Enter phi: 1 2225.32


>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> - <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<

    Mass Flux:       0.3368 kg/m^2/s 
    Temperature:        300 K 
    Mass Fractions: 
                      O2      0.2201 
                     CH4     0.05519 
                      N2      0.7248 



>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> flame <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<

    Pressure:   1.013e+05 Pa 

-------------------------------------------------------------------------------
        z             u           V           T      lambda          H2 
-------------------------------------------------------------------------------
          0         0.3           0         300           0           0 
      0.005      0.9605           0       954.9           0   9.044e-05 
       0.01       1.621           0        1610           0   0.0001809 
      0.015       2.242           0        2225           0   0.0002659 
       0.02       2.242           0        2225           0   0.0002659 
      0.021       2.242           0        2225           0   0.0002659 

-------------------------------------------------------------------------------
        z             H           O          O2          OH         H2O 
-------------------------------------------------------------------------------
          0           0           0      0.2201           0           0 
      0.005   4.883e-06   4.252e-05       0.147   0.0006044     0.04099 
       0.01   9.765e-06   8.504e-05     0.07399    0.001209     0.08197 
      0.015   1.436e-05    0.000125    0.005339    0.001777      0.1205 
       0.02   1.436e-05    0.000125    0.005339    0.001777      0.1205 
      0.021   1.436e-05    0.000125    0.005339    0.001777      0.1205 

-------------------------------------------------------------------------------
        z           HO2        H2O2           C          CH         CH2 
-------------------------------------------------------------------------------
          0           0           0           0           0           0 
      0.005   2.026e-07   1.918e-08   3.317e-18   5.463e-19   1.726e-18 
       0.01   4.051e-07   3.837e-08   6.634e-18   1.093e-18   3.451e-18 
      0.015   5.955e-07    5.64e-08   9.752e-18   1.606e-18   5.074e-18 
       0.02   5.955e-07    5.64e-08   9.752e-18   1.606e-18   5.074e-18 
      0.021   5.955e-07    5.64e-08   9.752e-18   1.606e-18   5.074e-18 

-------------------------------------------------------------------------------
        z        CH2(S)         CH3         CH4          CO         CO2 
-------------------------------------------------------------------------------
          0           0           0     0.05519           0           0 
      0.005   1.046e-19   1.175e-17     0.03642    0.003132     0.04657 
       0.01   2.091e-19    2.35e-17     0.01764    0.006265     0.09315 
      0.015   3.074e-19   3.454e-17   1.802e-17    0.009209      0.1369 
       0.02   3.074e-19   3.454e-17   1.802e-17    0.009209      0.1369 
      0.021   3.074e-19   3.454e-17   1.802e-17    0.009209      0.1369 

-------------------------------------------------------------------------------
        z           HCO        CH2O       CH2OH        CH3O       CH3OH 
-------------------------------------------------------------------------------
          0           0           0           0           0           0 
      0.005   2.873e-10   4.948e-12   1.597e-17   2.551e-19   1.403e-18 
       0.01   5.747e-10   9.895e-12   3.193e-17   5.102e-19   2.807e-18 
      0.015   8.447e-10   1.455e-11   4.694e-17   7.501e-19   4.126e-18 
       0.02   8.447e-10   1.455e-11   4.694e-17   7.501e-19   4.126e-18 
      0.021   8.447e-10   1.455e-11   4.694e-17   7.501e-19   4.126e-18 

-------------------------------------------------------------------------------
        z           C2H        C2H2        C2H3        C2H4        C2H5 
-------------------------------------------------------------------------------
          0           0           0           0           0           0 
      0.005   1.156e-24   3.007e-22   2.367e-27   2.573e-27   2.896e-32 
       0.01   2.312e-24   6.014e-22   4.734e-27   5.145e-27   5.791e-32 
      0.015   3.399e-24    8.84e-22   6.959e-27   7.563e-27   8.513e-32 
       0.02   3.399e-24    8.84e-22   6.959e-27   7.563e-27   8.513e-32 
      0.021   3.399e-24    8.84e-22   6.959e-27   7.563e-27   8.513e-32 

