JP3605389B2 - Method for producing polyorganosilsesquioxane fine particles - Google Patents
Method for producing polyorganosilsesquioxane fine particles Download PDFInfo
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- JP3605389B2 JP3605389B2 JP2001389663A JP2001389663A JP3605389B2 JP 3605389 B2 JP3605389 B2 JP 3605389B2 JP 2001389663 A JP2001389663 A JP 2001389663A JP 2001389663 A JP2001389663 A JP 2001389663A JP 3605389 B2 JP3605389 B2 JP 3605389B2
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- organotrichlorosilane
- polyorganosilsesquioxane
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- 239000010419 fine particle Substances 0.000 title claims description 24
- 238000004519 manufacturing process Methods 0.000 title description 9
- 238000006243 chemical reaction Methods 0.000 claims description 47
- 239000003513 alkali Substances 0.000 claims description 12
- 238000006460 hydrolysis reaction Methods 0.000 claims description 6
- 230000007062 hydrolysis Effects 0.000 claims description 4
- 238000009833 condensation Methods 0.000 claims description 3
- 230000005494 condensation Effects 0.000 claims description 3
- 239000003125 aqueous solvent Substances 0.000 claims 1
- 239000000243 solution Substances 0.000 description 33
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 17
- 239000002245 particle Substances 0.000 description 17
- 239000005055 methyl trichlorosilane Substances 0.000 description 10
- JLUFWMXJHAVVNN-UHFFFAOYSA-N methyltrichlorosilane Chemical compound C[Si](Cl)(Cl)Cl JLUFWMXJHAVVNN-UHFFFAOYSA-N 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- 238000006116 polymerization reaction Methods 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 7
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 7
- 230000002378 acidificating effect Effects 0.000 description 7
- 235000011114 ammonium hydroxide Nutrition 0.000 description 7
- 229920003217 poly(methylsilsesquioxane) Polymers 0.000 description 7
- 239000002904 solvent Substances 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 5
- 239000003021 water soluble solvent Substances 0.000 description 5
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical class Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 230000032683 aging Effects 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 125000003342 alkenyl group Chemical group 0.000 description 3
- 125000000217 alkyl group Chemical group 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 238000000635 electron micrograph Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- -1 oxides Chemical class 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 2
- 239000007810 chemical reaction solvent Substances 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 239000002270 dispersing agent Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 150000004679 hydroxides Chemical class 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 239000011859 microparticle Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 125000001477 organic nitrogen group Chemical group 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- DHXVGJBLRPWPCS-UHFFFAOYSA-N Tetrahydropyran Chemical compound C1CCOCC1 DHXVGJBLRPWPCS-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 125000000962 organic group Chemical group 0.000 description 1
