Week 7 - Simulation of a 1D Supersonic nozzle flow simulation using Macormack Method

Objective: To simulate the isentropic flow through a quasi 1D subsonic-supersonic nozzle using both the conservation and non-conservation forms of the governing equations and sovle them using the MacCormack's technique and comparing their solutions.

Description: We consider the study, isentropic flow through a convergent divergent nozzle. The flow at the inlet to the nozzle comes from reservoir. The cross section area of the reservoir is very large and hence velocity is very small. The flow is locally subsonic the convergent section of the nozzle, Sonic at the throat and Supersonic at the divergent section.

Let us consider a small control volume of the nozzle as shown below.

We assume that at a given section, where the cross section area is A, the flow properties are uniform across the section. Hence, although the area of the nozzle changes as a function of distance along the nozzle, X, and therefore in reality the flow field is two dimensional(the flow varies in the two dimensional x-y space), We make the assumption that the flow properties vary only with X; this is tantamount to asuming uniform flow properties across any given cross-section. Such flow is defined as Quasi one dimensional flow.

The governing continuty, momentum and energy equations in terms of non dimensional variables for this quassi one dimensional staedy and isentropc flow can be expressed respectively as:

For air at standard conditions, γ=1.4

These equations are solved by Macormack method using time marching process

Macormack Method:

Let f(x) is the equation to be solved.Then the following steps are followed

i. inital profile

Before the calculation, the initial profile for all the flow field variables which are velocity, density and temperature has to be determined. These are guess values but should be specified with more awareness on the problem.

ii. predector step

(∂f/dt)p=f(i+1)−f(i)/Δx

iii. solution update

fp=fInitial+(∂f/∂t)p⋅/Δt

fp=��= Flow field variables calculated after the predictor step

fInitial=flow field variable in the initial step

Δt=time step size

iv. Corrector step

(∂fp/dt)c=f(i)−f(i−1)/Δx

(∂f/dt)avg=0.5((∂f/dt)p+(∂fp/dt)c)

v. Final solution update

fsol=fInitial+(∂f∂t)avg⋅/Δt

`f_(sol) =`Final solution of the flow field variables for the first time step

Approach:

Approach is simple that

1. main function{

input

calling non conservative function

`calling conservative function

plotting graphs such as density, pressure, velocity ,mach no vs nozzle length

comparison plot

}

2.nonconservative function {

input

loop open

predictor method

updating value

collector method

updating input

calculating values for density, temperature, velocity and mach no across nozzle

calculating values for density, temperature, velocity and mach no across throat

plotting graphs like time step variation, mass flow rate at diff. time steps

loop close

like wise

3.conservative function {

input

loop open

predictor method

updating value

collector method

updating input

calculating values for density, temperature, velocity and mach no across nozzle

calculating values for density, temperature, velocity and mach no across throat

plotting graphs like time step variation, mass flow rate at diff. time steps

loop close

Matlab Code with explaination:

main fuction code

clear all
close all
clc

%SOLVING QUASI 1D SUPERSONIC NOZZLE FLOW EQUATIONS

%INPUT PARAMETERS
%No. of grid points    
n = 31;             

gamma = 1.4;
x = linspace(0,3,n);
dx = x(2) - x(1);

%No. of time step
nt = 1400;

%Courant Number
C = 0.5;            


%FUNCTION FOR NON CONSERVATIVE FORM
tic;
[Mass_flow_rate_NC, Pressure_NC, Mach_number_NC, rho_NC, v_NC, T_NC, rho_throat_NC, v_throat_NC, T_throat_NC, Mass_flow_rate_throat_NC, Pressure_throat_NC, Mach_number_throat_NC] = Non_conservative_form(x, dx, n, gamma, nt, C);
Time_elapsed_NC = toc;
fprintf('Time Elasped for Non Conservative form: %0.4f', Time_elapsed_NC);
hold on

