JPS6370246A - Coating and drying method for band-shaped material - Google Patents

Coating and drying method for band-shaped material

Info

Publication number
JPS6370246A
JPS6370246A JP21277286A JP21277286A JPS6370246A JP S6370246 A JPS6370246 A JP S6370246A JP 21277286 A JP21277286 A JP 21277286A JP 21277286 A JP21277286 A JP 21277286A JP S6370246 A JPS6370246 A JP S6370246A
Authority
JP
Japan
Prior art keywords
coating
inert gas
oven
solvent
coating chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP21277286A
Other languages
Japanese (ja)
Inventor
Masaharu Ogawa
小川 正春
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujifilm Holdings Corp
Original Assignee
Fuji Photo Film Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Photo Film Co Ltd filed Critical Fuji Photo Film Co Ltd
Priority to JP21277286A priority Critical patent/JPS6370246A/en
Priority to DE19873730651 priority patent/DE3730651A1/en
Publication of JPS6370246A publication Critical patent/JPS6370246A/en
Pending legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/74Applying photosensitive compositions to the base; Drying processes therefor
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/74Applying photosensitive compositions to the base; Drying processes therefor
    • G03C2001/7451Drying conditions

Abstract

PURPOSE:To reduce the size of a device and to permit the economization in the quantity of heat and the improvement in a coating stage by cooling an inert gas supplied into an oven and coating chamber successively provided adjacently to each other and recirculating an org. solvent after condensing and recovering said solvent. CONSTITUTION:A band-shaped material 1 on which a coating liquid 4 is coated in the coating chamber 11 is dried in the oven 5 adjacent to said chamber. The inert gas is supplied from an inert gas supplying device 26 through feed ports 9, 12 into both the chambers 11, 5 to dry the band-shaped material while said material is kept run. The gas is discharged from discharge ports 10, 13 and is introduced into a condenser 16 where the combustible org. solvent in the coating liquid is condensed and recovered. The remaining inert gas is introduced into a pipeline of the gas supplying device 26 and is recirculated. The size of the device is thus reduced without requiring diluting air. The quantity of heat is thereby economized and the uniformly coated surface is obtd., by which the recovery rate of the solvent is increased.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、例えば長尺のプラスチック製支持体に塗液を
塗布して乾燥することにより写真感光材料を製造する際
の乾燥工程を改良するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention improves the drying process when producing photographic materials, for example, by applying a coating liquid to a long plastic support and drying it. It is something.

〔従来の技術〕[Conventional technology]

プラスチックシートあるいは紙などの長尺の支持体に各
種の積層あるいはコーティングを行なう写真感光材料そ
の他各種の製品は一般に所定の成分を有機溶剤に溶解あ
るいは分散した塗液を支持体に塗布し、これを乾燥する
ことにより製造されている。
Photographic light-sensitive materials and various other products in which various types of lamination or coating are applied to a long support such as a plastic sheet or paper are generally produced by coating the support with a coating liquid in which predetermined components are dissolved or dispersed in an organic solvent. It is produced by drying.

この乾燥方法としては、従来は、塗液を塗布した支持体
に熱風を吹き付けたり赤外線を照射したりする方法が一
般に採用されてきた。このような乾燥方法においては、
オーブン内で気化薄光した溶剤が高濃度になって爆発す
るため大量の空気をオーブン内に供給して溶剤濃度を爆
発下限の約1/3以下に抑えるようにコントロールされ
ていた。
Conventionally, this drying method has generally been carried out by blowing hot air onto the support coated with the coating liquid or by irradiating it with infrared rays. In this drying method,
The solvent vaporized in the oven becomes highly concentrated and explodes, so a large amount of air was supplied into the oven to keep the solvent concentration below about 1/3 of the lower explosive limit.

その結果、溶剤を蒸発させるエネルギーに加えて、この
希釈用空気の加熱さらには多量の排ガスの焼却処理にも
熱エネルギーを消費せざるを得なかった。
As a result, in addition to the energy required to evaporate the solvent, thermal energy must be consumed to heat the dilution air and incinerate a large amount of exhaust gas.

