JPS598614A - Preparation of silica sol using organic solvent as dispersion medium - Google Patents

Preparation of silica sol using organic solvent as dispersion medium

Info

Publication number
JPS598614A
JPS598614A JP11429482A JP11429482A JPS598614A JP S598614 A JPS598614 A JP S598614A JP 11429482 A JP11429482 A JP 11429482A JP 11429482 A JP11429482 A JP 11429482A JP S598614 A JPS598614 A JP S598614A
Authority
JP
Japan
Prior art keywords
organic solvent
water
silica sol
dispersion medium
silica
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
JP11429482A
Other languages
Japanese (ja)
Other versions
JPH021087B2 (en
Inventor
Yusaku Arima
悠策 有馬
Jun Yuki
結城 諄
Hiroyasu Nishida
広泰 西田
Takashi Harada
孝 原田
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.)
SHOKUBAI KASEI KOGYO KK
JGC Catalysts and Chemicals Ltd
Original Assignee
SHOKUBAI KASEI KOGYO KK
Catalysts and Chemicals Industries 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 SHOKUBAI KASEI KOGYO KK, Catalysts and Chemicals Industries Co Ltd filed Critical SHOKUBAI KASEI KOGYO KK
Priority to JP11429482A priority Critical patent/JPS598614A/en
Publication of JPS598614A publication Critical patent/JPS598614A/en
Publication of JPH021087B2 publication Critical patent/JPH021087B2/ja
Granted legal-status Critical Current

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

Abstract

PURPOSE:To obtain high concentrated stable silica sol using an organic solvent as a dispersion medium, by blending silica sol using water as a dispersion medium with the organic solvent, dehydrating it by an ultrafilter. CONSTITUTION:Silica sol having particularly 70-300Angstrom average particle diameter of silica and preferably >=15wt% calculated at SiO2 of silica concentration, using water as a dispersion medium, is prepared. This silica sol is blended with a water-soluble organic solvent (e.g., methanol), the solution wherein both water and the organic solvent exist is filtered with an ultrafilter and concentrated. The concentrate is added to the organic solvent again, diluted, the operation of the filtration through the ultrafilter again is repeated plural times, to give silica sol using the organic solvent as the dispersion medium. In this case, the operation is preferably repeated to make a weight composition ratio of the organic solvent to water of (100:0.1)-(100:7.5). The concentration adjustment of the organosilica sol is carried out by a method to separate and to remove the solvent, and it can be concentrated up to 60wt% when methanol, etc. is used.

Description

【発明の詳細な説明】 本発明は水を分散媒としたシリカゾルから。[Detailed description of the invention] The present invention is based on silica sol using water as a dispersion medium.

有機溶剤を分散媒とした高S度で且つ安定なシリカゾル
を製造する方法に関する。
The present invention relates to a method for producing a stable silica sol with a high S degree using an organic solvent as a dispersion medium.

無機物と有機物からなる複合材料の開発は。The development of composite materials consisting of inorganic and organic materials.

有機物のどちらかと言えば貧弱な耐熱性や耐候性等を改
良するという従来からの目的に加えて。
In addition to the conventional purpose of improving the rather poor heat resistance and weather resistance of organic substances.

最近の石油資源の枯渇とこれに伴う価格高騰のため有機
物材料を節約するという目的で近年その要求が増大して
いる。複合材料の開発を進める上で特に大事なことは、
無機物と有機物の混合分散技術でめ9.これによって複
合材料の開発の成否が決定されるといっても過百ではな
い。
Due to the recent depletion of petroleum resources and the resulting rise in prices, the demand for organic materials has increased in recent years for the purpose of saving organic materials. What is especially important when proceeding with the development of composite materials is that
9. Mixing and dispersing technology of inorganic and organic substances. It is no exaggeration to say that this will determine the success or failure of the development of composite materials.

通常のシリカゾルはおしなべてその分散媒が水であるた
め、有機物との混合分散には制限が 9− めシ、有機物と充分に混合または反応させることができ
ないので、上記した複合材料へのオU用が難しい。シリ
カゾルを広く有機工業に応用するには、その分散媒會水
から有機溶媒に代えることが、つまジオルガノシリカゾ
ルを製造することが必袈であって、そのオルガノシリカ
ゾルが高濃度で且つ安定な場合には、接着剤、塗料。
Since the dispersion medium of ordinary silica sol is water, there is a limit to its mixing and dispersion with organic matter. is difficult. In order to widely apply silica sol to the organic industry, it is necessary to replace the dispersion medium water with an organic solvent and to produce diorganosilica sol, and if the organosilica sol is highly concentrated and stable. Includes adhesive and paint.

