Mixture of 2-Pentanol + Ethanamine, N-ethyl-

Excel

2-Pentanol

Name
2-Pentanol
InChI
InChI=1S/C5H12O/c1-3-4-5(2)6/h5-6H,3-4H2,1-2H3
InChI Key
JYVLIDXNZAXMDK-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CCCC(C)O
Mol. Weight (g/mol)
88.15
CAS
6032-29-7

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 0.0040
293.15 0.0218 0.0037
293.15 0.0810 0.0032
293.15 0.1600 0.0026
293.15 0.2399 0.0020
293.15 0.3499 0.0015
293.15 0.4400 0.0012
293.15 0.5600 0.0008
293.15 0.6501 0.0007
293.15 0.7400 0.0006
293.15 0.8497 0.0004
293.15 0.9397 0.0004
293.15 0.9811 0.0003
293.15 1.0000 0.0003
298.15 0.0000 0.0033
298.15 0.0218 0.0031
298.15 0.0810 0.0027
298.15 0.1600 0.0022
298.15 0.2399 0.0018
298.15 0.3499 0.0013
298.15 0.4400 0.0010
298.15 0.5600 0.0008
298.15 0.6501 0.0006
298.15 0.7400 0.0005
298.15 0.8497 0.0004
298.15 0.9397 0.0003
298.15 0.9811 0.0003
298.15 1.0000 0.0003
303.15 0.0000 0.0027
303.15 0.0218 0.0026
303.15 0.0810 0.0023
303.15 0.1600 0.0019
303.15 0.2399 0.0016
303.15 0.3499 0.0012
303.15 0.4400 0.0009
303.15 0.5600 0.0007
303.15 0.6501 0.0006
303.15 0.7400 0.0005
303.15 0.8497 0.0004
303.15 0.9397 0.0003
303.15 0.9811 0.0003
303.15 1.0000 0.0003
308.15 0.0000 0.0023
308.15 0.0218 0.0022
308.15 0.0810 0.0019
308.15 0.1600 0.0016
308.15 0.2399 0.0014
308.15 0.3499 0.0010
308.15 0.4400 0.0008
308.15 0.5600 0.0006
308.15 0.6501 0.0005
308.15 0.7400 0.0004
308.15 0.8497 0.0004
308.15 0.9397 0.0003
308.15 0.9811 0.0003
308.15 1.0000 0.0003
313.15 0.0000 0.0019
313.15 0.0218 0.0019
313.15 0.0810 0.0017
313.15 0.1600 0.0014
313.15 0.2399 0.0012
313.15 0.3499 0.0009
313.15 0.4400 0.0008
313.15 0.5600 0.0006
313.15 0.6501 0.0005
313.15 0.7400 0.0004
313.15 0.8497 0.0003
313.15 0.9397 0.0003
313.15 0.9811 0.0003
313.15 1.0000 0.0003
318.15 0.0000 0.0016
318.15 0.0218 0.0016
318.15 0.0810 0.0014
318.15 0.1600 0.0013
318.15 0.2399 0.0011
318.15 0.3499 0.0009
318.15 0.4400 0.0007
318.15 0.5600 0.0005
318.15 0.6501 0.0004
318.15 0.7400 0.0004
318.15 0.8497 0.0003
318.15 0.9397 0.0003
318.15 0.9811 0.0003
318.15 1.0000 0.0002
323.15 0.0000 0.0014
323.15 0.0218 0.0014
323.15 0.0810 0.0013
323.15 0.1600 0.0011
323.15 0.2399 0.0010
323.15 0.3499 0.0008
323.15 0.4400 0.0006
323.15 0.5600 0.0005
323.15 0.6501 0.0004
323.15 0.7400 0.0003
323.15 0.8497 0.0003
323.15 0.9397 0.0003
323.15 0.9811 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 0.0040
293.15 0.0218 0.0037
293.15 0.0810 0.0032
293.15 0.1600 0.0026
293.15 0.2399 0.0020
293.15 0.3499 0.0015
293.15 0.4400 0.0012
293.15 0.5600 0.0008
293.15 0.6501 0.0007
293.15 0.7400 0.0006
293.15 0.8497 0.0004
293.15 0.9397 0.0004
293.15 0.9811 0.0003
293.15 1.0000 0.0003
298.15 0.0000 0.0033
298.15 0.0218 0.0031
298.15 0.0810 0.0027
298.15 0.1600 0.0022
298.15 0.2399 0.0018
298.15 0.3499 0.0013
