JPH11135016A - Phosphor slurry applying device and applying device - Google Patents
Phosphor slurry applying device and applying deviceInfo
- Publication number
- JPH11135016A JPH11135016A JP29607197A JP29607197A JPH11135016A JP H11135016 A JPH11135016 A JP H11135016A JP 29607197 A JP29607197 A JP 29607197A JP 29607197 A JP29607197 A JP 29607197A JP H11135016 A JPH11135016 A JP H11135016A
- Authority
- JP
- Japan
- Prior art keywords
- slurry
- specific gravity
- viscosity
- tank
- sensor
- 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
- 239000002002 slurry Substances 0.000 title claims abstract description 103
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 230000005484 gravity Effects 0.000 claims abstract description 71
- 238000001514 detection method Methods 0.000 claims abstract description 10
- 238000000034 method Methods 0.000 claims description 7
- 238000007581 slurry coating method Methods 0.000 claims description 7
- 239000011248 coating agent Substances 0.000 claims description 2
- 238000000576 coating method Methods 0.000 claims description 2
- 238000012937 correction Methods 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 description 11
- 238000002347 injection Methods 0.000 description 8
- 239000007924 injection Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 4
- 241000270295 Serpentes Species 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 239000013256 coordination polymer Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Coating Apparatus (AREA)
- Formation Of Various Coating Films On Cathode Ray Tubes And Lamps (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、カラー陰極線管の
蛍光体膜作製工程における蛍光体スラリの比重・粘度を
一定に保つ蛍光体スラリ塗布装置及び蛍光体スラリ塗布
方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a phosphor slurry coating apparatus and a phosphor slurry coating method for maintaining the specific gravity and viscosity of a phosphor slurry in a process of forming a phosphor film of a color cathode ray tube.
【0002】[0002]
【従来の技術】従来の蛍光体スラリ塗布装置は、例えば
特開昭56−156639号公報に記載のように、スラ
リ液の比重を一定化するために、比重センサの検出出力
により高比重のスラリあるいは低比重のスラリ供給量を
制御していた。2. Description of the Related Art A conventional phosphor slurry coating apparatus is disclosed in, for example, Japanese Patent Application Laid-Open No. 56-156639, in order to stabilize the specific gravity of a slurry liquid by using a detection output of a specific gravity sensor. Alternatively, the supply amount of the slurry having a low specific gravity was controlled.
【0003】図3は、従来の蛍光体スラリディスペンサ
を一部破断したスラリ注入経路を示す図である。FIG. 3 is a diagram showing a slurry injection path in which a conventional phosphor slurry dispenser is partially broken.
【0004】ここで、ディスペンサタンク1内の蛍光体
スラリSは、注入時にはスネークポンプ2により送出ホ
ース3を通り注入電磁弁4をとしてパネル5内面へ、非
注入時には注入電磁弁4よりリターンホース6を通して
ディスペンサタンク1へ還流する。Here, the phosphor slurry S in the dispenser tank 1 passes through the delivery hose 3 by the snake pump 2 to the inside of the panel 5 as the injection solenoid valve 4 at the time of injection, and the return hose 6 from the injection electromagnetic valve 4 at the time of non-injection. To the dispenser tank 1 through
【0005】パネル5内面へ注入されたスラリSは、キ
ャリア9の高速回転により回収カバー10に集められ、
回収ホース11を通し回収スラリとしてディスペンサタ
ンク1に戻る。[0005] The slurry S injected into the inner surface of the panel 5 is collected by the recovery cover 10 by the high-speed rotation of the carrier 9.
It returns to the dispenser tank 1 as a collection slurry through the collection hose 11.
【0006】スラリSの一部は、ポンプ2によりバイパ
スホース8を通りミニホッパー13内に入る。A part of the slurry S enters the mini hopper 13 through the bypass hose 8 by the pump 2.
【0007】ミニホッパー13内に設けられた比重セン
サ14で検出された信号は電気信号に変換されコントロ
ーラ27に入る。The signal detected by the specific gravity sensor 14 provided in the mini hopper 13 is converted into an electric signal and enters the controller 27.
【0008】また、高比重のスラリ16を収容した高比
重タンク17と、低比重のスラリ18を収容した低比重
タンク19が設けられており、コントローラ27の信号
により、高比重のスラリ16と低比重のスラリ18がデ
ィスペンサタンク1内に補充される。A high specific gravity tank 17 containing a high specific gravity slurry 16 and a low specific gravity tank 19 containing a low specific gravity slurry 18 are provided, and the high specific gravity slurry 16 and the low specific gravity A slurry 18 having a specific gravity is refilled into the dispenser tank 1.
