/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 63 A stream of liquid \(n\) -pentan... [FREE SOLUTION] | 91Ó°ÊÓ

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A stream of liquid \(n\) -pentane flows at a rate of \(50.4 \mathrm{L} / \mathrm{min}\) into a heating chamber, where it evaporates into a stream of air \(15 \%\) in excess of the amount needed to burn the pentane completely. The temperature and gauge pressure of the entering air are \(336 \mathrm{K}\) and \(208.6 \mathrm{kPa}\). The pentane-laden heated gas flows into a combustion furnace in which a fraction of the pentane is burned. The product gas, which contains all of the unreacted pentane and no \(\mathrm{CO},\) goes to a condenser in which both the water formed in the furnace and the unreacted pentane are liquefied. The uncondensed gas leaves the condenser at \(275 \mathrm{K}\) and 1 atm absolute. The liquid condensate is separated into its components, and the flow rate of the pentane is measured and found to be \(3.175 \mathrm{kg} / \mathrm{min}\). (a) Calculate the fractional conversion of pentane achieved in the furnace and the volumetric flow rates ( \(\mathrm{L} / \mathrm{min}\) ) of the feed air, the gas leaving the condenser, and the liquid condensate before its components are separated. (b) Sketch the apparatus that could have been used to separate the pentane and water in the condensate. Hint: Remember that pentane is a hydrocarbon and recall what is said about oil (hydrocarbons) and water.

Short Answer

Expert verified
The conversion of pentane in the furnace is 89.9%. The volumetric flow rate of feed air, the gas leaving the condenser, and liquid condensate can be calculated using the ideal gas law and the known conditions. A separating funnel might be used to separate pentane and water in the condensate since pentane is a hydrocarbon and is not soluble in water.

Step by step solution

01

Calculation of the mass flow rate of pentane

The flow rate of pentane entering the heating chamber is given as 50.4 L/min. The density of \(n\)-pentane at room temperature is about 0.626 g/mL. Use this and convert the volume flow rate to mass flow rate: \( \text{mass flow rate of pentane} = 50.4\,L/min \times 1000\,mL/L \times 0.626\,g/mL \times 1\,kg/1000\,g = 31.55\,kg/min \)
02

Calculation of the fractional conversion of pentane

In this step, calculate the fraction of the initial pentane that gets converted in the furnace. It is found by comparing the mass flow rate of pentane before and after the combustion furnace. Fractional conversion \( X \) can be calculated as \( X = \frac{{\text{Initial flow rate} - \text{Final flow rate}}}{\text{Initial flow rate}} \). Plugging the known values: \( X = \frac{{31.55\,kg/min - 3.175\,kg/min}}{31.55\,kg/min} = 0.899 = 89.9 \% \)
03

Calculation of the flow rates

First calculate the flow rate of air. Using the ideal gas law \(PV = nRT\), where \(P\) is the pressure, \(V\) is volume, \(n\) the number of moles, \(R\) the gas constant and \(T\) the temperature in Kelvin, the volume flow rate can be calculated as \( V_{air} = \frac{{nRT}}{P} \). From the combustion reaction of \(n\)-Pentane (C5H12 + 15/2 O2 -> 5CO2 + 6H2O), the molar ratio of O2 to \(n\)-Pentane is 15/2 : 1. Thus, the flow rate of the feed air is 15% more the required amount, i.e., \(n_{O2} = 1.15 \times \frac{15}{2} \times \text{flow rate of \(n\)-pentane} \). The flow rate of the gas leaving the condenser can be calculated too using the ideal gas law under the new conditions. The flow rate of the liquid condensate is equivalent to the unreacted pentane and the water formed, i.e., 3.175 kg/min + 6 moles of water per mole of \(n\)-pentane reacted \( \times (1 - X) \times \text{flow rate of \(n\)-pentane} \times \text{Molar mass of water} \).
04

Sketch of the separation apparatus

To separate pentane and water in the condensate, a separating funnel can be used given the fact that pentane is insoluble in water. The mixture of pentane and water is added to the separating funnel which is then shaken gently to ensure complete mixing. Once it's left to settle, two layers will form with pentane being the upper layer due to its lesser density. The tap of the funnel can be opened to allow water (bottom layer) to run out, discharging the liquid until there's only pentane left in the funnel. After ensuring water has completely drained out, the remaining pentane can now be collected.

