JPS6220656B2 - - Google Patents
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- Publication number
- JPS6220656B2 JPS6220656B2 JP4091878A JP4091878A JPS6220656B2 JP S6220656 B2 JPS6220656 B2 JP S6220656B2 JP 4091878 A JP4091878 A JP 4091878A JP 4091878 A JP4091878 A JP 4091878A JP S6220656 B2 JPS6220656 B2 JP S6220656B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode material
- heating
- decomposition
- valve
- exhaust
- 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
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- 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、特に排
気工程における電子放射物質の加熱分解方法の改
良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, particularly to an improvement in a method for thermally decomposing an electron-emitting substance in an evacuation process.
近時、けい光ランプの電極に被着された炭酸バ
リウム(BaCO3)を含むアルカリ土類金属の複合
炭酸塩でなる電子放射物質(以下電極物質と称
す)を加熱分解する方法として、バルブを排気台
に取付け、バルブ内の排気が開始されたときよ
り、バルブが加熱炉によつて300℃近くまで加熱
される間に第1回目の加熱分解を行い、バルブが
加熱炉で最高温度にまで加熱された後に再び電極
物質を加熱して、第2回目の加熱分解を行うよう
にしたものが特開昭53−9082号公報で提案され
た。このものは第1回目の加熱分解で電極物質の
分解によつて放出される分解ガスの大半を放出さ
せるようにしたものであり、排気時間の短縮など
に効果がある。 Recently, bulbs have been developed as a method for thermally decomposing electron-emitting materials (hereinafter referred to as electrode materials) made of composite carbonates of alkaline earth metals including barium carbonate (BaCO 3 ) deposited on the electrodes of fluorescent lamps. When it is installed on an exhaust stand and the exhaust inside the valve starts, the first thermal decomposition is performed while the valve is heated to nearly 300℃ in the heating furnace, and the valve reaches its maximum temperature in the heating furnace. JP-A-53-9082 proposed a method in which the electrode material is heated again after being heated to perform a second thermal decomposition. This device is designed to release most of the decomposed gas released by the decomposition of the electrode material during the first thermal decomposition, and is effective in shortening the exhaust time.
しかしながら、上記の方法においては電極物質
の第1回目の分解は、バルブ内の不純ガスの影響
を避けるために、バルブ内の不純ガス圧が数トー
ルに減圧され、かつバルブ内面に被着されたけい
光体のガス放出が比較的少ない250〜300℃にバル
ブが加熱されるまでの極く限られた間に行うもの
であるから、熱い電極物質は自からが放出した分
解ガスの圧力の高いところでさらに加熱分解され
るようになり、そのため電極物質のうち例えば
BaCO3がBaOBaCO3等の固溶体を形成したり、ま
たBaCO3と電極のタングステンフイラメントコ
イルとの反応によつて生成される例えばBaxWOy
で表されるような中間層化合物を多く生成する欠
点があつた。このBaOBaCO3と表される固溶体は
電極物質の表面をシンター化させるので、電極物
質の第2回目の分解の妨げになるとともに、製品
になつた後電極物質の電子放射能を低下させる。
また中間層化合物は点灯中にバルブ内に酸素ガス
を放射させ、黒化特性等を損ねるものである。こ
のようなことから、第1回目の電極物質の分解時
には、電極を所望する加熱温度までに温度を高め
られず、必ずしも満足のゆく分解スケジユールを
得ることができなかつた。 However, in the above method, in the first decomposition of the electrode material, in order to avoid the influence of impure gas in the bulb, the pressure of impure gas in the bulb is reduced to several torr, and the impurity gas is deposited on the inner surface of the bulb. This is done for a very limited period of time until the bulb is heated to 250-300°C, when gas release from the phosphor is relatively low, so the hot electrode material is exposed to the high pressure of the decomposition gas released by itself. By the way, it is further thermally decomposed, and as a result, some of the electrode materials, e.g.
BaCO 3 forms a solid solution such as BaOBaCO 3 or BaxWOy, which is produced by the reaction of BaCO 3 with the tungsten filament coil of the electrode.
It had the disadvantage of producing a large amount of intermediate layer compounds as shown in the figure below. This solid solution, expressed as BaOBaCO 3 , sinteres the surface of the electrode material, which prevents the second decomposition of the electrode material and reduces the electron radioactivity of the electrode material after it is turned into a product.
Further, the intermediate layer compound causes oxygen gas to be emitted into the bulb during lighting, impairing the blackening properties and the like. For this reason, during the first decomposition of the electrode material, it was not possible to raise the temperature of the electrode to the desired heating temperature, and it was not always possible to obtain a satisfactory decomposition schedule.
