JP3484890B2 - Electrophoresis device - Google Patents
Electrophoresis deviceInfo
- Publication number
- JP3484890B2 JP3484890B2 JP22970196A JP22970196A JP3484890B2 JP 3484890 B2 JP3484890 B2 JP 3484890B2 JP 22970196 A JP22970196 A JP 22970196A JP 22970196 A JP22970196 A JP 22970196A JP 3484890 B2 JP3484890 B2 JP 3484890B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- film
- potential
- working electrode
- heater
- 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 - Fee Related
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- Electrodes For Cathode-Ray Tubes (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、新規な電気泳動法
で膜を形成するその装置に係わり、特に、ブラウン管陰
極加熱用ヒータの絶縁膜を形成する際に絶縁膜充填率を
高めた高性能ヒータを容易に生産することのできる電気
泳動装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for forming a film by a novel electrophoretic method, and more particularly, to a high performance in which an insulating film filling rate is increased when forming an insulating film of a heater for heating a cathode ray tube cathode. Electricity that can easily produce heaters
The present invention relates to an electrophoretic device .
【0002】[0002]
【従来の技術】従来から傍熱形及び含浸形のブラウン管
では陰極を加熱するヒータを有している。図2にヒータ
外観を示す。コイル状に巻いた金属線1を、絶縁膜2で
被覆し、絶縁膜2の外側にダーク層3を形成している。
ヒータはスリーブ4と呼ぶ筒状の金属覆いの中に位置し
ている。含浸形カソード用ヒータではヒータの頂部に含
浸形カソード5が配置されている。コイル部分の拡大断
面は図3になる。金属線は耐熱性を有する導電性材料、
例えばタングステン(W)やレニウム−タングステン合
金(Re−W)を用いている。金属線はまず素材自身の
ままで水素雰囲気中で加熱して表面を清浄にし、その後
に、金属線の表面にアルミナなどの絶縁物を電気泳動
法,吹き付け法,浸漬法などの手法を用いて形成する。
ヒータは金属線に通電して陰極加熱を行う。従って、ブ
ラウン管のオン,オフに伴って、通電時の1200℃前
後の高温と停止時の常温の温度環境下で繰り返し作動す
る。高温及び断続的通電の環境では、焼結によって絶縁
膜を構成する無機物の粒成長や絶縁膜の収縮が起こる。
その結果、絶縁膜の剥離やクラックが発生したり、金属
線同士が接触し短期間で絶縁不良が生じていた。また、
金属線の断線不良なども発生していた。それらを改善す
る手段として特開平3−37988号公報では電気泳動法での
電解質を目的に応じて選択し膜充填率を均一にした絶縁
膜を複数回形成し、強度及び絶縁特性を向上させ、絶縁
膜のクラックを防止し長寿命ヒータを得ている。特開平
7−220617 号公報では電気泳動法での膜形成電圧プロフ
ィールや電流密度を規定して、個々の空隙部を縮小・分
散させ高性能ヒータを得ている。2. Description of the Related Art Conventionally, indirectly heated cathode ray tubes and impregnated cathode ray tubes have a heater for heating a cathode. Fig. 2 shows the appearance of the heater. The metal wire 1 wound in a coil shape is covered with an insulating film 2, and a dark layer 3 is formed outside the insulating film 2.
The heater is located in a tubular metal cover called the sleeve 4. In the impregnated cathode heater, the impregnated cathode 5 is arranged on the top of the heater. An enlarged cross section of the coil portion is shown in FIG. Metal wire is a conductive material with heat resistance,
For example, tungsten (W) or rhenium-tungsten alloy (Re-W) is used. The metal wire is first heated in the hydrogen atmosphere as it is to clean the surface, and then an insulator such as alumina is applied to the surface of the metal wire by a method such as electrophoresis, spraying or dipping. Form.
The heater energizes the metal wire to heat the cathode. Therefore, as the cathode ray tube is turned on and off, the cathode ray tube repeatedly operates in a temperature environment of about 1200 ° C. when energized and at room temperature when stopped. In an environment of high temperature and intermittent energization, sintering causes grain growth of inorganic substances constituting the insulating film and contraction of the insulating film.
As a result, peeling or cracking of the insulating film has occurred, or metal wires have come into contact with each other, causing insulation failure in a short period of time. Also,
Defects in the metal wire were also broken. As a means for improving them, in JP-A-3-37988, an electrolyte in an electrophoretic method is selected according to the purpose to form an insulating film having a uniform film filling rate a plurality of times to improve strength and insulating properties, A long-life heater is obtained by preventing cracks in the insulating film. Kohei
In JP-A 7-220617, a film forming voltage profile and current density in the electrophoretic method are specified to reduce and disperse individual voids to obtain a high performance heater.
【0003】膜形成方法は溶射,蒸着,CVD(Chemic
al Vapor Deposition),吹き付け,浸漬塗布,電気泳
動法など各種方法があり、形成する膜の使用環境や生産
性に応じて選択されている。特に、電気泳動法は装置が
簡単で、数μm〜数mmの膜厚を容易に形成することがで
きるため、応用範囲が広い。Film forming methods include thermal spraying, vapor deposition, and CVD (Chemic
Al Vapor Deposition), spraying, dip coating, electrophoresis and various other methods, which are selected according to the use environment and productivity of the film to be formed. In particular, the electrophoresis method has a wide application range because the apparatus is simple and a film thickness of several μm to several mm can be easily formed.
