description: |-
  ---------------------------------------------------------------------------
    CTI File converted from Solution Object
  ---------------------------------------------------------------------------

generator: cti2yaml
cantera-version: 3.0.0
date: Thu, 01 Aug 2024 11:44:57 +0200
input-files: [B1_55_255_JW.cti]

units: {length: cm, quantity: mol, activation-energy: cal/mol}

phases:
- name: gas
  thermo: ideal-gas
  elements: [N, H, O, C]
  species: [N2, H2, H, O2, O, H2O, OH, H2O2, HO2, CO, CO2, CH4, CH3, CH2,
    CH2(S), C, CH, CH3O, CH2OH, CH2O, HCO, C2H6, C2H5, C2H4, C2H3, C2H2,
    C2H, CH3CO, CH2CHO, CH2CO, HCCO, C3H6, C3H5-A, C3H5-T, C3H5O, C3H4-P,
    C3H4-A, C3H3, C2H3CHO, CH3COCH2, IC4H9, TC4H9, IC4H8, IC4H7, IC4H7O,
    NEOC5H11, IC8H18, IC8H17, IC8H16, IC16H33, IC16H34, IC12H26, IC12H25,
    C4H9O2(L1), C3H7(L1)]
  kinetics: gas
  reactions: all
  state:
    T: 300.0
    P: 1.01325e+05

species:
- name: N2
  composition: {N: 2}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 1050.0, 3500.0]
    data:
    - [3.73100682, -1.8315973e-03, 4.32324661e-06, -3.04378151e-09, 7.46071562e-13,
      -1062.87426, 2.16821198]
    - [2.81166073, 1.67067353e-03, -6.79997428e-07, 1.32881379e-10, -1.02767442e-14,
      -869.81158, 6.6483805]
  transport:
    model: gas
    geometry: linear
    diameter: 3.621
    well-depth: 97.53
    polarizability: 1.76
    rotational-relaxation: 4.0
- name: H2
  composition: {H: 2}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 700.0, 3500.0]
    data:
    - [2.64204438, 5.49529275e-03, -1.27163634e-05, 1.28749174e-08, -4.7002775e-12,
      -943.236613, -0.512231094]
    - [3.78199881, -1.0187326e-03, 1.24226233e-06, -4.19011899e-10, 4.75543794e-14,
      -1102.83023, -5.6052591]
  transport:
    model: gas
    geometry: linear
    diameter: 2.9200000000000004
    well-depth: 38.0
    polarizability: 0.7900000000000001
    rotational-relaxation: 280.0
- name: H
  composition: {H: 1}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 860.0, 3500.0]
    data:
    - [2.49950544, 2.99164057e-06, -5.92759783e-09, 4.87810185e-12, -1.45539326e-15,
      2.54737866e+04, -0.444574018]
    - [2.50031493, -7.73406872e-07, 6.39345384e-10, -2.12551804e-13, 2.44479207e-17,
      2.54736474e+04, -0.448357228]
  transport:
    model: gas
    geometry: atom
    diameter: 2.05
    well-depth: 145.0
- name: O2
  composition: {O: 2}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 700.0, 3500.0]
    data:
    - [3.74403921, -2.79740148e-03, 9.8012256e-06, -1.03259643e-08, 3.79931247e-12,
      -1060.69827, 3.82132645]
    - [2.82012408, 2.48211357e-03, -1.51202094e-06, 4.48556202e-10, -4.87305668e-14,
      -931.350148, 7.94914552]
  transport:
    model: gas
    geometry: linear
    diameter: 3.458
    well-depth: 107.4
    polarizability: 1.6
    rotational-relaxation: 3.8
- name: O
  composition: {O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 720.0, 3500.0]
    data:
    - [3.14799201, -3.11174063e-03, 6.18137893e-06, -5.63808794e-09, 1.94866014e-12,
      2.91309118e+04, 2.1344655]
    - [2.62549143, -2.08959648e-04, 1.33918549e-07, -3.85875908e-11, 4.38918703e-15,
      2.92061519e+04, 4.48358518]
  transport:
    model: gas
    geometry: atom
    diameter: 2.7500000000000004
    well-depth: 80.0
- name: H2O
  composition: {H: 2, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 1420.0, 3500.0]
    data:
    - [4.06061172, -8.65807189e-04, 3.24409528e-06, -1.80243079e-09, 3.32483293e-13,
      -3.02831314e+04, -0.296150481]
    - [2.66777075, 3.05768849e-03, -9.00442411e-07, 1.43361552e-10, -1.00857817e-14,
      -2.98875645e+04, 6.91191131]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 2.6050000000000004
    well-depth: 572.4
    dipole: 1.8440005262719967
    rotational-relaxation: 4.0
- name: OH
  composition: {H: 1, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 1700.0, 3500.0]
    data:
    - [3.91354631, -1.66275926e-03, 2.30920029e-06, -1.02359508e-09, 1.58829629e-13,
      3400.05047, 0.205474719]
    - [2.49867369, 1.66635279e-03, -6.28251516e-07, 1.28346806e-10, -1.05735894e-14,
      3881.10716, 7.78218863]
  transport:
    model: gas
    geometry: linear
    diameter: 2.7500000000000004
    well-depth: 80.0
- name: H2O2
  composition: {H: 2, O: 2}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 1800.0, 3500.0]
    data:
    - [3.34774224, 7.05005437e-03, -3.84522006e-06, 1.16720661e-09, -1.47618105e-13,
      -1.75784785e+04, 7.17868851]
    - [4.76869639, 3.89237848e-03, -1.21382349e-06, 1.92615285e-10, -1.2258199e-14,
      -1.8090022e+04, -0.511811777]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.458
    well-depth: 107.4
    rotational-relaxation: 3.8
- name: HO2
  composition: {H: 1, O: 2}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 700.0, 3500.0]
    data:
    - [3.61994299, 1.05805704e-03, 5.06678942e-06, -6.33800762e-09, 2.41597281e-12,
      315.898234, 6.44411482]
    - [3.02391889, 4.46390907e-03, -2.23146492e-06, 6.127108e-10, -6.64266237e-14,
      399.341609, 9.10699973]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.458
    well-depth: 107.4
    rotational-relaxation: 1.0
- name: CO
  composition: {C: 1, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 960.0, 3500.0]
    data:
    - [3.75723891, -2.14465241e-03, 5.42079004e-06, -4.17025963e-09, 1.11901127e-12,
      -1.4357553e+04, 2.79976799]
    - [2.79255381, 1.87486886e-03, -8.59711925e-07, 1.9120007e-10, -1.67855286e-14,
      -1.41723335e+04, 7.4144356]
  transport:
    model: gas
    geometry: linear
    diameter: 3.65
    well-depth: 98.1
    polarizability: 1.9500000000000002
    rotational-relaxation: 1.8
- name: CO2
  composition: {C: 1, O: 2}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 1450.0, 3500.0]
    data:
    - [2.31684347, 9.22755036e-03, -7.75654093e-06, 3.2822536e-09, -5.48722482e-13,
      -4.83626067e+04, 10.0786234]
    - [4.70876468, 2.62914704e-03, -9.30606462e-07, 1.4389292e-10, -7.62581413e-15,
      -4.90562639e+04, -2.34976452]
  transport:
    model: gas
    geometry: linear
    diameter: 3.763
    well-depth: 244.0
    polarizability: 2.6500000000000004
    rotational-relaxation: 2.1
- name: CH4
  composition: {C: 1, H: 4}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 700.0, 3500.0]
    data:
    - [5.2396731, -0.0146835107, 5.29732676e-05, -5.41668788e-08, 1.96318554e-11,
      -1.02526308e+04, -4.97649641]
    - [0.505346456, 0.0123697844, -4.99807911e-06, 1.04392761e-09, -8.62897368e-14,
      -9589.82503, 16.1752773]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.7460000000000004
    well-depth: 141.4
    polarizability: 2.6
    rotational-relaxation: 13.0
- name: CH3
  composition: {C: 1, H: 3}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1060.0, 3500.0]
    data:
    - [3.4782931, 3.54764774e-03, 1.47408439e-06, -1.94375954e-09, 5.2192123e-13,
      1.64399516e+04, 2.40875956]
    - [2.78805104, 6.15233477e-03, -2.21179349e-06, 3.74402648e-10, -2.48151348e-14,
      1.65862829e+04, 5.77899817]
  transport:
    model: gas
    geometry: linear
    diameter: 3.8
    well-depth: 144.0
- name: CH2
  composition: {C: 1, H: 2}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1800.0, 3500.0]
    data:
    - [3.7648946, 1.43839191e-03, 4.75583077e-07, -4.31788591e-10, 7.58292874e-14,
      4.58645699e+04, 1.48953153]
    - [2.81272972, 3.55431388e-03, -1.28768523e-06, 2.21273744e-10, -1.48738147e-14,
      4.62073492e+04, 6.64284652]
  transport:
    model: gas
    geometry: linear
    diameter: 3.8
    well-depth: 144.0
- name: CH2(S)
  composition: {C: 1, H: 2}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 970.0, 3500.0]
    data:
    - [4.18185434, -2.21134312e-03, 7.71527537e-06, -5.95950378e-09, 1.58314628e-12,
      5.03669407e+04, -0.703002582]
    - [2.75934299, 3.65468306e-03, -1.35589913e-06, 2.74980408e-10, -2.36795469e-14,
      5.06429079e+04, 6.11646381]
  transport:
    model: gas
    geometry: linear
    diameter: 3.8
    well-depth: 144.0
- name: C
  composition: {C: 1}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 700.0, 3500.0]
    data:
    - [2.54495192, -2.47725281e-04, 5.48018277e-07, -5.4855125e-10, 2.04117331e-13,
      8.54434105e+04, 4.56874273]
    - [2.49472531, 3.92839476e-05, -6.7001498e-08, 3.71818694e-11, -5.07306885e-15,
      8.54504422e+04, 4.79314254]
  transport:
    model: gas
    geometry: atom
    diameter: 3.2980000000000005
    well-depth: 71.4
- name: CH
  composition: {C: 1, H: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1590.0, 3500.0]
    data:
    - [3.77264332, -1.5854735e-03, 2.83512238e-06, -1.36146058e-09, 2.23995331e-13,
      7.06312492e+04, 0.879407904]
    - [2.27990128, 2.16985238e-03, -7.07637884e-07, 1.23973494e-10, -9.56348511e-15,
      7.11059412e+04, 8.77326061]
  transport:
    model: gas
    geometry: linear
    diameter: 2.7500000000000004
    well-depth: 80.0
- name: CH3O
  composition: {C: 1, H: 3, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1740.0, 3500.0]
    data:
    - [0.889660986, 0.0170119767, -1.1380735e-05, 3.88280928e-09, -5.32841479e-13,
      1603.16121, 18.5001134]
    - [5.72238062, 5.90227638e-03, -1.8034072e-06, 2.1333501e-10, -5.61816419e-15,
      -78.6252217, -7.49173676]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.6900000000000004
