Note
Go to the end to download the full example code.
Burner-stabilized flame#
A burner-stabilized lean premixed hydrogen-oxygen flame at low pressure.
Requires: cantera >= 3.0
>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> burner <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<
Mass Flux: 0.06 kg/m^2/s
Temperature: 373 K
Mass Fractions:
H2 0.00961
O2 0.1017
AR 0.8887
>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> flame <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<
Pressure: 5066 Pa
-------------------------------------------------------------------------------
z velocity spread_rate T lambda eField
-------------------------------------------------------------------------------
0 1.109 0 373 0 0
0.05 3.286 0 1182 0 0
0.1 5.463 0 1991 0 0
0.15 5.463 0 1991 0 0
0.25 5.463 0 1991 0 0
0.35 5.463 0 1991 0 0
0.5 5.463 0 1991 0 0
-------------------------------------------------------------------------------
z H2 H O O2 OH
-------------------------------------------------------------------------------
0 0.00961 0 0 0.1017 0
0.05 0.004839 3.357e-06 0.0001047 0.06338 0.000771
0.1 6.811e-05 6.714e-06 0.0002094 0.02508 0.001542
0.15 6.811e-05 6.714e-06 0.0002094 0.02508 0.001542
0.25 6.811e-05 6.714e-06 0.0002094 0.02508 0.001542
0.35 6.811e-05 6.714e-06 0.0002094 0.02508 0.001542
0.5 6.811e-05 6.714e-06 0.0002094 0.02508 0.001542
-------------------------------------------------------------------------------
z H2O HO2 H2O2 AR N2
-------------------------------------------------------------------------------
0 0 0 0 0.8887 0
0.05 0.04219 1.715e-07 5.43e-09 0.8887 0
0.1 0.08439 3.43e-07 1.086e-08 0.8887 0
0.15 0.08439 3.43e-07 1.086e-08 0.8887 0
0.25 0.08439 3.43e-07 1.086e-08 0.8887 0
0.35 0.08439 3.43e-07 1.086e-08 0.8887 0
0.5 0.08439 3.43e-07 1.086e-08 0.8887 0
-------------------------------------------------------------------------------
z
-------------------------------------------------------------------------------
0
0.05
0.1
0.15
0.25
0.35
0.5
>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> outlet <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<
-------------------------------------------------------------------------------
z
-------------------------------------------------------------------------------
0
************ Solving on 7 point grid with energy equation enabled ************
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [7] point grid(s).
..............................................................................
grid refinement disabled.
******************** Solving with grid refinement enabled ********************
..............................................................................
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 4
to resolve AR H H2 H2O H2O2 HO2 O O2 OH T velocity
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... failure.
Take 10 timesteps 0.0002563 5.067
Attempt Newton solution of steady-state problem... failure.
Take 10 timesteps 0.004379 3.912
Attempt Newton solution of steady-state problem... failure.
Take 10 timesteps 0.002338 4.368
Attempt Newton solution of steady-state problem... failure.
Take 10 timesteps 0.0006242 4.562
Attempt Newton solution of steady-state problem... failure.
Take 10 timesteps 0.01066 3.03
Attempt Newton solution of steady-state problem... success.
Problem solved on [12] point grid(s).
..............................................................................
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3 4 5 6 7 8 10
to resolve AR H H2 H2O H2O2 HO2 O O2 OH T point 10 velocity
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... failure.
Take 10 timesteps 0.0002563 4.912
Attempt Newton solution of steady-state problem... failure.
Take 10 timesteps 0.004379 3.365
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 0 1 2 3 4 5 6 12
to resolve AR H H2 H2O H2O2 HO2 O O2 OH T velocity
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [30] point grid(s).
..............................................................................
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3 4 5 6 7
to resolve AR H H2 H2O H2O2 HO2 O O2 OH T velocity
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [38] point grid(s).
..............................................................................
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3 4 5 6 7 8 9
to resolve AR H H2 H2O H2O2 HO2 O O2 OH T velocity
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [48] 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
to resolve AR H H2 H2O H2O2 HO2 O O2 OH T velocity
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [60] 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
to resolve AR H H2 H2O H2O2 HO2 O O2 OH
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [80] 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 23 24 25 26 27
to resolve AR H2O2 HO2 OH
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [98] point grid(s).
..............................................................................
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3 4 12 13 14 15 16 17 18 19 20
to resolve H2O2 HO2 OH
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [112] point grid(s).
..............................................................................
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3 4 35
to resolve H2O2 HO2
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [118] point grid(s).
..............................................................................
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3
to resolve HO2
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [122] point grid(s).
..............................................................................
##############################################################################
Refining grid in flame.
