Mixture of Propane, 2-methoxy-2-methyl- + Heptane

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Propane, 2-methoxy-2-methyl-

Name
Propane, 2-methoxy-2-methyl-
InChI
InChI=1S/C5H12O/c1-5(2,3)6-4/h1-4H3
InChI Key
BZLVMXJERCGZMT-UHFFFAOYSA-N
Formula
C5H12O
SMILES
COC(C)(C)C
Mol. Weight (g/mol)
88.15
CAS
1634-04-4

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. ν - Kinematic viscosity, m2/s (2)
  4. Pc - Critical pressure, kPa (2)
  5. ρl - Mass density, kg/m3 (2)
  6. Tc - Critical temperature, K (2)

Mole fraction of Propane, 2-methoxy-2-methyl- (1) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Gas
0.0198 0.1038
0.0497 0.2232
0.0756 0.3096
0.1007 0.3814
0.1492 0.4858
0.1993 0.5793
0.2509 0.6251
0.3002 0.6930
0.3492 0.7310
0.3986 0.7747
0.4500 0.8081
0.4989 0.8324
0.5487 0.8563
0.5992 0.8747
0.6499 0.8976
0.6998 0.9169
0.7476 0.9303
0.7988 0.9470
0.8493 0.9565
0.8997 0.9723
0.9221 0.9795
0.9481 0.9864
0.9782 0.9945

Mole fraction of Propane, 2-methoxy-2-methyl- (1) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Gas
0.0198 0.1038
0.0497 0.2232
0.0756 0.3096
0.1007 0.3814
0.1492 0.4858
0.1993 0.5793
0.2509 0.6251
0.3002 0.6930
0.3492 0.7310
0.3986 0.7747
0.4500 0.8081
0.4989 0.8324
0.5487 0.8563
0.5992 0.8747
0.6499 0.8976
0.6998 0.9169
0.7476 0.9303
0.7988 0.9470
0.8493 0.9565
0.8997 0.9723
0.9221 0.9795
0.9481 0.9864
0.9782 0.9945

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Viscosity, Pa*s - Liquid
273.15 0.1004 0.0005
273.15 0.1998 0.0005
273.15 0.3008 0.0005
273.15 0.4024 0.0005
273.15 0.5007 0.0005
273.15 0.5989 0.0005
273.15 0.6981 0.0005
273.15 0.7887 0.0005
273.15 0.8980 0.0004
278.15 0.1004 0.0005
278.15 0.1998 0.0005
278.15 0.3008 0.0005
278.15 0.4024 0.0005
278.15 0.5007 0.0004
278.15 0.5989 0.0004
278.15 0.6981 0.0004
278.15 0.7887 0.0004
278.15 0.8980 0.0004
283.15 0.1004 0.0005
283.15 0.1998 0.0004
283.15 0.3008 0.0004
283.15 0.4024 0.0004
283.15 0.5007 0.0004
283.15 0.5989 0.0004
283.15 0.6981 0.0004
283.15 0.7887 0.0004
283.15 0.8980 0.0004
288.15 0.1004 0.0004
288.15 0.1998 0.0004
288.15 0.3008 0.0004
288.15 0.4024 0.0004
288.15 0.5007 0.0004
288.15 0.5989 0.0004
288.15 0.6981 0.0004
288.15 0.7887 0.0004
288.15 0.8980 0.0004
293.15 0.1004 0.0004
293.15 0.1998 0.0004
293.15 0.3008 0.0004
293.15 0.4024 0.0004
293.15 0.5007 0.0004
293.15 0.5989 0.0004
293.15 0.6981 0.0004
293.15 0.7887 0.0004
298.15 0.1004 0.0004
298.15 0.1998 0.0004
298.15 0.3008 0.0004
298.15 0.4024 0.0004
298.15 0.5007 0.0004
303.15 0.1004 0.0004
303.15 0.1998 0.0004
303.15 0.3008 0.0004
303.15 0.4024 0.0003
308.15 0.1004 0.0003
308.15 0.1998 0.0003
313.15 0.1004 0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Viscosity, Pa*s - Liquid
273.15 0.1004 0.0005
273.15 0.1998 0.0005
273.15 0.3008 0.0005
273.15 0.4024 0.0005
273.15 0.5007 0.0005
273.15 0.5989 0.0005
273.15 0.6981 0.0005
273.15 0.7887 0.0005
273.15 0.8980 0.0004
278.15 0.1004 0.0005
278.15 0.1998 0.0005
278.15 0.3008 0.0005
278.15 0.4024 0.0005
278.15 0.5007 0.0004
278.15 0.5989 0.0004
278.15 0.6981 0.0004
278.15 0.7887 0.0004
278.15 0.8980 0.0004
283.15 0.1004 0.0005
283.15 0.1998 0.0004
283.15 0.3008 0.0004
283.15 0.4024 0.0004
283.15 0.5007 0.0004
283.15 0.5989 0.0004
283.15 0.6981 0.0004
283.15 0.7887 0.0004
283.15 0.8980 0.0004
288.15 0.1004 0.0004
288.15 0.1998 0.0004
288.15 0.3008 0.0004
288.15 0.4024 0.0004
288.15 0.5007 0.0004
288.15 0.5989 0.0004
288.15 0.6981 0.0004
288.15 0.7887 0.0004
288.15 0.8980 0.0004
293.15 0.1004 0.0004
293.15 0.1998 0.0004
293.15 0.3008 0.0004
293.15 0.4024 0.0004
293.15 0.5007 0.0004
293.15 0.5989 0.0004
293.15 0.6981 0.0004
293.15 0.7887 0.0004
298.15 0.1004 0.0004
298.15 0.1998 0.0004
298.15 0.3008 0.0004
298.15 0.4024 0.0004
298.15 0.5007 0.0004
303.15 0.1004 0.0004
303.15 0.1998 0.0004
303.15 0.3008 0.0004
303.15 0.4024 0.0003
308.15 0.1004 0.0003
308.15 0.1998 0.0003
313.15 0.1004 0.0003