従来から、この問題を解決するため種々の秒針が行なわ
れ、例えば熱交換器を設けて排ガスの焼却により発生し
た熱を回収する方法及び溶剤を有機溶剤から水に変える
方法などが提案されている。
In the past, various methods have been proposed to solve this problem, such as installing a heat exchanger to recover the heat generated by incinerating exhaust gas, and changing the solvent from organic solvent to water. .

一方、乾燥工程においてオーブン内に不活性ガスの熱風
を吹き込むことによって溶剤の爆発を防止し希釈用空気
を不要にする方法が知られている(特公昭55−363
89号公報)、この方法においては排ガスに含まれる有
機溶剤を冷却凝縮してとりのぞき、その残りの排ガス(
不活性ガス)をオーブン内に循環させることにより前記
爆発を防いでいる。
On the other hand, a method is known in which hot inert gas air is blown into the oven during the drying process to prevent the solvent from exploding and eliminate the need for diluting air (Japanese Patent Publication No. 55-363
In this method, the organic solvent contained in the exhaust gas is removed by cooling and condensation, and the remaining exhaust gas (No. 89) is removed.
This explosion is prevented by circulating an inert gas (inert gas) through the oven.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

排ガスの燃焼熱を熱交換器で回収する方法は熱交換によ
る熱の回収率は50〜60%程度にすぎず、また熱交換
器に大容量のものが必要な為設備コストがかかって充分
な解決策とはいえないものであった。
In the method of recovering the combustion heat of exhaust gas using a heat exchanger, the heat recovery rate by heat exchange is only about 50 to 60%, and the heat exchanger requires a large capacity, so the equipment cost is high and it is not sufficient. It was not a solution.

また、溶剤に水を用いる方法は水を蒸発させるためにか
えって熱エネルギーの消費量がふえ、不適当であった。
In addition, the method of using water as a solvent is unsuitable because the amount of thermal energy consumed increases to evaporate the water.

不活性ガスのなかで乾燥させる方法も時折塗布の均一性
に問題を生じることがあった。
Drying in an inert gas also sometimes caused problems with coating uniformity.

本発明の目的は、このような問題点を解決して乾燥設備
をコンパクトにしかつ熱エネルギーの消費量を節減する
とともに塗布工程を改善した、帯状物の塗布、乾燥手段
を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a means for coating and drying a strip, which solves these problems, makes the drying equipment compact, reduces thermal energy consumption, and improves the coating process.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者はこのような目的を達成するべく鋭意検討を行
なった結果、塗布及び乾燥をいずれも不活性ガスで満た
された室内で行なうとともにこれらの室から排出される
排ガスから有機溶剤を回収してこれを循環供給すること
により、装置全体をコンパクトにし、かつ品質の均一性
の高い帯状物を安定して製造しうる等の数々の利点を見
出して本発明を完成するに至った。
As a result of intensive studies to achieve this purpose, the inventor of the present invention has developed a method in which coating and drying are both carried out in a room filled with inert gas, and organic solvents are recovered from the exhaust gas discharged from these rooms. By circulating and supplying this material, the present invention was completed based on the discovery of numerous advantages such as making the entire apparatus compact and stably producing strips of highly uniform quality.

すなわち本発明は、帯状支持体を走行させつつ可燃性有
機溶剤を含む塗液を塗布してこれを乾燥するにあたり、
該塗液を塗布する装置を塗布室内に設置するとともに乾
燥オーブンを該塗布室内に連設し、該オーブン及び該塗
布室内に不活性ガスを供給し、これらから排出される不
活性ガスを冷却してそこに含まれている前記有機溶剤を
凝縮回収し、残った不活性ガスを前記オーブン及び前記
塗布室内へ循環させることを特徴とする帯状物の塗布、
乾燥方法に関するものである。
That is, in the present invention, when applying a coating liquid containing a flammable organic solvent and drying it while running a belt-shaped support,
A device for applying the coating liquid is installed in a coating chamber, a drying oven is connected to the coating chamber, an inert gas is supplied into the oven and the coating chamber, and the inert gas discharged from these is cooled. coating the strip, characterized in that the organic solvent contained therein is condensed and recovered, and the remaining inert gas is circulated into the oven and the coating chamber;
This relates to a drying method.

