JP2012240370A - Apparatus for continuously heating long film - Google Patents

Apparatus for continuously heating long film Download PDF

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JP2012240370A
JP2012240370A JP2011114880A JP2011114880A JP2012240370A JP 2012240370 A JP2012240370 A JP 2012240370A JP 2011114880 A JP2011114880 A JP 2011114880A JP 2011114880 A JP2011114880 A JP 2011114880A JP 2012240370 A JP2012240370 A JP 2012240370A
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furnace
air
outside
long film
hot air
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Takashi Kobayashi
小林  隆
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Sumitomo Metal Mining Co Ltd
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Sumitomo Metal Mining Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide an apparatus for continuously heating a long film in which inflow of contaminated air containing dust etc., into a furnace can be prevented without causing trouble in transportation of the long film.SOLUTION: There is provided the apparatus for continuously heating in which hot air fed through an air feeding means having a fan 3, a heater 2, and an air filter 4 such as a HEPA filter (high efficiency particulate air filter) into the furnace 1 is circulated; a portion of the hot air is exhausted through an exhausting means to the outside of the furnace; a continuous heat treatment is applied to the long film 7 which is carried in and out from an opening 9 of the furnace body in the furnace; and the circulated amount of the hot air is composed of the total amount of an air flow rate of the return system which is exhausted to the outside of the furnace without passing through the exhausting means and returned to the air inlet side of the air feeding means and the air flow rate of the air inlet system newly introduced into the air inlet side of the air feeding means. In the continuously heating apparatus, a fine differential pressure gage 13 for detecting a pressure difference between the inside of the furnace and the outside of the furnace is installed in the furnace body, and the air flow rate exhausted with the exhausting means is finely adjusted to a lower air flow rate than the air flow rate of the air inlet system on the basis of the pressure difference detected with the fine differential pressure gage to maintain the inside of the furnace at a fine positive pressure.

Description

本発明は、炉内に連続搬入される長尺フィルムに対し炉内の処理室において連続的に加熱処理を行う長尺フィルムの連続加熱装置に係り、特に、塵等を含んだ汚染空気が炉内の処理室に流入することを防止でき、しかも、長尺フィルムの搬送に支障を来たさない連続加熱装置の改良に関するものである。   The present invention relates to a continuous heating apparatus for a long film that continuously heats a long film that is continuously carried into the furnace in a processing chamber in the furnace, and in particular, contaminated air containing dust or the like is contained in the furnace. The present invention relates to an improvement of a continuous heating apparatus that can prevent the flow into the inner processing chamber and that does not hinder the conveyance of the long film.

ポリイミド系、ポリエステル系等の長尺フィルムは、フレキシブル性を有し、容易に加工できることから、電子部品、光学部品、包装材料等の産業分野において広く用いられており、真空蒸着法、スパッタリング法、イオンプレーティング法、CVD法等の真空成膜法を適用して、長尺フィルム上に金属やその酸化物、窒化物、炭化物、有機物等の膜を形成する技術が古くから開発されている。また、近年、エレクトロニクス分野においては、利用される様々な材料で高密度化、高精細化が進み、高品質な材料が求められている。そして、長尺フィルムの種類にもよるが、長尺フィルム中には若干の水分や有機溶媒が含まれており、真空蒸着法、スパッタリング法等上述した真空成膜法を用いて金属やその酸化物等の膜を長尺フィルム上に成膜した場合、長尺フィルム中に含まれる水分や有機溶媒が長尺フィルム表面に拡散、脱離して膜質に悪影響を及ぼすことがあるため、金属やその酸化物等を成膜する前に長尺フィルムを加熱処理して有機溶媒等を除去する必要があった。また、金属やその酸化物等が成膜された後に長尺フィルムを加熱処理して金属等の結晶性を改善することもなされていた。   Long films such as polyimides and polyesters have flexibility and can be easily processed, so they are widely used in industrial fields such as electronic parts, optical parts, packaging materials, vacuum deposition methods, sputtering methods, A technique for forming a film of a metal, an oxide thereof, a nitride, a carbide, an organic substance, etc. on a long film by applying a vacuum film forming method such as an ion plating method or a CVD method has been developed for a long time. In recent years, in the electronics field, various materials used have been increased in density and definition, and high-quality materials have been demanded. Although depending on the type of the long film, the long film contains some moisture and organic solvent, and the metal and its oxidation are formed using the above-described vacuum film-forming methods such as vacuum deposition and sputtering. When a film such as an object is formed on a long film, moisture and organic solvent contained in the long film may diffuse and desorb on the surface of the long film, adversely affecting the film quality. Before forming an oxide film or the like, it was necessary to heat the long film to remove the organic solvent or the like. In addition, after a metal or its oxide is formed, the long film is heat-treated to improve the crystallinity of the metal or the like.

ところで、長尺フィルムの連続加熱処理に使用される従来の装置として、長尺フィルムを水平に搬送させる特許文献1に記載の装置が知られており、この装置におけるフィルムの処理能力を高めた連続加熱装置として、図1に示す構造のものが開発されている。   By the way, the apparatus of patent document 1 which conveys a long film horizontally as a conventional apparatus used for the continuous heat processing of a long film is known, and the continuation which raised the processing capability of the film in this apparatus. As a heating device, one having the structure shown in FIG. 1 has been developed.

以下、図1を用いてこの種の連続加熱装置について説明する。   Hereinafter, this type of continuous heating apparatus will be described with reference to FIG.

まず、この連続加熱装置は、内部に処理室を有する炉1本体と、炉1本体に設けられ上記処理室に長尺フィルム7を連続的に搬入しかつ搬出させるための開口部(フィルム搬入口とフィルム搬出口)9と、上記炉1内に熱風を供給しかつ循環させる給気手段と、炉1内において揮発成分(例えば長尺フィルムから除かれた溶媒成分)等が飽和することを防止するため炉1外へ熱風の一部を排気させる排気手段を備えている。   First, the continuous heating apparatus includes a furnace 1 main body having a processing chamber therein, and an opening (film inlet port) provided in the furnace 1 main body for continuously carrying in and out the long film 7 into the processing chamber. And film outlet) 9, supply means for supplying and circulating hot air into the furnace 1, and saturation of volatile components (for example, solvent components removed from the long film) in the furnace 1 are prevented. Therefore, an exhaust means for exhausting a part of the hot air to the outside of the furnace 1 is provided.

