Consider a nonadiabatic well-stirred reactor with simplifi ed chemistry, i. e., fuel, oxidizer, and a single product species. The reactants, consisting of fuel (YF = 0.2) and oxidizer (YOx = 0.8) at 298 K, fl ow into the 0.003-m3 reactor at 0.5 kg / s. The reactor operates at 1 atm and has a heat loss of 2000 W. Assume the following simplifi ed thermodynamic properties: cp = 1100 J / kg-K (all species), MW = 29 kg / kmol (all species), hf F o , = −2000 kJ/ kg, hf Ox o , = 0, and hf o , Pr = −4000 kJ/ kg. The fuel and oxidizer mass fractions in the outlet stream are 0.001 and 0.003, respectively. Determine the temperature in the reactor and the residence ti