JPH02298385A - Resin drying method of sandwich type resin composite metal plate - Google Patents

Resin drying method of sandwich type resin composite metal plate

Info

Publication number
JPH02298385A
JPH02298385A JP11768789A JP11768789A JPH02298385A JP H02298385 A JPH02298385 A JP H02298385A JP 11768789 A JP11768789 A JP 11768789A JP 11768789 A JP11768789 A JP 11768789A JP H02298385 A JPH02298385 A JP H02298385A
Authority
JP
Japan
Prior art keywords
resin
metal plate
oven
composite metal
air
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
JP11768789A
Other languages
Japanese (ja)
Inventor
Toshihiro Okochi
大河内 敏博
Kojiro Oikawa
及川 耕二郎
Yasuhiro Omura
大村 保弘
Ryoichi Matsuda
良一 松田
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP11768789A priority Critical patent/JPH02298385A/en
Publication of JPH02298385A publication Critical patent/JPH02298385A/en
Pending legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)
  • Laminated Bodies (AREA)

Abstract

PURPOSE:To prevent a lowering of heat efficiency by supplying a gaseous mixture of radiant tube combustion exhaust gas and air into a resin drying oven. CONSTITUTION:The combustion exhaust gas of the radiant tube 2 of a drying oven 1 is stirred along with the air from the duct 8 engaged with the conduit 7 connected to a suction port 6 to be supplied into the oven 1 as the gaseous mixture with air through the conduit 7. A lowering of oven temp. is suppressed by the supply of this gaseous mixture and the dilution of solvent evaporation gas is performed by the drying of the solvent type resin 4 applied to the surface of a metal plate 3. The temp. of the combustion exhaust gas of the radiant tube is about 700 deg.C and explosion can be prevented while lowering of oven temp. is suppressed and the quality of a composite metal plate can be enhanced.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、サンドイッチ型樹脂複合金属板の樹脂乾燥方
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a resin drying method for a sandwich-type resin composite metal plate.

(従来の技術とその課a) サンドイッチ型樹脂複合金属板の製造においては、一方
の金属板(帯)表面にトルエン、キシレン系の揮発性溶
剤を添加したいわゆる溶剤型樹脂を塗布し、これを乾燥
炉へ導入して乾燥し樹脂中の溶剤を除去した後、他方の
金属板(帯)を上記樹脂表面に位置せしめて、加圧して
サンドイッチ型樹脂複合金属板とするものである(特公
昭62−58897号公報)。
(Prior art and its problem a) In manufacturing sandwich-type resin composite metal plates, the surface of one metal plate (strip) is coated with a so-called solvent-based resin containing volatile solvents such as toluene and xylene. After the resin is introduced into a drying oven and dried to remove the solvent in the resin, the other metal plate (strip) is placed on the resin surface and pressurized to form a sandwich-type resin composite metal plate (Tokuko Showa). 62-58897).

しかして、樹脂乾燥に際しては、第1図に示すごとく、
乾燥炉1内に配置したラジアントチューブ2.2a内へ
燃料ガスと空気を導入し、これを燃焼して炉1内を間接
加熱し、金属板(帯)3表面に塗布した溶剤型樹脂4を
乾燥するのであるが、乾燥にともない炉l内に溶剤(ト
ルエン、キシレン等)が充満し、爆発の危険性が生ずる
ので、炉lの吸引口5から炉内ガスを吸引放出し、同時
に吸入口6がら空気を炉1内へ吸入して、炉内に充満し
ている溶剤を希釈し、爆発を防止している。
However, when drying the resin, as shown in Figure 1,
Fuel gas and air are introduced into the radiant tube 2.2a placed in the drying oven 1, and are burned to indirectly heat the inside of the oven 1, and the solvent-based resin 4 applied to the surface of the metal plate (strip) 3 is heated. During drying, the furnace 1 is filled with solvent (toluene, xylene, etc.) and there is a risk of explosion, so the gas inside the furnace is sucked and discharged from the suction port 5 of the furnace 1, Air is sucked into the furnace 1 to dilute the solvent filling the furnace and prevent explosions.

このようなことから、炉1内温度が低下することになり
、所定の炉内温度を確保するためにラジアントチューブ
2.2aでの燃料ガス量が増加し、熱効率を著しく低下
し、コストを上昇させる等の欠点をともなうものである
As a result, the temperature inside the furnace 1 decreases, and the amount of fuel gas in the radiant tube 2.2a increases in order to maintain the predetermined furnace temperature, which significantly reduces thermal efficiency and increases costs. However, there are some drawbacks such as:

(発明が解決しようとする課B) 本発明は、このような欠点を有利に解決するためなされ
たものである。
(Problem B to be Solved by the Invention) The present invention has been made to advantageously solve these drawbacks.