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Key Concepts

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

Fractional Conversion Calculation
Understanding the fractional conversion calculation in a chemical process is essential for evaluating the efficiency of a reaction. It measures the fraction of a reactant that has been converted into a product during a chemical process. In the context of the exercise provided, the fractional conversion, denoted as \(X\), of pentane in the heating chamber is determined by the decrease in its mass flow rate after passing through the combustion furnace.

To calculate the fractional conversion of pentane, we apply the formula: \(X = \frac{{\text{Initial flow rate} - \text{Final flow rate}}}{{\text{Initial flow rate}}}\). In the given problem, the initial mass flow rate of pentane was 31.55 kg/min and the final mass flow rate after the process was 3.175 kg/min. Substituting these values gives a fractional conversion of 89.9%, indicating a significant portion of pentane was converted during the process.

The concept of fractional conversion is a cornerstone in chemical engineering as it provides insight into the progress of reactions and the efficiency of the process, guiding the optimization of operational conditions for better performance.
Volumetric Flow Rate
The volumetric flow rate is a fundamental parameter in chemical engineering, defining the volume of fluid that passes through a given point per unit time. It's often measured in liters per minute (L/min) or cubic meters per second (m^3/s). This value becomes crucial when designing systems for chemical processing, where maintaining proper flow rates is necessary to ensure desired reaction times and overall process efficiency.

In the exercise, we encounter calculations of volumetric flow rates for different stages in the process. For instance, after finding the mass flow rate, the volume flow rate of the air fed into the reaction can be deduced from the ideal gas law, demonstrating how temperature, pressure, and the stoichiometric requirements of the reaction dictate the volume required for complete combustion. Subsequent calculations based on this parameter facilitate a deeper comprehension of the gas dynamics involved in the separation process.
Mass Flow Rate
Mass flow rate is the mass of a substance passing through a given surface per unit time. It's a key concept in chemical engineering, particularly when assessing the material balance around a process. In the context of this problem, the mass flow rate is critical for determining the fractional conversion of pentane. The given mass flow rate of the pentane inlet is 31.55 kg/min, found by converting the volumetric flow rate and considering the density of the pentane.

To enhance comprehension of mass flow rate, it's important to recognize it as a measure of the 'amount' of mass being transferred, distinct from the volumetric flow, which considers only volume. Grasping both concepts allows students to seamlessly switch between different units based on the phase of the compound (liquid or gas), and to understand the processes of combustion and separation more deeply.
Separation Apparatus Design
Separation apparatus design is vital in chemical engineering for the purification and isolation of components from a mixture. The design must consider the properties of the components, such as density, solubility, and boiling points. In the problem, the separation of pentane from water is required, which is achieved using a simple yet effective device: a separating funnel.

This apparatus leverages the difference in density between pentane and water. Pentane, being a hydrocarbon, is less dense and insoluble in water, forming a distinct upper layer when mixed. By gently mixing and allowing the mixture to settle, the two liquids separate out into their respective layers. The separating funnel is then used to drain the denser water from the bottom, leaving behind the lighter pentane. This represents a practical application of separation principles — a fundamental skill in the development and operation of chemical processes.

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Most popular questions from this chapter

The van der Waals equation of state (Equation \(5.3-7\) ) is to be used to estimate the specific molar volume \(\hat{V}(\mathrm{L} / \mathrm{mol})\) of air at specified values of \(T(\mathrm{K})\) and \(P(\mathrm{atm}) .\) The van der Waals constants for air are \(a=1.33 \mathrm{atm} \cdot \mathrm{L}^{2} / \mathrm{mol}^{2}\) and \(b=0.0366 \mathrm{L} / \mathrm{mol}\) (a) Show why the van der Waals equation is classified as a cubic equation of state by expressing it in the form $$f(\hat{V})=c_{3} \hat{V}^{3}+c_{2} \hat{V}^{2}+c_{1} \hat{V}+c_{0}=0$$ where the coefficients \(c_{3}, c_{2}, c_{1},\) and \(c_{0}\) involve \(P, R, T, a,\) and \(b .\) Calculate the values of these coefficients for air at \(223 \mathrm{K}\) and 50.0 atm. (Include the units when giving the values.) (b) What would the value of \(\hat{V}\) be if the ideal-gas equation of state were used for the calculation? Use this value as an initial estimate of \(\tilde{V}\) for air at \(223 \mathrm{K}\) and 50.0 atm and solve the van der Waals equation using Goal Seek or Solver in Excel. What percentage error results from the use of the ideal-gas equation of state, taking the van der Waals estimate to be correct? (c) Set up a spreadsheet to carry out the calculations of Part (b) for air at \(223 \mathrm{K}\) and several pressures. The spreadsheet should appear as follows: The polynomial expression for \(\hat{V}\left(f=c_{3} \hat{V}^{3}+c_{2} \hat{V}^{2}+\cdots\right)\) should be entered in the \(f(V)\) column, and the value in the \(V\) column should be determined using Goal Seek or Solver in Excel.

