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JPH0729845B2 - Rapid drying equipment for hollow clay compacts - Google Patents
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JPH0729845B2 - Rapid drying equipment for hollow clay compacts - Google Patents

Rapid drying equipment for hollow clay compacts

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Publication number
JPH0729845B2
JPH0729845B2 JP22325986A JP22325986A JPH0729845B2 JP H0729845 B2 JPH0729845 B2 JP H0729845B2 JP 22325986 A JP22325986 A JP 22325986A JP 22325986 A JP22325986 A JP 22325986A JP H0729845 B2 JPH0729845 B2 JP H0729845B2
Authority
JP
Japan
Prior art keywords
extruded
hollow
clay
air
extrusion
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
Application number
JP22325986A
Other languages
Japanese (ja)
Other versions
JPS63185851A (en
Inventor
隆一 高橋
Original Assignee
株式会社アイジー技術研究所
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 株式会社アイジー技術研究所 filed Critical 株式会社アイジー技術研究所
Priority to JP22325986A priority Critical patent/JPH0729845B2/en
Publication of JPS63185851A publication Critical patent/JPS63185851A/en
Publication of JPH0729845B2 publication Critical patent/JPH0729845B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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した原料を中空部を有する所定
形状で連続して押し出された粘土成形体を10分〜1時間
位の短時間にマイクロ波、遠赤外線およびエア等とを併
用してその相乗効果により反り、捩じれ、クラック、爆
裂もなく乾燥しうる中空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 provides a clay molded body obtained by continuously extruding a raw material containing clay as a main component in a predetermined shape having a hollow portion in a short time of about 10 minutes to 1 hour. The present invention relates to a rapid drying apparatus for hollow clay moldings which can be dried without warping, twisting, cracking, or explosion by the combined use of microwaves, far-infrared rays, air, or the like due to its 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、その後で焼成炉に供給す
る構成となっていた。
In general, an inner wall material and roof tile made of clay are extruded in a predetermined shape, and are immediately cut into a short length, for example, a length of 10 to 30 cm, and the waste heat of a firing furnace is used for about 1 to 1 cm. The water content was reduced to 1 to 0% in about 3 days and then supplied to the firing furnace.

〔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、従前の乾燥方式では長尺状の中空体、長
尺で薄肉の中空体を乾燥することが困難であり、かつ短
尺体でも乾燥に数日を要する欠点があった。すなわち、
従前は押出成形機を出た直後に定尺(10〜30cm位)に切
断し、これを台車上にのせ乾燥機に送給し数日間で乾燥
する工程のため長尺で、かつ中空状の押し出し直後の柔
らかい押出物を長時間に亘って原形を維持して乾燥する
ことができず、成形してしまい長尺中空体を乾燥できな
い欠点があった。さらに、従前は押出機と乾燥後は上記
のような日数の関係で連続ラインの技術思想が存在せ
ず、生産性に劣り、コストアップとなっていた。また、
中空状の長尺成形体を単にマイクロ波等で乾燥し、乾燥
時間を大幅に短縮しようとした場合は、中空部の水蒸気
圧の上昇と結露の発生、中空部内壁と外表面の乾燥度合
のズレによって相当の肉厚がないと爆裂、クラックの発
生、反り、捩じれ等の変形が生じる欠点があった。しか
も、マイクロ波は押出成形体の含水分を1%以下にする
ために温度を130℃以上に上昇させる必要があるが、こ
の温度まで上昇させるのに相当の時間とエネルギーロス
があった。その他、マイクロ波の代わりに遠赤外線を用
いて乾燥する方法もあるが、押出成形体を130℃以上に
昇温するのはマイクロ波よりはるかに短時間となる反
面、乾燥時間が長くなる弱点があった。その上、上記2
装置を用いた乾燥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。
However, the conventional drying method has a drawback that it is difficult to dry a long hollow body and a long thin hollow body, and even a short body requires several days to dry. That is,
Conventionally, it is long and hollow for the process of cutting it to a standard length (10 to 30 cm) immediately after leaving the extruder, placing it on a trolley and feeding it to the dryer for several days. The soft extrudate immediately after extrusion cannot be dried while maintaining its original shape for a long time, and there is a drawback that the long hollow body cannot be dried due to molding. Further, in the past, the technical idea of the continuous line did not exist due to the above-described number of days after the extruder and after drying, resulting in poor productivity and high cost. Also,
If you want to greatly reduce the drying time by simply drying the hollow long molded body with microwaves, etc., increase the water vapor pressure of the hollow part and the occurrence of dew condensation, and the dryness of the inner wall and outer surface of the hollow part If there is not a considerable thickness due to the displacement, there is a defect that explosion, cracking, warpage, deformation such as twisting occurs. In addition, the microwave needs to raise the temperature to 130 ° C. or more in order to reduce the water content of the extruded product to 1% or less, but there was a considerable time and energy loss to raise the temperature to this temperature. There is also a method of drying by using far infrared rays instead of microwaves, but heating the extruded body to 130 ° C or higher takes a much shorter time than microwaves, but there is a weakness that the drying time becomes long. there were. Moreover, above 2
In the drying device using the device, a large amount of water vapor generated during drying is prevented from dew condensation, and there are various problems in the transport structure during drying of the material to be dried, such as deformation due to friction resistance between the material to be dried and the conveyor belt, long There was non-uniform heating of microwaves on the scale.

