JPH0729842B2 - Rapid drying equipment for clay compacts - Google Patents

Rapid drying equipment for clay compacts

Info

Publication number
JPH0729842B2
JPH0729842B2 JP21507386A JP21507386A JPH0729842B2 JP H0729842 B2 JPH0729842 B2 JP H0729842B2 JP 21507386 A JP21507386 A JP 21507386A JP 21507386 A JP21507386 A JP 21507386A JP H0729842 B2 JPH0729842 B2 JP H0729842B2
Authority
JP
Japan
Prior art keywords
clay
extrusion
microwave
molded body
heater
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
JP21507386A
Other languages
Japanese (ja)
Other versions
JPS6369746A (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 JP21507386A priority Critical patent/JPH0729842B2/en
Priority to US07/004,054 priority patent/US4764102A/en
Priority to EP87100639A priority patent/EP0242503B1/en
Priority to DE8787100639T priority patent/DE3774751D1/en
Priority to NZ218984A priority patent/NZ218984A/en
Priority to CA000527651A priority patent/CA1296510C/en
Publication of JPS6369746A publication Critical patent/JPS6369746A/en
Publication of JPH0729842B2 publication Critical patent/JPH0729842B2/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する原料を所定形状で連続して
押し出された粘土成形体を押出速度で、かつスムーズに
マイクロ波加熱機に送給して粘土成形体を約5〜30分間
位の短時間の間に水分を第1次乾燥で約5〜10%も低減
させ無理なく次工程に搬送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 provides a clay molded body obtained by continuously extruding a raw material containing clay as a main component in a predetermined shape into a microwave heating machine at an extrusion speed and smoothly. A rapid drying device for clay compacts that can be fed to the next process without excessively reducing the water content by 5-10% in the first drying in a short time of about 5 to 30 minutes. It is about.

〔従来の技術〕[Conventional technology]

一般に、粘土を用いた内、外装材、屋根材は所定形状で
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た構造の乾燥
装置に運搬し、この装置で約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となっていた。
Generally, clay is used to extrude interior and exterior materials and roofing materials in a predetermined shape, and immediately cut this into a short length, for example, 10 to 30 cm in length, and dry this structure using the waste heat of the firing furnace. Transport it to the device and use this device to remove water for 1 to 3 days.
It was reduced to 0% and 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]

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押出直後で
は柔らかく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、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℃位までに昇温することができず水分を1%以下
に乾燥させることができなかった。また、遠赤外線ヒー
タ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13
0℃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が高
いので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%位収縮した寸法差を吸
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。
A conventional clay molded body drying apparatus not only takes several days to dry, but especially a clay molded body longer than before can be transported immediately after extrusion without using an underlay plate,
It was inferior in productivity, increased costs, and required a vast site. Furthermore, in the conventional drying device that heats and dries the surface, if the drying time is shortened by 1 day, the surface layer will be dried first and the inside will not be dried, so the steam inside will cause roof tiles, tiles, and outer wall materials to dry. Twisting, cracking, and breakage occurred, and shortening the drying time was extremely difficult. 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, although the former microwave heater can reduce the water content of clay in a short time, the material to be dried cannot be heated up to about 130 ° C. and the water content cannot be dried to 1% or less. Further, the far infrared heater requires a longer drying time than the microwave, and
Although the heating zone is longer than the microwave,
The temperature could be raised to 0 ° C. Therefore, both heating devices have merits and demerits, and there is a disadvantage that they are not put into practical use. Further, since the energy is high when heated by microwaves, a large amount of water vapor fills the heating zone, and there are disadvantages such as dew condensation on the surface of the object to be heated, the inner wall of the heating zone, and delay of drying time. Moreover, since the heating zone of the microwave heating device conveys the object to be heated by the drive belt, the soft object to be heated contracts about 10% during conveyance and cannot absorb the dimensional difference. However, there is a defect that the object to be heated is deformed, warped, cracked, or broken due to the frictional resistance.

〔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
押出口の次にフリローラ、駆動ベルトコンベアからなる
移送機を介してマイクロ波加熱機に送給し、押出成形体
をその状態でマイクロ波加熱機を経て次工程に搬送する
ように構成し、押し出し、第1次乾燥をスムーズに、か
つ連続押し出し、連続乾燥を変形、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
縮をも吸収して次工程に搬送できると共に、第1次乾燥
を5〜30分間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 a defect, the present invention sends the extruded product to a microwave heating device through a transfer device consisting of a fli roller and a driving belt conveyor next to the extrusion port of the extrusion device, and the extruded product in that state It is constructed so that it can be conveyed to the next step through a wave heater, and extrusion and primary drying are smoothly and continuously extruded, continuous drying is free from deformation, warpage, twisting, cracking, and moreover The present invention proposes a rapid drying device for a clay molded body, which can absorb the volume shrinkage of about% and can be conveyed to the next step, and can achieve the primary drying in 5 to 30 minutes.

