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saturated liquid HTF recirculation approach illustrated in the previous section, it is possible to recover CH4 from the desorption sink without a parasitic heat load; however, an independent treatment of the collected gas collected is needed as it would have different gas mole fractions than the product mole fractions. This is also why CH4 recovery values in the present work are lower than those of Pahinkar et al. (2016), because the gases recovered from the desorption sink are not considered for calculation of recovery in the present work. Nevertheless, the product purity remains comparable to those of Pahinkar et al. (2016). The CH4 recovery values reported here are also competitive with those from the bed-based PSA system investigated by Kapoor and Yang (1989). The similarity in recovery factors and the greater process capacity indicates the potential for large-scale feasibility of the system considered here. Figure 3.5. Product purity vs. CH4 recovery compared with the PSA and TSA processes in the literature (Kapoor and Yang, 1989; Olajossy et al., 2003; Pahinkar et al., 2016) 78PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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