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Permeability coefficients P for He, O 2 , N 2 , CO 2 CH 4 , C 2 H 4 , C 2 H 6 , and C 3 H 8 in 12 different silicone polymer membranes were determined at 35.0°C and pressures up to 9 atm. Values of P for CO 2 , CH 4 , and C 3 H 8 were also determined at 10.0 and 55.0°C. In addition, mean diffusion coefficients D and solubility coefficients S were obtained for CO 2 , CH 4 , and C 3 H 8 in 6 silicone polymers at 10.0, 35.0, and 55.0°C. Substitution of increasingly bulkier functional groups in the side and backbone chains of silicone polymers results in a significant decrease in P for a given penetrant gas. This is due mainly to a decrease in D , whereas S decreases to a much lesser extent. Backbone substitutions appear to have a somewhat lesser effect in depressing P than equivalent side‐chain substitutions. The selectivity of a silicone membrane for a gas A relative to a gas B, i.e., the permeability ratio P (A)/ P (B), may increase or decrease as a result of such substitutions, but only if the substituted groups are sufficiently bulky. The selectivity of the more highly permeable silicone membranes is controlled by the ratio S (A)/ S (B), whereas the selectivity of the less permeable membranes depends on both the ratios D (A)/ D (B) and S (A)/ S (B). The permeability as well as the selectivity of one silicone membrane toward CO 2 were significantly enhanced by the substitution of a fluorine‐containing side group that increased the solubility of CO 2 in that polymer.
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Stern et al. (1987) studied this question.
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