Abstract
The Michaelis–Menten enzymatic reaction is sufficient to perceive many subtleties of network modeling, including the concentration and time scales separations, the formal equivalence between bulk phase and single-molecule approaches, or the relationships between single-cycle transient probabilities and steady state rates. Seven methods proposed by different authors and yielding the same famous Michaelis–Menten equation, are selected here to illustrate the kinetic and probabilistic use of rate constants and to review basic techniques for handling them. Finally, the general rate of an ordered multistep reaction, of which the Michaelis–Menten reaction is a particular case, is deduced from a Markovian approach.
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P.R. is Senior Research Associate of the Belgian Fonds National de la Recherche Scientifique (FRS-FNRS).
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Appendices
Appendices
1.1 Branch pruning to generate a linear chain
The reduction of disordered cycles to ordered transitions has been addressed for example in [4, 13]. The most general treatment of a linear chain with one input and one output and including a branched module, leads to a Michaelian kinetics with respect to the distribution of the reaction time between the input and output, irrespective of the complexity of the intervening module.
In a simplified case, if the fraction of time spent by the enzyme in the forms \(EA\) and \(EB\) (Fig. 5), is negligible compared to its total mean cycling time, these alternative forms can be eliminated and the disordered individual rates can be replaced by ordered rates according to
In addition, postulating that the walk is random forces to assume that the transitions \(k_{A}\) and \(k_{B}\) do not influence each other. For example, if they are the pseudo-first order rates of ligation to two substrates \(A\) and \(B\), the binding of one substrate has no influence on the binding of the other one. In this case, \(k_{A}=k'_{A}\) and \(k_{B} = k'_{B}\) and the global rates are
with
1.2 Mean completion time for a general chain
Equation (14) can be rigorously obtained through a continuous time Markovian modeling. In the following formulation, the probabilities of the different enzymatic states are written \(P_i(t)\), \(i=0,1,\ldots ,n\), and correspond to the amount of final state \(i\) at time \(t\). Their evolution is determined by a linear differential system,
with the initial condition \(P_i(0) = \delta _{i,0}\). The matrix \(\hat{A}\) is numerical and contains the transition rates: the coefficient \(\hat{A}_{ij}\) is equal to the rate of the transition \(j \rightarrow i\). As the only allowed transitions are from \(j\) to \(j, j\pm 1\), the matrix \(\hat{A}\) is tridiagonal; in addition all its column sums are equal to 0, \(\sum _{i=0}^n \, \hat{A}_{ij} = 0\) (a consequence of the conservation law \(\sum _{i=0}^n P_i(t) = 0\)). The last column of \(\hat{A}\) is also zero since \(n\) is an absorbing state. For this reason, it is sufficient to consider the restriction \(A\) of \(\hat{A}\) to its first \(n\) rows and \(n\) columns, \(A = (\hat{A}_{ij})_{0 \le i,j \le n-1}\). The differential system can then be written as
supplemented by the extra equation \({\mathrm{d} \over \mathrm{d}t} P_n(t) = k^+_{n-1} P_{n-1}(t)\), as well as the initial condition \(\mathbf{P}(0) = (1,0,\ldots ,0)^t\).
Our purpose is to compute
Up to the factor \(k_{n-1}^+\), this is the last component of the length \(n\) vector \(\langle \mathbf{T} \rangle = \int _0^\infty \mathrm{d}t \, t\,\mathbf{P}(t)\).
Let us observe that the solution of the differential system is formally given by
where, as indicated, the exponential of the matrix \(tA\) is defined by its Taylor series. Applying \(A^2\) on \(\langle \mathbf{T} \rangle \), using \(A^2 \mathbf{P}(t) = {\mathrm{d}^2 \over \mathrm{d}t^2} \mathbf{P}(t)\) and integrating by parts, we obtain
where we have used the fact that \(\mathbf{P}(t)\) goes exponentially to zero when \(t \rightarrow \infty \). From this we obtain that \(\langle \mathbf{T} \rangle = A^{-2} \mathbf{P}(0)\). Taking the last component of this vector equation and using \(\mathbf{P}(0) = (1,0,0,\ldots ,0)\), we find that
is proportional to the scalar product of the last row of \(A^{-1}\) and its first column.
Let us first apply this formula to the simplest situation, namely when all transition rates \(k^\pm _i\) are equal to 1. In this case, the entries of \(A\) are equal to \(+1\) on the lower and upper diagonals, namely \(A_{i,i\pm 1}=+1\). They are equal to \(-2\) on the main diagonal, with the exception of \(A_{00}=-1\). One can verify that the inverse of \(A\) is given by
We therefore have \(A^{-1}_{n-1,i} = -1\) and \(A^{-1}_{i,0} = i-n\), and the following result for \(\langle T \rangle \),
In the completely general case with arbitrary rates, the matrix \(A\) takes the following form
Because the column sums of \(A\) are all zero except the last one which is \(-k^+_{n-1}\), the last row of \(A^{-1}\) is constant and equal to \(A^{-1}_{n-1,i} = -{1 \over k^+_{n-1}}\). Beside, the first column of \(A^{-1}\) is somewhat more complicated and given by
where, by convention, the term \(\ell =0\) is set to 1. We then obtain
which is equivalent to (14) upon the interchange of the two summations.
1.3 Testing another example: the 3-step enzymatic reaction
To validate the above recipes, let us apply them to a slightly more complicated (3-step) enzymatic reaction shown in Fig. 6.
The 3-step reaction is more realistic than the traditional 2-step MM reaction of Fig. 2. Indeed, the last transition of the MM scheme (rate \(k_{c}\) in Fig. 2) mixes two elementary reactions: the catalysis sensu-stricto and the dissociation of the product from the enzyme. From a chemical viewpoint, the catalytic reaction has no obvious reason to be micro-irreversible. Instead, irreversibility can be understood as the consequence of the very low concentration of the product in the medium preventing it to rebind to the enzyme. This is true in vitro when measuring initial reaction rates because no product molecules are added in the reaction mixture. This is also generally true in vivo because the products are immediately removed by sequestration or by subsequent reactions of which they are the substrates, so that their steady state concentration remains negligible in the cell. Whatever the method used, the rate corresponding to the scheme of Fig. 6 is the following function of the substrate concentration
The most direct methods to obtain this result are listed below.
1.3.1 The King and Altman method
The first order enzyme cycle corresponding to Fig. 6 is represented in Fig. 7.
The turnover rate of a single-enzyme corresponds to the reaction rate and is
where \(P_{EP}\) is given by the graphical method of King and Altman.
\(P_{EP}\) can be calculated by hand by replacing every graph by the product of rates corresponding to the arrows, but the result can be more safely obtained using an algorithm such as the KAPattern algorithm of [19], very useful for more complex networks.
1.3.2 The sum of direct conversion times
Here the rate reads
1.3.3 Markovian modeling of a random walk
We obtain by this method
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Michel, D., Ruelle, P. Seven competing ways to recover the Michaelis–Menten equation reveal the alternative approaches to steady state modeling. J Math Chem 51, 2271–2284 (2013). https://doi.org/10.1007/s10910-013-0237-5
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DOI: https://doi.org/10.1007/s10910-013-0237-5