For the purpose of disclosing the mechanism of gas permeation through porous polymeric membrane, the effects of the pore size distribution
N (r) and the chemical nature of permeating gas on the gas permeability coefficient
P (
P1,
P2) (
P1 and
P2 are pressure of both sides of the membrane,
P1≥
P2) of cylindrically straight through porous membrane having average pore size (2
r1) of 0.75-0.035μm were studied. Gas flow through a capillary (radius
r) consists of the free molecular (F) flow only in the case of 2
r≤λ (λ: mean free path of the gas) and can be approximated with a mixed flow of viscous and slip flow (V flow) for 2
r>λ. The experimental
P (
P1,
P2) value is in excellent agreement with the theoretical one calculated by assuming that, in the range
P2≤
P0<
P1 (
P0, pressure at which 2
r=λ is realized), V flow occurs at the inlet and F flow dominates near the outlet of the capillary. The dependence of
P (
P1,
P2) of inorganic gases on
P1,
P2,
N (r) and λ can be expressed by a theoretical equation proposed in this Journal, 34, 729 (1977). The experimental
P (
P1,
P2) values of membrane (2
r1=0.035μm) for organic gases under the conditions that F flow occurs exclusively, are much larger than the theoretical value. The difference increases with an increase in boiling temperature of the gas, suggesting strongly that the gas flow relating to interaction between membrane and gas (for example, surface diffusion) contributes to
P (
P1,
P2) significantly.
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