This problem invoves an inner pipe with a constant wall temp, an annular space with conduction only, and an insulated outer pipe (no heat transfer)
I'm trying to solve the following Partial Differental Equation as my Governing Equation:
Initial Condition:
@ t = 0s, T = 573 K (uniformly distributed)
Boundary Conditions:
@ r = ri, T = 673 K (constant)
@ r = ro, dT/dr = 0 (insulated end)
This is my first time using pdepe, any help would be appreciated.
I'd like to be able to plot (Temperature vs time) for varying points between the inner and outer radii.

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Torsten
Torsten 2023년 5월 6일
편집: Torsten 2023년 5월 6일

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C.ri = 0.0125;
C.ro = 0.0375;
C.alpha = 1.905*10^-5;
C.Ti = 673;
C.T0 = 573;
r = linspace(C.ri,C.ro,50);
t = linspace(0,2000,2001);
m = 1;
eqn = @(r,t,T,dudx)heatcondPDE(r,t,T,dudx,C);
ic = @(r)heatcondPDE_IC(r,C);
bc = @(rl,Tl,rr,Tr,t)heatcondPDE_BC(rl,Tl,rr,Tr,t,C);
sol = pdepe(m,eqn,ic,bc,r,t);
T = sol(:,:,1);
plot(r,[T(1,:);T(5,:);T(10,:);T(20,:);T(30,:);T(40,:);T(80,:)])
grid on
function T0 = heatcondPDE_IC(r,C)
if r == C.ri
T0 = C.Ti;
else
T0 = C.T0;
end
end
function [c, f, s] = heatcondPDE(r,t,T,dudx,C)
c = 1;
f = C.alpha *dudx;
s = 0;
end
function [pl,ql,pr,qr] = heatcondPDE_BC(rl,Tl,rr,Tr,t,C)
pl = Tl - C.Ti;
ql = 0;
pr = 0;
qr = 1;
end

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2023년 5월 6일

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2023년 5월 6일

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