JPH0729843B2 - Rapid drying equipment for clay compacts - Google Patents
Rapid drying equipment for clay compactsInfo
- Publication number
- JPH0729843B2 JPH0729843B2 JP21675786A JP21675786A JPH0729843B2 JP H0729843 B2 JPH0729843 B2 JP H0729843B2 JP 21675786 A JP21675786 A JP 21675786A JP 21675786 A JP21675786 A JP 21675786A JP H0729843 B2 JPH0729843 B2 JP H0729843B2
- Authority
- JP
- Japan
- Prior art keywords
- clay
- microwave
- extrusion
- molded body
- extruded product
- 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
- 239000004927 clay Substances 0.000 title claims description 28
- 238000001035 drying Methods 0.000 title claims description 22
- 238000001125 extrusion Methods 0.000 claims description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- 235000012438 extruded product Nutrition 0.000 claims description 18
- 239000002994 raw material Substances 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 description 15
- 239000000463 material Substances 0.000 description 4
- 238000010304 firing Methods 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000010433 feldspar Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009413 insulation 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
- 229930014626 natural product Natural products 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 230000007723 transport mechanism Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- 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所定形状で連続して
押し出された押出成形体を10分〜1時間位の短時間で乾
燥し、それを定尺に走行中に切断しうる粘土成形体の迅
速乾燥装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is to dry an extruded product obtained by continuously extruding a raw material mainly containing clay in a predetermined shape in a short time of about 10 minutes to 1 hour. The present invention relates to a rapid drying device for a clay molded body, which can be cut during running to a fixed length.
一般に、粘土を用いた内、外装材、瓦は所定形状で押出
成形され、これを直ちに短尺、例えば10〜30cmの長さに
切断し、これを焼成炉の廃熱を利用する構造の乾燥装置
では約1〜3日間位で水分を1〜0%まで低減し、焼成
炉に供給する構成の装置が普通であった。Generally, clay, inner and outer materials, roof tiles are extruded in a predetermined shape, immediately cut into a short length, for example, 10 to 30 cm in length, and a drying device having a structure that utilizes the waste heat of the firing furnace. In general, an apparatus having a structure in which the water content is reduced to 1 to 0% in about 1 to 3 days and then supplied to the firing furnace is common.
従来の粘土成形体の乾燥装置は乾燥に数日を要するばか
りでなく、特に従前より長めの粘土成形体は下敷板を用
いないと運搬搬することができず、生産性に劣り、かつ
コストアップを招くと共に、広大な敷地を必要とした。
さらに、従前の表面から熱を付加して乾燥する乾燥装置
では乾燥時間を1日短縮すると、表面層が最初に乾燥し
内部が未乾燥のため、内部の水蒸気によって瓦、タイ
ル、外壁材に捩じれ、クラック、反り、破壊が生じ、乾
燥時間の短縮は非常に困難であった。また、表面からの
加熱による乾燥に代わって内部加熱による装置、例えば
マイクロ波加熱機、遠赤外線ヒータによる乾燥も知られ
ている。しかしながら前者のマイクロ波加熱機は粘土の
水分を短時間に低減できるが被乾燥物を130℃位までに
昇温するのに大量のエネルギーを要し、経済性と大量の
エネルギーによる悪影響から水分を1%以下に乾燥させ
ることが困難であった。また、遠赤外線ヒータ単体では
乾燥時間がマイクロ波より長時間を要し、かつ、加熱ゾ
ーンもマイクロ波に比し長い反面、被加熱物を130℃に
昇温できるものであった。従って、両加熱装置にはいず
れも一長一短があり、実用化に欠ける不利があった。さ
らに、マイクロ波で加熱した際はエネルギーコストが高
く、大量の水蒸気が加熱ゾーンに充満し、被加熱物表
面、加熱ゾーン内壁への結露、乾燥時間の遅延等の不都
合があった。しかも、マイクロ波加熱機の加熱ゾーンは
駆動ベルトによって被加熱物を搬送する構造のため、柔
らかい被加熱物が搬送中に約10%位収縮する寸法差を吸
収できず被加熱物をベルトコンベア間の摩擦抵抗によっ
て被加熱物が変形したり、反ったり、クラックが入った
り、破断したりする欠点があった。さらに、従来は押出
成形機から走行カッタまでを一貫して行う工程は不可能
であった。Not only does the conventional dryer for clay moldings take several days to dry, but especially clay moldings that are longer than before cannot be transported without the use of an underlay plate, resulting in poor productivity and increased costs. And required a vast site.