樹脂加工などへ広く′!u用することができる。Widely used for resin processing, etc. It can be used for u.

ところで、有機溶剤に分散した無機酸化物ゾルの製造方
法としては、米国%許第2285446〜228544
9号に示ちれているように、水を分散媒とする酸化物ゾ
ルと、水と共沸組成′4を有する極性有機溶剤を混合し
て共沸で水を除去する方法、特公昭53−799号に示
されているように、水ガラスの中和水酊液からシロキシ
ン2ノールを極性有機溶剤で抽出分離し、得られた浴液
中にオルガノシリ々化剤を添加して製造する方法などが
従来知られている。しかし、前者の方法は加熱操作時に
シリカ粒子の衝突による凝集作用が起るためゾルの安定
性が悪化するばかpでなく、低沸点の有機溶剤を用いる
場合は。
By the way, as a method for producing an inorganic oxide sol dispersed in an organic solvent, US Pat.
As shown in No. 9, a method of removing water azeotropically by mixing an oxide sol using water as a dispersion medium and a polar organic solvent having an azeotropic composition of '4 with water, Japanese Patent Publication No. 53 As shown in No. 799, siloxine 2-nor is extracted and separated from the neutralized water solution of water glass using a polar organic solvent, and an organosiliconizing agent is added to the resulting bath solution. etc. are conventionally known. However, in the former method, the stability of the sol deteriorates due to the agglomeration effect caused by the collision of silica particles during the heating operation.In addition, when an organic solvent with a low boiling point is used.

共沸に際して有機溶剤の蒸発割合が水のそれに比較して
多いため、多蓋の有機溶剤が消費されてしまう欠点があ
る。一方後者の方法は水ガラスを中和する工程があるた
めにナトリウム塩の混入が避けられず、゛またシリカが
低分子−であることから、高濃度で且つ安定なオルガノ
シリカゾルt(4!ることは困難である。また、低沸点
の極性有機溶剤を用いて抽出法で行う場合は。
During azeotroping, the evaporation rate of the organic solvent is higher than that of water, so there is a drawback that a large amount of organic solvent is consumed. On the other hand, in the latter method, contamination with sodium salt is unavoidable due to the step of neutralizing water glass, and since silica has a low molecular weight, a highly concentrated and stable organosilica sol (4! It is also difficult to do so when extraction is performed using a polar organic solvent with a low boiling point.

シリカの収率が低いために安価にオルガノシリカゾル′
f:得ることができないばか9でなく1作業の面で細心
の注意と管理を行ってもなお再現性に乏しい欠点がおる
Because the yield of silica is low, organosilica sol′ can be produced at low cost.
f: Idiot who can't get it 9 Even if you pay close attention and control to each work, there is still a drawback of poor reproducibility.

本発明は上記した従来法の欠点を解消し、各棟のM@溶
剤に対して分散性にすぐれ、しかも高濃度で且つ安定な
オルガノシリカゾルの製造方法を提供することケ目的と
するものであって。
The purpose of the present invention is to eliminate the drawbacks of the conventional methods described above, and to provide a method for producing an organosilica sol that has excellent dispersibility in the M@solvent of each building, and is highly concentrated and stable. hand.

その方法は水を分散媒としたシリカゾルと有機溶剤と全
混合した後、限外濾過膜で脱水すること全特徴とする。
The method is characterized by completely mixing silica sol using water as a dispersion medium and an organic solvent, and then dehydrating the mixture using an ultrafiltration membrane.

