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Numerical Analysis of Defects Caused by Thermolysis in an Infinite ...

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A.B. Cumel <strong>an</strong>d E.H. Twizell<br />

BOILING CRITERION: NUMERICAL RESULTS<br />

The vapour pressure at the base time level til is given <strong>by</strong><br />

P:' = exp[-Lllij(RT") + a] (21)<br />

(Ev<strong>an</strong>s et al. 1991), <strong>in</strong> which Tn is the temperature at time tn, <strong>an</strong>d this is<br />

updated at time t<br />

ll<br />

+ 1<br />

<strong>by</strong> the relation<br />

Where<br />

(22)<br />

V m<br />

= Cpp~+1 /[Cpv;'+1 + (1 - Cp)W+ 1 ]<br />

<strong>in</strong> which<br />

V;1+! = 0.001098[1 + 0.0009774 {en + 1)1 + 100}]<br />

V;+I = 0.0009595[1 + 0.0004985 {en + 1)1+ 49}]<br />

<strong>an</strong>d<br />

(23)<br />

(24)<br />

(25)<br />

(26)<br />

(Matar et al. 1993).<br />

A bubble forms when the vapour pre sure exceeds the atmospheric pressure.<br />

A plot <strong>of</strong> vapour pressure aga<strong>in</strong>st temperature computed us<strong>in</strong>g the procedure<br />

described above with the data given <strong>in</strong> Table 1 is depicted <strong>in</strong> Fig 1. Unfortunately,<br />

no closed-form solution <strong>of</strong> the problem (9, 1-4) is available aga<strong>in</strong>st which the<br />

TABLE 1<br />

Parameter values used for computation<br />

Parameter value Vit<br />

a 22.255<br />

0.5<br />

0.005<br />

0.000692<br />

222000<br />

38940<br />

1.67 3 10 16<br />

99<br />

8.3143<br />

0.5<br />

1075<br />

0.361<br />

Pa<br />

m<br />

m 2 s- 1<br />

J mol-I<br />

J mol-I<br />

S-I<br />

J mol-'K-'<br />

dimensionless<br />

kg m- 3<br />

dimensionless<br />

20 Pert<strong>an</strong>ikaJ. Sci. & Techno\. Vol. 7 No.1, 1999

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