Compute state entropy without inventing an actual reversible process
Entropy is a state function defined for equilibrium states. Our ideal-gas packet has total Cv=12 J/K and nR=8 J/K, initially 300 K and 1 litre. Only the final temperature and volume are specified. A reversible reference path is a mathematical way to evaluate the state difference; it is not a description of an unknown actual history.
Learning outcome: Retain two reference-path integrations and both heat/work accounts. Predict a compression and an expansion before checking; distinguish the gas state difference from total entropy generation.
Starting recap
Review logarithmic integrals, equilibrium states, absolute temperature and the first-law work convention. State the domain and distinguish calibration data from unused validation.
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At T2=450 K and r=2, delta S=12 ln 1.5+8 ln 2≈10.410759 J/K and delta U=1800 J. Reference heats are 1800+3600 ln 2≈4295.329850 J and 1800+2400 ln 2≈3463.553233 J. The entropy change is the same.
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What is fixed by the two equilibrium endpoints?
Experiment
Retain two reference-path integrations and both heat/work accounts. Predict a compression and an expansion before checking; distinguish the gas state difference from total entropy generation.
Distinguish a reference path from actual heat
Worked teaching model · synthetic values · Ideal gas with total Cv=12 J/K and nR=8 J/K, initially 300 K and 1 litre. Equilibrium endpoints only. The reversible reference path computes a state difference; it does not assert that an unspecified actual process was reversible.
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Entropy is an endpoint function
Graph axes rescale independently; read units and values, not screen angles. 1: final temperature held fixed (solid). Joined curves show the supplied model, not additional observations.
Equivalent numerical coordinates for Entropy is an endpoint function
final temperature held fixed
| volume ratio | entropy change (J/K) |
|---|---|
| 0.5 | -0.6795961 |
| 0.53125 | -0.1945992 |
| 0.5625 | 0.2626681 |
| 0.59375 | 0.6952059 |
| 0.625 | 1.105552 |
| 0.65625 | 1.495874 |
| 0.6875 | 1.868034 |
| 0.71875 | 2.223648 |
| 0.75 | 2.564125 |
| 0.78125 | 2.890701 |
| 0.8125 | 3.204466 |
| 0.84375 | 3.506389 |
| 0.875 | 3.79733 |
| 0.90625 | 4.078061 |
| 0.9375 | 4.349273 |
| 0.96875 | 4.611592 |
| 1 | 4.865581 |
| 1.03125 | 5.111755 |
| 1.0625 | 5.350578 |
| 1.09375 | 5.582479 |
| 1.125 | 5.807846 |
| 1.15625 | 6.027037 |
| 1.1875 | 6.240383 |
| 1.21875 | 6.448187 |
| 1.25 | 6.65073 |
| 1.28125 | 6.848271 |
| 1.3125 | 7.041051 |
| 1.34375 | 7.229295 |
| 1.375 | 7.413211 |
| 1.40625 | 7.592994 |
| 1.4375 | 7.768825 |
| 1.46875 | 7.940875 |
| 1.5 | 8.109302 |
| 1.53125 | 8.274256 |
| 1.5625 | 8.435878 |
| 1.59375 | 8.594299 |
| 1.625 | 8.749644 |
| 1.65625 | 8.902029 |
| 1.6875 | 9.051566 |
| 1.71875 | 9.19836 |
| 1.75 | 9.342508 |
| 1.78125 | 9.484104 |
| 1.8125 | 9.623238 |
| 1.84375 | 9.759994 |
| 1.875 | 9.894451 |
| 1.90625 | 10.02668 |
| 1.9375 | 10.15677 |
| 1.96875 | 10.28477 |
| 2 | 10.41076 |
| 2.03125 | 10.53479 |
| 2.0625 | 10.65693 |
| 2.09375 | 10.77724 |
| 2.125 | 10.89576 |
| 2.15625 | 11.01255 |
| 2.1875 | 11.12766 |
| 2.21875 | 11.24113 |
| 2.25 | 11.35302 |
| 2.28125 | 11.46337 |
| 2.3125 | 11.57221 |
| 2.34375 | 11.6796 |
| 2.375 | 11.78556 |
| 2.40625 | 11.89014 |
| 2.4375 | 11.99336 |
| 2.46875 | 12.09528 |
| 2.5 | 12.19591 |
| 2.53125 | 12.29529 |
| 2.5625 | 12.39345 |
| 2.59375 | 12.49042 |
| 2.625 | 12.58623 |
| 2.65625 | 12.6809 |
| 2.6875 | 12.77447 |
| 2.71875 | 12.86696 |
| 2.75 | 12.95839 |
| 2.78125 | 13.04879 |
| 2.8125 | 13.13817 |
| 2.84375 | 13.22657 |
| 2.875 | 13.314 |
| 2.90625 | 13.40049 |
| 2.9375 | 13.48605 |
| 2.96875 | 13.57071 |
| 3 | 13.65448 |
At most 82 representative computed coordinates including endpoints; the plotted curve can use a finer grid. A table of a revealed generator is not independent measurement evidence.
| Quantity | Value | Unit |
|---|---|---|
| Temperature reference-leg entropy | 4.865581 | J/K |
| Volume reference-leg entropy | 5.545177 | J/K |
| Total gas entropy change | 10.41076 | J/K |
| Internal-energy change | 1800 | J |
| Reference-path heat: fixed volume then final isotherm | 4295.33 | J |
| Alternative reference-path heat: initial isotherm then fixed volume | 3463.553 | J |
Two reversible reference paths have the same entropy difference but generally different heat and work.
Integrate dS=Cv dT/T+nR dV/V. Heating first gives 12 ln(T2/300), then isothermal expansion gives 8 ln(r). Reversing the legs yields the same sum, although isothermal heat is proportional to the leg temperature. An actual irreversible process may have different heat; using actual Q/T without a reversible path or entropy balance is invalid.
Predict before inspecting the values. Save contrasting records with assumptions and one alternative explanation. This virtual display does not certify practical measurement technique.
Two reversible reference paths have the same entropy difference but generally different heat and work.
Integrate dS=Cv dT/T+nR dV/V. Heating first gives 12 ln(T2/300), then isothermal expansion gives 8 ln(r). Reversing the legs yields the same sum, although isothermal heat is proportional to the leg temperature. An actual irreversible process may have different heat; using actual Q/T without a reversible path or entropy balance is invalid.
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Which system boundary, reference path, constitutive law or independently calibrated record supports this entropy inference?
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