〔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
次に中空押出成形体をスムーズに次工程に移送する移送
機、次に連続帯状の中空押出成形体の含水分の1/3位を
短時間(5〜30分位)で蒸発させるマイクロ波加熱機、
次にこの中空押出成形体の含水分を例えば5〜30分位の
短時間で1%以下に低減する遠赤外線ヒータ装置の順に
配列すると共に、加熱時に中空部内部に滞溜する水蒸気
を押出成形機の中子に設けた送風口から送風する風(エ
ア、ドライエア)によって吹き払い、水蒸気圧を低下
し、かつ中空部内の加熱の効率を上げると共に、中空部
内に生ずる結露を排除して中空部内と中空押出成形体表
面層の含水比率を平均化し、またマイクロ波加熱空間内
の水蒸気と中空押出成形体表面の水蒸気を外部へ吹き払
って上記表面への結露と被加熱空間内壁への結露を防止
してより一層、中空押出成形体の内外の壁面をエアで常
時、吹き払われた状態として乾燥効率、乾燥時間を従前
の1/10〜300位に短縮し、被乾燥物のクラック、反り、
捩じれ等の変形、爆裂もなく長尺中空体を従前より大幅
にコンパクト化した装置で連続して乾燥できる中空粘土
成形体の迅速乾燥装置を提供するものである。
The present invention, in order to eliminate such defects, a transfer machine that smoothly transfers the hollow extrusion molded article to the next step after the extrusion molding machine, and then 1/3 of the water content of the continuous strip-shaped hollow extrusion molded article. Microwave heater that evaporates in a short time (about 5 to 30 minutes),
Next, the far-infrared heater device that reduces the water content of this hollow extruded body to 1% or less in a short time of, for example, 5 to 30 minutes is arranged in that order, and the steam that accumulates inside the hollow portion during heating is extruded. The air blown from the air outlet provided in the core of the machine (air, dry air) blows it off to reduce the water vapor pressure and increase the heating efficiency in the hollow part, while eliminating the dew condensation in the hollow part And the water content of the surface layer of the hollow extruded body is averaged, and the water vapor in the microwave heating space and the water vapor on the surface of the hollow extruded body are blown to the outside to prevent dew condensation on the surface and on the inner wall of the heated space. Prevents the inner and outer wall surfaces of the hollow extruded body from being blown away with air at all times, reducing the drying efficiency and drying time to 1/10 to 300 of the previous level, and cracking and warping the dried object. ,
It is intended to provide a rapid drying apparatus for hollow clay molded bodies, which can continuously dry long hollow bodies without causing deformation such as twisting and explosion and by a device that is much more compact than before.

