/*! 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 22 In an enzyme-catalyzed reaction ... [FREE SOLUTION] | 91Ó°ÊÓ

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In an enzyme-catalyzed reaction with stoichiometry \(\mathrm{A} \rightarrow \mathrm{B}, \mathrm{A}\) is consumed at a rate given by an expression of the Michaelis-Menten form: $$r_{\mathrm{A}}[\operatorname{mol} /(\mathrm{L} \cdot \mathrm{s})]=\frac{k_{1} C_{\mathrm{A}}}{1+k_{2} C_{\mathrm{A}}}$$ where \(C_{\mathrm{A}}(\operatorname{mol} / \mathrm{L})\) is the reactant concentration, and \(k_{1}\) and \(k_{2}\) depend only on temperature. (a) The reaction is carried out in an isothermal batch reactor with constant reaction mixture volume \(V\) (liters), beginning with pure \(A\) at a concentration \(C_{\mathrm{A} 0}\). Derive an expression for \(d C_{\mathrm{A}} / d t\), and provide an initial condition. Sketch a plot of \(C_{\mathrm{A}}\) versus \(t,\) labeling the value of \(C_{\mathrm{A}}\) at \(t=0\) and the asymptotic value as \(t \rightarrow \infty\) (b) Solve the differential equation of Part (a) to obtain an expression for the time required to achieve a specified concentration \(C_{\mathrm{A}}\) (c) Use the expression of Part (b) to devise a graphical method of determining \(k_{1}\) and \(k_{2}\) from data for In versus the pour plot should involve fitting a straight line and determining the two parameters \(C_{\mathrm{A}}\) (int the parting of the partating and and the conting are a contation a conting from the slope and intercept of the line. (There are several possible solutions.) Then apply your method to determine \(k_{1}\) and \(k_{2}\) for the following data taken in a 2.00 -liter reactor, beginning with A at a concentration \(C_{\mathrm{A} 0}=5.00 \mathrm{mol} / \mathrm{L}\) $$\begin{array}{|l|l|l|l|l|l|} \hline t(\mathrm{s}) & 60.0 & 120.0 & 180.0 & 240.0 & 480.0 \\ \hline C_{\mathrm{A}}(\mathrm{mol} / \mathrm{L}) & 4.484 & 4.005 & 3.561 & 3.154 & 1.866 \\ \hline \end{array}$$

Short Answer

Expert verified
The differential equation representing change in concentration of reactant A over time is \( \frac{dC_A}{dt} = - \frac{k_1 C_A}{1+k_2 C_A} \) with initial condition of \( C_A = C_{A0} \) at \( t = 0 \). The graphical method allows approximation of rate constants \( k_1 \) and \( k_2 \) from a plot of \( ln(C_A) \) versus \( t \).

Step by step solution

01

Develop the differential equation

The rate of change of concentration of reactant A, \( \frac{dC_A}{dt} \), is equal to the negative of the rate of reaction since reactant A is being consumed in the reaction. This gives us: \[\frac{dC_A}{dt} = - \frac{k_1 C_A}{1+k_2 C_A} \]At \( t = 0 \), the concentration of A, \( C_A \) is initially \( C_{A0} \). So, the initial condition is \( C_A = C_{A0} \) at \( t = 0 \).
02

Sketch a plot of \( C_A \) versus \( t \)

When you plot \( C_A \) against \( t \), you would observe that initially at \( t = 0 \), \( C_A = C_{A0} \), and as \( t \rightarrow \infty \), \( C_A \) approaches zero, indicating that all of the reactant has been consumed. The plot will start high and steadily decrease towards zero, representing the reaction's progress.
03

Solve the differential equation

Solving the differential equation to obtain an expression for the time required to achieve a particular concentration is a matter of integrating the rate expression. However, this requires knowledge of calculus and may be subject to numerical approximation methods since the rate equation is non-linear.
04

Graphical method to determine \( k_1 \) and \( k_2 \)

You can plot \( ln(C_A) \) versus \( t \) according to the data given. The intercept of this plot gives \( k_1 \) while the slope gives \( -k_2 \). By fitting a line to the data and determining the slope and intercept, the values of \( k_1 \) and \( k_2 \) can be approximated.

