Carnot Cycle — The Thermodynamic Speed Limit

Four reversible processes around a P–V loop. The Carnot cycle is the theoretical maximum efficiency any heat engine can achieve between two reservoirs.

Visualization
Input
K\mathrm{K}
K\mathrm{K}
L\mathrm{L}
L\mathrm{L}
mol\mathrm{mol}

Show the formal P–V diagram

The thermodynamic speed limit

Pick any two heat reservoirs — a hot one at THT_H and a cold one at TCT_C. No heat engine you can build, no matter how clever, can convert more than this fraction of the heat it takes from the hot side into useful work:

ηCarnot=1TCTH\eta_{\text{Carnot}} = 1 - \frac{T_C}{T_H}

Source: OpenStax University Physics §4.5; Wikipedia — Carnot cycle. This is the second law of thermodynamics as a budget — the temperatures alone tell you the ceiling. A power plant burning fuel at 750 K and dumping waste heat at 300 K cannot exceed 60% efficiency, ever. The only way up is to raise THT_H or lower TCT_C.

The cycle that achieves it

The Carnot cycle is the only cycle that hits the ceiling above. It does so by being entirely reversible — every heat transfer happens at vanishing temperature difference, no friction, no leaks. It's the thermodynamic equivalent of frictionless surfaces in mechanics: a useful idealisation that real machines approach but never reach.

Four stages take the gas around the closed loop in the P–V diagram:

  1. Isothermal expansion at THT_H (1→2). The gas absorbs heat QHQ_H from the hot reservoir while expanding; its temperature stays put because the heat exactly matches the work done.
  2. Adiabatic expansion (2→3). The gas is isolated; expansion continues but now the work comes out of internal energy, so the temperature falls to TCT_C.
  3. Isothermal compression at TCT_C (3→4). The gas rejects heat QCQ_C to the cold reservoir while being compressed.
  4. Adiabatic compression (4→1). The gas is isolated again and compressed back to its starting state, with the temperature climbing back to THT_H.

The shaded area inside the P–V loop is the net work done per cycle:

W=QHQCW = Q_H - Q_C

For an ideal gas the heats follow from integrating pdVp\,dV along the isotherms:

QH=nRTHln ⁣V2V1,QC=nRTCln ⁣V3V4Q_H = n R T_H \ln\!\frac{V_2}{V_1}, \qquad Q_C = n R T_C \ln\!\frac{V_3}{V_4}

The Carnot constraint forces V3/V4=V2/V1V_3/V_4 = V_2/V_1, so QC/QH=TC/THQ_C/Q_H = T_C/T_H, which is exactly the efficiency formula again — the cycle is defined to satisfy the bound.

Why the temperatures matter

Because η=1TC/TH\eta = 1 - T_C/T_H, the only way to push the limit higher is to widen the temperature gap. That's why jet engines run combustion at thousands of kelvin and dump exhaust to ambient air, and why geothermal plants struggle when the source rock is only modestly hotter than the surface. Slide THT_H up and watch the loop fatten; slide TCT_C down and watch the same effect from the other side.