New points inserted after grid points 0 1 2 3
to resolve HO2
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [126] point grid(s).
..............................................................................
no new points needed in flame
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [126] point grid(s).
..............................................................................
##############################################################################
Refining grid in flame.
New points inserted after grid points 23 50 54
to resolve H2O2
##############################################################################
..............................................................................
Attempt Newton solution of steady-state problem... success.
Problem solved on [129] point grid(s).
..............................................................................
no new points needed in flame
>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> burner <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<
Mass Flux: 0.06 kg/m^2/s
Temperature: 373 K
Mass Fractions:
H2 0.00961
O2 0.1017
AR 0.8887
>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> flame <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<
Pressure: 5066 Pa
-------------------------------------------------------------------------------
z velocity spread_rate T lambda eField
-------------------------------------------------------------------------------
0 1.103 0 373 0 0
1.221e-05 1.104 0 373.3 0 0
2.441e-05 1.105 0 373.6 0 0
3.662e-05 1.106 0 373.9 0 0
4.883e-05 1.106 0 374.2 0 0
6.104e-05 1.107 0 374.5 0 0
7.324e-05 1.108 0 374.8 0 0
8.545e-05 1.109 0 375.1 0 0
9.766e-05 1.11 0 375.4 0 0
0.0001221 1.112 0 376 0 0
0.0001465 1.113 0 376.7 0 0
0.0001709 1.115 0 377.3 0 0
0.0001953 1.117 0 377.9 0 0
0.0002441 1.121 0 379.2 0 0
0.000293 1.124 0 380.5 0 0
0.0003418 1.128 0 381.8 0 0
0.0003906 1.132 0 383.2 0 0
0.0004395 1.136 0 384.6 0 0
0.0004883 1.14 0 386 0 0
0.0005859 1.148 0 388.8 0 0
0.0006836 1.157 0 391.7 0 0
0.0007813 1.165 0 394.8 0 0
0.0008789 1.174 0 397.9 0 0
0.0009766 1.183 0 401.1 0 0
0.001074 1.193 0 404.4 0 0
0.001172 1.203 0 407.8 0 0
0.001367 1.223 0 414.8 0 0
0.001563 1.244 0 422.2 0 0
0.001758 1.266 0 430 0 0
0.001953 1.289 0 438 0 0
0.002148 1.313 0 446.4 0 0
0.002344 1.338 0 455.1 0 0
0.002441 1.35 0 459.5 0 0
0.002539 1.363 0 464 0 0
0.002637 1.376 0 468.6 0 0
0.002734 1.389 0 473.3 0 0
0.002832 1.403 0 478 0 0
0.00293 1.416 0 482.7 0 0
0.003027 1.43 0 487.5 0 0
0.003125 1.444 0 492.4 0 0
0.003223 1.458 0 497.4 0 0
0.00332 1.472 0 502.4 0 0
0.003418 1.486 0 507.4 0 0
0.003516 1.501 0 512.5 0 0
0.003613 1.515 0 517.6 0 0
0.003711 1.53 0 522.8 0 0
0.003809 1.545 0 528 0 0
0.003906 1.559 0 533.3 0 0
0.004004 1.574 0 538.6 0 0
0.004102 1.589 0 543.9 0 0
0.004199 1.605 0 549.3 0 0
0.004297 1.62 0 554.7 0 0
0.004395 1.635 0 560.1 0 0
0.004492 1.65 0 565.6 0 0
0.004688 1.681 0 576.6 0 0
0.004883 1.713 0 587.8 0 0
0.005078 1.744 0 599 0 0
0.005273 1.776 0 610.4 0 0
0.005469 1.808 0 621.8 0 0
0.005859 1.872 0 644.9 0 0
