Dortmund Data Bank
Vapor Pressure of Methane
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.
Component
Formula |
Molar Mass |
CAS Registry Number |
Name |
CH4 |
16.043 |
74-82-8 |
Methane |
Search the DDB for all data of Methane
Diagrams
Data Table
T [K] |
P [kPa] |
State |
Reference |
76.89 |
1.1626 |
Solid-Gas |
5 |
79.75 |
2.000 |
Solid-Gas |
5 |
81.74 |
2.9064 |
Solid-Gas |
5 |
83.82 |
4.104 |
Solid-Gas |
5 |
85.42 |
5.368 |
Solid-Gas |
5 |
87.25 |
7.113 |
Solid-Gas |
5 |
92.15 |
14.012 |
Vapor-Liquid |
4 |
93.15 |
15.852 |
Vapor-Liquid |
4 |
94.15 |
17.918 |
Vapor-Liquid |
4 |
95.15 |
20.145 |
Vapor-Liquid |
4 |
96.15 |
22.611 |
Vapor-Liquid |
4 |
96.30 |
26.265 |
Vapor-Liquid |
2 |
97.15 |
25.331 |
Vapor-Liquid |
4 |
97.20 |
29.064 |
Vapor-Liquid |
2 |
97.60 |
31.064 |
Vapor-Liquid |
2 |
98.15 |
28.278 |
Vapor-Liquid |
4 |
98.60 |
34.797 |
Vapor-Liquid |
2 |
99.15 |
31.477 |
Vapor-Liquid |
4 |
99.40 |
38.130 |
Vapor-Liquid |
2 |
100.15 |
34.931 |
Vapor-Liquid |
4 |
101.15 |
38.663 |
Vapor-Liquid |
4 |
102.15 |
42.716 |
Vapor-Liquid |
4 |
103.15 |
47.090 |
Vapor-Liquid |
4 |
104.15 |
51.836 |
Vapor-Liquid |
4 |
105.15 |
56.955 |
Vapor-Liquid |
4 |
106.15 |
62.422 |
Vapor-Liquid |
4 |
107.15 |
68.288 |
Vapor-Liquid |
4 |
108.15 |
74.567 |
Vapor-Liquid |
4 |
109.15 |
81.273 |
Vapor-Liquid |
4 |
109.20 |
92.792 |
Vapor-Liquid |
2 |
109.80 |
98.392 |
Vapor-Liquid |
2 |
110.15 |
88.499 |
Vapor-Liquid |
4 |
112.35 |
111.109 |
Vapor-Liquid |
3 |
117.82 |
164.850 |
Vapor-Liquid |
3 |
120.48 |
199.173 |
Vapor-Liquid |
3 |
122.71 |
233.791 |
Vapor-Liquid |
3 |
124.90 |
269.977 |
Vapor-Liquid |
3 |
126.96 |
308.321 |
Vapor-Liquid |
3 |
128.33 |
336.270 |
Vapor-Liquid |
3 |
130.25 |
378.341 |
Vapor-Liquid |
3 |
131.41 |
405.309 |
Vapor-Liquid |
3 |
131.77 |
402.073 |
Vapor-Liquid |
6 |
132.13 |
423.059 |
Vapor-Liquid |
3 |
135.60 |
512.790 |
Vapor-Liquid |
3 |
136.14 |
490.332 |
Vapor-Liquid |
6 |
137.91 |
581.240 |
Vapor-Liquid |
3 |
139.86 |
588.399 |
Vapor-Liquid |
6 |
140.23 |
655.575 |
Vapor-Liquid |
3 |
140.67 |
686.465 |
Vapor-Liquid |
6 |
142.21 |
724.613 |
Vapor-Liquid |
3 |
144.20 |
800.026 |
Vapor-Liquid |
3 |
145.41 |
784.532 |
Vapor-Liquid |
6 |
146.49 |
892.405 |
Vapor-Liquid |
6 |
146.70 |
900.545 |
Vapor-Liquid |
3 |
147.84 |
950.068 |
Vapor-Liquid |
3 |
148.40 |
990.472 |
Vapor-Liquid |
6 |
149.80 |
1037.250 |
Vapor-Liquid |
3 |
150.00 |
1078.730 |
Vapor-Liquid |
6 |
151.75 |
1186.600 |
Vapor-Liquid |
6 |
152.41 |
1163.170 |
Vapor-Liquid |
3 |
154.07 |
1284.670 |
Vapor-Liquid |
6 |
155.46 |
1328.600 |
Vapor-Liquid |
3 |
155.82 |
1372.930 |
Vapor-Liquid |
