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Influences of parameter uncertainty on model solutions are thoroughly examined.

Model solutions are published immediately after the deadline (Dihoff et al. 2004).

The model solutions are investigated by using well-known performance measures and also three problem-specific performance measures are proposed.

Experimental conditions of rheological test for model solutions are as follows: laminar steady-state flow, no slippage, homogeneity of samples and no chemical changes in the sample.

The simplified model solutions are compared to the results of a more complex and detailed multi-story finite element analysis model.

An asymptotic limit analysis based on the semi-geostrophic theory shows that the model solutions are converging to a solution in cross-front geostrophic balance.

Oscillatory behavior of the model solutions is also investigated.

Six model hydrocarbon systems (model solutions) were wax (52 54 °C m.p). in kerosene solutions.

These model solutions were obtained assuming an L2 measure of the misfit.

However, the highest recoveries for the model solutions were within the pH range of 8 10.

The effect of volume of sample on the model solutions were investigated within the range of 10 250 mL.