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Hypothetical rate constants

Even though k2 is a hypothetical rate constant for many reaction chain systems within the overall network of reactions in the reacting media and hence... [Pg.81]

Even though k2 is a hypothetical rate constant for many reaction chain systems within the overall network of reactions in the reacting media and hence cannot be evaluated to obtain a result from Eq. (10), it is still possible to extract some qualitative trends, perhaps even with respect to automotive knock. Most importantly, Eq. (9) establishes that a chemical explosion is possible only when there is chain branching. Earlier developments show that with small amounts of chain branching, reaction times are extremely small. What determines whether the system will explode or not is whether chain termination is faster or slower than chain branching. [Pg.63]

Hansch formulated a parabolic model (eq. 7, chapter 1.1) [15, 17—19] for the mathematical description of nonlinear relationships. He was aware that the sides of a parabola are always more or less curved, while in most cases at least the left side of the structure-activity relationship (i.e. the lipophilicity dependence of the more hydrophilic analogs) is strictly linear equations including a third-order lipophilicity term did not produce much improvement [19]. A computer simulation of the transport of drugs in a biological system, using hypothetical rate constants,... [Pg.68]

Viewed from the perspective of ethylene oxide, these reactions are competitive by contrast, from the perspective of the amines, they are consecutive. Consider a research scale batch reactor operating at 60°C and 20 bar to maintain all species in the liquid phase. Actual production of these commodity products on a large scale would be conducted in flow reactors, as described in Illustration 9.5. The rate laws are of the mixed second-order form (first-order in each reactant), with hypothetical rate constants ki, k2, and equal to 1,0.4, and 0.1 L-moCV min, respectively. MEA and DEA are both high-volume chemicals, while TEA is less in demand. The distribution of alkanolamine products obtained under the specified conditions can be influenced by controlling the initial mole ratio of EO to A and the time of reaction. [Pg.138]

Consider a flow reactor operating at 150°C and 20 bar so as to maintain all species in the liquid phase. The rate laws are of the mixed second-order form, with hypothetical rate constants k, 2, and k- equal to 1, 0.4, and 0.1 (L/mol- min), respectively. [Pg.288]

From this discussion it is seen that in order to make a quantitative measure of anchimeric assistance it is necessary to know k or the (often hypothetical) rate constants for reaction of the substrates without any form of nucleophilic assistance or with nucleophilic assistance from the solvent. The problems in estimating these constants will be discussed in Chapter 3. [Pg.15]

Initially, a first-trial mechanism is constructed by including all possibly relevant, known reactions as well as some that may be completely hypothetical Rate constant expressions for these reactions are selected from literature sources, estimated theoretically, or just guessed. At this stage preference is given to experimental rate constants, but when considering them the researcher must scrupulously analyze all the assumptions made and the parameter values used by the authors, for they may be out of date. The researcher must also check the consistency of the authors results with the reports of others. [Pg.439]

In the equations, k (0) is the hypothetical quenching rate constant when AE ( AG) = 0 and AG is the free energy change on quenching. [Pg.158]

Fig. 19. (A) Simulated bleaching of a hypothetical dye using Eq. (24) at different concentrations of Feni-TAML catalyst (in M) with the rate constants ki (in s-1) and ku (in M-1s-1). The numerical values are indicated on the graph. (B) Normalized experimental and simulated bleaching of Safranine O (4.3 x 10-5M) by H202 (0.012 M) catalyzed by la at pH 11 and 25°C. Experimental data are shown as a and. The simulations, shown as solid lines, were made as in (A). From Ref. (52). Fig. 19. (A) Simulated bleaching of a hypothetical dye using Eq. (24) at different concentrations of Feni-TAML catalyst (in M) with the rate constants ki (in s-1) and ku (in M-1s-1). The numerical values are indicated on the graph. (B) Normalized experimental and simulated bleaching of Safranine O (4.3 x 10-5M) by H202 (0.012 M) catalyzed by la at pH 11 and 25°C. Experimental data are shown as a and. The simulations, shown as solid lines, were made as in (A). From Ref. (52).
The catalyst is preliminarily oxidized to the state of the highest valence (vanadium to V5+ molybdenum to Mo6+). Only the complex of hydroperoxide with the metal in its highest valence state is catalytically active. Alcohol formed upon epoxidation is complexed with the catalyst. As a result, competitive inhibition appears, and the effective reaction rate constant, i.e., v/[olefin][ROOH], decreases in the course of the process due to the accumulation of alcohol. Water, which acts by the same mechanism, is still more efficient inhibitor. Several hypothetical variants were proposed for the detailed mechanism of epoxidation. [Pg.416]