    well-depth: 417.0
    dipole: 1.7000004851748343
    rotational-relaxation: 2.0
- name: CH2OH
  composition: {C: 1, H: 3, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1360.0, 3500.0]
    data:
    - [2.34821579, 0.0139600168, -1.08632206e-05, 4.62498415e-09, -8.08499162e-13,
      -3302.22106, 12.2661977]
    - [5.04534949, 6.0272706e-03, -2.11386821e-06, 3.36085906e-10, -2.00987483e-14,
      -4035.84143, -1.57524072]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.6900000000000004
    well-depth: 417.0
    dipole: 1.7000004851748343
    rotational-relaxation: 2.0
- name: CH2O
  composition: {C: 1, H: 2, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 700.0, 3500.0]
    data:
    - [4.3262128, -7.01151756e-03, 3.15176939e-05, -3.36478617e-08, 1.23454015e-11,
      -1.43270169e+04, 2.62028968]
    - [1.33335655, 0.0100905182, -5.12952555e-06, 1.25425205e-09, -1.19639106e-13,
      -1.3908017e+04, 15.9916142]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.59
    well-depth: 498.0
    rotational-relaxation: 2.0
- name: HCO
  composition: {C: 1, H: 1, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [200.0, 770.0, 3500.0]
    data:
    - [4.03483979, -2.15836864e-03, 1.18233875e-05, -1.18459406e-08, 4.00593955e-12,
      3836.36392, 4.2000877]
    - [2.60049318, 5.29278258e-03, -2.69184211e-06, 7.21357799e-10, -7.43521409e-14,
      4057.2533, 10.7450933]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.59
    well-depth: 498.0
- name: C2H6
  composition: {C: 2, H: 6}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1800.0, 3500.0]
    data:
    - [-0.241778723, 0.0253475709, -1.39645112e-05, 4.03257452e-09, -4.87754387e-13,
      -1.10391121e+04, 21.9572625]
    - [4.07959141, 0.0157445262, -5.96197393e-06, 1.06867182e-09, -7.61012341e-14,
      -1.25948053e+04, -1.43089411]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.35
    well-depth: 247.49999999999997
    rotational-relaxation: 1.5
- name: C2H5
  composition: {C: 2, H: 5}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1800.0, 3500.0]
    data:
    - [0.675421802, 0.0211542617, -1.20878017e-05, 3.6495118e-09, -4.59753237e-13,
      1.33457186e+04, 19.5628439]
    - [5.1979136, 0.01110428, -3.71281686e-06, 5.47665572e-10, -2.89412605e-14,
      1.17176215e+04, -4.91382512]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.35
    well-depth: 247.49999999999997
    rotational-relaxation: 1.5
- name: C2H4
  composition: {C: 2, H: 4}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1650.0, 3500.0]
    data:
    - [-0.0602932446, 0.020813397, -1.34307867e-05, 4.606383e-09, -6.51687481e-13,
      5511.51676, 21.0642172]
    - [4.60402718, 9.5059535e-03, -3.15129262e-06, 4.53052075e-10, -2.2394916e-14,
      3972.29102, -3.77420904]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.496
    well-depth: 238.4
    rotational-relaxation: 1.5
- name: C2H3
  composition: {C: 2, H: 3}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1450.0, 3500.0]
    data:
    - [1.23421214, 0.0156222204, -1.10171572e-05, 4.27989337e-09, -6.91541508e-13,
      3.46967692e+04, 16.8637048]
    - [4.18728376, 7.47581589e-03, -2.58984227e-06, 4.05265796e-10, -2.35022722e-14,
      3.38403785e+04, 1.51958752]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.7210000000000005
    well-depth: 265.3
    rotational-relaxation: 1.0
- name: C2H2
  composition: {C: 2, H: 2}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 790.0, 3500.0]
    data:
    - [0.770536982, 0.0237107994, -3.66622035e-05, 2.95989753e-08, -9.27579229e-12,
      2.64317975e+04, 14.090768]
    - [4.37267451, 5.47212836e-03, -2.03181547e-06, 3.75019136e-10, -2.77049085e-14,
      2.58626598e+04, -2.43835908]
  transport:
    model: gas
    geometry: linear
    diameter: 3.7210000000000005
    well-depth: 265.3
    rotational-relaxation: 2.5
- name: C2H
  composition: {C: 2, H: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1710.0, 3500.0]
    data:
    - [4.60873599, 1.42766785e-03, 8.54158643e-07, -6.83903344e-10, 1.21940589e-13,
      6.68801772e+04, -1.05894068]
    - [3.41788257, 4.21328989e-03, -1.58936946e-06, 2.68739191e-10, -1.73346358e-14,
      6.72874491e+04, 5.32512366]
  transport:
    model: gas
    geometry: linear
    diameter: 3.7210000000000005
    well-depth: 265.3
    rotational-relaxation: 2.5
- name: CH3CO
  composition: {C: 2, H: 3, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1800.0, 3500.0]
    data:
    - [1.47388064, 0.0183587034, -1.13426417e-05, 3.59576931e-09, -4.63999267e-13,
      -2410.92705, 18.7575232]
    - [6.07689016, 8.12979339e-03, -2.81854999e-06, 4.38698308e-10, -2.55171838e-14,
      -4068.01047, -6.15492452]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.97
    well-depth: 436.0
    rotational-relaxation: 2.0
- name: CH2CHO
  composition: {C: 2, H: 3, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1340.0, 3500.0]
    data:
    - [0.737868283, 0.0250454357, -2.20135026e-05, 1.00031294e-08, -1.80836357e-12,
      376.389339, 20.9962836]
    - [6.47703792, 7.91358605e-03, -2.83605892e-06, 4.62112658e-10, -2.832313e-14,
      -1161.70812, -8.37157284]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.97
    well-depth: 436.0
    rotational-relaxation: 2.0
- name: CH2CO
  composition: {C: 2, H: 2, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1360.0, 3500.0]
    data:
    - [2.49503978, 0.0158807592, -1.27171444e-05, 5.47226118e-09, -9.59140717e-13,
      -7188.9896, 11.8115657]
    - [5.69523628, 6.46841658e-03, -2.33588415e-06, 3.83408112e-10, -2.36897851e-14,
      -8059.44305, -4.61154401]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 3.97
    well-depth: 436.0
    rotational-relaxation: 2.0
- name: HCCO
  composition: {C: 2, H: 1, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1220.0, 3500.0]
    data:
    - [3.33028661, 0.0120351629, -1.14247949e-05, 5.70731267e-09, -1.13618105e-12,
      2.00087543e+04, 7.53650387]
    - [5.81420512, 3.8911678e-03, -1.41168609e-06, 2.35668534e-10, -1.49424973e-14,
      1.94026782e+04, -4.94089645]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 2.5
    well-depth: 150.0
    rotational-relaxation: 1.0
- name: C3H6
  composition: {C: 3, H: 6}
  thermo:
    model: NASA7
    temperature-ranges: [298.0, 1800.0, 3500.0]
    data:
    - [-0.085598719, 0.0308112255, -1.84574096e-05, 5.68686491e-09, -7.13747674e-13,
      1925.67819, 24.0935688]
    - [6.31755201, 0.0165820017, -6.59972302e-06, 1.29512916e-09, -1.03784375e-13,
      -379.456071, -10.5616188]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.14
    well-depth: 307.8
    rotational-relaxation: 1.0
- name: C3H5-A
  composition: {C: 3, H: 5}
  thermo:
    model: NASA7
    temperature-ranges: [298.0, 1600.0, 3500.0]
    data:
    - [-0.357888096, 0.0327028536, -2.40053581e-05, 9.07345729e-09, -1.37016487e-12,
      2.00235695e+04, 24.2845603]
    - [8.53877792, 0.0104611885, -3.15379708e-06, 3.85306883e-10, -1.26413688e-14,
      1.71766363e+04, -22.8181758]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.22
    well-depth: 316.0
    rotational-relaxation: 1.0
- name: C3H5-T
  composition: {C: 3, H: 5}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 770.0, 3500.0]
    data:
    - [2.52238868, 0.0180330582, -1.44114628e-06, -6.15086038e-09, 2.65919396e-12,
      2.85533009e+04, 12.9935192]
    - [1.49331935, 0.0233788729, -1.1855071e-05, 2.86552469e-09, -2.6820379e-13,
      2.87117775e+04, 17.6892214]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.22
    well-depth: 316.0
    rotational-relaxation: 1.0
- name: C3H5O
  composition: {C: 3, H: 5, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1610.0, 3500.0]
    data:
    - [0.927196847, 0.0340908988, -2.40959865e-05, 8.77622923e-09, -1.28545208e-12,
      1.04088818e+04, 22.3747992]
    - [9.11079978, 0.013758966, -5.15319199e-06, 9.32421983e-10, -6.74695911e-14,
      7773.7617, -21.0036658]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.820000000000001
    well-depth: 411.0
    rotational-relaxation: 1.0
- name: C3H4-P
  composition: {C: 3, H: 4}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1570.0, 3500.0]
    data:
    - [1.72714322, 0.0226902153, -1.51273023e-05, 5.4293002e-09, -8.07229635e-13,
      2.08991609e+04, 13.8804115]
    - [6.45797858, 0.0106371316, -3.61161722e-06, 5.39412692e-10, -2.85851276e-14,
      1.94136786e+04, -11.0770989]
  transport:
    model: gas
    geometry: linear
    diameter: 4.29
    well-depth: 324.8
    rotational-relaxation: 1.0
- name: C3H4-A
  composition: {C: 3, H: 4}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1420.0, 3500.0]
    data:
    - [0.508248695, 0.0275573205, -2.13550933e-05, 8.81402419e-09, -1.47914981e-12,
      2.17582498e+04, 19.0382079]
    - [6.37608366, 0.0110282079, -3.89476312e-06, 6.16686075e-10, -3.59564767e-14,
      2.00917847e+04, -11.3283006]
  transport:
    model: gas
    geometry: linear
    diameter: 4.29
    well-depth: 324.8
    rotational-relaxation: 1.0
- name: C3H3
  composition: {C: 3, H: 3}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 840.0, 3500.0]
    data:
    - [1.75584152, 0.0295861275, -3.88094537e-05, 2.80498008e-08, -8.1216346e-12,
      4.07276565e+04, 13.5345461]
    - [5.7505776, 0.0105635748, -4.84060957e-06, 1.0904007e-09, -9.8003615e-14,