0.00625 1.937 0 668.2 0 0
0.006641 2.002 0 691.8 0 0
0.007031 2.068 0 715.6 0 0
0.007422 2.133 0 739.6 0 0
0.007812 2.2 0 763.6 0 0
0.008203 2.266 0 787.7 0 0
0.008594 2.332 0 811.8 0 0
0.008984 2.398 0 835.7 0 0
0.00918 2.43 0 847.6 0 0
0.009375 2.463 0 859.4 0 0
0.00957 2.495 0 871.2 0 0
0.009766 2.527 0 882.8 0 0
0.009961 2.559 0 894.4 0 0
0.01016 2.591 0 905.8 0 0
0.01035 2.622 0 917 0 0
0.01055 2.653 0 928.1 0 0
0.01074 2.683 0 939 0 0
0.01094 2.713 0 949.7 0 0
0.01133 2.77 0 970.6 0 0
0.01172 2.826 0 990.6 0 0
0.01211 2.879 0 1010 0 0
0.0125 2.93 0 1028 0 0
0.01289 2.978 0 1045 0 0
0.01328 3.023 0 1061 0 0
0.01367 3.066 0 1077 0 0
0.01406 3.106 0 1091 0 0
0.01445 3.144 0 1104 0 0
0.01484 3.179 0 1117 0 0
0.01523 3.212 0 1129 0 0
0.01562 3.244 0 1140 0 0
0.01641 3.301 0 1161 0 0
0.01719 3.352 0 1179 0 0
0.01797 3.398 0 1196 0 0
0.01875 3.44 0 1212 0 0
0.02031 3.513 0 1239 0 0
0.02188 3.578 0 1262 0 0
0.02344 3.636 0 1284 0 0
0.025 3.688 0 1303 0 0
0.02656 3.736 0 1321 0 0
0.02813 3.779 0 1337 0 0
0.02969 3.82 0 1352 0 0
0.03125 3.858 0 1367 0 0
0.03438 3.925 0 1392 0 0
0.0375 3.984 0 1414 0 0
0.04063 4.038 0 1435 0 0
0.04375 4.087 0 1453 0 0
0.04688 4.131 0 1470 0 0
0.05 4.172 0 1485 0 0
0.05625 4.242 0 1512 0 0
0.0625 4.304 0 1536 0 0
0.06875 4.359 0 1557 0 0
0.075 4.408 0 1576 0 0
0.08125 4.452 0 1593 0 0
0.0875 4.492 0 1609 0 0
0.1 4.56 0 1635 0 0
0.1125 4.618 0 1658 0 0
0.125 4.669 0 1678 0 0
0.1375 4.714 0 1696 0 0
0.15 4.754 0 1711 0 0
0.1625 4.79 0 1726 0 0
0.175 4.823 0 1738 0 0
0.2 4.877 0 1760 0 0
0.225 4.924 0 1778 0 0
0.25 4.964 0 1794 0 0
0.275 4.999 0 1808 0 0
0.3 5.03 0 1821 0 0
0.35 5.079 0 1840 0 0
0.425 5.135 0 1862 0 0
0.5 5.135 0 1862 0 0
-------------------------------------------------------------------------------
z H2 H O O2 OH
-------------------------------------------------------------------------------
0 0.009214 1.187e-05 3.467e-06 0.1013 6.222e-05
1.221e-05 0.009212 1.191e-05 3.511e-06 0.1013 6.302e-05
2.441e-05 0.00921 1.195e-05 3.555e-06 0.1013 6.382e-05
3.662e-05 0.009207 1.199e-05 3.598e-06 0.1013 6.461e-05
4.883e-05 0.009205 1.203e-05 3.642e-06 0.1013 6.54e-05
6.104e-05 0.009203 1.208e-05 3.685e-06 0.1013 6.617e-05
7.324e-05 0.009201 1.212e-05 3.728e-06 0.1013 6.693e-05
8.545e-05 0.009198 1.217e-05 3.771e-06 0.1013 6.769e-05
9.766e-05 0.009196 1.222e-05 3.813e-06 0.1013 6.843e-05
0.0001221 0.009192 1.232e-05 3.898e-06 0.1012 6.989e-05
0.0001465 0.009187 1.243e-05 3.981e-06 0.1012 7.13e-05
0.0001709 0.009182 1.254e-05 4.064e-06 0.1012 7.268e-05
0.0001953 0.009178 1.266e-05 4.145e-06 0.1012 7.401e-05
0.0002441 0.009168 1.291e-05 4.305e-06 0.1012 7.656e-05
0.000293 0.009159 1.318e-05 4.461e-06 0.1011 7.896e-05
0.0003418 0.009149 1.348e-05 4.613e-06 0.1011 8.121e-05
0.0003906 0.009139 1.38e-05 4.762e-06 0.1011 8.334e-05
0.0004395 0.009129 1.414e-05 4.908e-06 0.101 8.536e-05
0.0004883 0.009119 1.45e-05 5.051e-06 0.101 8.727e-05
0.0005859 0.009098 1.529e-05 5.329e-06 0.1009 9.082e-05
0.0006836 0.009077 1.617e-05 5.599e-06 0.1008 9.409e-05
0.0007813 0.009054 1.714e-05 5.864e-06 0.1008 9.715e-05
