ode45 code runs indefinitely

I used this code to model ODEs f(1)-f(5) and it worked fine, I then added a sixth ODE f(6) for pressure drop and now the code runs indeffinatley. I have tried different ODE solvers including ones for stiff ODEs but get this error
Warning: Failure at t=1.056632e-20. Unable to meet
integration tolerances without reducing the step size
below the smallest value allowed (3.753912e-35) at time t.
my code is as follows:
clc
w = [0,500];
fch40 = 894065.3018;
fh2o0 = 3833657.964;
fco0 = 383170.8436;
fh20 = 1149512.531;
fco20 = 649.8427015;
P0 = 25;
f0 = [fch40,fh2o0,fco0,fh20,fco20,P0];
[w,f] = ode45(@dfdw_code2pluspd,w,f0);
plot(w,f(:,1),w,f(:,2),w,f(:,3),w,f(:,4),w,f(:,5));
xlabel('weight of catalyst');
ylabel('Flowrate');
title('F vs w');
legend('CH4','H2O','CO','H2','CO2');
plot(w,f(:,6));
xlabel('p or w');
ylabel('p or w');
title('pressure drop');
legend('pressure');
with dfdw_code2pluspd being:
function f = dfdw_code2pluspd(w,f)
fch40 = 894065.3018;
fh2o0 = 3833657.964;
fco0 = 383170.8436;
fh20 = 1149512.531;
fco20 = 649.8427015;
fi0 = 38082.53202;
ftot0 = fch40+fh2o0+fco0+fh20+fco20+fi0;
fch4 = f(1);
fh2o = f(2);
fco = f(3);
fh2 = f(4);
fco2 = f(5);
fi = fi0;
ftot = fch4+fh2o+fco+fh2+fco2+fco2+fi;
P0 = 25;
P = f(6);
Pch4 = (fch4/ftot)*P;
Ph2o = (fh2o/ftot)*P;
Pco = (fco/ftot)*P;
Ph2 = (fh2/ftot)*P;
Pco2 = (fco2/ftot)*P;
A1 = 4.225e15;
A2 = 1.955e6;
A3 = 1.020e15;
E1 = 240.1;
E2 = 67.13;
E3 = 243.9;
R = 8.314;
T0 = 900;
T = T0;
Hh2o = 88.68;
Hch4 = -38.28;
Hco = -70.61;
Hh2 = -82.90;
Bh2o = 1.77e5;
Bch4 = 6.65e-4;
Bco = 8.23e-5;
Bh2 = 6.12e-9;
Dh1 = 206; %kJ/mol
Dh2 = -41.1; %kJ/mol
Dh3 = 164.9; %kJ/mol
k1 = A1*exp(-E1/(R*T));
k2 = A2*exp(-E2/(R*T));
k3 = A3*exp(-E3/(R*T));
ke1 = A1*exp(-Dh1/(R*T));
ke2 = A2*exp(-Dh2/(R*T));
ke3 = A3*exp(-Dh3/(R*T));
kch4 = Bch4*exp(-Hch4/(R*T));
kco = Bco*exp(-Hco/(R*T));
kh2 = Bh2*exp(-Hh2/(R*T));
kh2o = Bh2o*exp(-Hh2o/(R*T));
D = 0.1;
Ac = (pi*(D^2))/4;
G = ftot/Ac;
ro0 = 1.225;
roc = 1300;
mu = 4.6e-5;
Dp = 0.0015;
phi = 0.37;
beta0 = (G/(ro0*Dp))*((1-phi)/(phi^3))*(((150*(1-phi)*mu)/Dp)+(1.75*G));
alpha = (2*beta0)/(Ac*(1-phi)*roc*P0);
DEN = 1+(kch4*Pch4)+(kco*Pco)+(kh2*Ph2)+((Ph2o*kh2o)/Ph2);
r1 = (k1/(Ph2^2.5))*((((Pch4*Ph2o)-(Pco*(Ph2^3))/ke1))/(DEN^2));
r2 = (k2/(Ph2))*((((Pco*Ph2o)-(Pco2*(Ph2))/ke2))/(DEN^2));
r3 = (k3/(Ph2^3.5))*((((Pch4*(Ph2o^2))-(Pco2*(Ph2^4))/ke3))/(DEN^2));
rch4 = -r1-r3;
rh2o = -r1-r2;
rco = r1-r2;
rh2 = (3*r1)+r2+(4*r3);
rco2 = r2+r3;
dPdw = -((alpha/2)*P0*(P0/P)*(ftot/ftot0)*(T/T0));
dfdw(1) = rch4;
dfdw(2) = rh2o;
dfdw(3) = rco;
dfdw(4) = rh2;
dfdw(5) = rco2;
dfdw(6) = dPdw;%dpdw
f = [dfdw(1), dfdw(2), dfdw(3), dfdw(4), dfdw(5), dfdw(6)]';
end

2 个评论

Shouldn't it be
ftot = fch4+fh2o+fco+fh2+fco2+fi;
instead of
ftot = fch4+fh2o+fco+fh2+fco2+fco2+fi;
?
Of course, CO2 is important in our days, but ..
beta0 and alpha are incredibly high (in the order 1e20). You should check the formulae.
Yes you are right about ftot, i will check my formulas. Thank you

请先登录,再进行评论。

回答(1 个)

Sam Chak
Sam Chak 2022-3-15

0 个投票

Hi @Thomas Laverick
The pressure drops rapidly. So, by the time sec.
If you look at the 6th equation (dPdw), you will notice that there is a division by P. When it reaches 0, singularity occurs. It's like falling into the "black hole" forever. Hope this explanation helps you understand what went wrong.

类别

帮助中心File Exchange 中查找有关 Commercial & Off-Highway Vehicles 的更多信息

产品

版本

R2020a

标签

Community Treasure Hunt

Find the treasures in MATLAB Central and discover how the community can help you!

Start Hunting!

Translated by