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 14914

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H10O 74.123 71-36-3 1-Butanol
2 C16H34 226.446 544-76-3 Hexadecane
Search the DDB for all data of this mixture

Constant Value

Temperature 293.18 K

Data Table

P [kPa] x1 [mol/mol]
0.2653 0.01750
0.35864 0.03160
0.4106 0.05050
0.4706 0.11770
0.5293 0.18610
0.5653 0.30010
0.5693 0.50430
0.584 0.58730
0.5933 0.66030
0.596 0.71820
0.6013 0.86010
0.6186 0.95850
0.620 1.00000

(P - pressure, x - liquid mole fraction)

Reference

Source
Banos I.; Sanchez F.; Perez P.; Valero J.; Gracia M.: Description of butan-1-ol + n-alkane systems by ERAS model. Fluid Phase Equilib. 81 (1992) 165-174


Vapor-Liquid Equilibrium Data Set 14915

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H10O 74.123 71-36-3 1-Butanol
2 C16H34 226.446 544-76-3 Hexadecane
Search the DDB for all data of this mixture

Constant Value

Temperature 298.14 K

Data Table

P [kPa] x1 [mol/mol]
0.35864 0.01740
0.4826 0.03140
0.580 0.05030
0.6653 0.11750
0.740 0.18590
0.8026 0.29990
0.8186 0.50420
0.8346 0.58720
0.8586 0.66030
0.8453 0.71820
0.8666 0.86000
0.8973 0.95850
0.9093 1.00000

(P - pressure, x - liquid mole fraction)

Reference

Source
Banos I.; Sanchez F.; Perez P.; Valero J.; Gracia M.: Description of butan-1-ol + n-alkane systems by ERAS model. Fluid Phase Equilib. 81 (1992) 165-174


Vapor-Liquid Equilibrium Data Set 14916

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H10O 74.123 71-36-3 1-Butanol
2 C16H34 226.446 544-76-3 Hexadecane
Search the DDB for all data of this mixture

Constant Value

Temperature 303.10 K

Data Table

P [kPa] x1 [mol/mol]
0.4653 0.01730
0.640 0.03120
0.7786 0.05010
0.9293 0.11730
1.028 0.18570
1.112 0.29970
1.1572 0.50410
1.176 0.58720
1.212 0.66020
1.204 0.71820
1.2212 0.86000
1.2786 0.95850
1.3012 1.00000

(P - pressure, x - liquid mole fraction)

Reference

Source
Banos I.; Sanchez F.; Perez P.; Valero J.; Gracia M.: Description of butan-1-ol + n-alkane systems by ERAS model. Fluid Phase Equilib. 81 (1992) 165-174

Diagrams

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

List of All References

Source
Banos I.; Sanchez F.; Perez P.; Valero J.; Gracia M.: Description of butan-1-ol + n-alkane systems by ERAS model. Fluid Phase Equilib. 81 (1992) 165-174

Vapor-Liquid Equilibrium Data Overview


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