0.0008789 0.009032 1.82e-05 6.125e-06 0.1007 0.0001
0.0009766 0.009008 1.936e-05 6.383e-06 0.1006 0.0001028
0.001074 0.008984 2.061e-05 6.642e-06 0.1005 0.0001054
0.001172 0.00896 2.196e-05 6.901e-06 0.1004 0.000108
0.001367 0.008909 2.497e-05 7.423e-06 0.1002 0.0001127
0.001563 0.008855 2.839e-05 7.957e-06 0.1 0.0001171
0.001758 0.008799 3.225e-05 8.508e-06 0.09981 0.0001211
0.001953 0.00874 3.658e-05 9.08e-06 0.09958 0.0001246
0.002148 0.008678 4.138e-05 9.678e-06 0.09934 0.0001275
0.002344 0.008614 4.667e-05 1.031e-05 0.09909 0.0001299
0.002441 0.008581 4.951e-05 1.064e-05 0.09896 0.0001309
0.002539 0.008547 5.248e-05 1.098e-05 0.09882 0.0001317
0.002637 0.008513 5.559e-05 1.134e-05 0.09869 0.0001324
0.002734 0.008478 5.882e-05 1.172e-05 0.09855 0.0001329
0.002832 0.008442 6.22e-05 1.211e-05 0.09841 0.0001333
0.00293 0.008406 6.571e-05 1.252e-05 0.09827 0.0001336
0.003027 0.008369 6.936e-05 1.297e-05 0.09812 0.0001337
0.003125 0.008331 7.315e-05 1.343e-05 0.09797 0.0001336
0.003223 0.008293 7.708e-05 1.394e-05 0.09782 0.0001335
0.00332 0.008254 8.116e-05 1.448e-05 0.09767 0.0001332
0.003418 0.008214 8.538e-05 1.506e-05 0.09751 0.0001329
0.003516 0.008174 8.975e-05 1.57e-05 0.09735 0.0001324
0.003613 0.008132 9.427e-05 1.639e-05 0.09719 0.0001319
0.003711 0.008091 9.893e-05 1.715e-05 0.09703 0.0001313
0.003809 0.008048 0.0001037 1.798e-05 0.09686 0.0001306
0.003906 0.008005 0.0001087 1.89e-05 0.09669 0.0001298
0.004004 0.007961 0.0001138 1.991e-05 0.09652 0.000129
0.004102 0.007917 0.0001191 2.103e-05 0.09635 0.0001281
0.004199 0.007871 0.0001245 2.228e-05 0.09617 0.0001272
0.004297 0.007825 0.0001301 2.366e-05 0.096 0.0001263
0.004395 0.007779 0.0001358 2.519e-05 0.09582 0.0001254
0.004492 0.007731 0.0001417 2.689e-05 0.09563 0.0001244
0.004688 0.007634 0.000154 3.086e-05 0.09525 0.0001225
0.004883 0.007534 0.0001668 3.573e-05 0.09487 0.0001207
0.005078 0.007431 0.0001804 4.167e-05 0.09446 0.000119
0.005273 0.007325 0.0001945 4.888e-05 0.09404 0.0001175
0.005469 0.007216 0.0002093 5.759e-05 0.09361 0.0001163
0.005859 0.006988 0.0002409 8.022e-05 0.09267 0.000115
0.00625 0.006748 0.000275 0.0001113 0.09165 0.0001156
0.006641 0.006495 0.0003117 0.0001526 0.09051 0.0001188
0.007031 0.00623 0.0003508 0.0002059 0.08923 0.0001254
0.007422 0.005953 0.0003922 0.0002728 0.0878 0.000136
0.007812 0.005664 0.0004357 0.0003542 0.0862 0.0001514
0.008203 0.005366 0.0004809 0.0004509 0.08441 0.0001721
0.008594 0.005059 0.0005276 0.0005627 0.08242 0.0001988
0.008984 0.004747 0.0005751 0.0006892 0.08025 0.0002318
0.00918 0.00459 0.0005989 0.0007575 0.0791 0.0002507
0.009375 0.004432 0.0006227 0.000829 0.0779 0.0002712
0.00957 0.004275 0.0006465 0.0009037 0.07666 0.0002933
0.009766 0.004119 0.00067 0.0009811 0.07539 0.0003168
0.009961 0.003963 0.0006933 0.001061 0.07408 0.0003419
0.01016 0.003809 0.0007162 0.001143 0.07275 0.0003682
0.01035 0.003657 0.0007387 0.001227 0.07139 0.0003958
0.01055 0.003507 0.0007607 0.001312 0.07002 0.0004245
0.01074 0.00336 0.000782 0.001399 0.06863 0.0004541
