JPS6163527A - Method for improving fluidity of lime powder - Google Patents

Method for improving fluidity of lime powder

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Publication number
JPS6163527A
JPS6163527A JP18399484A JP18399484A JPS6163527A JP S6163527 A JPS6163527 A JP S6163527A JP 18399484 A JP18399484 A JP 18399484A JP 18399484 A JP18399484 A JP 18399484A JP S6163527 A JPS6163527 A JP S6163527A
Authority
JP
Japan
Prior art keywords
lime powder
fluidity
formula
organopolysiloxane
general formula
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
JP18399484A
Other languages
Japanese (ja)
Other versions
JPH0121097B2 (en
Inventor
Shigeru Mori
滋 森
Yutaka Harasawa
原沢 裕
Tetsuya Mayuzumi
黛 哲也
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.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical 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 Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP18399484A priority Critical patent/JPS6163527A/en
Publication of JPS6163527A publication Critical patent/JPS6163527A/en
Publication of JPH0121097B2 publication Critical patent/JPH0121097B2/ja
Granted legal-status Critical Current

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  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

PURPOSE:To improve the fluidity of lime powder, quickly, safely, easily, surely and economically, by adding a specific amount of organopolysiloxane or cyclic organopolysiloxane represented by a specific general formula to lime powder. CONSTITUTION:100pts.wt. of lime powder finer than 100 mesh is mixed with 0.01-1pt.wt. of one or more compounds selected from the organopolysiloxane of formula I; Ra<1>(R<2>O)bSi(4-a-b)/2 and having -OR<2> at the molecular terminal, and a cyclic organopolysiloxane of general formula II (R<1> and R<2> are same or different hydrocarbon group; 0<=a<4; 0<a+b<=4; n is 3-10), in the absence of solvent at room temperature-100 deg.C. The fluidity of lime powder can be improved safely, easily and surely by the above treatment.

Description

【発明の詳細な説明】 産業上の利用 本発明は石灰粉の流動性を改善する方法に関し、更に詳
述すると操作上安全にしかも簡単かつ確実に石灰粉のm
s性を改善することができる石灰粉流動性改善方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION Industrial Application The present invention relates to a method for improving the fluidity of lime powder, and more specifically, to a method for improving the fluidity of lime powder in an operationally safe, simple and reliable manner.
The present invention relates to a method for improving lime powder fluidity that can improve s properties.

従来技術及びその  − 従来より、石灰粉、特に生石灰粉は耐火物製造、バルブ
及び紙の処理剤、脱硫剤等として有効に使用されている
が、生石灰粉は吸湿性を有するため、そのままでは吸湿
して流動性がなくなるので取り扱いに不便を生じる。
Prior art and related technologies - Lime powder, especially quicklime powder, has been effectively used in the manufacture of refractories, as a treatment agent for valves and paper, as a desulfurizing agent, etc. However, since quicklime powder has hygroscopic properties, it does not absorb moisture as it is. It becomes inconvenient to handle because it loses its fluidity.

このために従来、生石灰等の石灰粉の流動性を改善する
方法として、石灰粉をメチルハイドロジエンポリシロキ
サン、末端トリメチルジメチルシロキサン、末端水酸基
ジメチルシロキサン、末端トリメチルシロキシメチルメ
トキシポリシロキサン等で処理する方法が提案されてい
る(特開昭55−47223@、特開昭58−1205
19号、特公昭57−7085号、特公昭57−708
7号)。
To this end, a conventional method for improving the fluidity of lime powder such as quicklime is to treat lime powder with methylhydrodiene polysiloxane, terminal trimethyldimethylsiloxane, terminal hydroxyl dimethylsiloxane, terminal trimethylsiloxymethylmethoxypolysiloxane, etc. has been proposed (JP-A-55-47223@, JP-A-58-1205
No. 19, Special Publication No. 57-7085, Special Publication No. 57-708
No. 7).

