Gas permeability of membranes was measured using single gases with high purity (H2, CO2, CH4) by the barometric technique using a laboratory high-vacuum apparatus with a static permeation cell with an effective area of 5.25 cm2 at 30 °C. The membrane sample was placed and sealed in a module which was evacuated. At the beginning of the permeation experiment, the gas under constant pressure, p (150 kPa), was brought into the feed part of the permeation cell. The permeability was determined from the increase of pressure Δpp in a calibrated volume Vp of the product part of the cell per the time Δt interval during steady-state permeation. The gas permeability coefficient, Pexp, was estimated by the following equation [41]:
where l is a membrane thickness, S is its area, T is the absolute temperature, and R is the gas constant. The permeability coefficient P was expressed in Barrers (1 Barrer = 10−10 cm3 (STP)cm/(cm2 s cmHg)). Each experiment was repeated 3–5 times; several membranes of approximately the same thickness and prepared under the same conditions were used. The relative error of permeability value was 1–3%.
The ideal selectivity of gas i relatively gas j, αi/j, was calculated with the accuracy ± 0.05 according to the following equation:
The diffusion coefficient, D, was calculated from the initial transient regime, which determines the x-intercept that is a time-lag, θ:
The solubility coefficient, S, was calculated using the main gas transport equation:
Correlation analysis of gas transport parameters was performed using the data in Table 1.
Effective diameter, d, and the depth of the Lennard-Jones potential, (ε/k), for the gases under study [42].
The gas permeability coefficient for P84/ND film prepared by inclusion of non-porous impermeable filler in a continuous polymer matrix, PMaxwell, was calculated using Maxwell model [43]:
where PP84 is the gas permeability coefficient for pure polymer and ϕND is the volume fraction of nanodiamonds.
The volume fraction of the filler in the polymer matrix was estimated using the equation:
where ρP84 and ρND are the density of P84 and ND, respectively, and wtND is the weight fraction of the filler in the polymer matrix.
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