Specific Heat Capacity Gases
Reference data and engineering information about specific heat capacity gases for thermodynamics applications.
Overview
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The specific heat capacity of a gas describes how much energy is required to change its temperature. Gases have two distinct values: c_p (constant pressure) and c_v (constant volume). Their ratio, κ = c_p/c_v, governs isentropic processes such as compression and expansion in turbines, compressors, and nozzles.
For an ideal gas the individual gas constant satisfies:
R = c_p − c_v
All values below are approximate at 20 °C (68 °F) and 1 atm (14.7 psia).
Key Formulas
| Relationship | Equation | Description |
|---|---|---|
| Specific heat ratio | κ = c_p / c_v | Also called the isentropic exponent |
| Individual gas constant | R = c_p − c_v | Derived from Mayer's relation |
| Universal gas constant | R̄ = M · R | R̄ ≈ 8.314 kJ/(kmol·K) |
| Specific heat at constant volume | c_v = R / (κ − 1) | From combining the two relations above |
| Specific heat at constant pressure | c_p = κ · R / (κ − 1) | Equivalently c_p = κ · c_v |
Variables
| Symbol | Meaning | Typical SI Unit |
|---|---|---|
| c_p | Specific heat at constant pressure | kJ/(kg·K) |
| c_v | Specific heat at constant volume | kJ/(kg·K) |
| κ | Specific heat ratio (isentropic exponent) | dimensionless |
| R | Individual gas constant | kJ/(kg·K) |
| R̄ | Universal gas constant (≈ 8.314) | kJ/(kmol·K) |
| M | Molar mass | kg/kmol |
Specific Heat Capacity Data
Gas or Vapor | Formula | c_p(kJ/(kg·K)) | c_v(kJ/(kg·K)) | c_p(Btu/(lbm degF)) | c_v(Btu/(lbm degF)) | κ | R(kJ/(kg·K)) | R(ft lbf/(lbm degR)) |
|---|---|---|---|---|---|---|---|---|
| Acetone | (CH₃)₂CO | 1.47 | 1.32 | 0.35 | 0.32 | 1.11 | 0.15 | |
| Acetylene | C₂H₂ | 1.69 | 1.37 | 0.35 | 0.27 | 1.232 | 0.319 | 59.34 |
| Air | — | 1.007 | 0.718 | 0.24 | 0.17 | 1.4 | 0.287 | 53.34 |
| Ammonia | NH₃ | 2.16 | 1.66 | 0.52 | 0.4 | 1.31 | 0.53 | 96.5 |
| Argon | Ar | 0.52 | 0.312 | 0.12 | 0.07 | 1.667 | 0.208 | |
| Benzene | C₆H₆ | 1.09 | 0.99 | 0.26 | 0.24 | 1.12 | 0.1 | |
| Bromine | Br₂ | 0.25 | 0.2 | 0.06 | 0.05 | 1.28 | 0.05 | |
| Butane | C₄H₁₀ | 1.67 | 1.53 | 0.395 | 0.356 | 1.094 | 0.143 | 26.5 |
| Carbon dioxide | CO₂ | 0.846 | 0.655 | 0.21 | 0.16 | 1.289 | 0.189 | 38.86 |
| Carbon monoxide | CO | 1.02 | 0.72 | 0.24 | 0.17 | 1.4 | 0.297 | 55.14 |
| Carbon disulphide | CS₂ | 0.67 | 0.55 | 0.16 | 0.13 | 1.21 | 0.12 | |
| Chlorine | Cl₂ | 0.48 | 0.36 | 0.12 | 0.09 | 1.34 | 0.12 | |
| Chloroform | CHCl₃ | 0.63 | 0.55 | 0.15 | 0.13 | 1.15 | 0.08 | |
| Ethanol | C₂H₅OH | 1.88 | 1.67 | 0.45 | 0.4 | 1.13 | 0.22 | |
| Methanol | CH₃OH | 1.93 | 1.53 | 0.46 | 0.37 | 1.26 | 0.39 |
Source: engineeringtoolbox.com
Monoatomic vs Diatomic Gas Comparison
Specific Heat Ratio κ by Gas
Calculator: Derive c_p from R and κ
For an ideal gas with known individual gas constant R and specific heat ratio κ, you can compute both specific heats.
