JPH0720570B2 - Web drying controller in dryer - Google Patents

Web drying controller in dryer

Info

Publication number
JPH0720570B2
JPH0720570B2 JP63164440A JP16444088A JPH0720570B2 JP H0720570 B2 JPH0720570 B2 JP H0720570B2 JP 63164440 A JP63164440 A JP 63164440A JP 16444088 A JP16444088 A JP 16444088A JP H0720570 B2 JPH0720570 B2 JP H0720570B2
Authority
JP
Japan
Prior art keywords
hot air
web
temperature
dryer
unit
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP63164440A
Other languages
Japanese (ja)
Other versions
JPH0214772A (en
Inventor
宗知 中村
暉宏 小川
義晃 星野
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.)
Mitsubishi Paper Mills Ltd
Original Assignee
Mitsubishi Paper Mills 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 Mitsubishi Paper Mills Ltd filed Critical Mitsubishi Paper Mills Ltd
Priority to JP63164440A priority Critical patent/JPH0720570B2/en
Publication of JPH0214772A publication Critical patent/JPH0214772A/en
Publication of JPH0720570B2 publication Critical patent/JPH0720570B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
    • F26B21/04Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B13/00Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06Controlling, e.g. regulating, parameters of gas supply
    • F26B21/08Humidity
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06Controlling, e.g. regulating, parameters of gas supply
    • F26B21/10Temperature; Pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/02Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/04Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour circulating over or surrounding the materials or objects to be dried

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Textile Engineering (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Drying Of Solid Materials (AREA)
  • Coating Apparatus (AREA)

Description

【発明の詳細な説明】 (A)産業上の利用分野 本発明はドライヤーの乾燥制御装置に関する。更に詳し
くはドライヤー内の走行ウエブの表面温度と熱風の温度
及び湿度を測定し、ウエブの乾燥状態を制御する制御装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION (A) Field of Industrial Application The present invention relates to a dryer drying controller. More specifically, the present invention relates to a control device that measures the surface temperature of a traveling web in a dryer and the temperature and humidity of hot air to control the dry state of the web.

(B)従来の技術 従来ドライヤーは、ウエブに塗工した塗液を乾燥した
り、含湿または含水ウエブを乾燥したり、ウエブを加熱
処理するために用いられている。
(B) Conventional Technology A conventional dryer is used for drying a coating liquid applied to a web, for drying a wet or water-containing web, and for heat-treating the web.

ウエブに塗液をコーターで塗布し、ドライヤーで熱風乾
燥する場合、熱風の温度が高く、熱風量が大きいと、走
行ウエブがドライヤー前半で乾燥終了し、ドライヤー後
半で過乾燥となり、塗布層の含水率が低下し、ひび割れ
たり、塗布面の反対側が熱収縮したりする。特にウエブ
の表面が熱可塑性樹脂である場合、表面が過剰の加熱に
より融解し、不都合な光沢が発生したりする。逆に乾燥
温度が低い場合とか、熱風量が少ない場合などは、未乾
燥のウエブがドライヤーから出てきて、ドライヤー以降
のロールを塗液で汚してしまう。このような状態をなく
すために従来とられてきたウエブの乾燥状態を管理する
手段は、ドライヤーから出て巻きとられた後、ロールの
上巻部より試料をサンプリングし、例えばウエブの塗布
量、塗布面質、光沢、含水率、表面抵抗等を評価し運転
中の乾燥装置の乾燥温度、湿度及び風量などの設定値を
決定し、目標品質に合った乾燥条件になるよう各々の設
定値を最適化している。具体的手段としては、実験から
得られたデータをもとに塗工スピード、塗工量に応じて
乾燥条件にかかわる例えばヒーターの蒸気バルブ、熱風
供給ファンの回転数、ダンパー開度等を設定し、乾燥後
にウエブの品質項目をチェックし、調節している。好ま
しくない品質の場合は、過去のデータをもとに再び条件
の設定変更をする。また前記手段よりもできるだけリア
ルタイムでウエブの状態を管理するためにドライヤー出
口にβ線坪量計等の電磁放射線厚み計測装置を設けた
り、熱風の温度検出器を設け、出力をアウトプットし、
監視作業をしている。このような方法では要求される品
質に合ったものを常に安定して製造することは難しい。
When applying the coating liquid to the web with a coater and drying with hot air with a dryer, if the temperature of the hot air is high and the amount of hot air is large, the running web will finish drying in the first half of the dryer and over dry in the latter half of the dryer, and the water content of the coating layer Rate decreases, cracks occur, and the opposite side of the coated surface shrinks due to heat. In particular, when the surface of the web is made of a thermoplastic resin, the surface is melted by excessive heating and an inconvenient gloss is generated. On the contrary, when the drying temperature is low or the amount of hot air is small, the undried web comes out of the dryer and the rolls after the dryer are soiled with the coating liquid. In order to eliminate such a state, conventionally used means for controlling the dry state of the web is to sample the sample from the upper winding part of the roll after being taken out from the dryer and wound, for example, the coating amount of the web, coating. Evaluate the surface quality, gloss, moisture content, surface resistance, etc. to determine the set values such as the drying temperature, humidity and air volume of the dryer during operation, and optimize each set value to achieve the drying conditions that match the target quality. It has become. As a concrete means, based on the data obtained from the experiment, set the coating speed, the drying condition according to the coating amount, for example, the steam valve of the heater, the rotation speed of the hot air supply fan, the damper opening, etc. After drying, the quality of the web is checked and adjusted. If the quality is unfavorable, the condition setting is changed again based on the past data. Further, in order to manage the state of the web as much as possible in real time than the above means, an electromagnetic radiation thickness measuring device such as a β-ray basis weight meter is provided at the dryer outlet, a hot air temperature detector is provided, and the output is output.
I am doing monitoring work. With such a method, it is difficult to always stably manufacture a product that meets the required quality.

(C)発明が解決すべき課題 しかし、前記手段ではドライヤー内でのウエブの温度が
わからず、また走行ウエブの速度を変える必要が出た
り、含水率の異る巻取をドライヤーにかけた場合とか、
途中から塗布量が変更された場合など、乾燥前のウエブ
の持つ水分量によって乾燥後のウエブの品質が異なって
しまい、設定変更が遅れると品質不良ウエブを生じてし
まう。
(C) Problems to be Solved by the Invention However, in the above-mentioned means, the temperature of the web in the dryer is not known, and it is necessary to change the speed of the traveling web, or when the dryer is wound with different water contents. ,
When the coating amount is changed midway, the quality of the dried web varies depending on the water content of the web before drying, and if the setting change is delayed, a poor quality web will occur.

本発明の解決すべき課題はウエブの走行スピードや乾燥
前のウエブの含水率あるいは塗工量等乾燥前のウエブの
条件が変っても乾燥後に一定の品質のウエブが得られる
ようウエブの乾燥を制御するドライヤー制御装置を提供
することにある。
The problem to be solved by the present invention is to dry the web so that a constant quality web can be obtained after drying even if the web condition before drying such as the running speed of the web, the moisture content of the web before drying or the coating amount changes. It is to provide a dryer control device for controlling.

(D)課題を解決するための手段 前述の課題を解決するため、以下の構成によって達成す
ることができた。
(D) Means for Solving the Problems In order to solve the above-mentioned problems, it was possible to achieve by the following configurations.