      4.00565408e+04, -5.04125047]
  transport:
    model: gas
    geometry: linear
    diameter: 4.29
    well-depth: 324.8
    rotational-relaxation: 1.0
- name: C2H3CHO
  composition: {C: 3, H: 4, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1600.0, 3500.0]
    data:
    - [0.818908044, 0.0322215131, -2.33838148e-05, 8.71820988e-09, -1.30539747e-12,
      -9681.68587, 23.6968522]
    - [9.22597838, 0.0112038372, -3.67974366e-06, 5.08180254e-10, -2.25803378e-14,
      -1.23719484e+04, -20.813756]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.958000000000001
    well-depth: 428.8
    dipole: 2.900000827651188
    rotational-relaxation: 1.0
- name: CH3COCH2
  composition: {C: 3, H: 5, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1590.0, 3500.0]
    data:
    - [1.0036744, 0.0315622335, -2.18217955e-05, 7.96708585e-09, -1.18666713e-12,
      -5541.75085, 22.7480006]
    - [8.40473847, 0.0129432044, -4.25667367e-06, 6.02254913e-10, -2.8674842e-14,
      -7895.28923, -16.3899805]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.860000000000001
    well-depth: 435.5
    rotational-relaxation: 1.0
- name: IC4H9
  composition: {C: 4, H: 9}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1430.0, 3500.0]
    data:
    - [-1.15582376, 0.0510042938, -3.53657102e-05, 1.32774789e-08, -2.13948724e-12,
      5984.37685, 31.124482]
    - [7.95880517, 0.0255088283, -8.62221491e-06, 8.09648923e-10, 4.02033219e-14,
      3377.59298, -16.1084037]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 5.24
    well-depth: 352.0
    rotational-relaxation: 1.0
- name: TC4H9
  composition: {C: 4, H: 9}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1400.0, 3500.0]
    data:
    - [-1.29900233, 0.0518342142, -3.6839736e-05, 1.42467509e-08, -2.35878979e-12,
      3413.63196, 30.1901373]
    - [7.90871688, 0.025526445, -8.6528405e-06, 8.24419703e-10, 3.80550654e-14,
      835.470581, -17.3299272]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 5.24
    well-depth: 352.0
    rotational-relaxation: 1.0
- name: IC4H8
  composition: {C: 4, H: 8}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1800.0, 3500.0]
    data:
    - [0.717301598, 0.0401434653, -2.33509125e-05, 6.92571993e-09, -8.39035733e-13,
      -3723.72397, 20.1415164]
    - [7.63433967, 0.0247722696, -1.05415828e-05, 2.18152373e-09, -1.80119594e-13,
      -6213.85767, -17.2949366]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 5.089
    well-depth: 344.5
    dipole: 0.5000001426984807
    rotational-relaxation: 1.0
- name: IC4H7
  composition: {C: 4, H: 7}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 700.0, 3500.0]
    data:
    - [3.86129999, 0.0214653105, 1.51074231e-05, -2.75002866e-08, 1.0867862e-11,
      1.27462902e+04, 8.04059711]
    - [1.18177119, 0.0367769036, -1.77031336e-05, 3.74786264e-09, -2.92191282e-13,
      1.31214242e+04, 20.0120539]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.65
    well-depth: 355.0
    rotational-relaxation: 1.0
- name: IC4H7O
  composition: {C: 4, H: 7, O: 1}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1800.0, 3500.0]
    data:
    - [1.50010972, 0.0420632012, -2.66490883e-05, 8.53521488e-09, -1.09768177e-12,
      4897.27156, 20.5567447]
    - [11.8822163, 0.0189918532, -7.42296498e-06, 1.41442848e-09, -1.0868366e-13,
      1159.71319, -35.6333819]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 5.200000000000001
    well-depth: 495.99999999999994
    rotational-relaxation: 1.0
- name: NEOC5H11
  composition: {C: 5, H: 11}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1670.0, 3500.0]
    data:
    - [-1.29689709, 0.064108572, -4.38302105e-05, 1.52882069e-08, -2.14462305e-12,
      2276.42747, 31.8773552]
    - [14.3276289, 0.0266845577, -1.02158264e-05, 1.86929104e-09, -1.35803312e-13,
      -2942.16421, -51.5145769]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 5.640000000000001
    well-depth: 392.0
    rotational-relaxation: 1.0
- name: IC8H18
  composition: {C: 8, H: 18}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1390.0, 3500.0]
    data:
    - [-5.96912081, 0.12087217, -9.61538217e-05, 4.13489289e-08, -7.18982936e-12,
      -3.02675122e+04, 52.7954202]
    - [20.6155885, 0.0443694094, -1.35968858e-05, 1.75327622e-09, -6.83090879e-14,
      -3.76580614e+04, -84.2148793]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 6.170000000000001
    well-depth: 493.99999999999994
    rotational-relaxation: 1.0
- name: IC8H17
  composition: {C: 8, H: 17}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1530.0, 3500.0]
    data:
    - [-3.32961207, 0.108192845, -8.23053435e-05, 3.33403496e-08, -5.3694368e-12,
      -8906.25182, 41.6697269]
    - [26.510423, 0.0301796816, -5.8218499e-06, 1.42085851e-11, 7.6011076e-14,
      -1.80373025e+04, -114.981197]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 6.170000000000001
    well-depth: 493.99999999999994
    rotational-relaxation: 1.0
- name: IC8H16
  composition: {C: 8, H: 16}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1400.0, 3500.0]
    data:
    - [-5.35586581, 0.110622059, -8.69521729e-05, 3.69705048e-08, -6.36990285e-12,
      -1.56875145e+04, 51.1323811]
    - [18.8616063, 0.0414292819, -1.28170544e-05, 1.66806735e-09, -6.58961709e-14,
      -2.24684067e+04, -73.8514296]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 6.170000000000001
    well-depth: 493.99999999999994
    rotational-relaxation: 1.0
- name: IC16H33
  composition: {C: 16, H: 33}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1650.0, 3500.0]
    data:
    - [-8.95216175, 0.221020633, -1.60372651e-04, 5.84427492e-08, -8.4524958e-12,
      -3.63617056e+04, 76.9829165]
    - [51.1453588, 0.0753296743, -2.79263242e-05, 4.92908201e-09, -3.44364401e-13,
      -5.61938874e+04, -243.048234]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 8.35
    well-depth: 650.0
    rotational-relaxation: 1.0
- name: IC16H34
  composition: {C: 16, H: 34}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1590.0, 3500.0]
    data:
    - [-9.93612249, 0.229338723, -1.69388298e-04, 6.32906266e-08, -9.42998896e-12,
      -5.9688445e+04, 78.2391931]
    - [47.25246, 0.0854680758, -3.36612723e-05, 6.38202029e-09, -4.82094887e-13,
      -7.78744143e+04, -224.18295]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 8.35
    well-depth: 650.0
    rotational-relaxation: 1.0
- name: IC12H26
  composition: {C: 12, H: 26}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1800.0, 3500.0]
    data:
    - [-2.66627705, 0.147343892, -9.43301934e-05, 3.05488933e-08, -3.97016449e-12,
      -4.00651514e+04, 53.203335]
    - [36.1414095, 0.0611045883, -2.24641073e-05, 3.9318244e-09, -2.73349362e-13,
      -5.40359186e+04, -156.83196]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 7.6
    well-depth: 580.0
    rotational-relaxation: 1.0
- name: IC12H25
  composition: {C: 12, H: 25}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1800.0, 3500.0]
    data:
    - [-2.06085145, 0.141179787, -8.91506513e-05, 2.83740186e-08, -3.62710595e-12,
      -1.66984825e+04, 51.116166]
    - [31.7005579, 0.0661544325, -2.6629523e-05, 5.21804509e-09, -4.10998518e-13,
      -2.88525898e+04, -131.607624]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 7.6
    well-depth: 580.0
    rotational-relaxation: 1.0
- name: C4H9O2(L1)
  composition: {C: 4, H: 9, O: 2}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1000.0, 5000.0]
    data:
    - [0.6036022211, 0.05918662306, -4.415150304e-05, 1.785583748e-08, -3.035706167e-12,
      -1.234327857e+04, 26.00614028]
    - [8.771704072, 0.03440633924, -1.592794033e-05, 3.546482418e-09, -3.101813687e-13,
      -1.449803165e+04, -15.66138413]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 5.200000000000001
    well-depth: 495.99999999999994
    rotational-relaxation: 1.0
- name: C3H7(L1)
  composition: {C: 3, H: 7}
  thermo:
    model: NASA7
    temperature-ranges: [300.0, 1000.0, 5000.0]
    data:
    - [-0.1373270785, 0.03508814302, -2.304112061e-05, 8.148400118e-09,
      -1.194531329e-12, 1.084784648e+04, 26.20296145]
    - [6.962702594, 0.01694561468, -5.768942033e-06, 8.698899869e-10, -4.708662155e-14,
      8646.048933, -11.20237391]
  transport:
    model: gas
    geometry: nonlinear
    diameter: 4.81
    well-depth: 303.4
    rotational-relaxation: 1.0

reactions:
- equation: H2 + O <=> H + OH  # Reaction 1
  rate-constant: {A: 5.08e+04, b: 2.67, Ea: 6292.0}
- equation: H2 + OH <=> H + H2O  # Reaction 2
  rate-constant: {A: 4.38e+13, b: 0.0, Ea: 6990.0}
- equation: H + O2 <=> O + OH  # Reaction 3
  rate-constant: {A: 1.14e+14, b: 0.0, Ea: 1.5286e+04}
- equation: H + OH + M <=> H2O + M  # Reaction 4
  type: three-body
  rate-constant: {A: 3.5e+22, b: -2.0, Ea: 0.0}
- equation: H2O + O <=> 2 OH  # Reaction 5
  rate-constant: {A: 6.7e+07, b: 1.704, Ea: 1.49868e+04}
- equation: H2O2 (+M) <=> 2 OH (+M)  # Reaction 6
  type: falloff
  low-P-rate-constant: {A: 2.49e+24, b: -2.3, Ea: 4.8749e+04}
  high-P-rate-constant: {A: 2.0e+12, b: 0.9, Ea: 4.8749e+04}
  Troe: {A: 0.43, T3: 1.0e-30, T1: 1.0000000000000002e+30, T2: 0.0}
  efficiencies: {CO: 2.8, CO2: 1.6, H2O: 7.65, H2O2: 7.7, N2: 1.5, O2: 1.2}
- equation: H2O2 + OH <=> H2O + HO2  # Reaction 7
  rate-constant: {A: 1.74e+12, b: 0.0, Ea: 318.0}
  duplicate: true
- equation: H2O2 + OH <=> H2O + HO2  # Reaction 8
