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Mechanisms kinetic

The initial velocity patterns for two-substrate cases were dealt with in Volume [Pg.104]

but one quantitative analysis of such patterns has been developed since then. A sequential mechanism with two substrates has an initial velocity rate equation  [Pg.104]

In Eqs. (10) and (II), and are the dissociation constant from EA and the Michaelis constant (with B = ) for substrate A, which is the first one to add in an ordered mechanism, or either one in a random mechanism. [Pg.104]

An equation similar to Eq. (10) applies in the reverse direction, with P and Q replacing B and A. The vertical coordinate of the crossover point in this direction is given by [Pg.104]

As long as Vi and V2 are measured at equal enzyme concentrations (or corrected to this), we can calculate a parameter R  [Pg.104]

Formation of internal double bonds Pm + M Hydrogen abstraction Pn + Dm — Dp + Pp [Pg.199]

Taking into account all the above remarks, the detailed kinetic mechanism can be recast into a more realistic and simpler kinetic scheme that can predict the VCM consumption rate and the main molecular features of the PVC chains (e.g., number- and weight-average molecular weights, short- and long-chain branches, double bonds, etc.) [40,49]  [Pg.200]

The symbols I and Nj represent the primary initiator radicals and the number of initiators in the polymerization system, respectively. It should be noted that all the above reactions apart from the chain transfer to polymer can take place either in the monomer phase ) = 1) and/or in the polymer phase (j = 2). [Pg.201]


Numerous kinetic mechanisms have been proposed for oil shale pyrolysis reactions (11—14). It has been generally accepted that the kinetics of the oil shale pyrolysis could be represented by a simple first-order reaction (kerogen — bitumen — oil), or... [Pg.346]

G. Z. Whitten and co-workers. Modeling of Simulated Photochemical Smog with Kinetic Mechanism, Vols. I and II, Report No. EPA-600/3-79-001a, U.S. Environmental Protection Agency, Research Triangle Park, N.C., 1979. [Pg.388]

R. MUkovich, in J. E. McGrath, A., Anionic Polymerisation Kinetics, Mechanisms, and Synthesis, ACS Symposium Series, No. 166, American Chemical Society, Washington, D.C., 1981, p. 41. [Pg.190]

Asymptotic Solution Rate equations for the various mass-transfer mechanisms are written in dimensionless form in Table 16-13 in terms of a number of transfer units, N = L/HTU, for particle-scale mass-transfer resistances, a number of reaction units for the reaction kinetics mechanism, and a number of dispersion units, Np, for axial dispersion. For pore and sohd diffusion, q = / // p is a dimensionless radial coordinate, where / p is the radius of the particle, if a particle is bidisperse, then / p can be replaced by the radius of a suoparticle. For prehminary calculations. Fig. 16-13 can be used to estimate N for use with the LDF approximation when more than one resistance is important. [Pg.1526]

In addition to possible errors due to the steps in the kinetic mechanisms, there may be errors in the rate constants due to the smog chamber data... [Pg.330]

If the enzyme-catalyzed reaction is to be faster than the uncatalyzed case, the acceptor group on the enzyme must be a better attacking group than Y and a better leaving group than X. Note that most enzymes that carry out covalent catalysis have ping-pong kinetic mechanisms. [Pg.509]

FIGURE 19.34 The galactose-l-phosphate uridylyltransferase reaction involves a ping-pong kinetic mechanism. [Pg.635]

The kinetic mechanism of emulsion polymerization was developed by Smith and Ewart [10]. The quantitative treatment of this mechanism was made by using Har-kin s Micellar Theory [18,19]. By means of quantitative treatment, the researchers obtained an expression in which the particle number was expressed as a function of emulsifier concentration, initiation, and polymerization rates. This expression was derived for the systems including the monomers with low water solubility and partly solubilized within the micelles formed by emulsifiers having low critical micelle concentration (CMC) values [10]. [Pg.192]

Rg. 5.20. Kinetics mechanism with uncompetitive substrate inhibition and non-competitive product inhibition. [Pg.136]

Fig. 5.21. First-order reaction kinetics mechanism without inhibitions. Fig. 5.21. First-order reaction kinetics mechanism without inhibitions.
The plotting of Dixon plot and its slope re-plot (see 5.9.5.9) is a commonly used graphical method for verification of kinetics mechanisms in a particular enzymatic reaction.9 The proposed kinetic mechanism for the system is valid if the experimental data fit the rate equation given by (5.9.4.4). In this attempt, different sets of experimental data for kinetic resolution of racemic ibuprofen ester by immobilised lipase in EMR were fitted into the rate equation of (5.7.5.6). The Dixon plot is presented in Figure 5.22. [Pg.138]

Each of these variables will be considered in this book. We start with concentrations, because they determine the form of the rate law when other variables are held constant. The concentration dependences reveal possibilities for the reaction scheme the sequence of elementary reactions showing the progression of steps and intermediates. Some authors, particularly biochemists, term this a kinetic mechanism, as distinct from the chemical mechanism. The latter describes the stereochemistry, electron flow (commonly represented by curved arrows on the Lewis structure), etc. [Pg.9]

