P V = n R T
Pressure times volume equals n R T, using absolute temperature.
Ideal-gas equation of state relating pressure, volume, amount and temperature.
- P
- pressure (Pa)
- V
- volume (m^3)
- n
- amount of gas (mol)
- T
- absolute temperature (K)
Use when — Describing equilibrium states of an ideal gas.
Common trap — Using Celsius in place of kelvin.
Q = Delta U + W
Heat supplied equals the change in internal energy plus work done by the system.
First law with heat supplied to the system positive and work done by the system positive.
- Q
- heat supplied to the system (J)
- Delta U
- change in internal energy (J)
- W
- work done by the system (J)
Use when — Closed-system energy accounting under this convention.
Common trap — Combining it with a source using work-on-system positive without translating signs.
W = integral from V_1 to V_2 of P dV
Work equals the integral of pressure with respect to volume from the initial to the final volume.
Quasistatic boundary work done by the gas along a known pressure-volume path.
- P
- pressure (Pa)
- V
- volume (m^3)
- W
- work (J)
Use when — The pressure as a function of volume, P(V), is known along the path.
Common trap — Using endpoint pressure without a constant-pressure condition.
Delta U = n C_V Delta T
Change in internal energy equals n times C V times the change in temperature.
Internal-energy change of a fixed amount of ideal gas.
- n
- amount of gas (mol)
- C_V
- molar heat capacity at constant volume (J mol^-1 K^-1)
- Delta T
- temperature change (K)
Use when — Fixed ideal-gas amount with an applicable C_V.
Common trap — Applying it to a phase change or an unspecified non-ideal system.
W = P (V_2 - V_1)
Work equals pressure times the change in volume.
Boundary work done by the gas at constant pressure.
- P
- constant pressure (Pa)
- V_1, V_2
- initial and final volume (m^3)
Use when — Pressure is constant throughout the process.
Common trap — Using final pressure for a varying-pressure path.
W = n R T ln(V_2 / V_1)
Work equals n R T times the natural log of the ratio of final volume to initial volume.
Reversible isothermal work done by an ideal gas.
- n
- amount of gas (mol)
- T
- constant absolute temperature (K)
- V_1, V_2
- initial and final volume (m^3)
Use when — Constant temperature, ideal gas, quasistatic path.
Common trap — Using it for a general isothermal non-ideal path.
P V^gamma = constant
Pressure times volume to the power gamma remains constant.
Reversible adiabatic ideal-gas relation.
- gamma
- ratio C_P over C_V
Use when — Quasistatic adiabatic ideal gas with applicable constant heat capacities.
Common trap — Treating every insulated process as reversible.
eta = W_out / Q_H = 1 - Q_C / Q_H
Efficiency equals net work output over heat absorbed, which equals one minus the ratio of rejected heat to absorbed heat.
Heat-engine efficiency over a complete cycle.
- W_out
- net work output (J)
- Q_H
- heat absorbed from the hot reservoir (J)
- Q_C
- heat rejected to the cold reservoir (J)
Use when — Analysing a cyclic engine.
Common trap — Using total heat magnitude in the denominator instead of heat absorbed.
eta_C = 1 - T_C / T_H
Carnot efficiency equals one minus the ratio of cold-reservoir temperature to hot-reservoir temperature, both absolute.
Maximum possible efficiency of a reversible engine between two reservoirs.
- T_C
- cold-reservoir absolute temperature (K)
- T_H
- hot-reservoir absolute temperature (K)
Use when — Comparing a real engine's efficiency against the reversible limit.
Common trap — Using Celsius or claiming a real engine must attain the Carnot value.