Mixture of Di-n-propyl ether + Heptane

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Di-n-propyl ether

Name
Di-n-propyl ether
InChI
InChI=1S/C6H14O/c1-3-5-7-6-4-2/h3-6H2,1-2H3
InChI Key
POLCUAVZOMRGSN-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCCOCCC
Mol. Weight (g/mol)
102.17
CAS
111-43-3

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
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Di-n-propyl ether (1) [ref]

Operational condition: Pressure, kPa = 60 (Liquid)

Mole fraction of Di-n-propyl ether (1) - Liquid Mole fraction of Di-n-propyl ether (1) - Gas
0.0000 0.0000
0.0270 0.0380
0.0550 0.0780
0.0820 0.1150
0.1010 0.1440
0.1540 0.2150
0.1800 0.2320
0.2070 0.2660
0.2090 0.2730
0.2320 0.3070
0.2500 0.3250
0.2560 0.3390
0.3010 0.3810
0.3100 0.3860
0.3320 0.4110
0.3720 0.4500
0.3860 0.4670
0.4180 0.4960
0.4850 0.5580
0.4940 0.5700
0.5450 0.6190
0.5640 0.6320
0.5830 0.6520
0.6180 0.6830
0.6270 0.6880
0.6510 0.7120
0.6830 0.7380
0.7140 0.7620
0.7150 0.7650
0.7470 0.7920
0.7760 0.8130
0.8040 0.8370
0.8280 0.8570
0.8580 0.8830
0.8920 0.9110
0.9200 0.9330
0.9460 0.9550
0.9740 0.9790
1.0000 1.0000
1.0000 1.0000

Mole fraction of Di-n-propyl ether (1) [ref]

Operational condition: Pressure, kPa = 60 (Liquid)

Mole fraction of Di-n-propyl ether (1) - Liquid Mole fraction of Di-n-propyl ether (1) - Gas
0.0000 0.0000
0.0270 0.0380
0.0550 0.0780
0.0820 0.1150
0.1010 0.1440
0.1540 0.2150
0.1800 0.2320
0.2070 0.2660
0.2090 0.2730
0.2320 0.3070
0.2500 0.3250
0.2560 0.3390
0.3010 0.3810
0.3100 0.3860
0.3320 0.4110
0.3720 0.4500
0.3860 0.4670
0.4180 0.4960
0.4850 0.5580
0.4940 0.5700
0.5450 0.6190
0.5640 0.6320
0.5830 0.6520
0.6180 0.6830
0.6270 0.6880
0.6510 0.7120
0.6830 0.7380
0.7140 0.7620
0.7150 0.7650
0.7470 0.7920
0.7760 0.8130
0.8040 0.8370
0.8280 0.8570
0.8580 0.8830
0.8920 0.9110
0.9200 0.9330
0.9460 0.9550
0.9740 0.9790
1.0000 1.0000
1.0000 1.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 60 (Liquid)

Mole fraction of Di-n-propyl ether (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 354.63
0.0270 354.42
0.0550 354.01
0.0820 353.65
0.1010 353.33
0.1540 352.66
0.1800 352.55
0.2070 352.34
0.2090 352.17
0.2320 351.94
0.2500 351.75
0.2560 351.66
0.3010 351.25
0.3100 351.07
0.3320 350.92
0.3720 350.65
0.3860 350.46
0.4180 350.29
0.4850 349.60
0.4940 349.60
0.5450 349.23
0.5640 349.07
0.5830 348.96
0.6180 348.71
0.6270 348.62
0.6510 348.54
0.6830 348.35
0.7140 348.09
0.7150 348.09
0.7470 347.94
0.7760 347.74
0.8040 347.60
0.8280 347.49
0.8580 347.26
0.8920 347.11
0.9200 346.98
0.9460 346.82
0.9740 346.72
1.0000 346.63
1.0000 346.55

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 60 (Liquid)

Mole fraction of Di-n-propyl ether (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 354.63
0.0270 354.42
0.0550 354.01
0.0820 353.65
0.1010 353.33
0.1540 352.66
0.1800 352.55
0.2070 352.34
0.2090 352.17
0.2320 351.94
0.2500 351.75
0.2560 351.66
0.3010 351.25
0.3100 351.07
0.3320 350.92
0.3720 350.65
0.3860 350.46
0.4180 350.29
0.4850 349.60
0.4940 349.60
0.5450 349.23
0.5640 349.07
0.5830 348.96
0.6180 348.71
0.6270 348.62
0.6510 348.54
0.6830 348.35
0.7140 348.09
0.7150 348.09
0.7470 347.94
0.7760 347.74
0.8040 347.60
0.8280 347.49
0.8580 347.26
0.8920 347.11
0.9200 346.98
0.9460 346.82
0.9740 346.72
1.0000 346.63
1.0000 346.55

Sources