また、上記炉1内に熱風を供給しかつ循環させるための配管(すなわち上記給気手段)は、熱を発生させるためのヒータ2と、この熱を炉1内に送るための送風機(ブロアー)3と、炉1内における清浄度を保つためのHEPAフィルター(High Efficiency Particulate Airfilter)等のエアーフィルター4とを有しており、上記給気手段の入気口側には炉1外のフレッシュエアーを取り込むための入気系の配管が連設され、更に、上記給気手段の入気口側には排気手段を経由せずに炉1外へ排気されかつ循環用に供される熱風を取り込むための戻り系の配管が連設されている。尚、図1中、符号5は入気系の配管に付設されてフレッシュエアーの取り込み量を調整するダンパーを示し、符号6は戻り系の配管に付設されて循環用に供される熱風量を調整するダンパーを示している。また、熱風の一部を炉1外へ排気させるための配管(すなわち上記排気手段)は、熱風を炉1外へ排気させる排気ファン14と、排気させる熱風の排気量を調整するダンパー10とを有している。   A pipe for supplying and circulating hot air into the furnace 1 (that is, the air supply means) includes a heater 2 for generating heat and a blower (blower) for sending the heat into the furnace 1. 3 and an air filter 4 such as a HEPA filter (High Efficiency Particulate Airfilter) for maintaining cleanliness in the furnace 1, and fresh air outside the furnace 1 is provided on the inlet side of the air supply means. An intake system pipe for taking in air is connected in series, and further, hot air that is exhausted out of the furnace 1 without being passed through the exhaust means and used for circulation is taken into the inlet side of the air supply means. For this purpose, a return system pipe is provided continuously. In FIG. 1, reference numeral 5 denotes a damper attached to the inlet pipe to adjust the intake amount of fresh air, and reference numeral 6 denotes an amount of hot air attached to the return pipe and used for circulation. The damper to be adjusted is shown. Further, a pipe for exhausting a part of the hot air to the outside of the furnace 1 (that is, the exhaust means) includes an exhaust fan 14 for exhausting the hot air to the outside of the furnace 1 and a damper 10 for adjusting the exhaust amount of the hot air to be exhausted. Have.

そして、この連続加熱装置においては、上記炉1内の上部パンチングプレート12と下部パンチングプレート11とで区画された処理空間内に給気手段のエアーフィルター4を介して清浄化された熱風が循環供給され、処理空間内に搬入された長尺フィルム7が供給された熱風で加熱処理されるように構成されている。   And in this continuous heating apparatus, the hot air cleaned through the air filter 4 of the air supply means is circulated and supplied into the processing space defined by the upper punching plate 12 and the lower punching plate 11 in the furnace 1. The long film 7 carried into the processing space is heated with the supplied hot air.

近年、電子機器は、極めて薄く柔軟性のあるフレキシブルフィルムを用いた配線フィルムが多くなってきており、フレキシブルフィルムに対応させた連続加熱処理においては、フレキシブルフィルムが熱により容易に変形してしまうことから、通常、低いテンション(張力)を加えてフレキシブルフィルム(長尺フィルム)を搬送させている。   In recent years, the number of wiring films using extremely thin and flexible flexible films is increasing in electronic devices. In continuous heat treatment corresponding to flexible films, flexible films are easily deformed by heat. Therefore, a flexible film (long film) is usually conveyed by applying a low tension (tension).

ところで、上記給気手段により炉1内へ供給される熱風の循環量は、フレッシュエアーの取り込み量(入気系の風量)と戻り系の熱風量(戻り系の風量)により決まる(すなわち、入気系の風量と戻り系の風量の合計量で決まる)が、上記排気手段による熱風の排気量が多くなるにつれて炉1内の圧力が炉1外の圧力より低くなって炉1内が負圧になり、炉1内が負圧になるに伴い長尺フィルム7の開口部(フィルム搬入口とフィルム搬出口)9から塵等を含んだ汚染空気が処理空間内に流入し、この汚染空気により長尺フィルム7に塵等が付着してしまうことがあった。   By the way, the circulation amount of the hot air supplied into the furnace 1 by the above air supply means is determined by the intake amount of fresh air (inlet air amount) and the return hot air amount (return air amount) (that is, the input air amount). However, as the amount of hot air exhausted by the exhaust means increases, the pressure inside the furnace 1 becomes lower than the pressure outside the furnace 1 and the inside of the furnace 1 is negative. As the inside of the furnace 1 becomes negative pressure, contaminated air containing dust and the like flows into the processing space from the openings (film inlet and outlet) 9 of the long film 7, and this contaminated air causes In some cases, dust or the like may adhere to the long film 7.

そして、フレキシブルフィルム(長尺フィルム)に塵等が付着し、あるいは、加工された配線フィルムの金属配線回路上に塵等が付着することは、配線ショートの原因となるため品質上の問題となっていた。   And, dust or the like adheres to the flexible film (long film), or the dust or the like adheres to the metal wiring circuit of the processed wiring film, which causes a wiring short circuit, which is a quality problem. It was.

このような問題を回避するため、図1に示す連続加熱装置を用いて長尺フィルムの連続加熱を行なう場合には、上記排気手段のダンパー10を絞って排気風量を少なくし、入気風量より僅かに少ない排気風量となった条件で上記ダンパー10を固定(すなわち、排気風量を一定値に固定)し、長尺フィルムの連続加熱を行なう方法が採られている。   In order to avoid such a problem, when continuous heating of a long film is performed using the continuous heating apparatus shown in FIG. 1, the damper 10 of the exhaust means is squeezed to reduce the exhaust air volume, so that the exhaust air volume is less than that. A method is adopted in which the damper 10 is fixed (that is, the exhaust air volume is fixed at a constant value) under the condition that the exhaust air volume is slightly reduced, and the long film is continuously heated.

