JPH01153515A - Method for granulating magnesium oxide raw material for forming - Google Patents
Method for granulating magnesium oxide raw material for formingInfo
- Publication number
- JPH01153515A JPH01153515A JP62309314A JP30931487A JPH01153515A JP H01153515 A JPH01153515 A JP H01153515A JP 62309314 A JP62309314 A JP 62309314A JP 30931487 A JP30931487 A JP 30931487A JP H01153515 A JPH01153515 A JP H01153515A
- Authority
- JP
- Japan
- Prior art keywords
- magnesium oxide
- raw material
- powder
- forming
- grain size
- 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
Links
- 238000000034 method Methods 0.000 title claims abstract description 28
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 239000000395 magnesium oxide Substances 0.000 title claims abstract description 26
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 title claims abstract description 23
- 239000002994 raw material Substances 0.000 title claims abstract description 16
- 239000000843 powder Substances 0.000 claims abstract description 25
- 239000011230 binding agent Substances 0.000 claims abstract description 16
- 239000004094 surface-active agent Substances 0.000 claims abstract description 10
- 238000003756 stirring Methods 0.000 claims abstract description 9
- 238000002156 mixing Methods 0.000 claims abstract description 6
- 238000000465 moulding Methods 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 10
- 239000012776 electronic material Substances 0.000 abstract description 4
- 239000008187 granular material Substances 0.000 abstract description 4
- 239000000696 magnetic material Substances 0.000 abstract description 4
- 238000009826 distribution Methods 0.000 abstract description 3
- 229920002037 poly(vinyl butyral) polymer Polymers 0.000 abstract description 3
- 239000002202 Polyethylene glycol Substances 0.000 abstract description 2
- 229920001223 polyethylene glycol Polymers 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- MUHFRORXWCGZGE-KTKRTIGZSA-N 2-hydroxyethyl (z)-octadec-9-enoate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCCO MUHFRORXWCGZGE-KTKRTIGZSA-N 0.000 abstract 1
- 238000001354 calcination Methods 0.000 abstract 1
- 238000009817 primary granulation Methods 0.000 abstract 1
- 238000005469 granulation Methods 0.000 description 13
- 230000003179 granulation Effects 0.000 description 13
- 239000002904 solvent Substances 0.000 description 8
- 235000019441 ethanol Nutrition 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 239000002131 composite material Substances 0.000 description 3
- 238000010304 firing Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002075 main ingredient Substances 0.000 description 2
- 239000011356 non-aqueous organic solvent Substances 0.000 description 2
- 238000001694 spray drying Methods 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野コ
本発明は成形用酸化マグネシウム原料の造粒方法に係り
、特に電子材料及び磁性材料焼成用鞘等の製造に好適な
成形用酸化マグネシウム原料の造粒方法に関する。Detailed Description of the Invention [Industrial Field of Application] The present invention relates to a method for granulating a magnesium oxide raw material for molding, and in particular to a method for granulating a magnesium oxide raw material for molding, which is suitable for producing electronic materials and sheaths for firing magnetic materials. Regarding a granulation method.
[従来の技術]
従来、電子材料や磁性材料の焼成に用いられる酸化マグ
ネシウム製靴等の成形には、主にプレス成形法が採用さ
れている。このプレス成形法に用いられる原料は、酸化
マグネシウムの微粉を造粒したものが用いられており、
その造粒方法は、混合造粒、強制造粒、熱利用型等に分
類され、各々多数の方法が知られている。[Prior Art] Conventionally, a press molding method has been mainly used for molding magnesium oxide shoes and the like used for firing electronic materials and magnetic materials. The raw material used in this press molding method is granulated fine powder of magnesium oxide.
The granulation method is classified into mixed granulation, forced granulation, heat utilization type, etc., and many methods for each are known.
ところで、プレス成形法においては、原料の流動性が得
られる製品の品質を決定する極めて重要な因子となる。By the way, in the press molding method, the fluidity of the raw material is an extremely important factor that determines the quality of the product obtained.
従来、流動性の高い造粒粉を得るためには、専ら噴霧乾
燥造粒法が採用されている。Conventionally, in order to obtain granulated powder with high fluidity, a spray drying granulation method has been exclusively employed.
