Problem 1: Consider a spherical reactor with radius 30 cm and thickness 1 cm filled with propane-air mixture in stoichio
Posted: Fri Mar 04, 2022 10:29 am
Oxidation of Hydrocarbons Table 5.1 Single-step reaction rate parameters for use with Eqn. 5.2 (Adapted from Ref. (91) Pre-exponential Factor, A Activation Temperature, E_/R, (K) Fuel -0.3 13.10 83. 10 1.1 - 102 8.6. 1011 24.3585 15.0989 15.098 15.098 1.3 1.3 1.65 1.65 7.4 - 10 6.4 101 5.7. 1011 5.1 - 1011 15.098 15,098 15,098 15,098 0.5 0.25 0.25 0.25 1.6 1.5 1.5 1.5 CH, CH, С.Н. CH, CH10 C.H12 CH,4 CH CH: CH CH, CH, CH,OH С,НОН CH, С.Н. CH сн. CH, 4.6 1011 7.2. 1012 4.2. 1011 3.8 1011 15.098 20,1314 15,098 15,098 0.25 0.25 0.25 1.5 1.5 1.5 1.5 0.25 3.2 - 1012 1.5. 1012 2.0. 1011 1.6 - 10 15.098 15.098 15,098 15.098 0.25 0.15 -0.1 -0.1 15 1.6 1.85 1.85 2.0 . 1012 4.2 1011 6.5 . 1012 15,098 15.098 15.098 0.1 -0.1 0.5 1.65 1.85 1.25 "Units of A are consistent with concentrations in Egn. 5.2 expressed in units of gmol/em", i.e., A[=] (gmol/cm)-m-h/s. BE = 48.4 kcal/gmol. "E. = 30 kcal/gmol. E. = 40 kcal/gmol. where the parameters A, E,/R, m, and n. shown in Table 5.1, have been cho- sen to provide best agreement between experimental and predicted flame speeds and flammability limits (see Chapter 8). Note the treatment of units for A in the footnote