帯状物の種類は特に制限されるものではなく、各種プラ
スチックシートあるいは紙等の支持体に用途に応じて必
要な成分が加燃性有機溶剤に溶解あるいは分散された塗
液が塗布されているものである。
There are no particular restrictions on the type of band-shaped product, and it is one in which a coating liquid in which the necessary components are dissolved or dispersed in a flammable organic solvent is applied to a support such as various plastic sheets or paper, depending on the purpose. It is.

可燃性有機溶剤は溶解あるいは分散する成分などに応じ
て適当なものが選択されるが、例えばベンゼン、トルエ
ン、アルコール、アセトン、酢酸メチル、メチレングリ
コールなどである。
An appropriate flammable organic solvent is selected depending on the components to be dissolved or dispersed, and examples thereof include benzene, toluene, alcohol, acetone, methyl acetate, and methylene glycol.

塗液を塗布する装置は通常の装置を用いればよい。この
塗布装置は周囲を不活性ガス雰囲気に保つために密閉ケ
ーシングで形成された塗布室内に設置する。塗液は原則
としてこの塗布室の外で調製して塗布装置へは配管を介
して供給する。ケーシングにはそのほか支持体の入口及
び出口、不活性ガスの送風口及び排風口などを設ける、
支持体の入口及び出口は不活性ガスの漏出を少なくする
ために最小限の開口にとどめるのがよい。入口を通過す
る支持体にはまだ塗液が塗布されていないので対ロール
などを設けて密閉構造とすることが好ましい。
A conventional device may be used for applying the coating liquid. This coating device is installed in a coating chamber formed by a sealed casing in order to maintain an inert gas atmosphere around it. In principle, the coating liquid is prepared outside the coating chamber and supplied to the coating device via piping. In addition, the casing is provided with an inlet and an outlet for the support, an inert gas outlet and an exhaust outlet, etc.
The openings at the inlet and outlet of the support should be kept to a minimum in order to reduce leakage of inert gas. Since the coating liquid has not yet been applied to the support passing through the inlet, it is preferable to provide a pair of rolls or the like to create a sealed structure.

塗布室には乾燥オーブンを連設する。この乾燥オーブン
も密閉構造とし、帯状物の入口及び出口は不活性ガスの
漏出を少なくするため最小限の開口にとどめるようにす
る。
A drying oven is installed in the coating room. This drying oven also has a closed structure, and the openings at the inlet and outlet of the strip are kept to a minimum in order to reduce leakage of inert gas.

不活性ガスはその雰囲気内における燃焼を阻止しうるガ
スであり、例えば窒素ガス、炭酸ガスなどである。オー
ブンに吹き込まれる不活性ガスの温度及び風量は要は帯
状物を所定の程度まで乾燥しうるように設定され、帯状
物の種類、ザイズ及び走行速度、有機溶剤の種類などを
考慮して適当になるように設定される。オーブン内に赤
外線ヒータ等を補助熱源として配設することもできる。
The inert gas is a gas that can inhibit combustion in the atmosphere, such as nitrogen gas or carbon dioxide gas. The temperature and air volume of the inert gas blown into the oven are set so that the strip can be dried to a predetermined degree, and are set appropriately by taking into consideration the type of strip, size and running speed, type of organic solvent, etc. It is set so that An infrared heater or the like may also be provided within the oven as an auxiliary heat source.

