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 8612
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 100.792 |
0.00600 |
0.08600 |
| 100.792 |
0.04000 |
0.25500 |
| 99.192 |
0.04200 |
0.30000 |
| 100.925 |
0.19600 |
0.55900 |
| 100.658 |
0.28400 |
0.59600 |
| 100.392 |
0.36200 |
0.62600 |
| 100.125 |
0.43800 |
0.64500 |
| 99.992 |
0.50400 |
0.67000 |
| 100.125 |
0.58800 |
0.69400 |
| 100.125 |
0.59200 |
0.69600 |
| 100.125 |
0.60700 |
0.70200 |
| 100.125 |
0.64500 |
0.71800 |
| 100.525 |
0.68700 |
0.73600 |
| 99.059 |
0.72400 |
0.75200 |
| 98.925 |
0.74000 |
0.76200 |
| 98.925 |
0.75900 |
0.77200 |
| 100.258 |
0.78100 |
0.78600 |
| 99.725 |
0.85200 |
0.83100 |
| 100.258 |
0.87900 |
0.85500 |
| 100.258 |
0.88400 |
0.85500 |
| 100.258 |
0.91900 |
0.89500 |
| 99.858 |
0.98400 |
0.97300 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Bonauguri E.; Bicelli L.; Spiller G.: Ricerche sulla distillazione - I: Idrocarburi aromatici e alcooli. Chim.Ind. Milano 33 (1951) 81-90 |
Vapor-Liquid Equilibrium Data Set 23607
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
| 407.95 |
0.00000 |
| 398.15 |
0.09300 |
| 394.25 |
0.20110 |
| 392.45 |
0.30200 |
| 391.25 |
0.39000 |
| 390.15 |
0.50300 |
| 389.65 |
0.60300 |
| 389.15 |
0.69500 |
| 388.85 |
0.79600 |
| 389.05 |
0.90150 |
| 389.05 |
1.00000 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Vittal Prasad T.E.; Jaipuran Rao B.M.; Ajay Kumar V.; Bhatt S.S.; Prasad D.H.L.: Boiling Temperature Measurements on the Binary Mixtures of m-Xylene with some Aliphatic Alcohols. Phys.Chem.Liq. 40 (2002) 221-224 |
Vapor-Liquid Equilibrium Data Set 25037
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 2.200 |
0.05300 |
| 2.4505 |
0.11100 |
| 2.6904 |
0.17150 |
| 2.9504 |
0.25050 |
| 3.080 |
0.31900 |
| 3.200 |
0.39250 |
| 3.2304 |
0.44250 |
| 3.2704 |
0.50900 |
| 3.3104 |
0.59250 |
| 3.2704 |
0.64950 |
| 3.2104 |
0.72600 |
| 2.9104 |
0.83150 |
| 2.5705 |
0.89450 |
| 2.160 |
0.94600 |
| 1.7905 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Maken S.; Park J.J.; Bhardwaj U.; Chander Singh K.; Park J.-W.; Han S.D.; Deshwal B.R.: (Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K. J.Chem.Thermodyn. 36 (2004) 309-315 |
Diagrams
List of All References
| Source |
| Bonauguri E.; Bicelli L.; Spiller G.: Ricerche sulla distillazione - I: Idrocarburi aromatici e alcooli. Chim.Ind. Milano 33 (1951) 81-90 |
| Vittal Prasad T.E.; Jaipuran Rao B.M.; Ajay Kumar V.; Bhatt S.S.; Prasad D.H.L.: Boiling Temperature Measurements on the Binary Mixtures of m-Xylene with some Aliphatic Alcohols. Phys.Chem.Liq. 40 (2002) 221-224 |
| Maken S.; Park J.J.; Bhardwaj U.; Chander Singh K.; Park J.-W.; Han S.D.; Deshwal B.R.: (Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K. J.Chem.Thermodyn. 36 (2004) 309-315 |
Vapor-Liquid Equilibrium Data Overview
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