JP2866708B2 - Continuous ceramic plate manufacturing equipment - Google Patents
Continuous ceramic plate manufacturing equipmentInfo
- Publication number
- JP2866708B2 JP2866708B2 JP14400090A JP14400090A JP2866708B2 JP 2866708 B2 JP2866708 B2 JP 2866708B2 JP 14400090 A JP14400090 A JP 14400090A JP 14400090 A JP14400090 A JP 14400090A JP 2866708 B2 JP2866708 B2 JP 2866708B2
- Authority
- JP
- Japan
- Prior art keywords
- clay
- plate
- baking
- extruder
- drying
- 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
Links
Landscapes
- Finishing Walls (AREA)
- Press-Shaping Or Shaping Using Conveyers (AREA)
- Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は粘土を主成分とする原料を連続的に層状に押
し出し、その後、乾燥、切断、焼成して陶板を製造する
装置において、陶板の化粧面を研磨することにより化粧
面を鏡面化した陶板の連続製造装置に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an apparatus for manufacturing a ceramic plate by continuously extruding a raw material mainly composed of clay in a layered form, and then drying, cutting and firing the material. BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for continuously manufacturing a porcelain plate in which a decorative surface is mirror-finished by polishing the decorative surface.
従来、この種陶板を製造する装置としては、押出機に
より所定形状に成形し、その後、乾燥、切断、釉薬、焼
成する方法によって製造していた。Conventionally, as an apparatus for manufacturing this kind of porcelain plate, it has been manufactured by a method of forming into a predetermined shape by an extruder, followed by drying, cutting, glaze, and firing.
しかしながら、施釉し焼成した場合、粘土素地と釉薬
とのヌレ特性により、焼成中、および焼成後、施釉面に
ヒビ、フクレ、ワレが発生する不利があり、粘土素地に
より使用可能な釉薬が限定される不利があった。また釉
薬が焼成中の雰囲気により酸化、還元反応を起こし、色
ムラを招く欠点があった。しかも、粘土を押出成形によ
って成形した際の模様を釉薬が不明確にしてしまう不利
があった。このため、粘土素地そのものの色を活用する
方法も考えられている。しかしながら、この場合粘土原
料が高価になる欠点があった。さらに、この種装置によ
り製造した陶板は釉油により意匠性は向上したものの、
粘土を焼成したセラミックというイメージは全くなくな
ってしまい、意匠性に欠点があった。However, when glazed and fired, there is a disadvantage that cracks, blisters and cracks occur on the glazed surface during and after firing due to the wetting property of the clay base and the glaze, and the glaze that can be used depending on the clay base is limited. There was a disadvantage. Further, there is a disadvantage that the glaze causes an oxidation and a reduction reaction depending on the atmosphere during the firing, causing color unevenness. In addition, there is a disadvantage that the glaze makes the pattern when the clay is formed by extrusion molding unclear. For this reason, a method of utilizing the color of the clay body itself has been considered. However, in this case, there was a disadvantage that the clay raw material was expensive. Furthermore, although the porcelain plate produced by this type of equipment has been improved in design by glaze oil,
The image of a ceramic fired from clay was completely lost, and there was a defect in the design.
本発明はこのような欠点を除去するため、複数の押出
機を同一の口金に連絡し、各押出機より異なる素材の粘
土を同時に、かつ層状に積層した状態で押出成形を行
い、引き続き乾燥、切断、焼成、研磨を連続的に行うこ
とにより、陶板の化粧面を鏡面化し、釉薬では出せない
セラミックのイメージを大幅に向上すると共に、原料材
コストを大幅に低減した陶板の連続製造装置を提供する
ものである。In order to eliminate such disadvantages, the present invention connects a plurality of extruders to the same die, and simultaneously extrudes clays of different materials from each extruder in a state of being laminated in layers, followed by drying and drying. By continuously cutting, firing and polishing, the decorative surface of the porcelain plate is mirror-finished, and the image of ceramics that cannot be obtained with glaze is greatly improved. Is what you do.
