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SCIENCE · INVESTIGATE AND EXPLAIN

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 experiment

Predict

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.

Fixed amount scale: 0–2 mol; bars are not container volumesInitialFinal012 molNavy: liquid · gold: vapor · exact amounts in the ledger
Nominal heat to remove all initial vapor0.000 kJ
Nominal heat to vaporize remaining liquid77.400 kJ
Unrestricted algebraic vapor fraction0.500000
Propagated source range, before domain test0.498711 to 0.501295
Supported final vapor amount1.000000 mol
Supported final liquid amount1.000000 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

Try: heat changes the amount of vapor

Begin with two moles of liquid ethanol at 351 K and supplied heat 38.7 kJ. The selected reference vaporization enthalpy is 38.7 kJ/mol. The nominal transferred amount is one mole, so the final vapor fraction is one-half, not one. Inspect the conserved liquid/vapor amounts before comparing a one-mole sample.

The activity assumes pure ethanol at phase equilibrium under its saturation pressure at the specified temperature. Volume can change; the sample is closed to matter and only pressure-volume work is included. The selected reference rows do not give a numerical pressure. We do not silently set it to one atmosphere or apply this model to a rigid sealed container.

Understand the molecular change

During vaporization, molecules move from the liquid phase to the vapor phase. The substance remains ethanol; this is not atomization or a reaction that breaks all its covalent bonds. Adding heat can change intermolecular arrangements and phase amounts without increasing the equilibrium temperature. Condensation reverses the energy transfer.

The amount scale shows moles rather than physical volume. A half-mole fraction of vapor does not imply that vapor occupies half the container. Amount conservation is n_liquid + n_vapor = n_total.

Calculate the phase fraction

Let Q be signed heat into the material in kJ, n total moles, L the molar vaporization enthalpy in kJ/mol, f₀ the initial vapor mole fraction and f the final fraction. Inside the phase interval, Q = nL(f − f₀), so f = f₀ + Q/(nL). This relation uses enthalpy at the specified temperature and pressure conditions, not a temperature-independent universal value.

At n = 2, f₀ = 0 and Q = 38.7, f = 0.5 using L = 38.7. The reported source uncertainty magnitude ±0.1 gives a conditional range from 38.7/(2×38.8) to 38.7/(2×38.6). We treat those endpoints as an envelope, not a probability distribution or confidence interval. Supplied n and Q are exact teaching inputs.

Experiment at and beyond the boundary

For one mole, the same 38.7 kJ produces nominal fraction one. But the source envelope gives fractions on both sides of one. The lesson therefore does not claim certain complete vaporization. A nominal endpoint is not automatically a robust phase classification.

Now start two moles with half already vapor. Removing 19.35 kJ condenses nominally half a mole, leaving vapor fraction 0.25. Removing more heat than can condense the initial vapor requires liquid cooling; adding more than can vaporize the liquid requires a vapor-temperature model. This phase-only activity supplies neither heat capacity nor a final temperature outside its domain. It refuses rather than clipping impossible fractions and discarding energy.

Compare the matched 320 K source value, 41.0±0.1 kJ/mol, with the 351 K value. The same heat transfers a different nominal number of moles. A deliberately unmatched reference packet withholds inference: the row temperature is part of the evidence. At zero total amount, no vapor fraction is defined.

Apply and continue

For three moles initially 20% vapor, heat 23.22 kJ transfers nominally 0.60 mol into vapor at the 351 K reference. The fraction increases by 0.20 to 0.40. Explain the initial inventory, the sign and why a constant temperature does not mean an unchanged state.

Reuse warming and melting for the basic distinction between sensible heat and phase heat, and vapor inventory for a different, fixed-volume equilibrium model. Those model boundaries are not interchangeable.

The NIST ethanol phase table lists 38.7±0.1 kJ/mol at 351 K and 41.0±0.1 at 320 K, attributed to Counsell, Fenwick and Lees (1970), with method C. The NIST method key identifies C as calorimetry. These empirical inputs are distinct from the original hypothetical inventories, transfers and diagrams. The activity supports AP topic 6.5 but does not establish a performed practical, a full uncertainty budget or independent learner mastery.

Transfer beyond vaporization: fusion and sublimation

Melting (fusion) transfers solid to liquid; freezing reverses it. Sublimation transfers solid directly to gas; deposition is the reverse. For an ordinary endothermic melting or sublimation step, signed heat into the material is positive; reversing the same step reverses its enthalpy. Molecular identity need not change. A plateau describes phase reorganization rather than an increase in average thermal kinetic energy.

Use an original stipulated substance, not the ethanol data above: molar fusion enthalpy is 6.0 kJ/mol at its melting conditions. Two moles begin 25% liquid. Predict the liquid fraction after adding 3.0 kJ while both phases remain. Write the changed amount and the conserved solid/liquid ledger before opening the comparison.

Compare the fusion calculation

Transferred amount is 3.0/6.0 = 0.50 mol. Initial liquid is 0.50 mol; final liquid is 1.00 mol, so liquid fraction is 0.50. Final solid is 1.00 mol. Temperature remaining constant does not mean that no energy entered.

For a separate stipulated common-temperature state-function packet, solid-to-liquid enthalpy is +6.0 kJ/mol and liquid-to-gas is +40.0 kJ/mol. The solid-to-gas difference is +46.0 kJ/mol by adding endpoints, whether or not a direct equilibrium path visits liquid. Depositing 0.20 mol releases 9.2 kJ. Predict how the sign changes for sublimating that amount. Do not add tabulated latent heats at different temperatures without accounting for intervening heating/cooling: those endpoints do not match.

These written transfers extend the lesson without pretending that the vapor-only slider simulates melting or sublimation. Concepts checked 30 October 2026 against OpenStax phase transitions. Values here are synthetic; no heating experiment is requested.

Apply

At the supplied 351 K nominal reference, 3 mol ethanol starts with vapor fraction 0.20. Adding 23.22 kJ while remaining in the phase interval gives which nominal vapor fraction?

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

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