【0004】[0004]
【発明が解決しようとする課題】金属線同士の接触防止
や絶縁特性の向上を図るには、金属線と金属線の間に充
填する絶縁物の割合を高めることが重要である。単位体
積当りの絶縁物の量が増加すれば絶縁特性が向上し、絶
縁物同士の接触点数も増加し膜強度も向上する。従来技
術では、電気泳動法での膜形成に用いる無機物を分散す
る液に添加する電解質を目的に応じて選択し、複数回の
膜形成と焼成を行い膜充填率を均一にした絶縁膜を形成
し、絶縁膜の強度及び絶縁特性を向上させて絶縁膜のク
ラックを防止していた。しかし、複数回の膜形成と焼成
を繰り返すため工程数多く、膜厚や塗布長さが調整しに
くくヒータ製作精度維持が困難などの問題点が生じた。
また、電源の膜形成電圧や電流を制御する方法では、膜
形成工程における液組成変動や液に浸漬するヒータの取
り付け精度による影響を受けやすい。そのため、たえ
ず、膜形成状態が安定しており、しかも、膜厚を1回の
工程で形成でき、1度に膜形成するヒータ本数が変化し
ても容易に補正できる、簡便な膜形成方法が望まれてい
た。In order to prevent contact between metal wires and to improve insulation characteristics, it is important to increase the ratio of the insulating material filled between the metal wires. When the amount of the insulating material per unit volume increases, the insulating property improves, the number of contact points between the insulating materials also increases, and the film strength also improves. In the conventional technology, an electrolyte to be added to a liquid in which an inorganic substance used for forming a film by electrophoresis is added is selected according to the purpose, and an insulating film having a uniform film filling rate is formed by performing film formation and firing a plurality of times. However, cracks in the insulating film have been prevented by improving the strength and insulating properties of the insulating film. However, since the film formation and firing are repeated a plurality of times, there are many steps, and it is difficult to adjust the film thickness and the coating length, and it is difficult to maintain the heater manufacturing accuracy.
Further, the method of controlling the film forming voltage or current of the power source is easily affected by the liquid composition variation in the film forming step and the mounting accuracy of the heater immersed in the liquid. Therefore, there is always a stable film formation state, and moreover, a simple film formation method capable of forming the film thickness in one step and easily correcting even if the number of heaters forming the film at one time changes. Was wanted.
【0005】[0005]
【課題を解決するための手段】本発明は、電源と、無機
物を分散させた分散液を溜める貯液容器と、該貯液容器
内の分散液を循環又は撹拌を行う装置と、無機物を被覆
する材料を保持する作用電極と、該作用電極に通電させ
る対電極と、標準水素電極電位を測定できる参照電極と
を備え、前記作用電極と対電極と参照電極は前記貯液容
器内の分散液と接し、前記作用電極と参照電極間の電位
又は前記作用電極と対電極間の電流を制御する制御装置
を有することを特徴とする電気泳動装置にある。 更に、
本発明は、電源と、無機物を分散させた分散液を溜める
貯液容器と、該貯液容器内の分散液を循環又は撹拌を行
う装置と、前記無機物を被覆する材料を保持する作用電
極と、該作用電極に通電させる対電極と、標準水素電極
電位を測定できる参照電極と、電解質溶液を溜めた外部
容器と、前記貯液容器内の分散液と外部容器内の電解質
溶液を電解質を介して電気的に連結する管とを備え、前
記作用電極と対電極は貯液容器内の分散液と接し、前記
貯液容器内の分散液と外部容器内の電解質溶液は電解質
を介して電気的に連結され、前記参照電極は前記外部容
器内の電解質溶液に接し、前記作用電極と参照電極間の
電位又は作用電極と対電極間の電流を制御する制御装置
を有することを特徴とする電気泳動装置にある。電気化
学の分野では作用電極,対電極,参照電極の3電極を用
いて分散液中のイオンの性質を調査したり、作用電極の
材質を変えて材料の種類とイオンの酸化や還元反応の測
定などを調査する手法として一般的である。本発明では
この手法を電気泳動に応用した。通常の電気泳動では分
散液中の帯電した粉末又はイオンの泳動速度が電圧に比
例するため、作用極と対極間に印加される電位差が重要
となる。又、粉末が帯電する際にpHによってイオンの
状態が異なるため、水素指数であるpHを測定する場合
がある。しかし、一般に行われる電気泳動法では電極界
面での反応は起りうるものとして、泳動速度もしくは泳
動量を調整する手段として作用極と対極間の電位差であ
る電源の電圧を調整する方法が主流である。pHは分散
液中の水素イオンの量を示す数値であり、水素を発生さ
せる電位とは直接関係がない。そのため、電気泳動では
参照電極を追加して標準水素電極電位を測定したり、そ
れを利用して膜を形成する製造方法が見当たらなかっ
た。SUMMARY OF THE INVENTION The present invention is a power supply and an inorganic material.
Reservoir container for storing dispersion liquid in which substances are dispersed, and the reservoir container
A device that circulates or stirs the dispersion liquid inside and coats inorganic substances
And a working electrode that holds the material to be energized
Counter electrode and a reference electrode that can measure the standard hydrogen electrode potential
And the working electrode, the counter electrode and the reference electrode are
The potential between the working electrode and the reference electrode in contact with the dispersion liquid in the vessel
Or a control device for controlling the current between the working electrode and the counter electrode
An electrophoretic device having: Furthermore,
The present invention stores a power source and a dispersion liquid in which an inorganic substance is dispersed.
Circulate or stir the liquid storage container and the dispersion liquid in the liquid storage container.
Device and a working electrode for holding the material coating the inorganic substance.
A pole, a counter electrode for energizing the working electrode, and a standard hydrogen electrode
Reference electrode that can measure electric potential and external with electrolyte solution
Container, dispersion in the reservoir and electrolyte in an outer container
And a tube for electrically connecting the solution through an electrolyte,
The working electrode and the counter electrode are in contact with the dispersion liquid in the liquid storage container,
The dispersion liquid in the storage container and the electrolyte solution in the outer container are the electrolyte
And the reference electrode is electrically connected to the external capacitor.
