The new kinetically limited linear driving force (KLLDF) model was compared against the LDF model to predict the separation of CH
4/N
2 and CH
4/CO
2 via pressure swing adsorption (PSA) using carbon molecular sieve (CMS) 172K. The PSA cycle was carried out at room temperature in a single one liter bed and consisted of the following cycle steps: feed pressurization, feed, three equalizations down, countercurrent depressurization, light reflux, three equalizations up and idle. Three 3.8 liter tanks were used to temporarily store the gas during the equalization steps. In the case of CH
4/N
2 separation the PSA cycle was carried out with an 85/15 mixture with the pressures oscillating between 28 and 606 kPa. In the case CH
4/CO
2 separation the PSA cycle was carried out also with an 85/15 mixture with the pressures oscillating between 101 and 345 kPa. The results show that for both separations the KLLDF model consistently displayed a superior predictive ability than the LDF model under all conditions, especially for CH
4/CO
2 where experiments and modelling displayed excellent agreement. In the case of CH
4/N
2 separation, deviations were observed between predictions and experiments with the KLLDF model that became more significant with shorter cycle times. Such deviations resulted from apparently larger mass transfer coefficients observed by the experimental results. These deviations were consistent with penetration (Carta, 1993; Alpay and Scott, 1992; Nakao and Suzuki, 1983) because of the slow kinetics of N
2, which is the faster diffusing species in the CH
4/N
2 system. These results also explain why from this theory no such deviations were observed with the CH
4/CO
2 system. Specific details about how these two systems respectively agree with and disagree with penetration theory will be provided.
Carta, G. (1993) The linear driving force approximation for cyclic mass transfer in spherical particles. Chemical Engineering Science, 48(3), 622-625.
Alpay, E. and Scott, D. M. (1992) The linear driving force model for fast-cycle adsorption and desorption in a spherical particle. Chemical Engineering Science, 47(2), 499-502.
Nakao, S-I. and Suzuki, M. (1983) Mass transfer coefficient in cyclic adsorption and desorption. Journal of Chemical Engineering of Japan, 16(2), 114-119.