/*! 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 23 Phosgene (COCl_) is formed by CO... [FREE SOLUTION] | 91Ó°ÊÓ

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Phosgene (COCl_) is formed by CO and Cl_ reacting in the presence of activated charcoal: $$\mathrm{CO}+\mathrm{Cl}_{2} \rightarrow \mathrm{COCl}_{2}$$ At \(T=303.8 \mathrm{K}\) the rate of formation of phosgene in the presence of 1 gram of charcoal is $$R_{\mathrm{f}}(\mathrm{mol} / \mathrm{min})=\frac{8.75 C_{\mathrm{CO}} C_{\mathrm{C}_{2}}}{\left(1+58.6 C_{\mathrm{C}_{2}}+34.3 C_{\mathrm{COC}_{2}}\right)^{2}}$$ where C denotes concentration in mollL. (a) Suppose the charge to a 3.00 -liter batch reactor is \(1.00 \mathrm{g}\) of charcoal and a gas initially containing 60.0 mole\% CO and the balance \(\mathrm{Cl}_{2}\) at \(303.8 \mathrm{K}\) and 1 atm. Calculate the initial concentrations (mol/L) of both reactants, neglecting the volume occupied by the charcoal. Then, letting \(C_{\mathrm{P}}(t)\) be the concentration of phosgene at an arbitrary time \(t,\) derive relations for \(C_{\mathrm{P}}\) \(C_{\mathrm{CO}}\) and \(C_{\mathrm{C}_{2}}\) in terms of (b) Write a differential balance on phosgene and show that it simplifies to $$\frac{d C_{\mathrm{P}}}{d t}=\frac{2.92\left(0.02407-C_{\mathrm{P}}\right)\left(0.01605-C_{\mathrm{P}}\right)}{\left(1.941-24.3 C_{\mathrm{P}}\right)^{2}}$$ Provide an initial condition for this equation. (c) A plot of \(C_{\mathrm{P}}\) versus \(t\) starts at \(C_{\mathrm{P}}=0\) and asymptotically approaches a maximum value. Explain how you could predict that behavior from the form of the equation of Part (b). Without attempting to solve the differential equation, determine the maximum value of \(C_{\mathrm{P}}\) (d) Starting with the equation of Part (b), derive an expression for the time required to achieve a \(75 \%\) conversion of the limiting reactant. Your solution should have the form \(t=a\) definite integral. (e) The integral you derived in Part (d) can be evaluated analytically; however, more complex rate laws than the one given for the phosgene formation reaction would yield an integral that must be evaluated numerically. One procedure is to evaluate the integrand at a number of points between the limits of integration and to use a quadrature formula such as the trapezoidal rule or Simpson's rule (Appendix A.3) to estimate the value of the integral. Usea spreadsheet to evaluate the integrand of the integral of Part (c) at \(n_{p}\) equally spaced points between and including the limits of integration, where \(n_{p}\) is an odd number, and then to evaluate the integral using Simpson's rule. Perform the calculation for \(n_{p}=5,21,\) and \(51 .\) What can you conclude about the number of points needed to obtain a result accurate to three significant figures?

Short Answer

Expert verified
Answer to this exercise demands an understanding of chemical kinetics, material balance and numerical evaluation methods. This involves computing initial reactant concentrations, deriving relationships of reactant concentrations, setting up and interpreting differential equations influencing rate of formation to understand product formation over time, and determining requisite number of points for accurate numerical estimation.

Step by step solution

01

Calculation of initial concentrations

The initial concentration of CO, denoted as \(C_{\mathrm{COo}}\) and Cl2, denoted as \(C_{\mathrm{Cl_2o}}\), can be calculated using the ideal gas law \(PV = nRT\) where P is the pressure (1atm), V is the volume (3.00L), n is the number of moles of the gas, R is the gas constant (0.08206 L.atm/mol.K), and T is the temperature (303.8K). Given that the gas mixture contains 60 mol% of CO, the initial concentrations can be calculated as follows: \(C_{\mathrm{COo}} = \frac{(60/100)PV}{RT}\), \(C_{\mathrm{Cl_2o}} = \frac{(40/100)PV}{RT}\)
02