Between the working electrode and the reference electrode
Control device for controlling electric potential or current between working electrode and counter electrode
An electrophoretic device having: In the field of electrochemistry, using three electrodes, a working electrode, a counter electrode, and a reference electrode, the properties of ions in a dispersion liquid are investigated, and the material of the working electrode is changed to measure the type of material and the oxidation and reduction reaction of ions. It is a general method for investigating. In the present invention, this method was applied to electrophoresis. In ordinary electrophoresis, the migration speed of charged powder or ions in the dispersion is proportional to the voltage, so the potential difference applied between the working electrode and the counter electrode is important. In addition, since the state of ions varies depending on the pH when the powder is charged, pH, which is the hydrogen index, may be measured. However, in the generally performed electrophoretic method, the reaction at the electrode interface may occur, and the method of adjusting the voltage of the power source, which is the potential difference between the working electrode and the counter electrode, is the mainstream as a means for adjusting the migration speed or the migration amount. . The pH is a numerical value indicating the amount of hydrogen ions in the dispersion liquid and is not directly related to the potential for generating hydrogen. Therefore, in electrophoresis, a reference hydrogen electrode was added to measure the standard hydrogen electrode potential, or a manufacturing method for forming a film using it was not found.
【0006】本発明は電気泳動法での膜形成時に、標準
水素電極電位に対する作用電極電位を制御する、又は標
準水素電極電位に対する作用電極電位が設定値になるよ
うに作用電極と対電極間へ通電する電流を制御すること
により作用電極表面の状態を積極的に制御し高性能な膜
を容易に形成する。The present invention controls the working electrode potential with respect to the standard hydrogen electrode potential at the time of forming a film by the electrophoretic method, or moves between the working electrode and the counter electrode so that the working electrode potential with respect to the standard hydrogen electrode potential becomes a set value. The state of the surface of the working electrode is positively controlled by controlling the applied current, and a high-performance film is easily formed.
【0007】一般に標準水素電極電位は浸漬する電極の
材質,分散液の種類及び分散液中の電解質の価数や添加
量及び反応性などによって決定される。Generally, the standard hydrogen electrode potential is determined by the material of the electrode to be dipped, the type of dispersion, the valence of the electrolyte in the dispersion, the amount added, and the reactivity.
【0008】電気泳動法は、貯液容器中の分散液に電極
として作用電極と対電極を浸漬し通電すると、分散液中
で帯電した無機物が帯電した極性に応じた作用電極に泳
動し、作用電極上に付着し膜を形成する手法である。分
散液が水を含む場合、通電によって水の電気分解が起こ
り電極の極性が正の場合は酸素が、負の場合は水素が発
生する。これら気泡の発生が無機物の電極上への付着を
疎外する。気泡の発生を制御ができれば無機物の充填が
容易になり、高密度の膜を形成できる。図1に装置の概
略を示す。従来の電気泳動法での作用電極7,対電極8
の電極に加えて標準水素電極電位を測定出来る参照電極
9を追加している。作用電極電位が標準水素基準電位よ
り負電位では水素が発生する。電源12は参照電極9と
作用電極7間の電位を測定し、この電位が設定値になる
ように作用電極と対極間に流れる電流を制御することが
出来る。循環ポンプ13は貯液容器内の分散液を循環し
て分散液中の無機物の沈降を防止する。In the electrophoretic method, when a working electrode and a counter electrode as electrodes are immersed in a dispersion liquid in a reservoir and an electric current is applied thereto, an inorganic substance charged in the dispersion liquid migrates to a working electrode corresponding to a charged polarity, and acts. This is a method of forming a film by adhering on the electrode. When the dispersion liquid contains water, electrolysis of water is caused by energization, and oxygen is generated when the polarity of the electrode is positive, and hydrogen is generated when the polarity of the electrode is negative. The generation of these bubbles dissociates the adhesion of the inorganic substance on the electrode. If the generation of bubbles can be controlled, the inorganic material can be easily filled, and a high-density film can be formed. FIG. 1 shows an outline of the device. Working electrode 7 and counter electrode 8 in the conventional electrophoresis method
In addition to the above electrode, a reference electrode 9 capable of measuring the standard hydrogen electrode potential is added. Hydrogen is generated when the working electrode potential is more negative than the standard hydrogen reference potential. The power supply 12 can measure the potential between the reference electrode 9 and the working electrode 7, and can control the current flowing between the working electrode and the counter electrode so that this potential becomes a set value. The circulation pump 13 circulates the dispersion liquid in the storage container to prevent sedimentation of inorganic substances in the dispersion liquid.
【0009】一般に標準水素電極電位は浸漬する電極の
材質,分散液の種類及び分散液中の電解質の価数や添加
量及び反応性などによって決定される。従来技術では電
圧及び電流の制御は電源の機器電圧及び機器電流で行
い、標準水素電極電位に無関係の設定値で膜を形成す
る。そのため、同一種類の電極を用いて繰り返し膜形成
を実施する時には分散液の組成変動によって膜形態が異
なり、ヒータでは金属線に挟まれた部分(図3,6)の
無機物の充填度合が低下する傾向にあった。本発明の参
照電極から標準水素電極電位を求め、これを基に電位や
電流を制御して膜形成すれば、液の組成変動があっても
膜形態に大きな影響を及ぼす気泡の発生を制御できる。Generally, the standard hydrogen electrode potential is determined by the material of the electrode to be dipped, the type of dispersion, the valence of the electrolyte in the dispersion, the amount added, and the reactivity. In the prior art, control of voltage and current is performed by the device voltage and device current of the power supply, and the film is formed at a set value that is independent of the standard hydrogen electrode potential. Therefore, when the same type of electrode is repeatedly used to form a film, the film morphology varies depending on the composition variation of the dispersion liquid, and in the heater, the filling degree of the inorganic substance in the portion sandwiched by the metal wires (FIGS. 3 and 6) decreases. There was a tendency. If the standard hydrogen electrode potential is obtained from the reference electrode of the present invention and the potential or current is controlled based on this to form a film, it is possible to control the generation of bubbles that have a great influence on the film morphology even if the composition of the liquid changes. .
