JPH04190839A - Modified powder - Google Patents

Modified powder

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Publication number
JPH04190839A
JPH04190839A JP32027790A JP32027790A JPH04190839A JP H04190839 A JPH04190839 A JP H04190839A JP 32027790 A JP32027790 A JP 32027790A JP 32027790 A JP32027790 A JP 32027790A JP H04190839 A JPH04190839 A JP H04190839A
Authority
JP
Japan
Prior art keywords
powder
powders
heat treatment
organosilicones
hours
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.)
Pending
Application number
JP32027790A
Other languages
Japanese (ja)
Inventor
Akihiro Kuroda
章裕 黒田
Akira Tsugita
次田 章
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.)
Kanebo Ltd
Original Assignee
Kanebo 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 Kanebo Ltd filed Critical Kanebo Ltd
Priority to JP32027790A priority Critical patent/JPH04190839A/en
Publication of JPH04190839A publication Critical patent/JPH04190839A/en
Pending legal-status Critical Current

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  • Pigments, Carbon Blacks, Or Wood Stains (AREA)

Abstract

PURPOSE:To obtain modified powders having a skin of uniform organosilicones free from secondary aggregation by subjecting a mixture of specific ratio of powders and organosilicones of specific viscosity to two-step heating treatments. CONSTITUTION:Powders and organosilicones having viscosity 1-400cst at 25 deg.C are agitated and mixed at 100:0.3-100:20 weight ratio of powders to organosilicones. Next, the mixture is subjected to a primary heat treatment at 70-130 deg.C for 0.5-4 hours and then to a secondary heat treatment at a higher temperature than that of the primary heat treatment, i.e., 110-200 deg.C, for 1-12 hours to obtain modified powders. As powders, there are colored pigments such as yellow iron oxide, red iron oxide, black iron oxide, chromium oxide, carbon black, etc., and white pigments such as zinc oxide, rutile titanium oxide, anatase titanium oxide, cerium oxide, etc. For mixing powders and organosilicones, powder agitating devices such as Henschel mixer, etc., can be used.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、粉体類と特定粘度のオルガノシリコーン類と
を撹拌混合した後、加熱処理を行って得られる改質粉体
に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a modified powder obtained by stirring and mixing powders and organosilicones having a specific viscosity and then subjecting the mixture to a heat treatment.

更に詳しくは、粉体類のオルガノシリコーン類による二
次凝集か殆と生じず、澄水性に優れた粉体類か得られる
ことを特徴とする、新規な乾式法により製造された改質
粉体に関する。
More specifically, it is a modified powder produced by a novel dry method, which is characterized by almost no secondary aggregation of powders caused by organosilicones and which provides powders with excellent water clarity. Regarding.

〔従来の技術及び発明か解決しようとする課題〕従来、
粉体類をオルガノシリコーン類にて被覆する方法として
、 1)ホールミル等のメカノケミカルを利用する方法 2)粉体類に、溶媒に溶かしたオルガノシリコーン類を
加え、必要に応じて、溶媒留去した後加熱処理する湿式
法 3)粉体類に、気体状のオルガノシリコーン類を接触さ
せ、被覆する気相法 4)スプレードライヤー等を用いてオルガノシリコーン
類を粉体類に被覆する方法 等か一般に用いられている。しかし、上記1)のメカノ
ケミカルを用いる方法では、被覆か不均一であり、また
、−度に処理できる1か限られているため、生産性か低
い問題がある。2)の湿式法は粉体類にオルガノシリコ
ーン類を均一に被覆できる特徴かあるか、溶剤を留去或
いは乾燥する工程での粉体の凝集か避けられない問題か
あった。
[Prior art and invention or problem to be solved] Conventionally,
Methods for coating powders with organosilicones include: 1) Using mechanochemicals such as a whole mill 2) Adding organosilicones dissolved in a solvent to the powders and distilling off the solvent as necessary. 3) Wet method in which powders are brought into contact with gaseous organosilicones and then coated 4) Methods in which powders are coated with organosilicones using a spray dryer etc. Generally used. However, the above method using mechanochemicals in 1) has problems in that the coating is non-uniform and that the number of treatments that can be processed at a time is limited, resulting in low productivity. The wet method (2) has the characteristic of being able to uniformly coat the powder with the organosilicone, and has unavoidable problems such as agglomeration of the powder during the process of distilling off the solvent or drying.

3)の気相法は、粉体類上に均一な皮膜か形成できる特
徴かあるか、密閉型の製造装置か必要であるなとの問題
かあった。4)のスプレードライヤーは、大量に処理を
行う場合、製造装置か大きなものになってしまう問題か
あった。
3) The gas phase method has problems such as whether it has the ability to form a uniform film on powders or whether it requires a closed type manufacturing equipment. The problem with the spray dryer (4) is that it becomes a large manufacturing device when processing a large amount.

すなわち、本発明の目的は、粉体類の二次凝集か無く、
均一なオルガノシリコーン類の皮膜を持った改質粉体を
提供することにある。
That is, the purpose of the present invention is to eliminate secondary agglomeration of powders,
The object of the present invention is to provide a modified powder having a uniform organosilicon film.

〔課題を解決するだめの手段〕[Failure to solve the problem]

本発明者等は、上記の問題巨に鑑み鋭意研究した結果、
粉体類にオルガノンリコー〉類を被覆処理する工程に於
いて、粉体類の二次凝集か生しる原因は意外にも溶媒を
用いる二とに有ることを見いたし、また更には後記特定
の粉体類とオルガノシリコーン類の混合比率及びオルガ
ノシリコーン類の粘度に於いては、二段階の加熱処理を
行うことによって、粉体類の二次凝集か極めて少なくな
ることを見いだし、本発明を完成した。
As a result of intensive research in view of the above problems, the inventors of the present invention found that
In the process of coating powders with Organon Ricoh, we found that the cause of secondary aggregation of powders is surprisingly due to the use of solvents, and furthermore, we also discovered that Regarding the mixing ratio of powders and organosilicones and the viscosity of organosilicones, it has been found that by performing a two-step heat treatment, secondary aggregation of powders can be extremely reduced. completed.

