JPS6369745A - Quick drying apparatus for clay formed body - Google Patents

Quick drying apparatus for clay formed body

Info

Publication number
JPS6369745A
JPS6369745A JP21507286A JP21507286A JPS6369745A JP S6369745 A JPS6369745 A JP S6369745A JP 21507286 A JP21507286 A JP 21507286A JP 21507286 A JP21507286 A JP 21507286A JP S6369745 A JPS6369745 A JP S6369745A
Authority
JP
Japan
Prior art keywords
clay
air
extrusion
microwave heating
heated
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.)
Granted
Application number
JP21507286A
Other languages
Japanese (ja)
Other versions
JPH0437026B2 (en
Inventor
隆一 高橋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IG Technical Research Inc
Original Assignee
IG Technical Research Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by IG Technical Research Inc filed Critical IG Technical Research Inc
Priority to JP21507286A priority Critical patent/JPS6369745A/en
Publication of JPS6369745A publication Critical patent/JPS6369745A/en
Publication of JPH0437026B2 publication Critical patent/JPH0437026B2/ja
Granted legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.

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時間位の短時間に
マイクロ波、遠赤外線とエアとを併用してその相乗効果
により乾燥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 a method of extruding an extruded molded product, which is made by continuously extruding a raw material mainly composed of clay into a predetermined shape, by microwave treatment in a short period of about 10 minutes to 1 hour. This invention relates to a quick drying device for clay molded bodies that can be dried by using far infrared rays and air in combination due to their synergistic effect.

〔従来の技術〕[Conventional technology]

一般に、粘土を用いた内、外壁材、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して約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。
In general, inner and outer wall materials and roof tiles made of clay are extruded into a predetermined shape, and then immediately cut into short lengths, for example, 10 to 30 cm, and then cut into short lengths of about 1 to 30 cm using waste heat from a kiln. 3
It was common to use a device configured to reduce the moisture content to 1 to 0% within a few days and then supply it to the kiln.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

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
いないと運搬することができず、生産性に劣り、かつコ
ストアンプを招くと共に、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
乾燥時間を1日短縮した場合に、表面層が最初に乾燥し
、内部の水蒸気圧によって瓦、タイル、外壁材が捩じれ
たり、反ったり、クランクが入ったり、破壊したりする
欠点があり、乾燥時間の短縮は非常に困難なものであっ
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
タによる乾燥も考えられるが、単に各装置を用いた場合
は前者では被乾燥物を130℃位まで上昇させるのが困
難で、急激な加熱は爆裂を招き、その上後者より装置、
エネルギーコストが高価なものであった。また、後者で
は被乾燥物の内部までの到達時間が前者より長くかかる
が、内部温度を上昇させるのには前者よりもはるかに有
利であるということで各乾燥装置には一長一短があった
。その上、上記2装置では乾燥時に発生する大量の水蒸
気の結露防止処理、被乾燥物の乾燥時における搬送構造
にも種々の問題点、例えば被乾燥物とコンベアベルト間
の摩擦抵抗による変形、長尺体に対するマイクロ波の不
均一加熱等があった。
Conventional drying equipment for clay molded bodies not only takes several days to dry, but also makes it impossible to transport longer clay molded bodies without using an underboard, resulting in lower productivity and increased costs. It also required a large area of land. Furthermore, when drying time is shortened by one day using conventional drying equipment that applies heat from the surface to dry, the surface layer dries first, causing roof tiles, tiles, and exterior wall materials to twist or warp due to internal water vapor pressure. It has been very difficult to shorten the drying time because of the disadvantages of drying, cranking, and breaking. In addition, instead of drying by heating from the surface, drying by internal heating devices such as microwave heaters and far-infrared heaters can be considered, but if each device is simply used, the former will allow the material to be dried to reach a temperature of about 130°C. It is difficult to raise the temperature, rapid heating can lead to explosion, and the latter can damage the equipment,
Energy costs were high. In addition, although the latter takes longer to reach the inside of the material to be dried than the former, it is much more advantageous in raising the internal temperature than the former, so each drying device has its advantages and disadvantages. In addition, the above two devices have various problems in preventing condensation of a large amount of water vapor generated during drying, and in the conveying structure when drying objects to be dried, such as deformation due to frictional resistance between the objects to be dried and the conveyor belt, and long There was non-uniform heating of the microwave to the ulnar body.