【0009】比重が上限・下限の中間の位置にある値の
スラリSが注入・回収の動作を繰り返すと、ディスペン
サタンク1内の液面レベルが下がるとともに比重も下が
り、液面レベルの下限あるいは比重の下限のどちらかに
達する。When the slurry S of a value whose specific gravity is intermediate between the upper limit and the lower limit repeats the operation of injecting and collecting, the liquid level in the dispenser tank 1 is lowered and the specific gravity is lowered, and the lower limit or the specific gravity of the liquid level is lowered. Reaches one of the lower limits.
【0010】このとき、コントローラ27の信号により
高比重のスラリ16が補充され、液面レベルとともに比
重も上昇する。液面レベル上限に達すると高比重のスラ
リ16が補充が停止し最初の状態になる。At this time, the slurry 16 having a high specific gravity is replenished by a signal from the controller 27, and the specific gravity increases with the liquid level. When the liquid level reaches the upper limit, the replenishment of the high specific gravity slurry 16 is stopped, and the slurry 16 returns to the initial state.
【0011】上限に達すると高比重のスラリ16が補充
が停止し最初の状態になる。When the upper limit is reached, the replenishment of the high specific gravity slurry 16 is stopped and the slurry 16 returns to the initial state.
【0012】液面レベルが途中で、比重が適正値に達す
ると、高比重のスラリ16の補充が停止し低比重のスラ
リ18に補給が切り替わり、比重を下げながら液面レベ
ル上限点に達すると、低比重のスラリ16の補充が停止
する。When the specific gravity reaches an appropriate value in the middle of the liquid level, the replenishment of the high specific gravity slurry 16 is stopped and the replenishment is switched to the low specific gravity slurry 18, and when the specific gravity reaches the liquid level upper limit point while decreasing the specific gravity. Then, the replenishment of the low specific gravity slurry 16 is stopped.
【0013】[0013]
【発明が解決しようとする課題】ところが、従来の方法
においては、常に比重・粘度の一定なスラリSの注入は
困難であり、粘度の変動によりパネル5内面に注入され
たスラリSの液量、広がり状態は変化し、個々のパネル
5の蛍光体膜厚のに違いが生じ、画面上での白均一性が
ばらつくという問題があった。However, in the conventional method, it is difficult to inject the slurry S having a constant specific gravity and viscosity at all times, and the amount of the slurry S injected into the inner surface of the panel 5 due to the fluctuation of the viscosity is low. The spread state changes, causing a difference in the phosphor film thickness of each panel 5, causing a problem that the white uniformity on the screen varies.
【0014】その理由は、従来の方法では比重値のみの
補正を行っているため、高比重スラリ・低比重スラリ・
回収スラリの供給量・粘度値によりディスペンサタンク
1内の粘度は補正回数とともに変動幅が増大し、常に比
重、粘度ともに一定なスラリSの注入は困難であるから
である。The reason is that only the specific gravity value is corrected in the conventional method, so that a high specific gravity slurry, a low specific gravity slurry,
This is because the variation in the viscosity in the dispenser tank 1 increases with the number of corrections due to the supply amount and the viscosity value of the recovered slurry, and it is difficult to inject the slurry S that is always constant in specific gravity and viscosity.
【0015】[0015]
【課題を解決するための手段】本発明のスラリ供給方法
は、比重センサ・粘度センサにより、ディスペンサタン
クより送り出されるスラリの比重、粘度をそれぞれ測定
し、その検出出力に基づいて高比重・高粘度のスラリ、
低比重・低粘度のスラリ及び低比重・高粘度のスラリ
を、それぞれ選択的に供給制御することを特徴とする。A slurry supply method according to the present invention measures a specific gravity and a viscosity of a slurry sent from a dispenser tank using a specific gravity sensor and a viscosity sensor, and based on the detected output, a high specific gravity and a high viscosity. Slurry,
It is characterized in that a slurry having a low specific gravity and a low viscosity and a slurry having a low specific gravity and a high viscosity are selectively supplied and controlled.
【0016】[0016]
【発明の実施の形態】本発明の一実施の形態について、
図1を参照して説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described.
This will be described with reference to FIG.
【0017】なお、図3経路図と同一部分には同一符号
を付して、その説明を省略する。The same parts as those in the route diagram of FIG. 3 are denoted by the same reference numerals, and description thereof will be omitted.
