Mixture of Heptane + Acetic acid, propyl ester

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5

Acetic acid, propyl ester

Name
Acetic acid, propyl ester
InChI
InChI=1S/C5H10O2/c1-3-4-7-5(2)6/h3-4H2,1-2H3
InChI Key
YKYONYBAUNKHLG-UHFFFAOYSA-N
Formula
C5H10O2
SMILES
CCCOC(C)=O
Mol. Weight (g/mol)
102.13
CAS
109-60-4
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Datasets

  1. Mole fraction
  2. Excess molar enthalpy (molar enthalpy (3)
  3. Pvap - Vapor or sublimation pressure, kPa
  4. ρl - Mass density, kg/m3
  5. Tboil(P) - Boiling temperature at pressure P, K
  6. Excess molar volume, m3/mol

Mole fraction of Acetic acid, propyl ester (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Acetic acid, propyl ester (2) - Liquid Mole fraction of Acetic acid, propyl ester (2) - Gas
0.0000 0.0000
0.0298 0.0603
0.0590 0.1033
0.0954 0.1513
0.1398 0.2084
0.1895 0.2627
0.2337 0.3031
0.2761 0.3347
0.3070 0.3578
0.3411 0.3828
0.3789 0.4073
0.4138 0.4308
0.4450 0.4470
0.4716 0.4624
0.5025 0.4781
0.5492 0.5014
0.5694 0.5155
0.6001 0.5341
0.6279 0.5521
0.6498 0.5686
0.6729 0.5869
0.7003 0.6065
0.7306 0.6301
0.7556 0.6507
0.7801 0.6762
0.8033 0.7023
0.8275 0.7289
0.8508 0.7561
0.8823 0.7959
0.9069 0.8321
0.9372 0.8805
0.9652 0.9292
0.9912 0.9712
1.0000 1.0000

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, propyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0692 0.3455
0.1449 0.6329
0.2229 0.8839
0.2968 1.052
0.3635 1.1622
0.4256 1.2203
0.4840 1.2363
0.5350 1.2171
0.5539 1.187
0.6002 1.1302
0.6528 1.0508
0.6987 0.9556
0.7526 0.8282
0.8089 0.6592
0.8635 0.4933
0.9048 0.3544
0.9537 0.1852

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, propyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1087 0.5043
0.1348 0.5990
0.2399 0.8937
0.3594 1.084
0.4570 1.142
0.5004 1.144
0.5217 1.136
0.5427 1.128
0.5634 1.115
0.5838 1.098
0.6544 1.021
0.7495 0.8456
0.8346 0.6283
0.9200 0.3378
0.9526 0.2072

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, propyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0996 0.4360
0.2001 0.7560
0.2956 1.001
0.3852 1.14
0.4642 1.192
0.5309 1.195
0.5880 1.149
0.6380 1.073
0.6560 1.046
0.7113 0.9480
0.7717 0.8100
0.8326 0.6390
0.8942 0.4370
0.9501 0.2260

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid, propyl ester (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
273.15 0.0000 1.53
273.15 0.1278 1.68
273.15 0.2425 1.73
273.15 0.3762 1.73
273.15 0.4793 1.71
273.15 0.6179 1.65
273.15 0.7441 1.55
273.15 0.8996 1.32
273.15 1.0000 1.01
283.15 0.0000 2.76
283.15 0.1278 3.04
283.15 0.2425 3.13
283.15 0.3762 3.13
283.15 0.4793 3.10
283.15 0.6179 3.00
283.15 0.7441 2.83
283.15 0.8996 2.43
283.15 1.0000 1.91
293.15 0.0000 4.74
293.15 0.1278 5.21
293.15 0.2425 5.37
293.15 0.3762 5.39
293.15 0.4793 5.33
293.15 0.6179 5.18
293.15 0.7441 4.90
293.15 0.8996 4.26
293.15 1.0000 3.43
298.15 0.0000 6.10
298.15 0.1278 6.71
298.15 0.2425 6.92
298.15 0.3762 6.95
298.15 0.4793 6.88
298.15 0.6179 6.69
298.15 0.7441 6.34
298.15 0.8996 5.53
298.15 1.0000 4.51
303.15 0.0000 7.79
303.15 0.1278 8.56
303.15 0.2425 8.83
303.15 0.3762 8.88
303.15 0.4793 8.79
303.15 0.6179 8.56
303.15 0.7441 8.12
303.15 0.8996 7.12
303.15 1.0000 5.87
313.15 0.0000 12.32
313.15 0.1278 13.52
313.15 0.2425 13.96
313.15 0.3762 14.07
313.15 0.4793 13.95
313.15 0.6179 13.60
313.15 0.7441 12.95
313.15 0.8996 11.46
313.15 1.0000 9.64
323.15 0.0000 18.85
323.15 0.1278 20.65
323.15 0.2425 21.33
323.15 0.3762 21.53
323.15 0.4793 21.38
323.15 0.6179 20.89
323.15 0.7441 19.95
323.15 0.8996 17.82
323.15 1.0000 15.25
333.15 0.0000 27.99
333.15 0.1278 30.59
333.15 0.2425 31.61
333.15 0.3762 31.96
333.15 0.4793 31.79
333.15 0.6179 31.11
333.15 0.7441 29.79
333.15 0.8996 26.84
333.15 1.0000 23.33
343.15 0.0000 40.43
343.15 0.1278 44.07
343.15 0.2425 45.57
343.15 0.3762 46.16
343.15 0.4793 45.98
343.15 0.6179 45.07
343.15 0.7441 43.28
343.15 0.8996 39.30
343.15 1.0000 34.64
353.15 0.0000 56.99
353.15 0.1278 61.96
353.15 0.2425 64.10
353.15 0.3762 65.05
353.15 0.4793 64.87
353.15 0.6179 63.70
353.15 0.7441 61.33
353.15 0.8996 56.12
353.15 1.0000 50.07
363.15 0.0000 78.59
363.15 0.1278 85.19
363.15 0.2425 88.17
363.15 0.3762 89.63
363.15 0.4793 89.52
363.15 0.6179 88.03
363.15 0.7441 84.97
363.15 0.8996 78.33
363.15 1.0000 70.64

