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paraffin wax deposition and fouling

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— ALf1 —<br />

Equations L.7.4.3 <strong>and</strong> A7.6.2 were easily evaluated but<br />

couation A7.b.4 nau to be solved by iteration <strong>and</strong> numerical<br />

illtegraton.<br />

Simpson’ a rule was used for the integration where<br />

each interval was tacen in 10 steps. )her. was greater than 5<br />

<strong>and</strong> less or equal to 26, the first approximation for u was that<br />

of the previous distance y+_<br />

The iteration was considered<br />

completed when u changed by less than 0.001.<br />

The subroutine was tested by evaluating u at isothermal<br />

cOnc:ions.<br />

That is, the viscosity was cept constant in ;ne<br />

radial direction.<br />

The results are shown in Table .o.2.4 <strong>and</strong> plotted<br />

in fijre A8.2.4. At = 26 the subroutine gave u = 12.82 which<br />

is exactly what it should be according to Deissler. figure<br />

.o.2.4 snows tne nversa Velocity Pro:iie.<br />

It was coaparea<br />

wtn tne pro:lie given oy Deisser aa founa to concie.<br />

.‘.82.6 Calculation of Di:nsioniess Temperature<br />

Subroutine T?R0F calculated the dimensionless temperature<br />

T+ using the equations<br />

+<br />

(a) y ‘ 2o<br />

— dy<br />

— 1 2+÷r 2 ++<br />

÷nuy L1-exp(-n uy)J<br />

j<br />

..... (7.6.5)<br />

(b) y > 26<br />

= ]n + ..... (A7.5.3)<br />

yl<br />

Equation A7.6.3 was easily evaluated but equation A7,65<br />

had to be integrated nu;erically using Simpson’s.rule. The sa.<br />

mchod w.s used s for the evaluation of the dimensionless velocity,<br />

except no iteration was required.

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