JPH0725085B2 - Method for manufacturing long ceramic board - Google Patents
Method for manufacturing long ceramic boardInfo
- Publication number
- JPH0725085B2 JPH0725085B2 JP1437387A JP1437387A JPH0725085B2 JP H0725085 B2 JPH0725085 B2 JP H0725085B2 JP 1437387 A JP1437387 A JP 1437387A JP 1437387 A JP1437387 A JP 1437387A JP H0725085 B2 JPH0725085 B2 JP H0725085B2
- Authority
- JP
- Japan
- Prior art keywords
- extruded
- extrusion
- extruded body
- air
- continuous
- 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 - Lifetime
Links
- 239000000919 ceramic Substances 0.000 title claims description 12
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 238000000034 method Methods 0.000 title description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 238000010438 heat treatment Methods 0.000 claims description 16
- 238000001125 extrusion Methods 0.000 claims description 15
- 238000001035 drying Methods 0.000 claims description 7
- 239000002994 raw material Substances 0.000 claims description 4
- 238000007664 blowing Methods 0.000 claims description 2
- 239000002734 clay mineral Substances 0.000 claims description 2
- 239000004927 clay Substances 0.000 description 16
- 235000012438 extruded product Nutrition 0.000 description 12
- 238000001704 evaporation Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 3
- 239000002344 surface layer Substances 0.000 description 3
- 239000004809 Teflon Substances 0.000 description 2
- 229920006362 Teflon® Polymers 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010433 feldspar Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 229910052622 kaolinite Inorganic materials 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Press-Shaping Or Shaping Using Conveyers (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は粘土鉱物を主成分とする原料を連続して任意形
状、例えば平板、中空体で押し出した連続体を変形な
く、かつクラック等を発生させずに約1〜30分位の短時
間に迅速に乾燥する長尺セラミック板の製造方法に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is to continuously produce a raw material containing a clay mineral as a main component in an arbitrary shape, such as a flat plate or a continuous body extruded with a hollow body, without causing deformation and cracks. The present invention relates to a method for producing a long ceramic plate which is quickly dried in a short time of about 1 to 30 minutes without being generated.
瓦、タイル等は押出成形機の出口で短尺に切断され、こ
れは廃熱、自然乾燥の工程に送り、約1日〜1週間位で
乾燥し、次に施釉、焼成工程へ送給する方法によって製
造していた。Roof tiles, tiles, etc. are cut into short pieces at the exit of the extruder, sent to the process of waste heat and natural drying, dried for about 1 day to 1 week, and then sent to the glaze and baking process. Was manufactured by.
セラミック板、例えば瓦、タイル等は押し出された成形
体が軟らかく、変形なく乾燥工程に移動することが困難
なため変形やクラックのない長尺の乾燥体を得ることが
できなかった。しかも、従来の乾燥工程は単に押出成形
体の外表面からのみ水分を蒸発させる方法のため、急激
な加熱をすれば割れたり、変形が大きかったりしてゆっ
くりと乾燥しなければならず、長時間乾燥とそれによる
コストアップと生産性の低さおよび広い面積の置場の問
題があった。For ceramic plates, such as roof tiles and tiles, the extruded molded body is soft and it is difficult to move to the drying step without deformation, so that a long dried body without deformation or cracks could not be obtained. Moreover, since the conventional drying process is a method of evaporating water only from the outer surface of the extrusion molded body, it has to be dried slowly because it may be cracked or deformed significantly if it is heated rapidly, and it may take a long time. There were problems of drying, cost increase due to it, low productivity, and large-area storage.
本発明はこのような欠点を除去するため、押出成形体を
連続したままで、かつ押出速度で移動中にマイクロ波と
遠赤外線ヒータの雰囲気中を通過させると共に、特に中
空体においては内部にドライエアを押出方向に平行に送
給し、押出成形体の表、裏面には水蒸気を取り払うよう
にエア、ドライエア、温風等を吹込み連続した押出成形
体をより迅速に変形やクラックが生じないように直線ラ
イン上で乾燥させ、その後に定尺に切断してより中空部
内のドライエアの通風を改善して効率的に水分を蒸発さ
せて従前より長い、例えば0.5〜5m位の長尺セラミック
板を迅速に、高能率で、連続的に低コストで乾燥させて
製造する方法を提供するものである。In order to eliminate such drawbacks, the present invention allows the extruded body to remain continuous and pass through the atmosphere of the microwave and the far infrared heater while moving at the extrusion speed, and in particular, in the hollow body, dry air is internally provided. Is fed parallel to the extrusion direction, and air, dry air, warm air, etc. are blown to remove steam from the front and back of the extruded body so that continuous extrusion does not deform or crack more quickly. Then, dry it on a straight line, and then cut it to a fixed length to improve the ventilation of dry air in the hollow part to efficiently evaporate moisture and elongate a longer ceramic plate, for example, 0.5 to 5 m. It is intended to provide a method for producing by drying rapidly, at high efficiency, and continuously at low cost.