即ち、本発明は、走行ウエブ(2)に熱風を与える、ド
ライヤーフード(1)、熱風をウエブ(2)に吹付ける
複数のノズル(3)、ウエブ表面温度を測定する赤外線
放射温度測定器(8)を有するドライヤー部と、該ドラ
イヤー部に熱風を供給する、加熱器(4)、熱風供給フ
ァン(5)、外気取入ダンパー(6)、回収熱風排出ダ
ンパー(6b)、及び各々に連結した熱供給調節動力部
(4a)、熱風供給ファン駆動部(5a)、外気取入ダンパ
ー開度調節動力部(6a)、回収熱風排出ダンパー開度調
節動力部(6C)を有する熱風供給部と、前記ドライヤー
部と熱風供給部とを連繋する供給熱風温度湿度検出器
(9a)を有する熱風供給ダクト(7a)及び回収熱風温度
湿度検出器(9b)を有する熱風回収ダクト(7b)と、制
御部とからなり、該制御部がドライヤー内ウエブ表面温
度を測定する赤外線放射温度測定器(8)、供給、回収
熱風の温度、湿度を検出する温度湿度検出器(9a、9
b)、前記赤外線放射温度測定器(8)並びに温度湿度
検出器(9a、9b)によって検出された各々のアナログ信
号をデジタル信号に変換する変換器A(10)、前記デジ
タル信号がインプットされ乾燥制御演算を行う演算器
(11)及び該演算器(11)から出力されたデジタル信号
をインプットし、熱風供給部に、加熱温度の増減や熱風
の風量、外気取入ダンパー(6)や回収熱風排出ダンパ
ー(6b)の開度の変量を、熱風供給調節動力部(4a)、
熱風供給ファン駆動部(5a)、外気取入ダンパー開度調
節動力部(6a)、回収熱風排出ダンパー開度調節動力部
(6C)に、アウトプットする変換器B(12)を有するこ
とを特徴とするドライヤー内ウエブ乾燥制御装置であ
る。
That is, the present invention provides a dryer hood (1) for giving hot air to a running web (2), a plurality of nozzles (3) for blowing hot air to the web (2), and an infrared radiation thermometer (for measuring web surface temperature). 8) a dryer section, a heater (4) for supplying hot air to the dryer section, a hot air supply fan (5), an outside air intake damper (6), a recovered hot air discharge damper (6b), and each connection And a hot air supply unit having a heat supply adjustment power unit (4a), a hot air supply fan drive unit (5a), an outside air intake damper opening adjustment power unit (6a), and a recovered hot air discharge damper opening adjustment power unit (6C). A hot air supply duct (7a) having a supply hot air temperature / humidity detector (9a) connecting the dryer section and the hot air supply unit and a hot air recovery duct (7b) having a recovered hot air temperature / humidity detector (9b), and controlling And the control unit is Infrared radiation temperature measuring device for measuring a the web surface temperature Supplier (8), the supply, the temperature of the recovered hot air, temperature and humidity detector for detecting the humidity (9a, 9
b), a converter A (10) for converting each analog signal detected by the infrared radiation temperature measuring device (8) and the temperature / humidity detector (9a, 9b) into a digital signal, and the digital signal is input and dried. An arithmetic unit (11) for performing a control arithmetic operation and a digital signal output from the arithmetic unit (11) are input to the hot air supply unit to increase or decrease the heating temperature, the amount of hot air, the outside air intake damper (6), and the recovered hot air. The variable amount of the opening of the exhaust damper (6b) is adjusted to the hot air supply adjustment power unit (4a),
The hot air supply fan drive unit (5a), the outside air intake damper opening adjustment power unit (6a), and the recovered hot air discharge damper opening adjustment power unit (6C) have a converter B (12) for outputting. It is a web drying control device in the dryer.

本発明におけるドライヤーフード1は、ウエブ2を中心
に上下両方、またはいずれか一方に開閉する機構を有し
てもよいし、側面がドア式に開閉する機構を有していて
もよい。
The dryer hood 1 according to the present invention may have a mechanism that opens and closes both vertically and vertically with respect to the web 2, or may have a mechanism that opens and closes a side surface in a door manner.

本発明におけるノズル3は、ドライヤー内にウエブ2を
挟んで上下両方、またはいずれか一方に複数並べて置く
ことができる。並べ方は目的に応じてノズル本数ととも
に考慮される。
In the present invention, the nozzles 3 can be arranged in a dryer on both sides of the web 2 with the web 2 sandwiched therebetween. The arrangement is considered together with the number of nozzles according to the purpose.

また複数のノズル3を区分ごとに分け、ひとつのドライ
ヤーフード1の中で異なった温度、湿度、風量の熱風を
供給できるように熱風供給ダクト7aを区分に分け各々の
熱風供給ダクト7aにダンパー等を設け乾燥制御を行って
もよい。
In addition, the plurality of nozzles 3 are divided into sections, and the hot air supply ducts 7a are divided into sections so that hot air of different temperature, humidity, and air volume can be supplied in one dryer hood 1 into dampers for each hot air supply duct 7a. May be provided to control the drying.

ノズル3の形状は、ノズル3先端よりウエブ2に熱風を
吹付ける角度、風量、風速との関係を考慮し目的に応じ
て設計したものが使用できる。また熱風風量に応じてウ
エブ2とノズル3先端距離を調節する機構をノズル3に
付設することもできる。
The shape of the nozzle 3 may be designed according to the purpose in consideration of the relationship between the angle at which the hot air is blown from the tip of the nozzle 3 to the web 2, the air volume, and the wind speed. Further, a mechanism for adjusting the distance between the tip of the web 2 and the tip of the nozzle 3 depending on the hot air volume can be attached to the nozzle 3.

ドライヤー内の走行ウエブ2のサポート機構は上側のノ
ズル3から吹出す熱風に対し、ウエブ2下側でロールに
よって支持してもよいし、上側と同じく下側もノズル3
から熱風を吹出してエアーフロートさせてサポートさせ
てもよい。ドライヤー全長が短く、ウエブ2が強靱であ
れば、ドライヤー出入口のロールでやや強い張力でサポ
ートし、ドライヤー内はサポートなしでもよい。
The support mechanism for the traveling web 2 in the dryer may support the hot air blown from the upper nozzle 3 by a roll on the lower side of the web 2 or the nozzle 3 on the lower side as well as the upper side.
Alternatively, hot air may be blown from the air to float and support it. If the total length of the dryer is short and the web 2 is tough, the roll at the entrance and exit of the dryer may support it with a slightly high tension, and the inside of the dryer may be unsupported.

本発明における熱風供給部は蒸気、電熱、加熱オイルな
どの熱媒体を放熱フィン4bで放熱する熱源部を内蔵する
加熱器4、ターボファン、箱方ブロアーなどによる熱風
供給ファン5、及び湿度の高い回収熱風を排出し外気を
取入れ露点温度を下げるための回収熱風排出ダンパー6b
や外気取入ダンパー6、並びに熱媒体供給量、ファン送
風量、ダンパー開度等を調節する機構及び駆動部、例え
ばダイヤフラム調節弁、電磁弁、ピストン調節弁、ステ
ッピングモーター、インバーターモーター、ヒーター、
トランスなどからなる。
The hot air supply unit according to the present invention includes a heater 4 having a built-in heat source unit for radiating heat medium such as steam, electric heat, and heating oil with the radiation fins 4b, a hot air supply fan 5 such as a turbo fan, a box blower, and a high humidity. Collected hot air exhaust damper 6b for discharging collected hot air and taking in outside air to lower the dew point temperature
And an outside air intake damper 6, and a mechanism and a drive unit for adjusting the heat medium supply amount, the fan air flow amount, the damper opening degree, etc., for example, a diaphragm control valve, a solenoid valve, a piston control valve, a stepping motor, an inverter motor, a heater,
It consists of a transformer.

