Phase equilibrium properties of binary and ternary systems containing tert-amylmethyl ether (TAME) as oxygenate additive and gasoline substitution hydrocarbons at 313.15 K

Fluid Phase Equilibria

Volumn 156, Issue 1-2, 1999, Pages 73-87

  Chamorro, César R ^a   Segovia, José J ^a   Martín, María C ^a   Montero, Eduardo A ^b   Villamañán, Miguel A ^a  

^a Laboratorio de Termodinamica   (Spain)

^b UNIVERSITY OF BURGOS   (Spain)

Author keywords

Correlations; Data; Excess Gibbs energy; Hydrocarbons; TAME; VLE low pressure

Indexed keywords

ADDITIVES; BENZENE; BINARY MIXTURES; CORRELATION METHODS; ETHERS; GASOLINE; GIBBS FREE ENERGY; MATHEMATICAL MODELS; OLEFINS; PARAFFINS;

AMYLMETHYL ETHER; BARKER'S METHOD; CYCLOHEXANE; HEPTANE; HEXENE; MARGULES EQUATION;

PHASE EQUILIBRIA;

BENZENE; CYCLOHEXANE; ETHER DERIVATIVE; GASOLINE; HEPTANE; HYDROCARBON; TERT BUTYL METHYL ETHER;

ANALYTIC METHOD; CONFERENCE PAPER; ENERGY; EQUILIBRIUM CONSTANT; LIQUID; OXYGENATION; PRESSURE; TEMPERATURE; THERMODYNAMICS; VAPOR;

EID: 0033558773     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0378-3812(99)00033-3     Document Type: Conference Paper

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