- 150000001367 organochlorosilanes Chemical class 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 125000004368 propenyl group Chemical group C(=CC)* 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 239000005052 trichlorosilane Substances 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
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Description
【0001】
【産業上の利用分野】
本発明は、ポリオルガノシルセスキオキサン微粒子の新規な製造方法であり、簡便な製法により球状のポリオルガノシルセスキオキサン微粒子を製造する方法に関するものである。
【0002】
【従来の技術】
ポリオルガノシルセスキオキサンの微粒子を得る方法としては、オルガノトリクロロシランまたはオルガノトリアルコキシシランを加水分解・縮合させる方法が知られているが、オルガノトリアルコキシシランはオルガノトリクロロシランから製造されるので、オルガノトリクロロシランを製造原料とした方が安価に製造できることは明らかである。
【0003】
【発明が解決しようとする課題】
しかしながらオルガノトリクロロシランの加水分解反応は極めて激しいため、その反応を制御することは難しく、このため従来のものは不定形粗大粒子として取出されており、球状の微粒子として得ることは困難であった。その中において特開平6−179751号公報においてオルガノトリクロロシランを飽和塩化水素水中に添加し、加水分解・縮合を行うことで球状のポリオルガノシルセスキオキサン微粒子を合成する方法が開示されている。この方法によればオルガノトリクロロシランを用いて流動性に優れた球状微粒子を製造できるが、反応溶媒として飽和塩化水素水を使用している為、安全面、装置の腐食等の点で課題が残されている。
【0004】
【課題を解決するための手段】
本発明はこのような不利、欠点を解決した球状のポリオルガノシルセスキオキサン微粒子の製造方法に関するものであり、原料であるオルガノトリクロロシランを反応溶液となる水溶性溶媒に添加し、加水分解・縮合させる際、同時にアルカリを前記反応溶液内に添加することを特徴としたもので、このようにすることにより、球状の粒子表面を有するポリオルガノシルセスキオキサン微粒子が得られる知見を得、これに基づいて本発明を完成するに至った。
【0005】
【作用】
本発明は、オルガノトリクロロシランを反応溶媒となる水溶性溶媒に添加し、加水分解・縮合させる際、同時にアルカリを前記反応溶液内に添加することを特徴とするポリオルガノシルセスキオキサン微粒子の製造方法であり、該アルカリを同時添加することにより反応溶液内のpHを制御することになり、これによって、酸性からアルカリ性に至る殆どの溶媒領域において球状をしたポリオルガノシルセスキオキサン微粒子の合成が可能になる。
【0006】
この場合において、反応溶液の液性が酸性の領域で合成されたポリオルガノシルセスキオキサンは比較的低重合度のものであるのに対し、アルカリ性の領域で合成されたポリオルガノシルセスキオキサンは高重合度のものになるというように、液性により得られるポリオルガノシルセスキオキサンの特性が異なる。つまり、熱安定性の高い高重合度のポリオルガノシルセスキオキサン微粒子を得るためには、反応溶液の液性を中性からアルカリ性域にすることが必要であり、また、溶剤等に溶解し易い低重合度のポリオルガノシルセスキオキサンを得るためには反応溶液の液性を中性から酸性域にすることが必要であり、このことから、同時添加するアルカリ量により反応溶液の液性を調整し、これにより得られるポリオルガノシルセスキオキサンの重合度を制御することができる。また、酸性域で反応させた後、アルカリを添加し、反応溶液内のpHをアルカリ性とすることによっても高重合度の球形をしたオルガノシルセスキオキサン微粒子を得ることも出来る。
【0007】
本発明において、原料物質であるオルガノトリクロロシランは、一般式RSiCl3(Rはアルキル基、アルケニル基、アリール基を指す)で示される。上記アルキル基としては、メチル基、エチル基、プロピル基等の炭素数1〜8のものが挙げられる。また、上記アルケニル基としては、ビニル基、アリル基、プロペニル基等の炭素数2〜8のものが挙げられる。さらにまた、上記アリール基としては、フェニル基等が挙げられる。
上記アルキル基、アルケニル基、アリール基は、一部の水素が他の有機基で置換されていても良く、また、2種以上の混合物として使用しても良い。
また、オルガノトリクロロシランのなかに、R2SiCl2、R3SiClなどのオルガノクロロシランが含まれていても使用できる。
【0008】
本発明における加水分解の反応溶液となる水溶性溶媒は、そのpHが酸性域からアルカリ性域の殆どの領域において使用できるが、特に好ましくは水である。
上記反応溶液となる水溶性溶媒のpH調整に用いられるアルカリ種は、一般的に周期律表Ia属金属、IIa属金属の水酸化物、酸化物、炭酸塩および有機窒素酸化物、アンモニアなどが挙げられ、また、酸性種は、塩酸、硫酸等の無機酸、蟻酸、酢酸等の水溶性の有機酸が挙げられる。これら酸またはアルカリは2種以上の混合物として使用しても良い。また、水溶性の有機溶剤、界面活性剤、高分子分散剤などが含まれていても使用することができる。
【0009】
本発明における添加用アルカリは、一般的に周期律表Ia属、IIa属金属の水酸化物、酸化物、炭酸塩および有機窒素酸化物、アンモニアなどが用いられるが、これらのアルカリは単独でも、または2種以上を混合しても使用することができる。
上記添加用アルカリは、水と混合したアルカリ水溶液として用いることが好適であり、このアルカリ水溶液に、水溶性の有機溶剤、界面活性剤、高分子分散剤などが含まれていても使用することができる。
【0010】
本発明において、前記反応溶液となる水溶性溶媒に前記オルガノトリクロロシランを添加する際、前記添加用アルカリを反応溶液内に同時添加して、球状のポリオルガノシルセスキオキサン微粒子を析出させるにあたり、上記オルガノトリクロロシランを反応溶液内に添加する際には、該オルガノトリクロロシランの反応溶液内への拡散がし易いような添加方法とすることが望ましい。
また、オルガノトリクロロシランの添加量は、反応溶液1重量部に対して、オルガノトリクロロシランを0.1重量部以下とすることが好ましく、これ以上の添加量にすると不定形粗大粒子の割合が増大する。