以下に、図面を用いて本発明に係る長尺セラミック板の
製造方法の一実施例について詳細に説明する。第1図は
本発明の実施に供する装置の概略を示す説明図である。
図において、1は粘土で数種の原料とシャモット等を混
練機(図示せず)を介して混合したものであり、これを
押出成形機、例えば真空押出成形機2で口金3から例え
ば第2図(a)〜(s)に示す断面形状で押し出すもの
である。また、口金3には必要により中空体の押出成形
体用の例えば第3図(a)〜(c)に示すような中子4
と中空体内部に気体を吸気、あるいは排気する管5を中
子4に1本、もしくは各格子4aに1本づつ装着した構成
であり、格子4aとしては根本から出口に向かって断面積
が拡大する構成が押し出し抵抗の関係等で好ましい。さ
らに管5には制御バルブ6、所要の気体を送給したり、
排気したりする気体吸、排気装置7を連結し、中空体内
部の水蒸気を押出成形体Aへ排出するように移動、圧送
して連続状体の押出成形体Aの内部を迅速に乾燥するた
めのものである。なお、連続体の押出成形体Aとは乾燥
後までの長尺体であり、その後は定尺にカットするもの
である。なお、粘土1は天然物であり、各産地により成
分が異なるものであり、これらの特長、弱点を相互に利
用して所定の混合粘土を得る。その粘土1の一例として
は陶石、長石、カオリンナイト、ハロサイト、メタハロ
サイト、木節粘土、蛙目粘土、信楽木粘土などを打ち砕
き、水を加えて練り上げるものである。また、この粘土
1は必要によりマグネットによって除鉄されることもあ
る。8は搬送機でフリローラ9、駆動ベルト10等の1種
以上を口金3の出口と同一レベルで、かつ押出方向に沿
って直線状に配列したものであり、押出成形体Aをその
ままの状態でかつ、押出速度で次工程に搬送するための
ものである。11はマイクロ波加熱装置で押出成形体Aの
内部へマイクロ波αが浸透して熱伝導に時間を要するこ
となくマイクロ波αを熱エネルギーに変換し、数秒から
数分で発熱して粘土1内の水分を蒸発せしめるためのも
のである。なお、水分が押出成形体Aにおいて重量比で
22〜15%位含有させており、そのうち、例えば5〜10%
を蒸発する能力を有するものである。特に、この種押出
成形体Aは水分が5〜8%位になるまで体積が収縮する
が、それ以下の水分になると体積の収縮が生じないもの
となる。そこで、マイクロ波加熱装置11を第4図
(a)、および、(b)(第4図(a)におけるイ−イ
線断面図)を用いて具体的に説明すると、図示しないマ
イクロ波発振器から発振されたマイクロ波αを所要個所
に案内する導波管12と、案内されたマイクロ波αを反射
する反射板13と、反射されたマイクロ波αを攪拌する回
転羽根14と、押出成形体Aを押出速度で移動させると共
に、誘電はするがスパークしない構成のフリローラから
なる搬送部15と、押出成形体Aの入口、出口16、17とエ
ア等βを大量に被加熱空間18から吸引したり、被加熱空
間18へ供給したりするエア供給口19と、マイクロ波αが
外部へ漏洩しないように囲んだ包囲体20とから構成した
ものである。なお、入口、出口16、17はマイクロ波αが
外部へ漏洩しないフィルターとしても機能する構造、長
さに形成したものである。また、押出成形体Aを加熱す
る被加熱空間18は目的に応じて異なるが、例えば1〜5m
位としたものである。さらに、搬送部15はマイクロ波
α、エア等βが押出成形体Aに均一に照射もしくは送風
されることと、押出成形体Aが乾燥する際に1割程度全
体が収縮するため、これを吸収しながら押出成形体Aを
搬送できる構成としたものである。その一例を図示する
と第5図(a)、(b)に示すように、固定された芯棒
20とテフロンからなるパイプ状のフリローラ21と第6図
に示すような芯棒支持具22とから構成したものである。
さらに説明すると第5図(a)においてフリローラ21は
幅を例えば3分割し、押出成形体A通過時の抵抗をより
小さくした構成、(b)図は一本で構成したフリローラ
21aである。また、芯棒支持具22はマイクロ波αが押出
成形体Aの裏面からも照射されるように通過孔22aを穿
設したものである。また、エア供給口19はコンプレッ
サ、リングブロア等のエア(ドライエア、温風、熱風空
気も含む)の送風、もしくは吸引可能なエアサイクル用
原動機23に連結し、押出成形体Aの表、裏面側の表層に
存在する水蒸気をより効率的に排除し、水蒸気の蒸発を
助長するのに役立つものである。なお、搬送機8は搬送
部15と同一レベルに対応させ、かつ直列に配列したもの
である。24は遠赤外線ヒータ装置で押出成形体Aの中心
部から表層まで短時間に乾燥するのに有効なものであ
り、粘土1の水分を例えば8〜10%のものを1〜0%位
までに低減し、保形性を強化するためのものである。そ
の構成はフリローラの搬送部25と複数個の遠赤外線ヒー
タ26と包囲体27と必要により設ける送給、排気口28とか
らなり、押出成形体Aの特に、表層部をより加熱して水
分を低減し、乾燥体とするものである。なお、エア等β
は図示しないファン等で攪拌し、水蒸気の押出成形体A
の表面からの蒸発をより効率的に行うことができる。An embodiment of the method for producing a long ceramic plate according to the present invention will be described in detail below with reference to the drawings. FIG. 1 is an explanatory view showing an outline of an apparatus used for carrying out the present invention.
