Mixture of n-Hexane + 1-Butanol + Butane, 1-chloro-

Excel

n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3

Butane, 1-chloro-

Name
Butane, 1-chloro-
InChI
InChI=1S/C4H9Cl/c1-2-3-4-5/h2-4H2,1H3
InChI Key
VFWCMGCRMGJXDK-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CCCCCl
Mol. Weight (g/mol)
92.57
CAS
109-69-3
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Datasets

  1. Pressure, kPa x Mole fraction (2)
  2. ρl - Mass density, kg/m3 (2)
  3. γ - Surface tension liquid-gas, N/m (2)

Pressure, kPa x Mole fraction [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Fixed Measured
Pressure, kPa - Liquid Mole fraction of n-Hexane (1) - Gas Mole fraction of 1-Butanol (2) - Gas Mole fraction of n-Hexane (1) - Liquid Mole fraction of 1-Butanol (2) - Liquid
6.41 0.4040 0.1210 0.0330 0.8860
10.03 0.6490 0.0870 0.0940 0.8270
13.21 0.7580 0.0670 0.1700 0.7590
15.06 0.8210 0.0360 0.2330 0.7010
16.63 0.8670 0.0390 0.3140 0.6270
17.52 0.8900 0.0350 0.3890 0.5580
18.02 0.9090 0.0360 0.4420 0.5120
18.66 0.9250 0.0310 0.5170 0.4470
19.09 0.9410 0.0350 0.6050 0.3700
19.34 0.9550 0.0300 0.6780 0.3070
11.11 0.3240 0.0760 0.0590 0.7110
13.18 0.4990 0.0450 0.1190 0.6730
15.46 0.6330 0.0280 0.2040 0.6080
16.39 0.7090 0.0340 0.2650 0.5660
17.39 0.7640 0.0330 0.3400 0.5090
18.11 0.8120 0.0360 0.4210 0.4490
18.54 0.8390 0.0370 0.4850 0.4010
18.95 0.8670 0.0330 0.5550 0.3490
19.27 0.8680 0.0300 0.6050 0.2890
19.50 0.9140 0.0310 0.7050 0.2390
12.69 0.2060 0.0650 0.0560 0.5230
14.89 0.4000 0.0540 0.1350 0.4750
16.30 0.5210 0.0370 0.2220 0.4330
17.57 0.6280 0.0190 0.3320 0.3700
18.27 0.6970 0.0310 0.4190 0.3240
18.91 0.7560 0.0300 0.5100 0.2770
19.38 0.8010 0.0300 0.6010 0.2330
19.77 0.8580 0.0290 0.7020 0.1800
20.05 0.9020 0.0260 0.8010 0.1200
14.01 0.2150 0.0450 0.0870 0.3060
14.75 0.2730 0.0470 0.1120 0.2930
16.34 0.4200 0.0410 0.2060 0.2690
17.15 0.4990 0.0250 0.2870 0.2420
17.91 0.5760 0.0280 0.3610 0.2240
18.41 0.6150 0.0280 0.4270 0.1990
18.95 0.6750 0.0300 0.5040 0.1730
19.25 0.7240 0.0350 0.5840 0.1460
19.72 0.7850 0.0190 0.6750 0.1130
20.00 0.8180 0.0190 0.7580 0.0850
14.49 0.1890 0.0700 0.0920 0.0960
15.13 0.2010 0.0500 0.1040 0.0940
16.39 0.3430 0.0420 0.2000 0.0920
17.18 0.4440 0.0480 0.2760 0.0860
17.61 0.4720 0.0420 0.3270 0.0800
18.13 0.5200 0.0330 0.3830 0.0730
18.65 0.5780 0.0300 0.4520 0.0660
19.48 0.6880 0.0210 0.6080 0.0310
19.97 0.7780 0.0100 0.7360 0.0110