Ideal Gas Specific Heats from R and κ
Unit Converter
The source page included a specific heat Unit Converter. This migrated converter preserves the common engineering units for gas specific heat and gas constants.
Gas Specific Heat Unit Converter
Restored Original Source Tables
The following tables are restored from the original source page to preserve the complete reference data.
Gases - Specific Heats and Individual Gas Constants
The source table includes SI columns for cp and cv, Imperial columns for cp and cv in Btu/(lbm °F), the ratio cp/cv, and the individual gas constant R = cp - cv in both kJ/(kg K) and ft lbf/(lbm °R). All of those original data columns are retained below; the final two columns represent the source's cp-cv / individual gas constant values.
Gas or Vapor | Formula | cp (kJ/kgK) | cv (kJ/kgK) | cp (Btu/(lbmoF)) | cv (Btu/(lbmoF)) | κ = cp/cv | cp-cv (kJ/kgK) | cp-cv (ft lbf/(lbmoR)) |
|---|---|---|---|---|---|---|---|---|
| Acetone | (CH3)2CO | 1.47 | 1.32 | 0.35 | 0.32 | 1.11 | 0.15 | |
| Acetylene | C2H2 | 1.69 | 1.37 | 0.35 | 0.27 | 1.232 | 0.319 | 59.34 |
| Air | 1.007 | 0.718 | 0.24 | 0.17 | 1.4 | 0.287 | 53.34 | |
| Alcohol (ethanol) | C2H5OH | 1.88 | 1.67 | 0.45 | 0.4 | 1.13 | 0.22 | |
| Alcohol (methanol) | CH3OH | 1.93 | 1.53 | 0.46 | 0.37 | 1.26 | 0.39 | |
| Ammonia | NH3 | 2.16 | 1.66 | 0.52 | 0.4 | 1.31 | 0.53 | 96.5 |
| Argon | Ar | 0.52 | 0.312 | 0.12 | 0.07 | 1.667 | 0.208 | |
| Benzene | C6H6 | 1.09 | 0.99 | 0.26 | 0.24 | 1.12 | 0.1 | |
| Blast furnace gas | 1.03 | 0.73 | 0.25 | 0.17 | 1.41 | 0.3 | 55.05 | |
| Bromine | Br2 | 0.25 | 0.2 | 0.06 | 0.05 | 1.28 | 0.05 | |
| Butane | C4H10 | 1.67 | 1.53 | 0.395 | 0.356 | 1.094 | 0.143 | 26.5 |
| Carbon dioxide | CO2 | 0.8459 | 0.655 | 0.21 | 0.16 | 1.289 | 0.189 | 38.86 |
| Carbon monoxide | CO | 1.02 | 0.72 | 0.24 | 0.17 | 1.4 | 0.297 | 55.14 |
| Carbon disulphide | CS2 | 0.67 | 0.55 | 0.16 | 0.13 | 1.21 | 0.12 | |
| Chlorine | Cl2 | 0.48 | 0.36 | 0.12 | 0.09 | 1.34 | 0.12 | |
| Chloroform | CHCl3 | 0.63 | 0.55 | 0.15 | 0.13 | 1.15 | 0.08 | |
| Coal gas | 2.14 | 1.59 | ||||||
| Combustion products | 1 | 0.24 | ||||||
| Ethane | C2H6 | 1.75 | 1.48 | 0.39 | 0.32 | 1.187 | 0.276 | 51.5 |
| Ether (diethyl ether) | (C2H5)2O | 2.01 | 1.95 | 0.48 | 0.47 | 1.03 | 0.06 | |
| Ethylene | C2H4 | 1.53 | 1.23 | 0.4 | 0.33 | 1.24 | 0.296 | 55.08 |
| Chlorodifluoromethane, R-22 | CHClF2 | 1.18 | ||||||
| Helium | He | 5.251 | 3.12 | 1.25 | 0.75 | 1.667 | 2.08 | 386.3 |
| Hexane | C6H14 | 1.06 | ||||||
| Hydrochloric acid | 0.795 | 0.567 | ||||||
| Hydrogen | H2 | 14.32 | 10.16 | 3.42 | 2.43 | 1.405 | 4.12 | 765.9 |
| Hydrogen Chloride | HCl | 0.8 | 0.57 | 0.191 | 0.135 | 1.41 | 0.23 | 42.4 |
| Hydrogen Sulfide | H2S | 0.243 | 0.187 | 1.32 | 45.2 | |||
| Hydroxyl | OH | 1.76 | 1.27 | 1.384 | 0.489 | |||
| Krypton | Kr | 0.25 | 0.151 | |||||
| Methane | CH4 | 2.22 | 1.7 | 0.59 | 0.45 | 1.304 | 0.518 | 96.4 |
| Methyl Chloride | CH3Cl | 0.24 | 0.2 | 1.2 | 30.6 | |||