In the figure, reference numeral 1 denotes clay which is obtained by mixing several kinds of raw materials with chamotte or the like through a kneader (not shown), and this is extruded by a vacuum extruding machine 2, for example, from a die 3 to a second It is extruded in the cross-sectional shape shown in FIGS. If necessary, the die 3 may be a core 4 for an extruded hollow body, for example, as shown in FIGS. 3 (a) to 3 (c).
And a tube 5 for inhaling or exhausting gas inside the hollow body is attached to the core 4 or to each lattice 4a, and the cross-sectional area of the lattice 4a increases from the root to the outlet. The configuration described above is preferable in terms of extrusion resistance. Furthermore, the control valve 6 is supplied to the pipe 5 to supply a required gas,
In order to quickly dry the inside of the continuous extrusion-molded body A by connecting the exhaust gas suction / exhaust device 7 and moving the steam inside the hollow body so as to discharge it to the extrusion-molded body A. belongs to. The continuous extrusion-molded body A is a long body until it is dried, and thereafter is cut into regular lengths. Clay 1 is a natural product and has different components depending on each producing area. By utilizing these features and weak points mutually, a predetermined mixed clay is obtained. As an example of the clay 1, pottery stone, feldspar, kaolinite, halosite, metahalosite, kibushi clay, frog eyes clay, Shigaraki clay and the like are crushed, and water is added and kneaded. If necessary, the clay 1 may be ironed by a magnet. Reference numeral 8 denotes a conveyer in which one or more kinds of a flea roller 9, a drive belt 10 and the like are arranged at the same level as the outlet of the mouthpiece 3 and linearly arranged along the extrusion direction. In addition, it is for transporting to the next step at the extrusion speed. Reference numeral 11 is a microwave heating device, in which the microwave α penetrates into the extruded product A to convert the microwave α into heat energy without requiring time for heat conduction, and heat is generated in a few seconds to a few minutes to generate heat in the clay 1. It is for evaporating the water content of. In addition, the water content in the extruded product A is a weight ratio.
