JPS5916697B2 - How to manufacture fluorescent lamps - Google Patents
How to manufacture fluorescent lampsInfo
- Publication number
- JPS5916697B2 JPS5916697B2 JP52008367A JP836777A JPS5916697B2 JP S5916697 B2 JPS5916697 B2 JP S5916697B2 JP 52008367 A JP52008367 A JP 52008367A JP 836777 A JP836777 A JP 836777A JP S5916697 B2 JPS5916697 B2 JP S5916697B2
- Authority
- JP
- Japan
- Prior art keywords
- mercury
- electrode
- bulb
- exhaust
- fluorescent lamp
- 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
Links
Landscapes
- Manufacture Of Electron Tubes, Discharge Lamp Vessels, Lead-In Wires, And The Like (AREA)
Description
【発明の詳細な説明】
この発明はけい光ランプの製造方法に係り、さらに詳細
にはけい光ランプの特性を損わず、また作業環境を汚染
させずに少量の水銀を正確に封入する方法に関するもの
である。[Detailed Description of the Invention] The present invention relates to a method for manufacturing a fluorescent lamp, and more particularly, a method for accurately enclosing a small amount of mercury without impairing the characteristics of the fluorescent lamp or contaminating the working environment. It is related to.
けい光ランプに水銀を封入する従来の方法は一般に第1
図の平面図に示すような排気工程中で行なっている。Traditional methods of filling mercury in fluorescent lamps are generally
This is done during the exhaust process as shown in the plan view of the figure.
すなわち第1図の回転する複数個の排気ヘッド(図示せ
ず)を有する排気装置に於て、2の位置でバルブが排気
管を介して排気系に接続される。That is, in the exhaust system having a plurality of rotating exhaust heads (not shown) shown in FIG. 1, the valve is connected to the exhaust system via the exhaust pipe at position 2.
そして排気ヘッドが回転することによシバルプ内の空気
の排出が開始され、続いて加熱炉3に入る。As the exhaust head rotates, the air in the air pump starts to be discharged, and then enters the heating furnace 3.
この加熱炉3の中でバルブは400℃前後に加熱され、
バルブ内壁に塗布されているけい光体の吸蔵ガス(H2
O,02、CO2等)が排出され、次にバルブは電極処
理装置4,4′に入る。The valve is heated to around 400°C in this heating furnace 3,
The storage gas (H2) of the phosphor coated on the inner wall of the bulb
O, 02, CO2, etc.) are discharged and then the valve enters the electrode treatment device 4, 4'.
ここでバルブ両端の電極フィラメントに通電して電子放
射性物質となる炭酸塩を加熱して分解活性化する。Here, electricity is applied to the electrode filaments at both ends of the bulb to heat and decompose the carbonate, which becomes an electron radioactive substance, to activate it.
この間、炭酸塩より発生するH2O。CO2,C0,0
□等のガスを短時間に排出することを目的として、5の
位置で排気管上部に設置された滴下装置より少量の水銀
粒をバルブ内に滴下して蒸勿化し、その拡散効果により
バルブのガス排出を促進して真空度を高める、言わゆる
水銀フラッシュを行なった後、6の位置で再び前記水銀
滴下装置より適量の水銀粒を滴下する。During this time, H2O is generated from the carbonate. CO2,C0,0
For the purpose of discharging gas such as After performing a so-called mercury flush to promote gas discharge and increase the degree of vacuum, an appropriate amount of mercury particles is dropped again from the mercury dropping device at position 6.
次に電極処理装置4,4′に続いて配置された不活性ガ
ス封入装置7の位置で、バルブを排気系から隔離してバ
ルブ内にアルゴンガス等の不活性ガスを封入し、更にこ
れに続いて配置された排気管溶封装置8により排気管が
溶封され、9の位置で排気装置よりバルブは取り出され
る。Next, at the position of the inert gas filling device 7 placed next to the electrode processing devices 4 and 4', the valve is isolated from the exhaust system and an inert gas such as argon gas is filled in the valve. Subsequently, the exhaust pipe is melt-sealed by the disposed exhaust pipe melt-sealing device 8, and the valve is taken out from the exhaust device at position 9.