すなわち、本発明は粉体類と、25℃における粘度か1
〜400cstであるオルガノシリコーン類とを、粉体
類とオルガノシリコーン類の重量比率でl’ 00 :
 0.3〜+00:20の割合にて撹拌混合した後、7
0〜130℃にて一次加熱処理を0.5〜4時間行い、
ひきつついて一次加熱処理よりも高温であって、かつ1
10〜200℃にて二次加熱処理を1〜12時間行って
得られる改質粉体である。
That is, the present invention uses powders and a viscosity at 25°C of 1
~400cst of organosilicones, the weight ratio of powder and organosilicones is l' 00:
After stirring and mixing at a ratio of 0.3 to +00:20, 7
Primary heat treatment is performed at 0 to 130°C for 0.5 to 4 hours,
The temperature is higher than that of the primary heat treatment, and 1
It is a modified powder obtained by performing secondary heat treatment at 10 to 200°C for 1 to 12 hours.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

本発明で用いる粉体類は、黄酸化鉄、赤色酸化鉄、黒酸
化鉄、酸化クロム、カーホンブランク等の有色顔料、酸
化亜鉛、ルチル形、アナタース形酸化チタン、酸化セリ
ウム等の白色顔料、タルク、マイカ、セリサイト、カオ
リン等の体質顔料、雲母チタン等のパール顔料、硫酸ノ
\リウム、炭酸カルシウム、炭酸マグネシウム、珪酸ア
ルミニウム、珪酸マグネシウム等の金属塩、N−アンル
アスパラギン酸被覆マイカ等の有機物被覆顔料及び金属
石鹸処理顔料、ナイロンパウダー、シルクパウダー、ウ
レタンパウダー、テフロンパウダー、セルロースパウダ
ー等の高分子、七オライド、スメクタイト、シリカ、ア
ルミナ、石責、ガラスピーズ等の無機粉体、青色404
号等の色素、微粒子酸化チタン、微粒子酸化亜鉛、微粒
子黒酸化鉄、シリカ処理微粒子酸化チタン、アルミナ処
理微粒子酸化チタンか挙げられる。
The powders used in the present invention include colored pigments such as yellow iron oxide, red iron oxide, black iron oxide, chromium oxide, and carphone blank, white pigments such as zinc oxide, rutile type, anatase type titanium oxide, and cerium oxide; Extender pigments such as talc, mica, sericite, and kaolin, pearl pigments such as titanium mica, metal salts such as norium sulfate, calcium carbonate, magnesium carbonate, aluminum silicate, and magnesium silicate, and mica coated with N-anluaspartic acid. Organic substance-coated pigments and metallic soap-treated pigments, polymers such as nylon powder, silk powder, urethane powder, Teflon powder, cellulose powder, inorganic powders such as heptaolide, smectite, silica, alumina, stone powder, glass beads, etc., Blue 404
Examples include pigments such as No. 1, fine-particle titanium oxide, fine-particle zinc oxide, fine-particle black iron oxide, silica-treated fine-particle titanium oxide, and alumina-treated fine-particle titanium oxide.

本発明で用いられる粉体類の好ましい粒径は、例えば、
酸化チタンでは0.1−1.2μm、酸化亜鉛では0.
4〜1.0.am、酸化鉄ては0.1〜2.0μm、群
青では0.1〜5.0μm、セリサイト、カオリン、タ
ルク、マイカては0.5〜20.0μm、ノリ力ビーズ
、ガラスピーズては0.1〜1mm、微粒子酸化チタン
、微粒子酸化亜鉛、微粒子黒酸化鉄、アエロジルでは0
.01〜01μm、ナイロンパウダーでは10〜150
μmである。
Preferred particle sizes of the powders used in the present invention are, for example,
0.1-1.2 μm for titanium oxide and 0.1 μm for zinc oxide.
4-1.0. am, 0.1 to 2.0 μm for iron oxide, 0.1 to 5.0 μm for ultramarine, 0.5 to 20.0 μm for sericite, kaolin, talc, and mica, and 0.5 to 20.0 μm for nori beads and glass beads. 0.1 to 1 mm, 0 for fine titanium oxide, fine zinc oxide, fine black iron oxide, and Aerosil.
.. 01~01μm, 10~150 for nylon powder
It is μm.

本発明で用いるオルガノシリコーン類は、重合性、非重
合性に関係なく使用することかできる。
The organosilicones used in the present invention can be used regardless of whether they are polymerizable or non-polymerizable.

即ち、例えば、重合性のオルガノシリコーン類としては
、オレフィン変性シリコーン、メチルハイドロジエンポ
リシロキサン、アルキルハイドロジエンポリシロキサン
、Si −OH基基含有メチルポリンロケサン5i−H
基含有環状オルガノボリンロキサン、5i−H基含有フ
ッ素変性ノリコーン、アルキルアリルポリノロキサン等
が挙げられ、非重合性のオルガノシリコーン類としては
、ジメチルポリシロキサン、アルキルポリシロキサン。
That is, for example, examples of polymerizable organosilicones include olefin-modified silicone, methylhydrodiene polysiloxane, alkylhydrodiene polysiloxane, and Si-OH group-containing methylporinroquesan 5i-H.
Examples include group-containing cyclic organoborin loxane, 5i-H group-containing fluorine-modified noricone, alkylaryl polyoloxane, etc. Non-polymerizable organosilicones include dimethylpolysiloxane and alkylpolysiloxane.

メチルフェニルポリノロキサン、環状オルガノポリシロ
キサン、フッ素変性ンリコーン等が挙げられる。これら
のオルガノシリコーン類は単独もしくは2種類以上の組
み合わせによって使用することかできる。
Examples include methylphenyl polyoloxane, cyclic organopolysiloxane, and fluorine-modified silicone. These organosilicones can be used alone or in combination of two or more.

オルガノシリコーン類の粘度は1〜400cstてあり
、好ましくは1〜100cstである。
The viscosity of the organosilicones is 1 to 400 cst, preferably 1 to 100 cst.

1cstより小さいと、加熱時に於ける蒸発速度か速す
ぎて粉体への被覆か難しくなる。また、400cst以
上になると、オルガノシリコーン類を核として、粉体類
かその周りに集まった形の凝集塊か生じる。この傾向は
微粒子酸化チタン等、粒径か0.1μm以下の微粒子粉
体て顕著に認められる。
If it is smaller than 1 cst, the evaporation rate during heating will be too fast, making it difficult to coat the powder. Moreover, when the temperature exceeds 400 cst, powders or agglomerates are formed around organosilicones as a core. This tendency is particularly noticeable in fine powders with a particle size of 0.1 μm or less, such as fine titanium oxide.

