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Why ode45 returns NaN for a system of differential equations?

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Hou X.Y
Hou X.Y 2022 年 4 月 3 日
コメント済み: Hou X.Y 2022 年 4 月 5 日
clc,clear;
R = 8.314;
g = 9.8;
N = 10;
name = {'n2';'o2';'ar';'h2o';'h2o';'co2';'co';'so2';'o3';'no2';'c6h6'};
Mi(1) = 14.01;
c0(1) = 0.7809;
Mi(2) = 16;
c0(2) = 0.2095;
Mi(3) = 39.95;
c0(3) = 0.0093
Mi(4) = 18.02
c0(4) = 0.01
Mi(5) = 44.01
c0(5) = 500*0.000001
Mi(6) = 28.01
c0(6) = 20*0.000001
Mi(7) = 64.07
c0(7) = 75*0.000001
Mi(8) = 48
c0(8) = 70*1E-9
Mi(9) = 46.01
c0(9) = 53*1E-9
Mi(10) = 78.11
c0(10) = 50*1E-9
dTdz = 0.027
T0 = 293
syms T z x
%%
%initial moler concentration
% sum_mirho0_1 = 0;
% for i = 1:N
% sum_mirho0 = sum_mirho0_1+mirho0(i);
% sum_mirho0_1 = sum_mirho0
% end
% for i = 1:N
% rho0av = 1/sum_mirho0
% c0(i) = rho0av*m(i)*1000/Mi(i);
% end
%%
% dTdz = input('temperature gradient(K/m):')
% T0 = input('entrance temperature(K):')
T = T0 + dTdz*1000*z;%温度随深度的变化
%thermal diffusion factor
%%
syms z
c = sym('c',[N,1])
sum_c = sum(c);
sum_c01 = 0;
for i = 1:N
sum_c0 = sum_c01+c0(i)
sum_c01 = sum_c0
end
%%
x = c./sum_c;
alpha_0 = 0;
i = 1;
for i = 1:10
j = 1;
while j <= 10
if j ~= i
alpha_psn(j,i) = x(j).*log((c(i)./c0(i))*(c0(j)./c(j))).*(log(T./T0)^-1)
% alpha(i) = alpha_0+x(j)*alpha_psn(j,i)
% alpha_0 = alpha(i)
end
j = j+1;
end
end
%%
%individual height
for i = 1:10
Hi(i) = 1./((Mi(i)*g)./(R*T));
alpha(i) = sum(alpha_psn(i,:))
%ode for every species
dc(i) = -c(i).*((dTdz*1000.*((1 + alpha(i))./T)-(1./Hi(i))))
end
%%
f = matlabFunction(dc');
F = @(z,c)f(c(1),c(2),c(3),c(4),c(5),c(6),c(7),c(8),c(9),c(10),z)
% F = @(z,c)f(c(1),c(2),c(3),z)
%%
[z,c] = ode23(F,[0:100],c0)
figure
sum_carray0 = 0;
for i = 1:N
sum_carray = sum_carray0+c(:,i);
sum_carray0 = sum_carray;
end
for i = 1:N
plot(z,(c(:,i)./sum_carray),'linewidth',1.5)
hold on
end
grid on
legend(name)
xlabel('Depth(km)','fontsize',15)
ylabel('molar fraction','fontsize',15)
It returns a lot of NaN,and when I switch tspan [0:100] to other value,it may have some numerical results,and the result changes with the value of tspan,especially the initial points t0,for example,it may return some numerical results when I set 1 as t0.
This is the problem in the literature, which says the numerical solution can be obtained by ode23.

採用された回答

Torsten
Torsten 2022 年 4 月 3 日
N = 10;
Mi = zeros(N,1);
c0 = zeros(N,1);
Mi(1) = 14.01;
c0(1) = 0.7809;
Mi(2) = 16;
c0(2) = 0.2095;
Mi(3) = 39.95;
c0(3) = 0.0093;
Mi(4) = 18.02;
c0(4) = 0.01;
Mi(5) = 44.01;
c0(5) = 500*0.000001;
Mi(6) = 28.01;
c0(6) = 20*0.000001;
Mi(7) = 64.07;
c0(7) = 75*0.000001;
Mi(8) = 48;
c0(8) = 70*1E-9;
Mi(9) = 46.01;
c0(9) = 53*1E-9;
Mi(10) = 78.11;
c0(10) = 50*1E-9;
%f = matlabFunction(dc');
%F = @(z,c)f(c(1),c(2),c(3),c(4),c(5),c(6),c(7),c(8),c(9),c(10),z)
% F = @(z,c)f(c(1),c(2),c(3),z)
[z,c] = ode23(@(z,c)F(z,c,Mi,c0),[0:100],c0)
figure
sum_carray0 = 0;
for i = 1:N
sum_carray = sum_carray0+c(:,i);
sum_carray0 = sum_carray;
end
for i = 1:N
plot(z,(c(:,i)./sum_carray),'linewidth',1.5)
hold on
end
grid on
legend(name)
xlabel('Depth(km)','fontsize',15)
ylabel('molar fraction','fontsize',15)
function dc = F(z,c,Mi,c0);
R = 8.314;
g = 9.8;
N = 10;
name = {'n2';'o2';'ar';'h2o';'h2o';'co2';'co';'so2';'o3';'no2';'c6h6'};
dTdz = 0.027;
T0 = 293;
%syms T z x
%%
%initial moler concentration
% sum_mirho0_1 = 0;
% for i = 1:N
% sum_mirho0 = sum_mirho0_1+mirho0(i);
% sum_mirho0_1 = sum_mirho0
% end
% for i = 1:N
% rho0av = 1/sum_mirho0
% c0(i) = rho0av*m(i)*1000/Mi(i);
% end
%%
% dTdz = input('temperature gradient(K/m):')
% T0 = input('entrance temperature(K):')
T = T0 + dTdz*1000*z;%温度随深度的变化
%thermal diffusion factor
%%
%syms z
%c = sym('c',[N,1])
sum_c = sum(c);
sum_c01 = 0;
for i = 1:N
sum_c0 = sum_c01+c0(i);
sum_c01 = sum_c0;
end
%%
x = c./sum_c;
alpha_0 = 0;
i = 1;
for i = 1:10
j = 1;
while j <= 10
if j ~= i
alpha_psn(j,i) = x(j).*log((c(i)./c0(i))*(c0(j)./c(j)));%.*(log(T./T0)^-1);
% alpha(i) = alpha_0+x(j)*alpha_psn(j,i)
% alpha_0 = alpha(i)
end
j = j+1;
end
end
%%
%individual height
for i = 1:10
Hi(i) = 1./((Mi(i)*g)./(R*T));
alpha(i) = sum(alpha_psn(i,:));
%ode for every species
dc(i) = -c(i).*((dTdz*1000.*((1 + alpha(i))./T)-(1./Hi(i))));
end
%%
dc = dc.';
end
  7 件のコメント
Torsten
Torsten 2022 年 4 月 4 日
I find that if I don't set tspan as [0,100] directly,and divide it into [0,10],[10,20],[20,30],...,[90,100],it doesn't return NaN,and I don't konw why.If you know why,could you please tell me?
The reason is not the splitting of tspan.
Your code is different now.
Last time, you multiplied by log(T./T0)^-1 which is infinity since T = T0 at z = 0.
Now you multiply by log(T./T0) which gives 0 for T = T0 at z=0.
Hou X.Y
Hou X.Y 2022 年 4 月 5 日
Sorry,I am too careless.
But if I switch ' log(T./T0)' to 'log(T./T0)^-1',it still has numerical results,but this result is not consistent with the literature.

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