[Data] Remove optional 'three-body' in type field

Cantera · Jul 10, 2022 · 7b6258d · 7b6258d
1 parent 29e2a0b
commit 7b6258d
Show file tree

Hide file tree

Showing 14 changed files with 0 additions and 63 deletions.
diff --git a/data/air.yaml b/data/air.yaml
@@ -158,7 +158,6 @@ species:
 
 reactions:
 - equation: 2 O + M <=> O2 + M  # Reaction 1
-  type: three-body
   rate-constant: {A: 1.2e+17, b: -1.0, Ea: 0.0}
   efficiencies: {AR: 0.83}
 - equation: N + NO <=> N2 + O  # Reaction 2
@@ -175,7 +174,6 @@ reactions:
   high-P-rate-constant: {A: 7.91e+10, b: 0.0, Ea: 5.602e+04}
   efficiencies: {AR: 0.625}
 - equation: NO + O + M <=> NO2 + M  # Reaction 7
-  type: three-body
   rate-constant: {A: 1.06e+20, b: -1.41, Ea: 0.0}
   efficiencies: {AR: 0.7}
 - equation: NO2 + O <=> NO + O2  # Reaction 8

diff --git a/data/gri30.yaml b/data/gri30.yaml
@@ -952,12 +952,10 @@ species:
 
