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Consider the reversible product-formation reaction in an enzyme-catalyzed bioreaction: $$ \mathrm{E}+\mathrm{S} \stackrel{k_{1}}{\rightleftharpoons}(\mathrm{ES}) \stackrel{k_{2}}{\stackrel{k_{3}}{\sum}} \mathrm{E}+\mathrm{P} $$ Develop a rate expression for product-formation using the quasi-steady-state approximation and show that $$ v=\frac{d[\mathrm{P}]}{d t}=\frac{\left(v_{s} / K_{m}\right)[\mathrm{S}]-\left(v_{p} / K_{p}\right)[\mathrm{P}]}{1+\frac{[\mathrm{S}]}{K_{m}}+\frac{[\mathrm{P}]}{K_{p}}} $$ $$ \text { where } K_{m}=\frac{k_{-1}+k_{2}}{k_{1}} \text { and } K_{p}=\frac{k_{-1}+k_{2}}{k_{-2}} \text { and } V_{x}=k_{2}\left[\mathrm{E}_{0}\right], V_{p}=k_{-1}\left[\mathrm{E}_{0}\right] \text {. } $$

Short Answer

Expert verified
The rate expression for product formation is: \[ v = \frac{(V_{s}/K_{m})[\mathrm{S}] - (V_{p}/K_{p})[\mathrm{P}]}{1 + (\mathrm{S}/K_{m}) + (\mathrm{P}/K_{p})} \]

Step by step solution

01

- Write Down the Reaction

Consider the reversible product-formation reaction in an enzyme-catalyzed bioreaction: \[ \mathrm{E} + \mathrm{S} \stackrel{k_{1}}{\rightleftharpoons} (\mathrm{ES}) \stackrel{k_{2}}{\stackrel{k_{3}}{\sum}} \mathrm{E} + \mathrm{P} \]
02

- Apply the Quasi-Steady-State Approximation (QSSA)

Assume that the concentration of the intermediate complex (ES) is at steady state, so that \[ \frac{d[\mathrm{ES}]}{dt} = 0 \]This leads to \[ k_{1}[\mathrm{E}][\mathrm{S}] = (k_{-1} + k_{2})[\mathrm{ES}] \]
03

- Solve for [ES]

Using the steady-state assumption, rearrange for \([\mathrm{ES}]\):\[ [\mathrm{ES}] = \frac{k_{1}[\mathrm{E}][\mathrm{S}]}{k_{-1} + k_{2}} \]This expression describes the concentration of the enzyme-substrate complex.
04

- Express [E] in Terms of Total Enzyme Concentration

Use the conservation of total enzyme \([\mathrm{E}_{0}]\):\[ [\mathrm{E}_{0}] = [\mathrm{E}] + [\mathrm{ES}] \]and substituting for \([\mathrm{ES}]\) gives:\[ [\mathrm{E}] = [\mathrm{E}_{0}] - [\mathrm{ES}] \]
05

- Substitute [E] Back into [ES]

Substitute for \([\mathrm{E}]\) in the expression for \([\mathrm{ES}]\):\[ [\mathrm{ES}] = \frac{k_{1}[\mathrm{E}_{0}][\mathrm{S}]}{k_{-1} + k_{2} + k_{1}[\mathrm{S}]} \]
06

- Write the Rate Expression for Product Formation

The rate of product formation, \(v\) is given by:\[ v = k_{2}[\mathrm{ES}] \]Substitute for \([\mathrm{ES}]\):\[ v = k_{2} \cdot \frac{k_{1}[\mathrm{E}_{0}][\mathrm{S}]}{k_{-1} + k_{2} + k_{1}[\mathrm{S}]} \]
07

- Introduce Michaelis Constants and Maximum Velocities

Introduce the Michaelis constants:\[ K_{m} = \frac{k_{-1} + k_{2}}{k_{1}} \text{ and } K_{p} = \frac{k_{-1} + k_{2}}{k_{-2}} \]Define the maximum velocities:\[ V_{s} = k_{2}[\mathrm{E}_{0}] \text{ and } V_{p} = k_{-1}[\mathrm{E}_{0}] \]
08

