The following empirical equation correlates the values of variables in a system in which solid particles are suspended in a flowing gas 1/2 kg dpy 1/3 (dp u p = 2.00 + 0.600 D Both pD andp - are...

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Extracted text: The following empirical equation correlates the values of variables in a system in which solid particles are suspended in a flowing gas 1/2 kg dpy 1/3 (dp u p = 2.00 + 0.600 D Both pD andp - are dimensionless groups; k, is a coefficient that expresses the rate at which a particular species transfers from the gas to the solid particles; and the coefficients 2.00 and 0.600 are dimensionless constants obtained by fitting experimental data covering a wide range of values of the equation variables. Estimate the values of k, for the following data: Case dp D. (dimensionless) 1.00 x 10-5 (N-s)/m? 5.00 1.250 x 10 0.200 0.170 cm2/s 20.0 m/s m/s g/cm mm 1.05 x 10-4 ft2/s 3.00 x 10-7 (Ibr-s) /ft? 0.300 in 0.100 0.3000 Ib/ft 42.0 ft/s ft/s 0.250 2.60 x 10-5 4.00 x 104 1.30 kg/m 1000.0 cm/s 3 0.200 m2/s g/(cm-s) cm/s cm