JPH0729840B2 - Continuous production equipment for long ceramic plates - Google Patents
Continuous production equipment for long ceramic platesInfo
- Publication number
- JPH0729840B2 JPH0729840B2 JP62233784A JP23378487A JPH0729840B2 JP H0729840 B2 JPH0729840 B2 JP H0729840B2 JP 62233784 A JP62233784 A JP 62233784A JP 23378487 A JP23378487 A JP 23378487A JP H0729840 B2 JPH0729840 B2 JP H0729840B2
- Authority
- JP
- Japan
- Prior art keywords
- continuous
- raw material
- long
- raw materials
- 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
Links
- 239000000919 ceramic Substances 0.000 title claims description 11
- 238000010924 continuous production Methods 0.000 title claims description 7
- 239000002994 raw material Substances 0.000 claims description 55
- 239000000463 material Substances 0.000 claims description 32
- 238000010304 firing Methods 0.000 claims description 23
- 239000011248 coating agent Substances 0.000 claims description 17
- 238000000576 coating method Methods 0.000 claims description 17
- 239000004927 clay Substances 0.000 claims description 16
- 238000000465 moulding Methods 0.000 claims description 15
- 238000001035 drying Methods 0.000 claims description 12
- 238000001125 extrusion Methods 0.000 claims description 9
- 238000012546 transfer Methods 0.000 claims description 7
- 238000006116 polymerization reaction Methods 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 229910052573 porcelain Inorganic materials 0.000 description 11
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000003780 insertion Methods 0.000 description 3
- 230000037431 insertion Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 210000003298 dental enamel Anatomy 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010433 feldspar Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000003365 glass fiber Substances 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
- 238000004898 kneading Methods 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000002557 mineral fiber Substances 0.000 description 1
- 239000011490 mineral wool Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Press-Shaping Or Shaping Using Conveyers (AREA)
- Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (AREA)
- Laminated Bodies (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、粘土を主材とした原料を押出成形すると共
に、セラミックペーパーを原料間に層状に介在させた層
状成形帯を連続して押し出し、これを乾燥、切断、焼成
し、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 extrudes a raw material containing clay as a main material, and continuously extrudes a layered forming band in which ceramic paper is layered between the raw materials. The present invention relates to an apparatus for continuously producing long porcelain plates by drying, cutting and firing the same.
粘土、例えば木節粘土、蛙目粘土、信楽粘土を用いて
瓦、タイル等を製造するに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。また、タイル、瓦等
に意匠性を持たせるため、釉薬、フリットを施釉し、焼
成を行っていた。さらに、2台の押出機を用いて、2種
の粘土を層状に積層することも考えられている。しかし
ながら、この種装置は原料同士の重合は主原料の流れ方
向に対して、異種原料を垂直方向よりただ単に圧入した
だけのものであり、原料同士の結合が弱く、後工程の乾
燥、定尺切断、あるいは焼成時に、重合面においてフク
レ、ワレ、ヒビ等が発生し、歩留りが大幅に低下するも
のであった。また、粘土の乾燥時は、外部からの熱によ
り行われるため、粘土内部において不均質な乾燥状態と
なり、焼成時に、フクレ、ワレ、ヒビ等が発生する原因
ともなっていた。In order to manufacture roof tiles, tiles, etc. using clay, for example, Kibushi Clay, Frogme Clay, Shigaraki Clay, the continuous molding strip sent from the molding machine is cut into short pieces, and further shaped by press working, etc. It was manufactured by either drying and baking, or by filling a mold with the material, molding this by pressing, and then drying and baking. Further, in order to give tiles, roof tiles, etc. a design property, glaze and frits have been glazed and fired. Furthermore, it is also considered to laminate two kinds of clay in layers using two extruders. However, in this type of apparatus, polymerization of raw materials is performed by simply pressing different raw materials into the main material in the direction perpendicular to the flow direction of the main raw material. At the time of cutting or firing, blisters, cracks, cracks and the like were generated on the polymerized surface, and the yield was significantly reduced. Further, since the clay is dried by heat from the outside, it is in a non-uniform dry state inside the clay, which causes blisters, cracks, cracks and the like at the time of firing.