%PLOTTING 
%Timestep variation of properties at throat area in Non Conservative form
figure(2)

%Density
subplot(4,1,1)
plot(linspace(1,nt,nt),rho_throat_NC,'color','m')
ylabel('Density')
legend({'Density at throat'});
axis([0 1400 0 1.3]);
grid minor;
title('Timestep variation at throat area - NON CONSERVATIVE FORM')

%Temperature
subplot(4,1,2)
plot(linspace(1,nt,nt),T_throat_NC,'color','c')
ylabel('Temperature')
legend({'Temperature at throat'});
axis([0 1400 0.6 1]);
grid minor;

%Pressure
subplot(4,1,3)
plot(linspace(1,nt,nt),Pressure_throat_NC,'color','g')
ylabel('Pressure')
legend({'Pressure at throat'});
axis([0 1400 0.4 1.1]);
grid minor

%Mach Number
subplot(4,1,4)
plot(linspace(1,nt,nt),Mach_number_throat_NC,'color','y')
xlabel('Timesteps')
ylabel('Mach Number')
legend({'Mach Number at throat'});
axis([0 1400 0.6 1.4]);
grid minor;


%Steady state simulation for primitve values for Non Conservative form
figure(3);
%Density

subplot(4,1,1);
plot(x,rho_NC,'color','m')
ylabel('Density')
legend({'Density'});
axis([0 3 0 1])
grid minor;
title('Variation of Flow Rate Distribution - NON CONSERVATIVE')

%Temperature
subplot(4,1,2);
plot(x,T_NC,'color','c')
ylabel('Temperature')
legend({'Temperature'});
axis([0 3 0 1])
grid minor;

%Pressure
subplot(4,1,3);
plot(x,Pressure_NC,'color','g')
ylabel('Pressure')
legend({'Pressure'});
axis([0 3 0 1])
grid minor;

%Mach number
subplot(4,1,4);
plot(x,Mach_number_NC,'color','y')
xlabel('Nozzle Length')
ylabel('Mach number')
legend({'Mach number'});
axis([0 3 0 4])
grid minor;


%FUNCTION FOR CONSERVATIVE FORM
tic;
[Mass_flow_rate_C, Pressure_C, Mach_number_C, rho_C, v_C, T_C, rho_throat_C, v_throat_C, T_throat_C, Mass_flow_rate_throat_C, Pressure_throat_C, Mach_number_throat_C] = Conservative_form(x, dx, n, gamma, nt, C);
Time_elasped_C = toc;
fprintf('Time Elasped for Conservative form: %0.4f', Time_elasped_C);

%PLOTTING 
%Timestep variation of properties at throat area in Conservative form
figure(5)

%Density
subplot(4,1,1)
plot(rho_throat_C,'color','m')
ylabel('Density')
legend({'Density at throat'});
axis([0 1400 0 1]);
grid minor;
title('Timestep variation at throat area - CONSERVATIVE FORM')

%Temperature
subplot(4,1,2)
plot(T_throat_C,'color','c')
ylabel('Temperature')
legend({'Temperature at throat'});
axis([0 1400 0.6 1]);
grid minor;

%Pressure
subplot(4,1,3)
plot(Pressure_throat_C,'color','g')
ylabel('Pressure')
legend({'Pressure at throat'});
axis([0 1400 0.2 0.8]);
grid minor

%Mach Number
subplot(4,1,4)
plot(Mach_number_throat_C,'color','y')
xlabel('Timesteps')
ylabel('Mach Number')
legend({'Mach Number at throat'});
axis([0 1400 0.6 1.4]);
grid minor;


%Steady state simulation for primitve values for Non Conservative form
figure(6);

%Density 
subplot(4,1,1);
plot(x,rho_C,'color','m')
ylabel('Density')
legend({'Density'});
axis([0 3 0 1])
grid minor;
title('Variation of Flow Rate Distribution - CONSERVATIVE FORM')

