in the pressure adjusting space 22 on the outlet side of the drying furnace 2. On the contrary, when the valve 16a is operated and the oxygen concentration on the outlet side is high, the reverse operation is performed.
[0049]
(Example 3)
The feature of the third embodiment shown in FIG. 3 is that the pressure adjustment function described in the second embodiment (FIG. 2) is performed by the suction gas from the buffer space 20.
[0050]
The buffer space 20 of the seal box 5 and the downstream side of the drying furnace 2 are connected by a return pipe 27 having a fan 26 and a suction gas regulating valve 28. The gas in the seal box 5 is sucked by the fan 26 and dried. By returning the gas to the furnace 2, the pressure in the buffer space 20 can be reduced.
[0051]
The pressure balance adjustment method for maintaining the inert atmosphere is basically the same as described in the second embodiment (FIG. 2), and the pressure in the buffer space 20 is determined from the measured value of the differential pressure gauge 14 as the internal pressure of the pressure adjustment space 22. If higher, the suction gas regulating valve 28 installed on the discharge side of the fan 26 of the return pipe 27 is opened to lower the pressure in the buffer space 20 to increase the amount of suction from the buffer space 20 and adjust the pressure. Do. Conversely, when the pressure in the buffer space 20 is low, the pressure is adjusted by decreasing the suction gas amount and increasing the suction amount of the seal box 5 in the opposite opening 4.
[0052]
Further, the pressure balance adjustment based on the deviation of the oxygen concentration is the same as that in the second embodiment, and is omitted here.
[0053]
(Example 4)
The characteristic of Example 4 shown in FIG. 4 is a solvent recovery method according to the inert method described in Japanese Patent Publication No. 3-25228. A part of the gas containing solvent vapor in the drying furnace is introduced into the condenser, In the solvent recovery system that constitutes a closed circulation system that condenses and recovers the solvent vapor by cooling and returns the remaining gas to the drying furnace, the pressure in the seal box 5 is adjusted using the gas in the closed circulation system. It is.
[0054]
The gas in the drying furnace 2 in which the inert atmosphere is constituted by nitrogen gas is sent to the condenser 31 by the fan 29 and the exhaust pipe 30, and is cooled here to condense and recover the solvent vapor. The remaining gas constitutes a circulation system that is returned to the drying furnace 2 by the return pipe 32 again. Nitrogen gas is supplied from the nitrogen gas supply pipe 6 to the orifices 7a and 7b to the seal box 5 installed outside the first opening 4 through which the workpiece 1 formed on the wall surface of the drying furnace 2 passes. , Blow out from the tip. The pressure adjustment space 22 is provided with a return gas supply pipe 33 for supplying a part of the gas from the return pipe 32 and a return gas adjustment valve 34 for adjusting the flow rate. On the other hand, a suction pipe 35 and a suction gas adjusting valve 36 for adjusting the flow rate are provided from the buffer space 20 so that gas can be sucked into the exhaust pipe 30.
[0055]
The balance adjustment method for maintaining the inert atmosphere is basically performed by the method shown in the second and third embodiments in FIGS. This can be done by adjusting the flow rate of the return gas adjusting valve 34 and the suction gas adjusting valve 36 by the pressure signal from the differential pressure gauge 14 or the deviation signal of the oximeters 23 and 24.
[0056]
【The invention's effect】
The effect of adjusting the pressure balance for maintaining the inert atmosphere in the drying furnace was recognized by the sealing device for the processing object penetration part of the drying furnace of the present invention. As a result, the flow rate of nitrogen gas for sealing can be reduced, and leakage of atmospheric gas containing high-concentration solvent vapor to the outside can be prevented, and reduction of running cost and improvement of environmental conservation are recognized.
[0057]
In particular, the pressure balance in the drying furnace can be adjusted automatically by detecting the pressure balance fluctuation in the drying furnace with a differential pressure gauge or oxygen concentration meter. For example, a change in the wind speed of the blowing nozzle, a change in the traveling speed of the object to be processed, and the like are particularly effective.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view of an essential part of an embodiment of a sealing device of the present invention in which the pressure balance of an atmosphere in a drying furnace is adjusted by adjusting the pressure in a pressure adjusting chamber.
FIG. 2 is a cross-sectional view of an essential part showing another embodiment of the sealing device of the present invention in which the pressure balance of the drying furnace atmosphere is adjusted by adjusting the air supply amount in the pressure adjusting space in the seal box.
FIG. 3 is a partially cutaway cross-sectional view showing still another embodiment of the sealing device of the present invention in which the pressure balance of the drying furnace atmosphere is adjusted by adjusting the amount of gas suction from the buffer space in the seal box.
FIG. 4 is a cross-sectional view of an essential part showing still another embodiment of the sealing device of the present invention in which the pressure balance of the drying furnace atmosphere is adjusted by adjusting the gas flow in and out of the seal box in the closed circulation system solvent recovery device. FIG.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 To-be-processed object 2 Drying furnace 3 Blowing nozzle 4 1st opening part 5 Seal box 6 Nitrogen gas supply piping 7a, 7b Orifice 8a, 8b Slide plate 9 Pressure adjustment chamber 10 Supply pipe 11 Exhaust pipe 12 Pressure detection in a seal box Unit 13 Pressure detection unit 14 in pressure adjustment chamber Differential pressure gauge 15 Control unit 16, 16a, 16b Air supply adjustment valve 17 Exhaust adjustment valve 18 Third opening 19a, 19b of pressure adjustment chamber Slide plate 20 Buffer space 21 Partition plate 22 Pressure adjustment space 23 Inlet side oxygen concentration meter 24 Outlet side oxygen concentration meter 25 Control unit 26 Fan 27 Gas return pipe 28 Suction gas adjustment valve 29 Fan 30 Extraction pipe 31 Condenser 32 Return pipe 33 Return gas supply pipe 34 Return gas adjustment valve 35 Suction piping 36 Suction gas regulating valve 37 Second opening 40 Nitrogen gas space for sealing