本発明の方法に於て出発原料とし゛C使用されるところ
の水を分散媒としたシリカゾルは、イオン交換法、解膠
法、透析法など何れの方法で製造され六−ものでも良い
が、シリカの平均粒子径は40Xから100OXの範囲
であることが好止1.<、1時K 70 Xから300
Xの範囲のものが本発明には好適である。またシリカ繊
度はSin、として15重散慢以上のものが有機溶剤の
使用−紫節減できるので経済的である。
The silica sol using water as a dispersion medium, which is used as a starting material in the method of the present invention, may be produced by any method such as ion exchange method, peptization method, or dialysis method. It is preferable that the average particle size of 1. is in the range of 40X to 100OX. <, 1 o'clock K 70 X to 300
Those within the range of X are suitable for the present invention. Furthermore, the silica fineness of 15% or more is economical because the use of organic solvents can be reduced.

有機浴剤としては、メタノール、エタノール。Organic bath agents include methanol and ethanol.

ゾロノRノール眸のアルコール類、ジメチルエーテル等
のエーテル類、アセトン、エチルメチルケトン静のケト
ン類、酢酸エチル等のエステル類で例示される水m性有
機溶剤が使用可能である。これらの水m性有機溶剤は二
種以上を併用しても差支えない。
Aqueous organic solvents such as alcohols, ethers such as dimethyl ether, acetone, ketones such as ethyl methyl ketone, and esters such as ethyl acetate can be used. Two or more of these water-based organic solvents may be used in combination.

本発明の方法による分散媒の置換tよ、水を分散媒とし
たシリカゾルに上記した水溶性有機浴剤を混合し、限外
濾過膜にて水と有機溶剤の共存した液を濾過して濃縮を
行い、得られた濃縮 5− 物VC拘度有機溶剤を添加して希釈し、 F)[限外濾
過膜処理を施す操作を複数回くシかえずことによって行
なわれる。この場合、限外濾過を回分式に行わずに連続
的に行うこともできる。
Replacing the dispersion medium according to the method of the present invention, the water-soluble organic bath agent described above is mixed with the silica sol using water as the dispersion medium, and the liquid in which water and organic solvent coexist is filtered and concentrated using an ultrafiltration membrane. The concentrated product obtained is diluted by adding a VC-restricted organic solvent, and F) [ultrafiltration membrane treatment is performed by repeating the procedure several times. In this case, ultrafiltration can also be carried out continuously without being carried out batchwise.

有機溶剤と置換したシリカゾルの安定性は、水の残存量
によって異なるので、好ましくは有機溶剤対水の重量組
成比が100:0.1から100ニア、5の範囲になる
よう上記の操作tくシかえすことt可とする。水を分散
媒としたシリカゾルと有機溶剤の混合方法は、シリカゾ
ルへ有機浴剤を添加しても、また有機溶剤へシリカゾル
を添加してもかまわないが、有機溶剤の蒸発をなるべく
少なくシ、充分に混合することが肝要である。また、混
合に使用される装置には攪拌機。
The stability of the silica sol substituted with an organic solvent varies depending on the remaining amount of water, so it is preferable to carry out the above steps so that the weight composition ratio of organic solvent to water is in the range of 100:0.1 to 100:5. It is possible to return. The mixing method of silica sol and organic solvent using water as a dispersion medium may be done by adding an organic bath agent to the silica sol, or by adding the silica sol to the organic solvent, but the evaporation of the organic solvent should be minimized and the evaporation should be kept as low as possible. It is important to mix the Also, the equipment used for mixing is a stirrer.

ミキサーその他の混合機がいずれも使用可能である。Any mixer or other mixing device can be used.

限外濾過膜としては、孔径数芙から数uXのものであれ
ば使用できるが、原料とするシリカゾルのシリカ粒子径
、シリカ製置および使用される有機溶剤等を考慮しなが
ら選択し、瀘過条 6− 件を決める必要が必る。これらの条件に注意すれば、合
成樹脂系限外濾過膜の何れもが使用可能であると共に、
その形状も平板隔膜状、ノリ巻状、中空繊維状などの各
種形状のものが使用できる。また限外濾過に際しての圧
力6.膜の使用条件に合わせた操作圧力で充分目的′f
、達成することができるが、限外龍過器の運転中におけ
るシリカゾルの乾燥を防止するには低温下で行うか、ま
たは完全密閉状態にて操作するのが望ましい。
Any ultrafiltration membrane that has a pore size of several micrometers to several micrometers can be used, but it should be selected while taking into account the silica particle size of the silica sol used as a raw material, the silica preparation, the organic solvent used, etc. Article 6- It is necessary to decide on the conditions. If these conditions are taken into account, any synthetic resin ultrafiltration membrane can be used, and
Various shapes such as a flat diaphragm shape, a seaweed shape, and a hollow fiber shape can be used. Also, the pressure during ultrafiltration6. The operating pressure that matches the membrane usage conditions is sufficient for the purpose'f
However, in order to prevent the silica sol from drying out during operation of the ultrafilter, it is preferable to operate at a low temperature or in a completely closed state.