【0010】本発明では電気泳動法の際に参照電極を追
加し標準水素電極電位を求められるよう工夫し、それを
基にした膜形成電圧や電流を制御し膜形成を行うことに
より、作用電極上に発生する気泡を制御でき、金属線に
挟まれた部分に無機物を安定して充填させることができ
る。その結果、ヒータへの膜形成時には無機物に絶縁物
を用いることにより絶縁特性や機械的強度の向上を図る
ことができ、長寿命のヒータを得ることができる。又、
本発明は膜形成工程が1工程で済むため高精度のヒータ
を容易に作製できる。更に分散液組成が変動してもそれ
に応じた膜形成電圧や電流に制御でき、容易に高性能な
膜を形成できる。In the present invention, a reference electrode is added during the electrophoretic method so that the standard hydrogen electrode potential can be obtained, and the film formation voltage and current are controlled based on the reference electrode to form a film, thereby forming a working electrode. The bubbles generated above can be controlled, and the portion sandwiched by the metal wires can be stably filled with the inorganic substance. As a result, when a film is formed on the heater, an insulating material is used as an inorganic material, so that the insulation characteristics and mechanical strength can be improved, and a long-life heater can be obtained. or,
According to the present invention, since the film forming step is completed in one step, a highly accurate heater can be easily manufactured. Furthermore, even if the composition of the dispersion liquid changes, the film forming voltage and current can be controlled accordingly, and a high-performance film can be easily formed.
【0011】本発明は、電気泳動法で膜を形成する製品
に関わり、特にブラウン管陰極加熱用ヒータの絶縁膜を
形成する工程において、絶縁膜充填率を高めた高性能ヒ
ータを簡便な工程でかつ容易に生産する方法に関する。The present invention relates to a product in which a film is formed by an electrophoretic method, and particularly, in a process of forming an insulating film of a heater for heating a cathode ray tube cathode, a high-performance heater having an increased insulating film filling rate can be used in a simple and simple process. For easy production.
【0012】電気泳動法では被覆する無機物を分散させ
た液を使用する。この分散液中の無機物が時間とともに
沈降する。作用電極がミリ単位の大きさの場合は分散液
面直下で膜形成を行うため沈降による影響が大きい。そ
のため、図1の装置構成において、貯液容器内の分散液
は無機物の沈降防止のために分散液を循環させたり撹拌
する装置が必須となる。もちろん、作用電極に膜を形成
する時に分散液面の波が影響を与えないよう膜形成時は
循環や撹拌を停止してもよい。対電極は電位への影響が
少ない白金を用いることが望ましいが、分散液中へのイ
オンの溶出を考慮して導電性のある材料に変更しても構
わない。参照電極は水素電極,カロメル電極,銀・塩化
銀電極など各種の電極があるが、これらの出力する電位
を標準水素電極電位に換算できればいずれの電極を用い
てもよい。In the electrophoresis method, a liquid in which an inorganic substance to be coated is dispersed is used. Inorganic substances in this dispersion settle out over time. When the working electrode has a size in millimeters, the film is formed immediately below the surface of the dispersion liquid, so that the influence of sedimentation is large. Therefore, in the apparatus configuration of FIG. 1, it is essential that the dispersion liquid in the liquid storage container is a device that circulates or stirs the dispersion liquid in order to prevent sedimentation of inorganic substances. Of course, circulation and stirring may be stopped during the film formation so that the waves on the dispersion liquid surface do not affect the film formation on the working electrode. Although it is desirable to use platinum for the counter electrode, which has little influence on the potential, a conductive material may be used in consideration of the elution of ions into the dispersion liquid. There are various electrodes such as a hydrogen electrode, a calomel electrode, and a silver / silver chloride electrode as the reference electrode, and any electrode may be used as long as the output potential can be converted into a standard hydrogen electrode potential.
【0013】また、参照電極は作用電極との間が電解質
を介して導通が図られていれば機能を果たす。図4では
貯液容器11内の分散液10と同様組成の電解質溶液1
5をゼラチンや寒天などで固化させた管14によって外
部容器16内の電解質溶液15との間に導通を図り参照
電極と作用電極間の電位を測定出来る様にしている。参
照電極を外部に設置すると、参照電極から浸み出すイオ
ンの影響を防止できる。Further, the reference electrode functions when it is electrically connected to the working electrode through the electrolyte. In FIG. 4, an electrolyte solution 1 having the same composition as the dispersion liquid 10 in the liquid storage container 11
A tube 14 obtained by solidifying 5 with gelatin or agar is used to establish conduction with the electrolyte solution 15 in the outer container 16 so that the potential between the reference electrode and the working electrode can be measured. If the reference electrode is installed outside, it is possible to prevent the influence of ions leaching from the reference electrode.
【0014】膜形成時に水素発生電位又は酸素発生電位
以下に電位を制御することにより気泡の発生を防止しつ
つ膜形成を行うことができる。しかし、電気泳動法では
粉末を泳動させるための電位も必要なため、気泡発生量
を抑制しつつ充填率を高められる膜形成条件が必要にな
る。By controlling the electric potential to be equal to or lower than the hydrogen generation potential or the oxygen generation potential during the film formation, the film formation can be performed while preventing the generation of bubbles. However, since the electrophoretic method also requires a potential for migrating the powder, a film forming condition that can increase the filling rate while suppressing the amount of bubbles generated is necessary.
【0015】膜形成条件の検討では膜形成の良否を膜断
面の充填率で評価した。解析位置はヒータ断面の図3上
の金属線1に挟まれた部分6である。充填率は解析位置
の絶縁膜断面を撮影し、この写真上の全面積に対する無
機物断面積の占める割合である。金属線に挟まれた部分
6は、膜形成時に充填率が低くなりがちな部分である。
従って、この箇所の充填率を高めることが高性能膜を得
るために重要である。後述する実施例1の装置構成で膜
形成時の膜充填率を図5に示す。標準水素電極電位に対
する作用電極電位(vsNHE)の値が低い時に膜充填率
が高い傾向にあった。作用電極電位が高いと気泡の発生
量(この場合水素)が多く、膜の充填が阻害されるため
と考える。図5より作用電極電位を−6V(vsNHE)
以下にすると高充填の膜が得られる。望ましくは作用電
極電位が−3V(vsNHE)以下である。作用電極電位
が−6V(vsNHE)より高い場合は膜充填率が50%
に満たない。In the examination of film forming conditions, the quality of film formation was evaluated by the filling rate of the film cross section. The analysis position is a portion 6 sandwiched by the metal wires 1 on the heater cross section in FIG. The filling rate is the ratio of the cross-sectional area of the inorganic material to the total area on the photograph obtained by photographing the cross section of the insulating film at the analysis position. The portion 6 sandwiched by the metal wires is a portion having a low filling rate during film formation.