6 |
156.65 |
1395.490 |
Vapor-Liquid |
3 |
157.27 |
1471.000 |
Vapor-Liquid |
6 |
158.50 |
1506.100 |
Vapor-Liquid |
3 |
160.04 |
1657.320 |
Vapor-Liquid |
6 |
161.15 |
1675.560 |
Vapor-Liquid |
3 |
161.61 |
1863.260 |
Vapor-Liquid |
6 |
164.31 |
1893.170 |
Vapor-Liquid |
3 |
165.84 |
2079.010 |
Vapor-Liquid |
6 |
167.40 |
2126.380 |
Vapor-Liquid |
3 |
169.01 |
2333.980 |
Vapor-Liquid |
6 |
170.52 |
2381.050 |
Vapor-Liquid |
3 |
173.27 |
2624.260 |
Vapor-Liquid |
3 |
173.38 |
2716.440 |
Vapor-Liquid |
6 |
175.74 |
2759.690 |
Vapor-Liquid |
3 |
176.22 |
2981.220 |
Vapor-Liquid |
6 |
178.09 |
3092.330 |
Vapor-Liquid |
3 |
179.10 |
3285.230 |
Vapor-Liquid |
6 |
179.83 |
3276.210 |
Vapor-Liquid |
3 |
180.00 |
3286.850 |
Vapor-Liquid |
1 |
180.00 |
3393.100 |
Vapor-Liquid |
6 |
180.92 |
3500.970 |
Vapor-Liquid |
6 |
181.82 |
3495.380 |
Vapor-Liquid |
3 |
182.00 |
3508.870 |
Vapor-Liquid |
1 |
183.32 |
3668.470 |
Vapor-Liquid |
3 |
184.00 |
3742.280 |
Vapor-Liquid |
1 |
186.00 |
3987.820 |
Vapor-Liquid |
1 |
186.24 |
4026.120 |
Vapor-Liquid |
3 |
186.47 |
4030.830 |
Vapor-Liquid |
3 |
187.00 |
4115.450 |
Vapor-Liquid |
1 |
187.46 |
4181.850 |
Vapor-Liquid |
3 |
187.54 |
4190.380 |
Vapor-Liquid |
3 |
188.00 |
4246.550 |
Vapor-Liquid |
1 |
189.00 |
4381.370 |
Vapor-Liquid |
1 |
189.01 |
4392.200 |
Vapor-Liquid |
3 |
189.50 |
4450.300 |
Vapor-Liquid |
1 |
189.80 |
4492.200 |
Vapor-Liquid |
1 |
190.00 |
4520.370 |
Vapor-Liquid |
1 |
190.10 |
4534.540 |
Vapor-Liquid |
1 |
190.20 |
4548.760 |
Vapor-Liquid |
1 |
190.25 |
4559.600 |
Vapor-Liquid |
3 |
190.30 |
4563.040 |
Vapor-Liquid |
1 |
190.40 |
4577.380 |
Vapor-Liquid |
1 |
190.45 |
4584.580 |
Vapor-Liquid |
1 |
190.50 |
4591.800 |
Vapor-Liquid |
1 |
190.53 |
4596.150 |
Vapor-Liquid |
1 |
List of References
Number |
Source |
1 |
Kleinrahm R.; Duschek W.; Wagner W.: (Pressure, density, temperature) measurements in the critical region of methane. J.Chem.Thermodyn. 18 (1986) 1103-1114 |
2 |
Hunter M.A.: The Molecular Aggregation of Liquefied Gases. J.Phys.Chem. 10 (1906) 330-360 |
3 |
Van Itterbeek A.; Staes K.; Verbeke O.; Theeuwes F.: Vapour pressure of saturated liquid methane. Physica (Amsterdam) 30 (1964) 1896-1900 |
4 |
Stock A.; Henning F.; Kuß E.: Dampfdrucktafeln fuer Temperaturbestimmungen zwischen +25°C und -185°C. Ber.Dtsch.Chem.Ges./B:Abhandl. 54 (1921) 1119-1129 |
5 |
Karwat E.: Der Dampfdruck des festen Chlorwasserstoffs, Methans und Ammoniaks. Z.Phys.Chem.(Leipzig) 112 (1924) 486-490 |
6 |
Eucken A.; Berger W.: Das I-T-Diagramm des Methans. Z.Ges.Kälteindustrie 41 (1934) 145-152 |
Pure Component Data Overview
© DDBST GmbH