JPS6231923A - Heating method for cathode-ray tube - Google Patents
Heating method for cathode-ray tubeInfo
- Publication number
- JPS6231923A JPS6231923A JP17198185A JP17198185A JPS6231923A JP S6231923 A JPS6231923 A JP S6231923A JP 17198185 A JP17198185 A JP 17198185A JP 17198185 A JP17198185 A JP 17198185A JP S6231923 A JPS6231923 A JP S6231923A
- Authority
- JP
- Japan
- Prior art keywords
- ray tube
- panel
- cathode
- cathode ray
- fan
- 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
Links
Landscapes
- Manufacture Of Electron Tubes, Discharge Lamp Vessels, Lead-In Wires, And The Like (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はブラウン管内を真空にする際に適用されるブラ
ウン管の加熱方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for heating a cathode ray tube, which is applied when creating a vacuum inside the cathode ray tube.
ブラウン管はパネルとファンネルとからなり、パネル内
面には螢光塗料が塗布されている。そこでブラウン管内
を真空にする際、ノ(ネル内面に塗布されている螢光塗
料に含まれている揮発分を除去するために通常350〜
400℃程度に加熱することが行われている0
〔従来の技術〕
従来は第5図に示すように加熱炉(1)内に形成される
炉室(2)の土壁中央から送風機(3)を垂下し、その
両側からは加熱源であるラジアントチューブ(4)。A cathode ray tube consists of a panel and a funnel, and the inner surface of the panel is coated with fluorescent paint. Therefore, when vacuuming the inside of the cathode ray tube, the pressure is usually 350~
[Prior art] Conventionally, as shown in Fig. 5, a blower (3 ) hanging down from both sides of the radiant tube (4) which is a heating source.
(5)を垂下し、該ラジアントチューブ(4) 、 (
5)の内側に案内板f6) 、 (力を取付けた構成が
適用され、該加熱炉(1)の炉室(2)内に台車(8)
の支持部(9)に支持したブラウン管(101を送シ込
んで熱風を矢印に示すように送風機(3)によって矢印
に示すように循還させてブラウン管(10を加熱するも
のである(実開昭59−33727号)。(5) is suspended, and the radiant tube (4), (
A configuration in which a force is attached to the guide plate f6) inside the heating furnace (1) is applied, and a trolley (8) is installed inside the furnace chamber (2) of the heating furnace (1).
The cathode ray tube (101) supported on the support part (9) is blown into the tube and the hot air is circulated as shown by the arrow by the blower (3) to heat the cathode ray tube (10). No. 59-33727).
しかし上記従来技術においてはブラウン管(1(11に
吹付けられる熱風はパネル側からファンネル側に行くに
つれて温度が低下し例えば300℃の熱風をブラウン管
a〔のパネル側にl m / 56Cの速度で吹付けた
場合にはファンネル側では約265℃になり総括伝熱係
数が低下し、ブラウン管a〔のパネル側とファンネル側
とで加熱むらを生じブラウン管a@の破損が起シ易い0
〔問題点を解決するための手段〕
本発明は上記従来技術の問題点を解決する手段としてブ
ラウン管α0)のパネルθ〔A側とファンネル00)B
側とから交互に熱風を吹付けるものである。However, in the above-mentioned conventional technology, the temperature of the hot air blown onto the cathode ray tube (1) decreases as it goes from the panel side to the funnel side. If it is attached, the temperature on the funnel side will be approximately 265℃, which will lower the overall heat transfer coefficient, causing uneven heating between the panel side and the funnel side of the CRT A, which may easily cause damage to the CRT A. Means for Solving] The present invention provides a method for solving the above-mentioned problems of the prior art by improving panel θ [A side and funnel 00) B of a cathode ray tube α0).
Hot air is blown alternately from the sides.
本発明の作用は下記の通りである0
ブラウン管のパネル側から吠付けられた熱風はファンネ
ル111jに行くにしたがって温度低下しファンネル側
への総括伝熱係数が低下する。次いでブラウン管のファ
ンネル側から吹付けられた熱風はパネル側に行くに・し
たがって温度低下しパネル側への総括伝熱係数が低下す
る。The operation of the present invention is as follows.0 The temperature of the hot air blown from the panel side of the cathode ray tube decreases as it goes to the funnel 111j, and the overall heat transfer coefficient to the funnel side decreases. Next, the hot air blown from the funnel side of the cathode ray tube decreases in temperature as it goes toward the panel side, and the overall heat transfer coefficient toward the panel side decreases.