〔実施例〕〔Example〕

以下、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。は移送機でフリローラ3
と駆動ベルトコンベア4の順に配列したものであり、押
出成形機1の出口から送出される押出成形体Aを押出速
度と同じ速度で、かつ上記出口の延長線上で柔らかい押
出成形体Aを反り、捩じれ等の変形もなくスムーズに連
続して次工程に搬送するのに役立つものである。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出された押出部の重
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。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、数秒から数分で発熱して粘土
内の水分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C′が大量に、短時間の間に放
出するのを入口、出口11a、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、より乾短時間を短縮するのに役立つものであ
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. 2 is a transfer machine
And the driving belt conveyor 4 are arranged in this order, and the extruded product A sent from the exit of the extruder 1 is warped at the same speed as the extrusion speed and on the extension line of the exit. It is useful for smoothly and continuously carrying to the next process without deformation such as twisting. 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 somewhat harder than when extruded at a position about 0.5 to 2 m away from the outlet, and at the time of extruding. In order to prevent the above-mentioned force from being compressed due to the weight of the extruded portion which has been extruded first and thus preventing it from shrinking, the extruded product A is continuously transferred to the next step at substantially the same speed as during extrusion. . Reference numeral 5 denotes a microwave heater, which has an oven continuous system structure and mainly penetrates into the inside of the extruded body A so that the microwave B does not require much time for heat conduction.
Is converted into heat energy, and heat is generated in a few seconds to a few minutes to evaporate 5 to 10% by weight of water in the clay. In addition, the moisture content of the extrusion molded body A is 22 to 20% by weight.
It is contained in about 15%, and 5 to 10% of it is evaporated. In particular, this type of extruded product A has a water content of 5
The volume shrinks up to about 8%, but the volume does not shrink when the water content is less than that. Therefore, the microwave heater 5 will be described in detail. A microwave guide 5 for guiding the microwave B oscillated from a microwave oscillator (not shown) to a required location and a reflector 7 for reflecting the guided microwave B are provided. Conveyance part 10 consisting of rotary blade 8 for stirring reflected microwave B and frill roller 9 for moving extruded body A at the extruding speed and serves as an inlet and an outlet of extruded body A, and the microwave does not leak to the outside. And the air supply port 14 for guiding the air C to the heated space 13 and the surrounding body 15 so that the microwave B does not leak from the heated space 13 to the outside. It is a thing. 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. Further, the conveying unit 10 is about 1
Since the volume shrinks by about 10%,
It is absorbed by. Further, the air supply port 14 releases a large amount of water vapor C'in a short time by heating the microwave B to the outside through the inlets, outlets 11a and 12a, and the surface of the extrusion molded body A and the enclosure. Prevents dew condensation on the inner walls of 15 to prevent adverse effects (cracks, explosions) during drying,
In addition, the steam on the surface of the extruded product A is constantly blown off by the wind to help shorten the drying time.

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、
その出口の延長線上には移送機を設置し、次にマイク
ロ波加熱機を配列すると共に、搬送部10を移送機
延長線上、すなわち押出成形機1の出口からマイクロ波
加熱機の出口を同一パスラインとしたものである。マ
イクロ波加熱機としては、周波数2450MHz、出力5kw、
被加熱空間13の長さは3mとし、エア等Cを被加熱空間13
に大量に包囲体15のエア供給口14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C′を低下させ、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る。なお、マイクロ波加熱機では
押出成形体Aの水分18%(重量%)を5%(重量%)ま
で蒸発させ、残りの水分を図示しない遠赤外線ヒータで
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
加熱機に送給され、マイクロ波加熱機内の搬送部10
のフリローラ9で水分蒸発時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は移送機を介してマイクロ波加熱機にスムーズ
にそのまま押出速度で送給する。そしてマイクロ波加熱
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12aから次
工程のヒータ(図示しない)へ送給し、ヒータで水分を
1%(重量比)に約10分間で蒸発させ乾燥させるように
した。その結果、押出成形機1の出口からマイクロ波加
熱機の出口12aを、連続帯とした押出成形体Aを約15
〜20分で半乾燥体として次工程に送出できた。
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. Also,
The transfer machine 2 is installed on the extension line of the outlet, and then the microwave heater 5 is arranged, and the transfer unit 10 is installed on the extension line of the transfer machine 2 , that is, from the exit of the extrusion molding machine 1 to the microwave heater 5. The exit is the same pass line. The microwave heater 5 has a frequency of 2450 MHz, an output of 5 kw,
The length of the heated space 13 is 3 m, and air C etc.
A large amount of water is supplied from the air supply port 14 of the enclosure 15, and the water vapor C'generated during heating is discharged to the outside from the inlets / outlets 11a, 12a to lower the water vapor C'in the heated space 13, The heating object and the inner wall of the enclosure 15 are configured to prevent dew condensation water from being generated. 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 a far infrared heater (not shown). Further, the extrusion speed of the extruder 1 is 300 to 1000 mm / min, and here it is 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 fed to the microwave heater 5 by the driving belt at the same extrusion speed of the extruder 1. , The transfer part 10 in the microwave heater 5
The frill roller 9 is configured to absorb the difference in speed due to the volume contraction that occurs when water is evaporated. Therefore, the clay supplied to the extruder 1 is discharged from its outlet as shown in FIG. 2 (g).
It is delivered in a continuum of the cross section shown in. The extruded product A sent out is smoothly sent as it is at the extrusion speed to the microwave heater 5 via the transfer device 2 . Then, while passing through the heated space 13 of the microwave heater 5 , the moisture of the extruded product A is reduced to 5%.
% (Weight ratio) is reduced in 5 minutes, and it is fed from the outlet 12a to a heater (not shown) in the next step, and the heater evaporates water to 1% (weight ratio) in about 10 minutes to dry it. did. As a result, the extrusion molded body A in which the outlet 12a of the microwave heating machine 5 is made into a continuous strip from the outlet of the extrusion molding machine 1 is about 15
It could be delivered to the next step as a semi-dried product in about 20 minutes.