この従来の方法は電極処理装置の途中で水銀を滴下して
蒸気化してバルブ外に排出するため、バルブ内の不純ガ
ス除去効果は大きいが、バルブ内に残る水銀量には大き
なバラツキが出る欠点がある。In this conventional method, mercury is dropped midway through the electrode treatment device, vaporized, and discharged outside the bulb, which is highly effective in removing impurity gas inside the bulb, but the drawback is that the amount of mercury remaining inside the bulb varies widely. There is.
バルブ外に蒸気化して排出される水銀の量はバルブの温
度、水銀粒の表面積の大小、排気時間及び排気系の抵抗
等の変化により変ること、パルプ外に排出された水銀蒸
気の一部は比較的温度の低い排気管の内壁に凝結し、こ
れが再び機械的振動等によりバルブ内に落下すること等
の理由で最終的にバルブ内に残存する水銀の量は広い範
囲にわたって変動する。The amount of mercury vaporized and discharged outside the pulp varies depending on changes such as the temperature of the valve, the surface area of the mercury particles, the evacuation time, and the resistance of the evacuation system. The amount of mercury that ultimately remains in the bulb varies over a wide range because it condenses on the inner wall of the exhaust pipe, which has a relatively low temperature, and then falls back into the bulb due to mechanical vibrations.
どのバルブ内にも必要最少量の水銀を確保するためには
、前記変動を考慮すると、排気工程で必要な全水銀量は
封入必要水銀量の4〜6倍が必要となる。In order to secure the minimum necessary amount of mercury in any bulb, taking the above fluctuations into consideration, the total amount of mercury required in the evacuation process must be 4 to 6 times the amount of mercury required to be sealed.
従って、ランプによっては封入必要水銀量の3〜4倍程
度封入されるものもあり、これが水銀に起因したランプ
特性の悪化を引き起こす欠点があった。Therefore, depending on the lamp, the amount of mercury that needs to be filled may be about 3 to 4 times the amount that needs to be filled, which has the drawback of causing deterioration of the lamp characteristics due to the mercury.
また、水銀による作業環境汚染と言う観点から、前記水
銀フラッシュ時にバルブ外に排出した水銀を排気系から
回収する作業や排気系から大気中に水銀蒸気が拡散する
ことを防ぐトラップ装置等には膨大な費用と細心な注意
が必要となる欠点を有している。In addition, from the perspective of contaminating the work environment due to mercury, there is a huge amount of work needed to recover the mercury discharged outside the valve during the mercury flush from the exhaust system, and a trap device to prevent mercury vapor from diffusing into the atmosphere from the exhaust system. It has the drawbacks of high cost and the need for careful attention.
近時、これ等欠点を解決する方法として、バルブ内の電
極近傍に水銀合金や水銀化合物等の水銀放出素子と非蒸
発性ゲッター剤を設け、排気工程中では水銀を滴下せず
排気工程終了後に前記水銀放出素子と非蒸発性ゲッター
剤を加熱して管内に水銀を放出するとともに加熱時に出
る不純ガスをゲッター剤で除去する方法が実用され始め
た。Recently, as a method to solve these drawbacks, a mercury emitting element such as a mercury alloy or a mercury compound and a non-evaporable getter agent are installed near the electrodes in the bulb, and mercury is not dropped during the evacuation process, but after the evacuation process is completed. A method has begun to be put into practice in which the mercury emitting element and the non-evaporable getter agent are heated to release mercury into the tube and impurity gas released during heating is removed using the getter agent.
この方法は、ランプに必要最少量の水銀を正確に封入で
きる上に、排気工程で水銀を扱うことがないので作業環
境での水銀汚染の防止と言う従来法に比較し大きな長所
が得られる。This method not only allows the lamp to be filled with the minimum amount of mercury required, but also eliminates the need to handle mercury during the exhaust process, which provides a major advantage over conventional methods in preventing mercury contamination in the working environment.
しかし、この方法にも従来法に比べて欠点もある。However, this method also has drawbacks compared to conventional methods.
この方法は排気での電極処理の途中で水銀を滴下しない
ので、不純ガスの排出を促進する水銀フラッジユング効
果が得られないため、かなりの不純ガスを含んだままの
溶封バルブとなる。In this method, mercury is not dropped during the electrode treatment with exhaust, so the mercury flooding effect that promotes the discharge of impure gas cannot be obtained, resulting in a melt-sealed valve that still contains a considerable amount of impure gas.
