Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH082418B2 - Granulation method for inorganic granular raw material for ceramic industry - Google Patents
[go: Go Back, main page]

JPH082418B2 - Granulation method for inorganic granular raw material for ceramic industry - Google Patents

Granulation method for inorganic granular raw material for ceramic industry

Info

Publication number
JPH082418B2
JPH082418B2 JP63318935A JP31893588A JPH082418B2 JP H082418 B2 JPH082418 B2 JP H082418B2 JP 63318935 A JP63318935 A JP 63318935A JP 31893588 A JP31893588 A JP 31893588A JP H082418 B2 JPH082418 B2 JP H082418B2
Authority
JP
Japan
Prior art keywords
ceramics
inorganic
raw material
clay
inorganic clay
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
JP63318935A
Other languages
Japanese (ja)
Other versions
JPH02164431A (en
Inventor
志郎 谷口
Original Assignee
瀬戸製土株式会社
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 瀬戸製土株式会社 filed Critical 瀬戸製土株式会社
Priority to JP63318935A priority Critical patent/JPH082418B2/en
Publication of JPH02164431A publication Critical patent/JPH02164431A/en
Publication of JPH082418B2 publication Critical patent/JPH082418B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Glanulating (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、タイルなどの窯業製品用の粒状原料を得
るための造粒方法の改良に関する。
TECHNICAL FIELD The present invention relates to an improvement in a granulation method for obtaining a granular raw material for ceramic products such as tiles.

更にくわしく説明すれば、タイルなどの窯業製品を製
造するに際してその無機質粒状原料は成形後に焼成され
ることは広く知られるとおりである。
More specifically, it is widely known that when manufacturing ceramic products such as tiles, the inorganic granular raw material is fired after molding.

従って、その原料は嵩密度が高く、収縮率の低いもの
が要求されるから、この発明はこの条件を満足する原料
の造粒方法に関する。
Therefore, since the raw material is required to have a high bulk density and a low shrinkage rate, the present invention relates to a method for granulating a raw material satisfying this condition.

〔従来の方法〕[Conventional method]

この種の窯業製品用の粒状原料を得るため、発明者が
経験的に知っている方法はスプレードライヤーにより窯
業製品用の粒状原料を得るための造粒方法である。
In order to obtain a granular raw material for a ceramic product of this kind, the method that the inventor has empirically known is a granulation method for obtaining a granular raw material for a ceramic product by a spray dryer.

この従来方法は、粒子内の組織が均質であることなど
の利点があるため、タイル用の原料として採用されてい
ることを知っている。
It is known that this conventional method is adopted as a raw material for tiles because it has advantages such as a uniform structure in the particles.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

しかし、スプレードライヤーによる造粒方法は造粒時
に粒子の圧縮が実施されない結果、嵩密度の低いもので
ある。
However, the granulation method using a spray dryer has a low bulk density because the particles are not compressed during granulation.

そのため、原料としてタイルなどを圧縮成形した場
合、金型内に原料が付着し易い。そのため再三付着原料
の取り除き作業を必要とする問題点があった。
Therefore, when a tile or the like is compression-molded as a raw material, the raw material easily adheres to the mold. Therefore, there is a problem that it is necessary to repeatedly remove the deposited material.

また、嵩密度が低いため焼成収縮率が大きくなるた
め、圧縮成形して焼成した場合、正規の形態の窯業製品
が得られないという問題点があった。
Further, since the bulk density is low and the firing shrinkage is high, there is a problem that a ceramic product in a regular form cannot be obtained when compression-molding and firing.

更に、圧縮成形する場合に適度の水分を必要とする
が、圧縮成形時の原料に任意の水分を付与させることに
困難性があった。
Furthermore, although a proper amount of water is required for compression molding, it has been difficult to give arbitrary moisture to the raw material during compression molding.

この発明は、上記の問題点を解消しようとするもので
あって、嵩密度の高い窯業用無機質粒状原料を得ること
を目的としており、また、適度の粒径の原料を得るため
の前工程時における圧縮成形の容易性を図るため、原料
の水分の調整を自由に設定することも目的としている。
This invention is intended to solve the above problems, and an object thereof is to obtain an inorganic granular raw material for ceramics having a high bulk density, and at the time of a pre-process for obtaining a raw material having an appropriate particle size. In order to facilitate the compression molding in, the purpose is to freely set the water content of the raw material.