〔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、押出成形機の
次に押出成形体の内部へ浸透性がよいマイクロ波加熱機
、次に被乾燥物の温度上昇を図る赤外線(遠赤外線)を
熱源とする遠赤外線ヒータ装置の順に直線状に配列する
と共に、エアをマイクロ波加熱の被加熱空間に大量に供
給して乾燥時に発生する大量の水蒸気を上記被加熱空間
外へ供給、もしくは吸引されるエアによって放出させ押
出成形体表面への結露、加熱空間内壁への結露水の付着
を排除して粘土押出成形体の連続体を連続して約10分
〜1時間位の短時間で乾燥でき、しかも、被乾燥物にク
ランク、反り、捩じれ、爆裂もなく迅速に乾燥できる従
前に較べ大幅にコンパクト化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 these drawbacks, the present invention uses an extrusion molding machine, followed by a microwave heater that has good penetration into the inside of the extruded product, and then an infrared (far infrared) heat source that increases the temperature of the material to be dried. In addition to arranging far-infrared heater devices linearly in this order, a large amount of air is supplied to the space to be heated by microwave heating, and a large amount of water vapor generated during drying is supplied to or sucked out of the space to be heated. The continuum of clay extrudates can be continuously dried in a short period of about 10 minutes to 1 hour by releasing air using air to eliminate condensation on the surface of the extrusion and adhesion of condensed water to the inner wall of the heating space. Moreover, the present invention proposes a rapid drying device for clay molded bodies that is significantly more compact than the conventional device and can quickly dry the material to be dried without cranking, warping, twisting, or exploding.

〔実施例〕〔Example〕

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、■は押出成形機で粘土を主材とする原
料を例えば第2図(al〜(Jl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、例えば押し出
し速度は厚さ、幅によって異なるが200〜2000+
+n/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
ロザイト、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
トによって除鉄されることもある。
EMBODIMENT OF THE INVENTION Below, one Example of the quick drying apparatus of the clay molded object based on this invention is demonstrated in detail using drawing. Figure 1 (a
) and (b) are explanatory diagrams showing a typical example of the above device. In the figure, ■ indicates that an extrusion molding machine is used to continuously extrude a clay-based raw material, for example, into an extrusion molded body A having a cross-sectional shape shown in Figure 2 (al to (Jl). , depending on the width, 200 to 2000+
+n/min. Note that clay is a natural product and has different components depending on its production area, and these advantages and disadvantages are offset to obtain a predetermined mixed clay. Specific examples include pounding pottery stone, feldspar, kaolinite, halozite, metahalosite, Kibushi clay, Frogme clay, Shigaraki clay, chamotte, etc., and kneading them by adding water. In addition, iron may be removed from this clay using a magnet if necessary.

