Mixture of Hexane, 2,4-dimethyl- + 4,7-Methano-1H-indene, octahydro-

Hexane, 2,4-dimethyl-

Name
Hexane, 2,4-dimethyl-
InChI
InChI=1S/C8H18/c1-5-8(4)6-7(2)3/h7-8H,5-6H2,1-4H3
InChI Key
HDGQICNBXPAKLR-UHFFFAOYSA-N
Formula
C8H18
SMILES
CCC(C)CC(C)C
Mol. Weight (g/mol)
114.23
CAS
589-43-5

4,7-Methano-1H-indene, octahydro-

Name
4,7-Methano-1H-indene, octahydro-
InChI
InChI=1S/C10H16/c1-2-9-7-4-5-8(6-7)10(9)3-1/h7-10H,1-6H2
InChI Key
LPSXSORODABQKT-UHFFFAOYSA-N
Formula
C10H16
SMILES
C1CC2C3CCC(C3)C2C1
Mol. Weight (g/mol)
136.23
CAS
6004-38-2
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. n0 - Refractive index (Na D-line) (2)
  3. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0005
293.15 0.1017 0.0005
293.15 0.2008 0.0006
293.15 0.3005 0.0007
293.15 0.4002 0.0008
293.15 0.5006 0.0010
293.15 0.6001 0.0012
293.15 0.7001 0.0015
293.15 0.8012 0.0018
293.15 0.8999 0.0023
293.15 1.0000 0.0030
298.15 0.0000 0.0005
298.15 0.1017 0.0005
298.15 0.2008 0.0006
298.15 0.3005 0.0007
298.15 0.4002 0.0008
298.15 0.5006 0.0009
298.15 0.6001 0.0011
298.15 0.7001 0.0014
298.15 0.8012 0.0017
298.15 0.8999 0.0021
298.15 1.0000 0.0027
303.15 0.0000 0.0004
303.15 0.1017 0.0005
303.15 0.2008 0.0006
303.15 0.3005 0.0006
303.15 0.4002 0.0007
303.15 0.5006 0.0009
303.15 0.6001 0.0010
303.15 0.7001 0.0013
303.15 0.8012 0.0016
303.15 0.8999 0.0019
303.15 1.0000 0.0025
308.15 0.0000 0.0004
308.15 0.1017 0.0005
308.15 0.2008 0.0005
308.15 0.3005 0.0006
308.15 0.4002 0.0007
308.15 0.5006 0.0008
308.15 0.6001 0.0010
308.15 0.7001 0.0012
308.15 0.8012 0.0014
308.15 0.8999 0.0018
308.15 1.0000 0.0022
313.15 0.0000 0.0004
313.15 0.1017 0.0004
313.15 0.2008 0.0005
313.15 0.3005 0.0006
313.15 0.4002 0.0007
313.15 0.5006 0.0008
313.15 0.6001 0.0009
313.15 0.7001 0.0011
313.15 0.8012 0.0013
313.15 0.8999 0.0016
313.15 1.0000 0.0021

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0005
293.15 0.1017 0.0005
293.15 0.2008 0.0006
293.15 0.3005 0.0007
293.15 0.4002 0.0008
293.15 0.5006 0.0010
293.15 0.6001 0.0012
293.15 0.7001 0.0015
293.15 0.8012 0.0018
293.15 0.8999 0.0023
293.15 1.0000 0.0030
298.15 0.0000 0.0005
298.15 0.1017 0.0005
298.15 0.2008 0.0006
298.15 0.3005 0.0007
298.15 0.4002 0.0008
298.15 0.5006 0.0009
298.15 0.6001 0.0011
298.15 0.7001 0.0014
298.15 0.8012 0.0017
298.15 0.8999 0.0021
298.15 1.0000 0.0027
303.15 0.0000 0.0004
303.15 0.1017 0.0005
303.15 0.2008 0.0006
303.15 0.3005 0.0006
303.15 0.4002 0.0007
303.15 0.5006 0.0009
303.15 0.6001 0.0010
303.15 0.7001 0.0013
303.15 0.8012 0.0016
303.15 0.8999 0.0019
303.15 1.0000 0.0025
308.15 0.0000 0.0004
308.15 0.1017 0.0005
308.15 0.2008 0.0005
308.15 0.3005 0.0006
308.15 0.4002 0.0007
308.15 0.5006 0.0008
308.15 0.6001 0.0010
308.15 0.7001 0.0012
308.15 0.8012 0.0014
308.15 0.8999 0.0018
308.15 1.0000 0.0022
313.15 0.0000 0.0004
313.15 0.1017 0.0004
313.15 0.2008 0.0005
313.15 0.3005 0.0006
313.15 0.4002 0.0007
313.15 0.5006 0.0008
313.15 0.6001 0.0009
313.15 0.7001 0.0011
313.15 0.8012 0.0013
313.15 0.8999 0.0016
313.15 1.0000 0.0021

