Mixture of Toluene + 1-Hexene + Propane, 2-ethoxy-2-methyl-

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Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

1-Hexene

Name
1-Hexene
InChI
InChI=1S/C6H12/c1-3-5-6-4-2/h3H,1,4-6H2,2H3
InChI Key
LIKMAJRDDDTEIG-UHFFFAOYSA-N
Formula
C6H12
SMILES
C=CCCCC
Mol. Weight (g/mol)
84.16
CAS
592-41-6

Propane, 2-ethoxy-2-methyl-

Name
Propane, 2-ethoxy-2-methyl-
InChI
InChI=1S/C6H14O/c1-5-7-6(2,3)4/h5H2,1-4H3
InChI Key
NUMQCACRALPSHD-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCOC(C)(C)C
Mol. Weight (g/mol)
102.17
CAS
637-92-3
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Datasets

  1. Pvap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (3) - Liquid Mole fraction of 1-Hexene (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 7.87
0.0000 0.3051 21.25
0.0000 0.6591 33.42
0.0000 1.0000 44.96
0.0001 0.0000 7.87
0.0001 1.0000 44.94
0.0260 0.2971 21.51
0.0284 0.6404 33.40
0.0515 0.2894 21.76
0.0584 0.6206 33.35
0.1005 0.2744 22.25
0.1103 0.5864 33.28
0.1492 0.3487 25.92
0.1501 0.2593 22.75
0.1608 0.4632 30.21
0.1643 0.3840 27.47
0.1648 0.5505 33.20
0.1670 0.4425 29.63
0.1794 0.4195 29.01
0.1797 0.4002 28.43
0.1944 0.4545 30.52
0.1948 0.3496 26.96
0.2005 0.2440 23.26
0.2096 0.3000 25.51
0.2096 0.4899 32.05
0.2183 0.5153 33.11
0.2247 0.5251 33.58
0.2248 0.2495 23.98
0.2392 0.2011 22.48
0.2394 0.5595 35.07
0.2489 0.2292 23.75
0.2538 0.1524 20.92
0.2543 0.5944 36.58
0.2695 0.1000 19.19
0.2698 0.6307 38.17
0.2708 0.4807 33.02
0.2821 0.0580 17.78
0.2845 0.6649 39.67
0.2909 0.0283 16.74
0.2920 0.6824 40.45
0.2968 0.2146 24.23
0.2994 0.0000 15.72
0.2996 0.7004 41.25
0.3227 0.4466 32.93
0.3475 0.1505 22.87
0.3480 0.1990 24.75
0.3495 0.5002 35.41
0.3746 0.4123 32.83
0.3824 0.1656 24.19
0.3847 0.4499 34.42
0.3989 0.1835 25.27
0.4175 0.1808 25.49
0.4191 0.4006 33.44
0.4259 0.3785 32.75
0.4489 0.1683 25.78
0.4521 0.1958 26.80
0.4541 0.3506 32.42
0.4762 0.3454 32.66
0.4873 0.2110 28.10
0.4890 0.3006 31.40
0.4980 0.1533 26.28
0.5223 0.2262 29.40
0.5247 0.2495 30.33
0.5264 0.3124 32.57
0.5574 0.2414 30.70
0.5586 0.2011 29.30
0.5928 0.2567 32.02
0.5932 0.1516 28.24
0.6277 0.2718 33.33
0.6281 0.1017 27.15
0.6597 0.0563 26.14
0.6625 0.2869 34.64
0.6787 0.0292 25.53
0.6800 0.2945 35.31
0.6978 0.3022 36.00
0.6991 0.0000 24.88
1.0000 0.0000 31.63
1.0000 0.0000 31.64

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (3) - Liquid Mole fraction of 1-Hexene (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 7.87
0.0000 0.3051 21.25
0.0000 0.6591 33.42
0.0000 1.0000 44.96
0.0001 0.0000 7.87
0.0001 1.0000 44.94
0.0260 0.2971 21.51
0.0284 0.6404 33.40
0.0515 0.2894 21.76
0.0584 0.6206 33.35
0.1005 0.2744 22.25
0.1103 0.5864 33.28
0.1492 0.3487 25.92
0.1501 0.2593 22.75
0.1608 0.4632 30.21
0.1643 0.3840 27.47
0.1648 0.5505 33.20
0.1670 0.4425 29.63
0.1794 0.4195 29.01
0.1797 0.4002 28.43
0.1944 0.4545 30.52
0.1948 0.3496 26.96
0.2005 0.2440 23.26
0.2096 0.3000 25.51
0.2096 0.4899 32.05
0.2183 0.5153 33.11
0.2247 0.5251 33.58
0.2248 0.2495 23.98
0.2392 0.2011 22.48
0.2394 0.5595 35.07
0.2489 0.2292 23.75
0.2538 0.1524 20.92
0.2543 0.5944 36.58
0.2695 0.1000 19.19
0.2698 0.6307 38.17
0.2708 0.4807 33.02
0.2821 0.0580 17.78
0.2845 0.6649 39.67
0.2909 0.0283 16.74
0.2920 0.6824 40.45
0.2968 0.2146 24.23
0.2994 0.0000 15.72
0.2996 0.7004 41.25
0.3227 0.4466 32.93
0.3475 0.1505 22.87
0.3480 0.1990 24.75
0.3495 0.5002 35.41
0.3746 0.4123 32.83
0.3824 0.1656 24.19
0.3847 0.4499 34.42
0.3989 0.1835 25.27
0.4175 0.1808 25.49
0.4191 0.4006 33.44
0.4259 0.3785 32.75
0.4489 0.1683 25.78
0.4521 0.1958 26.80
0.4541 0.3506 32.42
0.4762 0.3454 32.66
0.4873 0.2110 28.10
0.4890 0.3006 31.40
0.4980 0.1533 26.28
0.5223 0.2262 29.40
0.5247 0.2495 30.33
0.5264 0.3124 32.57
0.5574 0.2414 30.70
0.5586 0.2011 29.30
0.5928 0.2567 32.02
0.5932 0.1516 28.24
0.6277 0.2718 33.33
0.6281 0.1017 27.15
0.6597 0.0563 26.14
0.6625 0.2869 34.64
0.6787 0.0292 25.53
0.6800 0.2945 35.31
0.6978 0.3022 36.00
0.6991 0.0000 24.88
1.0000 0.0000 31.63
1.0000 0.0000 31.64

Sources