Therefore, it is important to increase the filling rate of this portion in order to obtain a high performance film. FIG. 5 shows the film filling rate at the time of film formation in the device configuration of Example 1 described later. When the value of the working electrode potential (vsNHE) with respect to the standard hydrogen electrode potential was low, the film filling rate tended to be high. It is considered that when the working electrode potential is high, the amount of bubbles generated (hydrogen in this case) is large and the filling of the membrane is hindered. From Figure 5, the working electrode potential is -6V (vsNHE)
A highly filled film can be obtained by the following. Desirably, the working electrode potential is −3 V (vsNHE) or less. When the working electrode potential is higher than -6V (vsNHE), the film filling rate is 50%.
Less than
【0016】図6に作用電極電位(vsNHE)と膜形成
速度の関係を示す。作用電極電位(vsNHE)と膜形成
速度は比例関係にある。高充填の膜が得られる作用電極
電位が低い条件では成膜速度が遅い。そこで高充填の必
要な金属線に挟まれた部分の膜形成時の作用電極電位を
−6V(vsNHE)以下にし、金属線に挟まれた部分に
膜が形成された後は作用電極電位を高くして成膜速度を
高めて所定の膜厚まで膜を形成すると、金属線に挟まれ
た部分が高充填の膜が短時間で形成出来る。高充填の膜
を得るには標準水素電極電位に対する作用電極電位を−
6V(vsNHE)以下に制御することが必要である。電
流制御で膜形成する場合も標準水素電極電位に対する作
用電極電位が−6V(vsNHE)以下であれば同様の効
果が得られる。FIG. 6 shows the relationship between the working electrode potential (vsNHE) and the film formation rate. The working electrode potential (vsNHE) is proportional to the film formation rate. The deposition rate is low under the condition that the working electrode potential is low to obtain a highly filled film. Therefore, the working electrode potential at the time of film formation of the portion sandwiched between the metal wires that need to be highly filled is set to -6 V (vsNHE) or less, and the working electrode potential is increased after the film is formed in the portion sandwiched by the metal wires. Then, when the film formation speed is increased to form the film to a predetermined film thickness, the film sandwiched between the metal wires and highly filled can be formed in a short time. To obtain a highly filled membrane, the working electrode potential should be
It is necessary to control the voltage to 6 V (vs NHE) or less. Even when a film is formed by current control, the same effect can be obtained if the working electrode potential with respect to the standard hydrogen electrode potential is -6 V (vsNHE) or less.
【0017】本発明の電気泳動装置を用いることにより
前記導電材料又は前記導電膜に挟まれた無機物多孔質膜
の断面充填率が55%以上を70%以上の歩留まりでブ
ラウン管加熱用ヒータを作製できる。 特に、少なくとも
通電後1秒以内の標準水素電極電位に対する作用電極電
位が−6V以下であること、少なくとも通電後1秒以内
の標準水素電極電位に対する作用電極電位が−6V以下
で、かつ通電時間の経過につれて作用電極電位の絶対値
を増加させることが好ましい。 耐熱性を有する導電材料
または導電膜を有する絶縁材料に無機物の多孔質膜を前
述の電気泳動装置を用いて形成することにより10 -7 P
a以下の雰囲気で電圧6.3V以上7.6V以下を印加し
て八千時間以上動作できる割合が90%以上であるブラ
ウン管加熱用ヒータを得ることができる。 本発明は、蛍
光面と、前記蛍光面に対向して設けられた電子銃,前記
電子銃はスリーブ,前記スリーブ先端に配設された陰極
ペレットと前記スリーブ内に装着された陰極加熱用ヒー
タを備え、前記ヒータは無機絶縁物を被覆した陰極加熱
用ヒータを備えたブラウン管において、陰極加熱用ヒー
タに前述のヒータを用いたことを特徴とする。本装置は
ブラウン管用ヒータに限らず、通電時に気泡の発生を伴
う分散媒を使用した電気泳動法に応用できる。 By using the electrophoresis apparatus of the present invention
Inorganic porous film sandwiched between the conductive material or the conductive film
If the cross-section filling rate of 55% or more is higher than 70%,
A heater for heating a round tube can be manufactured. Especially at least
Working electrode voltage against standard hydrogen electrode potential within 1 second after energization
Must be -6V or less, at least 1 second after energization
Working electrode potential is -6V or less with respect to standard hydrogen electrode potential of
And the absolute value of the working electrode potential
Is preferably increased. Conductive material with heat resistance
Alternatively, an insulating material having a conductive film is coated with an inorganic porous film.
By using the above-mentioned electrophoretic device to form 10 -7 P
Apply a voltage of 6.3V or more and 7.6V or less in an atmosphere of a or less.
90% or more of the bras that can operate for over 8,000 hours
It is possible to obtain a heater for heating untube. The present invention
An electron gun provided opposite to the light surface and the fluorescent surface,
The electron gun is a sleeve, and the cathode is arranged at the tip of the sleeve.
The pellet and the cathode heating heater mounted in the sleeve.
And the heater is a cathode heater coated with an inorganic insulator.
In cathode ray tubes equipped with a heater for cathode,
The above-mentioned heater is used for the battery. This device is not limited to the cathode ray tube heater, but can be applied to an electrophoretic method using a dispersion medium in which bubbles are generated when energized.
【0018】[0018]
(実施例1)直径30μmの3%Re−W金属線を直径
110μmのMo金属芯線に巻きヒータコイルとした。(Example 1) A 3% Re-W metal wire having a diameter of 30 µm was wound on a Mo metal core wire having a diameter of 110 µm to form a heater coil.