 reactions:
 - equation: 2 O + M <=> O2 + M  # Reaction 1
-  type: three-body
   rate-constant: {A: 1.2e+17, b: -1.0, Ea: 0.0}
   efficiencies: {H2: 2.4, H2O: 15.4, CH4: 2.0, CO: 1.75, CO2: 3.6, C2H6: 3.0,
     AR: 0.83}
 - equation: O + H + M <=> OH + M  # Reaction 2
-  type: three-body
   rate-constant: {A: 5.0e+17, b: -1.0, Ea: 0.0}
   efficiencies: {H2: 2.0, H2O: 6.0, CH4: 2.0, CO: 1.5, CO2: 2.0, C2H6: 3.0,
     AR: 0.7}
@@ -1026,7 +1024,6 @@ reactions:
 - equation: O2 + CH2O <=> HO2 + HCO  # Reaction 32
   rate-constant: {A: 1.0e+14, b: 0.0, Ea: 4.0e+04}
 - equation: H + O2 + M <=> HO2 + M  # Reaction 33
-  type: three-body
   rate-constant: {A: 2.8e+18, b: -0.86, Ea: 0.0}
   efficiencies: {O2: 0.0, H2O: 0.0, CO: 0.75, CO2: 1.5, C2H6: 1.5, N2: 0.0,
     AR: 0.0}
@@ -1041,7 +1038,6 @@ reactions:
 - equation: H + O2 <=> O + OH  # Reaction 38
   rate-constant: {A: 2.65e+16, b: -0.6707, Ea: 1.7041e+04}
 - equation: 2 H + M <=> H2 + M  # Reaction 39
-  type: three-body
   rate-constant: {A: 1.0e+18, b: -1.0, Ea: 0.0}
   efficiencies: {H2: 0.0, H2O: 0.0, CH4: 2.0, CO2: 0.0, C2H6: 3.0, AR: 0.63}
 - equation: 2 H + H2 <=> 2 H2  # Reaction 40
@@ -1051,7 +1047,6 @@ reactions:
 - equation: 2 H + CO2 <=> H2 + CO2  # Reaction 42
   rate-constant: {A: 5.5e+20, b: -2.0, Ea: 0.0}
 - equation: H + OH + M <=> H2O + M  # Reaction 43
-  type: three-body
   rate-constant: {A: 2.2e+22, b: -2.0, Ea: 0.0}
   efficiencies: {H2: 0.73, H2O: 3.65, CH4: 2.0, C2H6: 3.0, AR: 0.38}
 - equation: H + HO2 <=> O + H2O  # Reaction 44
@@ -1395,7 +1390,6 @@ reactions:
 - equation: HCO + H2O <=> H + CO + H2O  # Reaction 166
   rate-constant: {A: 1.5e+18, b: -1.0, Ea: 1.7e+04}
 - equation: HCO + M <=> H + CO + M  # Reaction 167
-  type: three-body
   rate-constant: {A: 1.87e+17, b: -1.0, Ea: 1.7e+04}
   efficiencies: {H2: 2.0, H2O: 0.0, CH4: 2.0, CO: 1.5, CO2: 2.0, C2H6: 3.0}
 - equation: HCO + O2 <=> HO2 + CO  # Reaction 168
@@ -1446,7 +1440,6 @@ reactions:
 - equation: HO2 + NO <=> NO2 + OH  # Reaction 186
   rate-constant: {A: 2.11e+12, b: 0.0, Ea: -480.0}
 - equation: NO + O + M <=> NO2 + M  # Reaction 187
-  type: three-body
   rate-constant: {A: 1.06e+20, b: -1.41, Ea: 0.0}
   efficiencies: {H2: 2.0, H2O: 6.0, CH4: 2.0, CO: 1.5, CO2: 2.0, C2H6: 3.0,
     AR: 0.7}
@@ -1485,7 +1478,6 @@ reactions:
 - equation: NNH <=> N2 + H  # Reaction 204
   rate-constant: {A: 3.3e+08, b: 0.0, Ea: 0.0}
 - equation: NNH + M <=> N2 + H + M  # Reaction 205
-  type: three-body
   rate-constant: {A: 1.3e+14, b: -0.11, Ea: 4980.0}
   efficiencies: {H2: 2.0, H2O: 6.0, CH4: 2.0, CO: 1.5, CO2: 2.0, C2H6: 3.0,
     AR: 0.7}
@@ -1502,7 +1494,6 @@ reactions:
 - equation: NNH + CH3 <=> CH4 + N2  # Reaction 211
   rate-constant: {A: 2.5e+13, b: 0.0, Ea: 0.0}
 - equation: H + NO + M <=> HNO + M  # Reaction 212
-  type: three-body
   rate-constant: {A: 4.48e+19, b: -1.32, Ea: 740.0}
   efficiencies: {H2: 2.0, H2O: 6.0, CH4: 2.0, CO: 1.5, CO2: 2.0, C2H6: 3.0,
     AR: 0.7}
@@ -1535,7 +1526,6 @@ reactions:
 - equation: NCO + O2 <=> NO + CO2  # Reaction 226
   rate-constant: {A: 2.0e+12, b: 0.0, Ea: 2.0e+04}
 - equation: NCO + M <=> N + CO + M  # Reaction 227
-  type: three-body
   rate-constant: {A: 3.1e+14, b: 0.0, Ea: 5.405e+04}
   efficiencies: {H2: 2.0, H2O: 6.0, CH4: 2.0, CO: 1.5, CO2: 2.0, C2H6: 3.0,
     AR: 0.7}
@@ -1544,7 +1534,6 @@ reactions:
 - equation: NCO + NO <=> N2 + CO2  # Reaction 229
   rate-constant: {A: 3.8e+18, b: -2.0, Ea: 800.0}
 - equation: HCN + M <=> H + CN + M  # Reaction 230
-  type: three-body
   rate-constant: {A: 1.04e+29, b: -3.3, Ea: 1.266e+05}
   efficiencies: {H2: 2.0, H2O: 6.0, CH4: 2.0, CO: 1.5, CO2: 2.0, C2H6: 3.0,
     AR: 0.7}
@@ -1634,7 +1623,6 @@ reactions:
 - equation: HNCO + OH <=> NH2 + CO2  # Reaction 268
   rate-constant: {A: 3.3e+06, b: 1.5, Ea: 3600.0}
 - equation: HNCO + M <=> NH + CO + M  # Reaction 269
-  type: three-body
   rate-constant: {A: 1.18e+16, b: 0.0, Ea: 8.472e+04}
   efficiencies: {H2: 2.0, H2O: 6.0, CH4: 2.0, CO: 1.5, CO2: 2.0, C2H6: 3.0,
     AR: 0.7}