22 to 15% is included, of which, for example, 5 to 10%
It has the ability to evaporate. In particular, the volume of the seed extruded product A shrinks until the water content becomes about 5 to 8%, but when the water content is less than that, the volume shrinkage does not occur. Therefore, the microwave heating device 11 will be specifically described with reference to FIGS. 4A and 4B (cross-sectional view taken along the line EE in FIG. 4A). A waveguide 12 that guides the oscillated microwave α to a required location, a reflecting plate 13 that reflects the guided microwave α, a rotary blade 14 that stirs the reflected microwave α, and an extruded body A. While moving at a pushing speed, a large amount of suction is performed from the heated space 18 such as a conveying portion 15 composed of a fli roller having a structure that causes a dielectric but does not spark, a large amount of β such as the inlets and outlets 16 and 17 of the extruded body A and air β. An air supply port 19 for supplying the heated space 18 and an enclosure 20 surrounded by the microwave α so as not to leak to the outside. The inlets and outlets 16 and 17 are formed to have a structure and length that also function as a filter that prevents the microwave α from leaking to the outside. The heated space 18 for heating the extruded body A varies depending on the purpose, but is, for example, 1 to 5 m.
It is a place. Further, the conveying unit 15 absorbs the microwaves α, air β, etc. evenly radiated or blown onto the extruded product A, and shrinks about 10% of the entire extruded product A when it is dried. However, the extruded product A can be conveyed. As shown in FIGS. 5 (a) and 5 (b), an example of the fixed core rod is shown.
It is composed of a pipe-shaped fli roller 21 made of Teflon 20 and a core rod support 22 as shown in FIG.
To further explain, in FIG. 5 (a), the width of the fli roller 21 is divided into, for example, three parts, and the resistance when passing through the extruded product A is further reduced.
21a. Further, the core rod support 22 is provided with a through hole 22a so that the microwave α is also radiated from the back surface of the extrusion molded body A. Further, the air supply port 19 is connected to an air cycle prime mover 23 capable of blowing or sucking air (including dry air, warm air, hot air air) such as a compressor and a ring blower, and the front and back sides of the extrusion molded body A. It helps to more efficiently remove the water vapor existing in the surface layer and promote evaporation of the water vapor. The carrier 8 corresponds to the same level as the carrier 15 and is arranged in series. A far infrared heater device 24 is effective for drying the central portion of the extruded product A to the surface layer in a short time. For example, the water content of clay 1 is 8 to 10% and the water content is 1 to 0%. This is to reduce the shape and enhance the shape retention. The structure is composed of a conveying section 25 of a fli roller, a plurality of far infrared ray heaters 26, an enclosure 27, and a supply / exhaust port 28 provided if necessary, and in particular, the surface layer portion of the extruded body A is further heated to remove moisture. It is to be reduced and dried. In addition, air β
Is a steam extruded product A that is agitated by a fan or the like not shown.
Can be more efficiently evaporated from the surface.
次に本発明に係る長尺セラミック板の製造方法について
説明する。まず粘土1としては例えば信楽粘土とシャモ
ット減水剤と水からなる原料を準備する。なお、その重
量%は信楽粘土61.5%、シャモット20%、減水剤0.5%
(商品名セルフロー:第一工業製薬社製)、水18%を土
練機(MP−100型宮崎鉄工社製)で混練したものであ
る。また、押出成形機2は押し出し能力100〜150l/hrの
型名MV−FM−A−1型(宮崎鉄工社製)を用いた。気体
吸、排気装置は2HPで排気するように設定した。また、
マイクロ波加熱装置11は周波数が2450MHZ、出力5KW、ヒ
ータ加熱空間18の長さは3mとし、エア等βを被加熱空間
18に大量に包囲体20のエア供給口19から送給し、入、出
口16、17から加熱時に発生する水蒸気β′を外部へ放出
し、被加熱空間18内の水蒸気圧を低下し、被加熱物、包
囲体20の内壁に結露水が発生するのを防止できる構成と
したものであり、搬送部15はテフロン製パイプからなる
フリローラとした。なお、マイクロ波加熱は押出成形体
Aの水分18%(重量%)を7%(重量%)まで蒸発させ
ると仮定する。さらに、遠赤外線ヒータ装置24として
は、遠赤外線ヒータ26として波長4μ〜400μの遠赤外
線パネルヒータを10メートル間に10個配列し、押出成形
帯A内部の水分を表面に拡散して脱水を迅速化し、水分
を1〜0%まで低減しうるものである。また、遠赤外線
ヒータ装置24内はファンによってエアが攪拌され、より