さらに反応溶液内へのアルカリの同時添加は、連続的、間欠的、pHによる制御等により添加される。
【0011】
本発明における反応溶液の撹拌は、穏やかな撹拌とすると不定形粗大粒子の割合が増加するため、なるべく強力な撹拌とすることが望ましく、邪魔板等の設置も効果的である。
さらに、本発明における反応液温度は、0℃〜60℃の範囲から選ぶことができるが、好ましくは0℃〜40℃であり、これ以上の温度では、不定形粗大粒子の割合が増大する。
【0012】
本発明による反応を連続的に進行させ、反応容器から反応溶液の容量が略一定となるように、反応液スラリーを取出すことにより、連続的な球状ポリオルガノシルセスキオキサン微粒子の製造をすることも可能である。
【0013】
上記方法における反応においても、反応溶液内のオルガノトリクロロシラン量の割合を、反応溶液1重量部に対して0.1重量部以下となるように調整することが必要である。
【0014】
このようにして製造した球状のポリオルガノシルセスキオキサン微粒子は、その後、熟成した後、濾過分離・水洗浄あるいは有機溶剤洗浄後、乾燥し、場合によっては解砕し、球状のポリオルガノシルセスキオキサン微粒子を得る。
得られた微粒子は、球状のポリオルガノシルセスキオキサン微粒子であり、本発明によりオルガノトリクロロシランから簡便な製造方法により球状のポリオルガノシルセスキオキサン微粒子を効率よく製造することができる。
【0015】
【実験例】
以下、本発明の方法を実験例をあげて説明するが、本発明はこれらの例によって限定されるものでないことは勿論である。
【0016】
[実験例1]
500ml(ミリリットル)の反応容器に撹拌機、温度計を取り付け、反応容器に反応溶液となる水250mlを入れ、500rpm(回転 毎分)で撹拌しつつ、反応容器を20℃に恒温した後、定量ポンプにてメチルトリクロロシラン12.5gを1.5g/min(グラム 毎分)の供給速度で添加すると同時に、25%アンモニア水溶液を2.1g/minの速度で添加した。メチルトリクロロシランの供給終了と同時にアンモニア水溶液の供給も停止した。添加比(mol比)=(アンモニア/メチルトリクロロシラン中の塩素)は、1.03であり、反応溶液の液性はアルカリ性であった。その後、室温にて1時間熟成後、濾過・水洗・乾燥を実施し、白色粒子を得た。この粒子は、熱や溶媒に対して安定性の高い高重合度のポリメチルシルセスキオキサン微粒子であった。得られた粒子を電子顕微鏡で観察した結果、球状の微粒子であった(図1の電子顕微鏡写真図参照)。
【0017】
[比較例]
500ml反応容器に撹拌機、温度計を取り付け、反応容器に反応溶液となる25%アンモニア水溶液18g、水232gを入れ、500rpmで撹拌しつつ、反応容器を20℃に恒温した後、定量ポンプにてメチルトリクロロシラン12.5gを1.5g/minの供給速度で前記反応溶液に添加した。添加比(mol比)=(アンモニア/メチルトリクロロシラン中の塩素)は、1.06であり、反応溶液の液性はアルカリ性であった。供給終了後、室温にて1時間熟成後、濾過・水洗・乾燥を実施し、白色粒子を得た。この粒子は、ポリメチルシルセスキオキサン粒子であったが、電子顕微鏡で観察した結果、不定形凝集物が多く、流動性にすぐれた粉体として取出すことは出来なかった(図2の電子顕微鏡写真図参照)。
【0018】
[実験例2]
500ml反応容器に撹拌機、温度計を取り付け、反応容器に反応溶液となる水250mlを入れ、500rpmで撹拌しつつ、反応容器を20℃に恒温した後、定量ポンプにてメチルトリクロロシラン12.5gを1.5g/minの供給速度で添加すると同時に、25%アンモニア水溶液を1.8g/minの速度で添加した。メチルトリクロロシランの供給終了と同時にアンモニア水溶液の供給も停止した。添加比(mol比)=(アンモニア/メチルトリクロロシラン中の塩素)は、0.88であり、反応溶液の液性は酸性であった。その後、室温にて1時間熟成後、濾過・水洗を実施し、白色粒子を得た。この粒子はポリメチルシルセスキオキサンであり、電子顕微鏡で観察した結果、球状の微粒子であった。また、この粉末は各種溶媒に溶解し易く、昇温により溶融する性質を有している低重合度のポリメチルシルセスキオキサンであった。
【0019】
[実施例3]
実験例2と同様に調整して、メチルトリクロロシランとアンモニア水溶液とを同時添加した反応溶液に、該メチルトリクロロシランの添加終了後、さらに25%アンモニア水溶液2.7gを添加した。総添加比(mol比)=(アンモニア/メチルトリクロロシラン中の塩素)は1.04であった。その後、室温にて1時間熟成後、濾過・水洗・乾燥を実施し、白色粒子を得た。熟成時の反応溶液の液性はアルカリ性であった。前記得られた粒子は、熱や溶媒に対して安定性の高い高重合度のポリメチルシルセスキオキサン粒子であった。得られた粉末を電子顕微鏡で観察した結果、球状の微粒子であった。
【0020】
【本発明の効果】
本発明の方法によれば、オルガノトリクロロシランから製造装置等の腐食等が少ない簡便な方法で、球状のポリオルガノシルセスキオキサン微粒子を効率よく製造することができる。
【図面の簡単な説明】
【図1】実験例1で生成したポリメチルシルセスキオキサン粒子の電子顕微鏡写真図である。
【図2】比較例で生成したポリメチルシルセスキオキサン粒子の電子顕微鏡写真図である。[0001]
[Industrial applications]
The present invention relates to a novel method for producing polyorganosilsesquioxane fine particles, and more particularly to a method for producing spherical polyorganosilsesquioxane fine particles by a simple production method.
[0002]
[Prior art]
As a method for obtaining fine particles of polyorganosilsesquioxane, a method of hydrolyzing and condensing organotrichlorosilane or organotrialkoxysilane is known.However, since organotrialkoxysilane is produced from organotrichlorosilane, It is clear that the production can be performed at lower cost by using organotrichlorosilane as a raw material.
[0003]
[Problems to be solved by the invention]