また加熱器4の内部に熱風の露点温度を補正できるよう
加湿器が内蔵されてもよい。またドライヤーを区分ごと
に分け、ひとつのドライヤーフード1の中で異なった温
度、湿度、風量の熱風が供給できるように熱供給部を複
数設けてもよい。
A humidifier may be built in the heater 4 so that the dew point temperature of hot air can be corrected. Further, the dryers may be divided into sections, and a plurality of heat supply units may be provided so that hot air having different temperatures, humidity and air volumes can be supplied in one dryer hood 1.

本発明における供給、回収熱風の温度湿度検出器9a,9b
は乾燥前後の熱風の温度及び湿度を検出することが目的
であるので、ウエブ2に吹き付けられる直前の熱風と乾
燥に使われた直後の熱風をドライヤーフード1内に設置
された検出器で検出されることが理想であることは言う
までもないが、実質的に同一であるところのノズル3に
熱風を供給するダクト7a壁、及びドライヤーフード1か
らもどってくるダクト7b壁にそれぞれ穴をあけ温度、湿
度の検出センサーを挿入固定し、アナログ信号を取り出
すことができる。本発明は湿度を用いているが、露点温
度をそのかわりに用いてもよい。
Supply / recovery hot air temperature / humidity detectors 9a, 9b in the present invention
Since the purpose is to detect the temperature and humidity of the hot air before and after drying, the hot air just before being blown onto the web 2 and the hot air just after being used for drying are detected by the detector installed in the dryer hood 1. It goes without saying that it is ideal to make holes in the wall of the duct 7a that supplies hot air to the nozzles 3 that are substantially the same, and in the wall of the duct 7b that returns from the dryer hood 1, respectively. The detection sensor can be inserted and fixed to take out an analog signal. Although the present invention uses humidity, dew point temperature may be used instead.

本発明における赤外線放射温度測定器8は、第3図に従
って説明すると、ウエブ2より放射された赤外線がセン
サー部13で受光され、その強さをアナログ信号としてア
ウトプットし、ウエブ2の表面温度に対応させるもので
ある。赤外線受光センサー部13に外乱放射赤外線が入ら
ないよう光路は筒状の光路カバー14でカバーされ、ウエ
ブ表面からの放射赤外線だけが赤外線受光センサー部13
に入射される。赤外線受光センサー部13自体も赤外線入
射窓15を除いてセンサー部カバー16でカバーされ、セン
サー部カバー16は筒状の光路カバー14と一体化されてい
る。筒状の光路カバー14はドライヤーフード1の壁にあ
けられた穴よりウエブの1cm〜5cm直上まで挿入され、全
体はドライヤーフード1壁に固定台17で固定される。更
にセンサー部カバー16の内部へは、パージ空気吹込み口
18より冷却空気が吹込まれセンサー部カバー16内から光
路カバー14内を通りウエブ2の表面温度に影響されない
ようにパージされる構造となっており、ドライヤー熱風
によるセンサー部の過熱故障を防止している。赤外線放
射温度測定器8及びドライヤーフード1との位置関係
は、センサー部の過熱故障を起こさない限り、センサー
部を覆うカバーを含め赤外線放射測定装置全体がドライ
ヤーフード1内に入ってもかまわない。またドライヤー
フード1内のノズル3が複数並んでいる場合は、ノズル
3の間に筒状カバーが挿入され、ウエブ2の表面温度が
測定できる。該赤外線放射温度測定器8はドライヤーフ
ード1内のどこの場所にも、また複数設置されてもかま
わない。
The infrared radiation temperature measuring device 8 according to the present invention will be described with reference to FIG. 3. The infrared radiation radiated from the web 2 is received by the sensor portion 13 and the intensity thereof is output as an analog signal to determine the surface temperature of the web 2. It corresponds. The optical path is covered by a cylindrical optical path cover 14 so that the disturbance radiation infrared ray does not enter the infrared ray receiving sensor section 13, and only the infrared ray radiating from the web surface is received by the infrared ray receiving sensor section 13
Is incident on. The infrared light receiving sensor portion 13 itself is also covered by the sensor portion cover 16 except for the infrared incident window 15, and the sensor portion cover 16 is integrated with the cylindrical optical path cover 14. The cylindrical optical path cover 14 is inserted into the wall of the dryer hood 1 up to 1 cm to 5 cm directly above the web, and the whole is fixed to the wall of the dryer hood 1 with a fixing base 17. In addition, the purge air blow-in port is installed inside the sensor cover 16.
Cooling air is blown in from 18 and is purged from inside the sensor cover 16 through the optical path cover 14 so as not to be affected by the surface temperature of the web 2 to prevent overheating of the sensor due to hot air from the dryer. There is. As for the positional relationship between the infrared radiation temperature measuring device 8 and the dryer hood 1, the entire infrared radiation measuring device including the cover for covering the sensor part may be inside the dryer hood 1 as long as the sensor part does not overheat. When a plurality of nozzles 3 in the dryer hood 1 are lined up, a cylindrical cover is inserted between the nozzles 3 to measure the surface temperature of the web 2. A plurality of infrared radiation temperature measuring devices 8 may be installed anywhere in the dryer hood 1 and a plurality of infrared radiation temperature measuring devices 8 may be installed.

本発明における変換器A10は、センサー数に応じた多チ
ャンネルのA/Dコンバータである。演算器11はマイクロ
コンピューターを用いる。またデータボックスとしての
記憶装置11aを演算器11に連結すると更に良い。変換器B
12は演算器11からのデジタル信号を受けて熱風供給部の
各動力部が駆動するための熱風の風量や過熱温度の増
減、外気取入ダンパー6や回収熱風排出ダンパー6bの開
度の変量を出力する出力ゲートである。また、変換器A1
0、演算器11、記憶装置11a、変換器B12を全て一体化し
中央制御しても本発明に記載されている機能を有すれば
この限りではない。
The converter A10 in the present invention is a multi-channel A / D converter according to the number of sensors. The computing unit 11 uses a microcomputer. It is more preferable to connect the storage device 11a as a data box to the arithmetic unit 11. Converter B
12 receives the digital signal from the computing unit 11 and changes the amount of hot air and the superheat temperature for driving each power unit of the hot air supply unit, and the variation of the opening degree of the outside air intake damper 6 and the recovered hot air discharge damper 6b. It is an output gate that outputs. Also, the converter A1
Even if 0, the arithmetic unit 11, the storage device 11a, and the converter B12 are all integrated and centrally controlled as long as they have the functions described in the present invention, this does not apply.