The combination of photocurrent measurements with photoinduced microwave conductivity measurements yields, as we have seen [Eqs. (11), (12), and (13)], the interfacial rate constants for minority carrier reactions (kn sr) as well as the surface concentration of photoinduced minority carriers (Aps) (and a series of solid-state parameters of the electrode material). Since light intensity modulation spectroscopy measurements give information on kinetic constants of electrode processes, a combination of this technique with light intensity-modulated microwave measurements should lead to information on kinetic mechanisms, especially very fast ones, which would not be accessible with conventional electrochemical techniques owing to RC restraints. Also, more specific kinetic information may become accessible for example, a distinction between different recombination processes. Potential-modulation MC techniques may, in parallel with potential-modulation electrochemical impedance measurements, provide more detailed information relevant for the interpretation and measurement of interfacial capacitance (see later discus-... [Pg.460]

Otherwise, the effect of electrode potential and kinetic parameters as contained in the relevant expression for the PMC signal (21), which controls the lifetime of PMC transients (40), may lead to an erroneous interpretation of kinetic mechanisms. The fact that lifetime measurements of PMC transients largely match the pattern of PMC-potential curves, showing peaks in accumulation and depletion of the semiconductor electrode and a minimum at the flatband potential [Figs. 13, 16-18, 34, and 36(b)], demonstrates that kinetic constants are accessible via PMC transient measurements, as indicated by the simplified relation (40) derived for the depletion layer of an n-type electrode. [Pg.504]

ZnO instead of T1O2 because ZnO provides a 220 times higher mobility for photoinjected electrons, which would allow reduction of the exciting laser intensity. The slow PMC decay of TiOrbased nanostructured sensitization solar cells (the Ru complex as sensitizer), which cannot be matched by a single exponential curve and is influenced by a bias illumination, is strongly affected by the concentration of iodide in the electrolyte (Fig. 38). On the basis of PMC transients and their dependence on the iodide concentration, a kinetic mechanism for the reaction of photoinjected electrons could be elaborated.40... [Pg.506]

The computer model used for this analysis is based on a plug flow tubular reactor operating under restraints of the commonly accepted kinetic mechanism for polymerization reactions ( 5 ) ... [Pg.222]

Equation (l) shows the rate of polymerization is controlled by the radical concentration and as described by Equation (2) the rate of generation of free radicals is controlled by the initiation rate. In addition. Equation (3) shows this rate of generation is controlled by the initiator and initiator concentration. Further, the rate of initiation controls the rate of propagation which controls the rate of generation of heat. This combined with the heat transfer controls the reaction temperature and the value of the various reaction rate constants of the kinetic mechanism. Through these events it becomes obvious that the initiator is a prime control variable in the tubular polymerization reaction system. [Pg.226]

Kinetic Mechanism, The following ionic mechanism describes sytrene polymerization in a hydrocarbon solution with n-butyllithiiam as the initiator (1-6), ... [Pg.375]

Model Deyelopment. Rachow and Timm (] ) derived working relationships for the kinetic mechanism described. Degree of polymerization is considered to be a continuous variable. For quenched samples a relationship correlating population density of associated polymer molecules as a function of time, degree of polymerization and environmental factors is... [Pg.376]

The kinetic mechanism subject to quenched samples requires that each polymer molecule formed will contain one butyl residue... [Pg.379]

We deal with many reactions that are not elementary. Most industrially important reactions go through a complex kinetic mechanism before the final products are reached. The mechanism may give a rate expression far different than Equation (1.14), even though it involves only short-lived intermediates that never appear in conventional chemical analyses. Elementary reactions are generally limited to the following types. [Pg.6]

Free radical polymerization of MMA is a well understood process. The kinetic mechanism neglecting the chain transfer reactions is given as follows (Odian (1970), Rudin (1982)). [Pg.323]

Nomura and Fujita (12), Dougherty (13-14), and Storti et al. (12). Space does not permit a review of each of these papers. This paper presents the development of a more extensive model in terms of particle formation mechanism, copolymer kinetic mechanism, applicability to intervals I, II and III, and the capability to simulate batch, semibatch, or continuous stirred tank reactors (CSTR). Our aim has been to combine into a single coherent model the best aspects of previous models together with the coagulative nucleation theory of Feeney et al. (8-9) in order to enhance our understanding of... [Pg.361]

Rate of Reactions. The rates of reaction in the aqueous and polymer phases were calculated using the appropriate kinetic constants according to the kinetic mechanisms described above, radical and molecular concentrations, and the particle number concentration. [Pg.364]

Law, C.K., A compilation of experimental data on laminar burning velocities. Reduced Kinetic Mechanisms for Application in Combustion, Eds. N. Peters and B. Rogg, Springer-Verlag, Heidelberg, Germany, pp. 15-26, 1993. [Pg.45]


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See also in sourсe #XX -- [ Pg.280 ]

See also in sourсe #XX -- [ Pg.547 , Pg.548 , Pg.561 , Pg.567 , Pg.571 , Pg.574 ]




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