以下に、図面を用いて本発明に係る陶板の連続製造装
置の一実施例について詳細に説明する。第1図は上記装
置の代表的な一例を示す説明図である。図において、1
は押出成形機で複数台の押出機(図では2台)2、3を
同一の口金4に連結した構造である。さらに説明する
と、押出成形機1は第2図(a)(b)に出口部分を拡
大して示すように、押出機2、3によって異種の粘土
A、Bを同時に押し出し、同一の口金4によって例えば
第5図(a)〜(r)に示すような粘土A、Bの2層か
らなる所定断面形状の連続成形帯(以下、単に成形帯と
いう)Cを形成するものである。すなわち、粘土Aは成
形帯Cにおいて主体となる部分となり、粘土Bは化粧
面、あるいは模様となるものである。なお、粘土A、B
は主に天然物であり、各産地により成分が異なるもので
あり、これらの特徴、弱点を相互に相殺させて所定の混
合粘土を得る。その粘土Aの一例としては陶石、長石、
カオリナイト、ハロサイト、メタハロサイト、木節粘
土、蛙目粘土、信楽粘土などを打ち砕き、水を加えて練
り上げたものである。また粘土Bは粘土Aに準じた素材
であるが、焼成後、各種色を形成するように厳選された
ものである。さらに第2図(a)は第5図(a)〜
(l)に示すような、中空部aを有する成形帯Cを形成
するためのものであり、口金4は粘土A、Bの押し出し
力によって変形するものでなく、かつ、中子5を装着し
たものである。さらに説明すると中子5は、成形帯Aの
形状を第5図(a)〜(l)のように各種形状とする場
合、押出成形機1内において抵抗となり、成形帯Cの密
度分布のムラを除去し、乾燥、焼成時のワレ、変形を防
止するのに役立つものである。また中子5は第3図
(a)、(b)に示すように、成形帯Cに中空部aを形
成するための格子5aを複数有すると共に、中空部aにエ
ア、熱風、冷風、乾燥風、蒸気を強制的に送給、あるい
は排出するために格子5aをパイプ状とし、かつ、エア等
を外部より吸、排気するためのポンプ7と、吸、排気管
6に接続している。これは、押出成形機1によって成形
された成形帯Cの中空部aにエア、熱風、冷風、乾燥風
を強制的に送給、あるいは排出することによって中空部
aのエアサイクルを強制的に行い、成形帯C内部の乾燥
時間を大幅に短縮するのに有効なものである。8は駆動
用搬送機でフリーローラ、駆動ローラ、ベルト、メッシ
ュベルト等の1種以上から構成されるものであり、押出
成形機1から押し出された成形帯Cのスピードと同じ速
さに同調させた駆動をかけたものである。9は乾燥機
で、駆動用搬送機8の一部、あるいは図示しないが全部
を包囲し、赤外線ヒータ、遠赤外線ヒータ、マイクロ
波、後述する焼成炉12の廃熱などの一種以上を用い、そ
の熱源9aによって成形帯Aを上記中空部aのエアサイク
ルとの相乗効果によって短時間で乾燥するのに有効なも
のであり、粘土A、Bの水分を例えば18〜20%のものを
0〜5%位までに低減し、保形性を強化するのと、その
後の切断、焼成可能な性状にするためのものである。な
お、乾燥機9は赤外線ヒータ、マイクロ波のみ、あるい
は交互に、もしくは前段と後段のゾーンに分けて配設
し、雰囲気を200〜500℃位に生地がクラックや変形を生
じないようなある加熱曲線に対応して加熱するものであ
る。10は走行カッタで、乾燥された成形帯Cを定尺に回
転刃(ダイヤモンドソー)、レーザー、水圧(ウォータ
ージェット)、放電加工等により切断し、定尺の乾燥板
Dとするものである。もちろん、走行カッタ10は成形帯
Cに速度に同調して切断するものである。11は移送機
で、走行カッタ10で定尺に切断された乾燥板Dを駆動用
搬送機8より速い速度で焼成炉12まで搬送するものであ
り、成形帯Cと乾燥板Dとの衝突を防止するものであ
る。12は焼成炉でローラーハースキルン、トンネル型焼
成炉の1種からなり、その構成は入口12aから出口12bに
亘って、常温−高温(1300℃位)−常温というように、
山状の温度分布となり、予熱領域13、焼成領域14、冷却
領域15の順に一応区分して構成し、予熱領域13の温度は
30〜700℃、焼成領域14は300〜1300℃、冷却領域15は60
0〜30℃位までとしたものである。勿論、粘土1の種
類、組成によっては各領域間の温度設定が異なるもので
あり、かつ、各領域間の温度も明確に区分するものでは
なく連続焼成の中での一応の区分である。さらに焼成炉
12について詳細に説明すると、焼成炉12は可燃ガス、例
えばLPGガスを燃焼させて乾燥板Dを焼成するものであ
り、そのためのバーナ(図示せず)の配列は前記各領域
に対応して設けるものである。また、焼成炉12内の乾燥
板Dの搬送手段としてはメッシュベルト、金属ローラ、
セラミックローラ、アルミナローラ等を使用するが、特
に焼成領域14の範囲は1300℃位まで温度が上昇するの
で、例えば第4図に示すように金属主軸16、17間にアル
ミナローラ18を載置して熱伝導を駆動源に伝達しないよ
うにして搬送するものである。なお、焼成炉12の焼成領
域14は耐火レンガ等で炉を形成し、その中を直線的に連
続して通過させるものであり、各機器、領域間には排気
ダンパー(図示せず)を配設しておくものである。19は
搬送兼ストックヤードで、焼成炉12の出口12bから出て
きた30℃位に温度が低下した焼成板Eを、次工程の研磨
機20に送給するためのものであると共に、焼成板Eがま
だ熱い場合には冷却し、次工程の研磨機20での研磨中に
施される潤滑液により急冷されて割れるのを阻止するた
めのものである。20は研磨機であり、焼成炉12により焼
成されて焼き締まった焼成板Eの化粧面αを固定兼搬送
機21上において先端にダイヤモンド研磨ホイル22aを装
着した前後、左右、上下と立体的に移動可能なポリッシ
ングマシン22により研磨し、化粧面αを鏡面化して陶板
Fとするものである。なお、研磨機20では、焼成板Eを
停止させて研磨したり、搬送中に研磨することが可能で
あり、焼成板Eを停止させて加工する場合は、搬送兼ス
トックヤード19より送出される焼成板Eと研磨中の焼成
板Eとが衝突しないように、ある程度の時間差、所謂成
形帯Cのスピードと研磨機20における研磨加工時間を考
慮して搬送兼ストックヤード19のスピード、ストック時
間を調整するものである。23は搬送機で、研磨機20によ
り磨ぎ上げられた陶板Fを梱包などの次工程に搬送する
ためのものである。Hereinafter, an embodiment of a continuous production apparatus for a porcelain plate according to the present invention will be described in detail with reference to the drawings. FIG. 1 is an explanatory view showing a typical example of the above apparatus. In the figure, 1
Has a structure in which a plurality of extruders (two in the figure) 2 and 3 are connected to the same base 4 by an extruder. Explaining further, the extruder 1 simultaneously extrudes different kinds of clays A and B by the extruders 2 and 3 as shown in FIG. For example, as shown in FIGS. 5 (a) to 5 (r), a continuous formed band (hereinafter simply referred to as a formed band) C having a predetermined cross-sectional shape composed of two layers of clays A and B is formed. That is, the clay A is a main part in the molded band C, and the clay B is a decorative surface or a pattern. In addition, clay A, B
