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Mixtures various model reaction system

The purpose of this paper is to present a model for single metal-multiligand solution equilibrium which quantitatively describes the net binding of metal ions to the multiligand mixture as a whole. Equally important aspects of this model are that it yields a unified conceptual visualization of complexation in complicated multiligand mixtures, and provides a framework for interpreting the results of experiments on such systems. The model, as presented here, will be confined to mononuclear complexes, and it is assumed that no solid phases are present. The influence of pH on the complexation reactions is described. The model is illustrated by simulation of various metal-multiligand systems, and the properties of these systems are represented by means of three-dimensional plots, called stability surfaces. [Pg.202]

Fig. 22.6. Redox potentials (mV) of various half-cell reactions during mixing of fluid from a subsea hydrothermal vent with seawater, as a function of the temperature of the mixture. Since the model is calculated assuming 02(aq) and H2(aq) remain in equilibrium, the potential for electron acceptance by dioxygen is the same as that for donation by dihydrogen. Dotted line shows currently recognized upper temperature limit (121 °C) for microbial life in hydrothermal systems. A redox reaction is favored thermodynamically when the redox potential for the electron-donating half-cell reaction falls below that of the accepting half-reaction. Fig. 22.6. Redox potentials (mV) of various half-cell reactions during mixing of fluid from a subsea hydrothermal vent with seawater, as a function of the temperature of the mixture. Since the model is calculated assuming 02(aq) and H2(aq) remain in equilibrium, the potential for electron acceptance by dioxygen is the same as that for donation by dihydrogen. Dotted line shows currently recognized upper temperature limit (121 °C) for microbial life in hydrothermal systems. A redox reaction is favored thermodynamically when the redox potential for the electron-donating half-cell reaction falls below that of the accepting half-reaction.
In Fig. 1, various elements involved with the development of detailed chemical kinetic mechanisms are illustrated. Generally, the objective of this effort is to predict macroscopic phenomena, e.g., species concentration profiles and heat release in a chemical reactor, from the knowledge of fundamental chemical and physical parameters, together with a mathematical model of the process. Some of the fundamental chemical parameters of interest are the thermochemistry of species, i.e., standard state heats of formation (A//f(To)), and absolute entropies (S(Tq)), and temperature-dependent specific heats (Cp(7)), and the rate parameter constants A, n, and E, for the associated elementary reactions (see Eq. (1)). As noted above, evaluated compilations exist for the determination of these parameters. Fundamental physical parameters of interest may be the Lennard-Jones parameters (e/ic, c), dipole moments (fi), polarizabilities (a), and rotational relaxation numbers (z ,) that are necessary for the calculation of transport parameters such as the viscosity (fx) and the thermal conductivity (k) of the mixture and species diffusion coefficients (Dij). These data, together with their associated uncertainties, are then used in modeling the macroscopic behavior of the chemically reacting system. The model is then subjected to sensitivity analysis to identify its elements that are most important in influencing predictions. [Pg.99]

Other advantages include a mechanism that allows one to rationalize and predict the stereochemical outcome for various olefin systems with a reasonable level of confidence utilising a postulated spiro transition state model. The epoxidation conditions are mild and environmentally friendly with an easy workup whereby, in some cases, the epoxide can be obtained by simple extraction of the reaction mixture with hexane, leaving the ketone catalyst in the aqueous phase. [Pg.24]

The topic of Malllard Reactions was the subject of a recent American Chemical Society Symposium (6). The wide variety of reactions that can occur 1n simple model systems can be extraordinary. For example, Shibamoto commented In this symposium that a simple rhamnose/NH3/H2S reaction mixture generated 1,000 gas chromatographic peaks. A number of presentations In this book cover model systems of various compositions. Some of the mixtures studied 1n great detail and reported herein Include ... [Pg.7]

Two level factorial designs are primarily useful for exploratory purposes and calibration designs have special uses in areas such as multivariate calibration where we often expect an independent linear response from each component in a mixture. It is often important, though, to provide a more detailed model of a system. There are two prime reasons. The first is for optimisation - to find the conditions that result in a maximum or minimum as appropriate. An example is when improving die yield of synthetic reaction, or a chromatographic resolution. The second is to produce a detailed quantitative model to predict mathematically how a response relates to die values of various factors. An example may be how the near-infrared spectrum of a manufactured product relates to the nature of the material and processing employed in manufacturing. [Pg.76]

Model studies discussed in previous chapters show that the reactivity of cations and alkenes are very strongly affected by inductive and resonance effects in the substituents. Correlation of the rate constants of addition of benzhydryl cation to various styrenes with Hammett substituted benzhydryl cations to a standard alkene (2-methyl-2-pentene) gave also good correlation and p+ = 5.1 [28]. The large p value signals difficult copolymerizations between alkenes, even of similar structures. Thus, in contrast to radical copolymerization which easily provides random copolymers, cationic systems have a tendency to form either mixtures of two homopolymers or block copolymer (if the cross-over reaction is possible). [Pg.361]

In contrast to extracts obtained from nature, which usually consist of a mixture of substances and are available only in very limited amounts, synthetic model systems have the advantages of controlled purity and good availability. Such systems enable the scientist to vary reaction parameters in a systematic fashion and to adjust individual functions to analyze their influence on the system. However, model systems should be as close as possible to the natural system. Therefore, we have undertaken a study to elucidate the chemical behavior of polyamine-silica systems, including not only polyamines which can be purchased, but also polyamines specifically synthesized, with structures as close as possible to the naturally occurring ones [11], Here, we report on investigations on the kinetics of silica condensation in the presence of various polyamines... [Pg.949]

