Dortmund Data Bank

Solid-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.



Solid-Liquid Equilibrium Data Set 450

Components

No. Formula Molar Mass CAS Registry Number Name
1 CH4 16.043 74-82-8 Methane
2 C6H14 86.177 110-54-3 Hexane
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Data Table

T [K] xL1 [mol/mol]
176.20 0.08500
174.60 0.16200
173.10 0.24300
173.20 0.24600
172.50 0.28300
171.10 0.31500
170.60 0.35000
170.10 0.37000
168.80 0.43100
169.00 0.43200
167.90 0.45700
166.30 0.51200
166.30 0.52700
165.10 0.59300
163.80 0.65900
163.40 0.68400
162.90 0.73600
162.70 0.76400
162.30 0.79500
162.10 0.87500
161.70 0.91900
161.70 0.93800

(P - pressure, T - temperature, xl - liquid mole fraction)

Reference

Source
Dickinson E.; Knobler C.M.; Scott R.L.: Solid-Liquid Phase Equilibria in the Mixtures Methane + n-Hexane and Methane + n-Pentane. J.Chem.Soc.Faraday Trans.1 69 (1973) 2179-2187

Solid-Liquid Equilibrium Data Set 639

Components

No. Formula Molar Mass CAS Registry Number Name
1 CH4 16.043 74-82-8 Methane
2 C6H14 86.177 110-54-3 Hexane
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Data Table

T [K] P [bar] xL1 [mol/mol]
164.00 17.23 0.66050
162.00 16.755 0.92250
160.00 15.7 0.95790
158.00 14.516 0.97220
156.00 13.372 0.97730
154.00 12.308 0.98170
152.00 11.315 0.98510
150.00 10.383 0.98780
148.00 9.482 0.98990
146.00 8.702 0.99150
144.00 7.901 0.99290
142.00 7.314 0.99400
140.00 6.564 0.99490
138.00 5.875 0.99580

(P - pressure, T - temperature, xl - liquid mole fraction)

Reference

Source
Luks K.D.; Hottovy J.D.; Kohn J.P.: Three-Phase Solid-Liquid-Vapor Equilibria in the Binary Hydrocarbon Systems Methane-n-Hexane and Methane-Benzene. J.Chem.Eng.Data 26 (1981) 402-403

Comment: SVLE Molar volume of liquid given


Diagrams

Solid-Liquid Equilibrium of Hexane+Methane
See larger image

Solid-Liquid Equilibrium Data Overview


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