本発明は上述したような欠点を除去するため粘土を主材
とする原料を、複数台の押出機を同一口金に連結して原
料を同時に層状で押し出す押出成形機において、原料同
士が重合する直前に、セラミックペーパーからなる被覆
材を原料同士の重合面上に積層する被覆材供給部を形成
し、その後乾燥、切断、焼成を連続的に行うことによ
り、安価で、その上、原料同士の結合力を向上し、さら
に原料間に介在させたセラミックペーパーによる加熱時
の遠赤外線放射による内部加熱の促進により、原料間の
フクレ、ワレ、ヒビ等を排除した長尺陶板を連続して製
造し得る長尺陶板の連続製造装置を提案するものであ
る。The present invention, in order to eliminate the above-mentioned drawbacks, the raw material mainly composed of clay, in an extruder in which a plurality of extruders are connected to the same die and the raw materials are simultaneously extruded in layers, just before the raw materials are polymerized In addition, by forming a coating material supply part for laminating a coating material made of ceramic paper on the polymerized surface of the raw materials, and then continuously performing drying, cutting and firing, it is inexpensive and, moreover, the raw materials are bonded together. By improving the power and further promoting the internal heating by far-infrared radiation at the time of heating by the ceramic paper interposed between the raw materials, it is possible to continuously produce a long porcelain plate excluding blisters, cracks, cracks, etc. between the raw materials. It proposes a continuous production device for long ceramic plates.
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
は押出成形機であり、第2図(a)、(b)に示すよう
に複数台の押出機(図では2台)2、3を同一口金7に
連結し、押出機2、3間に被覆材供給部8を形成したも
のである。なお、押出機2、3は真空土練機、一軸、二
軸の成形機等である。さらに詳説すると、押出成形機1
は押出機2、3により粘土を主材とした原料(以下、単
に原料という)A、Bを同時に押し出し、さらに原料
A、B間に、被覆材供給部8よりセラミックペーパーか
らなる被覆材(以下、単に被覆材という)Cを連続的に
供給し、同一の口金7によって、例えば第4図(a)〜
(r)、第5図(a)〜(j)、および第6図(a)〜
(j)に示すような原料A、Bおよび被覆材Cの3層か
らなる所定断面形状の層状成形帯(以下、単に成形帯と
いう)Dを形成するものである。すなわち、原料Aは成
形帯Dの主体となる部分となり、原料Bは化粧面、ある
いは模様となるものであり、例えば陶石、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
粘土材料、もしくはこれらに石綿、岩綿等の鉱物繊維、
炭酸繊維、スチール繊維、有機繊維、ガラス繊維、木片
チップ、シャモット、ビーズ等の骨材を混入したもので
ある。なお、原料Aとして廉価なものを使用し、原料B
を水簸等した高級原料とすると、原料のコスト低減を図
ることができる。4は原料案内部であり、異種原料案内
部5と、主原料案内部6からなり、第3図(a)、
(b)((a)におけるイ−イ線断面図)に示すように
図示しないボルト等を介して一体に形成し、流路αを形
成するものである。さらに詳説すると、異種原料案内部
5は、後記する口金7の上口金7aとΔhの段差を形成す
ることにより、原料Bの積層厚さを設定すると共に原料
Bの流路βを形成し、さらに、原料A、B間に原料Aの
流れ方向に突出した楔状の案内片5aを設けることによ
り、被覆材Cへの原料Bの積層圧力を減少し流れをスム
ーズにするのに有効なものである。7は口金であり、上
口金7a、下口金7bをボルト等を介して固定し、成形帯D
の最終断面形状を決定する部分である。なお、上口金7a
は異種原料案内部5と組み合わさることにより、原料B
の案内面、および流路βの形成用としての機能も具備す
る。また8は被覆材供給部であり、押出機2より圧送さ
れている原料Aの原料Bとの重合面上に、連続的にアル
ミナやシリカを主成分とするセラミックペーパーからな
る被覆材Cを押出機2の挿入口2aより供給し、押出機2
の周方向より圧縮された被覆材Cは、原料Aと同速度で
送給されるものである。なお、被覆材供給部8と挿入口2
a間に、被覆材Cの供給をスムーズにするために、駆動
ローラ等よりなる被覆材送出部8aを設けることもでき
る。勿論、挿入口2aは原料Aが洩れ出さない構造とす
る。さらに、9は中子で、第5図(a)〜(j)に示す
ように、成形帯Dに中空孔aを形成する場合に設けるも
のであり、中子9は、固定用ボルト10により、中子固定
部11に固定されているものである。また、一点鎖線で示
すように管12によりエア供給機13と中子9とを連結し、
中空孔a内に温風、ドライエア等を供給、あるいは排気
することにより、成形帯Dの内部からの乾燥を助長する
こともできる。さらに第2図(a)、(b)の点線で示
した位置に邪魔棒14を設け、流路α、β内に自由に突出
することのできるように配設し、成形帯Dの原料A、B
の密度ムラを除去したりすることもできる。15は駆動用
搬送機でフリローラ、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Dのスピードと同じか、少
々速い速さに駆動をかけたものである。また、駆動用搬
送機15は、押出成形機1より少々速い駆動をかけると、
成形帯Dの捩じれ、反りを矯正する機能も果たすもので
ある。16は乾燥機で、駆動用搬送機15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19の廃熱などの一種
以上を熱源16aによって形成帯D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16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。17は
走行カッタで、乾燥された成形帯Dを定尺に回転刃、レ
ーザ、水圧、あるいは放電加工により切断し、定尺で長
尺の乾燥板E(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17は成形帯Dの速度に同調
して切断するものである。18は移送機で、走行カッタ17
で定尺に切断された乾燥板Eを駆動用搬送機15より速い
速度で焼成炉19まで搬送するものであり、成形帯Dと乾
燥板Eとの衝突を防止するものである。19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19aから出口19bに亘って山状の温度分布
