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The total uncertainty is the quadratic sum of the systematic (nominal) and statistical (associated with uncontrollable parameters) uncertainties: ( {sigma}_T=sqrt{{sigma_N}^2+{sigma_S}^2} ) [5].
The Cahn Hilliard theory was combined with original statistical associated fluid theory equation of states (SAFT EOS) in order to describe both the phase behaviour and interfacial properties with respect of association.
Age was statistical associated with MACE (p < 0.004).
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Heterosegmented statistical associating fluid theory is used to represent the density of ionic liquid.
Heterosegmented statistical associating fluid theory (SAFT) is developed to model the thermodynamic properties of aqueous imidazolium ionic liquid solutions.
Statistical associating fluid theory (SAFT) and perturbed-chain SAFT (PC-SAFT) are used to model the phase behavior of polymer solvent mixtures over a wide temperature and pressure range.
Statistical associating fluid theory (SAFT) is an equation of state that can be used to calculate the phase behavior of mixtures comprised of components that exhibit wide disparities in molecular size, such as solvent polymer mixtures.
Here we apply the group contribution based statistical associating fluid theory for potential of variable range (GC-SAFT-VR) equation of state to the study of long chain fatty acid methyl esters that comprise biodiesel fuels.
This means that in calculating variances and covariances across the deme, we do not use any of the statistical corrections associated with sample statistics.
Statistical Associating Fluid Theory (SAFT) equations of state (EoS) for mixtures require cross-interaction parameters.
Herein, the Perturbed-Chain Statistical Associating Fluid Theory (PC-SAFT) equation of state is used as a thermodynamic model.
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