Furthermore, if the drying time is shortened by one day in the drying device that heats and dries from the conventional surface, the surface layer will be dried first and the inside will not be dried, so it will be twisted into the roof tile, tile, and outer wall material by the steam inside. , Cracks, warpage, and breakage occurred, and it was very difficult to shorten the drying time. Further, instead of drying by heating from the surface, a device by internal heating, for example, a microwave heater or a far infrared heater is also known. However, the former microwave heater can reduce the moisture content of clay in a short time, but it requires a large amount of energy to heat the material to be dried up to around 130 ° C, which is economical and economically harmful. It was difficult to dry to less than 1%. Further, the far infrared heater alone required a longer drying time than the microwave and the heating zone was longer than that of the microwave, but the object to be heated could be heated to 130 ° C. Therefore, both heating devices have merits and demerits, and there is a disadvantage that they are not put into practical use. Further, when heated by microwaves, the energy cost is high, and a large amount of water vapor fills the heating zone, which causes inconveniences such as dew condensation on the surface of the object to be heated, the inner wall of the heating zone, and delay in drying time. In addition, the heating zone of the microwave heater has a structure that conveys the object to be heated by the drive belt, so the soft object to be heated contracts about 10% during conveyance, and the difference in size cannot be absorbed so that the object to be heated is transferred between the belt conveyors. However, there is a defect that the object to be heated is deformed, warped, cracked, or broken due to the frictional resistance. Further, conventionally, it was impossible to consistently carry out the steps from the extruder to the traveling cutter.
本発明はこのような欠点を除去するため、押出成形機の
押出口の次にこれをスムーズに次工程に送給する移送機
を介してマイクロ波加熱機、遠赤外線ヒータ装置の順に
送給し、連続した状態で押出成形体を乾燥させ、これを
走行カッタで所定長さに切断するように構成し、乾燥時
に押出成形体が変形、反り、捩じれ、クラックの発生も
なく、しかも押出成形体の10%位の体積収縮をも吸収し
て搬送できると共に、乾燥を10〜60分間位で達成できる
ようにした粘土成形体の迅速乾燥装置を提案するもので
ある。In order to eliminate such defects, the present invention sequentially feeds a microwave heater and a far-infrared heater device through a transfer device that smoothly feeds the extrusion port of the extruder next to the next step. , The extrusion molded body is dried in a continuous state, and is cut to a predetermined length by a traveling cutter, the extrusion molded body does not deform, warp, twist, or crack during drying, and the extrusion molded body The present invention proposes a rapid drying apparatus for a clay molded body, which can absorb and transport the volume shrinkage of about 10% and can be dried in about 10 to 60 minutes.
以下に、図面を用いて本発明に係る粘土成形体の迅速乾
燥装置の一実施例について詳細に説明する。第1図
(a)、(b)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は押出成形機で粘土を主材とす
る原料を例えば第2図(a)〜(j)に示す断面形状の
押出成形体Aを連続して押し出すものであり、例えば押
出速度は押出成形体Aの厚さ、幅によって異なるが100
〜2000mm/min位である。なお、粘土は天然物であり、各
産地により成分が異なるものであり、これらの長所、短
所を相互に相殺させて所定の混合粘土を得るものであ
る。その具体例としては陶石、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
楽粘土、シャモットなどを打ち砕き、水を加えて練り上
げるものである。また、この粘土には必要によりマグネ
ットで除鉄するものである。2は移送機で例えばフリロ
ーラ、あるいは図示しないが押出速度に同調した駆動ベ
ルト等の少なくとも1種以上からなるものであり、押出
成形体Aを押出速度のままで次工程に変形なくスムーズ
に送給するためのものである。特に、フリローラ3は押
出成形体Aを静摩擦抵抗なしに押し出された状態で移送
するのに役立ち、駆動ベルトコンベア4は出口から0.5
〜2m位離れた位置で押出された時より幾分硬く、かつ押
出時の力が先に押し出された押出時の重さに抵抗しきれ
ず圧縮され、縮むのを防止するために押出時とほぼ同じ