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid Refractive index (Na D-line) - Liquid
293.15 0.0000 1.3947
293.15 0.1017 1.4042
293.15 0.2008 1.4134
293.15 0.3005 1.4228
293.15 0.4002 1.432
293.15 0.5006 1.4414
293.15 0.6001 1.4504
293.15 0.7001 1.4596
293.15 0.8012 1.4688
293.15 0.8999 1.4779
293.15 1.0000 1.4871
298.15 0.0000 1.3926
298.15 0.1017 1.4022
298.15 0.2008 1.4114
298.15 0.3005 1.4207
298.15 0.4002 1.43
298.15 0.5006 1.4395
298.15 0.6001 1.4486
298.15 0.7001 1.4577
298.15 0.8012 1.467
298.15 0.8999 1.4761
298.15 1.0000 1.4853
303.15 0.0000 1.3898
303.15 0.1017 1.3993
303.15 0.2008 1.4087
303.15 0.3005 1.4183
303.15 0.4002 1.428
303.15 0.5006 1.4376
303.15 0.6001 1.4467
303.15 0.7001 1.4554
303.15 0.8012 1.4648
303.15 0.8999 1.474
303.15 1.0000 1.4833
308.15 0.0000 1.3881
308.15 0.1017 1.3976
308.15 0.2008 1.4071
308.15 0.3005 1.4172
308.15 0.4002 1.427
308.15 0.5006 1.436
308.15 0.6001 1.4449
308.15 0.7001 1.4538
308.15 0.8012 1.463
308.15 0.8999 1.4718
308.15 1.0000 1.4802
313.15 0.0000 1.3858
313.15 0.1017 1.3954
313.15 0.2008 1.4048
313.15 0.3005 1.415
313.15 0.4002 1.4245
313.15 0.5006 1.4337
313.15 0.6001 1.4426
313.15 0.7001 1.4514
313.15 0.8012 1.4603
313.15 0.8999 1.4688
313.15 1.0000 1.4773

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid Refractive index (Na D-line) - Liquid
293.15 0.0000 1.3947
293.15 0.1017 1.4042
293.15 0.2008 1.4134
293.15 0.3005 1.4228
293.15 0.4002 1.432
293.15 0.5006 1.4414
293.15 0.6001 1.4504
293.15 0.7001 1.4596
293.15 0.8012 1.4688
293.15 0.8999 1.4779
293.15 1.0000 1.4871
298.15 0.0000 1.3926
298.15 0.1017 1.4022
298.15 0.2008 1.4114
298.15 0.3005 1.4207
298.15 0.4002 1.43
298.15 0.5006 1.4395
298.15 0.6001 1.4486
298.15 0.7001 1.4577
298.15 0.8012 1.467
298.15 0.8999 1.4761
298.15 1.0000 1.4853
303.15 0.0000 1.3898
303.15 0.1017 1.3993
303.15 0.2008 1.4087
303.15 0.3005 1.4183
303.15 0.4002 1.428
303.15 0.5006 1.4376
303.15 0.6001 1.4467
303.15 0.7001 1.4554
303.15 0.8012 1.4648
303.15 0.8999 1.474
303.15 1.0000 1.4833
308.15 0.0000 1.3881
308.15 0.1017 1.3976
308.15 0.2008 1.4071
308.15 0.3005 1.4172
308.15 0.4002 1.427
308.15 0.5006 1.436
308.15 0.6001 1.4449
308.15 0.7001 1.4538
308.15 0.8012 1.463
308.15 0.8999 1.4718
308.15 1.0000 1.4802
313.15 0.0000 1.3858
313.15 0.1017 1.3954
313.15 0.2008 1.4048
313.15 0.3005 1.415
313.15 0.4002 1.4245
313.15 0.5006 1.4337
313.15 0.6001 1.4426
313.15 0.7001 1.4514
313.15 0.8012 1.4603
313.15 0.8999 1.4688
313.15 1.0000 1.4773