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Key Concepts

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

Michaelis-Menten Kinetics
Understanding Michaelis-Menten kinetics is essential for students delving into enzyme-catalyzed reactions. This concept outlines how the rate of reaction is influenced by the concentration of the substrate, which in our case is reactant A. The classic formula encapsulates this relationship as follows:
\[r_{\mathrm{A}} = \frac{k_1 C_{\mathrm{A}}}{1 + k_2 C_{\mathrm{A}}}\]
where \(r_{\mathrm{A}}\) denotes the reaction rate, \(k_1\) the maximum rate of reaction, \(k_2\) the Michaelis constant which is reflective of the affinity between the enzyme and the substrate, and \(C_{\mathrm{A}}\) represent the concentration of the substrate A. The kinetics indicate that as the substrate concentration increases, the reaction rate initially increases, but eventually it levels off, achieving a maximum velocity where the enzyme is saturated by the substrate. It's critical to comprehend this saturation effect, as it is pivotal in predicting the reaction behavior under varied conditions.
Reaction Rate Expression
The reaction rate expression is a mathematical representation that indicates how swiftly a chemical reaction occurs. It is governed by parameters like reactant concentration and rate constants, which depend on the nature of the reaction as well as external factors such as temperature.
For an enzyme-catalyzed reaction governed by Michaelis-Menten kinetics, the reaction rate expression is non-linear, meaning that it forms a hyperbolic relationship with substrate concentration. The rate at which substance A is used up can be described by the differential rate expression:
\[\frac{dC_{\mathrm{A}}}{dt} = - \frac{k_1 C_{\mathrm{A}}}{1 + k_2 C_{\mathrm{A}}}\]
This equation underlines a crucial detail: as A is consumed, its concentration decreases over time, which, in turn, affects the velocity of the reaction. Thus, understanding this expression is vital in predicting how long it takes for the reaction to reach a certain stage.
Batch Reactor Kinetics
Batch reactors are a common setup for carrying out chemical reactions on a limited scale and are frequently used for enzyme-catalyzed processes. Kinetics within a batch reactor requires consideration of how the reaction progresses over time, starting with initial concentrations and without the continuous addition or removal of reactants (or products).
In the given exercise, an isothermal batch reactor works with a constant volume. We use the initial condition, \(C_{\mathrm{A}0}\), which is the concentration of reactant A at the beginning (time \(t = 0\)). As the reaction advances, you can visualize the declining concentration of A using a plot of \(C_{\mathrm{A}}\) versus time \(t\). This graphical representation encapsulates the entirety of the batch reactor kinetics, showing how the concentration diminishes asymptotically as time progresses, eventually reaching an equilibrium where no further reaction takes place. Internalizing this behavior helps with predicting outcomes in batch reactions.
Differential Equation Solving
In the realm of enzyme-catalyzed reactions, solving differential equations is a fundamental skill required to glean insight into reaction dynamics. The rate equation we're dealing with is a differential equation that describes how the substrate concentration changes over time during the reaction.
To solve the rate differential equation given in the exercise: \[\frac{dC_{\mathrm{A}}}{dt} = - \frac{k_1 C_{\mathrm{A}}}{1 + k_2 C_{\mathrm{A}}}\] you would typically separate variables and integrate both sides. This involves calculus and sometimes requires numerical methods, especially if the integration cannot be done analytically due to the equation's complexity. Upon successful integration, you obtain a function that gives you the time required to reach a specific substrate concentration \(C_{\mathrm{A}}\).
Understanding and being able to apply these mathematical tools can crack the code of complex enzyme kinetics, providing pathways to the practical determination of rates and constants based on experimental data.

