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

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umerical <strong>Analysis</strong> <strong>of</strong> <strong>Defects</strong> <strong>Caused</strong> <strong>by</strong> <strong>Thermolysis</strong><br />

value <strong>of</strong> a variable is <strong>of</strong>ten referred to <strong>by</strong> numerical <strong>an</strong>alysts as the frozen value<br />

<strong>of</strong> the variable. Clearly, symmetry requires this PDE to be solved only <strong>in</strong> the<br />

half <strong>in</strong>terval °::; r::; B. This, <strong>in</strong> turn, imposes the flux boundary condition<br />

dC(O,t) = ° t > °.r = °<br />

dr ' ,<br />

(2)<br />

on the axis <strong>of</strong> the cyl<strong>in</strong>der <strong>an</strong>d the assumption <strong>of</strong> zero concentration on the<br />

surface gives rise to the boundary condition<br />

c(B, T) = 0, t > ° (3)<br />

Initially it will be assumed that the concentration throughout the cyl<strong>in</strong>der is c*<br />

;;f. 0, giv<strong>in</strong>g rise to the <strong>in</strong>titial condition<br />

c(r,O) = C*, 0::; r::; B (4)<br />

Note, there is a discont<strong>in</strong>uity between <strong>in</strong>itial <strong>an</strong>d boundry conditions.<br />

In (l), Q is the rate <strong>of</strong> production <strong>of</strong> monomer caused <strong>by</strong> pyrolysis based<br />

on the total volume <strong>of</strong> ceramic-powder suspension <strong>an</strong>d is given <strong>by</strong><br />

Q. = K exp [-E/(RT)] p (1 - V)H<br />

ope<br />

(5)<br />

(Ev<strong>an</strong>s et al. 1991), where H is the mass fraction <strong>of</strong> polymer rema<strong>in</strong><strong>in</strong>g after a<br />

given absolute temperature is reached <strong>an</strong>d is given <strong>by</strong><br />

KoRT2exP[-E/(RT)]{ 2RT 6(RT 2 )}]<br />

H = exp<br />

[<br />

ZE 1 - -E- + --'--E-'2,.-------'- (6)<br />

The parameters <strong>in</strong> (5) <strong>an</strong>d (6) are described <strong>in</strong> the nomenclature. Clearly, Q,<br />

which is a function <strong>of</strong> T, is not const<strong>an</strong>t but at a given time t its (frozen) value<br />

at that time will be used <strong>in</strong> the algorithm.<br />

The PDE (l) c<strong>an</strong>not be solved on the axis <strong>of</strong> the cyl<strong>in</strong>der (r=O). Us<strong>in</strong>g the<br />

boundary condition (2) <strong>in</strong> the Maclaur<strong>in</strong> exp<strong>an</strong>sion<br />

dc(r,t) dC(O,t) d 2 C(0,t) r 2 d 3 C(0,t)<br />

---=---+ +- + ...<br />

dr dr dr 2 2 dr 3<br />

(7)<br />

it<br />

is easily seen that<br />

lim 1 dc(r,t)<br />

r~O ~~<br />

(8)<br />

=<br />

Pert<strong>an</strong>ikaJ. Sci. & Techno!. Vo!. 7 No.1, 1999 15

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