オルガノシリコーン類と粉体類の配合量の比率は、粉体
類100重量部に対し、0,3〜20重量部であり、好
ましくは1〜12重量部である。
The blending ratio of organosilicones and powders is 0.3 to 20 parts by weight, preferably 1 to 12 parts by weight, based on 100 parts by weight of powders.

オルガノシリコーン類か0.3重量部以下であると、オ
ルガノシリコーン類の効果か得られない。
If the amount of organosilicones is less than 0.3 parts by weight, the effects of organosilicones cannot be obtained.

オルガノシリコーン類か20重量部を超えると1、粉体
類の二次凝集か生じる。
If the amount of organosilicones exceeds 20 parts by weight, secondary agglomeration of powders may occur.

本発明で用いる粉体類とオルガノシリコーン類の撹拌混
合方法は、ヘンシェルミキサー等の従来使用されている
粉体撹拌装置を用いることかできる。ただし酸化チタン
のように凝集か生し易い粉体類については、ヘンシェル
ミキサーにて混合撹拌を行った後で、アトマイサー、自
由粉砕機等の粉砕装置を用いて、加熱処理前に充分に粉
体類の凝集を解除し、一次粒子化しておく必要かある。
A conventionally used powder stirring device such as a Henschel mixer can be used to stir and mix the powders and organosilicones used in the present invention. However, for powders that tend to agglomerate, such as titanium oxide, after mixing and stirring with a Henschel mixer, use a grinding device such as an atomizer or free grinder to thoroughly pulverize the powder before heat treatment. It is necessary to release the agglomeration and convert it into primary particles.

加熱処理前に粉体類の凝集か充分に解除されていないと
、加熱処理後に粉体類の二次凝集塊か生じる。
If the agglomeration of the powders is not sufficiently released before the heat treatment, secondary agglomerates of the powders will occur after the heat treatment.

本発明で用いる加熱処理は、金属製バットに上記で処理
された粉体を静置後、送風乾燥機等で行うか、リボンブ
レンダー等を用いて粉体を撹拌しなから行う。また加熱
処理条件は、2段階からなる。一次加熱処理は、加熱に
よってオルガノシリコーン類か一部ガス化して粉体中を
移動する現象を用いて、粉体全体を均一に被覆処理する
工程である。一次加熱処理は、70〜130℃の加熱温
度にて、0.5〜4時間行われる。70℃の場合は加熱
時間は長めにし、130℃の場合は加熱時間は短めにす
ることか好ましい。これより加熱温度か高く、かつ加熱
時間か長い場合、オルガノシリコーン類か粉体全体に行
き渡らない内に、オルガノシリコーン類の重合反応か進
み、部分的に粉体類の二次凝集塊か生しる場合かある。
The heat treatment used in the present invention is carried out using a blow dryer or the like after leaving the powder treated above in a metal vat, or it is carried out without stirring the powder using a ribbon blender or the like. Moreover, the heat treatment conditions consist of two stages. The primary heat treatment is a process in which the entire powder is uniformly coated using a phenomenon in which organosilicones partially gasify and move through the powder by heating. The primary heat treatment is performed at a heating temperature of 70 to 130°C for 0.5 to 4 hours. When the temperature is 70°C, the heating time is preferably longer, and when the temperature is 130°C, the heating time is preferably shorter. If the heating temperature is higher and the heating time is longer than this, the polymerization reaction of the organosilicones will proceed before the organosilicones are distributed throughout the powder, and secondary agglomerates of the powder may partially form. There are cases where

この現象は特に凝集の生し易い粉体類、例えば微粒子酸
化チタンや微粒子酸化亜鉛等で観察される。二次加熱処
理は、一次加熱処理で均一に被覆したオルガノシリコー
ン類を、より強い加熱条件を用いて、重合を進ませ、粉
体上に強固な皮膜を形成させる工程である。二次加熱処
理は、一次加熱処理よりも高温でかつ、110〜200
℃の加熱温度にて、1〜12時間行われる。
This phenomenon is particularly observed with powders that tend to agglomerate, such as fine titanium oxide and fine zinc oxide. The secondary heat treatment is a process in which the organosilicones uniformly coated in the primary heat treatment are polymerized using stronger heating conditions to form a strong film on the powder. The secondary heat treatment is performed at a higher temperature than the primary heat treatment and at a temperature of 110 to 200
It is carried out at a heating temperature of 1 to 12 hours.

この二段階加熱処理を行うことにより、粉体類の二次凝
集か極めて改善され、均一なオルガノシリコーン類の皮
膜を持った改質粉体を得ることかできる。この効果は特
に粒径0.01〜0.1μmの微粒子粉体において顕著
に表われる。
By carrying out this two-step heat treatment, the secondary agglomeration of the powder is greatly improved, and a modified powder having a uniform organosilicon film can be obtained. This effect is particularly noticeable in fine particle powders with a particle size of 0.01 to 0.1 μm.

また従来の製法と本発明の違いは粉体類処理時の溶媒の
量にある。従来の製法では、比較的溶媒量か少ない製法
であっても、粉体類に対する溶媒量か粉体100重量部
に対して6〜15重量部必要であった。しかし粉体類と
オルガノシリコーン類を混合撹拌した後、アトマイサー
処理等て粉砕し、二次凝集粒子を低減せしめても、粉体
の二次凝集は完全には解除されなかった。この場合、凝
集塊は加熱処理の前段階では弱い力でほぐれる程度の凝
集塊でしかないが、次の加熱処理工程により、強い凝集
塊へと変化する。特にメチルハイドロジエンポリシロキ
サン等の重合性のオルガノシリコーン類を用いた場合、
より強固な凝集塊を形成する。粘性の高いオルガノシリ
コーン類や油剤を用いた場合も同様の現象か生しる。本
発明てはこれらの原因を考慮した結果、+Sffを用い
ず、かつ粘性の低いオルガノシリコーン類を使用し、加
熱処理前に粉体類の粉砕を充分に行い、二段階の加熱処
理を行う二とによって、加熱処理後も凝集か大変少ない
改T1粉体を得ること(こ成功した。
Furthermore, the difference between the conventional production method and the present invention lies in the amount of solvent used during powder processing. In conventional manufacturing methods, even if the amount of solvent is relatively small, the amount of solvent for powders is 6 to 15 parts by weight per 100 parts by weight of powder. However, even if the powders and organosilicones were mixed and stirred and then pulverized by an atomizer treatment or the like to reduce the secondary agglomerated particles, the secondary agglomeration of the powders was not completely released. In this case, the agglomerates are only agglomerates that can be loosened by a weak force before the heat treatment, but they change into strong agglomerates by the next heat treatment step. Especially when using polymerizable organosilicones such as methylhydrodiene polysiloxane,
Forms stronger agglomerates. A similar phenomenon occurs when highly viscous organosilicones or oils are used. As a result of considering these causes, the present invention does not use +Sff, uses organosilicones with low viscosity, thoroughly crushes the powder before heat treatment, and performs two-step heat treatment. By doing so, we were able to obtain a modified T1 powder with very little agglomeration even after heat treatment (this was successful).

