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Frans_M_Everaerts_Isotachophoresis_378342.pdf

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Chapter 8<br />

Introduction<br />

SUMMARY<br />

In ths chapter some practical information is given on the Section Applications, and a<br />

scheme is given for ‘trouble-shooting’.<br />

8. INTRODUCTION<br />

The Section Applications contains almost all of the practical information about<br />

isotachophoretic separations in narrow-bore tubes. In this section, applications and results<br />

are given for separations classified according to chemical compounds that belong to clearly<br />

distinguishable classes.<br />

The separations were carried out in so-called operational systems in which the electro-<br />

lytes were shown to give optimal results. The operational systems are listed in tables, in<br />

order to make a comparison between them possible. The systems listed were chosen<br />

somewhat arbitrarily; many more possibilities could be given. Also, the separations con-<br />

sidered were mainly chosen arbitrarily: many real problems from industry or hospitals<br />

proved to be much simpler. The separations are shown in order to indicate their possi-<br />

bilities and to make patterns recognizable.<br />

When a specific operational system is chosen, one always has to bear in mind that the<br />

pH in anionic separations by isotachophoresis tends to increase, while in cationic separa-<br />

tions it tends to decrease, going from the leading zone towards the terminating zone.<br />

Therefore, the pH must always be chosen such that the optimal effect of the buffering<br />

counter ion is used. In some instances a buffering counter ion is not necessary, while in<br />

other instances two or more counter ions with overlapping buffer regions are needed.<br />

A difference of 0.5 pH unit can give an operational system that has completely<br />

different characteristics for a specific analytical problem, as shown in the following<br />

example.<br />

If a separation of anions is sought and the operational system at pH 6 (Table 12.1) is<br />

found to be suitable, one can adjust the pH of the leading electrolyte from its initial<br />

value of 6; the buffering capacity of histidine is sufficient until a pH of ca. 7. If, however,<br />

an anion is present with a very low effective mobility, which needs a terminator with an<br />

even lower effective mobility than the anion to be separated, it may be preferable to<br />

adjust the pH of the leading electrolyte to 5.5. If the pH of the leading’electrolyte is<br />

decreased too much, sometimes difficulties can arise because too few counter ions are<br />

present and the buffering capacity may not be sufficient (see Fig.9.5). Experimentally, we<br />

found it best to adjust the pH of the leading electrolyte, with the chosen counter ion, to<br />

the selected value as accurately as possible and to check the pH of the solution again the<br />

following day. In most instances the pH is shifted (kO.1-0.2 pH unit).<br />

Step heights listed in the various tables are proportional to the effective mobilities of<br />

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