Is mainly a natural product, and has different components depending on each locality. These characteristics and weak points are mutually offset to obtain a predetermined mixed clay. Pottery stone, feldspar,
It is made by shattering kaolinite, halosite, metahalosite, Kibushi clay, Frogme clay, Shigaraki clay, and adding water to make it. Clay B is a material similar to Clay A, but has been carefully selected to form various colors after firing. Further, FIG. 2 (a) shows FIGS. 5 (a) to
This is for forming a molded band C having a hollow part a as shown in (l). The base 4 is not deformed by the pushing force of the clays A and B, and the core 5 is attached. Things. More specifically, when the shape of the molding band A is variously shaped as shown in FIGS. 5A to 5L, the core 5 becomes a resistance in the extruder 1 and the density distribution of the molding band C becomes uneven. And helps to prevent cracking and deformation during drying and firing. As shown in FIGS. 3 (a) and 3 (b), the core 5 has a plurality of lattices 5a for forming the hollow portions a in the molding band C, and air, hot air, cold air, and dry air are formed in the hollow portions a. The grid 5a has a pipe shape for forcibly sending or discharging wind and steam, and is connected to a pump 7 for sucking and exhausting air and the like from outside and a suction and exhaust pipe 6. This is to forcibly perform an air cycle of the hollow part a by forcibly sending or discharging air, hot air, cold air, and dry air to or from the hollow part a of the forming band C formed by the extruder 1 . This is effective for greatly shortening the drying time inside the forming zone C. Numeral 8 denotes a driving conveyor, which is composed of at least one of a free roller, a driving roller, a belt, a mesh belt and the like, and is tuned to the same speed as the speed of the forming belt C extruded from the extruder 1. Drive. Numeral 9 denotes a dryer, which surrounds a part of the driving transfer machine 8 or the whole, not shown, and uses one or more of an infrared heater, a far infrared heater, a microwave, and waste heat of a baking furnace 12 described later. The heat source 9a is effective for drying the molded zone A in a short time by a synergistic effect with the air cycle of the hollow portion a. % In order to enhance the shape retention and to make it into a property that can be cut and fired thereafter. The dryer 9 is provided with an infrared heater, a microwave only, or alternately, or divided into a first stage and a second stage. The atmosphere is heated to about 200 to 500 ° C. so that the dough does not crack or deform. Heating is performed according to the curve. Numeral 10 denotes a traveling cutter, which cuts the dried molded strip C into a fixed length by a rotary blade (diamond saw), laser, water pressure (water jet), electric discharge machining, or the like to form a fixed-size drying plate D. Of course, the traveling cutter 10 cuts the forming band C in synchronization with the speed. Numeral 11 denotes a transfer machine which conveys the drying plate D cut to a fixed size by the traveling cutter 10 to the firing furnace 12 at a speed higher than that of the driving conveying machine 8. It is to prevent. Numeral 12 is a firing furnace consisting of one type of roller hearth kiln and a tunnel type firing furnace. The configuration is from room temperature to high temperature (about 1300 ° C.) to room temperature, from the inlet 12a to the outlet 12b.