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)において二点鎖線
で示す位置にヒータ付の送風機回路を設け、エア供給口
14を必要により除去することもできる。
What has been described above is only one example of the quick-drying device for a clay molded body according to the present invention. A blower circuit with a heater is provided at a position indicated by a chain double-dashed line in FIG.
14 can be removed if necessary.

〔発明の効果〕〔The invention's effect〕

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)含有した押出成
形体を押出成形機の出口から柔らかい連続した押出成形
体をスムーズに変形なくマイクロ波加熱機(一次乾燥
機)に送給し、かつマイクロ波加熱機では乾燥時の押出
成形体の体積収縮を押出成形体に悪影響を与えずに吸収
して次工程に送給でき、かつ乾燥時間を従前の1/100〜1
/300に短縮した特徴がある。さらに、本発明では押し出
しから乾燥までを直線状に配列したため、長尺体をスム
ーズに半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, an extruded molded body containing 22 to 15% (weight ratio) of water can be smoothly formed into a soft continuous extruded molded body from the outlet of the extruder. It is sent to the microwave heater (primary dryer) without deformation, and the microwave heater absorbs the volume shrinkage of the extruded product during drying without adversely affecting the extruded product and sends it to the next process. The drying time is 1/100 to 1
/ 300 has a shortened feature. Further, in the present invention, since the process from extrusion to drying is linearly arranged, the long body can be smoothly semi-dried.

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

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、……移送機、……マイクロ波加
熱機。
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, 2 ... Transfer machine, 5 ... Microwave heating machine.

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
体の水分を短時間に低減するオーブン連続方式のマイク
ロ波加熱機間にフリローラと押出成形体の押出速度とほ
ぼ同調した速度で回転する駆動ベルトコンベアとからな
る移送機を前記押出成形機−マイクロ波加熱機間のパス
ラインと同一ラインに設け、また前記マイクロ波加熱機
の搬送部をフリローラ構造で、かつマイクロ波加熱ゾー
ン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. Between an extruder for extruding a raw material containing clay as a main material in a predetermined shape and an oven continuous microwave heater for reducing the water content of an extruded product delivered from the extruder in a short time. In addition, a transfer machine consisting of a fli roller and a drive belt conveyor that rotates at a speed substantially synchronized with the extrusion speed of the extrusion-molded body is provided on the same line as the pass line between the extrusion-molding machine and the microwave heater, and the microwave heating is performed. A quick-drying device for a clay molded body, characterized in that a conveying section of the machine has a free-roller structure and an air supply port is provided in a microwave heating zone.
JP21507386A 1986-04-22 1986-09-11 Rapid drying equipment for clay compacts Expired - Lifetime JPH0729842B2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP21507386A JPH0729842B2 (en) 1986-09-11 1986-09-11 Rapid drying equipment for clay compacts
US07/004,054 US4764102A (en) 1986-04-22 1987-01-16 Continuous elongate ceramic article manufacturing system
EP87100639A EP0242503B1 (en) 1986-04-22 1987-01-19 Continuous elongate ceramic article manufacturing system
DE8787100639T DE3774751D1 (en) 1986-04-22 1987-01-19 SYSTEM FOR PRODUCING CONTINUOUS LONG CERAMIC OBJECTS.
NZ218984A NZ218984A (en) 1986-04-22 1987-01-20 Extruding continuous elongate ceramic article
CA000527651A CA1296510C (en) 1986-04-22 1987-01-20 Continuous elongate ceramic article manufacturing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21507386A JPH0729842B2 (en) 1986-09-11 1986-09-11 Rapid drying equipment for clay compacts

Publications (2)

Publication Number Publication Date
JPS6369746A JPS6369746A (en) 1988-03-29
JPH0729842B2 true JPH0729842B2 (en) 1995-04-05

Family

ID=16666305

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21507386A Expired - Lifetime JPH0729842B2 (en) 1986-04-22 1986-09-11 Rapid drying equipment for clay compacts

Country Status (1)

Country Link
JP (1) JPH0729842B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1017677A (en) * 1996-07-04 1998-01-20 Akebono Brake Ind Co Ltd Production of nonasbestine friction material

Also Published As

Publication number Publication date
JPS6369746A (en) 1988-03-29

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