しかしながら、メチルハイドロジエンポリシロキサンを
石灰粉の流動性改善剤として用いる方法は、処理が進む
に従い水素ガスが発生し、爆発の危険性が生じる。例え
ば、石灰粉100牙をで示されるメチルハイドロジエン
ポリシロキサン0.19で処理すると、最大36 yl
の水素ガスが発生する。従って、石灰粉を容器内で処理
したり処理品を貯蔵する場合、水素ガスの爆発範囲外に
するため、不活性ガスや不燃性溶剤(塩素化溶剤等)で
希釈したり、容器の開口部を大きくする必要があるが、
希釈処理を行なうことは煩雑である上、特に不燃性溶剤
で希釈した場合には後工程で溶剤を除去しなければなら
ない面倒がある。また、容器の開口部を大きくした場合
、処理が進んで石灰粉の流動性が増大すると粉体が飛散
するおそれが生じる。
However, in the method of using methylhydrodiene polysiloxane as a fluidity improver for lime powder, hydrogen gas is generated as the treatment progresses, creating a risk of explosion. For example, when 100 lime powder is treated with 0.19 methyl hydrodiene polysiloxane, up to 36 yl
of hydrogen gas is generated. Therefore, when processing lime powder or storing processed products in a container, it is necessary to dilute it with an inert gas or nonflammable solvent (chlorinated solvent, etc.) to keep it out of the explosion range of hydrogen gas, or to close the opening of the container. It is necessary to increase the
Dilution treatment is complicated, and especially when diluted with a nonflammable solvent, the solvent must be removed in a subsequent step, which is a hassle. Furthermore, if the opening of the container is made large, there is a risk that the powder will scatter as the treatment progresses and the fluidity of the lime powder increases.

また、末端トリメチルシリル又は末端水B基ジメチルポ
リシOキサンを流動性改善剤とした場合は、長時間の処
Iffvf間を要し、流動性改善効果が発現するまでに
かなりの時間を必要とする上、強力な撹拌処理を行なわ
なければならず、処理性に問題がある。
In addition, when terminal trimethylsilyl or terminal water B group dimethylpolysiloxane is used as a fluidity improving agent, a long treatment time is required, and a considerable amount of time is required for the fluidity improvement effect to appear. , it is necessary to carry out a strong stirring process, which poses a problem in processability.

更に、末端トリメチルシリルメチルメトキシポリシロキ
サンを用いる方法は、この化合物自体を製造するのが?
lJ、雑で、コストが高価なものになる。
Furthermore, is there a method using terminal trimethylsilylmethylmethoxypolysiloxane to produce this compound itself?
lJ, it is sloppy and expensive.

11悲11 本発明者らは、上記事情に鑑み、安全に作業でき、しか
も作業性の良好な石灰粉の流動性改善方法につぎ鋭意検
討を行なった結果、下記一般式%式%() で示され、分子鎖末端が一〇R2であるオルガノで示さ
れる環状オルガノポリシロキサン(ここで、上記式にお
いて、RL 、R2はそれぞれ互に同種又は異種の炭化
水素基、0≦a<4.Q<b≦4゜Q<a+b≦4.n
=3〜10である)から選ばれる1種又は2種以上の化
合物が石灰粉流動性改善剤として優れた特性を有し、こ
の種の化合物を石灰粉100部(重量部、以下同じ)に
対して0.01〜1部の割合で用いて処理を行なうこと
により、上記目的を達成し得ることを知見した。
11 Sad 11 In view of the above circumstances, the present inventors have conducted extensive studies on a method for improving the fluidity of lime powder that is safe to work with and has good workability.As a result, the following general formula % formula % () Cyclic organopolysiloxane represented by an organo group having a molecular chain terminal of 10R2 (wherein, in the above formula, RL and R2 are mutually the same or different hydrocarbon groups, 0≦a<4.Q <b≦4゜Q<a+b≦4.n
= 3 to 10) has excellent properties as a lime powder fluidity improver, and this type of compound is added to 100 parts (parts by weight, the same hereinafter) of lime powder. It has been found that the above object can be achieved by using 0.01 to 1 part of the above object.