【0019】分散液は電解質成分のAl(NO3)3,M
g(NO3)2・6H2O をエタノール水溶液8リットル
に溶解し、無機物として純度99.9% 以上の平均粒径
4μmのアルミナ(Al2O3)粉末を9kg配合した。The dispersion is composed of Al (NO 3 ) 3 , M as an electrolyte component.
g (NO 3) the 2 · 6H 2 O was dissolved in aqueous ethanol solution 8 l, average particle size 4μm of alumina (Al 2 O 3) having a purity of 99.9% or more as inorganic powder was 9kg formulation.
【0020】図1の装置構成でヒータコイル30本を作
用電極とし、アルミニウム電極を対電極として接続し、
参照電極は銀・塩化銀を飽和KClに浸漬した電極(A
g/AgCl/飽和KCl)を使用した。この参照電極
と標準水素電極(NHE)の電位とは0.199V(vsN
HE)の関係にある。分散液に各電極を浸漬し作用電極
電位を−5V(vsNHE)一定で10秒間通電して膜形
成した。In the apparatus configuration of FIG. 1, 30 heater coils are used as working electrodes and aluminum electrodes are connected as counter electrodes,
The reference electrode is an electrode in which silver / silver chloride is immersed in saturated KCl (A
g / AgCl / saturated KCl) was used. The potentials of the reference electrode and the standard hydrogen electrode (NHE) are 0.199V (vsN
HE). Each electrode was immersed in the dispersion liquid, and the working electrode potential was kept at -5 V (vsNHE) constant for 10 seconds to form a film.
【0021】その後、平均粒径1μm,純度99.9%
以上のタングステン粉末を分散懸濁した液で浸漬塗布し
ダーク層を形成した。Thereafter, the average particle size is 1 μm and the purity is 99.9%.
A liquid in which the above tungsten powder was dispersed and suspended was applied by dip coating to form a dark layer.
【0022】次いで、これを1600℃の水素雰囲気中
で5分間焼成した。焼成後のダーク層を含む絶縁膜厚は
110μmであった。Next, this was baked in a hydrogen atmosphere at 1600 ° C. for 5 minutes. The insulating film thickness including the dark layer after firing was 110 μm.
【0023】焼成終了後、Mo金属芯線を硝酸と硫酸と
の混合液により溶解除去し、水洗い,乾燥してヒータを
作製した。After firing, the Mo metal core wire was dissolved and removed with a mixed solution of nitric acid and sulfuric acid, washed with water and dried to prepare a heater.
【0024】比較のためのアルミナ膜形成条件は、比較
例1では、機器電圧80Vで3秒間通電し、比較例2で
は電流密度を0.35mA/mm2で10秒、1.5mA/m
m2で2秒通電した。両ヒータはその後ダーク層塗布及び
水素雰囲気中で焼成しMo芯線除去を実施したヒータで
ある。The conditions for forming the alumina film for comparison are as follows. In Comparative Example 1, a device voltage of 80 V is applied for 3 seconds, and in Comparative Example 2, the current density is 0.35 mA / mm 2 for 10 seconds and 1.5 mA / m.
Electricity was applied for 2 seconds at m 2 . Both heaters are heaters after which a dark layer is applied and fired in a hydrogen atmosphere to remove the Mo core wire.
【0025】本実施例と比較例のヒータの膜断面の金属
線に挟まれた部分6の充填率をヒータ1ケについて4視
野の測定を行い平均値を求めた。この測定を各々ヒータ
20個について算出した。その結果を表1に示す。The filling rate of the portion 6 sandwiched between the metal wires in the film cross sections of the heaters of this example and the comparative example was measured in four fields of view for one heater, and the average value was obtained. This measurement was calculated for each of 20 heaters. The results are shown in Table 1.
【0026】[0026]
【表1】 [Table 1]
【0027】測定全体の平均充填率は、比較例1が40
%、比較例2が55%、本実施例が57%であった。平
均充填率が55%以上のヒータの歩留まりは、比較例1
が0%、比較例2が55%、本実施例が75%となっ
た。The average filling rate of the whole measurement is 40 in Comparative Example 1.
%, Comparative Example 2 was 55%, and this Example was 57%. The yield of heaters having an average filling rate of 55% or more is shown in Comparative Example 1
Was 0%, Comparative Example 2 was 55%, and this Example was 75%.
【0028】本実施例と比較例のヒータを寿命試験に供
試した時のヒータ電流,リーク電流を図7に示す。寿命
試験ではヒータ使用電圧6.3Vより高い電圧7.6Vで
行った。通電のサイクルは5分通電し、15分休止を繰
り返す。絶縁膜の劣化やクラックの発生などがあるとリ
ーク電流は増加し、ヒータ電流は減少する。比較例1で
は寿命試験時間四千時間を超えるとリーク電流の増加,
ヒータ電流の低下が認められるの対して、比較例2及び
本発明のヒータでは六千時間まで変化がない。又、各々
百個のヒータを寿命試験に供したときの歩留まりを図8
に示す。ここでの歩留まりは、寿命試験中にヒータ電流
の減少やリーク電流の増加が規定値を超えたヒータを除
外し正常動作しているヒータの割合である。寿命試験八
千時間の歩留まりは、比較例1では0%、比較例2では
80%に対して、本発明では92%である。本発明品は
従来ヒータと比較して耐久性に優れ、信頼性が高い。FIG. 7 shows the heater current and the leak current when the heaters of this example and the comparative example were subjected to the life test. The life test was performed at a voltage of 7.6 V, which is higher than the heater operating voltage of 6.3 V. In the energization cycle, energization is carried out for 5 minutes, and rest for 15 minutes is repeated. If the insulating film deteriorates or cracks occur, the leak current increases and the heater current decreases. In Comparative Example 1, when the life test time exceeds 4000 hours, the leak current increases,
In contrast to the decrease in the heater current, in the heaters of Comparative Example 2 and the present invention, there is no change until 6,000 hours. In addition, the yield when each of the 100 heaters was subjected to the life test is shown in FIG.
