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principles of extraction and the extraction of semivolatile organics ...

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66 <strong>principles</strong> <strong>of</strong> <strong>extraction</strong><br />

In this instance, <strong>the</strong> value for D would be substituted for KD in equation<br />

(2.29).<br />

The formula for expressing repeated <strong>extraction</strong>s is<br />

% RX ¼ 1<br />

1<br />

1 þ KDðVE=VOÞ<br />

n<br />

100 ð2:32Þ<br />

Applying equation (2.32) to <strong>the</strong> previous calculation having three successive<br />

multiple <strong>extraction</strong>s where KD ¼ 5, VE ¼ 50 mL, VO ¼ 1 L, <strong>and</strong> n ¼ 3, <strong>the</strong><br />

cumulative recovery is calculated to be 48.8% (Table 2.4).<br />

Repeated <strong>extraction</strong>s may be required to recover <strong>the</strong> analyte su‰ciently<br />

from <strong>the</strong> aqueous phase. Neutral compounds can have substantial values <strong>of</strong><br />

KD. However, organic compounds that form hydrogen bonds with water,<br />

are partially soluble in water, or are ionogenic (weak acid or bases) may have<br />

lower distribution coe‰cients <strong>and</strong>/or pH-dependent distribution coe‰cients.<br />

Additionally, <strong>the</strong> sample matrix itself (i.e., blood, urine, or wastewater) may<br />

contain impurities that shift <strong>the</strong> value <strong>of</strong> <strong>the</strong> distribution coe‰cient relative<br />

to that observed in purified water.<br />

Investigation <strong>of</strong> <strong>the</strong> principle <strong>of</strong> repeated <strong>extraction</strong>s demonstrates that:<br />

The net amount <strong>of</strong> analyte extracted depends on <strong>the</strong> value <strong>of</strong> <strong>the</strong> distribution<br />

coe‰cient.<br />

The net amount <strong>of</strong> analyte extracted depends on <strong>the</strong> ratio <strong>of</strong> <strong>the</strong> volumes<br />

<strong>of</strong> <strong>the</strong> two phases used.<br />

More analyte is extracted with multiple portions <strong>of</strong> extracting solvent<br />

than with a single portion <strong>of</strong> an equivalent volume <strong>of</strong> <strong>the</strong> extracting<br />

phase.<br />

Recovery is independent <strong>of</strong> <strong>the</strong> concentration <strong>of</strong> <strong>the</strong> original aqueous<br />

sample.<br />

2.2.2. Methodology<br />

The LLE process can be accomplished by shaking <strong>the</strong> aqueous <strong>and</strong> organic<br />

phases toge<strong>the</strong>r in a separatory funnel (Figure 2.13a). Following mixing, <strong>the</strong><br />

layers are allowed to separate. Flow from <strong>the</strong> bottom <strong>of</strong> <strong>the</strong> separatory funnel<br />

is controlled by a glass or Teflon stopcock <strong>and</strong> <strong>the</strong> top <strong>of</strong> <strong>the</strong> separatory<br />

funnel is sealed with a stopper. The stopper <strong>and</strong> stopcock must fit tightly<br />

<strong>and</strong> be leakpro<strong>of</strong>. Commonly, separatory funnels are globe, pear, or cylindrically<br />

shaped. They may be shaken mechanically, but are <strong>of</strong>ten shaken<br />

manually.<br />

With <strong>the</strong> stopcock closed, both phases are added to <strong>the</strong> separatory funnel.<br />

The stopper is added, <strong>and</strong> <strong>the</strong> funnel is inverted without shaking. The stop-

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