即ち、上記の化合物を用いて石灰粉の処理を行なった場
合、水素ガスの発生がなく、またメチルアルコールのよ
うな可燃性ガスの発生も少ないので、安全に作業でき、
しかもこのように水素ガスの発生がなく、メチルアルコ
ールの発生が少ないため、不活性ガスや不燃性溶剤で希
釈する必要がない上、空温で作業でき、必ずしも強い撹
拌を行なわなくてもよく、更に石灰粉に対し微量の使用
でかつ比較的短時間で流動性改善効果を付与することが
できるなど、作業性が良好で簡単かつ確実に石灰粉の流
動性を改善し得、また上記化合物は比較的簡単に製造で
きて安価であるため、処I!l費を低減し得ることを知
見し、本発明をなすに至ったちのである。
In other words, when lime powder is treated using the above compound, there is no generation of hydrogen gas, and there is little generation of flammable gases such as methyl alcohol, so the work can be done safely.
Moreover, since no hydrogen gas is generated and little methyl alcohol is generated, there is no need to dilute with inert gas or nonflammable solvent, and work can be done at air temperature, so strong stirring is not necessarily required. Furthermore, the fluidity improving effect of lime powder can be imparted to lime powder in a relatively short amount of time using only a small amount, and the above-mentioned compounds have good workability and can easily and reliably improve the fluidity of lime powder. Because it is relatively easy to manufacture and inexpensive, it is It was discovered that the cost could be reduced, and the present invention was developed.

以下、本発明につき更に詳しく説明する。The present invention will be explained in more detail below.

11へ11 本発明の石灰粉流動性改善方法は、生石灰、消石灰、炭
酸カルシウム等の石灰粉、特に100メツシユより細か
い粒度の石灰粉の流動性を改善するのに好適に採用し得
、これらの石灰粉を下記一般式(I) R1α (R20)b 5LOiii ・・・(1)ス で示され、分子鎖末端が一〇R2であるオルガノポリシ
ロキサン及び下記一般式(n) で示される環状オルガノポリシロキサン(ここで、上記
式において、R1、R2はそれぞれ互に同種又は異種の
炭化水素基、0≦a <4.Q<b≦4゜Q < a+
5≦4.n =3〜10である)から選ばれる1種又は
2種以上の化合物でlI!11!l!することを特徴と
するものである。
11 to 11 The method for improving the fluidity of lime powder of the present invention can be suitably employed to improve the fluidity of lime powder such as quicklime, slaked lime, calcium carbonate, etc., especially lime powder with a particle size finer than 100 mesh. Lime powder is combined with an organopolysiloxane represented by the following general formula (I) R1α (R20)b 5LOiii...(1), whose molecular chain ends are 10R2, and a cyclic organopolysiloxane represented by the following general formula (n). Polysiloxane (here, in the above formula, R1 and R2 are the same or different hydrocarbon groups, 0≦a<4.Q<b≦4゜Q<a+
5≦4. lI! with one or more compounds selected from n = 3 to 10). 11! l! It is characterized by:

ここで、末端OR2基を有する(I)式及び(ff>式
の化合物としては、R1及びR2がそれぞれメチル基、
エチル基等の低級アルキル基であり、特にメチル基であ
るものが好適に用いられる。
Here, as for the compounds of the formula (I) and the formula (ff> having a terminal OR2 group, R1 and R2 are each a methyl group,
A lower alkyl group such as an ethyl group, particularly a methyl group, is preferably used.

また末端OR2基を有する(I>式の化合物としては、
メトキシ基含有量が34〜65重邑%のものが好ましく
使用される。
Moreover, as a compound of the formula (I>) having a terminal OR2 group,
Those having a methoxy group content of 34 to 65% by weight are preferably used.

更に、上記の化合物としては、粘度が25℃において1
〜500 C81特に1〜100csのものが好ましい
Furthermore, the above compound has a viscosity of 1 at 25°C.
~500 C81 Especially preferred is 1 to 100 cs.

なお、上記化合物は公知の方法で製造し得る。In addition, the said compound can be manufactured by a well-known method.