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0431 6.6060e-07
283.15 0.0987 6.5120e-07
283.15 0.1892 6.3530e-07
283.15 0.2958 6.1680e-07
283.15 0.3844 6.0300e-07
283.15 0.4986 5.8450e-07
283.15 0.6007 5.7000e-07
283.15 0.6999 5.5670e-07
283.15 0.7998 5.4210e-07
283.15 0.8997 5.2980e-07
283.15 0.9499 5.2410e-07
298.15 0.0431 5.6830e-07
298.15 0.0987 5.5990e-07
298.15 0.1892 5.4610e-07
298.15 0.2958 5.3000e-07
298.15 0.3844 5.1690e-07
298.15 0.4986 5.0120e-07
298.15 0.6007 4.8810e-07
298.15 0.6999 4.7770e-07
298.15 0.7998 4.6800e-07
298.15 0.8997 4.6040e-07
298.15 0.9499 4.5660e-07
313.15 0.0431 4.9260e-07
313.15 0.0987 4.8620e-07
313.15 0.1892 4.7670e-07
313.15 0.2958 4.6580e-07
313.15 0.3844 4.5690e-07
313.15 0.4986 4.4540e-07
313.15 0.6007 4.3470e-07
313.15 0.6999 4.2460e-07
313.15 0.7998 4.1440e-07
313.15 0.8997 4.0470e-07
313.15 0.9499 4.0040e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0431 6.6060e-07
283.15 0.0987 6.5120e-07
283.15 0.1892 6.3530e-07
283.15 0.2958 6.1680e-07
283.15 0.3844 6.0300e-07
283.15 0.4986 5.8450e-07
283.15 0.6007 5.7000e-07
283.15 0.6999 5.5670e-07
283.15 0.7998 5.4210e-07
283.15 0.8997 5.2980e-07
283.15 0.9499 5.2410e-07
298.15 0.0431 5.6830e-07
298.15 0.0987 5.5990e-07
298.15 0.1892 5.4610e-07
298.15 0.2958 5.3000e-07
298.15 0.3844 5.1690e-07
298.15 0.4986 5.0120e-07
298.15 0.6007 4.8810e-07
298.15 0.6999 4.7770e-07
298.15 0.7998 4.6800e-07
298.15 0.8997 4.6040e-07
298.15 0.9499 4.5660e-07
313.15 0.0431 4.9260e-07
313.15 0.0987 4.8620e-07
313.15 0.1892 4.7670e-07
313.15 0.2958 4.6580e-07
313.15 0.3844 4.5690e-07
313.15 0.4986 4.4540e-07
313.15 0.6007 4.3470e-07
313.15 0.6999 4.2460e-07
313.15 0.7998 4.1440e-07
313.15 0.8997 4.0470e-07
313.15 0.9499 4.0040e-07

