JPS61204033A - Granulating method for powder of inorganic raw material - Google Patents

Granulating method for powder of inorganic raw material

Info

Publication number
JPS61204033A
JPS61204033A JP4351785A JP4351785A JPS61204033A JP S61204033 A JPS61204033 A JP S61204033A JP 4351785 A JP4351785 A JP 4351785A JP 4351785 A JP4351785 A JP 4351785A JP S61204033 A JPS61204033 A JP S61204033A
Authority
JP
Japan
Prior art keywords
oil
water
spherical
raw material
reaction product
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP4351785A
Other languages
Japanese (ja)
Other versions
JPH0339962B2 (en
Inventor
Migiwa Ando
安藤 汀
Takashi Kato
隆史 加藤
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.)
Niterra Co Ltd
Original Assignee
NGK Spark Plug Co Ltd
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 NGK Spark Plug Co Ltd filed Critical NGK Spark Plug Co Ltd
Priority to JP4351785A priority Critical patent/JPS61204033A/en
Publication of JPS61204033A publication Critical patent/JPS61204033A/en
Publication of JPH0339962B2 publication Critical patent/JPH0339962B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/14Methods for preparing oxides or hydroxides in general
    • C01B13/32Methods for preparing oxides or hydroxides in general by oxidation or hydrolysis of elements or compounds in the liquid or solid state or in non-aqueous solution, e.g. sol-gel process
    • C01B13/328Methods for preparing oxides or hydroxides in general by oxidation or hydrolysis of elements or compounds in the liquid or solid state or in non-aqueous solution, e.g. sol-gel process by processes making use of emulsions, e.g. the kerosine process

Abstract

PURPOSE:To form the spherical granulated grains excellent in fluidity by dissolving or dispersing a metal alkoxide in the oil emulsified with water, preparing an oily slurry contg. a spherical structural material of the reaction product and thereafter removing the oil therefrom. CONSTITUTION:One and more kinds of metal alkoxides are dissolved or dis persed in the oil emulsified with water and an oily slurry contg. a spherical structural material of the following reaction product is prepared. The reaction product is obtained by hydrolyzing the metal alkoxides with water. Then the oil is removed form this slurry and the powder of an inorganic raw material is granulated. By this method, since the grains are spherical and excellent in the fluidity and also breakable, the dense product can be obtained by increasing the packing density in the press molding. Still more an organic solvent hard- soluble in water such as higher alcohol, ketone and turpentine oil other than gas oil can be used as the oil.

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は各種無機質材料焼結体の製造工程中プレス作業
における加工性に優れた原料粉末の造粒法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to a method for granulating raw material powder that has excellent workability in pressing operations during the manufacturing process of various inorganic material sintered bodies.

「従来の技術」 この種の原料粉末の造粒法として、一旦スラリーとした
原料粉末を噴霧乾燥によって顆粒状に造粒する噴霧乾燥
法が広く実用されている。
"Prior Art" As a method for granulating this type of raw material powder, a spray drying method is widely used in which raw material powder, which has been made into a slurry, is granulated into granules by spray drying.

「発明が解決しようとする問題点」 上記の噴霧乾燥によって造粒された顆粒は球状を呈し、
型内における流動性が高く、充填密度も大きいが、顆粒
は乾燥に際し有機質結合剤によって一次粒子の凝集によ
って形成されるものであるから本質的に固く、プレス成
型に際して潰れ難い不満があった。
"Problem to be solved by the invention" The granules granulated by the above spray drying have a spherical shape,
Although the fluidity in the mold is high and the packing density is high, since the granules are formed by agglomeration of primary particles by an organic binder during drying, they are essentially hard and difficult to crush during press molding.

「問題点を解決するための手段」 水を乳化させた油中に、1種以上の金属アルコキシドを
加え、これを上記の水によって加水反応させた後、反応
生成物を油と分離して取出す。
"Means for solving the problem" One or more metal alkoxides are added to oil that has been emulsified with water, and this is subjected to a hydrolysis reaction with the above water, and then the reaction product is separated from the oil and taken out. .

[作用] 上記の水を乳化させた油系のスラリー中の金属アルコキ
シドは油と水の界面において加水分解を生じ、油よりも
高い水の表面張力によって球状の反応生成物を形成する
ので、油系のスラリーから油を取除くことによって、上
記の球状の反応生成物を取出すことができる。
[Function] The metal alkoxides in the oil-based slurry emulsified with water undergo hydrolysis at the oil-water interface and form spherical reaction products due to the surface tension of water, which is higher than that of oil. By removing the oil from the slurry of the system, the spherical reaction products described above can be removed.