この不純ガスは、その後の水銀放出素子とゲッターの加
熱までにかなり管壁のけい光体に吸着されてしまうこと
、またゲッターが活性化されても不純ガスの除去能力が
水銀放出素子の加熱時に出る不純ガス(H2O,CO2
、C09H2等)を除去するだけで通常の電極部に設置
したゲッターでは能カ一杯であり、不純ガスを全て除去
出来ない。This impure gas is largely adsorbed by the phosphor on the tube wall by the time the mercury emitting element and getter are heated, and even if the getter is activated, its ability to remove impurity gas is limited by the time the mercury emitting element is heated. Impure gases (H2O, CO2
, C09H2, etc.), a getter installed in a normal electrode part is at full capacity and cannot remove all impurity gases.
従って、この不純ガスがランプを点灯した場合、管端部
の黒化や光束の劣化などの点灯特性を損う欠点がある。Therefore, when a lamp is lit with this impure gas, there are drawbacks such as blackening of the end of the tube and deterioration of the luminous flux, which impairs the lighting characteristics.
これら不純ガスを点灯前に完全に除去するためにゲッタ
ーの表面積を大きくすることも考えられるが、このため
には電極部近傍以外にもかなり広い面積でゲッターを設
置することが必要となり、これは製造工程を複雑化し、
歩留を低下させることになる。In order to completely remove these impurity gases before lighting, it is possible to increase the surface area of the getter, but this would require installing the getter over a fairly large area other than the vicinity of the electrode. Complicating the manufacturing process,
This will reduce the yield.
またゲッターの処理状態によりゲッターの化学的活性度
が変化し十分に制御することができず、ゲッターの活性
度が大き過ぎてランプ点灯中の管端黒化を早期に発生さ
せることなど問題がある。In addition, the chemical activity of the getter changes depending on the processing conditions of the getter, making it impossible to control it sufficiently.There are also problems such as the getter's activity being too high, which can lead to early blackening of the end of the tube while the lamp is being lit. .
この発明は上記の欠点を改良するためになされたもので
あり、けい光ランプの電極近傍に水銀合金や水銀化合物
等の水銀放出素子を設け、排気工程終了後に前記水銀放
出素子を加熱して水銀を放出し、ランプ内に必要最少量
の水銀を正確に封入する方法に於て、排気工程中の電極
物質の加熱活性化処理をバルブの加熱工程の前半と後半
とに2分割して行なうと言う簡単で安価な方法により、
水銀放出素子およびゲッター剤を使用する方法の欠点を
除去し、ランプ内の不純ガスを除去しランプの管端部黒
化と光束劣化を防止する方法を提供するものである。This invention was made in order to improve the above-mentioned drawbacks.A mercury-emitting element made of a mercury alloy or a mercury compound is provided near the electrode of a fluorescent lamp, and the mercury-emitting element is heated after the evacuation process is completed to release mercury. In this method, the heating activation treatment of the electrode material during the exhaust process is divided into two parts: the first half of the bulb heating process and the second half of the bulb heating process. By a simple and inexpensive method,
The present invention provides a method that eliminates the drawbacks of the method using a mercury emitting element and a getter agent, removes impurity gas within the lamp, and prevents blackening of the end of the lamp tube and deterioration of the luminous flux.
次にこの発明の詳細を図面を用いて説明する。Next, the details of this invention will be explained using the drawings.
電極近傍に水銀放出素子、例えばTi(チタン)−Zr
(ジルコニウム)−Hg(水銀)化合物と非蒸発性ゲッ
ター、例えば、Zr(ジルコニウム)−At(アルミニ
ウム)合金を設置したけい光ランプ用バルブを本発明の
実施例である第2図の排気装置を用いてけい光ランプを
製造する場合を説明する。A mercury-emitting element, such as Ti (titanium)-Zr, is placed near the electrode.
A fluorescent lamp bulb equipped with a (zirconium)-Hg (mercury) compound and a non-evaporable getter, such as a Zr (zirconium)-At (aluminum) alloy, is used with the exhaust system shown in FIG. 2, which is an embodiment of the present invention. A case in which a fluorescent lamp is manufactured using this method will be explained.