diff --git a/data/gri30_highT.yaml b/data/gri30_highT.yaml
@@ -936,12 +936,10 @@ species:
 
 reactions:
 - equation: 2 O + M <=> O2 + M  # Reaction 1
-  type: three-body
   rate-constant: {A: 1.2e+17, b: -1, Ea: 0}
   efficiencies: {AR: 0.83, C2H6: 3, CH4: 2, CO: 1.75, CO2: 3.6, H2: 2.4,
     H2O: 15.4}
 - equation: O + H + M <=> OH + M  # Reaction 2
-  type: three-body
   rate-constant: {A: 5.0e+17, b: -1, Ea: 0}
   efficiencies: {AR: 0.7, C2H6: 3, CH4: 2, CO: 1.5, CO2: 2, H2: 2, H2O: 6}
 - equation: O + H2 <=> H + OH  # Reaction 3
@@ -1009,7 +1007,6 @@ reactions:
 - equation: O2 + CH2O <=> HO2 + HCO  # Reaction 32
   rate-constant: {A: 1.0e+14, b: 0, Ea: 40000}
 - equation: H + O2 + M <=> HO2 + M  # Reaction 33
-  type: three-body
   rate-constant: {A: 2.8e+18, b: -0.86, Ea: 0}
   efficiencies: {AR: 0, C2H6: 1.5, CO: 0.75, CO2: 1.5, H2O: 0, N2: 0, O2: 0}
 - equation: H + 2 O2 <=> HO2 + O2  # Reaction 34
@@ -1023,7 +1020,6 @@ reactions:
 - equation: H + O2 <=> O + OH  # Reaction 38
   rate-constant: {A: 2.65e+16, b: -0.6707, Ea: 17041}
 - equation: 2 H + M <=> H2 + M  # Reaction 39
-  type: three-body
   rate-constant: {A: 1.0e+18, b: -1, Ea: 0}
   efficiencies: {AR: 0.63, C2H6: 3, CH4: 2, CO2: 0, H2: 0, H2O: 0}
 - equation: 2 H + H2 <=> 2 H2  # Reaction 40
@@ -1033,7 +1029,6 @@ reactions:
 - equation: 2 H + CO2 <=> H2 + CO2  # Reaction 42
   rate-constant: {A: 5.5e+20, b: -2, Ea: 0}
 - equation: H + OH + M <=> H2O + M  # Reaction 43
-  type: three-body
   rate-constant: {A: 2.2e+22, b: -2, Ea: 0}
   efficiencies: {AR: 0.38, C2H6: 3, CH4: 2, H2: 0.73, H2O: 3.65}
 - equation: H + HO2 <=> O + H2O  # Reaction 44
@@ -1364,7 +1359,6 @@ reactions:
 - equation: HCO + H2O <=> H + CO + H2O  # Reaction 166
   rate-constant: {A: 1.5e+18, b: -1, Ea: 17000}
 - equation: HCO + M <=> H + CO + M  # Reaction 167
-  type: three-body
   rate-constant: {A: 1.87e+17, b: -1, Ea: 17000}
   efficiencies: {C2H6: 3, CH4: 2, CO: 1.5, CO2: 2, H2: 2, H2O: 0}
 - equation: HCO + O2 <=> HO2 + CO  # Reaction 168
@@ -1413,7 +1407,6 @@ reactions:
 - equation: HO2 + NO <=> NO2 + OH  # Reaction 186
   rate-constant: {A: 2.11e+12, b: 0, Ea: -480}
