of metal ions. The greater 2"!Am extraction by the HNO 3-Na0H system in the
alkaline pH range is a reflection of the fact that NaOH is a more effective
extractant of soil organic matter than NH,OH.
After the removal of organic matter, the effectiveness of the CH3COOH-NH,,OH
system in extracting 24lam increased. Apparently, the stability constant of

some “*lam-soil organic matter complexes were greater than that of 7"!am-acetate

Treatment 1

Control

complex.

T

100;

Dose icpmt.

PERCENT OF DOSE EXTRACTABLE

A
8

TT

Distribution Coefficients.
It is well recognized that sorption and extractability are inseparably interrelated. This relationship is usually expressed
by distribution coefficients (K,), i.e., the ratio of activities in the solid
phase to that in the liquid phase. Since our emphasis here has been the
extractability rather than the sorption, the distribution coefficients presented
(Table 2) are defined as the ratio of the activities in the liquid phase to
that in the solid phase, t.e.,

T

Bo- - ---© CH3COOH - NH AOH System

YT

A e——-—* HNO,-Na0H System

28, 650 + 963
30,805 + 3063

»
TTT TT

100r

Treatment T

F

Et

K, 7 (A/a) (w/v)
where A; = equilibrium activity in the solution phase, A_ = equilibrium activity
in the solid phase, m = mass in grams, and v = volume of solution in milliliters.
The K, values (Table 2) reflect,the curves shown in Figs. 1 and 2. With the
HNO,-NaoH system, the minimum K, value occurred at pH 7.58, whereas it was at
pH 10.20 with the CH3COOH-NHAOH system. The occurrence of the minimum extraction at the higher pH level by the latter system was considered to be due to
the lower effectiveness of NH,OH compared to NaOH in extracting soil organic

Treatment TV

matter.
g

L

100;

on

~~

“A

ON

‘

x

h.

>>

~~,

TTT
Treatment I

:

GENERAL DISCUSSION

Treatment Y
The results provide several implications on the possible behavior of Am in
soils. In a kaolinitic soil containing appreciable amounts of organic matter,
Am is likely to move fairly readily by the leaching action of water under
strongly acidic (pH < 3) or alkaline (pH > 8) condition.
In the intermediate
pH range (pH 3-8), the movement of Am is expected to be low, but it is likely
to be higher on the alkaline side due to the solubilization of alkali~soluble
organic matter. With the addition of a relatively weak complexing agent such
as the CH,COO ions, the movement is likely to be appreciably increased in the
acidic side, but not necessarily in the alkaline side of the pH range. Our
unpublished results of the extraction of 239Pu have shown that complexing
action of CH3;COO ions is very weak compared to citrate, tartrate, or oxalate
fons.
In view of this, the addition of a strong complexing or chelating agent
probably will increase the Am movement on the alkaline side of the pH range as
well. This, however, remains to be determined.

Fig. 3.

Relative effect of extracting systems on the extractability
of 24am from contaminated Aiken clay loam chemically treated
to remove various components

In a kaolinitic soil, which is devoid or very low in organic matter content,
Am is likely to move quite readily under strongly acidic condition (pH < 4),
but only slightly under alkaline condition (pH > 7).
In the intermediate pH

89

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