Mixture of Methane, nitro- + Propane, 1,3-dichloro-

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Methane, nitro-

Name
Methane, nitro-
InChI
InChI=1S/CH3NO2/c1-2(3)4/h1H3
InChI Key
LYGJENNIWJXYER-UHFFFAOYSA-N
Formula
CH3NO2
SMILES
C[N+](=O)[O-]
Mol. Weight (g/mol)
61.04
CAS
75-52-5

Propane, 1,3-dichloro-

Name
Propane, 1,3-dichloro-
InChI
InChI=1S/C3H6Cl2/c4-2-1-3-5/h1-3H2
InChI Key
YHRUOJUYPBUZOS-UHFFFAOYSA-N
Formula
C3H6Cl2
SMILES
ClCCCCl
Mol. Weight (g/mol)
112.99
CAS
142-28-9
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Datasets

  1. Mole fraction (2)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. n0 - Refractive index (Na D-line) (2)
  4. ρl - Mass density, kg/m3 (2)
  5. csound,fluid - Speed of Sound, m/s (2)

Mole fraction of Methane, nitro- (1) [ref]

Fixed Measured
Mole fraction of Methane, nitro- (1) - Liquid Temperature, K - Liquid Mole fraction of Methane, nitro- (1) - Gas
0.0000 343.15 0.0000
0.0000 353.15 0.0000
0.0000 363.15 0.0000
0.0690 343.15 0.2018
0.0690 353.15 0.1958
0.0690 363.15 0.1857
0.1214 353.15 0.3107
0.1235 343.15 0.3198
0.1256 363.15 0.2996
0.2038 363.15 0.4176
0.2078 353.15 0.4226
0.2098 343.15 0.4359
0.2810 363.15 0.4988
0.2848 343.15 0.5128
0.2848 353.15 0.5034
0.3556 363.15 0.5614
0.3574 353.15 0.5673
0.3609 343.15 0.5732
0.4392 353.15 0.6194
0.4409 343.15 0.6264
0.4441 363.15 0.6165
0.5143 363.15 0.6650
0.5159 343.15 0.6758
0.5159 353.15 0.6677
0.5835 353.15 0.7088
0.5849 343.15 0.7127
0.5864 363.15 0.7049
0.6528 363.15 0.7446
0.6541 353.15 0.7484
0.6569 343.15 0.7509
0.7256 353.15 0.7889
0.7256 363.15 0.7877
0.7282 343.15 0.7889
0.7901 343.15 0.8255
0.7901 353.15 0.8255
0.7901 363.15 0.8255
0.8518 353.15 0.8675
0.8529 343.15 0.8686
0.8529 363.15 0.8675
0.9152 343.15 0.9152
0.9152 353.15 0.9152
0.9152 363.15 0.9152
0.9636 343.15 0.9586
0.9636 353.15 0.9606
0.9636 363.15 0.9606
1.0000 343.15 1.0000
1.0000 353.15 1.0000
1.0000 363.15 1.0000

Mole fraction of Methane, nitro- (1) [ref]

Fixed Measured
Mole fraction of Methane, nitro- (1) - Liquid Temperature, K - Liquid Mole fraction of Methane, nitro- (1) - Gas
0.0000 343.15 0.0000
0.0000 353.15 0.0000
0.0000 363.15 0.0000
0.0690 343.15 0.2018
0.0690 353.15 0.1958
0.0690 363.15 0.1857
0.1214 353.15 0.3107
0.1235 343.15 0.3198
0.1256 363.15 0.2996
0.2038 363.15 0.4176
0.2078 353.15 0.4226
0.2098 343.15 0.4359
0.2810 363.15 0.4988
0.2848 343.15 0.5128
0.2848 353.15 0.5034
0.3556 363.15 0.5614
0.3574 353.15 0.5673
0.3609 343.15 0.5732
0.4392 353.15 0.6194
0.4409 343.15 0.6264
0.4441 363.15 0.6165
0.5143 363.15 0.6650
0.5159 343.15 0.6758
0.5159 353.15 0.6677
0.5835 353.15 0.7088
0.5849 343.15 0.7127
0.5864 363.15 0.7049
0.6528 363.15 0.7446
0.6541 353.15 0.7484
0.6569 343.15 0.7509
0.7256 353.15 0.7889
0.7256 363.15 0.7877
0.7282 343.15 0.7889
0.7901 343.15 0.8255
0.7901 353.15 0.8255
0.7901 363.15 0.8255
0.8518 353.15 0.8675
0.8529 343.15 0.8686
0.8529 363.15 0.8675
0.9152 343.15 0.9152
0.9152 353.15 0.9152
0.9152 363.15 0.9152
0.9636 343.15 0.9586
0.9636 353.15 0.9606
0.9636 363.15 0.9606
1.0000 343.15 1.0000
1.0000 353.15 1.0000
1.0000 363.15 1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Methane, nitro- (1) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 343.15 18.31
0.0000 353.15 26.84
0.0000 363.15 38.65
0.0690 343.15 21.46
0.0690 353.15 31.18
0.0690 363.15 44.48
0.1214 353.15 34.34
0.1235 343.15 23.81
0.1256 363.15 48.61
0.2038 363.15 53.68
0.2078 353.15 38.00
0.2098 343.15 26.37
0.2810 363.15 57.50
0.2848 343.15 28.36
0.2848 353.15 40.74
0.3556 363.15 60.53
0.3574 353.15 43.06
0.3609 343.15 30.00
0.4392 353.15 44.94
0.4409 343.15 31.32
0.4441 363.15 63.25
0.5143 363.15 65.46
0.5159 343.15 32.33
0.5159 353.15 46.44
0.5835 353.15 47.68
0.5849 343.15 33.17
0.5864 363.15 67.21
0.6528 363.15 68.54
0.6541 353.15 48.60
0.6569 343.15 33.85
0.7256 353.15 49.46
0.7256 363.15 69.66
0.7282 343.15 34.38
0.7901 343.15 34.84
0.7901 353.15 50.10
0.7901 363.15 70.59
0.8518 353.15 50.46
0.8529 343.15 35.12
0.8529 363.15 71.07
0.9152 343.15 35.17
0.9152 353.15 50.57
0.9152 363.15 71.21
0.9636 343.15 35.00
0.9636 353.15 50.36
0.9636 363.15 71.07
1.0000 343.15 34.93
1.0000 353.15 50.14
1.0000 363.15 70.81