したがって本発明においてはブラウン管のパネル側とフ
ァンネル側とから交互に熱風を吹付ける結果、ブラウン
管は均一に加熱されることになυ熱的歪に起因するブラ
ウン管の破損を確実に防止することが出来る。またパネ
ル側もファンネル側も均一に加熱される結果パネル側ま
たはファンネル側から吹付けられる熱風の温度低下が小
さく、したがって総括伝熱係数の低下も小さい。かくし
て本発明では熱風の必要量が従来の60チ程度になる。Therefore, in the present invention, as a result of blowing hot air alternately from the panel side and the funnel side of the cathode ray tube, the cathode ray tube is heated uniformly, and damage to the cathode ray tube due to thermal distortion can be reliably prevented. . In addition, since both the panel side and the funnel side are heated uniformly, the temperature drop of the hot air blown from the panel side or the funnel side is small, and therefore the overall heat transfer coefficient is also small. Thus, according to the present invention, the required amount of hot air is reduced to about 60 inches compared to the conventional method.
第1図および第2図には第1実施例を示す0図において
加熱炉(1)内に形成される炉室(2)の土壁中央から
は正逆回転可能なファン(3)Aを有する送風機(3)
が垂下され、該送風機(3)の両側からは加熱源である
ラジアントチューブ(4) 、 (5)が垂下され、該
ラジアントチューブ(41、(5)の内側には案内板(
6)。In Figures 1 and 2, a fan (3) A that can rotate forward and backward is installed from the center of the clay wall of the furnace chamber (2) formed in the heating furnace (1) in Figure 0 showing the first embodiment. Blower with (3)
is suspended from both sides of the blower (3), and radiant tubes (4) and (5), which are heating sources, are suspended from both sides of the blower (3), and a guide plate (
6).
(7)が取付けられる。該加熱炉(1)には該炉室(2
)が第2図に示すように複数個並列せられ該炉室(2)
内にはレール0υに乗架している台車(8)が所定の速
さで送通され、該台車(8)の支持部(9)にはブラウ
ン管a0がパネル側を上向きにして支持されている。そ
して送風機(3)のファン(3)Aが正回転する時には
熱風は実線矢印のように循還しブラウン管OQをパネル
側から加熱しかつ熱風自体は冷却されラジアントチュー
ブ+4) 、 (5)によシ再び加熱される。またファ
ン(3)Aが逆回転する時には熱風は点線矢印のよう
iに循還しブラウン管OIをファンネル側から加
熱しかつ熱風自体は冷却されラジアントチューブ(4)
。(7) is installed. The heating furnace (1) has a furnace chamber (2).
) are arranged in parallel as shown in Fig. 2 to form the furnace chamber (2).
Inside, a trolley (8) mounted on a rail 0υ is conveyed at a predetermined speed, and a cathode ray tube a0 is supported on the support portion (9) of the trolley (8) with the panel side facing upward. There is. When the fan (3) A of the blower (3) rotates forward, the hot air circulates as shown by the solid arrow, heating the cathode ray tube OQ from the panel side, and the hot air itself is cooled by the radiant tube +4) and (5). It will be heated again. Also, when fan (3) A rotates in the opposite direction, the hot air flows as shown by the dotted arrow.
The hot air circulates to the radiant tube (4) and heats the cathode ray tube OI from the funnel side, and the hot air itself is cooled.
.
(5)によ)再び加熱される。同時にブラウン管0〔内
は支持部(9)を介して真空にされブラウン管0(支)
のパネル内面に塗布されている螢光塗料の揮発分が除去
される。(5)) is heated again. At the same time, the inside of the cathode ray tube 0 is evacuated via the support part (9).
The volatile components of the fluorescent paint applied to the inner surface of the panel are removed.
第3図に示すようにブラウン管00)はパネル(10A
とファンネル00)Bとからなり例えばパネル(10)
Aの厚さtlは12.5uoa、7アンネル(10Bの
上部の厚さtlは9.4 rsttr、下部の厚さt3
は2.5鵬でありこの場合パネルQOIAの重さは約1
0kg、ンアンネル(IOIBの重さは約5〜である。As shown in Figure 3, the cathode ray tube 00) is connected to the panel (10A
For example, panel (10)
The thickness tl of A is 12.5 uoa, 7 annel (the upper thickness tl of 10B is 9.4 rsttr, the lower thickness t3
is 2.5 peng, and in this case the weight of the panel QOIA is about 1
0kg, n-annel (IOIB weighs about 5~
したがって熱容量比はパネル:ファンネルで略2:1に
なる。そこでブラウン管α■を均一に加熱するには送に
機(3)のファン(3)Aの正回転時間:逆回転時間を
略2:1とすることが望ましい。Therefore, the heat capacity ratio of panel:funnel is approximately 2:1. Therefore, in order to uniformly heat the cathode ray tube α■, it is desirable that the forward rotation time:reverse rotation time of the fan (3)A of the feeder (3) be approximately 2:1.
