mirror of
https://github.com/Cantera/cantera.git
synced 2025-02-25 18:55:29 -06:00
[Matlab] Remove automatic figure generation for kinetic rate functions
Miscellaneous formatting updates
This commit is contained in:
ssun30
Ray Speth
parent
3dad11e9ff
commit
c11b157add
@ -346,7 +346,7 @@ classdef Stack < handle
|
||||
% step to be taken first time the steady-state solution
|
||||
% attempted. If this failed, two time steps would be taken.
|
||||
checklib;
|
||||
calllib(ct, 'sim1D_', s.st_id, ...
|
||||
calllib(ct, 'sim1D_TimeStep', s.st_id, ...
|
||||
stepsize, length(steps), steps);
|
||||
end
|
||||
|
||||
|
||||
@ -53,17 +53,17 @@ classdef Interface < handle & ThermoPhase & Kinetics
|
||||
calllib(ct, 'surf_getCoverages', surf_id, xx);
|
||||
c = pt.Value;
|
||||
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Coverages')
|
||||
bar(c);
|
||||
colormap(summer);
|
||||
nm = s.speciesNames;
|
||||
set(gca, 'XTickLabel', nm);
|
||||
xlabel('Species Name');
|
||||
ylabel('Coverage');
|
||||
title('Surface Species Coverages');
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Coverages')
|
||||
% bar(c);
|
||||
% colormap(summer);
|
||||
% nm = s.speciesNames;
|
||||
% set(gca, 'XTickLabel', nm);
|
||||
% xlabel('Species Name');
|
||||
% ylabel('Coverage');
|
||||
% title('Surface Species Coverages');
|
||||
% end
|
||||
end
|
||||
|
||||
function c = concentrations(s)
|
||||
@ -82,17 +82,17 @@ classdef Interface < handle & ThermoPhase & Kinetics
|
||||
calllib(ct, 'surf_getConcentrations', surf_id, xx);
|
||||
c = pt.Value;
|
||||
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Concentrations')
|
||||
bar(c);
|
||||
colormap(summer);
|
||||
nm = speciesNames(s);
|
||||
set(gca, 'XTickLabel', nm);
|
||||
xlabel('Species Name');
|
||||
ylabel('Concentration [kmol/m^2]');
|
||||
title('Surface Species Concentrations');
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Concentrations')
|
||||
% bar(c);
|
||||
% colormap(summer);
|
||||
% nm = speciesNames(s);
|
||||
% set(gca, 'XTickLabel', nm);
|
||||
% xlabel('Species Name');
|
||||
% ylabel('Concentration [kmol/m^2]');
|
||||
% title('Surface Species Concentrations');
|
||||
% end
|
||||
end
|
||||
|
||||
function set.coverages(s, cov, norm)
|
||||
|
||||
@ -240,14 +240,14 @@ classdef Kinetics < handle
|
||||
pt = libpointer('doublePtr', xx);
|
||||
calllib(ct, 'kin_getCreationRates', kin.kin_id, nsp, pt);
|
||||
cdot = pt.Value;
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Creation Rates')
|
||||
bar(q)
|
||||
xlabel('Species Number')
|
||||
ylabel('Creation Rate [kmol/m^3-s]')
|
||||
title('Species Chemical Reaction Rates')
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Creation Rates')
|
||||
% bar(q)
|
||||
% xlabel('Species Number')
|
||||
% ylabel('Creation Rate [kmol/m^3-s]')
|
||||
% title('Species Chemical Reaction Rates')
|
||||
% end
|
||||
end
|
||||
|
||||
function ddot = destructionRates(kin)
|
||||
@ -264,14 +264,14 @@ classdef Kinetics < handle
|
||||
pt = libpointer('doublePtr', xx);
|
||||
calllib(ct, 'kin_getDestructionRates', kin.kin_id, nsp, pt);
|
||||
ddot = pt.Value;
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Destruction Rates')
|
||||
bar(q)
|
||||
xlabel('Species Number')
|
||||
ylabel('Destruction Rate [kmol/m^3-s]')
|
||||
title('Species Chemical Reaction Rates')
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Destruction Rates')
|
||||
% bar(q)
|
||||
% xlabel('Species Number')
|
||||
% ylabel('Destruction Rate [kmol/m^3-s]')
|
||||
% title('Species Chemical Reaction Rates')
|
||||
% end
|
||||
end
|
||||
|
||||
function wdot = netProdRates(kin)
|
||||
@ -288,14 +288,14 @@ classdef Kinetics < handle
|
||||
pt = libpointer('doublePtr', xx);
|
||||
calllib(ct, 'kin_getNetProductionRates', kin.kin_id, nsp, pt);
|
||||
wdot = pt.Value;
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Production Rates')
|
||||
bar(q)
|
||||
xlabel('Species Number')
|
||||
ylabel('Net Production Rate [kmol/m^3-s]')
|
||||
title('Species Net Chemical Reaction Rates')
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Production Rates')
|
||||
% bar(q)
|
||||
% xlabel('Species Number')
|
||||
% ylabel('Net Production Rate [kmol/m^3-s]')
|
||||
% title('Species Net Chemical Reaction Rates')
|
||||
% end
|
||||
end
|
||||
|
||||
function q = rop_f(kin)
|
||||
@ -312,14 +312,14 @@ classdef Kinetics < handle
|
||||
pt = libpointer('doublePtr', xx);
|
||||
calllib(ct, 'kin_getFwdRateOfProgress', kin.kin_id, nr, pt);
