Dortmund Data Bank
Vapor-Liquid Equilibrium Data
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Vapor-Liquid Equilibrium Data Set 7426
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 3 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 351.15 |
0.47600 |
0.34000 |
0.49000 |
0.41600 |
| 351.75 |
0.47160 |
0.31400 |
0.47860 |
0.41340 |
| 352.25 |
0.62280 |
0.15500 |
0.65280 |
0.24160 |
| 352.35 |
0.65480 |
0.12800 |
0.68000 |
0.21550 |
| 352.45 |
0.57840 |
0.16400 |
0.61240 |
0.26760 |
| 352.55 |
0.49480 |
0.21600 |
0.54440 |
0.26760 |
| 352.55 |
0.54080 |
0.18000 |
0.64000 |
0.25000 |
| 352.65 |
0.48000 |
0.21800 |
0.49840 |
0.36440 |
| 352.85 |
0.37620 |
0.27340 |
0.47300 |
0.40000 |
| 353.15 |
0.00750 |
0.73400 |
0.01000 |
0.85640 |
| 353.15 |
0.67660 |
0.03800 |
0.79700 |
0.07100 |
| 353.45 |
0.76500 |
0.00100 |
0.87620 |
0.00180 |
| 353.55 |
0.71980 |
0.01200 |
0.84500 |
0.02000 |
| 353.55 |
0.79440 |
0.00100 |
0.88640 |
0.00160 |
| 353.65 |
0.01500 |
0.67800 |
0.02100 |
0.85220 |
| 353.65 |
0.65380 |
0.04320 |
0.80500 |
0.07400 |
| 353.65 |
0.74100 |
0.00200 |
0.87840 |
0.00360 |
| 353.65 |
0.89960 |
0.00400 |
0.92740 |
0.00620 |
| 353.65 |
0.94500 |
0.01100 |
0.95600 |
0.01400 |
| 353.85 |
0.95680 |
0.00120 |
0.96840 |
0.00160 |
| 353.95 |
0.56440 |
0.08360 |
0.70700 |
0.15500 |
| 354.15 |
0.34800 |
0.23360 |
0.47200 |
0.38800 |
| 354.15 |
0.48000 |
0.13120 |
0.62700 |
0.23200 |
| 354.25 |
0.02420 |
0.61600 |
0.03200 |
0.83600 |
| 354.65 |
0.02800 |
0.60240 |
0.04140 |
0.81060 |
| 354.65 |
0.32200 |
0.23080 |
0.41400 |
0.43200 |
| 354.65 |
0.38800 |
0.18820 |
0.51200 |
0.34000 |
| 354.95 |
0.38250 |
0.19500 |
0.54000 |
0.32500 |
| 355.15 |
0.27200 |
0.25100 |
0.38600 |
0.45400 |
| 355.55 |
0.00600 |
0.52800 |
0.01020 |
0.83380 |
| 355.55 |
0.28800 |
0.22280 |
0.47000 |
0.38000 |
| 355.65 |
0.47360 |
0.10800 |
0.62240 |
0.20720 |
| 355.85 |
0.35200 |
0.16920 |
0.53000 |
0.32000 |
| 356.05 |
0.31000 |
0.21200 |
0.49440 |
0.36300 |
| 356.15 |
0.35100 |
0.19420 |
0.53640 |
0.34200 |
| 356.45 |
0.01600 |
0.49520 |
0.03000 |
0.80200 |
| 356.75 |
0.10500 |
0.29920 |
0.20000 |
0.64000 |
| 357.05 |
0.00960 |
0.38100 |
0.02100 |
0.81640 |
| 357.25 |
0.01250 |
0.37600 |
0.02780 |
0.79020 |
| 357.55 |
0.34840 |
0.14440 |
0.59340 |
0.26460 |
| 357.95 |
0.01080 |
0.32200 |
0.02360 |
0.76940 |
| 357.95 |
0.29700 |
0.14800 |
0.51840 |
0.29760 |
| 358.25 |
0.26040 |
0.15700 |
0.47800 |
0.33300 |
| 358.95 |
0.23320 |
0.16300 |
0.45200 |
0.35600 |
| 358.95 |
0.25620 |
0.14160 |
0.46060 |
0.34880 |
| 359.45 |
0.18500 |
0.17200 |
0.40200 |
0.39000 |
| 359.85 |
0.13120 |
0.19200 |
0.30600 |
0.48200 |
| 360.95 |
0.10620 |
0.18020 |
0.27400 |
0.49760 |
| 362.55 |
0.18940 |
0.09080 |
0.50200 |
0.31000 |
| 363.55 |
0.04800 |
0.14000 |
0.17120 |
0.55880 |
| 365.75 |
0.04520 |
0.13200 |
0.15440 |
0.55560 |
| 367.15 |
0.13520 |
0.08780 |
0.40000 |
0.30000 |
| 369.45 |
0.07260 |
0.10180 |
0.25600 |
0.40200 |
| 371.15 |
0.08120 |
0.02440 |
0.37600 |
0.11600 |
