Dynamic array storage with for loop

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Temidayo BOBOYE
Temidayo BOBOYE am 18 Mai 2020
Beantwortet: Temidayo BOBOYE am 3 Jun. 2020
D = 0.067;
Ugs = [0.047,0.061,0.288,0.344,0.404,0.544,0.709,0.945,1.418,1.891,2.363,2.836,4.727];
Uls = ones(1,13)*0.047;
Uls1 = ones(1,13)*0.071;
Uls2 = ones(1,13)*0.095;
Uls3 = ones(1,13)*0.142;
g = 9.81;
rho_gas=1.18;
rho_liq=900;
Ugs_aht= Ugs *((rho_gas).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
Uls_aht= Uls *((rho_liq).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
Uls1_aht= Uls1 *((rho_liq).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
Uls2_aht= Uls2 *((rho_liq).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
Uls3_aht= Uls3 *((rho_liq).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
print(Uls_aht, Uls1_aht,Uls2_aht,Uls3_aht)
C = ((Ugs_aht).^0.5) + ((Uls_aht).^0.5);
C1 = ((Ugs_aht).^0.5) + ((Uls1_aht).^0.5);
C2 = ((Ugs_aht).^0.5) + ((Uls2_aht).^0.5);
C3 = ((Ugs_aht).^0.5) + ((Uls3_aht).^0.5);
flow = ones(1,13);
flow = string('flow');
for i = 1:13
if C <= 0.2(i)
flow(i)= 'Bubble'
if C1 <= 0.89(i)
flow(i)= 'Slug'
if C2 <= 0.98(i)
flow(i)= 'Transition'
if C3 >= 1.00(i)
flow(i)= 'Churn'
end
end
end
end
% end
Ugs = Ugs.';
Usl = Usl.';
Usl1 = Usl1.';
Usl2 = Usl2.';
Usl3 = Usl3.';
C = C.';
C1 = C1.';
C2 = C2.';
C3 = C3.';
Uls_aht = Uls_aht.';
Uls1_aht = Uls1_aht.';
Uls2_aht = Uls2_aht.';
Uls3_aht = Uls3_aht.';
% flow = flow.';
T = table(Ugs,Uls_aht,Uls1_aht,Uls2_aht,Uls3_aht,C,C1,C2,C3)

Akzeptierte Antwort

Temidayo BOBOYE
Temidayo BOBOYE am 3 Jun. 2020
D = 0.067;% Diameter of tube in meters
Ugs = [0.047,0.061,0.288,0.344,0.404,0.544,0.709,0.945,1.418,1.891,2.363,2.836,4.727];
Uls = ones(1,13)*0.047;
Uls1 = ones(1,13)*0.071;
Uls2 = ones(1,13)*0.095;
Uls3 = ones(1,13)*0.142;
Uls4 = ones(1,13)*0.284;
Uls5 = ones(1,13)*0.378;
g = 9.81;% Acceleartion due to gravity (m/s^2)
rho_gas=1.18;% Gas density (Kg/m^3)
rho_liq=900;% Liquid density (Kg/m^3)
for i = 1:13
Ugs_aht(i)= Ugs(i) *((sqrt(rho_gas))/(sqrt(g * D *(rho_liq - rho_gas))));
end
Uls_aht= Uls *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht1= Uls1 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht2 = Uls2 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht3 = Uls3 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht4 = Uls4 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht5 = Uls5 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
C = (sqrt(Ugs_aht)) + (sqrt(Uls_aht));
C1 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht1));
C2 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht2));
C3 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht3));
C4 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht4));
C5 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht5));
Ugs =Ugs.';
Uls = Uls.';
Uls1 = Uls1.';
Uls2 = Uls2.';
Uls3 = Uls3.';
Uls4 = Uls4.';
Uls5 = Uls5.';
Ugs_aht = Ugs_aht.';
Uls_aht = Uls_aht.';
Uls_aht1 = Uls_aht1.';
Uls_aht2 = Uls_aht2.';
Uls_aht3 = Uls_aht3.';
Uls_aht4 = Uls_aht4.';
Uls_aht5 = Uls_aht5.';
C = C.';
C1 = C1.';
C2 = C2.';
C3 = C3.';
C4 = C4.';
C5 = C5.';
plot(C,Ugs_aht,'--r')
xlabel('C (sqrt(m/s))')
ylabel('Ugs_aht (m/s)')
title('Flooding Mechanism')
T= table(Ugs, Uls,Uls_aht, Ugs_aht, C,C1,C2,C3,C4,C5);
hold on
plot(C1,Ugs_aht,'--b')
hold on
plot(C2,Ugs_aht,'--g')
hold on
plot(C3,Ugs_aht,'--y')
hold on
plot(C4,Ugs_aht,'--c')
hold on
plot(C5,Ugs_aht,'--k')

