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 36204

Components

No. Formula Molar Mass CAS Registry Number Name
1 H2O 18.015 7732-18-5 Water
2 C4H10O 74.123 71-36-3 1-Butanol
3 C8H10 106.167 106-42-3 p-Xylene
Search the DDB for all data of this mixture

Constant Value

Pressure 101.30 kPa

Data Table

T [K] x1 [mol/mol] x2 [mol/mol] y1 [mol/mol] y2 [mol/mol]
368.02 0.31200 0.67600 0.73700 0.24500
369.39 0.26400 0.72400 0.70400 0.27900
369.92 0.25300 0.73500 0.70800 0.27600
371.26 0.23100 0.76100 0.68400 0.30300
373.42 0.18400 0.80900 0.66700 0.32200
375.18 0.15200 0.84300 0.61200 0.37900
377.07 0.12600 0.86900 0.56000 0.43300
379.28 0.10000 0.89500 0.54400 0.45000
379.73 0.10900 0.88700 0.47600 0.51800
378.00 0.10900 0.87400 0.52400 0.45300
375.83 0.13400 0.83400 0.59700 0.36600
372.21 0.17800 0.77700 0.65200 0.30100
370.44 0.20400 0.73800 0.65900 0.28500
368.14 0.25300 0.67500 0.69300 0.23700
366.56 0.28600 0.62900 0.70700 0.21300
365.23 0.31600 0.58700 0.70300 0.20400
365.05 0.41800 0.54100 0.72600 0.21700
365.13 0.44300 0.52700 0.73300 0.22000
365.43 0.42000 0.55200 0.73400 0.22300
365.86 0.39600 0.57800 0.73500 0.22900
366.09 0.38100 0.59300 0.73600 0.22700
366.40 0.35700 0.62000 0.73700 0.22900
365.75 0.24200 0.60400 0.69500 0.19200
364.71 0.27400 0.55700 0.68700 0.18800
367.16 0.23000 0.62700 0.68500 0.21400
369.18 0.19500 0.68100 0.64900 0.25600
371.49 0.17200 0.72400 0.62700 0.28700
373.95 0.13800 0.77700 0.60400 0.32100
376.87 0.10600 0.82600 0.52000 0.41300
378.99 0.09200 0.85700 0.43500 0.51100
380.55 0.08300 0.89300 0.39900 0.57000
384.65 0.04800 0.94400 0.26700 0.72000
384.04 0.04800 0.92100 0.28300 0.67700
383.20 0.04700 0.89100 0.29500 0.63600
382.13 0.05700 0.84800 0.29900 0.60500
381.41 0.05300 0.80600 0.31800 0.55500
381.95 0.04300 0.78300 0.30100 0.55300
382.20 0.03900 0.75200 0.27600 0.55700
382.91 0.03700 0.71500 0.26100 0.55500
382.49 0.03300 0.67400 0.25500 0.54400
379.96 0.04300 0.62300 0.35900 0.44500
378.12 0.05400 0.57300 0.43600 0.37300
376.45 0.05600 0.52600 0.46800 0.33900
375.26 0.05900 0.48700 0.49600 0.31200
374.66 0.05500 0.44600 0.54800 0.27200
373.80 0.06000 0.40600 0.57400 0.24800
372.87 0.06300 0.36200 0.58500 0.23500
371.08 0.05800 0.33100 0.61800 0.20500
368.21 0.14000 0.52000 0.65500 0.20200
369.19 0.13300 0.54900 0.64100 0.21700
371.55 0.10700 0.60100 0.59700 0.26000
373.58 0.09700 0.66600 0.54500 0.31400
376.41 0.08200 0.71600 0.46500 0.39500
377.94 0.08100 0.75000 0.44800 0.42300

(T - temperature, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Gomis V.; Font A.; Saquete M.D.; Garcia-Cano J.: Isothermal (liquid + liquid) equilibrium data at T = 313.15 K and isobaric (vapor + liquid + liquid) equilibrium data at 101.3 kPa for the ternary system (water + 1-butanol + p-xylene). J.Chem.Thermodyn. 79 (2014) 242-247

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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