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Interactions in the liquid phase

Complexation has a significant influence on dissolution and precipitation of minerals as already described in chapter 1.1.4.1.3. In contrast to the dissolution of minerals, complexation is a homogeneous reaction. It can be described by the mass-action law. The complexation constant, K, gives information about the complex stability. Large complex constants indicate a strong tendency for complexation, or high complex stability. [Pg.34]

From the periodic table of elements the following elements can be possible ligands  [Pg.34]

Beside these inorganic ligands there are also organic ligands like humic or fulvic acids, which occur naturally in almost all waters, but also NTA and EDTA, which enter the hydrosphere as phosphate substitutes in detergents (Bernhardt et al. 1984) and can mobilize metals. [Pg.34]

The complex binding can be electrostatic, covalent, or a combination of both. Electrostatically bound complexes, where the metal atom and the ligand are separated by one or more hydrogen molecules, are called outer-sphere complexes. They are less stable and are formed when hard cations come into contact with hard ligands (Table 10). [Pg.34]

The Pearson concept of hard and soft acids and bases considers the number of electrons in the outer shell. Elements with a saturated outer shell and low tendency for polarization (noble gas configuration) are called hard acids, while elements with only partially filled outer shell, low electronegativity, and high tendency for polarization are soft acids. [Pg.34]


The ideal solubility equation (Eq. 2) is the simplest form of model that is applicable to solvent based crystallization process design. Even though the equation excludes non-ideal interactions in the liquid phase, it is still a useful tool in certain circumstances. [Pg.52]

Solvent extraction processes usually run at ambient pressures and temperatures. If higher pressures are applied, it is mostly because a higher extraction temperature is required when equilibrium or mass transfer conditions are more favorable at an elevated temperature. Distillation, on the other hand, is usually carried out at higher temperatures and ambient pressures. To avoid thermal degradation, the pressure sometimes has to be lowered below ambient pressure. Distillation is based on the differences in vapor pressures of the components to be separated, whereas solvent extraction utilizes the differences in intermolecular interactions in the liquid phase. [Pg.447]

An interesting case of SB is presented by enantiomer formation. In recent papers [15] it was shown that enantiomers can be presented as the low symmetry, PJT distorted configurations of a hypothetical high-symmetry structure, and as such their interaction in the liquid phase via collisions under special conditions may lead to some kind of cooperativity and phase transition (SB) resulting in singleenantiomer broken symmetry configuration. [Pg.13]

In this chapter we will first discuss coherent anti-Stokes Raman scattering (CARS) of simple liquids and binary mixtures for the determination of vibrational dephasing and correlation times. The time constants represent detailed information on the intermolecular interactions in the liquid phase. In the second section we consider strongly associated liquids and summarize the results of time-resolved IR spectroscopy (see, e.g., Ref. 17) on the dynamics of monomeric and associated alcohols as well as isotopic water mixtures. [Pg.16]

The hrst interest is to obtain from the information in the gas phase results that are representative of the species present in the liquid phase. However, transposition of the results has to be done with many caution. The forces responsible for the molecular interactions in the liquid phase are not the same as those in the gas phase. Indeed, the main interactions acting in solution result from van der Waals forces, hydrophobic forces and hydrogen bonding. In the gas phase, electrostatic forces are predominant. Even if a great number demonstrate that complexes in the gas phase reflect the properties in the liquid phase, no generalization can be made. Each case is unique. Several controls have to be performed in order to confirm that the gas-phase observations are related to the liquid-phase behaviour [128,129]. [Pg.336]

While most of the mentioned (fluoromethyl)silanes are stable compounds at ambient temperature, the partially Si-chlorinated silanes F2HCSiH2Cl and FClHCSiH Cl3. , n = 1, 2, are dangerously shock-sensitive. In line with intermolecular interaction in the liquid phase of these compounds is a large phase... [Pg.23]

Margitfalvi, J.L. Hegediis, M. Tfirst, E. Enantio-selective hydrogenation of a-keto esters over cinchona-Pt/Al203 catalyst. Kinetic evidence for the substrate-modifier interaction in the liquid phase. Tetrahedron Asymm. 1996, 7, 571-580. [Pg.1335]

An enhancement of the regioselectivity was observed when the catalyst modifier concentration was increased (Figure 3). The enhancement might be caused by 1) the modifier-reactant interaction in the liquid-phase, 2) the modifier-reactant interaction on the catalyst surface, 3) the coverage dependent adsorption modes of the reactant and modifier or a combination of factors 1-3. [Pg.363]

Nonideal Solutions, The final level of complexity for modeling the relationship between vapor and liquid compositions accounts for nonideal interactions in the liquid phase. The equilibrium ratio is still ased for such systems, but in this instance it is defined as... [Pg.10]

Given the precision of the data, the correlation between the low- and high-density values of is quite good. For some mixtimes, however, the liquid-phase values are markedly smaller than those obtained from the gas. These are typically systems such as HgS + QH4 for which a specific acid-base interaction in the liquid phase might be expected. Generally speaking, however, gas-phase determinations of i provide valuable information for the prediction and correlation of the properties of liquid mixtures. [Pg.221]

This model is highly empirical in nature and the two interrelated polarizability descriptors (section 1.2.2) can be only vaguely related to dispersive interactions in the liquid phase. The estimates for the respective monofunctional compounds are generally within 5-10% of the experimental data, but larger deviations occur for polyfunctional substances. For a set of heterogeneous compounds, a mean method error of 21% (°C) has been reported (Lynch et a/., 1991). Significant outliers comprise (lUCT, 1992) ... [Pg.106]

The theoretical analysis of experimentally observed VPIE data has furnished information, among others, (1) about the details of the intermolecular interactions in the liquid phase, (2) on the vibrational coupling between internal vibrations and molecular translations and/or rotations, which occurs in the condensed phase, (3) on the density dependence of the force constants, which govern the external molecular motions and internal vibrations in the liquid, (4) on changes in vibrational anharmonicity, which occur on condensation, as well as (5) on the magnitude of the dielectric correction to IR absorption peaks in condensed phases. [Pg.711]

A good understanding of chemistry is obviously one of the underpinnings of CRE. This is particularly so in certain areas. PTC is one such area where the role of the catalysts used and ionic interactions in the liquid phases are important considerations. It is worth remembering that PTC always involves at least one liquid phase. These facts will become evident as we proceed further in this chapter. For a deeper understanding of the more chemistry-based areas of CRE, reference to the book Organic Synthesis Engineering (Doraiswamy, 2001) is recommended. [Pg.475]

All relevant thermodynamic and phase diagram data in the CaO-FetO-CaF2 system were critically reviewed. One set of model parameters describing the Gibbs energy of all phases has been obtained as a result of critical evaluation of the available data and optimization of the model parameters. The Modified Quasichemical Model was used to describe the interactions in the liquid phase. All calculations were performed using the FactSage thermochemical software. [Pg.425]


See other pages where Interactions in the liquid phase is mentioned: [Pg.49]    [Pg.425]    [Pg.32]    [Pg.49]    [Pg.52]    [Pg.58]    [Pg.139]    [Pg.220]    [Pg.134]    [Pg.162]    [Pg.34]    [Pg.560]    [Pg.23]    [Pg.161]    [Pg.265]    [Pg.360]    [Pg.363]    [Pg.351]    [Pg.44]    [Pg.40]    [Pg.249]   


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