JPH0729827B2 - Continuous production equipment for long ceramic plates - Google Patents

Continuous production equipment for long ceramic plates

Info

Publication number
JPH0729827B2
JPH0729827B2 JP11233086A JP11233086A JPH0729827B2 JP H0729827 B2 JPH0729827 B2 JP H0729827B2 JP 11233086 A JP11233086 A JP 11233086A JP 11233086 A JP11233086 A JP 11233086A JP H0729827 B2 JPH0729827 B2 JP H0729827B2
Authority
JP
Japan
Prior art keywords
air
continuous
long
firing
firing furnace
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
Application number
JP11233086A
Other languages
Japanese (ja)
Other versions
JPS62270454A (en
Inventor
雅彦 阿部
寿衛 小関
聖一 富田
英喜 滝口
Original Assignee
株式会社アイジー技術研究所
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Priority to JP11233086A priority Critical patent/JPH0729827B2/en
Publication of JPS62270454A publication Critical patent/JPS62270454A/en
Publication of JPH0729827B2 publication Critical patent/JPH0729827B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (AREA)
  • Press-Shaping Or Shaping Using Conveyers (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は粘土を主成分とする原料を連続押し出しによっ
て中空状の連続帯を形成し、これを5〜30分間位の短時
間で乾燥し、定尺にカットした後に連続的に焼成して所
定長さの長尺陶板を連続して製造する装置に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention forms a hollow continuous zone by continuously extruding a raw material containing clay as a main component, and drying this in a short time of about 5 to 30 minutes. The present invention relates to an apparatus for continuously producing long ceramic plates of a predetermined length by cutting them into a regular size and then continuously firing them.

〔従来の技術〕[Conventional technology]

瓦、タイルは成形機から送出される連続成形帯を短尺に
切断し、さらにプレス加工等して成形し、これを乾燥、
焼成するか、型に材料を充填し、これをプレスによって
成形し、次に乾燥、焼成するかのいずれかの方法によっ
て製造していた。
For roof tiles and tiles, a continuous molding strip sent from a molding machine is cut into short pieces, and further shaped by pressing, etc., and dried,
It was manufactured by firing, filling a mold with material, molding it by pressing, and then drying and firing.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかしながら、この種装置では乾燥工程、焼成工程に1
〜2日を要し、生産性に劣り、コストアップとなる欠点
があった。また、従来の装置では上記のような時間を必
要とするため一貫ラインとしては長大になり、場所の関
係で一枚づつの乾燥、焼成は不可能であった。しかも、
瓦、タイル等を多数にスペーサを介在し積層して乾燥、
焼成すると製造途中のタイル等が捩じれたり、1角が垂
れ下ったり、クラックが入ったりし、歩留りが悪い不利
があった。さらに、従来装置では1〜3m位の長尺体を連
続して、かつ1〜30分位の短時間に乾燥することにより
一貫ラインを直線状に、しかも焼成工程を含めて配列す
る装置など全く考えられなかった。
However, with this type of equipment, 1
It took ~ 2 days, the productivity was poor, and the cost increased. Further, in the conventional apparatus, since the above-mentioned time is required, the integrated line becomes long, and it is impossible to dry and fire one by one due to the location. Moreover,
A large number of roof tiles, tiles, etc. are stacked with a spacer interposed therebetween and dried.
When fired, the tiles and the like in the process of manufacture were twisted, one corner drooped, cracks were formed, and there was a disadvantage in poor yield. Further, in the conventional device, a long line of about 1 to 3 m is continuously dried in a short time of about 1 to 30 minutes, so that an integrated line is linearly arranged, and a device for arranging the firing process is included. I couldn't think of it.

〔問題点を解決するための手段〕[Means for solving problems]

