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Problem 2: Consider ethane combustion with air in a well-stirred reactor, with Af = 4.24*108 (kg/m3)-0.755-7, n=1.75, p = 1 atm, Ta = 15100K. Assume
Problem 2: Consider ethane combustion with air in a well-stirred reactor, with Af = 4.24*108 (kg/m3)-0.755-7, n=1.75, p = 1 atm, Ta = 15100K. Assume Cp to be equal and constant for all species at 2 KJ/kg-K. Using the approach as developed in class: m A. Plot reactor Temperature and fuel mass fraction vs normalized Mass flow rate, V (in kg/m3-s) until blowout as in Fig 6.7 in Turns. Assume To=600K. B. Produce a plot of To vs normalized mass flow rate at the blowout condition (in kg/m3-s), similar to fig 6.8 in Turns. Take the range of To to be 450K-800K. You may use equation 8.1.94 (from uploaded chapter notes)
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