Weitere Antworten (2)

Ameer Hamza
Ameer Hamza am 18 Mai 2020
Bearbeitet: Ameer Hamza am 18 Mai 2020
There are several syntax errors in your code. Compare it with the following code to see the issues
D = 0.067;
Ugs = [0.047,0.061,0.288,0.344,0.404,0.544,0.709,0.945,1.418,1.891,2.363,2.836,4.727];
Uls = ones(1,13)*0.047;
Uls1 = ones(1,13)*0.071;
Uls2 = ones(1,13)*0.095;
Uls3 = ones(1,13)*0.142;
g = 9.81;
rho_gas=1.18;
rho_liq=900;
Ugs_aht= Ugs *((rho_gas).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
Uls_aht= Uls *((rho_liq).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
Uls1_aht= Uls1 *((rho_liq).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
Uls2_aht= Uls2 *((rho_liq).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
Uls3_aht= Uls3 *((rho_liq).^0.5)/(g * D *(rho_liq - rho_gas)).^0.5;
C = ((Ugs_aht).^0.5) + ((Uls_aht).^0.5);
C1 = ((Ugs_aht).^0.5) + ((Uls1_aht).^0.5);
C2 = ((Ugs_aht).^0.5) + ((Uls2_aht).^0.5);
C3 = ((Ugs_aht).^0.5) + ((Uls3_aht).^0.5);
flow = strings(1,13);
for i = 1:13
if C(i) <= 0.2
flow(i) = 'Bubble';
elseif C1(i) <= 0.89
flow(i) = 'Slug';
elseif C2(i) <= 0.98
flow(i) = 'Transition';
elseif C3(i) >= 1.00
flow(i) = 'Churn';
end
end
% end
Ugs = Ugs.';
Uls = Uls.';
Uls1 = Uls1.';
Uls2 = Uls2.';
Uls3 = Uls3.';
C = C.';
C1 = C1.';
C2 = C2.';
C3 = C3.';
Uls_aht = Uls_aht.';
Uls1_aht = Uls1_aht.';
Uls2_aht = Uls2_aht.';
Uls3_aht = Uls3_aht.';
% flow = flow.';
T = table(Ugs,Uls_aht,Uls1_aht,Uls2_aht,Uls3_aht,C,C1,C2,C3)
Result
T =
13×9 table
Ugs Uls_aht Uls1_aht Uls2_aht Uls3_aht C C1 C2 C3
_____ ________ ________ ________ ________ _______ _______ _______ _______
0.047 0.058011 0.087634 0.11726 0.17527 0.28669 0.34186 0.38826 0.46448
0.061 0.058011 0.087634 0.11726 0.17527 0.29307 0.34824 0.39464 0.47086
0.288 0.058011 0.087634 0.11726 0.17527 0.35431 0.40948 0.45588 0.5321
0.344 0.058011 0.087634 0.11726 0.17527 0.36485 0.42002 0.46642 0.54264
0.404 0.058011 0.087634 0.11726 0.17527 0.37523 0.4304 0.4768 0.55302
0.544 0.058011 0.087634 0.11726 0.17527 0.39678 0.45195 0.49835 0.57457
0.709 0.058011 0.087634 0.11726 0.17527 0.41886 0.47404 0.52044 0.59666
0.945 0.058011 0.087634 0.11726 0.17527 0.44636 0.50154 0.54794 0.62416
1.418 0.058011 0.087634 0.11726 0.17527 0.4926 0.54777 0.59417 0.67039
1.891 0.058011 0.087634 0.11726 0.17527 0.53157 0.58674 0.63314 0.70936
2.363 0.058011 0.087634 0.11726 0.17527 0.56583 0.621 0.6674 0.74362
2.836 0.058011 0.087634 0.11726 0.17527 0.59687 0.65205 0.69844 0.77467