速度で押出成形体Aを連続して次工程に移送するもので
ある。5はマイクロ波加熱機でオーブン連続方式構造と
し、主に押出成形体Aの内部へ浸透して熱伝導にほとん
ど時間を要することなくマイクロ波Bを熱エネルギーに
変換し、数秒から数分までに発熱して粘土内の水分を例
えば5〜10%(重量%)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
%位含有されており、そのうちの5〜10%を蒸発せしめ
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である。そこで、マイ
クロ波加熱機5を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Bを所要個所に
案内する導波管6と、案内されたマイクロ波Bを反射す
る反射板7と、反射されたマイクロ波Bを撹拌する回転
羽根8と、押出成形体Aを押出速度で移動させると共
に、マイクロ波Bが押出成形体Aの裏面からも照射され
るようにしたフリローラ9からなる搬送部10と、押出成
形体Aの入口、出口となると共に、マイクロ波Bが外部
へ漏洩しないように減衰させるフィルター部11、12とエ
ア等Cを被加熱空間13に案内するエア供給口14と、マイ
クロ波Bが被加熱空間13から外部へ漏洩しないように囲
んだ包囲体15とから構成したものである。また、押出成
形体Aの被加熱空間13の大きさ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
10は押出成形体Aが乾燥中に約1割程度体積収縮するた
め、これを無理なくフリローラ9で吸収するものであ
る。また、エア供給口14はマイクロ波Bの加熱により水
蒸気が大量に、短時間の間に放出するのを入口、出口11
a、12aから外部へ放出し、押出成形体Aの表面、包囲体
15の内壁に結露が発生しないようにして乾燥時の悪影響
(クラック、爆裂)を防止し、かつ押出成形体A表面の
水蒸気を風によって常時、吹きとばし、より乾燥時間を
短縮するのに役立つものである。16は赤外線、特に遠赤
外線を熱源とする遠赤外線ヒータ装置で押出成形体Aの
水分を1〜0%まで低減するために押出成形体Aを130
℃以上まで上昇させるものである。その構成はフリロー
ラ、駆動ベルトからなる搬送機構17と遠赤外線ヒータ18
と保温箱19とからなり、加熱ゾーンは約2〜5m位であ
る。勿論、加熱ゾーンは半乾燥体となった押出成形体A
の厚さ、幅、大きさ、搬送速度によって異なるものであ
る。20は走行カッタで乾燥された連続体状の押出成形体
Aを所定寸法に走行中に切断するものであり、丸ノコ状
の回転刃、あるいは図示しないがレーザ、加圧水等を利
用して切断するものである。Hereinafter, an embodiment of a rapid drying apparatus for a clay molded body according to the present invention will be described in detail with reference to the drawings. 1 (a) and 1 (b) are explanatory views showing a typical example of the above apparatus. In the figure, reference numeral 1 denotes an extruder for continuously extruding a raw material containing clay as a main material, for example, an extruded body A having a cross-sectional shape shown in FIGS. 2 (a) to (j). 100 depending on the thickness and width of extruded product A
It is about 2000 mm / min. It should be noted that clay is a natural product and has different components depending on each producing area, and these advantages and disadvantages are mutually offset to obtain a predetermined mixed clay. Specific examples are pottery stone, feldspar, kaolinite,
This is to crush halosite, metahalosite, kibushi clay, frog eye clay, Shigaraki clay, chamotte, etc. and add water to knead. If necessary, the clay will be ironed with a magnet. Reference numeral 2 denotes a transfer device, which is composed of, for example, a flea roller, or at least one driving belt (not shown) which is synchronized with the extrusion speed, and smoothly feeds the extrusion-molded body A to the next step without changing the extrusion speed. It is for doing. In particular, the fli roller 3 is useful for transporting the extruded product A in the extruded state without static friction resistance, and the drive belt conveyor 4 is 0.5 out of the outlet.
It is somewhat harder than when it is extruded at a position about 2 m away, and the force at the time of extrusion is almost the same as that at the time of extrusion in order to prevent it from being compressed because it cannot resist the weight of the extruded extrusion that was extruded first. The extrusion molded body A is continuously transferred to the next step at the same speed. Numeral 5 is a microwave heater having a continuous oven structure, which mainly permeates the inside of the extruded body A and converts the microwave B into heat energy with almost no time required for heat conduction, and within a few seconds to a few minutes. This is for generating heat to evaporate the water content in the clay, for example, 5 to 10% (% by weight). In addition, the water content in the extrusion-molded product A is 22 to 15 by weight.
