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Nonporous inorganic membrane

Paglieri, S.N., Palladium membranes, Nonporous Inorganic Membranes, Chapter 3, eds. A.F. Sammells and M.V. Mundschau, Wiley-VCH Verlag GmBH, Weinheim, 2006. [Pg.321]

Sirman, J. (2006) in Nonporous Inorganic Membranes for Chemical Processing (eds F. Sander and M.V. Mundschau), Wiley-VCH, Weinheim, pp. 165-184. [Pg.218]

Fig. 8.1 Plots of hydrogen permeability of selected elements based upon the equations of Steward [15] (Copyright Wiley-VCH Verlag, GmbH Co. KGaA, 2006. Adapted with permission from [8], Nonporous Inorganic Membranes.)... Fig. 8.1 Plots of hydrogen permeability of selected elements based upon the equations of Steward [15] (Copyright Wiley-VCH Verlag, GmbH Co. KGaA, 2006. Adapted with permission from [8], Nonporous Inorganic Membranes.)...
Fig. 8.10 Hydrogen flux data of a composite membrane incorporating a Group IVB-VB material. Sieverts Law is followed very weU and a permeability at 440°C of 2.3 10 mol m s Pa was achieved. The membrane, sealed with copper gaskets, was essentially 100% selective towards hydrogen showing no detectable leak to helium. The disk withstood 33 bar differential pressure (Copyright Wiley-VCH Verlag, GmbH Co. KGaA, 2006. Adapted with permission from [8], Nonporous Inorganic Membranes.)... Fig. 8.10 Hydrogen flux data of a composite membrane incorporating a Group IVB-VB material. Sieverts Law is followed very weU and a permeability at 440°C of 2.3 10 mol m s Pa was achieved. The membrane, sealed with copper gaskets, was essentially 100% selective towards hydrogen showing no detectable leak to helium. The disk withstood 33 bar differential pressure (Copyright Wiley-VCH Verlag, GmbH Co. KGaA, 2006. Adapted with permission from [8], Nonporous Inorganic Membranes.)...
Mundschau, Michael V, Xie, Xiaobing, Evenson IV Carl R. Superpermeable hydrogen transport membranes. In SammeUs, A. F, Mundschau, M. V, editors. Nonporous inorganic membranes. Weinheim, Germany WUey-VCH 2006. pp. 107-38, and references therein. [Pg.150]

The aim of this chapter is to give a critical analysis of parameters that must be taken into account each time an economic study on membrane reactors is performed. In particular, nonporous inorganic membrane reactors for reactions involving gases are considered. [Pg.245]

Abe A, Aibertsson AC, Dusek K, Jeu WH, Kausch HH, Kobayashi S, Lee KS, Leibler L, Long TE, Manners I, Mdlier M, Nuyken O, Terentjev EM, Voit B, Wegner G, Wiesner U, Vicent MI (eds) (1985) Polymer membranes (Advances in Polymer Science). SpiingCT Verlag Baker RW (2004) Membrane technology and applications. Wiley, New York Sammells AF et al (eds) (2006) Nonporous inorganic membranes for chemical processing. Wiley VCH, Weinheim... [Pg.359]

A. F. Sammells, M.V. Mundschau (Eds.) Nonporous inorganic membranes for chemical processing, Wiley-VCH, New York, Weinheim, Cambridge 2006. [Pg.89]

Paglieri, S.N. (2006). Palladium Membranes, in Nonporous Inorganic Membranes. Published Online 3 Aug 2006, Eds. A.F. SammeUs, MV. Mundschau, Print ISBN 9783527313426, Online ISBN 9783527608799, pp77-105. [Pg.227]

Gas transport through nonporous inorganic membranes falls into two categories. It is known that the conventional solution-diffusion permeation mechanism is valid for nonporous membranes of silica, zeolite and inorganic salts. It is no longer so when the membrane is metallic in nature (Hwang and Kammermeyer, 1975). Diatomic gases such as O2, H2 and N2 dissolve atomically in the metallic membrane (see (3.3.67)). While a conventional flux expression is valid for atomic species i dissolved in the membrane, Le. [Pg.180]


See other pages where Nonporous inorganic membrane is mentioned: [Pg.219]    [Pg.278]    [Pg.279]    [Pg.281]    [Pg.344]    [Pg.723]    [Pg.147]    [Pg.370]    [Pg.1]   
See also in sourсe #XX -- [ Pg.180 ]




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