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Methane, nitro- (1) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 343.15 18.31
0.0000 353.15 26.84
0.0000 363.15 38.65
0.0690 343.15 21.46
0.0690 353.15 31.18
0.0690 363.15 44.48
0.1214 353.15 34.34
0.1235 343.15 23.81
0.1256 363.15 48.61
0.2038 363.15 53.68
0.2078 353.15 38.00
0.2098 343.15 26.37
0.2810 363.15 57.50
0.2848 343.15 28.36
0.2848 353.15 40.74
0.3556 363.15 60.53
0.3574 353.15 43.06
0.3609 343.15 30.00
0.4392 353.15 44.94
0.4409 343.15 31.32
0.4441 363.15 63.25
0.5143 363.15 65.46
0.5159 343.15 32.33
0.5159 353.15 46.44
0.5835 353.15 47.68
0.5849 343.15 33.17
0.5864 363.15 67.21
0.6528 363.15 68.54
0.6541 353.15 48.60
0.6569 343.15 33.85
0.7256 353.15 49.46
0.7256 363.15 69.66
0.7282 343.15 34.38
0.7901 343.15 34.84
0.7901 353.15 50.10
0.7901 363.15 70.59
0.8518 353.15 50.46
0.8529 343.15 35.12
0.8529 363.15 71.07
0.9152 343.15 35.17
0.9152 353.15 50.57
0.9152 363.15 71.21
0.9636 343.15 35.00
0.9636 353.15 50.36
0.9636 363.15 71.07
1.0000 343.15 34.93
1.0000 353.15 50.14
1.0000 363.15 70.81

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1,3-dichloro- (2) - Liquid Refractive index (Na D-line) - Liquid
298.15 0.0000 1.3795
298.15 0.0878 1.3881
298.15 0.1939 1.3976
298.15 0.2938 1.4057
298.15 0.3998 1.4134
298.15 0.5028 1.4202
298.15 0.6154 1.427
298.15 0.7207 1.4328
298.15 0.8326 1.4384
298.15 0.9404 1.4435
298.15 1.0000 1.4462
308.15 0.0000 1.3748
308.15 0.0878 1.3833
308.15 0.1939 1.3928
308.15 0.2938 1.4009
308.15 0.3998 1.4087
308.15 0.5028 1.4155
308.15 0.6154 1.4224
308.15 0.7207 1.4283
308.15 0.8326 1.4336
308.15 0.9404 1.4385
308.15 1.0000 1.4412
318.15 0.0000 1.3701
318.15 0.0878 1.3786
318.15 0.1939 1.3881
318.15 0.2938 1.3963
318.15 0.3998 1.4042
318.15 0.5028 1.4109
318.15 0.6154 1.4178
318.15 0.7207 1.4234
318.15 0.8326 1.4288
318.15 0.9404 1.4335
318.15 1.0000 1.4361

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1,3-dichloro- (2) - Liquid Refractive index (Na D-line) - Liquid
298.15 0.0000 1.3795
298.15 0.0878 1.3881
298.15 0.1939 1.3976
298.15 0.2938 1.4057
298.15 0.3998 1.4134
298.15 0.5028 1.4202
298.15 0.6154 1.427
298.15 0.7207 1.4328
298.15 0.8326 1.4384
298.15 0.9404 1.4435
298.15 1.0000 1.4462
308.15 0.0000 1.3748
308.15 0.0878 1.3833
308.15 0.1939 1.3928
308.15 0.2938 1.4009
308.15 0.3998 1.4087
308.15 0.5028 1.4155
308.15 0.6154 1.4224
308.15 0.7207 1.4283
308.15 0.8326 1.4336
308.15 0.9404 1.4385
308.15 1.0000 1.4412
318.15 0.0000 1.3701
318.15 0.0878 1.3786
318.15 0.1939 1.3881
318.15 0.2938 1.3963
318.15 0.3998 1.4042
318.15 0.5028 1.4109
318.15 0.6154 1.4178
318.15 0.7207 1.4234
318.15 0.8326 1.4288
318.15 0.9404 1.4335
318.15 1.0000 1.4361

