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An adiabatic constant-volume tank contains a mixture of \(1 \mathrm{kmol}\) of hydrogen \(\left(\mathrm{H}_{2}\right)\) gas and the stoichiometric amount of air at \(25^{\circ} \mathrm{C}\) and 1 atm. The contents of the tank are now ignited. Assuming complete combustion, determine the final temperature in the tank.

Short Answer

Expert verified
Answer: The final temperature after complete combustion is 298 K or 25°C.

Step by step solution

01

Determine the stoichiometric equation

First, we need to write the stoichiometric equation for the combustion of hydrogen with oxygen (from air). The balanced equation for the combustion of hydrogen in oxygen is given by: 2H2 + O2 -> 2H2O
02

Determine the initial moles of each component and the final moles after the combustion process

We are given 1 kmol of hydrogen (H2), and the stoichiometric amount of air. Since air contains roughly 21% oxygen (O2) and 79% nitrogen (N2) by volume according to the problem, we can calculate the initial moles of O2 and N2: Initial amount of O2 needed = (1 kmol H2) * 1/2 = 0.5 kmol O2 Initial amount of N2 in the mixture = (0.5 kmol O2) * (79% N2/21% O2) = 1.88 kmol N2 All O2 will be consumed in the combustion process, and the number of moles of N2 will be conserved. After the combustion process, the moles of other components in the mixture are: Final amount of H2O = (1 kmol H2) * 1 = 1 kmol H2O Final amount of N2 = 1.88 kmol N2
03

Apply the energy conservation principle

Since the combustion process is adiabatic and constant-volume, we can apply the energy conservation principle: ΔU = Q - W = 0 where ΔU is the change in internal energy of the gas mixture, Q is the heat transfer, and W is the work done. The change in internal energy (ΔU) of the mixture can be expressed as: ΔU = nCv(T_final - T_initial) where n is the total moles of the mixture, Cv is the molar specific heat at constant volume, T_initial is the initial temperature, and T_final is the final temperature. Using the ideal gas law and the known properties of each component, we can determine the final temperature.
04

Calculate the final temperature

First, let's find the total initial moles in the mixture: n_initial = n_H2 + n_O2 + n_N2 = 1 + 0.5 + 1.88 = 3.38 kmol Now, let's find the total final moles in the mixture after the combustion process: n_final = n_H2O + n_N2 = 1 + 1.88 = 2.88 kmol After this, we can calculate the molar specific heat at constant volume (Cv) for each component of the mixture. For simplicity, we will assume the following values: - Cv for H2 = 2.40R - Cv for O2 = 2.79R - Cv for N2 = 2.49R - Cv for H2O = 3.00R Now, using the energy conservation principle: ΔU = (n_final * Cv_final - n_initial * Cv_initial) * (Tf - Ti) From the above equation, we only have Tf as the unknown value. We can now solve for Tf: Tf = Ti + (ΔU / (n_final * Cv_final - n_initial * Cv_initial)) Considering given initial temperature Ti = 25°C: Tf = 298 K + (0 / ( (1 kmol * 3.00R) + (1.88 kmol * 2.49R) - ((0.5 kmol * 2.79R) + (1.88 kmol * 2.49R) + (1 kmol * 2.40R)))) Tf = 298 K + 0 = 298 K The final temperature in the adiabatic constant-volume tank after complete combustion is 298 K or 25°C.

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Most popular questions from this chapter

A mixture of 40 percent by volume methane \(\left(\mathrm{CH}_{4}\right),\) and 60 percent by volume propane \(\left(\mathrm{C}_{3} \mathrm{H}_{8}\right),\) is burned completely with theoretical air and leaves the combustion chamber at \(100^{\circ} \mathrm{C}\). The products have a pressure of \(100 \mathrm{kPa}\) and are cooled at constant pressure to \(39^{\circ} \mathrm{C} .\) Sketch the \(T\) -s diagram for the water vapor that does not condense, if any. How much of the water formed during the combustion process will be condensed, in kmol \(\mathrm{H}_{2} \mathrm{O} / \mathrm{kmol}\) fuel?

Is the number of atoms of each element conserved during a chemical reaction? How about the total number of moles?

Acetylene \(\left(\mathrm{C}_{2} \mathrm{H}_{2}\right)\) is burned with 25 percent excess oxygen in a cutting torch. Determine the mass fraction of each of the products. Calculate the mass of oxygen used per unit mass of acetylene burned.

Using EES (or other) software, determine the effect of the amount of air on the adiabatic flame temperature of liquid octane \(\left(\mathrm{C}_{8} \mathrm{H}_{18}\right)\). Assume both the air and the octane are initially at \(25^{\circ} \mathrm{C}\). Determine the adiabatic flame temperature for 75,90,100,120,150,200,300 \(500,\) and 800 percent theoretical air. Assume the hydrogen in the fuel always burns \(\mathrm{H}_{2} \mathrm{O}\) and the carbon \(\mathrm{CO}_{2}\), except when there is a deficiency of air. In the latter case, assume that part of the carbon forms CO. Plot the adiabatic flame temperature against the percent theoretical air, and discuss the results.

Calculate the higher and lower heating values of a coal from Illinois which has an ultimate analysis (by mass) as 67.40 percent \(\mathrm{C}, 5.31\) percent \(\mathrm{H}_{2}, 15.11\) percent \(\mathrm{O}_{2}, 1.44\) percent \(\mathrm{N}_{2}, 2.36\) percent \(\mathrm{S},\) and 8.38 percent ash (non- combustibles). The enthalpy of formation of \(\mathrm{SO}_{2}\) is \(-297,100 \mathrm{kJ} / \mathrm{kmol}\).

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