〔実施例〕〔Example〕

以下に、図面を用いて本発明に係る中空粘土成形体の迅
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し
た原料を第2図(a)、(b)に示すような口金2と中
子3を介して例えば第3図(a)〜(n)に示す中空部
を有する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200〜2000mm/min位である。さらに説明
すると、中子3は多数個の出口部4と共通部5に外部か
らエアを供給、もしくは内部からエア、水蒸気を排気す
るための連結管6とから形成したものであり、出口部4
は押出成形体Aの中空部aの断面形状と同じ断面となる
中空体に形成し、これを押出成形体Aの中空部aの配列
に対応するように共通部5と一体に形成したものであ
る。しかも、中子3は押出成形機1の押出口1′から押
し出される粘土を支障なくその口金2から所定形状の中
空部aを有する連続体で押し出しできるように先端3aか
ら末端3bに亘って例えば流線形状に形成したものであ
る。また、中子3の中空部3cには外部に設置したポンプ
7からホース8を介してエア、ドライエア、ウェットエ
ア、温風等の1種以上を所要量供給、もしくは中空部a
の水蒸気を排出したりして押出成形体Aの乾燥しにくい
中空部aの乾燥を促進すると共に、その際の変形等の悪
影響を排除するように機能するものである。なお、前記
した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。その一具体例としては陶
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。は移送機で例えばフリローラ10、あるいは押
出速度に同調した駆動ベルト11等の少なくとも1種、ま
たは図示するようにその組合わせ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送給
するためのものである。12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達に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12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13と、案内されたマイクロ波Bを反
射する反射板14と、反射されたマイクロ波を撹拌する回
転羽根15と、押出成形体Aを押出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16と、押出成形体Aの入口、出口17、18とエア等Cを
大量に被加熱空間19から、吸引したり、被加熱空間19へ
供給したりするエア出入口20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21とから構成したものであ
る。なお、入口、出口17、18はマイクロ波Bが外部へ漏
洩しないように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19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16はマイクロ波
B、エア等Cが押出成形体Aに表面、裏面、側面からも
均一に照射もしくは送風されることと、押出成形体Aが
乾燥する際に1割程度、全体が収縮するため、これを吸
収しながら押出成形体Aを搬送できる構成としたもので
ある。その一例を図示すると、第4図(a)、(b)に
示すように、固定された芯棒22とテフロンからなるパイ
プ状のフリローラ23と第5図に示すような芯棒支持具24
と必要に応じて設ける遮蔽板25とから構成したものであ
る。さらに説明すると第4図(a)においてフリローラ
23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、(b)図は一本で構成したフリローラ2
3′である。また、芯棒支持具24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24aを穿
設したものである。なお、遮蔽板25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に
マイクロ波Bの照射が高密度となる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、エア出入口20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
クル用のポンプ7に連結されている。26は遠赤外線ヒー
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℃以上まで昇温させるものであ
り、その構成はフリローラ、駆動ベルトの1種以上から
なる搬送機構27と遠赤外線ヒータ28と保温箱29とからな
り、加熱ゾーンは約2〜10m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、搬送速
度によって異なるものである。30は走行カッタであり乾
燥押出成形体A′を所定長さに切断するものである。
An embodiment of a rapid drying apparatus for hollow clay molded bodies according to the present invention will be described in detail below 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 is an extruder, and a raw material containing clay as a main material is introduced through a die 2 and a core 3 as shown in FIGS. 2 (a) and 2 (b), for example, FIGS. The extrusion molding body A having a hollow cross-section shown in) is continuously extruded. For example, the extrusion speed is about 200 to 2000 mm / min although it depends on the thickness and width of the extrusion molding body A. More specifically, the core 3 is formed of a large number of outlet portions 4 and a connecting pipe 6 for supplying air to the common portion 5 from the outside or discharging air and water vapor from the inside.
Is formed into a hollow body having the same cross section as the hollow portion a of the extruded body A, and is formed integrally with the common portion 5 so as to correspond to the arrangement of the hollow portions a of the extruded body A. is there. In addition, the core 3 is formed from the tip 3a to the end 3b, for example, so that the clay extruded from the extrusion port 1'of the extrusion molding machine 1 can be extruded from the die 2 without interruption by a continuous body having a hollow portion a of a predetermined shape. It is formed in a streamlined shape. Further, the hollow portion 3c of the core 3 is supplied with a required amount of at least one kind of air, dry air, wet air, warm air, etc. from a pump 7 installed outside through a hose 8, or the hollow portion a