本発明に於けるドライヤー内ウエブ乾燥制御装置の制御
方法はドライヤー内を走行するウエブ2に熱風を吹付け
ることにより、ウエブ2から水分等の揮発物が潜熱を吸
収し蒸発するので、蒸発速度の大小により、また、単に
加熱される場合はウエブ2の顕熱の蓄積の大小により、
ウエブ2の表面温度が変化するので、表面温度が常に一
定になるよう走行するウエブ2に吹付ける熱風の風量、
温度及び湿度の変化量を増加減することにより、一定品
質が得られるよう制御するものである。
The method of controlling the web drying control device in the dryer according to the present invention is such that when hot air is blown onto the web 2 running in the dryer, volatile matter such as water content absorbs latent heat from the web 2 and evaporates. Depending on the size, and the size of the accumulation of sensible heat of the web 2 when heated simply,
Since the surface temperature of the web 2 changes, the amount of hot air blown onto the traveling web 2 so that the surface temperature is always constant,
By increasing or decreasing the amount of change in temperature and humidity, control is performed so that a constant quality is obtained.

乾燥制御における各構成要素の相互関係を具体的に説明
すると、赤外線放射温度測定器8によりウエブ2の表面
温度が測定され、ドライヤーノズル3に供給される熱風
の温度、湿度が供給熱風温度湿度検出器9aにより検出さ
れ、ドライヤーフード1より回収される熱風の温度、湿
度が回収熱風温度湿度検出器9bにより検出される。各々
検出されたアナログ信号は変換器A10によりデジタル信
号に変換され演算器11に入力される。演算器11では目標
とするウエブ2の表面温度、熱風の上下限温度、湿度、
及び風量の設定値、並びに入力信号と設定値の関係を示
す演算式が入力されている。演算器11において、赤外線
放射温度測定器8で測定されたウエブ2表面温度の値と
設定値とが比較演算され、ウエブ表面温度が設定値より
高い場合は加熱器4の熱供給及び熱風供給量を減少する
信号が、演算器11より出力され、変換器B12に入力さ
れ、変換器B12から各々の熱供給調節動力部4a及び熱風
供給ファン駆動部5aに動力量が小さくなるよう変量が出
力される。例えば、熱供給が蒸気である場合、蒸気弁開
度を閉じ、ファン駆動部がインバーターモーターであれ
ば、回転数を下げる方向に動作する。演算された結果、
逆にウエブ表面温度が設定値より低い場合は加熱器4の
熱風供給及び熱風供給量が増加するための信号が演算器
11より出力され、変換器B12に入力され、更に変換器B12
より前記熱供給調節動力部4a及び熱風供給ファン駆動部
5aに動力増加の変量がアウトプットされ熱風の温度、風
量が増加し乾燥が促進し、ウエブ2の表面温度が上昇
し、設定値に近づく。変換器B12より出力される熱風供
給調節動力部4a及び熱風供給ファン駆動部5aへの変量の
割合は予め演算器11に入力された演算式により信号が分
配される。
Explaining the mutual relation of each component in the drying control concretely, the surface temperature of the web 2 is measured by the infrared radiation temperature measuring device 8 and the temperature and the humidity of the hot air supplied to the dryer nozzle 3 are detected. The temperature and humidity of the hot air detected by the container 9a and collected from the dryer hood 1 are detected by the collected hot air temperature / humidity detector 9b. The detected analog signals are converted into digital signals by the converter A10 and input to the arithmetic unit 11. With the calculator 11, the target surface temperature of the web 2, the upper and lower limit temperatures of the hot air, the humidity,
And the set value of the air volume, and the arithmetic expression indicating the relationship between the input signal and the set value are input. In the calculator 11, the value of the surface temperature of the web 2 measured by the infrared radiation temperature measuring device 8 and the set value are compared and calculated, and when the web surface temperature is higher than the set value, the heat supply and the hot air supply amount of the heater 4 Is output from the arithmetic unit 11, is input to the converter B12, from the converter B12 to each heat supply adjustment power unit 4a and the hot air supply fan drive unit 5a variable amount is output to reduce the amount of power. It For example, when the heat supply is steam, the steam valve opening is closed, and when the fan drive unit is an inverter motor, the rotation speed is decreased. The calculated result,
On the contrary, when the web surface temperature is lower than the set value, the signal for increasing the hot air supply and the hot air supply amount of the heater 4 is calculated by the calculator.
11 output, input to converter B12, and further converter B12
From the heat supply adjustment power unit 4a and the hot air supply fan drive unit
The variable of power increase is output to 5a, the temperature and volume of hot air increase, drying is promoted, the surface temperature of the web 2 rises, and approaches the set value. A signal is distributed to the ratio of the variation amounts to the hot air supply adjusting power unit 4a and the hot air supply fan driving unit 5a output from the converter B12 by the arithmetic expression previously input to the arithmetic unit 11.

また、熱風の温度の変動幅が極端な加熱や低下が発生し
ないように、熱風の温度の上下限が、条件として演算器
11に設定入力され供給熱風温度湿度検出器9aによりチェ
ックされ、調節温度が上下限の範囲外の温度を必要とす
る状態になった場合は風量で調節される。
In addition, the upper and lower limits of the temperature of the hot air must be set as a condition so that the fluctuation range of the temperature of the hot air does not heat up or drop extremely.
It is set and input to 11, and is checked by the hot air temperature / humidity detector 9a for supply, and when the adjusted temperature is in a state requiring a temperature outside the upper and lower limits, it is adjusted by the air volume.

湿度についてみると、熱風は循環するので、湿度が増加
するため一定の湿度の熱風が供給されるよう制御されね
ばならない。
As for humidity, since hot air circulates, it must be controlled so that hot air with a constant humidity is supplied because the humidity increases.

即ち、予め熱風の相対湿度を設定しておく。That is, the relative humidity of hot air is set in advance.

供給及び回収熱風温度湿度検出器9bから変換器A10によ
り変換され演算器11に入力されてきた信号は、演算器11
において、予め設定された相対湿度の値と比較演算さ
れ、熱風の湿度が設定より高いと外気取入ダンパーの開
度を上げるための信号が演算器11よりアウトプットされ
変換器B12に入力され、更に変換器B12より外気取入ダン
パー開度調節動力部6aに変量が出力され、フレッシュエ
アーを取り込む。外気取入ダンパー6の開度に比例し
て、回収熱風排出ダンパー開度調節動力部6cにも開度を
上げる変量が出力され、回収熱風排出ダンパー6bの開度
が増し、その結果、湿度の低い熱風がノズル3に供給さ
れる。
The signal converted by the converter A10 from the supply / recovery hot air temperature / humidity detector 9b and input to the calculator 11 is the calculator 11
In the above, the value is calculated by comparison with a preset relative humidity value, and when the humidity of the hot air is higher than the setting, a signal for increasing the opening degree of the outside air intake damper is output from the calculator 11 and input to the converter B12. Further, a variable amount is output from the converter B12 to the outside air intake damper opening adjustment power unit 6a to take in fresh air. In proportion to the opening of the outside air intake damper 6, a variable that increases the opening is also output to the recovery hot air exhaust damper opening adjustment power unit 6c, and the opening of the recovery hot air exhaust damper 6b increases, resulting in a change in humidity. Low hot air is supplied to the nozzle 3.