となり、予熱領域20、焼成領域21、冷却領域22の順に一
応区分して構成し、予熱領域20の温度は150〜700℃、焼
成領域21は300〜1300℃、冷却領域22は600〜100℃まで
としたものである。勿論、原料A、Bの種類、組成、お
よび組み合わせ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19について説明すると、焼成炉19は可燃ガス、例
えばLPGガスを燃焼させて乾燥板E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
に対応して設けたものである。また、焼成炉19内の乾燥
板E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21の範囲は1300℃位まで温度が上昇するの
で、例えば第7図に示すように金属主軸23、24間にアル
ミナローラ25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19の焼成領
域21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、領域間に排気ダ
ンパー(図示せず)を配設しておくものである。26は搬
送機で、焼成炉19の出口19bから出てきた長尺陶板Fを
梱包などの工程に搬送するためのものである。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 1
Is an extruder, and as shown in FIGS. 2 (a) and 2 (b), a plurality of extruders (two in the figure) 2 and 3 are connected to the same base 7, and between the extruders 2 and 3. The coating material supply unit 8 is formed. The extruders 2 and 3 are vacuum kneaders, uniaxial or biaxial molding machines, and the like. More specifically, the extruder 1
Is the extruders 2 and 3 that simultaneously extrude clay-based raw materials (hereinafter simply referred to as raw materials) A and B, and between the raw materials A and B, a coating material made of ceramic paper from the coating material supply unit 8 (hereinafter (Referred to simply as a coating material) C is continuously supplied, and the same base 7 is used, for example, as shown in FIG.
(R), FIGS. 5 (a) to (j), and FIG. 6 (a) to
A layered molding strip (hereinafter simply referred to as a molding strip) D having a predetermined cross-sectional shape consisting of three layers of raw materials A and B and a coating material C as shown in (j) is formed. That is, the raw material A is a main part of the forming belt D, and the raw material B is a decorative surface or a pattern. For example, porcelain stone, feldspar, kaolinite, halosite, metahalosite, kibushi clay, frog. Clay material made by crushing eye clay, Shigaraki clay, etc. and kneading with water, or mineral fibers such as asbestos and rock wool,
Carbon fiber, steel fiber, organic fiber, glass fiber, wood chips, chamotte, beads and other aggregates are mixed. It should be noted that the raw material A is inexpensive and the raw material B is
By using a high-quality raw material such as elutriation, the cost of the raw material can be reduced. Reference numeral 4 denotes a raw material guide section, which comprises a different raw material guide section 5 and a main raw material guide section 6, and is shown in FIG.
As shown in (b) (cross-sectional view taken along the line EE in (a)), it is integrally formed through a bolt or the like (not shown) to form the flow path α. More specifically, the dissimilar raw material guide unit 5 forms a flow path β of the raw material B while setting the laminated thickness of the raw material B by forming a step difference of Δh with the upper die 7a of the die 7, which will be described later. By providing the wedge-shaped guide piece 5a protruding in the flow direction of the raw material A between the raw materials A and B, it is effective to reduce the stacking pressure of the raw material B on the coating material C and smooth the flow. . Reference numeral 7 denotes a die, which is formed by fixing the upper die 7a and the lower die 7b with bolts or the like,
Is a part that determines the final cross-sectional shape of. The upper base 7a
Is combined with the different raw material guide unit 5 to produce the raw material B.
