JPH031902A - Automatic control of moisture and viscosity of slip - Google Patents
Automatic control of moisture and viscosity of slipInfo
- Publication number
- JPH031902A JPH031902A JP13678989A JP13678989A JPH031902A JP H031902 A JPH031902 A JP H031902A JP 13678989 A JP13678989 A JP 13678989A JP 13678989 A JP13678989 A JP 13678989A JP H031902 A JPH031902 A JP H031902A
- Authority
- JP
- Japan
- Prior art keywords
- slip
- viscosity
- tank
- slurry
- moisture
- 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.)
- Granted
Links
Landscapes
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明はセラミック製品の成形原料のちととなる泥漿の
水分および粘性の自動制御法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a method for automatically controlling the moisture content and viscosity of a slurry that is used as a raw material for forming ceramic products.
(従来の技術)
セラミック製品の成形原料のもととなる泥漿は使用時に
その水分と粘性を一定に保つことが必要であり、このた
めに従来から各種の測定方法が工夫されている。(Prior Art) It is necessary to keep the moisture and viscosity of slurry, which is the raw material for forming ceramic products, constant during use, and various measuring methods have been devised for this purpose.
その代表的なものは、サンプリングした泥漿の比重を測
定して換算表から水分を知る比重法や、サンプリングし
た泥漿中にビスコテスターを入れて粘性を測定する方法
であるが、これらの方法はいずれも泥漿をサンプリング
したうえ時間をかけて人手により測定を行う必要がある
。しかも泥5?は使用中の水分蒸発や撹拌により水分や
粘性が変化し易い性質を持つ、このため、使用中の泥漿
の水分と粘性を一定に保つためには作業者がしばしば測
定と調整作業を繰り返す必要があり、そのために多くの
手数を必要とし、しかも水分と粘性を正確に制御子るこ
とは熟練を要する作業とされていた。Typical methods include the specific gravity method, which measures the specific gravity of sampled slurry and determines the water content from a conversion table, and the method of measuring viscosity by inserting a visco tester into the sampled slurry. However, it is necessary to sample the slurry and then conduct measurements manually, which takes time. And mud 5? The water content and viscosity of slurry tend to change easily due to water evaporation and agitation during use. Therefore, in order to keep the water content and viscosity of slurry constant during use, workers often have to repeat measurements and adjustments. This required a lot of time and effort, and accurate control of moisture and viscosity was considered to be a task that required skill.
(発明が解決しようとする課題)
本発明は上記したような従来の問題点を解決して、泥漿
の水分と粘性とを短時間で自動的に測定するとともに、
その測定値に基づいて全く人手を要することなく泥漿の
水分と粘性を常に一定範囲内に維持することができる泥
漿の水分および粘性の自動制御法を提供するために完成
されたものである。(Problems to be Solved by the Invention) The present invention solves the above-mentioned conventional problems and automatically measures the water content and viscosity of slurry in a short time.
The present invention was completed in order to provide an automatic control method for the moisture content and viscosity of slurry, which can always maintain the moisture content and viscosity of slurry within a certain range based on the measured values without requiring any human intervention.
(課題を解決するための手段)
上記の課題を解決するためになされた本発明は、泥漿タ
ンク内の泥漿を内部にフロートが設けられた計測槽の底
部から一定速度で流入させてフロートの浮上高さを動出
力として測定するとともに、泥漿の流入を停止してフロ
ートの静止高さを静出力として測定し、これらの測定値
に基づいて泥漿の水分と粘性とを算出し、これらの値を
演算制御部に入力して水分が低下したときには水を泥漿
タンク内へ自動添加し、粘性が低下したときには調整釉
を泥漿タンク内へ自動添加することを特徴とするもので
ある。(Means for Solving the Problems) The present invention, which has been made to solve the above problems, allows slurry in a slurry tank to flow at a constant speed from the bottom of a measuring tank in which a float is provided, thereby causing the float to float. In addition to measuring the height as a dynamic force, the inflow of slurry is stopped and the static height of the float is measured as a static force. Based on these measured values, the water content and viscosity of the slurry are calculated, and these values are calculated. The system is characterized in that water is automatically added into the slurry tank when the water content is lowered by input to the arithmetic control unit, and adjusted glaze is automatically added into the slurry tank when the viscosity is lowered.
