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Pressure Swing Adsorption for Hydrogen Purification Appendix 5 Parameter estimation 5.1 LDF coefficients estimation 5.1.1 Variance of 0.05 Table 5.12 – gPROMS® output for the parameter estimation performed considering a constant variance of 0.05 H2 CH4 CO2 CO N2 H2 CH4 CO2 CO N2 Original ω 0.700 0.195 0.035 0.15 0.261 0.700 0.147 0.0135 0.063 0.099 Final value, 𝜔 0.665 0.167 0.027 0.108 0.23 0.665 0.185 0.0599 0.045 0.14 Confidence interval 90% 95% 99% Activated Carbon 477.4 568.9 748 11.69 13.93 0.5692 0.6783 0.8919 18.32 23.27 27.73 21.74 25.91 Zeolite 166.8 198.7 36.47 34.07 261.3 0.5071 0.6043 0.7946 0.2978 0.08414 0.6762 0.355 0.1003 0.8059 0.4667 0.1318 1.06 Parameter Estimation 67PDF Image | PRESSURE SWING ADSORPTION FOR THE PURIFICATION OF HYDROGEN
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CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info
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