298.15 0.4400 0.0010
298.15 0.5600 0.0008
298.15 0.6501 0.0006
298.15 0.7400 0.0005
298.15 0.8497 0.0004
298.15 0.9397 0.0003
298.15 0.9811 0.0003
298.15 1.0000 0.0003
303.15 0.0000 0.0027
303.15 0.0218 0.0026
303.15 0.0810 0.0023
303.15 0.1600 0.0019
303.15 0.2399 0.0016
303.15 0.3499 0.0012
303.15 0.4400 0.0009
303.15 0.5600 0.0007
303.15 0.6501 0.0006
303.15 0.7400 0.0005
303.15 0.8497 0.0004
303.15 0.9397 0.0003
303.15 0.9811 0.0003
303.15 1.0000 0.0003
308.15 0.0000 0.0023
308.15 0.0218 0.0022
308.15 0.0810 0.0019
308.15 0.1600 0.0016
308.15 0.2399 0.0014
308.15 0.3499 0.0010
308.15 0.4400 0.0008
308.15 0.5600 0.0006
308.15 0.6501 0.0005
308.15 0.7400 0.0004
308.15 0.8497 0.0004
308.15 0.9397 0.0003
308.15 0.9811 0.0003
308.15 1.0000 0.0003
313.15 0.0000 0.0019
313.15 0.0218 0.0019
313.15 0.0810 0.0017
313.15 0.1600 0.0014
313.15 0.2399 0.0012
313.15 0.3499 0.0009
313.15 0.4400 0.0008
313.15 0.5600 0.0006
313.15 0.6501 0.0005
313.15 0.7400 0.0004
313.15 0.8497 0.0003
313.15 0.9397 0.0003
313.15 0.9811 0.0003
313.15 1.0000 0.0003
318.15 0.0000 0.0016
318.15 0.0218 0.0016
318.15 0.0810 0.0014
318.15 0.1600 0.0013
318.15 0.2399 0.0011
318.15 0.3499 0.0009
318.15 0.4400 0.0007
318.15 0.5600 0.0005
318.15 0.6501 0.0004
318.15 0.7400 0.0004
318.15 0.8497 0.0003
318.15 0.9397 0.0003
318.15 0.9811 0.0003
318.15 1.0000 0.0002
323.15 0.0000 0.0014
323.15 0.0218 0.0014
323.15 0.0810 0.0013
323.15 0.1600 0.0011
323.15 0.2399 0.0010
323.15 0.3499 0.0008
323.15 0.4400 0.0006
323.15 0.5600 0.0005
323.15 0.6501 0.0004
323.15 0.7400 0.0003
323.15 0.8497 0.0003
323.15 0.9397 0.0003
323.15 0.9811 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 809.3
293.15 0.0218 808.2
293.15 0.0810 805.0
293.15 0.1600 800.1
293.15 0.2399 794.4
293.15 0.3499 785.5
293.15 0.4400 777.1
293.15 0.5600 764.5
293.15 0.6501 753.9
293.15 0.7400 742.4
293.15 0.8497 727.4
293.15 0.9397 714.1
293.15 0.9811 707.7
293.15 1.0000 704.8
298.15 0.0000 805.3
298.15 0.0218 804.2
298.15 0.0810 800.9
298.15 0.1600 796.0
298.15 0.2399 790.3
298.15 0.3499 781.2
298.15 0.4400 772.6
298.15 0.5600 759.8
298.15 0.6501 749.1
298.15 0.7400 737.4
298.15 0.8497 722.2
298.15 0.9397 708.8
298.15 0.9811 702.3
298.15 1.0000 699.3
303.15 0.0000 801.2
303.15 0.0218 800.0
303.15 0.0810 796.7
303.15 0.1600 791.8
303.15 0.2399 785.9
303.15 0.3499 776.9
303.15 0.4400 768.2
303.15 0.5600 755.4
303.15 0.6501 744.4
303.15 0.7400 732.7
303.15 0.8497 717.2
303.15 0.9397 703.6
303.15 0.9811 697.0
303.15 1.0000 694.0
308.15 0.0000 797.0
308.15 0.0218 795.9
308.15 0.0810 792.5
308.15 0.1600 787.6
308.15 0.2399 781.9
308.15 0.3499 772.7
308.15 0.4400 764.0
308.15 0.5600 751.0
308.15 0.6501 739.8
308.15 0.7400 727.9
308.15 0.8497 712.1
308.15 0.9397 698.3
308.15 0.9811 691.7
308.15 1.0000 688.7
313.15 0.0000 792.7
313.15 0.0218 791.6