[発明が解決しようとする問題点]
しかしながら、酸化マグネシウムは水和性を有するため
、噴霧乾燥造粒法においては、スラリー調製用の懸濁溶
媒に非水系有機溶媒を多量に使用しなければならない。[Problems to be solved by the invention] However, since magnesium oxide is hydratable, in the spray drying granulation method, a large amount of non-aqueous organic solvent must be used as a suspending solvent for slurry preparation. .
このため、造粒に要する費用が多額になり、製造コスト
の高騰を招いていた。しかも、非水系有機溶媒は、作業
者への悪影響、環境汚染問題を引き起す可能性があるた
め、その使用は極力避るべきである。For this reason, the cost required for granulation becomes large, leading to a rise in manufacturing costs. Furthermore, the use of non-aqueous organic solvents should be avoided as much as possible since they may have an adverse effect on workers and cause environmental pollution problems.
[問題点を解決するための手段]
本発明の成形用酸化マグネシウム原料の造粒方法は、酸
化マグネシウム粉末を、界面活性剤な含むバインダ溶液
を用いて攪拌混合法により1次造粒した後、解砕法によ
り粒度を揃えることを特徴とする。[Means for Solving the Problems] The method for granulating a magnesium oxide raw material for molding of the present invention involves first granulating magnesium oxide powder by a stirring and mixing method using a binder solution containing a surfactant, and then It is characterized by uniform particle size using a crushing method.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明においては、まず、酸化マグネシウム原料を粉砕
し、好ましくは平均粒径1〜2μm程度の微粉を得る。In the present invention, first, a magnesium oxide raw material is pulverized to obtain a fine powder preferably having an average particle size of about 1 to 2 μm.
これをヘンシェルミキサ等の混合機に、界面活性剤を含
むバインダ溶液と共に投入し、酸化マグネシウム微粉を
バインダ溶液と混合して攪拌混合造粒を行なう。ここで
用いるバインダ溶液は、3.0〜40重量%、特に20
重量%程度のバインダを含有する溶液に対して、1〜6
0重量%重量%界面活性剤を添加したものが好適である
。なお、バインダとしては、一般に、ポリビニルブチラ
ール等が用いられ、その溶媒としてはエチルアルコール
等が用いられる。界面活性剤としてはステアリン酸等が
用いられる。This is put into a mixer such as a Henschel mixer together with a binder solution containing a surfactant, and the fine magnesium oxide powder is mixed with the binder solution and granulated with stirring. The binder solution used here is 3.0 to 40% by weight, especially 20% by weight.
1 to 6% by weight for a solution containing binder.
Preferably, 0% by weight surfactant is added. Note that polyvinyl butyral or the like is generally used as the binder, and ethyl alcohol or the like is used as the solvent. Stearic acid or the like is used as the surfactant.
また、用いるバインダ溶液の量は、酸化マグネシウム微
粉に対する重量割合で5〜15重量%とするのが好まし
い。Further, the amount of the binder solution used is preferably 5 to 15% by weight relative to the magnesium oxide fine powder.
なお、本発明において、混合機としては、ヘンシェルミ
キサの他、ニーダ−、アイリッヒミキサ等を用いること
もできる。In addition, in the present invention, as the mixer, in addition to the Henschel mixer, a kneader, Eirich mixer, etc. can also be used.
次いで、攪拌混合造粒して得られた攪拌造粒物を解砕造
粒機により、ハンマー等の解砕具で粉砕し、スクリーン
を通して粒度を下げ、かつ粒度を。Next, the stirred granules obtained by stirring and granulating are crushed by a crushing tool such as a hammer using a crushing granulator, and passed through a screen to reduce the particle size.
整える。Arrange.
解砕造粒機としては、回転ナイフ(垂直)型、回転ナイ
フ(水平)型、回転バー型等の解砕造粒機を用いること
ができる。As the crushing and granulating machine, a crushing and granulating machine such as a rotating knife (vertical) type, a rotating knife (horizontal) type, and a rotating bar type can be used.
このような本発明の方法によれば、60〜SOOμmの
範囲に粒径分布を有する、流動性に極めて優れた酸化マ
グネシウム造粒粉が得られる。According to such a method of the present invention, a magnesium oxide granulated powder having extremely excellent fluidity and having a particle size distribution in the range of 60 to SOO μm can be obtained.