Derive relations for \(C_{\mathrm{P}}\), \(C_{\mathrm{CO}}\) and \(C_{\mathrm{Cl_2}}\)

Start by representing the consumption and formation rates of reactants and products. As per stoichiometry of the reaction: \(-r_{\mathrm{CO}} = -r_{\mathrm{Cl_2}} = r_{\mathrm{COCl2}}\). Then, the change in concentration with time is presented as: \(C_{\mathrm{P}}(t) = C_{\mathrm{COCl_2}} = C_{\mathrm{COo}} - C_{\mathrm{CO}} = C_{\mathrm{Cl_2o}} - C_{\mathrm{Cl_2}}\)
03

Write a differential balance on phosgene

Substitute the derived expression from step 2 into the given rate equation to get \(R_{\mathrm{f}}\). As \(R_{\mathrm{f}} = r_{\mathrm{COCl_2}}\), the rate of formation of phosgene, \(R_{\mathrm{f}}\), can be related to the rate of change of phosgene concentration, \(dC_{\mathrm{P}}/dt\) over time. The initial condition would be that at \(t = 0\), \(C_{\mathrm{P}} = 0\)
04

Understand nature of phosgene concentration with time

As per the differential rate equation in step 3, as time increases, \(C_{\mathrm{P}}(t)\) increases, and the denominator of the rate of change of phosgene decreases. Therefore, \(dC_{\mathrm{P}}/dt\) decreases, which means the rate of formation of phosgene decreases with time. So even though \(C_{\mathrm{P}}\) keeps increasing as time goes on, it does so at an increasingly slower rate, leading to the asymptotic behavior. The maximum value of \(C_{\mathrm{P}}\) can be obtained by solving the equation obtained in the denominator with \(dC_{\mathrm{P}}/dt = 0\)
05

Derive expression for conversion time

75% conversion of limiting reactant implies that 75% of the initial concentration of the limiting reactant has been consumed and is present in the product. Setting up an equation with initial and final concentrations and integrating, an equation in the form of \(t = a \int{}{}\) can be attained.
06

Evaluate integral numerically

To calculate the conversion time evaluated previously, one must evaluate the integral. However, this may not be feasible analytically where certain complex rate equations are concerned. In such cases, numerical methods such as Simpson's rule or Trapezoidal rule can be applied. Using Simpson's rule, the integral is evaluated at a number of equally spaced intervals. Through comparison of results obtained with different number of points, the necessary number of points needed to achieve a specific level of accuracy can be determined.

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Key Concepts

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

Phosgene Formation
Phosgene is a toxic and corrosive gas, often formed industrially through the reaction of carbon monoxide (CO) and chlorine gas (\(Cl_2\)). The reaction typically occurs in the presence of a catalyst such as activated charcoal, which can enhance the rate of reaction by providing a large surface area for the gases to react. The chemical equation for this reaction is:\[\mathrm{CO} + \mathrm{Cl}_2 \rightarrow \mathrm{COCl}_2\]This simple mole-to-mole reaction means one mole of carbon monoxide reacts with one mole of chlorine to produce one mole of phosgene.Understanding the conditions needed for the reaction is important:
  • Temperature: The reaction is often conducted at moderately elevated temperatures to increase reaction rates.
  • Pressure: Pressure influences concentration and thus affects reaction kinetics, with higher pressures usually increasing the rate.
  • Catalysts: Substances like charcoal help speed up the reaction without being consumed.
Awareness of these parameters is crucial since phosgene is hazardous, requiring careful control and monitoring during synthesis.
Differential Rate Equations
Differential rate equations describe how the concentration of a reactant or product changes over time during a chemical reaction. In the context of phosgene formation, such an equation helps us understand the kinetics of the reaction. Considering the rate of formation of phosgene, the differential rate equation is given by:\[\frac{dC_{\mathrm{P}}}{dt} = \frac{8.75 C_{\mathrm{CO}} C_{\mathrm{Cl_2}}}{(1 + 58.6 C_{\mathrm{Cl_2}} + 34.3 C_{\mathrm{CO}})^2}\]This equation can be simplified and rearranged to provide insights into various kinetic parameters:
  • The numerator reflects the reaction's dependency on the initial concentrations of CO and \(Cl_2\).
  • The denominator shows how the reaction rate decreases as concentrations of reactants increase, due to saturation effects in the catalyst surface.
Integrating this differential equation can predict the concentration profiles of reactants and products over time, but this often requires numerical methods due to the complexity of real-world situations.
Ideal Gas Law Calculations
The Ideal Gas Law is a fundamental principle in chemistry that relates the pressure, volume, temperature, and the number of moles of a gas. The formula is:\[PV = nRT\]where
  • \(P\) is the pressure of the gas, typically in atmospheres (atm),
  • \(V\) represents the volume of the gas in liters (L),
  • \(n\) is the number of moles of the gas,
  • \(R\) is the gas constant (0.08206 \(L \, atm / mol \, K\)), and
  • \(T\) is the temperature in Kelvin (K).
In the context of the exercise, the initial concentrations of CO and \(Cl_2\) are calculated by assuming the gases behave ideally. By knowing the percentage composition and the initial conditions, we can set up formulas for initial concentration:\[C_{\mathrm{COo}} = \frac{(60/100)PV}{RT}, \quad C_{\mathrm{Cl_2o}} = \frac{(40/100)PV}{RT}\]These equations allow us to determine the starting point of the reaction in terms of concentration, which is essential for analyzing the kinetics and the progression of the reaction over time.

