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n-Pentane is burned with excess air in a continuous combustion chamber. (a) A technician runs an analysis and reports that the product gas contains 0.270 mole\% pentane, \(5.3 \%\) oxygen, \(9.1 \%\) carbon dioxide, and the balance nitrogen on \(a\) dry basis. Assume 100 mol of dry product gas as a basis of calculation, draw and label a flowchart, perform a degree-offreedom analysis based on atomic species balances, and show that the system has -1 degree of freedom. Interpret this result. (b) Use balances to prove that the reported percentages could not possibly be correct. (c) The technician reruns the analysis and reports new values of 0.304 mole\% pentane, \(5.9 \%\) oxygen, \(10.2 \%\) carbon dioxide, and the balance nitrogen. Verify that this result could be correct and, assuming that it is, calculate the percent excess air fed to the reactor and the fractional conversion of pentane. (d) It was emphasized in Part (c) that the new composition could be correct. Explain why it isn't possible to say for sure; illustrate your response by considering a set of equations with -1 degree of freedom.

Short Answer

Expert verified
The reported initial compositions are incorrect because they give us one degree of freedom instead of the specified -1. This inconsistency is fixed with the revised values, allowing us to calculate the excess air provided in the process and the fractional conversion of pentane. However, certainty is only as good as the degrees of freedom allow. In this case, with -1 degrees of freedom, an additional variable could change and may not have been accounted for, affecting the certainty of the compositions reported.

Step by step solution

01

Calculating Degree of Freedom

A degree of freedom analysis involves counting the number of unknowns versus the number of independent equations you have to solve for them. The stoichiometry of the combustion reaction of pentane (C5H12) is as follows \(C5H12 + 8O2 → 5CO2 + 6H2O\) . Hence, the number of unknowns in this case are the moles of pentane, oxygen, carbon dioxide, and water vapor, which gives us a total of 4 unknowns. Since we are dealing with an excess air scenario, the moles of nitrogen are not unknown. As for the number of independent equations at hand, they are obtained from the atomic species balances (i.e., carbon balance, hydrogen balance, and oxygen balance). There are 3 such independent equations. Therefore, the degree of freedom is calculated as the number of unknowns minus the number of independent equations, which in this case equals 1 (4-3). But the question mentions the degree of freedom to be -1, which is a discrepancy.
02

Validity of Reported Percentages

In order to check if the reported percentages of product gases are plausible, insert them into the species balance equations that were derived from reacting stoichiometry. If the results do not conform to said equations, then these percentages are incorrect.
03

Verification of Revised Percentages and Calculation of Excess Air and Conversion

Perform a similar process for the revised values. If these new compositions match the species balance equations, then they are correct. Calculate the amount of excess air in the feed by comparing the moles of oxygen present in the products to the amount required for complete combustion of pentane. Furthermore, the fractional conversion of pentane is calculated by comparing the initial number of moles of pentane with the final number of unreacted moles (if any) in the products.
04

Reasoning on Certainty

When there is -1 degree of freedom, this indicates there is an additional variable that is currently not being considered. One cannot definitively assert the correctness of the compositions without further information.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Combustion Reaction Stoichiometry
Understanding the stoichiometry of a combustion reaction is critical when analyzing chemical processes involving the burning of a compound. Stoichiometry involves the quantitative relationship between the reactants and products in a chemical reaction. In the context of combustion, this typically involves a hydrocarbon (like n-pentane) reacting with oxygen to produce carbon dioxide, water, and other gases.

For instance, the stoichiometric combustion of n-pentane (\(C_5H_{12}\)) can be represented by the equation: \[C_5H_{12} + 8O_2 \rightarrow 5CO_2 + 6H_2O\].

