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cantera/samples/python/flames/flame_fixed_T/output_blessed_0.txt
Ray Speth 2528df0f75 Reorganized source tree structure 
These changes make it unnecessary to copy header files around during
the build process, which tends to confuse IDEs and debuggers. The
headers which comprise Cantera's external C++ interface are now in
the 'include' directory.

All of the samples and demos are now in the 'samples' subdirectory.
2012-02-12 02:27:14 +00:00

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read 69 temperature values.
>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> burner <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<
Mass Flux: 0.04 kg/m^2/s
Temperature: 373.7 K
Mass Fractions:
O2 0.2166
CH4 0.07057
N2 0.7129
>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> flame <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<
Pressure: 1.013e+05 Pa
-------------------------------------------------------------------------------
z u V T lambda H2
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z H O O2 OH H2O
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z HO2 H2O2 C CH CH2
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z CH2(S) CH3 CH4 CO CO2
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z HCO CH2O CH2OH CH3O CH3OH
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z C2H C2H2 C2H3 C2H4 C2H5
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z C2H6 HCCO CH2CO HCCOH N
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z NH NH2 NH3 NNH NO
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z NO2 N2O HNO CN HCN
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z H2CN HCNN HCNO HOCN HNCO
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z NCO N2 AR C3H7 C3H8
-------------------------------------------------------------------------------
0 0 0 0 0 0
0.0025 0 0 0 0 0
0.005 0 0 0 0 0
0.0075 0 0 0 0 0
0.0099 0 0 0 0 0
0.01 0 0 0 0 0
-------------------------------------------------------------------------------
z CH2CHO CH3CHO
-------------------------------------------------------------------------------
0 0 0
0.0025 0 0
0.005 0 0
0.0075 0 0
0.0099 0 0
0.01 0 0
>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> outlet <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<
-------------------------------------------------------------------------------
z outlet dummy
-------------------------------------------------------------------------------
0 0
..............................................................................
Attempt Newton solution of steady-state problem... failure.
..............................................................................
Take 1 timesteps 3.75e-06 1.691
..............................................................................
Attempt Newton solution of steady-state problem... failure.
..............................................................................
Take 2 timesteps 8.438e-06 1.217
..............................................................................
Attempt Newton solution of steady-state problem... failure.
..............................................................................
Take 5 timesteps 6.407e-05 1.135
..............................................................................
Attempt Newton solution of steady-state problem... failure.
..............................................................................
Take 10 timesteps 0.001847 0.2885
..............................................................................
Attempt Newton solution of steady-state problem... failure.
..............................................................................
Take 20 timesteps 1.536 -0.6442
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [6] point grid(s).
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3
to resolve C2H2 C2H3 C2H4 C2H5 C2H6 C3H8 CH2 CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH CH4 CO CO2 H H2 H2O H2O2 HCCO HCCOH HCN HCNO HCO HNCO HO2 NH3 NO O O2 OH point 3
..............................................................................
Attempt Newton solution of steady-state problem... failure.
..............................................................................
Take 1 timesteps 0.0001406 0.8491
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [10] point grid(s).
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3 7
to resolve C2H2 C2H3 C2H4 C2H5 C2H6 C3H7 C3H8 CH2 CH2(S) CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH CH4 CO CO2 H H2 H2O H2O2 HCCO HCCOH HCN HCO HNCO HO2 NH3 NO O O2 OH point 7
..............................................................................
Attempt Newton solution of steady-state problem... failure.
..............................................................................
Take 1 timesteps 0.0002109 0.8033
..............................................................................
Attempt Newton solution of steady-state problem... failure.
..............................................................................
Take 2 timesteps 0.0004745 0.746
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [15] point grid(s).
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3 4 5 12
to resolve C2H2 C2H3 C2H4 C2H5 C2H6 C3H7 C3H8 CH2 CH2(S) CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH CO H H2O2 HCCO HCCOH HCO HO2 NO2 O OH point 12
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [22] point grid(s).
##############################################################################
Refining grid in flame.
New points inserted after grid points 1 2 3 4 5 6 7 8 19
to resolve C2H3 C2H5 C2H6 C3H8 CH2 CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH H H2O2 HCCO HCO NO2 O OH point 19
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [31] point grid(s).
no new points needed in flame
Solution saved to file ch4_flame_fixed_T.xml as solution mixav.
switching to multicomponent transport...
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [31] point grid(s).
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22
to resolve C2H2 C2H3 C2H4 C2H5 C2H6 C3H8 CH2 CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH CH4 H H2 H2O H2O2 HCCO HCCOH HCO HO2 NO2 O OH
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [54] point grid(s).
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 34 35 36 40
to resolve C2H3 C2H5 C3H8 CH2 CH3 CH3CHO H H2O2 HCCO HCO O OH
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [75] point grid(s).
no new points needed in flame
Solution saved to file ch4_flame_fixed_T.xml as solution multi.
solution saved to flame_fixed_T.csv
Statistics:
Grid Functions Time Jacobians Time
8 410 0.6800 15 1.0000
12 94 0.2100 16 2.0200
17 20 0.0800 3 0.6300
24 4 0.0100 1 0.3200
33 2 0.0100 1 0.4900
33 2 0.8300 1 0.7700
56 15 8.8300 2 1.9000
77 2 1.6400 1 1.4300
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