Appendix A
The UDF code, needed to calculate the residence time ⌧ in JHC burner (Section 2.2), is reported below.
DEFINE_SOURCE( rt_source , c , t , dS , eqn ) {
r e a l source=C_R( c , t ) ; dS [ eqn ] = 0 . 0 ;
return source ; }
DEFINE_DIFFUSIVITY( rtd_diff , c , t , i ) {
return C_R( c , t ) ∗ 1 . 0 e 05+C_MU_EFF( c , t ) / 1 . 0 ; }
Table B.1: Kinetic parameters applied to New model in JHC conditions, using Glarborg [19] detailed kinetic scheme. Units: mol, cm, s, cal
Reactiona Forward Backward
A Ea A Ea
N + N O)kf 1*
kr1
N2+ O 3.30· 1012 0.3 0 6.17· 109 0.4 74884 N + O2
kf 2
)*
kr2
N O + O 6.40· 109 1 6280 6.36· 105 1.1 37980 CO2+ N )kf 22*
kr22
N O + CO 1.90· 1011 0 20237 2.16· 103 0.9 26372 N H + H)kf 17*
kr17
N + H2 3.00· 1013 0 0 5.66· 1010 0.1 24228 N2O + M )kf 4*
kr4
N2+ O + M 4.0· 1014 0 56100 1.07· 103 1.1 15654 N2O + H )kf 18*
kr18
N2+ OH 3.30· 1010 0 4729 2.96· 101 1.3 66092 N2O + C)kf 23*
kr23
N2+ CO2 3.20· 1011 0 20237 8.25· 108 0.1 107481 N H + N O)kf 15*
kr15
N2O + H 2.90· 1014 0.4 0 6.42· 1017 1.5 35932 N2+ OH)kf 50*
kr50
N2+ HO2 1.30· 10 2 4.7 36561 3.91· 10 8 5.3 62719 N2O + O)kf 6*
kr6
N O + N O 6.60· 1013 0 26630 1.00· 106 0.9 61961
kf 8
* 13 9
Appendix B.
Reactiona Forward Backward
A Ea A Ea
HN O + H)kf 28*
kr28
N O + H2 4.50· 1011 0.7 655 7.66· 106 1.2 54457 H + N O + M)kf 31*
kr31
HN O + M 4.00· 1020 1.8 0 1.40· 1019 1.9 49824 N O + HCO)kf 32*
kr32
CO + HN O 7.20· 1012 0 0 2.93· 1010 0.1 34525 H + N O + N2
kf 49
)*
kr49
N2+ HN O 7.00· 1019 1.5 0 2.46· 1018 1.7 49824 N O + HO2
kf 33
)*
kr33
N O2+ OH 2.10· 1012 0 480 1.93· 1010 0.07 7195 N O2+ CH3
kf 34
)*
kr34
N O + CH3O 1.50· 1013 0 40000 2.11· 1010 0.05 17704 N O2+ H )kf 35*
kr35
N O + OH 1.32· 1014 0 360 3.13· 106 0.83 29175 N O2+ H2
kf 36
)*
kr36
HON O + H 3.00· 1013 0 29000 2.98· 1013 0.86 3883 N O + OH + M)kf 37*
kr37
HON O + M 2.40· 1013 0 0 5.83· 1027 3.86 49694 HON O + OH )kf 46*
kr46
N O2+ H2O 4.00· 1012 0 0 5.18· 107 0.7 40471 N O2+ CH2O)kf 47*
kr47
HON O + HCO 8.00· 102 2.7 13730 1.07 2.4 1819 N O2+ HCO)kf 48*
kr48
HON O + CO 1.23· 1023 3.4 2355 8.25· 1021 3.6 65566 N H2+ H2
kf 40
)*
kr40
N H3+ H 1.42 2.9 5077 6.40· 105 2.4 10171 N H3+ OH )kf 41*
kr41
N H2+ H2O 2.00· 106 2 566 5.76· 101 2.4 10827 N H3+ O)kf 51*
kr51
N H2+ OH 9.40· 106 1.9 6460 1.18· 101 2.4 0 N H2+ OH)kf 52*
kr52
H2O + N H 4.00· 106 2 1000 6.76· 103 2.1 28375 CH3+ M )kf 43*
kr43
CH2O + H + M 6.00· 1012 0 0 5.40· 1011 0.5 2600 CH3+ HO2
kf 44
)*
kr44
CH3O + OH 8.00· 1012 0 0 1.27· 1011 0.2 24499 CH3+ O2
kf 45
)*
kr45
CH3O + O 2.90· 1013 0 30480 4.72· 1012 0.5 2621
a k = AT exp( Ea/RT ).