-------------------------------------------------------------------------------
        z          C2H6        HCCO       CH2CO       HCCOH           N 
-------------------------------------------------------------------------------
          0           0           0           0           0           0 
      0.005   2.182e-33   2.762e-20   3.758e-20   3.683e-23   2.469e-09 
       0.01   4.365e-33   5.523e-20   7.515e-20   7.365e-23   4.937e-09 
      0.015   6.416e-33   8.119e-20   1.105e-19   1.083e-22   7.258e-09 
       0.02   6.416e-33   8.119e-20   1.105e-19   1.083e-22   7.258e-09 
      0.021   6.416e-33   8.119e-20   1.105e-19   1.083e-22   7.258e-09 

-------------------------------------------------------------------------------
        z            NH         NH2         NH3         NNH          NO 
-------------------------------------------------------------------------------
          0           0           0           0           0           0 
      0.005   4.394e-10   1.875e-10   5.707e-10   2.721e-10   0.0006988 
       0.01   8.789e-10    3.75e-10   1.141e-09   5.443e-10    0.001398 
      0.015   1.292e-09   5.512e-10   1.678e-09       8e-10    0.002055 
       0.02   1.292e-09   5.512e-10   1.678e-09       8e-10    0.002055 
      0.021   1.292e-09   5.512e-10   1.678e-09       8e-10    0.002055 

-------------------------------------------------------------------------------
        z           NO2         N2O         HNO          CN         HCN 
-------------------------------------------------------------------------------
          0           0           0           0           0           0 
      0.005   1.956e-07   5.439e-08    1.29e-08   2.198e-14   6.529e-12 
       0.01   3.911e-07   1.088e-07    2.58e-08   4.396e-14   1.306e-11 
      0.015    5.75e-07   1.599e-07   3.793e-08   6.462e-14   1.919e-11 
       0.02    5.75e-07   1.599e-07   3.793e-08   6.462e-14   1.919e-11 
      0.021    5.75e-07   1.599e-07   3.793e-08   6.462e-14   1.919e-11 

-------------------------------------------------------------------------------
        z          H2CN        HCNN        HCNO        HOCN        HNCO 
-------------------------------------------------------------------------------
          0           0           0           0           0           0 
      0.005   1.924e-18   6.749e-22   5.464e-17   6.064e-13   2.073e-10 
       0.01   3.847e-18    1.35e-21   1.093e-16   1.213e-12   4.145e-10 
      0.015   5.656e-18   1.984e-21   1.606e-16   1.783e-12   6.094e-10 
       0.02   5.656e-18   1.984e-21   1.606e-16   1.783e-12   6.094e-10 
      0.021   5.656e-18   1.984e-21   1.606e-16   1.783e-12   6.094e-10 

-------------------------------------------------------------------------------
        z           NCO          N2          AR        C3H7        C3H8 
-------------------------------------------------------------------------------
          0           0      0.7248           0           0           0 
      0.005   8.061e-12      0.7244           0    1.96e-47    1.38e-48 
       0.01   1.612e-11      0.7241           0   3.921e-47    2.76e-48 
      0.015    2.37e-11      0.7238           0   5.763e-47   4.057e-48 
       0.02    2.37e-11      0.7238           0   5.763e-47   4.057e-48 
      0.021    2.37e-11      0.7238           0   5.763e-47   4.057e-48 

-------------------------------------------------------------------------------
        z        CH2CHO      CH3CHO 
-------------------------------------------------------------------------------
          0           0           0 
      0.005   1.601e-25   3.258e-26 
       0.01   3.203e-25   6.517e-26 
      0.015   4.708e-25    9.58e-26 
       0.02   4.708e-25    9.58e-26 
      0.021   4.708e-25    9.58e-26 


>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> - <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<


-------------------------------------------------------------------------------
        z    outlet dummy 
-------------------------------------------------------------------------------
          0           0 
T in between 300 and 954.871
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 1 timesteps      3.75e-06      2.669 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 2 timesteps     4.219e-06      1.819 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 5 timesteps     8.009e-06      1.453 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     2.887e-05       1.36 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps       1.3e-05      2.469 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     1.172e-05      2.477 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [7] point grid(s).

grid refinement disabled.
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [7] point grid(s).

