The design of chemical processes relies on simulation. However, the results
are strongly dependent on thermodynamic models for the basic properties. W
hile proper choice of the thermodynamic model is important, even with the b
est available model, the uncertainties in the model parameters and the expe
rimental data that are used to regress them can be significant. The uncerta
inty induced from the different simulators is another factor to be consider
ed in process design. Through a series of case studies on steady-state and
dynamic simulation, we show how uncertainties of the thermodynamic data and
models of the system can have a profound effect on the process design. In
the meantime, the strategies for quantification of such thermodynamic-param
eter-induced uncertainties via Monte Carlo simulation, with the Latin hyper
cube sampling technique, equal probability sampling technique, and regressi
on analyses, are described, The study indicates that the designs developed
through use of these models are significantly sensitive to the parameter un
certainties.