押出成形体Aの表面部の水蒸気が拡散されやすくした。
そこで、いま第2図(a)に示す断面のセラミック板の
押出成形体Aを0.5〜10m/min、ここでは400mm/minで連
続して厚さ20mmで押し出すと仮定する。押し出された連
続成形体Aは口金3から搬送機8を介して押出速度で直
線的に、変形やクラックが生じないようにして搬送し、
マイクロ波加熱装置11に送給し、押出成形体Aの22〜18
%の水分を約5〜10分で7〜5%に平均に低減し、次に
遠赤外線ヒータ装置24に連続体状で送給し、残りの水分
を約1〜10分位で蒸発させ、乾燥体とするものである。
この際、水蒸気β′はエア等βと同時にマイクロ波加熱
装置11の入、出口16、17、遠赤外線ヒータ装置24の入出
口から噴射するごとく外部へ放出される。これは押出成
形体Aの表面に出た水蒸気をふきはらうと共に、中空体
内部の水蒸気β′はドライエアによって外部へ放出され
るようになり、より水蒸気の蒸発を強化するものであ
る。なお、エアの流れと押出成形体Aの進行方向への移
動との相乗効果によってより蒸発が促進される。また、
比較例としてはマイクロ波加熱装置11にエアが供給され
ないと、水蒸気が包囲体内に飽和状態となり、エアを供
給した場合に比べ約1/3の蒸発と、結露による不利が生
ずる。Next, a method for manufacturing a long ceramic plate according to the present invention will be described. First, as the clay 1, for example, a raw material composed of Shigaraki clay, chamotte water reducing agent, and water is prepared. The weight% is Shigaraki clay 61.5%, chamotte 20%, water reducing agent 0.5%.
(Trade name: Cell Flow: manufactured by Dai-ichi Kogyo Seiyaku Co., Ltd.), and 18% of water was kneaded with a clay kneader (MP-100 type manufactured by Miyazaki Tekko Co., Ltd.). As the extruder 2, a model name MV-FM-A-1 type (manufactured by Miyazaki Tekko Co., Ltd.) having an extrusion capacity of 100 to 150 l / hr was used. The gas suction and exhaust system was set to exhaust at 2 HP. Also,
The microwave heating device 11 has a frequency of 2450 MHZ, an output of 5 KW, and the heater heating space 18 has a length of 3 m.
A large amount of air is supplied to the enclosure 18 from the air supply port 19 of the enclosure 20, and the steam β'generated during heating is discharged to the outside from the inlets / outlets 16 and 17, and the steam pressure in the heated space 18 is reduced to The heating object and the inner wall of the enclosure 20 are configured so that dew condensation water can be prevented from being generated, and the transport unit 15 is a free roller made of a Teflon pipe. In addition, it is assumed that the microwave heating evaporates the water content of the extruded product A from 18% (% by weight) to 7% (% by weight). Further, as far-infrared heater device 24 , ten far-infrared panel heaters having a wavelength of 4μ to 400μ are arrayed for 10 meters as far-infrared heater 26, and moisture in extrusion molding zone A is diffused to the surface for quick dehydration. The water content can be reduced to 1 to 0%. Further, the air is agitated by the fan in the far infrared heater device 24 , so that the water vapor on the surface of the extruded product A is more easily diffused.
Therefore, it is assumed that the extruded body A of the ceramic plate having the cross section shown in FIG. 2 (a) is continuously extruded at a thickness of 20 mm at 0.5 to 10 m / min, here 400 mm / min. The extruded continuous molded body A is conveyed linearly from the die 3 through the conveyor 8 at the extrusion speed without deformation or cracks,
It is fed to the microwave heating device 11 and the extruded body A 22 to 18
% Moisture is reduced to an average of 7-5% in about 5-10 minutes, then fed to the far-infrared heater device 24 in a continuous form to evaporate the remaining moisture in about 1-10 minutes. It is a dried product.
At this time, the water vapor β ′ is discharged to the outside at the same time as the air β and the like as being injected from the inlet / outlets 16 and 17 of the microwave heating device 11 and the inlet / outlet of the far infrared heater device 24 . This wipes off the water vapor that has come out on the surface of the extruded body A, and the water vapor β ′ inside the hollow body is released to the outside by the dry air, so that the evaporation of the water vapor is further enhanced. Note that evaporation is further promoted by the synergistic effect of the flow of air and the movement of the extruded product A in the traveling direction. Also,
As a comparative example, if air is not supplied to the microwave heating device 11 , water vapor is saturated in the enclosure, and vaporization is about 1/3 of that in the case where air is supplied, and a disadvantage due to dew condensation occurs.