しかし、上記ダンパー10を絞って排気風量を固定させる方法を採ったとしても、長尺フィルムの連続加熱処理を継続して行なった場合、炉1外の圧力(例えば、連続加熱装置が設置された室内の圧力)が経時的に変動してしまうことがあり、いつのまにか炉1内の圧力が炉1外の圧力に対して負圧状態になり、炉1外(連続加熱装置が設置された室内)の塵等を含んだ汚染空気が上記開口部(フィルム搬入口とフィルム搬出口)9から流入してしまう問題が存在した。   However, even if the damper 10 is squeezed to fix the exhaust air volume, when the continuous heat treatment of the long film is continued, the pressure outside the furnace 1 (for example, a continuous heating device is installed). The pressure inside the furnace may fluctuate over time, and the pressure inside the furnace 1 becomes negative with respect to the pressure outside the furnace 1 before long. The outside of the furnace 1 (the room where the continuous heating device is installed) There is a problem that contaminated air containing dust and the like flows from the openings (film inlet / outlet) 9.

この場合、上記ダンパー10を絞って排気風量を大幅に下げ、入気風量を大きくする方法が考えられるが、上記開口部(フィルム搬入口とフィルム搬出口)9を介して炉1内から炉1外(室内)へ流れ出る風量が多くなってしまい、その風量に起因して、開口部(フィルム搬入口とフィルム搬出口)9の近傍を搬送される長尺フィルムがバタバタと揺れ動いてしまい、フィルムへ強いテンション(張力)を加えないと安定したフィルム搬送が困難となる別の問題が存在した。   In this case, a method is conceivable in which the damper 10 is squeezed to greatly reduce the exhaust air volume and increase the intake air volume. However, the furnace 1 from the furnace 1 through the opening (film inlet / outlet) 9 can be considered. The amount of air that flows outside (inside the room) increases, and due to the amount of air, the long film transported in the vicinity of the opening (film inlet and outlet) 9 shakes and flutters to the film. There has been another problem that stable film transportation becomes difficult unless a strong tension is applied.

そして、加熱されている状態の長尺フィルムに対し強いテンション(張力)を加えた場合、長尺フィルムが容易に伸びてフィルム内部に応力が残ってしまい、最終製品にしたときにフィルムが反るという新たな問題を発生させてしまう。   And when a strong tension (tension) is applied to the heated long film, the long film easily stretches and stress remains in the film, and the film warps when it is made into a final product. Will cause a new problem.

特開2002−18970号公報JP 2002-18970 A 特開2008−185388号公報JP 2008-185388 A

本発明はこのような問題点に着目してなされたもので、その課題とするところは、塵等を含んだ汚染空気が炉内の処理室に流入することを防止でき、しかも、長尺フィルムの搬送に支障を来たさない連続加熱装置を提供することにある。   The present invention has been made paying attention to such problems, and the problem is that the contaminated air containing dust and the like can be prevented from flowing into the processing chamber in the furnace, and the long film An object of the present invention is to provide a continuous heating apparatus that does not hinder the conveyance of the sheet.

すなわち、請求項1に係る発明は、
送風機とヒータおよびエアーフィルターを有する給気手段を経由して炉内に供給される熱風が循環し、一部の熱風が排気手段を経由して炉内から炉外へ排気されると共に、炉本体のフィルム搬入口から炉内に搬入されフィルム搬出口から炉外へ搬出される長尺フィルムに対し炉内の処理室において熱風による連続加熱処理を行い、かつ、上記熱風の循環量が、上記排気手段を経由せずに炉内から炉外へ排気されて上記給気手段の入気口側に戻される戻り系の風量と、炉外から上記給気手段の入気口側に新たに導入される入気系の風量との合計量にて構成される長尺フィルムの連続加熱装置において、
上記炉内と炉外との圧力差を検出する微差圧計を炉本体に設け、微差圧計で検出された圧力差に基づき上記排気手段により排気する風量を入気系の風量より少なく微調整して、炉内を微正圧に維持することを特徴とする。
That is, the invention according to claim 1
Hot air supplied into the furnace via the air supply means having a blower, a heater and an air filter circulates, and part of the hot air is exhausted from the inside of the furnace to the outside of the furnace via the exhaust means, and the furnace body The long film carried into the furnace from the film carry-in port and carried out from the film carry-out port to the outside of the furnace is subjected to continuous heat treatment with hot air in the treatment chamber in the furnace, and the circulation amount of the hot air is A return air volume that is exhausted from the inside of the furnace to the outside of the furnace without passing through the means and returned to the inlet side of the air supply means, and newly introduced from the outside of the furnace to the inlet side of the air supply means. In the continuous heating device for long films composed of the total amount of airflow of the inlet system
A fine differential pressure gauge that detects the pressure difference between the inside of the furnace and the outside of the furnace is provided in the furnace body, and the air volume exhausted by the exhaust means based on the pressure difference detected by the fine differential pressure gauge is finely adjusted to be less than the air volume of the inlet system. Then, the inside of the furnace is maintained at a slight positive pressure.

