Audit a complete thermal cycle before claiming useful work
A cyclic device returns its working gas to the starting state, so its net internal-energy change is zero. That statement does not mean every stage has zero ΔU. Compute heat and work stage by stage, then add the signed values. Forgetting one cooling or compression segment can create a fictitious device that produces work without a complete energy account.
Learning outcome: Capture ratios 1.6/1.6 and reconstruct all four stage ledgers. Then change only pressure ratio and compare enclosed area, total positive heat and net work. Explain why zero net ΔU cannot be applied separately to every stage.
Starting recap
Use absolute temperature, signed energy changes, algebraic ratios and graph areas. State the system boundary and distinguish heat transfer from temperature.
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Try
At pressure and volume ratios 1.6, enclosed area is(160−100) kPa×(4.8−3.0) L=108 J. Stage heats are 270, 720,−432 and−450 J; total input 990 J, rejection 882 J and net 108 J. Efficiency is 108/990≈10.91%, not 100%.
Open the experimentPredict
Predict whether doubling a cycle’s heat input alone is enough to infer twice its useful work.
Experiment
Capture ratios 1.6/1.6 and reconstruct all four stage ledgers. Then change only pressure ratio and compare enclosed area, total positive heat and net work. Explain why zero net ΔU cannot be applied separately to every stage.
Reconcile an entire cycle energy ledger
Worked teaching model · synthetic values · Clockwise rectangular quasistatic monatomic ideal-gas cycle: A=(3 L, 100 kPa), nR=1 J/K. Constant heat capacities. Supplied hot/cold reservoirs 1200/300 K bracket all gas temperatures. Efficiency and reservoir-limit numbers are enrichment; no engine construction or laboratory performance is claimed.
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Axes rescale with settings; compare numerical values, not screen angles or apparent lengths. Solid/points show the selected model relationship or observations; the dashed comparison is explained below.
| Quantity | Value | Unit |
|---|---|---|
| Net work delivered | 108 | J/cycle |
| Heat absorbed | 990 | J/cycle |
| Heat rejected | 882 | J/cycle |
| Cycle internal energy change | 0 | J |
| Efficiency | 0.10909 | fraction |
| Maximum gas temperature | 768 | K |
| Reversible reservoir efficiency bound (enrichment) | 0.75 | fraction |
Accessible plot coordinates
| volume (L) | pressure (kPa) |
|---|---|
| 3 | 100 |
| 3 | 160 |
| 4.8 | 160 |
| 4.8 | 100 |
| 3 | 100 |
| Stage | Q into gas | W on gas | ΔU |
|---|---|---|---|
| A→B | 270 | 0 | 270 |
| B→C | 720 | -288 | 432 |
| C→D | -432 | 0 | -432 |
| D→A | -450 | 180 | -270 |
The gas returns to its initial state, so net heat input equals work delivered; heat rejection remains essential.
Path order is A→B→C→D→A. Positive Q enters the gas; positive W_on enters as work. The fixed 1200 K hot and 300 K cold reservoirs bracket the gas states. The numerical efficiency bound 1−300/1200 is optional enrichment; the AP second-law claim is qualitative: cyclic conversion of all heat from one reservoir into work is not possible.
The gas returns to its initial state, so net heat input equals work delivered; heat rejection remains essential.
Path order is A→B→C→D→A. Positive Q enters the gas; positive W_on enters as work. The fixed 1200 K hot and 300 K cold reservoirs bracket the gas states. The numerical efficiency bound 1−300/1200 is optional enrichment; the AP second-law claim is qualitative: cyclic conversion of all heat from one reservoir into work is not possible.
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Public practice checks a specific claim. It does not establish independent mastery.
Identify the denominator of efficiency and explain why net heat is the wrong one. Give an energy-balanced proposal that the qualitative second law would still reject.
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