The water vapor is discharged to promote the drying of the hollow portion a of the extrusion molded body A, which is difficult to dry, and at the same time, it functions to eliminate the adverse effects such as deformation at that time. In addition, the above-mentioned clay is a natural product and has different components depending on each production site, and these advantages and disadvantages are mutually offset to obtain a predetermined mixed clay. As a specific example thereof, porcelain stone, feldspar, kaolinite, halosite, metahalosite, kibushi clay, frog eye clay, Shigaraki clay, chamotte, etc. are crushed and added with water and kneaded. If necessary, this clay may be ironed by a magnet. Reference numeral 9 denotes a transfer device, which is, for example, a flea roller 10, or at least one kind of a drive belt 11 synchronized with an extrusion speed, or a combination thereof as shown in the drawing.
It is for feeding the extrusion-molded body A to the next step without deformation at the extrusion speed. Reference numeral 12 is a microwave heater having an oven continuous structure, which mainly permeates into the inside of the extruded product A and converts the microwave B into heat energy without taking time to transfer the heat, and from several seconds to several seconds. It is for generating heat in minutes to evaporate the water in the clay. In addition,
Moisture is contained in the extruded product A in an amount of about 22 to 15% by weight, of which 5 to 10%, for example, can be evaporated. In particular, the volume of this type of extruded product A shrinks until the water content becomes about 5 to 8%, but when the water content is less than that, the volume shrinkage does not occur. Therefore,
The microwave heater 12 will be described in detail. A waveguide 13 that guides the microwave B oscillated from a microwave oscillator (not shown) to a required location, and a reflection plate 14 that reflects the guided microwave B. A rotary blade 15 for stirring the reflected microwaves, a conveying unit 16 composed of a fli roller configured to move the extruded body A at an extruding speed at the extrusion speed but not spark, and the inlets and outlets 17 and 18 of the extruded body A. And an air inlet / outlet 20 for sucking a large amount of air C or the like from the heated space 19 and supplying the heated space 19 to the heated space 19 and an enclosure 21 enclosing the microwave B so as not to leak outside. Is. The inlets and outlets 17 and 18 are formed to have a structure and length that also function as a filter so that the microwave B does not leak to the outside. The heated space 19 for heating the extruded body A differs depending on the purpose, but is, for example, about 1 to 5 m.
It is a place. Further, the conveying unit 16 uniformly irradiates or blows the microwave B, air or the like C onto the extruded product A from the front surface, the back surface, and the side surface, and when the extruded product A dries, about 10% of the whole. Contracts, so that the extruded product A can be conveyed while absorbing this. As an example, as shown in FIGS. 4 (a) and 4 (b), a fixed core rod 22 and a pipe-shaped flee roller 23 made of Teflon and a core rod support 24 as shown in FIG.
And a shielding plate 25 provided as needed. To further explain, referring to FIG.
23 is a structure in which the width is divided into three, and the resistance when passing through the extruded product A is further reduced.
3 '. Further, the core rod support 24 is provided with a through hole 24a so that the microwave B is also irradiated from the back surface of the extrusion molded body A. In addition, when the extruded body A is a long body, the shielding plate 25 suppresses the irradiation of the microwave B at a high density on both upper ends of the extruded body A and in the longitudinal direction, and uniformly heats the shielding plate 25. It is useful for. Further, the air inlet / outlet 20 is connected to an air cycle pump 7 capable of blowing air (including dry air, warm air, and air) such as a compressor and a ring blower, or sucking air. 26 is a far-infrared heater device for raising the temperature of the extruded product A to 130 ° C. or more in order to reduce the water content of the extruded product A to 1 to 0%, and its constitution is at least one of a flea roller and a drive belt. And a far-infrared heater 28 and a heat insulation box 29, and the heating zone is about 2 to 10 m. Of course, the heating zone differs depending on the thickness, width, and conveyance speed of the extruded product A that has become a semi-dried product. A traveling cutter 30 cuts the dry extruded body A'to a predetermined length.