%Temperature 
subplot(4,1,2);
plot(x,T_C,'color','c')
ylabel('Temperature')
legend({'Temperature'});
axis([0 3 0 1])
grid minor;

%Pressure
subplot(4,1,3);
plot(x,Pressure_C,'color','g')
ylabel('Pressure')
legend({'Pressure'});
axis([0 3 0 1])
grid minor;

%Mach number
subplot(4,1,4);
plot(x,Mach_number_C,'color','y')
xlabel('Nozzle Length')
ylabel('Mach number')
legend({'Mach number'});
axis([0 3 0 4])
grid minor;


%COMPARISON PLOT of Normalized Mass Flow Rate of both forms
figure(7)
hold on
plot(x,Mass_flow_rate_NC,'r','linewidth',1.25)
hold on;
plot(x,Mass_flow_rate_C,'b','linewidth',1.25)
hold on;
grid on

legend('Non Conservative','Conservative');
xlabel('Length of the Domain')
ylabel('Mass Flow Rate')

title('Comparison of Normalized Mass Flow Rate of both forms')

Explanation:

• Code is started with clear all, close all and clc to enable a fresh start without the manipulation of previous values.
• Input parameters are assigned for the variables x, dx, n, gamma, nt and C.
• Non Conservative and Conservative forms are created as separate functions with the neccessary inputs which is detailed below this section.
• tic toc command is used for calculating the time elasped between the functions.
• Plotting is done for the following solutions
  1)Timestep variation at throat area of both forms
  2)Variation of Flow Rate Distribution of both forms
  3)Comparison of Normalized Mass Flow Rate of both forms
• Each plot is computed as subplots of four primitive variables such as Density, Temperature, Pressure and Mach Number at throat as well as Convergent/Divergent section.

NON CONSERVATIVE FORM

function [Mass_flow_rate_NC, Pressure_NC, Mach_number_NC, rho_NC, v_NC, T_NC, rho_throat_NC, v_throat_NC, T_throat_NC, Mass_flow_rate_throat_NC, Pressure_throat_NC, Mach_number_throat_NC] = Non_conservative_form(x, dx, n, gamma, nt, C)

%Intial boundary conditions
rho_NC = 1 - 0.3146*x;
T_NC = 1 - 0.2341*x;
v_NC = (0.1 + 1.09*x).*T_NC.^0.5;

%Area & Throat profiles
a = 1 + 2.2*(x - 1.5).^2;
throat = find(a==1);


%Outer Time Loop
for k = 1:nt
    
    %Time-step control
    dt = min(C.*dx./(sqrt(T_NC) + v_NC));
    
    %Saving a copy of Old Values
    rho_old = rho_NC;
    T_old = T_NC;
    v_old = v_NC;
    

    %Predictor Method
    for j = 2:n-1
        
        %Simplifying the Equation's spatial terms
        dv_dx = (v_NC(j + 1) - v_NC(j))/dx;
        drho_dx = (rho_NC(j + 1) - rho_NC(j))/dx;
        dT_dx = (T_NC(j + 1) - T_NC(j))/dx;
        dlog_a_dx = (log(a(j + 1)) - log(a(j)))/dx;
        
        %Continuity Equation
        drho_dt_P(j) = -rho_NC(j)*dv_dx - rho_NC(j)*v_NC(j)*dlog_a_dx - v_NC(j)*drho_dx;
        
        %Momentum Equation
        dv_dt_P(j) = -v_NC(j)*dv_dx - (1/gamma)*(dT_dx + (T_NC(j)*drho_dx/rho_NC(j)));
        
        %Energy Equation
        dT_dt_P(j) = -v_NC(j)*dT_dx - (gamma - 1)*T_NC(j)*(dv_dx + v_NC(j)*dlog_a_dx);
        