  rate-constant: {A: 7.59e+13, b: 0.0, Ea: 7269.0}
  duplicate: true
- equation: H + HO2 <=> 2 OH  # Reaction 9
  rate-constant: {A: 7.079e+13, b: 0.0, Ea: 295.0}
- equation: H + HO2 <=> H2 + O2  # Reaction 10
  rate-constant: {A: 1.1402e+10, b: 1.083, Ea: 553.78}
- equation: HO2 + O <=> O2 + OH  # Reaction 11
  rate-constant: {A: 3.25e+13, b: 0.0, Ea: 0.0}
- equation: HO2 + OH <=> H2O + O2  # Reaction 12
  rate-constant: {A: 7.0e+12, b: 0.0, Ea: -1092.96}
  duplicate: true
- equation: HO2 + OH <=> H2O + O2  # Reaction 13
  rate-constant: {A: 4.5e+14, b: 0.0, Ea: 1.09296e+04}
  duplicate: true
- equation: 2 HO2 <=> H2O2 + O2  # Reaction 14
  rate-constant: {A: 1.0e+14, b: 0.0, Ea: 1.104088e+04}
  duplicate: true
- equation: 2 HO2 <=> H2O2 + O2  # Reaction 15
  rate-constant: {A: 1.9e+11, b: 0.0, Ea: -1408.92}
  duplicate: true
- equation: H + O2 (+M) <=> HO2 (+M)  # Reaction 16
  type: falloff
  low-P-rate-constant: {A: 1.74e+19, b: -1.23, Ea: 0.0}
  high-P-rate-constant: {A: 4.65e+12, b: 0.44, Ea: 0.0}
  Troe: {A: 0.67, T3: 1.0e-30, T1: 1.0000000000000002e+30, T2: 1.0e+30}
  efficiencies: {CO: 1.9, CO2: 3.8, H2O: 10.0}
- equation: CO + OH <=> CO2 + H  # Reaction 17
  rate-constant: {A: 7.015e+04, b: 2.053, Ea: -355.7}
  duplicate: true
- equation: CO + OH <=> CO2 + H  # Reaction 18
  rate-constant: {A: 5.757e+12, b: -0.664, Ea: 331.8}
  duplicate: true
- equation: CH3 + H (+M) <=> CH4 (+M)  # Reaction 19
  type: falloff
  low-P-rate-constant: {A: 2.48e+33, b: -4.76, Ea: 2440.0}
  high-P-rate-constant: {A: 1.27e+16, b: -0.63, Ea: 383.0}
  Troe: {A: 0.783, T3: 74.0, T1: 2941.0, T2: 6964.0}
  efficiencies: {CH4: 2.0, CO: 1.5, CO2: 2.0, H2O: 6.0}
- equation: CH4 + H <=> CH3 + H2  # Reaction 20
  rate-constant: {A: 6.14e+05, b: 2.5, Ea: 9587.0}
- equation: CH4 + OH <=> CH3 + H2O  # Reaction 21
  rate-constant: {A: 5.83e+04, b: 2.6, Ea: 2190.0}
- equation: CH3 + HO2 <=> CH4 + O2  # Reaction 22
  rate-constant: {A: 1.16e+05, b: 2.23, Ea: -3022.0}
- equation: CH2(S) + N2 <=> CH2 + N2  # Reaction 23
  rate-constant: {A: 1.5e+13, b: 0.0, Ea: 600.0}
- equation: CH2(S) + O2 => CO + H + OH  # Reaction 24
  rate-constant: {A: 2.8e+13, b: 0.0, Ea: 0.0}
- equation: CH2(S) + O2 <=> CO + H2O  # Reaction 25
  rate-constant: {A: 1.2e+13, b: 0.0, Ea: 0.0}
- equation: CH2(S) + H2 <=> CH3 + H  # Reaction 26
  rate-constant: {A: 7.0e+13, b: 0.0, Ea: 0.0}
- equation: CH2 + O2 <=> HCO + OH  # Reaction 27
  rate-constant: {A: 1.06e+13, b: 0.0, Ea: 1500.0}
- equation: CH2 + O2 => CO2 + 2 H  # Reaction 28
  rate-constant: {A: 2.64e+12, b: 0.0, Ea: 1500.0}
- equation: CH2 + H <=> CH + H2  # Reaction 29
  rate-constant: {A: 3.0e+13, b: 0.0, Ea: 0.0}
- equation: CH + O2 <=> HCO + O  # Reaction 30
  rate-constant: {A: 3.3e+13, b: 0.0, Ea: 0.0}
- equation: CH + H <=> C + H2  # Reaction 31
  rate-constant: {A: 1.1e+14, b: 0.0, Ea: 0.0}
- equation: C + O2 <=> CO + O  # Reaction 32
  rate-constant: {A: 5.0e+13, b: 0.0, Ea: 0.0}
- equation: CH3 + O2 <=> CH3O + O  # Reaction 33
  rate-constant: {A: 7.546e+12, b: 0.0, Ea: 2.832e+04}
- equation: CH3 + O2 <=> CH2O + OH  # Reaction 34
  rate-constant: {A: 2.641, b: 3.283, Ea: 8105.0}
- equation: CH3 + O <=> CH2O + H  # Reaction 35
  rate-constant: {A: 5.54e+13, b: 0.05, Ea: -136.0}
- equation: CH3 + OH <=> CH2(S) + H2O  # Reaction 36
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1013.25, A: 4.936e+14, b: -0.669, Ea: -445.8}
  - {P: 1.01325e+04, A: 1.207e+15, b: -0.778, Ea: -175.6}
  - {P: 1.01325e+05, A: 5.282e+17, b: -1.518, Ea: 1772.0}
  - {P: 1.01325e+06, A: 4.788e+23, b: -3.155, Ea: 7003.0}
  - {P: 1.01325e+07, A: 8.433e+19, b: -1.962, Ea: 8244.0}
- equation: CH3 + OH <=> CH2OH + H  # Reaction 37
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1013.25, A: 1.621e+10, b: 0.965, Ea: 3214.0}
  - {P: 1.01325e+04, A: 1.807e+10, b: 0.95, Ea: 3247.0}
  - {P: 1.01325e+05, A: 4.686e+10, b: 0.833, Ea: 3566.0}
  - {P: 1.01325e+06, A: 1.525e+13, b: 0.134, Ea: 5641.0}
  - {P: 1.01325e+07, A: 3.59e+14, b: -0.186, Ea: 8601.0}
- equation: CH3 + OH <=> CH2 + H2O  # Reaction 38
  rate-constant: {A: 4.293e+04, b: 2.568, Ea: 3997.8}
- equation: CH3 + HO2 <=> CH3O + OH  # Reaction 39
  rate-constant: {A: 1.0e+12, b: 0.269, Ea: -687.5}
- equation: CH2OH + O2 <=> CH2O + HO2  # Reaction 40
  rate-constant: {A: 1.51e+15, b: -1.0, Ea: 0.0}
  duplicate: true
- equation: CH2OH + O2 <=> CH2O + HO2  # Reaction 41
  rate-constant: {A: 2.41e+14, b: 0.0, Ea: 5017.0}
  duplicate: true
- equation: CH3O + O2 <=> CH2O + HO2  # Reaction 42
  rate-constant: {A: 4.38e-19, b: 9.5, Ea: -5501.0}
- equation: CH2O + O2 <=> HCO + HO2  # Reaction 43
  rate-constant: {A: 8.07e+15, b: 0.0, Ea: 5.342e+04}
- equation: CH2O + H <=> H2 + HCO  # Reaction 44
  rate-constant: {A: 5.74e+07, b: 1.9, Ea: 2740.0}
- equation: CH2O + OH <=> H2O + HCO  # Reaction 45
  rate-constant: {A: 7.82e+07, b: 1.63, Ea: -1055.0}
- equation: CH2O + HO2 <=> H2O2 + HCO  # Reaction 46
  rate-constant: {A: 1.88e+04, b: 2.7, Ea: 1.152e+04}
- equation: CH2O + CH3 <=> CH4 + HCO  # Reaction 47
  rate-constant: {A: 38.3, b: 3.36, Ea: 4312.0}
- equation: HCO + M <=> CO + H + M  # Reaction 48
  type: three-body
  rate-constant: {A: 5.7e+11, b: 0.66, Ea: 1.487e+04}
  efficiencies: {CO: 1.5, CO2: 2.0, H2O: 6.0}
- equation: HCO + O2 <=> CO + HO2  # Reaction 49
  rate-constant: {A: 7.58e+12, b: 0.0, Ea: 410.0}
- equation: H + HCO <=> CO + H2  # Reaction 50
  rate-constant: {A: 7.34e+13, b: 0.0, Ea: 0.0}
- equation: HCO + OH <=> CO + H2O  # Reaction 51
  rate-constant: {A: 3.011e+13, b: 0.0, Ea: 0.0}
- equation: HCO + HO2 => CO2 + H + OH  # Reaction 52
  rate-constant: {A: 3.0e+13, b: 0.0, Ea: 0.0}
- equation: CH2O + H (+M) <=> CH2OH (+M)  # Reaction 53
  type: falloff
  low-P-rate-constant: {A: 1.27e+32, b: -4.82, Ea: 6530.0}
  high-P-rate-constant: {A: 5.4e+11, b: 0.454, Ea: 3600.0}
  Troe: {A: 0.7187, T3: 103.00000000000001, T1: 1291.0, T2: 4160.0}
  efficiencies: {CO: 1.5, CO2: 2.0, H2O: 6.0}
- equation: CH3O (+M) <=> CH2O + H (+M)  # Reaction 54
  type: falloff
  low-P-rate-constant: {A: 1.87e+25, b: -3.0, Ea: 2.4307e+04}
  high-P-rate-constant: {A: 6.8e+13, b: 0.0, Ea: 2.617e+04}
  Troe: {A: 0.9, T3: 2500.0, T1: 1300.0, T2: 1.0e+99}
  efficiencies: {CO: 1.5, CO2: 2.0, H2O: 6.0}
- equation: 2 CH3 (+M) <=> C2H6 (+M)  # Reaction 55
  type: falloff
  low-P-rate-constant: {A: 8.05e+31, b: -3.75, Ea: 981.6}
  high-P-rate-constant: {A: 2.277e+15, b: -0.69, Ea: 174.9}
  Troe: {A: 0.0, T3: 570.0, T1: 1.0000000000000002e+30, T2: 1.0e+30}
  efficiencies: {CO: 2.0, CO2: 3.0, H2O: 5.0}
- equation: C2H6 + O <=> C2H5 + OH  # Reaction 56
  rate-constant: {A: 3.55e+06, b: 2.4, Ea: 5830.0}
- equation: C2H6 + H <=> C2H5 + H2  # Reaction 57
  rate-constant: {A: 1.15e+08, b: 1.9, Ea: 7530.0}
- equation: C2H6 + CH3 <=> C2H5 + CH4  # Reaction 58
  rate-constant: {A: 5.55e-04, b: 4.72, Ea: 3231.0}
- equation: C2H4 + H (+M) <=> C2H5 (+M)  # Reaction 59
  type: falloff
  low-P-rate-constant: {A: 1.42e+39, b: -6.642, Ea: 5769.0}
  high-P-rate-constant: {A: 9.569e+08, b: 1.463, Ea: 1355.0}
  Troe: {A: -0.569, T3: 299.0, T1: -9147.0, T2: 152.4}
  efficiencies: {CO: 1.5, CO2: 2.0, H2O: 6.0}
- equation: 2 CH3 <=> C2H5 + H  # Reaction 60
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1013.25, A: 4.74e+12, b: 0.105, Ea: 1.06643e+04}
  - {P: 1.01325e+04, A: 2.57e+13, b: -0.096, Ea: 1.14061e+04}
  - {P: 1.01325e+05, A: 3.1e+14, b: -0.362, Ea: 1.33725e+04}
  - {P: 1.01325e+06, A: 2.15e+10, b: 0.885, Ea: 1.35325e+04}
  - {P: 1.01325e+07, A: 103.2, b: 3.23, Ea: 1.12361e+04}
- equation: C2H5 + O2 <=> C2H4 + HO2  # Reaction 61
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 4053.0, A: 2.094e+09, b: 0.49, Ea: -391.4}
  - {P: 1.01325e+05, A: 1.843e+07, b: 1.13, Ea: -720.6}
  - {P: 1.01325e+06, A: 7.561e+14, b: -1.01, Ea: 4749.0}
- equation: C2H4 + OH <=> C2H3 + H2O  # Reaction 62
  rate-constant: {A: 2.23e+04, b: 2.745, Ea: 2215.5}
- equation: C2H4 + CH3 <=> C2H3 + CH4  # Reaction 63
  rate-constant: {A: 976.0, b: 2.947, Ea: 1.5148e+04}
  duplicate: true
- equation: C2H4 + CH3 <=> C2H3 + CH4  # Reaction 64
  rate-constant: {A: 8.13e-05, b: 4.417, Ea: 8835.8}
  duplicate: true
- equation: C2H4 + O <=> CH2CHO + H  # Reaction 65
  rate-constant: {A: 6.098e+06, b: 1.88, Ea: 183.0}
- equation: C2H2 + H (+M) <=> C2H3 (+M)  # Reaction 66
  type: falloff
  low-P-rate-constant: {A: 6.35e+31, b: -4.664, Ea: 3780.0}
  high-P-rate-constant: {A: 1.71e+10, b: 1.266, Ea: 2709.0}
  Troe: {A: 0.788, T3: -1.02e+04, T1: 1.0e-30, T2: 0.0}
  efficiencies: {CO: 1.5, CO2: 2.0, H2O: 6.0}
- equation: C2H3 + O2 <=> CH2CHO + O  # Reaction 67
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 7.88e+20, b: -2.67, Ea: 6742.0}
  - {P: 1.01325e+04, A: 7.72e+20, b: -2.67, Ea: 6713.0}
  - {P: 3.20187e+04, A: 9.87e+20, b: -2.7, Ea: 6724.0}
  - {P: 1.01325e+05, A: 7.1e+20, b: -2.65, Ea: 6489.0}
  - {P: 3.20187e+05, A: 4.5e+20, b: -2.53, Ea: 6406.0}
  - {P: 1.01325e+06, A: 1.76e+23, b: -3.22, Ea: 8697.0}
  - {P: 3.20187e+06, A: 3.14e+25, b: -3.77, Ea: 1.153e+04}
  - {P: 1.01325e+07, A: 1.02e+26, b: -3.8, Ea: 1.391e+04}
- equation: C2H3 + O2 <=> CH2CHO + O  # Reaction 68
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.36e+10, b: 0.62, Ea: -277.6}
  - {P: 1.01325e+04, A: 1.42e+10, b: 0.62, Ea: -247.7}
  - {P: 3.20187e+04, A: 1.66e+10, b: 0.6, Ea: -162.5}
  - {P: 1.01325e+05, A: 2.02e+10, b: 0.58, Ea: 38.4}
