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Steady-state mechanisms

Steady-state mechanism. Derive the expression for -d[hR]/dt in this scheme, making the steady-state approximation for [A] and [B]. The answer must contain no concentration other than [AB],... [Pg.99]

Steady-state mechanism. Consider the oxidation of RufNHj) by CL, which is believed to occur by the scheme shown below at constant pH. Imagine that one does a series of experiments with [Ru(NHs)g+ ] [O2]. Derive the steady-state rate law. Could these experiments equally well have had the reverse inequality of concentrations Should [RulNH.O ] also be adjusted (how and why) What apparent rate constant could be obtained from the concentration conditions that you consider optimum How would you design a longer series of experiments, and what rate constants could be obtained from the data If the data were examined graphically, what quantities would be displayed on the axes to obtain linear plots, and how would the rate constants be obtained from them ... [Pg.99]

It was pointed out in Section 6.5 on pH profiles that substrate titrations and certain steady-state mechanisms take the same algebraic form. This ambiguity also prevails when association equilibria can be established. This is illustrated by the reaction17... [Pg.147]

Despite the explicit dependence on Reynolds number, in its present form the model does not describe low-Reynolds-number effects on the steady-state mechanical-to-scalar time-scale ratio (R defined by (3.72), p. 76). In order to include such effects, they would need to be incorporated in the scalar spectral energy transfer rates. In the original model, the spectral energy transfer rates were chosen such that R(t) —> AV, = 2 for Sc = 1 and V

model parameter. DNS data for 90 < R-,. suggest that Re, is nearly constant. However, for lower... [Pg.146]

The applicability of Eqs. (4.27) - (4.30) is somewhat restricted because the bulk concentration is assumed to be constant because either its depletion is negligible (adsorbed quantity quantity present in the system) or because it is kept constant by a steady state mechanism. Analytical expressions of F as a function of time for situations where the approach to adsorption equilibrium is accompanied by a corresponding adjustment of c are available only for a few relatively simple cases. [Pg.105]

Focusing is a steady-state mechanism with regard to pH. Proteins approach their respective pi values at differing rates, but remain relatively hxed at those... [Pg.143]

It is possible to test the applicability of the rapid equihbrium or steady-state mechanisms to a particular enzyme reaction, if the concentration of enzyme is known (Price and Stevens, 1999). If... [Pg.112]

The Steady-State Mechanism If the interconversion step is not the sole rate-determining step and binding steps are not in rapid equilibrium, then a steady-state description of the reaction is applicable. If there is a single ternary complex, EXY, (thus, [EXY] = [EAB] + [EPQ]), the scheme can be depicted as... [Pg.525]

The Steady-State Mechanism If we consider the ordered Bi Uni mechanism with only one central complex. [Pg.526]

Steady-State Mechanism. Consider the reaction scheme with only one central complex (thus, EA + EPQ = EXY) ... [Pg.605]

Mechanism. We wish to analyze the decay data in terms of the mechanism proposed for the steady-state reaction (3). Obviously the two reactions are related in fact. If the steady-state mechanism can be analyzed to give the observed decay kinetics, we will have support for the mechanism. We may also obtain rate constants for some of the elementary reactions. [Pg.248]

B. The / -Dimensional Subspace of All Steady-State Mechanisms and the / -Dimensional Subspace... [Pg.273]

B. Basic Overall Reactions, Steady-State Mechanisms,... [Pg.273]

To define a system in a steady state it is necessary to distinguish two kinds of species, the intermediates a,.., a, and the terminal species a/ + 1,...,af + r, where I + T = A. In such a system a steady-state mechanism is one whose reaction only involves terminal species. The net rate of production of each intermediate in such a mechanism is zero, which is equivalent to saying that the first / coefficients are zero in the general expression (5) for a reaction. This gives us the characterization, introduced by Horiuti (4, 7), for a steady-... [Pg.280]

If H denotes the rank of the S x / matrix in Eq. (7), then the dimension P of the space of all steady-state mechanisms equals S - H, and the dimension R of the space of all reactions which they produce equals Q — H. Let us describe the reactions in this P-dimensional space as the overall reactions, their essential property being that they involve terminal species only. [Pg.281]

The dimension of a space equals the number of elements in a basis, which is defined as a set of elements such that every element in the space is equal to a unique linear combination of them. Therefore, P steady-state mechanisms can be chosen in terms of which all others can be uniquely expressed. This gives us a unique way to symbolize each steady-state mechanism and its overall reaction, but it does not provide a classification system for them which is valid from a chemical viewpoint, because the choice of a basis is arbitrary and is not dictated, in general, by any consideration of chemistry. A classification system for mechanisms is our next topic. [Pg.281]

Hence in the entire system there are at most (q) direct mechanisms for r, but usually there are many less than this, not only because of the excluded subsystems, but also because different subsystems can contain the same direct mechanism for a particular r. This approach to finding direct mechanisms is implemented in Section IV, where an efficient procedure is given for making a complete list of all the direct steady-state mechanisms for a given reaction, simple or multiple. [Pg.282]