| 372.45 |
0.10680 |
0.01320 |
0.49040 |
0.06200 |
| 372.55 |
0.08840 |
0.00400 |
0.42800 |
0.02200 |
| 378.65 |
0.05880 |
0.00680 |
0.35140 |
0.04000 |
| 383.75 |
0.03860 |
0.01260 |
0.24800 |
0.08200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Subbarao B.V.; Ventakarao C.: Isobaric Ternary Vapour-Liquid Equilibria System: Benzene-Cyclohexane-n-Butanol. J.Appl.Chem. 18 (1968) 61-64 |
Vapor-Liquid Equilibrium Data Set 12957
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 3 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 382.65 |
0.03200 |
0.02000 |
0.09700 |
0.06500 |
| 362.00 |
0.04200 |
0.21000 |
0.10300 |
0.55000 |
| 357.75 |
0.03500 |
0.31500 |
0.06600 |
0.70300 |
| 355.30 |
0.04400 |
0.41000 |
0.06900 |
0.74700 |
| 353.75 |
0.06600 |
0.49800 |
0.09200 |
0.76700 |
| 353.50 |
0.06300 |
0.57800 |
0.08000 |
0.78300 |
| 353.15 |
0.04800 |
0.67600 |
0.05800 |
0.81900 |
| 352.75 |
0.03400 |
0.74600 |
0.04200 |
0.85200 |
| 352.45 |
0.05400 |
0.79000 |
0.06500 |
0.84500 |
| 352.35 |
0.03500 |
0.86200 |
0.04400 |
0.86700 |
| 351.72 |
0.12900 |
0.78000 |
0.15000 |
0.77300 |
| 351.24 |
0.22100 |
0.68500 |
0.24000 |
0.68700 |
| 351.80 |
0.20200 |
0.57400 |
0.23800 |
0.65900 |
| 351.40 |
0.27100 |
0.53600 |
0.30700 |
0.59900 |
| 351.10 |
0.32400 |
0.51100 |
0.35400 |
0.55900 |
| 351.15 |
0.32400 |
0.53500 |
0.35000 |
0.56800 |
| 351.13 |
0.28100 |
0.61800 |
0.30600 |
0.62400 |
| 350.81 |
0.38500 |
0.52600 |
0.39600 |
0.53600 |
| 350.72 |
0.46700 |
0.44900 |
0.46700 |
0.46500 |
| 350.80 |
0.56000 |
0.36600 |
0.55100 |
0.38900 |
| 351.03 |
0.65100 |
0.28400 |
0.62900 |
0.31800 |
| 351.33 |
0.73200 |
0.20100 |
0.70300 |
0.24300 |
| 351.78 |
0.80600 |
0.14800 |
0.77800 |
0.17800 |
| 351.98 |
0.84200 |
0.12200 |
0.81200 |
0.15600 |
| 352.52 |
0.76100 |
0.10100 |
0.77000 |
0.14100 |
| 352.60 |
0.83700 |
0.06400 |
0.83400 |
0.09300 |
| 353.02 |
0.83700 |
0.03900 |
0.85200 |
0.06500 |
| 353.53 |
0.73000 |
0.05400 |
0.80200 |
0.08700 |
| 354.60 |
0.62600 |
0.05700 |
0.76300 |
0.09200 |
| 356.65 |
0.51900 |
0.04500 |
0.73300 |
0.08300 |
| 357.75 |
0.40800 |
0.05200 |
0.69700 |
0.11300 |
| 361.00 |
0.29800 |
0.05100 |
0.60700 |
0.13200 |
| 365.75 |
0.20700 |
0.03800 |
0.51000 |
0.13200 |
| 369.85 |
0.14400 |
0.03700 |
0.40000 |
0.15300 |
| 359.95 |
0.13500 |
0.14200 |
0.30700 |
0.40800 |
| 355.45 |
0.13000 |
0.25800 |
0.23900 |
0.57200 |
| 353.10 |
0.12900 |
0.38800 |
0.19400 |
0.64900 |
| 352.75 |
0.13100 |
0.50500 |
0.17600 |
0.69600 |
| 352.55 |
0.13400 |
0.59600 |
0.16300 |
0.72300 |
| 351.92 |
0.14300 |
0.68300 |
0.16800 |
0.74200 |
| 351.48 |
0.57100 |
0.26300 |
0.58800 |
0.32100 |
| 351.83 |
0.63600 |
0.21200 |
0.65000 |
0.26300 |
| 351.83 |
0.69200 |
0.16700 |
0.69600 |
0.21800 |
| 352.05 |
0.69500 |
0.14900 |
0.70900 |
0.19700 |
| 351.75 |
0.58800 |
0.22200 |
0.61500 |
0.28800 |
| 353.35 |
0.48500 |
0.19400 |
0.58400 |
0.28200 |
| 352.69 |
0.59600 |
0.14400 |
0.67500 |
0.21300 |
| 353.03 |
0.69300 |
0.10700 |
0.74300 |
0.14500 |
