Mixture of n-Hexane + Pentane, 1-chloro-

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n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

Pentane, 1-chloro-

Name
Pentane, 1-chloro-
InChI
InChI=1S/C5H11Cl/c1-2-3-4-5-6/h2-5H2,1H3
InChI Key
SQCZQTSHSZLZIQ-UHFFFAOYSA-N
Formula
C5H11Cl
SMILES
CCCCCCl
Mol. Weight (g/mol)
106.59
CAS
543-59-9
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Datasets

  1. Mole fraction (2)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. γ - Surface tension liquid-gas, N/m (2)

Mole fraction of n-Hexane (1) [ref]

Fixed Measured
Mole fraction of n-Hexane (1) - Gas Temperature, K - Liquid Mole fraction of n-Hexane (1) - Liquid
0.2359 308.15 0.0471
0.3178 288.15 0.0643
0.3178 298.15 0.0643
0.3706 308.15 0.0863
0.4075 288.15 0.0769
0.4289 298.15 0.1033
0.4480 308.15 0.1188
0.5479 288.15 0.1328
0.5497 308.15 0.1711
0.5969 298.15 0.1898
0.6274 288.15 0.1792
0.6520 308.15 0.2514
0.6902 308.15 0.3004
0.7251 288.15 0.2697
0.7387 298.15 0.3239
0.7940 308.15 0.4506
0.7966 298.15 0.4282
0.8005 288.15 0.3753
0.8407 308.15 0.5483
0.8467 298.15 0.5420
0.8488 288.15 0.4962
0.8727 288.15 0.5668
0.8741 298.15 0.5964
0.8812 308.15 0.6440
0.8983 298.15 0.6790
0.9044 288.15 0.6557
0.9200 308.15 0.7530
0.9287 298.15 0.7621
0.9294 288.15 0.7586
0.9417 288.15 0.7999
0.9423 308.15 0.8221
0.9445 298.15 0.8296
0.9683 298.15 0.8998
0.9728 308.15 0.9195
0.9799 298.15 0.9395

Mole fraction of n-Hexane (1) [ref]

Fixed Measured
Mole fraction of n-Hexane (1) - Gas Temperature, K - Liquid Mole fraction of n-Hexane (1) - Liquid
0.2359 308.15 0.0471
0.3178 288.15 0.0643
0.3178 298.15 0.0643
0.3706 308.15 0.0863
0.4075 288.15 0.0769
0.4289 298.15 0.1033
0.4480 308.15 0.1188
0.5479 288.15 0.1328
0.5497 308.15 0.1711
0.5969 298.15 0.1898
0.6274 288.15 0.1792
0.6520 308.15 0.2514
0.6902 308.15 0.3004
0.7251 288.15 0.2697
0.7387 298.15 0.3239
0.7940 308.15 0.4506
0.7966 298.15 0.4282
0.8005 288.15 0.3753
0.8407 308.15 0.5483
0.8467 298.15 0.5420
0.8488 288.15 0.4962
0.8727 288.15 0.5668
0.8741 298.15 0.5964
0.8812 308.15 0.6440
0.8983 298.15 0.6790
0.9044 288.15 0.6557
0.9200 308.15 0.7530
0.9287 298.15 0.7621
0.9294 288.15 0.7586
0.9417 288.15 0.7999
0.9423 308.15 0.8221
0.9445 298.15 0.8296
0.9683 298.15 0.8998
0.9728 308.15 0.9195
0.9799 298.15 0.9395

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of n-Hexane (1) - Gas Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.2359 308.15 8.49
0.3178 288.15 5.62
0.3178 298.15 5.62
0.3706 308.15 9.90
0.4075 288.15 3.68
0.4289 298.15 6.57
0.4480 308.15 10.90
0.5479 288.15 4.38
0.5497 308.15 12.47
0.5969 298.15 8.32
0.6274 288.15 5.07
0.6520 308.15 15.00
0.6902 308.15 16.16
0.7251 288.15 6.21
0.7387 298.15 10.93
0.7940 308.15 20.00
0.7966 298.15 12.76
0.8005 288.15 7.50
0.8407 308.15 22.05
0.8467 298.15 14.34
0.8488 288.15 8.64
0.8727 288.15 9.30
0.8741 298.15 15.05
0.8812 308.15 23.90
0.8983 298.15 16.25
0.9044 288.15 10.11
0.9200 308.15 26.12
0.9287 298.15 17.27
0.9294 288.15 11.00
0.9417 288.15 11.29
0.9423 308.15 27.32
0.9445 298.15 18.09
0.9683 298.15 18.91
0.9728 308.15 29.11
0.9799 298.15 19.42

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of n-Hexane (1) - Gas Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.2359 308.15 8.49
0.3178 288.15 5.62
0.3178 298.15 5.62
0.3706 308.15 9.90
0.4075 288.15 3.68
0.4289 298.15 6.57
0.4480 308.15 10.90
0.5479 288.15 4.38
0.5497 308.15 12.47
0.5969 298.15 8.32
0.6274 288.15 5.07
0.6520 308.15 15.00
0.6902 308.15 16.16
0.7251 288.15 6.21
0.7387 298.15 10.93
0.7940 308.15 20.00
0.7966 298.15 12.76
0.8005 288.15 7.50
0.8407 308.15 22.05
0.8467 298.15 14.34
0.8488 288.15 8.64
0.8727 288.15 9.30
0.8741 298.15 15.05
0.8812 308.15 23.90
0.8983 298.15 16.25
0.9044 288.15 10.11
0.9200 308.15 26.12
0.9287 298.15 17.27
0.9294 288.15 11.00
0.9417 288.15 11.29
0.9423 308.15 27.32
0.9445 298.15 18.09
0.9683 298.15 18.91
0.9728 308.15 29.11
0.9799 298.15 19.42