This means that one mole of n-pentane requires eight moles of oxygen to completely react to form five moles of carbon dioxide and six moles of water. In real-world scenarios, however, the reaction would typically take place with excess air to ensure complete combustion. This is important for analyses because it affects the composition of the product gases and their subsequent use in calculations such as species balance equations and determining the percentage of excess air.
Degree of Freedom Analysis
A degree of freedom analysis is an essential part of chemical process analysis. It helps determine if the system of equations describing the process has a unique solution. The degrees of freedom are calculated as the number of independent variables minus the number of independent equations. In chemical processes, the independent variables usually include the moles or concentrations of reactants and products, while the independent equations arise from mass balances, energy balances, and species balances.

In our example, with the combustion of n-pentane, we consider four unknowns (moles of pentane, oxygen, carbon dioxide, and water vapor) and three atomic species balances (carbon, hydrogen, and oxygen), resulting in one degree of freedom. However, negative degrees of freedom, as suggested by the exercise, indicate an over-specified system and typically point to an error in the data or the assumption of excess species that was not accounted for. This discrepancy requires a re-evaluation of the system's parameters.
Species Balance Equations
Species balance equations are foundational to solving combustion and chemical reaction problems. They elucidate how different elements and compounds are transformed and conserved in the reaction process. The key to species balances is the law of conservation of mass, which states that in a closed system not subjected to a nuclear reaction, the mass of an element must remain constant over the course of a chemical reaction.

In the given problem, we derive species balances for carbon, hydrogen, and oxygen. For example, the carbon balance ensures that the moles of carbon in n-pentane entering the reaction are equal to the moles of carbon in the carbon dioxide and any unreacted pentane in the output. \[C_5H_{12} \rightarrow xCO_2 + yC_5H_{12}\]
The reported percentages can be converted to mole percentages and checked against these balance equations to see if the reported outcome is reasonable. This not only allows us to verify the accuracy of the technician's report but also helps us understand the conversion efficiency and the excess air provided during the combustion process.

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Most popular questions from this chapter

If the percentage of fuel in a fuel-air mixture falls below a certain value called the lower flammability limit (LFL), which sometimes is referred to as the lower explosion limit (LEL), the mixture cannot be ignited. In addition there is an upper flammability limit (UFL), which also is known as the upper explosion limit (UEL). For example, the LFL of propane in air is 2.3 mole \(\% \mathrm{C}_{3} \mathrm{H}_{8}\) and the UFL is \(9.5 \%^{14}\). If the percentage of propane in a propane-air mixture is greater than \(2.3 \%\) and less than \(9.5 \%,\) the gas mixture can ignite if it is exposed to a flame or spark. A mixture of propane in air containing 4.03 mole \(\% \mathrm{C}_{3} \mathrm{H}_{8}\) (fuel gas) is the feed to a combustion furnace. If there is a problem in the furnace, a stream of pure air (dilution air) is added to the fuel mixture prior to the furnace inlet to make sure that ignition is not possible. (a) Draw and label a flowchart of the fuel gas-dilution air mixing unit, presuming that the gas entering the furnace contains propane at the LFL, and do the degree-of-freedom analysis. (b) If propane flows at a rate of \(150 \mathrm{mol} \mathrm{C}_{3} \mathrm{H}_{8} / \mathrm{s}\) in the original fuel-air mixture, what is the minimum molar flow rate of the dilution air? (c) How would the actual dilution air feed rate probably compare with the value calculated in Part (b)? (>, \(<,=\) ) Explain.

Seawater containing 3.50 wt\% salt passes through a series of 10 evaporators. Roughly equal quantities of water are vaporized in each of the 10 units and then condensed and combined to obtain a product stream of fresh water. The brine leaving each evaporator but the tenth is fed to the next evaporator. The brine leaving the tenth evaporator contains \(5.00 \mathrm{wt} \%\) salt. (a) Draw a flowchart of the process showing the first, fourth, and tenth evaporators. Label all the streams entering and leaving these three evaporators. (b) Write in order the set of equations you would solve to determine the fractional yield of fresh water from the process \(\left(\mathrm{kg} \mathrm{H}_{2} \mathrm{O} \text { recovered } / \mathrm{kg} \mathrm{H}_{2} \mathrm{O}\) in process feed) and the weight percent of salt in the \right. solution leaving the fourth evaporator. Each equation you write should contain no more than one previously undetermined variable. In each equation, circle the variable for which you would solve. Do not do the calculations. (c) Solve the equations derived in Part (b) for the two specified quantities. (d) The problem statement made no mention of the disposition of the 5 wt\% effluent from the tenth evaporator. Suggest two possibilities for its disposition and describe any environmental concerns that might need to be considered.