It is contained in about%, and 5 to 10% of it is evaporated. In particular, this type of extruded product A has a water content of 5 to 5.
The volume shrinks until it reaches about 8%, but when the water content is less than that, the volume does not shrink. Therefore, the microwave heater 5 will be specifically described. A waveguide 6 that guides the microwave B oscillated from a microwave oscillator (not shown) to a required location, and a reflection plate 7 that reflects the guided microwave B. A rotary blade 8 that stirs the reflected microwave B, and a flir roller 9 that moves the extruded product A at the extruding speed and irradiates the microwave B from the back surface of the extruded product A. The conveying section 10 , the inlets and outlets of the extruded body A, and the filter sections 11 and 12 that attenuate the microwave B so as not to leak to the outside and the air supply port 14 that guides the air C and the like to the heated space 13. And a surrounding body 15 that surrounds the microwave B so as not to leak from the heated space 13 to the outside. The size of the heated space 13 of the extruded body A varies depending on the purpose, but is, for example, about 1 to 5 m. Furthermore, the transport section
Since the volume of the extruded product A shrinks by about 10% during drying, the extruded product A is absorbed by the flea roller 9 without difficulty. In addition, the air supply port 14 is designed to release a large amount of water vapor by heating the microwave B in a short time.
Release from a, 12a to the outside, surface of extruded product A, enclosure
Prevents dew condensation on the inner wall of 15 to prevent adverse effects (cracks, explosions) during drying, and constantly blows off the steam on the surface of the extruded product A by wind to help reduce the drying time. Is. Reference numeral 16 denotes a far-infrared heater device using infrared rays, particularly far-infrared rays as a heat source, and the extrusion molded body A is 130% in order to reduce the water content of the extrusion molded body A to 1 to 0%.
It is intended to raise the temperature above ℃. Its structure is a transport mechanism 17 consisting of a fli roller and a drive belt and a far infrared heater 18.
And the heat insulation box 19, and the heating zone is about 2 to 5 m. Of course, the heating zone is a semi-dried extruded product A
The thickness depends on the thickness, width, size, and transport speed. Reference numeral 20 is for cutting a continuous extruded product A dried by a traveling cutter during traveling to a predetermined size, and is cut by using a circular saw blade or a laser (not shown), pressurized water or the like. It is a thing.
次に動作について説明する。Next, the operation will be described.
まず、信楽粘土とシャモットと減水剤と水からなる粘土
を原料として準備する。なお、その重量%は例えば信楽
粘土61.5%、シャモット18%、減水剤0.5%(商品名:
セルフロー、第一工業製薬社製)、水20%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としては押し出し能力100〜150/hrの型
名MV−FM−A−1型(宮崎鉄工社製)を用いた。また、
移送機2としてはフリローラ3、駆動ベルトコンベア4
の順に配列したもの、マイクロ波加熱機5としては周波
数2450MHz、出力5kw、被加熱空間13の長さは3mとし、必
要によりエアを被加熱空間13に大量に包囲体15の一壁面
から送給され、入、出口11a、12aから加熱時に発生する
水蒸気C′を外部へ放出し、被加熱空間13内の水蒸気圧
を低下し、被加熱物、包囲体15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10はテ
フロン製パイプからなるフリローラ9とした。また、遠
赤外線ヒータ装置16は遠赤外線ヒータ18を複数個、約3
〜10mのゾーン内に配列したものであり、その出力は例
えば20kwとした。なお、マイクロ波加熱機5では押出成
形体Aの水分18%(重量%)を5%(重量%)まで蒸発
させ、残りの水分を遠赤外線ヒータ装置16で蒸発させる
ように設定した。さらに押出成形機1の押出速度は300
〜1000mm/minであり、ここでは400mm/minとした。その
他、押出成形体A(ここでは連続成形体状である)のパ
スラインは同一高さとし、押出成形体Aは押出成形機1
の押出速度をそのまま駆動ベルトでマイクロ波加熱機5
に送給され、マイクロ波加熱機5内の搬送部10のフリロ
ーラ9で水分蒸発に生ずる体積収縮による速度の差を吸
収するようにしたものである。そこで、押出成形機1に
供給された粘土はその出口から第2図(g)に示す断面
の連続体で送出される。送出された押出成形体Aは移送
機2を介してマイクロ波加熱機5に送給され、マイクロ
波加熱機5の被加熱空間13を通過中に押出成形体Aの水
分を5%(重量比)まで5分間で低減し、その出口から
遠赤外線ヒータ装置16へ送給し、遠赤外線ヒータ装置16
では水分を1%(重量比)に約10分間で蒸発させ乾燥さ
せた。その結果、、押出成形機1の出口から遠赤外線ヒ
