Mixture of Isopropyl Alcohol + Ethanamine, N-ethyl-

Excel

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

Ethanamine, N-ethyl-

Name
Ethanamine, N-ethyl-
InChI
InChI=1S/C4H11N/c1-3-5-4-2/h5H,3-4H2,1-2H3
InChI Key
HPNMFZURTQLUMO-UHFFFAOYSA-N
Formula
C4H11N
SMILES
CCNCC
Mol. Weight (g/mol)
73.14
CAS
109-89-7
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanamine, N-ethyl- (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0024
293.15 0.0215 0.0023
293.15 0.0807 0.0020
293.15 0.1595 0.0016
293.15 0.2401 0.0013
293.15 0.3491 0.0010
293.15 0.4399 0.0008
293.15 0.5598 0.0006
293.15 0.6501 0.0006
293.15 0.7395 0.0005
293.15 0.8496 0.0004
293.15 0.9400 0.0004
293.15 0.9863 0.0003
293.15 1.0000 0.0003
298.15 0.0000 0.0021
298.15 0.0215 0.0020
298.15 0.0807 0.0017
298.15 0.1595 0.0014
298.15 0.2401 0.0012
298.15 0.3491 0.0009
298.15 0.4399 0.0008
298.15 0.5598 0.0006
298.15 0.6501 0.0005
298.15 0.7395 0.0004
298.15 0.8496 0.0004
298.15 0.9400 0.0003
298.15 0.9863 0.0003
298.15 1.0000 0.0003
303.15 0.0000 0.0018
303.15 0.0215 0.0017
303.15 0.0807 0.0015
303.15 0.1595 0.0013
303.15 0.2401 0.0010
303.15 0.3491 0.0008
303.15 0.4399 0.0007
303.15 0.5598 0.0005
303.15 0.6501 0.0005
303.15 0.7395 0.0004
303.15 0.8496 0.0003
303.15 0.9400 0.0003
303.15 0.9863 0.0003
303.15 1.0000 0.0003
308.15 0.0000 0.0016
308.15 0.0215 0.0015
308.15 0.0807 0.0013
308.15 0.1595 0.0011
308.15 0.2401 0.0009
308.15 0.3491 0.0007
308.15 0.4399 0.0006
308.15 0.5598 0.0005
308.15 0.6501 0.0004
308.15 0.7395 0.0004
308.15 0.8496 0.0003
308.15 0.9400 0.0003
308.15 0.9863 0.0003
308.15 1.0000 0.0003
313.15 0.0000 0.0014
313.15 0.0215 0.0013
313.15 0.0807 0.0012
313.15 0.1595 0.0010
313.15 0.2401 0.0008
313.15 0.3491 0.0006
313.15 0.4399 0.0005
313.15 0.5598 0.0004
313.15 0.6501 0.0004
313.15 0.7395 0.0003
313.15 0.8496 0.0003
313.15 0.9400 0.0003
313.15 0.9863 0.0003
313.15 1.0000 0.0003
318.15 0.0000 0.0012
318.15 0.0215 0.0011
318.15 0.0807 0.0010
318.15 0.1595 0.0009
318.15 0.2401 0.0007
318.15 0.3491 0.0006
318.15 0.4399 0.0005
318.15 0.5598 0.0004
318.15 0.6501 0.0003
318.15 0.7395 0.0003
318.15 0.8496 0.0003
318.15 0.9400 0.0003
318.15 0.9863 0.0003
318.15 1.0000 0.0002
323.15 0.0000 0.0010
323.15 0.0215 0.0010
323.15 0.0807 0.0009
323.15 0.1595 0.0008
323.15 0.2401 0.0007
323.15 0.3491 0.0005
323.15 0.4399 0.0005
323.15 0.5598 0.0004
323.15 0.6501 0.0003
323.15 0.7395 0.0003
323.15 0.8496 0.0003
323.15 0.9400 0.0002
323.15 0.9863 0.0002
323.15 1.0000 0.0002