It also has a function as a guide surface and for forming the flow path β. Reference numeral 8 denotes a coating material supply section, which continuously extrudes a coating material C made of ceramic paper containing alumina or silica as a main component on the polymerization surface of the raw material A pumped from the extruder 2 with the raw material B. The extruder 2 is supplied from the insertion port 2a of the machine 2.
The coating material C compressed in the circumferential direction is fed at the same speed as the raw material A. In addition, the coating material supply unit 8 and the insertion port 2
In order to make the supply of the covering material C smooth between a and a, it is possible to provide a covering material feeding portion 8a composed of a driving roller or the like. Of course, the insertion port 2a has a structure in which the raw material A does not leak out. Further, 9 is a core, which is provided when forming a hollow hole a in the molding strip D as shown in FIGS. 5 (a) to 5 (j). The core 9 is fixed by a fixing bolt 10. It is fixed to the core fixing portion 11. In addition, as shown by the alternate long and short dash line, the air supply device 13 and the core 9 are connected by a pipe 12,
By supplying hot air, dry air, or the like into the hollow holes a or exhausting the air, it is possible to promote drying from the inside of the molding strip D. Further, a baffle bar 14 is provided at a position shown by a dotted line in FIGS. 2A and 2B, and the baffle bar 14 is arranged so as to freely project into the flow paths α and β. , B
It is also possible to remove the uneven density. The reference numeral 15 denotes a driving conveyer, which is composed of at least one kind of a flea roller, a driving roller, a belt, a mesh belt, etc., and has a speed equal to or slightly faster than the speed of the molding strip D extruded from the extrusion molding machine 1. It was driven by. Further, when the driving carrier 15 is driven a little faster than the extruder 1 ,
It also has a function of correcting twisting and warping of the forming belt D. Reference numeral 16 denotes a dryer, which encloses a part of the driving carrier 15 or all (not shown), and one or more of infrared heaters, far-infrared heaters, microwaves, waste heat of a firing furnace 19 described later, etc. are provided by a heat source 16a. For example, the water content of the formation zone D is 18 to 20
% For reducing the content to 0 to 2% to enhance the shape retention and to make it a calcinable property. In addition, the dryer 16 is provided with an infrared heater, only microwaves, or alternately or divided into front and rear zones, and the atmosphere is heated to about 200 to 500 ° C. so that the dough does not crack or deform. It heats according to the curve. Reference numeral 17 denotes a traveling cutter, which cuts the dried forming belt D into a regular length by a rotary blade, laser, water pressure, or electric discharge machining to form a long and constant length drying plate E (hereinafter, simply referred to as a drying plate). Is. Of course, the traveling cutter 17 cuts in synchronization with the speed of the forming belt D. 18 is a transfer machine, a traveling cutter 17
The drying plate E, which is cut to a fixed length by the above method, is conveyed to the firing furnace 19 at a speed higher than that of the driving conveyer 15, and the collision between the molding strip D and the drying plate E is prevented. 19 is a firing furnace, which consists of a roller hearth kiln and a tunnel type firing furnace.
The structure has a mountain-shaped temperature distribution from the inlet 19a to the outlet 19b, and is configured by temporarily dividing the preheating region 20, the firing region 21, and the cooling region 22, and the temperature of the preheating region 20 is 150 to 700 ° C. The area 21 is 300 to 1300 ° C, and the cooling area 22 is 600 to 100 ° C. Of course, the temperature setting between the regions differs depending on the type, composition, and combination of the raw materials A and B, and the temperature between the regions is not clearly divided, and it is tentative during the continuous firing. It is a division. Further the sintering furnace 19 will be described, the firing furnace 19 is intended to firing the dried plate E by burning combustible gas, for example LPG gas, the arrangement of the burner (not shown) therefor in correspondence with the respective areas It is provided. Further, as a conveying means of the dry plate E in the baking furnace 19 , a mesh belt, a metal roller,
A ceramic roller, an alumina roller, or the like is used. Especially, since the temperature of the firing region 21 rises to about 1300 ° C., an alumina roller 25 is placed between the metal spindles 23 and 24, as shown in FIG. 7, for example. Then, the heat transfer is carried so as not to transfer the heat conduction to the drive source. The firing area 21 of the firing furnace 19 is formed by refractory bricks or the like, and the furnace is made to pass through it linearly and continuously, and an exhaust damper (not shown) is provided between each equipment and area. It is something to keep. The reference numeral 26 denotes a carrier for carrying the long porcelain plate F coming out of the outlet 19b of the firing furnace 19 to a process such as packing.
