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Specific heat ratio of common gases

Including isentropic coefficient of air, ammonia, natural gas, water vapor

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This page provides a data table for the specific heat ratio (isentropic coefficient) of various common gases. Utilize our interactive calculator below to perform quick estimations for isentropic processes, such as gas compression or expansion, using these coefficients.


Interactive Isentropic Process Calculator

⚠️ ENGINEERING NOTICE & EDUCATIONAL DISCLAIMER: This interactive calculator is provided exclusively for preliminary estimation and educational purposes. It is not intended for detailed design or equipment procurement without certified vendor rating. No warranty, expressed or implied, is provided, and no liability is assumed.
bar
°C
bar
Calculated Final Temperature (T2):
Calculated Final Pressure (P2):
Pressure Ratio (P2/P1):
Temperature Ratio (T2/T1):

Isentropic Process Formulas

The following formulas describe the relationship between pressure (P), temperature (T), and volume (V) for an ideal gas undergoing a reversible adiabatic (isentropic) process, where \(k\) is the isentropic coefficient or specific heat ratio (\(C_p/C_v\)).

Temperature-Pressure Relationship:

\[ T_2 = T_1 \left( \frac{P_2}{P_1} \right)^{\frac{k-1}{k}} \] Isentropic Temperature-Pressure Formula

Pressure-Temperature Relationship:

\[ P_2 = P_1 \left( \frac{T_2}{T_1} \right)^{\frac{k}{k-1}} \] Isentropic Pressure-Temperature Formula

Pressure-Volume Relationship:

\[ P_1 V_1^k = P_2 V_2^k \] Isentropic Pressure-Volume Formula

Temperature-Volume Relationship:

\[ T_1 V_1^{k-1} = T_2 V_2^{k-1} \] Isentropic Temperature-Volume Formula

⚙️ Practical Plant Engineering Rules of Thumb & Safety Limits

  • Ideal Gas Assumption: The isentropic relations are based on ideal gas behavior. For real gases, especially at high pressures or low temperatures near condensation, deviations can be significant. Consult steam tables or real gas equations of state for accurate calculations.
  • Isentropic Efficiency: Real compression and expansion processes are not perfectly isentropic due to irreversibilities (e.g., friction, turbulence). Turbines and compressors have an isentropic efficiency, typically 70-85%, which must be applied to the ideal isentropic work/temperature change.
  • Temperature Limits: Be mindful of material limits. High temperatures from compression (e.g., in air compressors) can lead to material degradation or autoignition of lubricants. Low temperatures from expansion can cause embrittlement of materials or condensation/freezing.
  • Pressure Ratios: For practical single-stage compression, pressure ratios typically don't exceed 4-5 without significant temperature rise or efficiency loss. Higher ratios often require multi-stage compression with intercooling.
  • Erosional Velocities: While not directly calculated here, high fluid velocities resulting from extreme expansion (e.g., in nozzles) can lead to erosion of equipment. Ensure outlet velocities are within acceptable limits (e.g., typically < 100 m/s for gases in many applications, but check specific guidelines).

1. Data table

Gas Isentropic coefficient
Specific heat ratio
at 15 degrees celcius
Acetylene 1.24
Air 1.40
Ammonia 1.31
Benzene 1.12
Carbon dioxide 1.30
Carbon monoxide 1.40
Chlorine 1.36
Ethane 1.19
Ethyle Alcohol 1.13
Ethyle Chloride 1.19
Ethylene 1.24
Hydrogene 1.41
Methane 1.31
Methyl Alcohol 1.20
Methyl Chloride 1.20
Natural Gas 1.27
Nitrogen 1.40
Oxygen 1.40
Propane 1.13
Propylene 1.15
Water vapor 1.33

Source : Chemical Engineering, 1974