Methane · CH4
Methane (CH4, CAS 74-82-8) is an industrial and utility gas; this page gives its density, heat capacity and viscosity from 1 to 200 bar and -20 to 100 °C.
Values are computed from CoolProp==6.6.0 - reference Helmholtz equation of state for Methane (single-phase density, isobaric heat capacity and dynamic viscosity) and tabulated over 1–200 bar (absolute) and -20–100 °C.
- Also known as
- CH4, natural gas (pure component), marsh gas, R-50
- CAS number
- 74-82-8
- Tabulated range
- 1–200 bar · -20–100 °C
- Molar mass
- 16.043g/mol
- Critical temperature
- -82.59°C
- Critical pressure
- 45.992bar
- Normal boiling point
- -161.48°C
NIST Chemistry WebBook, SRD 69 - Thermophysical Properties of Fluid Systems. NIST Chemistry WebBook, SRD 69, Thermophysical Properties of Fluid Systems, methane (CH4, CAS 74-82-8): molar mass, critical point and normal boiling point. https://webbook.nist.gov/cgi/fluid.cgi?ID=C74828&Action=Page
- Density · 1 bar
- 0.6483kg/m³
- Density · 200 bar
- 157.1kg/m³
- Heat capacity · 1 bar
- 2232J/kg·K
- Viscosity · 1 bar
- 11.196uPa.s
- Compressibility · 200 bar
- 0.824Z
Read a value at any pressure and temperature
Set a pressure (bar absolute) and a temperature (°C) to interpolate between the tabulated grid points. The readout and chart never go outside the validated 1–200 bar and -20–100 °C range, and every number is interpolated from the committed table below — nothing is computed from an equation of state in your browser.
Values are interpolated between the tabulated grid points below — pressure (bar absolute) and temperature (°C) stay within the validated 1–200 bar and -20–100 °C range and are never extrapolated.
- Density
- 0.6483 kg/m³
- Specific volume
- 1.542 m³/kg
- Compressibility Z
- 0.9982
- Heat capacity
- 2232 J/kg·K
- Viscosity
- 11.196 uPa.s
Every tabulated point
Rows are temperature (°C); columns are pressure (bar absolute). Read the cell at the intersection. Density is the single-phase fluid density at that state.
| °C \ bar | 1 | 2 | 5 | 10 | 20 | 50 | 100 | 200 |
|---|---|---|---|---|---|---|---|---|
| -20 | 0.7645 | 1.5337 | 3.8699 | 7.8622 | 16.24 | 45.17 | 108.4 | 217.8 |
| 0 | 0.7081 | 1.4195 | 3.5740 | 7.2343 | 14.83 | 39.98 | 90.04 | 186.7 |
| 15 | 0.6709 | 1.3445 | 3.3811 | 6.8292 | 13.93 | 36.98 | 80.86 | 167.8 |
| 25 | 0.6483 | 1.2988 | 3.2639 | 6.5848 | 13.40 | 35.27 | 75.99 | 157.1 |
| 50 | 0.5979 | 1.1972 | 3.0045 | 6.0470 | 12.25 | 31.73 | 66.60 | 135.9 |
| 75 | 0.5547 | 1.1105 | 2.7840 | 5.5935 | 11.29 | 28.93 | 59.70 | 120.4 |
| 100 | 0.5174 | 1.0356 | 2.5941 | 5.2053 | 10.48 | 26.64 | 54.35 | 108.5 |
| °C \ bar | 1 | 2 | 5 | 10 | 20 | 50 | 100 | 200 |
|---|---|---|---|---|---|---|---|---|
| -20 | 2149 | 2158 | 2186 | 2235 | 2345 | 2802 | 4009 | 4111 |
| 0 | 2181 | 2188 | 2211 | 2250 | 2335 | 2653 | 3370 | 3899 |
| 15 | 2210 | 2216 | 2236 | 2269 | 2341 | 2596 | 3125 | 3697 |
| 25 | 2232 | 2237 | 2255 | 2286 | 2350 | 2573 | 3018 | 3570 |
| 50 | 2293 | 2298 | 2313 | 2337 | 2388 | 2555 | 2865 | 3320 |
| 75 | 2365 | 2369 | 2380 | 2400 | 2442 | 2573 | 2804 | 3168 |
| 100 | 2443 | 2447 | 2457 | 2473 | 2507 | 2614 | 2795 | 3089 |
| °C \ bar | 1 | 2 | 5 | 10 | 20 | 50 | 100 | 200 |
|---|---|---|---|---|---|---|---|---|
| -20 | 9.725 | 9.737 | 9.776 | 9.850 | 10.030 | 10.910 | 13.997 | 23.701 |
| 0 | 10.390 | 10.402 | 10.442 | 10.515 | 10.686 | 11.432 | 13.649 | 20.883 |
| 15 | 10.877 | 10.889 | 10.929 | 11.001 | 11.165 | 11.843 | 13.691 | 19.615 |
| 25 | 11.196 | 11.209 | 11.249 | 11.320 | 11.480 | 12.122 | 13.792 | 19.044 |
| 50 | 11.978 | 11.991 | 12.030 | 12.099 | 12.250 | 12.821 | 14.183 | 18.242 |
| 75 | 12.738 | 12.751 | 12.789 | 12.856 | 12.999 | 13.518 | 14.681 | 17.982 |
| 100 | 13.479 | 13.491 | 13.528 | 13.592 | 13.728 | 14.206 | 15.231 | 18.018 |
Methane density at pressure (25 °C)
At 100 bar and 25 °C, methane density is about 76.0 kg/m³. At 200 bar and 25 °C, methane density is about 157.1 kg/m³.