以上説明したのは本発明に係る長尺陶板の連続製造装置
の一実施例にすぎず、第8図〜第10図(a)〜(c)に
示すように形成することもできる。すなわち第8図は押
出機2と原料案内部4間の中子固定部11の形状を、固定
用ボルト10、管12の位置において、流路αの断面積が入
口部11a、出口部11bよりも大きくなるように形成し、固
定用ボルト10、管12による抵抗により圧力が上昇するの
を防止した押出成形機1である。また第9図は、押出機
3を複数台(図では2台)、被覆材供給部8を複数台
(図では2台)を形成することにより、原料A、B、G
間に被覆材Cを介在させるようにした押出成形機1であ
る。さらに第10図(a)〜(c)は被覆材Cおよび、成
形帯Dの断面の変形例であり、(a)図に示すように、
被覆材Cに四角形、あるいは図示しないが、三角形、台
形、円形、蟻溝状の凹凸部C1を表面側、裏面側、あるい
は両方に形成することにより、(b)、(c)図に示す
ように成形帯Dを押し出し、凹凸部C1によりアンカー効
果を発揮させると共に、意匠性を向上したものである。
また第1図で点線で示した位置に施釉機27を設け、ホー
ロー仕上げを施すこともできる。The above description is merely one example of the continuous porcelain plate continuous production apparatus according to the present invention, and the continuous porcelain plate can be formed as shown in FIGS. 8 to 10 (a) to (c). That is, FIG. 8 shows the shape of the core fixing portion 11 between the extruder 2 and the raw material guide portion 4 , in which the cross-sectional area of the flow path α is at the positions of the fixing bolt 10 and the pipe 12 from the inlet portion 11a and the outlet portion 11b. The extrusion molding machine 1 is formed so as to be large, and prevents the pressure from rising due to resistance by the fixing bolt 10 and the pipe 12. Further, FIG. 9 shows that the raw materials A, B and G are formed by forming a plurality of extruders 3 (two in the figure) and a plurality of coating material supply units 8 (two in the figure).
The extruder 1 has a covering material C interposed therebetween. Further, FIGS. 10 (a) to 10 (c) are modified examples of the cross section of the covering material C and the molding strip D, and as shown in FIG.
By forming a quadrangle, or a triangular, trapezoidal, circular, or dovetail-shaped uneven portion C 1 on the covering C on the front surface side, the back surface side, or both, as shown in FIGS. As described above, the molding band D is extruded, the anchor effect is exerted by the uneven portion C 1 , and the designability is improved.
Further, a glazing machine 27 may be provided at a position shown by a dotted line in FIG. 1 to perform enamel finish.