| Natural Gas | 2.34 | 1.85 | 0.56 | 0.44 | 1.27 | 0.5 | 79.1 | |
| Neon | Ne | 1.03 | 0.618 | 1.667 | 0.412 | |||
| Nitric Oxide | NO | 0.995 | 0.718 | 0.23 | 0.17 | 1.386 | 0.277 | |
| Nitrogen | N2 | 1.041 | 0.743 | 0.25 | 0.18 | 1.4 | 0.297 | 54.99 |
| Nitrogen tetroxide | N2O4 | 4.69 | 4.6 | 1.12 | 1.1 | 1.02 | 0.09 | |
| Nitrous oxide | N2O | 0.88 | 0.69 | 0.21 | 0.17 | 1.27 | 0.18 | 35.1 |
| Oxygen | O2 | 0.9189 | 0.659 | 0.22 | 0.16 | 1.395 | 0.26 | 48.24 |
| Pentane | C5H12 | 1.07 | ||||||
| Propane | C3H8 | 1.67 | 1.48 | 0.39 | 0.34 | 1.13 | 0.189 | 35 |
| Propene (propylene) | C3H6 | 1.5 | 1.31 | 0.36 | 0.31 | 1.15 | 0.18 | 36.8 |
| Water Vapor Steam 1 psia. 120 – 600 oF | H2O | 1.93 | 1.46 | 0.46 | 0.35 | 1.32 | 0.462 | |
| Steam 14.7 psia. 220 – 600 oF | H2O | 1.97 | 1.5 | 0.47 | 0.36 | 1.31 | 0.46 | |
| Steam 150 psia. 360 – 600 oF | H2O | 2.26 | 1.76 | 0.54 | 0.42 | 1.28 | 0.5 | |
| Sulfur dioxide (Sulphur dioxide) | SO2 | 0.64 | 0.51 | 0.15 | 0.12 | 1.29 | 0.13 | 24.1 |
| Xenon | Xe | 0.16 | 0.097 |
Source: engineeringtoolbox.com
For conversion of units, use the Specific heat online unit converter.
See also tabulated values of specific heat capacity of food and foodstuff, metals and semimetals, common liquids and fluids, common solids and other common substances as well as values of molar heat capacity of common organic substances and inorganic substances.
See Also
The source cross-references tabulated values of specific heat capacity of food and foodstuff, metals and semimetals, common liquids and fluids, common solids and other common substances, plus molar heat capacity values for common organic and inorganic substances.
Engineering Notes
- See also specific heat for common solids, food and foodstuff, metals and semimetals, liquids and fluids, and other related heat-capacity tables.
- Ideal-gas assumption: The listed values assume ideal-gas behaviour. At high pressures or near the saturation line, real-gas corrections (departure functions) become significant.
- Temperature dependence: Specific heats increase with temperature, especially for polyatomic gases. The values here apply near 20 °C; for combustion or cryogenic work, use temperature-dependent correlations (e.g., polynomial fits from NIST-JANAF tables).
- Monatomic gases (He, Ar, Ne) have κ ≈ 5/3 = 1.667, a theoretical result from kinetic theory. Diatomic gases near room temperature have κ ≈ 1.4.
- Specific heat ratio κ directly sets isentropic relations: T₂/T₁ = (p₂/p₁)^((κ−1)/κ). A small error in κ can propagate into large errors in compressor or turbine outlet temperatures.
- Blast furnace gas and other fuel-gas mixtures should be treated with caution—composition varies with process conditions.
- R = c_p − c_v holds exactly only for ideal gases. For real gases, Mayer's relation includes a correction term involving the equation of state.
- The individual gas constant R is related to the universal gas constant R̄ by R = R̄ / M, where M is the molar mass in kg/kmol.