Ternary Vapor-Liquid Equilibria for System n-Butanol–sec-Butanol–tert-Butanol

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Abstract

Isobarlc vapor-liquid equilibrium was measured for the system n-butanol–sec-butanol–tert-butanol at 760 mm Hg with a Dvorak-Boublik recirculation still. Liquid activity coefficients were evaluated for the three components and correlated with a Redlich-Kister type equation. Vapor composition and boiling points were correlated from binary and ternary data and showed good agreement with the experimental information.

Original languageEnglish
Pages (from-to)393-396
Number of pages4
JournalJournal of Chemical & Engineering Data
Volume20
Issue number4
DOIs
StatePublished - 1 Oct 1975

ASJC Scopus subject areas

  • Chemistry (all)
  • Chemical Engineering (all)

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