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Solubility of Supercritical CO2 in Polystyrene during Foam Formation via Statistical Associated Fluid Theory (SAFT) Equation of State

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Figure

Figure 1: Liquid and vapor phase fugacity coefficients of carbon dioxide at -13 oC as a function of pressure
Figure 2: Saturation pressure versus temperature for carbon dioxide.  The solid line is SAFT EOS
Figure 3: Equilibrium liquid and vapor densities versus temperature for carbon dioxide
Figure 4: P-x-y diagram for the carbon dioxide/methanol system at 40 is the SAFT EOS and the dashed line is the SRK EOS
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