        
        %Solution Update
        rho_NC(j) = rho_NC(j) + drho_dt_P(j)*dt;
        v_NC(j) = v_NC(j) + dv_dt_P(j)*dt;
        T_NC(j) = T_NC(j) + dT_dt_P(j)*dt;
        
    end
    
    
    %Corrector Method
    for j = 2:n-1
        
        %Simplifying the Equation's spatial terms
        dv_dx = (v_NC(j) - v_NC(j - 1))/dx;
        drho_dx = (rho_NC(j) - rho_NC(j - 1))/dx;
        dT_dx = (T_NC(j) - T_NC(j - 1))/dx;
        dlog_a_dx = (log(a(j)) - log(a(j - 1)))/dx;
        
        %Continuity Equation
        drho_dt_C(j) = - rho_NC(j)*dv_dx - rho_NC(j)*v_NC(j)*dlog_a_dx - v_NC(j)*drho_dx;
        
        %Momentum Equation
        dv_dt_C(j) = - v_NC(j)*dv_dx - (1/gamma)*(dT_dx + (T_NC(j)*drho_dx/rho_NC(j)));
        
        %Energy Equation
        dT_dt_C(j) = - v_NC(j)*dT_dx - (gamma - 1)*T_NC(j)*(dv_dx + v_NC(j)*dlog_a_dx);
       
    end
    
    %Compute Average Time derivative
    drho_dt = 0.5.*(drho_dt_P + drho_dt_C);
    dv_dt = 0.5.*(dv_dt_P + dv_dt_C);
    dT_dt = 0.5.*(dT_dt_P + dT_dt_C);
    
    %Final Solution Update
    for i = 2:n-1
        rho_NC(i) = rho_old(i) + drho_dt(i)*dt;
        v_NC(i) = v_old(i) + dv_dt(i)*dt;
        T_NC(i) = T_old(i) + dT_dt(i)*dt;
        
    end
    
    %Applying Boundary Conditions
    %At Inlet
    rho_NC(1) = 1;
    v_NC(1) = 2*v_NC(2) - v_NC(3);
    T_NC(1) = 1;
    
    %At Outlet
    rho_NC(n) = 2*rho_NC(n-1) - rho_NC(n - 2);
    v_NC(n) = 2*v_NC(n - 1) - v_NC(n - 2);
    T_NC(n) = 2*T_NC(n - 1) - T_NC(n - 2);
    
    
    %Defining Mass flow rate, Pressure and Mach number
    Mass_flow_rate_NC = rho_NC.*a.*v_NC;
    Pressure_NC = rho_NC.*T_NC;
    Mach_number_NC = (v_NC./sqrt(T_NC));
    
    %Calculating Variables at throat section
    rho_throat_NC(k) = rho_NC(throat);
    T_throat_NC(k) = T_NC(throat);
    v_throat_NC(k) = v_NC(throat);
    Mass_flow_rate_throat_NC(k) = Mass_flow_rate_NC(throat);
    Pressure_throat_NC(k) = Pressure_NC(throat);
    Mach_number_throat_NC(k) = Mach_number_NC(throat);
    
    
    %PLOTTING
    %Comparison of non-dimensional Mass flow rates at different time steps
    figure(1);
    if k == 50
       plot(x, Mass_flow_rate_NC, 'm', 'linewidth', 1.25);
       hold on
    elseif k == 100
       plot(x, Mass_flow_rate_NC, 'c', 'linewidth', 1.25);
       hold on
    elseif k == 200
       plot(x, Mass_flow_rate_NC, 'g', 'linewidth', 1.25);
       hold on
    elseif k == 400
       plot(x, Mass_flow_rate_NC, 'y', 'linewidth', 1.25);
       hold on
    elseif k == 800
       plot(x, Mass_flow_rate_NC, 'k', 'linewidth', 1.25);
       hold on
    end
    
    %Labelling
    title('Mass flow rates at different Timesteps - NON CONSERVATIVE FORM)')
    xlabel('Distance')
    ylabel('Mass flow rate')
    legend({'50^t^h Timestep','100^t^h Timestep','200^t^h Timestep','400^t^h Timestep','800^t^h Timestep'})
    axis([0 3 0 2])
    grid on
    
end

end

Explanation:

• The purpose of the function is to calculate the values of
  Mass flow rate, Pressure, Mach number, Density, velocity, Temperature, Density at throat, velocity at throat, Temperature at throat, Mass flow rate at throat, Pressure at throat, Mach number at throat by the known equations for all the grid points.
  