 - equation: NO + O + M <=> NO2 + M  # Reaction 187
-  type: three-body
   rate-constant: {A: 1.06e+20, b: -1.41, Ea: 0}
   efficiencies: {AR: 0.7, C2H6: 3, CH4: 2, CO: 1.5, CO2: 2, H2: 2, H2O: 6}
 - equation: NO2 + O <=> NO + O2  # Reaction 188
@@ -1451,7 +1444,6 @@ reactions:
 - equation: NNH <=> N2 + H  # Reaction 204
   rate-constant: {A: 3.3e+08, b: 0, Ea: 0}
 - equation: NNH + M <=> N2 + H + M  # Reaction 205
-  type: three-body
   rate-constant: {A: 1.3e+14, b: -0.11, Ea: 4980}
   efficiencies: {AR: 0.7, C2H6: 3, CH4: 2, CO: 1.5, CO2: 2, H2: 2, H2O: 6}
 - equation: NNH + O2 <=> HO2 + N2  # Reaction 206
@@ -1467,7 +1459,6 @@ reactions:
 - equation: NNH + CH3 <=> CH4 + N2  # Reaction 211
   rate-constant: {A: 2.5e+13, b: 0, Ea: 0}
 - equation: H + NO + M <=> HNO + M  # Reaction 212
-  type: three-body
   rate-constant: {A: 4.48e+19, b: -1.32, Ea: 740}
   efficiencies: {AR: 0.7, C2H6: 3, CH4: 2, CO: 1.5, CO2: 2, H2: 2, H2O: 6}
 - equation: HNO + O <=> NO + OH  # Reaction 213
@@ -1499,15 +1490,13 @@ reactions:
 - equation: NCO + O2 <=> NO + CO2  # Reaction 226
   rate-constant: {A: 2.0e+12, b: 0, Ea: 20000}
 - equation: NCO + M <=> N + CO + M  # Reaction 227
-  type: three-body
   rate-constant: {A: 3.1e+14, b: 0, Ea: 54050}
   efficiencies: {AR: 0.7, C2H6: 3, CH4: 2, CO: 1.5, CO2: 2, H2: 2, H2O: 6}
 - equation: NCO + NO <=> N2O + CO  # Reaction 228
   rate-constant: {A: 1.9e+17, b: -1.52, Ea: 740}
 - equation: NCO + NO <=> N2 + CO2  # Reaction 229
   rate-constant: {A: 3.8e+18, b: -2, Ea: 800}
 - equation: HCN + M <=> H + CN + M  # Reaction 230
-  type: three-body
   rate-constant: {A: 1.04e+29, b: -3.3, Ea: 126600}
   efficiencies: {AR: 0.7, C2H6: 3, CH4: 2, CO: 1.5, CO2: 2, H2: 2, H2O: 6}
 - equation: HCN + O <=> NCO + H  # Reaction 231
@@ -1594,7 +1583,6 @@ reactions:
 - equation: HNCO + OH <=> NH2 + CO2  # Reaction 268
   rate-constant: {A: 3.3e+06, b: 1.5, Ea: 3600}
 - equation: HNCO + M <=> NH + CO + M  # Reaction 269
-  type: three-body
   rate-constant: {A: 1.18e+16, b: 0, Ea: 84720}
   efficiencies: {AR: 0.7, C2H6: 3, CH4: 2, CO: 1.5, CO2: 2, H2: 2, H2O: 6}
 - equation: HCNO + H <=> H + HNCO  # Reaction 270

