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 1330

Components

No. Formula Molar Mass CAS Registry Number Name
1 CHCl3 119.377 67-66-3 Chloroform
2 C4H10O 74.123 71-36-3 1-Butanol
Search the DDB for all data of this mixture

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
390.65 0.00000 0.00000
382.15 0.06450 0.52500
377.65 0.10000 0.63500
373.15 0.13420 0.75000
365.15 0.20000 0.85500
364.65 0.21000 0.90000
356.45 0.29240 0.91500
356.15 0.30000 0.88000
351.65 0.38150 0.94500
350.65 0.40000 0.91500
347.15 0.48100 0.94500
346.45 0.50000 0.92500
343.35 0.59000 0.94500
342.95 0.60000 0.94500
340.15 0.70000 0.94500
339.75 0.71250 0.96500
338.15 0.80000 0.98000
337.15 0.84750 0.96500
336.35 0.90000 0.98000
334.35 1.00000 1.00000

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

Reference

Source
Lepin L.K.; Matseevsky B.I.: Isobaric Binary System n-Butyl alcohol - Chloroform. Zinatniskie Raksti (Riga) 9 (1956) 65-67


Vapor-Liquid Equilibrium Data Set 1331

Components

No. Formula Molar Mass CAS Registry Number Name
1 CHCl3 119.377 67-66-3 Chloroform
2 C4H10O 74.123 71-36-3 1-Butanol
Search the DDB for all data of this mixture

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
388.25 0.01800 0.10000
386.95 0.03000 0.16400
379.55 0.07640 0.36600
372.85 0.13880 0.56800
366.55 0.20160 0.69500
363.45 0.22720 0.72800
362.45 0.24840 0.74800
357.95 0.30360 0.80800
357.55 0.31560 0.81200
355.35 0.34520 0.84000
353.15 0.38380 0.85600
351.85 0.40600 0.87000
350.65 0.42440 0.88200
348.25 0.47980 0.89800
347.75 0.49400 0.90500
346.15 0.53000 0.91900
343.95 0.59800 0.93200
342.35 0.65240 0.94400
340.35 0.72200 0.95500
339.45 0.76980 0.96000
338.55 0.80840 0.96800
337.65 0.85280 0.97400
337.05 0.90320 0.98200
335.75 0.95360 0.99100

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

Reference

Source
Rao B.V.S.; Rao C.V.: Isopiestic binary vapour liquid equilibria system chloroform (1) - n-butanol (2). Chem.Eng.Sci. 17 (1962) 574-576


Vapor-Liquid Equilibrium Data Set 16242

Components

No. Formula Molar Mass CAS Registry Number Name
1 CHCl3 119.377 67-66-3 Chloroform
2 C4H10O 74.123 71-36-3 1-Butanol
Search the DDB for all data of this mixture

Constant Value

Pressure 105.00 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
391.61 0.00000 0.00000
390.62 0.00910 0.04490
388.96 0.02130 0.12550
387.43 0.03570 0.18010
383.69 0.06120 0.30660
380.17 0.08650 0.39370
376.14 0.11950 0.49740
370.37 0.17070 0.61710
365.64 0.22030 0.68990
361.90 0.26440 0.75750
357.72 0.32470 0.80650
354.43 0.37730 0.84990
351.34 0.42780 0.87670
349.62 0.46240 0.89090
347.67 0.50910 0.91660
343.31 0.63860 0.94050
341.13 0.69670 0.94610
340.09 0.74450 0.94970
339.67 0.77980 0.96080
339.36 0.79810 0.96330
339.09 0.81130 0.96350
337.54 0.87550 0.97620
336.60 0.94000 0.98930
336.34 0.96610 0.98930
335.56 0.98040 0.99210
335.37 1.00000 1.00000

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

Reference

Source
Chen G.-H.; Wang Q.; Ma Z.M.; Yan X.-H.; Han S.-J.: Phase Equilibria at Superatmospheric Pressures for Systems Containing Halohydrocarbon, Aromatic Hydrocarbon, and Alcohol. J.Chem.Eng.Data 40 (1995) 361-366

Diagrams

Vapor-Liquid Equilibrium of 1-Butanol+Chloroform
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Vapor-Liquid Equilibrium of 1-Butanol+Chloroform
See larger image

List of All References

Source
Lepin L.K.; Matseevsky B.I.: Isobaric Binary System n-Butyl alcohol - Chloroform. Zinatniskie Raksti (Riga) 9 (1956) 65-67
Rao B.V.S.; Rao C.V.: Isopiestic binary vapour liquid equilibria system chloroform (1) - n-butanol (2). Chem.Eng.Sci. 17 (1962) 574-576
Chen G.-H.; Wang Q.; Ma Z.M.; Yan X.-H.; Han S.-J.: Phase Equilibria at Superatmospheric Pressures for Systems Containing Halohydrocarbon, Aromatic Hydrocarbon, and Alcohol. J.Chem.Eng.Data 40 (1995) 361-366

Vapor-Liquid Equilibrium Data Overview


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