Mixture of 2-Propanol, 2-methyl- + Monoethanolamine

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2-Propanol, 2-methyl-

Name
2-Propanol, 2-methyl-
InChI
InChI=1S/C4H10O/c1-4(2,3)5/h5H,1-3H3
InChI Key
DKGAVHZHDRPRBM-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)(C)O
Mol. Weight (g/mol)
74.12
CAS
75-65-0

Monoethanolamine

Name
Monoethanolamine
InChI
InChI=1S/C2H7NO/c3-1-2-4/h4H,1-3H2
InChI Key
HZAXFHJVJLSVMW-UHFFFAOYSA-N
Formula
C2H7NO
SMILES
NCCO
Mol. Weight (g/mol)
61.08
CAS
141-43-5
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Datasets

  1. Pvap - Vapor or sublimation pressure, kPa (2)
  2. ρl - Mass density, kg/m3 (2)
  3. Tboil - Boiling temperature at pressure P, K (2)

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Monoethanolamine (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
373.15 1.0000 6.17
373.15 0.9784 13.75
373.15 0.9568 22.11
373.15 0.9375 29.11
373.15 0.9160 36.16
373.15 0.8669 48.60
373.15 0.8178 58.39
373.15 0.7717 67.40
373.15 0.7211 73.75
373.15 0.6707 85.58
373.15 0.6201 92.48
373.15 0.5735 99.56
373.15 0.5670 101.12
373.15 0.5218 107.09
373.15 0.5148 108.69
373.15 0.4712 114.26
373.15 0.4617 116.04
373.15 0.4193 122.38
373.15 0.3664 129.72
373.15 0.3142 135.54
373.15 0.2611 144.90
373.15 0.2089 154.76
373.15 0.1556 163.52
373.15 0.1055 173.14
373.15 0.0822 177.13
373.15 0.0623 181.01
373.15 0.0424 185.36
373.15 0.0000 192.46
423.15 1.0000 52.71
423.15 0.9798 79.21
423.15 0.9593 105.91
423.15 0.9410 132.56
423.15 0.9204 159.74
423.15 0.8728 211.99
423.15 0.8246 258.65
423.15 0.7787 297.64
423.15 0.7280 338.10
423.15 0.6771 374.24
423.15 0.6258 408.93
423.15 0.5763 432.11
423.15 0.5717 443.46
423.15 0.5252 463.89
423.15 0.5185 476.70
423.15 0.4752 494.48
423.15 0.4643 508.80
423.15 0.4238 525.54
423.15 0.3712 559.51
423.15 0.3190 591.77
423.15 0.2658 626.39
423.15 0.2133 662.39
423.15 0.1594 701.12
423.15 0.1084 739.46
423.15 0.0846 759.47
423.15 0.0642 776.76
423.15 0.0437 793.62
423.15 0.0000 818.16

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Monoethanolamine (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
373.15 1.0000 6.17
373.15 0.9784 13.75
373.15 0.9568 22.11
373.15 0.9375 29.11
373.15 0.9160 36.16
373.15 0.8669 48.60
373.15 0.8178 58.39
373.15 0.7717 67.40
373.15 0.7211 73.75
373.15 0.6707 85.58
373.15 0.6201 92.48
373.15 0.5735 99.56
373.15 0.5670 101.12
373.15 0.5218 107.09
373.15 0.5148 108.69
373.15 0.4712 114.26
373.15 0.4617 116.04
373.15 0.4193 122.38
373.15 0.3664 129.72
373.15 0.3142 135.54
373.15 0.2611 144.90
373.15 0.2089 154.76
373.15 0.1556 163.52
373.15 0.1055 173.14
373.15 0.0822 177.13
373.15 0.0623 181.01
373.15 0.0424 185.36
373.15 0.0000 192.46
423.15 1.0000 52.71
423.15 0.9798 79.21
423.15 0.9593 105.91
423.15 0.9410 132.56
423.15 0.9204 159.74
423.15 0.8728 211.99
423.15 0.8246 258.65
423.15 0.7787 297.64
423.15 0.7280 338.10
423.15 0.6771 374.24
423.15 0.6258 408.93
423.15 0.5763 432.11
423.15 0.5717 443.46
423.15 0.5252 463.89
423.15 0.5185 476.70
423.15 0.4752 494.48
423.15 0.4643 508.80
423.15 0.4238 525.54
423.15 0.3712 559.51
423.15 0.3190 591.77
423.15 0.2658 626.39
423.15 0.2133 662.39
423.15 0.1594 701.12
423.15 0.1084 739.46
423.15 0.0846 759.47
423.15 0.0642 776.76
423.15 0.0437 793.62
423.15 0.0000 818.16