第2図に於て、図中の番号で水銀滴下法の説明に用いた
第1図と同一番号で示したものは従来の排気装置と同じ
ものであ、b、io、1o’は加熱炉3の前半に設置し
た電極処理装置である。In Figure 2, the numbers in the figure that are the same as those in Figure 1 used to explain the mercury dropping method are the same as the conventional exhaust equipment, and b, io, and 1o' are the heating furnaces. This is the electrode processing equipment installed in the first half of Section 3.
第2図に於て、反時計方向に回転する複数個の排気ヘッ
ド(図示せず)を有する排気装置1の2の位置に於てバ
ルブは一端に設けられた排気管を介して排気系に接続さ
れる。In FIG. 2, in position 2 of the exhaust system 1 having a plurality of exhaust heads (not shown) rotating in a counterclockwise direction, the valve is connected to the exhaust system through an exhaust pipe provided at one end. Connected.
そして排気ヘッドが回転することによりバルブ内の空気
の排出が開始され続いてバルブは加熱炉3に入り外部か
らの強制加熱が開始されるが、同時に前記加熱炉3の内
部に設けられた第1の電極処理装置10.10’により
バルブ両端の電極フィラメントへの通電が始まり電極物
質の加熱分解が開始される。As the exhaust head rotates, the air inside the valve starts to be discharged, and then the valve enters the heating furnace 3 and starts forced heating from the outside. The electrode processing device 10.10' starts energizing the electrode filaments at both ends of the bulb, and thermal decomposition of the electrode material begins.
但し、ここで電極物質の加熱分解の開始時期は実験によ
れば電極フィラメントの酸化を防ぐためバルブ内の圧力
が6.0Torr以下に減圧された後であることが重要
である。However, according to experiments, it is important to start the thermal decomposition of the electrode material after the pressure inside the bulb is reduced to 6.0 Torr or less in order to prevent oxidation of the electrode filament.
実験によると6.0Torrをこえると電極の酸化が起
りランプの黒化、寿命特性を損うことがわかった。Experiments have shown that when the temperature exceeds 6.0 Torr, oxidation of the electrodes occurs, causing blackening of the lamp and impairing its life characteristics.
バルブの温度上昇に伴い、バルブ内壁に塗布されたけい
光体が吸蔵している水、0□ 、CO2等のガスがバル
ブ内に放出され、また、電極からは炭酸塩等の電極物質
の加熱分解に伴いCO2,02、CO等のガスがバルブ
内に放出され、これ等のガスは排気管を通して排気系に
より同時にバルブ外に排出される。As the temperature of the bulb increases, gases such as water, CO2, etc. stored in the phosphor applied to the inner wall of the bulb are released into the bulb, and the electrode material such as carbonate is heated. As the decomposition occurs, gases such as CO2, 02, and CO are released into the valve, and these gases are simultaneously exhausted to the outside of the valve by the exhaust system through the exhaust pipe.
この時、けい光体は高温状態にあるため電極物質からの
不純ガスはけい光体には吸着されない。At this time, since the phosphor is in a high temperature state, impurity gas from the electrode material is not adsorbed by the phosphor.
前記の第1の電極処理装置10 、10’による電極処
理はバルブ温度が300℃になる前に完了させる。Electrode processing by the first electrode processing apparatuses 10 and 10' is completed before the bulb temperature reaches 300°C.
この過程で炭酸塩がほぼ分解され電極からのガス放出の
大部分が完了し炭酸塩は酸化物に変る。During this process, most of the carbonate is decomposed, most of the gas release from the electrode is completed, and the carbonate is converted into an oxide.
300’C以上の温度まで第1の電極処理工程を続ける
とバルブから放出される吸蔵不純ガス等のバルブ内の酸
化性不純ガスにより電極フィラメントやリード材が酸化
を起すため避けるべきである。Continuing the first electrode treatment step to a temperature of 300'C or higher will cause oxidation of the electrode filament and lead material due to oxidizing impurity gas in the bulb, such as occluded impurity gas released from the bulb, and should be avoided.
バルブの加熱は更に継続され前記加熱炉3の出口附近で
ぽ400〜450℃となる。Heating of the bulb continues further, and the temperature near the outlet of the heating furnace 3 reaches 400-450°C.