diff --git a/data/h2o2.yaml b/data/h2o2.yaml
@@ -191,11 +191,9 @@ species:
 
 reactions:
 - equation: 2 O + M <=> O2 + M  # Reaction 1
-  type: three-body
   rate-constant: {A: 1.2e+17, b: -1.0, Ea: 0.0}
   efficiencies: {H2: 2.4, H2O: 15.4, AR: 0.83}
 - equation: O + H + M <=> OH + M  # Reaction 2
-  type: three-body
   rate-constant: {A: 5.0e+17, b: -1.0, Ea: 0.0}
   efficiencies: {H2: 2.0, H2O: 6.0, AR: 0.7}
 - equation: O + H2 <=> H + OH  # Reaction 3
@@ -205,7 +203,6 @@ reactions:
 - equation: O + H2O2 <=> OH + HO2  # Reaction 5
   rate-constant: {A: 9.63e+06, b: 2.0, Ea: 4000.0}
 - equation: H + O2 + M <=> HO2 + M  # Reaction 6
-  type: three-body
   rate-constant: {A: 2.8e+18, b: -0.86, Ea: 0.0}
   efficiencies: {O2: 0.0, H2O: 0.0, N2: 0.0, AR: 0.0}
 - equation: H + 2 O2 <=> HO2 + O2  # Reaction 7
@@ -219,15 +216,13 @@ reactions:
 - equation: H + O2 <=> O + OH  # Reaction 11
   rate-constant: {A: 2.65e+16, b: -0.6707, Ea: 1.7041e+04}
 - equation: 2 H + M <=> H2 + M  # Reaction 12
-  type: three-body
   rate-constant: {A: 1.0e+18, b: -1.0, Ea: 0.0}
   efficiencies: {H2: 0.0, H2O: 0.0, AR: 0.63}
 - equation: 2 H + H2 <=> 2 H2  # Reaction 13
   rate-constant: {A: 9.0e+16, b: -0.6, Ea: 0.0}
 - equation: 2 H + H2O <=> H2 + H2O  # Reaction 14
   rate-constant: {A: 6.0e+19, b: -1.25, Ea: 0.0}
 - equation: H + OH + M <=> H2O + M  # Reaction 15
-  type: three-body
   rate-constant: {A: 2.2e+22, b: -2.0, Ea: 0.0}
   efficiencies: {H2: 0.73, H2O: 3.65, AR: 0.38}
 - equation: H + HO2 <=> O + H2O  # Reaction 16