- Rewrite the Rate Expression in Terms of the Constants

Rewrite the rate expression using the constants defined earlier:\[ v = \frac{(V_{s}/K_{m})[\mathrm{S}]}{1 + (\mathrm{S}/K_{m}) + (\mathrm{P}/K_{p})} - \frac{(V_{p}/K_{p})[\mathrm{P}]}{1 + (\mathrm{S}/K_{m}) + (\mathrm{P}/K_{p})} \]
09

- Simplify the Final Rate Expression

Combine the terms to give the final rate expression:\[ v = \frac{(V_{s}/K_{m})[\mathrm{S}] - (V_{p}/K_{p})[\mathrm{P}]}{1 + (\mathrm{S}/K_{m}) + (\mathrm{P}/K_{p})} \]

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Key Concepts

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

quasi-steady-state approximation
The quasi-steady-state approximation (QSSA) simplifies the complex equations of enzyme kinetics. It assumes the concentration of the enzyme-substrate complex (ES) remains constant over time. This is valid because the complex forms and breaks down quickly compared to the product formation. Mathematically, we can write this as:
\[\frac{d[\text{ES}]}{dt} \approx 0 \/\].
Using this assumption, the rate of formation and breakdown of the complex can be equated to yield: \[\text{k}_{1}[\text{E}][\text{S}] = (\text{k}_{-1} + \text{k}_{2})[\text{ES}]\]
This simplification allows us to solve for \[\text{[ES]}\] and subsequently understand how the enzyme and substrate concentrations affect the reaction.
Michaelis-Menten kinetics
Michaelis-Menten kinetics describe the rate of enzymatic reactions by incorporating the enzyme, substrate, and the enzyme-substrate complex into a single equation. The key idea is that the formation of the enzyme-substrate complex is in a state of dynamic equilibrium. Using the QSSA, we derived \[\text{[ES]} = \frac{k_1[\text{E}][\text{S}]}{k_{-1} + k_2}\]
With this, the rate of product formation is \[v = k_2[\text{ES}]\].
Introducing the Michaelis constant \[K_m = \frac{k_{-1} + k_2}{k_1}\] simplifies the expression. This results in
\[v = \frac{V_{max}[\text{S}]}{K_m + [\text{S}]}\]
where \[V_{max}\] is the maximum rate, given by \[V_{max} = k_{\text{cat}}[\text{E}_0]\], with \[k_{\text{cat}} = k_2\].
rate expression for product formation
By combining QSSA and Michaelis-Menten kinetics, we derive the rate expression for product formation. Introducing \[K_p = \frac{k_{-1} + k_{2}}{k_{-2}}\] and the velocities \[V_s = k_2[\text{E}_0]\] and \[V_p = k_{-1}[\text{E}_0]\], we obtain:
\[v = \frac{(V_s / K_m)[\text{S}] - (V_p / K_p)[\text{P}]}{1 + (\text{S} / K_m) + (\text{P} / K_p)}\]
This equation combines the substrate concentration, enzyme kinetics, and product formation into a single, elegant expression. It tells us how the rate of product formation is influenced by substrate and product concentrations, the enzyme's efficiency, and the reaction's reversibility.

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Most popular questions from this chapter

You are working for company A and you join a research group working on immobilized enzymes. Harry, the head of the lab, claims that immobilization improves the stability of the enzyme. His proof is that the enzyme has a half- life of 10 days in free solution, but under identical conditions of temperature, \(\mathrm{pH}\), and medium composition, the measured half-life of a packed column is 30 days. The enzyme is immobilized in a porous sphere \(5 \mathrm{~mm}\) in diameter. Is Harry's reasoning right? Do you agree with him? Why or why not?

