Mixture of Formamide, N,N-dimethyl- + Di-n-propyl ether

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Formamide, N,N-dimethyl-

Name
Formamide, N,N-dimethyl-
InChI
InChI=1S/C3H7NO/c1-4(2)3-5/h3H,1-2H3
InChI Key
ZMXDDKWLCZADIW-UHFFFAOYSA-N
Formula
C3H7NO
SMILES
CN(C)C=O
Mol. Weight (g/mol)
73.09
CAS
68-12-2

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
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Datasets

  1. Mole fraction (2)
  2. ρl - Mass density, kg/m3 (2)
  3. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Di-n-propyl ether (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Di-n-propyl ether (2) - Liquid Mole fraction of Di-n-propyl ether (2) - Gas
0.0000 0.0000
0.0020 0.0380
0.0090 0.1480
0.0160 0.2280
0.0250 0.3030
0.0340 0.3800
0.0510 0.4950
0.1050 0.6870
0.1580 0.7750
0.2220 0.8200
0.2960 0.8540
0.3400 0.8650
0.3910 0.8760
0.4390 0.8840
0.4890 0.8950
0.5400 0.8990
0.6250 0.9040
0.6820 0.9110
0.7380 0.9190
0.8000 0.9290
0.8710 0.9450
0.9390 0.9680
1.0000 1.0000

Mole fraction of Di-n-propyl ether (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Di-n-propyl ether (2) - Liquid Mole fraction of Di-n-propyl ether (2) - Gas
0.0000 0.0000
0.0020 0.0380
0.0090 0.1480
0.0160 0.2280
0.0250 0.3030
0.0340 0.3800
0.0510 0.4950
0.1050 0.6870
0.1580 0.7750
0.2220 0.8200
0.2960 0.8540
0.3400 0.8650
0.3910 0.8760
0.4390 0.8840
0.4890 0.8950
0.5400 0.8990
0.6250 0.9040
0.6820 0.9110
0.7380 0.9190
0.8000 0.9290
0.8710 0.9450
0.9390 0.9680
1.0000 1.0000

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0499 749.01
298.15 0.1072 756.74
298.15 0.1515 763.14
298.15 0.2129 772.12
298.15 0.2528 778.22
298.15 0.3142 787.82
298.15 0.3508 793.89
298.15 0.3895 800.55
298.15 0.4353 808.57
298.15 0.4788 816.49
298.15 0.5053 821.46
298.15 0.5243 825.12
298.15 0.5454 829.23
298.15 0.6019 840.66
298.15 0.6475 850.32
298.15 0.7054 863.22
298.15 0.7502 873.74
298.15 0.7900 883.5
298.15 0.8514 899.37
298.15 0.9075 914.86
298.15 0.9594 933.76
313.15 0.0499 735.06
313.15 0.1072 742.84
313.15 0.1515 749.17
313.15 0.2129 758.15
313.15 0.2528 764.23
313.15 0.3142 773.92
313.15 0.3508 780.0
313.15 0.3895 786.59
313.15 0.4353 794.67
313.15 0.4788 802.63
313.15 0.5053 807.64
313.15 0.5243 811.32
313.15 0.5454 815.46
313.15 0.6019 826.99
313.15 0.6475 836.74
313.15 0.7054 849.75
313.15 0.7502 860.32
313.15 0.7900 870.11
313.15 0.8514 886.42
313.15 0.9075 902.16
313.15 0.9594 921.32
328.15 0.0499 720.89
328.15 0.1072 728.72
328.15 0.1515 735.12
328.15 0.2129 743.94
328.15 0.2528 749.93
328.15 0.3142 759.52
328.15 0.3508 765.58
328.15 0.3895 772.07
328.15 0.4353 780.13
328.15 0.4788 788.03
328.15 0.5053 793.01
328.15 0.5243 796.66
328.15 0.5454 800.8
328.15 0.6019 812.28
328.15 0.6475 821.98
328.15 0.7054 834.83
328.15 0.7502 845.39
328.15 0.7900 854.95
328.15 0.8514 871.19
328.15 0.9075 886.61
328.15 0.9594 905.81
343.15 0.0499 706.81
343.15 0.1072 714.64
343.15 0.1515 720.81
343.15 0.2129 729.67
343.15 0.2528 735.72
343.15 0.3142 745.25
343.15 0.3508 751.24
343.15 0.3895 757.74
343.15 0.4353 765.72
343.15 0.4788 773.58
343.15 0.5053 778.54
343.15 0.5243 782.18
343.15 0.5454 786.3
343.15 0.6019 797.75
343.15 0.6475 807.43
343.15 0.7054 820.5
343.15 0.7502 830.97
343.15 0.7900 840.56
343.15 0.8514 856.91
343.15 0.9075 872.33
343.15 0.9594 891.47
358.15 0.0499 692.16
358.15 0.1072 699.96
358.15 0.1515 706.1
358.15 0.2129 714.89
358.15 0.2528 720.91
358.15 0.3142 730.4
358.15 0.3508 736.39
358.15 0.3895 742.88
358.15 0.4353 750.85
358.15 0.4788 758.7
358.15 0.5053 763.66
358.15 0.5243 767.29
358.15 0.5454 771.4
358.15 0.6019 782.85
358.15 0.6475 792.53
358.15 0.7054 805.64
358.15 0.7502 816.13
358.15 0.7900 825.74
358.15 0.8514 842.07
358.15 0.9075 857.58
358.15 0.9594 876.94

