Solve reversible adiabatic steps with clear units and checks. Choose a gas, enter known states, get values and work. Export to CSV and PDF.
Sample inputs and solved outputs for air (γ ≈ 1.4).
| P1 (kPa) | V1 (L) | T1 (°C) | Known | Value | P2 (kPa) | V2 (L) | T2 (°C) |
|---|---|---|---|---|---|---|---|
| 101.325 | 10.0 | 25 | V2 | 20.0 L | 38.4 | 20.0 | -56.7 |
| 200 | 5.0 | 80 | P2 | 120 kPa | 120 | 6.78 | 39.1 |
| 150 | 8.0 | 20 | T2 | 0 °C | 121 | 9.38 | 0.0 |
These numbers are illustrative; your results depend on units and γ.
For a reversible adiabatic change of an ideal gas:
Energetics (with Q = 0):
This calculator focuses on thermodynamic state relations, not chemical reactions. Use consistent units, and prefer absolute temperature for clarity. If you enter Celsius or Fahrenheit, the tool converts internally to kelvin before applying power-law relations for stable, comparable scenario results.
An adiabatic process is a thermodynamic change with negligible heat exchange between the system and surroundings, so Q≈0. Energy changes appear as work and internal energy shifts, making temperature vary strongly during compression or expansion.
The parameter γ=Cp/Cv controls how steeply pressure and temperature respond to volume change. For many gases near room conditions, γ is about 1.4 for air, 1.67 for monatomic gases, and roughly 1.3–1.33 for carbon dioxide and steam.
For a reversible ideal-gas adiabatic step, the calculator applies P·V^γ=constant and T·V^(γ−1)=constant. These relations let you enter an initial state and any one final variable to compute the remaining final pressure, volume, and temperature.
Because Q=0, the first law reduces to ΔU=−W (sign conventions vary). This calculator reports work done by the gas, W=(P2V2−P1V1)/(1−γ), and ΔU based on nRΔT/(γ−1). Expansion typically yields positive work and negative ΔU.
Typical lab-scale examples use pressures from 50–500 kPa, volumes from milliliters to liters, and temperatures from 250–500 K. The built-in consistency check compares P1V1^γ and P2V2^γ; close agreement indicates inputs align with the reversible adiabatic assumption.
Fast piston strokes, nozzle expansions, and compressor stages can be close to adiabatic, but not always reversible. Friction, turbulence, and heat leaks reduce accuracy. For high pressures, real-gas behavior and variable heat capacities may require more advanced equations of state.
Adiabatic relations support preliminary sizing of compressors and expanders, estimating discharge temperatures, and evaluating pressure drops across throttling alternatives. In aerospace, they help approximate conditions through intakes and expansions. In meteorology, similar relations describe rising air parcels.
After solving, export CSV for spreadsheets or PDF for quick documentation. Record the chosen γ, units, and which final variable was specified. These details are essential for reproducibility when comparing scenarios, tuning designs, or building teaching examples.
It assumes no frictional losses and no dissipative effects, so the process can be reversed by an infinitesimal change. Real devices deviate, but the reversible model is a useful upper-bound for work and a clean reference case.
In an adiabatic model, heat transfer is negligible over the process time scale. That does not mean temperature stays constant; instead, temperature changes because work is exchanged with the surroundings.
Choose the value you actually know or can measure reliably. In piston problems, V2 is common. In nozzle or chamber problems, P2 is often known. If you have a target outlet temperature, use T2.
Dry air near room temperature is commonly approximated with γ≈1.4. For higher temperatures or humid air, γ can shift. If you need better accuracy, use a thermodynamic table or a variable-heat-capacity model.
Celsius is relative to a reference point. Strong expansion can drop absolute temperature below 273.15 K, which appears as a negative Celsius value. The calculator converts to kelvin internally, so the physics stays consistent.
They test whether P·V^γ is consistent between initial and final states. If values differ strongly, inputs may be inconsistent with the selected known final variable, or the process is not well approximated as reversible adiabatic.
No. It uses ideal-gas relations with a constant γ. At high pressures, near condensation, or with large temperature swings, consider real-gas equations of state and temperature-dependent heat capacities.
Use this tool to model reversible adiabatic changes safely.
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.