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chemical physics of discharges - Argonne National Laboratory

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532<br />

and can be expressed in terms <strong>of</strong> Equation 8 to give<br />

Therefore<br />

[Bl =I?)<br />

[BH+]lI2<br />

I<br />

!<br />

I<br />

i<br />

(16) ' I<br />

Thus, for a given concentration [BH'] in the aqueous extract, the concentra- ~<br />

tion [B] <strong>of</strong> base is high for bases <strong>of</strong> low base strength (Kb).<br />

From Equations 12 and 17, the following generalizations can be<br />

made concerning the selection <strong>of</strong> an acid and.a base for recovery <strong>of</strong> nitrogen<br />

i<br />

bases by a regenerative process. To get good extraction, maximize [BH+) by<br />

using an acid with as large a value for Ka as is possible, consistent with<br />

other requirements <strong>of</strong> the process. To get good regeneration, maximize [B]<br />

(a base with a small Kb value should be involved).<br />

i<br />

Accordingly, suitabie systems appear to involve an acid extractant<br />

with a large 1<br />

Ka value and a nitrogen base with a small Kb value. Consistent;<br />

with the above, the ApK was examined as a useful guide in selecting compo.-<br />

1<br />

nents 'for regenerative systems, . ,<br />

where<br />

pK = -log K (19) 1<br />

ApK = (pKb -pKa) , and (20)<br />

ApK is expressed as the absolute value <strong>of</strong> (PKb - pKa). It is<br />

anticipated that the larger the ApK <strong>of</strong> a system, the better it w ill function!<br />

in a regenerative recovery process. Therefore it appears that recovery <strong>of</strong><br />

nitrogen bases is facilitated by combinations <strong>of</strong> relatively weak bases and<br />

relatively strong acids or relatively strong bases and weak acids. /<br />

\<br />

Systems for Recovery <strong>of</strong> Ammonia and Pyridine Bases<br />

\<br />

As mentioned above, several processes have previously been<br />

reported for recovery <strong>of</strong> ammonia and pyridine bases from coke-oven product<br />

streams. The data on ammonia and pyridine are consistent with the discussiol<br />

presented above, Tables I and 11. Experimentally it has been demonstrated I<br />

that, although ammonia can be recovered in a regenerative manner using<br />

'q<br />

monoammonium phosphate, neither phosphoric acid nor sulfuric acid can be<br />

(<br />

used (H2PO4- is suitable for NH3 recovery, whereas H3PO4, HS04-, and H2S04<br />

are not applicable). '.<br />

\<br />

It has also been shown that pyridine can be recovered successfull<br />

with either HjPOl or HSOq-; however, neither H2P04- nor H2S04 can be '6<br />

employed.<br />

i<br />

1<br />

k

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