Critical pressure, kPa [ref]

Mole fraction of Heptane (2) - Liquid Critical pressure, kPa - Liquid
0.0000 3448.00
0.1000 3417.00
0.2011 3375.00
0.3056 3310.00
0.3978 3267.00
0.4970 3188.00
0.5996 3105.00
0.6933 3043.00
0.8001 2969.00
0.8984 2894.00
1.0000 2761.00

Critical pressure, kPa [ref]

Mole fraction of Heptane (2) - Liquid Critical pressure, kPa - Liquid
0.0000 3448.00
0.1000 3417.00
0.2011 3375.00
0.3056 3310.00
0.3978 3267.00
0.4970 3188.00
0.5996 3105.00
0.6933 3043.00
0.8001 2969.00
0.8984 2894.00
1.0000 2761.00

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 1000 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Mass density, kg/m3 - Liquid
273.15 0.1042 705.19
273.15 0.2146 710.4
273.15 0.3024 714.67
273.15 0.3982 719.73
273.15 0.4996 725.44
273.15 0.5875 730.85
273.15 0.6985 738.08
273.15 0.7940 744.8
273.15 0.8890 752.0
278.15 0.1042 700.96
278.15 0.2146 706.09
278.15 0.3024 710.3
278.15 0.3982 715.27
278.15 0.4996 720.9
278.15 0.5875 726.22
278.15 0.6985 733.34
278.15 0.7940 739.96
278.15 0.8890 747.05
283.15 0.1042 696.72
283.15 0.2146 701.76
283.15 0.3024 705.9
283.15 0.3982 710.79
283.15 0.4996 716.32
283.15 0.5875 721.55
283.15 0.6985 728.56
283.15 0.7940 735.08
283.15 0.8890 742.07
288.15 0.1042 692.45
288.15 0.2146 697.4
288.15 0.3024 701.47
288.15 0.3982 706.28
288.15 0.4996 711.72
288.15 0.5875 716.86
288.15 0.6985 723.76
288.15 0.7940 730.17
288.15 0.8890 737.04
293.15 0.1042 688.15
293.15 0.2146 693.02
293.15 0.3024 697.02
293.15 0.3982 701.73
293.15 0.4996 707.09
293.15 0.5875 712.13
293.15 0.6985 718.92
293.15 0.7940 725.22
293.15 0.8890 731.98
298.15 0.1042 683.83
298.15 0.2146 688.62
298.15 0.3024 692.54
298.15 0.3982 697.16
298.15 0.4996 702.42
298.15 0.5875 707.37
298.15 0.6985 714.04
298.15 0.7940 720.23
298.15 0.8890 726.87
303.15 0.1042 679.49
303.15 0.2146 684.18
303.15 0.3024 688.02
303.15 0.3982 692.55
303.15 0.4996 697.72
303.15 0.5875 702.57
303.15 0.6985 709.11
303.15 0.7940 715.19
303.15 0.8890 721.72
308.15 0.1042 675.12
308.15 0.2146 679.71
308.15 0.3024 683.48
308.15 0.3982 687.91
308.15 0.4996 692.98
308.15 0.5875 697.73
308.15 0.6985 704.14
308.15 0.7940 710.11
313.15 0.1042 670.71
313.15 0.2146 675.19
313.15 0.3024 678.89
313.15 0.3982 683.23
313.15 0.4996 688.2
313.15 0.5875 692.85
313.15 0.6985 699.12
318.15 0.1042 666.28
318.15 0.2146 670.65
318.15 0.3024 674.26
318.15 0.3982 678.51
318.15 0.4996 683.38
318.15 0.5875 687.92
323.15 0.1042 661.8
323.15 0.2146 666.08
323.15 0.3024 669.6
323.15 0.3982 673.75
323.15 0.4996 678.5
328.15 0.1042 657.27
328.15 0.2146 661.46
328.15 0.3024 664.89
328.15 0.3982 668.93
333.15 0.1042 652.74
333.15 0.2146 656.77
333.15 0.3024 660.13
338.16 0.1042 648.13
338.16 0.2146 652.07
343.16 0.1042 643.27