Claims (7)

乾燥炉の壁面に設けられた被処理体が貫通し得る第1の開口部を通るガスの流通を減少するための、乾燥炉壁面の被処理体貫通部シール装置であって、
該乾燥炉の該第1の開口部に連通して設けられており、該被処理体が貫通し得る第2の開口部を有するシールボックスと、
該シールボックスの外側に配設された第3の開口部を有する圧力調整室と、
該シールボックス内に不活性ガスを供給する手段と、
該第1の開口部を通るガスの流通を検知する手段と、
検知したガスの流通量を低減するための該圧力調整室の圧力調整手段と、
を具備するシール装置。
To reduce the circulation of gas through the first opening through which the object to be processed provided on the wall surface of the drying furnace can penetrate,
A seal box provided in communication with the first opening of the drying furnace and having a second opening through which the object can pass;
A pressure regulating chamber having a third opening disposed outside the seal box;
Means for supplying an inert gas into the seal box;
Means for detecting the flow of gas through the first opening;
Pressure adjusting means of the pressure adjusting chamber for reducing the flow rate of the detected gas;
A sealing device comprising:
乾燥炉の壁面に設けられた被処理体が貫通し得る第1の開口部を通るガスの流通を減少するための、乾燥炉壁面の被処理体貫通部シール装置であって、
該乾燥炉の該第1の開口部に連通して設けられており、該被処理体が貫通し得る第2の開口部を有するシールボックスと、
該シールボックス内に設けられており、該被処理体が貫通し得る該第2の開口部を共有する圧力調整空間と、
該シールボックス内に不活性ガスを供給する手段と、
該圧力調整空間内に空気を供給および/または排除する手段と、
該第1の開口部を通るガスの流通を検知する手段と、
検知したガスの流通量を低減するための該圧力調整空間の圧力調整手段と、
を具備するシール装置。
A processing object through-portion sealing device for a drying furnace wall for reducing the flow of gas through the first opening through which the object to be processed provided on the wall of the drying furnace can pass,
A seal box provided in communication with the first opening of the drying furnace and having a second opening through which the object can be passed;
A pressure adjusting space provided in the seal box and sharing the second opening through which the object to be processed can pass;
Means for supplying an inert gas into the seal box;
Means for supplying and / or excluding air into the pressure regulating space;
Means for detecting the flow of gas through the first opening;
Pressure adjusting means of the pressure adjusting space for reducing the flow rate of the detected gas;
A sealing device comprising:
前記第1の開口部を流通するガスの流通を検知する手段が、前記シールボックス内の第1の開口部側と圧力調整室内との圧力差信号または乾燥炉内の入口側及び出口側の酸素濃度計測定値の偏差信号により行われる、請求項1記載のシール装置。The means for detecting the flow of the gas flowing through the first opening is a pressure difference signal between the first opening side in the seal box and the pressure adjustment chamber, or oxygen on the inlet side and outlet side in the drying furnace. The sealing device according to claim 1, which is performed by a deviation signal of a densitometer measurement value. 前記第1の開口部を流通するガスの流通を検知する手段が、前記シールボックス内と前記圧力調整空間内の圧力差信号または乾燥炉内の入口側及び出口側の酸素濃度計測定値の偏差信号により行われる、請求項2記載のシール装置。The means for detecting the flow of the gas flowing through the first opening is a pressure difference signal in the seal box and the pressure adjustment space, or a deviation signal of the oximeter measurement values on the inlet side and the outlet side in the drying furnace. The sealing device according to claim 2, wherein 前記圧力調整手段が、前記圧力調整室内または圧力調整空間内への空気の供給手段に設けられた給気調整弁および/または排除手段に設けられた排気調整弁の開閉により行われる、請求項1又は2に記載のシール装置。The pressure adjusting means is performed by opening and closing an air supply adjusting valve provided in an air supply means and / or an exhaust adjusting valve provided in an exclusion means in the pressure adjusting chamber or the pressure adjusting space. Or the sealing apparatus of 2. 前記圧力調整手段が、前記シールボックス内のガスをファンで乾燥炉内に戻す配管に設置した吸引ガス調整弁で圧力を調整することにより行われる、請求項1又は2に記載のシール装置。The sealing device according to claim 1 or 2, wherein the pressure adjusting means is performed by adjusting the pressure with a suction gas adjusting valve installed in a pipe for returning the gas in the seal box to the drying furnace with a fan. 前記圧力調整手段が、乾燥炉に接続されたイナート方式による溶剤回収装置におけるシールボックスヘのガスの流出入量調整手段である請求項1又は2に記載のシール装置。3. The sealing device according to claim 1, wherein the pressure adjusting means is a gas inflow / outflow amount adjusting means for a seal box in an inert solvent recovery apparatus connected to a drying furnace.
JP29602997A 1997-10-28 1997-10-28 Drying furnace wall surface processing object penetration part sealing device Expired - Lifetime JP3616485B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP29602997A JP3616485B2 (en) 1997-10-28 1997-10-28 Drying furnace wall surface processing object penetration part sealing device
AU89558/98A AU8955898A (en) 1997-10-28 1998-10-27 Sealing apparatus for drying furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29602997A JP3616485B2 (en) 1997-10-28 1997-10-28 Drying furnace wall surface processing object penetration part sealing device

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JP3616485B2 true JP3616485B2 (en) 2005-02-02

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JP2006194546A (en) * 2005-01-14 2006-07-27 Dainippon Printing Co Ltd Continuously decompressed drying method and apparatus
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