熱風の湿度が設定値より低いとフレッシューエアーの取
込みを抑制するために外気取入ダンパー6開度を小さく
し、それに比例して回収熱風排出ダンパー6b開度も絞ら
れる信号が演算器11より変換器B12にアウトプットさ
れ、更に変換器B12より回収熱風排出ダンパー開度調節
動力部6cに変量が出力される。また極端な加湿、減湿が
発生しないよう湿度の上下限が、演算器11に設定入力さ
れ、供給側と回収側の湿度の差が定常状態を保つように
両者の比較が演算され、演算式に組込まれ比例制御され
る。
If the humidity of the hot air is lower than the set value, the opening of the outside air intake damper 6 will be reduced to suppress the intake of fresh air, and the signal from the calculator 11 will also proportionally reduce the opening of the collected hot air exhaust damper 6b. It is output to the converter B12, and the variable amount is further output from the converter B12 to the recovered hot air exhaust damper opening adjustment power unit 6c. Also, the upper and lower limits of humidity are set and input to the calculator 11 so that extreme humidification and dehumidification do not occur, and the comparison between the two is calculated so that the difference in humidity between the supply side and the recovery side maintains a steady state. It is incorporated into and is proportionally controlled.

本発明におけるウエブ2とは帯状シート物なら、その種
類を問わない。また乾燥のみならず、本発明の制御装置
を用いての熱処理を目的とするウエブ2も含まれる。特
に好ましくは塗工乾燥工程における紙、ラミネート紙、
フィルム、不織布、布帛、金属シート等が上げられる。
また熱処理工程における含浸紙、不織布、フィルム、ウ
エブ状網状物等があげられる。
The web 2 in the present invention may be of any type as long as it is a strip-shaped sheet. Further, the web 2 is intended not only for drying but also for heat treatment using the control device of the present invention. Particularly preferably, paper in the coating drying step, laminated paper,
Films, non-woven fabrics, cloths, metal sheets, etc. are listed.
In addition, examples include impregnated paper, non-woven fabric, film, web-like mesh in the heat treatment step.

本発明は塗工液を塗布した写真用支持体の乾燥制御装置
として好適である。
The present invention is suitable as a drying control device for a photographic support coated with a coating liquid.

即ち、精密な乾燥条件を要求される写真用支持体の乾燥
過程での写真用支持体の上昇温度を制御することによ
り、写真用支持体としてのトラブルを最小限に抑えるこ
とができる。例えば、写真用支持体の原紙水分の減少に
よる写真印画紙となってからのカブリ、ゼラチン組成物
溶液を塗布し乾燥する際の過乾燥によるカール、急激な
乾燥によるゼラチン組成物塗被層の異常光沢、同じく塗
被層の膜強度の低下、あるいは乾燥不足によるベタツ
キ、写真乳剤塗布後の乳剤膜付不足などを抑制または改
善することができる。
That is, by controlling the rising temperature of the photographic support during the drying process of the photographic support which requires precise drying conditions, troubles as the photographic support can be minimized. For example, fogging after the photographic printing paper becomes a photographic printing paper due to a decrease in water content of the photographic support, curling due to overdrying when the gelatin composition solution is applied and dried, abnormalities in the gelatin composition coating layer due to rapid drying. It is possible to suppress or ameliorate glossiness, similarly decrease in film strength of the coating layer, stickiness due to insufficient drying, insufficient adhesion of emulsion film after coating of photographic emulsion, and the like.

また、本発明は熱可塑性樹脂被覆層を有するウエブに対
しては樹脂層の加熱融解による光沢のギラツキ発生、微
粗面加工の微細な型の融解を抑えることに有効であり、
上述の写真用支持体を考慮に加えると、ポリオレフィン
樹脂被覆写真用支持体にゼラチン組成物溶液あるいは合
成バインダー組成物溶液を下引あるいは裏塗りすること
に対して、特に好適な乾燥制御装置である。
Further, the present invention is effective for suppressing the melting of the fine mold for the glossy glare caused by the heating and melting of the resin layer for the web having the thermoplastic resin coating layer, and the fine mold for the surface roughening treatment.
Taking the above photographic support into consideration, it is a particularly suitable drying control device for undercoating or back-coating a polyolefin resin-coated photographic support with a gelatin composition solution or a synthetic binder composition solution. .

(E)作用 作用を実施例を示す第2図とともに説明する。第2図
は、本発明の制御信号のブロック図を示す。まず、記憶
装置11aまたは演算器11にウエブ2の表面温度、供給熱
風の上下限の温度、湿度、風量を予め設定し、走行ウエ
ブ2の乾燥を開始する。赤外線放射温度測定器8により
ドライヤー内走行ウエブ2の表面温度が測定され、ドラ
イヤーノズル3に供給する熱風の温度及び湿度が供給熱
風温度湿度検出器9aにより検出され、ドライヤーフード
1より回収される熱風の温度及び湿度が回収熱風温度湿
度検出器9bにより検出される。各々検出されたアナログ
信号は変換器A10によりデジタル信号に変換された演算
器11に入力される。デジタル信号が入力された演算器11
において、ウエブ表面温度は予め設定された温度との差
が演算され、その差分に対応する風量かつ/または加熱
温度を増加減する出力デジタル信号が変換器B12に送ら
れ、信号を受けた変換器B12より加熱器4の熱供給量を
調節する熱供給調節動力部4aかつ/または熱風供給ファ
ン駆動部5aに変量が出力される。
(E) Action The action will be described with reference to FIG. FIG. 2 shows a block diagram of the control signal of the present invention. First, the surface temperature of the web 2, the temperature of the upper and lower limits of the supplied hot air, the humidity, and the air volume are preset in the storage device 11a or the computing unit 11, and the drying of the running web 2 is started. The surface temperature of the traveling web 2 inside the dryer is measured by the infrared radiation temperature measuring device 8, the temperature and humidity of the hot air supplied to the dryer nozzle 3 are detected by the supplied hot air temperature humidity detector 9a, and the hot air collected from the dryer hood 1 is detected. The temperature and humidity of the temperature are detected by the recovered hot air temperature and humidity detector 9b. The detected analog signals are input to the arithmetic unit 11 converted into digital signals by the converter A10. A calculator 11 to which a digital signal is input
, The difference between the web surface temperature and a preset temperature is calculated, and an output digital signal for increasing / decreasing the air volume and / or the heating temperature corresponding to the difference is sent to the converter B12, and the converter receiving the signal A variable amount is output from B12 to the heat supply adjustment power unit 4a and / or the hot air supply fan drive unit 5a for adjusting the heat supply amount of the heater 4.

熱供給調節動力部4aと熱供給ファン駆動部5aとの出力の
分配は予め演算式を演算器11に入力しておく。また過度
の高熱または低温にならないよう上下限温度が演算器11
に入力されており、供給熱風温度湿度検出器9aより検出
された信号が変換器A10を通り、演算器11に入力され、
設定値と比較されチェックされる。加熱温度の上下限が
設定されるため、加熱温度で制御できない場合は風量に
その分が増加減される。
For the distribution of the outputs of the heat supply adjusting power unit 4a and the heat supply fan drive unit 5a, an arithmetic expression is input to the arithmetic unit 11 in advance. In addition, the upper and lower limit temperatures are set in the calculator 11 to prevent excessive heat or low temperature.
The signal detected by the supply hot air temperature / humidity detector 9a passes through the converter A10 and is input to the calculator 11,
It is compared with the set value and checked. Since the upper and lower limits of the heating temperature are set, if the heating temperature cannot control, the amount of air flow is increased or decreased by that amount.

