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Handbook of Size Exclusion Chromatography and Related ...

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widely used also for the semiquantitative characterization <strong>of</strong> eluent strength<br />

towardsilicagel<strong>and</strong>other polarcolumnpackings.Snyderproposedtoexpressthe<br />

solvent strength for binary eluents AB, 1 0 AB as<br />

1 0 AB ¼10 A<br />

þ log NB<br />

anB<br />

where 1 0 A issolvent strength <strong>of</strong> the weaker eluent component, A, NB is mole<br />

fraction <strong>of</strong> the stronger component B, <strong>and</strong> nB is the effective molecular area <strong>of</strong> an<br />

adsorbed molecule B. The adsorbent surface activity function, a, is defined as<br />

(4)<br />

log K 0 ¼log Va þaf(X,S) (5)<br />

whereK 0 issample adsorption distribution coefficient (milliliters pergram), Va is<br />

the volume <strong>of</strong> an adsorbed solvent monolayer per unit weight <strong>of</strong> adsorbent, <strong>and</strong><br />

f(X,S) is afunction describing properties <strong>of</strong> sample X <strong>and</strong> solvent S. The<br />

simplified Eq. (4) holds for A plus B mixed eluents with not very low<br />

concentration <strong>of</strong> the stronger component B. The role <strong>of</strong> molecular interactions<br />

between A<strong>and</strong> Bsolvents is not considered.<br />

Solubility <strong>of</strong> analytes plays an important role not only in phase separation<br />

but also in partition-based HPLC <strong>of</strong> macromolecules. Thermodynamic quality<br />

<strong>of</strong> the eluent allows controlling <strong>of</strong> both phase separation <strong>and</strong> enthalpic partition<br />

polymer retention mechanisms <strong>and</strong> to some extent it may also influence polymer<br />

adorption. The thermodynamic quality <strong>of</strong> asolvent for apolymer is expressed by<br />

the Flory–Huggins interaction parameter x (6) or by the exponent in the<br />

Staudinger–Mark–Houwink–Sakurada viscosity law<br />

[h] ¼KvM a<br />

where [h] is the limiting viscosity number <strong>of</strong> linear macromolecules with molar<br />

mass M (in practice, molar mass <strong>of</strong> the species that is most abundant in the<br />

sample), <strong>and</strong> a<strong>and</strong> Kv are constants for agiven polymer–solvent system. [h]<br />

reflects the volume <strong>of</strong> polymer coils in the infinitively diluted solution. In<br />

thermodynamically good solvents, [h] values little depend on temperature (Fig.<br />

10) while theyrapidly change at thevicinity<strong>of</strong> the theta point. The product <strong>of</strong> [h]<br />

<strong>and</strong> M is the hydrodynamic volume <strong>of</strong> polymer coils <strong>and</strong> represents a base for the<br />

famous Benoit’s SEC “universal calibration dependence” (51), which is a plot <strong>of</strong><br />

log[h]M vs. VR for appropriate polymer st<strong>and</strong>ards (largely polystyrenes). In the<br />

absence <strong>of</strong> enthalpic interactions (1 0) universal calibration plots for a particular<br />

SEC column coincide for different coiled polymer species in different eluents.<br />

For many linear macromolecules, exponent a in Eq. (6) assumes values from<br />

0.5 (for theta solvents) up to 0.7–0.8 (for thermodynamically good solvents).<br />

Both x <strong>and</strong> a values for numerous polymer–solvent systems are collected,<br />

for example, in Polymer <strong>H<strong>and</strong>book</strong> (52).<br />

© 2004 by Marcel Dekker, Inc.<br />

(6)

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