  
• For this initial boundary conditions are established for Density, Temperature & Velocity and profiles for calculating area & throat.
• Now Outer Time loop is computed for for loop to calculate all the grid points for various formulas inside the loop.
• MacCarmack technique is used to solve the numerical solution of governing equations such as Continuity, Momentum & Energy Equation.
• The technique implies two methods for solving namely Predictor method followed by Corrector method.
• Predictor & Corrector method are assigned within the for loop individually for calculating values.
• The calculated values are averaged in the next step and updating the solution with old values.
• Boundary Conditions are applied within the for loop and subsequently used for calculating the Mass Flow Rate, Mach Number & Pressure and also calculating the values throat section.
• Finally plotting is done for Distance(x) & Mass Flow Rate for differrent Timesteps.
• Program is ended.

CONSERVATIVE FORM

function [Mass_flow_rate_C, Pressure_C, Mach_number_C,  rho_C, v_C, T_C, rho_throat_C, v_throat_C, T_throat_C, Mass_flow_rate_throat_C, Pressure_throat_C, Mach_number_throat_C] = Conservative_form(x, dx, n, gamma, nt, C)

%Determining Initial profile of Density and Temperature
for i = 1:n
    
    if (x(i) >= 0 && x(i) <= 0.5)
        rho_C(i) = 1;
        T_C(i) = 1;
    elseif (x(i) >= 0.5 && x(i) <= 1.5)
        rho_C(i) = 1 - 0.366*(x(i) - 0.5);
        T_C(i) = 1 - 0.167*(x(i) - 0.5);
    elseif (x(i) >= 1.5 && x(i) <= 3)
        rho_C(i) = 0.634 - 0.3879*(x(i) - 1.5);
        T_C(i) = 0.833 - 0.3507*(x(i) - 1.5);
    end
    
end

%Area & Throat profiles
a = 1 + 2.2*(x - 1.5).^2;
throat = find(a==1);

%Initial profile fot Velocity and Pressure
v_C = 0.59./(rho_C.*a);
Pressure_C = rho_C.*T_C;

%Calculate the Initial Solution Vectors(U)
U1 = rho_C.*a;
U2 = rho_C.*a.*v_C;
U3 = rho_C.*a.*(T_C./(gamma - 1)) + ((gamma/2).*v_C.^2);


%Outer Time Loop
for k =1:nt
    
    %Time-step control
    dt = min(C.*dx./(sqrt(T_C) + v_C));
    
    %Saving a copy of Old Values
    U1_old = U1;
    U2_old = U2;
    U3_old = U3;

    %Calculating the Flux vector(F)
    F1 = U2;
    F2 = ((U2.^2)./U1) + ((gamma - 1)/gamma)*(U3 - (gamma/2)*((U2.^2)./U1));
    F3 = ((gamma*U2.*U3)./U1) - (gamma*(gamma - 1)*((U2.^3)./(2*U1.^2)));
    
    
    %Predictor Method
    for j = 2:n-1
    
        %Calculating the Source term(J)
        J2(j) = (1/gamma)*rho_C(j)*T_C(j)*((a(j + 1) - a(j))/dx);
        
        
        %Continuity Equation
        dU1_dt_P(j) = -((F1(j + 1) - F1(j))/dx);
        
        %Momentum Equation
        dU2_dt_P(j) = -((F2(j + 1) - F2(j))/dx) + J2(j);
        