熱風の温度湿度は、供給熱風温度湿度検出器9aと回収熱
風温度湿度検出器9bとの差、及び設定値と供給熱風温度
湿度検出器9aとの差が演算され、熱風温度の低下分に対
応する温度を加熱器4によって昇温する信号が演算器11
より変換器B12にアウトプットされ、変換器B12より加熱
器4の蒸気バルブを駆動する熱供給調節動力部4aに蒸気
量を増加させる変量が出力される。また、ウエブ2から
の蒸発による熱風湿度の増加に対応して演算器11よりデ
ジタル信号が変換器B12にアウトプットされ、変換器B12
より、ダンパー開度を上げて調節する変量が外気取入れ
ダンパー開度調節動力部6aに出力されフレッシュエアー
が取込まれる。
The temperature and humidity of the hot air are calculated by calculating the difference between the supplied hot air temperature / humidity detector 9a and the recovered hot air temperature / humidity detector 9b, and the difference between the set value and the supplied hot air temperature / humidity detector 9a. The signal for raising the temperature to be generated by the heater 4 is the calculator 11
Is output to the converter B12, and the converter B12 outputs a variable amount for increasing the amount of steam to the heat supply control power unit 4a that drives the steam valve of the heater 4. In addition, in response to the increase in hot air humidity due to evaporation from the web 2, the digital signal is output from the calculator 11 to the converter B12, and the converter B12
As a result, a variable amount for increasing and adjusting the damper opening is output to the outside air intake damper opening adjusting power unit 6a to take in fresh air.

また、必要に応じてフレッシュエアの導入に応じた外気
取入ダンパー6の開度に比例して回収熱風を排出すべく
回収熱風排出ダンパー6bの開度を調節する信号も同時に
変換器B12に出力され、変換器B12より、ダンパー開度を
上げて調節する変量が回収熱風排出ダンパー開度調節動
力部6cに出力される。
Also, if necessary, a signal for adjusting the opening of the collected hot air exhaust damper 6b to discharge the collected hot air in proportion to the opening of the outside air intake damper 6 according to the introduction of fresh air is also output to the converter B12 at the same time. Then, the converter B12 outputs a variable amount for increasing and adjusting the damper opening degree to the recovered hot air exhaust damper opening degree adjusting power unit 6c.

フレッシュエアー取込みによる熱風の温度低下分は供給
熱風温度湿度検出器9aまたは赤外線放射温度測定器8に
よって検出され変換器A10を経て演算器11において加熱
器4で昇温されるべき値が演算され、変換器B12に出力
される。
The temperature drop of the hot air due to the intake of fresh air is detected by the hot air temperature / humidity detector 9a or the infrared radiation temperature measuring device 8 and the value to be raised by the heater 4 is calculated by the calculator 11 via the converter A10. Output to converter B12.

(F)実施例 本発明の実施例を実施例に対応する第1図を用いて説明
する。
(F) Embodiment An embodiment of the present invention will be described with reference to FIG. 1 corresponding to the embodiment.

ドライヤーフード1、その内部を走行するウエブ2、及
び熱風を吹付けるノズル3を有するドライヤー部と、ノ
ズルに熱風を供給するための加熱器4、加熱器内部で放
熱効率を上げる放熱フィン4b、熱風供給ファン5、外気
取入ダンパー6、及び回収熱風排出ダンパー6b、並びに
各々に連結した動力部、即ち、熱供給調節動力部4a、熱
風供給ファン駆動部5a、外気取入ダンパー開度調節動力
部6a、回収熱風排出ダンパー開度調節動力部6cからなる
熱風供給部と、前記ドライヤー部のノズル3と熱風供給
部と連繋しノズル3に熱風を供給する熱風供給ダクト7
a、ドライヤーフード1と熱風供給部とを連繋し熱風を
回収する熱風回収ダクト7bと、制御部とからなり、該制
御部はドライヤー内を走行するウエブ2の表面温度を測
定する赤外線放射温度測定器8、供給熱風、回収熱風各
々の温度湿度を検出する温度湿度検出器9a及び9b、更に
前記赤外線放射温度測定器8、供給熱風温度湿度検出器
9a、及び回収熱風温度湿度検出器9bのアナログ信号をイ
ンプットしデジタル信号をアウトプットする変換器A1
0、前記デジタル信号がインプットされ演算または制御
を行う演算器11、及び演算器11からアウトプットされた
出力を熱風供給部の加熱器4の加熱を加減する熱供給調
節動力部4a、熱風供給ファン5の風量を調節する熱風供
給ファン駆動部5a、外気取入ダンパー6の開度を調節す
る外気取入ダンパー開度調節動力部6a、及び回収熱風排
出ダンパー6bの開度を調節する回収熱風排出ダンパー開
度調節動力部6cに各々のダンパーを開閉する変量をアウ
トプットする変換器B12を有することによってドライヤ
ー内の走行ウエブ2の乾燥を制御することができる乾燥
制御装置である。
A dryer hood 1, a web 2 running inside the dryer hood, and a dryer unit having a nozzle 3 for blowing hot air, a heater 4 for supplying hot air to the nozzle, radiation fins 4b for increasing heat radiation efficiency inside the heater, hot air The supply fan 5, the outside air intake damper 6, the recovered hot air exhaust damper 6b, and the power unit connected to each, that is, the heat supply adjustment power unit 4a, the hot air supply fan drive unit 5a, and the outside air intake damper opening degree adjustment power unit. 6a, a hot air supply unit including a recovery hot air discharge damper opening adjustment power unit 6c, and a hot air supply duct 7 that is connected to the nozzle 3 of the dryer unit and the hot air supply unit to supply hot air to the nozzle 3.
a, a hot air collecting duct 7b for connecting the dryer hood 1 and the hot air supply unit to collect hot air, and a control unit, and the control unit measures infrared radiation temperature for measuring the surface temperature of the web 2 running in the dryer. Device 8, temperature and humidity detectors 9a and 9b for detecting the temperature and humidity of each of the supplied hot air and the recovered hot air, and further the infrared radiation temperature measuring device 8 and the supplied hot air temperature and humidity detector
Converter A1 that inputs the analog signal of 9a and the recovered hot air temperature and humidity detector 9b and outputs the digital signal
0, a computing unit 11 that receives the digital signal and performs computation or control, and an output output from the computing unit 11 that controls the heating of the heater 4 of the hot-air supply unit by a heat-supply adjusting power unit 4a and a hot-air supply fan Hot air supply fan drive unit 5a for adjusting the air volume of 5, external air intake damper opening adjustment power unit 6a for adjusting the opening degree of the external air intake damper 6, and recovered hot air exhaust for adjusting the opening degree of the recovered hot air exhaust damper 6b This is a drying control device that can control the drying of the traveling web 2 in the dryer by having the converter B12 that outputs a variable for opening and closing each damper in the damper opening adjustment power unit 6c.

また、銘柄、塗液種類等に応じて、各々の設定値を記憶
装置11aにインプットしておき、銘柄、塗液種類等を指
定するだけでドライヤー内走行ウエブ2の乾燥が制御で
きる。
Further, depending on the brand, the type of coating liquid, etc., each set value is input to the storage device 11a, and the drying of the traveling web 2 in the dryer can be controlled only by specifying the brand, the type of coating liquid, etc.

