Exemplo n.º 1
0
# set the properties at the burner
f.burner.set(massflux=mdot, mole_fractions=comp, temperature=tburner)

f.set(tol=tol_ss, tol_time=tol_ts)
f.setMaxJacAge(5, 10)
f.set(energy='off')
f.init()
f.showSolution()

f.solve(loglevel, refine_grid)

f.setRefineCriteria(ratio=200.0, slope=0.0502, curve=0.1)
f.set(energy='on')
f.solve(loglevel, refine_grid)

f.save('flame1.xml')
f.showSolution()

# write the velocity, temperature, and mole fractions to a CSV file
z = f.flame.grid()
T = f.T()
u = f.u()
V = f.V()
fcsv = open('flame1.csv', 'w')
writeCSV(fcsv, ['z (m)', 'u (m/s)', 'V (1/s)', 'T (K)', 'rho (kg/m3)'] +
         list(gas.speciesNames()))
for n in range(f.flame.nPoints()):
    f.setGasState(n)
    writeCSV(fcsv,
             [z[n], u[n], V[n], T[n], gas.density()] +
             list(gas.moleFractions()))
Exemplo n.º 2
0
f.set(tol=tol_ss, tol_time=tol_ts)

# show the initial estimate for the solution
f.showSolution()

# don't solve the energy equation
f.set(energy='off')

# first solve the flame with mixture-averaged transport properties
f.setRefineCriteria(ratio=3.0, slope=0.3, curve=1)
f.setMaxJacAge(50, 50)
f.setTimeStep(1.0e-5, [1, 2, 5, 10, 20])

f.solve(loglevel, refine_grid)
f.save('ch4_flame_fixed_T.xml', 'mixav',
       'solution with mixture-averaged transport')

print '\n\n switching to multicomponent transport...\n\n'
gas.switchTransportModel('Multi')
f.flame.setTransportModel(gas)

f.setRefineCriteria(ratio=3.0, slope=0.1, curve=0.2)
f.solve(loglevel, refine_grid)
f.save('ch4_flame_fixed_T.xml', 'multi',
       'solution with  multicomponent transport')

# write the velocity, temperature, density, and mole fractions to a CSV file
z = f.flame.grid()
T = f.T()
u = f.u()
V = f.V()
Exemplo n.º 3
0
f = BurnerFlame(gas=gas, grid=initial_grid)

# set the properties at the burner
f.burner.set(massflux=mdot, mole_fractions=comp, temperature=tburner)

f.set(tol=tol_ss, tol_time=tol_ts)
f.showSolution()

f.set(energy='off')
f.setRefineCriteria(ratio=10.0, slope=1, curve=1)
f.setMaxJacAge(50, 50)
f.setTimeStep(1.0e-5, [1, 2, 5, 10, 20])

f.solve(loglevel, refine_grid)
f.save('ch4_flame1.xml', 'no_energy',
       'solution with the energy equation disabled')

f.set(energy='on')
f.setRefineCriteria(ratio=3.0, slope=0.1, curve=0.2)
f.solve(loglevel, refine_grid)
f.save('ch4_flame1.xml', 'energy', 'solution with the energy equation enabled')

gas.switchTransportModel('Multi')
f.flame.setTransportModel(gas)
f.solve(loglevel, refine_grid)
f.save(
    'ch4_flame1.xml', 'energy_multi',
    'solution with the energy equation enabled and multicomponent transport')
f.flame.enableSoret()
f.solve(loglevel, refine_grid)
f.save(
Exemplo n.º 4
0
# set the properties at the burner
f.burner.set(massflux = mdot, mole_fractions = comp, temperature = tburner)

f.set(tol = tol_ss, tol_time = tol_ts)
f.setMaxJacAge(5, 10)
f.set(energy = 'off')
f.init()
f.showSolution()

f.solve(loglevel, refine_grid)

f.setRefineCriteria(ratio = 200.0, slope = 0.0502, curve = 0.1)
f.set(energy = 'on')
f.solve(loglevel,refine_grid)

f.save('flame1.xml')
f.showSolution()


# write the velocity, temperature, and mole fractions to a CSV file
z = f.flame.grid()
T = f.T()
u = f.u()
V = f.V()
fcsv = open('flame1.csv','w')
writeCSV(fcsv, ['z (m)', 'u (m/s)', 'V (1/s)', 'T (K)', 'rho (kg/m3)']
         + list(gas.speciesNames()))
for n in range(f.flame.nPoints()):
    f.setGasState(n)
    writeCSV(fcsv, [z[n], u[n], V[n], T[n], gas.density()]
             +list(gas.moleFractions()))
Exemplo n.º 5
0
f.set(tol = tol_ss, tol_time = tol_ts)

# show the initial estimate for the solution
f.showSolution()

# don't solve the energy equation
f.set(energy = 'off')

# first solve the flame with mixture-averaged transport properties
f.setRefineCriteria(ratio = 3.0, slope = 0.3, curve = 1)
f.setMaxJacAge(50, 50)
f.setTimeStep(1.0e-5, [1, 2, 5, 10, 20])

f.solve(loglevel, refine_grid)
f.save('ch4_flame_fixed_T.xml','mixav',
       'solution with mixture-averaged transport')

print '\n\n switching to multicomponent transport...\n\n'
gas.switchTransportModel('Multi')
f.flame.setTransportModel(gas)

f.setRefineCriteria(ratio = 3.0, slope = 0.1, curve = 0.2)
f.solve(loglevel, refine_grid)
f.save('ch4_flame_fixed_T.xml','multi',
       'solution with  multicomponent transport')

# write the velocity, temperature, density, and mole fractions to a CSV file
z = f.flame.grid()
T = f.T()
u = f.u()
V = f.V()
Exemplo n.º 6
0
f = BurnerFlame(gas = gas, grid = initial_grid)

# set the properties at the burner
f.burner.set(massflux = mdot, mole_fractions = comp, temperature = tburner)

f.set(tol = tol_ss, tol_time = tol_ts)
f.showSolution()

f.set(energy = 'off')
f.setRefineCriteria(ratio = 10.0, slope = 1, curve = 1)
f.setMaxJacAge(50, 50)
f.setTimeStep(1.0e-5, [1, 2, 5, 10, 20])

f.solve(loglevel, refine_grid)
f.save('ch4_flame1.xml','no_energy',
       'solution with the energy equation disabled')

f.set(energy = 'on')
f.setRefineCriteria(ratio = 3.0, slope = 0.1, curve = 0.2)
f.solve(loglevel, refine_grid)
f.save('ch4_flame1.xml','energy',
       'solution with the energy equation enabled')

gas.switchTransportModel('Multi')
f.flame.setTransportModel(gas)
f.solve(loglevel, refine_grid)
f.save('ch4_flame1.xml','energy_multi',
       'solution with the energy equation enabled and multicomponent transport')
f.flame.enableSoret()
f.solve(loglevel, refine_grid)
f.save('ch4_flame1.xml','energy_multi_soret',