However, since the hydrolysis reaction of organotrichlorosilane is extremely violent, it is difficult to control the reaction. For this reason, the conventional one has been taken out as irregular coarse particles, and it has been difficult to obtain spherical fine particles. Among them, Japanese Patent Application Laid-Open No. Hei 6-179751 discloses a method of synthesizing spherical polyorganosilsesquioxane fine particles by adding organotrichlorosilane to a saturated aqueous hydrogen chloride solution and performing hydrolysis and condensation. According to this method, spherical fine particles having excellent fluidity can be produced using organotrichlorosilane. However, since saturated hydrogen chloride water is used as a reaction solvent, problems remain in terms of safety, corrosion of equipment, and the like. Have been.
[0004]
[Means for Solving the Problems]
The present invention relates to a method for producing spherical polyorganosilsesquioxane fine particles that solves such disadvantages and drawbacks, and comprises adding organotrichlorosilane, which is a raw material, to a water-soluble solvent serving as a reaction solution, and performing hydrolysis and when condensing, which was characterized by adding an alkali to the reaction solution in the same time, by doing so, obtain the knowledge polyorganosilsesquioxane particles having a spherical particle surface is obtained, which Based on the above, the present invention has been completed.
[0005]
[Action]
The present invention is added to a water-soluble solvent comprising a organotrichlorosilane and reaction solvent, time of hydrolysis and condensation, the production of polyorganosilsesquioxane particles characterized by adding an alkali to the reaction solution in the same time By adding the alkali simultaneously, the pH in the reaction solution is controlled, whereby the synthesis of spherical polyorganosilsesquioxane fine particles in most solvent regions from acidic to alkaline can be achieved. Will be possible.
[0006]
In this case, the polyorganosilsesquioxane synthesized in the region where the liquidity of the reaction solution is acidic has a relatively low degree of polymerization, whereas the polyorganosilsesquioxane synthesized in the alkaline region is used. The properties of the polyorganosilsesquioxane obtained differ depending on the liquid property, such as that the polymer has a high degree of polymerization. In other words, in order to obtain polyorganosilsesquioxane fine particles having high thermal stability and a high degree of polymerization, it is necessary to change the liquidity of the reaction solution from a neutral to an alkaline range, and it is also necessary to dissolve the solvent in a solvent or the like. In order to obtain a polyorganosilsesquioxane having a low degree of polymerization easily, it is necessary to adjust the liquid property of the reaction solution from a neutral to an acidic range. And the degree of polymerization of the resulting polyorganosilsesquioxane can be controlled. Alternatively, spherical organosilsesquioxane fine particles having a high degree of polymerization can be obtained by adding an alkali after the reaction in an acidic region and making the pH in the reaction solution alkaline.