本発明はこのような欠点を除去するため、長尺陶板を中
空状に形成し、かつ中空状に押出成形する際に中空部に
エア、熱風、乾燥風、温風を送給すると共にイソシアネ
ート粉末を供給し、次工程の乾燥機による陶板の乾燥を
外部からの加温による表面蒸発と、中空部内の気体流通
による内部拡散、およびイソシアネート粉末による吸水
反応と反応熱による乾燥によって、陶板全体の乾燥時間
を5〜30分位に大幅に短縮し、かつ、捩じれや、クラッ
クも発生しないようにして乾燥した成形帯を走行カッタ
で任意長さ、例えば1〜3m位にカットし、引き続き、移
送している最中に連続して焼成する焼成炉を直接的に配
設して陶板を長尺体で、かつ、連続し、従前よりも短時
間で、安価に製造する長尺陶板の連続製造装置を提案す
るものである。
In order to eliminate such drawbacks, the present invention forms a long porcelain plate in a hollow shape, and when it is extrusion-molded into a hollow shape, air, hot air, dry air, and warm air are fed to the hollow portion and an isocyanate powder The surface of the porcelain plate is dried by a dryer in the next step, and the entire porcelain plate is dried by surface evaporation by external heating, internal diffusion by gas flow in the hollow part, and water absorption reaction by isocyanate powder and drying by reaction heat. The time is drastically shortened to about 5 to 30 minutes, and the dried molding strip is cut to a desired length, for example, 1 to 3 m, with a traveling cutter so that twisting and cracks do not occur, and then transferred. A continuous production device for long ceramic plates that directly and continuously manufactures a continuous baking process while the ceramic plates are long and continuous, and at a lower cost in a shorter time than before. Is proposed.