Equation (7) characterizes a steady-state mechanism algebraically, but it does not provide an explicit formula for any such mechanism. Therefore, using only the matrix (2) of elementary reaction coefficients and the knowledge of which columns in the matrix correspond to terminal species, let us derive a general formula for any steady-state mechanism. [Pg.283]

The basis s,..., ss for the mechanism space will be changed to one which contains H non-steady-state mechanisms and P steady-state mechanisms. The latter will be what Temkin (16) calls a "basis for all routes. A route is what we are calling a steady-state mechanism, and a basis is a maximal linearly independent set of them. The basis is stoichiometric in Temkin s... [Pg.283]

A basis for the space of all steady-state mechanisms is (mH + i,. .., ms). Since m, is a linear combination of steps, this basis has the following form ... [Pg.285]

The rows in (12) from mQ+1 through ms are a basis for the space of all cycles, and the coefficients in these rows form a C x S matrix which will be needed in Section IV for the construction of the unique set of all direct steady-state mechanisms. [Pg.286]

Every element of a space is a unique linear combination of its basis elements. Therefore, a general expression for any steady-state mechanism m, including cycles, has the following form ... [Pg.286]

If R = 1 in a chemical system, it means that all steady-state mechanisms [i.e., all m which can be obtained by assigning particular numerical values to fii,..., fis in Eq. (13)] will have the same overall reaction r or a multiple of it, because then Eq. (14) reduces to r = /iH + 1R(mJf+t). In this case the system is said to have a simple overall reaction, and, when we come to list all the direct mechanisms for r, there is no loss of generality if we take the multiple pH+ to be unity. [Pg.286]

In all of the cases treated above the set of direct steady-state mechanisms which has been generated is exhaustive. However, it is possible for repetitions to occur among the mechanisms, but we can eliminate the possibility of repetitions in the following manner. [Pg.290]

This displays the convention, tacitly assumed later, that the positive direction of a step corresponds to the advancement from left to right of the stated chemical equation. The matrix of stoichiometric coefficients for these reactions is shown in Table II. The diagonalization of the matrix in Table II gives the matrix in Table III, from which the steady-state mechanism is S + 2s2 + 2s3 + 2s4. In Horiuti s terminology the stoichiometric numbers are 1 for Sj and 2 for s2, s3, and s4. [Pg.292]

Since H+ and e are always together, let us regard H+ + e as a single component and write it simply as H +. The matrix of stoichiometric coefficients is given in Table IV, the diagonalization of which gives the matrix in Table V. From this we conclude that the general steady-state mechanism is as follows ... [Pg.293]

Diagonalization of the matrix of stoichiometric coefficients gives Table XVI, from which we read off the general steady-state mechanism (37) and its overall reaction (38), where p, a, and (j> are unrestricted ... [Pg.303]

Let the isomers be denoted by 1, 2C, and 2T. Then diagonalizing the matrix of stoichiometric coefficients gives matrix of Table XIX. From the matrix of Table XIX we obtain the general steady-state mechanism (40) with p and a unrestricted ... [Pg.305]

Net rate of advancement of step Sj in steady-state mechanism m,. [Pg.321]

Figure 6.1 Schematic evolution of steady-state mechanical properties of a thermoset as a function of reaction time or conversion. Representative properties are the steady shear viscosity for the liquid state and the equilibrium modulus for the solid state. Figure 6.1 Schematic evolution of steady-state mechanical properties of a thermoset as a function of reaction time or conversion. Representative properties are the steady shear viscosity for the liquid state and the equilibrium modulus for the solid state.
For all these reasons, steady-state mechanical measurements, even if they are very simple and very often used in practice, lead to an apparent gel point. [Pg.199]

IEF is a steady-state mechanism in which the net flow of molecules ceases on attainment of focusing. This means that the time derivative in Eq. (4) is zero when focusing is achieved dc/dt = 0. Thus,... [Pg.293]

Since we know the frictional losses, Ev, we can use the steady state mechanical energy balance to solve for W. [Pg.147]

Starting with the open system balance equation, derive the steady-state mechanical energy balance equation (Equation 7.7-2) for an incompressible fluid and simplify the equation further to derive the Bernoulli equation. List all the assumptions made in the derivation of the latter equation. [Pg.315]


See other pages where Steady-state mechanisms is mentioned: [Pg.272]    [Pg.226]    [Pg.230]    [Pg.231]    [Pg.387]    [Pg.26]    [Pg.284]    [Pg.320]    [Pg.321]    [Pg.73]   
See also in sourсe #XX -- [ Pg.32 ]

See also in sourсe #XX -- [ Pg.280 , Pg.283 , Pg.284 , Pg.285 , Pg.286 ]




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