また、本発明の改質粉体を化粧料、樹脂、塗料、接着剤
、固定化担体、クロマトグラフィー用カラム充填剤等に
応用した場合、二次凝集か極めて少ないため、紫外線散
乱能に優れ、かつ分散性に優れるため、保存安定性に優
れた製品を得ることかできる。
Furthermore, when the modified powder of the present invention is applied to cosmetics, resins, paints, adhesives, immobilization carriers, column packing materials for chromatography, etc., there is very little secondary aggregation, so it has excellent ultraviolet scattering ability. Moreover, since it has excellent dispersibility, it is possible to obtain a product with excellent storage stability.

〔実施例〕〔Example〕

以下、実施例にて本発明を説明する。 The present invention will be explained below with reference to Examples.

実施例に記載の凝集性及び感触に関する試験法は、以下
の通りである。
The test methods for cohesion and feel described in the Examples are as follows.

また、以下に記載の粘度はすへて25℃における粘度で
ある。
Further, the viscosity described below is the viscosity at 25°C.

(1)−■ (凝集性の評価) 粒度分布測定装置(SK l、ASER+IIICRO
N 5IZERPRO−7000セインン企業■製)を
用いて、改質粉体の平均粒径を求めた。測定条件は、分
散溶媒としてエチルアルコールを用い、改質粉体の分散
は付属の超音波発信装置を60秒間作動させて行った。
(1)-■ (Evaluation of cohesiveness) Particle size distribution measuring device (SK l, ASER + IIICRO
The average particle size of the modified powder was determined using N5IZERPRO-7000 (manufactured by Seinen Enterprises). The measurement conditions were as follows: ethyl alcohol was used as a dispersion solvent, and the modified powder was dispersed by operating the attached ultrasonic transmitter for 60 seconds.

一次粒子径をり。、改質粉体の粒子径をDとし、D/D
oの値から次のように凝集性を評価した。
Primary particle size. , the particle size of the modified powder is D, and D/D
Cohesiveness was evaluated from the value of o as follows.

尚、本装置では測定不可能な微粒子粉体については次の
(+)−〇で示した方法により、凝集性の評価を行った
For fine particle powders that could not be measured with this device, the cohesiveness was evaluated by the method indicated by (+)-〇 below.

(I)−■ (微粒子粉体の凝集性の評価)透過型電子
顕微鏡により、被覆処理された微粒子粉体の写真を撮り
、次のように粉体の凝集状態を評価した。尚、評価の基
準としては、未処理粉(11)  (粉体の感触の評価
方法)各実施例及び比較例によって作成した粉体を用い
、20〜50才の男女計10人を対象として、感触の評
価を行った。数値は各評価項目に対して10人中何人か
判定したかを示すものであり、10ならば10人全員か
、1ならば10人中1人か判定したことを示す。
(I)-■ (Evaluation of cohesiveness of fine particle powder) A photograph of the coated fine particle powder was taken using a transmission electron microscope, and the agglomeration state of the powder was evaluated as follows. The evaluation criteria were as follows: Untreated powder (11) (Method for evaluating the feel of powder) A total of 10 men and women aged 20 to 50 were tested using the powders prepared in each example and comparative example. The feel was evaluated. The numerical value indicates how many out of 10 people judged each evaluation item; 10 indicates that all 10 people judged, and 1 indicates that 1 out of 10 people judged.

実施例1 酸化チタン(粒径0.6μm)IKgにメチルハイドロ
ジエンポリシロキサン(KF−99P粘度19cst信
越化学工業■製)30gを加え、ミキサーにて混合、粉
砕を行った。得られた粉体をステンレス製バットに移し
、送風乾燥機を用いて、100℃にて2時間一次加熱処
理し、ついて180℃にて8時間二次加%fi理を行い
、改質粉体を得て、前記諸試験を実施した。
Example 1 30 g of methyl hydrodiene polysiloxane (KF-99P, viscosity 19 cst, manufactured by Shin-Etsu Chemical Co., Ltd.) was added to 1 kg of titanium oxide (particle size 0.6 μm), mixed with a mixer, and pulverized. The obtained powder was transferred to a stainless steel vat and subjected to primary heat treatment at 100°C for 2 hours using a blow dryer, followed by secondary heating treatment at 180°C for 8 hours to obtain a modified powder. was obtained, and the various tests described above were conducted.

比較例1 酸化チタン(粒径0.6μm)IKgにメチルハイトロ
ジエンポリソロキサン(KF−99P) 30 gをイ
ソプロピルアルコール120gに溶かした溶液を加え、
ミキサーにて混合、粉砕を行った。粉砕の条件は実施例
1と同様にした。得られた粉体をステンレス製バットに
移し、送風乾燥機を用いて、180″Cにて8時間加熱
処理を行い、粉体を得て、前記諸試験を実施した。
Comparative Example 1 A solution of 30 g of methylhydrodiene polysoloxane (KF-99P) dissolved in 120 g of isopropyl alcohol was added to IKg of titanium oxide (particle size 0.6 μm),
Mixing and pulverization were performed using a mixer. The conditions for pulverization were the same as in Example 1. The obtained powder was transferred to a stainless steel vat, and heat-treated at 180''C for 8 hours using a blow dryer to obtain a powder, which was then subjected to the various tests described above.