塗布室に吹き込まれる不活性ガスは塗液の状態を一定に
保つことを目的としている。温度が低すぎては塗液成分
の析出等の問題を生じ、一方高ずぎては溶剤の蒸発量が
多くなるところから不活性ガスの温度はその中間で一定
に保たれるように設定する。風量も室内を一定条件に保
ちうる範囲でなるべく少なくすることが溶剤の蒸発量を
少なくする点で好ましい。オーブンから塗布室への伝熱
量を少なくするためにその間に断熱材等の断熱機構を設
けることが望ましい。
The purpose of the inert gas blown into the coating chamber is to maintain a constant state of the coating liquid. If the temperature is too low, problems such as precipitation of coating liquid components will occur, while if it is too high, the amount of solvent will evaporate, so the temperature of the inert gas should be set so as to be kept constant in the middle. . It is preferable to reduce the amount of airflow as much as possible within a range that can maintain a constant indoor condition in order to reduce the amount of solvent evaporation. In order to reduce the amount of heat transferred from the oven to the coating chamber, it is desirable to provide a heat insulating mechanism such as a heat insulating material therebetween.

不活性ガスをオーブン及び塗布室内に吹き込むため送風
機を設け、一方オーブン及び塗布室内から排出させるた
めに排風機を設ける。オーブンあるいは塗布室の大きさ
等により送風機及び排風機の一方を省略できることはい
うまでもない。
A blower is provided to blow inert gas into the oven and coating chamber, while an exhaust fan is provided to exhaust the inert gas from the oven and coating chamber. It goes without saying that either the blower or the exhaust fan can be omitted depending on the size of the oven or coating chamber.

該オーブン及び塗布室から排出されるガスには蒸発した
有機溶剤の蒸気が高濃度で含まれている。
The gas discharged from the oven and coating chamber contains a high concentration of evaporated organic solvent vapor.

そこで、この排出ガスをまず冷却して有機溶剤蒸気を凝
縮させ、これを回収する。この凝縮は一般の有機溶剤蒸
気を冷却凝縮させる通常の装置を用いて行なえばよい。
Therefore, the exhaust gas is first cooled to condense the organic solvent vapor and then recovered. This condensation may be carried out using a conventional device for cooling and condensing organic solvent vapor.

次に、凝縮器から排出される不活性ガスはオーブン内及
び塗布室内に循環させる。凝縮器とオーブンの間及び凝
縮器と塗布室の間には不活性ガスを加熱ヒーター、さら
に防塵装置及び前記の送風機などを適宜設ける。
The inert gas discharged from the condenser is then circulated within the oven and into the coating chamber. Between the condenser and the oven and between the condenser and the coating chamber, a heater for heating an inert gas, a dust prevention device, the above-mentioned blower, and the like are provided as appropriate.

本発明の方法の実施に利用される乾燥装置は上述の説明
かられかるようにほぼ密閉系であり、不活性ガスの循環
回路を有するものである。
As can be seen from the above description, the drying apparatus used to carry out the method of the present invention is a substantially closed system, and has an inert gas circulation circuit.

〔作 用〕[For production]

本発明の方法においては、塗布装置をケーシングで覆っ
て塗布を不活性ガス雰囲気中で行なわせることによって
溶剤の高濃度蒸気下での塗布を可能にし、溶剤の蒸発を
減少させて塗布条件の一定化を達成している。また、乾
燥を不活性ガス雰囲気中で行わせることによって蒸発し
た溶剤蒸気の爆発を防止し、オーブン内の高濃度状態を
可能にしている。
In the method of the present invention, the coating device is covered with a casing and coating is performed in an inert gas atmosphere, thereby enabling coating under high concentration vapor of the solvent, reducing evaporation of the solvent, and maintaining constant coating conditions. has been achieved. Further, by performing drying in an inert gas atmosphere, explosion of the evaporated solvent vapor is prevented and a high concentration state in the oven is made possible.

〔実施例〕〔Example〕

第1図は本発明の方法に利用される塗布、乾燥装置の一
例をフローシートで示したものである。
FIG. 1 is a flow sheet showing an example of a coating and drying apparatus used in the method of the present invention.

図示のように、帯状物1は原反ロール2から繰出され、
公知の塗布装置3で塗液4が塗布される。
As shown in the figure, a strip 1 is unwound from a raw roll 2,
A coating liquid 4 is applied using a known coating device 3 .