なお1本発明の方法によって得られたオルガノシリカゾ
ルの濃度調整は、溶剤全分離除去することによって行う
が1%に低沸点の溶剤を用いた場合tよ、高譲鮭壕で濃
縮でき、メチルアルコール等の場合60重M′チ゛まで
の濃縮が可能である。但し、尚#度ゾルは乾燥しやすい
丸めに。
Note that the concentration of the organosilica sol obtained by the method of the present invention is adjusted by completely separating and removing the solvent, but if a low-boiling point solvent is used for 1%, it can be concentrated in a high yielding tank, and methyl alcohol In such cases, it is possible to concentrate up to 60 times M'. However, the #degree sol should be rolled up so that it dries easily.

濃縮液の取扱いKtま注意を要する。また1本発明の反
応機構等の峰純に関しては、シリカゾルの構造が明確に
解析されていないため不明な点もめるが、7’cとえば
シリカ粒子表面−ま水酸基で覆われ、更に1分子以上の
水利膜が介在して有機溶剤に分散した状態II′chυ
、これがゾルの安定化に役立っているものと推定される
Care must be taken when handling the concentrate. Regarding the purity of the reaction mechanism of the present invention, there are some points that are unclear because the structure of silica sol has not been clearly analyzed, but for example, 7'c, the surface of a silica particle is covered with hydroxyl groups, and one or more molecules II'chυ dispersed in an organic solvent with a water-conserving membrane intervening
It is presumed that this helps stabilize the sol.

次に比較例と実施例を挙げて説明するが、実施例は本発
明の範囲を制限するものではない。
Next, explanation will be given with reference to comparative examples and examples, but the examples are not intended to limit the scope of the present invention.

比較例1 本比較例は後述する本発明の方法で行った実施例全理解
しやすくするためのものである。
Comparative Example 1 This comparative example is provided to facilitate understanding of all the examples carried out by the method of the present invention, which will be described later.

本発明の特徴である限外濾過膜を使用しないで、有機溶
剤を分散媒としたシリカゾルを作るため、水を分散媒と
するシリカゾル(Sin、 一度20重蓋饅、平均粒子
径120 X、 sro、7N日、0重蓋比500)1
00dとエチルアルコール(純度99%以上)ioom
a會良く混合した後、500dのエノ々ボレーター用ナ
ス型フラスコに注ぎ、オイルノ々スで加温しながら脱水
しfc。この際ナス型フラスコ内の液面を一定に保ちな
がら、新fcなエチルアルコール<9oorrrl補給
した。しかる後フラスコ内のMWIi’ 50 ynl
になるまで濃縮し*、、なお、蒸発する水とエテルアル
コール1よ、コンデンサーで冷却して補集した。
In order to make silica sol using an organic solvent as a dispersion medium without using an ultrafiltration membrane, which is a feature of the present invention, silica sol using water as a dispersion medium (Sin, 20 layers at a time, average particle size 120X, sro , 7N days, 0 heavy lid ratio 500) 1
00d and ethyl alcohol (purity 99% or more) ioom
After mixing thoroughly, pour into a 500d eggplant-shaped flask for an enovolator, and dehydrate while heating with an oil spray. At this time, <9 oorrrl of new fc ethyl alcohol was replenished while keeping the liquid level in the eggplant-shaped flask constant. Afterwards MWIi' 50 ynl in the flask
The evaporated water and ether alcohol were collected by cooling in a condenser.

このようにして得られたオルガノシリカゾルは、水分含
有量も多く、他の有機溶剤−\の相溶性は良くなかった
The organosilica sol thus obtained had a high water content and poor compatibility with other organic solvents.

比較例2 有機溶剤としてイソプロピルアルコール(純度99%以
上)f:用いた以外は比較例1と同じ処法でオルガノシ
リカゾルを作った。
Comparative Example 2 An organosilica sol was prepared in the same manner as in Comparative Example 1, except that isopropyl alcohol (purity 99% or higher) f: was used as the organic solvent.