〔実施例〕〔Example〕

以下に、図面を用いて本発明に係る長尺陶板の連続製造
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は粘土で数種の原料と必要に応じて添加するシャモッ
ト等を混練機(図示せず)を介して混合したものであ
り、ベルトコンベア2を介して真空押出成形機、あるい
は真空土練押出成形機の1種からなる押出成形機3に供
給されるものである。押出成形機3は口金4、中子5を
介して例えば第2図(a)〜(j)に示すような形状で
連続して粘土1を押し出し、中空部Bを有する形状に成
形するものである。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、本節粘土、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たものである。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
れるここともある。さらに、口金4は粘土1の押し出し
た力によって変形するものではなく、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、連続成
形帯(以下、単に成形帯という)Aの形状を第2図
(a)〜(j)のように各種形状とする場合、押出成形
機3内において抵抗となり、成形帯A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)〜(d)に
示すように、成形帯Aに中空部Bを形成するための格子
5aを複数有すると共に、中空部Bにエア、熱風、冷風、
乾燥風、およびイソシアネート粉末を強制的に送給する
ために格子5aをパイプ状とし、かつ、第4図(a)、
(b)に示すようにエア等を外部より吸、排気するため
のポンプ7と排気管6と接続している。これは、押出成
形機3によって成形された成形帯Aの中空部Bにエア、
熱風、冷風、乾燥風を強制的に送給することによって中
空部Bのエアサイクルを強制的に行ない、中空部B内に
おける成形帯Aの内部蒸発と、拡散を起こし、後述する
乾燥機9による外部からの加温による表面蒸発とにより
成形帯Aの乾燥を迅速化するためである。さらに排気管
6、中子5を通してイソシアネート(R−NCO)の粉末
を中空部Bに供給する。このイソシアネートは成形帯A
の水分、あるいは、同時に供給するエアなどに含まれて
いる水分と反応し、発蒸する。すなわち、イソシアネー
トは水分と、 R-NCO+H2O→R-NHCOOH →R-NH2+CO2 R-NH2+R-NCO→R-NH2-CO-NH-R のように反応し、成形帯Aから直接水分を除去したり、
中空部Bに供給するエア等を乾燥させ、中空部Bにおけ
る乾燥を助長するものである。さらに、上記イソシアネ
ートの反応は発熱反応であるため、この熱を利用するこ
とにより、乾燥機9の熱量を大きくしても成形帯Aの
内、外部の乾燥のバランスを図ることが容易となり、よ
り迅速に乾燥させることが可能である。なお、イソシア
ネートと水との反応は初期において熱を加えなければな
らないため、乾燥機9内で反応を開始することができ、
内、外部の乾燥をほぼ同時に行うことができる。また、
イソシアネートとしては、例えばMDI(4、4′‐Diphe
nylmethane diisocyanate)、 TDI(Toly lene diisocyanate)などの2官能基、3官
能基タイプのいずれを用いてもかまわない。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3から押し出された成形帯A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。また、駆動用搬
送機8は、押出成形機3と同調した駆動をかけるため、
成形帯Aの捩じれ、反りを矯正する機能も果たすもので
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
以上を熱源9aによって成形帯Aを上記中空部Bのエアサ
イクル、イソシアネートの吸水、および発熱反応との相
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1の水分を例えば18〜20%のものを0〜2%位
までに低減し、保形性を強化するのと焼成可能な性状に
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Aを定尺に回転刃、レーザ、水圧、放電加
工により切断し、定尺で長尺の乾燥板A′(以下、単に
乾燥板という)とするものである。もちろん、走行カッ
タ10は成形帯Aの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
A′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Aと乾燥板A′との衝突を防止
するものである。12は焼成炉でローラハースキルン、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に亘って山状の温度分布となり、予熱領域1
3、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150〜700℃、焼成領域14は300
〜1300℃、冷却領域15は600〜100℃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A′
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A′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5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。なお、乾燥工程に用いたイソシアネ
ート、および水分との反応による生成物は焼成炉12中に
おいて燃焼し、出口12bから送給される長尺陶板A″で
は残留しないものである。19は搬送機で、焼成炉12の出
口12bから出てきた長尺陶板A″を梱包などの工程に搬
送するもためのものである。
An embodiment of a continuous production apparatus for long porcelain plates according to the present invention will be described in detail below with reference to the drawings. FIG. 1 is an explanatory view showing a typical example of the above apparatus. In the figure,
Reference numeral 1 is clay, which is a mixture of several raw materials and chamotte or the like which is added as needed through a kneader (not shown). A belt extruder 2 is used to form a vacuum extruder or a vacuum clay extruder. It is supplied to the extrusion molding machine 3 which is one type of molding machine. The extrusion molding machine 3 continuously extrudes the clay 1 through the die 4 and the core 5 in a shape as shown in FIGS. 2 (a) to (j) to form a shape having a hollow portion B, for example. is there. Clay 1 is a natural product and has different components depending on each production site. These characteristics and weak points are mutually offset to obtain a predetermined mixed clay. The clay 1
As an example, porcelain stone, feldspar, kaolinite, halosite, metahalosite, Honobushi clay, frog eyes clay, Shigaraki clay, etc. are crushed and kneaded by adding water. Further, the clay 1 is also removed here by a magnet if necessary. Furthermore, the die 4 is not deformed by the force of the clay 1 pushed out, and is equipped with the core 5. To further explain, the core 5 becomes a resistance in the extrusion molding machine 3 when the shape of the continuous forming band (hereinafter, simply referred to as forming band) A has various shapes as shown in FIGS. 2 (a) to (j). Also, it is useful for removing unevenness in the density distribution of the molding strip A and preventing cracks and deformation during drying and firing. Further, the core 5 is, as shown in FIGS. 3 (a) to 3 (d), a grid for forming the hollow portion B in the forming band A.
In addition to having a plurality of 5a, air, hot air, cold air in the hollow portion B,
In order to forcibly feed the dry air and the isocyanate powder, the lattice 5a has a pipe shape, and FIG. 4 (a),
As shown in (b), a pump 7 for sucking and exhausting air and the like from the outside and an exhaust pipe 6 are connected. This is the air in the hollow portion B of the forming band A formed by the extruder 3.
By forcibly feeding hot air, cold air, and dry air, the air cycle of the hollow portion B is forcibly performed, causing internal evaporation and diffusion of the molding strip A in the hollow portion B, and by the dryer 9 described later. This is to accelerate the drying of the molding strip A due to the surface evaporation due to the heating from the outside. Further, powder of isocyanate (R—NCO) is supplied to the hollow portion B through the exhaust pipe 6 and the core 5. This isocyanate is a molding strip A
