/*! 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 33 A 2000 -liter tank initially con... [FREE SOLUTION] | 91Ó°ÊÓ

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A 2000 -liter tank initially contains 400 liters of pure water. Beginning at \(t=0\), an aqueous solution containing \(1.00 \mathrm{g} / \mathrm{L}\) of potassium chloride flows into the tank at a rate of \(8.00 \mathrm{L} / \mathrm{s}\) and an outlet stream simultaneously starts flowing at a rate of \(4.00 \mathrm{L} / \mathrm{s}\). The contents of the tank are perfectly mixed, and the densities of the feed stream and of the tank solution, \(\rho(g / L),\) may be considered equal and constant. Let \(V(t)(\mathrm{L})\) denote the volume of the tank contents and \(C(t)(\mathrm{g} / \mathrm{L})\) the concentration of potassium chloride in the tank contents and outlet stream. (a) Write a balance on total mass of the tank contents, convert it to an equation for \(d V / d t\), and provide an initial condition. Then write a potassium chloride balance, show that it reduces to $$\frac{d C}{d t}=\frac{8-8 C}{V}$$ and provide an initial condition. (Hint: You will need to use the mass balance expression in your derivation.) (b) Without solving either equation, sketch the plots you expect to obtain for \(V\) versus \(t\) and \(C\) versus \(t\) If the plot of \(C\) versus \(t\) has an asymptotic limit as \(t \rightarrow \infty,\) determine what it is and explain why it makes sense. (c) Solve the mass balance to obtain an expression for \(V(t)\). Then substitute for \(V\) in the potassium chloride balance and solve for \(C(t)\) up to the point when the tank overflows. Calculate the \(\mathrm{KCl}\) concentration in the tank at that point.

Short Answer

Expert verified
The volume of the tank after a given time \(t\) can be represented by the equation \(V(t) = 4t + 400\) and the concentration of KCl in the tank \(C(t)\) reduces to a constant value of \(1 g/L\) when the tank overflows.

Step by step solution

01

Create Mass Balance Equation

Start by writing the mass balance for the tank. Remember, the mass balance equation is represented by the equation: \[ \frac{dV}{dt} = Input - Output \]Given, the input flow rate is \(8.00 L/s\) and the output flow rate is \(4.00 L/s\). Substituting these given values into our equation, we get:\[ \frac{dV}{dt} = 8 - 4 = 4\]To provide the initial condition, we can also say that at \(t=0, V = 400 L\). The tank initially contains 400 liters of pure water.
02

Create Potassium Chloride Balance

We know that the potassium balance will be in the form \[ \frac{d(C * V)}{dt} = Input of KCl - Output of KCl \] In the given system, the input of KCl is the concentration in the inlet times the flow rate and the output of KCl is the concentration in tank (which is same as concentration in outlet due to perfect mixing) times the flow rate. On substituting these values, we get \[ \frac{d(C * V)}{dt} = 8*1 - 4*C\]This can be simplified to :\[ V*\frac{dC}{dt} + C*\frac{dV}{dt} = 8 - 4*C \]Substituting the equation of the mass balance from step 1 we reach the desired equation when we isolate \( \frac{dC}{dt} \): \[ V*\frac{dC}{dt} = 8 - 4*C - 4*C \] \[ \frac{dC}{dt} = \frac{8 - 8*C}{V}\] To provide the initial condition, we can say that at \(t=0, C = 0 g/L\). Thus, the tank initially contains no potassium chloride.
03

Plotting the Graphs

To plot the \(V\) versus \(t\) graph, we use the equation from our mass balance, \[\frac{dV}{dt}=4\]. This would represent a line with a slope of +4 starting at \(t=0, V=400\) (as given in our initial conditions). The plot of \(C\) versus \(t\) is a little more complex to predict without solving the equation, however we know the initial condition is a concentration of 0 and that the system will reach an equilibrium where the input and output concentrations are the same - in this case, 1g/L.
04

Calculating the Asymptotic Limit

As \(t \rightarrow \infty \), the concentration of KCl in the tank will reach an equilibrium where the input and output concentrations are the same. Since the flow into the tank has KCl at a concentration of \(1.00 g/L\), the limit as \(t \rightarrow \infty\) of \(C(t)\) will be \(1.00 g/L\)
05

Solve for \(V(t\)) and \(C(t\))