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanamine, N-ethyl- (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0024
293.15 0.0215 0.0023
293.15 0.0807 0.0020
293.15 0.1595 0.0016
293.15 0.2401 0.0013
293.15 0.3491 0.0010
293.15 0.4399 0.0008
293.15 0.5598 0.0006
293.15 0.6501 0.0006
293.15 0.7395 0.0005
293.15 0.8496 0.0004
293.15 0.9400 0.0004
293.15 0.9863 0.0003
293.15 1.0000 0.0003
298.15 0.0000 0.0021
298.15 0.0215 0.0020
298.15 0.0807 0.0017
298.15 0.1595 0.0014
298.15 0.2401 0.0012
298.15 0.3491 0.0009
298.15 0.4399 0.0008
298.15 0.5598 0.0006
298.15 0.6501 0.0005
298.15 0.7395 0.0004
298.15 0.8496 0.0004
298.15 0.9400 0.0003
298.15 0.9863 0.0003
298.15 1.0000 0.0003
303.15 0.0000 0.0018
303.15 0.0215 0.0017
303.15 0.0807 0.0015
303.15 0.1595 0.0013
303.15 0.2401 0.0010
303.15 0.3491 0.0008
303.15 0.4399 0.0007
303.15 0.5598 0.0005
303.15 0.6501 0.0005
303.15 0.7395 0.0004
303.15 0.8496 0.0003
303.15 0.9400 0.0003
303.15 0.9863 0.0003
303.15 1.0000 0.0003
308.15 0.0000 0.0016
308.15 0.0215 0.0015
308.15 0.0807 0.0013
308.15 0.1595 0.0011
308.15 0.2401 0.0009
308.15 0.3491 0.0007
308.15 0.4399 0.0006
308.15 0.5598 0.0005
308.15 0.6501 0.0004
308.15 0.7395 0.0004
308.15 0.8496 0.0003
308.15 0.9400 0.0003
308.15 0.9863 0.0003
308.15 1.0000 0.0003
313.15 0.0000 0.0014
313.15 0.0215 0.0013
313.15 0.0807 0.0012
313.15 0.1595 0.0010
313.15 0.2401 0.0008
313.15 0.3491 0.0006
313.15 0.4399 0.0005
313.15 0.5598 0.0004
313.15 0.6501 0.0004
313.15 0.7395 0.0003
313.15 0.8496 0.0003
313.15 0.9400 0.0003
313.15 0.9863 0.0003
313.15 1.0000 0.0003
318.15 0.0000 0.0012
318.15 0.0215 0.0011
318.15 0.0807 0.0010
318.15 0.1595 0.0009
318.15 0.2401 0.0007
318.15 0.3491 0.0006
318.15 0.4399 0.0005
318.15 0.5598 0.0004
318.15 0.6501 0.0003
318.15 0.7395 0.0003
318.15 0.8496 0.0003
318.15 0.9400 0.0003
318.15 0.9863 0.0003
318.15 1.0000 0.0002
323.15 0.0000 0.0010
323.15 0.0215 0.0010
323.15 0.0807 0.0009
323.15 0.1595 0.0008
323.15 0.2401 0.0007
323.15 0.3491 0.0005
323.15 0.4399 0.0005
323.15 0.5598 0.0004
323.15 0.6501 0.0003
323.15 0.7395 0.0003
323.15 0.8496 0.0003
323.15 0.9400 0.0002
323.15 0.9863 0.0002
323.15 1.0000 0.0002

