Gas Permeation Characteristics of Zirconia-Silica Composite Membranes at High Temperature.
スポンサーリンク
概要
- 論文の詳細を見る
Permeabilities for pure gases of H<SUB>2</SUB>, He, CH<SUB>4</SUB>, NH<SUB>3</SUB>, H<SUB>2</SUB>O, N<SUB>2</SUB>, N<SUB>2</SUB>, O<SUB>2</SUB> and CO<SUB>2</SUB> were measured at trans-membrane pressures up to 0.2 MPa and 303, 423, 523 and 773 K for two types (with small pores and large pores) of composite zirconia-silica membranes coated on the surface of porous ceramic tubes (0.5μm). The composition of the metal-alkoxides solution used successfully in the coating process was Zr (OC<SUB>3</SUB>H<SUB>7</SUB>) <SUB>4</SUB> : 3.09, Si (OC<SUB>2</SUB>H<SUB>5</SUB>) <SUB>4</SUB> : 7.20, Y (CH<SUB>3</SUB>COO) <SUB>3</SUB>.4H<SUB>2</SUB>O : 0.21, i-PrOH : 89.50 in molar %.<BR>At low temperatures, with large-and small-pore membranes, the permeation mechanism for H<SUB>2</SUB>O, NH<SUB>3</SUB> and CO<SUB>2</SUB> is surface diffusion, and for other gases it is Knudsen flow.<BR>At higher temperature, with a large-pore membrane, the permeation mechanism for H<SUB>2</SUB>O, NH<SUB>3</SUB>, CO, and CH<SUB>4</SUB> is Knudsen flow, and for other gases it is a combination of Knudsen flow and activated diffusion. With a small-pore membrane, for H<SUB>2</SUB>O it is Knudsen flow, and for all other gases it is activated diffusion.
- 日本膜学会の論文
著者
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大矢 晴彦
Department of Material Sciense and Chemical Engineering, Yokohama National University
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Negishi Y.
Department of Material Science and Chemical Engineering, Yokohama National University
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OHYA H.
Department of Material Science and Chemical Engineering, Yokohama National University
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HISAMATSU T.
Terumo Co. Ltd.
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FUJIMOTO H.
TOTO Co. Ltd.
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OSAWA F.
Dainihon Printing Co. Ltd.
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NAKAJIMA H.
Daicel Chemical Industries Co. Ltd.
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