(If!i!題を解決するための手段)本発明の要旨と
するところは、サンドイッチ型樹脂複合金属板の製造に
際し、一方の金属板(帯)の表面に塗布された溶剤型樹
脂を、ラジアントチューブを配設した樹脂乾燥炉内で乾
燥するにあたり、ラジアントチューブ燃焼排ガスと空気
の混合ガスを前記樹脂乾燥炉内へ供給することを特徴と
するサンドイッチ型樹脂複合金属板の樹脂乾燥方法にあ
る。
(Means for solving the If!i! problem) The gist of the present invention is that when manufacturing a sandwich-type resin composite metal plate, a solvent-based resin applied to the surface of one metal plate (strip) is A resin drying method for a sandwich-type resin composite metal plate, characterized in that during drying in a resin drying oven equipped with radiant tubes, a mixed gas of radiant tube combustion exhaust gas and air is supplied into the resin drying oven. .

本発明においては、上記のごとく、ラジアントチューブ
の燃焼排ガスである高温ガスと空気との混合ガスを炉内
へ導入し、炉内温度の低下を抑制しつつ、炉内の溶剤蒸
発ガスを希釈するものである。すなわち、樹脂の乾燥温
度としては、一般に約200 ’Cであり、一方ラジア
ントチューブの燃焼排ガスは約700°Cであり、これ
を空気と混合して炉内へ導入することにより、充分炉温
低下を抑制しつつ、爆発を防止することができる。
In the present invention, as described above, a mixed gas of high-temperature gas, which is the combustion exhaust gas of the radiant tube, and air is introduced into the furnace to dilute the solvent evaporation gas in the furnace while suppressing a decrease in the temperature inside the furnace. It is something. In other words, the drying temperature of resin is generally about 200°C, while the combustion exhaust gas of the radiant tube is about 700°C, and by mixing this with air and introducing it into the furnace, the furnace temperature can be sufficiently lowered. It is possible to prevent explosions while suppressing them.

次に本発明の実施の態様の一例を第2図により説明する
Next, an example of an embodiment of the present invention will be explained with reference to FIG.

第2図において、乾燥炉1のラジアントチューブ2の燃
焼排ガスは、吸入口6に接続した導管7に係合したダク
ト8がら空気を随伴しつつ、空気との混合ガスとして導
管7を介して吸入口6から炉1内へ供給されるように構
成されている。この混合ガスの供給によって、炉温低下
が抑制されるとともに、金属板(帯)3の表面に塗布さ
れた溶剤型樹脂4の乾燥による熔剤莫発ガスの希釈が行
われる。
In FIG. 2, the combustion exhaust gas from the radiant tube 2 of the drying oven 1 is inhaled through the conduit 7 as a mixed gas with air while accompanying air through the duct 8 engaged with the conduit 7 connected to the suction port 6. It is configured to be supplied into the furnace 1 through the port 6. By supplying this mixed gas, a decrease in the furnace temperature is suppressed, and the solvent-based resin 4 applied to the surface of the metal plate (strip) 3 is dried, thereby diluting the melt gas.

(実施例) 次に本発明の実施例を比較例とともに挙げる。(Example) Next, examples of the present invention will be listed together with comparative examples.

実施例 金属帯(厚0.4 m X幅1300mm)の表面に1
30gmの樹脂(トルエン含有ff1700g/f)を
塗布し、通板速度10m/分、炉温150°Cで乾燥し
、炉内からガスを15ONa+’/分排気し、一方、7
00℃のラジアントチューブ燃焼排ガス1ONs+3/
分と空気(2″0°C) 4 ONm’/分との混合ガ
スを炉内へ導入しつつ、残りの10 ONg3/分は炉
出口からの侵入空気により樹脂を乾燥したところ、ラジ
アントチューブにより炉内温度を150℃に維持するた
めのコークス炉発生ガス(燃料)使用量は、51 Nt
a3/ hであった。
1 on the surface of the example metal strip (thickness 0.4 m x width 1300 mm)
30 gm of resin (containing toluene ff 1700 g/f) was applied, dried at a threading speed of 10 m/min and a furnace temperature of 150°C, and gas was exhausted from the furnace at 15ONa+'/min.
00℃ radiant tube combustion exhaust gas 1ONs+3/
While introducing a mixed gas of 4 ONm'/min and air (2"0°C) into the furnace, the remaining 10 ONg3/min was used to dry the resin with air entering from the furnace outlet. The amount of coke oven generated gas (fuel) used to maintain the temperature inside the oven at 150°C is 51 Nt.
It was a3/h.