0.01094 0.003216 0.0008027 0.001486 0.06724 0.0004845
0.01133 0.002939 0.0008418 0.001662 0.06447 0.0005473
0.01172 0.002679 0.0008774 0.001836 0.06175 0.0006114
0.01211 0.002438 0.0009093 0.002007 0.05912 0.0006758
0.0125 0.002217 0.0009373 0.002173 0.05662 0.0007395
0.01289 0.002016 0.0009611 0.002331 0.05427 0.0008015
0.01328 0.001836 0.000981 0.00248 0.0521 0.0008613
0.01367 0.001677 0.000997 0.002619 0.0501 0.0009186
0.01406 0.001536 0.001009 0.002747 0.04829 0.0009731
0.01445 0.001414 0.001018 0.002864 0.04667 0.001025
0.01484 0.001309 0.001024 0.002971 0.04523 0.001074
0.01523 0.001219 0.001028 0.003066 0.04395 0.001121
0.01562 0.001142 0.001029 0.003151 0.04283 0.001165
0.01641 0.001024 0.001025 0.00329 0.04104 0.001247
0.01719 0.000942 0.001015 0.003396 0.03967 0.001323
0.01797 0.0008857 0.001001 0.003476 0.03863 0.001394
0.01875 0.0008478 0.0009848 0.003533 0.03785 0.00146
0.02031 0.0008102 0.0009489 0.003598 0.03682 0.00158
0.02188 0.0007952 0.0009125 0.003625 0.03614 0.001688
0.02344 0.0007903 0.0008778 0.003631 0.03564 0.001786
0.025 0.0007891 0.0008455 0.003624 0.03525 0.001876
0.02656 0.0007891 0.0008156 0.003609 0.03491 0.001959
0.02813 0.0007891 0.000788 0.003589 0.03462 0.002035
0.02969 0.0007887 0.0007625 0.003566 0.03435 0.002105
0.03125 0.0007878 0.0007388 0.003541 0.0341 0.00217
0.03438 0.0007844 0.0006966 0.003486 0.03366 0.002285
0.0375 0.0007797 0.0006595 0.003428 0.03328 0.002385
0.04063 0.000774 0.0006264 0.003368 0.03293 0.002474
0.04375 0.0007677 0.0005968 0.003309 0.03262 0.002552
0.04688 0.0007609 0.00057 0.003251 0.03234 0.002622
0.05 0.0007538 0.0005457 0.003194 0.03208 0.002684
0.05625 0.0007389 0.0005036 0.003084 0.03163 0.002787
0.0625 0.0007238 0.0004675 0.00298 0.03125 0.002871
0.06875 0.0007087 0.0004361 0.002882 0.0309 0.00294
0.075 0.0006937 0.0004086 0.00279 0.0306 0.002997
0.08125 0.0006792 0.0003841 0.002703 0.03033 0.003044
0.0875 0.000665 0.0003624 0.002621 0.03008 0.003083
0.1 0.0006383 0.0003258 0.002474 0.02966 0.003139
0.1125 0.0006131 0.0002952 0.002341 0.02931 0.003176
0.125 0.0005894 0.0002693 0.002222 0.029 0.0032
0.1375 0.0005671 0.000247 0.002113 0.02873 0.003213
0.15 0.0005462 0.0002276 0.002013 0.02849 0.003218
0.1625 0.0005266 0.0002107 0.001922 0.02828 0.003216
0.175 0.0005082 0.0001957 0.001839 0.02809 0.00321
0.2 0.0004754 0.0001712 0.001694 0.02777 0.003187
0.225 0.0004458 0.0001511 0.001568 0.0275 0.003153
0.25 0.0004191 0.0001344 0.001458 0.02728 0.003114
0.275 0.0003949 0.0001204 0.00136 0.02708 0.003071
0.3 0.000373 0.0001085 0.001274 0.02691 0.003025
0.35 0.0003363 9.016e-05 0.001132 0.02665 0.002935
0.425 0.0002952 7.174e-05 0.0009778 0.02635 0.002814
0.5 0.0002952 7.174e-05 0.0009778 0.02635 0.002814
-------------------------------------------------------------------------------
z H2O HO2 H2O2 AR N2
-------------------------------------------------------------------------------
0 0.0004611 1.998e-05 2.309e-06 0.8889 -8.588e-16
1.221e-05 0.0004691 2.039e-05 2.356e-06 0.8889 -7.649e-15
2.441e-05 0.0004772 2.076e-05 2.404e-06 0.8889 8.408e-16
3.662e-05 0.0004853 2.11e-05 2.451e-06 0.8889 -5.514e-15
