Methanol synthesis under supercritical conditions: Calculations of equilibrium conversions by using the Soave-Redlich-Kwong equation of state

Industrial and Engineering Chemistry Research

Volumn 40, Issue 17, 2001, Pages 3801-3805

  Liu, J ^a   Qin, Z ^a   Wang, J ^a  

^a INSTITUTE OF COAL CHEMISTRY   (China)

Author keywords

[No Author keywords available]

Indexed keywords

CALCULATIONS; EQUATIONS OF STATE; SOLVENTS; SYNTHESIS (CHEMICAL);

SUPERCRITICAL CONDITIONS;

METHANOL;

ACETONE; CARBON MONOXIDE; HEXANE; METHANOL; NITROGEN; PENTANE;

EQUILIBRIUM; MATHEMATICAL ANALYSIS; METHANOL; SUPERCRITICAL FLOW; SYNTHESIS;

ARTICLE; CALCULATION; CHEMICAL ANALYSIS; CHEMICAL REACTION; CONCENTRATION RESPONSE; REACTION ANALYSIS; SYNTHESIS; TEMPERATURE; THEORY;

EID: 0035934038     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie0100479     Document Type: Article

References (7)

1. Chemical equilibria in methanol synthesis
2. Study on synthesis of higher alcohols from syngas under supercritical conditions
3. Equilibrium constants from a modified Redlich-Kwong equation of state
4. A modified Soave equation of state for phase equilibrium calculations. 1. Hydrocarbon system
5. Vapor-liquid equilibrium at high pressures. Vapor-phase fugacity coefficients in nonpolar and quantum-gas mixtures