4.727 0.058011 0.087634 0.11726 0.17527 0.70049 0.75566 0.80206 0.87828
  4 Kommentare
Temidayo BOBOYE
Temidayo BOBOYE am 21 Mai 2020
This loop should be able to store Ugs for each of the values of Uls and run the script and finally generate the table
Temidayo BOBOYE
Temidayo BOBOYE am 3 Jun. 2020
D = 0.067;% Diameter of tube in meters
Ugs = [0.047,0.061,0.288,0.344,0.404,0.544,0.709,0.945,1.418,1.891,2.363,2.836,4.727];
Uls = ones(1,13)*0.047;
Uls1 = ones(1,13)*0.071;
Uls2 = ones(1,13)*0.095;
Uls3 = ones(1,13)*0.142;
Uls4 = ones(1,13)*0.284;
Uls5 = ones(1,13)*0.378;
g = 9.81;% Acceleartion due to gravity (m/s^2)
rho_gas=1.18;% Gas density (Kg/m^3)
rho_liq=900;% Liquid density (Kg/m^3)
for i = 1:13
Ugs_aht(i)= Ugs(i) *((sqrt(rho_gas))/(sqrt(g * D *(rho_liq - rho_gas))));
end
Uls_aht= Uls *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht1= Uls1 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht2 = Uls2 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht3 = Uls3 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht4 = Uls4 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
Uls_aht5 = Uls5 *((sqrt(rho_liq))/(sqrt(g * D *(rho_liq - rho_gas))));
C = (sqrt(Ugs_aht)) + (sqrt(Uls_aht));
C1 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht1));
C2 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht2));
C3 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht3));
C4 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht4));
C5 = (sqrt(Ugs_aht)) + (sqrt(Uls_aht5));
Ugs =Ugs.';
Uls = Uls.';
Uls1 = Uls1.';
Uls2 = Uls2.';
Uls3 = Uls3.';
Uls4 = Uls4.';
Uls5 = Uls5.';
Ugs_aht = Ugs_aht.';
Uls_aht = Uls_aht.';
Uls_aht1 = Uls_aht1.';
Uls_aht2 = Uls_aht2.';
Uls_aht3 = Uls_aht3.';
Uls_aht4 = Uls_aht4.';
Uls_aht5 = Uls_aht5.';
C = C.';
C1 = C1.';
C2 = C2.';
C3 = C3.';
C4 = C4.';
C5 = C5.';
plot(C,Ugs_aht,'--r')
xlabel('C (sqrt(m/s))')
ylabel('Ugs_aht (m/s)')
title('Flooding Mechanism')
T= table(Ugs, Uls,Uls_aht, Ugs_aht, C,C1,C2,C3,C4,C5);
hold on
plot(C1,Ugs_aht,'--b')
hold on
plot(C2,Ugs_aht,'--g')
hold on
plot(C3,Ugs_aht,'--y')
hold on
plot(C4,Ugs_aht,'--c')
hold on
plot(C5,Ugs_aht,'--k')

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Walter Roberson
Walter Roberson am 18 Mai 2020
flow = ones(1,13);
flow = string(flow);
for i = 1:13
if C(i) <= 0.2
flow(i) = 'Bubble';
elseif C1(i) <= 0.89
flow(i) = 'Slug';
elseif C2(i) <= 0.98
flow(i) = 'Transition';
elseif C3(i) >= 1.00
flow(i) = 'Churn';
end
end

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