実施例2 黄酸化鉄(ffl径0−7μm)100gにメチルハイ
ドロジエンポリシロキサン(KF−99P) 2 gを
加え、ミキサーにて混合、粉砕を行った。得られた粉体
をステンレス製バットに移し、送風乾燥機を用いて、9
0℃にて3時間一次加熱処理し、ついて+40’cにて
5時間二次加熱処理を行い、改質粉体を得て、前記諸試
験を実施した。
Example 2 2 g of methylhydrodiene polysiloxane (KF-99P) was added to 100 g of yellow iron oxide (ffl diameter 0-7 μm), mixed and pulverized using a mixer. The obtained powder was transferred to a stainless steel vat and dried using a blow dryer.
A primary heat treatment was performed at 0° C. for 3 hours, followed by a secondary heat treatment at +40° C. for 5 hours to obtain a modified powder, and the various tests described above were conducted.

比較例2 黄酸化鉄(粒径0.7μm)100gにメチルハイドロ
ジエンポリシロキサン(KF−99P) 2 gをイソ
プロピルアルコール10gに溶かした溶液を加え、ミキ
サーにて混合、粉砕を行った。粉砕の条件は実施例2と
同様にした。得られた粉体をステンレス製ハツトに移し
、送風乾燥機を用いて、140℃にて5時間加熱処理を
行い、粉体を得て、前記諸試験を実施した。
Comparative Example 2 A solution of 2 g of methylhydrodiene polysiloxane (KF-99P) dissolved in 10 g of isopropyl alcohol was added to 100 g of yellow iron oxide (particle size 0.7 μm), and the mixture was mixed and pulverized using a mixer. The conditions for pulverization were the same as in Example 2. The obtained powder was transferred to a stainless steel hat and heat-treated at 140° C. for 5 hours using a blow dryer to obtain a powder, and the various tests described above were conducted.

実施例3 セリサイト(粒径10.6μm)lOKgにメチルハイ
ドロジエンポリノロキサン(KF−99P) 0.5K
gとメチルハイトロジエンポリソロキサン(KF−99
01粘度19cst信越化学工業■製)0.5Kgの混
合物を加え、ヘンシェルミキサーを用いて混合撹拌した
。得られた粉体をステンレス製バットに移し、送風乾燥
機を用いて、130℃にて1時間一次加熱処理し、つい
て160℃にて6時間二次加熱処理を行い、改質粉体を
得て、前記諸試験を実施した。
Example 3 Methylhydrodiene polyoloxane (KF-99P) 0.5K to 1Kg of sericite (particle size 10.6μm)
g and methylhydrodiene polysoloxane (KF-99
0.5 kg of a mixture of 0.01 (viscosity: 19 cst, manufactured by Shin-Etsu Chemical Co., Ltd.) was added, and the mixture was mixed and stirred using a Henschel mixer. The obtained powder was transferred to a stainless steel vat, and a primary heat treatment was performed at 130°C for 1 hour using a blow dryer, followed by a secondary heat treatment at 160°C for 6 hours to obtain a modified powder. The various tests mentioned above were conducted.

比較例3 セリサイト(粒径10.6μm)1Kgにメチルハイト
ロンエンポリシロキサン(KF−99P) 50 gと
メチルハイトロノニンポリシロキサン(KF−9901
)50gをトリクロロエタン100gに溶かした溶液を
加え、ヘンシェルミキサーを用いて混合撹拌した。混合
撹拌の条件は実施例3と同様にした。
Comparative Example 3 1 kg of sericite (particle size 10.6 μm) was mixed with 50 g of methylhytronene polysiloxane (KF-99P) and methylhytrononine polysiloxane (KF-9901).
A solution of 50 g of ) dissolved in 100 g of trichloroethane was added, and the mixture was mixed and stirred using a Henschel mixer. The mixing and stirring conditions were the same as in Example 3.

得られた粉体をステンレス製バットに移し、送風乾燥機
を用いて、160℃にて6時間加熱処理を行い、粉体を
得て、前記諸試験を実施した。
The obtained powder was transferred to a stainless steel vat, and heat-treated at 160° C. for 6 hours using a blow dryer to obtain a powder, and the various tests described above were conducted.

実施例4 雲母チタン(粒径12.2μm)l(]Ogにメチルハ
イドロジエンポリシロキサン(KF−99P) 8 g
を加え、ミキサーにて混合、粉砕を行った。得られた粉
体をステンレス製バットに移し、送風乾燥機を用いて、
130℃にて2時間一次加熱処理し、ついて190℃に
て6時間二次加熱処理を行い、改質粉体を得て、前記諸
試験を実施した。
Example 4 Mica titanium (particle size 12.2 μm) l (]Og and 8 g of methylhydrodiene polysiloxane (KF-99P)
was added, mixed and pulverized using a mixer. The obtained powder was transferred to a stainless steel vat and dried using a blow dryer.
A primary heat treatment was performed at 130° C. for 2 hours, followed by a secondary heat treatment at 190° C. for 6 hours to obtain a modified powder, and the various tests described above were conducted.

比較例4 雲母チタン(粒径12.2μm)100gにメチルハイ
ドロジエンポリシロキサン(KF−99P) 8 gを
トリクレン10gに溶解した溶液を加え、ミキサーにて
混合、粉砕を行った。粉砕の条件は実施例4と同様にし
た。得られた粉体をステンレス製バットに移し、送風乾
燥機を用いて190℃にて6時間加熱処理を行い、粉体
を得て、前記諸試験を実施した。
Comparative Example 4 A solution prepared by dissolving 8 g of methylhydrodiene polysiloxane (KF-99P) in 10 g of trichlene was added to 100 g of mica titanium (particle size 12.2 μm), and the mixture was mixed and pulverized using a mixer. The conditions for pulverization were the same as in Example 4. The obtained powder was transferred to a stainless steel vat and heat-treated at 190° C. for 6 hours using a blow dryer to obtain a powder, and the various tests described above were conducted.

実施例5 酸化亜鉛(粒径0.4μm)loOgにオレフィン変性
シリコーン(KF−413粘度100cst信越化学工
業■製)4gとメチルハイトロノニンポリシロキサン(
KF−99P) 4 gを加え、ミキサーにて混合、粉
砕を行った。得られた粉体をステンレス製バットに移し
、送風乾燥機を用いて、120″Cにて2時間一次加熱
処理し、ついて150℃にて4時間二次加熱処理を行い
、改質粉体を得て、前記諸試験を実施した。
Example 5 Zinc oxide (particle size 0.4 μm) loOg, 4 g of olefin-modified silicone (KF-413 viscosity 100 cst, manufactured by Shin-Etsu Chemical Co., Ltd.) and methylhytrononine polysiloxane (
KF-99P) 4 g was added, mixed and pulverized using a mixer. The obtained powder was transferred to a stainless steel vat and subjected to primary heat treatment at 120"C for 2 hours using a blow dryer, followed by secondary heat treatment at 150"C for 4 hours to obtain a modified powder. The various tests described above were conducted.

