发明名称 Method for manufacturing microparticulate anatase or rutile titanium oxide dispersion and component having photocatalytic thin film on surface
摘要 A method for manufacturing a microparticulate anatase or rutile titanium oxide dispersion from a peroxotitanic acid solution optionally containing tin, wherein the method for manufacturing an anatase or rutile titanium oxide dispersion is characterized in that the peroxotitanic acid solution is fed continuously to a flow reactor and subjected to hydrothermal treatment at 150 to 250° C. and 0.5 to 10 MPa. The invention makes it possible to provide a method for manufacturing a microparticulate anatase or rutile titanium oxide dispersion having excellent stability in regard to the titanium oxide microparticles and enabling a high-transparency photocatalytic thin film to be produced, and to provide a member having a photocatalytic thin film formed on the surface using this dispersion.
申请公布号 US9463436(B2) 申请公布日期 2016.10.11
申请号 US201214115209 申请日期 2012.05.10
申请人 SHIN-ETSU CHEMICAL CO., LTD. 发明人 Furudate Manabu;Inoue Tomohiro;Takahashi Shiro;Eguchi Yoshitsugu;Amano Tadashi
分类号 B01J21/08;B01J37/03;B01J37/08;B01J23/14;B01J35/00;C09D1/00;C09D5/16;B01J21/06;C01G23/047;C01G23/04;C01G23/053;B01J35/02;C08K3/22 主分类号 B01J21/08
代理机构 Birch, Stewart, Kolasch & Birch, LLP 代理人 Birch, Stewart, Kolasch & Birch, LLP
主权项 1. A method for continuously manufacturing an anatase titanium oxide ultrafine particle dispersion from a peroxotitanic acid solution, the method comprising: providing a flow reactor comprising a first feedstock tank for containing an aqueous medium except alcohol, a second feedstock tank for containing a peroxotitanic acid solution, a high-pressure feed pump, a heating section, a cooling section, and a collector section, wherein the first feedstock tank is connected to the high-pressure feed pump via a first pipe,the second feedstock tank is connected to the high-pressure feed pump via a second pipe,the high-pressure feed pump is connected at a suction side to the first and second feedstock tanks via valves, respectively, and at a discharge side to a metal tube extending to the heating section and then to the cooling section, so as to feed the aqueous medium and the peroxotitanic acid solution from the first and second feedstock tanks, respectively, to the heating section,the heating section having a coiled metal tube which is connected to the discharge side of the high-pressure feed pump and is externally heated for subjecting the peroxotitanic acid solution flowing through a bore of the tube to hydrothermal treatment, so that the peroxotitanic acid solution is converted into an anatase titanium oxide ultrafine particle dispersion,the cooling section having a coiled metal tube which is connected to an outlet tube of the heating section and is externally cooled so that the anatase titanium oxide dispersion flowing through a bore of the tube is cooled to stop the reaction, and a back-pressure valve is disposed at the outlet of the cooling section, andthe collector section having a collector tank which is connected to the outlet tube of the cooling section; filling the first feedstock tank with the aqueous medium except alcohol and the second feedstock tank with the peroxotitanic acid solution, respectively; supplying the aqueous medium from the first feedstock tank to the coiled metal tube of the heating section via the first pipe by the high-pressure feed pump and heating the aqueous medium to 150 to 250° C. in the coiled metal tube prior to supplying the peroxotitanic acid solution from the second feedstock tank to the coiled metal tube of the heating section; stopping the supply of the aqueous medium to the coiled metal tube of the heating section; then supplying the peroxotitanic acid solution from the second feedstock tank to the coiled metal tube of the heating section via the second pipe and heating the peroxotitanic acid solution in the coiled metal tube, so that the peroxotitanic acid solution is subjected to hydrothermal reaction at 150 to 250° C. and 0.5 to 10 MPa for 0.5 to 20 minutes to convert the peroxotitanic acid solution into the anatase titanium oxide ultrafine particle dispersion; transferring the anatase titanium oxide ultrafine particle dispersion to the coiled metal tube of the cooling section to cool the anatase titanium oxide ultrafine particle dispersion so that the reaction is stopped, and collecting the anatase titanium oxide ultrafine particle dispersion from the outlet tube of the collector section.
地址 Tokyo JP