Shown in. The yield here is the ratio of the heaters that are operating normally excluding the heaters in which the decrease in the heater current or the increase in the leak current exceeds the specified value during the life test. The yield of the life test 8,000 hours is 0% in Comparative Example 1, 80% in Comparative Example 2, and 92% in the present invention. The product of the present invention has excellent durability and high reliability as compared with the conventional heater.
【0029】また、本発明と比較例2において分散液を
交換しないで連続して膜形成した時の膜形成回数と絶縁
膜不良率を図9に示す。比較例2では百回付近から不良
率の増加が見られるのに対して、本発明のヒータでは2
88回でも不良発生率は低く、標準水素電極電位を基準
にした作用電極電位の制御により同一液を用いて多数回
膜形成したときでも不良発生率が低く安定した生産が可
能になる。FIG. 9 shows the number of times of film formation and the insulating film defect rate when the film was continuously formed without exchanging the dispersion liquid in the present invention and Comparative Example 2. In Comparative Example 2, the defect rate increases from around 100 times, while in the heater of the present invention,
The defect occurrence rate is low even after 88 times, and the defect occurrence rate is low even when a film is formed many times by using the same liquid by controlling the working electrode potential based on the standard hydrogen electrode potential, and stable production is possible.
【0030】(実施例2)実施例1と同様に作製したヒ
ータコイル30本を参照電極を外部に設置した装置構成
(図4)で作用電極電位を−4V(vsNHE)で11秒
間通電して膜形成した。その後、実施例1と同様な工程
でヒータを作成し、寿命試験に行った結果、実施例1と
同じ結果が得られた。(Embodiment 2) 30 heater coils manufactured in the same manner as in Embodiment 1 were energized at a working electrode potential of -4 V (vsNHE) for 11 seconds in an apparatus configuration (FIG. 4) in which a reference electrode was installed outside. A film was formed. After that, a heater was produced in the same process as in Example 1 and a life test was performed. As a result, the same result as in Example 1 was obtained.
【0031】(実施例3)実施例1と同様に作製したヒ
ータコイル30本を作用電極とし、膜形成時の作用電極
電位を−3V(vsNHE)から−0.5V (vsNHE)
/秒の割合で電位を増加させ合計7秒間通電して膜を形
成した。最終の作用電極電位が−6.5V(vsNHE)
である。その後、実施例1と同様な工程でヒータを作成
し、寿命試験に行った結果、実施例1と同じ結果が得ら
れた。(Embodiment 3) Thirty heater coils manufactured in the same manner as in Embodiment 1 are used as working electrodes, and the working electrode potential during film formation is from -3V (vsNHE) to -0.5V (vsNHE).
The potential was increased at a rate of / sec and a current was applied for a total of 7 seconds to form a film. Final working electrode potential is -6.5V (vsNHE)
Is. After that, a heater was produced in the same process as in Example 1 and a life test was performed. As a result, the same result as in Example 1 was obtained.
【0032】(実施例4)図10はブラウン管の断面図
である。ブラウン管は漏斗状をしたガラス管で、電子銃
17と蛍光面18を封入してある。ガラスバルブは膨ら
んだコーン部と細い円筒状のネック部から構成され、コ
ーン部の底に蛍光体(電子銃照射により蛍光する物質)
が塗布されており、高真空で封入されている。電子銃1
7は、本発明の膜形成法を用いて製作された陰極加熱用
ヒータ19によって電子を放出する陰極20、その電子
の流束をまとめて電子ビームとして高速度に加速すると
共に、蛍光面上に収束するための円筒電極(グリッド)
21から構成されている。偏向ヨーク22,アノードボ
タン23を備え、ネック部やコーン部の内面には導電膜
24(蛍光面18を覆っているアルミニウム膜)が形成
されている。電子銃17の後方には電気接続のソケット
ピン25が設けられている。(Embodiment 4) FIG. 10 is a sectional view of a cathode ray tube. The cathode ray tube is a funnel-shaped glass tube in which an electron gun 17 and a fluorescent screen 18 are enclosed. The glass bulb consists of a bulging cone and a thin cylindrical neck, and the bottom of the cone is a phosphor (a substance that fluoresces when irradiated with an electron gun).
Is applied, and it is enclosed in a high vacuum. Electron gun 1
Reference numeral 7 denotes a cathode 20 which emits electrons by a heater 19 for heating a cathode manufactured by using the film forming method of the present invention, and the flux of the electrons is collectively accelerated as an electron beam at a high speed, and at the same time, a fluorescent screen is formed. Cylindrical electrode (grid) for focusing
21. A deflection yoke 22 and an anode button 23 are provided, and a conductive film 24 (aluminum film covering the fluorescent screen 18) is formed on the inner surfaces of the neck portion and the cone portion. A socket pin 25 for electrical connection is provided behind the electron gun 17.
【0033】ヒータを組み込んだブラウン管は実施例1
に示す様に長寿命作動が可能になり、その信頼性も向上
した。The cathode ray tube incorporating the heater is the first embodiment.
As shown in, long life operation is possible and its reliability is improved.
【0034】[0034]
【発明の効果】本発明は電気泳動法での膜形成時に標準
水素電極電位を基に測定・制御することにより高密度の
膜を簡単な工程で容易に形成できる方法である。特にブ
ラウン管陰極加熱用ヒータの絶縁膜を形成する工程にお
いて、絶縁膜充填率を高め絶縁膜強度及び絶縁特性を向
上させた高性能ヒータを容易に生産することができヒー
タを備えたブラウン管には高信頼性と長寿命の効果があ
る。The present invention is a method for easily forming a high-density film in a simple process by measuring and controlling it based on the standard hydrogen electrode potential when forming a film by electrophoresis. Especially in the process of forming the insulating film of the heater for cathode ray tube cathode heating, it is possible to easily produce a high-performance heater having an increased insulating film filling rate and improved insulating film strength and insulating characteristics. Has the effect of reliability and long life.
