How do I solve Differential Algebraic Equations?
2 visualizaciones (últimos 30 días)
Mostrar comentarios más antiguos
How do I solve my DAE systems in gas lift system? My codes are giving results that are not acceptable. For example, my densities sometimes give negative values.
Thanks so much.
The code for my function is:
mga = x(1); %mass of gas in the annulus
mgt = x(2); %mass of gas in the well tubing
mot = x(3); %mass of oil in the well tubing
Pa = x(4); % pressure of gas in the annulus
rho_a = x(5); % density of gas in the annulus
Pwh = x(6); % Wellhead pressure
rho_w = x(7); % density of mixture in the well
wpc = x(8);
Pw = x(9); % Well pressure
Pbh = x(10); % bottomhole pressure
wiv = x(11);
wpg = x(12);
wpo = x(13);
wro = x(14);
wrg = x(15);
Lbh = 500;
La = 1500;
Hw=1000;
Dw=0.121;
Da=0.189;
Aw = 0.25*pi*Dw^2;
Aa=0.25*pi*(Da^2-Dw^2);
Va=Aa*La;
Abh = Aw;
uk=01; us=0.4;
rho_o = 800;
Civ = 1*1e-4; Cpc = 2e-3;Crh= 10^-2; Cr = 2.623*10^-4;
PI=0.7;
Pr = 150; Ps= 20; tf=300;
Ta = 301; Tw = 305; Mw = 0.02; R = 8.314;
g = 9.8;wgl = us*1; GOR = 0.1;
x(1,1) = wgl - wiv;
x(2,1) = wiv - wpg+ wrg;
x(3,1) = wro - wpo;
x(4,1) = -Pa*1e5+((Ta*R/(Va*Mw)+g*La/Va)*mga*1e3) ;
x(5,1) = -rho_a*10^3 +((Mw/(Ta*R))*Pa);
x(6,1) = -Pwh*1e5 + ((Tw*R/Mw)*(mgt*1e3/(Lw*Aw+Lbh*Abh-(mot*1e3/rho_o))))-(0.5*((mgt*1e3 + mot*1e3)*g*Hw/(Lw*Aw)));%
x(7,1) = -rho_w*10^3 +((mgt*1e3+ mot*1e3)*Pwh*Mw*rho_o)/(mot*1e3*Pwh*Mw +rho_o*R*Tw*mgt*1e3);
x(8,1) = -wpc +Cpc*sqrt(rho_w*(max(0.001,(Pwh - Ps*1e5))));
x(9,1) = -Pw*1e5 + Pwh +((g*Hw/(Lw*Aw))*max(0.001,(mot*1e3 + mgt*1e3 -(rho_o*Lbh*Abh))))+(128*0.003*Lw*wpc/(pi*Dw^4*((mgt*1e3+ mot*1e3)*Pwh*Mw*rho_o)/(mot*1e3*Pwh*Mw +rho_o*R*Tw*mgt*1e3)));
x(10,1) = -Pbh*1e5 + Pw + (rho_o*g*Lbh)+ (128*0.003*wro*Lbh/(3.14*Dw^4*rho_o));
x(11,1) = -wiv +Civ*sqrt(rho_a*(max (0.001,(Pa-Pw))));
x(12,1) = -wpg + ((mgt*1e3/max(0.001,(mgt*1e3+mot*1e3)))*wpc);
x(13,1) = -wpo + ((mot*1e3/max(0.001,(mgt*1e3+mot*1e3)))*wpc);
x(14,1) = -wro + 0.7*10^-5*(Pr*1e5-Pbh);
x(15,1) = -wrg + (GOR*wro);
The corresponding code for the script is
tspan = 0:36000;
x0 =[1.3268; 0.8093; 6.2694; 74.70300; 59.7027;
47.57000; 240.7129; 51.5223 ; 63.48600; 102.69000;
0.8184; 5.8905; 45.6318; 33.1200; 3.3120];
M = diag([ones(1,3) zeros(1,12)]);
options = odeset('Mass',M,'RelTol',1e-3,'AbsTol',1e-5);
[t,x] = ode23t(@gasLiftFnReal2,tspan,x0,options);
subplot(2,2,1)
plot(t/3600, 1000*x(:,5), '--')
xlabel('tspan')
ylabel('density of gas in annulus')
subplot(2,2,2)
plot(t/3600,1000*x(:,5), '-')
xlabel('tspan')
ylabel('density of gas in annulus')
subplot(2,2,3)
plot(t/3600, 1000*x(:,7), '-')
xlabel('tspan')
ylabel('density of mixtures in tubing')
subplot(2,2,4)
plot(t/3600, 1000*x(:,7), '-')
xlabel('tspan')
ylabel('density of mixtures in tubing')
% title
title ('Gas-lift Network')
6 comentarios
Fabio Freschi
el 31 de Oct. de 2019
Editada: Fabio Freschi
el 31 de Oct. de 2019
Do not undersetimate the power of numerical approximation: you could have negative values because of the local and global discretization error of the ODE: look the example here
You maybe be interested in using other solvers than ode23t.
Respuestas (0)
Ver también
Categorías
Más información sobre Ordinary Differential Equations en Help Center y File Exchange.
Community Treasure Hunt
Find the treasures in MATLAB Central and discover how the community can help you!
Start Hunting!