| 354.30 |
0.45000 |
0.14800 |
0.61300 |
0.25400 |
| 353.43 |
0.35900 |
0.27100 |
0.46300 |
0.39700 |
| 355.10 |
0.32900 |
0.20000 |
0.48900 |
0.34700 |
| 357.10 |
0.24600 |
0.15400 |
0.45000 |
0.33900 |
| 362.60 |
0.16400 |
0.09600 |
0.39400 |
0.29300 |
| 355.50 |
0.24600 |
0.22100 |
0.39800 |
0.42700 |
| 354.10 |
0.24400 |
0.29300 |
0.35600 |
0.49000 |
| 352.80 |
0.25000 |
0.38700 |
0.32400 |
0.54600 |
| 351.82 |
0.25100 |
0.47800 |
0.29900 |
0.59000 |
| 352.10 |
0.34800 |
0.37900 |
0.40600 |
0.48900 |
| 351.79 |
0.35400 |
0.41600 |
0.39700 |
0.49500 |
| 351.80 |
0.44200 |
0.33800 |
0.48000 |
0.40600 |
| 352.25 |
0.43900 |
0.27900 |
0.50500 |
0.36900 |
| 352.45 |
0.51800 |
0.22600 |
0.57700 |
0.30600 |
| 351.59 |
0.52300 |
0.26200 |
0.56000 |
0.33700 |
| 351.35 |
0.41600 |
0.40100 |
0.44400 |
0.46500 |
| 351.13 |
0.47500 |
0.36600 |
0.49000 |
0.41900 |
| 350.72 |
0.49100 |
0.47600 |
0.49100 |
0.47700 |
| 350.73 |
0.53200 |
0.42600 |
0.52700 |
0.43700 |
| 350.77 |
0.54500 |
0.43300 |
0.54000 |
0.43900 |
| 350.82 |
0.46600 |
0.51300 |
0.47500 |
0.50600 |
| 350.85 |
0.46200 |
0.52000 |
0.47000 |
0.51300 |
| 350.98 |
0.41800 |
0.56300 |
0.43300 |
0.55300 |
| 390.85 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 353.26 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
| 353.81 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Arce A.; Blanco A.; Correa A.; Tojo J.: Prediction and Experimental Determination of Vapour-Liquid Equilibria for Benzene + Cyclohexane + 1-Butanol Mixtures at 101.325 kPa. Can.J.Chem.Eng. 66 (1988) 452-457 |
Vapor-Liquid Equilibrium Data Set 30087
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 3 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 351.55 |
0.20330 |
0.16210 |
0.44690 |
0.33050 |
| 351.95 |
0.24250 |
0.16510 |
0.45780 |
0.37020 |
| 347.80 |
0.10870 |
0.29850 |
0.33540 |
0.52640 |
| 347.25 |
0.38530 |
0.22550 |
0.53200 |
0.35700 |
| 346.35 |
0.34240 |
0.27600 |
0.39800 |
0.46820 |
| 346.30 |
0.49840 |
0.24770 |
0.52740 |
0.31370 |
| 346.05 |
0.40390 |
0.30220 |
0.48510 |
0.42270 |
| 345.80 |
0.60310 |
0.19380 |
0.69730 |
0.23460 |
| 345.55 |
0.29280 |
0.46880 |
0.37580 |
0.56490 |
| 346.00 |
0.65190 |
0.16010 |
0.69560 |
0.21900 |
| 345.15 |
0.95100 |
0.00690 |
0.96200 |
0.01290 |
| 345.75 |
0.21920 |
0.54230 |
0.29370 |
0.61030 |
| 344.75 |
0.53340 |
0.32150 |
0.54800 |
0.37750 |
| 344.15 |
0.26470 |
0.68490 |
0.26470 |
0.68490 |
| 343.95 |
0.30710 |
0.60280 |
0.33200 |
0.60460 |
| 343.85 |
0.41690 |
0.57650 |
0.42110 |
0.56760 |
| 342.80 |
0.51880 |
0.38240 |
0.51920 |
0.40460 |
| 351.85 |
0.46210 |
0.02230 |
0.80350 |
0.05740 |
| 381.45 |
0.00930 |
0.01010 |
0.02010 |
0.01550 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Muralidharan N.; Satyanarayana M.: Vapour-Liquid Equilibria for Benzene-Cyclohexane-n-Butanol System at Subatmospheric Pressure. Indian J.Technol. 12 (1974) 4-7 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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