Surface tension liquid-gas, N/m [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Hexane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
283.15 0.0482 0.0254
283.15 0.1185 0.0247
283.15 0.1991 0.0240
283.15 0.3080 0.0232
283.15 0.3925 0.0226
283.15 0.5087 0.0219
283.15 0.5953 0.0214
283.15 0.7076 0.0209
283.15 0.7889 0.0205
283.15 0.9069 0.0200
283.15 0.9474 0.0198
288.15 0.0482 0.0250
288.15 0.1185 0.0243
288.15 0.1991 0.0236
288.15 0.3080 0.0228
288.15 0.3925 0.0222
288.15 0.5087 0.0214
288.15 0.5953 0.0209
288.15 0.7076 0.0204
288.15 0.7889 0.0200
288.15 0.9069 0.0194
288.15 0.9474 0.0192
293.15 0.0482 0.0245
293.15 0.1185 0.0238
293.15 0.1991 0.0231
293.15 0.3080 0.0222
293.15 0.3925 0.0217
293.15 0.5087 0.0209
293.15 0.5953 0.0205
293.15 0.7076 0.0199
293.15 0.7889 0.0195
293.15 0.9069 0.0189
293.15 0.9474 0.0187
298.15 0.0482 0.0240
298.15 0.1185 0.0233
298.15 0.1991 0.0226
298.15 0.3080 0.0218
298.15 0.3925 0.0212
298.15 0.5087 0.0205
298.15 0.5953 0.0200
298.15 0.7076 0.0194
298.15 0.7889 0.0190
298.15 0.9069 0.0185
298.15 0.9474 0.0183
303.15 0.0482 0.0236
303.15 0.1185 0.0230
303.15 0.1991 0.0222
303.15 0.3080 0.0214
303.15 0.3925 0.0208
303.15 0.5087 0.0200
303.15 0.5953 0.0196
303.15 0.7076 0.0190
303.15 0.7889 0.0186
303.15 0.9069 0.0180
303.15 0.9474 0.0178
308.15 0.0482 0.0231
308.15 0.1185 0.0225
308.15 0.1991 0.0217
308.15 0.3080 0.0208
308.15 0.3925 0.0202
308.15 0.5087 0.0194
308.15 0.5953 0.0189
308.15 0.7076 0.0183
308.15 0.7889 0.0179
308.15 0.9069 0.0173
308.15 0.9474 0.0170
313.15 0.0482 0.0226
313.15 0.1185 0.0220
313.15 0.1991 0.0213
313.15 0.3080 0.0204
313.15 0.3925 0.0198
313.15 0.5087 0.0191
313.15 0.5953 0.0186
313.15 0.7076 0.0180
313.15 0.7889 0.0176
313.15 0.9069 0.0170
313.15 0.9474 0.0168

Surface tension liquid-gas, N/m [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Hexane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
283.15 0.0482 0.0254
283.15 0.1185 0.0247
283.15 0.1991 0.0240
283.15 0.3080 0.0232
283.15 0.3925 0.0226
283.15 0.5087 0.0219
283.15 0.5953 0.0214
283.15 0.7076 0.0209
283.15 0.7889 0.0205
283.15 0.9069 0.0200
283.15 0.9474 0.0198
288.15 0.0482 0.0250
288.15 0.1185 0.0243
288.15 0.1991 0.0236
288.15 0.3080 0.0228
288.15 0.3925 0.0222
288.15 0.5087 0.0214
288.15 0.5953 0.0209
288.15 0.7076 0.0204
288.15 0.7889 0.0200
288.15 0.9069 0.0194
288.15 0.9474 0.0192
293.15 0.0482 0.0245
293.15 0.1185 0.0238
293.15 0.1991 0.0231
293.15 0.3080 0.0222
293.15 0.3925 0.0217
293.15 0.5087 0.0209
293.15 0.5953 0.0205
293.15 0.7076 0.0199
293.15 0.7889 0.0195
293.15 0.9069 0.0189
293.15 0.9474 0.0187
298.15 0.0482 0.0240
298.15 0.1185 0.0233
298.15 0.1991 0.0226
298.15 0.3080 0.0218
298.15 0.3925 0.0212
298.15 0.5087 0.0205
298.15 0.5953 0.0200
298.15 0.7076 0.0194
298.15 0.7889 0.0190
298.15 0.9069 0.0185
298.15 0.9474 0.0183
303.15 0.0482 0.0236
303.15 0.1185 0.0230
303.15 0.1991 0.0222
303.15 0.3080 0.0214
303.15 0.3925 0.0208
303.15 0.5087 0.0200
303.15 0.5953 0.0196
303.15 0.7076 0.0190
303.15 0.7889 0.0186
303.15 0.9069 0.0180
303.15 0.9474 0.0178
308.15 0.0482 0.0231
308.15 0.1185 0.0225
308.15 0.1991 0.0217
308.15 0.3080 0.0208
308.15 0.3925 0.0202
308.15 0.5087 0.0194
308.15 0.5953 0.0189
308.15 0.7076 0.0183
308.15 0.7889 0.0179
308.15 0.9069 0.0173
308.15 0.9474 0.0170
313.15 0.0482 0.0226
313.15 0.1185 0.0220
313.15 0.1991 0.0213
313.15 0.3080 0.0204
313.15 0.3925 0.0198
313.15 0.5087 0.0191
313.15 0.5953 0.0186
313.15 0.7076 0.0180
313.15 0.7889 0.0176
313.15 0.9069 0.0170
313.15 0.9474 0.0168

Sources