以上説明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、複数の素材の粘土を用途に応じて一体に
形成できるため、原料のコストダウンと、意匠性の向上
が図れる。原料間に被覆材が存在するため、主材とな
る原料が別の押出機方向に流れ込むことがない。原料
間にセラミックペーパーよりなる被覆材を介在させたた
め、焼成時にクッション材となり原料間のハクリ、フク
レ、ワレ、変形を防止し、さらに被覆材より発せられる
加熱時の遠赤外線の放射により、均質焼成が可能とな
り、その上、原料同士の一体化が確実となる。押出成
形機内の原料同士が重合する面に、流れ方向に沿った案
内片を突出させた異種原料案内部を形成したため、主材
となる原料上に異種原料を垂直方向より蓄層しても、流
れがスムーズとなり、押出圧力、押出スピードのコント
ロールが簡素化される。押出成形−乾燥−切断−焼成
を連続的に行うことができ、低コストで、意匠性があ
り、しかも連続的に長尺陶板を製造できる。陶板の長
さは任意長さに切断でき、さらに乾燥後に切断するため
に、切り口を美しく切断できる。大量生産が可能とな
り、歩留りが従前に比し大幅に向上する。等の特徴、効
果がある。As described above, according to the continuous production apparatus for a long porcelain plate according to the present invention, it is possible to integrally form clay of a plurality of raw materials according to the use, so that the cost of raw materials can be reduced and the designability can be improved. Since the coating material exists between the raw materials, the raw material as the main material does not flow into another extruder. Since a covering material made of ceramic paper is interposed between the raw materials, it becomes a cushioning material during firing, preventing peeling, blistering, cracking, and deformation between the raw materials, and further radiating far-infrared rays from the covering material during heating to achieve homogeneous firing. In addition, the raw materials are surely integrated with each other. On the surface where the raw materials in the extruder are polymerized, a different raw material guide part is formed by projecting a guide piece along the flow direction, so even if different raw materials are accumulated in the vertical direction on the raw material that is the main material, The flow becomes smooth and the control of extrusion pressure and extrusion speed is simplified. Extrusion molding-drying-cutting-firing can be carried out continuously, and at low cost, there is design, and a long porcelain plate can be continuously manufactured. The length of the porcelain plate can be cut to any length, and since it is cut after drying, the cut end can be cut beautifully. Mass production is possible, and the yield is greatly improved compared to before. There are characteristics and effects.
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)、(b)は押出成形
機を説明する説明図、第3図(a)、(b)は原料案内
部を説明する説明図、第4図(a)〜(r)、第5図
(a)〜(j)、および第6図(a)〜(j)は層状成
形帯の例を示す説明図、第7図は焼成炉の一部を示す斜
視図、第8図、第9図、第10図(a)、(c)その他の
実施例を説明する説明図である。1 ……押出成形機、2、3……押出機、4……原料案内
部、5……異種粘土案内部、7……口金、8……被覆材
供給部、16……乾燥機、17……走行カッタ、19……焼成
炉。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) and 2 (b) are explanatory views explaining an extruder, and FIG. 3 (a). ) And (b) are explanatory views for explaining the raw material guide part, FIGS. 4 (a) to (r), 5 (a) to (j), and 6 (a) to (j) are layered. Explanatory drawing showing an example of a forming band, FIG. 7 is a perspective view showing a part of a firing furnace, FIG. 8, FIG. 9, FIG. 10 (a), (c) Explanatory drawing for explaining other embodiments Is. 1 …… Extrusion molding machine 2, 3 …… Extrusion machine, 4 …… Raw material guide section, 5 …… Different clay guide section, 7 …… Mouthpiece, 8 …… Coating material supply section, 16 …… Dryer, 17 …… Traveling cutter, 19 …… Baking furnace.
───────────────────────────────────────────────────── 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 33/30 L 33/32 L ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical indication C04B 33/30 L 33/32 L
Claims (1)
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
を配列し、また前記押出成形機は複数台の押出機を同一
口金に連結して原料を同時に層状で押し出し、原料同士
が重合する直前に、セラミックペーパーからなる被覆材
を原料同士の重合面上に積層する被覆材供給部を形成し
た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 that continuously preheats, fires, and gradually cools a long dry plate, and a conveyer that sends the long drying plate to the next step from the outlet of the firing furnace are arranged, and the extruder is a plurality of extruders. Immediately before the raw materials are polymerized by connecting the Continuous production apparatus for a long ceramic plate to a coating material consisting of ceramic paper, characterized in that the formation of the coating material supply unit to be stacked on the polymerization surface of the material with each other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62233784A JPH0729840B2 (en) | 1987-09-17 | 1987-09-17 | Continuous production equipment for long ceramic plates |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62233784A JPH0729840B2 (en) | 1987-09-17 | 1987-09-17 | Continuous production equipment for long ceramic plates |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6476938A JPS6476938A (en) | 1989-03-23 |
| JPH0729840B2 true JPH0729840B2 (en) | 1995-04-05 |
Family
ID=16960514
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62233784A Expired - Fee Related JPH0729840B2 (en) | 1987-09-17 | 1987-09-17 | Continuous production equipment for long ceramic plates |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0729840B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111168825B (en) * | 2020-03-05 | 2021-07-09 | 杭州诺贝尔陶瓷有限公司 | Full-digital decorative ceramic polished tile and production method thereof |
-
1987
- 1987-09-17 JP JP62233784A patent/JPH0729840B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6476938A (en) | 1989-03-23 |
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