Mixture of Propane, 2-methoxy-2-methyl- + 1-Hexanol + Water

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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

1-Hexanol

Name
1-Hexanol
InChI
InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3
InChI Key
ZSIAUFGUXNUGDI-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCCCCCO
Mol. Weight (g/mol)
102.17
CAS
111-27-3

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Temperature, K x Mole fraction (2)
  2. ρl - Mass density, kg/m3 (4)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 Mole fraction of 1-Hexanol (2) - Liquid mixture 2 Mole fraction of 1-Hexanol (2) - Liquid mixture 1 Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1
288.15 0.0156 0.0000 0.0000 0.9098
288.15 0.0119 0.0002 0.0728 0.8105
288.15 0.0106 0.0003 0.1386 0.7105
288.15 0.0094 0.0006 0.2213 0.5844
288.15 0.0084 0.0007 0.4424 0.3293
288.15 0.0075 0.0007 0.3805 0.3810
288.15 0.0038 0.0021 0.5010 0.1829
288.15 0.0031 0.0020 0.5411 0.1518
288.15 0.0022 0.0023 0.5860 0.1030
288.15 0.0011 0.0021 0.6239 0.0572
288.15 0.0000 0.0026 0.6720 0.0000
298.15 0.0087 0.0000 0.0000 0.9329
298.15 0.0079 0.0002 0.0687 0.8329
298.15 0.0072 0.0003 0.1226 0.7529
298.15 0.0068 0.0004 0.2053 0.6361
298.15 0.0060 0.0005 0.2630 0.5505
298.15 0.0054 0.0005 0.3164 0.4764
298.15 0.0023 0.0009 0.5066 0.1948
298.15 0.0020 0.0009 0.5388 0.1462
298.15 0.0014 0.0009 0.5851 0.1081
298.15 0.0008 0.0010 0.6351 0.0576
298.15 0.0000 0.0012 0.6763 0.0000
308.15 0.0072 0.0000 0.0000 0.9180
308.15 0.0065 0.0003 0.0860 0.7971
308.15 0.0061 0.0003 0.1465 0.7161
308.15 0.0054 0.0004 0.2049 0.6259
308.15 0.0050 0.0004 0.2413 0.5832
308.15 0.0045 0.0005 0.3110 0.4878
308.15 0.0042 0.0007 0.3463 0.4270
308.15 0.0021 0.0014 0.4426 0.1595
308.15 0.0016 0.0011 0.4738 0.1330
308.15 0.0012 0.0016 0.5155 0.0880
308.15 0.0006 0.0018 0.5513 0.0494
308.15 0.0000 0.0023 0.6039 0.0000

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 Mole fraction of 1-Hexanol (2) - Liquid mixture 2 Mole fraction of 1-Hexanol (2) - Liquid mixture 1 Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1
288.15 0.0156 0.0000 0.0000 0.9098
288.15 0.0119 0.0002 0.0728 0.8105
288.15 0.0106 0.0003 0.1386 0.7105
288.15 0.0094 0.0006 0.2213 0.5844
288.15 0.0084 0.0007 0.4424 0.3293
288.15 0.0075 0.0007 0.3805 0.3810
288.15 0.0038 0.0021 0.5010 0.1829
288.15 0.0031 0.0020 0.5411 0.1518
288.15 0.0022 0.0023 0.5860 0.1030
288.15 0.0011 0.0021 0.6239 0.0572
288.15 0.0000 0.0026 0.6720 0.0000
298.15 0.0087 0.0000 0.0000 0.9329
298.15 0.0079 0.0002 0.0687 0.8329
298.15 0.0072 0.0003 0.1226 0.7529
298.15 0.0068 0.0004 0.2053 0.6361
298.15 0.0060 0.0005 0.2630 0.5505
298.15 0.0054 0.0005 0.3164 0.4764
298.15 0.0023 0.0009 0.5066 0.1948
298.15 0.0020 0.0009 0.5388 0.1462
298.15 0.0014 0.0009 0.5851 0.1081
298.15 0.0008 0.0010 0.6351 0.0576
298.15 0.0000 0.0012 0.6763 0.0000
308.15 0.0072 0.0000 0.0000 0.9180
308.15 0.0065 0.0003 0.0860 0.7971
308.15 0.0061 0.0003 0.1465 0.7161
308.15 0.0054 0.0004 0.2049 0.6259
308.15 0.0050 0.0004 0.2413 0.5832
308.15 0.0045 0.0005 0.3110 0.4878
308.15 0.0042 0.0007 0.3463 0.4270
308.15 0.0021 0.0014 0.4426 0.1595
308.15 0.0016 0.0011 0.4738 0.1330
308.15 0.0012 0.0016 0.5155 0.0880
308.15 0.0006 0.0018 0.5513 0.0494
308.15 0.0000 0.0023 0.6039 0.0000