例えば、トリクロルメチルシランにメチルアルコールと
水を反応させる脱塩酸部分メトキシ化加水分解法、トリ
クロルメチルシランにメチルアルコールを反応させてク
ロルメトキシメチルシランを1qた侵、これを水素又は
塩化第二鉄の存在下で脱メチルクロライドする部分メト
キシシランの脱メチルクロライド重合法などを用いて製
造することができる。
For example, a dehydrochloric acid partial methoxylation hydrolysis method in which trichloromethylsilane is reacted with methyl alcohol and water, a method in which trichloromethylsilane is reacted with methyl alcohol to produce 1 q of chloromethoxymethylsilane, and this is reacted with hydrogen or ferric chloride. It can be produced using a method such as demethylchloride polymerization of partial methoxysilane in which demethylchloride is performed in the presence of methoxysilane.

本発明は上記化合物を用いて石灰粉を処理するものであ
るが、この場合上記化合物の使用量は石灰粉100部に
対し0.01〜1部とするものであり、使用量がO,O
IJMより少ない場合、1部より多い場合のいずれも石
灰粉流動性改善効果が十分発揮されない。なお、上記化
合物の好適な使用母範囲は石灰粉100部に対し0.1
〜0.5部である。
The present invention is to treat lime powder using the above compound, but in this case, the amount of the above compound used is 0.01 to 1 part per 100 parts of lime powder, and the amount used is O, O.
When the amount is less than IJM, and when it is more than 1 part, the lime powder fluidity improving effect is not sufficiently exhibited. In addition, the preferred range of use of the above compound is 0.1 parts per 100 parts of lime powder.
~0.5 part.

上記化合物で石灰粉を処理する方法としては、通常採用
されている方法を用いることができ、例   □えば石
灰粉に上記化合物を添加し、振盪撹拌等の適宜な撹拌法
を使用して石灰粉に上記化合物を均一に混合する方法が
採用し得る。この場合、撹拌は必ずしも強撹拌でなくて
もよい。処理温度は特に制限されず、室温〜100℃と
することができるが、室温で十分処理でき、本発明によ
れば雰囲気温度で混合処理することにより流動性の高い
石灰粉を確実に1ηることができる。また、処理時間も
限定されないが、通常10分〜1時間であり、本発明に
よれば比較的短時間の処理で石灰粉の流動性を改善し得
る。なお、本発明においては、水素ガスは発生せず、メ
チルアルコール発生けも非常に少ないため、不活性ガス
や不燃性ガスで希釈する必要はなく、空気雰囲気下で処
理を行なうことができ、無溶剤状態で処理し得る。
As a method for treating lime powder with the above compound, a commonly adopted method can be used. For example, the above compound is added to lime powder, and the lime powder is treated using an appropriate stirring method such as shaking and stirring. A method may be adopted in which the above-mentioned compounds are uniformly mixed. In this case, stirring does not necessarily have to be strong stirring. The treatment temperature is not particularly limited and can be from room temperature to 100°C, but it can be sufficiently treated at room temperature, and according to the present invention, highly fluid lime powder can be reliably produced at 1η by mixing at ambient temperature. I can do it. Further, the treatment time is not limited, but is usually 10 minutes to 1 hour, and according to the present invention, the fluidity of lime powder can be improved with a relatively short treatment time. In addition, in the present invention, hydrogen gas is not generated and methyl alcohol is generated very little, so there is no need to dilute with inert gas or nonflammable gas, and the treatment can be carried out in an air atmosphere. Can be processed in solvent.

11匹11 以上述べたように、本発明の石灰粉流動性改善方法は特
定のオルガノポリシロキサンを特定ffi lff1用
したことにより、水素の発生をなくシ、かつメチルアル
コールの発生を少なくして安全に処理を行なうことがで
き、かつ室温において比較的短時間で処理し1りる上、
微量の処理剤を用いるだけで十分高い流動性を有する石
灰粉を確実に(qることができ、しかもコスト的にも安
価である。
As mentioned above, the lime powder fluidity improvement method of the present invention uses a specific organopolysiloxane to eliminate hydrogen generation and reduce methyl alcohol generation, making it safe. It can be processed in a relatively short time at room temperature, and
It is possible to reliably produce lime powder with sufficiently high fluidity by using only a small amount of processing agent, and it is also inexpensive.

