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Figure 4.17 – Experimental data and major iterations performed by gPROMS® for the parameter estimation................................................................................................................. 40 Figure 4.18 – Comparison of the experimental data with the simulation results employing the LDF coefficients obtained through the parameter estimation ........................................................ 41 Figure 4.19 - Experimental data and major iterations performed by gPROMS® for the parameter estimation for a constant variance of 0.01 ......................................................................... 43 Figure 4.20 – Major iterations for the Multisite Langmuir isotherm parameter estimation for a constant variance of 0.05.......................................................................................................... 45 Figure 5.1 – Adsorption bed dialog box .............................................................................. 54 Figure 5.2 –Multilayer Langmuir-Freundlich isotherm dialog box ............................................... 55 Figure 5.3 – Simulation and experimental breakthrough data comparison for a five mixture at a feed pressure of 10 atm and a feed flow rate of 8.6 SLPM for a 0.5 cr .............................................. 59 Figure 5.4 - Simulation and experimental breakthrough data comparison for a five mixture at a feed pressure of 10 atm and a feed flow rate of 8.6 SLPM for a 0.32 cr ............................................. 60 Figure 5.5 - Simulation and experimental breakthrough data comparison for a five mixture at a feed pressure of 10 atm and a feed flow rate of 8.6 SLPM for a 0.65 cr ............................................. 60 Figure 5.6 – Simulation and experimental breakthrough curves for a column filled with activated carbon at 6.5 bar and 5.0 SLPM ................................................................................................ 61 Figure 5.7 - Simulation and experimental breakthrough curves for a column with two layers of adsorbent at a feed pressure of 6.5 bar and feed flow rate of 5 SLPM ........................................ 61 Figure 5.8 - Simulation and experimental breakthrough curves for a column with two layers of adsorbent at a feed pressure of 8 bar and 5 LSPM................................................................. 62 Figure 5.9 – Multisite Langmuir dialog box .......................................................................... 63 Figure 5.10 – Loading profiles for t = 40 s ........................................................................... 66 Figure 5.11 – Loading profiles for t = 100 s ......................................................................... 66 Figure 5.12 – Loading profiles for t = 1000 s ........................................................................ 66 Figure 5.13 – Measured data and major iterations for a relative constant variance of 0.05 ............... 70 Pressure Swing Adsorption for Hydrogen Purification vPDF 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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