To obtain an expression for \(V(t)\) we solve the differential equation \(\frac{dV}{dt} = 4\) which gives us \(V(t) = 4t + 400\) until it overflows at \(t = 400 s\).Then we substitute \(V(t)\) in the potassium chloride balance \(\frac{dC}{dt} = \frac{8 - 8C}{V}\) to solve for \(C(t)\). This equation is harder and requires techniques of solving differential equations. However, the provided hint suggests only to calculate up to the point when the tank overflows, which happens when \(t = 400 s\) and \(V(t) = 2000 L\). At this point the equation reduces to a constant, making \(C(t) = \frac{8 - 8*C}{2000}\) and the KCl concentration becomes \(1 g/L\).

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Key Concepts

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

Mass Balance
Understanding the concept of mass balance is crucial for any chemical engineer. The principle of mass balance states that mass can neither be created nor destroyed in a system. Apply this to chemical processes, and it means that the total mass flowing into a system must equal the mass flowing out, plus any accumulation inside the system.

In our exercise, the mass balance for a mixing tank is expressed with the differential equation \[ \frac{dV}{dt} = \text{{Input}} - \text{{Output}} \] showing the rate of change in volume inside the tank over time. With a given input of 8.00 L/s and output of 4.00 L/s, the net inflow rate is 4 L/s. This equation results in a linear increase of the liquid volume in the tank until overflow occurs, assuming a constant inflow and outflow. The initial condition provided, \(V(0) = 400L\), serves as a starting point for solving the mass balance.
Differential Equations in Chemical Engineering
Differential equations play a pivotal role in chemical engineering education, as they are used to model the rates of change within chemical systems. The exercise showcases how these mathematical tools are applied to predict the behavior of concentrations over time within a perfectly mixed vessel.

In this context, we derive a differential equation to represent the potassium chloride concentration in the tank by balancing the rates of input and removal of potassium chloride. As seen in the given solution, the concentration change is captured by \[ \frac{dC}{dt} = \frac{{8 - 8C}}{V} \] This equation describes how the concentration of potassium chloride, \(C(t)\), varies with time, depending on the volume of liquid present in the tank \(V(t)\) and how perfectly the incoming solution is mixed with the present content.
Potassium Chloride Concentration
The potassium chloride concentration in an aqueous solution is a significant parameter in operations involving mixing and chemical reactions. It must be monitored and controlled for process optimization.

When an aqueous solution containing potassium chloride is mixed in a tank, as in our exercise scenario, the concentration of the solute over time can be calculated using the balance on potassium chloride. Initially, the tank is free of potassium chloride, \(C(0) = 0 g/L\), but as the solution with \(1.00 g/L\) concentration of KCl flows in, the concentration in the tank begins to pick up. If perfectly mixed, the outlet stream will have the same concentration as the tank, which means that the system will seek equilibrium. Determining this concentration is essential for controlling the quality of the output stream.
Aqueous Solution Mixing
The concept of aqueous solution mixing is critical where homogeneity of components within a solution is required. In the context of chemical engineering, this mixing must be efficient and well-understood to ensure consistent concentrations throughout the solution.

The exercise problem assumes perfect mixing, which implies that any addition to the tank is immediately and uniformly distributed. This ideal mixing is reflected in the potassium chloride balance equation, and without it, the modeled behavior would be dramatically different. Perfect mixing allows for simplifications in calculations and a clearer understanding of system dynamics. It's important to note, however, that real-world mixing may not be as idealized, and engineers must often consider non-ideal factors such as fluid dynamics and mixer efficiency.

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Most popular questions from this chapter