2は移送機構で例えばフリローラ、あるいは図示しない
が押し出し速度に同調した駆動ベルト等の少なくとも1
種からなるものであり、押出成形体Aを押し出し速度の
ままで次工程に変形なく送給するだめのものである。主
はマイクロ波加熱機でオーブン連続方式構造としたもの
であり、主に押出成形体Aの内部へ浸透して熱伝導に時
間を要することなくマイクロ波を熱エネルギーに変換し
、数秒から数分で発熱して粘土内の水分を蒸発せしめる
ためのものである。なお、水分が押出成形体Aにおいて
重量比で22〜15%位含有されており、そのうちの例
えば5〜10%を蒸発する能力を有するものである。特
にこの種押出成形体Aは水分が5〜8%位になるまで体
積が収縮するが、それ以下の水分になると体積の収縮が
生じないものとなる。そこで、マイクロ波加熱機ユを具
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を所要個所に案内する導波管4と、
案内されたマイクロ波Bを反射する反射板5と、反射さ
れたマイクロ波を攪拌する回転羽根6と、押出成形体A
を押し出し速度で移動させる誘電はするがスパークしな
い構成のフリローラからなる搬送部7と、押出成形体A
の入口、出口8.9とエア等Cを大量に被加熱空間12
から吸引したり、被加熱空間12へ供給したりするエア
供給口13と、マイクロ波Bが外部へ漏洩しないように
囲んだ包囲体14とから構成したものである。なお、入
口、出口8.9はマイクロ波Bが外部へ漏洩しないフィ
ルターとしても機能する構造、長さに形成したものであ
る。また、押出成形体Aを加熱する被加熱空間12は目
的に応じて異なるが、例えば約1〜5m位としたもので
ある。さらに、搬送部7はマイクロ波B、エア等Cが押
出成形体Aに均一に照射もしくは送付されることと、押
出成形体Aが乾燥する際に1割程全体が収縮するため、
これを吸収しなから押出成形体Aを搬送できる構成とし
たものである。その−例を図示すると第3図(a)、(
b)に示すように、固定された芯棒7aとテフロンから
なるパイプ状のフリローラ7bと第4図に示すような芯
棒支持具10と、必要に応じて設ける遮蔽板11とから
構成したものである。さらに説明すると(a)図におい
てフリローラ7bは幅を3分割し、押出成形体A通過時
の抵抗をより小さくした構成、fb)図は一本で構成し
たフリローラ7bである。また、芯棒支持具10はマイ
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
通過孔10aを穿設したものである。なお、遮蔽板11
は押出成形体Aが長尺体の場合、物理的に上部の、かつ
長手方向の両側端が高密度となるものを抑制して均一加
熱となるのに有用なものである。また、エア供給口13
はコンプレッサ、リングブロア等のエア(ドライエア、
温風、空気も含む)の送風、もしくは吸引可能なエアサ
イクル用原動機15に連結されている616は遠赤外線
ヒータ装置で赤外線、特に遠赤外線を熱源とするもので
あり、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の温度を130°C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〜lOm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。
Reference numeral 2 denotes a transfer mechanism, for example, a free roller or at least one drive belt (not shown) synchronized with the extrusion speed.
It is made of seeds and is used to feed the extruded product A to the next process at the same extrusion speed without deformation. The main type is a microwave heating machine with a continuous oven structure, which converts microwaves into thermal energy without penetrating the inside of extruded product A and requiring time for heat conduction, which lasts from a few seconds to a few minutes. This is to generate heat and evaporate the water in the clay. The extruded product A contains about 22 to 15% water by weight, and has the ability to evaporate, for example, 5 to 10% of this water. In particular, this type of extruded product A shrinks in volume until the moisture content reaches about 5 to 8%, but when the moisture content falls below that, the volume does not shrink. Therefore, to explain the microwave heating unit in detail, it includes a waveguide 4 that guides microwaves oscillated from a microwave oscillator (not shown) to a required location;
A reflecting plate 5 that reflects the guided microwaves B, a rotary blade 6 that stirs the reflected microwaves, and an extruded body A
a conveyor section 7 consisting of a free roller that is dielectric but does not cause sparks to move at an extrusion speed;
The inlet and outlet 8.9 and a large amount of air etc. C are heated in the heated space 12.
It is composed of an air supply port 13 for sucking air from the air and supplying it to the heated space 12, and an enclosure 14 that surrounds the microwave B to prevent it from leaking to the outside. Note that the inlet and outlet 8.9 are formed to have a structure and length that also function as a filter to prevent the microwave B from leaking to the outside. Further, the space to be heated 12 in which the extrusion molded product A is heated varies depending on the purpose, but is, for example, about 1 to 5 m. Furthermore, in the conveying section 7, the microwave B, air, etc.
The structure is such that the extrusion molded product A can be transported without absorbing this. An example of this is shown in Figure 3 (a), (
As shown in b), it is composed of a fixed core rod 7a, a pipe-shaped free roller 7b made of Teflon, a core rod support 10 as shown in FIG. 4, and a shielding plate 11 provided as necessary. It is. To explain further, in the figure (a), the width of the free roller 7b is divided into three parts to reduce the resistance when the extruded body A passes through, and in the figure fb), the free roller 7b is composed of one piece. In addition, the core rod support 10 is provided with a passage hole 10a so that the microwave B can be irradiated from the back side of the extrusion molded body A as well. In addition, the shielding plate 11
When the extruded body A is a long body, it is useful for suppressing the physically high density at the upper and both ends in the longitudinal direction and achieving uniform heating. In addition, air supply port 13
is air from a compressor, ring blower, etc. (dry air,
Reference numeral 616 connected to the air cycle prime mover 15 capable of blowing or suctioning warm air (including air) is a far-infrared heater device that uses infrared rays, especially far infrared rays, as a heat source, The temperature of the extruded product A is raised to 130°C or higher in order to reduce the temperature to 1 to 0%. Its structure consists of a conveyance mechanism 17 consisting of free rollers and a drive belt, a far-infrared heater 18, and a heat-retaining box 19, and the heating zone is about 2 to 10m. Of course, the heating zone depends on the thickness, width, and
It varies depending on the size and conveyance speed.