4.883e-05 0.0004936 2.14e-05 2.499e-06 0.8889 -9e-15
6.104e-05 0.0005018 2.168e-05 2.547e-06 0.8889 5.501e-15
7.324e-05 0.0005102 2.193e-05 2.595e-06 0.8889 -4.136e-15
8.545e-05 0.0005185 2.215e-05 2.643e-06 0.8889 -5.641e-15
9.766e-05 0.000527 2.235e-05 2.691e-06 0.8889 4.47e-15
0.0001221 0.0005441 2.269e-05 2.786e-06 0.8889 -3.322e-15
0.0001465 0.0005614 2.295e-05 2.882e-06 0.8889 -2.42e-15
0.0001709 0.000579 2.316e-05 2.977e-06 0.8889 -4.879e-15
0.0001953 0.0005968 2.332e-05 3.072e-06 0.8889 -2.63e-15
0.0002441 0.0006332 2.351e-05 3.261e-06 0.8889 -7.327e-15
0.000293 0.0006705 2.359e-05 3.448e-06 0.8889 -5.233e-15
0.0003418 0.0007088 2.358e-05 3.632e-06 0.8889 1.963e-15
0.0003906 0.000748 2.352e-05 3.813e-06 0.8889 -9.143e-15
0.0004395 0.0007881 2.343e-05 3.99e-06 0.8889 -1.291e-14
0.0004883 0.0008292 2.331e-05 4.162e-06 0.8889 -1.079e-14
0.0005859 0.0009142 2.302e-05 4.495e-06 0.8889 -1.06e-14
0.0006836 0.001003 2.271e-05 4.808e-06 0.8889 -6.785e-15
0.0007813 0.001096 2.24e-05 5.101e-06 0.8889 -1.103e-14
0.0008789 0.001192 2.208e-05 5.371e-06 0.8889 -1.489e-14
0.0009766 0.001292 2.177e-05 5.617e-06 0.8889 5.26e-16
0.001074 0.001396 2.146e-05 5.839e-06 0.8889 -1.54e-14
0.001172 0.001505 2.114e-05 6.035e-06 0.889 -1.066e-14
0.001367 0.001733 2.05e-05 6.349e-06 0.889 -1.095e-14
0.001563 0.001977 1.985e-05 6.565e-06 0.889 1.611e-15
0.001758 0.002237 1.919e-05 6.681e-06 0.889 -6.376e-15
0.001953 0.002512 1.851e-05 6.703e-06 0.889 -1.058e-14
0.002148 0.002802 1.784e-05 6.635e-06 0.889 -1.059e-14
0.002344 0.003106 1.716e-05 6.485e-06 0.889 9.697e-15
0.002441 0.003264 1.683e-05 6.383e-06 0.889 -6.206e-15
0.002539 0.003425 1.649e-05 6.263e-06 0.889 5.68e-15
0.002637 0.00359 1.616e-05 6.127e-06 0.889 -1.251e-14
0.002734 0.003758 1.583e-05 5.975e-06 0.889 -4.64e-15
0.002832 0.00393 1.551e-05 5.81e-06 0.889 -1.836e-14
0.00293 0.004106 1.519e-05 5.633e-06 0.889 -1.366e-14
0.003027 0.004285 1.488e-05 5.445e-06 0.889 -6.491e-15
0.003125 0.004467 1.456e-05 5.248e-06 0.889 2.072e-15
0.003223 0.004653 1.426e-05 5.043e-06 0.889 1.8e-15
0.00332 0.004842 1.396e-05 4.833e-06 0.889 5.089e-15
0.003418 0.005035 1.367e-05 4.618e-06 0.889 -6.967e-15
0.003516 0.005231 1.338e-05 4.4e-06 0.889 -9.711e-15
0.003613 0.00543 1.309e-05 4.181e-06 0.889 5.845e-17
0.003711 0.005633 1.282e-05 3.962e-06 0.889 3.602e-15
0.003809 0.005839 1.255e-05 3.743e-06 0.889 -3.469e-15
0.003906 0.006048 1.228e-05 3.527e-06 0.889 -3.632e-15
0.004004 0.006261 1.203e-05 3.314e-06 0.889 -1.202e-15
0.004102 0.006478 1.178e-05 3.105e-06 0.889 3.284e-15
0.004199 0.006698 1.153e-05 2.902e-06 0.889 -7.505e-15
0.004297 0.006922 1.129e-05 2.705e-06 0.889 8.038e-15
0.004395 0.00715 1.106e-05 2.514e-06 0.889 -5.121e-15
0.004492 0.007381 1.083e-05 2.331e-06 0.8889 -1.105e-14
0.004688 0.007857 1.039e-05 1.989e-06 0.8889 1.03e-14
0.004883 0.00835 9.981e-06 1.68e-06 0.8889 1.392e-14
0.005078 0.008861 9.591e-06 1.405e-06 0.8889 6.82e-15
0.005273 0.009393 9.221e-06 1.164e-06 0.8889 1.478e-14
0.005469 0.009946 8.873e-06 9.565e-07 0.8888 3.191e-15