        %Energy Equation
        dU3_dt_P(j) = -((F3(j + 1) - F3(j))/dx);
        
        
        %Updating New values
        U1(j) = U1(j) + dU1_dt_P(j)*dt;
        U2(j) = U2(j) + dU2_dt_P(j)*dt;
        U3(j) = U3(j) + dU3_dt_P(j)*dt;
        
    end
    
    %Updating Flux vectors
    F1 = U2;
    F2 = ((U2.^2)./U1) + ((gamma - 1)/gamma)*(U3 - ((gamma*0.5*(U2.^2))./(U1)));
    F3 = ((gamma*U2.*U3)./U1) - ((gamma*0.5*(gamma - 1)*(U2.^3))./(U1.^2));

    
    %Corrector Method
    for j = 2:n-1
        
        %Updating the Source term(J)
        J2(j) = (1/gamma)*rho_C(j)*T_C(j)*((a(j) - a(j - 1))/dx);

        %Simplifying the Equation's spatial terms
        dU1_dt_C(j) = -((F1(j) - F1(j - 1))/dx);
        dU2_dt_C(j) = -((F2(j) - F2(j - 1))/dx) + J2(j);
        dU3_dt_C(j) = -((F3(j) - F3(j - 1))/dx);

    end

    %Compute Average Time derivative
    dU1_dt = 0.5*(dU1_dt_P + dU1_dt_C);
    dU2_dt = 0.5*(dU2_dt_P + dU2_dt_C);
    dU3_dt = 0.5*(dU3_dt_P + dU3_dt_C);

    %Final Solution Update
    for i = 2:n-1
        U1(i) = U1_old(i) + dU1_dt(i)*dt;
        U2(i) = U2_old(i) + dU2_dt(i)*dt;
        U3(i) = U3_old(i) + dU3_dt(i)*dt;
        
    end
    
    
    %Applying Boundary Conditions
    %At Inlet
    U1(1) = rho_C(1)*a(1);
    U2(1) = 2*U2(2) - U2(3);
    
    v_C(1) = U2(1)./U1(1);
    U3(1) = U1(1)*((T_C(1)/(gamma - 1)) + ((gamma/2)*(v_C(1)).^2));
    
    %At Outlet
    U1(n) = 2*U1(n - 1) - U1(n - 2);
    U2(n) = 2*U2(n - 1) - U2(n - 2);
    U3(n) = 2*U3(n - 1) - U3(n - 2);
    
    %Final Primitive value update
    rho_C = U1./a;
    v_C = U2./U1;
    T_C = (gamma - 1)*((U3./U1 - (gamma/2)*(v_C).^2));
    
    %Defining Mass flow rate, Pressure and Mach number
    Mass_flow_rate_C = rho_C.*a.*v_C;
    Pressure_C = rho_C.*T_C;
    Mach_number_C = (v_C./sqrt(T_C));
    
    %Calculating Variables at throat section
    rho_throat_C(k) = rho_C(throat);
    T_throat_C(k) = T_C(throat);
    v_throat_C(k) = v_C(throat);
    Mass_flow_rate_throat_C(k) = Mass_flow_rate_C(throat);
    Pressure_throat_C(k) = Pressure_C(throat);
    Mach_number_throat_C(k) = Mach_number_C(throat);

    %PLOTTING
    %Comparison of non-dimensional Mass flow rates at different time steps
    figure(4)
    if k == 50
       plot(x, Mass_flow_rate_C, 'm', 'linewidth', 1.25);
       hold on
    elseif k == 100
       plot(x, Mass_flow_rate_C, 'c', 'linewidth', 1.25);
       hold on
    elseif k == 200
       plot(x, Mass_flow_rate_C, 'g', 'linewidth', 1.25);
       hold on
    elseif k == 400
       plot(x, Mass_flow_rate_C, 'y', 'linewidth', 1.25);
       hold on
    elseif k == 800
       plot(x, Mass_flow_rate_C, 'k', 'linewidth', 1.25);
       hold on
    end
           