ウエブ2として、ゼラチン、顔料、硬膜剤、界面活性剤
からなる塗液を塗布したポリエチレン樹脂被覆写真支持
体を乾燥する際、ドライヤー内走行前記写真用支持体の
表面温度を68±2℃になるように赤外線放射温度測定器
8の検出温度を定め、また、ドライヤー内のノズル3か
ら吹出す熱風量をノズル3より吹き出す風速が10m/sec
〜12m/secに対応する量を設定し、供給熱風の上限温度
を100℃、下限温度60℃、相対湿度を上限70RH%、下限5
0RH%となるよう設定し乾燥した。
When drying a polyethylene resin-coated photographic support coated with a coating liquid consisting of gelatin, pigment, hardener, and surfactant as the web 2, the inside temperature of the photographic support was adjusted to 68 ± 2 ° C. The temperature detected by the infrared radiation thermometer 8 is determined so that the hot air flow rate from the nozzle 3 in the dryer is 10 m / sec.
Set the amount corresponding to ~ 12m / sec, the upper limit temperature of the supplied hot air is 100 ℃, the lower limit temperature is 60 ℃, the relative humidity is upper limit 70RH%, the lower limit 5
It was set to 0 RH% and dried.

その結果、紙面温度は68±2℃の範囲に入り、ポリエチ
レン被覆樹脂の融解による光沢の増加や原紙水分の減少
がなく、また乾燥不足になることもなく乾燥制御するこ
とができた。
As a result, the surface temperature of the paper was in the range of 68 ± 2 ° C., and the drying was able to be controlled without increasing the gloss and decreasing the water content of the base paper due to melting of the polyethylene-coated resin, and without causing insufficient drying.

(G)発明の効果 本発明は制御部がドライヤー内ウエブ表面温度を測定す
る赤外線放射温度測定器、供給、回収熱風の温度、湿度
を検出する温度湿度検出器、前記赤外線放射温度測定器
並びに温度湿度検出器によって検出された各々のアナロ
グ信号をデジタル信号に変換する変換器A、前記デジタ
ル信号がインプットされ、乾燥制御演算を行う演算器、
及び該演算器からの出力をインプットし熱風供給部に熱
風の風量や加熱温度の増減、外気取入ダンパー6や回収
熱風排出ダンパー6bの開度の変量をアウトプットする変
換器Bを有することを特徴とするドライヤー内ウエブ乾
燥制御装置であるので、ドライヤー内ウエブの水分率が
変化すると赤外線放射温度測定器、熱風温度検出器のア
ナログ信号が変化し、演算器において、設定値と比較演
算され、設定との偏差をなくすべく、熱風供給ファン、
加熱器、及びダンパーを適性変化させ、走行ウエブが未
乾燥や過乾燥でドライヤーから出てくることはなく、一
定の乾燥状態のウエブが得られ、乾燥が制御される。
(G) Effect of the Invention In the present invention, the controller controls the infrared radiation temperature measuring device for measuring the surface temperature of the web inside the dryer, the temperature and humidity detector for detecting the temperature and humidity of the hot air supplied and recovered, the infrared radiation temperature measuring device and temperature. A converter A that converts each analog signal detected by the humidity detector into a digital signal, a calculator that receives the digital signal and performs a drying control calculation,
And a converter B which inputs the output from the arithmetic unit and outputs to the hot air supply unit a change in the amount of hot air and the heating temperature, and a variable amount of opening of the outside air intake damper 6 and the recovered hot air exhaust damper 6b. Since it is a web drying control device inside the dryer, when the moisture content of the web inside the dryer changes, the infrared radiation temperature measuring instrument, the analog signal of the hot air temperature detector changes, and the calculator calculates and compares it with the set value. In order to eliminate the deviation from the setting, a hot air supply fan,
By appropriately changing the heater and the damper, the running web does not come out of the dryer due to undried or overdried, a web in a constant dry state is obtained, and the drying is controlled.

特に実施例に述べられているようにポリオレフィン樹脂
被覆写真用支持体のドライヤー内ウエブ乾燥制御装置に
好適であることがわかる。
In particular, as described in the examples, it is found that it is suitable for a web drying control device in a dryer of a photographic support coated with a polyolefin resin.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の実施例を説明する概略図を示す。第2
図は乾燥制御装置の制御系フローと制御すべき駆動部と
の関係を示す。 第3図は赤外線放射温度測定器及びドライヤーフードと
の位置関係を示す。そのうち(3−1)はウエブの流れ
方向からみたW−Z断の立面図であり、(3−2)はX
−Y断面の平面図である。 1…ドライヤーフード、2…ウエブ、3…ノズル、4…
加熱器、4a…熱供給調節動力部、4b…放熱フィン、5…
熱風供給ファン、5a…熱風供給ファン駆動部、6…外気
取入ダンパー、6a…外気取入ダンパー開度調節動力部、
6b…回収熱風排出ダンパー、6c…回収熱風排出ダンパー
開度調節動力部、7a…熱風供給ダクト、7b…熱風回収ダ
クト、8…赤外線放射温度測定器、9a…供給熱風温度湿
度検出器、9b…回収熱風温度湿度検出器、10…変換器
A、11…演算器、11a…記憶装置、12…変換器B、13…
赤外線受光センサー部、14…光路カバー、15…赤外線入
射窓、16…センサー部カバー、17…固定台、18…パージ
空気吹込み口
FIG. 1 shows a schematic diagram for explaining an embodiment of the present invention. Second
The figure shows the relationship between the control system flow of the drying controller and the drive unit to be controlled. FIG. 3 shows the positional relationship between the infrared radiation thermometer and the dryer hood. Among them, (3-1) is an elevation view of WZ cross section as seen from the flow direction of the web, and (3-2) is X-axis.
It is a top view of a -Y cross section. 1 ... dryer hood, 2 ... web, 3 ... nozzle, 4 ...
Heater, 4a ... Heat supply adjusting power unit, 4b ... Radiating fins, 5 ...
Hot air supply fan, 5a ... Hot air supply fan drive unit, 6 ... Outside air intake damper, 6a ... Outside air intake damper opening adjustment power unit,
6b ... Recovered hot air exhaust damper, 6c ... Recovered hot air exhaust damper opening adjustment power unit, 7a ... Hot air supply duct, 7b ... Hot air recovery duct, 8 ... Infrared radiation temperature measuring device, 9a ... Supplied hot air temperature / humidity detector, 9b ... Recovered hot air temperature / humidity detector, 10 ... Converter A, 11 ... Arithmetic unit, 11a ... Storage device, 12 ... Converter B, 13 ...
Infrared light receiving sensor section, 14 ... Optical path cover, 15 ... Infrared incident window, 16 ... Sensor section cover, 17 ... Fixing base, 18 ... Purge air blowing port