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。ポンプ
7はリングブロアで20〜50℃に送風時の圧縮により加温
されたドライエアをホース8を介して口金2の外部へ露
出させた連結管6に連結し、もう1つのホース8(一点
鎖線で示す)をマイクロ波加熱機12のエア出入口20に連
結した構成とした。また、遠赤外線ヒータ装置26は遠赤
外線ヒータ28を10メートル間に10個配列し、押出成形体
A内部の水分を表面に拡散して脱水を迅速化し、水分を
1%以下まで低減しうるものである。さらに押出成形機
1の押出速度は200mm/minで第3図(a)に示す断面で
押し出すものとし、長さ900mm、3030mmに押出成形体A
を切断して乾燥押出成形体A′とし、かつ口金2から走
行カッタ30までのラインの直線距離は15mとした。勿
論、このラインの長さは押出成形体Aの形状、幅、厚さ
に対応して設定するものである。なお、押出成形体Aの
パスラインは同じ高さにあり、かつ、移送機の移動速
度は押出速度に同調するように設定した。そこで、粘土
を主材とした原料は押出成形機1から第3図(a)に示
す断面で連続して移送機上に押し出される。押し出さ
れた押出成形体Aは前記速度でマイクロ波加熱機12に送
給され、マイクロ波加熱機12の被加熱空間19を通過中に
マイクロ波Bとエア等Cによって押出成形体Aの中空部
aと外表面に送給されるエア等Cによってマイクロ波加
熱により発生する大量の水蒸気を中空部aの内外ともに
同時に吹き払って常に蒸発しやすい環境にし、結露の発
生を排除すると共に、柔らかい押出成形体Aを短時間の
間に剛性を平均に上昇させ、クラック、反り、変形、オ
ーバヒートによる爆裂のないようにし、かつ押出成形体
Aの含水分の1/3位を5〜10分位で蒸発させ、その出口
から遠赤外線ヒータ装置26に送給し、含水分を1%以下
に乾燥させ、走行カッタ30に送給し、乾燥した連続帯状
の乾燥押出成形体Aを所定長さに切断した。そして、押
出成形体Aは押出から切断まで約15〜30分位の短時間
に、かつ連続体のまま乾燥した。なお、単にマイクロ波
を用いて押出成形体Aを加熱した際は短時間の間に内部
から急加熱されるため爆裂と結露による悪影響がひど
く、実用とならなかった。
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. The pump 7 uses a ring blower to connect dry air heated by compression when blown to 20 to 50 ° C. to the connecting pipe 6 exposed to the outside of the base 2 via the hose 8 and another hose 8 (one-dot chain line). (Indicated by) is connected to the air inlet / outlet port 20 of the microwave heater 12 . Further, the far-infrared heater device 26 has ten far-infrared heaters 28 arranged every 10 meters so that the moisture in the extruded product A can be diffused to the surface to accelerate dehydration and reduce the moisture to 1% or less. Is. Further, the extrusion speed of the extrusion molding machine 1 is 200 mm / min and the extrusion is performed in the cross section shown in FIG. 3 (a).
Was cut into a dry extruded product A ′, and the line distance from the die 2 to the traveling cutter 30 was set to 15 m. Of course, the length of this line is set according to the shape, width, and thickness of the extruded product A. The pass lines of the extrusion molded body A were at the same height, and the moving speed of the transfer machine 9 was set so as to be synchronized with the extrusion speed. Therefore, the raw material containing clay as the main material is continuously extruded from the extruder 1 onto the transfer machine 9 in the cross section shown in FIG. The extruded product A that has been extruded is fed to the microwave heating machine 12 at the above-mentioned speed, and while passing through the heated space 19 of the microwave heating device 12 , the hollow part of the extruded product A is generated by the microwave B and the air C. a and a large amount of water vapor generated by microwave heating by air C sent to the outer surface at the same time both inside and outside the hollow portion a to make it easy to evaporate at all times, thereby eliminating the occurrence of dew condensation and soft extruding. The rigidity of the molded body A is increased to an average in a short time so as to prevent cracking, warpage, deformation, and explosion due to overheating, and the 1 / 3rd position of the water content of the extruded molding A is reduced to about 5 to 10 minutes. Evaporate and feed it to the far infrared heater device 26 to dry it to less than 1% of water content, feed it to the traveling cutter 30, and cut the dried continuous strip dry extruded product A into a predetermined length. did. Then, the extrusion-molded body A was dried in a short time of about 15 to 30 minutes from extrusion to cutting and as a continuous body. When the extruded product A was simply heated using microwaves, it was rapidly heated from the inside for a short period of time, and the adverse effects of explosion and dew condensation were severe and it was not practical.