「発明の効果」 本発明は以上の通シ、金属アルコキシドの加水分解によ
って球状の反応生成物を造粒するものであるから、従来
の噴霧乾燥における粒子間を結合する有機質粘結剤の加
熱、硬化によって得られる硬い顆粒と異なシ、流動性の
よい球状を呈し、しかも潰れ易いからプレス成形におい
て充填密度を高め、緻密な製品を得ることができる。
"Effects of the Invention" As described above, the present invention is to granulate a spherical reaction product by hydrolysis of a metal alkoxide. Unlike the hard granules obtained by hardening, they have a spherical shape with good fluidity and are easily crushed, so they can increase the packing density in press molding and produce dense products.

「実施例」 軽油500mΩに、有機質粘結剤としてポリビニルアル
コール1.51を溶解した水toomΩを混合、マグネ
チックスターラ1800RPMによって攪拌、乳化分散
させW10エマルジョンとする。
"Example" 500 mΩ of light oil and 1.51 mΩ of water dissolved in polyvinyl alcohol as an organic binder were mixed, stirred with a magnetic stirrer at 1800 RPM, and emulsified and dispersed to form a W10 emulsion.

乳化された水粒子の平均粒径は20μであった。The average particle size of the emulsified water particles was 20μ.

上記マグネチックスターラの攪拌を60 ORPMに落
とし、ムライト(:1lA1z03・2SiO2)組成
が得られるように秤量したアルミニウムアルコキシド(
アルミニウムイソプロポキシド・〔A1(OC3臣)3
〕・試薬) 144Fと、シリコンアルコキシド(テト
ラメトキシシラン・〔5i(OCH3)4〕・試薬)3
61を溶解、分散させる。
The agitation of the magnetic stirrer was reduced to 60 ORPM, and aluminum alkoxide (
Aluminum isopropoxide [A1 (OC3 minister) 3
]・Reagent) 144F and silicon alkoxide (tetramethoxysilane・[5i(OCH3)4]・Reagent) 3
61 is dissolved and dispersed.

約80分間の攪拌によって油と水の界面において生成さ
れたアルコキシドの加水分解反応によるAI(OH)s
とS i (CH)4の混合物で粒径的30μの水を含
む球状構造体を含む油系のスラリーが得られた。
AI(OH)s due to the hydrolysis reaction of alkoxides generated at the oil-water interface by stirring for about 80 minutes
An oil-based slurry containing water-containing spherical structures with a particle size of 30 μm was obtained from a mixture of S i (CH)4 and S i (CH)4.

得られた油系のスラリーを、軽油が凍結せずに液状を保
つ零下約15℃の冷凍庫において上記の水を含む球状構
造体を凍結し、これを350メツシユの篩を通して軽油
を流下させて凍結した球状構造体を取出し、約1時間の
冷凍乾燥(装置:東京理化器械株式会社・真空度0.2
mmH?、)によって内部の水分を蒸発、揮散させ、粒
径的25μの球状構造体を維持し、しかも潰れ易く充填
性の高いムライト組成の顆粒状原料粉末を得た。
The obtained oil-based slurry is frozen by freezing the above-mentioned water-containing spherical structure in a freezer at about 15 degrees Celsius below zero, where the light oil remains liquid without freezing, and then passing the light oil through a 350-mesh sieve and freezing it. The spherical structure was taken out and freeze-dried for about 1 hour (equipment: Tokyo Rikakikai Co., Ltd., vacuum degree 0.2).
mmH? ) to evaporate and volatilize the internal moisture to obtain a granular raw material powder with a mullite composition that maintains a spherical structure with a particle size of 25 μm and is easily crushed and has a high filling property.

次に最終生成物として同じくムライト (8A120!・2SiO2)組成を呈するよう、平均
粒径0.5μ、純度約99.5チのアルミナ(RC−H
P−DBM・レイノルズ社) 86(lと、平均粒径0
.8μ、純度約99.2%の無水硅酸(SP−8・雪印
) 140Fを有機質粘結剤ポリビニルアルコール1.
51及び水soomnと混合、15mφアルミナ球石2
胸と共に内容積2ρのボールミルに入れ、84RPM、
48時間混合、粉砕し、得られたスラリーをガス温度1
70℃、アトマイザ径110wφ、 7200RPM 
、毎秒5mflの条件で噴霧乾燥を行ない、平均粒径5
0μの従来法による顆粒に造粒した。
Next, alumina (RC-H
P-DBM/Reynolds) 86 (l and average particle size 0
.. 8μ, approximately 99.2% purity silicic anhydride (SP-8, Snow Brand) 140F, organic binder polyvinyl alcohol 1.
51 and mixed with water soomn, 15mφ alumina ball 2
Put it together with the chest in a ball mill with an internal volume of 2ρ, 84 RPM,
Mix and grind for 48 hours, and the resulting slurry at a gas temperature of 1
70℃, atomizer diameter 110wφ, 7200RPM
, Spray drying was carried out under the conditions of 5 mfl/sec, and the average particle size was 5.
It was granulated into 0μ conventional granules.

