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An equimolar mixture of carbon dioxide and water vapor at 1 atm and \(60^{\circ} \mathrm{C}\) enter a dehumidifying section where the entire water vapor is condensed and removed from the mixture, and the carbon dioxide leaves at 1 atm and \(60^{\circ} \mathrm{C}\). The entropy change of carbon dioxide in the dehumidifying section is \((a)-2.8 \mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}\) \((b)-0.13 \mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}\) \((c) 0\) \((d) 0.13 \mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}\) \((e) 2.8 \mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}\)

Short Answer

Expert verified
a) Positive b) Negative c) Zero d) Cannot be determined Answer: c) Zero

Step by step solution

01

Calculate the initial entropy of CO2

As the initial and final temperatures are the same, the initial entropy of CO2, \(S_{initial}\), will be the same as final entropy, \(S_{final}\). Hence, we don't need to calculate the initial entropy of CO2.
02

Calculate the final entropy of CO2

Since the final temperature is the same as the initial temperature, the final entropy of CO2, \(S_{final}\), will be the same as the initial entropy, \(S_{initial}\). Hence, we don't need to calculate the final entropy of CO2 either.
03

Calculate the entropy change of CO2

Now, we can calculate the entropy change of carbon dioxide using the formula: \(\Delta S = S_{final} - S_{initial}\) But we know that \(S_{final} = S_{initial}\), so the equation becomes: \(\Delta S = S_{final} - S_{initial} = 0\) Therefore, the entropy change of carbon dioxide in the dehumidifying section is: \(\Delta S = 0\) The correct answer is \((c) 0\).

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Most popular questions from this chapter

Ethylene \(\left(\mathrm{C}_{2} \mathrm{H}_{4}\right)\) is burned with 175 percent theoretical air during a combustion process. Assuming complete combustion and a total pressure of 14.5 psia, determine (a) the air-fuel ratio and ( \(b\) ) the dew-point temperature of the products.

One kmol of ethane \(\left(\mathrm{C}_{2} \mathrm{H}_{6}\right)\) is burned with an unknown amount of air during a combustion process. An analysis of the combustion products reveals that the combustion is complete, and there are 3 kmol of free \(\mathrm{O}_{2}\) in the products. Determine ( \(a\) ) the air-fuel ratio and ( \(b\) ) the percentage of theoretical air used during this process.

Liquid propane \(\left(\mathrm{C}_{3} \mathrm{H}_{8}(\ell)\right)\) enters a combustion chamber at \(25^{\circ} \mathrm{C}\) and 1 atm at a rate of \(0.4 \mathrm{kg} / \mathrm{min}\) where it is mixed and burned with 150 percent excess air that enters the combustion chamber at \(25^{\circ} \mathrm{C}\). The heat transfer from the combustion process is \(53 \mathrm{kW}\). Write the balanced combustion equation and determine \((a)\) the mass flow rate of air; \((b)\) the average molar mass (molecular weight) of the product gases; \((c)\) the average specific heat at constant pressure of the product gases; and ( \(d\) ) the temperature of the products of combustion.

Acetylene gas \(\left(\mathrm{C}_{2} \mathrm{H}_{2}\right)\) at \(25^{\circ} \mathrm{C}\) is burned during a steady-flow combustion process with 30 percent excess air at \(27^{\circ} \mathrm{C} .\) It is observed that \(75,000 \mathrm{kJ}\) of heat is being lost from the combustion chamber to the surroundings per kmol of acetylene. Assuming combustion is complete, determine the exit temperature of the product gases.

What is enthalpy of formation? How does it differ from the enthalpy of combustion?

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