そして、オーブン5内で乾燥され巻取ロール6に巻取ら
れる。オーブン5は長面状の密閉形のものであり、長手
方向の両端面には帯状物1が通るスリット状開ロア、7
′が設けられている。オーブン5の上面には不活性ガス
の送風口9及び排風口10が設けられている。
Then, it is dried in an oven 5 and wound onto a winding roll 6. The oven 5 is a long-sided sealed type, and has a slit-shaped open lower 7 on both end faces in the longitudinal direction, through which the strip 1 passes.
' is provided. An inert gas outlet 9 and an exhaust outlet 10 are provided on the upper surface of the oven 5.

塗布装置3はオーブン5に連設された塗布室11の中に
おさめられている。塗布室の上面には不活性ガスの送風
口12と排風口13が設けられている。又、塗布装置と
原反ロールとの間には対ロールの密閉装置8が設けられ
ている。排風口10からは排風機14を介して凝縮機1
6に配管されている。同様に排風口13からは排風機1
5を介して凝縮器16に配管されている。17は凝縮器
16に冷媒を送る冷却機であり、18は凝縮した溶剤の
受槽である。凝縮器から出る排ガスのうち一つの系は防
塵装置19、加熱ヒーター20及び送風機21と経由し
て送風口9に接続されている。別の一つの系は防塵装置
22加熱ヒーター23及び送風機24を経由して送風口
12に接続されている。オーブン5からは防塵装置と凝
縮器との間の配管にフィードバック配管25が設けられ
、オーブン内の不活性ガスを循環させることにより、熱
エネルギーを節約している。26は不活性ガスを補給す
るためのガス供給装置である。
The coating device 3 is housed in a coating chamber 11 connected to the oven 5. An inert gas outlet 12 and an exhaust outlet 13 are provided on the upper surface of the coating chamber. Further, a sealing device 8 for the pair of rolls is provided between the coating device and the original roll. From the exhaust port 10, the condenser 1 is connected via the exhaust fan 14.
6. Similarly, from the exhaust port 13, the exhaust fan 1
5 to a condenser 16. 17 is a cooler that sends refrigerant to the condenser 16, and 18 is a receiving tank for the condensed solvent. One system of exhaust gas coming out of the condenser is connected to the air outlet 9 via a dust prevention device 19, a heating heater 20, and an air blower 21. Another system is connected to the air outlet 12 via a dust prevention device 22, heater 23, and blower 24. Feedback piping 25 is provided from the oven 5 to the piping between the dust prevention device and the condenser, and by circulating inert gas within the oven, thermal energy is saved. 26 is a gas supply device for replenishing inert gas.

ポリエチレンテレフタレートを支持体としてこれに感光
性ジアゾ化合物、光重合性組成物等をアセトンに溶解し
た塗液4を塗布した帯状物1をこのような装置で乾燥し
た。オーブン内の温度は90℃そして塗布室内の温度は
30°Cとし、オーブン5及び塗布室11からの排出ガ
スに含まれている溶剤の95%を凝縮器16で回収した
。帯状物は完全に乾燥され、品質も一定であって特にト
ラブルもなく運転を継続できた。
A strip 1 was coated with a coating liquid 4 in which a photosensitive diazo compound, a photopolymerizable composition, etc. were dissolved in acetone using polyethylene terephthalate as a support, and was dried using such an apparatus. The temperature inside the oven was 90° C. and the temperature inside the coating chamber was 30° C., and 95% of the solvent contained in the exhaust gas from the oven 5 and the coating chamber 11 was recovered in the condenser 16. The strips were completely dried, the quality was constant, and operation continued without any particular trouble.

〔発明の効果〕〔Effect of the invention〕

本発明の方法は希釈空気も必要とせず、従って、循環系
全体をコンパクトにできる。得られる帯状物の塗布も一
定であり、均質のものを安定して得ることができる。オ
ーブン及び塗布室からも排ガス中の有機溶剤を回収する
ので溶剤の回収率を高めることができる。また回収した
溶剤を再利用しあるいは他に有効利用することができる
The method of the invention also does not require dilution air, thus making the entire circulation system compact. The coating of the resulting strip is also constant, and a homogeneous product can be stably obtained. Since the organic solvent in the exhaust gas is also recovered from the oven and the coating chamber, the recovery rate of the solvent can be increased. In addition, the recovered solvent can be reused or used for other purposes.