ータ装置16までを連続帯とした押出成形体Aを約15〜20
分で乾燥体として走行カッタ20に送給し所定寸法に切断
した。勿論、図示しないがその後は続いて施釉、もしく
は焼成工程に連続して送給することも可能である。First, a clay consisting of Shigaraki clay, chamotte, a water reducing agent and water is prepared as a raw material. The weight% is, for example, Shigaraki clay 61.5%, chamotte 18%, water reducing agent 0.5% (trade name:
Cell Flow, manufactured by Dai-ichi Kogyo Seiyaku Co., Ltd., water 20% clay mixer (MP
-100 type manufactured by Miyazaki Tekko Co., Ltd.). Also,
As the extrusion molding machine 1, a model name MV-FM-A-1 type (manufactured by Miyazaki Tekko Co., Ltd.) having an extrusion capacity of 100 to 150 / hr was used. Also,
The transfer device 2 includes a fli roller 3, a drive belt conveyor 4
The microwave heater 5 has a frequency of 2450 MHz, an output of 5 kw, and the length of the heated space 13 is 3 m. If necessary, a large amount of air is supplied to the heated space 13 from one wall surface of the enclosure 15. The steam C'generated during heating is discharged to the outside through the inlets / outlets 11a, 12a, the steam pressure in the heated space 13 is reduced, and condensed water is generated on the heated object and the inner wall of the enclosure 15. The transport section 10 is the fli roller 9 made of a Teflon pipe. In addition, the far infrared heater device 16 includes a plurality of far infrared heaters 18, approximately 3
They are arranged in a zone of ~ 10 m, and the output is set to 20 kw, for example. In the microwave heater 5 , the moisture content of the extruded product A was set to 18% (wt%) to 5% (wt%) and the remaining moisture was vaporized by the far infrared heater device 16 . Furthermore, the extrusion speed of the extruder 1 is 300.
~ 1000 mm / min, and here 400 mm / min. In addition, the pass lines of the extrusion-molded body A (here, a continuous-molded body) have the same height, and the extrusion-molded body A is the extruder 1.
The microwave heating machine 5 is driven by the driving belt at the same extrusion speed.
And is adapted to absorb a difference in speed due to volume contraction caused by evaporation of water at the fli roller 9 of the conveying section 10 in the microwave heater 5 . Therefore, the clay supplied to the extruder 1 is delivered from its outlet in a continuous body having a cross section shown in FIG. 2 (g). The extruded product A sent out is sent to the microwave heating device 5 via the transfer device 2, and while passing through the heated space 13 of the microwave heating device 5 , the water content of the extruded product A is 5% (weight ratio). ) Is reduced in 5 minutes, and the far infrared heater device 16 is fed from the outlet to the far infrared heater device 16.
Then, the water content was evaporated to 1% (weight ratio) in about 10 minutes and dried. As a result, about 15 to 20 extruded bodies A having a continuous band from the outlet of the extruder 1 to the far infrared heater device 16 are obtained.
In minutes, it was fed as a dried body to the traveling cutter 20 and cut into a predetermined size. Of course, although not shown, it is also possible to subsequently feed the glazing or the firing process continuously.
以上説明したのは本発明に係る粘土成形体の迅速乾燥装
置の一実施例にすぎず、第1図(a)において一点鎖線
で示す位置にエア、温風、ドライエア、熱風を併用して
供給し、押出成形体Aのより一層の乾燥促進を図ること
もできる。またエア供給口14は被加熱空間13内の気体を
図示しないポンプにより吸引することも同様に可能であ
る。The above description is merely one example of the rapid drying apparatus for a clay molded body according to the present invention, in which air, warm air, dry air, and hot air are used in combination at the position shown by the alternate long and short dash line in FIG. 1 (a). However, it is possible to further promote the drying of the extrusion molded body A. Further, the air supply port 14 can also suck the gas in the heated space 13 by a pump (not shown).
