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 |
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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 |
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 |
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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: Data also cited/presented in L100727 as result of literature survey
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 |
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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 Data Overview
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