The intermediates which play a role in a cycle of a homogeneous catcilyst can be characterized by various spectroscopic techniques such as NMR, IR, Raman spectroscopy, and UV-vis spectroscopy. Also, intermediates may crystallize from a reaction mixture and the structure can then be solved with a single-crystal X-ray determination. Only on rare occasions do intermediates crystallize from the reacting systems since their concentrations are low. Often one turns to model compounds of the actual catalyst by changing the ligand or the metal. For example, iridium complexes show the same catalytic behaviour as the rhodium complexes. Since they are often much slower as catalysts the intermediates can be intercepted (see below). Another common approach is the synthesis of a ligand that simultaneously contains the substrate of the catalytic reaction this may also lead to the isolation of likely intermediates. [Pg.308]

These results reflect the importance of the employment of these types of binary solvent systems can be, for instance, as reaction media. Additionally, the experimental data of n, P and a parameters of 15 binary mixtures of the type [protic molecular solvent + IL] at various compositions have been fitted to the CNIBS/R-K model. The model proved to be statistically valuable, showing a strong correlation between predicted and experimentally measured values. [Pg.352]

The addition of various surfactants and micelle forming agents on the biphasic hydroformylation of olefins was also considered as a tool for enhancement of the reaction rate. The relation between the extent of emulsification of the reaction mixture and the performance of hydroformylation reaction was also investigated. Mass transfer effects in biphasic hydroformylation of 1-octene in the presence of cetyltri-methylammoniumbromide (CTAB), was studied by Lekhal etal. [33], A mass-transfer model based on the Higbie s penetration theory was proposed to predict the rate of hydroformylation in a heterogeneous gas-liquid-liquid system under... [Pg.372]

It seems that models are still restricted because of various reasons (i) adsorption characteristics are related not only to the system conditions (i.e., solid types, concentrations and adsorbing species), but also to changes in the net system surface properties resulting from particle/particle interactions such as coagulation (ii) influences of organic ligands in the aqueous phase can rarely be predicted as yet (iii) effects of competition between various sorption sites, and (iv) reaction kinetics of the individual constituents cannot be evaluated in a mixture of sedimentary components. [Pg.89]

A second mechanism, the possible interaction of aldehydes with amino acids or peptides forming Schiff base reaction products, was also studied. Initial results (Hansen, A. P. Heinis J. J., North Carolina State University, Raleigh, unpublished data) showed a decrease in the aldehyde concentration when model systems containing various aldehydes and amino acids were heat processed. Losses ranging from 8 to 50% of various aldehydes have been observed in the pasteurization of aldehydes and amino acids mixtures in simulated milk ultrafiltrate. [Pg.331]

As was presented in Section III, chlorophyll a adducts with ethanol have been prepared that successfully mimic the optical and ESR properties of photosystem I reaction center chlorophyll. These chlorophyll a special pair systems are assembled from the two monomer units by cooling a mixture of chlorophyll a in the presence of water or toluene to 100 K. The formation of the desired structure depends not only on the chlorophyll a concentration, but also on the mole ratio of chlorophyll a to nucleophiles in solution, the solvent, the rate of cooling, etc. There is reason to suppose that mixtures of various species of poorly defined structure are present in even the best of these preparations. The uncertainties in composition and structure and the experimental problems and restrictions imposed by working at low temperature in organic glasses have limited the information that can be derived from such model systems. The solution to this problem is to provide a mode of physical attachment between two chlorophyll molecules so that the magnitude of the entropy of dimerization is lowered. [Pg.611]

Several studies on the reactivities of small radicals with donor-acceptor monomer pairs have been carried out to provide insight into the mechanism of copolymerizations of donor-acceptor pairs. Tirrell and coworkers " reported on the reaction of n-butyl radicals with mixtures of N-phcnylmalcimidc and various donor monomers e.g. S, 2-chloroethyl vinyl ether),. lenkins and coworkers have examined the reaction of t-butoxy radicals with mixtures of AN and VAc. Both groups have examined the S-AN system (see also Section 7.3.1.2). In each of these donor-acceptor systems only simple (one monomer) adducts are observed. Incorporation of monomers as pairs is not an important pathway i.e. the complex participation model is not applicable). Furthermore, the product mixtures can be predicted on the basis of what is observed in single monomer experiments. The reactivity of the individual monomers (towards initiating radicals) is unaffected by the presence of the other monomer i.e. the complex dissociation model is not applicable). Unless propagating species are shown to behave differently, these results suggest that neither the complex participation nor complex dissociation models apply in these systems. [Pg.353]

Industrial aromatic nitration, carried out heterogeneously with aqueous mixtures of nitric emd sulphuric acids as nitrating agent, is cui example of simultaneous mass transfer and chemical reaction, for the system forms two phases with the reactants distributed between them. For this type of system, either the chemical kinetics or the meuss transfer process may limit the overall rate, depending on the reaction conditions. It is not our intention here to discuss the various mathematical models... [Pg.235]


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See also in sourсe #XX -- [ Pg.515 , Pg.516 ]




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