0.005859 0.01113 8.232e-06 6.361e-07 0.8888 -1.541e-15
0.00625 0.01241 7.66e-06 4.137e-07 0.8887 -3.164e-15
0.006641 0.01382 7.15e-06 2.673e-07 0.8886 -4.483e-15
0.007031 0.01537 6.694e-06 1.759e-07 0.8885 5.428e-15
0.007422 0.01708 6.285e-06 1.219e-07 0.8884 8.386e-15
0.007812 0.01895 5.915e-06 9.213e-08 0.8882 1.811e-15
0.008203 0.021 5.58e-06 7.752e-08 0.8881 8.651e-15
0.008594 0.02323 5.273e-06 7.216e-08 0.888 9.858e-15
0.008984 0.02562 4.989e-06 7.25e-08 0.8879 1.223e-14
0.00918 0.02686 4.855e-06 7.403e-08 0.8878 -1.784e-16
0.009375 0.02815 4.725e-06 7.632e-08 0.8878 -2.325e-15
0.00957 0.02946 4.599e-06 7.922e-08 0.8878 -1.853e-15
0.009766 0.0308 4.477e-06 8.26e-08 0.8877 -4.002e-15
0.009961 0.03216 4.358e-06 8.637e-08 0.8877 3.533e-15
0.01016 0.03354 4.242e-06 9.044e-08 0.8877 8.569e-15
0.01035 0.03494 4.129e-06 9.475e-08 0.8877 4.07e-15
0.01055 0.03633 4.018e-06 9.923e-08 0.8876 5.54e-15
0.01074 0.03773 3.911e-06 1.038e-07 0.8876 6.747e-15
0.01094 0.03912 3.806e-06 1.085e-07 0.8876 1.108e-14
0.01133 0.04188 3.603e-06 1.178e-07 0.8877 7.893e-16
0.01172 0.04454 3.411e-06 1.269e-07 0.8877 -2.394e-15
0.01211 0.04709 3.229e-06 1.355e-07 0.8878 4.046e-15
0.0125 0.04949 3.059e-06 1.434e-07 0.8878 5.679e-15
0.01289 0.05173 2.901e-06 1.506e-07 0.8879 -3.106e-16
0.01328 0.05378 2.754e-06 1.569e-07 0.888 8.123e-16
0.01367 0.05565 2.62e-06 1.625e-07 0.888 5.278e-15
0.01406 0.05733 2.498e-06 1.674e-07 0.8881 3.035e-15
0.01445 0.05882 2.387e-06 1.716e-07 0.8882 2.469e-15
0.01484 0.06015 2.287e-06 1.753e-07 0.8882 3.872e-15
0.01523 0.06131 2.197e-06 1.786e-07 0.8883 4.524e-15
0.01562 0.06231 2.117e-06 1.816e-07 0.8884 2.397e-15
0.01641 0.06393 1.982e-06 1.866e-07 0.8884 3.756e-15
0.01719 0.06514 1.872e-06 1.909e-07 0.8885 3.95e-15
0.01797 0.06605 1.783e-06 1.945e-07 0.8886 4.249e-15
0.01875 0.06673 1.709e-06 1.975e-07 0.8886 3.68e-15
0.02031 0.06761 1.596e-06 2.019e-07 0.8886 4.286e-15
0.02188 0.06819 1.509e-06 2.038e-07 0.8886 3.583e-15
0.02344 0.06861 1.439e-06 2.037e-07 0.8887 4.472e-15
0.025 0.06895 1.38e-06 2.018e-07 0.8887 3.555e-15
0.02656 0.06925 1.329e-06 1.984e-07 0.8887 4.65e-15
0.02813 0.06952 1.285e-06 1.941e-07 0.8887 3.7e-15
0.02969 0.06976 1.245e-06 1.89e-07 0.8887 3.404e-15
0.03125 0.07 1.21e-06 1.836e-07 0.8887 3.705e-15
0.03438 0.07042 1.149e-06 1.722e-07 0.8887 3.739e-15
0.0375 0.0708 1.098e-06 1.608e-07 0.8887 4.308e-15
0.04063 0.07116 1.054e-06 1.499e-07 0.8887 3.642e-15
0.04375 0.07149 1.015e-06 1.398e-07 0.8887 3.706e-15
0.04688 0.07179 9.811e-07 1.305e-07 0.8887 3.924e-15
0.05 0.07208 9.507e-07 1.222e-07 0.8887 4.089e-15
0.05625 0.07259 8.995e-07 1.08e-07 0.8887 3.463e-15
0.0625 0.07305 8.564e-07 9.638e-08 0.8887 3.947e-15
0.06875 0.07347 8.194e-07 8.676e-08 0.8887 3.778e-15
0.075 0.07385 7.87e-07 7.874e-08 0.8887 3.609e-15
0.08125 0.0742 7.583e-07 7.202e-08 0.8887 3.773e-15
0.0875 0.07453 7.327e-07 6.633e-08 0.8887 3.776e-15
0.1 0.0751 6.899e-07 5.75e-08 0.8887 3.756e-15
0.1125 0.07561 6.536e-07 5.073e-08 0.8887 3.557e-15
0.125 0.07606 6.223e-07 4.542e-08 0.8887 3.903e-15
0.1375 0.07647 5.949e-07 4.116e-08 0.8887 3.608e-15