[0007]
In the present invention, the organotrichlorosilane as a raw material is represented by the general formula RSiCl 3 (R represents an alkyl group, an alkenyl group, and an aryl group). Examples of the alkyl group include those having 1 to 8 carbon atoms such as a methyl group, an ethyl group, and a propyl group. Examples of the alkenyl group include those having 2 to 8 carbon atoms, such as a vinyl group, an allyl group, and a propenyl group . Furthermore, examples of the aryl group include a phenyl group.
In the above alkyl group, alkenyl group and aryl group, some of the hydrogens may be replaced by other organic groups, and they may be used as a mixture of two or more.
Further, even if organochlorosilane such as R 2 SiCl 2 or R 3 SiCl is contained in the organotrichlorosilane, it can be used.
[0008]
The water-soluble solvent used as the hydrolysis reaction solution in the present invention can be used in most of the pH range from the acidic range to the alkaline range, but water is particularly preferable.
Alkali species used for adjusting the pH of the water-soluble solvent to be the reaction solution generally include hydroxides, oxides, carbonates and organic nitrogen oxides of Group Ia metals and Group IIa metals, and ammonia. Examples of the acidic species include inorganic acids such as hydrochloric acid and sulfuric acid, and water-soluble organic acids such as formic acid and acetic acid. These acids or alkalis may be used as a mixture of two or more. In addition, even if a water-soluble organic solvent, a surfactant, a polymer dispersant, and the like are contained, they can be used.
[0009]
As the alkali for addition in the present invention, hydroxides, oxides, carbonates and organic nitrogen oxides of metals belonging to Group Ia and Group IIa of the Periodic Table are generally used, and these alkalis are used alone. Alternatively, a mixture of two or more types can be used.
The above-mentioned alkali for addition is preferably used as an aqueous alkali solution mixed with water, and this alkali aqueous solution may be used even if it contains a water-soluble organic solvent, a surfactant, a polymer dispersant, or the like. it can.
[0010]
In the present invention, when adding the organotrichlorosilane to a water-soluble solvent to be the reaction solution, simultaneously adding the alkali for addition into the reaction solution, in order to precipitate spherical polyorganosilsesquioxane fine particles, When the above-mentioned organotrichlorosilane is added to the reaction solution, it is desirable to use an addition method that facilitates diffusion of the organotrichlorosilane into the reaction solution.
The amount of organo trichlorosilane, the reaction solution 1 part by weight, it is preferred that the organotrichlorosilane than 0.1 part by weight, the proportion of the irregular-sized coarse large particles when any more addition amount Increase.
Further, simultaneous addition of alkali to the reaction solution is performed continuously, intermittently, by pH control, or the like.
[0011]
The stirring of the reaction solution in the present invention is preferably performed as strong as possible because the ratio of irregularly shaped coarse particles increases when the stirring is gentle, and the installation of baffles and the like is also effective.
Further, the reaction solution temperature in the present invention can be selected from the range of 0 ° C. to 60 ° C., preferably from 0 ° C. to 40 ° C., in which temperatures above the proportion of amorphous coarse large particles is increased .
[0012]
The reaction according to the present invention proceeds continuously, and the reaction solution slurry is taken out from the reaction vessel so that the volume of the reaction solution becomes substantially constant, thereby producing continuous spherical polyorganosilsesquioxane fine particles. Is also possible.
[0013]
Also in the reaction in the above method, it is necessary to adjust the ratio of the amount of organotrichlorosilane in the reaction solution to 0.1 part by weight or less based on 1 part by weight of the reaction solution .
[0014]
The spherical polyorganosilsesquioxane microparticles thus produced are then aged, filtered, separated and washed with water or an organic solvent, dried and, if necessary, crushed to obtain a spherical polyorganosilsesquioxane fine particle. Oxane fine particles are obtained.
The obtained fine particles are spherical polyorganosilsesquioxane fine particles. According to the present invention, spherical polyorganosilsesquioxane fine particles can be efficiently produced from organotrichlorosilane by a simple production method.