この発明は、上記事情に鑑みてなされたもの
で、バルブ加熱工程の前段部に行われる電極物質
の加熱分解に際して、電極へ通電するための複数
の通電ポジシヨンの中途のポジシヨンで通電加熱
を停止し、一担電極物質の加熱を中断するととも
に、この間に不活性ガスによるフラツシユ排気を
行い、かつ加熱中断直後の通電で電極物質を最高
温度にまで加熱するようにし、電極物質のシンタ
ー化が防げ、かつ中間層化合物が適正に生成で
き、ランプ特性の改善が図れ、また排気時間の短
縮化も可能にしたけい光ランプの製造方法を提供
することを目的とする。 The present invention has been made in view of the above circumstances, and is designed to stop energization heating at an intermediate position among a plurality of energization positions for energizing the electrode during thermal decomposition of the electrode material performed in the first stage of the bulb heating process. , the heating of the one-carrying electrode material is interrupted, and during this time flash exhaust is performed using an inert gas, and the electrode material is heated to the maximum temperature by applying electricity immediately after the heating is interrupted, thereby preventing sintering of the electrode material, Another object of the present invention is to provide a method for manufacturing a fluorescent lamp, which can appropriately generate an intermediate layer compound, improve lamp characteristics, and shorten evacuation time.
以下この発明の詳細を図にしたがつて説明す
る。第1図はバルブが排気台に取り付けられた後
の排気スケジユールの状態を示すもので、図の横
軸は排気時間、縦軸における1は排気工程、2は
バルブ加熱工程で、イはバルブ温度が300℃の
点、ロは同じく最高温度に加熱された点を表し、
またハはこのバルブ加熱工程2の前段部、ニは同
じくその後段部を示している。3はアルゴンガス
をバルブ内に注入し再び排気するフラツシユ排気
工程、4は電極物質の加熱分解工程で、上記バル
ブ加熱工程2の前段部ハに行う第1回目の分解工
程41と後段部以降ニに行う第2回目の分解工程
42とからなり、かつ上記第1回目の分解工程4
1の中途には一担加熱を中断する分解停止部4b
を有している。5はバルブ内に所定量のアルゴン
ガスおよび水銀を封入する封入物封入工程、6は
排気管を溶断するチツプオフ工程である。 The details of this invention will be explained below with reference to the drawings. Figure 1 shows the state of the exhaust schedule after the valve is attached to the exhaust stand. The horizontal axis of the figure is the exhaust time, 1 on the vertical axis is the exhaust process, 2 is the valve heating process, and A is the valve temperature. represents the point at 300℃, and b represents the point heated to the highest temperature.
Further, C indicates the front stage of this valve heating step 2, and D also indicates the rear stage. 3 is a flash exhaust process in which argon gas is injected into the valve and exhausted again; 4 is a thermal decomposition process of the electrode material; the first decomposition process 41 is carried out in the first stage C of the above-mentioned valve heating process 2, and the subsequent stages are the subsequent stages. and a second decomposition step 42 carried out in the first decomposition step 4.
In the middle of 1, there is a decomposition stop part 4b that interrupts the heating.
have. Reference numeral 5 is a filler filling step in which a predetermined amount of argon gas and mercury are sealed in the valve, and 6 is a tip-off step in which the exhaust pipe is melted.
次に、この発明の一実施例を説明する。まずバ
ルブを排気台に取り付ける。次いで、バルブ内の
排気を行う排気工程1によつてバルブ内の不純ガ
スが4Torrに減圧されたならば、第1回目の分解
工程41により電極物質の加熱分解を開始する。
このとき、最初の加熱ポジシヨン4aでは、電極
物質を加熱分解する際の最高温度の70〜80%の加
熱温度で加熱分解させる。次に分解停止部4bで
電極物質の加熱分解を中断し、直ちにバルブ内に
数トールのアルゴンガスを注入し、再び排気する
フラツシユ排気工程3を実施する。この後、再び
電極物質の加熱分解を行うが、4cのポジシヨン
に最高加熱温度を配する。この場合、バルブ内の
不純ガス圧力の変化は第2図のAに示すようにな
る。つまり、最初の加熱分解4aで放出された分
解ガスの圧力は、次のポジシヨンが分解停止部4
bなので、電極物質の分解が行われず、しかも加
熱温度を最高温度の70〜80%としたから、従来の
ように連続的に加熱分解を行うスケジユールの場
合Bに比し、約80%程度に抑えられる。またアル
ゴンガスによるフラツシユ排気3を行うと、見か
け上のバルブ内圧力は鎖線Cで示すような高い圧
力の曲線を描く。しかし分解ガス等の不純ガスは
真空ポンプの排気速度の大きい領域で外に排出さ
れるので、フラツシユ排気3後直ちに加熱分解温
度の最高値を配しても、バルブ内不純ガス圧力は
従来のように高まらない。次にバルブ加熱工程2
でバルブ内に被着されたけい光体の加熱脱ガスを
行つた後、従来と同様に第2回目の分解工程42
を行うとともに、この第2回目の分解工程42時
にフラツシユ排気を行い、ついで封入物封入工程
5で水銀およびアルゴンガス封入し、チツプオフ
6を経て排気処理工程は終了する。 Next, one embodiment of the present invention will be described. First, attach the valve to the exhaust stand. Next, when the pressure of the impure gas inside the valve is reduced to 4 Torr by the exhaust step 1 in which the inside of the valve is evacuated, thermal decomposition of the electrode material is started in the first decomposition step 41.