[作用]
本発明は、原料粉体を攪拌混合法と解砕法の2段階の造
粒工程を経る複合造粒法により造粒するものである。[Function] In the present invention, raw material powder is granulated by a composite granulation method that involves a two-step granulation process of stirring and mixing and crushing.
本発明の複合造粒法では、攪拌混合時に混合機の回転羽
根の回転により、原料の酸化マグネシウム粉が回転・流
動する際に、バインダ溶液が適度に分散・混合される。In the composite granulation method of the present invention, the binder solution is appropriately dispersed and mixed when the raw material magnesium oxide powder is rotated and fluidized by the rotation of the rotary blade of the mixer during stirring and mixing.
このため、スラリーを調製する必要がなく、また、バイ
ンダ溶液の溶媒のみで造粒が可能となるので、使用する
溶媒量は少量で良く、人体・環境に対する影響が極めて
小さい。Therefore, there is no need to prepare a slurry, and granulation can be performed using only the solvent of the binder solution, so only a small amount of solvent can be used, and the impact on the human body and environment is extremely small.
また、解砕法においては、解砕具により解砕された粉体
はスクリーンを通過して、粒径が小さく粒度が均一な、
高特性酸化マグネシウム粉が得られる。In addition, in the crushing method, the powder crushed by the crusher passes through a screen to produce small and uniform particles.
High-quality magnesium oxide powder is obtained.
[実施例]
以下、実施例及び比較例を挙げて本発明をより具体的に
説明するが、本発明はその要旨を超えない限り、以下の
実施例に限定されるものではない。[Examples] Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples unless it exceeds the gist thereof.
実施例1
平均粒径1.6μmの電融酸化マグネシウム1000g
と、界面活性剤(「ポリノン〇−44」鐵野化成製(主
成分:ポリエチレングリコールモンで一ト))5.0g
を添加した、20重量%バインダ溶液(「セルナ5E−
604J中家油脂製(主成分:ワックス類、溶媒:エチ
ルアルコール)75gとをヘンシェルミキサにて200
〜600rpmで3分間攪拌混合造粒した。次いで、得
られた造粒物を解砕造粒機にて90Orpmで回転する
ハンマーで衝撃粉砕した。Example 1 1000 g of fused magnesium oxide with an average particle size of 1.6 μm
and 5.0 g of surfactant (“Polynon 〇-44” manufactured by Tetsuno Kasei (main ingredient: polyethylene glycolmon))
20% by weight binder solution ("Serna 5E-
604J Nakaya Yushi Co., Ltd. (main ingredients: waxes, solvent: ethyl alcohol) 75g and 200g in a Henschel mixer.
The mixture was mixed and granulated with stirring at ~600 rpm for 3 minutes. Next, the obtained granules were impact-pulverized using a hammer rotating at 90 rpm in a crushing granulator.
このようにして得られた造粒粉は、流動性が高く、固め
見掛比重は2.00、圧縮度は6.3%であった。また
、この造粒粉を1000kg/crn”のプレス圧で成
形したところ、成形体の密度は2.72g/err?と
極めて高密度であった。The granulated powder thus obtained had high fluidity, a compacted apparent specific gravity of 2.00, and a degree of compression of 6.3%. Further, when this granulated powder was molded at a press pressure of 1000 kg/crn'', the density of the molded product was extremely high at 2.72 g/err?.
実施例2
界面活性剤、バインダ溶液を下記のものに代えたこと以
外は、実施例1と同様にして造粒を行なった。Example 2 Granulation was carried out in the same manner as in Example 1, except that the surfactant and binder solution were replaced with those shown below.
界面活性剤:
種類;ポリエチレングリコール
(平均分子量400)
(和光純薬工業製)
使用量、5.0g
バインダ溶液:
バインダ:ポリビニルブチラール
(rG−7,211J第−工業製薬製)溶媒:エチルア
ルコール
濃度:18.8重量%
使用量:80g
得られた造粒粉は、流動性が高く、固め見掛比重は1.
93、圧縮度は10.1%であった。また、この造粒粉
を1000kg/cm’のプレス圧で成形したところ、
成形体の密度は2.51g/Cm′と極めて高密度であ
った。Surfactant: Type: Polyethylene glycol (average molecular weight 400) (Wako Pure Chemical Industries) Amount used: 5.0g Binder solution: Binder: Polyvinyl butyral (rG-7,211J Dai-Kogyo Seiyaku) Solvent: Ethyl alcohol concentration : 18.8% by weight Amount used: 80g The obtained granulated powder has high fluidity and has an apparent specific gravity of 1.
