Thermodynamics · Chapter 10 of 10 · Intermediate
Vapor and Refrigeration Cycles
The Rankine cycle turns heat into electricity in nearly every power plant, and running its logic backwards gives the vapor-compression cycle in every fridge and air conditioner. Both come straight from the device models you already know.
Readiness check
This chapter assembles the device models into cycles. Tick only what you can do closed-notes.
- Read enthalpy and entropy from a steam or refrigerant table.
- Find a quality from entropy inside the dome.
- Apply turbine, pump, and throttle balances.
- Compute thermal efficiency and a coefficient of performance.
- Interpolate between two table rows.
The core idea
The Rankine cycle circulates water through a boiler, turbine, condenser, and pump, turning a heat input into net work. Reverse the flow of energy and the same four-component loop becomes a refrigerator.
ηth = wnet/qin = 1 − qout/qinCOPR = qL/winIn the Rankine cycle, the boiler adds heat to make high-pressure steam, the turbine expands it to produce work, the condenser rejects heat to turn it back to liquid, and a pump raises the liquid pressure cheaply. Each component is a steady-flow device from Chapter 5, so the whole cycle is just four enthalpy differences. The vapor-compression refrigeration cycle uses the same four roles, compressor, condenser, throttle, and evaporator, to move heat from cold to hot, rated by its coefficient of performance.
The skills, taught in order
Five skills build the Rankine cycle, analyse it, note how it is improved, and then run the logic backwards for refrigeration.
10.1 The Rankine cycle components
Water flows through four steady-flow devices: a pump raises the liquid pressure (work in), a boiler adds heat to make superheated steam, a turbine expands it (work out), and a condenser rejects heat back to saturated liquid. Using water lets the cycle add and reject heat at nearly constant temperature during phase change, which is what makes it efficient.
10.2 Analysing the cycle
Fix the four states from the tables, then apply each device balance: pump wp = vf(P₂ − P₁); boiler qin = h₃ − h₂; turbine wt = h₃ − h₄; condenser qout = h₄ − h₁. The thermal efficiency is η = wnet/qin = (wt − wp)/qin. Pump work is tiny because liquid is nearly incompressible.
| Device | Process | Energy term |
|---|---|---|
| Pump | isentropic, liquid | wp = vf(P₂ − P₁) |
| Boiler | constant pressure | qin = h₃ − h₂ |
| Turbine | isentropic (ideal) | wt = h₃ − h₄ |
| Condenser | constant pressure | qout = h₄ − h₁ |
10.3 Improving the Rankine cycle
Three moves raise efficiency: superheating the steam (hotter average heat-addition temperature), reheating between turbine stages (keeps the steam dry and adds area), and regeneration (using extracted steam to preheat the feedwater). All work by raising the average temperature at which heat is added.
10.4 The vapor-compression refrigeration cycle
Reverse the energy flow and the loop becomes a refrigerator: a compressor raises the refrigerant pressure (work in), a condenser rejects heat outdoors, a throttle drops the pressure (h constant), and an evaporator absorbs heat from the cold space. The throttle replaces the turbine because recovering the tiny work is not worth the cost.
10.5 Coefficient of performance
The refrigerator is rated by COPR = qL/win = (h₁ − h₄)/(h₂ − h₁), the cooling delivered per unit of compressor work, and a heat pump by COPHP = qH/win. Both exceed one and both fall short of the Carnot limit for the same temperatures.
Engineering connection: these two cycles, joined with the gas cycles of Chapter 9, cover almost all power generation, heating, and cooling in service today.
Worked example 1: an ideal Rankine cycle
An ideal Rankine cycle uses steam at the turbine inlet at 3 MPa and 350 °C (h₃ = 3115.3 kJ/kg, s₃ = 6.7427 kJ/kg·K) and condenses at 10 kPa (hf = 191.81 kJ/kg, vf = 0.001010 m³/kg, sf = 0.6492, sfg = 7.5010 kJ/kg·K, hfg = 2392.82 kJ/kg). Find the pump work, the heat added, the net work, and the thermal efficiency.
