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 640

Components

No. Formula Molar Mass CAS Registry Number Name
1 CH4 16.043 74-82-8 Methane
2 C6H6 78.114 71-43-2 Benzene
Search the DDB for all data of this mixture

Data Table

T [K] P [bar] xL1 [mol/mol]
277.70 10.13 0.01850
276.80 20.26 0.03650
275.80 30.39 0.05670
274.90 40.52 0.07530
273.90 50.65 0.09810
273.10 60.78 0.11760
272.20 70.91 0.14020
271.60 81.04 0.15560
270.90 91.17 0.17510
270.40 101.3 0.19080
269.90 111.43 0.20690
269.40 121.56 0.22250
269.00 131.7 0.23580
268.70 141.82 0.24650
268.40 151.95 0.25910
268.20 162.08 0.26920
268.10 172.2 0.27540
190.50 46.25 0.99985
185.00 38.9 0.99983
180.00 33.226 0.99984
175.00 30.086 0.99985
170.00 23.603 0.99986
165.00 19.753 0.99989

(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


Solid-Liquid Equilibrium Data Set 651

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 CH4 16.043 74-82-8 Methane
Search the DDB for all data of this mixture

Data Table

T [K] P [bar] xL1 [mol/mol]
199.80 136.8 0.00140
199.80 126.1 0.00129
199.80 105.4 0.00108
188.70 136.1 0.000916
188.70 125.4 0.000868
188.70 105.4 0.000779
183.10 136.1 0.000711
183.10 105.4 0.000614
183.10 86.1 0.000537
183.10 61.3 0.00044
183.10 54.1 0.000419
177.60 54.1 0.000363
172.00 54.1 0.000293
166.40 135.8 0.000295
166.40 105.4 0.00027
166.40 86.1 0.000252
166.40 54.1 0.000226
160.90 54.1 0.000167
155.30 54.1 0.000122
149.80 54.1 8.189999789E-5
144.20 135.8 6.209999992E-5
144.20 126.1 6.140000187E-5
144.20 105.4 5.890000102E-5
144.20 83.7 5.650000094E-5
144.20 69.9 5.450000026E-5
144.20 60.6 0.000055
144.20 54.1 5.470000178E-5
138.60 54.1 3.490000017E-5
133.00 54.1 2.060000043E-5
127.40 54.1 1.250000059E-5
125.10 54.1 9.700000192E-6
121.80 136.1 7.600000117E-6
121.80 54.1 7.099999948E-6
116.20 54.1 3.600000127E-6
110.60 54.1 0.000002
105.00 54.1 9.000000318E-7
99.40 54.1 3.899999967E-7

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

Reference

Source
Kuebler G.P.; McKinley C.: Solubility of Solid Benzene, Toluene, n-Hexane, and n-Heptane in Liquid Methane. Proceedings of the 1973 Cryogenic Engineering Conference 19 (1974) 320-326

Comment: SVLE Molar volume of liquid given


Solid-Liquid Equilibrium Data Set 775

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 CH4 16.043 74-82-8 Methane
Search the DDB for all data of this mixture

Data Table

T [K] xL1 [mol/mol]
153.10 0.000081
162.80 0.000118
175.00 0.000202
177.90 0.00027
180.10 0.000403
185.40 0.000483

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

Reference

Source
Neumann A.; Mann R.; von Szalghary W.-D.: Löslichkeit von festem Benzol in flüssigen Kohlenwasserstoffen. Kältetechnik, Klimatisierung 24 (1972) 145-149

Diagrams

Solid-Liquid Equilibrium of Benzene+Methane
See larger image

Solid-Liquid Equilibrium Data Overview


© DDBST GmbH