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Most popular questions from this chapter

A 7.35 million gallon tank used for storing liquefied natural gas (LNG, which may be taken to be pure methane) must be taken out of service and inspected. All the liquid that can be pumped from the tank is first removed, and the tank is allowed to warm from its service temperature of about \(-260^{\circ} \mathrm{F}\) to \(80^{\circ} \mathrm{F}\) at 1 atm. The gas remaining in the tank is then purged in two steps: (1) Liquid nitrogen is sprayed gently onto the tank floor, where it vaporizes. As the cold nitrogen vapor is formed, it displaces the methane in a piston-like flow until the tank is completely filled with nitrogen. Once all the methane has been displaced, the nitrogen is allowed to warm to ambient temperature. (2) Air is blown into the tank where it rapidly and completely mixes with the nitrogen until the composition of the gas leaving the tank is very close to that of air. (a) Use the ideal-gas equation of state to estimate the densities of methane at \(80^{\circ} \mathrm{F}\) and 1 atm and of nitrogen at \(-260^{\circ} \mathrm{F}\) and 1 atm. How confident are you about the accuracy of each estimate? Explain. (b) If the density of liquid nitrogen is \(50 \mathrm{lb}_{\mathrm{m}} / \mathrm{ft}^{3}\), how many gallons will be required to displace all the methane from the tank? (c) How many cubic feet of air will be required to increase the oxygen concentration to \(20 \%\) by volume? (d) Explain the logic behind vaporizing nitrogen in the manner described. Why purge with nitrogen first as opposed to purging with air?

A stirred tank contains \(1500 \mathrm{lb}_{\mathrm{m}}\) of pure water at \(70^{\circ} \mathrm{F}\). At time \(t=0,\) two streams begin to flow into the tank and one is withdrawn. One input stream is a \(20.0 \mathrm{wt} \%\) aqueous solution of \(\mathrm{NaCl}\) at \(85^{\circ} \mathrm{F}\) flowing at a rate of \(15 \mathrm{lb}_{\mathrm{m}} / \mathrm{min},\) and the other is pure water at \(70^{\circ} \mathrm{F}\) flowing at \(10 \mathrm{lb}_{\mathrm{m}} / \mathrm{min} .\) The mass of liquid in the tank is held constant at \(1500 \mathrm{lb}_{\mathrm{m}}\). Perfect mixing in the tank may be assumed, so that the outlet stream has the same \(\mathrm{NaCl}\) mass fraction \((x)\) and temperature \((T)\) as the tank contents. Also assume that the heat of mixing is zero and the heat capacity of all fluids is \(C_{p}=1 \mathrm{Btu} /\left(\mathrm{lb}_{\mathrm{m}} \cdot^{\circ} \mathrm{F}\right)\) (a) Write differential material and energy balances and use them to derive expressions for \(d x / d t\) and \(d T / d t\) (b) Without solving the equations derived in Part (a), sketch plots of \(T\) and \(x\) as a function of time \((t)\) Clearly identify values at time zero and as \(t \rightarrow \infty\)