- ProblemFind wp, qin, wnet, and η for the Rankine cycle in Figure 1.
- Given / findTurbine inlet 3 MPa, 350 °C (h₃, s₃ given); condenser 10 kPa (saturation data given). Find pump work, heat added, net work, efficiency.
- AssumptionsIdeal cycle: isentropic pump and turbine, constant-pressure boiler and condenser, saturated liquid leaving the condenser.
- ModelState 1 is saturated liquid at 10 kPa; the pump raises it to 3 MPa; the turbine exit follows from s₄ = s₃; then apply the four device balances.
- Equationswp = vf(P₂ − P₁), h₂ = h₁ + wpx₄ = (s₃ − sf)/sfg, h₄ = hf + x₄ hfgη = (wt − wp)/qin
- Solvewp = 0.001010 × (3000 − 10) = 3.02 kJ/kg, so h₂ = 191.81 + 3.02 = 194.83 kJ/kg. x₄ = (6.7427 − 0.6492)/7.5010 = 0.812, h₄ = 191.81 + 0.812 × 2392.82 = 2135.6 kJ/kg. qin = h₃ − h₂ = 3115.3 − 194.83 = 2920.4 kJ/kg. wt = h₃ − h₄ = 979.6 kJ/kg, so wnet = 979.6 − 3.02 = 976.6 kJ/kg. η = 976.6/2920.4 = 0.334.
- CheckThe Carnot limit between 350 °C (623 K) and 45.81 °C (319 K) is 1 − 319/623 = 0.488, well above 0.334, as required. The pump work is under one percent of the turbine work, confirming why pumping a liquid is cheap.
- ConclusionA real plant raises this efficiency with superheat, reheat, and regeneration, but the skeleton is exactly these four enthalpy differences.
Worked example 2: a vapor-compression refrigerator
An ideal R-134a refrigeration cycle evaporates at −20 °C (saturated vapor: h₁ = 386.08 kJ/kg, s₁ = 1.7395 kJ/kg·K) and condenses at 800 kPa, leaving as saturated liquid (h₃ = 243.7 kJ/kg). The compressor is isentropic; at 800 kPa the superheated table gives h = 415.72 kJ/kg at s = 1.7150 and h = 424.86 kJ/kg at s = 1.7446 kJ/kg·K. Find the compressor work, the refrigeration effect, and the coefficient of performance.
- ProblemFind win, qL, and COPR for the refrigerator in Figure 2.
- Given / findState 1 (sat vapor, −20 °C): h₁ = 386.08, s₁ = 1.7395; state 3 (sat liquid, 800 kPa): h₃ = 243.7; throttle gives h₄ = h₃; compressor isentropic with the 800 kPa data given. Find win, qL, COPR.
- AssumptionsIdeal cycle: isentropic compressor, saturated states at evaporator and condenser exits, constant-enthalpy throttle.
- ModelFind h₂ by interpolating the 800 kPa superheated table at s₂ = s₁; then qL = h₁ − h₄, win = h₂ − h₁, and COPR = qL/win.
- Equationsh₂ = 415.72 + [(1.7395 − 1.7150)/(1.7446 − 1.7150)](424.86 − 415.72)qL = h₁ − h₄, win = h₂ − h₁COPR = qL/win
- SolveThe interpolation fraction is 0.0245/0.0296 = 0.828, so h₂ = 415.72 + 0.828 × 9.14 = 423.3 kJ/kg. qL = 386.08 − 243.7 = 142.4 kJ/kg. win = 423.3 − 386.08 = 37.2 kJ/kg. COPR = 142.4/37.2 = 3.83.
- CheckThe heat rejected qH = h₂ − h₃ = 179.6 kJ/kg equals qL + win = 142.4 + 37.2, closing the energy balance. The Carnot COP between −20 °C and 31.3 °C is 4.93, so 3.83 sits below it, as it must.
- ConclusionThe cycle delivers 3.8 units of cooling per unit of work, and the throttle, not a turbine, is what makes it simple and cheap. Smaller temperature lifts give higher COP.