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanamine, N-ethyl- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 785.4
293.15 0.0215 784.4
293.15 0.0807 781.4
293.15 0.1595 776.8
293.15 0.2401 771.8
293.15 0.3491 764.0
293.15 0.4399 756.9
293.15 0.5598 746.9
293.15 0.6501 738.9
293.15 0.7395 730.5
293.15 0.8496 719.9
293.15 0.9400 710.9
293.15 0.9863 706.2
293.15 1.0000 704.8
298.15 0.0000 781.1
298.15 0.0215 780.1
298.15 0.0807 777.3
298.15 0.1595 772.7
298.15 0.2401 767.4
298.15 0.3491 759.6
298.15 0.4399 752.3
298.15 0.5598 742.1
298.15 0.6501 733.9
298.15 0.7395 725.5
298.15 0.8496 714.7
298.15 0.9400 705.5
298.15 0.9863 700.7
298.15 1.0000 699.3
303.15 0.0000 776.8
303.15 0.0215 775.8
303.15 0.0807 773.0
303.15 0.1595 768.4
303.15 0.2401 763.0
303.15 0.3491 755.1
303.15 0.4399 747.7
303.15 0.5598 737.4
303.15 0.6501 729.0
303.15 0.7395 720.4
303.15 0.8496 709.4
303.15 0.9400 700.3
303.15 0.9863 695.4
303.15 1.0000 694.0
308.15 0.0000 772.4
308.15 0.0215 771.4
308.15 0.0807 768.5
308.15 0.1595 764.1
308.15 0.2401 758.7
308.15 0.3491 750.8
308.15 0.4399 743.5
308.15 0.5598 733.0
308.15 0.6501 724.5
308.15 0.7395 715.8
308.15 0.8496 704.6
308.15 0.9400 695.2
308.15 0.9863 690.2
308.15 1.0000 688.7
313.15 0.0000 768.0
313.15 0.0215 767.0
313.15 0.0807 764.0
313.15 0.1595 759.5
313.15 0.2401 754.3
313.15 0.3491 746.3
313.15 0.4399 738.8
313.15 0.5598 728.3
313.15 0.6501 719.7
313.15 0.7395 710.7
313.15 0.8496 699.3
313.15 0.9400 689.7
313.15 0.9863 684.8
313.15 1.0000 683.3
318.15 0.0000 763.4
318.15 0.0215 762.4
318.15 0.0807 759.5
318.15 0.1595 754.8
318.15 0.2401 749.5
318.15 0.3491 741.4
318.15 0.4399 733.9
318.15 0.5598 723.2
318.15 0.6501 714.4
318.15 0.7395 705.4
318.15 0.8496 693.9
318.15 0.9400 684.1
318.15 0.9863 679.0
318.15 1.0000 677.5
323.15 0.0000 758.8
323.15 0.0215 757.8
323.15 0.0807 754.8
323.15 0.1595 750.2
323.15 0.2401 744.9
323.15 0.3491 736.8
323.15 0.4399 729.2
323.15 0.5598 718.3
323.15 0.6501 709.4
323.15 0.7395 700.3
323.15 0.8496 688.7
323.15 0.9400 678.8
323.15 0.9863 673.6
323.15 1.0000 672.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanamine, N-ethyl- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 785.4
293.15 0.0215 784.4
293.15 0.0807 781.4
293.15 0.1595 776.8
293.15 0.2401 771.8
293.15 0.3491 764.0
293.15 0.4399 756.9
293.15 0.5598 746.9
293.15 0.6501 738.9
293.15 0.7395 730.5
293.15 0.8496 719.9
293.15 0.9400 710.9
293.15 0.9863 706.2
293.15 1.0000 704.8
298.15 0.0000 781.1
298.15 0.0215 780.1
298.15 0.0807 777.3
298.15 0.1595 772.7
298.15 0.2401 767.4
298.15 0.3491 759.6
298.15 0.4399 752.3
298.15 0.5598 742.1
298.15 0.6501 733.9
298.15 0.7395 725.5
298.15 0.8496 714.7
298.15 0.9400 705.5
298.15 0.9863 700.7
298.15 1.0000 699.3
303.15 0.0000 776.8
303.15 0.0215 775.8
303.15 0.0807 773.0
303.15 0.1595 768.4
303.15 0.2401 763.0
303.15 0.3491 755.1
303.15 0.4399 747.7
303.15 0.5598 737.4
303.15 0.6501 729.0
303.15 0.7395 720.4
303.15 0.8496 709.4
303.15 0.9400 700.3
303.15 0.9863 695.4
303.15 1.0000 694.0
308.15 0.0000 772.4
308.15 0.0215 771.4
308.15 0.0807 768.5
308.15 0.1595 764.1
308.15 0.2401 758.7
308.15 0.3491 750.8
308.15 0.4399 743.5
308.15 0.5598 733.0
308.15 0.6501 724.5
308.15 0.7395 715.8
308.15 0.8496 704.6
308.15 0.9400 695.2
308.15 0.9863 690.2
308.15 1.0000 688.7
313.15 0.0000 768.0
313.15 0.0215 767.0
313.15 0.0807 764.0
313.15 0.1595 759.5
313.15 0.2401 754.3
313.15 0.3491 746.3
313.15 0.4399 738.8
313.15 0.5598 728.3
313.15 0.6501 719.7
313.15 0.7395 710.7
313.15 0.8496 699.3
313.15 0.9400 689.7
313.15 0.9863 684.8
313.15 1.0000 683.3
318.15 0.0000 763.4
318.15 0.0215 762.4
318.15 0.0807 759.5
318.15 0.1595 754.8
318.15 0.2401 749.5
318.15 0.3491 741.4
318.15 0.4399 733.9
318.15 0.5598 723.2
318.15 0.6501 714.4
318.15 0.7395 705.4
318.15 0.8496 693.9
318.15 0.9400 684.1
318.15 0.9863 679.0
318.15 1.0000 677.5
323.15 0.0000 758.8
323.15 0.0215 757.8
323.15 0.0807 754.8
323.15 0.1595 750.2
323.15 0.2401 744.9
323.15 0.3491 736.8
323.15 0.4399 729.2
323.15 0.5598 718.3
323.15 0.6501 709.4
323.15 0.7395 700.3
323.15 0.8496 688.7
323.15 0.9400 678.8
323.15 0.9863 673.6
323.15 1.0000 672.1

Sources