Where the numbers come from
Every value on this page is computed by a deterministic equation of state — none is entered by hand. The generating method and the references it is checked against:
- ▸NIST Chemistry WebBook, SRD 69 - Thermophysical Properties of Fluid Systems (REFPROP-derived isothermal tables), methane (CAS 74-82-8)
- ▸CoolProp 6.6.0 - reference Helmholtz equation of state for Methane (Setzmann & Wagner, 1991); dynamic viscosity from the Quinones-Cisneros & Deiters, 2006 model
Model: CoolProp==6.6.0 - reference Helmholtz equation of state for Methane (single-phase density, isobaric heat capacity and dynamic viscosity) · Generated 2026-06-07
The committed data file for this page is published as JSON on GitHub under CC BY 4.0.
Checked against cited values
The equation of state is cross-checked against independently cited NIST WebBook reference points — a near-ambient and a compressed density, plus the heat-capacity and viscosity columns. The page is published only because every check passes.
| Property / point | Density · 1 bar · 25 °C |
| Cited reference value | 0.6483 kg/m3 |
| Model computed | 0.6483 kg/m3 |
| Error vs reference | 0% (tolerance 1%) |
NIST Chemistry WebBook, SRD 69 - Thermophysical Properties of Fluid Systems. NIST Chemistry WebBook, SRD 69, Thermophysical Properties of Fluid Systems, methane (CH4, CAS 74-82-8), isothermal table at 298.15 K: density at 1 bar = 0.64828 kg/m3. https://webbook.nist.gov/cgi/fluid.cgi?ID=C74828&Action=Page
| Property / point | Density · 200 bar · 25 °C |
| Cited reference value | 157.09 kg/m3 |
| Model computed | 157.0944 kg/m3 |
| Error vs reference | 0.003% (tolerance 1%) |
NIST Chemistry WebBook, SRD 69 - Thermophysical Properties of Fluid Systems. NIST Chemistry WebBook, SRD 69, Thermophysical Properties of Fluid Systems, methane (CH4, CAS 74-82-8), isothermal table at 298.15 K: density at 200 bar = 157.09 kg/m3. https://webbook.nist.gov/cgi/fluid.cgi?ID=C74828&Action=Page
| Property / point | Isobaric heat capacity · 1 bar · 25 °C |
| Cited reference value | 2231.6 J/kg.K |
| Model computed | 2231.6 J/kg.K |
| Error vs reference | 0% (tolerance 2%) |
NIST Chemistry WebBook, SRD 69 - Thermophysical Properties of Fluid Systems. NIST Chemistry WebBook, SRD 69, Thermophysical Properties of Fluid Systems, methane (CH4, CAS 74-82-8), isothermal table at 298.15 K: isobaric heat capacity Cp at 1 bar = 2231.6 J/kg.K. https://webbook.nist.gov/cgi/fluid.cgi?ID=C74828&Action=Page
| Property / point | Dynamic viscosity · 1 bar · 25 °C |
| Cited reference value | 11.076 uPa.s |
| Model computed | 11.196 uPa.s |
| Error vs reference | 1.085% (tolerance 2%) |
NIST Chemistry WebBook, SRD 69 - Thermophysical Properties of Fluid Systems. NIST Chemistry WebBook, SRD 69, Thermophysical Properties of Fluid Systems, methane (CH4, CAS 74-82-8), isothermal table at 298.15 K: dynamic viscosity at 1 bar = 11.076 uPa.s. https://webbook.nist.gov/cgi/fluid.cgi?ID=C74828&Action=Page
Before you use these numbers
- ▸CoolProp reference Helmholtz equation of state (Setzmann & Wagner, 1991) for methane; dynamic viscosity from the Quinones-Cisneros & Deiters, 2006 model. Single-phase density, isobaric heat capacity and dynamic viscosity, tabulated on a 1-200 bar (absolute) by -20 to 100 degC grid; two-phase, saturation and liquid states are out of scope for this page. The correlation is not extrapolated beyond the tabulated range. Values are for preliminary design; verify against vendor or reference data for critical service.
- ▸Every tabulated state is single-phase. A grid cell is left blank only where the state at that pressure and temperature would be two-phase or liquid - at or above the saturation pressure at that temperature - and the explorer will not interpolate across such a cell. Because the critical temperature of methane is -82.59 degC, below the -20 degC floor of this grid, every (pressure, temperature) point tabulated here is a supercritical single-phase fluid, so no cell is blank.
- ▸Values are tabulated only inside the 1–200 bar and -20–100 °C ranges shown; the equation of state is not extrapolated beyond them here.
- ▸Use for preliminary design; verify for critical service.
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