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

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%、シャモン目8%、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
〜150I!/hrの型名MV−FM−A−1型(宮崎
鉄工社製)を用いた。また、移送機構2としてはフリロ
ーラ、駆動ベルトコンベアの順に配列したもの、マイク
ロ波加熱機ユとしては周波数2450MHz、出力5k
w、被加熱空間12の長さは3mとし、必要によりエア
等Cを被加熱空間12に大量に包囲体14の一壁面から
送給され、人、出口8.9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12内の水蒸気圧を低
下し、被加熱物、包囲体14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7はテフ
ロン製パイプからなるフリローラとした。また、遠赤外
線ヒータ装置16は遠赤外線ヒーター8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20に−とじた。なお、マイクロ波加熱機1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の押し
出し速度は300〜10001m/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の押し出し速度を
そのまま駆動ベルトでマイクロ波加熱機1に送給され、
マイクロ波加熱機1内の搬送部7のフリローラ上での水
分蒸発で体積が収縮するがこれ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は移送機構
2を介してマイクロ波加熱機1に送給され、マイクロ波
加熱機主の被加熱空間12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分で乾燥体として次工程に送出できた。
First, clay consisting of Shigaraki clay, chamotte, water reducing agent, and water is prepared as raw materials. The weight percentage is, for example, 61.5% Shigaraki clay, 8% Chamonite, 0.5% water reducing agent (product name: Celluflo, manufactured by Dai-ichi Kogyo Seiyaku Co., Ltd.), and 20% water in a clay kneading machine (MP-100). It was mixed using a mold (manufactured by Miyazaki Tekko Co., Ltd.). In addition, the extrusion molding machine 1 has an extrusion capacity of 100
~150I! /hr type name MV-FM-A-1 type (manufactured by Miyazaki Tekko Co., Ltd.) was used. The transfer mechanism 2 includes a free roller and a drive belt conveyor arranged in this order, and the microwave heating unit has a frequency of 2450 MHz and an output of 5 k.
The length of the space to be heated 12 is 3 m, and if necessary, a large amount of air or the like C is fed into the space to be heated 12 from one wall of the enclosure 14, and water vapor C generated during heating is supplied from an outlet 8.9. ' to the outside, lowering the water vapor pressure in the heated space 12, and preventing dew condensation from forming on the heated object and the inner wall of the enclosure 14. It was made into a free roller made of manufactured pipes. Further, the far-infrared heater device 16 includes a plurality of far-infrared heaters 8, approximately three
They were arranged in a zone of ~10 m, and their output was, for example, 20 m. In addition, in the microwave heating machine 1, the moisture content of extrusion molded body A was reduced to 18% (weight %) to 5% (weight %).
The remaining water was evaporated by the far-infrared heater device 16. Further, the extrusion speed of the extrusion molding machine 1 was 300 to 10,001 m/min, and here it was set to 400 mm/min. Others, extrusion molded product A
(Here, it is a continuous molded product) The pass lines of the extruded molded product A are set at the same height, and the extruded molded product A is fed to the microwave heating machine 1 by a drive belt at the same extrusion speed of the extrusion molding machine 1.
Although the volume shrinks due to moisture evaporation on the free roller of the conveying section 7 in the microwave heating machine 1, the difference in speed due to this shrinkage is absorbed. Therefore, the clay supplied to the extrusion molding machine 1 is sent out from the outlet in a continuous body having a cross section shown in FIG. 2(g). The delivered extrusion molded product A is fed to the microwave heating machine 1 via the transfer mechanism 2, and while passing through the heated space 12 of the main microwave heating machine, the moisture content of the extrusion molded product A is reduced to 5% (weight ratio). ) in 5 minutes, and fed from the outlet to the far-infrared heater device 16, where the water content was evaporated to 1% (weight ratio) in about 10 minutes and dried. As a result, the extruded product A, which had a continuous band extending from the exit of the extrusion molding machine 1 to the far-infrared heater device 16, could be sent to the next process as a dry product in about 15 to 20 minutes.

