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With the silicalite–water pair and a Dh of 530 m and th of 30 m, the proposed concept can produce high purity output with a moderate CH4 recovery in purification cycles of 203 s duration. The estimated process capacity of the present study is not only about two orders of magnitude greater than the capacity of the bed-based PSA processes, but is also an improvement over a design with separate alternating microchannels for gas and HTF flow. Chapter 3 reports a comprehensive investigation of this process for a range of attainable purities, recovery factors and energy efficiencies to determine its viability for an actual large scale installation. 67PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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