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II Table of Contents IV 5.2.1 Half-cycle time..................................................................................................... 52 5.2.2 Purge flow rate ..................................................................................................... 54 5.2.3 Cutting time .......................................................................................................... 57 5.3 Effect of plant design................................................................................................. 59 5.3.1 Flow resistances in the piping system .................................................................. 59 5.3.2 Volume of the N2-receiver tank ........................................................................... 68 5.4 6 7 8 8.1 8.2 8.3 9 10 Accuracy evaluation of the results............................................................................. 71 PSA process dynamics.................................................................................................... 73 Performance intensification strategies ............................................................................ 78 Summary and final conclusions ...................................................................................... 82 Overview of findings ................................................................................................. 82 Critical discussion of the work .................................................................................. 82 Outlook ...................................................................................................................... 83 References ....................................................................................................................... 85 Appendix......................................................................................................................... 92 10.1 Interparticle diffusion coefficients............................................................................. 92 10.2 Gas thermal conductivity........................................................................................... 93 10.3 Gas-solid heat transfer coefficient ............................................................................. 94 10.4 Adsorbed phase heat capacity.................................................................................... 94 10.5 Pressure drop due to uncontrolled flow resistances in the piping system ................. 95 10.6 Flow coefficients of controlled flow resistances in the piping system...................... 95 10.7 Pressure drop along the packed-bed .......................................................................... 98 10.8 Statistical analysis of adsorbent pellets geometry ..................................................... 99 10.9 Implementation of the kinetic model into the process simulator............................. 100PDF Image | Modelling and Simulation of Twin-Bed Pressure Swing Adsorption Plants
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