0.15 0.07685 5.707e-07 3.767e-08 0.8887 4.049e-15
0.1625 0.07719 5.49e-07 3.477e-08 0.8887 3.766e-15
0.175 0.07751 5.295e-07 3.233e-08 0.8887 3.744e-15
0.2 0.07805 4.969e-07 2.857e-08 0.8887 3.712e-15
0.225 0.07852 4.693e-07 2.568e-08 0.8887 3.877e-15
0.25 0.07894 4.457e-07 2.34e-08 0.8887 3.73e-15
0.275 0.07932 4.253e-07 2.156e-08 0.8887 3.77e-15
0.3 0.07965 4.076e-07 2.005e-08 0.8887 3.75e-15
0.35 0.08021 3.796e-07 1.78e-08 0.8886 3.8e-15
0.425 0.08084 3.505e-07 1.559e-08 0.8886 3.747e-15
0.5 0.08084 3.505e-07 1.559e-08 0.8886 3.747e-15
-------------------------------------------------------------------------------
z
-------------------------------------------------------------------------------
0
1.221e-05
2.441e-05
3.662e-05
4.883e-05
6.104e-05
7.324e-05
8.545e-05
9.766e-05
0.0001221
0.0001465
0.0001709
0.0001953
0.0002441
0.000293
0.0003418
0.0003906
0.0004395
0.0004883
0.0005859
0.0006836
0.0007813
0.0008789
0.0009766
0.001074
0.001172
0.001367
0.001563
0.001758
0.001953
0.002148
0.002344
0.002441
0.002539
0.002637
0.002734
0.002832
0.00293
0.003027
0.003125
0.003223
0.00332
0.003418
0.003516
0.003613
0.003711
0.003809
0.003906
0.004004
0.004102
0.004199
0.004297
0.004395
0.004492
0.004688
0.004883
0.005078
0.005273
0.005469
0.005859
0.00625
0.006641
0.007031
0.007422
0.007812
0.008203
0.008594
0.008984
0.00918
0.009375
0.00957
0.009766
0.009961
0.01016
0.01035
0.01055
0.01074
0.01094
0.01133
0.01172
0.01211
0.0125
0.01289
0.01328
0.01367
0.01406
0.01445
0.01484
0.01523
0.01562
0.01641
0.01719
0.01797
0.01875
0.02031
0.02188
0.02344
0.025
0.02656
0.02813
0.02969
0.03125
0.03438
0.0375
0.04063
0.04375
0.04688
0.05
0.05625
0.0625
0.06875
0.075
0.08125
0.0875
0.1
0.1125
0.125
0.1375
0.15
0.1625
0.175
0.2
0.225
0.25
0.275
0.3
0.35
0.425
0.5
>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>>> outlet <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<
-------------------------------------------------------------------------------
z
-------------------------------------------------------------------------------
0
from pathlib import Path
import cantera as ct
p = 0.05 * ct.one_atm
tburner = 373.0
mdot = 0.06
reactants = 'H2:1.5, O2:1, AR:7' # premixed gas composition
width = 0.5 # m
loglevel = 1 # amount of diagnostic output (0 to 5)
gas = ct.Solution('h2o2.yaml')
gas.TPX = tburner, p, reactants
f = ct.BurnerFlame(gas, width=width)
f.burner.mdot = mdot
f.set_refine_criteria(ratio=3.0, slope=0.05, curve=0.1)
f.show()
f.transport_model = 'mixture-averaged'
f.solve(loglevel, auto=True)
if "native" in ct.hdf_support():
output = Path() / "burner_flame.h5"
else:
output = Path() / "burner_flame.yaml"
output.unlink(missing_ok=True)
f.save(output, name="mix", description="solution with mixture-averaged transport")
f.transport_model = 'multicomponent'
f.solve(loglevel) # don't use 'auto' on subsequent solves
f.show()
f.save(output, name="multi", description="solution with multicomponent transport")
f.save('burner_flame.csv', basis="mole", overwrite=True)
Total running time of the script: (0 minutes 0.454 seconds)