Phase equilibrium behavior of the carbon dioxide + benzophenone binary system

Journal Article · Fri Dec 31 23:00:00 EST 1993 · Journal of Chemical and Engineering Data; (United States)

DOI:https://doi.org/10.1021/je00013a044· OSTI ID:5324405

Tarantino, D E; Kohn, J P; Brennecke, J F ^[1]

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1. Univ. of Notre Dame, IN (United States). Dept. of Chemical Engineering

Phase equilibrium behavior of various binary CO[sub 2] + hydrocarbon mixtures has been studied by many researchers, providing data which are useful in the design of economically attractive separation processes using carbon dioxide as a solvent. Pressure, liquid-phase composition, and liquid-phase molar volumes are presented for the binary vapor-liquid system CO[sub 2] + benzophenone at 25, 35, and 50 C. Also, pressure, liquid-phase compositions, and liquid-phase molar volumes on the S[sub 1]-L[sub 1]-V curve and L[sub 1]-L[sub 2]-V curve are presented. The termination points of these loci are located and characterized.

• OSTI ID: 5324405
• Journal Information: Journal of Chemical and Engineering Data; (United States), Journal Name: Journal of Chemical and Engineering Data; (United States) Vol. 39:1; ISSN JCEAAX; ISSN 0021-9568
• Country of Publication: United States
• Language: English

Related Subjects

02 PETROLEUM
020400* -- Petroleum-- Processing
37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY
400105 -- Separation Procedures
BENZOPHENONE
CARBON COMPOUNDS
CARBON DIOXIDE
CARBON OXIDES
CHALCOGENIDES
DATA
EXPERIMENTAL DATA
EXTRACTION
INFORMATION
KETONES
NUMERICAL DATA
ORGANIC COMPOUNDS
OXIDES
OXYGEN COMPOUNDS
PHASE STUDIES
PHYSICAL PROPERTIES
SEPARATION PROCESSES
SOLVENT EXTRACTION
SOLVENT PROPERTIES
SUPERCRITICAL GAS EXTRACTION
THERMODYNAMIC PROPERTIES