また、請求項2に係る発明は、
請求項1に記載の発明に係る長尺フィルムの連続加熱装置において、
上記排気手段が、回転速度可変モータで駆動する排気ファンと上記モータの回転速度を制御するインバーター制御装置とで構成されていることを特徴とし、
請求項3に係る発明は、
請求項1または2に記載の発明に係る長尺フィルムの連続加熱装置において、
炉内の上記処理室が、炉内の上方側に設けられた上部パンチングプレートと炉内の下方側に設けられた下部パンチングプレートとで区画された処理空間を有し、上記上部パンチングプレートを介して処理空間内に熱風が導入されかつ上記下部パンチングプレートを介して処理空間内の熱風が炉外へ排気されると共に、処理空間内の上部パンチングプレートと下部パンチングプレートの各近傍にそれぞれ一列に配置された複数の上部ローラ群と下部ローラ群を交互に経由させて上記長尺フィルムが処理空間内を搬送されるようになっていることを特徴とするものである。
The invention according to claim 2
In the continuous heating apparatus of the long film which concerns on invention of Claim 1,
The exhaust means is composed of an exhaust fan driven by a rotational speed variable motor and an inverter control device for controlling the rotational speed of the motor,
The invention according to claim 3
In the continuous heating apparatus for a long film according to the invention of claim 1 or 2,
The processing chamber in the furnace has a processing space defined by an upper punching plate provided on the upper side of the furnace and a lower punching plate provided on the lower side of the furnace, and the processing chamber is interposed via the upper punching plate. The hot air is introduced into the processing space, and the hot air in the processing space is exhausted to the outside of the furnace through the lower punching plate, and is arranged in a row near each of the upper punching plate and the lower punching plate in the processing space. The long film is conveyed in the processing space through a plurality of upper roller groups and lower roller groups alternately.

本発明に係る長尺フィルムの連続加熱装置によれば、
炉内と炉外との圧力差を検出する微差圧計を炉本体に設け、微差圧計で検出された圧力差に基づき上記排気手段により排気する風量を入気系の風量より少なく微調整して炉内を微正圧に維持している。
According to the continuous heating device for a long film according to the present invention,
A fine differential pressure gauge that detects the pressure difference between the inside and outside of the furnace is installed in the furnace body, and based on the pressure difference detected by the fine differential pressure gauge, the air volume exhausted by the exhaust means is finely adjusted to be less than the air volume of the inlet system. The inside of the furnace is maintained at a slight positive pressure.

従って、炉内が微正圧に維持されているため、炉外(例えば連続加熱装置が設置された室内)の塵等を含んだ汚染空気がフィルム搬入口や搬出口を構成する開口部から炉内に流入してしまうことがなく、かつ、上記微正圧に起因して炉外へ極少量流れ出る風により上記開口部近傍を搬送される長尺フィルムがバタバタと揺れ動いてしまうこともないため、フィルムへ強いテンション(張力)を加えることなく安定したフィルムの搬送が可能となり、更に、フィルムに強いテンション(張力)を加える必要がないことからフィルム内部に応力が残ることもないため、最終製品にしたときにフィルムが反ってしまうといった問題も解消することが可能となる。   Therefore, since the inside of the furnace is maintained at a slight positive pressure, contaminated air containing dust and the like outside the furnace (for example, the room where the continuous heating device is installed) enters the furnace from the openings constituting the film inlet and outlet. Because the long film that is transported in the vicinity of the opening by the wind that flows out to the outside of the furnace due to the fine positive pressure does not sway with the flutter, without flowing into the inside, Since it is possible to transport the film stably without applying strong tension (tension) to the film, and since there is no need to apply strong tension (tension) to the film, there is no stress remaining inside the film. It is possible to solve the problem that the film warps when it is done.

処理能力を高めた従来例に係る長尺フィルムの連続加熱装置の説明図。Explanatory drawing of the continuous heating apparatus of the elongate film which concerns on the prior art example which raised processing capacity. 本発明に係る長尺フィルムの連続加熱装置の説明図。Explanatory drawing of the continuous heating apparatus of the long film which concerns on this invention.

以下、本発明の実施の形態について詳細に説明する。   Hereinafter, embodiments of the present invention will be described in detail.

この実施の形態に係る長尺フィルムの連続加熱装置は、図2に示すように、内部に処理室を有する炉1本体と、炉1本体に設けられ上記処理室に長尺フィルム7を連続的に搬入しかつ搬出させるための開口部(フィルム搬入口とフィルム搬出口)9と、上記炉1内に熱風を供給しかつ循環させるための給気手段と、炉1内において揮発成分(例えば、加熱処理により長尺フィルムから除かれた有機溶媒成分)等が飽和することを防止するため炉1外へ熱風の一部を排気させる排気手段と、炉1本体に設けられ上記炉1内と炉1外(例えば、この装置が設置された室内)との圧力差を検出する微差圧計13とを備えている。   As shown in FIG. 2, the continuous heating apparatus for a long film according to this embodiment is a furnace 1 main body having a processing chamber inside, and a continuous film 7 is provided in the furnace 1 main body. An opening (film carry-in port and film carry-out port) 9 for carrying in and out, and an air supply means for supplying and circulating hot air into the furnace 1, and a volatile component (for example, In order to prevent saturation of the organic solvent component removed from the long film by the heat treatment) and the like, exhaust means for exhausting a part of the hot air to the outside of the furnace 1, and the furnace 1 and the furnace provided in the main body of the furnace 1 1 is provided with a fine differential pressure gauge 13 for detecting a pressure difference from the outside (for example, a room in which the apparatus is installed).

まず、上記炉1内に熱風を供給しかつ循環させるための図示外の配管(すなわち上記給気手段)は、熱を発生させるためのヒータ2と、この熱を炉1内に送るための送風機(ブロアー)3と、炉1内における清浄度を保つためのHEPAフィルター等のエアーフィルター4とを有しており、上記給気手段の入気口側には炉1外のフレッシュエアーを取り込むための入気系の配管が連設され、更に、上記給気手段の入気口側には排気手段を経由せずに炉1外へ排気されかつ循環用に供される熱風を取り込むための戻り系の配管が連設されている。   First, piping (not shown) for supplying and circulating hot air into the furnace 1 (that is, the air supply means) includes a heater 2 for generating heat and a blower for sending the heat into the furnace 1. (Blower) 3 and an air filter 4 such as a HEPA filter for maintaining the cleanliness in the furnace 1, in order to take in fresh air outside the furnace 1 to the inlet side of the air supply means In addition, a return pipe for taking in hot air that is exhausted out of the furnace 1 without passing through the exhaust means and used for circulation is provided on the inlet side of the air supply means. System piping is connected.

