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********* CHEMICAL EQUILIBRIUM COMPUTATION ***************
Pressure P = 100 bar Temperature T = 1800 K
38 species 3 elements
38 gaseous species (G) 0 single species phases
0 species in solution (M)
40 iterations
Species Moles Mole fraction
G CO(g) 9.9958407E-01 4.1699441E-01
G CH4(g) 4.9118940E-01 2.0490846E-01
G H2(g) 6.5417340E-01 2.7290015E-01
G C2H2(g) 1.4945955E-01 6.2349730E-02
G C2H4(g) 9.1692631E-02 3.8251224E-02
G C3H6(g;1) 6.1358747E-03 2.5596901E-03
G C2H6(g) 3.2809454E-03 1.3687052E-03
G CH3(g) 6.9195880E-04 2.8866301E-04
G C2H3(g) 3.6874657E-04 1.5382924E-04
G H2O(g) 2.2433040E-04 9.3583447E-05
G CO2(g) 8.9283301E-05 3.7246129E-05
G C2H5(g) 8.4042799E-05 3.5059959E-05
G C3H8(g) 5.3716560E-05 2.2408825E-05
A H(g) 4.4893579E-05 1.8728161E-05
G C3H6(g) 1.7726288E-05 7.3948388E-06
G C3H4(g) 1.1959419E-05 4.9890861E-06
G H2CO(g) 1.1607051E-05 4.8420894E-06
G HCO(g) 1.1124439E-06 4.6407590E-07
G C3H(g) 7.6945894E-07 3.2099358E-07
G C3O2(g) 1.4764198E-07 6.1591499E-08
G CH2(g) 5.2687653E-08 2.1979599E-08
G C2H(g) 4.0269737E-08 1.6799242E-08
G C2O(g) 4.6922616E-09 1.9574610E-09
G HCOOH(g) 3.8613518E-09 1.6108321E-09
G OH(g) 1.0078791E-09 4.2045484E-10
G C3(g) 1.1701232E-10 4.8813787E-11
G COOH(g) 6.2719124E-11 2.6164406E-11
G CH(g) 1.3634084E-11 5.6877025E-12
G C5(g) 6.2834150E-12 2.6212391E-12
G C2(g) 2.7134354E-13 1.1319582E-13
A C(g) 2.1142511E-13 8.8199773E-14
G C4(g) 5.4018752E-14 2.2534890E-14
A O(g) 5.3410392E-14 2.2281102E-14
G O2(g) 8.0534843E-18 3.3596553E-18
G H2O2(g) 3.7095286E-18 1.5474963E-18
G HO2(g) 8.2573359E-20 3.4446956E-20
G CH2O2(g) 1.2342066E-21 5.1487140E-22
Less than 1.E-32 moles:
G O3(g)
2.397116 moles in gaseous phase
Elemental abundances:
O 1
H 4
C 2
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