比較例 上記実施例において、ラジアントチューブの燃焼排ガス
を空気に混入することなく空気(20°C)のみ508
m”7分を炉内に導入しつつ、炉温を150°Cに保持
して樹脂を乾燥したところ、炉温保持のために使用した
コークス炉発生ガス(燃料)量は150 Nm3/ h
と、実施例に比べ約3倍の燃料を使用した。
Comparative Example In the above example, only air (20°C) was used without mixing the combustion exhaust gas of the radiant tube with the air.
When the resin was dried by maintaining the furnace temperature at 150°C while introducing the coke oven into the furnace for 7 minutes, the amount of coke oven gas (fuel) used to maintain the furnace temperature was 150 Nm3/h.
This means that about three times as much fuel was used as in the example.

(発明の効果) 本発明によれば、乾燥炉の燃料消費量を著しく低減させ
ることができるので、コストの軽減および省エネルギー
を図ることができる。
(Effects of the Invention) According to the present invention, the amount of fuel consumed by the drying furnace can be significantly reduced, so that it is possible to reduce costs and save energy.

又炉温の局部的な低下がなくなり、樹脂乾燥が均一にで
き、樹脂と金属板(帯)の密着性が均一になり、樹脂複
合金属板の品質を向上することができる等の優れた効果
が得られる。
In addition, there is no local drop in furnace temperature, the resin can be dried uniformly, the adhesion between the resin and the metal plate (strip) is uniform, and the quality of the resin composite metal plate can be improved. is obtained.

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

第1図は、従来の乾燥炉の断面説明図、第2図は、本発
明の実施の態様の一例を示す乾燥炉の断面説明図である
FIG. 1 is a cross-sectional explanatory diagram of a conventional drying oven, and FIG. 2 is a cross-sectional explanatory diagram of a drying oven showing an example of an embodiment of the present invention.

Claims (1)

【特許請求の範囲】[Claims] サンドイッチ型樹脂複合金属板の製造に際し、一方の金
属板(帯)の表面に塗布された溶剤型樹脂を、ラジアン
トチューブを配設した樹脂乾燥炉内で乾燥するにあたり
、ラジアントチューブ燃焼排ガスと空気との混合ガスを
前記樹脂乾燥炉内へ供給することを特徴とするサンドイ
ッチ型樹脂複合金属板の樹脂乾燥方法。
When manufacturing sandwich-type resin composite metal plates, the solvent-based resin coated on the surface of one metal plate (strip) is dried in a resin drying oven equipped with radiant tubes. A method for drying a sandwich type resin composite metal plate, characterized in that a mixed gas of: is supplied into the resin drying furnace.
JP11768789A 1989-05-11 1989-05-11 Resin drying method of sandwich type resin composite metal plate Pending JPH02298385A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11768789A JPH02298385A (en) 1989-05-11 1989-05-11 Resin drying method of sandwich type resin composite metal plate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11768789A JPH02298385A (en) 1989-05-11 1989-05-11 Resin drying method of sandwich type resin composite metal plate

Publications (1)

Publication Number Publication Date
JPH02298385A true JPH02298385A (en) 1990-12-10

Family

ID=14717810

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11768789A Pending JPH02298385A (en) 1989-05-11 1989-05-11 Resin drying method of sandwich type resin composite metal plate

Country Status (1)

Country Link
JP (1) JPH02298385A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04310270A (en) * 1991-04-09 1992-11-02 Nippon Steel Corp Resin drying method for sandwich-type resin composite metal plate
CN102233317A (en) * 2011-04-20 2011-11-09 江苏剑桥涂装工程有限公司 Direct-fired blast heater

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63305965A (en) * 1987-06-06 1988-12-13 Toyo Seikan Kaisha Ltd Method for drying or baking film

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63305965A (en) * 1987-06-06 1988-12-13 Toyo Seikan Kaisha Ltd Method for drying or baking film

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04310270A (en) * 1991-04-09 1992-11-02 Nippon Steel Corp Resin drying method for sandwich-type resin composite metal plate
CN102233317A (en) * 2011-04-20 2011-11-09 江苏剑桥涂装工程有限公司 Direct-fired blast heater

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