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SUMMARY Natural gas has become increasingly important as a fuel source with lower environmental impact; therefore, there is a growing need for scalable natural gas purification systems with small footprints. Current industrial purification systems are based on absorption, membrane separation, or adsorption techniques; however, each of these technologies requires large capital costs or suffers from scalability issues. Adsorption-based separation techniques are categorized into pressure-swing adsorption (PSA) and temperature-swing adsorption (TSA). Among adsorption-based gas purification techniques, PSA has typically been preferred over TSA due to the ease of operation and reliability. TSA processes have not commonly been used for industrial gas separation due to the typically low thermal conductivity of the adsorbent bed, which poses challenges for desorption of impurities and regeneration of the adsorbent. However, the high heat and mass transfer coefficients possible with microchannels offer the potential for using the TSA process for gas purification. The present work investigates the fluid mechanics and coupled heat and mass transfer processes within a microchannel monolith with a polymer-adsorbent matrix coating the inner walls of the microchannels during TSA-based gas separation. Carbon dioxide is separated from methane by passing the feed gas through microchannels, followed by sequential flow of desorbing hot liquid, cooling liquid, and purge gas through the same microchannels. For selected operating conditions and geometries, the process shows merit when compared to current technologies. A combination of spatially- and temporally-resolved analyses was conducted to assess these processes and select optimal configurations and process parameters. Experimental validation followed, xxviPDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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