B.4.2 (HL)—Gas work

Syllabus
First assessment 2025
Objective
Level
HL

Calculate Gas Work from a PV Change

HL only

Work from pressure and volume

For a constant-pressure change, the work done by the gas is

W=PΔVW=P\Delta V

Expansion has ΔV>0\Delta V>0 and work done by the gas is positive in the first-law convention.

PV interpretation

On a pressure–volume diagram, work is the area under the process path. For constant pressure this is a rectangle; for changing pressure, use the area or integral specified by the model.

Units and direction

Use pressure in pascals and volume in cubic metres so PΔVP\Delta V is in joules. Compression gives ΔV<0\Delta V<0, so work done by the gas is negative.

Worked example from the mapped local textbook

A gas expands at constant pressure 1.0×105Pa1.0\times10^5\,\mathrm{Pa} from 0.020m30.020\,\mathrm{m^3} to 0.050m30.050\,\mathrm{m^3}.

W=PΔV=(1.0×105)(0.0500.020)=3.0×103JW=P\Delta V=(1.0\times10^5)(0.050-0.020)=3.0\times10^3\,\mathrm{J}

The work is positive because the gas expands and does work on its surroundings.

Common trap

Do not multiply pressure by the final volume alone. Work depends on the change in volume and on the process path.

B.4.2 (HL) Exam Analysis

HL only

Assessment in practice

1–2 marks
How it is assessed

The evidence uses direct numerical work calculations from pressure and initial/final volumes.

Command terms

Calculate

What earns marks

Use W=PΔV for a constant-pressure process with pressure in Pa and volume change in m³. Expansion gives positive work by the gas. On a PV diagram, identify the area under the path and do not use final volume alone.

Watch for

Using pressure times final volume or mixing kPa and m³ without conversion.

Representative question

Question 1

[Maximum number: 2]

Calculate, in J , the work done by the gas during this expansion.

Synthesize B.4 Thermodynamics

HL only

Energy accounting

For a closed system, Q=ΔU+WQ=\Delta U+W. Gas work is linked to volume change by W=PΔVW=P\Delta V for constant pressure, and for a monatomic ideal gas ΔU=32nRΔT\Delta U=\frac32nR\Delta T.

Entropy and direction

Entropy measures accessible microstates: S=kBlnΩS=k_B\ln\Omega and, for a reversible thermal transfer, ΔS=ΔQ/T\Delta S=\Delta Q/T. The total entropy of an isolated system does not decrease; real processes are generally irreversible.

Gas processes and engines

Classify isovolumetric, isobaric, isothermal and adiabatic paths by what is fixed. Cyclic paths can run heat engines; net work is the signed PV-loop area.

Efficiency limits

η=WusefulQH=1QCQH\eta=\frac{W_{\mathrm{useful}}}{Q_H}=1-\frac{Q_C}{Q_H} and no real engine can exceed ηC=1TC/TH\eta_C=1-T_C/T_H. Always state the sign convention, system boundary and reservoir temperatures.