93, and the degree of compression was 10.1%. In addition, when this granulated powder was molded with a press pressure of 1000 kg/cm',
The density of the molded product was extremely high at 2.51 g/Cm'.
比較例1
実施例1で用いた電融マグネシア原料1000gを2.
OILの溶媒(エチルアルコール)に懸濁させてスラリ
ーを調製し、これをスプレードライヤー装置により噴霧
乾燥して造粒した。Comparative Example 1 1000g of the electrofused magnesia raw material used in Example 1 was mixed into 2.
A slurry was prepared by suspending OIL in a solvent (ethyl alcohol), and the slurry was spray-dried using a spray dryer to form granules.
得られた造粒粉の流動性は実施例1.2で得られたもの
に比べて相当に劣り、固め見掛比重は1゜58、圧縮度
は17.4%であり、1000k g / c rn’
のプレス圧で成形したところ、成形体の密度は2.40
g/CJT!’であった。The fluidity of the obtained granulated powder was considerably inferior to that obtained in Example 1.2, and the compacted apparent specific gravity was 1°58, the degree of compaction was 17.4%, and the powder was 1000 kg/c. rn'
When molded with a press pressure of , the density of the molded product was 2.40.
g/CJT! 'Met.
[発明の効果]
以上詳述した通り、本発明の成形用酸化マグネシウム原
料の造粒方法は、攪拌混合法と解砕法との複合造粒法で
あフて、溶媒使用量を大幅に低減することができるので
、安全な作業環境下で安価にかつ効率的に酸化マグネシ
ウム造粒粉を得ることができる。しかも、得られる造粒
粉は極めて粒度分布の整った粉体であることから、その
流動性は著しく高く、電子材料、磁性材料焼成用鞘等の
高特性を要求される酸化マグネシウム成形体の成形用原
料粉として、極めて有用である。[Effects of the Invention] As detailed above, the method of granulating the magnesium oxide raw material for molding of the present invention is a composite granulation method of a stirring and mixing method and a crushing method, and the amount of solvent used is significantly reduced. Therefore, magnesium oxide granulated powder can be obtained efficiently and at low cost in a safe working environment. Moreover, since the obtained granulated powder has an extremely uniform particle size distribution, its fluidity is extremely high, and it can be used to mold magnesium oxide compacts that require high properties such as electronic materials and sheaths for firing magnetic materials. It is extremely useful as a raw material powder.
Claims (1)
ンダ溶液を用いて攪拌混合法により1次造粒した後、解
砕法により粒度を揃えることを特徴とする成形用酸化マ
グネシウム原料の造粒方法。(1) A method for granulating a magnesium oxide raw material for molding, which comprises first granulating magnesium oxide powder by a stirring and mixing method using a binder solution containing a surfactant, and then adjusting the particle size by a crushing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62309314A JPH01153515A (en) | 1987-12-07 | 1987-12-07 | Method for granulating magnesium oxide raw material for forming |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62309314A JPH01153515A (en) | 1987-12-07 | 1987-12-07 | Method for granulating magnesium oxide raw material for forming |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01153515A true JPH01153515A (en) | 1989-06-15 |
JPH054332B2 JPH054332B2 (en) | 1993-01-19 |
Family
ID=17991522
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62309314A Granted JPH01153515A (en) | 1987-12-07 | 1987-12-07 | Method for granulating magnesium oxide raw material for forming |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01153515A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5438450A (en) * | 1992-12-29 | 1995-08-01 | Canon Kabushiki Kaisha | Optical scanning apparatus |
JP2013251503A (en) * | 2012-06-04 | 2013-12-12 | Toshiba Corp | Current-voltage nonlinear resistor and manufacturing method thereof |
-
1987
- 1987-12-07 JP JP62309314A patent/JPH01153515A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5438450A (en) * | 1992-12-29 | 1995-08-01 | Canon Kabushiki Kaisha | Optical scanning apparatus |
JP2013251503A (en) * | 2012-06-04 | 2013-12-12 | Toshiba Corp | Current-voltage nonlinear resistor and manufacturing method thereof |
Also Published As
Publication number | Publication date |
---|---|
JPH054332B2 (en) | 1993-01-19 |
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