##############################################################################
Refining grid in flame.
    New points inserted after grid points 0 1 2 3 
    to resolve C C2H C2H2 C2H3 C2H4 C2H5 C2H6 C3H7 C3H8 CH CH2 CH2(S) CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH CH4 CN CO CO2 H H2 H2O H2O2 HCCO HCCOH HCN HCNO HCO HNCO HNO HO2 HOCN N N2O NCO NH NH2 NH3 NNH NO NO2 O O2 OH T point 0 point 2 u 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 1 timesteps       7.5e-06      6.312 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 2 timesteps     8.438e-06      5.874 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 5 timesteps     1.602e-05      5.367 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     2.887e-05      6.143 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps       1.3e-05       5.96 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [11] point grid(s).

##############################################################################
Refining grid in flame.
    New points inserted after grid points 0 1 2 3 4 5 
    to resolve C C2H C2H2 C2H3 C2H4 C2H5 C2H6 C3H7 C3H8 CH CH2 CH2(S) CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH CH4 CN CO CO2 H H2 H2O H2O2 HCCO HCCOH HCN HCNO HCO HNCO HNO HO2 HOCN N N2O NCO NH NH2 NH3 NNH NO NO2 O O2 OH T point 1 point 4 u 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 1 timesteps     9.753e-06      6.642 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 2 timesteps     1.097e-05      6.231 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 5 timesteps     5.207e-06      6.369 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     4.692e-06      6.297 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [17] point grid(s).

##############################################################################
Refining grid in flame.
    New points inserted after grid points 2 3 5 6 7 8 9 
    to resolve C C2H C2H2 C2H3 C2H4 C2H5 C2H6 C3H7 C3H8 CH CH2 CH2(S) CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH CH4 CN CO CO2 H H2 H2O H2O2 HCCO HCCOH HCN HCNN HCNO HCO HNCO HNO HO2 HOCN N N2O NCO NH NH2 NH3 NNH NO NO2 O O2 OH T point 3 point 8 u 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 1 timesteps     3.519e-06       6.98 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 2 timesteps     3.959e-06      6.734 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 5 timesteps     3.758e-06      6.646 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     6.772e-06      6.115 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     2.441e-05      5.613 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     0.0001759      4.849 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     0.0001585      4.722 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps      3.57e-05      5.598 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     8.043e-06      6.731 
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 10 timesteps     7.246e-06      6.466 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [24] point grid(s).

##############################################################################
Refining grid in flame.
    New points inserted after grid points 4 5 6 7 8 9 10 11 12 13 14 
    to resolve C C2H C2H2 C2H3 C2H4 C2H5 C2H6 C3H7 C3H8 CH CH2 CH2(S) CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH CH4 CN CO H H2 H2CN H2O H2O2 HCCO HCCOH HCN HCNN HCNO HCO HNCO HNO HO2 HOCN N NCO NH NH2 NH3 NNH NO2 O O2 OH T point 13 u 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [35] point grid(s).

##############################################################################
Refining grid in flame.
    New points inserted after grid points 6 7 8 9 10 11 12 13 14 15 16 17 18 19 22 
    to resolve C C2H C2H2 C2H3 C2H4 C2H5 C2H6 C3H7 C3H8 CH CH2 CH2(S) CH2CHO CH2CO CH2O CH2OH CH3 CH3CHO CH3O CH3OH CH4 CN CO H2 H2CN H2O H2O2 HCCO HCCOH HCN HCNN HCO HNCO HNO HO2 HOCN N NCO NH NH3 NO2 T point 22 u 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [50] point grid(s).

##############################################################################
Refining grid in flame.
    New points inserted after grid points 7 8 9 12 13 36 
    to resolve C2H4 C2H5 C2H6 C3H7 C3H8 CH2CHO CH2O CH3 CH3CHO CH3O CH3OH CN CO H2O2 HO2 HOCN NCO NH NH3 NO2 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [56] point grid(s).

##############################################################################
Refining grid in flame.
    New points inserted after grid points 9 10 11 12 41 
    to resolve C2H4 C2H6 C3H7 C3H8 CH2CHO CH2O CH3O CH3OH CN H2O2 HO2 NCO NO2 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [61] point grid(s).