It becomes a mountain-like temperature distribution, and is configured by dividing the preheating region 13, the firing region 14, and the cooling region 15 in this order, and the temperature of the preheating region 13 is
30-700 ° C, firing area 14 is 300-1300 ° C, cooling area 15 is 60
The temperature was set to 0 to 30 ° C. Of course, depending on the type and composition of the clay 1, the temperature setting between the respective regions differs, and the temperature between the respective regions is not a clear division but a tentative division in continuous firing. Further firing furnace
To describe in detail 12, the firing furnace 12 is intended to firing combustible gas, for example dry plate D by burning LPG gas, arrangement of the burner for the (not shown) is provided corresponding to the respective areas Things. Further, as a conveying means of the drying plate D in the firing furnace 12 , a mesh belt, a metal roller,
A ceramic roller, an alumina roller, or the like is used. In particular, since the temperature of the range of the sintering region 14 rises to about 1300 ° C., an alumina roller 18 is placed between the metal spindles 16 and 17 as shown in FIG. In this case, the heat is not transferred to the drive source to transfer the heat. The sintering area 14 of the sintering furnace 12 is made of a furnace made of refractory bricks and the like, and is passed through the furnace continuously and linearly. An exhaust damper (not shown) is arranged between each device and the area. It should be set up. Reference numeral 19 denotes a transfer / stock yard for feeding a baking plate E, which has come out of the outlet 12b of the baking furnace 12 and whose temperature has dropped to about 30 ° C., to the polishing machine 20 in the next step. If E is still hot, it is cooled to prevent it from being quenched and broken by the lubricating liquid applied during polishing by the polishing machine 20 in the next step. Reference numeral 20 denotes a polishing machine which fixes the decorative surface α of the fired plate E which has been fired and baked by the firing furnace 12 and has a diamond polishing foil 22a attached to the tip thereof on a transfer machine 21 before, after, right and left, and vertically. Polishing is performed by a movable polishing machine 22, and the decorative surface α is mirror-finished to obtain a ceramic plate F. In the polishing machine 20 , it is possible to stop the baking plate E for polishing, or to grind during transportation. When the baking plate E is stopped and processing is performed, it is sent out from the transportation and stock yard 19. The speed and stock time of the transfer and stock yard 19 are determined in consideration of a certain time difference, that is, the speed of the so-called forming band C and the polishing time in the polishing machine 20 so that the fired plate E and the fired plate E being polished do not collide. It is to adjust. Reference numeral 23 denotes a transfer device for transferring the porcelain plate F polished by the polishing machine 20 to the next step such as packing.