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】走行ウエブ(2)に熱風を与える、ドライ
ヤーフード(1)、熱風をウエブ(2)に吹付ける複数
のノズル(3)、ウエブ表面温度を測定する赤外線放射
温度測定器(8)を有するドライヤー部と、 該ドライヤー部に熱風を供給する、加熱器(4)、熱風
供給ファン(5)、外気取入ダンパー(6)、回収熱風
排出ダンパー(6b)、及び各々に連結した熱供給調節動
力部(4a)、熱風供給ファン駆動部(5a)、外気取入ダ
ンパー開度調節動力部(6a)、回収熱風排出ダンパー開
度調節動力部(6C)を有する熱風供給部と、 前記ドライヤー部と熱風供給部とを連繋する供給熱風温
度湿度検出器(9a)を有する熱風供給ダクト(7a)及び
回収熱風温度湿度検出器(9b)を有する熱風回収ダクト
(7b)と、制御部とからなり、 該制御部がドライヤー内ウエブ表面温度を測定する赤外
線放射温度測定器(8)、供給、回収熱風の温度、湿度
を検出する温度湿度検出器(9a、9b)、前記赤外線放射
温度測定器(8)並びに温度湿度検出器(9a、9b)によ
って検出された各々のアナログ信号をデジタル信号に変
換する変換器A(10)、前記デジタル信号がインプット
され乾燥制御演算を行う演算器(11)及び該演算器(1
1)から出力されたデジタル信号をインプットし、 熱風供給部に、加熱温度の増減や熱風の風量、外気取入
ダンパー(6)や回収熱風排出ダンパー(6b)の開度の
変量を、熱風供給調節動力部(4a)、熱風供給ファン駆
動部(5a)、外気取入ダンパー開度調節動力部(6a)、
回収熱風排出ダンパー開度調節動力部(6C)に、アウト
プットする変換器B(12)を有することを特徴とするド
ライヤー内ウエブ乾燥制御装置。
1. A dryer hood (1) for giving hot air to a running web (2), a plurality of nozzles (3) for blowing hot air to the web (2), and an infrared radiation thermometer (8) for measuring the web surface temperature. ), A heater (4), a hot air supply fan (5), an outside air intake damper (6), a recovered hot air discharge damper (6b), and a heater (4) for supplying hot air to the dryer unit. A hot air supply unit having a heat supply adjustment power unit (4a), a hot air supply fan drive unit (5a), an outside air intake damper opening adjustment power unit (6a), and a recovered hot air discharge damper opening adjustment power unit (6C), A hot air supply duct (7a) having a supply hot air temperature / humidity detector (9a) and a hot air recovery duct (7b) having a recovered hot air temperature / humidity detector (9b), which connects the dryer unit and the hot air supply unit, and a control unit. And the control unit is Infrared radiation temperature measuring device (8) for measuring the surface temperature of the web in the ear, temperature and humidity detectors (9a, 9b) for detecting the temperature and humidity of the supply and recovery hot air, the infrared radiation temperature measuring device (8) and temperature and humidity A converter A (10) for converting each analog signal detected by the detectors (9a, 9b) into a digital signal, a calculator (11) for receiving the digital signal and performing a drying control calculation, and the calculator (1)
The digital signal output from 1) is input to the hot air supply unit to increase or decrease the heating temperature, the amount of hot air, and the open air intake damper (6) or the recovered hot air exhaust damper (6b) opening degree variation. Adjustment power unit (4a), hot air supply fan drive unit (5a), outside air intake damper opening adjustment power unit (6a),
A web drying control device in a dryer, which has a converter B (12) for outputting to a power unit (6C) for adjusting the opening degree of the recovered hot air exhaust damper.
【請求項2】該ウエブ(2)が熱可塑性樹脂層を有する
ウエブ(2)である請求項(1)記載のドライヤー内ウ
エブ乾燥制御装置。
2. A dryer web drying control device according to claim 1, wherein said web (2) is a web (2) having a thermoplastic resin layer.
【請求項3】該ウエブ(2)が写真用支持体である請求
項(1)または(2)記載のドライヤー内ウエブ乾燥制
御装置。
3. The web drying control device in a dryer according to claim 1, wherein the web (2) is a photographic support.
JP63164440A 1988-06-30 1988-06-30 Web drying controller in dryer Expired - Lifetime JPH0720570B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63164440A JPH0720570B2 (en) 1988-06-30 1988-06-30 Web drying controller in dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63164440A JPH0720570B2 (en) 1988-06-30 1988-06-30 Web drying controller in dryer

Publications (2)

Publication Number Publication Date
JPH0214772A JPH0214772A (en) 1990-01-18
JPH0720570B2 true JPH0720570B2 (en) 1995-03-08

Family

ID=15793205

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63164440A Expired - Lifetime JPH0720570B2 (en) 1988-06-30 1988-06-30 Web drying controller in dryer

Country Status (1)

Country Link
JP (1) JPH0720570B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2024089168A1 (en) * 2022-10-27 2024-05-02 Weiss Technik Gmbh Drying system and method for drying a product

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH072636Y2 (en) * 1988-11-11 1995-01-25 セーレン株式会社 Steamer for fabric processing
JPH0618168A (en) * 1992-07-03 1994-01-25 Kubota Corp Air conditioning device of drying chamber
JPH06344536A (en) * 1993-05-14 1994-12-20 Japan Small Corp Dryer controlling method for gravure printer
JP5534771B2 (en) * 2009-10-09 2014-07-02 パナソニック株式会社 Coating film drying method and drying device
ITUB20160825A1 (en) * 2016-02-18 2017-08-18 New Instruments And Res For Analysis S R L Automatic exhaust air recirculation system for a flexographic or rotary printing machine or for a laminating machine or for a laminating machine.
CN108800897A (en) * 2017-05-03 2018-11-13 天津海裕纸制品有限公司 A kind of paper products drying equipment convenient for adjusting temperature
IT201800004996A1 (en) * 2018-05-02 2019-11-02 DRYER FOR DRYING WET METALLIC ELEMENTS SUCH AS NEEDLES OF WEAVING FRAMES OR FRONT OF KNITWEAR MACHINES THAT ARE CLEANED WITH A WASHING LIQUID
CN108787352A (en) * 2018-06-29 2018-11-13 常德金德新材料科技股份有限公司 It is a kind of to prevent coated film from hazing the device to whiten

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2024089168A1 (en) * 2022-10-27 2024-05-02 Weiss Technik Gmbh Drying system and method for drying a product

Also Published As

Publication number Publication date
JPH0214772A (en) 1990-01-18

Similar Documents

Publication Publication Date Title
US20180045463A1 (en) Method and apparatus for controlling cooling temperature and pressure in wood veneer jet dryers
US5984002A (en) Temperature and humidity control apparatus and temperature and humidity prediction apparatus used therefor
US5625962A (en) Method for measuring the moisture content of a web of goods on a through-flow dryer and device for working the method
JPH0720570B2 (en) Web drying controller in dryer
US20110047812A1 (en) Method for controlling drying of clothes and dryer for clothes
EP0458825B1 (en) Apparatus for drying
JPS5824779A (en) Method of improving thermal efficiency of drier and its controller
JP3474745B2 (en) Temperature / humidity control device for air conditioner and recording medium recording temperature / humidity control program used for same
JPH04139345A (en) Method and apparatus for supplying constant temperature and constant moisture air
JP3797010B2 (en) Air conditioning method
JP2517463B2 (en) Air conditioner
US20210323323A1 (en) Media conditioning
JP2007078246A (en) Sheet drying method and device, and method of manufacturing coated sheet
JP2857431B2 (en) Grain drying equipment
JPS637870A (en) Apparatus for controlling film on painted steel plate
JPH05288375A (en) Method and apparatus for detecting humidity of humidifier
JPH0237245A (en) Operation control device in air conditioner
CN110887347B (en) Drying method and drying system
JP2646376B2 (en) Supply and exhaust volume control method and apparatus in dryer hood for paper machine
JPH06344536A (en) Dryer controlling method for gravure printer
JPS5818588B2 (en) Netsupuujiyunkanshikikansohouhou Oyobi Souchi
JPS6291786A (en) Heat pump type drier
JPH04272798A (en) Drier
Saputra et al. Effect of changes in the regeneration temperature and the regeneration airflow velocity on the system performance of the solid desiccant air conditioning
JPH0113880B2 (en)