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Frans_M_Everaerts_Isotachophoresis_378342.pdf

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92 CHOICE OF ELECTROLYTE SYSTEMS<br />

In the pH* measurements carried out in the work described in this chapter, the same<br />

procedure was used as described by De Ligny et al. Standard buffer solutions and pH*<br />

values used were as determined De Ligny et al.<br />

Determination of pK values in methanolic solutions<br />

The determinations of pK values [13] can be carried out in several ways, the most<br />

important of which are the conductivity, electrometric, spectrometric and colorimetric<br />

methods. In this section, the electrometric method is discussed,<br />

Rorabacher et al. [14] gave some definitions relating to the pK. The activity<br />

equilibrium constant is defined as<br />

The equilibrium constant based on concentrations is<br />

K,* = [HI [A1 /[HA1<br />

and the mixed-mode equilibrium constant is defined as<br />

K$ = a$ [A] /[HA] or K z = K:rfi<br />

Hence<br />

In the electrometric method, the concept of the half neutralization point (HNP) is<br />

used. The HNF’ is the point in the acid-base titration at which half of the amount of<br />

acid (or base) present has been neutralized. According to eqn. 5.1 1 , this means that the<br />

pK; is determined. The thermodynamic equilibrium constant can be calculated from<br />

the mixed-mode constant by correcting for the activity coefficients (eqn. 5.20).<br />

(5.17)<br />

(5.18)<br />

(5.19)<br />

Ex penmen tal values<br />

In order to choose an optimum electrolyte system in isotachophoresis, the pK values<br />

of the buffers and the pK values of the sample ionic species must be known. Some<br />

pKk values for anionic species and bases have been determined in 95% methanol by<br />

the electrometric method and the results are given in Table 5.6.<br />

5.3. CHOICE OF THE BUFFERING COUNTER IONIC SPECIES<br />

(5.20)<br />

With regard to the choice of the buffering counter ionic species, three important<br />

points can be distinguished. Firstly, the buffering counter ions act as a counter ion by<br />

which the principle of electroneutrality is obeyed. At the same time, the counter ionic<br />

species can be used to form complexes with the sample ionic species in order to affect<br />

the effective mobility of these ionic species in a favourable manner, particularly if the<br />

ionic species to be separated have similar mobilities. Even buffering counter ionic species<br />

with which particular sample ionic species do not migrate or are precipitated can be<br />

chosen; by this they do not disturb the separation procedure. Deman [ 11 used this

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