  - {P: 3.20187e+05, A: 9.75e+09, b: 0.67, Ea: 248.0}
  - {P: 1.01325e+06, A: 7.34e+09, b: 0.72, Ea: 778.1}
  - {P: 3.20187e+06, A: 1.57e+09, b: 0.92, Ea: 1219.0}
  - {P: 1.01325e+07, A: 7.85e+07, b: 1.28, Ea: 1401.0}
- equation: C2H3 + O2 <=> C2H2 + HO2  # Reaction 69
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.08e+07, b: 1.28, Ea: 3322.0}
  - {P: 1.01325e+04, A: 7.75e+06, b: 1.33, Ea: 3216.0}
  - {P: 3.20187e+04, A: 1.21e+07, b: 1.27, Ea: 3311.0}
  - {P: 1.01325e+05, A: 2.15e+07, b: 1.19, Ea: 3367.0}
  - {P: 3.20187e+05, A: 1.13e+08, b: 1.0, Ea: 3695.0}
  - {P: 1.01325e+06, A: 1.31e+11, b: 0.12, Ea: 5872.0}
  - {P: 3.20187e+06, A: 1.19e+09, b: 0.82, Ea: 5617.0}
  - {P: 1.01325e+07, A: 1.06e+17, b: -1.45, Ea: 1.223e+04}
- equation: C2H3 + O2 <=> C2H2 + HO2  # Reaction 70
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 47.6, b: 2.75, Ea: -796.4}
  - {P: 1.01325e+04, A: 51.6, b: 2.73, Ea: -768.3}
  - {P: 3.20187e+04, A: 55.5, b: 2.73, Ea: -658.5}
  - {P: 1.01325e+05, A: 46.0, b: 2.76, Ea: -492.8}
  - {P: 3.20187e+05, A: 3.75, b: 3.07, Ea: -601.0}
  - {P: 1.01325e+06, A: 5.48, b: 3.07, Ea: 85.7}
  - {P: 3.20187e+06, A: 4.47e+08, b: 0.0, Ea: 955.0}
  - {P: 1.01325e+07, A: 20.2, b: 2.94, Ea: 1847.0}
- equation: C2H3 + O2 <=> CH2CO + OH  # Reaction 71
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 866.0, b: 2.41, Ea: 6061.0}
  - {P: 1.01325e+04, A: 891.0, b: 2.41, Ea: 6078.0}
  - {P: 3.20187e+04, A: 943.0, b: 2.4, Ea: 6112.0}
  - {P: 1.01325e+05, A: 1060.0, b: 2.39, Ea: 6180.0}
  - {P: 3.20187e+05, A: 1090.0, b: 2.38, Ea: 6179.0}
  - {P: 1.01325e+06, A: 1390.0, b: 2.36, Ea: 6074.0}
  - {P: 3.20187e+06, A: 2.49e+06, b: 1.42, Ea: 8480.0}
  - {P: 1.01325e+07, A: 1.66e+10, b: 0.36, Ea: 1.201e+04}
- equation: C2H3 + O2 <=> CH2CO + OH  # Reaction 72
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 0.182, b: 3.12, Ea: 1331.0}
  - {P: 1.01325e+04, A: 0.207, b: 3.11, Ea: 1383.0}
  - {P: 3.20187e+04, A: 0.271, b: 3.08, Ea: 1496.0}
  - {P: 1.01325e+05, A: 0.526, b: 3.01, Ea: 1777.0}
  - {P: 3.20187e+05, A: 1.37, b: 2.9, Ea: 2225.0}
  - {P: 1.01325e+06, A: 0.419, b: 2.93, Ea: 2052.0}
  - {P: 3.20187e+06, A: 1.19e-04, b: 4.21, Ea: 2043.0}
  - {P: 1.01325e+07, A: 1.3e-03, b: 3.97, Ea: 3414.0}
- equation: C2H3 + O2 <=> CH2O + HCO  # Reaction 73
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 2.49e+36, b: -7.6, Ea: 1.264e+04}
  - {P: 1.01325e+04, A: 2.43e+36, b: -7.6, Ea: 1.261e+04}
  - {P: 3.20187e+04, A: 1.95e+36, b: -7.57, Ea: 1.249e+04}
  - {P: 1.01325e+05, A: 2.73e+35, b: -7.32, Ea: 1.182e+04}
  - {P: 3.20187e+05, A: 1.43e+36, b: -7.47, Ea: 1.246e+04}
  - {P: 1.01325e+06, A: 5.18e+35, b: -7.2, Ea: 1.343e+04}
  - {P: 3.20187e+06, A: 3.19e+20, b: -2.57, Ea: 5578.0}
  - {P: 1.01325e+07, A: 2.73e+33, b: -6.28, Ea: 1.6e+04}
- equation: C2H3 + O2 <=> CH2O + HCO  # Reaction 74
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 4.54e+15, b: -1.28, Ea: 515.3}
  - {P: 1.01325e+04, A: 4.59e+15, b: -1.28, Ea: 513.0}
  - {P: 3.20187e+04, A: 4.81e+15, b: -1.29, Ea: 520.6}
  - {P: 1.01325e+05, A: 6.08e+15, b: -1.31, Ea: 645.7}
  - {P: 3.20187e+05, A: 9.45e+15, b: -1.36, Ea: 1066.0}
  - {P: 1.01325e+06, A: 2.56e+15, b: -1.18, Ea: 1429.0}
  - {P: 3.20187e+06, A: 1.03e+69, b: -19.23, Ea: 1.476e+04}
  - {P: 1.01325e+07, A: 4.21e+10, b: 0.19, Ea: 830.6}
- equation: C2H3 + O2 => CH2O + CO + H  # Reaction 75
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 5.82e+36, b: -7.6, Ea: 1.264e+04}
  - {P: 1.01325e+04, A: 5.66e+36, b: -7.6, Ea: 1.261e+04}
  - {P: 3.20187e+04, A: 4.55e+36, b: -7.57, Ea: 1.249e+04}
  - {P: 1.01325e+05, A: 6.36e+35, b: -7.32, Ea: 1.182e+04}
  - {P: 3.20187e+05, A: 3.35e+36, b: -7.47, Ea: 1.246e+04}
  - {P: 1.01325e+06, A: 1.21e+36, b: -7.2, Ea: 1.343e+04}
  - {P: 3.20187e+06, A: 7.43e+20, b: -2.57, Ea: 5578.0}
  - {P: 1.01325e+07, A: 6.36e+33, b: -6.28, Ea: 1.6e+04}
- equation: C2H3 + O2 => CH2O + CO + H  # Reaction 76
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.06e+16, b: -1.28, Ea: 515.3}
  - {P: 1.01325e+04, A: 1.07e+16, b: -1.28, Ea: 513.0}
  - {P: 3.20187e+04, A: 1.13e+16, b: -1.29, Ea: 520.6}
  - {P: 1.01325e+05, A: 1.42e+16, b: -1.31, Ea: 645.7}
  - {P: 3.20187e+05, A: 2.2e+16, b: -1.36, Ea: 1066.0}
  - {P: 1.01325e+06, A: 5.98e+15, b: -1.18, Ea: 1429.0}
  - {P: 3.20187e+06, A: 2.39e+69, b: -19.23, Ea: 1.476e+04}
  - {P: 1.01325e+07, A: 9.81e+10, b: 0.19, Ea: 830.6}
- equation: C2H3 + O2 <=> CH3O + CO  # Reaction 77
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 8.19e+18, b: -2.66, Ea: 3201.0}
  - {P: 1.01325e+04, A: 4.06e+14, b: -1.32, Ea: 885.8}
  - {P: 3.20187e+04, A: 4.34e+14, b: -1.33, Ea: 900.6}
  - {P: 1.01325e+05, A: 1.03e+11, b: -0.33, Ea: -747.8}
  - {P: 3.20187e+05, A: 1.89e+12, b: -3.0, Ea: -8995.0}
  - {P: 1.01325e+06, A: 1.93e+24, b: -5.63, Ea: 1.8}
  - {P: 3.20187e+06, A: 1.1e+18, b: -2.22, Ea: 5178.0}
  - {P: 1.01325e+07, A: 5.79e+32, b: -6.45, Ea: 1.681e+04}
- equation: C2H3 + O2 <=> CH3O + CO  # Reaction 78
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.29e+09, b: 0.18, Ea: -1717.0}
  - {P: 1.01325e+04, A: 5.99e+11, b: -2.93, Ea: -9564.0}
  - {P: 3.20187e+04, A: 2.91e+11, b: -2.93, Ea: -1.012e+04}
  - {P: 1.01325e+05, A: 5.77e+21, b: -3.54, Ea: 4772.0}
  - {P: 3.20187e+05, A: 4.99e+15, b: -1.62, Ea: 1849.0}
  - {P: 1.01325e+06, A: 9.33e+16, b: -1.96, Ea: 3324.0}
  - {P: 3.20187e+06, A: 1.02e+72, b: -20.69, Ea: 1.586e+04}
  - {P: 1.01325e+07, A: 1.1e+09, b: 0.31, Ea: 1024.0}
- equation: C2H3 + O2 <=> CH3 + CO2  # Reaction 79
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 2.37e+35, b: -7.76, Ea: 1.263e+04}
  - {P: 1.01325e+04, A: 1.73e+35, b: -7.72, Ea: 1.252e+04}
  - {P: 3.20187e+04, A: 4.47e+34, b: -7.55, Ea: 1.214e+04}
  - {P: 1.01325e+05, A: 7.25e+31, b: -6.7, Ea: 1.044e+04}
  - {P: 3.20187e+05, A: 3.63e+35, b: -7.75, Ea: 1.283e+04}
  - {P: 1.01325e+06, A: 2.09e+35, b: -7.53, Ea: 1.405e+04}
  - {P: 3.20187e+06, A: 3.84e+18, b: -2.44, Ea: 5408.0}
  - {P: 1.01325e+07, A: 1.21e+32, b: -6.32, Ea: 1.619e+04}
- equation: C2H3 + O2 <=> CH3 + CO2  # Reaction 80
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 6.27e+13, b: -1.16, Ea: 406.3}
  - {P: 1.01325e+04, A: 6.24e+13, b: -1.16, Ea: 401.4}
  - {P: 3.20187e+04, A: 6.12e+13, b: -1.16, Ea: 397.0}
  - {P: 1.01325e+05, A: 5.32e+13, b: -1.14, Ea: 446.7}
  - {P: 3.20187e+05, A: 1.45e+14, b: -1.26, Ea: 987.7}
  - {P: 1.01325e+06, A: 5.02e+13, b: -1.11, Ea: 1409.0}
  - {P: 3.20187e+06, A: 1.4e+70, b: -20.11, Ea: 1.543e+04}
  - {P: 1.01325e+07, A: 9.21e+08, b: 0.25, Ea: 855.3}
- equation: C2H3 + H <=> C2H2 + H2  # Reaction 81
  rate-constant: {A: 9.6353e+13, b: 0.0, Ea: 0.0}
- equation: C2H3 + OH <=> C2H2 + H2O  # Reaction 82
  rate-constant: {A: 3.011e+13, b: 0.0, Ea: 0.0}
- equation: C2H2 + O <=> H + HCCO  # Reaction 83
  rate-constant: {A: 2.958e+09, b: 1.28, Ea: 2472.0}
- equation: C2H2 + OH <=> CH2CO + H  # Reaction 84
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1013.25, A: 1578.0, b: 2.56, Ea: -844.5}
  - {P: 2533.125, A: 1.518e+04, b: 2.28, Ea: -292.1}
  - {P: 1.01325e+04, A: 3.017e+05, b: 1.92, Ea: 598.1}
  - {P: 1.01325e+05, A: 7.528e+06, b: 1.55, Ea: 2106.0}
  - {P: 1.01325e+06, A: 5.101e+06, b: 1.65, Ea: 3400.0}
  - {P: 1.01325e+07, A: 1.457e+04, b: 2.45, Ea: 4477.0}
- equation: C2H + O2 <=> CO + HCO  # Reaction 85
  rate-constant: {A: 5.0e+13, b: 0.0, Ea: 1500.0}
- equation: CH3CO <=> CH3 + CO  # Reaction 86
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1.01325e+04, A: 1.96e+16, b: -2.09, Ea: 1.51966e+04}
  - {P: 1.01325e+05, A: 6.45e+18, b: -2.52, Ea: 1.64365e+04}
  - {P: 1.01325e+06, A: 8.18e+19, b: -2.55, Ea: 1.72631e+04}
  - {P: 1.01325e+07, A: 1.26e+20, b: -2.32, Ea: 1.80121e+04}
- equation: CH2CHO (+M) <=> CH3 + CO (+M)  # Reaction 87
  type: falloff
  low-P-rate-constant: {A: 9.52e+33, b: -5.07, Ea: 4.13e+04}
  high-P-rate-constant: {A: 2.93e+12, b: 0.29, Ea: 4.03e+04}
  Troe: {A: 7.13e-17, T3: 1150.0, T1: 4.99e+09, T2: 1.79e+09}
- equation: CH2CO + H <=> CH3 + CO  # Reaction 88
  rate-constant: {A: 7.77e+08, b: 1.45, Ea: 2780.0}
- equation: CH2CO + OH <=> CH2OH + CO  # Reaction 89
  rate-constant: {A: 2.0e+12, b: 0.0, Ea: -1010.0}
- equation: HCCO + OH => 2 CO + H2  # Reaction 90
  rate-constant: {A: 1.0e+14, b: 0.0, Ea: 0.0}
- equation: H + HCCO <=> CH2(S) + CO  # Reaction 91
  rate-constant: {A: 1.0e+14, b: 0.0, Ea: 0.0}
- equation: HCCO + O2 => CO + CO2 + H  # Reaction 92
  rate-constant: {A: 4.78e+12, b: -0.142, Ea: 1150.0}
- equation: C2H3 + CH3 (+M) <=> C3H6 (+M)  # Reaction 93
  type: falloff
  low-P-rate-constant: {A: 4.27e+58, b: -11.94, Ea: 9769.8}
  high-P-rate-constant: {A: 2.5e+13, b: 0.0, Ea: 0.0}
  Troe: {A: 0.175, T3: 1341.0, T1: 6.0e+04, T2: 1.014e+04}
- equation: C2H4 + CH2(S) <=> C3H6  # Reaction 94
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 4.82e+57, b: -14.3, Ea: 1.71e+04}
  - {P: 1.01325e+04, A: 3.84e+59, b: -14.4, Ea: 1.84e+04}
  - {P: 1.01325e+05, A: 2.13e+58, b: -13.5, Ea: 2.04e+04}
  - {P: 1.01325e+06, A: 8.48e+52, b: -11.6, Ea: 2.07e+04}
  - {P: 1.01325e+07, A: 6.07e+47, b: -9.85, Ea: 2.21e+04}
- equation: C2H4 + CH2(S) <=> C3H6  # Reaction 95
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.15e+45, b: -11.1, Ea: 6145.2}
  - {P: 1.01325e+04, A: 1.83e+45, b: -10.7, Ea: 6638.5}
  - {P: 1.01325e+05, A: 1.3e+40, b: -8.77, Ea: 5863.8}
  - {P: 1.01325e+06, A: 2.27e+32, b: -6.14, Ea: 4317.9}