〔課題を解決するための手段〕[Means for solving the problem]

上記の目的を達成するため、この発明は、水分を含有
してなるスラリー状の窯業用無機質坏土を加熱され回転
中のドラムの表面に付着させることにより略完全乾燥さ
せ、略完全乾燥済の窯業用無機質坏土をドラムから剥が
し、その窯業用無機質坏土を混練処理と加湿処理を施
し、ついでその湿潤状態の窯業用無機質坏土を圧縮さ
せ、さらに圧縮した窯業用無機質坏土を粉砕させて適宜
の大きさと形態の窯業用無機質坏土を得た後、これを適
当な大きさの粒状のものとすることを特徴とする窯業用
無機質粒状原料の造粒方法。
In order to achieve the above object, the present invention is a slurry-like inorganic clay for ceramics containing water is heated to be substantially completely dried by adhering to the surface of a rotating drum, which is substantially completely dried. Peel the inorganic clay for ceramics from the drum, knead and humidify the inorganic clay for ceramics, and then compress the wet inorganic clay for ceramics, and further crush the compressed inorganic mineral clay for ceramics. A method for granulating an inorganic granular raw material for ceramics, which comprises obtaining an inorganic kneaded clay for ceramics having an appropriate size and shape, and then making this into a granular material having an appropriate size.

〔実施例〕〔Example〕

この発明の詳細を添付図面を参照して説明する。 The details of the present invention will be described with reference to the accompanying drawings.

ドラムドライヤーは、従来から小型な機構が知られて
おり、液状、ペースト状、泥状の染料、顔料などを乾燥
するに採用されている。
Drum dryers have conventionally been known to have a small mechanism, and are used to dry liquid, paste, and mud dyes, pigments, and the like.

そこで、この発明では、改良された比較的大型のドラ
ムドライヤー10を設け、予め30〜40%程度の比較的多量
の水分を含有してなるスラリー状に処理された窯業用無
機質坏土12をフィードパイプ14を介して一対のドラム16
間の上方に配置された供給槽18へ供給させる。
Therefore, in the present invention, an improved relatively large-sized drum dryer 10 is provided to feed the ceramic inorganic clay 12 previously processed into a slurry containing a relatively large amount of water of about 30 to 40%. A pair of drums 16 via pipes 14
It is supplied to the supply tank 18 arranged above the space.

そして一対のドラム16を互いに外側に向けてゆっくり
回転させる。
Then, the pair of drums 16 are slowly rotated outward from each other.

ドラム16の大きさや形状によって異なるが、一般的に
は毎分1〜4回程度が適当である。
Although it depends on the size and shape of the drum 16, about 1 to 4 times per minute is generally suitable.

ドラム16を外側に向けて回転させることを説明した
が、外側に向けて回転させることにのみ制限する趣旨で
はない。
Although it has been described that the drum 16 is rotated outward, it is not intended to limit the rotation of the drum 16 outward.

しかし、発明者の実験によれば、内側方向へドラム16
を回転させた場合、スラリー状の窯業用無機質坏土を乾
燥するに際して乾燥処理量が効率的でないことが判明し
た。
However, according to an experiment by the inventor, the drum 16 is inwardly moved.
It was found that when the slurry was rotated, the drying treatment amount was not efficient when the slurry-like inorganic clay for ceramics was dried.

よって、乾燥処理量を特に考慮すれば、好ましくはド
ラム16を外側に向けて回転させることがよい。
Therefore, it is preferable to rotate the drum 16 toward the outside, especially when the dry processing amount is taken into consideration.

前記したスラリー状の窯業用無機質坏土12を供給槽18
から一対のドラム16間に供給させる。
Supply tank 18 for the above-mentioned slurry-like inorganic clay for ceramics 12
To be supplied between the pair of drums 16.