次に動作について説明する。そこで、粘土A、Bの素
材として硅砂排泥、数種の融点降下剤、繊維鉱物を準備
する。なお、その重量%は硅酸排泥65%、融点降下剤
(釜戸長石、セリサイド系鉱物等)25%、ワラストナイ
ト10%であり、その主原料100重量%に対し、水20重量
%、解膠剤としてピロリン酸ソーダ0.3重量%を混入
し、これを、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1は押し出し能力50
kg/cm2の押出圧力を持つものを使用した。ポンプ7は5H
Pで排気するように設定し、乾燥機9としてはマイクロ
波加熱機、遠赤外線加熱機を用い、35kcal・h相当の発
熱量により成形帯Cの水分を対流による表面蒸発と吸、
排気管6からの30℃位の温風排気による内部拡散とによ
って水分を0〜5%位までに約20〜40分間で減水して、
変形なく乾燥させるものである。次に乾燥された成形帯
Cは走行カッタ10によって3mに切断され、乾燥板Dとな
って移送機11によって連続的に焼成炉12に送給される。
この焼成炉12はローラハースキルン構造に形成されてお
り、このローラに対し乾燥板Dを入口12aから出口12bま
で順次送給すると共に搬送し、予熱→焼成→徐冷して焼
成板Eとして送出する。次に搬送兼ストックヤード19に
より焼成板Eを研磨機20に送給し、搬送兼ストックヤー
ド19から次の焼成板Eが送られて来る間に化粧面αをポ
リッシングマシン22により研磨し磨き上げて陶板Fとし
て送出する。次に搬送機23によって図示しないが梱包工
程などの次工程に搬送されるものである。Next, the operation will be described. Therefore, silica sand sludge, several kinds of melting point depressants, and fiber minerals are prepared as materials for the clays A and B. The weight percent is silicic acid wastewater 65%, melting point depressant (Kamado feldspar, sericide mineral, etc.) 25%, wollastonite 10%, water 20% by weight, As a peptizer, 0.3% by weight of sodium pyrophosphate was mixed and kneaded with a clay kneading machine (MP-100, manufactured by Miyazaki Iron Works Co., Ltd.). The extrusion machine 1 has an extrusion capacity of 50.
Those having an extrusion pressure of kg / cm 2 were used. Pump 7 is 5H
P was set to exhaust, and a microwave heater and a far-infrared heater were used as the dryer 9 , and the surface of the molding zone C was evaporated and absorbed by convection with a heat value equivalent to 35 kcal · h.
The water is reduced to about 0 to 5% in about 20 to 40 minutes by the internal diffusion by the warm air exhaust at about 30 ° C. from the exhaust pipe 6,
It is dried without deformation. Next, the dried forming band C is cut into 3 m by the traveling cutter 10, becomes a drying plate D, and is continuously fed to the firing furnace 12 by the transfer device 11.
The firing furnace 12 is formed in a roller hearth kiln structure. The drying plate D is sequentially fed from the inlet 12a to the outlet 12b and transported to the rollers, and is preheated, fired, gradually cooled, and sent out as the fired plate E. I do. Next, the fired plate E is sent to the polishing machine 20 by the transfer and stockyard 19, and the decorative surface α is polished and polished by the polishing machine 22 while the next fired plate E is sent from the transfer and stockyard 19. And send it out as a ceramic plate F. Next, although not shown, the sheet is conveyed to the next step such as a packing step by the conveyor 23.
上述したように、本発明に係る陶板の連続製造装置に
よれば、化粧面を鏡面化し、従来にない意匠性のある
陶板を製造できる。陶板の色合いを、素地を利用して
現出させることにより、大理石調の光沢を持つ陶板を製
造することができる。窯業系の製品との差別化を図る
ことができる製品を製造できる。釉薬を使用すること
がない。押出機を2台とし、主体を廉価な粘土、表層
を効果な水簸等した粘土を使用することができ、原材料
コストが大幅に低減する。意匠性が飛躍的に向上した
陶板を、生産性、歩留まり良く、従来の装置に簡単に組
み込んで製造することができる。等の特徴、効果があ
る。As described above, according to the continuous production apparatus for a porcelain plate according to the present invention, a decorative surface can be mirror-finished, and a porcelain plate with an unprecedented design can be produced. By making the color of the ceramic plate appear using the base material, a ceramic plate having a marble-like luster can be manufactured. Products that can be differentiated from ceramic products can be manufactured. No glaze is used. It is possible to use two extruders and use inexpensive clay as the main component and clay with effective elutriation on the surface layer, and the cost of raw materials is greatly reduced. A porcelain plate with dramatically improved design can be easily incorporated into a conventional device and manufactured with good productivity and yield. There are features and effects such as.