このようにして得られたオルガノシリカゾルは粘度の高
いものであった。
The organosilica sol thus obtained had a high viscosity.

実施例1 水を分散媒とするシリカゾル(8i0.411度20重
、t%、平均粒子径120 i 、Sin、/NatO
重蓋比500 ) 10100Oとエチルアルコール(
純度99チ以上)1000di良く混合した後、限外濾
過膜(分画分子蓋50000 )にて濾過を行い。
Example 1 Silica sol using water as a dispersion medium (8i 0.411 degrees 20%, t%, average particle size 120i, Sin, /NatO
Heavy lid ratio 500) 10100O and ethyl alcohol (
After mixing well for 1000 di (purity: 99 or higher), filtration was performed using an ultrafiltration membrane (fraction molecule lid 50,000).

濾水量が1oooauに達t、fC,時、さらに母液へ
新たなエチルアルコール1000mgを添加した。その
後同様に濾過ケ行い、濾水蓋100100Oを採取−〇
 − した。この操作全全部で6回行い、シリカ濃度20.1
重蓋饅のシリカゾル980gを得た。
When the amount of filtration reached 1 oooau, 1000 mg of fresh ethyl alcohol was added to the mother liquor. Thereafter, filtration was carried out in the same manner, and 100,100 O of the filter cap was collected. This operation was performed 6 times in total, and the silica concentration was 20.1.
980 g of silica sol was obtained.

このようにして得られたオルガノシリカゾルは、水分含
有量も少なく、他の有機溶剤との相溶性は良いものであ
った。また、さらに限外濾過Mにて上述のオルガノシリ
カゾルヲ譲縮し。
The organosilica sol thus obtained had a low water content and good compatibility with other organic solvents. Further, the above-mentioned organosilica sol was further reduced by ultrafiltration M.

シリカ濃度30.5重量饅のシリカゾル641g會得た
641g of silica sol with a silica concentration of 30.5% by weight was obtained.

このようにして得られた#紬オルガノシリカゾルは、粘
度も低く、他の有機溶剤への相溶性は良いものでめった
The #Pongee organosilica sol thus obtained had low viscosity and good compatibility with other organic solvents.

実施例2 水を分散媒とするシリカゾル(StO,濃度20重量饅
、平均粒子径120 i 、 8i02/Na、0重蓋
比500)1000TILlとイソプロピルアルコール
(純度99%以上)tooomll良く混合した彼。
Example 2 1000 TIL of silica sol (StO, concentration 20% by weight, average particle diameter 120, 8I02/Na, zero-cover ratio 500) using water as a dispersion medium and too much isopropyl alcohol (purity 99% or more) were mixed well.

限外濾過M(分画分子蓋50000 )Kて実施例1と
同じ処法で全部で6回濾過を行い、シリカ濃度30.1
重t%のオルガノシリカゾル630gを得た。
Using ultrafiltration M (fraction molecule lid 50000) K, filtration was performed a total of 6 times using the same method as in Example 1, and the silica concentration was 30.1.
630 g of organosilica sol with weight t% was obtained.

このようにし、て得られたオルガノシリカゾルは、水分
含有−も少なく、他の有+1&溶剤への相溶性は良いも
のであつ′fC,。
The organosilica sol thus obtained has low water content and good compatibility with other solvents.

次に各比較例および実施例で得られたオルガノシリカゾ
ルの4!I8i有機溶剤に対する分散性を評価すべく、
オルガノシリカゾルを個別に有機溶剤とl:1の皿−比
で混付し、混合液の分散状mTh観観1た。また、オル
ガノシリカゾルの粘度奮25°Cの恒温下でオストワル
ド法により測定した。なお、水分はカールフィッシャー
法にて測定した。結果を表−1に示す。
Next, 4! of the organosilica sols obtained in each comparative example and example. In order to evaluate the dispersibility in I8i organic solvent,
The organosilica sol was individually mixed with an organic solvent in a dish ratio of 1:1, and the dispersion mTh of the mixture was observed. In addition, the viscosity of organosilica sol was measured by the Ostwald method at a constant temperature of 25°C. In addition, water content was measured by the Karl Fischer method. The results are shown in Table-1.

