(10 points) The overall reaction order n for a global one-step hydrocarbon-air mechanism is given to be n = 1.75, where the global reaction rate is expressed in standard Arrhenius form: ( ) exp{ } R T E k T A U − A = . What are the units (SI units, as we have been using in lecture) for the preexponential factor A in this case?
(10 points) Consider a steady one-dimensional laminar premixed flame with hydrocarbon-air reactants (a non-methane paraffin fuel). For a reference condition of ambient pressure and temperature reactants (p = 1 atm, Tu = 298 K) and no dilution (Ydil = 0), the laminar flame speed is approximately sl,ref = 0.5 m/s at an equivalence ratio of Φ = 1.1. Use the Metghalchi & Keck laminar flame speed correlation (with BM = 0.5 m/s, B2 = -3 BM , ΦM = 1.1) to estimate the laminar flame speed sl for each of the following sets of conditions: a. p = 1 atm, Tu = 600 K, Φ = 1.1, Ydil = 0 b. p = 10 atm, Tu = 298 K, Φ = 1.1, Ydil = 0 c. p = 1 atm, Tu = 298 K, Φ = 0.7, Ydil = 0 d. p = 1 atm, Tu = 298 K, Φ = 1.1, Ydil = 0.10
(10 points) Consider a fully turbulent momentum-dominated axisymmetric hydrocarbon-air jet flame. By approximately what factor does the mean flame length change with: a. A factor of two increase in fuel nozzle diameter (fixed flowrate and fuel type)? b. A factor of two increase in fuel flow rate (fixed nozzle diameter and fuel type)? c. A switch in fuel from propane to hydrogen (fixed nozzle diameter and flowrate)? d. A switch in fuel from propane to methanol (fixed nozzle diameter and flowrate)?
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