Lewis \(^{12}\) describes the hazards of breathing air containing appreciable amounts of an asphyxiant (a gas that has no specific toxicity but, when inhaled, excludes oxygen from the lungs). When the mole percent of the asphyxiant in the air reaches \(50 \%,\) marked symptoms of distress appear, and at \(75 \%\) death occurs in a matter of minutes. A small storage room whose dimensions are \(2 \mathrm{m} \times 1.5 \mathrm{m} \times 3 \mathrm{m}\) contains a number of expensive and dangerous chemicals. To prevent unauthorized entry, the door to the room is always locked and can be opened with a key from either side. A cylinder of liquid carbon dioxide is stored in the room. The valve on the cylinder is faulty and some of the contents have escaped over the weekend. The room temperature is \(25^{\circ} \mathrm{C}\). (a) If the concentration of \(\mathrm{CO}_{2}\) reaches the lethal 75 mole \(\%\) level, what would be the mole percent of \(\mathrm{O}_{2} ?\) (b) How much \(\mathrm{CO}_{2}(\mathrm{kg})\) is present in the room when the lethal concentration is reached? Why would more than that amount have to escape from the cylinder for this concentration to be reached? (c) Describe a set of events that could result in a fatality in the given situation. Suggest at least two measures that would reduce the hazards associated with storage of this scemingly harmless substance.

A slurry contains crystals of copper sulfate pentahydrate \(\left[\mathrm{CuSO}_{4} \cdot 5 \mathrm{H}_{2} \mathrm{O}(\mathrm{s}), \text { specific gravity }=2.3\right]\) suspended in an aqueous copper sulfate solution (liquid SG \(=1.2\) ). A sensitive transducer is used to measure the pressure difference, \(\Delta P(\mathrm{Pa}),\) between two points in the sample container separated by a vertical distance of \(h\) meters. The reading is in turn used to determine the mass fraction of crystals in the slurry, \(x_{\mathrm{c}}(\mathrm{kg}\) crystals/kg slurry). (a) Derive an expression for the transducer reading, \(\Delta P(\mathrm{Pa}),\) in terms of the overall slurry density, \(\rho_{\mathrm{s}}\left(\mathrm{kg} / \mathrm{m}^{3}\right),\) assuming that the equation used to calculate the pressure head in Chapter 3 \(\left(P=P_{0}+\rho g h\right)\) is valid for this two-phase system. (b) Validate the following expression relating the overall slurry density to the liquid and solid crystal densities \(\left(\rho_{1} \text { and } \rho_{c}\right)\) and the mass fraction of crystals in the slurry: $$\frac{1}{\rho_{\mathrm{si}}}=\frac{x_{\mathrm{c}}}{\rho_{\mathrm{c}}}+\frac{\left(1-x_{\mathrm{c}}\right)}{\rho_{1}}$$ (c) Suppose \(175 \mathrm{kg}\) of the slurry is placed in the sample container with \(h=0.200 \mathrm{m}\) and a transducer reading \(\Delta P=2775\) Pa is obtained. Calculate \((\mathrm{i}) \rho_{\mathrm{s}_{\mathrm{s}},(\mathrm{ii})} x_{\mathrm{c}},\) (iii) the total slurry volume, (iv) the mass of crystals in the slurry, (v) the mass of anhydrous copper sulfate (CuSO \(_{4}\) without the water of hydration) in the crystals, (vi) the mass of liquid solution, and (vii) the volume of liquid solution. (d) Prepare a spreadsheet to generate a calibration curve of \(x_{c}\) versus \(\Delta P\) for this device. Take as inputs \(\rho_{\mathrm{c}}\left(\mathrm{kg} / \mathrm{m}^{3}\right), \rho_{1}\left(\mathrm{kg} / \mathrm{m}^{3}\right),\) and \(h(\mathrm{m}),\) and calculate \(\Delta P(\mathrm{Pa})\) for \(x_{\mathrm{c}}=0.0,0.05,0.10, \ldots, 0.60\) Run the program for the parameter values in this problem \(\left(\rho_{\mathrm{c}}=2300, \rho_{1}=1200, \text { and } h=0.200\right)\) Then plot \(x_{c}\) versus \(\Delta P\) (have the spreadsheet program do it, if possible), and verify that the value of \(x_{c}\) corresponding to \(\Delta P=2775\) Pa on the calibration curve corresponds to the value calculated in Part (c). (e) Derive the expression in Part (b). Take a basis of \(1 \mathrm{kg}\) of slurry \(\left[x_{\mathrm{c}}(\mathrm{kg}), V_{c}\left(\mathrm{m}^{3}\right)\right.\) crystals, \(\left.\left(1-x_{\mathrm{c}}\right)(\mathrm{kg}), V_{l}\left(\mathrm{m}^{3}\right) \text { liquid }\right],\) and use the fact that the volumes of the crystals and liquid are additive.