比較例5 酸化亜鉛(粒径0,4μm)100gにオレフィン変性
シリコーン(KF−413) 4 gとメチルハイトロ
ンエンポリシロキサン(KF−99P) 4 gをアセ
トンlOgに溶かした溶液を加え、ミキサーにて混合、
粉砕を行った。得られた粉体をステンレス製バットに移
し、送風乾燥機を用いて、150℃にて4時間加熱処理
を行い、粉体を得て、前記諸試験を実施した。
Comparative Example 5 A solution of 4 g of olefin-modified silicone (KF-413) and 4 g of methylhytronene polysiloxane (KF-99P) dissolved in 10 g of acetone was added to 100 g of zinc oxide (particle size 0.4 μm), and mixed in a mixer. mixture,
Shredded. The obtained powder was transferred to a stainless steel vat and heat-treated at 150° C. for 4 hours using a blow dryer to obtain a powder, and the various tests described above were conducted.

実施例6 シリカビーズ(粒径0.2mm)100gにフン素変性
ノリコーン(X−22−822粘度100cst信越化
学工業札製)6gを加え、ミキサーにて混合、粉砕を行
った。得られた粉体をステンレス製ハツトに移し、送風
乾燥機を用いて、130℃にて1時間一次加熱処理し、
ついて150℃にて12時間二次加熱処理を行い、改質
粉体を得て、前記諸試験を実施した。
Example 6 6 g of fluorine-modified noricorn (X-22-822, viscosity 100 cst, manufactured by Shin-Etsu Chemical Co., Ltd.) was added to 100 g of silica beads (particle size 0.2 mm), and the mixture was mixed and pulverized using a mixer. The obtained powder was transferred to a stainless steel hat and subjected to primary heat treatment at 130°C for 1 hour using a blow dryer.
The powder was then subjected to secondary heat treatment at 150° C. for 12 hours to obtain a modified powder, and the various tests described above were conducted.

比較例6 シリカビーズ(粒径0.2mm) 100 gとフッ素
変性ソリコーン(X−22−822) 6 gにトリク
ロロエタン100gを加え、ミキサーにて撹拌混合を行
った。エバポレーターを用いて溶媒を留去した後、得ら
れた粉体をステンレス製ハツトに移し、送風乾燥機を用
いて、150℃にて12時間加熱処理を行い、粉体を得
て、前記諸試験を実施した。
Comparative Example 6 100 g of trichloroethane was added to 100 g of silica beads (particle size 0.2 mm) and 6 g of fluorine-modified soricone (X-22-822), and the mixture was stirred and mixed using a mixer. After distilling off the solvent using an evaporator, the obtained powder was transferred to a stainless steel hat, and heat-treated at 150°C for 12 hours using a blow dryer to obtain a powder, and the various tests described above were carried out. was carried out.

実施例7 球状微粒子酸化チタン(平均粒径0.03μm)IKg
にメチルハイトロノニンポリシロキサン(KF−99P
) 80 gを加え、ヘンシェルミキサーにて撹拌混合
した。ついてア)・マイサーを用いて、粉砕を行った。
Example 7 Spherical fine particle titanium oxide (average particle size 0.03 μm) IKg
Methylhydrononine polysiloxane (KF-99P)
) 80 g were added and mixed by stirring using a Henschel mixer. Then, a) pulverization was performed using a mixer.

得られた粉体をステンレス製容器に移し、送風乾燥機を
用いて、+00℃にて2時間一次加熱処理し、ついて+
50℃にて8時間二次加熱処理を行って、改質粉体を得
て、前記諸試験を実施した。
The obtained powder was transferred to a stainless steel container and subjected to primary heat treatment at +00℃ for 2 hours using a blow dryer.
Secondary heat treatment was performed at 50° C. for 8 hours to obtain a modified powder, and the various tests described above were conducted.

比較例7 球状微粒子酸化チタン(平均粒径0.03μm)1Kg
にメチルハイドロジエンポリシロキサン(KF−99P
) 80 gをイソプロピルアルコール120gに溶か
した溶液を加え、ヘンシェルミキサーにて撹拌混合した
。ついてアトマイサーを用いて、粉砕を行った。撹拌混
合及び粉砕の条件は実施例7と同様にした。得られた粉
体をステンレス製容器に移し、送風乾燥機を用いて、1
50℃にて8時間加熱処理を行って、粉体を得て、前記
諸試験を実施した。
Comparative Example 7 Spherical fine particle titanium oxide (average particle size 0.03 μm) 1Kg
Methylhydrodiene polysiloxane (KF-99P)
) A solution of 80 g dissolved in 120 g of isopropyl alcohol was added and mixed by stirring using a Henschel mixer. Then, it was pulverized using an atomizer. The stirring mixing and pulverizing conditions were the same as in Example 7. The obtained powder was transferred to a stainless steel container and dried using a blow dryer.
Heat treatment was performed at 50° C. for 8 hours to obtain powder, and the various tests described above were conducted.

実施例8 微粒子酸化亜鉛(平均粒径0.03μm)100gにメ
チルハイドロジエンポリシロキサン(KF−99P>5
gを加え、ミキサーにて混合、粉砕を行った。
Example 8 Methylhydrodiene polysiloxane (KF-99P>5
g, and mixed and pulverized using a mixer.

得られた粉体をステンレス製ハツトに移し、送風乾燥機
を用いて、120℃にて1時間一次加熱処理し、ついて
180℃にて5時間二次加熱処理を行って、改質粉体を
得て、前記諸試験を実施した。
The obtained powder was transferred to a stainless steel hat, and a primary heat treatment was performed at 120°C for 1 hour using a blow dryer, followed by a secondary heat treatment at 180°C for 5 hours to obtain a modified powder. The various tests described above were conducted.

比較例8 微粒子酸化亜鉛(平均粒径0.03μm)100gにメ
チルハイドロジエンポリシロキサン(KF−99P)5
gをイソプロピルアルコール7gに溶かした溶液を加え
、ミキサーにて混合、粉砕を行った。
Comparative Example 8 5 methyl hydrodiene polysiloxane (KF-99P) was added to 100 g of fine particle zinc oxide (average particle size 0.03 μm).
A solution prepared by dissolving 1.5 g in 7 g of isopropyl alcohol was added, and the mixture was mixed and pulverized using a mixer.