  - {P: 1.01325e+07, A: 1.28e+24, b: -3.49, Ea: 2529.9}
- equation: C2H4 + CH2(S) <=> C3H5-A + H  # Reaction 96
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 8.2e+19, b: -2.06, Ea: 1150.0}
  - {P: 1.01325e+04, A: 2.27e+21, b: -2.44, Ea: 2650.0}
  - {P: 1.01325e+05, A: 4.44e+35, b: -6.55, Ea: 1.39e+04}
  - {P: 1.01325e+06, A: 1.18e+28, b: -4.09, Ea: 1.4e+04}
  - {P: 1.01325e+07, A: 6.51e+26, b: -3.58, Ea: 1.89e+04}
- equation: C2H4 + CH2(S) <=> C3H5-A + H  # Reaction 97
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.08e+07, b: 1.62, Ea: -3174.6}
  - {P: 1.01325e+04, A: 1.37e+05, b: 2.15, Ea: -3799.2}
  - {P: 1.01325e+05, A: 3.89e+14, b: -0.42, Ea: 1237.6}
  - {P: 1.01325e+06, A: 2.45e+10, b: 0.67, Ea: 750.93}
  - {P: 1.01325e+07, A: 181.0, b: 2.97, Ea: -746.03}
- equation: C2H4 + CH2(S) <=> C2H3 + CH3  # Reaction 98
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.77e+19, b: -1.94, Ea: 6790.0}
  - {P: 1.01325e+04, A: 1.68e+19, b: -1.8, Ea: 4310.0}
  - {P: 1.01325e+05, A: 4.16e+24, b: -3.19, Ea: 9760.0}
  - {P: 1.01325e+06, A: 7.89e+24, b: -3.07, Ea: 1.39e+04}
  - {P: 1.01325e+07, A: 7.36e+29, b: -4.28, Ea: 2.38e+04}
- equation: C2H4 + CH2(S) <=> C2H3 + CH3  # Reaction 99
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 4.3e+12, b: 0.19, Ea: -110.41}
  - {P: 1.01325e+04, A: 2.26e+11, b: 0.54, Ea: 47.81}
  - {P: 1.01325e+05, A: 4.92e+09, b: 1.02, Ea: 599.77}
  - {P: 1.01325e+06, A: 1.47e+08, b: 1.33, Ea: 1228.4}
  - {P: 1.01325e+07, A: 8.11e+10, b: 0.55, Ea: 5506.5}
- equation: C2H3 + CH3 <=> C3H5-A + H  # Reaction 100
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 4.12e+29, b: -4.95, Ea: 8000.0}
  - {P: 1.01325e+04, A: 4.86e+30, b: -5.03, Ea: 1.13e+04}
  - {P: 1.01325e+05, A: 5.3e+29, b: -4.57, Ea: 1.44e+04}
  - {P: 1.01325e+06, A: 1.32e+30, b: -4.54, Ea: 1.93e+04}
  - {P: 1.01325e+07, A: 5.16e+28, b: -4.03, Ea: 2.38e+04}
- equation: C2H3 + CH3 <=> C3H5-A + H  # Reaction 101
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 5.73e+15, b: -0.77, Ea: 1195.9}
  - {P: 1.01325e+04, A: 2.06e+13, b: -0.074, Ea: 1428.7}
  - {P: 1.01325e+05, A: 4.48e+10, b: 0.6, Ea: 1421.6}
  - {P: 1.01325e+06, A: 4.1e+06, b: 1.71, Ea: 1056.9}
  - {P: 1.01325e+07, A: 0.137, b: 3.91, Ea: -353.55}
- equation: C3H6 <=> C2H3 + CH3  # Reaction 102
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.88e+78, b: -18.7, Ea: 1.3e+05}
  - {P: 1.01325e+04, A: 8.73e+76, b: -17.9, Ea: 1.32e+05}
  - {P: 1.01325e+05, A: 5.8e+75, b: -17.2, Ea: 1.34e+05}
  - {P: 1.01325e+06, A: 8.12e+71, b: -15.8, Ea: 1.36e+05}
  - {P: 1.01325e+07, A: 2.15e+64, b: -13.4, Ea: 1.35e+05}
- equation: C3H6 <=> C2H3 + CH3  # Reaction 103
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.69e+59, b: -13.6, Ea: 1.1329e+05}
  - {P: 1.01325e+04, A: 2.0e+60, b: -13.7, Ea: 1.1489e+05}
  - {P: 1.01325e+05, A: 6.7e+54, b: -11.8, Ea: 1.1384e+05}
  - {P: 1.01325e+06, A: 1.06e+47, b: -9.27, Ea: 1.1151e+05}
  - {P: 1.01325e+07, A: 7.29e+38, b: -6.7, Ea: 1.0874e+05}
- equation: C3H6 <=> C3H5-A + H  # Reaction 104
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 9.16e+74, b: -17.6, Ea: 1.2e+05}
  - {P: 1.01325e+04, A: 1.73e+70, b: -16.0, Ea: 1.2e+05}
  - {P: 1.01325e+05, A: 1.08e+71, b: -15.9, Ea: 1.2486e+05}
  - {P: 1.01325e+06, A: 6.4e+65, b: -14.2, Ea: 1.25e+05}
  - {P: 1.01325e+07, A: 8.05e+56, b: -11.5, Ea: 1.22e+05}
- equation: C3H6 <=> C3H5-A + H  # Reaction 105
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 2.98e+54, b: -12.3, Ea: 1.012e+05}
  - {P: 1.01325e+04, A: 1.37e+43, b: -8.87, Ea: 9.6365e+04}
  - {P: 1.01325e+05, A: 6.28e+42, b: -8.51, Ea: 9.8004e+04}
  - {P: 1.01325e+06, A: 4.73e+35, b: -6.26, Ea: 9.5644e+04}
  - {P: 1.01325e+07, A: 4.34e+28, b: -4.06, Ea: 9.3114e+04}
- equation: C3H5-T + H <=> C3H6  # Reaction 106
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 4.96e+60, b: -15.2, Ea: 1.8e+04}
  - {P: 1.01325e+04, A: 3.2e+62, b: -15.1, Ea: 2.01e+04}
  - {P: 1.01325e+05, A: 2.31e+60, b: -14.0, Ea: 2.19e+04}
  - {P: 1.01325e+06, A: 3.69e+54, b: -12.0, Ea: 2.21e+04}
  - {P: 1.01325e+07, A: 1.15e+50, b: -10.4, Ea: 2.33e+04}
- equation: C3H5-T + H <=> C3H6  # Reaction 107
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 1.49e+48, b: -12.0, Ea: 7203.3}
  - {P: 1.01325e+04, A: 6.76e+46, b: -11.1, Ea: 7629.9}
  - {P: 1.01325e+05, A: 1.09e+40, b: -8.66, Ea: 6447.8}
  - {P: 1.01325e+06, A: 2.38e+31, b: -5.73, Ea: 4506.0}
  - {P: 1.01325e+07, A: 5.69e+25, b: -3.83, Ea: 3250.4}
- equation: C3H5-T + H <=> C3H5-A + H  # Reaction 108
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 2.11e+17, b: -1.08, Ea: 1290.0}
  - {P: 1.01325e+04, A: 9.05e+29, b: -4.91, Ea: 8540.0}
  - {P: 1.01325e+05, A: 2.98e+30, b: -4.79, Ea: 1.2e+04}
  - {P: 1.01325e+06, A: 8.22e+28, b: -4.14, Ea: 1.54e+04}
  - {P: 1.01325e+07, A: 2.28e+29, b: -4.12, Ea: 2.09e+04}
- equation: C3H5-T + H <=> C3H5-A + H  # Reaction 109
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 6410.0, b: 2.61, Ea: -3778.4}
  - {P: 1.01325e+04, A: 5.19e+14, b: -0.3, Ea: 1090.4}
  - {P: 1.01325e+05, A: 8.17e+11, b: 0.49, Ea: 1184.6}
  - {P: 1.01325e+06, A: 2.79e+09, b: 1.09, Ea: 1187.5}
  - {P: 1.01325e+07, A: 6750.0, b: 2.7, Ea: 373.8}
- equation: C3H5-T + H <=> C2H3 + CH3  # Reaction 110
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 3.31e+16, b: -0.69, Ea: 5200.0}
  - {P: 1.01325e+04, A: 9.04e+16, b: -0.81, Ea: 4800.0}
  - {P: 1.01325e+05, A: 2.01e+24, b: -2.86, Ea: 1.09e+04}
  - {P: 1.01325e+06, A: 2.75e+26, b: -3.31, Ea: 1.58e+04}
  - {P: 1.01325e+07, A: 3.15e+32, b: -4.83, Ea: 2.6e+04}
- equation: C3H5-T + H <=> C2H3 + CH3  # Reaction 111
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 1013.25, A: 8.04e+13, b: -0.14, Ea: 1150.0}
  - {P: 1.01325e+04, A: 7.17e+10, b: 0.67, Ea: 673.8}
  - {P: 1.01325e+05, A: 9.97e+08, b: 1.36, Ea: 1596.4}
  - {P: 1.01325e+06, A: 7.41e+07, b: 1.57, Ea: 2108.8}
  - {P: 1.01325e+07, A: 2.7e+12, b: 0.32, Ea: 6791.8}
- equation: C3H6 + H <=> C3H5-A + H2  # Reaction 112
  rate-constant: {A: 3.644e+05, b: 2.455, Ea: 4361.2}
- equation: C3H6 + O2 <=> C3H5-A + HO2  # Reaction 113
  rate-constant: {A: 1.2e+20, b: -1.67, Ea: 4.61921e+04}
- equation: C3H6 + O <=> C3H5-A + OH  # Reaction 114
  rate-constant: {A: 5.24e+11, b: 0.7, Ea: 5884.0}
- equation: C3H6 + OH <=> C3H5-A + H2O  # Reaction 115
  rate-constant: {A: 4.46e+06, b: 2.072, Ea: 1050.8}
- equation: C3H6 + CH3 <=> C3H5-A + CH4  # Reaction 116
  rate-constant: {A: 2.21, b: 3.5, Ea: 5675.0}
- equation: C3H6 + H <=> C3H5-T + H2  # Reaction 117
  rate-constant: {A: 149.8, b: 3.381, Ea: 8909.5}
- equation: C3H6 + OH <=> C3H5-T + H2O  # Reaction 118
  rate-constant: {A: 1.8e+06, b: 1.979, Ea: 2235.2}
- equation: C3H6 + O <=> C2H5 + HCO  # Reaction 119
  rate-constant: {A: 7.45e+06, b: 1.88, Ea: 183.0}
- equation: C3H6 + H <=> C3H7(L1)  # Reaction 120
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 7.99e+81, b: -23.161, Ea: 2.2239e+04}
  - {P: 4053.0, A: 4.24e+68, b: -18.427, Ea: 1.9665e+04}
  - {P: 1.01325e+05, A: 1.04e+49, b: -11.5, Ea: 1.5359e+04}
  - {P: 1.01325e+06, A: 6.2e+41, b: -8.892, Ea: 1.4637e+04}
  - {P: 1.01325e+07, A: 1.0e-10, b: 0.0, Ea: 0.0}
- equation: C3H6 + H <=> C3H7(L1)  # Reaction 121
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 1.85e+26, b: -5.83, Ea: 3865.8}
  - {P: 4053.0, A: 2.82e+30, b: -6.49, Ea: 5470.8}
  - {P: 1.01325e+05, A: 3.78e+28, b: -5.57, Ea: 5625.1}
  - {P: 1.01325e+06, A: 1.46e+25, b: -4.28, Ea: 5247.8}
  - {P: 1.01325e+07, A: 4.22e+27, b: -4.39, Ea: 9345.8}
- equation: C3H6 + H <=> C2H4 + CH3  # Reaction 122
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 1.54e+09, b: 1.35, Ea: 2542.0}
  - {P: 4053.0, A: 7.88e+10, b: 0.87, Ea: 3599.6}
  - {P: 1.01325e+05, A: 2.67e+12, b: 0.47, Ea: 5431.1}
  - {P: 1.01325e+06, A: 9.25e+22, b: -2.6, Ea: 1.2898e+04}
  - {P: 1.01325e+07, A: 1.32e+23, b: -2.42, Ea: 1.65e+04}
- equation: C3H6 + H <=> C2H4 + CH3  # Reaction 123
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 1.0e-10, b: 0.0, Ea: 0.0}
  - {P: 4053.0, A: 1.0e-10, b: 0.0, Ea: 0.0}
  - {P: 1.01325e+05, A: 1.0e-10, b: 0.0, Ea: 0.0}
  - {P: 1.01325e+06, A: 1.24e+05, b: 2.52, Ea: 3679.1}
  - {P: 1.01325e+07, A: 2510.0, b: 2.91, Ea: 3980.9}
- equation: C3H6 + H <=> C3H7(L1)  # Reaction 124
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 1.35e+44, b: -10.68, Ea: 8196.4}
  - {P: 4053.0, A: 2.11e+57, b: -14.23, Ea: 1.5147e+04}
  - {P: 1.01325e+05, A: 3.26e+61, b: -14.94, Ea: 2.0161e+04}
  - {P: 1.01325e+06, A: 5.3e+56, b: -13.12, Ea: 2.0667e+04}
  - {P: 1.01325e+07, A: 1.11e+50, b: -10.8, Ea: 2.0202e+04}
- equation: C3H6 + H <=> C3H7(L1)  # Reaction 125
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 2.17e+130, b: -32.58, Ea: 1.3614e+05}
  - {P: 4053.0, A: 2.25e+29, b: -5.84, Ea: 4241.9}
  - {P: 1.01325e+05, A: 1.06e+30, b: -5.63, Ea: 5613.4}
  - {P: 1.01325e+06, A: 6.11e+26, b: -4.44, Ea: 5182.3}
  - {P: 1.01325e+07, A: 2.73e+23, b: -3.26, Ea: 4597.0}
- equation: C2H4 + CH3 <=> C3H7(L1)  # Reaction 126
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 8.67e+48, b: -12.54, Ea: 1.8206e+04}
  - {P: 4053.0, A: 1.06e+49, b: -12.04, Ea: 2.0001e+04}
  - {P: 1.01325e+05, A: 7.67e+47, b: -11.17, Ea: 2.2366e+04}
  - {P: 1.01325e+06, A: 1.81e+45, b: -10.03, Ea: 2.3769e+04}
  - {P: 1.01325e+07, A: 2.04e+40, b: -8.25, Ea: 2.4214e+04}
- equation: C2H4 + CH3 <=> C3H7(L1)  # Reaction 127
