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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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492 Jacopo Tomasi, Benedetta Mennucci, Chiara Cappelli<br />

Shear viscosity<br />

To end this section, we would like to report an example <strong>of</strong> calculation <strong>of</strong> the shear viscosity<br />

again taking as an example pure acetone.<br />

The viscosity can be computed by using molecular dynamics simulations from the<br />

virial form <strong>of</strong> the molecular pressure tensor P, which can be represented as a sum <strong>of</strong> four<br />

contributions:<br />

N pp i i<br />

PV = + PV S + PRV+ PV C<br />

m<br />

∑ 1<br />

i=<br />

i<br />

[8.142]<br />

where V is the volume <strong>of</strong> the cell, N the number <strong>of</strong> molecules, pi and mi the momentum and<br />

mass <strong>of</strong> molecule i.<br />

The first term in eq. [8.142] is the kinetic contribution, while PS is the short-range potential<br />

interaction contribution, PR the reciprocal-space portion <strong>of</strong> the pressure tensor, and<br />

PC a correction tensor term.<br />

From the xy elements <strong>of</strong> the time-averaged molecular pressure tensor [8.142] and the<br />

applied shear (or strain) rate γ = ∂vx / ∂y,<br />

the viscosityηcan be computed using the constitutive<br />

relation:<br />

η =−<br />

Pxy −Pyx<br />

2γ<br />

[8.143]<br />

the calculated values for acetone (extrapolated data) are in reasonable agreement with experimental<br />

data, as well as results for acetone/methanol and acetone/water mixtures. 117<br />

8.9 LIQUID SURFACES<br />

Until now our task has been relatively easy, as we have only considered the general methodological<br />

aspects <strong>of</strong> the computational description <strong>of</strong> liquids.<br />

To proceed further, we have to be more specific, entering into details <strong>of</strong> specific problems,<br />

all requiring the introduction and the characterization <strong>of</strong> different properties, and <strong>of</strong><br />

the opportune methodological (computational) tools to treat them. We also note that, as additional<br />

complication, it can happen that things change considerably when the full range <strong>of</strong><br />

macroscopic variables (temperature, pressure, volume) is considered, and when other components<br />

are added to the liquid system.<br />

Not much effort is needed to convince readers <strong>of</strong> the overwhelming complexity <strong>of</strong> the<br />

task we are here considering. Let us take a simple pure liquid: to span the range <strong>of</strong> the<br />

thermodynamical variables means to consider systems in which the liquid is in presence <strong>of</strong><br />

the solid, <strong>of</strong> the vapor, including supercritical as well as super-cooled states, and all the related<br />

phenomena, as ebullition, vaporization, condensation and freezing.<br />

All states and all dynamical processes connecting states are <strong>of</strong> interest for chemistry,<br />

chemical engineering, and physical chemistry. Some properties can be defined for all the<br />

states (such as the thermodynamic basic quantities); others are specific for some situations,<br />

such as the surface tension. But also for properties <strong>of</strong> general definition, the techniques to<br />

use have <strong>of</strong>ten to be very different. It is not possible, for example, to use the same technique

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