Peroxynitrite reacts with heme proteins such as prostacycline synthase (PGI2), microperoxidase, and the heme thiolate protein P450 to form a ferryl nitrogen dioxide complex as an intermediate [120]. Peroxynitrite also reacts with acetaldehyde with the rate constant of 680 1 mol 1 s" 1 forming a hypothetical adduct, which is decomposed into acetate, formate, and methyl radicals [121]. The oxidation of NADH and NADPH by peroxynitrite most certainly occurs by free radical mechanism [122,123], Kirsch and de Groot [122] concluded that peroxynitrite oxidized NADH by a one-electron transfer mechanism to form NAD and superoxide ... [Pg.704]

Figure 3.27 Representation of the rates ofthefonvard and reverse reactions for non- and near-equilibrium reactions in one reaction in a hypothetical pathway. The values represent actual rates, not rate constants. The net flux through the pathway is given by (1/f-l/r). In the non-equilibrium reaction, the rate of the forward reaction dominates, so that the net flux is almost identical to this rate. In the near-equilibrium reaction, both forward and reverse rates are almost identical but considerably in excess of the flux. Figure 3.27 Representation of the rates ofthefonvard and reverse reactions for non- and near-equilibrium reactions in one reaction in a hypothetical pathway. The values represent actual rates, not rate constants. The net flux through the pathway is given by (1/f-l/r). In the non-equilibrium reaction, the rate of the forward reaction dominates, so that the net flux is almost identical to this rate. In the near-equilibrium reaction, both forward and reverse rates are almost identical but considerably in excess of the flux.
Note that detecting a well-characterized intermediate as the product of a given reaction does not prove that the rate constant determined corresponds exclusively to that reaction. Let us take the hypothetical reaction of Scheme 18.6, to give radicals A" and B". While benzylic radical B" will be readily detectable, we expect A to be silent. However, even if the rate constant is determined by monitoring only B, the value obtained will correspond to both reaction paths, that is, ... [Pg.863]

The intercept on the ordinate in Figure 2 corresponds to a numerical value of ki of 1.60 x KT /sec. In physical terms, the rate constant ki represents the rate constant for generation of Co(CN)5 2 from Co(CN)50H2. It also represents the rate constant for formation of Co(CN)5X 3 by a hypothetical nucleophile so efficient in its scavenger action that it would be able to capture all of the Co(CN)5-2 generated in Reaction 1 before reaction with water could occur. [Pg.33]

Some semi-quantitative confirmation of these A factors comes from the consideration that the pyrolysis of C2H8 at 900°K. is a chain reaction in which the data on maximal inhibition indicate a chain length X of the order of 10. Since the only likely homogeneous, initiation process is the fission of C2H8 into 2CH3, the hypothetical first-order rate constant for the pyrolysis can be set equal to this initiation rate constant multiplied by X ... [Pg.7]

Note that % is the inverse of the mean flushing rate constant kw li defined according to Eq. 12-50. Yet, the upper limit of th is hypothetical, since lakes like Greifensee are usually completely mixed during the winter. [Pg.842]

Figure 21.5 Response of linear system to external periodic perturbation (Eq. 21-12). Full lines show hypothetical steady-state (Eq. 21-19) dashed lines give system response (Eq. 21-18). The system rate constant k = 4.0 yr 1 corresponds to the behavior of PCE in Greifensee (Box 21.2). Curve A corresponds to an annual variation with relative amplitude Aj = 0.5, curve B to a variation with period of 4 years and A, = 1. Figure 21.5 Response of linear system to external periodic perturbation (Eq. 21-12). Full lines show hypothetical steady-state (Eq. 21-19) dashed lines give system response (Eq. 21-18). The system rate constant k = 4.0 yr 1 corresponds to the behavior of PCE in Greifensee (Box 21.2). Curve A corresponds to an annual variation with relative amplitude Aj = 0.5, curve B to a variation with period of 4 years and A, = 1.
It may be concluded from the known rate coefficients for the hydrolysis of acetic anhydride, for example, that the hypothetical k0H value is larger than a diffusion-controlled rate constant. If Xd is taken as about 107 for acetic anhydride, then from k0n = h2o where kHiQ is the second-order water... [Pg.222]

The preceding experiments prove that there is an intermediate on the reaction pathway in each case, the measured rate constants for the formation and decay of the intermediate are at least as high as the value of kcat for the hydrolysis of the ester in the steady state. They do not, however, prove what the intermediate is. The evidence for covalent modification of Ser-195 of the enzyme stems from the early experiments on the irreversible inhibition of the enzyme by organo-phosphates such as diisopropyl fluorophosphate the inhibited protein was subjected to partial hydrolysis, and the peptide containing the phosphate ester was isolated and shown to be esterified on Ser-195.1516 The ultimate characterization of acylenzymes has come from x-ray diffraction studies of nonspecific acylenzymes at low pH, where they are stable (e.g., indolylacryloyl-chymotrypsin),17 and of specific acylenzymes at subzero temperatures and at low pH.18 When stable solutions of acylenzymes are restored to conditions under which they are unstable, they are found to react at the required rate. These experiments thus prove that the acylenzyme does occur on the reaction pathway. They do not rule out, however, the possibility that there are further intermediates. For example, they do not rule out an initial acylation on His-57 followed by rapid intramolecular transfer. Evidence concerning this and any other hypothetical intermediates must come from additional kinetic experiments and examination of the crystal structure of the enzyme. [Pg.122]

