Methane and \(30 \%\) excess air are to be fed to a combustion reactor. An
inexperienced technician mistakes his instructions and charges the gases
together in the required proportion into an evacuated closed tank. (The gases
were supposed to be fed directly into the reactor.) The contents of the
charged tank are at \(25^{\circ} \mathrm{C}\) and 4.00 atm absolute.
(a) Calculate the standard internal energy of combustion of the methane
combustion reaction. \(\Delta \hat{U}_{c}^{\circ}(\mathrm{kJ} / \mathrm{mol}),\)
taking \(\mathrm{CO}_{2}(\mathrm{g})\) and \(\mathrm{H}_{2}
\mathrm{O}(\mathrm{v})\) as the presumed products. Then prove that if the
constant-pressure heat capacity of an ideal-gas species is independent of
temperature, the specific internal energy of that species at temperature
\(T\left(^{\circ} \mathrm{C}\right)\) relative to the same species at
\(25^{\circ} \mathrm{C}\) is given by the expression
$$\hat{U}=\left(C_{p}-R\right)\left(T-25^{\circ} \mathrm{C}\right)$$
where \(R\) is the gas constant. Use this formula in the next part of the
problem.
(b) You wish to calculate the maximum temperature, \(T_{\max }\left(^{\circ}
\mathrm{C}\right),\) and corresponding pressure, \(P_{\max }(\text { atm }),\)
that the tank would have to withstand if the mixture it contains were to be
accidentally ignited. Taking molecular species at \(25^{\circ} \mathrm{C}\) as
references and treating all species as ideal gases, prepare an inlet-outlet
internal energy table for the closed system combustion process. In deriving
expressions for each \(\dot{U}_{i}\) at the final reactor condition
\(\left(T_{\max }, P_{\max }\right),\) use the following approximate values for
\(C_{p_{i}}\left[\mathrm{k} J /\left(\mathrm{mol} \cdot^{\circ}
\mathrm{C}\right)\right]: 0.033 \mathrm{for} \mathrm{O}_{2}, 0.032\) for
\(\mathrm{N}_{2}, 0.052 \mathrm{for} \mathrm{CO}_{2},\) and \(0.040 \mathrm{for}
\mathrm{H}_{2} \mathrm{O}(\mathrm{v}) .\) Then use an energy balance and the
ideal-gas equation of state to perform the required calculations.
(c) Why would the actual temperature and pressure attained in a real tank be
less than the values calculated in Part (a)? (State several reasons.)
(d) Think of ways that the tank contents might be accidentally ignited. The
list should suggest why accepted plant safety regulations prohibit the storage
of combustible vapor mixtures.