Reactiona Forward Backward
A Ea A Ea
N + N O)kf 1*
kr1
N2+ O 3.30· 1012 0.3 0 6.20· 109 0.41 74884 N + O2
kf 2
)*
kr2
N O + O 6.40· 109 1 6280 6.36· 105 1.09 37980 CO2+ N)kf 22*
kr22
N O + CO 1.19· 1011 0 3400 2.16· 103 0.91 26372 N H + H)kf 17*
kr17
N + H2 3.00· 1013 0 0 5.66· 1010 0.11 24228 N2O + M )kf 4*
kr4
N2+ O + M 1.40· 1016 0 66100 3.74· 104 1.09 25654 N2O + H )kf 18*
kr18
N2+ OH 3.30· 1010 0 4729 2.66· 101 1.30 66497 N2O + CO)kf 23*
kr23
N2+ CO2 2.70· 1011 0 20237 6.96· 108 0.09 107481 N H + N O)kf 15*
kr15
N2O + H 4.32· 1014 0.5 0 9.56· 1017 1.60 35932 N N H + O)kf 8*
kr8
N O + N H 5.00· 1013 0 0 1.61· 109 0.36 10963 N N H + O2
kf 21
)*
kr21
HO2+ N2 6.67· 1013 0 0 4.82· 1010 0.20 55425 N N H)kf 7*
kr7
N2+ H 1.10· 106 0 0 2.09· 103 0.35 6450 N N H + O2
kf 20
)*
kr20
N2+ H + O2 5.00· 1013 0 0 9.45· 106 0.35 6450 N H2+ H )kf 24*
kr24
N H + H2 4.00· 1013 0 3650 5.24· 109 0.20 15670 N H + O2
kf 25
)*
kr25
HN O + O 4.60· 105 2.00 6500 5.07· 103 1.75 8626 N H + O2
kf 26
)*
kr26
N O + OH 1.30· 107 1.50 100 1.23· 102 1.68 54616 N H2+ OH)kf 27*
kr27
N H + H2O 4.00· 106 2 1000 7.52· 103 2.06 27970 HN O + H)kf 28*
kr28
N O + H2 4.40· 1011 0.72 650 7.48· 106 1.17 54452 N O + CH4
kf 29
)*
kr29
HN O + CH3 5.00· 1011 0 50000 6.31· 107 0.10 5292
Appendix B.
Reactiona Forward Backward
A Ea A Ea
N O + OH + M)kf 37*
kr37
HON O + M 2.40· 1013 0 0 5.83· 1027 3.86 49694 HON O + CH3
kf 38
)*
kr38
N O2+ CH4 8.10· 105 1.87 5504 3.79· 102 2.39 32110 N O2+ HO2
kf 39
)*
kr39
HON O + O2 6.31· 108 1.25 5000 9.85· 107 0.76 34534 N H2+ H2
kf 40
)*
kr40
N H3+ H 1.58· 105 2.00 3954 7.05· 104 1.50 9048 N H3+ OH)kf 41*
kr41
N H2+ H2O 1.19· 107 2.00 4067 3.84· 102 2.35 13924 N H2+ CH4
kf 42
)*
kr42
N H3+ CH3 7.68· 104 2.00 6420 7.58· 101 1.85 10023 CH3+ M )kf 43*
kr43
CH2O + H + M 6.00· 1011 0 18000 5.68· 1016 2.25 9845 CH3+ HO2
kf 44
)*
kr44
CH3O + OH 6.00· 1012 0 0 7.75· 1010 0.12 25380 CH3+ O2
kf 45
)*
kr45
CH3O + O 4.00· 1012 0 27000 6.51· 1011 0.48 0
a k = AT exp( Ea/RT ).
Table C.1: Kinetic parameters applied to New model in pilot-scale burner conditions, using Glarborg [19] detailed kinetic scheme. Units: mol, cm, s, cal
Reactiona Forward Backward
A Ea A Ea
N + N O)kf 1*
kr1
N2+ O 3.30· 1012 0.3 0 6.17· 109 0.4 74884 N + O2
kf 2
)*
kr2
N O + O 6.40· 109 1 6280 6.36· 105 1.1 37980 N + OH )kf 3*
kr3
N O + H 3.80· 1013 0 0 1.10· 1014 0.0 4750 N2O + M )kf 4*
kr4
N2+ O + M 4.0· 1014 0 56100 1.07· 103 1.1 15654 N2O + O)kf 6*
kr6
N O + N O 6.60· 1013 0 26630 1.00· 106 0.9 61961 N N H + O)kf 9*
kr9
N2O + H 1.10· 1014 0 0 1.47· 1016 0.0 46100 N H + N O)kf 15*
kr15
N2O + H 2.90· 1014 0.4 0 6.42· 1017 1.5 35932 N2O + H )kf 18*
kr18
N2+ OH 3.30· 1010 0 4729 2.96· 101 1.3 66092 N N H)kf 7*
kr7
N2+ H 1.10· 107 0 0 1.89· 103 0.35 6450 N N H + O)kf 8*
kr8
N O + N H 5.00· 1013 0 0 1.61· 109 0.4 10963
kf 20
* 13 6
Appendix C.