なお、被加熱空間12の水蒸気C′は人、出口8.9か
ら矢印に放出することによって下記の効果が得られるも
のである。すなわち、被加熱空間12からのエアの放出
は被加熱空間12の水蒸気圧が増加しないように、およ
び押出成形体Aが急激な加熱によってオーバーヒートし
破壊するのを防止し、かつエア等Cが加熱中の押出成形
体Aの表、裏面近傍の空気層に流れを与えることによっ
て押出成形体Aの露出面を冷却することと合俟ってオー
バーヒートの抑制と乾燥時間の短縮を図ると共に、押出
成形体Aの露出面、被加熱空間12の内壁へ結露が発生
するのを防止するものである。そして、この乾燥された
連続帯状の押出成形体Aは走行力・ツタ20で定尺に切
断され、図示しない施釉工程、もしくは焼成工程に送給
するものである。
The following effects can be obtained by releasing the water vapor C' in the heated space 12 in the direction of the arrow from the exit 8.9. That is, the release of air from the heated space 12 prevents the water vapor pressure in the heated space 12 from increasing, prevents the extruded product A from overheating and breaking due to rapid heating, and prevents the air etc. C from being heated. By providing a flow to the air layers near the front and back surfaces of the extrusion molded product A inside the extrusion molded product A, the exposed surface of the extrusion molded product A is cooled, and together with this, overheating is suppressed and drying time is shortened, and the extrusion molding This prevents dew condensation from forming on the exposed surface of the body A and the inner wall of the heated space 12. Then, this dried continuous band-shaped extrusion molded product A is cut into regular lengths by a running force/vine 20 and sent to a glazing process or a firing process (not shown).

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)において移送機構
2部分に一点鎖線で示す位置に力・ツタを設は短尺に切
断したり、二点鎖線で示すようにマイクロ波加熱機1、
遠赤外線ヒータ装置16(遠赤外線ヒータ装置16の部
分にのみ図示)に温風、または熱風を送給し、より乾燥
時間を短縮するように構成することもできる。また、第
1図(a)においてマイクロ波f>o%機主1部分一点
鎖線で示すようにエアサイクル回線をエア供給口13の
他に、もしくは代りに設けることも可能である。
What has been described above is only one embodiment of the quick drying device for clay molded bodies according to the present invention. Cut or microwave heating machine 1, as shown by the two-dot chain line.
It is also possible to supply warm air or hot air to the far-infrared heater device 16 (only the far-infrared heater device 16 is shown) to further shorten the drying time. Further, as shown by the dashed line in the microwave f>o% machine main 1 section in FIG. 1(a), it is also possible to provide an air cycle line in addition to or in place of the air supply port 13.

〔発明の効果〕〔Effect of the invention〕

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)、その連続体を2段階の加熱工程
と加熱空間における水蒸気及びその上昇を押えることに
よってクラック、爆裂、反り、捩じれもなく、かつ乾燥
時間を従前の1/100〜300に短縮できる特徴があ
る。また、押出成形体の体積は押し出し時に比べ1割以
上収縮するが、それによる搬送速度が押出成形体へ及ぼ
す悪影響もなく吸収し次工程に移送できる利点がある。
As described above, according to the quick drying device for clay molded bodies according to the present invention, a clay extrusion molded body (short length) containing about 22 to 15% water (weight ratio) and a continuous body thereof are subjected to a two-stage heating process. By suppressing water vapor and its rise in the heating space, there is no cracking, explosion, warping, or twisting, and the drying time can be shortened to 1/100 to 300 times of the conventional drying time. Further, although the volume of the extruded body shrinks by 10% or more compared to when it is extruded, there is an advantage that the transport speed due to this shrinks without any adverse effect on the extruded body and can be absorbed and transferred to the next process.

