Apply molar phase energy only within the available phase inventory
Use temperature-matched vaporization data, signed heat and finite molar inventory while refusing unsupported phase-boundary extrapolation.
Learning outcome: Relate heat to changed phase amount and distinguish nominal endpoints, source uncertainty and missing models beyond the phase interval.
Starting recap
Molar vaporization enthalpy is energy per mole transferred from liquid to vapor at stated conditions. Condensation reverses the sign; a phase fraction is not a volume fraction.
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Try
Two moles of liquid receive 38.7 kJ at a stated vaporization enthalpy 38.7 kJ/mol. Does all of the liquid become vapor?
Open the experimentPredict
Predict how halving the total moles changes the vapor fraction for the same heat. Predict what uncertainty does to a nominal exactly-all-vapor result.
Experiment
Compare two and one mole at the same heat, then remove heat from an initially half-vapor sample. Test nominal completion, heat beyond available phase inventory, a different matched temperature and a wrong-temperature reference. Capture an interior result and a withheld endpoint inference.
Use molar phase energy without extending a plateau past its inventory
Frozen NIST phase data · original molar inventory scenarios · Selected NIST ethanol calorimetric vaporization rows: 38.7 ± 0.1 kJ/mol at 351 K and 41.0 ± 0.1 at 320 K. Original closed variable-volume pure-ethanol equilibrium scenarios at each temperature’s saturation pressure; the selected rows do not supply a numerical pressure. Positive heat vaporizes, negative heat condenses while phase inventory remains. Source uncertainty magnitudes are treated as an endpoint range; amount and supplied heat are stipulated exact. No phase fraction or final temperature is inferred beyond this model.
Reset keeps your prediction, captures and practice history.
Heat changes phase amount before it changes temperature
Selected ethanol reference: 38.7 ± 0.1 kJ/mol at 351 K. Proposed state: 351 K, 2 mol total, initial vapor fraction 0. Positive heat enters the material; negative heat leaves it. Current supplied heat: 38.7 kJ.
This is a closed variable-volume model at the pure substance's saturation pressure for the selected temperature, with only pressure-volume work. The reference table gives no numerical pressure for these rows; this lesson does not assume one atmosphere or a rigid sealed volume. A fixed-volume gas inventory requires a different model.
| Nominal heat to remove all initial vapor | 0.000 kJ |
|---|---|
| Nominal heat to vaporize remaining liquid | 77.400 kJ |
| Unrestricted algebraic vapor fraction | 0.500000 |
| Propagated source range, before domain test | 0.498711 to 0.501295 |
| Supported final vapor amount | 1.000000 mol |
| Supported final liquid amount | 1.000000 mol |
The full propagated range remains within the phase-change inventory. The nominal final vapor fraction is 0.500000, with range 0.498711–0.501295; temperature remains 351 K within this phase-equilibrium model.
Calculation, molecules and source limits
Q = n ΔHᵥₐₚ (f − f₀), so f = f₀ + Q/(n ΔHᵥₐₚ). Here n is total moles, f is final vapor mole fraction and f₀ is its initial value. The sign reverses for condensation. Vaporization separates molecules without changing ethanol into different chemical species; it does not break every covalent bond. The equilibrium temperature need not rise during this phase change.
Source uncertainty magnitudes are treated as an endpoint envelope, not a confidence interval. The amount and heat are exact teaching inputs. The two rows are NIST-listed calorimetric results from Counsell, Fenwick and Lees (1970); their temperatures differ, so they are not interchangeable constants. NIST ethanol phase data and method-code definitions. The inventories, controls and diagrams are original model scenarios, not new physical measurements.
The full propagated range remains within the phase-change inventory.
Nominal vapor fraction 0.500000, endpoint range 0.498711–0.501295. Temperature remains 351 K within the stated phase model.
Captures preserve inventory and signed heat selections. Replay uses frozen phase-energy references with explicit temperature and domain tests; it is not a new calorimetric measurement or an observed phase fraction.
Understand
Apply
Public practice checks a specific claim. It does not establish independent mastery.
Explain fixed temperature during a phase change, mole conservation, heat sign and the information needed beyond a phase boundary. Distinguish empirical input values from original hypothetical scenarios.
Continue
Completion requires a saved prediction, at least one capture and a reflection. Presence checks do not grade your reasoning.
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