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    • 2. 发明授权
    • Process for production of zeolite film
    • 沸石膜生产工艺
    • US07973090B2
    • 2011-07-05
    • US12118911
    • 2008-05-12
    • Kenji SuzukiShinji NakamuraMiyuki YabukiToshihiro Tomita
    • Kenji SuzukiShinji NakamuraMiyuki YabukiToshihiro Tomita
    • C08J5/20
    • B01D71/028B01D61/362B01D67/0051B01D2323/08B01D2325/04C01B37/02C01B39/04
    • A process for producing a zeolite membrane comprising a seed crystal forming step of placing, in a pressure-resistant vessel, a seeding sol containing silica, water and a structure-directing agent and a support in a state that the support is immersed in the seeding sol and heating the heat-resistant vessel to form a zeolite seed crystal on the surface of the support, and a membrane formation step of allowing the zeolite seed crystal to grow to form a zeolite membrane on the surface of the support. In the seed crystal forming step, the molar ratio of water/silica in the seeding sol is set 10 to 50 and the heating of the pressure-resistant vessel is conducted at 90 to 130° C. The crystal c-axis of the present zeolite membrane is oriented in a direction vertical to the surface of the support and its thickness is uniform.
    • 一种沸石膜的制造方法,其特征在于,包括晶种形成工序,在所述耐压容器中,将所述载体浸渍在所述接种中的状态下,将含有二氧化硅,水和结构导向剂的载置溶胶和载体 溶胶并加热耐热容器以在载体表面上形成沸石晶种,以及允许沸石晶种生长以在载体表面上形成沸石膜的膜形成步骤。 在晶种形成工序中,将接种溶胶中的水/二氧化硅的摩尔比设定为10〜50,耐压容器的加热在90〜130℃下进行。本沸石的晶体c轴 膜在垂直于支撑体表面的方向上取向,并且其厚度是均匀的。
    • 7. 发明授权
    • Carbon membrane laminated body and method for manufacturing the same
    • 碳膜层叠体及其制造方法
    • US07891499B2
    • 2011-02-22
    • US12471532
    • 2009-05-26
    • Akimasa IchikawaMiyuki Yabuki
    • Akimasa IchikawaMiyuki Yabuki
    • B01D69/12B01D71/06B01D71/64B01D67/00B01D53/22
    • B01D71/021B01D53/228B01D63/066B01D67/0067B01D69/12B01D69/125B01D2325/04
    • A carbon membrane laminated body includes: a porous substrate, a first porous carbon membrane as a carbon membrane underlayer disposed on a surface of the porous substrate, and a second porous carbon membrane as a carbon membrane separation layer disposed on a surface of the carbon membrane underlayer, having a smaller film thickness, and a smaller average pore diameter, compared with those of the carbon membrane underlayer. It is preferable to form the carbon membrane underlayer and the carbon membrane separation layer by carbonizing a carbon membrane underlayer precursor disposed on a surface of the porous substrate and the carbon membrane separation layer precursor disposed on a surface of the carbon membrane underlayer precursor at 400 to 1000° C. in a non-oxidation atmosphere. The carbon membrane laminated body is a separation membrane excellent in both separation performance and flux when it is used as a separation membrane of a mixture.
    • 碳膜层压体包括:多孔基材,作为设置在多孔基材的表面上的碳膜底层的第一多孔碳膜和设置在碳膜表面上的作为碳膜分离层的第二多孔碳膜 与碳膜底层相比具有更小的膜厚度和更小的平均孔径。 优选通过将设置在多孔基材的表面上的碳膜下层前体碳化和碳膜下层前体的碳膜分离层前体在400〜80℃下碳化来形成碳膜底层和碳膜分离层 1000℃,在非氧化气氛中。 碳膜层叠体是当用作混合物的分离膜时,分离性能和通量均优异的分离膜。