以下、実施例と比較例を示し、本発明を具体的に説明す
るが、本発明は下記の実施例に制限されるものではない
EXAMPLES Hereinafter, the present invention will be specifically explained by showing examples and comparative examples, but the present invention is not limited to the following examples.

[実施例1.比較例1,2] JISフルイ#200メツシュバスの粒度を有する生石
灰1002にトリメトキシシランの加水分解物であるメ
チルメトキシポリシロキサン(メトキシ基含有ff13
9.8%、粘度7C3)をそれぞれ0.05牙、0.1
’)、0.310.52添加し、これを内容積160c
cのガラス瓶に入れて横型振盪機で2時間振罎した。
[Example 1. Comparative Examples 1 and 2] Methylmethoxypolysiloxane (methoxy group-containing ff13
9.8%, viscosity 7C3) respectively 0.05 fang and 0.1
'), 0.310.52 was added, and the internal volume was 160c.
The mixture was placed in a glass bottle (c) and shaken for 2 hours using a horizontal shaker.

比較のため、25℃における粘度が20csの末端トリ
メチルシリル基封鎖メチルハイドロジエンシロキサン(
比較例1)及び末端トリメチルシリル基封鎖ジメチルシ
ロキサンを用いて同様の処理を行なった。
For comparison, methylhydrodiene siloxane endblocked with trimethylsilyl groups and having a viscosity of 20 cs at 25°C was used.
Similar treatment was carried out using Comparative Example 1) and dimethylsiloxane endblocked with trimethylsilyl groups.

次に、以上の方法で処理された生石灰の安息角を測定し
、流動性を評価した。結果を第1表に示す。なお、未処
理の生石灰の安息角は53°であった。
Next, the angle of repose of the quicklime treated in the above manner was measured to evaluate its fluidity. The results are shown in Table 1. Note that the angle of repose of untreated quicklime was 53°.

第1表 [実施例2] 実施例1で用いた生石灰100部に対しメトキシ基含有
!21.3%のジメチルシロキシ単位とメチルメトキシ
シロキシ単位からなる末端メトキシ基コポリマー0.0
5’)、0.1?、0.3’)。
Table 1 [Example 2] Contains methoxy groups per 100 parts of quicklime used in Example 1! 0.0 methoxy-terminated copolymer consisting of 21.3% dimethylsiloxy units and methylmethoxysiloxy units
5'), 0.1? , 0.3').

0.52を添加し、実施例1と同様の処理を行なった。0.52 was added and the same treatment as in Example 1 was performed.

その結果、処理された生石灰はいずれも良好な流動性を
示し、その安息角はそれぞれ41°。
As a result, the treated quicklime all showed good fluidity, and their angle of repose was 41°.

39’ 、36’ 、36°であった。The angles were 39', 36', and 36°.

[比較例3] 実施例1で用いた生石灰100部に対しメチルトリメト
キシシラン0.1部を添加し、実施例1と同様の処理を
行なったが、処理された生石灰の安息角は4°であり、
流動性改善効果が十分認められなかった。
[Comparative Example 3] 0.1 part of methyltrimethoxysilane was added to 100 parts of quicklime used in Example 1, and the same treatment as in Example 1 was performed, but the angle of repose of the treated quicklime was 4°. and
The fluidity improvement effect was not sufficiently observed.

[実施例3.比較例4] 実施例1で用いた生石灰100部に対し、メトキシ基含
有ff142.2%のメチルメトキシポリシロキサン0
.1部及び実施例1で用いたメチルハイドロジエンシロ
キサン0.1部をそれぞれ添加し、実施例1と同様の処
理を行ない、その間に発生ずる水素及びメチルアルコー
ルの容器内雰囲気濃度をガスクロマトグラフィーによっ
て測定した。
[Example 3. Comparative Example 4] Methylmethoxypolysiloxane containing methoxy group ff142.2% was added to 100 parts of quicklime used in Example 1.
.. 1 part and 0.1 part of the methylhydrodienesiloxane used in Example 1 were added, and the same treatment as in Example 1 was carried out, and the atmospheric concentration of hydrogen and methyl alcohol generated in the container was measured by gas chromatography. It was measured.

