Selection of fuel, oxidizer and calculation mode

fuel:	Natural gas Natural gas low LHV gas gasoline CH4 ` methane C2H6 ` ethane C3H8 ` propane C4H10 ` n-butane H2S H2
oxydizer:	air air atmospheric air O2
calculate lambda:	Yes No Yes
dissociation:	Yes No Yes

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Combustion settings

oxidizer temperature (°C)
fuel temperature (°C)
chamber efficiency
lambda
combustion temperature (°C)
quenching temperature (°C)
dissociation rate
fuel flow rate (kmol/s)
combustion efficiency
Delta H (kW)

lambda : 2, e : 1, R : 0.5
T products (K): 1,773.15
quenching T (K): 1,399.15
diss rate: 0

oxydizer mole number: 21.21
O2 mole number in the oxydizer: 4.454

C available in the fuel (mol): 1.154
H2 available in the fuel (mol): 2.146
S available in the fuel (mol): 0
O2 available in the fuel (mol): 0

total mole number of products: 17.296

CO2 mole number: 1.154
CO mole number: 0
H2 mole number: 0
H2O mole number: 2.146
SO2 mole number: 0
O2 mole number: 1.178

Fuel composition LHV: 48,714 kJ/kg

component	molar fraction	mass fraction
CH4 ` methane	0.87100	0.75897
C2H6 ` ethane	0.08800	0.14373
C3H8 ` propane	0.02500	0.05988
C4H10 ` n-butane	0.00800	0.02526
N2	0.00800	0.01218

Oxidizer composition LHV: 0 kJ/kg

component	molar fraction	mass fraction
O2	0.21000	0.23206
N2	0.78100	0.75554
Ar	0.00900	0.01242

Burnt gas composition LHV: 0 kJ/kg

component	molar fraction	mass fraction
CO2	0.06673	0.10409
H2O	0.12408	0.07923
O2	0.06812	0.07726
N2	0.73266	0.72749
Ar	0.00844	0.01195