2                       ! ipea: =0 -> no PEA; =1 -> PEA
'KERO_LUCHE'            ! name of the fuel species
10 20 0                 ! number of carbon and hydrogen atoms in fuel
'C'                     ! atom retained for mixture fraction calculation
'O2' 0 0.233            ! species, mass fractions in fuel tank and oxydizer tank
'KERO_LUCHE' 1 0        !
'CO' 0 0                !
'CO2' 0 0               !
'H2O' 0 0               !
'N2' 0 0.767            !

-- PEA on fuel oxidation reaction only -------------------------------------------------------
-- f=f1+f2
-- f1 = 1/2*{1+tanh[(phi0-phi)/sigma0]}
-- f2 = B*1/4*{1+tanh[(phi-phi1)/sigma1]}*{1+tanh[(phi2-phi)/sigma2]}
PEA_1
0.00d0               ! phi0
0.00d0               ! sigma0
0.00d0               ! B
0.00d0               ! phi1
0.00d0               ! sigma1
0.00d0               ! phi2
0.00d0               ! sigma2


-- PEA on fuel oxidation (1) and CO-CO2 equilibrium (2) reactions ---------------------------
-- f1 = 2/[{1+tanh[(phi0,1-phi)/sigma0,1]}+B1{1+tanh[(phi-phi1,1)/sigma1,1]}+C1{1+tanh[(phi-phi2,1)/sigma2,1]}]
-- f2 = 0.5*{1+tanh[(phi0,2-phi)/sigma0,2]}+B2/2*{1+tanh[(phi-phi1,2)/sigma1,2]}+C2/2*{1+tanh[(phi-phi2,2)/sigma2,2]}*{1+tanh[(phi3,2-phi)/sigma3,2]}
PEA_2
1.173d0              ! phi01
0.04d0               ! sigma01
0.29d0               ! B1
1.2d0                ! phi11
0.02d0               ! sigma11
7.1d0                ! C1
1.8d0                ! phi21
0.18d0               ! sigma21
1.146d0              ! phi02
0.045d0              ! sigma02
0.00015d0            ! B2
1.2d0                ! phi12
0.04d0               ! sigma12
0.035d0              ! C2
1.215d0              ! phi22
0.03d0               ! sigma22
1.32d0               ! phi32
0.09d0               ! sigma32