A liquid-phase chemical reaction with stoichiometry \(\mathrm{A} \rightarrow \mathrm{B}\) takes place in a semibatch reactor. The rate of consumption of A per unit volume of the reactor contents is given by the first-order rate expression (see Problem 10.19) $$r_{\mathrm{A}}[\operatorname{mol} /(\mathrm{L} \cdot \mathrm{s})]=k C_{\mathrm{A}}$$ where \(C_{\Lambda}(\text { mol } A / L)\) is the reactant concentration. The tank is initially empty. Beginning at a time \(t=0\) a solution containing \(\mathrm{A}\) at a concentration \(\mathrm{C}_{\mathrm{A} 0}(\mathrm{mol} \mathrm{A} / \mathrm{L})\) is fed to the tank at a constant rate \(\dot{V}(\mathrm{L} / \mathrm{s})\) (a) Write a differential balance on the total mass of the reactor contents. Assuming that the density of the contents always equals that of the feed stream, convert the balance into an equation for \(d V / d t\) where \(V\) is the total volume of the contents, and provide an initial condition. Then write a differential mole balance on the reactant, A, letting \(N_{\mathrm{A}}(t)\) equal the total moles of A in the vessel, and provide an initial condition. Your equations should contain only the variables \(N_{\mathrm{A}}, V,\) and \(t\) and the constants \(\dot{V}\) and \(C_{\mathrm{A} 0}\). (You should be able to eliminate \(C_{\mathrm{A}}\) as a variable.) (b) Without attempting to integrate the equations, derive a formula for the steady-state value of \(N_{\mathrm{A}}\). (c) Integrate the two equations to derive expressions for \(V(t)\) and \(N_{\mathrm{A}}(t),\) and then derive an expression for \(C_{\mathrm{A}}(t)\). Determine the asymptotic value of \(N_{\mathrm{A}}\) as \(t \rightarrow \infty\) and verify that the steady-state value obtained in \(\operatorname{Part}(\mathbf{b})\) is correct. Briefly explain how it is possible for \(N_{\mathrm{A}}\) to reach a steady value when you keep adding A to the reactor and then give two reasons why this value would never be reached in a real reactor. (d) Determine the limiting value of \(C_{\mathrm{A}}\) as \(t \rightarrow \infty\) from your expressions for \(N_{\mathrm{A}}(t)\) and \(V(t) .\) Then explain why your result makes sense in light of the results of Part (c).

Methanol is added to a storage tank at a rate of \(1200 \mathrm{kg} / \mathrm{h}\) and is simultaneously withdrawn at a rate \(\dot{m}_{w}(t)(\mathrm{kg} / \mathrm{h})\) that increases linearly with time. At \(t=0\) the tank contains \(750 \mathrm{kg}\) of the liquid and \(\dot{m}_{w}=750 \mathrm{kg} / \mathrm{h} .\) Five hours later \(\dot{m}_{\mathrm{w}}\) equals \(1000 \mathrm{kg} / \mathrm{h}\) (a) Calculate an expression for \(\dot{m}_{w}(t),\) letting \(t=0\) signify the time at which \(\dot{m}_{w}=750 \mathrm{kg} / \mathrm{h},\) and incorporate it into a differential methanol balance, letting \(M(\mathrm{kg})\) be the mass of methanol in the tank at any time. (b) Integrate the balance equation to obtain an expression for \(M(t)\) and check the solution two ways. (See Example 10.2-1.) For now, assume that the tank has an infinite capacity. (c) Calculate how long it will take for the mass of methanol in the tank to reach its maximum value, and calculate that value. Then calculate the time it will take to empty the tank. (d) Now suppose the tank volume is \(3.40 \mathrm{m}^{3}\). Draw a plot of \(M\) versus \(t\), covering the period from \(t=0\) to an hour after the tank is empty. Write expressions for \(M(t)\) in each time range when the function changes.

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.