以上、説明したのは本発明に係る長尺セラミック板の製
造方法の一実施例にすぎず、マイクロ波加熱装置11、遠
赤外線ヒータ装置24に関係しない焼成炉の廃熱を利用す
ることもできる。What has been described above is merely one example of the method for manufacturing a long ceramic plate according to the present invention, and the waste heat of the firing furnace not related to the microwave heating device 11 and the far infrared heater device 24 can be used. .
上述したように、本発明に係るセラミック板の製造方法
によれば、粘土からなる押出成形体を変形させずに、か
つクラックを生じないようにして迅速にしかも低コスト
で効率よく乾燥して次工程に送給できる特徴がある。As described above, according to the method for producing a ceramic plate according to the present invention, the extrusion molded body made of clay is not deformed, and cracks are not generated rapidly, efficiently and efficiently at low cost. It has the feature that it can be sent to the process.
第1図は本発明に係る長尺セラミック板の製造方法の実
施に供する装置の概略を示す説明図、第2図(a)〜
(s)は長尺セラミック板の断面の一例を示す説明図、
第3図(a)〜(c)は中子の一例を示す斜視図、第4
図(a)、(b)、第5図(a)、(b)および第6図
はマイクロ波加熱装置の一例を示す説明図である。 1……粘土、2……押出成形機、4……中子、7……気
体吸、排気装置、11……マイクロ波加熱装置。FIG. 1 is an explanatory view showing the outline of an apparatus used for carrying out the method for producing a long ceramic plate according to the present invention, and FIGS.
(S) is an explanatory view showing an example of a cross section of a long ceramic plate,
3 (a) to 3 (c) are perspective views showing an example of the core, and FIG.
Drawing (a), (b), Drawing 5 (a), (b), and Drawing 6 are explanatory views showing an example of a microwave heating device. 1 ... Clay, 2 ... Extruder, 4 ... Core, 7 ... Gas suction / exhaust device, 11 ... Microwave heating device.
Claims (1)
から連続して口金に対応した任意形状の平板、中空体で
押し出し、該連続して押し出された押出成形体を搬送機
を介してそのまま平行移動させマイクロ波加熱装置、遠
赤外線ヒータ装置の順に押出速度に対応して搬送し、該
搬送中に連続した押出成形体の中空部内壁に対して、ド
ライエアを押出成形体の進行方向に全部の中子からドラ
イエアの量、湿度、温度を制御しつつ送給し、また少な
くともマイクロ波加熱装置内の連続体状の押出成形体の
表、裏面の水蒸気を強制的な送風により排除して水分を
押し出しから乾燥までを約1〜30分位で1〜0%に迅速
に、かつ均質に連続体状の押出成形体を乾燥したことを
特徴とする長尺セラミック板の製造方法。1. A raw material made of clay mineral is continuously extruded from an outlet of an extruder by a flat plate or a hollow body having an arbitrary shape corresponding to a die, and the continuously extruded extruded body is passed through a conveyer. The microwave heating device and the far-infrared heater device are moved in parallel in that order and conveyed at a speed corresponding to the extrusion speed, and dry air is fed to the inner wall of the hollow portion of the extruded body that is continuous during the conveyance in the direction of travel of the extruded body. Dry air is supplied from all cores while controlling the amount, humidity, and temperature, and at least the steam on the front and back surfaces of the continuous extruded body in the microwave heating device is removed by forced blowing. A method for producing a long ceramic plate, characterized in that a continuous extruded body is rapidly and uniformly dried to about 1 to 0% in about 1 to 30 minutes from extrusion of water to drying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1437387A JPH0725085B2 (en) | 1987-01-23 | 1987-01-23 | Method for manufacturing long ceramic board |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1437387A JPH0725085B2 (en) | 1987-01-23 | 1987-01-23 | Method for manufacturing long ceramic board |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63182105A JPS63182105A (en) | 1988-07-27 |
| JPH0725085B2 true JPH0725085B2 (en) | 1995-03-22 |
Family
ID=11859245
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1437387A Expired - Lifetime JPH0725085B2 (en) | 1987-01-23 | 1987-01-23 | Method for manufacturing long ceramic board |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0725085B2 (en) |
-
1987
- 1987-01-23 JP JP1437387A patent/JPH0725085B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63182105A (en) | 1988-07-27 |
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