以上説明したのは本発明に係る中空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、二
点鎖線で示すようにマイクロ波加熱機12にポンプ7と併
用、もしくはポンプ7の代わりにエア供給装置を独立し
て設けたり、一点鎖線で示すように遠赤外線ヒータ装置
26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。勿論、図示しないがマ
イクロ波加熱機12に温風、熱風等の1種以上を供給する
ことも可能である。
What has been described above is only one example of the rapid drying apparatus for a hollow clay molded body according to the present invention. In FIG. 1 (a), the microwave heating machine 12 is used in combination with the pump 7 as shown by the chain double-dashed line. Alternatively, an air supply device may be independently provided instead of the pump 7, or a far-infrared heater device may be provided as indicated by a chain line.
It is also possible to supply hot air or hot air to the 26 to further shorten the drying time. Of course, although not shown, it is possible to supply one or more kinds of hot air, hot air, etc. to the microwave heater 12 .

〔発明の効果〕〔The invention's effect〕

上述したように本発明に係る中空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)含有した中
空状の押出成形体を2段階の加熱と中空部に押出時にエ
ア等を送給して乾燥時の水蒸気による悪影響を押出成形
体の内外面から排除し、短時間に連続体のままでクラッ
ク、捩じれ、反り、爆裂もなく乾燥できる特徴がある。
また、生産性は従前の数日を要したスピードに対し、10
〜60分で乾燥してしまう特徴がある。さらに、押出成形
体の体積は乾燥時に押出時に比べ1割以上収縮するが、
それによる押出成形体への悪影響をフリローラ等で吸収
し製造できる利点がある。また、本発明では押出から乾
燥までを直列に配列したため、長尺体、連続体を迅速に
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
の低下を阻止した特徴がある。その他マイクロ波を押出
成形体に対して裏面、表面および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を図った特徴がある。
As described above, according to the apparatus for rapidly drying a hollow clay molded body according to the present invention, a hollow extruded molded body containing water in an amount of 22 to 15% (weight ratio) is heated in two stages and extruded into the hollow portion. It is characterized in that air or the like is sent to eliminate the adverse effect of water vapor during drying from the inner and outer surfaces of the extruded product, and the extruded product can be dried without cracking, twisting, warping or explosion in a continuous state in a short time.
In addition, productivity is 10% compared to the speed that took several days before.
It has the characteristic that it takes about 60 minutes to dry. Furthermore, the volume of the extruded product shrinks by 10% or more when dried, compared to when extruded.
There is an advantage that the adverse effect on the extruded product due to it can be absorbed and manufactured by a flea roller or the like. Further, in the present invention, since the process from extrusion to drying is arranged in series, there is a feature that a long body and a continuous body can be dried quickly. In addition, since the water vapor in the heated space is released to the outside, it has a characteristic that the adverse effect on the inner wall of the heated space and the surface of the object to be heated, the occurrence of dew condensation, and the reduction of the evaporation speed are prevented. Another characteristic is that the drying is made uniform by concentrating microwaves on the back surface, front surface, and weakly heated portion of the extruded body.

