(356a) Hydrogen Sorption in Polymers | AIChE

(356a) Hydrogen Sorption in Polymers

Authors 

Smith, Z. P. - Presenter, The University of Texas at Austin
Tiwari, R., The University of Texas at Austin
Guo, R., The University of Notre Dame
Freeman, B. D., The University of Texas at Austin
McGrath, J. E., Virginia Tech
Paul, D. R., University of Texas at Austin


For over 30 years, dense polymer membranes have been used for industrial applications in hydrogen separation, including syngas ratio adjustment, refinery off-gas purification, and ammonia purge gas recovery [1].  These membranes operate based on the solution-diffusion model, where permeability is defined as the product of an effective diffusion coefficient and an effective sorption coefficient.  Determining sorption of H2, however, is difficult owing to its highly non-condensable nature and, therefore, low sorption in polymer films.  This study seeks to quantify how H2 sorption changes during conversion of a thermally rearranged (TR) polymer and assess differences between H2 sorption in TR polymers and in other polymers reported in the membrane literature.

TR polymers are synthesized from reactive polyimide precursors, which contain hydroxyl groups ortho-position to the diamine [2-4].  These polyimide precursors are synthesized through traditional polyimide chemistry [5, 6], cast as films, and converted to TR polymers in the solid state via a thermally induced reaction.  For this study, we focus on a polyimide precursor prepared from 3,3'-dihydroxy-4,4'-diamino-biphenyl (HAB) and 2,2'-bis-(3,4-dicarboxyphenyl) hexafluoropropane dianhydride (6FDA).  This polyimide, along with three partially converted HAB-6FDA TR polymers were tested in this study.  The partially converted TR polymers were converted 39%, 60%, and 76% by heating the polyimide precursor under N2 for different amounts of time and at different temperatures.  To avoid polymer degradation, which occurs at sufficiently high temperatures, samples were not converted above 76%.  Samples were characterized using 1HNMR, TGA-MS, DSC, FT-IR, and XRD, and sorption was determined using a Rubotherm Magnetic Suspension Balance.

H2 sorption in the HAB-6FDA polyimide is similar to that of Matrimid™, which is a polyimide used industrially for gas separations.  Interestingly, thermal rearrangement induces significant changes in sorption capacity for HAB-6FDA.  Compared to the polyimide, H2 sorption increases by a factor of approximately 2.6 for the 76% converted HAB-6FDA TR polymer.  This dramatic increase in sorption (i.e., a factor of 2.6) is largely driven by non-equilibrium free volume in the polymer and matches the increase in sorption observed for N2, O2, and CH4 in the same material.  Surprisingly, over the same extent of conversion, CO2 sorption only increases by a factor of approximately 1.7.  This difference is likely attributed to a quadrupolar moment that exists in CO2 but not in H2, N2, O2, and CH4 [7].  This quadrupolar moment would encourage favorable interactions with polymer carbonyl groups [8] that are found in the HAB-6FDA polyimide, but are lost during the thermal rearrangement process.  When compared to Matrimid™, polysulfone, AF2400, and the other partially converted TR polymers, H2 sorption was highest in the 76% converted HAB-6FDA TR polymer. 

The enthalpy of sorption was also determined as a function of conversion for HAB-6FDA.  The HAB-6FDA polyimide had a similar enthalpy of sorption to Matrimid™.  However, the enthalpy of sorption decreased in magnitude as the polyimide was converted to its TR polymer.  This change in the enthalpy of sorption likely results from increasing free volume within the polymer film [9].  For the 76% converted HAB-6FDA TR polymer, the enthalpy of sorption decreased in magnitude to values similar to AF2400, which is another high free volume polymer.

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See more of this Session: Membranes for Hydrogen Purification II

See more of this Group/Topical: Separations Division