A gas that contains \(\mathrm{CO}_{2}\) is contacted with liquid water in an agitated batch absorber. The equilibrium solubility of \(\mathrm{CO}_{2}\) in water is given by Henry's law (Section \(6.4 \mathrm{b}\) ) $$C_{\mathrm{A}}=p_{\mathrm{A}} / H_{\mathrm{A}}$$ where \(C_{\mathrm{A}}\left(\mathrm{mol} / \mathrm{cm}^{3}\right)=\) concentration of \(\mathrm{CO}_{2}\) in solution, \(p_{\mathrm{A}}(\mathrm{atm})=\) partial pressure of \(\mathrm{CO}_{2}\) in the gas phase, and \(H_{\mathrm{A}}\left[\mathrm{atm} /\left(\mathrm{mol} / \mathrm{cm}^{3}\right)\right]=\) Henry's law constant. The rate of absorption of \(\mathrm{CO}_{2}\) (i.e., the rate of transfer of \(\mathrm{CO}_{2}\) from the gas to the liquid per unit area of gas-liquid interface) is given by the expression $$r_{\mathrm{A}}\left[\operatorname{mol} /\left(\mathrm{cm}^{2} \cdot \mathrm{s}\right)\right]=k\left(C_{\mathrm{A}}^{*}-C_{\mathrm{A}}\right)$$ where \(C_{A}=\) actual concentration of \(\mathrm{CO}_{2}\) in the liquid, \(C_{\mathrm{A}}^{*}=\) concentration of \(\mathrm{CO}_{2}\) in the liquid that would be in equilibrium with the \(\mathrm{CO}_{2}\) in the gas phase, and \(k(\mathrm{cm} / \mathrm{s})=\) a mass transfer coefficient. The gas phase is at a total pressure \(\mathrm{P}\left(\text { atm) and contains } y_{\mathrm{A}}\left(\mathrm{mol} \mathrm{CO}_{2} / \mathrm{mol}\text { gas), and the liquid }\right.\right.\) phase initially consists of \(V\left(\mathrm{cm}^{3}\right)\) of pure water. The agitation of the liquid phase is sufficient for the composition to be considered spatially uniform, and the amount of \(\mathrm{CO}_{2}\) absorbed is low enough for \(P, V,\) and \(y_{\mathrm{A}}\) to be considered constant throughout the process. (a) Derive an expression for \(d C_{\mathrm{A}} / d t\) and provide an initial condition. Without doing any calculations, sketch a plot of \(C_{\mathrm{A}}\) versus \(t,\) labeling the value of \(C_{\mathrm{A}}\) at \(t=0\) and the asymptotic value at \(t \rightarrow \infty\) Give a physical explanation for the asymptotic value of the concentration. (b) Prove that $$C_{\mathrm{A}}(t)=\frac{p_{\mathrm{A}}}{H_{\mathrm{A}}}[1-\exp (-k S t / V)]$$ where \(S\left(\mathrm{cm}^{2}\right)\) is the effective contact area between the gas and liquid phases. (c) Suppose the system pressure is 20.0 atm, the liquid volume is 5.00 liters, the tank diameter is \(10.0 \mathrm{cm},\) the gas contains 30.0 mole \(\% \mathrm{CO}_{2},\) the Henry's law constant is \(9230 \mathrm{atm} / \mathrm{mole} / \mathrm{cm}^{3}\) ), and the mass transfer coefficient is \(0.020 \mathrm{cm} / \mathrm{s}\). Calculate the time required for \(C_{\mathrm{A}}\) to reach \(0.620 \mathrm{mol} / \mathrm{L}\) if the gas-phase properties remain essentially constant. (d) If A were not \(\mathrm{CO}_{2}\) but instead a gas with a moderately high solubility in water, the expression for \(C_{\mathrm{A}}\) given in Part (b) would be incorrect. Explain where the derivation that led to it would break down.