[0015]
[Experimental example]
Hereinafter, the method of the present invention will be described with reference to experimental examples, but it is needless to say that the present invention is not limited to these examples.
[0016]
[Experimental example 1]
A stirrer and a thermometer were attached to a 500 ml (milliliter) reaction vessel, 250 ml of water serving as a reaction solution was added to the reaction vessel, and the reaction vessel was stirred at 500 rpm (rotation per minute). 12.5 g of methyltrichlorosilane was added at a supply rate of 1.5 g / min (gram per minute) by a pump, and a 25% aqueous ammonia solution was added at a rate of 2.1 g / min. At the same time as the completion of the supply of methyltrichlorosilane, the supply of the aqueous ammonia solution was stopped. The addition ratio (mol ratio) = (ammonia / chlorine in methyltrichlorosilane) was 1.03, and the liquidity of the reaction solution was alkaline. Then, after aging at room temperature for 1 hour, filtration, washing and drying were performed to obtain white particles. These particles were polymethylsilsesquioxane fine particles having a high degree of polymerization and high stability to heat and solvents. Observation of the obtained particles with an electron microscope revealed spherical fine particles (see the electron micrograph in FIG. 1).
[0017]
[Comparative example]
A stirrer and a thermometer were attached to a 500 ml reaction vessel, and 18 g of a 25% aqueous ammonia solution serving as a reaction solution and 232 g of water were added to the reaction vessel. The reaction vessel was kept at 20 ° C. while stirring at 500 rpm. 12.5 g of methyltrichlorosilane was added to the reaction solution at a feed rate of 1.5 g / min. The addition ratio (mol ratio) = (ammonia / chlorine in methyltrichlorosilane) was 1.06, and the liquidity of the reaction solution was alkaline. After completion of the supply, the mixture was aged at room temperature for 1 hour, and then filtered, washed with water and dried to obtain white particles. Although these particles were polymethylsilsesquioxane particles, as observed by an electron microscope, they had many irregular aggregates and could not be taken out as a powder having excellent fluidity (see the electron microscope in FIG. 2). See photo).
[0018]
[Experimental example 2]
A stirrer and a thermometer were attached to a 500 ml reaction vessel, 250 ml of water serving as a reaction solution was added to the reaction vessel, and the reaction vessel was kept at a constant temperature of 20 ° C. while stirring at 500 rpm. Was added at a feed rate of 1.5 g / min, and at the same time, a 25% aqueous ammonia solution was added at a rate of 1.8 g / min. At the same time as the completion of the supply of methyltrichlorosilane, the supply of the aqueous ammonia solution was stopped. The addition ratio (mol ratio) = (ammonia / chlorine in methyltrichlorosilane) was 0.88, and the liquidity of the reaction solution was acidic. Then, after aging for 1 hour at room temperature, filtration and washing were performed to obtain white particles. These particles were polymethylsilsesquioxane, and as a result of observation with an electron microscope, were spherical fine particles. This powder was a low-polymerization degree polymethylsilsesquioxane having a property of being easily dissolved in various solvents and having a property of melting when heated.
[0019]
[Example 3]
After the addition of methyltrichlorosilane was completed, 2.7 g of a 25% aqueous ammonia solution was further added to the reaction solution prepared by simultaneously adding methyltrichlorosilane and an aqueous ammonia solution in the same manner as in Experimental Example 2. The total addition ratio (mol ratio) = (ammonia / chlorine in methyltrichlorosilane) was 1.04. Then, after aging at room temperature for 1 hour, filtration, washing and drying were performed to obtain white particles. The liquid property of the reaction solution during aging was alkaline. The particles obtained were polymethylsilsesquioxane particles having a high degree of polymerization and high stability to heat and solvents. Observation of the obtained powder with an electron microscope revealed spherical fine particles.
[0020]
[Effects of the present invention]
ADVANTAGE OF THE INVENTION According to the method of this invention, spherical polyorganosilsesquioxane microparticles | fine-particles can be manufactured efficiently from an organotrichlorosilane by a simple method with little corrosion etc. of a manufacturing apparatus.
[Brief description of the drawings]
FIG. 1 is an electron micrograph of polymethylsilsesquioxane particles produced in Experimental Example 1.
FIG. 2 is an electron micrograph of polymethylsilsesquioxane particles produced in a comparative example.
Claims (1)
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