    
    %Labelling
    title('Mass flow rates at different Timesteps - CONSERVATIVE FORM')
    xlabel('Distance')
    ylabel('Mass flow rate')
    legend({'50^t^h Timestep','100^t^h Timestep','200^t^h Timestep','400^t^h Timestep','800^t^h Timestep'})
    axis([0 3 0.4 1])
    grid on
    
end

end

Explanation:

• The purpose of the function is to calculate the values of
  Mass flow rate, Pressure, Mach number, Density, velocity, Temperature, Density at throat, velocity at throat, Temperature at throat, Mass flow rate at throat, Pressure at throat, Mach number at throat by the known equations for all the grid points.
  To determine the initial profile of Density & Temperature, for loop is used inputing the known conditions within an else-if command.
• Initial values of area, throat, velocity & Pressure are calculated using formulas.
• In order to simplify and avoid errors, equation is splitted into Solution Vector(U), Flux Vector(F) and Source Term(J).
• Now Outer Time loop is computed for for loop to calculate all the grid points for various formulas inside the loop.
• MacCarmack technique is used to solve the numerical solution of governing equations such as Continuity, Momentum & Energy Equation.
• The technique implies two methods for solving namely Predictor method followed by Corrector method.
• Predictor & Corrector method are assigned within the for loop individually for calculating values.
• The calculated values are averaged in the next step and updating the solution with old values.
• Boundary Conditions are applied within the for loop and subsequently used for calculating the Mass Flow Rate, Mach Number & Pressure and also calculating the values throat section.
• Finally plotting is done for Distance(x) & Mass Flow Rate for differrent Timesteps.
• Program is ended.

Output:

1. time step variation across throat area

Observation:

From the above plots we can conclude that initial variations observed in Non Conservative form for a certain period of time makes it consume higher amount of time to acheive stable solution when compared to Conservative form.

2.variation of flow rate distribution

Observation:

Here by observing the above plots we could see that both the forms are in same phase giving the exact same solution for all the values.

3.mass flow rates at diff. time steps

Observation:

Above plots shows that Mass Flow Rate at different Time steps along the Distance oscillates initially, however the solution becomes stable after the 400th Timestep for both the forms attaining a constant value.

COMPARISON PLOT of Normalized Mass Flow Rate of both NON CONSERVATIVE & CONSERVATIVE FORMS:

Observation:

Eventhough the final solution of both the forms are almost similar, the Non Conservative form oscillates much when compared to Conservative form. The latter also gives almost stable solution along the length. By this we can conclude that Conservative form attains stability in lesser number of iterations with earliest time.

Observation:

Grid dependency is an important factor to determine whether the problem can be solved faster. So here we increased the Grid points from 31 to 61 and populated them in a sheet.

It is clear from the above table that the values are almost same along all the Primitive Variables for both the forms even when the Grid points(n) is changed from 31 to 61 showcasing that it doesn't get affected by the increase of Grid points.

So we can safely conclude that the above problem is Grid Dependant.

Conclusion

1] Simulation time increases with increase in number of grid points but accuracy increases.

2]Non conservative form is faster then conservative form.

3]Mass flow distribution is better in conservative form then in non conservative form as conservative form conserves mass efficiency better.

4]Initially at lower time steps there are oscillations in the solution but as the time steps increases the solution moves to steady state and converges near to 800 time steps.

5]So the simulation must run at least upto 800 time steps for it to converge.

6] Simulation time non -conservative form n=31 is 155.4 seconds

Simulation time conservative form n=31 is 130 seconds

Simulation time non -conservative form n=61 is 140 seconds

Simulation time conservative form n=61 is 122.2 seconds

Note- Data taken from JD Andersons CFD basics textbook.