このようにして造粒した2種類の顆粒状原料粉末を15
00〜/dの金型プレスによって18.5 X5.5X
54mmの板状素体各5個を製作し、電気炉によって焼
成した試料の緒特性について比較した結果(平均値)を
示す。
The two types of granular raw material powders granulated in this way were
18.5X5.5X by mold press of 00~/d
The results (average values) are shown in which five 54 mm plate-like bodies were manufactured and the properties of samples fired in an electric furnace were compared.

上表から本発明により造粒された原料粉末を使用した試
料は、従来の噴霧乾燥によって造粒し、た原料粉末を使
用した試料に比して著しく焼結温度を低下し、しかも密
度、抗折力等を大巾に高めることが明らかにされた。
From the table above, the samples using the raw material powder granulated according to the present invention have a significantly lower sintering temperature than the samples using the raw material powder granulated by conventional spray drying, and have lower density and resistance. It has been revealed that it greatly increases the strength and strength.

なお、上記実施例はムライト組成の原料粉末を対象とし
てAIとSiのアルコキシドを用いたが、Ca 1Mg
 r Zr r Sr r Be等のアルコキシドを使
用してフォルステライト組成2Mg0−8io2の如き
2成分系、あるいは8成分系のコージライト組成2Mg
0・2A1203・5SiO2等、更には極めて微量の
鉱化剤を含む高純度アルミナ磁器等を対象として効果を
奏する。
In the above example, AI and Si alkoxides were used for the raw material powder having a mullite composition, but Ca 1Mg
r Zr r Sr r Using alkoxides such as Be, forsterite composition 2Mg0-8io2 or 8-component cordierite composition 2Mg
It is effective for 0.2A1203.5SiO2, etc., and also for high-purity alumina porcelain containing extremely small amounts of mineralizing agents.

次に上記実施例において、最初のW10エマルジョンを
生成するに際して有機質粘結剤を溶解した水を直接、軽
油に混合して攪拌したが、有機質粘結剤は必ずしも必要
ではなく、該軽油に対し、油中に水を乳化するためHL
B価6以下の乳化剤、又は滑石粉末等の固形乳化剤の少
量、前者液体の場合は油に対して8%以下、後者固形の
場合は5チ以下の配合が好ま・しく、また、金属アルコ
キシドは上記の生成したW10エマルジョンに対して添
加したが予め軽油中に溶解、分散させてもよく、ここで
本発明にいう油は軽油に限らず高級アルコール、ケトン
、テレピン油等の水と難溶性の有機質溶剤をいうもので
ある。
Next, in the above example, when producing the first W10 emulsion, the water in which the organic binder was dissolved was directly mixed with light oil and stirred, but the organic binder was not necessarily necessary, and HL to emulsify water in oil
It is preferable to mix a small amount of an emulsifier with a B value of 6 or less, or a solid emulsifier such as talcum powder, in the case of the former liquid, 8% or less based on the oil, and in the case of the latter solid, 5% or less, and metal alkoxides Although it was added to the W10 emulsion produced above, it may be dissolved or dispersed in light oil in advance, and the oil referred to in the present invention is not limited to light oil, but also includes higher alcohols, ketones, turpentine, etc. that are poorly soluble in water. It refers to an organic solvent.

また、金属アルコキシドの加水分解による生成物を取出
す手段として、該生成物を凍結して機械的強度を付与し
たが、有機質粘結剤によって上記生成物に必要な微粒子
間の結合強度が得られるときは常温において油を篩通し
することもでき、散出した上記生成物が有機質粘結剤を
含むときは冷凍乾燥が微粒子間の結合強度を高めず、か
つプレス成形密度を上昇させる理由から好ましいが乾燥
方法はこれに限定するものではない。
In addition, as a means of extracting the product of hydrolysis of metal alkoxide, the product is frozen to give it mechanical strength. It is also possible to pass the oil through a sieve at room temperature, and when the dispersed product contains an organic binder, freeze-drying is preferred because it does not increase the bond strength between fine particles and increases the press-molding density. The drying method is not limited to this.