【図面の簡単な説明】 第1図(a)、(b)は本発明に係る中空粘土成形体の
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)は押出成形機の出口部を示す説明
図、(b)図は中子を抽出して示す説明図、第3図
(a)〜(n)は押出成形体の一例を示す断面図、第4
図(a)、(b)、および第5図はマイクロ波加熱機の
搬送部の主要構成材を示す説明図である。 1……押出成形機、3……中子、7……ポンプ、……
移送機、12……マイクロ波加熱機、26……遠赤外線ヒー
タ装置。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 (a) and FIG. 1 (b) are schematic configuration diagrams showing an embodiment of a rapid drying apparatus for hollow clay molded articles according to the present invention, a sectional view taken along the line EE, and FIG. (A) is explanatory drawing which shows the exit part of an extrusion molding machine, (b) is an explanatory drawing which extracts and shows a core, FIG.3 (a)-(n) is sectional drawing which shows an example of an extrusion molded body. , 4th
FIGS. (A), (b), and FIG. 5 are explanatory views showing the main constituent members of the transfer section of the microwave heater. 1 ... Extruder, 3 ... Core, 7 ... Pump, 9 ...
Transfer machine, 12 ...... Microwave heating machine, 26 ...... Far infrared heater device.

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中空部を有する所
定形状で連続して押し出す中子付の押出成形機と、該押
出成形機から連続して押し出される押出成形体をスムー
ズに次工程に移送する移送機と、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水分低減と温度上昇を図る遠赤外線
ヒータ装置とを直列に配列してなり、また前記押出成形
機の口金に設置した中子に外部から気体を押出成形体に
支障を与えることなく送給するポンプと前記マイクロ波
加熱機の出入口以外の被加熱空間内の壁体にエアを供給
するエア出入口を穿設したことを特徴とする中空粘土成
形体の迅速乾燥装置。
1. An extruder having a core for continuously extruding a raw material containing clay as a main material in a predetermined shape having a hollow portion, and an extrusion molded body continuously extruded from the extruder smoothly A transfer machine for transferring to the process, an oven continuous microwave heater for reducing the water content of the extruded product delivered from the extruding machine in a short time, and the water content of the extruded product that has passed through the microwave heating device. A far infrared heater device for reducing and increasing the temperature is arranged in series, and a pump for feeding gas from the outside to the core installed in the mouthpiece of the extrusion molding machine without hindering the extrusion molding body. An apparatus for rapid drying of a hollow clay molded body is provided with an air inlet / outlet for supplying air to a wall in the heated space other than the inlet / outlet of the microwave heater.
JP22325986A 1986-09-19 1986-09-19 Rapid drying equipment for hollow clay compacts Expired - Lifetime JPH0729845B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22325986A JPH0729845B2 (en) 1986-09-19 1986-09-19 Rapid drying equipment for hollow clay compacts

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22325986A JPH0729845B2 (en) 1986-09-19 1986-09-19 Rapid drying equipment for hollow clay compacts

Publications (2)

Publication Number Publication Date
JPS63185851A JPS63185851A (en) 1988-08-01
JPH0729845B2 true JPH0729845B2 (en) 1995-04-05

Family

ID=16795298

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22325986A Expired - Lifetime JPH0729845B2 (en) 1986-09-19 1986-09-19 Rapid drying equipment for hollow clay compacts

Country Status (1)

Country Link
JP (1) JPH0729845B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1846958B (en) 2005-04-13 2010-08-25 上海麦风微波设备有限公司 Light wall board producing process and apparatus
CN100420650C (en) * 2005-11-16 2008-09-24 勾学军 Honeycomb ceramic continuous finalizing drying method and its dedicated apparatus
JP6524514B2 (en) * 2015-01-13 2019-06-05 清水建設株式会社 Method of drying bentonite compact

Also Published As

Publication number Publication date
JPS63185851A (en) 1988-08-01

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