上述したように本発明に係る粘土成形体の迅速乾燥装置
によれば、水分を22〜15%位(重量比)含有した粘土押
出成形体(短尺、長尺、連続体)の水分の1/3位を押出
成形体の内部を含み平均に蒸発させて歪なく乾燥させる
マイクロ波加熱機と、残り2/3の含水分をマイクロ波よ
り高熱に効率よくできる遠赤外線ヒータ装置の2段階の
加熱によってクラック、爆裂、捩じれ、反りもなく、し
かも従前の1/100〜300に乾燥時間を短縮できる特徴があ
る。また、押出成形体の体積は押出時に比べ乾燥体は1
割以上収縮することがそれによる搬送速度への影響をフ
リローラによって吸収し次工程に移送できる特徴があ
る。さらに、本発明では押出から乾燥までを直線状に配
列したため、長尺体等をスムーズに乾燥できる特徴があ
る。As described above, according to the rapid drying apparatus for a clay molded body according to the present invention, 1/100% of the water content of the clay extruded molded body (short length, long length, continuous body) containing 22 to 15% (weight ratio) of water. Microwave heater that evaporates evenly in the 3rd place including the inside of the extrusion to dry without distortion, and far-infrared heater device that can efficiently heat the remaining 2/3 of the moisture content higher than microwave There are no cracks, explosions, twists, and warpages, and there is a feature that the drying time can be shortened to 1/100 to 300 of the previous one. In addition, the volume of the extruded product is 1 for the dried product as compared with that during extrusion.
There is a feature that the shrinkage of more than 50% absorbs the influence on the conveying speed due to the shrinkage, and it can be transferred to the next step. Further, in the present invention, since the process from extrusion to drying is linearly arranged, a long body or the like can be smoothly dried.
第1図(a)、(b)は本発明に係る粘土成形体の迅速
乾燥装置の一実施例を示す構成略図とそのイ−イ線断面
図、第2図(a)〜(j)は押出成形体の断面を示す説
明図である。 1……押出成形機、5……マイクロ波加熱機、16……遠
赤外線ヒータ装置、20……走行カッタ。1 (a) and 1 (b) are schematic configuration diagrams showing an embodiment of a quick-drying device for a clay molded body according to the present invention and a sectional view taken along the line ii, and FIGS. 2 (a) to (j) are It is explanatory drawing which shows the cross section of an extrusion molded body. 1 …… Extrusion molding machine, 5 …… Microwave heating machine, 16 …… Far infrared heater device, 20 …… Running cutter.
Claims (1)
で押し出す押出成形機と、該押出成形機から送出される
押出成形体の水分を短時間で低減するオーブン連続方式
のマイクロ波加熱機と、該マイクロ波加熱機を通過した
押出成形体の主に温度上昇を図る遠赤外線ヒータ装置
と、該遠赤外線ヒータ装置を通過した連続乾燥状態の押
出成形体を定尺に切断する走行カッタの順に、直列に配
設したことを特徴とする粘土成形体の迅速乾燥装置。1. An extrusion molding machine for continuously extruding a raw material mainly made of clay in a predetermined shape, and an oven continuous microwave for reducing the water content of an extrusion molding product sent from the extrusion molding machine in a short time. A heater, a far-infrared heater device that mainly raises the temperature of the extruded product that has passed through the microwave heater, and a travel that cuts the continuously dried extruded product that has passed through the far-infrared heater device to a fixed length A quick-drying device for a clay molded body, which is arranged in series in the order of a cutter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21675786A JPH0729843B2 (en) | 1986-09-12 | 1986-09-12 | Rapid drying equipment for clay compacts |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21675786A JPH0729843B2 (en) | 1986-09-12 | 1986-09-12 | Rapid drying equipment for clay compacts |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6369747A JPS6369747A (en) | 1988-03-29 |
| JPH0729843B2 true JPH0729843B2 (en) | 1995-04-05 |
Family
ID=16693440
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21675786A Expired - Lifetime JPH0729843B2 (en) | 1986-09-12 | 1986-09-12 | Rapid drying equipment for clay compacts |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0729843B2 (en) |
-
1986
- 1986-09-12 JP JP21675786A patent/JPH0729843B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6369747A (en) | 1988-03-29 |
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