Index in position 2 exceeds array bounds (must not exceed 1).
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Chinaemerem Valentine Nwobi
2019 年 5 月 4 日
コメント済み: Chinaemerem Valentine Nwobi
2019 年 5 月 4 日
%% am encountering difficulty with my codes below and I will be pasting the
%the function file and the input parameters to run them with.
%%
function [gamma,a]=ACTIVITY_WILSON(MW,rhoL,BIP,T,x)
%This program calculates the activity coefficients (gamma) and the
%activities (a) of each component of a mixture of c components using the
%Wilson model.
%INPUT PARAMETERS: MW: vector (1xc) reporting the molecular weights of the
%c components; rhoL, vector (1xc) reporting the liquid density of the c
%pure components at temperature T; BIP is a matrix cxc reporting the energy
%interaction parameters (BIP(i,j)=lambda_ij-lambda_ii, J/mol). The energy
%interaction parameters are temperature independent; T: temperature of the
%system; x vector (1xc) reporting the mole fractions of the components of
%the mixture.
%OUTPUT PARAMETERS: gamma: vector 1xc reporting the activity
%coefficients of the components of the mixture; a: vector 1xc reporting the
%activities of the components of the mixture.
%Unless otherwise stated, all input/output parameters are expressed
%according to MKS.
R=8.314;
c=length(x);
%Molar volumes of the pure liquid components composing the mixture
Vl=1./((rhoL*1000)./MW);
%Lambda terms (dimensionless) of the Wilson formula
for i=1:c
for j=1:c
Lambda(i,j)=(Vl(j)/Vl(i))*exp(-BIP(i,j)/(R*T));
end
end
for i=1:c
for j=1:c
A=sum(x.*Lambda(j,:));
C(j)=x(j)*Lambda(j,i)/A;
end
lngamma(i)=1-log(sum(x.*Lambda(i,:)))-sum(C);
gamma(i)=exp(lngamma(i));
a(i)=gamma(i)*x(i);
end
end
%%
x= Varying from 0 to 1;
MW=[46.0684 18.0153];
rhoL=[785 997];
BIP=[1972.2 ; 3700.1];
%%
Please help me find what am doing wrong . thank you but please comment if there is something am doing wrong with the way i ask because I never got replies before now.
採用された回答
KALYAN ACHARJYA
2019 年 5 月 4 日
編集済み: KALYAN ACHARJYA
2019 年 5 月 4 日
Save the following function file>Save as : ACTIVITY_WILSON.m file name
function [gamma,a]=ACTIVITY_WILSON(MW,rhoL,BIP,T,x)
R=8.314;
c=length(x);
%Molar volumes of the pure liquid components composing the mixture
Vl=1./((rhoL*1000)./MW);
%Lambda terms (dimensionless) of the Wilson formula
for i=1:c
for j=1:c
Lambda(i,j)=(Vl(j)/Vl(i))*exp(-BIP(i,j)/(R*T));
end
end
for i=1:c
for j=1:c
A=sum(x.*Lambda(j,:));
C(j)=x(j)*Lambda(j,i)/A;
end
lngamma(i)=1-log(sum(x.*Lambda(i,:)))-sum(C);
gamma(i)=exp(lngamma(i));
a(i)=gamma(i)*x(i);
end
end
Now call the above function from different Matlab scripts file:
%%
x=0.2; % Any value 0 to 1
MW=[46.0684 18.0153];
rhoL=[785 997];
BIP=[1972.2; 3700.1];
T=30; % Hopefully this is tempature, set accordingly
[gamma,a]=ACTIVITY_WILSON(MW,rhoL,BIP,T,x)
Result
gamma =
1.358311135425136e+04
a =
2.716622270850272e+03
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