続いて前記加熱炉3に連なる第2の電極処理装置4,4
′にバルブが入ると、再び電極フィラメントへの通電が
開始され電極物質の処理が行なわれる。Next, a second electrode processing device 4, 4 connected to the heating furnace 3
When the valve is turned on, the electrode filament is energized again and the electrode material is processed.
この処理は前記の第1の電極処理装置10 、10’に
於てほぼ酸化物に変った電極物質を加熱して活性化状態
にするとともに、後述する不活性ガス封入工程布の間に
電極が不純ガスで汚染されるのを防ぐ目的で行なわれる
。This treatment is performed by heating the electrode material, which has almost changed to an oxide, in the first electrode treatment apparatus 10, 10' to activate it, and at the same time, the electrode material is heated during the inert gas filling process described later. This is done to prevent contamination with impure gases.
従って、放出ガスは少い。つまり、水銀放出素子および
ゲッター剤を使用する方法においては電極物質からの不
純ガスを水銀フラッシング等で放出する工程がないため
、結果的に不純ガスがかなりけい光体に吸着されてしま
っていたが、このようなことが防止できた。Therefore, less gas is released. In other words, in the method using a mercury emitting element and a getter agent, there is no step to release impure gas from the electrode material by mercury flushing, etc., and as a result, a considerable amount of impure gas is adsorbed by the phosphor. , this kind of thing could have been prevented.
次に前記の第2の電極処理装置4,4′に連なって配置
された不活性ガス封入装置7の位置でバルブは排気系と
遮断されて数Torrの圧力のアルゴン・ガス等の不活
性ガスが封入される。Next, the valve is cut off from the exhaust system at the position of the inert gas filling device 7 arranged in series with the second electrode processing device 4, 4', and an inert gas such as argon gas at a pressure of several Torr is supplied. is included.
次に前記不活性ガス封入装置Tに続いて配置された排気
管溶封装置8により、バルブの排気管が溶封され、続い
て9の位置でバルブは排気装置1より取り出され、次の
水銀放出素子と非蒸発性ゲッターの加熱工程、例えば高
周波誘導加熱装置に送られ、水銀放出素子の加熱により
水銀が放出されるとともに、この水銀放出時にランプ内
に放出された不純ガスを吸着させるために、非蒸発性ゲ
ッター材が同時に加熱活性化され次の工程に送られ、以
下口金骨は工程、エージング工程、ベーシング工程など
の通常のけい光ランプ製造工程を経て完成ランプとなる
。Next, the exhaust pipe of the valve is melt-sealed by the exhaust pipe melt-sealing device 8 disposed following the inert gas filling device T, and then the valve is taken out from the exhaust device 1 at position 9, and the next mercury In the heating process of the emitting element and the non-evaporable getter, for example, the mercury is sent to a high frequency induction heating device, and mercury is released by heating the mercury emitting element, and in order to adsorb impurity gas released into the lamp at the time of this mercury release. At the same time, the non-evaporable getter material is heat-activated and sent to the next process, and then the base frame undergoes the usual fluorescent lamp manufacturing processes such as process, aging process, and basing process to become a finished lamp.
この発明は通常この一連の製造工程で作られるが、必要
ならば前記第2の電極処理装置のある工程、あるいはそ
れに連なる排気管溶封装置8までの工程中に簡単な不活
性ガスの封入・排気の操作(装置は図示せず)を繰り返
してもよい。The present invention is normally manufactured through this series of manufacturing steps, but if necessary, it is possible to simply fill in an inert gas during a certain step of the second electrode processing device or a step up to the exhaust pipe melt sealing device 8 that is connected thereto. The evacuation operation (equipment not shown) may be repeated.
次に本発明の効果を実施例を上げて説明する。Next, the effects of the present invention will be explained with reference to examples.
実施例 1
40ワツト・ラビットスタート形ランプに用いた例を説
明する。Example 1 An example of use in a 40 watt rabbit start type lamp will be explained.
厚さ0.12mm、巾6.0mmノ=ッケルメツキ鉄板
上の中央部に巾31にわたり不揮発性ゲッターとしてZ
r −A を合金を、また水銀放出素子としてT i
−Hf合金を各々表裏に圧着したものを電極を囲うよ
うに形成した電極部を作成し、これをバルブに封着する
。Z as a non-volatile getter is placed in the center of a 0.12 mm thick, 6.0 mm wide iron plate over a width of 31 mm.
r −A as an alloy and T i as a mercury-releasing element.