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

第1図は本発明の方法に使用される乾燥装置の一例をフ
ローシートで示したものである。 1・・・帯状物、3・・・塗布装置、4・・・塗液、5
・・・オーブン、11・・・塗布室、16・・・凝縮器
、26・・・不活性ガス供給装置。 特許出願人  冨士フィルム株式会社 代理人 弁理士  1) 中  政  浩(ほか1名) 手続ネ山正書(自発) 昭和62年3月30日 特許庁長官 黒 1)明 雄 殿 1 事件の表示 特願昭61−212772号 2 発明の名称 帯状物の塗布、乾燥方法 3 補正をする者 事件との関係   特許出願人 名称 (520)富士写真フィルム株式会社4代理人 居所 〒104東京都中央区八丁堀三丁目21番3−6
67号明細書の発明の詳細な説明の欄 6 補正の内容 (1)明細書の第5頁第5行の「加燃性」を「可燃性」
と訂正する。 (2)明細書の第7項第20行の「加熱」の後に「する
」を加入する。 以上
FIG. 1 is a flow sheet showing an example of a drying apparatus used in the method of the present invention. DESCRIPTION OF SYMBOLS 1... Band-shaped object, 3... Coating device, 4... Coating liquid, 5
...Oven, 11...Coating chamber, 16...Condenser, 26...Inert gas supply device. Patent Applicant Fuji Film Co., Ltd. Agent Patent Attorney 1) Masahiro Naka (and 1 other person) Prosecution Neyama Masashi (spontaneous) March 30, 1985 Commissioner of the Japan Patent Office Kuro 1) Tono Akihiro 1 Special indication of the case Application No. 61-212772 2 Name of the invention Method for coating and drying a strip 3 Relationship with the case of the person making the amendment Name of patent applicant (520) Fuji Photo Film Co., Ltd. 4 Agent residence Address: 3 Hatchobori, Chuo-ku, Tokyo 104 Chome 21-3-6
Column 6 of Detailed Description of the Invention in Specification No. 67 Contents of amendment (1) Changed “flammability” from line 5 on page 5 of the specification to “combustible”
I am corrected. (2) Add "do" after "heating" in paragraph 7, line 20 of the specification. that's all

Claims (1)

【特許請求の範囲】[Claims] 帯状支持体を走行させつつ可燃性有機溶剤を含む塗液を
塗布してこれを乾燥するにあたり、該塗液を塗布する装
置を塗布室内に設置するとともに乾燥オーブンを該塗布
室に連設し、該オーブン及び該塗布室内に不活性ガスを
供給し、これらから排出される不活性ガスを冷却してそ
こに含まれている前記有機溶剤を凝縮回収し、残った不
活性ガスを前記オーブン及び前記塗布室内へ循環させる
ことを特徴とする帯状物の塗布、乾燥方法
When applying and drying a coating liquid containing a flammable organic solvent while running a strip support, a device for applying the coating liquid is installed in a coating chamber, and a drying oven is connected to the coating chamber, An inert gas is supplied into the oven and the coating chamber, the inert gas discharged from these is cooled, the organic solvent contained therein is condensed and recovered, and the remaining inert gas is transferred to the oven and the coating chamber. A method for coating and drying a strip, characterized by circulating the material into a coating chamber.
JP21277286A 1986-09-11 1986-09-11 Coating and drying method for band-shaped material Pending JPS6370246A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP21277286A JPS6370246A (en) 1986-09-11 1986-09-11 Coating and drying method for band-shaped material
DE19873730651 DE3730651A1 (en) 1986-09-11 1987-09-11 Method for applying a coating solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21277286A JPS6370246A (en) 1986-09-11 1986-09-11 Coating and drying method for band-shaped material

Publications (1)

Publication Number Publication Date
JPS6370246A true JPS6370246A (en) 1988-03-30

Family

ID=16628137

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21277286A Pending JPS6370246A (en) 1986-09-11 1986-09-11 Coating and drying method for band-shaped material