diff --git a/data/nDodecane_Reitz.yaml b/data/nDodecane_Reitz.yaml
@@ -2291,20 +2291,16 @@ reactions:
 - equation: ch3 + o2 <=> ch3o + o  # Reaction 357
   rate-constant: {A: 1.995e+18, b: -1.57, Ea: 2.921009e+04}
 - equation: ch2 + h + M => ch3 + M  # Reaction 358
-  type: three-body
   rate-constant: {A: 2.107e+11, b: 1.0, Ea: -1.961998e+04}
 - equation: ch3 + M => ch2 + h + M  # Reaction 359
-  type: three-body
   rate-constant: {A: 1.968e+16, b: 0.0, Ea: 9.252008e+04}
 - equation: ch3 + oh <=> ch2 + h2o  # Reaction 360
   rate-constant: {A: 3.0e+06, b: 2.0, Ea: 2500.0}
 - equation: ch3 + o2 <=> ch2o + oh  # Reaction 361
   rate-constant: {A: 7.47e+11, b: 0.0, Ea: 1.425e+04}
 - equation: ch3o2 + M => ch3 + o2 + M  # Reaction 362
-  type: three-body
   rate-constant: {A: 4.343e+28, b: -3.42, Ea: 3.046989e+04}
 - equation: ch3 + o2 + M => ch3o2 + M  # Reaction 363
-  type: three-body
   rate-constant: {A: 5.44e+25, b: -3.3, Ea: 0.0}
 - equation: ch3o2 + ch3 <=> 2 ch3o  # Reaction 364
   rate-constant: {A: 7.0e+12, b: 0.0, Ea: -1000.0}
@@ -2321,10 +2317,8 @@ reactions:
 - equation: ch3o + o2 <=> ch2o + ho2  # Reaction 369
   rate-constant: {A: 5.5e+10, b: 0.0, Ea: 2424.0}
 - equation: ch2o + M => hco + h + M  # Reaction 370
-  type: three-body
   rate-constant: {A: 6.283e+29, b: -3.57, Ea: 9.320005e+04}
 - equation: hco + h + M => ch2o + M  # Reaction 371
-  type: three-body
   rate-constant: {A: 2.66e+24, b: -2.57, Ea: 427.1}
 - equation: ch2o + oh <=> hco + h2o  # Reaction 372
   rate-constant: {A: 3.43e+09, b: 1.18, Ea: -446.94}
@@ -2349,11 +2343,9 @@ reactions:
 - equation: hco + oh <=> co + h2o  # Reaction 382
   rate-constant: {A: 1.02e+14, b: 0.0, Ea: 0.0}
 - equation: hco + M => h + co + M  # Reaction 383
-  type: three-body
   rate-constant: {A: 1.86e+17, b: -1.0, Ea: 1.7e+04}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: h + co + M => hco + M  # Reaction 384
-  type: three-body
   rate-constant: {A: 6.467e+13, b: 0.0, Ea: -441.92}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: hco + h <=> co + h2  # Reaction 385
@@ -2392,11 +2384,9 @@ reactions:
 - equation: h + h2o => oh + h2  # Reaction 400
   rate-constant: {A: 9.352e+08, b: 1.51, Ea: 1.858007e+04}
 - equation: h + oh + M => h2o + M  # Reaction 401
-  type: three-body
   rate-constant: {A: 2.25e+22, b: -2.0, Ea: 0.0}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: h2o + M => h + oh + M  # Reaction 402
-  type: three-body
   rate-constant: {A: 1.837e+27, b: -3.0, Ea: 1.225999e+05}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: h + o2 (+ M) <=> ho2 (+ M)  # Reaction 403
@@ -2414,27 +2404,21 @@ reactions:
 - equation: h2o2 + h <=> h2o + oh  # Reaction 407
   rate-constant: {A: 2.41e+13, b: 0.0, Ea: 3969.89}
 - equation: o + h + M => oh + M  # Reaction 408
-  type: three-body
   rate-constant: {A: 4.72e+18, b: -1.0, Ea: 0.0}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: oh + M => o + h + M  # Reaction 409
-  type: three-body
   rate-constant: {A: 3.909e+22, b: -2.0, Ea: 1.0529995e+05}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: 2 o + M => o2 + M  # Reaction 410
-  type: three-body
   rate-constant: {A: 6.17e+15, b: -0.5, Ea: 0.0}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: o2 + M => 2 o + M  # Reaction 411
-  type: three-body
   rate-constant: {A: 6.473e+20, b: -1.5, Ea: 1.215e+05}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: h2 + M => 2 h + M  # Reaction 412
-  type: three-body
   rate-constant: {A: 4.57e+19, b: -1.4, Ea: 1.044001e+05}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: 2 h + M => h2 + M  # Reaction 413
-  type: three-body
   rate-constant: {A: 2.423e+15, b: -0.4, Ea: -3039.91}
   efficiencies: {co: 1.9, co2: 3.8, h2o: 12.0, h2: 2.5}
 - equation: h2o2 + o <=> oh + ho2  # Reaction 414
@@ -2462,7 +2446,6 @@ reactions:
 - equation: c2h2 + oh <=> c2h + h2o  # Reaction 423
   rate-constant: {A: 6.0e+13, b: 0.0, Ea: 1.292e+04}
 - equation: c2h2 + M <=> c2h + h + M  # Reaction 424
-  type: three-body
   rate-constant: {A: 1.14e+17, b: 0.0, Ea: 1.068e+05}
   efficiencies: {o2: 0.4, co: 0.75, h2o: 6.5}
 - equation: c4h2 + o <=> c3h2 + co  # Reaction 425
@@ -2488,7 +2471,6 @@ reactions:
 - equation: c3h3 + oh <=> c3h2 + h2o  # Reaction 435
   rate-constant: {A: 2.0e+13, b: 0.0, Ea: 0.0}
 - equation: c4h3 + M <=> c4h2 + h + M  # Reaction 436
-  type: three-body
   rate-constant: {A: 1.12e+16, b: 0.0, Ea: 4.651e+04}
   efficiencies: {o2: 0.4, co: 0.75, h2o: 6.5}
 - equation: c2h2 + ch2 <=> c3h3 + h  # Reaction 437
@@ -2538,7 +2520,6 @@ reactions:
 - equation: c4h4 <=> 2 c2h2  # Reaction 459
   rate-constant: {A: 3.4e+13, b: 0.0, Ea: 7.664e+04}
 - equation: c4h4 + M <=> c4h3 + h + M  # Reaction 460
-  type: three-body
   rate-constant: {A: 1.1e+20, b: 0.0, Ea: 9.863e+04}
 - equation: c4h4 + o <=> hco + c3h3  # Reaction 461
   rate-constant: {A: 3.2e+08, b: 1.44, Ea: 549.4}