かくして、窯業用無機質坏土12は水分を有するもの
の、加熱された回転するドラム16によりドラム16の表面
に付着した窯業用無機質坏土12は徐々に乾燥され、薄い
被膜状態となる。
Thus, although the ceramic inorganic clay 12 has water, the ceramic inorganic clay 12 adhered to the surface of the drum 16 by the heated rotating drum 16 is gradually dried and becomes a thin film state.

その際、ドラム16をゆっくり回転させつつ蒸気などに
より加熱させることによって、ドラム16の表面に付着さ
れた窯業用無機質坏土を乾燥させる。
At this time, the drum 16 is slowly rotated and heated by steam or the like to dry the inorganic clay for ceramics attached to the surface of the drum 16.

かくしてフィルム状の窯業用無機質坏土は、含水率0.
33〜0.60%程度に乾燥される。
Thus, the film-like inorganic clay for ceramics has a water content of 0.
It is dried to about 33 to 0.60%.

そこで、ドラム16に付着しているフィルム状の窯業用
無機質坏土をドラム16の表面からナイフ20により掻取
り、ドラム16の下方に配設された格納箱22へ落下させ
る。
Therefore, the film-shaped inorganic clay for ceramics adhering to the drum 16 is scraped off from the surface of the drum 16 by the knife 20 and dropped into the storage box 22 arranged below the drum 16.

この掻取られた乾燥済み窯業用無機質坏土24は、その
形態と大きさは当然のことながらばらつきの多いもので
あって、かつ水分を前記したとおりほとんど含有しない
ものである。
The scraped-out dried inorganic clay for ceramics 24 naturally has many variations in shape and size, and contains almost no water as described above.

従って、このままの状態では次工程において圧縮成形
できないから、圧縮成形し易くするために混練機26内に
乾燥済み窯業用無機質坏土24を投入させ、適度の水分例
えば5〜11%程度を供給させる。
Therefore, in this state as it is, compression molding cannot be carried out in the next step. Therefore, in order to facilitate compression molding, the dried ceramic inorganic clay 24 is put into the kneading machine 26, and an appropriate amount of water, for example, 5 to 11% is supplied. .

この乾燥済み窯業用無機質坏土は、単に物理的に不規
則な形態に乾燥されるから、従来のスプレードライヤー
による造粒方法では、その造粒物が中空体として成形さ
れる結果、爾後工程において水分の補給調整が困難とい
う欠点があったが、この発明では前記したとおり、ドラ
ムドライヤー10により乾燥させるため、水分の供給は自
由に実施できる利益がある。
Since this dried inorganic clay for ceramics is simply dried in a physically irregular form, in the conventional spray dryer granulation method, the granulated product is molded as a hollow body, resulting in the subsequent step. Although there is a drawback that it is difficult to adjust the supply of water, the present invention has an advantage that the water can be freely supplied because it is dried by the drum dryer 10 as described above.

かくして乾燥済みの窯業用無機質坏土24は水分を含有
した状態で圧縮成形し易い湿潤状態に変化する。
In this way, the dried inorganic clay for ceramics 24 changes into a wet state in which it is easy to perform compression molding while containing water.

そこで、混練機26から湿潤状態の窯業用無機質坏土28
を取り出して、一定の型30内に収納して圧縮成形するこ
とにより、圧縮成形された窯業用無機質坏土32を得る。
Therefore, from the kneading machine 26, the inorganic clay for ceramics 28 in a wet state
Is taken out, housed in a fixed mold 30, and compression-molded to obtain a compression-molded inorganic clay 32 for ceramics.

この場合、窯業用無機質坏土28を圧縮成形する目的
は、タイルなどの窯業製品用の窯業用無機質粒状原料と
して採用するについて高密度が高く、収縮率の低いもの
を得ることにほかならない。
In this case, the purpose of compression-molding the inorganic clay for ceramics 28 is nothing but to obtain a material having a high density and a low shrinkage rate when used as an inorganic granular raw material for ceramics for ceramic products such as tiles.