And reacts with the water contained in the supplied air or the air supplied at the same time to generate steam. That is, isocyanate reacts with water as in R-NCO + H 2 O → R-NHCOOH → R-NH 2 + CO 2 R-NH 2 + R-NCO → R-NH 2 -CO-NH-R, forming zone A To remove water directly from
The air or the like supplied to the hollow portion B is dried to promote the drying in the hollow portion B. Furthermore, since the reaction of the isocyanate is an exothermic reaction, by utilizing this heat, it becomes easy to balance the drying of the molding band A and the outside even if the heat amount of the dryer 9 is increased, It can be dried quickly. Since the reaction between the isocyanate and water must be heated in the initial stage, the reaction can be started in the dryer 9 ,
Inner and outer drying can be performed almost simultaneously. Also,
Examples of the isocyanate include MDI (4, 4′-Diphe
Either a bifunctional group or trifunctional group type such as nylmethane diisocyanate) or TDI (Toly lene diisocyanate) may be used. Reference numeral 8 denotes a drive transporting machine, which is composed of one or more kinds of free rollers, drive rollers, belts, mesh belts, etc., and is synchronized with the speed of the molding strip A extruded from the extruder 3. It was driven. Further, since the driving carrier 8 applies driving in synchronization with the extrusion molding machine 3,
It also has a function of correcting twisting and warping of the molding strip A. Reference numeral 9 denotes a dryer, which surrounds a part of the drive carrier 8 or the whole of the drive carrier 8 (not shown). One or more of infrared heaters, far infrared heaters, microwaves, waste heat of the firing furnace 12 to be described later, etc. are heated by a heat source 9a. It is effective to dry the molding zone A in a short time by the synergistic effect of the air cycle of the hollow portion B, the water absorption of isocyanate, and the exothermic reaction, and the moisture content of the clay 1 is, for example, 18 to 20%. This is for reducing the content to about 0 to 2% to enhance the shape retention and to make it a calcinable property. In addition, the dryer 9 is provided with an infrared heater, only microwaves, or alternately or divided into front and rear zones, and the atmosphere is heated at about 200 to 500 ° C. so that the dough does not crack or deform. It heats according to the curve. Reference numeral 10 denotes a traveling cutter, which cuts the dried forming band A into a regular length by a rotary blade, laser, water pressure, and electric discharge machining to form a long and constant length drying plate A '(hereinafter simply referred to as a drying plate). Is. Of course, the traveling cutter 10 cuts in synchronization with the speed of the forming belt A.
Reference numeral 11 denotes a transfer machine, which conveys the drying plate A ′ cut to a fixed length by the traveling cutter 10 to the firing furnace 12 at a speed faster than that of the driving transporting device 8, and the forming strip A and the drying plate A ′. It is to prevent a collision. Numeral 12 is a calcining furnace consisting of one of a roller hearth kiln and a tunnel type calcining furnace, and its configuration has a mountain-shaped temperature distribution from the inlet 12a to the outlet 12b, and the preheating region 1
3, the firing region 14 and the cooling region 15 are divided in this order, and the temperature of the preheating region 13 is 150 to 700 ° C. and the firing region 14 is 300
~ 1300 ℃, the cooling region 15 is about 600 ~ 100 ℃. Of course, the temperature setting between the regions differs depending on the type and composition of the clay 1, and the temperature between the regions is not a clear division but a temporary division during continuous firing. To further explain the firing furnace 12 , the firing furnace
12 is a drying plate A'combusted with a combustible gas such as LPG gas.
And a burner (not shown) for that purpose.
The array of is provided corresponding to each area. Further, a mesh belt, a metal roller, a ceramic roller, an alumina roller or the like is used as a conveying means for the drying plate A'in the firing furnace 12 , but since the temperature rises up to about 1300 ° C especially in the firing area 14, For example, as shown in FIG. 5, an alumina roller 18 is placed between the metal main shafts 16 and 17 to convey the heat conduction so as not to transfer heat conduction to the drive source. Incidentally, the firing region 14 of the firing furnace 12 forms a furnace with refractory bricks, etc., and is to pass through it linearly and continuously,
An exhaust damper (not shown) is arranged between each device and area. The isocyanate used in the drying step and the product of the reaction with water are burned in the firing furnace 12 and do not remain on the long porcelain plate A ″ fed from the outlet 12b. 19 is a carrier. This is also for transporting the long porcelain plate A ″ coming out of the outlet 12b of the firing furnace 12 to a process such as packing.