その結果、メチルメトキシポリシロキサンの場合は、2
5℃の処理温度で0.004容旦%、60℃の処I!l
温度で0.01容吊%であり、この門は24時間接も変
らなかった。
As a result, in the case of methylmethoxypolysiloxane, 2
0.004 volume dan% at 5℃ treatment temperature, 60℃ treatment I! l
The temperature was 0.01% by volume, and this gate did not change even after 24 hours of contact.

これに対し、メチルハイドロジエンポリシロキサンの場
合は、25℃の処理温度で1時間後3.0容間%、2時
間後5.3容吊%、4時間後9.5容量%であった。
On the other hand, in the case of methylhydrodiene polysiloxane, at a treatment temperature of 25°C, the volume reduction was 3.0% by volume after 1 hour, 5.3% by volume after 2 hours, and 9.5% by volume after 4 hours. .

Claims (1)

【特許請求の範囲】 1、下記一般式( I ) R^1a(R^2O)bSiO(4−a−b)/2・・
・( I )で示され、分子鎖末端が−OR^2であるオ
ルガノポリシロキサン及び下記一般式(II) ▲数式、化学式、表等があります▼・・・(II) で示される環状オルガノポリシロキサン(ここで、上記
式において、R^1、R^2はそれぞれ互に同種又は異
種の炭化水素基、0≦a<4、0<b≦4、0<a+b
≦4、n=3〜10である)から選ばれる1種又は2種
以上の化合物0.01〜1重量部を用いて石灰粉100
重量部を処理することを特徴とする石灰粉の流動性改善
方法。 2、100メッシュより細かい石灰粉に末端OR^2基
を有する( I )式のオルガノポリシロキサン及び(II
)式の環状オルガノポリシロキサンから選ばれる1種又
は2種以上の化合物を無溶剤状態で添加し、室温〜10
0℃で混合撹拌することにより処理を行なうようにした
特許請求の範囲第1項記載の方法。
[Claims] 1. The following general formula (I) R^1a(R^2O)bSiO(4-a-b)/2...
・Organopolysiloxanes represented by (I) whose molecular chain ends are -OR^2 and cyclic organopolysiloxanes represented by the following general formula (II) ▲Mathical formulas, chemical formulas, tables, etc. are available▼...(II) Siloxane (here, in the above formula, R^1 and R^2 are the same or different hydrocarbon groups, 0≦a<4, 0<b≦4, 0<a+b
≦4, n=3 to 10) using 0.01 to 1 part by weight of one or more compounds selected from
A method for improving the fluidity of lime powder, which comprises treating the weight part. 2. Organopolysiloxane of formula (I) having terminal OR^2 groups and (II) in lime powder finer than 100 mesh.
) One or more compounds selected from the cyclic organopolysiloxanes of the formula are added in a solvent-free state, and the mixture is heated at room temperature to 10
The method according to claim 1, wherein the treatment is carried out by mixing and stirring at 0°C.
JP18399484A 1984-09-03 1984-09-03 Method for improving fluidity of lime powder Granted JPS6163527A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18399484A JPS6163527A (en) 1984-09-03 1984-09-03 Method for improving fluidity of lime powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18399484A JPS6163527A (en) 1984-09-03 1984-09-03 Method for improving fluidity of lime powder

Publications (2)

Publication Number Publication Date
JPS6163527A true JPS6163527A (en) 1986-04-01
JPH0121097B2 JPH0121097B2 (en) 1989-04-19

Family

ID=16145457

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18399484A Granted JPS6163527A (en) 1984-09-03 1984-09-03 Method for improving fluidity of lime powder

Country Status (1)

Country Link
JP (1) JPS6163527A (en)

Also Published As

Publication number Publication date
JPH0121097B2 (en) 1989-04-19

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