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 700.57
293.15 0.1017 723.35
293.15 0.2008 745.85
293.15 0.3005 768.89
293.15 0.4002 792.17
293.15 0.5006 815.78
293.15 0.6001 839.18
293.15 0.7001 862.85
293.15 0.8012 887.35
293.15 0.8999 911.32
293.15 1.0000 935.66
298.15 0.0000 696.43
298.15 0.1017 719.24
298.15 0.2008 741.75
298.15 0.3005 764.81
298.15 0.4002 788.11
298.15 0.5006 811.8
298.15 0.6001 835.17
298.15 0.7001 858.86
298.15 0.8012 883.39
298.15 0.8999 907.4
298.15 1.0000 931.79
303.15 0.0000 692.26
303.15 0.1017 715.09
303.15 0.2008 737.62
303.15 0.3005 760.7
303.15 0.4002 784.02
303.15 0.5006 807.73
303.15 0.6001 831.13
303.15 0.7001 854.86
303.15 0.8012 879.42
303.15 0.8999 903.45
303.15 1.0000 927.88
308.15 0.0000 688.06
308.15 0.1017 710.92
308.15 0.2008 733.48
308.15 0.3005 756.58
308.15 0.4002 779.93
308.15 0.5006 803.67
308.15 0.6001 827.09
308.15 0.7001 850.84
308.15 0.8012 875.43
308.15 0.8999 899.5
308.15 1.0000 923.97
313.15 0.0000 683.85
313.15 0.1017 706.73
313.15 0.2008 729.31
313.15 0.3005 752.44
313.15 0.4002 775.81
313.15 0.5006 799.53
313.15 0.6001 823.03
313.15 0.7001 846.81
313.15 0.8012 871.44
313.15 0.8999 895.54
313.15 1.0000 920.05

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 700.57
293.15 0.1017 723.35
293.15 0.2008 745.85
293.15 0.3005 768.89
293.15 0.4002 792.17
293.15 0.5006 815.78
293.15 0.6001 839.18
293.15 0.7001 862.85
293.15 0.8012 887.35
293.15 0.8999 911.32
293.15 1.0000 935.66
298.15 0.0000 696.43
298.15 0.1017 719.24
298.15 0.2008 741.75
298.15 0.3005 764.81
298.15 0.4002 788.11
298.15 0.5006 811.8
298.15 0.6001 835.17
298.15 0.7001 858.86
298.15 0.8012 883.39
298.15 0.8999 907.4
298.15 1.0000 931.79
303.15 0.0000 692.26
303.15 0.1017 715.09
303.15 0.2008 737.62
303.15 0.3005 760.7
303.15 0.4002 784.02
303.15 0.5006 807.73
303.15 0.6001 831.13
303.15 0.7001 854.86
303.15 0.8012 879.42
303.15 0.8999 903.45
303.15 1.0000 927.88
308.15 0.0000 688.06
308.15 0.1017 710.92
308.15 0.2008 733.48
308.15 0.3005 756.58
308.15 0.4002 779.93
308.15 0.5006 803.67
308.15 0.6001 827.09
308.15 0.7001 850.84
308.15 0.8012 875.43
308.15 0.8999 899.5
308.15 1.0000 923.97
313.15 0.0000 683.85
313.15 0.1017 706.73
313.15 0.2008 729.31
313.15 0.3005 752.44
313.15 0.4002 775.81
313.15 0.5006 799.53
313.15 0.6001 823.03
313.15 0.7001 846.81
313.15 0.8012 871.44
313.15 0.8999 895.54
313.15 1.0000 920.05

Sources

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