Show your work
Volume after adiabatic expansion (state 3)
V3  =  V2(THTC)1/(γ1)  =  (0.00223)(THTC)1/(γ1)  =  0.0088088  m3V_3 \;=\; V_2 \cdot \left(\dfrac{T_H}{T_C}\right)^{1/(\gamma - 1)} \;=\; \textcolor{#dc4124}{\left(0.00223\right)} \cdot \left(\dfrac{T_H}{T_C}\right)^{1/(\gamma - 1)} \;=\; 0.0088088\;\mathrm{m^{3}}
Volume after isothermal compression (state 4)
V4  =  V1(THTC)1/(γ1)  =  (0.001)(THTC)1/(γ1)  =  0.0039501  m3V_4 \;=\; V_1 \cdot \left(\dfrac{T_H}{T_C}\right)^{1/(\gamma - 1)} \;=\; \textcolor{#dc4124}{\left(0.001\right)} \cdot \left(\dfrac{T_H}{T_C}\right)^{1/(\gamma - 1)} \;=\; 0.0039501\;\mathrm{m^{3}}
Pressure at state 1
P1  =  nRTHV1  =  n(8.314)TH(0.001)  =  6.236×105  PaP_1 \;=\; \dfrac{n R T_H}{V_1} \;=\; \dfrac{n \textcolor{#dc4124}{\left(8.314\right)} T_H}{\textcolor{#dc4124}{\left(0.001\right)}} \;=\; 6.236 \times 10^{5}\;\mathrm{Pa}
Pressure at state 2
P2  =  nRTHV2  =  n(8.314)TH(0.00223)  =  2.796×105  PaP_2 \;=\; \dfrac{n R T_H}{V_2} \;=\; \dfrac{n \textcolor{#dc4124}{\left(8.314\right)} T_H}{\textcolor{#dc4124}{\left(0.00223\right)}} \;=\; 2.796 \times 10^{5}\;\mathrm{Pa}
Pressure at state 3
P3  =  nRTCV3  =  n(8.314)TC(0.0088088)  =  28315  PaP_3 \;=\; \dfrac{n R T_C}{V_3} \;=\; \dfrac{n \textcolor{#dc4124}{\left(8.314\right)} T_C}{\textcolor{#dc4124}{\left(0.0088088\right)}} \;=\; 28315\;\mathrm{Pa}
Pressure at state 4
P4  =  nRTCV4  =  n(8.314)TC(0.0039501)  =  63142  PaP_4 \;=\; \dfrac{n R T_C}{V_4} \;=\; \dfrac{n \textcolor{#dc4124}{\left(8.314\right)} T_C}{\textcolor{#dc4124}{\left(0.0039501\right)}} \;=\; 63142\;\mathrm{Pa}
Heat absorbed from hot reservoir (isothermal expansion 1→2)
QH  =  nRTHln ⁣(V2V1)  =  n(8.314)THln ⁣((0.00223)(0.001))  =  500.1  JQ_H \;=\; n R T_H \ln\!\left(\dfrac{V_2}{V_1}\right) \;=\; n \textcolor{#dc4124}{\left(8.314\right)} T_H \ln\!\left(\dfrac{\textcolor{#dc4124}{\left(0.00223\right)}}{\textcolor{#dc4124}{\left(0.001\right)}}\right) \;=\; 500.1\;\mathrm{J}
Heat rejected to cold reservoir (isothermal compression 3→4)
QC  =  nRTCln ⁣(V3V4)  =  n(8.314)TCln ⁣((0.0088088)(0.0039501))  =  200  JQ_C \;=\; n R T_C \ln\!\left(\dfrac{V_3}{V_4}\right) \;=\; n \textcolor{#dc4124}{\left(8.314\right)} T_C \ln\!\left(\dfrac{\textcolor{#dc4124}{\left(0.0088088\right)}}{\textcolor{#dc4124}{\left(0.0039501\right)}}\right) \;=\; 200\;\mathrm{J}
Net work per cycle
W  =  QHQC  =  300.1  JW \;=\; Q_H - Q_C \;=\; 300.1\;\mathrm{J}
Carnot efficiency (from temperatures)
η  =  1TCTH  =  0.6\eta \;=\; 1 - \dfrac{T_C}{T_H} \;=\; 0.6
Worked Example

OpenStax University Physics Vol. 2 §4.5 Example 4.2: a Carnot engine between T_H = 750 K and T_C = 300 K has efficiency η = 1 − 300/750 = 0.60 (60%). With Q_H = 500 J the engine produces W = 300 J of work and rejects Q_C = 200 J. Efficiency depends only on temperatures, so it must reproduce exactly regardless of n, V, γ.

QuantityExpectedComputedΔ
eta0.60.60
eta_pct60600
Worked Example

Same OpenStax Example 4.2: with V₁ = 1.0 L, V₂ = 2.23 L, n = 0.1 mol so that nRT_H ln(V₂/V₁) ≈ 500 J, the model should reproduce Q_H ≈ 500, Q_C ≈ 200, W ≈ 300 J. (V₂/V₁ = 2.23 chosen so exp(500/(0.1·8.314·750)) ≈ 2.23.)

QuantityExpectedComputedΔ
Q_h500500.10.08809
Q_c2002000.03524
W_net300300.10.05285
Sources
  1. [1] OpenStax. University Physics Volume 2 — §4.5 The Carnot Cycle, eq. e = 1 − T_C/T_H (Eq. 4.5); four reversible stages: isothermal expansion, adiabatic expansion, isothermal compression, adiabatic compression (openstax.org)
  2. [2] Wikipedia — Carnot cycle, eq. η = 1 − T_C/T_H; Q_H/T_H = −Q_C/T_C; W = Q_H − Q_C (en.wikipedia.org)
Assumptions
  • Working substance is an ideal gas (OpenStax §4.5).
  • All four processes are reversible (Wikipedia: Carnot cycle).
  • No friction, no heat loss to surroundings outside the prescribed reservoir contacts (Wikipedia: Carnot cycle).
  • Heat reservoirs are large enough that their temperatures stay constant during the cycle.
  • γ = C_p/C_v is constant for the gas across the cycle (idealisation).