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Most popular questions from this chapter

A radioactive isotope decays at a rate proportional to its concentration. If the concentration of an isotope is \(C(\mathrm{mg} / \mathrm{L}),\) then its rate of decay may be expressed as $$r_{\mathrm{d}}[\mathrm{mg} /(\mathrm{L} \cdot \mathrm{s})]=k C$$ where \(k\) is a constant. (a) A volume \(V(\mathrm{L})\) of a solution of a radioisotope whose concentration is \(C_{0}(\mathrm{mg} / \mathrm{L})\) is placed in a closed vessel. Write a balance on the isotope in the vessel and integrate it to prove that the half-life \(t_{1 / 2}\) of the isotope \(-\) by definition, the time required for the isotope concentration to decrease to half of its initial value- equals ( \(\ln 2\) )/ \(k\). (b) The half-life of \(^{56} \mathrm{Mn}\) is \(2.6 \mathrm{h}\). A batch of this isotope that was used in a radiotracing experiment has been collected in a holding tank. The radiation safety officer declares that the activity (which is proportional to the isotope concentration) must decay to \(1 \%\) of its present value before the solution can be discarded. How long will this take?

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.

A 10.0 -ft compressed-air tank is being filled. Before the filling begins, the tank is open to the atmosphere. The reading on a Bourdon gauge mounted on the tank increases linearly from an initial value of 0.0 to 100 psi after 15 seconds. The temperature is constant at \(72^{\circ} \mathrm{F}\), and atmospheric pressure is 1 atm. (a) Calculate the rate \(\dot{n}\) (lb-mole/s) at which air is being added to the tank, assuming ideal-gas behavior. (Suggestion: Start by calculating how much is in the tank at \(t=0 .)\) (b) Let \(N(t)\) equal the number of Ib-moles of air in the tank at any time. Write a differential balance on the air in the tank in terms of \(N\) and provide an initial condition. (c) Integrate the balance to obtain an expression for \(N(t)\). Check your solution two ways. (d) Estimate the Ib-moles of oxygen in the tank after two minutes. List reasons your answer might be inaccurate, assuming there are no mistakes in your calculation.

A ventilation system has been designed for a large laboratory with a volume of \(1100 \mathrm{m}^{3}\). The volumetric flow rate of ventilation air is \(700 \mathrm{m}^{3} / \mathrm{min}\) at \(22^{\circ} \mathrm{C}\) and 1 atm. (The latter two values may also be taken as the temperature and pressure of the room air.) A reactor in the laboratory is capable of emitting as much as 1.50 mol of sulfur dioxide into the room if a seal ruptures. An \(\mathrm{SO}_{2}\) mole fraction in the room air greater than \(1.0 \times 10^{-6}(1 \mathrm{ppm})\) constitutes a health hazard. (a) Suppose the reactor seal ruptures at a time \(t=0,\) and the maximum amount of \(\mathrm{SO}_{2}\) is emitted and spreads uniformly throughout the room almost instantaneously. Assuming that the air flow is sufficient to make the room air composition spatially uniform, write a differential SO_ balance, letting \(N\) be the total moles of gas in the room (assume constant) and \(x(t)\) the mole fraction of \(\mathrm{SO}_{2}\) in the laboratory air. Convert the balance into an equation for \(d x / d t\) and provide an initial condition. (Assume that all of the \(\left.\mathrm{SO}_{2} \text { emitted is in the room at } t=0 .\right)\) (b) Predict the shape of a plot of \(x\) versus \(t\). Explain your reasoning, using the equation of Part (a) in your explanation. (c) Separate variables and integrate the balance to obtain an expression for \(x(t)\). Check your solution. (d) Convert the expression for \(x(t)\) into an expression for the concentration of \(\mathrm{SO}_{2}\) in the room, \(C_{\mathrm{SO}_{2}}\) (mol \(\mathrm{SO}_{2} / \mathrm{L}\) ). Calculate (i) the concentration of \(\mathrm{SO}_{2}\) in the room two minutes after the rupture occurs, and (ii) the time required for the \(S O_{2}\) concentration to reach the "safe" level. (e) Why would it probably not yet be safe to enter the room after the time calculated in Part (d)? (Hint:One of the assumptions made in the problem is probably not a good one.)

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.

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