diff --git a/interfaces/cython/cantera/reaction.pyx b/interfaces/cython/cantera/reaction.pyx
@@ -1664,7 +1664,6 @@ cdef class ThreeBodyReaction(Reaction):
     The YAML description corresponding to this reaction is::
 
         equation: 2 O + M <=> O2 + M
-        type: three-body
         rate-constant: {A: 1.2e+17 cm^6/mol^2/s, b: -1.0, Ea: 0.0 cal/mol}
         efficiencies: {H2: 2.4, H2O: 15.4, AR: 0.83}
 

diff --git a/test/data/duplicate-reactions.yaml b/test/data/duplicate-reactions.yaml
@@ -123,7 +123,6 @@ H-reactions:
 - equation: O + H2 <=> H + OH  # Reaction 17
   rate-constant: {A: 1.0e+10, b: 0, Ea: 100}
 - equation: O + H2 + M <=> H + OH + M  # Reaction 18
-  type: three-body
   rate-constant: {A: 1.0e+10, b: 0, Ea: 100}
 
 I-reactions:

diff --git a/test/data/explicit-reverse-rate.yaml b/test/data/explicit-reverse-rate.yaml
@@ -90,10 +90,8 @@ reactions:
 - equation: P1 + H => R1A + R1B
   rate-constant: {A: 3.9e+09, b: 1.0, Ea: 6500.0 cal/mol}
 - equation: R1A + R1B + M => P1 + H + M
-  type: three-body
   rate-constant: {A: 1.0e-08, b: 0.0, Ea: 5000.0 cal/mol}
 - equation: P1 + H + M => R1A + R1B + M
-  type: three-body
   rate-constant: {A: 3.9e+06, b: 1.0, Ea: 6500.0 cal/mol}
 - equation: R3 + H => P3A + P3B
   rate-constant: {A: 1.0e+16, b: 0.0, Ea: 5000.0 cal/mol}
diff --git a/test/data/explicit-third-bodies.yaml b/test/data/explicit-third-bodies.yaml
@@ -76,7 +76,6 @@ species:
 
 reactions:
 - equation: R1A + R1B + M <=> P1 + H + M
-  type: three-body
   rate-constant: {A: 3.0e+13, b: -2.0, Ea: 1900.0 cal/mol}
   duplicate: true
 - equation: R1A + R1B (+ M) <=> P1 + H (+ M)

diff --git a/test/data/jacobian-tests.yaml b/test/data/jacobian-tests.yaml
@@ -30,7 +30,6 @@ reactions:
   orders: {H2: 0.8, O2: 1.0, OH: 2.0}
   note: Fractional reaction order
 - equation: O + H + M <=> OH + M  # Reaction 5
-  type: three-body
   rate-constant: {A: 5.0e+5, b: -1.0, Ea: 0.0}
   default-efficiency: 0.
   efficiencies: {H2: 2.0, H2O: 6.0, AR: 0.7}

diff --git a/test/data/kineticsfromscratch.yaml b/test/data/kineticsfromscratch.yaml
@@ -37,7 +37,6 @@ reactions:
 - equation: O + H2 <=> H + OH  # Reaction 1
   rate-constant: {A: 38.7, b: 2.7, Ea: 6260.0}
 - equation: 2 O + M <=> O2 + M  # Reaction 2
-  type: three-body
   rate-constant: {A: 1.2e+11, b: -1.0, Ea: 0.0}
   efficiencies: {AR: 0.83, H2: 2.4, H2O: 15.4}
 - equation: 2 OH (+ M) <=> H2O2 (+ M)  # Reaction 3