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Monoethanolamine (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.1188 801.37
298.15 0.2328 821.17
298.15 0.3421 842.86
298.15 0.4472 865.97
298.15 0.5482 887.94
298.15 0.6454 912.32
298.15 0.7390 938.36
298.15 0.8291 962.65
298.15 0.9161 988.97
303.15 0.1188 796.64
303.15 0.2328 816.75
303.15 0.3421 838.57
303.15 0.4472 861.74
303.15 0.5482 883.79
303.15 0.6454 908.2
303.15 0.7390 934.25
303.15 0.8291 958.59
303.15 0.9161 984.91
308.15 0.1188 791.93
308.15 0.2328 812.34
308.15 0.3421 834.31
308.15 0.4472 857.55
308.15 0.5482 879.69
308.15 0.6454 904.13
308.15 0.7390 930.2
308.15 0.8291 954.6
308.15 0.9161 980.92
313.15 0.1188 787.14
313.15 0.2328 807.85
313.15 0.3421 829.98
313.15 0.4472 853.33
313.15 0.5482 875.55
313.15 0.6454 900.04
313.15 0.7390 926.15
313.15 0.8291 950.59
313.15 0.9161 976.92
318.15 0.1188 782.16
318.15 0.2328 803.17
318.15 0.3421 825.49
318.15 0.4472 848.95
318.15 0.5482 871.27
318.15 0.6454 895.8
318.15 0.7390 921.97
318.15 0.8291 946.45
318.15 0.9161 972.81
323.15 0.1188 777.17
323.15 0.2328 798.52
323.15 0.3421 821.03
323.15 0.4472 844.64
323.15 0.5482 867.05
323.15 0.6454 891.65
323.15 0.7390 917.86
323.15 0.8291 942.41
323.15 0.9161 968.8
298.15 1.0000 1012.53
303.15 1.0000 1008.47
308.15 1.0000 1004.49
313.15 1.0000 1000.5
318.15 1.0000 996.39
323.15 1.0000 992.41
298.15 0.0000 780.61
303.15 0.0000 775.42
308.15 0.0000 770.21
313.15 0.0000 764.92
318.15 0.0000 759.42
323.15 0.0000 753.95

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Monoethanolamine (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.1188 801.37
298.15 0.2328 821.17
298.15 0.3421 842.86
298.15 0.4472 865.97
298.15 0.5482 887.94
298.15 0.6454 912.32
298.15 0.7390 938.36
298.15 0.8291 962.65
298.15 0.9161 988.97
303.15 0.1188 796.64
303.15 0.2328 816.75
303.15 0.3421 838.57
303.15 0.4472 861.74
303.15 0.5482 883.79
303.15 0.6454 908.2
303.15 0.7390 934.25
303.15 0.8291 958.59
303.15 0.9161 984.91
308.15 0.1188 791.93
308.15 0.2328 812.34
308.15 0.3421 834.31
308.15 0.4472 857.55
308.15 0.5482 879.69
308.15 0.6454 904.13
308.15 0.7390 930.2
308.15 0.8291 954.6
308.15 0.9161 980.92
313.15 0.1188 787.14
313.15 0.2328 807.85
313.15 0.3421 829.98
313.15 0.4472 853.33
313.15 0.5482 875.55
313.15 0.6454 900.04
313.15 0.7390 926.15
313.15 0.8291 950.59
313.15 0.9161 976.92
318.15 0.1188 782.16
318.15 0.2328 803.17
318.15 0.3421 825.49
318.15 0.4472 848.95
318.15 0.5482 871.27
318.15 0.6454 895.8
318.15 0.7390 921.97
318.15 0.8291 946.45
318.15 0.9161 972.81
323.15 0.1188 777.17
323.15 0.2328 798.52
323.15 0.3421 821.03
323.15 0.4472 844.64
323.15 0.5482 867.05
323.15 0.6454 891.65
323.15 0.7390 917.86
323.15 0.8291 942.41
323.15 0.9161 968.8
298.15 1.0000 1012.53
303.15 1.0000 1008.47
308.15 1.0000 1004.49
313.15 1.0000 1000.5
318.15 1.0000 996.39
323.15 1.0000 992.41
298.15 0.0000 780.61
303.15 0.0000 775.42
308.15 0.0000 770.21
313.15 0.0000 764.92
318.15 0.0000 759.42
323.15 0.0000 753.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 94.4 (Liquid)

Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 441.45
0.0957 392.55
0.1747 378.65
0.2410 371.95
0.2975 368.05
0.3461 365.45
0.3884 363.65
0.4325 362.15
0.4879 360.55
0.5595 359.15
0.6558 357.55
0.7921 356.15
0.9105 355.25
1.0000 354.15

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 94.4 (Liquid)

Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 441.45
0.0957 392.55
0.1747 378.65
0.2410 371.95
0.2975 368.05
0.3461 365.45
0.3884 363.65
0.4325 362.15
0.4879 360.55
0.5595 359.15
0.6558 357.55
0.7921 356.15
0.9105 355.25
1.0000 354.15

Sources