At this time, in the first heating position 4a, the electrode material is thermally decomposed at a heating temperature of 70 to 80% of the maximum temperature at which the electrode material is thermally decomposed. Next, the thermal decomposition of the electrode material is interrupted in the decomposition stop section 4b, and immediately a flash exhaust step 3 is performed in which several torr of argon gas is injected into the valve and exhausted again. After this, the electrode material is thermally decomposed again, but the highest heating temperature is set at position 4c. In this case, the change in impure gas pressure within the valve becomes as shown in A of FIG. In other words, the pressure of the decomposed gas released in the first thermal decomposition 4a is such that the next position is the decomposition stop part 4.
B, the electrode material is not decomposed, and the heating temperature is set to 70 to 80% of the maximum temperature, so compared to the conventional schedule B in which thermal decomposition is performed continuously, the heating temperature is about 80%. It can be suppressed. Furthermore, when flush exhaust 3 is performed using argon gas, the apparent pressure inside the valve draws a high pressure curve as shown by the chain line C. However, since impure gases such as cracked gas are discharged outside when the pumping speed of the vacuum pump is high, even if the maximum thermal decomposition temperature is set immediately after flash pumping 3, the impure gas pressure inside the valve will remain the same as before. It doesn't increase. Next, valve heating step 2
After heating and degassing the phosphor deposited inside the bulb, a second decomposition step 42 is carried out as in the conventional method.
At the same time, flash evacuation is performed during the second decomposition step 42, and then mercury and argon gas are filled in the filler filling step 5, and after a tip-off step 6, the evacuation treatment step is completed.
このような排気工程によれば、第1回目の分解
工程41時のバルブ内の不純ガス圧を低く抑える
ことができるから、この第1回目の分解工程41
中に電極物質を分解温度の最高値で加熱分解して
も、電極物質がシンター化しないばかりか、中間
層化合物の生成量が過多になることを抑え得る。
したがつて、ランプ特性の良好なけい光ランプが
得られる。また第2回目の分解工程42で電極物
質を最高温度に加熱しないですむため、第2回目
の分解工程42中に放出される電極物質からの分
解ガス圧力を低くでき、排気時間をより短縮でき
る。 According to such an evacuation step, the impure gas pressure inside the valve during the first decomposition step 41 can be kept low;
Even if the electrode material is thermally decomposed at the highest decomposition temperature, not only will the electrode material not be sintered, but it can also be prevented from producing an excessive amount of the intermediate layer compound.
Therefore, a fluorescent lamp with good lamp characteristics can be obtained. In addition, since the electrode material does not need to be heated to the maximum temperature in the second decomposition step 42, the pressure of decomposed gas from the electrode material released during the second decomposition step 42 can be lowered, and the exhaust time can be further shortened. .
なお、分解停止部4bは分解工程の前段部41
の中途に設けることにより、電極物質の分解ガス
をフラツシユ排気と絡ませて効率的に排出できる
もので、前段部41であつても最初や最後ではバ
ルブ内の電極物質分解ガスを含めた不純ガス圧を
低める効果は小さい。 Note that the decomposition stop part 4b is a pre-stage part 41 of the decomposition process.
By providing it midway, the decomposed gas of the electrode material can be efficiently exhausted by entangling it with the flash exhaust, and even in the front stage 41, at the beginning and end, the pressure of impure gas including the decomposed gas of the electrode material in the valve is reduced. The effect of reducing this is small.