313.15 0.0810 788.4
313.15 0.1600 783.4
313.15 0.2399 777.6
313.15 0.3499 768.3
313.15 0.4400 759.5
313.15 0.5600 746.3
313.15 0.6501 735.0
313.15 0.7400 722.9
313.15 0.8497 707.1
313.15 0.9397 692.9
313.15 0.9811 686.4
313.15 1.0000 683.3
318.15 0.0000 788.4
318.15 0.0218 787.2
318.15 0.0810 783.8
318.15 0.1600 778.9
318.15 0.2399 773.1
318.15 0.3499 763.8
318.15 0.4400 754.9
318.15 0.5600 741.6
318.15 0.6501 730.1
318.15 0.7400 717.8
318.15 0.8497 701.6
318.15 0.9397 687.4
318.15 0.9811 680.6
318.15 1.0000 677.5
323.15 0.0000 784.0
323.15 0.0218 782.9
323.15 0.0810 779.7
323.15 0.1600 774.5
323.15 0.2399 768.4
323.15 0.3499 758.7
323.15 0.4400 749.7
323.15 0.5600 736.1
323.15 0.6501 724.6
323.15 0.7400 712.3
323.15 0.8497 696.1
323.15 0.9397 682.0
323.15 0.9811 675.2
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 809.3
293.15 0.0218 808.2
293.15 0.0810 805.0
293.15 0.1600 800.1
293.15 0.2399 794.4
293.15 0.3499 785.5
293.15 0.4400 777.1
293.15 0.5600 764.5
293.15 0.6501 753.9
293.15 0.7400 742.4
293.15 0.8497 727.4
293.15 0.9397 714.1
293.15 0.9811 707.7
293.15 1.0000 704.8
298.15 0.0000 805.3
298.15 0.0218 804.2
298.15 0.0810 800.9
298.15 0.1600 796.0
298.15 0.2399 790.3
298.15 0.3499 781.2
298.15 0.4400 772.6
298.15 0.5600 759.8
298.15 0.6501 749.1
298.15 0.7400 737.4
298.15 0.8497 722.2
298.15 0.9397 708.8
298.15 0.9811 702.3
298.15 1.0000 699.3
303.15 0.0000 801.2
303.15 0.0218 800.0
303.15 0.0810 796.7
303.15 0.1600 791.8
303.15 0.2399 785.9
303.15 0.3499 776.9
303.15 0.4400 768.2
303.15 0.5600 755.4
303.15 0.6501 744.4
303.15 0.7400 732.7
303.15 0.8497 717.2
303.15 0.9397 703.6
303.15 0.9811 697.0
303.15 1.0000 694.0
308.15 0.0000 797.0
308.15 0.0218 795.9
308.15 0.0810 792.5
308.15 0.1600 787.6
308.15 0.2399 781.9
308.15 0.3499 772.7
308.15 0.4400 764.0
308.15 0.5600 751.0
308.15 0.6501 739.8
308.15 0.7400 727.9
308.15 0.8497 712.1
308.15 0.9397 698.3
308.15 0.9811 691.7
308.15 1.0000 688.7
313.15 0.0000 792.7
313.15 0.0218 791.6
313.15 0.0810 788.4
313.15 0.1600 783.4
313.15 0.2399 777.6
313.15 0.3499 768.3
313.15 0.4400 759.5
313.15 0.5600 746.3
313.15 0.6501 735.0
313.15 0.7400 722.9
313.15 0.8497 707.1
313.15 0.9397 692.9
313.15 0.9811 686.4
313.15 1.0000 683.3
318.15 0.0000 788.4
318.15 0.0218 787.2
318.15 0.0810 783.8
318.15 0.1600 778.9
318.15 0.2399 773.1
318.15 0.3499 763.8
318.15 0.4400 754.9
318.15 0.5600 741.6
318.15 0.6501 730.1
318.15 0.7400 717.8
318.15 0.8497 701.6
318.15 0.9397 687.4
318.15 0.9811 680.6
318.15 1.0000 677.5
323.15 0.0000 784.0
323.15 0.0218 782.9
323.15 0.0810 779.7
323.15 0.1600 774.5
323.15 0.2399 768.4
323.15 0.3499 758.7
323.15 0.4400 749.7
323.15 0.5600 736.1
323.15 0.6501 724.6
323.15 0.7400 712.3
323.15 0.8497 696.1
323.15 0.9397 682.0
323.15 0.9811 675.2
323.15 1.0000 672.1

Sources