Country Status (2)

Country Link
JP (1) JPS6370246A (en)
DE (1) DE3730651A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102229678A (en) * 2011-05-17 2011-11-02 内蒙古阜丰生物科技有限公司 Drying method applied to xanthan gum production

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE9000821U1 (en) * 1990-01-25 1990-04-26 Enowa, Eberhard Nowak, 8037 Olching, De
DE4023442A1 (en) * 1990-07-24 1992-01-30 Pagendarm Gmbh METHOD AND DEVICE FOR DRYING A COATED SUBSTRATE RAIL
DE4143025A1 (en) * 1991-12-24 1993-07-01 Werzalit Ag & Co Method for spray-painting of objects using paint mist - has objects in spray booth during spraying, those not to be painted are kept at lower temp. than dew point of mist which is later sucked out of booth and recycled
GB2311484A (en) * 1996-03-27 1997-10-01 Viscofil Consolidated Corp Solvent recovery in dope spinning process
DE102004025528B4 (en) * 2004-05-25 2010-03-04 Eisenmann Anlagenbau Gmbh & Co. Kg Method and apparatus for drying coated articles

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5214636A (en) * 1975-06-06 1977-02-03 Eastman Kodak Co Method of appication
JPS5225728A (en) * 1975-08-22 1977-02-25 Ciba Geigy Ag Thiocarbamate*process for preparing same and pesticide containing said compound
JPS5536389A (en) * 1978-08-30 1980-03-13 Dynamit Nobel Ag Method and apparatus for producing monofilament from polyfluorinatedvinylidene

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5214636A (en) * 1975-06-06 1977-02-03 Eastman Kodak Co Method of appication
JPS5225728A (en) * 1975-08-22 1977-02-25 Ciba Geigy Ag Thiocarbamate*process for preparing same and pesticide containing said compound
JPS5536389A (en) * 1978-08-30 1980-03-13 Dynamit Nobel Ag Method and apparatus for producing monofilament from polyfluorinatedvinylidene

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102229678A (en) * 2011-05-17 2011-11-02 内蒙古阜丰生物科技有限公司 Drying method applied to xanthan gum production

Also Published As

Publication number Publication date
DE3730651A1 (en) 1988-03-17

Similar Documents

Publication Publication Date Title
US4894927A (en) Process for drying coated web
US4051278A (en) Method for reducing mottle in coating a support with a liquid coating composition
US4926567A (en) Process and apparatus for drying coated web
US5881476A (en) Apparatus and method for drying a coating on a substrate employing multiple drying subzones
US7526878B2 (en) Method and apparatus for drying coating film and method for producing optical film
US4979965A (en) Method of dehumidifying gases
US6481118B1 (en) Dryer with integrated cooling unit and method of operation
EP0890067A1 (en) Apparatus and method for drying a coating on a substrate
JPS6370246A (en) Coating and drying method for band-shaped material
CA1279482C (en) Air conditioning process and apparatus therefor
US4484396A (en) Oxygen reduction system and condenser apparatus with automatic defrost
FI73144B (en) FOERFARANDE FOER AVFUKTNING AV VAOTLUFT ELLER MAETTAD AONGA.
JPS5953530B2 (en) Photosensitive material manufacturing equipment
US11040553B2 (en) Method and device for drying a printed recording medium
JPH05202496A (en) Method and device for sealing treatment of base for lithographic printing plate
US4864830A (en) Air conditioning process and apparatus
JPH03217215A (en) Gas recovery system
JPS627472A (en) Method and drying strip like article
JPS6370247A (en) Drying method for band-shaped material
JPH0233515B2 (en) OBIJOINSATSUBUTSUNOKANSOSOCHI
JP2794290B2 (en) Paint drying equipment
KR20000070316A (en) Absorption refrigerating system and working mixture for said system
TWI679097B (en) Method and device for manufacturing solvent-based film or solvent-based film
JPH1157577A (en) Drying device for solvent-containing material to be treated
WO2023032250A1 (en) Drying system