次に動作について説明する。Next, the operation will be described.

まず、信楽木粘土とシャモットと減水剤と水分からなる
粘土1を準備する。なお、その重量%は信楽木粘土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3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。ポンプ7は5HPで中子5
の格子5aを通して乾燥風を供給すると共に、イソシアネ
ートの粉末を混入して供給する。乾燥機9としては波長
4μ〜400μの遠赤外線パネルヒータを10メートル間に1
0個配列し、成形帯Aの水分を対流による表面蒸発と、
排気管6、中子5から30℃位の温風排気による内部拡
散、およびイソシアネートの反応熱、吸水反応によって
水分を0〜2%位までに約10分間で減水して乾燥させる
ものである。次に乾燥された成形帯Aは走行カッタ10に
よって3mに切断され、乾燥板A′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A′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→徐冷して長尺陶板A″とし
て送出するものである。次に搬送機19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。
First, a clay 1 composed of Shigaraki clay, chamotte, a 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 Daiichi Kogyo Seiyaku Co., Ltd.), and water 18% were kneaded by a clay kneader (MP-100 type manufactured by Miyazaki Iron Works Co., Ltd.). Further, the extrusion molding machine 3 has a model name MV-FM-A-1 with an extrusion capacity of 100 to 150 l / hr.
A mold (manufactured by Miyazaki Tekko Co., Ltd.) was used. Pump 7 is 5 HP and core 5
The dry air is supplied through the grid 5a, and the isocyanate powder is mixed and supplied. As the dryer 9 , a far-infrared panel heater with a wavelength of 4μ to 400μ is used for every 10 meters.
0 pieces are arranged, and the water in the molding zone A is evaporated by the surface by convection,
The water content is reduced to about 0 to 2% in about 10 minutes by the internal diffusion of the hot air exhausted from the exhaust pipe 6 and the core 5 by hot air exhaust at about 30 ° C., and the reaction heat of isocyanate and the water absorption reaction, and dried. Next, the dried forming strip A is cut into 3 m by the traveling cutter 10 and becomes a drying plate A ', which is continuously fed to the firing furnace 12 by the transfer device 11. This firing furnace 12 is formed in a roller hearth kiln structure, and a drying plate A'is sequentially fed to and conveyed from the inlet 12a to the outlet 12b to the roller, and is preheated → fired → gradually cooled to obtain a long ceramic plate A. Then, it is conveyed to the next step such as a packing step, which is not shown, by the conveyor 19.