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid, propyl ester (2) - Liquid Mass density, kg/m3 - Liquid
328.15 0.0000 653.7
328.15 0.0373 658.5
328.15 0.0866 665.4
328.15 0.1645 676.8
328.15 0.2401 688.6
328.15 0.3096 700.0
328.15 0.3783 711.8
328.15 0.4478 724.3
328.15 0.5142 736.8
328.15 0.5756 748.9
328.15 0.6377 761.7
328.15 0.6884 772.5
328.15 0.7560 787.5
328.15 0.8074 799.5
328.15 0.8560 811.2
328.15 0.9097 824.7
328.15 0.9638 838.7
328.15 1.0000 848.3
318.15 0.0000 662.1
318.15 0.0291 666.1
318.15 0.0843 673.9
318.15 0.1595 685.1
318.15 0.2300 696.3
318.15 0.2972 707.3
318.15 0.3638 718.8
318.15 0.4295 730.8
318.15 0.4902 742.3
318.15 0.5530 754.6
318.15 0.6057 765.4
318.15 0.6734 779.8
318.15 0.7260 791.4
318.15 0.7727 802.1
318.15 0.7949 807.7
318.15 0.8645 824.4
318.15 0.9242 839.3
318.15 1.0000 859.8
298.15 0.0000 679.5
298.15 0.0149 681.8
298.15 0.0308 684.0
298.15 0.0953 693.5
298.15 0.1680 704.8
298.15 0.2358 715.8
298.15 0.3084 728.2
298.15 0.3750 740.2
298.15 0.4386 752.1
298.15 0.5062 765.3
298.15 0.5643 777.2
298.15 0.6488 795.2
298.15 0.6684 799.5
298.15 0.7446 816.9
298.15 0.7930 828.4
298.15 0.8688 847.3
298.15 0.9100 858.0
298.15 0.9508 868.8
298.15 1.0000 882.5
291.15 0.0000 685.3
291.15 0.0086 686.6
291.15 0.0320 690.1
291.15 0.0864 698.2
291.15 0.1706 711.3
291.15 0.2573 725.7
291.15 0.3308 738.6
291.15 0.3974 750.9
291.15 0.4644 763.7
291.15 0.5398 778.9
291.15 0.6055 792.8
291.15 0.6723 807.4
291.15 0.7257 819.6
291.15 0.8000 837.2
291.15 0.8457 848.5
291.15 0.9057 864.0
291.15 0.9708 881.6
291.15 1.0000 889.6

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Acetic acid, propyl ester (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 371.55
0.0298 370.51
0.0590 370.13
0.0954 369.57
0.1398 368.86
0.1895 368.29
0.2337 367.78
0.2761 367.46
0.3070 367.27
0.3411 367.11
0.3789 367.08
0.4138 367.07
0.4450 367.05
0.4716 367.12
0.5025 367.23
0.5492 367.35
0.5694 367.46
0.6001 367.64
0.6279 367.79
0.6498 367.90
0.6729 368.19
0.7003 368.44
0.7306 368.74
0.7556 369.06
0.7801 369.43
0.8033 369.85
0.8275 370.29
0.8508 370.75
0.8823 371.26
0.9069 371.73
0.9372 372.54
0.9652 373.25
0.9912 373.98
1.0000 374.34

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, propyl ester (2) - Liquid Excess molar volume, m3/mol - Liquid
0.0727 3.3200e-07
0.1288 4.9800e-07
0.1829 6.4500e-07
0.2463 7.6800e-07
0.2995 8.3800e-07
0.3536 8.8700e-07
0.4040 9.0900e-07
0.4630 9.2300e-07
0.5069 9.1000e-07
0.5618 8.8500e-07
0.6574 7.9600e-07
0.6914 7.5200e-07
0.7928 5.6100e-07
0.8765 3.6200e-07
0.9436 1.7500e-07

Sources

Note: These property values are available through the Cheméo API. A free account gives you an access key.