Reactiona Forward Backward
A Ea A Ea
N H + N O)kf 58*
kr58
N2+ OH 2.20· 1012 0.07 512 4.37· 1010 0.04 97296 N H + OH)kf 59*
kr59
N + H2O 5.00· 1011 0.5 2000 1.21· 1010 0.48 41583 N H2+ H2
kf 40
)*
kr40
N H3+ H 1.42 2.9 5077 6.40· 105 2.4 10171 N H3+ OH)kf 41*
kr41
N H2+ H2O 2.00· 106 2 566 5.76· 101 2.4 10827 N H3+ O)kf 51*
kr51
N H2+ OH 9.40· 106 1.9 6460 1.18· 101 2.4 0 N H2+ O)kf 65*
kr65
HN O + H 6.60· 1014 0.5 0 1.76· 1014 0.96 29482 HN O + H)kf 28*
kr28
N O + H2 4.50· 1011 0.7 655 7.66· 106 1.2 54457 N O + HCO)kf 32*
kr32
CO + HN O 7.20· 1012 0 0 2.93· 1010 0.1 34525 H + N O + N2
kf 49
)*
kr49
N2+ HN O 7.00· 1019 1.5 0 2.46· 1018 1.7 49824 H + N O + N2
kf 63
)*
kr63
N2+ HN O 1.30· 107 1.9 950 7.89· 109 0.31 69157 H + N O + N2
kf 64
)*
kr64
N2+ HN O 1.00· 1013 0 0 9.57· 107 0.41 51985 N O2+ H2
kf 36
)*
kr36
HON O + H 3.00· 1013 0 29000 2.98· 1013 0.86 3883 N O + OH + M)kf 37*
kr37
HON O + M 2.40· 1013 0 0 5.83· 1027 3.86 49694 HON O + OH )kf 46*
kr46
N O2+ H2O 4.00· 1012 0 0 5.18· 107 0.7 40471 HON O + O)kf 62*
kr62
N O2+ OH 1.20· 1013 0 5961 6.79· 106 0.83 29260 N O + HO2
kf 33
)*
kr33
N O2+ OH 2.10· 1012 0 480 1.93· 1010 0.07 7195 N O2+ H)kf 35*
kr35
N O + OH 1.32· 1014 0 360 3.13· 106 0.83 29175 N O + O + M )kf 60*
kr60
N O2+ M 1.30· 1015 0.75 0 9.55· 1018 2.0 73398 N O2+ O)kf 61*
kr61
N O + O2 1.10· 1014 0.52 0 3.37· 107 0.42 45324
a k = AT exp( Ea/RT ).
The concentrations of the intermediate species, involved in the new compre- hensive model developed for NOx evaluation in pilot-scale burner conditions of Chapter 3, are listed below.
[N ] =kr1[O][N2] + kr2[N O][O] + kr3[N O][H] + kf 53[CH][N O]
kf 1[N O] + kr2[O2] + kf 3[OH] + kr53[HCO] (C.1)
[N2O] =kr4[O][N2][M ] + kr18[N2][OH] + kr6[N O][N O] + kf 15[N H][N O] + kf 9[N N H][O]
kf 4[M ] + kf 18[H] + kf 6[O] + kr9[H] (C.2)
[HN O] = [N O](kr28[H2] + kr63[H2O] + kf 32[HCO] + kf 49[H][N2] + kr64[OH]) + kf 57[N H][OH]
kf 28[H] + kf 63[OH] + kr32[CO] + kr49[N2] + kf 64[O] + kr57[H] (C.4)
[N O2] =[N O](kf 60[O][M ] + kr35[OH] + kr61[O2] + kf 33[HO2]
kr60[M ] + kf 35[H] + kf 61[O] + kr33[OH] (C.5)
[HON O] = [N O2](kr36[H2] + kr46[H2O] + kr62[OH]) + kf 37[N O][OH][M ]
kf 36[H] + kf 38[CH3] + kr39[O2] + kr37[M ] (C.6)
[N H2] =[N H3](kr40[H] + kf 41[OH] + kf 52[O]) + [N H](kr27[H2O] + kr66[H2]) + kr65[HN O][H]
kf 40[H2] + kr41[H2O] + kr52[OH] + kf 27[OH] + kf 66[H] + kf 65[O] (C.7)
[N N H] =[N2](kr7[H] + kr20[H][O2] + kr21[HO2] + kr54[H2O] + kr55[H2] + kr56[OH]) + kr8[N H][N O]
kf 7+ kf 20[O2] + kf 21[O2] + kf 54[OH] + kf 55[H] + kf 56[O] + kf 8[O] (C.8)