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1,3-dichloro- (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 1130.9
298.15 0.0878 1135.58
298.15 0.1939 1141.34
298.15 0.2938 1146.79
298.15 0.3998 1152.41
298.15 0.5028 1157.65
298.15 0.6154 1163.15
298.15 0.7207 1168.07
298.15 0.8326 1173.04
298.15 0.9404 1177.55
298.15 1.0000 1180.1
308.15 0.0000 1117.28
308.15 0.0878 1122.12
308.15 0.1939 1128.05
308.15 0.2938 1133.64
308.15 0.3998 1139.39
308.15 0.5028 1144.76
308.15 0.6154 1150.38
308.15 0.7207 1155.41
308.15 0.8326 1160.49
308.15 0.9404 1165.1
308.15 1.0000 1167.7
318.15 0.0000 1103.53
318.15 0.0878 1108.53
318.15 0.1939 1114.63
318.15 0.2938 1120.37
318.15 0.3998 1126.26
318.15 0.5028 1131.76
318.15 0.6154 1137.51
318.15 0.7207 1142.65
318.15 0.8326 1147.84
318.15 0.9404 1152.56
318.15 1.0000 1155.21

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1,3-dichloro- (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 1130.9
298.15 0.0878 1135.58
298.15 0.1939 1141.34
298.15 0.2938 1146.79
298.15 0.3998 1152.41
298.15 0.5028 1157.65
298.15 0.6154 1163.15
298.15 0.7207 1168.07
298.15 0.8326 1173.04
298.15 0.9404 1177.55
298.15 1.0000 1180.1
308.15 0.0000 1117.28
308.15 0.0878 1122.12
308.15 0.1939 1128.05
308.15 0.2938 1133.64
308.15 0.3998 1139.39
308.15 0.5028 1144.76
308.15 0.6154 1150.38
308.15 0.7207 1155.41
308.15 0.8326 1160.49
308.15 0.9404 1165.1
308.15 1.0000 1167.7
318.15 0.0000 1103.53
318.15 0.0878 1108.53
318.15 0.1939 1114.63
318.15 0.2938 1120.37
318.15 0.3998 1126.26
318.15 0.5028 1131.76
318.15 0.6154 1137.51
318.15 0.7207 1142.65
318.15 0.8326 1147.84
318.15 0.9404 1152.56
318.15 1.0000 1155.21

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1,3-dichloro- (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0000 1321.2
298.15 0.0878 1303.01
298.15 0.1939 1285.88
298.15 0.2938 1273.61
298.15 0.3998 1263.48
298.15 0.5028 1255.92
298.15 0.6154 1249.39
298.15 0.7207 1244.73
298.15 0.8326 1240.82
298.15 0.9404 1237.91
298.15 1.0000 1236.45
308.15 0.0000 1281.78
308.15 0.0878 1263.96
308.15 0.1939 1247.34
308.15 0.2938 1235.4
308.15 0.3998 1225.59
308.15 0.5028 1218.18
308.15 0.6154 1212.0
308.15 0.7207 1207.52
308.15 0.8326 1203.81
308.15 0.9404 1201.02
308.15 1.0000 1199.72
318.15 0.0000 1242.46
318.15 0.0878 1225.05
318.15 0.1939 1208.88
318.15 0.2938 1197.29
318.15 0.3998 1187.81
318.15 0.5028 1180.73
318.15 0.6154 1174.76
318.15 0.7207 1170.51
318.15 0.8326 1167.01
318.15 0.9404 1164.4
318.15 1.0000 1163.22

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1,3-dichloro- (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0000 1321.2
298.15 0.0878 1303.01
298.15 0.1939 1285.88
298.15 0.2938 1273.61
298.15 0.3998 1263.48
298.15 0.5028 1255.92
298.15 0.6154 1249.39
298.15 0.7207 1244.73
298.15 0.8326 1240.82
298.15 0.9404 1237.91
298.15 1.0000 1236.45
308.15 0.0000 1281.78
308.15 0.0878 1263.96
308.15 0.1939 1247.34
308.15 0.2938 1235.4
308.15 0.3998 1225.59
308.15 0.5028 1218.18
308.15 0.6154 1212.0
308.15 0.7207 1207.52
308.15 0.8326 1203.81
308.15 0.9404 1201.02
308.15 1.0000 1199.72
318.15 0.0000 1242.46
318.15 0.0878 1225.05
318.15 0.1939 1208.88
318.15 0.2938 1197.29
318.15 0.3998 1187.81
318.15 0.5028 1180.73
318.15 0.6154 1174.76
318.15 0.7207 1170.51
318.15 0.8326 1167.01
318.15 0.9404 1164.4
318.15 1.0000 1163.22

Sources