Trouton’s rule
E807318
Trouton’s rule is an empirical thermodynamic relationship stating that many non-associated liquids have nearly constant molar entropy of vaporization at their normal boiling points.
Statements (50)
| Predicate | Object |
|---|---|
| instanceOf |
empirical thermodynamic rule
ⓘ
thermodynamic relationship ⓘ |
| appliesBestTo |
monatomic liquids like noble gases
ⓘ
simple, non-polar, non-associated organic liquids ⓘ |
| appliesTo |
non-associated liquids
ⓘ
normal boiling point ⓘ |
| approximateValue |
ΔSvap ≈ 21 cal·mol⁻¹·K⁻¹ at the normal boiling point
ⓘ
ΔSvap ≈ 85–88 J·mol⁻¹·K⁻¹ at the normal boiling point ⓘ |
| assumes |
liquid and vapor behave nearly ideally at the normal boiling point
ⓘ
no strong specific intermolecular associations in the liquid phase ⓘ |
| category |
empirical correlation in thermodynamics
ⓘ
phase transition rule ⓘ |
| countryOfOrigin | United Kingdom ⓘ |
| describes | molar entropy of vaporization ⓘ |
| doesNotApplyWellTo |
liquid acetic acid
ⓘ
liquid ammonia ⓘ liquid ethanol ⓘ liquid formic acid ⓘ liquid glycerol ⓘ liquid hydrogen fluoride ⓘ liquid ionic liquids ⓘ liquid metals ⓘ liquid methanol ⓘ strongly hydrogen-bonded liquids ⓘ water ⓘ |
| field |
physical chemistry
ⓘ
thermodynamics ⓘ |
| historicalPeriod | late 19th century ⓘ |
| involvesQuantity |
molar entropy
ⓘ
normal boiling temperature ⓘ |
| limitation |
accuracy decreases for highly non-ideal systems
ⓘ
does not account explicitly for association or complex formation in the liquid ⓘ does not account explicitly for molecular structure ⓘ |
| mathematicalForm | ΔSvap = ΔHvap / Tb ⓘ |
| namedAfter | Frederick Thomas Trouton NERFINISHED ⓘ |
| nature | empirical ⓘ |
| predicts | similar entropy change for vaporization of many simple liquids ⓘ |
| relatedConcept |
Clausius–Clapeyron equation
NERFINISHED
ⓘ
Hildebrand solubility parameter NERFINISHED ⓘ Walden’s rule NERFINISHED ⓘ enthalpy of vaporization ⓘ entropy of vaporization ⓘ |
| statement | many non-associated liquids have nearly constant molar entropy of vaporization at their normal boiling points ⓘ |
| typicalValueRange | ΔSvap between 80 and 90 J·mol⁻¹·K⁻¹ for many non-associated liquids ⓘ |
| usedFor |
estimating enthalpy of vaporization from boiling point
ⓘ
estimating normal boiling point from enthalpy of vaporization ⓘ |
| usedIn |
chemical engineering design
ⓘ
engineering thermodynamics ⓘ estimation methods for phase equilibria ⓘ |
| validAt | normal boiling point where liquid and vapor are in equilibrium at 1 atm ⓘ |
Referenced by (3)
Full triples — surface form annotated when it differs from this entity's canonical label.