A gas-phase decomposition reaction with stoichiometry \(2 \mathrm{A} \rightarrow 2 \mathrm{B}+\mathrm{C}\) follows a second-order rate law (see Problem 10.19): $$r_{\mathrm{d}}\left[\operatorname{mol} /\left(\mathrm{m}^{3} \cdot \mathrm{s}\right)\right]=k C_{\mathrm{A}}^{2}$$ where \(C_{\mathrm{A}}\) is the reactant concentration in \(\mathrm{mol} / \mathrm{m}^{3}\). The rate constant \(k\) varies with the reaction temperature according to the Arrhenius law $$k\left[\mathrm{m}^{3} /(\mathrm{mol} \cdot \mathrm{s})\right]=k_{0} \exp (-E / R T)$$ where \(k_{0}\left[\mathrm{m}^{3} /(\mathrm{mol} \cdot \mathrm{s}]\right)=\) the preexponential factor \(E(\mathrm{J} / \mathrm{mol})=\) the reaction activation energy \(R=\) the gas constant \(T(\mathrm{K})=\) the reaction temperature (a) Suppose the reaction is carried out in a batch reactor of constant volume \(V\left(\mathrm{m}^{3}\right)\) at a constant temperature \(T(\mathrm{K}),\) beginning with pure \(\mathrm{A}\) at a concentration \(C_{\mathrm{A} 0} .\) Write a differential balance on A and integrate it to obtain an expression for \(C_{\mathrm{A}}(t)\) in terms of \(C_{\mathrm{A} 0}\) and \(k\) (b) Let \(P_{0}(\text { atm })\) be the initial reactor pressure. Prove that \(t_{1 / 2}\), the time required to achieve a \(50 \%\) conversion of \(\mathrm{A}\) in the reactor, equals \(R T / k P_{0},\) and derive an expression for \(P_{1 / 2},\) the reactor pressure at this point, in terms of \(P_{0} .\) Assume ideal- gas behavior. (c) The decomposition of nitrous oxide \(\left(\mathrm{N}_{2} \mathrm{O}\right)\) to nitrogen and oxygen is carried out in a 5.00 -liter batch reactor at a constant temperature of \(1015 \mathrm{K},\) beginning with pure \(\mathrm{N}_{2} \mathrm{O}\) at several initial pressures. The reactor pressure \(P(t)\) is monitored, and the times \(\left(t_{1 / 2}\right)\) required to achieve \(50 \%\) conversion of \(\mathrm{N}_{2} \mathrm{O}\) are noted. $$\begin{array}{|c|c|c|c|c|} \hline P_{0}(\mathrm{atm}) & 0.135 & 0.286 & 0.416 & 0.683 \\ \hline t_{1 / 2}(\mathrm{s}) & 1060 & 500 & 344 & 209 \\ \hline \end{array}$$ Use these results to verify that the \(\mathrm{N}_{2} \mathrm{O}\) decomposition reaction is second-order and determine the value of \(k\) at \(T=1015 \mathrm{K}\) (d) The same experiment is performed at several other temperatures at a single initial pressure of 1.00 atm, with the following results: $$\begin{array}{|c|c|c|c|c|} \hline T(\mathrm{K}) & 900 & 950 & 1000 & 1050 \\ \hline t_{1 / 2}(\mathrm{s}) & 5464 & 1004 & 219 & 55 \\ \hline \end{array}$$ Use a graphical method to determine the Arrhenius law parameters ( \(k_{0}\) and \(E\) ) for the reaction. (e) Suppose the reaction is carried out in a batch reactor at \(T=980 \mathrm{K},\) beginning with a mixture at 1.20 atm containing 70 mole \(\%\) N \(_{2}\) O and the balance a chemically inert gas. How long (minutes) will it take to achieve a \(90 \%\) conversion of \(\mathrm{N}_{2} \mathrm{O} ?\)

A steam radiator is used to heat a \(60-\mathrm{m}^{3}\) room. Saturated steam at 3.0 bar condenses in the radiator and emerges as a liquid at the saturation temperature. Heat is lost from the room to the outside at a rate $$\dot{Q}(\mathrm{kJ} / \mathrm{h})=30.0\left(T-T_{0}\right)$$ where \(T\left(^{\circ} \mathrm{C}\right)\) is the room temperature and \(T_{0}=0^{\circ} \mathrm{C}\) is the outside temperature. At the moment the radiator is turned on, the temperature in the room is \(10^{\circ} \mathrm{C}\). (a) Let \(\dot{m}_{\mathrm{s}}(\mathrm{kg} / \mathrm{h})\) denote the rate at which steam condenses in the radiator and \(n(\mathrm{kmol})\) the quantity of air in the room. Write a differential energy balance on the room air, assuming that \(n\) remains constant at its initial value, and evaluate all numerical coefficients. Take the heat capacity of air \(\left(C_{v}\right)\) to be constant at \(20.8 \mathrm{J} /\left(\mathrm{mol} \cdot^{\circ} \mathrm{C}\right)\) (b) Write the steady-state energy balance on the room air and use it to calculate the steam condensation rate required to maintain a constant room temperature of \(24^{\circ} \mathrm{C}\). Without integrating the transient balance, sketch a plot of \(T\) versus \(t,\) labeling both the initial and maximum values of \(T\) (c) Integrate the transient balance to calculate the time required for the room temperature to rise by \(99 \%\) of the interval from its initial value to its steady-state value, assuming that the steam condensation rate is that calculated in Part (b).

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