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 Mass density, kg/m3 - Liquid mixture 1
288.15 0.0000 806.0
288.15 0.0572 803.0
288.15 0.1030 805.0
288.15 0.1518 802.0
288.15 0.1829 803.0
288.15 0.3293 790.0
288.15 0.3810 795.0
288.15 0.5844 776.0
288.15 0.7105 767.0
288.15 0.8105 760.0
288.15 0.9098 742.0
298.15 0.0000 807.0
298.15 0.0576 812.0
298.15 0.1081 816.0
298.15 0.1462 821.0
298.15 0.1948 823.0
298.15 0.4764 782.0
298.15 0.5505 775.0
298.15 0.6361 767.0
298.15 0.7529 758.0
298.15 0.8329 750.0
298.15 0.9329 744.0
308.15 0.0000 802.0
308.15 0.0494 804.0
308.15 0.0880 799.0
308.15 0.1330 792.0
308.15 0.1595 786.0
308.15 0.4270 785.0
308.15 0.4878 780.0
308.15 0.5832 773.0
308.15 0.6259 768.0
308.15 0.7161 761.0
308.15 0.7971 748.0
308.15 0.9180 736.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 Mass density, kg/m3 - Liquid mixture 2
288.15 0.0000 974.0
288.15 0.0011 981.0
288.15 0.0022 985.0
288.15 0.0031 983.0
288.15 0.0038 989.0
288.15 0.0075 987.0
288.15 0.0084 986.0
288.15 0.0094 986.0
288.15 0.0106 985.0
288.15 0.0119 979.0
288.15 0.0156 976.0
298.15 0.0000 1000.0
298.15 0.0008 998.0
298.15 0.0014 996.0
298.15 0.0020 997.0
298.15 0.0023 998.0
298.15 0.0054 990.0
298.15 0.0060 987.0
298.15 0.0068 986.0
298.15 0.0072 986.0
298.15 0.0079 986.0
298.15 0.0087 985.0
308.15 0.0000 991.0
308.15 0.0006 985.0
308.15 0.0012 978.0
308.15 0.0016 976.0
308.15 0.0021 975.0
308.15 0.0042 991.0
308.15 0.0045 995.0
308.15 0.0050 997.0
308.15 0.0054 995.0
308.15 0.0061 994.0
308.15 0.0065 994.0
308.15 0.0072 997.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 Mass density, kg/m3 - Liquid mixture 1
288.15 0.0000 806.0
288.15 0.0572 803.0
288.15 0.1030 805.0
288.15 0.1518 802.0
288.15 0.1829 803.0
288.15 0.3293 790.0
288.15 0.3810 795.0
288.15 0.5844 776.0
288.15 0.7105 767.0
288.15 0.8105 760.0
288.15 0.9098 742.0
298.15 0.0000 807.0
298.15 0.0576 812.0
298.15 0.1081 816.0
298.15 0.1462 821.0
298.15 0.1948 823.0
298.15 0.4764 782.0
298.15 0.5505 775.0
298.15 0.6361 767.0
298.15 0.7529 758.0
298.15 0.8329 750.0
298.15 0.9329 744.0
308.15 0.0000 802.0
308.15 0.0494 804.0
308.15 0.0880 799.0
308.15 0.1330 792.0
308.15 0.1595 786.0
308.15 0.4270 785.0
308.15 0.4878 780.0
308.15 0.5832 773.0
308.15 0.6259 768.0
308.15 0.7161 761.0
308.15 0.7971 748.0
308.15 0.9180 736.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 Mass density, kg/m3 - Liquid mixture 2
288.15 0.0000 974.0
288.15 0.0011 981.0
288.15 0.0022 985.0
288.15 0.0031 983.0
288.15 0.0038 989.0
288.15 0.0075 987.0
288.15 0.0084 986.0
288.15 0.0094 986.0
288.15 0.0106 985.0
288.15 0.0119 979.0
288.15 0.0156 976.0
298.15 0.0000 1000.0
298.15 0.0008 998.0
298.15 0.0014 996.0
298.15 0.0020 997.0
298.15 0.0023 998.0
298.15 0.0054 990.0
298.15 0.0060 987.0
298.15 0.0068 986.0
298.15 0.0072 986.0
298.15 0.0079 986.0
298.15 0.0087 985.0
308.15 0.0000 991.0
308.15 0.0006 985.0
308.15 0.0012 978.0
308.15 0.0016 976.0
308.15 0.0021 975.0
308.15 0.0042 991.0
308.15 0.0045 995.0
308.15 0.0050 997.0
308.15 0.0054 995.0
308.15 0.0061 994.0
308.15 0.0065 994.0
308.15 0.0072 997.0

Sources