An enzyme ATPase has a molecular weight of \(5 \times 10^{4}\) daltons, a \(K_{M}\) value of \(10^{-4} M\), and a \(k_{2}\) value of \(k_{2}=10^{4}\) molecules ATP/min molecule enzyme at \(37^{\circ} \mathrm{C}\). The reaction catalyzed is the following: $$ \mathrm{ATP} \stackrel{\text { ATPase }}{\longrightarrow} \mathrm{ADP}+\mathrm{P}_{i} $$ which can also be represented as $$ \mathrm{E}+\mathrm{S} \underset{k_{1}}{\stackrel{A_{1}}{\longrightarrow} \mathrm{ES} \stackrel{k_{2}}{\longrightarrow} \mathrm{E}+\mathrm{P} $$ where \(S\) is ATP. The enzyme at this temperature is unstable. The enzyme inactivation kinetics are first order: $$ \mathrm{E}=\mathrm{E}_{0} e^{-k_{\alpha} r} $$ where \(\mathrm{E}_{0}\) is the initial enzyme concentration and \(k_{d}=0.1 \mathrm{~min}^{-1}\). In an experiment with a partially pure enzyme preparation, \(10 \mu \mathrm{g}\) of total crude protein (containing enzyme) is added to a \(1 \mathrm{ml}\) reaction mixture containing \(0.02 \mathrm{M}\) ATP and incubated at \(37^{\circ} \mathrm{C}\). After 12 hours the reaction ends (i.e., \(t \rightarrow \infty\) ) and the inorganic phosphate \(\left(\mathrm{P}_{i}\right)\) concentration is found to be \(0.002 M\), which was initially zero. What fraction of the crude protein preparation was the enzyme? Hint: Since \([\mathrm{S}]>>K_{m}\), the reaction rate can be represented by $$ \frac{d(\mathrm{P})}{d t}=k_{2}[\mathrm{E}] $$

The following data were obtained from enzymatic oxidation of phenol by phenol oxidase at different phenol concentrations. \(\begin{array}{lrccllllcrrr}\mathrm{S}(\mathrm{mg} / \mathrm{l}) & 10 & 20 & 30 & 50 & 60 & 80 & 90 & 110 & 130 & 140 & 150 \\ v(\mathrm{mg} / \mathrm{l}-\mathrm{h}) & 5 & 7.5 & 10 & 12.5 & 13.7 & 15 & 15 & 12.5 & 9.5 & 7.5 & 5.7\end{array}\) a. What type of inhibition is this ? b. Determine the constants \(V_{\mathrm{m}}, K_{m}\) and \(K_{s i-}\) c. Determine the oxidation rate at \([\mathrm{S}]=70 \mathrm{mg} / 1\).

Michaelis-Menten kinetics are used to describe intracellular reactions. Yet \(\left[\mathrm{E}_{0}\right] \approx\left[\mathrm{S}_{0}\right]\). In in vitro batch reactors, the quasi-steady-state hypothesis does not hold for \(\left[\mathrm{E}_{0}\right] \approx\left[\mathrm{S}_{0}\right]\). The rapid equilibrium assumption also will not hold. Explain why Michaelis-Menten kinetics and the quasi-steady-state approximation are still reasonable descriptions of intracellular enzyme reactions.

The enzyme, urease, is immobilized in Ca-alginate beads \(2 \mathrm{~mm}\) in diameter. When the urea concentration in the bulk liquid is \(0.5 \mathrm{~m} M\) the rate of urea hydrolysis is \(v=10 \mathrm{mmoles-1- \textrm {h } .}\) Diffusivity of urea in \(\mathrm{Ca}\)-alginate beads is \(D_{e}=1.5 \times 10^{-5} \mathrm{~cm}^{2} / \mathrm{sec}\), and the Michaelis constant for the enzyme is \(K_{m}^{\prime}=0.2 \mathrm{~m} M\). By neglecting the liquid film resistance on the beads (i.e., \(\left.\left[\mathrm{S}_{0}\right]=\left[\mathrm{S}_{\mathrm{s}}\right]\right)\) determine the following: a. Maximum rate of hydrolysis \(V_{m}\), Thiele modulus \((\phi)\), and effectiveness factor \((\eta)\). b. What would be the \(V_{w}, \phi\), and \(\eta\) values for a particle size of \(\mathrm{Dp}=4 \mathrm{~mm}\) ?

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