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 1.12e+43, b: -11.3, Ea: 1.308e+04}
  - {P: 4053.0, A: 7.28e+39, b: -9.88, Ea: 1.3164e+04}
  - {P: 1.01325e+05, A: 2.6e+33, b: -7.46, Ea: 1.2416e+04}
  - {P: 1.01325e+06, A: 3.85e+27, b: -5.38, Ea: 1.1455e+04}
  - {P: 1.01325e+07, A: 1.66e+21, b: -3.17, Ea: 1.0241e+04}
- equation: C3H5-T + O2 <=> CH3COCH2 + O  # Reaction 128
  rate-constant: {A: 9.86e+25, b: -3.751, Ea: 1.12554e+04}
- equation: C3H5-T + O2 <=> CH2O + CH3CO  # Reaction 129
  rate-constant: {A: 2.55e+20, b: -2.608, Ea: 1565.7}
- equation: C3H5-A + HO2 <=> C3H5O + OH  # Reaction 130
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1013.25, A: 1.02e+13, b: -0.158, Ea: -1417.0}
  - {P: 1.01325e+04, A: 4.98e+14, b: -0.642, Ea: -349.1}
  - {P: 1.01325e+05, A: 7.77e+17, b: -1.52, Ea: 2379.2}
  - {P: 1.01325e+06, A: 2.93e+15, b: -0.684, Ea: 3615.3}
  - {P: 1.01325e+07, A: 1.64e+04, b: 2.74, Ea: 1144.4}
- equation: C3H5O <=> C2H3 + CH2O  # Reaction 131
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 101.325, A: 7.26e+06, b: 0.182, Ea: 1.78155e+04}
  - {P: 1013.25, A: 6.97e+16, b: -2.5, Ea: 2.08787e+04}
  - {P: 1.01325e+04, A: 6.64e+23, b: -4.23, Ea: 2.3565e+04}
  - {P: 1.01325e+05, A: 1.07e+26, b: -4.56, Ea: 2.46229e+04}
  - {P: 1.01325e+06, A: 6.5e+29, b: -5.37, Ea: 2.6645e+04}
  - {P: 1.01325e+07, A: 4.63e+31, b: -5.59, Ea: 2.89153e+04}
  - {P: 1.01325e+08, A: 8.52e+25, b: -3.61, Ea: 2.78634e+04}
- equation: C3H5O <=> C2H3CHO + H  # Reaction 132
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 101.325, A: 3.0e+15, b: -2.31, Ea: 1.46679e+04}
  - {P: 1013.25, A: 1.5e+22, b: -3.96, Ea: 1.8283e+04}
  - {P: 1.01325e+04, A: 1.95e+23, b: -3.99, Ea: 1.91433e+04}
  - {P: 1.01325e+05, A: 1.15e+25, b: -4.24, Ea: 2.03112e+04}
  - {P: 1.01325e+06, A: 1.76e+28, b: -4.89, Ea: 2.27652e+04}
  - {P: 1.01325e+07, A: 1.41e+27, b: -4.28, Ea: 2.37706e+04}
  - {P: 1.01325e+08, A: 2.57e+20, b: -2.06, Ea: 2.20401e+04}
- equation: C3H4-A + OH <=> C3H3 + H2O  # Reaction 133
  rate-constant: {A: 2.0e+07, b: 2.0, Ea: 5000.0}
- equation: C3H4-A + CH3 <=> C3H3 + CH4  # Reaction 134
  rate-constant: {A: 1.3e+12, b: 0.0, Ea: 7700.0}
- equation: C3H4-A + H <=> C3H4-P + H  # Reaction 135
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 8.49e+10, b: 0.89, Ea: 2503.0}
  - {P: 3951.675, A: 1.48e+13, b: 0.26, Ea: 4103.0}
  - {P: 1.01325e+05, A: 2.48e+15, b: -0.33, Ea: 6436.0}
  - {P: 1.01325e+06, A: 2.35e+25, b: -3.23, Ea: 1.3165e+04}
  - {P: 1.01325e+07, A: 1.02e+24, b: -2.67, Ea: 1.5552e+04}
- equation: C3H4-A + H <=> C3H4-P + H  # Reaction 136
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 1.0e-10, b: 0.0, Ea: 0.0}
  - {P: 3951.675, A: 1.0e-10, b: 0.0, Ea: 0.0}
  - {P: 1.01325e+05, A: 1.0e-10, b: 0.0, Ea: 0.0}
  - {P: 1.01325e+06, A: 1.79e+07, b: 1.98, Ea: 4521.0}
  - {P: 1.01325e+07, A: 4.63e+04, b: 2.62, Ea: 4466.0}
- equation: C3H4-A + H <=> C3H5-A  # Reaction 137
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 2.21e+61, b: -15.25, Ea: 2.0076e+04}
  - {P: 3951.675, A: 1.24e+52, b: -12.02, Ea: 1.7839e+04}
  - {P: 1.01325e+05, A: 4.67e+51, b: -11.45, Ea: 2.134e+04}
  - {P: 1.01325e+06, A: 3.75e+48, b: -10.27, Ea: 2.2511e+04}
  - {P: 1.01325e+07, A: 4.23e+43, b: -8.61, Ea: 2.2522e+04}
- equation: C3H4-A + H <=> C3H5-A  # Reaction 138
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 2.8e+38, b: -8.67, Ea: 8035.0}
  - {P: 3951.675, A: 9.33e+36, b: -8.19, Ea: 7462.0}
  - {P: 1.01325e+05, A: 3.32e+30, b: -5.78, Ea: 6913.0}
  - {P: 1.01325e+06, A: 2.29e+26, b: -4.32, Ea: 6163.0}
  - {P: 1.01325e+07, A: 4.38e+21, b: -2.71, Ea: 5187.0}
- equation: C3H4-A + H <=> C3H5-T  # Reaction 139
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 6.44e+102, b: -27.51, Ea: 5.1768e+04}
  - {P: 3951.675, A: 1.55e+53, b: -13.1, Ea: 1.4472e+04}
  - {P: 1.01325e+05, A: 1.9e+53, b: -12.59, Ea: 1.6726e+04}
  - {P: 1.01325e+06, A: 7.95e+51, b: -11.82, Ea: 1.8286e+04}
  - {P: 1.01325e+07, A: 4.21e+52, b: -11.64, Ea: 2.2262e+04}
- equation: C3H4-A + H <=> C3H5-T  # Reaction 140
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 1.1e+54, b: -14.29, Ea: 1.0809e+04}
  - {P: 3951.675, A: 9.88e+44, b: -11.21, Ea: 8212.0}
  - {P: 1.01325e+05, A: 2.81e+40, b: -9.42, Ea: 7850.0}
  - {P: 1.01325e+06, A: 2.6e+35, b: -7.57, Ea: 7147.0}
  - {P: 1.01325e+07, A: 9.88e+29, b: -5.53, Ea: 6581.0}
- equation: C3H4-A + H <=> C2H2 + CH3  # Reaction 141
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 1.23e+08, b: 1.53, Ea: 4737.0}
  - {P: 3951.675, A: 2.72e+09, b: 1.2, Ea: 6834.0}
  - {P: 1.01325e+05, A: 1.26e+20, b: -1.83, Ea: 1.5003e+04}
  - {P: 1.01325e+06, A: 1.68e+16, b: -0.6, Ea: 1.4754e+04}
  - {P: 1.01325e+07, A: 1.37e+17, b: -0.79, Ea: 1.7603e+04}
- equation: C3H4-A + H <=> C2H2 + CH3  # Reaction 142
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 1.0e-10, b: 0.0, Ea: 0.0}
  - {P: 3951.675, A: 1.0e-10, b: 0.0, Ea: 0.0}
  - {P: 1.01325e+05, A: 1.23e+04, b: 2.68, Ea: 6335.0}
  - {P: 1.01325e+06, A: 3.31e+08, b: 1.14, Ea: 8886.0}
  - {P: 1.01325e+07, A: 1.28e+06, b: 1.71, Ea: 9774.0}
- equation: C3H4-P + H <=> C3H5-T  # Reaction 143
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 8.85e+51, b: -13.04, Ea: 1.2325e+04}
  - {P: 3951.675, A: 3.17e+52, b: -12.69, Ea: 1.4226e+04}
  - {P: 1.01325e+05, A: 2.87e+53, b: -12.51, Ea: 1.6853e+04}
  - {P: 1.01325e+06, A: 9.51e+51, b: -11.74, Ea: 1.8331e+04}
  - {P: 1.01325e+07, A: 4.51e+52, b: -11.58, Ea: 2.2207e+04}
- equation: C3H4-P + H <=> C3H5-T  # Reaction 144
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 101.325, A: 1.97e+46, b: -11.91, Ea: 7456.0}
  - {P: 3951.675, A: 2.59e+45, b: -11.23, Ea: 8046.0}
  - {P: 1.01325e+05, A: 6.93e+39, b: -9.11, Ea: 7458.0}
  - {P: 1.01325e+06, A: 6.8e+34, b: -7.29, Ea: 6722.0}
  - {P: 1.01325e+07, A: 5.65e+29, b: -5.39, Ea: 6150.0}
- equation: C3H4-P + H <=> C2H2 + CH3  # Reaction 145
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 101.325, A: 2.44e+10, b: 1.04, Ea: 3980.0}
  - {P: 3951.675, A: 3.89e+10, b: 0.989, Ea: 4114.0}
  - {P: 1.01325e+05, A: 3.46e+12, b: 0.442, Ea: 5463.0}
  - {P: 1.01325e+06, A: 1.72e+14, b: -0.01, Ea: 7134.0}
  - {P: 1.01325e+07, A: 1.9e+15, b: -0.29, Ea: 8306.0}
- equation: C3H4-A + O <=> C2H4 + CO  # Reaction 146
  rate-constant: {A: 2.0e+07, b: 1.8, Ea: 1000.0}
- equation: C3H3 + O <=> C2H + CH2O  # Reaction 147
  rate-constant: {A: 2.0e+13, b: 0.0, Ea: 0.0}
- equation: C3H3 + O2 <=> CH2CO + HCO  # Reaction 148
  rate-constant: {A: 1.7e+05, b: 1.7, Ea: 1500.0}
- equation: C3H3 + OH <=> C2H3 + HCO  # Reaction 149
  rate-constant: {A: 1.0e+13, b: 0.0, Ea: 0.0}
- equation: IC4H9 <=> TC4H9  # Reaction 150
  rate-constant: {A: 3.56e+10, b: 0.88, Ea: 3.46e+04}
- equation: IC4H9 <=> C3H6 + CH3  # Reaction 151
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1.01325e+04, A: 3.15e+41, b: -9.5, Ea: 3.3486e+04}
  - {P: 1.01325e+05, A: 6.75e+44, b: -10.07, Ea: 3.7209e+04}
  - {P: 1.01325e+06, A: 7.79e+44, b: -9.7, Ea: 3.9751e+04}
  - {P: 1.01325e+07, A: 3.61e+39, b: -7.78, Ea: 3.9583e+04}
- equation: IC4H8 <=> H + IC4H7  # Reaction 152
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1.01325e+04, A: 7.51e+95, b: -23.38, Ea: 1.29214e+05}
  - {P: 1.01325e+05, A: 3.59e+88, b: -20.99, Ea: 1.27813e+05}
  - {P: 3.546375e+05, A: 2.96e+82, b: -19.12, Ea: 1.25456e+05}
  - {P: 1.01325e+06, A: 2.13e+76, b: -17.27, Ea: 1.22629e+05}
  - {P: 3.546375e+06, A: 1.13e+68, b: -14.82, Ea: 1.18416e+05}
  - {P: 1.01325e+07, A: 4.73e+60, b: -12.66, Ea: 1.14404e+05}
- equation: IC4H8 + OH <=> H2O + IC4H7  # Reaction 153
  rate-constant: {A: 4.395e+04, b: 2.678, Ea: -827.1}
- equation: IC4H8 + O2 <=> HO2 + IC4H7  # Reaction 154
  rate-constant: {A: 3.12e+13, b: 0.0, Ea: 3.745e+04}
- equation: IC4H8 + O <=> IC4H7 + OH  # Reaction 155
  rate-constant: {A: 1.05e+12, b: 0.7, Ea: 5884.0}
- equation: C3H4-A + CH3 <=> IC4H7  # Reaction 156
  rate-constant: {A: 4.021e+04, b: 2.5, Ea: 8847.5}
- equation: HO2 + IC4H7 <=> IC4H7O + OH  # Reaction 157
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1013.25, A: 1.02e+13, b: -0.158, Ea: -1417.0}
  - {P: 1.01325e+04, A: 4.98e+14, b: -0.642, Ea: -349.1}
  - {P: 1.01325e+05, A: 7.77e+17, b: -1.52, Ea: 2379.2}
  - {P: 1.01325e+06, A: 2.93e+15, b: -0.684, Ea: 3615.3}
  - {P: 1.01325e+07, A: 1.64e+04, b: 2.74, Ea: 1144.4}
- equation: IC4H7O <=> C3H5-T + CH2O  # Reaction 158
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 101.325, A: 7.26e+06, b: 0.182, Ea: 1.78155e+04}
  - {P: 1013.25, A: 6.97e+16, b: -2.5, Ea: 2.08787e+04}
  - {P: 1.01325e+04, A: 6.64e+23, b: -4.23, Ea: 2.3565e+04}
  - {P: 1.01325e+05, A: 1.07e+26, b: -4.56, Ea: 2.46229e+04}
  - {P: 1.01325e+06, A: 6.5e+29, b: -5.37, Ea: 2.6645e+04}
  - {P: 1.01325e+07, A: 4.63e+31, b: -5.59, Ea: 2.89153e+04}
  - {P: 1.01325e+08, A: 8.52e+25, b: -3.61, Ea: 2.78634e+04}
- equation: IC4H7O <=> C3H6 + HCO  # Reaction 159
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 101.325, A: 6.62e+16, b: -2.84, Ea: 1.3197e+04}
  - {P: 1013.25, A: 1.26e+20, b: -3.53, Ea: 1.54692e+04}
  - {P: 1.01325e+04, A: 2.13e+21, b: -3.64, Ea: 1.65845e+04}
  - {P: 1.01325e+05, A: 1.07e+24, b: -4.16, Ea: 1.8985e+04}
  - {P: 1.01325e+06, A: 8.42e+25, b: -4.4, Ea: 2.23826e+04}
  - {P: 1.01325e+07, A: 1.86e+21, b: -2.73, Ea: 2.36588e+04}
  - {P: 1.01325e+08, A: 4.75e+08, b: 1.14, Ea: 2.09225e+04}
- equation: H + IC4H8 <=> IC4H9  # Reaction 160