また、熱風の一部を炉1外へ排気させる図示外の配管(すなわち上記排気手段)は、回転速度可変モータにより駆動されかつ熱風を炉1外へ排気させるための排気ファン14と、上記モータの回転速度を制御するためのインバーター制御装置15とで構成され、上述した微差圧計13で検出された炉1内と炉1外との圧力差信号がインバーター制御装置15に入力され、この圧力差信号に基づきインバーター制御装置15が作動して上記モータの回転速度を制御し、これにより排気ファン14の排気風量が入気系の風量より少なくなるように微調整されて、炉1内を微正圧に維持するように構成されている。尚、上述の微差圧計13として、例えば、特許文献2に記載された微差圧計が挙げられる。   An unillustrated pipe for exhausting a part of the hot air to the outside of the furnace 1 (that is, the exhaust means) is driven by a variable speed motor, and the exhaust fan 14 for exhausting the hot air to the outside of the furnace 1 and the motor. The pressure difference signal between the inside of the furnace 1 and the outside of the furnace 1 detected by the above-mentioned fine differential pressure gauge 13 is inputted to the inverter control apparatus 15 and this pressure is controlled. Based on the difference signal, the inverter control device 15 is operated to control the rotational speed of the motor, thereby finely adjusting the exhaust air flow rate of the exhaust fan 14 to be smaller than the air flow rate of the intake system. It is configured to maintain a positive pressure. An example of the above-described fine differential pressure gauge 13 is the fine differential pressure gauge described in Patent Document 2.

また、炉1内の上記処理室は、炉内の上方側に設けられた上部パンチングプレート12と炉内の下方側に設けられた下部パンチングプレート11とで区画された処理空間を有しており、上記上部パンチングプレート12を介して処理空間内に熱風が均一に導入されると共に、上記下部パンチングプレート11を介して処理空間内の熱風が炉外へ均一に排気されるようになっている。   The processing chamber in the furnace 1 has a processing space defined by an upper punching plate 12 provided on the upper side in the furnace and a lower punching plate 11 provided on the lower side in the furnace. The hot air is uniformly introduced into the processing space through the upper punching plate 12, and the hot air in the processing space is uniformly exhausted outside the furnace through the lower punching plate 11.

更に、処理空間内の上部パンチングプレート12と下部パンチングプレート11の各近傍には、図2に示すように複数の上部ローラ8群と下部ローラ8群がそれぞれ一列に配置され、かつ、上記開口部(フィルム搬入口)9から処理空間内に搬入された長尺フィルム7が上部ローラ8群と下部ローラ8群を交互に経由して上記開口部(フィルム搬出口)9から処理空間外へ搬出されるように構成されており、上記給気手段のエアーフィルター4を介し処理空間内に供給される清浄化された熱風により長尺フィルム7の連続加熱処理が行われるようになっている。   Further, in the vicinity of the upper punching plate 12 and the lower punching plate 11 in the processing space, a plurality of upper roller 8 groups and lower roller 8 groups are respectively arranged in a row as shown in FIG. The long film 7 carried into the processing space from the (film carry-in port) 9 is carried out of the processing space from the opening (film carry-out port) 9 via the upper roller 8 group and the lower roller 8 group alternately. The long film 7 is continuously heated by the purified hot air supplied into the processing space via the air filter 4 of the air supply means.

この場合、この実施の形態に係る連続加熱装置においては、上部ローラ8群と下部ローラ8群を交互に経由して長尺フィルム7が処理空間内を蛇行搬送されるように構成されているため、長尺フィルムが処理空間内を水平に搬送される特許文献1に記載の装置と比較してフィルムの処理能力が高められる利点を有している。   In this case, the continuous heating device according to this embodiment is configured such that the long film 7 is meandered and conveyed in the processing space via the upper roller 8 group and the lower roller 8 group alternately. Compared with the apparatus described in Patent Document 1 in which a long film is transported horizontally in the processing space, it has an advantage that the processing capability of the film is enhanced.

尚、炉1内における清浄度を保つための上記エアーフィルター4としては、広く利用されている従来のフィルターから目的の清浄度に応じて適宜選択され、例えば、ULPAフィルター(Ultra Low Penetoration Airfilter)、HEPAフィルター(High Efficiency Particulate Airfilter)、MEPA(Medium Efficiency Particulate Airfilter)、および、特殊フィルター(高温雰囲気中で使用可能なULPA・HEPAフィルターや、プレフィルター・HEPA・中性能フィルター等)等が挙げられる。   The air filter 4 for maintaining the cleanliness in the furnace 1 is appropriately selected according to the target cleanliness from widely used conventional filters, for example, an ULPA filter (Ultra Low Penetoration Airfilter), Examples include HEPA filters (High Efficiency Particulate Airfilter), MEPA (Medium Efficiency Particulate Airfilter), and special filters (ULPA / HEPA filters that can be used in high-temperature atmospheres, prefilters / HEPA / medium performance filters, etc.).

また、図2中、符号5は入気系の配管に付設されてフレッシュエアーの取り込み量を調整するダンパー、符号6は戻り系の配管に付設されて循環用に供される熱風量を調整するダンパーを示しており、この実施の形態に係る装置を用いて長尺フィルム7の連続加熱を行う場合には、各ダンパー5、6を絞り込んで上記取り込み量(すなわち、入気系の風量)と循環用に供される熱風量(すなわち、戻り系の風量)が固定されている。   In FIG. 2, reference numeral 5 is a damper attached to the inlet piping to adjust the intake amount of fresh air, and reference numeral 6 is attached to the return piping to adjust the amount of hot air supplied for circulation. In the case of performing continuous heating of the long film 7 using the apparatus according to this embodiment, the dampers 5 and 6 are squeezed to obtain the above intake amount (that is, the air volume of the intake system). The amount of hot air supplied for circulation (that is, the amount of air in the return system) is fixed.