粉砕の条件は実施例8と同様にした。得られた粉体をス
テンレス製ハントに移し、送風乾燥機を用いて、180
℃にて5時間加熱処理を行って、粉体を得て、前記諸試
験を実施した。
The conditions for pulverization were the same as in Example 8. The obtained powder was transferred to a stainless steel hunt, and dried at 180°C using a blow dryer.
Heat treatment was performed at ℃ for 5 hours to obtain a powder, and the various tests described above were conducted.

実施例9 微粒子黒酸化鉄(平均粒径0,01μm)IOKgにメ
チルハイトロンエンポリノロキサン(KF−99P)0
.5Kgとメチルハイドロジエンポリシロキサン(KF
−9901) 0.5 K gの混合物を加え、ヘンン
エルミキサーを用いて混合撹拌した。ついてアトマイサ
ーを用いて、粉砕を行った。得られた粉体をステンレス
製容器に移し、送風乾燥機を用いて、90℃にて3時間
一次加熱処理し、ついて120℃にて8時間加熱処理を
行って、改質粉体を得て、前記諸試験を実施した。
Example 9 Particulate black iron oxide (average particle size 0.01 μm) IOKg with 0 methylhytron polyoloxane (KF-99P)
.. 5Kg and methylhydrodiene polysiloxane (KF
-9901) 0.5 Kg of the mixture was added and mixed and stirred using a Hennel mixer. Then, it was pulverized using an atomizer. The obtained powder was transferred to a stainless steel container, and a primary heat treatment was performed at 90°C for 3 hours using a blow dryer, followed by a heat treatment at 120°C for 8 hours to obtain a modified powder. , conducted the various tests mentioned above.

比較例9 微粒子黒酸化鉄(平均粒径0.01μm)1Kgにメチ
ルハイドロジエンポリシロキサン(KF−99P)50
gとメチルハイド0ンエンポリシロキサン(KF−99
01) 50 gをシクロヘキサンIKgに溶解した溶
液を加え、ミキサーを用いて混合撹拌した。
Comparative Example 9 50% of methylhydrodiene polysiloxane (KF-99P) was added to 1kg of fine black iron oxide (average particle size 0.01 μm).
g and methyl hydride polysiloxane (KF-99
01) A solution prepared by dissolving 50 g of cyclohexane in Ikg of cyclohexane was added, and the mixture was mixed and stirred using a mixer.

溶媒を減圧留去し、得られた粉体をアトマイサーを用い
て粉砕した。粉体をステンレス製容器に移し、送風乾燥
機を用いて、120℃にて8時間加熱処理を行って、粉
体を得て、前記諸試験を実施した。
The solvent was distilled off under reduced pressure, and the resulting powder was pulverized using an atomizer. The powder was transferred to a stainless steel container and heat-treated at 120° C. for 8 hours using a blow dryer to obtain a powder, and the various tests described above were performed.

実施例10 微粒子酸化チタン(平均粒径0,06μm)100gに
メチルポリシロキサン(KF−56粘度5cst)5g
を加え、ミキサーにて混合、粉砕を行った。得られた粉
体をステンレス製バットに移し、送風乾燥機を用いて、
80℃にて4時間一次加熱処理し、ついて160℃にて
10時間加熱処理を行って、改質粉体を得て、前記諸試
験を実施した。
Example 10 5 g of methyl polysiloxane (KF-56 viscosity 5 cst) to 100 g of fine particle titanium oxide (average particle size 0.06 μm)
was added, mixed and pulverized using a mixer. The obtained powder was transferred to a stainless steel vat and dried using a blow dryer.
A primary heat treatment was performed at 80° C. for 4 hours, followed by a heat treatment at 160° C. for 10 hours to obtain a modified powder, and the various tests described above were conducted.

比較例10 微粒子酸化チタン(平均粒径006μm)100gにメ
チルポリシロキサン(KF−56) 5 gをトリクレ
ン200gに溶解した溶液を加え、ミキサーにて撹拌混
合を行った。エバポレーターを用いて溶媒を留去した後
、得られた粉体をステンレス製バットに移し、送風乾燥
機を用いて+60℃にて10時間加熱処理を行った。得
られた粉体をミキサーを用いて粉砕して、粉体を得て、
前記諸試験を実施した。
Comparative Example 10 A solution prepared by dissolving 5 g of methylpolysiloxane (KF-56) in 200 g of trichlene was added to 100 g of fine particle titanium oxide (average particle size: 006 μm), and the mixture was stirred and mixed using a mixer. After distilling off the solvent using an evaporator, the obtained powder was transferred to a stainless steel vat and heat-treated at +60° C. for 10 hours using a blow dryer. The obtained powder is crushed using a mixer to obtain a powder,
The various tests mentioned above were conducted.

実施例11 微粒子酸化チタン(平均粒径0.06μm)100gに
下記に示される5i−H基含有フッ素変性ソリコーン2
gとメチルハイドロジエンポリシロキサン(KF−99
P) 5 gを加え、ミキサーにて混合、粉砕を行った
。得られた粉体をステンレス製ハツトに移し、送風乾燥
機を用いて、100℃にて2時間一次加熱処理し、つい
て150℃にて8時間二次加熱処理を行い、改質粉体を
得て、前記諸試験を実施した。
Example 11 5i-H group-containing fluorine-modified soricone 2 shown below in 100 g of fine-particle titanium oxide (average particle size 0.06 μm)
g and methylhydrodiene polysiloxane (KF-99
P) 5 g was added, mixed and pulverized using a mixer. The obtained powder was transferred to a stainless steel hat, and a primary heat treatment was performed at 100°C for 2 hours using a blow dryer, followed by a secondary heat treatment at 150°C for 8 hours to obtain a modified powder. The various tests mentioned above were conducted.

5i−H基含有フッ素変性シリコーンは、なる構造を持
ち、a : b=5 : 5、粘度100cstである
The 5i-H group-containing fluorine-modified silicone has the following structure, a:b=5:5, and a viscosity of 100cst.