以下に本発明を碍子施釉用の泥漿の水分と粘性の自動制
御に適用した実施例により更に詳細に説明する。The present invention will be explained in more detail below using an example in which the present invention is applied to automatic control of water content and viscosity of slurry for glazing insulators.
(実施例)
第1図において(1)は内部に撹拌器(2)を備えた泥
漿タンク、(3)は泥漿圧送用ポンプであり、泥漿タン
ク(1)内の泥漿はノズル(4)から碍子(5)に向か
って噴射され、施釉が行われる構造となっている。(Example) In Fig. 1, (1) is a slurry tank equipped with an agitator (2) inside, (3) is a pump for pumping the slurry, and the slurry in the slurry tank (1) is supplied from a nozzle (4). The structure is such that it is sprayed toward the insulator (5) and glazed.
(6)は泥漿タンク(1)の上方に設けられた計測槽で
あり、その下半部は円錐状とされ、その内部にフロート
(7)が上下動自在に設けられている。この計測槽(6
)の底部中心には泥漿供給管(8)が接続されており、
測定対象である泥漿を泥漿タンク(1)から定量ポンプ
(9)によって圧送し、泥漿供給管(8)を介して計測
槽(6)の底部から一定速度で流入させることができる
構造となっている。(9)は計測槽(6)からオーバー
フローした泥漿を集めて泥漿タンク(1)へ戻すための
外槽である。また0ωはフロート(7)の高さを検出す
るセンサである。(6) is a measurement tank provided above the slurry tank (1), the lower half of which is shaped like a cone, and a float (7) is provided inside thereof so as to be movable up and down. This measurement tank (6
) A slurry supply pipe (8) is connected to the center of the bottom.
The structure allows the slurry to be measured to be pumped from the slurry tank (1) by a metering pump (9), and to flow at a constant speed from the bottom of the measuring tank (6) via the slurry supply pipe (8). There is. (9) is an outer tank for collecting the slurry overflowing from the measurement tank (6) and returning it to the slurry tank (1). Further, 0ω is a sensor that detects the height of the float (7).
このような装置により泥漿の水分と粘性を測定するには
、定量ポンプ(9)を始動して泥漿タンク(1)内の泥
漿を泥漿供給管(8)から計測槽(6)の内部へ連続的
に流入させる。このとき、フロート(7)は流入する泥
漿の浮力により上方に押上げられて第2図に示すAの位
置からB−C−Dで示すカーブを描いて上方へ移動する
。ここでAからBへの移動は瞬間的な弾性伸び、Bから
Cへの移動は弾性余効によるもので粘弾性の性質を示し
、CからDへの移動は粘性流動によるものである。そこ
で一定時間が経過したD点のフロート(7)の浮上高さ
をセンサ0fflにより測定する。次に計測槽(6)へ
の泥漿の流入を停止させると、フロート(7)は第2図
にD−E−F−Gとして示すカーブを描いて低下する。To measure the water content and viscosity of slurry using such a device, start the metering pump (9) and continuously pump the slurry in the slurry tank (1) from the slurry supply pipe (8) into the measuring tank (6). Inflow into the target market. At this time, the float (7) is pushed upward by the buoyancy of the inflowing slurry and moves upward from position A shown in FIG. 2 in a curve shown by B-C-D. Here, the movement from A to B is due to instantaneous elastic elongation, the movement from B to C is due to elastic aftereffects and exhibits viscoelastic properties, and the movement from C to D is due to viscous flow. Then, the floating height of the float (7) at point D after a certain period of time is measured by the sensor 0ffl. Next, when the flow of the slurry into the measuring tank (6) is stopped, the float (7) lowers in a curve shown as D-E-F-G in FIG.