|
||||
q = pt.Value;
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Rates of Progress')
|
||||
bar(q)
|
||||
xlabel('Reaction Number')
|
||||
ylabel('Forward Rate of Progress [kmol/m^3]')
|
||||
title('Forward Rates of Progress')
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Rates of Progress')
|
||||
% bar(q)
|
||||
% xlabel('Reaction Number')
|
||||
% ylabel('Forward Rate of Progress [kmol/m^3]')
|
||||
% title('Forward Rates of Progress')
|
||||
% end
|
||||
end
|
||||
|
||||
function q = rop_r(kin)
|
||||
@ -336,14 +336,14 @@ classdef Kinetics < handle
|
||||
pt = libpointer('doublePtr', xx);
|
||||
calllib(ct, 'kin_getRevRateOfProgress', kin.kin_id, nr, pt);
|
||||
q = pt.Value;
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Rates of Progress')
|
||||
bar(q)
|
||||
xlabel('Reaction Number')
|
||||
ylabel('Reverse Rate of Progress [kmol/m^3]')
|
||||
title('Reverse Rates of Progress')
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Rates of Progress')
|
||||
% bar(q)
|
||||
% xlabel('Reaction Number')
|
||||
% ylabel('Reverse Rate of Progress [kmol/m^3]')
|
||||
% title('Reverse Rates of Progress')
|
||||
% end
|
||||
end
|
||||
|
||||
function q = rop(kin)
|
||||
@ -360,15 +360,15 @@ classdef Kinetics < handle
|
||||
f = rop_f(kin);
|
||||
r = rop_r(kin);
|
||||
q = [f, r];
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Rates of Progress')
|
||||
bar(q)
|
||||
xlabel('Reaction Number')
|
||||
ylabel('Rate of Progress [kmol/m^3]')
|
||||
title('Rates of Progress')
|
||||
legend('Forward', 'Reverse')
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Rates of Progress')
|
||||
% bar(q)
|
||||
% xlabel('Reaction Number')
|
||||
% ylabel('Rate of Progress [kmol/m^3]')
|
||||
% title('Rates of Progress')
|
||||
% legend('Forward', 'Reverse')
|
||||
% end
|
||||
end
|
||||
|
||||
function q = rop_net(kin)
|
||||
@ -385,14 +385,14 @@ classdef Kinetics < handle
|
||||
pt = libpointer('doublePtr', xx);
|
||||
calllib(ct, 'kin_getNetRatesOfProgress', kin.kin_id, nr, pt);
|
||||
q = pt.Value;
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Rates of Progress')
|
||||
bar(q)
|
||||
xlabel('Reaction Number')
|
||||
ylabel('Net Rate of Progress [kmol/m^3]')
|
||||
title('Net Rates of Progress')
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Rates of Progress')
|
||||
% bar(q)
|
||||
% xlabel('Reaction Number')
|
||||
% ylabel('Net Rate of Progress [kmol/m^3]')
|
||||
% title('Net Rates of Progress')
|
||||
% end
|
||||
end
|
||||
|
||||
function rxn = reactionEqn(kin, irxn)
|
||||
@ -492,14 +492,14 @@ classdef Kinetics < handle
|
||||
pt = libpointer('doublePtr', xx);
|
||||
calllib(ct, 'kin_getEquilibriumConstants', kin.kin_id, nr, pt);
|
||||
k = pt.Value;
|
||||
if nargout == 0
|
||||
figure
|
||||
set(gcf, 'Name', 'Equilibrium Constants')
|
||||
bar(k)
|
||||
xlabel('Reaction Number')
|
||||
ylabel('log_{10} Kc [kmol,m, s]')
|
||||
title('Equilibrium Constants')
|
||||
end
|
||||
% if nargout == 0
|
||||
% figure
|
||||
% set(gcf, 'Name', 'Equilibrium Constants')
|
||||
% bar(k)
|
||||
% xlabel('Reaction Number')
|
||||
% ylabel('log_{10} Kc [kmol,m, s]')
|
||||
% title('Equilibrium Constants')
|
||||
% end
|
||||
end
|
||||
|
||||
function k = get.Kf(kin)
|
||||
|
||||
@ -2,4 +2,3 @@ function w = Water()
|
||||
% Return an object representing water.
|
||||
w = Solution('liquidvapor.yaml', 'water');
|
||||
end
|
||||
|
||||
|
||||
@ -115,7 +115,7 @@ for i = 2:length(x_calc)
|
||||
%--------------------------------------------------------------------------
|
||||
%--------------------------------------------------------------------------
|
||||
% These values are passed onto the ode15s solver
|
||||
[~,y] = ode15s(@PFR_Solver, limits, inlet_soln, options,...,
|
||||
[~,y] = ode15s(@PFR_Solver, limits, inlet_soln, options, ...
|
||||
gas_calc, mdot_calc, A_in, dAdx, k);
|
||||
|
||||
T_calc(i) = y(end, 2);
|
||||
|
||||
@ -47,7 +47,7 @@ gas = Solution(rxnmech, 'gri30', 'Mix');
|
||||
gas.TPX = {tin, p, comp2};
|
||||
|
||||
%% Create the flow object
|
||||
|
||||
%
|
||||
f = AxisymmetricFlow(gas,'flow');
|
||||
f.setPressure(p);
|
||||
f.setupGrid(initial_grid);
|
||||
@ -65,7 +65,7 @@ inlet_o.setMdot(mdot_o);
|
||||
inlet_o.setMoleFractions(comp1);
|
||||
|
||||
%% Create the fuel inlet
|
||||
|
||||
%
|
||||
inlet_f = Inlet('fuel_inlet');
|
||||
inlet_f.T = tin;
|
||||
inlet_f.setMdot(mdot_f);
|
||||
|
||||
Loading…
Reference in New Issue
Block a user