The reaction between ethylene and hydrogen bromide to form ethyl bromide is carried out in a continuous reactor. The product stream is analyzed and found to contain 51.7 mole \(\% \mathrm{C}_{2} \mathrm{H}_{5} \mathrm{Br}\) and 17.3\% HBr. The feed to the reactor contains only ethylene and hydrogen bromide. Calculate the fractional conversion of the limiting reactant and the percentage by which the other reactant is in excess. If the molar flow rate of the feed stream is \(165 \mathrm{mol} / \mathrm{s}\), what is the extent of reaction?

Ethylene oxide is produced by the catalytic oxidation of ethylene: $$ 2 \mathrm{C}_{2} \mathrm{H}_{4}+\mathrm{O}_{2} \longrightarrow 2 \mathrm{C}_{2} \mathrm{H}_{4} \mathrm{O} $$ An undesired competing reaction is the combustion of ethylene: $$ \mathrm{C}_{2} \mathrm{H}_{4}+3 \mathrm{O}_{2} \longrightarrow 2 \mathrm{CO}_{2}+2 \mathrm{H}_{2} \mathrm{O} $$ The feed to the reactor (not the fresh feed to the process) contains 3 moles of ethylene per mole of oxygen. The single-pass conversion of ethylene is \(20 \%,\) and for every 100 moles of ethylene consumed in the reactor, 90 moles of ethylene oxide emerge in the reactor products. A multiple-unit process is used to separate the products: ethylene and oxygen are recycled to the reactor, ethylene oxide is sold as a product, and carbon dioxide and water are discarded. (a) Assume a quantity of the reactor feed stream as a basis of calculation, draw and label the flowchart, perform a degree-of-freedom analysis, and write the equations you would use to calculate (i) the molar flow rates of ethylene and oxygen in the fresh feed, (ii) the production rate of ethylene oxide, and (iii) the overall conversion of ethylene. Do no calculations. (b) Calculate the quantities specified in Part (a), either manually or with an equation-solving program. (c) Calculate the molar flow rates of ethylene and oxygen in the fresh feed needed to produce 1 ton per hour of ethylene oxide.

Inside a distillation column (see Problem 4.8), a downward-flowing liquid and an upward-flowing vapor maintain contact with each other. For reasons we will discuss in greater detail in Chapter \(6,\) the vapor stream becomes increasingly rich in the more volatile components of the mixture as it moves up the column, and the liquid stream is enriched in the less volatile components as it moves down. The vapor leaving the top of the column goes to a condenser. A portion of the condensate is taken off as a product (the overhead product), and the remainder (the reflux) is returned to the top of the column to begin its downward journey as the liquid stream. The condensation process can be represented as shown below: A distillation column is being used to separate a liquid mixture of ethanol (more volatile) and water (less volatile). A vapor mixture containing 89.0 mole \(\%\) ethanol and the balance water enters the overhead condenser at a rate of \(100 \mathrm{lb}\) -mole/h. The liquid condensate has a density of \(49.01 \mathrm{b}_{\mathrm{m}} / \mathrm{ft}^{3},\) and the reflux ratio is \(3 \mathrm{lb}_{\mathrm{m}}\) reflux/lb \(_{\mathrm{m}}\) overhead product. When the system is operating at steady state, the tank collecting the condensate is half full of liquid and the mean residence time in the tank (volume of liquid/volumetric flow rate of liquid) is 10.0 minutes. Determine the overhead product volumetric flow rate (ft \(^{3}\) /min) and the condenser tank volume (gal).

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