そして圧縮成形された窯業用無機質坏土32は当然のこ
とながらそのままでは、タイルなどの窯業製品用の原料
として採用できないから、60〜10メッシュ程度の粒度に
細かくする必要がある。
Naturally, the compression-molded inorganic clay 32 for ceramics cannot be used as it is as a raw material for ceramic products such as tiles, so it is necessary to make it fine to a particle size of about 60 to 10 mesh.

そこで、前記した圧縮成形された窯業用無機質坏土32
をまずネットデシン機などの粉砕機34にかけて粉砕させ
る。
Therefore, the above-described compression molded inorganic clay 32 for ceramics is used.
Is first crushed by a crusher 34 such as a net decine machine.

しかし、粉砕されたこの状態の窯業用無機質坏土は、
未だ粒度にむらが多いから、篩機36にかけて60〜10メッ
シュ程度の粒度になるように篩分ける。
However, the crushed inorganic clay for ceramics in this state is
Since the particle size is still uneven, it is sieved through a sieving machine 36 to obtain a particle size of about 60 to 10 mesh.

かくして、60〜10メッシュ程度の粒度による嵩密度の
高く、収縮率の低いタイルなどの窯業製品用の無機質粒
状原料が得られる。
Thus, an inorganic granular raw material for ceramic products such as tiles having a high bulk density and a low shrinkage rate due to a particle size of about 60 to 10 mesh can be obtained.

〔発明の効果〕〔The invention's effect〕

この発明は、上記の構成であるから以下の利点を奏す
る。
The present invention has the following advantages because of the above configuration.

造粒工程に先立って予め窯業用無機質坏土を略完全乾
燥させる工程を採用しているから、用途に応じて設定し
た必要な水分を正確にかつ簡便に供給できるので、用途
に対応させた水分含有率の無機質粒状原料が得られる。
Since the process of almost completely drying the inorganic clay for ceramics prior to the granulation process is adopted, the required moisture set according to the application can be supplied accurately and simply, so the moisture corresponding to the application can be used. A content of inorganic granular raw material is obtained.

したがって、従来経験しなかった嵩密度が高く、収縮
率の低い窯業用無機質粒状原料を楽に得ることができ
る。
Therefore, it is possible to easily obtain an inorganic granular raw material for ceramics having a high bulk density and a low shrinkage ratio, which has not been experienced in the past.

【図面の簡単な説明】 第1図ないし第6図は、窯業用無機質粒状原料の造粒工
程の概略図で、第1図はドラムドライヤーの断面図、第
2図は、混練機の概略側面図、第3図は、成形型の概略
断面図、第4図は、圧縮成形された窯業用無機質坏土の
概略断面図、第5図は、粉砕機に窯業用無機質坏土を投
入する状態を示す概略側面図、第6図は、篩機の概略側
面図である。 (主要部分の符号の説明) 10……ドラムドライヤー 12……スラリー状の窯業用無機質坏土 24……乾燥済み窯業用無機質坏土 32……圧縮成形された窯業用無機質坏土
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 to FIG. 6 are schematic views of a granulating process of inorganic granular raw materials for ceramics, FIG. 1 is a sectional view of a drum dryer, and FIG. 2 is a schematic side view of a kneader. Fig. 3 is a schematic sectional view of a molding die, Fig. 4 is a schematic sectional view of a compression-molded inorganic clay for ceramics, and Fig. 5 is a state in which the inorganic clay for ceramics is put into a crusher. And FIG. 6 is a schematic side view of the sieving machine. (Explanation of symbols of main parts) 10 …… Drum dryer 12 …… Slurry ceramic inorganic clay 24 …… Dried ceramic inorganic clay 32 …… Compression-molded ceramic inorganic clay