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 7.99e+81, b: -23.161, Ea: 2.2239e+04}
  - {P: 4053.0, A: 4.24e+68, b: -18.427, Ea: 1.9665e+04}
  - {P: 1.01325e+05, A: 1.04e+49, b: -11.5, Ea: 1.5359e+04}
  - {P: 1.01325e+06, A: 6.2e+41, b: -8.892, Ea: 1.4637e+04}
- equation: H + IC4H8 <=> IC4H9  # Reaction 161
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 1.85e+26, b: -5.83, Ea: 3865.8}
  - {P: 4053.0, A: 2.82e+30, b: -6.49, Ea: 5470.8}
  - {P: 1.01325e+05, A: 3.78e+28, b: -5.57, Ea: 5625.1}
  - {P: 1.01325e+06, A: 1.46e+25, b: -4.28, Ea: 5247.8}
  - {P: 1.01325e+07, A: 4.22e+27, b: -4.39, Ea: 9345.8}
- equation: H + IC4H8 <=> TC4H9  # Reaction 162
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 1.35e+44, b: -10.68, Ea: 8196.4}
  - {P: 4053.0, A: 2.11e+57, b: -14.23, Ea: 1.5147e+04}
  - {P: 1.01325e+05, A: 3.26e+61, b: -14.94, Ea: 2.0161e+04}
  - {P: 1.01325e+06, A: 5.3e+56, b: -13.12, Ea: 2.0667e+04}
  - {P: 1.01325e+07, A: 1.11e+50, b: -10.8, Ea: 2.0202e+04}
- equation: H + IC4H8 <=> TC4H9  # Reaction 163
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 2.17e+130, b: -32.58, Ea: 1.3614e+05}
  - {P: 4053.0, A: 2.25e+29, b: -5.84, Ea: 4241.9}
  - {P: 1.01325e+05, A: 1.06e+30, b: -5.63, Ea: 5613.4}
  - {P: 1.01325e+06, A: 6.11e+26, b: -4.44, Ea: 5182.3}
  - {P: 1.01325e+07, A: 2.73e+23, b: -3.26, Ea: 4597.0}
- equation: H + IC4H8 <=> C3H6 + CH3  # Reaction 164
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 5.13e+08, b: 1.35, Ea: 2542.0}
  - {P: 4053.0, A: 2.63e+10, b: 0.87, Ea: 3599.6}
  - {P: 1.01325e+05, A: 8.9e+11, b: 0.47, Ea: 5431.1}
  - {P: 1.01325e+06, A: 3.08e+22, b: -2.6, Ea: 1.2898e+04}
  - {P: 1.01325e+07, A: 4.4e+22, b: -2.42, Ea: 1.65e+04}
- equation: H + IC4H8 <=> C3H6 + CH3  # Reaction 165
  type: pressure-dependent-Arrhenius
  duplicate: true
  rate-constants:
  - {P: 131.7225, A: 770.0, b: 1.35, Ea: 2542.0}
  - {P: 4053.0, A: 3.94e+04, b: 0.87, Ea: 3599.6}
  - {P: 1.01325e+05, A: 1.34e+06, b: 0.47, Ea: 5431.1}
  - {P: 1.01325e+06, A: 4.13e+04, b: 2.52, Ea: 3679.1}
  - {P: 1.01325e+07, A: 837.0, b: 2.91, Ea: 3980.9}
- equation: C3H4-A + O2 => CH2CO + CH2O  # Reaction 166
  rate-constant: {A: 1.0e+15, b: 0.0, Ea: 4.1e+04}
- equation: CH2CO + O2 => CO + HCO + OH  # Reaction 167
  rate-constant: {A: 3.0e+14, b: 0.0, Ea: 4.0e+04}
- equation: CH2CHO + O2 => CH2CO + HO2  # Reaction 168
  rate-constant: {A: 5.0e+11, b: 0.0, Ea: 3000.0}
- equation: O + OH + M <=> HO2 + M  # Reaction 169
  type: three-body
  rate-constant: {A: 1.0e+16, b: 0.0, Ea: 0.0}
- equation: CH3COCH2 <=> CH2CO + CH3  # Reaction 170
  rate-constant: {A: 1.0e+14, b: 0.0, Ea: 3.1e+04}
- equation: CH2 + O <=> CO + H2  # Reaction 171
  rate-constant: {A: 5.0e+13, b: 0.0, Ea: 0.0}
- equation: CH2 + OH <=> CH2O + H  # Reaction 172
  rate-constant: {A: 3.0e+13, b: 0.0, Ea: 0.0}
- equation: CH2(S) + CH4 <=> 2 CH3  # Reaction 173
  rate-constant: {A: 4.3e+13, b: 0.0, Ea: 0.0}
- equation: C3H3 + H <=> C3H4-P  # Reaction 174
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 4053.0, A: 3.63e+36, b: -7.36, Ea: 6039.0}
  - {P: 1.01325e+05, A: 7.94e+29, b: -5.06, Ea: 4861.0}
  - {P: 1.01325e+06, A: 1.07e+24, b: -3.15, Ea: 3261.0}
  - {P: 1.01325e+07, A: 6.4e+13, b: 0.102, Ea: -31.2}
- equation: C3H6 + O => C2H3CHO + 2 H  # Reaction 175
  rate-constant: {A: 1.0e+13, b: 0.0, Ea: 3000.0}
- equation: CH2O + O => CO2 + 2 H  # Reaction 176
  rate-constant: {A: 2.0e+13, b: 0.0, Ea: 5000.0}
- equation: C2H4 + O2 => CH3O + HCO  # Reaction 177
  rate-constant: {A: 1.0e+14, b: 0.0, Ea: 4.3e+04}
- equation: IC4H7 + O2 => C3H4-A + CH3 + O2  # Reaction 178
  rate-constant: {A: 8.0e+12, b: 0.0, Ea: 2.2e+04}
- equation: IC4H7 + O => C3H5-T + CH2O  # Reaction 179
  rate-constant: {A: 5.0e+13, b: 0.0, Ea: 0.0}
- equation: HO2 + IC4H7 => C3H5-T + CH2O + OH  # Reaction 180
  rate-constant: {A: 3.0e+11, b: 0.0, Ea: 0.0}
- equation: CH2CHO <=> CH3CO  # Reaction 181
  rate-constant: {A: 2.0e+11, b: 0.0, Ea: 3.2e+04}
- equation: C2H3CHO + OH => C2H3 + CO + H2O  # Reaction 182
  rate-constant: {A: 9.9996e+06, b: 2.0, Ea: -3343.83}
- equation: C3H5-A + H (+M) <=> C3H6 (+M)  # Reaction 183
  type: falloff
  low-P-rate-constant: {A: 1.33e+60, b: -12.0, Ea: 5967.8}
  high-P-rate-constant: {A: 1.0e+14, b: 0.0, Ea: 0.0}
  Troe: {A: 0.02, T3: 1097.0, T1: 1.097e+04, T2: 6860.0}
  efficiencies: {CO: 1.5, CO2: 2.0, H2O: 6.0}
- equation: C3H5-A + IC4H7 <=> C3H4-A + IC4H8  # Reaction 184
  rate-constant: {A: 2.0e+11, b: 0.0, Ea: 0.0}
- equation: C3H4-P <=> C3H4-A  # Reaction 185
  type: pressure-dependent-Arrhenius
  rate-constants:
  - {P: 1.01325e+04, A: 6.4e+61, b: -14.59, Ea: 8.82e+04}
  - {P: 1.01325e+05, A: 5.2e+60, b: -13.93, Ea: 9.11e+04}
  - {P: 1.01325e+06, A: 1.9e+57, b: -12.62, Ea: 9.33e+04}
  - {P: 1.01325e+07, A: 1.4e+52, b: -10.86, Ea: 9.54e+04}
- equation: O2 + TC4H9 <=> HO2 + IC4H8  # Reaction 186
  rate-constant: {A: 1.8e+12, b: 0.0, Ea: 3000.0}
- equation: C2H2 + O => C2H + OH  # Reaction 187
  rate-constant: {A: 4.7e+06, b: 2.0, Ea: 8057.53}
- equation: C2H4 + O => C2H3 + OH  # Reaction 188
  rate-constant: {A: 1.88e+07, b: 2.0, Ea: 8057.53}
- equation: C3H4-A + O => C3H3 + OH  # Reaction 189
  rate-constant: {A: 1.41e+08, b: 2.0, Ea: 8057.53}
- equation: CH2CO + H => H2 + HCCO  # Reaction 190
  rate-constant: {A: 2.4e+07, b: 2.0, Ea: 9455.88}
- equation: CH2CO + O => HCCO + OH  # Reaction 191
  rate-constant: {A: 1.88e+07, b: 2.0, Ea: 8057.53}
- equation: CH2CO + OH => H2O + HCCO  # Reaction 192
  rate-constant: {A: 1.2e+10, b: 1.0, Ea: 2307.85}
- equation: H + IC4H8 => H2 + IC4H7  # Reaction 193
  rate-constant: {A: 1.8e+07, b: 2.0, Ea: 4389.88}
- equation: IC4H9 + O2 => C4H9O2(L1)  # Reaction 194
  rate-constant: {A: 1.5e+12, b: 0.0, Ea: 0.0}
- equation: O2 + TC4H9 => C4H9O2(L1)  # Reaction 195
  rate-constant: {A: 1.5e+12, b: 0.0, Ea: 0.0}
- equation: C4H9O2(L1) => IC4H9 + O2  # Reaction 196
  rate-constant: {A: 4.34071e+04, b: 2.509943, Ea: 2.672837e+04}
- equation: C4H9O2(L1) => O2 + TC4H9  # Reaction 197
  rate-constant: {A: 8.726576e+17, b: -1.402041, Ea: 3.181709e+04}
- equation: C4H9O2(L1) => HO2 + IC4H8  # Reaction 198
  rate-constant: {A: 5.655438e+13, b: -0.7629124, Ea: 2.552263e+04}
  duplicate: true
- equation: C4H9O2(L1) => C3H6 + CH2O + OH  # Reaction 199
  rate-constant: {A: 1.413859e+14, b: -0.7629124, Ea: 2.652263e+04}
- equation: C4H9O2(L1) => HO2 + IC4H8  # Reaction 200
  rate-constant: {A: 8.070114e+22, b: -3.078473, Ea: 3.31751e+04}
  duplicate: true
- equation: NEOC5H11 <=> CH3 + IC4H8  # Reaction 201
  rate-constant: {A: 4.0e+13, b: 0.0, Ea: 3.08e+04}
- equation: IC8H18 => 0.2 C3H7(L1) + 0.8 IC4H9 + 0.2 NEOC5H11 + 0.8 TC4H9  # Reaction 202
  rate-constant: {A: 2.0e+17, b: 0.0, Ea: 7.8e+04}
- equation: IC8H16 <=> IC4H7 + TC4H9  # Reaction 203
  rate-constant: {A: 1.0e+16, b: 0.0, Ea: 7.1e+04}
- equation: H + IC8H16 => IC8H17  # Reaction 204
  rate-constant: {A: 2.5e+13, b: 0.0, Ea: 2000.0}
- equation: IC8H17 => C3H6 + NEOC5H11  # Reaction 205
  rate-constant: {A: 7.8e+12, b: 0.0, Ea: 3.0e+04}
- equation: IC8H17 => IC4H8 + TC4H9  # Reaction 206
  rate-constant: {A: 2.16e+13, b: 0.0, Ea: 3.0e+04}
- equation: IC8H17 => IC4H8 + IC4H9  # Reaction 207
  rate-constant: {A: 1.5e+13, b: 0.0, Ea: 3.0e+04}
- equation: IC8H17 => CH3 + 0.25 IC4H8 + 0.75 IC8H16  # Reaction 208
  rate-constant: {A: 1.56e+13, b: 0.0, Ea: 3.0e+04}
- equation: IC8H17 => H + IC8H16  # Reaction 209
  rate-constant: {A: 2.0e+14, b: 0.0, Ea: 3.8e+04}
- equation: IC8H17 + O2 => HO2 + IC8H16  # Reaction 210
  rate-constant: {A: 1.34e+11, b: 0.0, Ea: 2500.0}
- equation: IC8H18 + OH => H2O + IC8H17  # Reaction 211
  rate-constant: {A: 1.0e+05, b: 2.56, Ea: -1125.0}
- equation: H + IC8H18 => H2 + IC8H17  # Reaction 212
  rate-constant: {A: 2.7e+07, b: 2.0, Ea: 4000.0}
- equation: H + IC8H16 => 0.5 C3H4-A + H2 + 0.5 IC4H7 + 0.5 IC4H8 + 0.5
    NEOC5H11  # Reaction 213
  rate-constant: {A: 1.8e+07, b: 2.0, Ea: 4000.0}
- equation: IC8H16 + OH => 0.5 C3H4-A + H2O + 0.5 IC4H7 + 0.5 IC4H8 + 0.5
    NEOC5H11  # Reaction 214
  rate-constant: {A: 9.0e+09, b: 1.0, Ea: 50.0}
- equation: IC4H7 + O2 => CH2O + CH3COCH2  # Reaction 215
  rate-constant: {A: 5.0e+11, b: 0.0, Ea: 1.75e+04}
- equation: IC12H26 => IC8H17 + TC4H9  # Reaction 216
  rate-constant: {A: 4.0e+17, b: 0.0, Ea: 7.75e+04}
- equation: IC12H25 => IC4H8 + IC8H17  # Reaction 217
  rate-constant: {A: 2.0e+13, b: 0.0, Ea: 3.0e+04}
- equation: IC16H34 => 0.67 C3H6 + IC4H8 + 0.33 IC8H17 + 0.67 NEOC5H11 +
    TC4H9  # Reaction 218
  rate-constant: {A: 2.5e+17, b: 0.0, Ea: 7.7e+04}
- equation: IC16H33 => 0.56 C3H6 + 0.67 CH3 + IC4H8 + IC8H16 + 0.33 NEOC5H11  # Reaction 219
  rate-constant: {A: 2.0e+13, b: 0.0, Ea: 2.9e+04}
- equation: IC16H33 => IC8H16 + IC8H17  # Reaction 220
  rate-constant: {A: 5.0e+13, b: 0.0, Ea: 2.9e+04}
- equation: IC16H33 + O2 => HO2 + 2 IC8H16  # Reaction 221
  rate-constant: {A: 2.5e+11, b: 0.0, Ea: 3500.0}
- equation: H + IC12H26 => H2 + IC12H25  # Reaction 222
  rate-constant: {A: 3.9e+07, b: 2.0, Ea: 4000.0}
- equation: IC12H26 + OH => H2O + IC12H25  # Reaction 223
  rate-constant: {A: 1.95e+10, b: 1.0, Ea: 50.0}
- equation: H + IC16H34 => H2 + IC16H33  # Reaction 224
  rate-constant: {A: 4.8e+07, b: 2.0, Ea: 4000.0}
- equation: IC16H34 + OH => H2O + IC16H33  # Reaction 225
  rate-constant: {A: 2.4e+10, b: 1.0, Ea: 50.0}