第4図には第2実施例を示す。本実施例においては送風
機(3)のファン(3)Aが正回転する炉室(2)Aと
逆回転する炉室(2)Bとが複数個並列せられている。FIG. 4 shows a second embodiment. In this embodiment, a plurality of furnace chambers (2)A in which the fan (3)A of the blower (3) rotates in the forward direction and a plurality of furnace chambers (2)B in which the fan (3)A of the blower (3) rotates in the reverse direction are arranged in parallel.
そして炉室(2)Aと炉室(2)Bとはブラウン管(1
0)のパネルQOAとファンネルQGBとの熱容量比に
等しい比率で配列される。第3図に示すブラウン管aO
)ノ場合ハ炉室(2)A:F室(2)B=2:1として
炉室(2)八−炉室(2)A−炉室(2)B−炉室(2
)A−・・・・・山と云うように配列される。かぐして
ブラウン管α0)はパネル側とファンネル側とから交互
処熱風を吹付けられるが熱風吹付量はパネルとファンネ
ルの熱容量比に等しいものであるからブラウン管θ0)
は均一に加熱される。Furnace chamber (2) A and furnace chamber (2) B are cathode ray tube (1)
0) are arranged at a ratio equal to the heat capacity ratio of the panel QOA and the funnel QGB. Braun tube aO shown in Figure 3
) In the case of (2) A: F chamber (2) B = 2:1, the furnace chamber (2) 8-furnace chamber (2) A-furnace chamber (2) B-furnace chamber (2)
)A-...They are arranged like a mountain. The cathode ray tube α0) is blown with heated air alternately from the panel side and the funnel side, but the amount of hot air blown is equal to the heat capacity ratio of the panel and the funnel, so the cathode ray tube θ0)
is heated evenly.
上記実施例以外、送風機を炉室側面にも取付は側方から
も熱風を吹付けてもよい。また加熱源はラジアントチス
ーブ以外、バーナー、電熱器等周知のものが用いられ得
る。そしてブラウン管の加熱温度は通常350〜400
℃程度である。また本発明においてはブラウン管のパネ
ル側とファンネル側からの送風量をパネルとファンネル
の熱容量比に一致させることが望ましいけれどもこのこ
とは本発明を限定するものではない。In addition to the embodiments described above, the blower may also be attached to the side of the furnace chamber to blow hot air from the side. In addition to the radiant heat source, a well-known heating source such as a burner or an electric heater may be used. The heating temperature of a cathode ray tube is usually 350 to 400.
It is about ℃. Further, in the present invention, it is desirable that the amount of air blown from the panel side and the funnel side of the cathode ray tube match the heat capacity ratio of the panel and the funnel, but this does not limit the present invention.
第1図および第2図は本発明の第1実施例に関するもの
であシ、第1図は横断面図、第2図は平面図、第3図は
ブラウン管の断面図、第4図は第2実施例の模式部分縦
断面図、第5図は従来例の横断面図である。
図中 (1)・・・加熱炉、(2)・・・炉室、(3)
・・・送風機、(3)A・・・ファン、00)・・・ブ
ラウン管、(10)A・・・パネル、(In)B・・・
ファンネル
特許出願人 大同特殊鋼株式会社
プ 1 図
ブ2図1 and 2 relate to a first embodiment of the present invention, in which FIG. 1 is a cross-sectional view, FIG. 2 is a plan view, FIG. 3 is a sectional view of a cathode ray tube, and FIG. FIG. 5 is a schematic partial vertical cross-sectional view of the second embodiment, and FIG. 5 is a cross-sectional view of the conventional example. In the figure (1)...Heating furnace, (2)...Furnace chamber, (3)
...Blower, (3)A...Fan, 00)...Cathode ray tube, (10)A...Panel, (In)B...
Funnel patent applicant: Daido Steel Co., Ltd. Figure 1 Figure 2
Claims (1)
を吹付けることを特徴とするブラウン管の加熱方法A method for heating a cathode ray tube characterized by blowing hot air alternately from the panel side and the funnel side of the cathode ray tube.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17198185A JPS6231923A (en) | 1985-08-05 | 1985-08-05 | Heating method for cathode-ray tube |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17198185A JPS6231923A (en) | 1985-08-05 | 1985-08-05 | Heating method for cathode-ray tube |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6231923A true JPS6231923A (en) | 1987-02-10 |
Family
ID=15933320
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17198185A Pending JPS6231923A (en) | 1985-08-05 | 1985-08-05 | Heating method for cathode-ray tube |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6231923A (en) |
-
1985
- 1985-08-05 JP JP17198185A patent/JPS6231923A/en active Pending
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