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