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0499 749.01
298.15 0.1072 756.74
298.15 0.1515 763.14
298.15 0.2129 772.12
298.15 0.2528 778.22
298.15 0.3142 787.82
298.15 0.3508 793.89
298.15 0.3895 800.55
298.15 0.4353 808.57
298.15 0.4788 816.49
298.15 0.5053 821.46
298.15 0.5243 825.12
298.15 0.5454 829.23
298.15 0.6019 840.66
298.15 0.6475 850.32
298.15 0.7054 863.22
298.15 0.7502 873.74
298.15 0.7900 883.5
298.15 0.8514 899.37
298.15 0.9075 914.86
298.15 0.9594 933.76
313.15 0.0499 735.06
313.15 0.1072 742.84
313.15 0.1515 749.17
313.15 0.2129 758.15
313.15 0.2528 764.23
313.15 0.3142 773.92
313.15 0.3508 780.0
313.15 0.3895 786.59
313.15 0.4353 794.67
313.15 0.4788 802.63
313.15 0.5053 807.64
313.15 0.5243 811.32
313.15 0.5454 815.46
313.15 0.6019 826.99
313.15 0.6475 836.74
313.15 0.7054 849.75
313.15 0.7502 860.32
313.15 0.7900 870.11
313.15 0.8514 886.42
313.15 0.9075 902.16
313.15 0.9594 921.32
328.15 0.0499 720.89
328.15 0.1072 728.72
328.15 0.1515 735.12
328.15 0.2129 743.94
328.15 0.2528 749.93
328.15 0.3142 759.52
328.15 0.3508 765.58
328.15 0.3895 772.07
328.15 0.4353 780.13
328.15 0.4788 788.03
328.15 0.5053 793.01
328.15 0.5243 796.66
328.15 0.5454 800.8
328.15 0.6019 812.28
328.15 0.6475 821.98
328.15 0.7054 834.83
328.15 0.7502 845.39
328.15 0.7900 854.95
328.15 0.8514 871.19
328.15 0.9075 886.61
328.15 0.9594 905.81
343.15 0.0499 706.81
343.15 0.1072 714.64
343.15 0.1515 720.81
343.15 0.2129 729.67
343.15 0.2528 735.72
343.15 0.3142 745.25
343.15 0.3508 751.24
343.15 0.3895 757.74
343.15 0.4353 765.72
343.15 0.4788 773.58
343.15 0.5053 778.54
343.15 0.5243 782.18
343.15 0.5454 786.3
343.15 0.6019 797.75
343.15 0.6475 807.43
343.15 0.7054 820.5
343.15 0.7502 830.97
343.15 0.7900 840.56
343.15 0.8514 856.91
343.15 0.9075 872.33
343.15 0.9594 891.47
358.15 0.0499 692.16
358.15 0.1072 699.96
358.15 0.1515 706.1
358.15 0.2129 714.89
358.15 0.2528 720.91
358.15 0.3142 730.4
358.15 0.3508 736.39
358.15 0.3895 742.88
358.15 0.4353 750.85
358.15 0.4788 758.7
358.15 0.5053 763.66
358.15 0.5243 767.29
358.15 0.5454 771.4
358.15 0.6019 782.85
358.15 0.6475 792.53
358.15 0.7054 805.64
358.15 0.7502 816.13
358.15 0.7900 825.74
358.15 0.8514 842.07
358.15 0.9075 857.58
358.15 0.9594 876.94

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Di-n-propyl ether (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 425.63
0.0020 423.99
0.0090 420.79
0.0160 417.24
0.0250 413.81
0.0340 410.79
0.0510 405.08
0.1050 391.86
0.1580 384.08
0.2220 378.87
0.2960 374.67
0.3400 373.08
0.3910 371.77
0.4390 370.62
0.4890 369.55
0.5400 368.76
0.6250 367.65
0.6820 366.87
0.7380 366.18
0.8000 365.43
0.8710 364.57
0.9390 363.77
1.0000 363.16

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Di-n-propyl ether (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 425.63
0.0020 423.99
0.0090 420.79
0.0160 417.24
0.0250 413.81
0.0340 410.79
0.0510 405.08
0.1050 391.86
0.1580 384.08
0.2220 378.87
0.2960 374.67
0.3400 373.08
0.3910 371.77
0.4390 370.62
0.4890 369.55
0.5400 368.76
0.6250 367.65
0.6820 366.87
0.7380 366.18
0.8000 365.43
0.8710 364.57
0.9390 363.77
1.0000 363.16

Sources