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Diffusion separation of hydrogen from gas mixtures

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Abstract

Experiments are described and a model is evaluated for the process of production of superpure hydrogen from mixtures with ammonia and nitrogen by selective diffusion through thin metallic membranes.

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Abbreviations

jH, jC :

molar fluxes of hydrogen and ballast gas

k:

effective permeability coefficient (product of hydrogen solubility coefficient times diffusion coefficient, divided by membrane thickness)

l, L:

coordinate measured along supply channel and maximum value thereof (channel length)

M:

molecular weight of hydrogen

P:

working perimeter of diffusion cell

p, p′:

pressure in supply and output channels

Q, QH :

mixture flow rate and hydrogen output for one cell or entire unit

S:

area of working section of supply channel

v′:

velocity in output channel

x, xo :

molar fraction of hydrogen in mixture and value thereof at inlet

z, Z:

dimensionless coordinate and length of apparatus

α, β:

dimensional and dimensionless hydraulic resistance coefficients

η, η* :

dimensionless pressure in output channel and value thereof at outlet

ξ:

dimensionless pressure (concentration) of hydrogen in supply channel

ρ′:

hydrogen density in output channel

ϕ:

relative output

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Translated from Inzhenerno-Fizicheskii Zhurnal, Vol. 47, No. 1, pp. 100–108, July, 1984.

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Baboshin, V.M., Buevich, Y.A., Ivonin, A.K. et al. Diffusion separation of hydrogen from gas mixtures. Journal of Engineering Physics 47, 821–826 (1984). https://doi.org/10.1007/BF00832599

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  • DOI: https://doi.org/10.1007/BF00832599

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