【図1】電気泳動法で膜形成時の参照電極を加えた装置
のブロック図。FIG. 1 is a block diagram of an apparatus in which a reference electrode is added when a film is formed by an electrophoretic method.
【図2】ヒータの断面図。FIG. 2 is a sectional view of a heater.
【図3】ヒータコイル部分拡大膜の断面図。FIG. 3 is a cross-sectional view of a heater coil partial enlarged film.
【図4】電気泳動法で膜形成時の参照電極を外部に設置
した時の装置のブロック図。FIG. 4 is a block diagram of an apparatus in which a reference electrode at the time of film formation by an electrophoretic method is installed outside.
【図5】電気泳動法時の水素基準電位と膜充填率の特性
図。FIG. 5 is a characteristic diagram of hydrogen reference potential and membrane filling rate during electrophoresis.
【図6】電気泳動法時の水素基準電位と膜厚の関係の特
性図。FIG. 6 is a characteristic diagram showing the relationship between hydrogen reference potential and film thickness during electrophoresis.
【図7】リーク電流とヒータ電流の寿命時間変化の特性
図。FIG. 7 is a characteristic diagram showing changes in the leak current and the heater current over a lifetime.
【図8】歩留まりの寿命時間変化の特性図。FIG. 8 is a characteristic diagram of a change in yield over time.
【図9】電気泳動法による膜形成回数と絶縁膜不良率の
特性図。FIG. 9 is a characteristic diagram of the number of times of film formation by an electrophoretic method and the insulating film defect rate.
【図10】ブラウン管断面図。FIG. 10 is a sectional view of a cathode ray tube.
7…作用電極、8…対極、9…参照電極、10…分散
液、11…貯液容器、12…電源、13…分散液循環ポ
ンプ。7 ... Working electrode, 8 ... Counter electrode, 9 ... Reference electrode, 10 ... Dispersion liquid, 11 ... Storage container, 12 ... Power supply, 13 ... Dispersion liquid circulation pump.
フロントページの続き (72)発明者 柴田 倫秀 千葉県茂原市早野3300番地 株式会社 日立製作所 電子デバイス事業部内 (56)参考文献 特開 平7−220617(JP,A) (58)調査した分野(Int.Cl.7,DB名) C25D 13/02 C25D 13/22 H01J 1/22 H01J 9/08 H01J 29/04 Front page continued (72) Inventor Norihide Shibata 3300 Hayano, Mobara-shi, Chiba Hitachi, Ltd. Electronic Device Division (56) Reference JP-A-7-220617 (JP, A) (58) Fields investigated ( Int.Cl. 7 , DB name) C25D 13/02 C25D 13/22 H01J 1/22 H01J 9/08 H01J 29/04
Claims (2)
る貯液容器と、該貯液容器内の分散液を循環又は撹拌を
行う装置と、前記無機物を被覆する材料を保持する作用
電極と、該作用電極に通電させる対電極と、標準水素電
極電位を測定できる参照電極とを備え、前記作用電極と
対電極と参照電極は前記貯液容器内の分散液と接し、前
記作用電極と参照電極間の電位又は前記作用電極と対電
極間の電流を制御する制御装置を有することを特徴とす
る電気泳動装置。 And 1. A power, a reservoir container for storing a dispersion obtained by dispersing an inorganic substance, a device for performing the circulation or stirring the dispersion in the reservoir vessel, acts to retain the material covering the inorganic an electrode, a counter electrode Ru is energized to the working electrode, and a reference electrode capable of measuring the standard hydrogen electrode potential, the reference electrode and the working electrode and the counter electrode is in contact with a dispersion of the liquid storage container, before
It is characterized in that it has a control device for controlling the current between the potential or the working electrode and the counter electrode between the serial working and reference electrodes
Electrophoresis device.
る貯液容器と、該貯液容器内の分散液を循環又は撹拌を
行う装置と、前記無機物を被覆する材料を保持する作用
電極と、該作用電極に通電させる対電極と、標準水素電
極電位を測定できる参照電極と、電解質溶液を溜めた外
部容器と、前記貯液容器内の分散液と外部容器内の電解
質溶液を電解質を介して電気的に連結する管とを備え、
前記作用電極と対電極は貯液容器内の分散液と接し、前
記貯液容器内の分散液と外部容器内の電解質溶液は電解
質を介して電気的に連結され、前記参照電極は前記外部
容器内の電解質溶液に接し、前記作用電極と参照電極間
の電位又は作用電極と対電極間の電流を制御する制御装
置を有することを特徴とする電気泳動装置。 2. A power, a reservoir container for storing a dispersion obtained by dispersing an inorganic substance, a device for performing the circulation or stirring the dispersion in the reservoir vessel, acts to retain the material covering the inorganic an electrode, a counter electrode Ru is energized to the working electrode, a reference electrode capable of measuring the standard hydrogen electrode potential, an external container reservoir electrolyte solution, the electrolyte solution of the dispersion liquid and the external container of the liquid storage container And a tube electrically connected through the electrolyte ,
The working electrode and the counter electrode is in contact with a dispersion of the liquid storage container, before
Serial electrolytic solution of the dispersion liquid and the external container in reservoir container is electrically connected through the electrolyte, the reference electrode is in contact with the electrolyte solution in the outer container, the potential between the reference electrode and the working electrode or Control device for controlling the current between the working electrode and the counter electrode
An electrophoretic device having a storage device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22970196A JP3484890B2 (en) | 1996-08-30 | 1996-08-30 | Electrophoresis device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22970196A JP3484890B2 (en) | 1996-08-30 | 1996-08-30 | Electrophoresis device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH1074463A JPH1074463A (en) | 1998-03-17 |
| JP3484890B2 true JP3484890B2 (en) | 2004-01-06 |
Family
ID=16896352
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22970196A Expired - Fee Related JP3484890B2 (en) | 1996-08-30 | 1996-08-30 | Electrophoresis device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3484890B2 (en) |
-
1996
- 1996-08-30 JP JP22970196A patent/JP3484890B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH1074463A (en) | 1998-03-17 |
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