6533b833fe1ef96bd129ca5f

RESEARCH PRODUCT

Phase equilibrium for the systems diisopropyl ether, isopropyl alcohol+2,2,4-trimethylpentane and +n-heptane at 101.3kPa

Estela LladosaM.c. BurguetJuan B. Montón

subject

Activity coefficientTernary numeral systemUNIQUACGeneral Chemical EngineeringGeneral Physics and AstronomyThermodynamicsIsopropyl alcoholchemistry.chemical_compoundchemistryNon-random two-liquid modelDiisopropyl etherOrganic chemistry224-TrimethylpentanePhysical and Theoretical ChemistryTernary operation

description

Abstract Consistent vapour–liquid equilibrium data for the ternary systems diisopropyl ether + isopropyl alcohol + 2,2,4-trimethylpentane and diisopropyl ether + isopropyl alcohol + n-heptane are reported at 101.3 kPa. The vapour–liquid equilibrium data have been correlated by Wilson, NRTL and UNIQUAC equations. The ternary systems do not present ternary azeotropes.

yearjournalcountryeditionlanguage
2010-03-01Fluid Phase Equilibria
https://doi.org/10.1016/j.fluid.2009.11.027