(以下余白〕 上表から明らかな通シ1本発明の方法によれば、各種の
有機溶剤に対する分散性eζすぐれ。
(The following is a blank space) It is clear from the above table that: 1. According to the method of the present invention, the dispersibility in various organic solvents is excellent.

高濃度で目、つ安定なオルガノシリカゾルを製造するこ
とがで色、有機物と組合わせた複合材料へ広く利用可能
なオルガノシリカゾルライ(することができ/E、。
At high concentrations, a highly stable organosilica sol can be produced, making it a widely applicable organosilica sol (Ly/E), which can be combined with organic matter to produce composite materials.

%W[出願人   触媒化成]:業株式会社13−%W [Applicant: Catalyst Chemicals]: Gyo Co., Ltd. 13-

Claims (1)

【特許請求の範囲】 1、水を分散媒としたシリカゾルと有機溶剤とを混合し
た後、限外濾過膜で脱水することを特徴とする有機溶剤
を分散媒とするシリカゾルの製造方法。 2、水を分散媒とし九シリカゾルとしてシリカの平均粒
子径が40X〜100OXの範囲にあるシリカゾルを用
いる特許請求の範囲第1項記載゛の方法。 3、有機溶剤としてアルコール、エーテル、ケトン、エ
ステル等の水溶性有機溶剤を用いる特許請求の範囲第1
項記載の方法。 4、 シリカゾル中のシリカ粒子よシ小さい孔径を有す
る限外濾過膜で脱水する特許請求の範囲第1項記載の方
法。 5、限外濾過脱水によシシリカ濃度を8i0.として2
0〜60重量%にする特許請求の範囲第11− 項記載の方法。 6、水を分散媒としたシリカゾルに有機溶剤を混合して
限外濾過膜で脱水する操作を、新たな有機溶剤?連続的
に添加しながら連続的に行う特許請求の範囲第1項記載
の方法。
[Claims] 1. A method for producing silica sol using an organic solvent as a dispersion medium, which comprises mixing silica sol using water as a dispersion medium and an organic solvent, and then dehydrating the mixture using an ultrafiltration membrane. 2. The method according to claim 1, which uses water as a dispersion medium and uses a silica sol having an average particle size of silica in the range of 40X to 100OX. 3. Claim 1 in which a water-soluble organic solvent such as alcohol, ether, ketone, or ester is used as the organic solvent
The method described in section. 4. The method according to claim 1, wherein the water is dehydrated using an ultrafiltration membrane having a smaller pore size than the silica particles in the silica sol. 5. By ultrafiltration and dehydration, the silica concentration was reduced to 8i0. as 2
The method according to claim 11, wherein the concentration is 0 to 60% by weight. 6. Is the operation of mixing an organic solvent with silica sol using water as a dispersion medium and dehydrating it with an ultrafiltration membrane a new organic solvent? The method according to claim 1, which is carried out continuously with continuous addition.
JP11429482A 1982-06-30 1982-06-30 Preparation of silica sol using organic solvent as dispersion medium Granted JPS598614A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11429482A JPS598614A (en) 1982-06-30 1982-06-30 Preparation of silica sol using organic solvent as dispersion medium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11429482A JPS598614A (en) 1982-06-30 1982-06-30 Preparation of silica sol using organic solvent as dispersion medium

Publications (2)

Publication Number Publication Date
JPS598614A true JPS598614A (en) 1984-01-17
JPH021087B2 JPH021087B2 (en) 1990-01-10

Family

ID=14634253

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11429482A Granted JPS598614A (en) 1982-06-30 1982-06-30 Preparation of silica sol using organic solvent as dispersion medium

Country Status (1)

Country Link
JP (1) JPS598614A (en)

Cited By (10)