We can use the two hypothetical steps of section Clb i.e., that kcJKM be maximized and that KM be greater than [S], to set up criteria for judging the state of evolution of an enzyme whose function is to maximize rate. We recall from Chapter 3 that the maximum value of kcJKM is the rate constant for the diffusion-controlled encounter of the enzyme and substrate, and from Chapter 4 that this is about 108 to 109 s "1 M l. A perfectly evolved enzyme should have a kcJKM in the range of 108 to 109 s"1 and a KM greater than [S]. Using the data for kcJKM listed in Table 4.4 and the substrate concentrations and KM values mentioned in this chapter, it appears that carbonic anhydrase and triosephosphate isomerase are perfectly evolved for the maximization of rate, which agrees with the conclusions of W. J. Albery and J. R. Knowles on triosephosphate isomerase.5... [Pg.195]

Thus the ratio of the forward and back rate constants. (K2IK ) is not the equilibrium constant for the overall reaction, but K, the exponent being the reciprocal of the stoicheiometric number of the limiting reaction. This significance and its exploitation have been examined by Horiuti [10. Frank-Kamenetsky [11] has developed some safe conditions for the applicability of certain forms of the hypothetical method, in the form of rather strong inequalities on the partial derivatives of the kinetic expressions. [Pg.165]

As shown in the preceding reaction sequence, a rate-determining chemical step is interposed between the two electrode reactions. (See Chap. 2 for an explanation and an example of this mechanism.) The two dashed lines in Figure 3.4A show hypothetical chronoamperograms for the le reduction of O to R and for the direct 2e reduction of O to P with no kinetic complications. The solid line shows a typical chronoamperogram for an ECE mechanism. The current is intermediate between the le and 2e reductions, since the reduction of X to P is controlled by the rate of the chemical reaction of R to generate X. The exact position of the solid line is determined by the value of the rate constant k. [Pg.59]

The value of the kinetic isotope effect method lies mainly in the possibility of making a substitution within tlve reactive center of the molecule, while still retaining the original type of the read ion, thus allowing the cancellation of many poorly defined quantities in the absolute rate equations and permitting a direct comparison between the measured and calculated values of the relative rate constants. Since the magnitude of these latter values depends on the hypothetical transition state model, a diagnostic means is provided by the method for the experimental verification of the nature of tlie transition state in question. [Pg.209]

The interpretation of kinetic data begins with a hypothetical sequence of ele mentary reaction steps, each characterized by two microscopic rate constants, one for the forward and one for the reverse reaction. From this proposed mechanism a rate equation is derived, predicting the dependence of the observed reaction rate on concentrations and on microscopic rate constants, and its form is tested against the observations. If the form of the rate equation meets the test of experiment, it may be possible to derive from the data numerical values for the microscopic rate constants of the proposed elementary reaction steps. While inconsistency is clear grounds for modifying or rejecting a mechanistic hypothesis, agreement does not prove the proposed mechanism correct. [Pg.90]

A) In activated complex theory the rate constant can be expressed in terms of the free energy F of a system hypothetically constrained to exist on a certain hypersurface, the activated complex,99 cf. Marcus, R. A., J. Chem. Phys. 41, 2624 (1964). F can be expressed in terms of the free energy F of a system centered on that hypersurface (5). The difference between F and F contributes a factor to p. A second factor in p arises from the fluctuations in the separation distance of the reactants in the activated complex (5). [Pg.153]


See other pages where Hypothetical rate constants is mentioned: [Pg.117]    [Pg.347]    [Pg.361]    [Pg.279]    [Pg.569]    [Pg.117]    [Pg.347]    [Pg.361]    [Pg.279]    [Pg.569]    [Pg.2947]    [Pg.47]    [Pg.182]    [Pg.83]    [Pg.88]    [Pg.123]    [Pg.356]    [Pg.647]    [Pg.393]    [Pg.176]    [Pg.143]    [Pg.47]    [Pg.1016]    [Pg.356]    [Pg.355]    [Pg.302]    [Pg.33]    [Pg.364]    [Pg.84]   
See also in sourсe #XX -- [ Pg.68 ]




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