A tank in a room at \(19^{\circ} \mathrm{C}\) is initially open to the atmosphere on a day when the barometric pressure is 102 kPa. A block of dry ice (solid \(\mathrm{CO}_{2}\) ) with a mass of \(15.7 \mathrm{kg}\) is dropped into the tank, which is then sealed. The reading on the tank pressure gauge initially rises very quickly, then much more slowly, eventually reaching a value of 3.27 MPa. Assume \(T_{\text {final }}=19^{\circ} \mathrm{C}\) (a) How many moles of air were in the tank initially? Neglect the volume occupied by \(\mathrm{CO}_{2}\) in the solid state, and assume that a negligible amount of \(\mathrm{CO}_{2}\) escapes prior to the sealing of the tank. (b) Estimate the percentage error made by neglecting the volume of the block of dry ice placed in the tank. (The specific gravity of solid carbon dioxide is approximately 1.56 .) (c) What is the final density (g/L) of the gas in the tank? (d) Explain the observed variation of pressure with time. More specifically, what is happening in the tank during the initial rapid pressure increase and during the later slow pressure increase?

The oxidation of nitric oxide $$\mathrm{NO}+\frac{1}{2} \mathrm{O}_{2} \rightleftharpoons \mathrm{NO}_{2}$$ takes place in an isothermal batch reactor. The reactor is charged with a mixture containing 20.0 volume percent NO and the balance air at an initial pressure of \(380 \mathrm{kPa}\) (absolute). (a) Assuming ideal-gas behavior, determine the composition of the mixture (component mole fractions) and the final pressure (kPa) if the conversion of NO is 90\%. (b) Suppose the pressure in the reactor eventually equilibrates (levels out) at \(360 \mathrm{kPa}\). What is the equilibrium percent conversion of NO? Calculate the reaction equilibrium constant at the prevailing temperature, \(K_{p}\left[(\mathrm{atm})^{-0.5}\right]\), defined as $$K_{p}=\frac{\left(p_{\mathrm{NO}_{2}}\right)}{\left(p_{\mathrm{NO}}\right)\left(p_{\mathrm{O}_{2}}\right)^{0.5}}$$ where \(p_{i}(\mathrm{atm})\) is the partial pressure of species \(i\left(\mathrm{NO}_{2}, \mathrm{NO}, \mathrm{O}_{2}\right)\) at equilibrium. (c) Assuming that \(K_{\mathrm{p}}\) depends only on temperature, estimate the final pressure and composition in the reactor if the feed ratio of NO to \(\mathrm{O}_{2}\) and the initial pressure are the same as in \(\operatorname{Part}(\) a), but the feed to the reactor is pure \(\mathrm{O}_{2}\) instead of air. (d) Replace the partial pressures in the expression for \(K_{\mathrm{p}}\), and use the result to explain how reactor pressure influences the conversion of NO to \(\mathrm{NO}_{2}\)

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