The demand for biopharmaceutical products in the form of complex proteins is growing. These proteins are most often produced by cells genetically engineered to produce the protein of interest, known as a recombinant protein. The cells are grown in a liquid culture, and the protein is harvested and purified to generate the final product. Sf9 cells obtained from the fall armyworm can be used to produce protein therapeutics. Consider the growth of Sf9 cells in a bench-top bioreactor operating at \(22^{\circ} \mathrm{C}\), with a liquid volume of 4.0 liters that may be assumed constant. Oxygen required for cell growth and protein production is supplied in air fed at \(22^{\circ} \mathrm{C}\) and 1.1 atm. During the process, the gas leaving the bioreactor at \(22^{\circ} \mathrm{C}\) and 1 atm is analyzed continuously. The data can be used to calculate the rate at which oxygen is taken up in the culture, which in turn can be used to determine the Sf9 cell growth rate (a quantity difficult to measure directly) and consistency of the operation from batch to batch. (a) Analysis of the exhaust gas at a time 25 hours after the process is started shows a composition of \(15.5 \mathrm{mol} \% \mathrm{O}_{2}, 78.7 \% \mathrm{N}_{2},\) and the balance \(\mathrm{CO}_{2}\) and small amounts of other gases. Determine the value of the oxygen use rate (OUR) in mmol \(\mathrm{O}_{2}\) consumed \((\mathrm{L} \cdot \mathrm{h})\) at that point in time. Assume that nitrogen is not absorbed by the culture. (b) OUR is related to cell concentration, \(X(\mathrm{g} \text { cells } / \mathrm{L}),\) by \(\mathrm{OUR}=q_{0_{2}} X,\) where \(q_{0_{2}}\) is the specific rate of oxygen consumption. Analysis of a sample of the culture taken at \(t=25 \mathrm{h}\) finds that the concentration of cells is \(5.0 \mathrm{g}\) cells/L. What is the value of \(q_{\mathrm{O}_{2}} ?\) (Do not forget to include its units.) (c) Six hours after this measurement, the exhaust gas contains 14.5 mol\% \(\mathrm{O}_{2}\) and the percentage of \(\mathrm{N}_{2}\) is unchanged. What is the concentration of cells, \(X,\) at that point? Assume that the specific rate of oxygen consumption does not change as long as the process temperature is constant. (d) The growth rate of cells can be expressed as: $$\frac{d X}{d t}=\mu_{\mathrm{g}} X$$ where \(\mu_{g}\) is the specific growth rate, with units of \(\mathrm{h}^{-1}\). Beginning with this equation and treating \(\mu_{\mathrm{g}}\) as a constant, derive an expression for \(t(X) .\) Use the data from the previous parts of the problem to determine \(\mu_{\mathrm{g}}\) (include units). Then calculate the cell-doubling time \(\left(t_{\mathrm{d}}\right),\) defined as the time for the cell concentration to double.

One hundred fifty kmol of an aqueous phosphoric acid solution contains 5.00 mole\% \(\mathrm{H}_{3} \mathrm{PO}_{4}\). The solution is concentrated by adding pure phosphoric acid at a rate of \(20.0 \mathrm{L} / \mathrm{min}\). (a) Write a differential mole balance on phosphoric acid and provide an initial condition. [Start by defining \(n_{\mathrm{p}}(\mathrm{kmol})\) to be the total quantity of phosphoric acid in the tank at any time.] Without solving the equation, sketch a plot of \(n_{\mathrm{p}}\) versus \(t\) and explain your reasoning. (b) Solve the balance to obtain an expression for \(n_{\mathrm{p}}(t) .\) Use the result to derive an expression for \(x_{\mathrm{p}}(t)\) the mole fraction of phosphoric acid in the solution. Without doing any numerical calculations, sketch a plot of \(x_{\mathrm{p}}\) versus \(t\) from \(t=0\) to \(t \rightarrow \infty,\) labeling the initial and asymptotic values of \(x_{\mathrm{p}}\) on the plot. Explain your reasoning. (c) How long will it take to concentrate the solution to \(15 \% \mathrm{H}_{3} \mathrm{PO}_{4} ?\)

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