DからEへの移動は瞬間的な弾性収縮であり、EからF
への移動は遅れ弾性収縮であって、粘弾性の性質を示し
ている。その後フロート(7)はG点で静止するので、
その静止高さを測定する。この静止高さはフロート(7
)の浮力を示し、ここから泥漿の比重と水分とを知るこ
とができる。また第2図のD点とG点の差は泥漿の粘弾
性収縮を示すので、ここから泥漿の粘性を知ることがで
きる。このような測定は5〜10分のインターバルで自
動的に行うことかできる。The movement from D to E is an instantaneous elastic contraction, and from E to F
The movement to is a delayed elastic contraction and exhibits viscoelastic properties. After that, the float (7) comes to rest at point G, so
Measure its static height. This static height is a float (7
), from which the specific gravity and water content of the slurry can be determined. Furthermore, since the difference between points D and G in FIG. 2 indicates the viscoelastic contraction of the slurry, the viscosity of the slurry can be determined from this. Such measurements can be performed automatically at 5-10 minute intervals.
このようにして得られた水分と粘性の測定値は演算制御
部01)に人力され、演算制御部(11)は第3図に示
すようにこれらの測定値を基準値と比較し、調節弁面と
i1節弁06)を開閉して次の通りの制御を行う。The measured values of moisture and viscosity obtained in this way are manually input to the arithmetic and control unit (01), which compares these measured values with reference values as shown in Fig. 3, and controls the control valve. The control is performed as follows by opening and closing the surface and i1 section valve 06).
まず水分が基準値よりも低下したときには、調整水タン
ク021から調節弁側を介して泥漿タンク(1)内に水
を供給する。供給された水は撹拌器(2)によりただち
に撹拌混合されて泥漿タンク(1)内の泥漿の水分を上
昇させる。一般に泥漿の水分は使用中に次第に低下して
行くものであり、通常は水分が基準値を越えることはな
いので、水分が基準値を越えた場合については水の供給
を停止しておけばよい。First, when the water content drops below the reference value, water is supplied from the regulating water tank 021 into the slurry tank (1) via the regulating valve side. The supplied water is immediately stirred and mixed by the stirrer (2) to raise the water content of the slurry in the slurry tank (1). Generally, the moisture content of the slurry gradually decreases during use, and the moisture content usually does not exceed the standard value, so if the moisture content exceeds the standard value, the water supply can be stopped. .
次に粘性が基準値よりも低下したときには、調整釉タン
ク051′から調節弁00を介して泥漿タンク(1)内
に調整釉を供給する。これにより泥漿の粘性は次第に増
加する。一方、粘性が基準値よりも増加したときには水
を添加すればよいが、水分を増加させたくない場合には
、泥漿タンク(1)内の撹拌器(2)の回転速度を上げ
て激しく撹拌を行えば泥漿の粘性は次第に低下すること
となる。このようにして、本発明によれば泥漿の水分と
粘性とをごく短いタイムインターバルで自動制御するこ
とが可能となる。Next, when the viscosity decreases below the reference value, the adjusted glaze is supplied from the adjusted glaze tank 051' into the slurry tank (1) via the adjustment valve 00. This gradually increases the viscosity of the slurry. On the other hand, if the viscosity increases above the standard value, water can be added, but if you do not want to increase the water content, increase the rotational speed of the stirrer (2) in the slurry tank (1) and stir vigorously. If this is done, the viscosity of the slurry will gradually decrease. In this way, according to the present invention, it is possible to automatically control the water content and viscosity of the slurry in a very short time interval.
なお、第4図は撹拌による泥漿の粘性低下効果を示した
グラフである。即ち、このグラフは初期の粘性(マリオ
ツドチューブ粘性)が66秒、水分が41%、釉温が8
’Cに調整された泥漿をタンク内で連続的に撹拌した
場合の粘性の変化を示すものである。このグラフから明
らかなように、撹拌により泥漿の粘性は大きく低下し、
また水分を添加しても低下することが分かる。Incidentally, FIG. 4 is a graph showing the effect of reducing the viscosity of the slurry by stirring. In other words, this graph shows that the initial viscosity (mariot tube viscosity) is 66 seconds, the moisture content is 41%, and the glaze temperature is 8 seconds.
This figure shows the change in viscosity when slurry adjusted to 'C' is continuously stirred in a tank. As is clear from this graph, stirring greatly reduces the viscosity of the slurry.
It can also be seen that the value decreases even when water is added.