-Hf alloy is crimped on the front and back sides to form an electrode part surrounding the electrode, and this is sealed to the bulb.
この封着バルブを排気炉で従来の如く加熱炉の後で電極
の分解活性化を行ないその工程中でアルゴンガスの封入
・排気を行なう言わゆるアルゴンフラシュを行なう方法
(仕様B)とアルゴンフラシュを行なわない方法(仕様
A)及びアルゴンフラシュを行ない、かつその後の排気
能力を高めた(排気速度を20係向上)方法(仕様C)
と、この発明の排気加熱炉の前半と後半に電極の分解活
性化する方法(仕様D)との四方法で排気工程を終了さ
せ、その後高周波加熱装置により水銀放出素子とゲッタ
ーとを950℃30秒加熱して水銀を管内に放するとと
もにゲッターを活性化させ、以下通常の方法でランプを
製造し特性を測定した結果を表1に示す。This sealed valve is heated in an exhaust furnace in the conventional manner, and the electrode is decomposed and activated after the heating furnace, and argon gas is sealed in and exhausted during that process, which is the so-called argon flush method (specification B). A method in which argon flushing is not performed (Specification A), and a method in which argon flush is performed and the subsequent exhaust capacity is increased (increasing the exhaust speed by 20 factors) (Specification C).
The exhaust process is completed by four methods: 1) and a method of activating the decomposition of the electrode in the first and second half of the exhaust heating furnace of this invention (specification D), and then the mercury releasing element and getter are heated to 950°C and 30°C using a high-frequency heating device. The lamp was heated for seconds to release mercury into the tube and activate the getter, and then a lamp was manufactured in the usual manner and its characteristics were measured. Table 1 shows the results.
また、水銀を電極処理の途中で滴下機(ド:ロツハー)
より滴下させ、水銀フラッシュをさせる従来の一般的な
方法(仕様E)で製造したランプも比較測定した。In addition, mercury is added using a dropping machine (Rotsher) during electrode treatment.
Comparative measurements were also carried out on lamps manufactured by the conventional general method (specification E) of dripping and flashing mercury.
尚、封入ガスは全てアルゴンを使用した。Note that argon was used as the filler gas in all cases.
表1に於ては、管端部の黒化発生度は点灯初期を0級、
寿命末期の黒化発生度を5.0級として黒化を級数分け
して発生度を示している。In Table 1, the degree of blackening at the end of the tube is grade 0 at the initial stage of lighting;
The degree of occurrence of blackening at the end of life is set as 5.0 grade, and the degree of occurrence of blackening is divided into series.
仕様Aのものは残留不純ガスが多いため放電開始電圧、
初光束、光束維持率、黒化発生度とも悪く、アルゴン・
フラシュを行なったもの(仕様Bは諸將性とも改良方向
にあるが、水銀の滴下を用いる従来法(仕様E)程度の
特性にするためには排気腸性の改良等の設備の改造が必
要となる(仕様C)。Specification A has a large amount of residual impurity gas, so the discharge starting voltage
The initial luminous flux, luminous flux maintenance rate, and incidence of blackening are poor, and argon
Flushed products (Specification B has improved in all properties, but in order to achieve the characteristics of the conventional method using mercury dripping (Specification E), it is necessary to modify the equipment such as improving the evacuation property. (Specification C).
これらに対し、この発明の排気加熱炉の前半と後半とに
電極の分解活性化を行なう方法(仕様D)は前半の加熱
分解工程で大部分の電極分解ガスが放出され、このガス
は排気炉の加熱工程中でほとんど排気され、後半の電極
活性化時ガス放出が少いため封入ガスの封入位置では残
留不純ガスがほとんどなくなるため、簡単な方法であり
ながら良好な特性を得ることが出来た。On the other hand, in the method (specification D) in which electrode decomposition is activated in the first and second halves of the exhaust heating furnace of the present invention, most of the electrode decomposition gas is released in the first half thermal decomposition process, and this gas is Most of the gas is evacuated during the heating process, and there is little gas released during electrode activation in the latter half, so there is almost no residual impurity gas at the filling position, so it was possible to obtain good characteristics despite being a simple method.