しかして、本発明における必須成分の内、まず水は金属
アルコキシドを加水分解するに必要な量として、例えば
実施例のアルミニウムインプロキシド1七ルチに対して
最少3モルチ、テトラメトキシシラン1モルチに対して
は最少4モルチとそれらの化学式から計算され、かつ水
(金属アルコキシドを含む)が油に完全に乳化されるた
めには容量比で油の70チ以下にする必要がある。
Therefore, among the essential components in the present invention, water is used in an amount necessary to hydrolyze the metal alkoxide, for example, a minimum of 3 molty per 17 mol of aluminum improxide in the example, and 1 mol of tetramethoxysilane. It is calculated from their chemical formulas that the minimum amount is 4 mol, and in order for water (including metal alkoxides) to be completely emulsified in oil, the volume ratio needs to be 70 mol or less of oil.

Claims (1)

【特許請求の範囲】[Claims] 水を乳化させた油中に、1種以上の金属アルコキシドを
溶解あるいは分散させ、上記水分によって金属アルコキ
シドを加水分解して得られた反応生成物の球状構造体を
含む油系のスラリーとしたのち、該スラリーから油を除
去することを特徴とした無機質原料粉末の造粒法。
One or more metal alkoxides are dissolved or dispersed in an oil emulsified with water to form an oil-based slurry containing spherical structures of reaction products obtained by hydrolyzing the metal alkoxides with the water. , a method for granulating inorganic raw material powder, characterized by removing oil from the slurry.
JP4351785A 1985-03-05 1985-03-05 Granulating method for powder of inorganic raw material Granted JPS61204033A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4351785A JPS61204033A (en) 1985-03-05 1985-03-05 Granulating method for powder of inorganic raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4351785A JPS61204033A (en) 1985-03-05 1985-03-05 Granulating method for powder of inorganic raw material

Publications (2)

Publication Number Publication Date
JPS61204033A true JPS61204033A (en) 1986-09-10
JPH0339962B2 JPH0339962B2 (en) 1991-06-17

Family

ID=12665934

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4351785A Granted JPS61204033A (en) 1985-03-05 1985-03-05 Granulating method for powder of inorganic raw material

Country Status (1)

Country Link
JP (1) JPS61204033A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2621030A1 (en) * 1987-09-29 1989-03-31 Centre Nat Rech Scient PROCESS FOR THE PREPARATION OF METAL OXIDES
EP0363926A2 (en) * 1988-10-12 1990-04-18 Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. Particulate polycondensates, process for their preparation and use thereof
JPH02277481A (en) * 1989-04-20 1990-11-14 Daiichi Shokai:Kk Prize winning controlling method for pin ball machine
AU608352B2 (en) * 1987-08-19 1991-03-28 Alcan International Limited Production of precursor powders for ceramic materials by emulsion precipitation processes and the products thereof
JP2011093798A (en) * 2010-12-14 2011-05-12 Asahi Glass Co Ltd Method for producing inorganic spherical body
JP2020055702A (en) * 2018-09-28 2020-04-09 日揮触媒化成株式会社 Method for producing spherical particles

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59182237A (en) * 1983-03-31 1984-10-17 Shimadzu Corp Manufacture of spherical glass article

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59182237A (en) * 1983-03-31 1984-10-17 Shimadzu Corp Manufacture of spherical glass article

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU608352B2 (en) * 1987-08-19 1991-03-28 Alcan International Limited Production of precursor powders for ceramic materials by emulsion precipitation processes and the products thereof
FR2621030A1 (en) * 1987-09-29 1989-03-31 Centre Nat Rech Scient PROCESS FOR THE PREPARATION OF METAL OXIDES
US5112676A (en) * 1987-09-29 1992-05-12 Centre National De La Recherche Scientifique 'cnrs Method for the preparation of metallic oxide coatings
EP0363926A2 (en) * 1988-10-12 1990-04-18 Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. Particulate polycondensates, process for their preparation and use thereof
JPH02277481A (en) * 1989-04-20 1990-11-14 Daiichi Shokai:Kk Prize winning controlling method for pin ball machine
JP2011093798A (en) * 2010-12-14 2011-05-12 Asahi Glass Co Ltd Method for producing inorganic spherical body
JP2020055702A (en) * 2018-09-28 2020-04-09 日揮触媒化成株式会社 Method for producing spherical particles

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JPH0339962B2 (en) 1991-06-17

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