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US4772660A (en) * 1985-10-18 1988-09-20 Sumitomo Chemical Company, Limited Oxide sol using reactive monomer as dispersion medium
FR2684367A1 (en) * 1991-12-02 1993-06-04 Hoechst France Process for obtaining a silica sol dispersed in a lower alkanol and application of the organosol thus obtained, especially to the preparation of compositions for the surface coating of organic glass
EP0699626A1 (en) 1994-08-05 1996-03-06 Nissan Chemical Industries Ltd. A method of preparing a propanol sol of silica
JP2001213617A (en) * 2000-01-28 2001-08-07 Jsr Corp Process of producing hydrophobic colloidal silica
EP1754685A2 (en) 2005-08-02 2007-02-21 Nissan Chemical Industries, Ltd. Organosol of silica and process for producing the same
WO2009101974A1 (en) 2008-02-12 2009-08-20 Nissan Chemical Industries, Ltd. Colloidal silica particles, process for producing the same, and silica sol in organic solvent, silica sol in polymerizable compound, and silica sol in dicarboxylic anhydride each obtained from the same
JP2015034106A (en) * 2013-08-08 2015-02-19 信越化学工業株式会社 Organosol and production method thereof
US9272916B2 (en) 2007-11-30 2016-03-01 Jgc Catalysts And Chemicals Ltd. Non-spherical silica sol, process for producing the same, and composition for polishing
JP2019151498A (en) * 2018-02-28 2019-09-12 株式会社ダイセル Method for producing nanodiamond organic solvent dispersion
CN113636562A (en) * 2021-09-02 2021-11-12 上海新安纳电子科技有限公司 Silicon dioxide dispersion liquid and preparation method and application thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4772660A (en) * 1985-10-18 1988-09-20 Sumitomo Chemical Company, Limited Oxide sol using reactive monomer as dispersion medium
FR2684367A1 (en) * 1991-12-02 1993-06-04 Hoechst France Process for obtaining a silica sol dispersed in a lower alkanol and application of the organosol thus obtained, especially to the preparation of compositions for the surface coating of organic glass
EP0699626A1 (en) 1994-08-05 1996-03-06 Nissan Chemical Industries Ltd. A method of preparing a propanol sol of silica
US5902226A (en) * 1994-08-05 1999-05-11 Nissan Chemical Industries, Ltd. Method of preparing a propanol sol of silica
JP4631119B2 (en) * 2000-01-28 2011-02-16 Jsr株式会社 Method for producing hydrophobized colloidal silica
JP2001213617A (en) * 2000-01-28 2001-08-07 Jsr Corp Process of producing hydrophobic colloidal silica
EP1754685A2 (en) 2005-08-02 2007-02-21 Nissan Chemical Industries, Ltd. Organosol of silica and process for producing the same
JP2007063117A (en) * 2005-08-02 2007-03-15 Nissan Chem Ind Ltd Silica sol dispersed in organic solvent and process for producing the same
US9272916B2 (en) 2007-11-30 2016-03-01 Jgc Catalysts And Chemicals Ltd. Non-spherical silica sol, process for producing the same, and composition for polishing
US10160894B2 (en) 2007-11-30 2018-12-25 Jgc Catalysts And Chemicals Ltd. Non-spherical silica sol, process for producing the same, and composition for polishing
WO2009101974A1 (en) 2008-02-12 2009-08-20 Nissan Chemical Industries, Ltd. Colloidal silica particles, process for producing the same, and silica sol in organic solvent, silica sol in polymerizable compound, and silica sol in dicarboxylic anhydride each obtained from the same
US9284197B2 (en) 2008-02-12 2016-03-15 Nissan Chemical Industries, Ltd. Colloidal silica particles, process for producing the same, and organic solvent-dispersed silica sol, polymerizable compound-dispersed silica sol, and dicarboxylic anhydride-dispersed silica sol each obtained from the same
US9376322B2 (en) 2008-02-12 2016-06-28 Nissan Chemical Industries, Ltd. Process for producing colloidal silica particles
US9527749B2 (en) 2008-02-12 2016-12-27 Nissan Chemical Industries, Ltd. Colloidal silica particles, process for producing the same, and organic solvent-dispersed silica sol, polymerizable compound-dispersed silica sol, and dicarboxylic anhydride-dispersed silica sol each obtained from the same
JP2015034106A (en) * 2013-08-08 2015-02-19 信越化学工業株式会社 Organosol and production method thereof
JP2019151498A (en) * 2018-02-28 2019-09-12 株式会社ダイセル Method for producing nanodiamond organic solvent dispersion
CN113636562A (en) * 2021-09-02 2021-11-12 上海新安纳电子科技有限公司 Silicon dioxide dispersion liquid and preparation method and application thereof

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