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Essentials of Computational Chemistry

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416 11 IMPLICIT MODELS FOR CONDENSED PHASES<br />

clear when such situations will arise, and modeling must simply be carried out with great<br />

care to ensure that the possibility is not overlooked.<br />

11.4.2 Partitioning<br />

The free energy <strong>of</strong> solvation may be regarded as the quantity describing the partitioning <strong>of</strong><br />

a solute between the gas phase and a particular solvent. However, one is <strong>of</strong>ten interested in<br />

the free energy associated with the partitioning <strong>of</strong> a solute between two different condensed<br />

phases. Continuum solvent models may still conveniently be used to predict such partitioning<br />

behavior, based on the procedure outlined in Figure 11.11. The validity <strong>of</strong> the thermodynamic<br />

cycle is secure as drawn; however, under certain experimental conditions, the cycle is not<br />

representative <strong>of</strong> the experiment and the performance <strong>of</strong> the model may thus be degraded.<br />

For instance, the two solvents may be immiscible in a bulk sense, so the experiment may<br />

be carried out simply by dissolving a solute into a container holding both solvents, shaking<br />

the system until equilibrium is reached, and then measuring the solute concentration in the<br />

two phases. However, in spite <strong>of</strong> the phases being immiscible in bulk, the small percentages<br />

<strong>of</strong> each solvent that dissolve into the other may significantly affect the bulk’s ability to<br />

solvate the solute in question. The continuum model, on the other hand, necessarily assumes<br />

a homogeneous ‘pure’ medium.<br />

One major motivation for studying partitioning behavior has been a desire to understand<br />

the fashion in which drug molecules pass through largely non-polar (lipid) biomembranes<br />

that separate largely aqueous biocompartments. Historically, the octanol/water partition<br />

coefficient has been useful in this regard, as have some others. Such partition coefficients<br />

are usually not expressed as free energies <strong>of</strong> transfer, but as the logarithm <strong>of</strong> the associated<br />

equilibrium constant P . From a modeling perspective, using the formalism embodied in<br />

Figure 11.11, one computes<br />

log PA/B =− Go SA − Go SB<br />

2.303RT<br />

(11.30)<br />

where A and B are the solvents <strong>of</strong> interest and the two terms in the numerator are the free<br />

energies <strong>of</strong> transfer from the gas phase into solvent A and solvent B, respectively.<br />

The similar accuracies <strong>of</strong> different well-parameterized continuum models implies that they<br />

will also perform similarly for the computation <strong>of</strong> partition coefficients, and that has proven<br />

to be the case in most studies to date (see, for example, Bordner, Cavasotto, and Abagyan<br />

2002 and Curutchet et al. 2003b). In Table 11.4 the previously presented SMx results for the<br />

chlor<strong>of</strong>orm/water partitioning <strong>of</strong> the methylated canonical nucleic acid bases are compared to<br />

results from the MST-ST/HF/6-31G* method, and also to purely electrostatic results obtained<br />

using a multipole expansion SCRF method. As the latter does not include any accounting for<br />

non-electrostatic effects, its performance is significantly degraded compared to the other two.<br />

11.4.3 Non-isotropic Media<br />

All <strong>of</strong> the continua discussed thus far have been isotropic in nature. An interesting question<br />

arises as to the ability <strong>of</strong> the continuum approximation to model non-isotropic media. In

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