〔発明の効果〕〔The invention's effect〕

上述したように、本発明に係る長尺陶板の連続製造装置
によれば、長尺陶板を粘土の押し出し、迅速乾燥、焼
成、徐冷の順に直線状に配列した直線ラインによって行
なえるようにし、かつ高速生産で歩留りよく低コスト
で、しかも連続的に長尺陶板を製造できる特徴がある。
また、粘土の水分の低減には乾燥機による成形帯の外部
からの加温による乾燥(表面蒸発)と、中空部内のエア
等の流通による乾燥(内部拡散)、および中空部内での
イソシアネートによる吸水、発熱反応による相乗効果に
よって、成形帯の変形、クラックもなく低コストで、か
つ、短時間に水分をスムーズに低減でき、しかも高能率
で大量に製造できる特徴がある。しかも、中空部に供給
したイソシアネートが吸水、発熱反応を起こすため乾燥
機の加温を強く行っても、成形帯の内部、外部での乾燥
のバランスを容易に得ることができる。その上、陶板の
長さは任意長さに切断できる特徴がある。その他、製造
ラインは乾燥工程が従前の約1/160に短縮できるため設
置場所も生産量も大幅に改善された特徴がある。
As described above, according to the continuous production apparatus for a long porcelain plate according to the present invention, the long porcelain plate is extruded from clay, so that rapid drying, firing, and slow cooling can be performed by a linear line arranged linearly in this order, Moreover, it is characterized by high-speed production, high yield, low cost, and continuous production of long porcelain plates.
In order to reduce the water content of clay, drying by heating from the outside of the molding zone by a dryer (surface evaporation), drying by circulation of air in the hollow part (internal diffusion), and water absorption by isocyanate in the hollow part Due to the synergistic effect of the exothermic reaction, there is a feature that the molding band is not deformed or cracked at a low cost, the water content can be smoothly reduced in a short time, and the mass production can be performed with high efficiency. Moreover, since the isocyanate supplied to the hollow portion causes water absorption and an exothermic reaction, it is possible to easily obtain a balance of drying inside and outside the molding strip even when the dryer is heated strongly. In addition, the length of the porcelain plate has the feature that it can be cut to any length. In addition, the manufacturing line has the feature that the drying process can be shortened to about 1/160 of the previous one, and the installation place and the production amount have been greatly improved.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明に係る長尺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)〜(j)は連続成形
帯の一例を示す説明図、第3図(a)〜(d)は中子の
形状を示す説明図、第4図(a)、(b)は中子の装着
状態を示す説明図、第5図は焼成炉の一部を示す斜視図
である。 1……粘土、3……押出成形機、4……口金、5……中
子、7……ポンプ、9……乾燥機、10……走行カッタ、1
2……焼成炉、A……連続成形帯、A′……長尺の乾燥
板、A″……長尺陶板。
FIG. 1 is an explanatory view showing a typical example of a continuous production apparatus for a long porcelain plate according to the present invention, FIGS. 2 (a) to (j) are explanatory views showing an example of a continuous forming band, and FIG. 3 ( a) to (d) are explanatory views showing the shape of the core, FIGS. 4 (a) and 4 (b) are explanatory views showing the mounted state of the core, and FIG. 5 is a perspective view showing a part of the firing furnace. Is. 1 ... Clay, 3 ... Extruder, 4 ... Clasp, 5 ... Core, 7 ... Pump, 9 ... Dryer, 10 ... Traveling cutter, 1
2 ... Baking furnace, A ... Continuous forming strip, A '... Long dry plate, A ″ ... Long ceramic plate.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C04B 33/32 L 審査官 平塚 政宏 (56)参考文献 特開 昭58−114906(JP,A)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Internal reference number FI technical display location C04B 33/32 L Examiner Masahiro Hiratsuka (56) Reference JP-A-58-114906 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】粘土を主材とした原料を連続して押し出す
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水分を0〜2%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
切断された長尺の乾燥板を前記駆動用搬送機より速い速
度で焼成炉まで移送する移送機と、該移送機から送出さ
れる長尺の乾燥板を連続的に予熱−焼成−徐冷を行う焼
成炉と、該焼成炉の出口から次工程に送出する搬送機と
を直線状に配列し、また前記押出成形機の口金に、連続
成形帯の中央に中空部を形成するためのパイプ状の多数
の格子を有する中子を装着すると共に、該中子の入口、
または出口側にエア、熱風、冷風、乾燥風を排気する排
気管を設け、かつ、該エア、熱風、冷風、乾燥風と一緒
にイソシアネートの粉末を混入し、連続成形帯の中空部
に供給することを特徴とする長尺陶板の連続製造装置。
1. An extrusion molding machine for continuously extruding a raw material containing clay as a main material, a drive transportation machine for transporting a continuous molding strip fed from the extrusion molding machine in that state, and the transportation machine. And a continuous dryer which surrounds a part of or all of the above, and which dries the continuous molding belt to 0 to 2% while being conveyed in an extruded state, and a continuous molding belt dried by the dryer. A traveling cutter that cuts to a fixed length, a transfer device that transfers a long drying plate that is cut to a fixed size by the traveling cutter to a firing furnace at a speed faster than the drive transfer device, and is sent from the transfer device. A firing furnace for continuously preheating, firing, and gradually cooling a long dry plate, and a conveyer for delivering to the next step from the exit of the firing furnace are linearly arranged, and a die of the extruder is used. , With a large number of pipe-shaped lattices for forming hollows in the center of the continuous forming band Together with mounting the inlet of the tang,
Alternatively, an exhaust pipe for exhausting air, hot air, cold air, and dry air is provided on the outlet side, and isocyanate powder is mixed together with the air, hot air, cold air, and dry air and supplied to the hollow portion of the continuous molding zone. A continuous production device for long porcelain plates, which is characterized in that
JP11233086A 1986-05-15 1986-05-15 Continuous production equipment for long ceramic plates Expired - Fee Related JPH0729827B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11233086A JPH0729827B2 (en) 1986-05-15 1986-05-15 Continuous production equipment for long ceramic plates

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11233086A JPH0729827B2 (en) 1986-05-15 1986-05-15 Continuous production equipment for long ceramic plates

Publications (2)

Publication Number Publication Date
JPS62270454A JPS62270454A (en) 1987-11-24
JPH0729827B2 true JPH0729827B2 (en) 1995-04-05

Family

ID=14583978

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11233086A Expired - Fee Related JPH0729827B2 (en) 1986-05-15 1986-05-15 Continuous production equipment for long ceramic plates

Country Status (1)

Country Link
JP (1) JPH0729827B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107599151B (en) * 2017-10-23 2022-12-30 浙江新光阳照明股份有限公司 Production line for ceramic tubes

Also Published As

Publication number Publication date
JPS62270454A (en) 1987-11-24

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