そして、この実施の形態に係る連続加熱装置によれば、上記炉1内と炉1外との圧力差を検出する微差圧計13が設けられており、この微差圧計13で検出された炉1内と炉1外との圧力差信号がインバーター制御装置15に入力され、この圧力差信号に基づきインバーター制御装置15が作動して排気ファン14の排気風量を入気系の風量(固定値)より少なくなるように微調整し、これにより炉1内を微正圧に維持している。   And according to the continuous heating apparatus which concerns on this embodiment, the fine differential pressure gauge 13 which detects the pressure difference between the said furnace 1 and the furnace 1 outside is provided, and the furnace detected with this fine differential pressure gauge 13 A pressure difference signal between the inside of the furnace 1 and the outside of the furnace 1 is input to the inverter control device 15, and the inverter control device 15 is operated based on this pressure difference signal, and the exhaust air volume of the exhaust fan 14 is changed to the air volume of the intake system (fixed value). The furnace 1 is finely adjusted so as to be smaller, thereby maintaining the inside of the furnace 1 at a slightly positive pressure.

従って、炉1外の塵等を含んだ汚染空気がフィルム搬入口や搬出口を構成する開口部9から炉1内に流入してしまうことがなく、かつ、上記微正圧に起因して炉1外へ極少量流れ出る風により上記開口部9近傍を搬送される長尺フィルム7がバタバタと揺れ動いてしまうこともないため、フィルム7へ強いテンション(張力)を加えることなく安定したフィルム7の搬送が可能となり、更に、フィルム7に強いテンション(張力)を加える必要がないことからフィルム7内部に応力が残ることもないため、最終製品にしたときにフィルム7が反ってしまうといった問題も解消される利点を有している。   Therefore, the contaminated air containing dust and the like outside the furnace 1 does not flow into the furnace 1 from the opening 9 constituting the film carry-in port and the carry-out port, and the furnace is caused by the fine positive pressure. Since the long film 7 transported in the vicinity of the opening 9 is not shaken by the wind that flows in a very small amount to the outside, the film 7 can be transported stably without applying strong tension (tension) to the film 7. Furthermore, since it is not necessary to apply a strong tension to the film 7, no stress remains in the film 7, so that the problem that the film 7 is warped when it is made into a final product is solved. Has the advantage of

以下、本発明の実施例について具体的に説明する。   Examples of the present invention will be specifically described below.

この実施例に係る長尺フィルムの連続加熱装置は、図2に示すように、内部に処理室を有する炉1本体と、炉1本体に設けられ上記処理室に長尺フィルム7を連続的に搬入しかつ搬出させるための開口部(フィルム搬入口とフィルム搬出口)9と、炉1内に200℃の熱風を供給しかつ循環させるための給気手段と、炉1内において揮発成分等が飽和することを防止するため炉1外へ熱風の一部を排気させる排気手段と、炉1本体の壁に設置され上記炉1内と炉1外(例えば、実施例に係る装置が設置された室内)との圧力差を検出する微差圧計13とを備えている。   As shown in FIG. 2, the continuous heating device for a long film according to this embodiment has a furnace 1 main body having a processing chamber inside, and a continuous long film 7 provided in the processing chamber provided in the furnace 1 main body. An opening (film inlet / outlet) 9 for carrying in and out, air supply means for supplying and circulating hot air at 200 ° C. in the furnace 1, volatile components etc. in the furnace 1 Exhaust means for exhausting part of the hot air to the outside of the furnace 1 to prevent saturation, and the inside of the furnace 1 and outside the furnace 1 (for example, the apparatus according to the embodiment was installed) And a micro differential pressure gauge 13 for detecting a pressure difference from the room.

まず、上記炉1内に200℃の熱風を供給しかつ循環させるための図示外の配管(すなわち上記給気手段)は、熱を発生させる30kWのヒータ2と、200℃の熱風を炉1内に送る11kWの送風機(ブロアー)3と、炉1内における清浄度を保つためのHEPAフィルター等のエアーフィルター4とを有しており、上記給気手段の入気口側には炉1外のフレッシュエアーを取り込む(炉1内において揮発成分等が飽和することを防止できる)ための入気系の配管が連設され、更に、上記給気手段の入気口側には排気手段を経由せずに炉1外へ排気されかつ循環用に供される熱風を取り込むための戻り系の配管が連設されている。   First, a pipe (not shown) for supplying and circulating hot air of 200 ° C. in the furnace 1 (that is, the air supply means) includes a 30 kW heater 2 for generating heat and hot air of 200 ° C. in the furnace 1. 11 kW blower 3 and an air filter 4 such as a HEPA filter for maintaining cleanliness in the furnace 1. The inlet side of the air supply means is outside the furnace 1. An intake system piping for taking in fresh air (saturation of volatile components in the furnace 1 can be prevented) is continuously provided, and further, an exhaust means is provided on the inlet side of the supply means. Instead, a return system pipe for taking in hot air exhausted out of the furnace 1 and used for circulation is connected.

また、熱風の一部を炉1外へ排気させる図示外の配管(すなわち上記排気手段)は、回転速度可変モータにより駆動されかつ熱風を炉1外へ排気させるための排気ファン14と、上記モータの回転速度を制御するためのインバーター制御装置15とで構成され、上述した微差圧計13で検出された炉1内と炉1外との圧力差信号がインバーター制御装置15に入力されるようになっている。そして、この圧力差信号に基づきインバーター制御装置15が作動して上記モータの回転速度を制御し、これにより排気ファン14の排気風量が以下に示す入気系の風量(4m3/min)より少なくなるように微調整(4m3/min−α)されて、炉1内を微正圧(炉1内の圧力が炉1外に較べて例えば10Pa高い)に維持するように構成されている。尚、この実施例では、上記微差圧計13として「山本電気工業(株)社製のデジタル微差圧計 EMD−8」が適用されている。 An unillustrated pipe for exhausting a part of the hot air to the outside of the furnace 1 (that is, the exhaust means) is driven by a variable speed motor, and the exhaust fan 14 for exhausting the hot air to the outside of the furnace 1 and the motor. The inverter control device 15 for controlling the rotational speed of the furnace 1 is configured such that the pressure difference signal between the inside of the furnace 1 and the outside of the furnace 1 detected by the fine differential pressure gauge 13 is input to the inverter control device 15. It has become. Based on this pressure difference signal, the inverter control device 15 is operated to control the rotational speed of the motor, whereby the exhaust air volume of the exhaust fan 14 is less than the air volume (4 m 3 / min) of the intake system shown below. The inside of the furnace 1 is finely adjusted (4 m 3 / min−α) so as to be maintained at a slightly positive pressure (the pressure inside the furnace 1 is, for example, 10 Pa higher than that outside the furnace 1). In this embodiment, “digital fine differential pressure gauge EMD-8 manufactured by Yamamoto Electric Co., Ltd.” is applied as the fine differential pressure gauge 13.

