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To test this hypothesis, IDTs with a detailed gasoline surrogate chemical kinetic model have been calculated at various temperatures and pressures.
Stark tuning rates have been calculated at various CO coverages; a linear dependence between the CO Stark tuning rate and the CO surface coverage has been found.
DEG) at 30°, 35° and 40°C, have been calculated at various concentrations, from the electromotive force measurements of the cell of the type: Standard free energy of transfer, ΔG°t r., from water to AQ·DEG and from DEG to AQ. DEG has also been calculated from the E° values of the cell.
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Dependence Nu(Re) was calculated at various parameters of system.
In this study, the optimal absorber cut-off wavelength is calculated at various solar concentrating factors.
The inhibition efficiency IEw is calculated at various concentrations using Eq. (6).
The particle size was calculated at various cumulative factors using particle analyser.
Finally, the energy density of the DBPFC system operating at the optimum voltage efficiency was calculated at various fuel concentrations.
Thermal energy associated with the microwave transesterification process was calculated at various temperature levels using the optimized process parameters.
Finally, the different components of the power (stored and dissipated) and relative intensities are calculated at various operating conditions.
Pressure drop and overall heat-transfer coefficient is calculated at various tube and shell side process conditions.
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