実施例 2
実施例1と同様の方法で110ワツトラビツトスタート
形ランプを製作した。Example 2 A 110 Watt Rabbit Start type lamp was manufactured in the same manner as in Example 1.
仕様は実施例1の仕様C,D、Eの他に、仕様Fとして
排気加熱炉の前半と後半に分けて電極の分解活性化を行
なう方法に於て、後半の電極分解活性化工程あるいはそ
の工程に連らなる工程でアルゴンフラシュを行う方法で
もランプを製作した。In addition to Specifications C, D, and E in Example 1, the specifications are F, which is a method for activating electrode decomposition in the first half and second half of the exhaust heating furnace. The lamp was also manufactured using an argon flush method in the process.
特性結果を表2に示す。The characteristic results are shown in Table 2.
表2に於て仕様りは現在一般に使われている仕様C,E
より良好であるが、仕様Fは残留不純ガスが更に少くな
ったため仕様りより特性を更に向−トさせることが出来
た。In Table 2, the specifications are currently commonly used specifications C and E.
Although the performance was better, specification F had even less residual impurity gas, so it was possible to improve the characteristics even more than the specification.
なお、上記実施例においては、水銀供給素子としてT
i −Z r −Hg化合物を使用しているが、他の水
銀化合物、水銀合金でもよく、さらには水銀の粒を容器
に入れ、ランプ管内に封入したものでもよく、この場合
には容器を高周波加熱して切断し、水銀を管内に供出す
ればよいものである。In addition, in the above embodiment, T is used as the mercury supply element.
Although the i-Zr-Hg compound is used, other mercury compounds or mercury alloys may also be used. Furthermore, mercury particles may be placed in a container and sealed inside the lamp tube. In this case, the container may be exposed to high frequency All you have to do is heat it, cut it, and release the mercury into the tube.
以上のように、この発明はけい光ランプに必要最少量の
水銀をバラツキ小さく封入し、しかもランプ製造工程で
水銀蒸気を全く排出させないために、所定量の水銀放出
素子をランプ内に設置し、これを排気溶封後に加熱して
水銀を放出させてけい光ランプを製造する方法に於て、
従来の水銀滴下方法より排気時の残留不純ガスが多くな
り放電開始電圧、光束、黒化発生度等の特性が低下する
のを改良するために行ったものであり、その方法は排気
加熱炉の前半と後半に電極分解活性化処理を2分割して
行うというもので、排気装置等に特別の改善を行うこと
な〈従来の水銀滴下法の装置をそのまま使用できるなど
極めて簡単な方法で大きな効果を得ることができるもの
である。As described above, in order to fill a fluorescent lamp with the minimum amount of mercury necessary for small variations and to prevent mercury vapor from being emitted at all during the lamp manufacturing process, the present invention installs a predetermined amount of mercury emitting elements in the lamp. In the method of manufacturing a fluorescent lamp by heating this after exhaust gas sealing and releasing mercury,
This method was used to improve the characteristics such as discharge starting voltage, luminous flux, and degree of blackening due to the increase in residual impurity gas during exhaust compared to the conventional mercury dropping method. The electrode decomposition activation process is carried out in two parts, the first half and the second half.It is an extremely simple method with great effects, as it does not require any special improvements to the exhaust system, etc. (the conventional mercury dripping method equipment can be used as is). This is something that can be obtained.
またこの発明は水銀放出素子およびゲッターを使用する
方法の欠点、つまし電極処理工程で発生する不純ガスが
けい光体に吸着されてしまうという欠点を除去できるも
のであり、封入水銀量の一定化、特性の向上、製造装置
の簡略化など数々の効果を与えるものである。In addition, this invention can eliminate the drawbacks of the method using a mercury emitting element and getter, in that impurity gas generated in the blind electrode treatment process is adsorbed by the phosphor, and it is possible to stabilize the amount of encapsulated mercury. , it provides many effects such as improved characteristics and simplification of manufacturing equipment.