##############################################################################
Refining grid in flame.
    New points inserted after grid points 12 13 14 15 16 
    to resolve C3H8 CH2CHO CH3O NO2 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [66] point grid(s).

no new points needed in flame
Flame speed with mixture-averaged transport: 0.387255 m/s
..............................................................................

Attempt Newton solution of steady-state problem...    failure. 

..............................................................................
Take 1 timesteps      3.75e-06      5.758 
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [66] point grid(s).

no new points needed in flame
Flame speed with multicomponent transport: 0.392151 m/s
..............................................................................

Attempt Newton solution of steady-state problem...    success.

Problem solved on [66] point grid(s).

no new points needed in flame
Flame speed with multicomponent transport + Soret: 0.39215 m/s

    z (m)	   T (K)	U (m/s)	  Y(CO)
 0.000000	 300.000	0.392	0.00000
 0.001145	 300.000	0.392	0.00000
 0.002291	 300.002	0.392	0.00000
 0.002863	 300.015	0.392	0.00000
 0.003436	 300.158	0.393	0.00000
 0.003722	 300.765	0.394	0.00001
 0.004008	 304.365	0.399	0.00008
 0.004152	 312.675	0.411	0.00026
 0.004223	 324.053	0.426	0.00050
 0.004295	 347.691	0.458	0.00103
 0.004331	 368.328	0.486	0.00151
 0.004366	 398.192	0.526	0.00223
 0.004402	 439.859	0.582	0.00325
 0.004420	 466.246	0.618	0.00393
 0.004438	 496.834	0.659	0.00474
 0.004456	 531.832	0.707	0.00568
 0.004474	 571.364	0.760	0.00678
 0.004492	 615.466	0.820	0.00804
 0.004509	 664.081	0.886	0.00947
 0.004527	 717.075	0.958	0.01108
 0.004545	 774.239	1.035	0.01288
 0.004563	 835.315	1.119	0.01487
 0.004581	 900.000	1.207	0.01706
 0.004607	1000.385	1.344	0.02056
 0.004633	1106.461	1.489	0.02443
 0.004647	1161.011	1.564	0.02655
 0.004660	1216.241	1.641	0.02874
 0.004673	1271.756	1.717	0.03100
 0.004686	1327.105	1.793	0.03329
 0.004699	1381.783	1.869	0.03558
 0.004712	1435.243	1.943	0.03785
 0.004725	1486.908	2.015	0.04002
 0.004738	1536.197	2.083	0.04206
 0.004751	1582.549	2.147	0.04391
 0.004764	1625.459	2.206	0.04551
 0.004777	1664.517	2.260	0.04680
 0.004791	1699.443	2.308	0.04774
 0.004804	1730.117	2.350	0.04832
 0.004817	1756.596	2.386	0.04853
 0.004830	1779.104	2.416	0.04838
 0.004843	1798.010	2.441	0.04791
 0.004856	1813.777	2.462	0.04718
 0.004869	1826.914	2.479	0.04623
 0.004882	1837.921	2.493	0.04514
 0.004895	1847.254	2.504	0.04396
 0.004908	1855.303	2.514	0.04272
 0.004921	1862.379	2.522	0.04149
 0.004935	1868.724	2.529	0.04027
 0.004948	1874.519	2.535	0.03909
 0.004974	1884.859	2.547	0.03690
 0.005000	1894.157	2.557	0.03497
 0.005039	1906.651	2.570	0.03254
 0.005078	1917.968	2.582	0.03058
 0.005156	1937.747	2.604	0.02781
 0.005312	1969.272	2.640	0.02485
 0.005625	2013.447	2.692	0.02234
 0.005938	2045.633	2.730	0.02083
 0.006250	2070.220	2.759	0.01966
 0.006875	2103.487	2.797	0.01792
 0.007500	2126.991	2.824	0.01655
 0.008750	2155.560	2.857	0.01469
 0.010000	2174.268	2.878	0.01339
 0.012500	2194.717	2.900	0.01185
 0.015000	2206.910	2.914	0.01090
 0.020000	2218.182	2.926	0.01002
 0.021000	2218.182	2.926	0.01002

Adiabatic flame temperature from equilibrium is: 2225.32
Flame speed for phi=1 is 0.39215 m/s.