Pressure, kPa x Mole fraction [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Fixed Measured
Pressure, kPa - Liquid Mole fraction of n-Hexane (1) - Gas Mole fraction of 1-Butanol (2) - Gas Mole fraction of n-Hexane (1) - Liquid Mole fraction of 1-Butanol (2) - Liquid
6.41 0.4040 0.1210 0.0330 0.8860
10.03 0.6490 0.0870 0.0940 0.8270
13.21 0.7580 0.0670 0.1700 0.7590
15.06 0.8210 0.0360 0.2330 0.7010
16.63 0.8670 0.0390 0.3140 0.6270
17.52 0.8900 0.0350 0.3890 0.5580
18.02 0.9090 0.0360 0.4420 0.5120
18.66 0.9250 0.0310 0.5170 0.4470
19.09 0.9410 0.0350 0.6050 0.3700
19.34 0.9550 0.0300 0.6780 0.3070
11.11 0.3240 0.0760 0.0590 0.7110
13.18 0.4990 0.0450 0.1190 0.6730
15.46 0.6330 0.0280 0.2040 0.6080
16.39 0.7090 0.0340 0.2650 0.5660
17.39 0.7640 0.0330 0.3400 0.5090
18.11 0.8120 0.0360 0.4210 0.4490
18.54 0.8390 0.0370 0.4850 0.4010
18.95 0.8670 0.0330 0.5550 0.3490
19.27 0.8680 0.0300 0.6050 0.2890
19.50 0.9140 0.0310 0.7050 0.2390
12.69 0.2060 0.0650 0.0560 0.5230
14.89 0.4000 0.0540 0.1350 0.4750
16.30 0.5210 0.0370 0.2220 0.4330
17.57 0.6280 0.0190 0.3320 0.3700
18.27 0.6970 0.0310 0.4190 0.3240
18.91 0.7560 0.0300 0.5100 0.2770
19.38 0.8010 0.0300 0.6010 0.2330
19.77 0.8580 0.0290 0.7020 0.1800
20.05 0.9020 0.0260 0.8010 0.1200
14.01 0.2150 0.0450 0.0870 0.3060
14.75 0.2730 0.0470 0.1120 0.2930
16.34 0.4200 0.0410 0.2060 0.2690
17.15 0.4990 0.0250 0.2870 0.2420
17.91 0.5760 0.0280 0.3610 0.2240
18.41 0.6150 0.0280 0.4270 0.1990
18.95 0.6750 0.0300 0.5040 0.1730
19.25 0.7240 0.0350 0.5840 0.1460
19.72 0.7850 0.0190 0.6750 0.1130
20.00 0.8180 0.0190 0.7580 0.0850
14.49 0.1890 0.0700 0.0920 0.0960
15.13 0.2010 0.0500 0.1040 0.0940
16.39 0.3430 0.0420 0.2000 0.0920
17.18 0.4440 0.0480 0.2760 0.0860
17.61 0.4720 0.0420 0.3270 0.0800
18.13 0.5200 0.0330 0.3830 0.0730
18.65 0.5780 0.0300 0.4520 0.0660
19.48 0.6880 0.0210 0.6080 0.0310
19.97 0.7780 0.0100 0.7360 0.0110

Mass density, kg/m3 [ref]

Operational conditions:

Fixed Measured
Mole fraction of 1-Butanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Mass density, kg/m3 - Liquid
0.0544 0.8825 672.11
0.0585 0.0520 861.58
0.0610 0.8385 679.96
0.0611 0.1010 847.92
0.0970 0.0535 858.31
0.1008 0.5934 726.27
0.1013 0.1103 842.45
0.1027 0.5004 746.47
0.1029 0.2001 818.54
0.1064 0.3976 769.69
0.1070 0.2967 793.9
0.1082 0.8380 676.41
0.1118 0.6834 706.66
0.1131 0.7856 686.17
0.1955 0.4013 762.19
0.1992 0.3017 785.8
0.2009 0.0957 839.21
0.2022 0.4943 740.35
0.2037 0.6971 696.94
0.2064 0.1976 811.64
0.2067 0.5932 718.43
0.2971 0.0986 831.6
0.2975 0.2017 803.98
0.2978 0.3007 778.89
0.2985 0.6004 710.07
0.2991 0.4992 732.16
0.2994 0.2032 803.51
0.3007 0.3962 755.62
0.3945 0.5028 724.23
0.3975 0.3998 747.75
0.3985 0.1990 797.45
0.3985 0.3028 771.1
0.3997 0.0970 824.73
0.4892 0.3061 763.6
0.4908 0.1046 816.1
0.4947 0.4000 740.38
0.4948 0.2019 789.75
0.5911 0.2022 782.51
0.5932 0.1028 809.09
0.5939 0.3020 756.67
0.6883 0.2020 775.01
0.6885 0.1019 802.12
0.7934 0.1003 794.26
0.8394 0.1004 790.44
0.8459 0.0516 803.78

Mass density, kg/m3 [ref]

Operational conditions:

Fixed Measured
Mole fraction of 1-Butanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Mass density, kg/m3 - Liquid
0.0544 0.8825 672.11
0.0585 0.0520 861.58
0.0610 0.8385 679.96
0.0611 0.1010 847.92
0.0970 0.0535 858.31
0.1008 0.5934 726.27
0.1013 0.1103 842.45
0.1027 0.5004 746.47
0.1029 0.2001 818.54
0.1064 0.3976 769.69
0.1070 0.2967 793.9
0.1082 0.8380 676.41
0.1118 0.6834 706.66
0.1131 0.7856 686.17
0.1955 0.4013 762.19
0.1992 0.3017 785.8
0.2009 0.0957 839.21
0.2022 0.4943 740.35
0.2037 0.6971 696.94
0.2064 0.1976 811.64
0.2067 0.5932 718.43
0.2971 0.0986 831.6
0.2975 0.2017 803.98
0.2978 0.3007 778.89
0.2985 0.6004 710.07
0.2991 0.4992 732.16
0.2994 0.2032 803.51
0.3007 0.3962 755.62
0.3945 0.5028 724.23
0.3975 0.3998 747.75
0.3985 0.1990 797.45
0.3985 0.3028 771.1
0.3997 0.0970 824.73
0.4892 0.3061 763.6
0.4908 0.1046 816.1
0.4947 0.4000 740.38
0.4948 0.2019 789.75
0.5911 0.2022 782.51
0.5932 0.1028 809.09
0.5939 0.3020 756.67
0.6883 0.2020 775.01
0.6885 0.1019 802.12
0.7934 0.1003 794.26
0.8394 0.1004 790.44
0.8459 0.0516 803.78

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Fixed Measured
Mole fraction of 1-Butanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0544 0.8825 0.0183
0.0585 0.0520 0.0228
0.0610 0.8385 0.0185
0.0611 0.1010 0.0224
0.0970 0.0535 0.0228
0.1008 0.5934 0.0193
0.1013 0.1103 0.0222
0.1027 0.5004 0.0197
0.1029 0.2001 0.0215
0.1064 0.3976 0.0202
0.1070 0.2967 0.0208
0.1082 0.8380 0.0184
0.1118 0.6834 0.0189
0.1131 0.7856 0.0186
0.1955 0.4013 0.0200
0.1992 0.3017 0.0206
0.2009 0.0957 0.0223
0.2022 0.4943 0.0196
0.2037 0.6971 0.0189
0.2064 0.1976 0.0214
0.2067 0.5932 0.0192
0.2971 0.0986 0.0222
0.2975 0.2017 0.0213
0.2978 0.3007 0.0206
0.2985 0.6004 0.0192
0.2991 0.4992 0.0196
0.2994 0.2032 0.0213
0.3007 0.3962 0.0201
0.3945 0.5028 0.0195
0.3975 0.3998 0.0200
0.3985 0.1990 0.0213
0.3985 0.3028 0.0205
0.3997 0.0970 0.0222
0.4892 0.3061 0.0205
0.4908 0.1046 0.0222
0.4947 0.4000 0.0199
0.4948 0.2019 0.0213
0.5911 0.2022 0.0214
0.5932 0.1028 0.0223
0.5939 0.3020 0.0205
0.6883 0.2020 0.0214
0.6885 0.1019 0.0224
0.7934 0.1003 0.0225
0.8394 0.1004 0.0226
0.8459 0.0516 0.0232

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Fixed Measured
Mole fraction of 1-Butanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0544 0.8825 0.0183
0.0585 0.0520 0.0228
0.0610 0.8385 0.0185
0.0611 0.1010 0.0224
0.0970 0.0535 0.0228
0.1008 0.5934 0.0193
0.1013 0.1103 0.0222
0.1027 0.5004 0.0197
0.1029 0.2001 0.0215
0.1064 0.3976 0.0202
0.1070 0.2967 0.0208
0.1082 0.8380 0.0184
0.1118 0.6834 0.0189
0.1131 0.7856 0.0186
0.1955 0.4013 0.0200
0.1992 0.3017 0.0206
0.2009 0.0957 0.0223
0.2022 0.4943 0.0196
0.2037 0.6971 0.0189
0.2064 0.1976 0.0214
0.2067 0.5932 0.0192
0.2971 0.0986 0.0222
0.2975 0.2017 0.0213
0.2978 0.3007 0.0206
0.2985 0.6004 0.0192
0.2991 0.4992 0.0196
0.2994 0.2032 0.0213
0.3007 0.3962 0.0201
0.3945 0.5028 0.0195
0.3975 0.3998 0.0200
0.3985 0.1990 0.0213
0.3985 0.3028 0.0205
0.3997 0.0970 0.0222
0.4892 0.3061 0.0205
0.4908 0.1046 0.0222
0.4947 0.4000 0.0199
0.4948 0.2019 0.0213
0.5911 0.2022 0.0214
0.5932 0.1028 0.0223
0.5939 0.3020 0.0205
0.6883 0.2020 0.0214
0.6885 0.1019 0.0224
0.7934 0.1003 0.0225
0.8394 0.1004 0.0226
0.8459 0.0516 0.0232

Sources