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】水分を含有してなるスラリー状の窯業用無
機質坏土を加熱され回転中のドラムの表面に付着させる
ことにより略完全乾燥させ、 略完全乾燥済の窯業用無機質坏土をドラムから剥がし、 その窯業用無機質坏土を混練処理と加湿処理を施し、 ついでその湿潤状態の窯業用無機質坏土を圧縮させ、 さらに圧縮した窯業用無機質坏土を粉砕させて適宜の大
きさと形態の窯業用無機質坏土を得た後、 これを適当な大きさの粒状のものとすることを特徴とす
る窯業用無機質粒状原料の造粒方法。
1. A ceramic inorganic clay in the form of a slurry containing water is heated to adhere to the surface of a rotating drum to be substantially completely dried, and a substantially completely dried inorganic inorganic clay for ceramics is used as a drum. Peel it off, and subject the inorganic clay for ceramics to kneading and humidification, then compress the inorganic clay for ceramics in the wet state, and crush the compressed inorganic inorganic clay for ceramics to obtain an appropriate size and shape. A method for granulating an inorganic granular raw material for ceramics, which comprises obtaining an inorganic kneaded clay for ceramics, and then making the granular material into an appropriate size.
JP63318935A 1988-12-16 1988-12-16 Granulation method for inorganic granular raw material for ceramic industry Expired - Lifetime JPH082418B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63318935A JPH082418B2 (en) 1988-12-16 1988-12-16 Granulation method for inorganic granular raw material for ceramic industry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63318935A JPH082418B2 (en) 1988-12-16 1988-12-16 Granulation method for inorganic granular raw material for ceramic industry

Publications (2)

Publication Number Publication Date
JPH02164431A JPH02164431A (en) 1990-06-25
JPH082418B2 true JPH082418B2 (en) 1996-01-17

Family

ID=18104630

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63318935A Expired - Lifetime JPH082418B2 (en) 1988-12-16 1988-12-16 Granulation method for inorganic granular raw material for ceramic industry

Country Status (1)

Country Link
JP (1) JPH082418B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH066501B2 (en) * 1990-07-27 1994-01-26 丸美陶料株式会社 Method for manufacturing kneaded clay for tiles
IT1269247B (en) * 1994-08-05 1997-03-26 Manfredini E Schianchi Srl METHOD FOR THE GRANULES AGGROMERATION OF MIXTURES ATOMIZED FOR CERAMIC USE, IN PARTICULAR FOR PORCELAIN STONEWARE, AND RELATED PRODUCT
JP2002283317A (en) * 2001-03-23 2002-10-03 Ngk Insulators Ltd Method of filling powder into mold

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5756370A (en) * 1980-09-17 1982-04-03 Kazuo Takatsu Mosaic dressed body
JPS6033654A (en) * 1983-08-04 1985-02-21 Nec Corp Inter-microprocessor data transferring system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
(社)日本機械学会著「造粒と造粒装置」昭和42年11月20日(社)日本機械学会発行209〜214頁

Also Published As

Publication number Publication date
JPH02164431A (en) 1990-06-25

Similar Documents

Publication Publication Date Title
US4082532A (en) Process for making extruded cattle manure pellets
US4028030A (en) Installation for pelletizing organic waste materials
US2167432A (en) Granulation of nongranular materials
JPH082418B2 (en) Granulation method for inorganic granular raw material for ceramic industry
US4897029A (en) Device for preparing a very homogeneous and finely divided fine-ceramics mass
JPH0618583Y2 (en) Granulator for inorganic granular raw material for ceramic industry
JPH0519072B2 (en)
EP0699640A1 (en) Method for producing granules from ceramic powders, said granules and apparatus for their production
JPS591693Y2 (en) Granulation equipment
RU2803935C1 (en) Method for producing a composite material from municipal solid waste
JP2883883B2 (en) Activated dewatering cake granulator for cement wastewater
JPS6033654B2 (en) Method for producing flat grains for ceramic raw materials
JPS61291031A (en) Preparation of coagulated granular ceramic stock material
JP4258223B2 (en) Quantitative powder supply equipment
CN88101837A (en) Method for granulating lime powder or similar materials
JPS62106B2 (en)
JPH0224581B2 (en)
JPS5921651B2 (en) Granulation method and equipment
JPH0212547B2 (en)
SU601259A1 (en) Method of preparing moulding powder for manufacturing refractories
JPH01234352A (en) Far-infrared radiating sintered body and its production
JPH072036Y2 (en) Granular ceramic raw material manufacturing equipment
JP2898535B2 (en) Granulation of raw materials for ceramics
US3315015A (en) Method for granulating material
SU863643A1 (en) Unit for reducing starch