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The equilibrium constant describing phenolic OH/ester carbonyl hydrogen bonds (KA) has been experimentally determined from the quantification of the hydrogen-bonded carbonyl group fraction as a function of temperature, and the effect of functional group accessibility on KA values has been discussed.
(b) Bar chart showing the packing fraction as a function of a/b ratio.
The solution gives the expression of dissociation fraction as a function of temperature on a streamline.
Results are presented in terms of bifurcation diagrams for the phase fraction as a function of milling power.
Existing correlations for interfacial shear stress friction factor and the void fraction as a function of gas superficial velocity were also gathered and briefly discussed.
Correlations are obtained for the distribution of melting front and solid fraction as a function of time during charging and discharging of LHTES.
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Figure 6 presents the results of the viscosity of the nanofluids with different volume fractions as a function of temperature.
A detailed soot model is included which can predict soot volume fractions as a function of the strain rate and the fuel mole fraction.
The convective heat transfer coefficient of the nanofluids with different volume fractions as a function of Reynolds number (Re) was shown in Fig. 9.
The substrate response model calculates the distribution of the alloying elements as well as the evolution of the phase fractions as a function of depth and oxidation time.
A comparison with experimental measurements is given, showing variation of phase fractions as a function of particle size for Al Ni atomized droplets.
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