発明者等はこの発明ランプが従来問題となつて
いたランプ始動特性や、点灯後2000時間を経過す
るあたりから急速に進展する端部黒化(イエロー
バンド)に対し、従来方法に比べて著しい効果が
有ることを確認した。 The inventors believe that the lamp of this invention is significantly more effective than conventional methods in reducing lamp starting characteristics, which had been a problem in the past, and in preventing blackening of the edges (yellow band), which rapidly develops after 2,000 hours of lighting. I confirmed that there is.
以上説明したようにこの発明は、バルブ加熱工
程の前段部に行われる複数の通電加熱ポジシヨン
を通じて電極物質の分解に際して、その分解の中
途に一担加熱を停止するとともに、この間にフラ
ツシユ排気を行い、さらに加熱停止部直後の加熱
電極ポジシヨンで電極物質を最高温度に加熱する
ようにしたものであるから、電極物質のシンター
化および中間層化合物の生成量過多を防止でき、
ランプ特性の向上した蛍光ランプを提供すること
ができる。またバルブ加熱工程の後段部以降の分
解工程中に放出された分解ガス圧を高めずにすむ
ので、排気時間をより短縮できる効果も有する。 As explained above, in the present invention, when decomposing an electrode material through a plurality of energized heating positions performed in the first stage of the bulb heating process, the heating is temporarily stopped in the middle of the decomposition, and during this period, flash exhaust is performed, Furthermore, since the electrode material is heated to the maximum temperature at the heating electrode position immediately after the heating stop section, sintering of the electrode material and excessive generation of intermediate layer compounds can be prevented.
A fluorescent lamp with improved lamp characteristics can be provided. Furthermore, since it is not necessary to increase the pressure of the cracked gas released during the decomposition process after the latter part of the valve heating process, there is also an effect that the exhaust time can be further shortened.
第1図はこの発明の一実施例のタイムスケジユ
ールを示す説明図、第2図はバルブ内の不純ガス
圧力の変化を示す図である。
1は排気工程、2はバルブ加熱工程、3はフラ
ツシユ排気工程、4は電極物質加熱分解工程、4
bは分解停止部である。なお、各図中同一符号は
同一または相当部分を示す。
FIG. 1 is an explanatory diagram showing a time schedule of an embodiment of the present invention, and FIG. 2 is a diagram showing changes in impure gas pressure within a valve. 1 is an exhaust process, 2 is a valve heating process, 3 is a flash exhaust process, 4 is an electrode material thermal decomposition process, 4
b is a decomposition stop part. Note that the same reference numerals in each figure indicate the same or corresponding parts.
Claims (1)
るバルブ加熱工程の前段部と後段部以降とに分け
てそれぞれ設けた複数の通電加熱ポジシヨンによ
り電極を順次通電加熱し電極物質の分解を行うよ
うにしたけい光ランプの製造方法において、上記
バルブ加熱工程の前段部に配された通電加熱ポジ
シヨンの中途ポジシヨンを、通電加熱を一旦停止
する分解停止部とし、この分解停止部において不
活性ガスによるフラツシユ排気を行い、かつこの
フラツシユ排気直後の通電加熱ポジシヨンにて電
極物質を最高温度にまで加熱するようにしたこと
を特徴とするけい光ランプの製造方法。1. The electrodes are sequentially energized and heated to decompose the electrode material using a plurality of energization heating positions that are installed separately in the front and rear stages of the valve heating process in which the bulb is heated while the inside of the bulb is evacuated. In the method for manufacturing a fluorescent lamp, an intermediate position of the energization heating position disposed at the front stage of the bulb heating process is used as a decomposition stop section where the energization heating is temporarily stopped, and in this decomposition stop section, flash exhaust by inert gas is performed. A method for manufacturing a fluorescent lamp, characterized in that the electrode material is heated to a maximum temperature in an energized heating position immediately after the flash exhaust.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4091878A JPS54133771A (en) | 1978-04-07 | 1978-04-07 | Method of manufacturing fluorescent lamp |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4091878A JPS54133771A (en) | 1978-04-07 | 1978-04-07 | Method of manufacturing fluorescent lamp |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54133771A JPS54133771A (en) | 1979-10-17 |
| JPS6220656B2 true JPS6220656B2 (en) | 1987-05-08 |
Family
ID=12593870
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4091878A Granted JPS54133771A (en) | 1978-04-07 | 1978-04-07 | Method of manufacturing fluorescent lamp |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS54133771A (en) |
-
1978
- 1978-04-07 JP JP4091878A patent/JPS54133771A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54133771A (en) | 1979-10-17 |
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