第1図は従来の排気装置を説明する平面図、第2図はこ
の発明方法を説明するための排気装置及びそれに連らな
る高周波誘導加熱装置を示す平面図である。
なお、 図中同一符号は同一または相当部分を示し、1
は排気装置、2はバルブ取付位置、3は加熱炉、4,4
′は第2の電極処理装置、6は水銀滴下位置、Iは不活
性ガス封入装置、8は排気管溶封装置、9はバルブ取出
し位置である。FIG. 1 is a plan view for explaining a conventional exhaust device, and FIG. 2 is a plan view for explaining the method of the present invention, showing an exhaust device and a high-frequency induction heating device connected thereto. In addition, the same reference numerals in the figures indicate the same or equivalent parts, and 1
is the exhaust system, 2 is the valve mounting position, 3 is the heating furnace, 4, 4
' is a second electrode processing device, 6 is a mercury dropping position, I is an inert gas filling device, 8 is an exhaust pipe melt sealing device, and 9 is a valve extraction position.
Claims (1)
た電極と、この電極近傍に設置された水銀放出素子およ
び非蒸発性ゲッターと、排気管とを有するけい光ランプ
用バルブを備えたバルブの内部のガス抜きを前記排気管
を介して行なう排気工程、この排気工程の前段部と後段
部とに分けて前記電極に被着された電子放射性物質の加
熱分解活性処理を行なう電極処理工程、前記排気工程終
了後に所定圧の不活性ガスを前記バルブ内に封入する工
程、前記バルブ内に不活性ガスを封入後に前記排気管を
溶封する工程、この排気管の溶封工程終了後に前記水銀
放出素子から水銀をバルブ内に供出するとともにゲッタ
ーの活性化処理を行う工程とからなるけい光ランプの製
造方法。 2 排気工程における後段部の電極処理工程の所定時期
にバルブ内に不活性ガスを封入してバルブ内の排気を促
進させることを特徴とする特許請求の範囲第1項記載の
けい光ランプの製造方法。 3 排気工程の前段部における電極処理工程の開始は、
バルブ内の圧力が6トール以下のときとしたことを特徴
とする特許請求の範囲第1項または第2項記載のけい光
ランプの製造方法。 4 排気工程の前段部における電極処理工程の終りは、
バルブの温度が300℃を越えないところとしたことを
特徴とする特許請求の範囲第1項ないし第3項のいずれ
かに記載のけい光ランプの製造方法。[Claims] 1. Comprising a phosphor coated on the inner surface, an electrode provided at the inner end, a mercury emitting element and a non-evaporable getter installed near the electrode, and an exhaust pipe. An evacuation step in which gas is vented from the inside of a bulb equipped with a fluorescent lamp bulb via the exhaust pipe, and heating of the electron radioactive material deposited on the electrode is divided into a front stage and a rear stage of this exhaust step. an electrode treatment step for performing a decomposition activation treatment; a step for filling inert gas at a predetermined pressure into the valve after the exhaust step; a step for melt-sealing the exhaust pipe after filling the inert gas in the valve; A method for manufacturing a fluorescent lamp, comprising the steps of supplying mercury from the mercury emitting element into the bulb after the tube is melt-sealed, and activating the getter. 2. Manufacture of a fluorescent lamp according to claim 1, characterized in that an inert gas is sealed in the bulb at a predetermined time of the electrode treatment step in the latter stage of the exhaust step to promote exhaustion of the bulb. Method. 3 The start of the electrode treatment process in the first stage of the exhaust process is as follows:
3. The method of manufacturing a fluorescent lamp according to claim 1, wherein the method is performed when the pressure inside the bulb is 6 Torr or less. 4 At the end of the electrode treatment process in the first stage of the exhaust process,
A method for manufacturing a fluorescent lamp according to any one of claims 1 to 3, characterized in that the temperature of the bulb does not exceed 300°C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52008367A JPS5916697B2 (en) | 1977-01-28 | 1977-01-28 | How to manufacture fluorescent lamps |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52008367A JPS5916697B2 (en) | 1977-01-28 | 1977-01-28 | How to manufacture fluorescent lamps |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5448982A JPS5448982A (en) | 1979-04-17 |
| JPS5916697B2 true JPS5916697B2 (en) | 1984-04-17 |
Family
ID=11691258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52008367A Expired JPS5916697B2 (en) | 1977-01-28 | 1977-01-28 | How to manufacture fluorescent lamps |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5916697B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6055947B2 (en) * | 1976-07-14 | 1985-12-07 | 三菱電機株式会社 | Fluorescent lamp exhaust system |
-
1977
- 1977-01-28 JP JP52008367A patent/JPS5916697B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5448982A (en) | 1979-04-17 |
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