I am recieving an error in creating the solution however it still prints a result.

clc
clear all
close all
%Homework 7 Question 3
Tin=298; %K
Cp=80; %J/(mol K)
CAin=2000; %mol/m^3
k0=10e-7; %m3/(mol min)
Ea_R=5000; %K
rho=1000; %mol/m^3
CA=linspace(2,2000,61);
xA=(CAin-CA)/CAin;
T_sol=zeros(1,length(CA));
k_sol=zeros(1,length(CA));
tau_sol=zeros(1,length(CA));
DHR=-50000; %J/mol exothermic (gets hot)
for i=1:length(CA)
syms T k tau
eqn1=k==k0*exp((-Ea_R)*((1/T)-(1/Tin)));
eqn2=2*k*(CA(i)^2)==(CAin-CA(i))/tau;
eqn3=k*tau*(CA(i))^2*DHR==rho*Cp*(Tin-T);
solution=solve([eqn1,eqn2,eqn3],[T,k,tau]);
T_sol(i)=double(solution.T);
k_sol(i)=double(solution.k);
tau_sol(i)=double(solution.tau);
end
figure(1)
plot(log10(tau_sol),xA,'-bo');
xlabel('log_{10}(\tau, min)')
ylabel('x_A')

 Respuesta aceptada

In the last iteration of the loop, the results are all empty. One way to avoid the error is to test for at least one field to be empty:
if ~any(structfun(@isempty, solution))
T_sol(i)=double(solution.T);
k_sol(i)=double(solution.k);
tau_sol(i)=double(solution.tau);
end
Try this —
clc
clear all
close all
%Homework 7 Question 3
Tin=298; %K
Cp=80; %J/(mol K)
CAin=2000; %mol/m^3
k0=10e-7; %m3/(mol min)
Ea_R=5000; %K
rho=1000; %mol/m^3
CA=linspace(2,2000,61);
xA=(CAin-CA)/CAin;
T_sol=zeros(1,length(CA));
k_sol=zeros(1,length(CA));
tau_sol=zeros(1,length(CA));
DHR=-50000; %J/mol exothermic (gets hot)
for i=1:length(CA)
syms T k tau
eqn1=k==k0*exp((-Ea_R)*((1/T)-(1/Tin)));
eqn2=2*k*(CA(i)^2)==(CAin-CA(i))/tau;
eqn3=k*tau*(CA(i))^2*DHR==rho*Cp*(Tin-T);
solution=solve([eqn1,eqn2,eqn3],[T,k,tau]);
if ~any(structfun(@isempty, solution))
T_sol(i)=double(solution.T);
k_sol(i)=double(solution.k);
tau_sol(i)=double(solution.tau);
end
end
figure(1)
plot(log10(tau_sol),xA,'-bo');
xlabel('log_{10}(\tau, min)')
ylabel('x_A')
EDIT — (21 Apr 2024 at 20:14)
Changed if condition to use:
structfun(@isempty, solution)
Code otherwise unchanged.
.

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R2023b

Preguntada:

el 21 de Abr. de 2024

Comentada:

el 21 de Abr. de 2024

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