さらに、本発明では押し出しから乾燥までを直列に配列
したため、長尺帯、連続帯を迅速に乾燥できる特徴があ
る。その上、被加熱空間内の水蒸気を外部へ放出するよ
うにしたため、被加熱空間内壁および被加熱物表面への
悪影響と結露の発生、蒸発スピードの低下を防止した特
徴がある。また、マイクロ波の被加熱物に対して下部か
らの照射、弱加熱部への集中化等を行うことによって乾
燥の均一化と乾燥時の悪影響を防止できる特徴がある。
Furthermore, in the present invention, since the processes from extrusion to drying are arranged in series, a long band or continuous band can be dried quickly. Furthermore, since the water vapor in the space to be heated is released to the outside, it is possible to prevent an adverse effect on the inner wall of the space to be heated and the surface of the object to be heated, to prevent condensation, and to prevent a decrease in the evaporation speed. Furthermore, by irradiating the heated object with microwaves from below, concentrating on the weak heating part, etc., drying can be made uniform and adverse effects during drying can be prevented.

【図面の簡単な説明】[Brief explanation of the drawing]

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ーイ線断面
図、第2図(a)〜fj)は押出成形体の断面を示す説
明図、第3図(a)、(bl、第4図はマイクロ波加熱
機の搬送部の構成を示す説明図である。 ■・・・押出成形機、1!・・マイクロ波加熱機、7・
・・搬送部、13・・・エア供給口、16・・・遠赤外
線ヒータ装置、A・・・押出成形体、B・・・マイクロ
波、C・・・エア、C′・・・水蒸気。 第1図 (幻 第2図 (α)        f八 (b)   、A (c)   、A (dン (A Ce) fへ 一二譜=ゴ==倒=) 第1図 fへ ″>)       〜へ 暢 (い       〜ハ (メ)     Iへ (ハ 第3図 六 ] (l:l) 弓父 第十図
FIGS. 1(a) and (b) are schematic diagrams showing an embodiment of the rapid drying device for clay molded bodies according to the present invention and a cross-sectional view taken along the line E, and FIGS. 2(a) to fj) are extruded molded bodies. 3(a) and 4 are explanatory diagrams showing the configuration of the conveying section of the microwave heating machine. ■...Extrusion molding machine, 1!...Micro Wave heating machine, 7.
...Conveyance section, 13...Air supply port, 16...Far infrared heater device, A...Extrusion molded product, B...Microwave, C...Air, C'...Water vapor. Figure 1 (Illusion Figure 2 (α) f8 (b) , A (c), A (ddon (A Ce) f to 12 staves = go = = down =) Figure 1 to f''>) ~Hero (I ~Ha (Me) I Go (Ha 3rd Figure 6) (l:l) Yumichichi Figure 10

Claims (1)

【特許請求の範囲】[Claims] (1)粘土を主材とした原料を連続して所定形状で押し
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の順に配
列してなり、また前記マイクロ波加熱機の出、入口以外
の外周面にエア供給口を設け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 that continuously extrudes clay-based raw materials into a predetermined shape, and a continuous oven-type microwave heating machine that quickly reduces moisture in the extruded product sent out from the extrusion molding machine. and far-infrared heater devices that mainly raise the temperature of the extruded product passed through the microwave heating machine, and air supply ports are provided on the outer circumferential surface of the microwave heating machine other than the exit and inlet. 1. A quick drying device for clay molded bodies.
JP21507286A 1986-09-11 1986-09-11 Quick drying apparatus for clay formed body Granted JPS6369745A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21507286A JPS6369745A (en) 1986-09-11 1986-09-11 Quick drying apparatus for clay formed body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21507286A JPS6369745A (en) 1986-09-11 1986-09-11 Quick drying apparatus for clay formed body

Publications (2)

Publication Number Publication Date
JPS6369745A true JPS6369745A (en) 1988-03-29
JPH0437026B2 JPH0437026B2 (en) 1992-06-18

Family

ID=16666289

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21507286A Granted JPS6369745A (en) 1986-09-11 1986-09-11 Quick drying apparatus for clay formed body

Country Status (1)

Country Link
JP (1) JPS6369745A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52104949U (en) * 1976-02-04 1977-08-10

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52104949U (en) * 1976-02-04 1977-08-10

Also Published As

Publication number Publication date
JPH0437026B2 (en) 1992-06-18

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