比較例11 微粒子酸化チタン(平均粒径0,06μm)100gに
実施例11て用いたのと同しSi−H基含有フッ素変性
シリコーン2gとメチルハイトロジエンポリシロキサン
(KF−99P) 5 gを加え、メタノール5gに溶
かした溶液を加え、ミキサーにて混合、粉砕を行った。
Comparative Example 11 2 g of the same Si-H group-containing fluorine-modified silicone used in Example 11 and 5 g of methylhydrodiene polysiloxane (KF-99P) were added to 100 g of fine-particle titanium oxide (average particle size 0.06 μm). A solution dissolved in 5 g of methanol was added, and the mixture was mixed and pulverized using a mixer.

得られた粉体をステンレス製ハツトに移し、送風乾燥機
を用いて、150℃にて8時間加熱処理を行い、粉体を
得て、前記諸試験を実施した。
The obtained powder was transferred to a stainless steel hat and heat-treated at 150° C. for 8 hours using a blow dryer to obtain a powder, and the various tests described above were conducted.

実施例12 群青(粒径1.0μm)IKgにテトラハイドロジエン
テトラメチルシクロテトラシロキサン(粘度2.5cs
t ) 200 gを加え、ミキサーにて混合、粉砕を
行った。得られた粉体をステンレス製ハツトに移し、送
風乾燥機を用いて、70℃にて1時間一次加熱処理し、
ついて130℃にて4時間二次加熱処理を行って、改質
粉体を得た。
Example 12 Tetrahydrodienetetramethylcyclotetrasiloxane (viscosity 2.5 cs
t) 200 g was added and mixed and pulverized using a mixer. The obtained powder was transferred to a stainless steel hat and subjected to primary heat treatment at 70°C for 1 hour using a blow dryer.
Then, a secondary heat treatment was performed at 130° C. for 4 hours to obtain a modified powder.

実施例13 ナイロンパウダー(粒径14.0μm)100gにメチ
ルハイドロジエンポリシロキサン(粘度350cst)
3gを加え、ミキサーにて混合、粉砕を行った。得られ
た粉体をステンレス製ハツトに移し、送風乾燥機を用い
て、90℃にて2時間一次加熱処理し、ついて140℃
にて4時間加第  1  表 第1表より明らかな如・く、本方法によって得られる改
質粉体は、従来の製法によって得られる粉体類とは異な
り、粉体類の二次凝集か少なく、感触に優れた粉体かえ
られることかわかる。
Example 13 Methylhydrodiene polysiloxane (viscosity 350 cst) to 100 g of nylon powder (particle size 14.0 μm)
3 g was added, mixed and pulverized using a mixer. The obtained powder was transferred to a stainless steel hat and subjected to primary heat treatment at 90°C for 2 hours using a blow dryer, and then heated to 140°C.
As is clear from Table 1, the modified powder obtained by this method is different from the powder obtained by the conventional manufacturing method, due to secondary aggregation of powder. You can see that you can use powder with less powder and better texture.

〔発明の効果〕〔Effect of the invention〕

以上記載のごとく、本発明は、化粧料、樹脂、塗料、接
着剤、固定化担体、クロマトグラフィー用カラム充填剤
等の原料として、二次凝集か少ない、溶水性、分散性に
優れた、有用なる改質粉体を与えることは明らかである
As described above, the present invention is useful as a raw material for cosmetics, resins, paints, adhesives, immobilization carriers, column packing materials for chromatography, etc., with less secondary aggregation and excellent water solubility and dispersibility. It is clear that a modified powder having the following properties can be obtained.

手続補正書 平成 3年 2月26日Procedural amendment February 26, 1991

Claims (1)

【特許請求の範囲】[Claims] 粉体類と、25℃における粘度が1〜400cstであ
るオルガノシリコーン類とを、粉体類とオルガノシリコ
ーン類の重量比率で100:0.3〜100:20の割
合にて混合撹拌した後、70〜130℃にて一次加熱処
理を0.5〜4時間行い、ひきつづいて一次加熱処理よ
りも高温であって、かつ110〜200℃にて二次加熱
処理を1〜12時間行って得られる改質粉体。
After mixing and stirring powders and organosilicones having a viscosity of 1 to 400 cst at 25°C at a weight ratio of powders and organosilicones of 100:0.3 to 100:20, Obtained by performing primary heat treatment at 70 to 130°C for 0.5 to 4 hours, followed by secondary heat treatment at 110 to 200°C for 1 to 12 hours at a higher temperature than the primary heat treatment. Modified powder.
JP32027790A 1990-11-24 1990-11-24 Modified powder Pending JPH04190839A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32027790A JPH04190839A (en) 1990-11-24 1990-11-24 Modified powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32027790A JPH04190839A (en) 1990-11-24 1990-11-24 Modified powder

Publications (1)

Publication Number Publication Date
JPH04190839A true JPH04190839A (en) 1992-07-09

Family

ID=18119711

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32027790A Pending JPH04190839A (en) 1990-11-24 1990-11-24 Modified powder

Country Status (1)

Country Link
JP (1) JPH04190839A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07178335A (en) * 1993-11-09 1995-07-18 Nippon Shokubai Co Ltd Organic polymer combined inorganic fine particle, its production and dispersed body and film forming composition containing the same
WO1998006787A1 (en) * 1996-08-12 1998-02-19 The Yokohama Rubber Co., Ltd. Process for the production of surface-treated carbon black for the reinforcement of rubbers
EP1858597A1 (en) * 2005-03-07 2007-11-28 Basf Aktiengesellschaft Cosmetic and dermatological preparations containing transparent surface-coated titanium dioxide particles
CN103289441A (en) * 2013-05-23 2013-09-11 铜陵瑞莱科技有限公司 Method for preparing flame-retardant iron oxide black granules

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07178335A (en) * 1993-11-09 1995-07-18 Nippon Shokubai Co Ltd Organic polymer combined inorganic fine particle, its production and dispersed body and film forming composition containing the same
WO1998006787A1 (en) * 1996-08-12 1998-02-19 The Yokohama Rubber Co., Ltd. Process for the production of surface-treated carbon black for the reinforcement of rubbers
US6020068A (en) * 1996-08-12 2000-02-01 The Yokohama Rubber Co., Ltd. Process for the production of surface-treated carbon black for the reinforcement of rubbers
EP1858597A1 (en) * 2005-03-07 2007-11-28 Basf Aktiengesellschaft Cosmetic and dermatological preparations containing transparent surface-coated titanium dioxide particles
CN103289441A (en) * 2013-05-23 2013-09-11 铜陵瑞莱科技有限公司 Method for preparing flame-retardant iron oxide black granules

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