Misconceptions and diagnostics
| Mistake | Symptom | Diagnostic question | Correction |
|---|---|---|---|
| Pump work as a gas | Huge, wrong pump work | "Is the fluid a liquid here?" | Use wp = vf(P₂ − P₁) for the nearly incompressible liquid. |
| Wrong condenser-exit state | h₁ taken as a mixture | "Does the condenser deliver saturated liquid?" | In the ideal cycle, state 1 is saturated liquid at the condenser pressure. |
| Turbine instead of throttle | Refrigerator with a turbine expander | "Is the expansion device a throttle?" | Refrigeration uses a throttle, where h is constant, not a turbine. |
| COP above Carnot | COPR exceeds TL/(TH − TL) | "Is my COP under the Carnot value?" | No real cycle can beat the Carnot COP for its temperatures. |
Practice ladder
A Rankine turbine takes steam at h₃ = 3115.3 kJ/kg and exhausts it at h₄ = 2135.6 kJ/kg. Ignoring pump work, find the turbine work and the heat added if h₂ = 191.8 kJ/kg.
Show answer
wt = h₃ − h₄ = 979.7 kJ/kg. qin = h₃ − h₂ = 3115.3 − 191.8 = 2923.5 kJ/kg. The rough efficiency 979.7/2923.5 = 0.335 matches the full result, since pump work is negligible.
The refrigerator of Worked Example 2 must provide 3 kW of cooling. What compressor power does it need?
Show answer
Ẇ = Q̇L/COPR = 3/3.83 = 0.78 kW. The mass flow would be ṁ = Q̇L/qL = 3/142.4 = 0.021 kg/s.
The same R-134a cycle is used as a heat pump for the warm space. Using qH = 179.6 kJ/kg and win = 37.2 kJ/kg, find its COP.
Show answer
COPHP = qH/win = 179.6/37.2 = 4.83, which is COPR + 1 = 3.83 + 1, exactly as expected for the same cycle.
Explain why power plants superheat the steam before the turbine, using both efficiency and the wetness of the steam leaving the turbine.
What good work looks like
Superheating raises the average temperature of heat addition, lifting efficiency, and it keeps the turbine-exit quality high so less liquid forms, protecting the blades from erosion.
Working with AI, and proving it yourself
Use AI as an examiner, not a solver
Portfolio task
Analyse a real power plant or refrigerator at a chosen pair of pressures. Fix the four states from the tables, compute the efficiency or COP, and compare it with the Carnot limit.
Retrieval and spaced review
Closed notes. Answer out loud, then reveal.
1. Name the four Rankine components and their roles.
Pump (raise liquid pressure), boiler (add heat), turbine (produce work), condenser (reject heat).
2. Why is pump work small?
Liquid is nearly incompressible, so wp = vf(P₂ − P₁) is tiny next to the turbine work.
3. How does the refrigeration cycle differ from Rankine?
Energy flows the other way: a compressor and throttle replace the turbine and pump, moving heat from cold to hot.
4. Write the refrigerator COP.
COPR = qL/win = (h₁ − h₄)/(h₂ − h₁).
5. Name three ways to improve a Rankine cycle.
Superheat, reheat, and regeneration, all raising the average heat-addition temperature.
Textbook mapping
| Item | Mapping |
|---|---|
| Primary source | Borgnakke and Sonntag, Fundamentals of Thermodynamics, Chapter 11 (Power and Refrigeration Systems, Vapor Working Fluids) and Appendix B |
| Cross-reference | Çengel and Boles, Ch. 10 and 11 · Moran, Ch. 8 and 10 |
| Core topics | 10.1 Rankine components · 10.2 Cycle analysis · 10.3 Improvements · 10.4 Vapor-compression refrigeration · 10.5 Coefficient of performance |
| Engineering connection | The Rankine and refrigeration cycles run nearly all power generation, heating, and cooling. |
| Read next | Return to the course home, then continue to Heat Transfer. |