(発明の効果)
以上に説明したように、本発明によればフロートの変位
により泥漿の水分と粘性とを短い周期で自動的に測定し
たうえ、これらの測定値に応じて泥漿の水分と粘性を人
手を要することなく一定範囲内に維持することができる
。従って本発明によれば、変化し易い泥漿の性状を常に
安定に維持することができるので、工程の安定と自動化
を図るうえで極めて有効である。(Effects of the Invention) As explained above, according to the present invention, the moisture and viscosity of the slurry are automatically measured in short cycles by the displacement of the float, and the moisture and viscosity of the slurry are measured according to these measured values. can be maintained within a certain range without requiring human intervention. Therefore, according to the present invention, the easily changeable properties of the slurry can be maintained stably at all times, which is extremely effective in stabilizing and automating the process.
よって本発明は従来の問題点を解決した泥漿の水分およ
び粘性の自動制御法として、産業の発展に寄与するとこ
ろは極めて大きいものである。Therefore, the present invention can greatly contribute to the development of industry as a method for automatically controlling the water content and viscosity of slurry by solving the conventional problems.
第1図は本発明の詳細な説明するフローシート、第2図
は泥漿の流とフロートの変位との関係を示すグラフ、第
3図は制御内容を説明するブロック図、第4図は撹拌に
よる泥漿の粘性変化を示すグラフである。
(1):泥漿タンク、(6):計測槽、(7);フロー
ト、θ0:演算制御部、021:調整水タンク、051
:調整釉タンク。Fig. 1 is a flow sheet explaining the details of the present invention, Fig. 2 is a graph showing the relationship between the flow of slurry and the displacement of the float, Fig. 3 is a block diagram explaining the control details, and Fig. 4 is based on stirring. It is a graph showing viscosity change of slurry. (1): Slurry tank, (6): Measurement tank, (7); Float, θ0: Arithmetic control unit, 021: Adjustment water tank, 051
: Adjustment glaze tank.
Claims (1)
けられた計測槽(6)の底部から一定速度で流入させて
フロート(7)の浮上高さを動出力として測定するとと
もに、泥漿の流入を停止してフロート(7)の静止高さ
を静出力として測定し、これらの測定値に基づいて泥漿
の水分と粘性とを算出し、これらの値を演算制御部(1
1)に入力して水分が低下したときには水を泥漿タンク
(1)内へ自動添加し、粘性が低下したときには調整釉
を泥漿タンク(1)内へ自動添加することを特徴とする
泥漿の水分および粘性の自動制御法。The slurry in the slurry tank (1) is made to flow at a constant speed from the bottom of the measurement tank (6) in which a float (7) is installed, and the floating height of the float (7) is measured as a dynamic force. The static height of the float (7) is measured as a static force, the moisture and viscosity of the slurry are calculated based on these measured values, and these values are sent to the calculation control unit (1).
1), water is automatically added into the slurry tank (1) when the water content has decreased, and adjusted glaze is automatically added into the slurry tank (1) when the viscosity has decreased. and automatic control methods for viscosity.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13678989A JPH031902A (en) | 1989-05-30 | 1989-05-30 | Automatic control of moisture and viscosity of slip |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13678989A JPH031902A (en) | 1989-05-30 | 1989-05-30 | Automatic control of moisture and viscosity of slip |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH031902A true JPH031902A (en) | 1991-01-08 |
| JPH0585329B2 JPH0585329B2 (en) | 1993-12-07 |
Family
ID=15183557
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13678989A Granted JPH031902A (en) | 1989-05-30 | 1989-05-30 | Automatic control of moisture and viscosity of slip |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH031902A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101015331B1 (en) * | 2003-06-27 | 2011-02-15 | 엘모텍 스타토맷 버트리브스 게엠베하 | Method and apparatus for inducing wave windings into rotor and stator lamination packets of an electric machine |
-
1989
- 1989-05-30 JP JP13678989A patent/JPH031902A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101015331B1 (en) * | 2003-06-27 | 2011-02-15 | 엘모텍 스타토맷 버트리브스 게엠베하 | Method and apparatus for inducing wave windings into rotor and stator lamination packets of an electric machine |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0585329B2 (en) | 1993-12-07 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |