JPH01171808A - Controller for moisture of plastic waste earth - Google Patents

Controller for moisture of plastic waste earth

Info

Publication number
JPH01171808A
JPH01171808A JP33225887A JP33225887A JPH01171808A JP H01171808 A JPH01171808 A JP H01171808A JP 33225887 A JP33225887 A JP 33225887A JP 33225887 A JP33225887 A JP 33225887A JP H01171808 A JPH01171808 A JP H01171808A
Authority
JP
Japan
Prior art keywords
moisture
fragments
clay
weight
processing unit
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
Application number
JP33225887A
Other languages
Japanese (ja)
Inventor
Haruaki Kito
鬼頭 春秋
Seiji Kumazawa
熊沢 誠治
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Narumi China Corp
Original Assignee
Narumi China Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Narumi China Corp filed Critical Narumi China Corp
Priority to JP33225887A priority Critical patent/JPH01171808A/en
Publication of JPH01171808A publication Critical patent/JPH01171808A/en
Pending legal-status Critical Current

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  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)

Abstract

PURPOSE:To reduce the amount of scatter in moisture of plastic waste earth, by measuring the moisture and the weight of fragments of dried plate-like waste earth, processing the measured values on real time and adding water thereto. CONSTITUTION:Mud slurry 1 is dehydrated in a dehydrator 11 to be plate-like waste earth 2. It becomes dried plate-like waste earth 3 in a storage chamber 12 and then fragments 4 in a crusher 13. The weight of the fragments 4 is measured with a weigher 24 immediately after being crushed in the crusher 13 or on a conveying device 14. The moisture of the fragments 4 is measured on real time with a moisture meter 23 and measured values are entered into a processing unit 25 together with the values of weight. The processing unit 25 processes such values periodically, derives the average moisture of the fragments from the values of moisture and weight a controlled unit of fragments and the difference between the aimed moisture and the average moisture. If the average moisture is less than the aimed moisture, the processing unit sends an instruction to the dehydrator 27 to make it to add water. Then, the fragments have the aimed moisture and such fragments are conveyed into a deaerator-kneader 15 to be plastic waste earth 5, where the amount of scatter in moisture of the plastic waste earth 5 is + or -0.5%.

Description

【発明の詳細な説明】 イ1発明の目的 [産業上の利用分野] 陶磁器用原料の可塑性坏土の水分の制御装置に関する。[Detailed description of the invention] B1 Purpose of the invention [Industrial application field] This invention relates to a moisture control device for plastic clay used as a raw material for ceramics.

詳しくは、可塑性坏土の水分のバラツキを小さくするこ
とを目的とした坏土水分の制御装置に係る。
Specifically, the present invention relates to a clay moisture control device aimed at reducing variations in moisture content of plastic clay.

[従来技術] 可塑性坏土の作成工程は、泥漿をフィルタープレス等の
脱水装置で脱水して板状坏土とし、該坏土を貯蔵室で自
然乾燥する。その乾燥した板状坏土はパグミルに投入す
るために破砕して小片の破砕物とし、また水分値を調整
するための水を添加して投入される。その破砕物と水は
パグミル等の真空式混線機で脱気、混練して可塑性坏土
とする。
[Prior Art] In the process of producing plastic clay, slurry is dehydrated using a dewatering device such as a filter press to form a plate-shaped clay, and the clay is naturally dried in a storage room. The dried plate-shaped clay is crushed into small pieces for feeding into a pug mill, and water is added to adjust the moisture content. The crushed material and water are degassed and kneaded using a vacuum mixer such as a pug mill to form plastic clay.

従来、可塑性坏土の水分値を目標値にする調整は、パグ
ミルに投入する前工程の自然乾燥された板状坏土におい
てなされる。すなわち、貯蔵室に1日以上自然乾燥され
た板状坏土の1部を指で押さえた際のへこみ具合や割っ
た際の割れ口の状況等の経験による判断、バネつき針を
板状坏土に押し仕込み、その押し込み深さから水分値を
推定する等で選んだロットから、抜き取りでサンプリン
グしたサンプルを用いてて水分値を測定している。
Conventionally, adjustment of the moisture value of plastic clay to a target value is performed in a plate-shaped clay that has been air-dried in a process prior to feeding into a pug mill. In other words, judgments are made based on experience, such as the degree of dents when a part of the plate-shaped clay that has been left to air dry in a storage room for more than a day is pressed with one's fingers, or the state of the cracks when the plate-shaped clay is split. Moisture values are measured using samples taken from lots selected by pushing the material into the soil and estimating the moisture value from the depth of the push.

しかし、貯蔵室に1日以上自然乾燥された板状坏土は、
フィルタープレス等で脱水した板状坏土に比べればロッ
トの各部位の水分値のバラツキはより小さくなっている
とはいえ、要求に対してはバラツキは大きく、精度を上
げるために相当の数のサンプルを測定しなければならず
、工数のかかるものであった。
However, the plate-shaped clay that has been left to dry naturally in the storage room for more than a day,
Although the variation in the moisture value of each part of the lot is smaller compared to plate-shaped clay dehydrated using a filter press, etc., the variation is large in relation to the requirements, and a considerable number of steps are required to improve accuracy. The sample had to be measured, which required a lot of man-hours.

しかも、10枚以上積み重ねられた板状坏土の中央部な
どはサンプリングすることが位置的に困難な部位もあっ
て、ロット全体を正確に捕らえて水分値を測定すること
は容易ではなかった。
Moreover, it is difficult to sample the central part of ten or more plate-shaped clay blocks due to the location, and it is not easy to accurately capture the entire lot and measure the moisture content.

また、可塑性坏土を測定してフィトバックすることもな
されるが、結果が出てからであり適切に目標水分を得る
方法としては難しかった。
In addition, phyto-backing of plastic clay is also carried out by measuring the amount of plastic clay, but this method is difficult to obtain properly after the results are obtained.

し発明が解決しようとする問題点] この可塑性坏土の水分値がその目標値からのバラツキが
大きと、製品を製造する工程の成形、乾燥、焼成等にお
いて、クラック、変形、寸法不良等に影響を及ぼし製品
不良の要因となる。
[Problems to be Solved by the Invention] If the moisture value of this plastic clay varies greatly from its target value, cracks, deformation, dimensional defects, etc. may occur during the molding, drying, firing, etc. processes of manufacturing the product. This can lead to product defects.

したがって、本発明ではパグミルに投入する直前の破砕
物の水分値を測定して、可塑性坏土の水分値を小さなバ
ラツキで目標値にするための可塑性坏土水分制御装置を
提供することを目的とする。
Therefore, it is an object of the present invention to provide a plastic clay moisture control device that measures the moisture content of crushed materials immediately before being fed into a pug mill and adjusts the moisture content of the plastic clay to a target value with small variations. do.

口1発明の構成 [問題を解決するための手段] 本発明は泥漿1から板状坏土2を経て陶磁器用の可塑性
坏土を作成する工程において、前記板状坏土2を破砕し
て破砕物とする破砕装置13と、該破砕物を搬送する搬
送装置14と、前記搬送装置14上の破砕物のレベルを
調整するレベル調整装置22と、前記搬送装置14で搬
送中の破砕物の水分値および重量を測定する水分計23
および重量計24と、前記水分値および重量の測定値を
リアルタイムに入力する演算処理袋!25と、前記演算
処理装置25の指令で可塑性坏土水分値の目標値との差
分から加水量を加水する加水量制御装置27よりなるこ
とを特徴とする陶磁器用の可塑性坏土水分制御装置であ
る。
1. Structure of the invention [Means for solving the problem] The present invention provides a method of crushing and crushing the plate-shaped clay 2 in the step of creating a plastic clay for ceramics from the slurry 1 through the plate-shaped clay 2. A crushing device 13 that transports the crushed materials, a conveying device 14 that conveys the crushed materials, a level adjustment device 22 that adjusts the level of the crushed materials on the conveying device 14, and a moisture content of the crushed materials being transported by the conveying device 14. Moisture meter 23 for measuring value and weight
And a weighing scale 24, and a calculation processing bag for inputting the moisture value and weight measurement value in real time! 25, and a water addition amount control device 27 that adds water based on the difference between the plastic clay moisture value and the target value in response to a command from the arithmetic processing unit 25. be.

[作用] 本発明の作用について、本発明の可塑性坏土水分制御装
置の物の流れと物を加工する装置の関係を示した第1図
で説明する。泥漿1は脱水装置11で板状坏土2とされ
、貯蔵室12で乾燥板状坏土3とされ、破砕装置13で
小片の破砕物4とされる。
[Function] The function of the present invention will be explained with reference to FIG. 1, which shows the relationship between the flow of materials and the device for processing materials in the plastic clay moisture control device of the present invention. The slurry 1 is made into plate-shaped clay 2 in a dewatering device 11, dried plate-shaped clay 3 in a storage room 12, and crushed into small pieces 4 in a crushing device 13.

レベル調整装置は搬送装置14上の破砕物層の高さのレ
ベルを調整するためのものである。破砕物の重量は破砕
装置13で破砕された直後または搬送装置上で重量計2
4によって測定される。破砕物の水分値は水分計23と
よってリアルタイムに測定され重量と同様に演算処理装
置25に入力される。演算処理装置25は一定周期で測
定し破砕物の水分値、重量から、ある制御単位の破砕物
の平均的水分値を求め、目標水分値に対する不足分があ
れば、加水IIIal装置27へ指令し、加水装置28
から加水される。こうして破砕物は目標値の水分値とな
り脱気・混練装置15に投入してされて可塑性坏土5と
される。
The level adjustment device is for adjusting the height of the crushed material layer on the conveying device 14. The weight of the shredded material is measured immediately after being shredded by the shredding device 13 or on a weighing scale 2 on the conveying device.
Measured by 4. The moisture value of the crushed material is measured in real time by a moisture meter 23 and is input to the processing unit 25 in the same way as the weight. The arithmetic processing unit 25 calculates the average moisture value of the crushed material in a certain control unit from the moisture value and weight of the crushed material measured at regular intervals, and if there is a shortage of the target moisture value, it issues a command to the hydration IIIal device 27. , water adding device 28
Water is added from In this way, the crushed material has a moisture content of the target value and is fed into the deaeration/kneading device 15 to be made into the plastic clay 5.

[実施例] 本発明の実施例を示す。[Example] An example of the present invention is shown.

[実施例1] 泥漿1はフィルタープレスで脱水されて板状坏土2とな
る。この板状坏土2の1枚の重量は30Kgで、10ツ
トは約15枚である。板状坏土2は貯蔵室で胛蔵されて
、乾燥板状坏土3とされる。この乾燥板状坏土3の1部
を指で押さえ、割り等の経験による判断、バネつき針を
板状坏土に押し仕込み、その押し込み深さから水分値を
推定する等でロットを選ぶ、こうして選ばれたロットの
乾燥板状坏土3は破砕装置13に送られて平均10m■
程度の小片の破砕物4とされる。破砕物4はパグミル1
5に投入するためにベルトコンベヤ14上に送り出され
る。
[Example 1] Sludge 1 is dehydrated using a filter press to form plate-shaped clay 2. The weight of one sheet of this plate-shaped clay 2 is 30 kg, and 10 pieces is about 15 pieces. The plate-shaped clay 2 is stored in a storage room to form a dried plate-shaped clay 3. A lot is selected based on judgment based on experience such as holding down a part of this dried plate-shaped clay 3 with one's fingers, splitting it, pushing a spring-loaded needle into the plate-shaped clay, and estimating the moisture content from the depth of the push. The dried plate-shaped clay 3 of the lot selected in this way is sent to the crushing device 13, and the average length is 10 m.
It is considered as crushed material of small pieces of about 4. Crushed material 4 is pug mill 1
5 onto a belt conveyor 14.

ベルトコンベヤ14の破砕eJI4の有無はセンサー2
1で判断される。ベルトコンベヤ14上の送り出された
破砕物4の高さのレベルの調整のためにレベル調整装置
22が設けられている。こうしてベルトコンベヤ14上
には一定量の破砕物4は連続的にパグミル15に搬送さ
れるされている。水分値と単位面積当たりの重量とを水
分計23(例えば赤外線式水分針)と水分計の直下に設
置されている重量計24(例えばコンベヤスケール)で
測定される。すなわち、ベルトコンベヤ14の単位長さ
毎にサンプリング測定しくエンコーダでにパルスとする
)、iサンプリング時点の水分値XIJとし、水分計2
3の台数を3台とし、破砕物4の重量WIとし、ベルト
コンベヤ速度からサンプリング周期(kパルス)T 1
1 @ 0とし、9サンプリング毎に制御し、目標水分
値を又とすると、制御単位毎の破砕物の重量はW加水量
Uは −x となり補正係数は調整段階で決定する。
The presence or absence of crushing eJI4 on the belt conveyor 14 is detected by sensor 2.
It is determined by 1. A level adjustment device 22 is provided for adjusting the height of the crushed material 4 delivered on the belt conveyor 14. In this way, a certain amount of crushed material 4 is continuously conveyed to the pug mill 15 on the belt conveyor 14. The moisture value and the weight per unit area are measured using a moisture meter 23 (for example, an infrared moisture needle) and a weight scale 24 (for example, a conveyor scale) installed directly below the moisture meter. In other words, sampling is performed for each unit length of the belt conveyor 14 (the encoder is pulsed), the moisture value at sampling point i is XIJ, and the moisture meter 2 is
3 is 3, the weight of the crushed material 4 is WI, and the sampling period (k pulses) is T 1 from the belt conveyor speed.
1 @ 0, control is performed every 9 samplings, and the target moisture value is set to 0. The weight of the crushed material for each control unit is W and the amount of water added is -x, and the correction coefficient is determined at the adjustment stage.

これらの測定値は演算処理装置22にリアルタイムに入
力される。制御の頻度はtT@・Oの一定周期で行われ
るが、ベルトコンベヤ14の後部に設置されたセンサー
26(例えばエンコーダ〉で調整するこができる。
These measured values are input to the arithmetic processing unit 22 in real time. The frequency of control is performed at a constant cycle of tT@·O, and can be adjusted by a sensor 26 (for example, an encoder) installed at the rear of the belt conveyor 14.

一方、演算処理装置25は入力された測定値から、一定
制御単位の破砕物の平均水分値を演算処理し、かつ目標
水分値との差分を計算し、加水量制御装置27に指令さ
れて、スプレ一部28からベルトコンベヤ14からパグ
ミル15に投入されてきた破砕物4に加水される。こう
したパグミルで脱気・混練されて可塑性坏土を得る。
On the other hand, the arithmetic processing device 25 calculates the average moisture value of the crushed material in a certain control unit from the input measurement value, calculates the difference from the target moisture value, and instructs the water addition amount control device 27 to Water is added from the spray part 28 to the crushed material 4 that has been fed into the pug mill 15 from the belt conveyor 14. The clay is degassed and kneaded in these pug mills to obtain plastic clay.

すなわち、単位時間当たりの加水量は Δu = u / Q Tとなる。ただし、1サンプリ
ング毎の水分量を求める方法もある。
That is, the amount of water added per unit time is Δu=u/QT. However, there is also a method of determining the moisture content for each sampling.

演算処理装置25は破砕物4のパグミル15に投入され
るタイミングをエンコーダ26等で判断して加水量制御
装置へ指令して滴下量ΔUを出力する。
The arithmetic processing unit 25 determines the timing at which the crushed material 4 is introduced into the pug mill 15 using an encoder 26 or the like, and instructs the water addition amount control device to output the dripping amount ΔU.

こうして得た可塑性坏土の含水分率のバラツキを測定し
たところ目標の水分値23.0%に対して、バラツキは
±0.5%あった。
When the variation in the moisture content of the plastic clay thus obtained was measured, the variation was ±0.5% with respect to the target moisture content of 23.0%.

本実施例で用いた破砕装置のほかにニーグーを用いるこ
ともできる。
In addition to the crushing device used in this example, a Ni-Goo can also be used.

また水分計23はベルトコンベヤ14の幅方向に複数台
設置することも出来る。
Further, a plurality of moisture meters 23 can be installed in the width direction of the belt conveyor 14.

[実施例2] 実施例1と同様に平均10mm程度の小片の破砕物4と
しベルトコンベヤ14に搬送する前に、前記破砕物の重
量を重量計24で秤量し、ベルトコンベヤ14上に送り
出される。ベルトコンベヤ14の破砕物4の有無はセン
サー21で判断される。ベルトコンベヤ14上の送り出
された破砕物4の高さのレベルの調整のためにレベル調
整装置22が設けられている。こうしてベルトコンベヤ
14上には一定量の破砕物4は連続的にパグミル15に
搬送されるされている。水分値は水分計23(赤外線式
水分計)で測定される。 測定値は演算処理装置25に
リアルタイムに入力等は実施例1と同様である。
[Example 2] As in Example 1, the crushed materials 4 are made into small pieces of about 10 mm on average, and before being conveyed to the belt conveyor 14, the weight of the crushed materials is weighed using a weighing scale 24, and the crushed materials are sent onto the belt conveyor 14. . The presence or absence of crushed material 4 on the belt conveyor 14 is determined by a sensor 21. A level adjustment device 22 is provided for adjusting the height of the crushed material 4 delivered on the belt conveyor 14. In this way, a certain amount of crushed material 4 is continuously conveyed to the pug mill 15 on the belt conveyor 14. The moisture value is measured with a moisture meter 23 (infrared moisture meter). The measurement values are input to the arithmetic processing unit 25 in real time, etc., in the same manner as in the first embodiment.

なお、実施例1.2のいずれであっても、可塑性坏土の
実績水分値を測定して、目標水分値のバラツキの範囲で
あるか否かを測定して、演算処理装置に入力してフィト
バックをかけて、水分値の安定を計ることもできる。
In addition, in either of Examples 1 and 2, the actual moisture value of the plastic clay is measured, it is determined whether it is within the range of variation of the target moisture value, and the result is input to the arithmetic processing device. You can also measure the stability of your water level by applying Phytovac.

ハ1発明の効果 以上の説明のように本発明によって、脱気・混練する直
前に、乾燥板状坏土の破砕物の含水分と重量を測定し、
リアルタイムに演算処理し、加水することによって、可
塑性坏土水分のバラツキを小さくすることができた。
C1 Effects of the Invention As explained above, according to the present invention, the water content and weight of the crushed dried plate-shaped clay are measured immediately before degassing and kneading,
By performing calculation processing and adding water in real time, we were able to reduce the variation in the moisture content of the plastic clay.

この優れた可塑性坏土を用いることにより、製品を効率
良く製造することに貢献した。
The use of this excellent plastic clay contributed to the efficient manufacture of products.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の可塑性坏土水分制御装置の機構のフロ
ーを示す。 1・・・泥漿 2・・・板状坏土 3・・・乾燥板状坏
土4・・・破砕物 5・・・可塑性坏土
FIG. 1 shows the flow of the mechanism of the plastic clay moisture control device of the present invention. 1...Sludge 2...Plat-shaped clay 3...Dry plate-shaped clay 4...Crushed material 5...Plastic clay

Claims (1)

【特許請求の範囲】[Claims]  泥漿1から板状坏土2を経て陶磁器用の可塑性坏土を
作成する工程において、前記板状坏土2を破砕して破砕
物とする破砕装置13と、前記破砕物を搬送する搬送装
置14と、前記搬送装置14上の破砕物4のレベルを調
整するレベル調整装置22と、前記破砕物4の重量を秤
量する重量計24と、前記搬送装置14で搬送中の破砕
物4の水分値を測定する水分計23と、前記水分値およ
び重量の測定値をリアルタイムに入力する演算処理装置
25と、前記演算処理装置25の指令で可塑性坏土水分
値の目標値との差分から加水量を加水する加水量制御装
置27よりなることを特徴とする陶磁器用の可塑性坏土
水分制御装置。
In the process of creating plastic clay for ceramics from slurry 1 through plate-shaped clay 2, a crushing device 13 that crushes the plate-shaped clay 2 into crushed materials, and a conveying device 14 that transports the crushed materials , a level adjustment device 22 that adjusts the level of the crushed material 4 on the conveying device 14 , a scale 24 that weighs the weight of the crushed material 4 , and a moisture value of the crushed material 4 being conveyed by the conveying device 14 . a moisture meter 23 that measures the moisture content, an arithmetic processing unit 25 that inputs the measured moisture value and weight in real time, and an arithmetic processing unit 25 that calculates the amount of water to be added based on the difference between the plastic clay moisture value and the target value based on a command from the arithmetic processing unit 25. A plastic clay moisture control device for ceramics, comprising a water addition amount control device 27 for adding water.
JP33225887A 1987-12-27 1987-12-27 Controller for moisture of plastic waste earth Pending JPH01171808A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33225887A JPH01171808A (en) 1987-12-27 1987-12-27 Controller for moisture of plastic waste earth

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33225887A JPH01171808A (en) 1987-12-27 1987-12-27 Controller for moisture of plastic waste earth

Publications (1)

Publication Number Publication Date
JPH01171808A true JPH01171808A (en) 1989-07-06

Family

ID=18252936

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33225887A Pending JPH01171808A (en) 1987-12-27 1987-12-27 Controller for moisture of plastic waste earth

Country Status (1)

Country Link
JP (1) JPH01171808A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0524318U (en) * 1991-09-13 1993-03-30 施 惠定 Added water amount control device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0524318U (en) * 1991-09-13 1993-03-30 施 惠定 Added water amount control device

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