253b Mixture Permeability, Solubility, and Diffusivity in Vapor Selective Polymers

Roy D. Raharjo1, Benny D. Freeman1, and Edgar S. Sanders2. (1) Chemical Engineering, University of Texas at Austin, 10100 Burnet Rd., Bldg 133, Center for Energy and Environmental Resources, Austin, TX 78758, (2) MEDAL - Air Liquide, 305 Water St., Newport, DE 19804-2410

Membrane separation technology has recently emerged as a potential alternative technique to remove higher hydrocarbons (C3+) from natural gas1. For economic reasons, membranes for this application should be organic vapor selective materials such as poly(dimethylsiloxane) (PDMS) or ultra-high free volume polymers such as poly(1-trimethylsilyl-1-propyne) (PTMSP). These polymers, often called solubility selective polymers, sieve penetrant molecules based strongly on relative penetrant solubility in the polymer. Traditionally, membrane separation performance is estimated from pure gas permeation measurements. However, this approach is not accurate in certain cases, especially in glassy polymers. For example, the presence of CO2 in cellulose acetate induces membrane plasticization and decreases the CO2/CH4 selectivity as the CO2 partial pressure increases2. In some cases, the selectivity of a vapor over a permanent gas in a mixture is actually higher than that estimated from pure gas measurements, which is attributed to the high solubility of vapor in the polymer, which partially blocks the permeation pathway of the smaller, less soluble permanent gas3. To accurately estimate the membrane separation performance, the mixed gas studies are required. This paper presents the n-C4H10/CH4 mixed gas permeability, solubility, and diffusivity in vapor selective polymers at various temperatures from -20oC to 50oC. The dilation isotherms are also reported to complement the mixture sorption data. In rubbery PDMS, the presence of larger, more condensable n-C4H10 considerably improves the CH4 solubility, permeability, and diffusivity in the polymer. On the other hand, the n-C4H10 sorption and transport properties in mixtures are unaffected by the presence of CH4 and are similar to those observed under pure gas conditions. The overall n-C4H10/CH4 permeability selectivity in mixtures increases as n-C4H10 activity increases and as temperature decreases, and the selectivity is lower than that estimated from pure gas measurements. The overall selectivity in PDMS is mainly governed by solubility selectivity. This report represents the first combined presentation of gas mixture permeability, solubility, and diffusivity in PDMS, which is the most widely used vapor separation polymer. Another polymer whose properties will be discussed is poly(1-trimethylsilyl-1-propyne) (PTMSP), an ultra-high free volume, solubility selective, glassy polymer. These studies help illustrate the fundamental mechanism of competitive permeation, sorption, and diffusion in glassy polymers. (1)        Baker, R. W. Membrane Technology and Applications; McGraw-Hill: New York, 2000.

(2)        Lee, S. Y.; Minhas, B. S. AICHE Symposium Series 1970, 84, 93-101.

(3)        Pinnau, I.;  Casillas, C. G.;  Morisato, A.; Freeman, B. D. Journal of Polymer Science: Part B: Polymer Physics 1996, 34, 2613-2621.