【0018】本実施の形態の特徴とするところは、ディ
スペンサタンク1のバイパスホース8の経路に比重セン
サ14検出端15とともに粘度センサ29検出端を入れ
るミニホッパ20を設け、ディスペンサタンク1内の蛍
光体スラリSの一部がスネークポンプ2によりバイパス
ホース8を通してミニホッパ20内に入るようにしたこ
とである。The present embodiment is characterized in that a mini-hopper 20 for receiving a detection end 15 of a specific gravity sensor 14 and a detection end of a viscosity sensor 29 is provided in a path of a bypass hose 8 of the dispenser tank 1, and a fluorescent substance in the dispenser tank 1 is provided. A part of the slurry S is caused to enter the mini hopper 20 through the bypass hose 8 by the snake pump 2.
【0019】ミニホッパ20内で検出された比重・粘度
の信号は、電気信号に変更され、コントローラ8に入
る。The specific gravity / viscosity signal detected in the mini hopper 20 is changed into an electric signal and enters the controller 8.
【0020】コントローラ28では、比重・粘度の上限
・下限の設定・記録が可能で、液面レベルの上限・下限
も検出されるようになっている。The controller 28 can set and record the upper and lower limits of specific gravity and viscosity, and detect the upper and lower limits of the liquid level.
【0021】ディスペンサタンク1に補給する補正液
は、高比重・高粘度の蛍光体スラリ(以下スラリA)2
1を入れたタンク22、低比重・低粘度の蛍光体スラリ
23(以下スラリB)を入れたタンク24、低比重・高
粘度の蛍光体スラリ25(以下スラリC)を入れたタン
ク26が設けられておりコントローラ28の信号によ
り、スラリA21、スラリB23、スラリC25が供給
される。The correction liquid supplied to the dispenser tank 1 is a high specific gravity and high viscosity phosphor slurry (hereinafter, slurry A) 2
1, a tank 24 containing a low specific gravity, low viscosity phosphor slurry 23 (hereinafter, slurry B), and a tank 26 containing a low specific gravity, high viscosity phosphor slurry 25 (hereinafter, slurry C). The slurry A21, the slurry B23, and the slurry C25 are supplied by a signal of the controller 28.
【0022】以下に、図1と、図2のフローチャートを
用いて、蛍光体スラリSの各状態の場合における供給ス
ラリの選択、供給の仕方について述べる。The method of selecting and supplying the supply slurry in each state of the phosphor slurry S will be described below with reference to the flowcharts of FIGS.
【0023】ディスペンサタンク1内の蛍光体スラリS
の液面が上限・下限の中間の位置にある場合、比重セン
サ14の出力に基づいて、比重が適正値よりも低いとき
にはスラリA21のみを供給し、粘度が適正値よりも高
いときには粘度センサ29の出力に基づいて、粘度が適
正値よりも高いときにはスラリB23のみを供給し、粘
度が適正値よりも低いときにはスラリC25を供給する
ようにする。The phosphor slurry S in the dispenser tank 1
When the liquid level is at an intermediate position between the upper limit and the lower limit, based on the output of the specific gravity sensor 14, when the specific gravity is lower than the appropriate value, only the slurry A21 is supplied, and when the viscosity is higher than the appropriate value, the viscosity sensor 29 is used. When the viscosity is higher than the appropriate value, only the slurry B23 is supplied, and when the viscosity is lower than the appropriate value, the slurry C25 is supplied.
【0024】また、ディスペンサタンク1内の蛍光体ス
ラリSの液面が下限以下にある場合には、スラリA21
を供給とともに粘度センサ29の出力に基づいて、粘度
が適正値よりも高いときにはスラリB23を供給し、粘
度が適正値よりも低いときにはスラリC25を供給する
ようにする。If the liquid level of the phosphor slurry S in the dispenser tank 1 is below the lower limit, the slurry A 21
When the viscosity is higher than the appropriate value, the slurry B23 is supplied based on the output of the viscosity sensor 29, and when the viscosity is lower than the appropriate value, the slurry C25 is supplied.
【0025】このように、各スラリの供給を制御するこ
とにより、蛍光体スラリSの比重・粘度が一定に保た
れ、塗布後の蛍光体膜厚が均一化される。As described above, by controlling the supply of each slurry, the specific gravity and viscosity of the phosphor slurry S are kept constant, and the phosphor film thickness after application is made uniform.
【0026】[0026]
【発明の効果】本発明によれば、蛍光体スラリの比重・
粘度が一定に保たれ、塗布後の蛍光体膜厚も均一化さ
れ、画面上の白均一性良好なカラー陰極線管を得ること
ができる。According to the present invention, the specific gravity of the phosphor slurry
The viscosity is kept constant, the thickness of the phosphor after coating is also made uniform, and a color cathode ray tube with good white uniformity on the screen can be obtained.