また、炉1内の上記処理室は、炉内の上方側に設けられた上部パンチングプレート12と炉内の下方側に設けられた下部パンチングプレート11とで区画された処理空間を有しており、上記上部パンチングプレート12を介して処理空間内に熱風が均一に導入されると共に、上記下部パンチングプレート11を介して処理空間内の熱風が炉外へ均一に排気されるようになっている。   The processing chamber in the furnace 1 has a processing space defined by an upper punching plate 12 provided on the upper side in the furnace and a lower punching plate 11 provided on the lower side in the furnace. The hot air is uniformly introduced into the processing space through the upper punching plate 12, and the hot air in the processing space is uniformly exhausted outside the furnace through the lower punching plate 11.

更に、処理空間内の上部パンチングプレート12と下部パンチングプレート11の各近傍には、図2に示すように複数の上部ローラ8群と下部ローラ8群がそれぞれ一列に配置され、かつ、上記開口部(フィルム搬入口)9から処理空間内に搬入された長尺フィルム7が上部ローラ8群と下部ローラ8群を交互に経由して上記開口部(フィルム搬出口)9から処理空間外へ搬出されるように構成されており、上記給気手段のHEPAフィルター等のエアーフィルター4を介し処理空間内に供給される清浄化された熱風により長尺フィルム7の連続加熱処理が行われるようになっている。   Further, in the vicinity of the upper punching plate 12 and the lower punching plate 11 in the processing space, a plurality of upper roller 8 groups and lower roller 8 groups are respectively arranged in a row as shown in FIG. The long film 7 carried into the processing space from the (film carry-in port) 9 is carried out of the processing space from the opening (film carry-out port) 9 via the upper roller 8 group and the lower roller 8 group alternately. The long film 7 is continuously heated by the purified hot air supplied into the processing space through the air filter 4 such as the HEPA filter of the air supply means. Yes.

尚、図2中、符号5は入気系の配管に付設されてフレッシュエアーの取り込み量を調整するダンパー、符号6は戻り系の配管に付設されて循環用に供される熱風量を調整するダンパーを示しており、実施例に係る装置を用いて長尺フィルム7の連続加熱を行う場合、各ダンパー5、6を絞り込んで上記取り込み量(すなわち、入気系の風量)を4m3/min(熱風循環量の20%に相当する)に固定すると共に、循環用に供される熱風量(すなわち、戻り系の風量)を16m3/min(熱風循環量の80%に相当する)に固定し、これにより熱風の循環量が20m3/minに設定されている。 In FIG. 2, reference numeral 5 is a damper attached to the inlet piping to adjust the intake amount of fresh air, and reference numeral 6 is attached to the return piping to adjust the amount of hot air supplied for circulation. In the case where the long film 7 is continuously heated using the apparatus according to the embodiment, the dampers 5 and 6 are squeezed to reduce the intake amount (that is, the air volume of the intake system) to 4 m 3 / min. (The amount of hot air circulated is fixed to 20%) and the amount of hot air supplied for circulation (that is, the amount of return air) is fixed to 16 m 3 / min (corresponding to 80% of the amount of hot air circulated). As a result, the circulation rate of hot air is set to 20 m 3 / min.

そして、この実施例に係る連続加熱装置によれば、上記炉1内と炉1外との圧力差を検出する微差圧計13が設けられており、この微差圧計13で検出された炉1内と炉1外との圧力差信号がインバーター制御装置15に入力され、この圧力差信号に基づきインバーター制御装置15が作動して排気ファン14の排気風量を入気系の風量(4m3/min)より少なくなるように微調整(4m3/min−α)し、これにより炉1内を微正圧(炉1内の圧力が炉1外の圧力より10Pa高い)に維持している。 And according to the continuous heating apparatus which concerns on this Example, the fine differential pressure gauge 13 which detects the pressure difference between the said furnace 1 and the outside of the furnace 1 is provided, The furnace 1 detected with this fine differential pressure gauge 13 A pressure difference signal between the inside and the outside of the furnace 1 is input to the inverter control device 15, and the inverter control device 15 is operated based on this pressure difference signal, and the exhaust air volume of the exhaust fan 14 is changed to the air volume (4 m 3 / min of the intake system). ) Fine adjustment (4 m 3 / min−α) is performed so as to reduce the pressure, thereby maintaining the inside of the furnace 1 at a slightly positive pressure (the pressure inside the furnace 1 is 10 Pa higher than the pressure outside the furnace 1).

