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od of calibrating that could be used in the field<br />

in the absence of the rotating arm apparatus.<br />

In quiescent solutions or solutions with very<br />

low forced convection rates, the density difference<br />

between the (saturated) liquid-solid interface<br />

and the bulk solution drives a convection<br />

current which is the principal mechanism<br />

that moves solution away from the solid. The<br />

natural and forced convection terms are in<br />

general not directly additive (Pei 1965; Churchill<br />

1977) in determining total convection or<br />

the dissolution rates.<br />

We suspended clod cards in quiescent solutions<br />

in ice chests under constant temperature<br />

conditions indoors. The ice chests supported<br />

dissolution rates roughly following Eq.<br />

4 over 4-6 d (Fig. 11A); Fig. 11 B correlates<br />

the natural convection ice-chest data. The<br />

equation fitting the data is<br />

[ 1 - ( W,lWi)1’3]/8<br />

= 2.81 ($)[(&)(+L.,,] 1.25 (10)<br />

with r = 0.994.<br />

Equations 8 and 10 can be combined to<br />

give an expression that will allow an equivalent<br />

integrated velocity to be determined from<br />

data obtained in the field. The group Sn =<br />

[ 1 - (~~ Wi)“]lB is obtained in natural convection<br />

clod card tests with water from the<br />

field test site. Weight loss data from cards exposed<br />

to water motion in the field is reduced<br />

to a corresponding form:<br />

Then the integrated<br />

calculated as<br />

Sf = [ 1 - ( Wr/ Wi)“]/8-<br />

water speed in the field is<br />

I/= 4.31(5=(y). (11)<br />

S’.25/Sn is similar to DF (Doty 197 1) but should<br />

be superior as an indicator of water motion in<br />

that it corrects for the effects of decreasing surface<br />

area during the tests and the greater effect<br />

of forced convection in producing dissolution<br />

relative to free convection (the 1.25 exponent<br />

for S&<br />

If field tests are conducted in water with lim-<br />

12<br />

'; 0.03<br />

0<br />

3<br />

?<br />

-y 0.02<br />

c<br />

r'<br />

Y<br />

C<br />

a ~0~/6.,25~C,n=Z<br />

. 25 3.. 16.5-C<br />

Time, d<br />

0.04<br />

, 0 Tap<br />

0 20 '/..<br />

0.01<br />

0.01<br />

0.02<br />

(T/T~~)&/P) AC250 mol Ihr-'<br />

A .<br />

Fig. 11. Free convection data obtained by suspending<br />

clod cards in large volumes of quiescent solutions in ice<br />

chests (A), and (B) correlation of the data using Eq. 8 at<br />

T,, = 298°K (25°C).<br />

ited motion, say V < 2 cm s-l, Eq. 11 will<br />

give erroneous results because free convection<br />

forces can also produce dissolution in the field.<br />

If it is necessary to separate the forced and free<br />

convection effects, multiply the right-hand side<br />

of Eq. 11 by [ 1 - (SJSf)3]5/12. This is a rough<br />

correction derived from Churchill (1977) for<br />

heat transfer with assisting forced and free convection.<br />

Many of the applications for clod cards involve<br />

measurement of unsteady flow, ranging<br />

from wind waves to oscillatory tidal currents.<br />

The methods presented here will indicate an<br />

integrated average speed near the scalar arithmetic<br />

mean velocity of the water because<br />

[ 1 - ( Wj &)“I/8 is nearly linear with velocity<br />

(actually Ve8). For example, if the water velocity<br />

over the card varies linearly from V, at<br />

time zero to V, at time 8, Eq. 1 and 2 can be<br />

used with the mass transfer coefficient from<br />

Eq. 8 to derive the expression<br />

0.03

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