【0027】具体的には、この装置により、従来の粘度
の管理幅が±1.5CPに対し、±0.5CPにするこ
とが可能となる。Specifically, this apparatus makes it possible to set the conventional viscosity control range to ± 0.5 CP, compared to ± 1.5 CP.
【0028】その理由は、蛍光体スラリの比重・粘度を
測定し、比重・粘度を同時に制御するようにしたからで
ある。The reason is that the specific gravity and the viscosity of the phosphor slurry are measured and the specific gravity and the viscosity are simultaneously controlled.
【図1】 本発明の蛍光体スラリ塗布装置のスラリ注入
経路を示す図FIG. 1 is a diagram showing a slurry injection path of a phosphor slurry applying apparatus of the present invention.
【図2】 本発明のスラリの制御状況を示すフローチャ
ートFIG. 2 is a flowchart showing the control status of the slurry according to the present invention.
【図3】 従来の蛍光体スラリ塗布装置のスラリ注入経
路を示す図FIG. 3 is a diagram showing a slurry injection path of a conventional phosphor slurry coating device.
1 ディスペンサタンク 2 スネークポンプ 4 注入電磁弁 5 パネル 6 リターンホース 7 メッシュフィルタ(フィルタ) 8 バイパスホース 9 キャリア 10 回収カバー 11 回収ホース 12 海面レベルセンサ 14 比重センサ 15 比重センサ検出端 20 ミニホッパー 21 高比重・高粘度蛍光体スラリ(スラリA) 22 高比重・高粘度蛍光体スラリタンク 23 低比重・低粘度蛍光体スラリ(スラリB) 24 低比重・低粘度蛍光体スラリタンク 25 低比重・高粘度蛍光体スラリ(スラリC) 26 低比重・高粘度蛍光体スラリタンク 28 コントローラ 29 粘度センサ S 蛍光体スラリ DESCRIPTION OF SYMBOLS 1 Dispenser tank 2 Snake pump 4 Injection solenoid valve 5 Panel 6 Return hose 7 Mesh filter (filter) 8 Bypass hose 9 Carrier 10 Collection cover 11 Collection hose 12 Sea level sensor 14 Specific gravity sensor 15 Specific gravity sensor detection end 20 Mini hopper 21 High specific gravity・ High viscosity phosphor slurry (Slurry A) 22 High specific gravity / High viscosity phosphor slurry tank 23 Low specific gravity / Low viscosity phosphor slurry (Slurry B) 24 Low specific gravity / Low viscosity phosphor slurry tank 25 Low specific gravity / High viscosity fluorescence Body slurry (slurry C) 26 Low specific gravity / high viscosity phosphor slurry tank 28 Controller 29 Viscosity sensor S Phosphor slurry
Claims (6)
容した第1のタンクと、低比重・低粘度のスラリを収容
した第2のタンクと、低比重・高粘度のスラリを収容し
た第3のタンクと、各タンクに接続されて開閉制御する
第1、第2、第3のバルブと、それぞれのバルブにより
選択的に供給されるスラリがフィルタを通して貯蔵され
るされるディスペンサタンクと、ディスペンサタンク内
のスラリの量を検出するレベルセンサと、ディスペンサ
タンクより送り出されたスラリを回転した状態のパネル
に注入する塗布ノズルと、ディスペンサタンクより送り
出されるスラリの粘度と比重とを、それぞれ測定する粘
度センサ及び比重センサと、パネルと対向配置され遠心
力により振り切られたスラリを受ける回収カバーと、回
収カバーによって回収された余剰のスラリをフィルタを
通してディスペンサタンクに戻すリターンホースと、比
重センサ、粘度センサ、レベルセンサのそれぞれの検出
出力に基づいて第1、第2、第3のバルブを開閉制御す
るコントローラとを具備したことを特徴とする蛍光体ス
ラリ塗布装置。1. A first tank containing a slurry having a high specific gravity and a high viscosity containing a phosphor, a second tank containing a slurry having a low specific gravity and a low viscosity, and a slurry containing a low specific gravity and a high viscosity slurry. A third tank connected to each of the tanks, first, second, and third valves for controlling opening and closing, and a dispenser tank for storing slurry selectively supplied by the respective valves through a filter. , A level sensor that detects the amount of slurry in the dispenser tank, a coating nozzle that injects the slurry sent from the dispenser tank into a rotating panel, and a viscosity and specific gravity of the slurry sent from the dispenser tank. Viscosity sensor and specific gravity sensor, a collection cover that is placed opposite the panel and receives the slurry shaken off by centrifugal force, A return hose for returning the collected excess slurry to the dispenser tank through a filter, and a controller for controlling opening and closing of the first, second, and third valves based on respective detection outputs of a specific gravity sensor, a viscosity sensor, and a level sensor. A phosphor slurry coating device, comprising:
内のスラリ量あるいは塗布回数に基づいて第1、第2、
第3のタンクに収容されたそれぞれのスラリのディスペ
ンサタンクへの供給量を制御することを特徴とする蛍光
体スラリ塗布方法。2. The method according to claim 1, wherein the first, second, and / or third slurry is applied based on the amount of slurry or the number of times of application.