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 1000 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Mass density, kg/m3 - Liquid
273.15 0.1042 705.19
273.15 0.2146 710.4
273.15 0.3024 714.67
273.15 0.3982 719.73
273.15 0.4996 725.44
273.15 0.5875 730.85
273.15 0.6985 738.08
273.15 0.7940 744.8
273.15 0.8890 752.0
278.15 0.1042 700.96
278.15 0.2146 706.09
278.15 0.3024 710.3
278.15 0.3982 715.27
278.15 0.4996 720.9
278.15 0.5875 726.22
278.15 0.6985 733.34
278.15 0.7940 739.96
278.15 0.8890 747.05
283.15 0.1042 696.72
283.15 0.2146 701.76
283.15 0.3024 705.9
283.15 0.3982 710.79
283.15 0.4996 716.32
283.15 0.5875 721.55
283.15 0.6985 728.56
283.15 0.7940 735.08
283.15 0.8890 742.07
288.15 0.1042 692.45
288.15 0.2146 697.4
288.15 0.3024 701.47
288.15 0.3982 706.28
288.15 0.4996 711.72
288.15 0.5875 716.86
288.15 0.6985 723.76
288.15 0.7940 730.17
288.15 0.8890 737.04
293.15 0.1042 688.15
293.15 0.2146 693.02
293.15 0.3024 697.02
293.15 0.3982 701.73
293.15 0.4996 707.09
293.15 0.5875 712.13
293.15 0.6985 718.92
293.15 0.7940 725.22
293.15 0.8890 731.98
298.15 0.1042 683.83
298.15 0.2146 688.62
298.15 0.3024 692.54
298.15 0.3982 697.16
298.15 0.4996 702.42
298.15 0.5875 707.37
298.15 0.6985 714.04
298.15 0.7940 720.23
298.15 0.8890 726.87
303.15 0.1042 679.49
303.15 0.2146 684.18
303.15 0.3024 688.02
303.15 0.3982 692.55
303.15 0.4996 697.72
303.15 0.5875 702.57
303.15 0.6985 709.11
303.15 0.7940 715.19
303.15 0.8890 721.72
308.15 0.1042 675.12
308.15 0.2146 679.71
308.15 0.3024 683.48
308.15 0.3982 687.91
308.15 0.4996 692.98
308.15 0.5875 697.73
308.15 0.6985 704.14
308.15 0.7940 710.11
313.15 0.1042 670.71
313.15 0.2146 675.19
313.15 0.3024 678.89
313.15 0.3982 683.23
313.15 0.4996 688.2
313.15 0.5875 692.85
313.15 0.6985 699.12
318.15 0.1042 666.28
318.15 0.2146 670.65
318.15 0.3024 674.26
318.15 0.3982 678.51
318.15 0.4996 683.38
318.15 0.5875 687.92
323.15 0.1042 661.8
323.15 0.2146 666.08
323.15 0.3024 669.6
323.15 0.3982 673.75
323.15 0.4996 678.5
328.15 0.1042 657.27
328.15 0.2146 661.46
328.15 0.3024 664.89
328.15 0.3982 668.93
333.15 0.1042 652.74
333.15 0.2146 656.77
333.15 0.3024 660.13
338.16 0.1042 648.13
338.16 0.2146 652.07
343.16 0.1042 643.27

Critical temperature, K [ref]

Mole fraction of Heptane (2) - Liquid Critical temperature, K - Liquid
0.0000 497.00
0.1000 499.40
0.2011 503.70
0.3056 508.30
0.3978 513.10
0.4970 518.00
0.5996 522.60
0.6933 525.60
0.8001 530.90
0.8984 535.00
1.0000 540.00

Critical temperature, K [ref]

Mole fraction of Heptane (2) - Liquid Critical temperature, K - Liquid
0.0000 497.00
0.1000 499.40
0.2011 503.70
0.3056 508.30
0.3978 513.10
0.4970 518.00
0.5996 522.60
0.6933 525.60
0.8001 530.90
0.8984 535.00
1.0000 540.00

Sources