第1図は本発明に係る陶板の連続製造装置の代表的な一
例を示す説明図、第2図(a)、(b)は押出成形機の
口金部分を示す説明図、第3図(a)、(b)は口金を
示す説明図、第4図は焼成炉の一例を示す説明図、第5
図(a)〜(r)は連続成形帯の一例を示す説明図であ
る。 A、B……粘土、1……押出成形機、2、3……押出
機、4……口金、5……中子、7……ポンプ、9……乾
燥機、10……走行カッタ、12……焼成炉、19……搬送兼
ストックヤード、20……研磨機、21……固定兼搬送機、
22……ポリッシングマシン。FIG. 1 is an explanatory view showing a typical example of a continuous production apparatus for a porcelain plate according to the present invention, FIGS. 2 (a) and 2 (b) are explanatory views showing a die portion of an extrusion molding machine, and FIG. 3 (a). ) And (b) are explanatory diagrams showing a die, FIG. 4 is an explanatory diagram showing an example of a firing furnace, and FIG.
Drawings (a)-(r) are explanatory views showing an example of a continuous formation zone. A, B: clay, 1 ... extruder, 2, 3 ... extruder, 4 ... die, 5 ... core, 7 ... pump, 9 ... dryer, 10 ... running cutter, 12 … Baking furnace, 19… Transport and stock yard, 20 … Polisher, 21… Fixed and transport machine,
22 ... Polishing machine.
Claims (1)
2台の押出機を同一の口金に連結し粘土を同時に層状に
積層して成形する押出成形機と、該押出成形機から送出
される連続成形帯をその状態のままで搬送する駆動用搬
送機と、該搬送機の一部または全部を包囲し、上記連続
成形帯を押し出された状態で搬送している最中に乾燥す
る乾燥機と、該乾燥機によって乾燥された連続成形帯を
定尺にカットする走行カッタと、該走行カッタで定尺に
切断された乾燥板を前記駆動用搬送機より速い速度で移
送する移送機と、該移送機から送出される乾燥板を連続
的に予熱−焼成−徐冷を行う焼成炉と、該焼成炉から送
出された焼成板の化粧面を研磨する研磨機とからなるこ
とを特徴とする陶板の連続製造装置。1. An extruder for connecting two extruders for continuously extruding a raw material mainly composed of clay to the same die and simultaneously laminating and forming clay in a layered form, and sending out from the extruder. And a driving carrier for transporting the continuously formed belt as it is, and surrounding part or all of the transporter, and drying while the continuous belt is being transported in an extruded state. A dryer, a traveling cutter for cutting the continuous formed belt dried by the dryer to a fixed size, and a transfer device for transferring the drying plate cut to the fixed size by the traveling cutter at a speed higher than the driving transfer device. And a baking furnace for continuously preheating, baking, and gradually cooling the dried plate sent from the transfer machine, and a polishing machine for polishing a decorative surface of the baking plate sent from the baking furnace. Continuous production equipment for porcelain plates.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14400090A JP2866708B2 (en) | 1990-05-31 | 1990-05-31 | Continuous ceramic plate manufacturing equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14400090A JP2866708B2 (en) | 1990-05-31 | 1990-05-31 | Continuous ceramic plate manufacturing equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0435905A JPH0435905A (en) | 1992-02-06 |
JP2866708B2 true JP2866708B2 (en) | 1999-03-08 |
Family
ID=15351987
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14400090A Expired - Fee Related JP2866708B2 (en) | 1990-05-31 | 1990-05-31 | Continuous ceramic plate manufacturing equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2866708B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05278093A (en) * | 1992-03-31 | 1993-10-26 | Agency Of Ind Science & Technol | Method for lamination extrusion molding and its apparatus |
WO2010108930A2 (en) * | 2009-03-23 | 2010-09-30 | Engin Hasan Hueseyin | Laboratory type quick film drying oven |
CN106166794A (en) * | 2016-08-26 | 2016-11-30 | 中民筑友科技投资有限公司 | A kind of preform production line |
CN107553702B (en) * | 2017-09-06 | 2020-07-03 | 景德镇善隐陶瓷有限公司 | Intelligent automatic carving glazing method based on big data operation |
-
1990
- 1990-05-31 JP JP14400090A patent/JP2866708B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0435905A (en) | 1992-02-06 |
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