A method for applying a phosphor slurry, comprising: controlling a supply amount of each slurry contained in a third tank to a dispenser tank.
限と下限の中間の位置にあるとき、比重センサ及び粘度
センサの検出出力に基づいて第1、第2、第3のタンク
に収容されたそれぞれのスラリのディスペンサタンクへ
の供給量を制御することを特徴とする請求項2記載の蛍
光体スラリ塗布方法。3. When the amount of slurry in the dispenser tank is at an intermediate position between the upper limit and the lower limit, the amount stored in the first, second, and third tanks is determined based on the output of the specific gravity sensor and the viscosity sensor. 3. The method according to claim 2, wherein the amount of the slurry supplied to the dispenser tank is controlled.
ンサタンク内のスラリの比重が所定値よりも低いとき、
第1タンク内のスラリのみを供給することを特徴とする
請求項3記載の蛍光体スラリ塗布方法。4. When the specific gravity of the slurry in the dispenser tank is lower than a predetermined value based on the detection output of the specific gravity sensor,
4. The method according to claim 3, wherein only the slurry in the first tank is supplied.
定下限レベルを超えるとき、、第1タンク内のスラリを
供給すると共に、粘度センサの検出出力に基づいて粘度
が所定値以下のときには第2タンク内のスラリを、粘度
が所定値以上のときには第3タンク内のスラリをそれぞ
れ供給することを特徴とする請求項2記載の蛍光体スラ
リ塗布方法。5. When the amount of slurry in the dispenser tank exceeds a predetermined lower limit level, the slurry in the first tank is supplied, and when the viscosity is lower than a predetermined value based on a detection output of a viscosity sensor, the second tank is supplied. 3. The phosphor slurry coating method according to claim 2, wherein the slurry in the third tank is supplied when the viscosity is equal to or more than a predetermined value.
比重が所定値よりも高い場合には、粘度センサの検出出
力に基づいて粘度が所定値以下のときには第2タンク内
のスラリを、粘度が所定値以上のときには第3タンク内
のスラリをそれぞれ供給することを特徴とする請求項3
記載の蛍光体スラリ塗布方法。6. When the specific gravity of the slurry is higher than a predetermined value based on the detection output of the specific gravity sensor, the slurry in the second tank is removed based on the detection output of the viscosity sensor when the viscosity is equal to or lower than the predetermined value. The slurry in the third tank is supplied when the value is equal to or more than a predetermined value.
The phosphor slurry coating method as described in the above.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29607197A JPH11135016A (en) | 1997-10-29 | 1997-10-29 | Phosphor slurry applying device and applying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29607197A JPH11135016A (en) | 1997-10-29 | 1997-10-29 | Phosphor slurry applying device and applying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH11135016A true JPH11135016A (en) | 1999-05-21 |
Family
ID=17828744
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29607197A Pending JPH11135016A (en) | 1997-10-29 | 1997-10-29 | Phosphor slurry applying device and applying device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH11135016A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2375072A (en) * | 2001-05-05 | 2002-11-06 | Psi Global Ltd | Method and apparatus for making moulded filter elements |
| KR101065113B1 (en) | 2009-03-17 | 2011-09-16 | 키스마트 코포레이션 | Fluorescent material coating method |
| WO2025200260A1 (en) * | 2024-03-27 | 2025-10-02 | 宁德时代新能源科技股份有限公司 | Slurry recovery method |
-
1997
- 1997-10-29 JP JP29607197A patent/JPH11135016A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2375072A (en) * | 2001-05-05 | 2002-11-06 | Psi Global Ltd | Method and apparatus for making moulded filter elements |
| US7297235B2 (en) | 2001-05-05 | 2007-11-20 | Psi Global Ltd. | Method and apparatus for making molded filter elements |
| KR101065113B1 (en) | 2009-03-17 | 2011-09-16 | 키스마트 코포레이션 | Fluorescent material coating method |
| WO2025200260A1 (en) * | 2024-03-27 | 2025-10-02 | 宁德时代新能源科技股份有限公司 | Slurry recovery method |
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