従って、炉1外の塵等を含んだ汚染空気がフィルム搬入口や搬出口を構成する開口部9から炉1内に流入してしまうことがなく、かつ、上記微正圧(炉1内の圧力が炉1外の圧力より10Pa高い)に起因して炉1外へ極少量流れ出る風により上記開口部9近傍を搬送される長尺フィルム7がバタバタと揺れ動いてしまうこともないため、フィルム7へ強いテンション(張力)を加えることなく安定したフィルム7の搬送が可能となり、更に、フィルム7に強いテンション(張力)を加える必要がないことからフィルム7内部に応力が残ることもないため、最終製品にしたときにフィルム7が反ってしまうといった問題も解消される。   Therefore, the contaminated air containing dust and the like outside the furnace 1 does not flow into the furnace 1 from the opening 9 constituting the film carry-in port and the carry-out port, and the fine positive pressure (in the furnace 1) Since the long film 7 transported in the vicinity of the opening 9 is not shaken by the wind that flows out to the outside of the furnace 1 due to the pressure being 10 Pa higher than the pressure outside the furnace 1, the film 7 The film 7 can be transported stably without applying a strong tension (tension), and since there is no need to apply a strong tension (tension) to the film 7, no stress remains in the film 7. The problem that the film 7 warps when made into a product is also solved.

本発明に係る連続加熱装置によれば、塵等を含んだ汚染空気がフィルム搬入口や搬出口を構成する開口部から炉内に流入してしまうことがなく、かつ、上記開口部近傍を搬送される長尺フィルムがバタバタと揺れ動いてしまうこともないためフィルムへ強いテンション(張力)を加えることなく安定したフィルムの搬送が可能となる。従って、樹脂フィルム、エンプラフィルム等の熱処理に利用される産業上の利用可能性を有している。   According to the continuous heating apparatus according to the present invention, contaminated air containing dust or the like does not flow into the furnace from the openings constituting the film carry-in port and the carry-out port, and is transported in the vicinity of the opening. Since the long film to be swayed does not shake, the film can be stably conveyed without applying a strong tension. Therefore, it has industrial applicability used for heat treatment of resin films, engineering plastic films and the like.

1 炉
2 ヒータ
3 送風機(ブロアー)
4 エアーフィルター
5 入気系のダンパー
6 戻りのダンパー
7 長尺フィルム
8 ローラ群
9 開口部
10 排気系のダンパー
11 下部パンチングプレート
12 上部パンチングプレート
13 微差圧計
14 排気ファン
15 インバーター制御装置
1 furnace 2 heater 3 blower
DESCRIPTION OF SYMBOLS 4 Air filter 5 Intake system damper 6 Return damper 7 Long film 8 Roller group 9 Opening part 10 Exhaust system damper 11 Lower punching plate 12 Upper punching plate 13 Fine differential pressure gauge 14 Exhaust fan 15 Inverter control device

Claims (3)

送風機とヒータおよびエアーフィルターを有する給気手段を経由して炉内に供給される熱風が循環し、一部の熱風が排気手段を経由して炉内から炉外へ排気されると共に、炉本体のフィルム搬入口から炉内に搬入されフィルム搬出口から炉外へ搬出される長尺フィルムに対し炉内の処理室において熱風による連続加熱処理を行い、かつ、上記熱風の循環量が、上記排気手段を経由せずに炉内から炉外へ排気されて上記給気手段の入気口側に戻される戻り系の風量と、炉外から上記給気手段の入気口側に新たに導入される入気系の風量との合計量にて構成される長尺フィルムの連続加熱装置において、
上記炉内と炉外との圧力差を検出する微差圧計を炉本体に設け、微差圧計で検出された圧力差に基づき上記排気手段により排気する風量を入気系の風量より少なく微調整して、炉内を微正圧に維持することを特徴とする長尺フィルムの連続加熱装置。
Hot air supplied into the furnace via the air supply means having a blower, a heater and an air filter circulates, and part of the hot air is exhausted from the inside of the furnace to the outside of the furnace via the exhaust means, and the furnace body The long film carried into the furnace from the film carry-in port and carried out from the film carry-out port to the outside of the furnace is subjected to continuous heat treatment with hot air in the treatment chamber in the furnace, and the circulation amount of the hot air is A return air volume that is exhausted from the inside of the furnace to the outside of the furnace without passing through the means and returned to the inlet side of the air supply means, and newly introduced from the outside of the furnace to the inlet side of the air supply means. In the continuous heating device for long films composed of the total amount of airflow of the inlet system
A fine differential pressure gauge that detects the pressure difference between the inside of the furnace and the outside of the furnace is provided in the furnace body, and the air volume exhausted by the exhaust means based on the pressure difference detected by the fine differential pressure gauge is finely adjusted to be less than the air volume of the inlet system. And the continuous heating apparatus of the long film characterized by maintaining the inside of a furnace at a fine positive pressure.
上記排気手段が、回転速度可変モータで駆動する排気ファンと上記モータの回転速度を制御するインバーター制御装置とで構成されていることを特徴とする請求項1に記載の長尺フィルムの連続加熱装置。   2. The continuous heating device for a long film according to claim 1, wherein the exhaust means comprises an exhaust fan driven by a rotational speed variable motor and an inverter control device for controlling the rotational speed of the motor. . 炉内の上記処理室が、炉内の上方側に設けられた上部パンチングプレートと炉内の下方側に設けられた下部パンチングプレートとで区画された処理空間を有し、上記上部パンチングプレートを介して処理空間内に熱風が導入されかつ上記下部パンチングプレートを介して処理空間内の熱風が炉外へ排気されると共に、処理空間内の上部パンチングプレートと下部パンチングプレートの各近傍にそれぞれ一列に配置された複数の上部ローラ群と下部ローラ群を交互に経由させて上記長尺フィルムが処理空間内を搬送されるようになっていることを特徴とする請求項1または2に記載の長尺フィルムの連続加熱装置。   The processing chamber in the furnace has a processing space defined by an upper punching plate provided on the upper side of the furnace and a lower punching plate provided on the lower side of the furnace, and the processing chamber is interposed via the upper punching plate. The hot air is introduced into the processing space, and the hot air in the processing space is exhausted to the outside of the furnace through the lower punching plate, and is arranged in a row near each of the upper punching plate and the lower punching plate in the processing space. The long film according to claim 1 or 2, wherein the long film is conveyed in the processing space through a plurality of upper roller groups and lower roller groups alternately. Continuous heating device.
JP2011114880A 2011-05-23 2011-05-23 Apparatus for continuously heating long film Pending JP2012240370A (en)

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