New vapor-liquid equilibria (VLE) data at 323.15, 333.15, 343.15, and 353.15 K and pressures up to 112.9 bar are reported for the carbon dioxide + 2-methyl-2-propanol system. The experimental method used in this work was a static analytical method with liquid and vapor phases sampling using a rapid online sampler injector (ROLSI™) coupled to a gas chromatograph (GC) for analysis. Measured VLE data and literature data for carbon dioxide + 2-methyl-2-propanol system were modeled with the Soave-Redlich-Kwong (SRK) cubic equation of state with classical van der Waals (two-parameter conventional mixing rule, 2PCMR) mixing rules. A single set of interaction parameters that lead to a correct phase behavior was used in this work to model the new VLE data and critical points of the mixtures in a wide range of temperature and pressure. The SRK prediction results were compared to the new data measured in this study and to available literature data.
Issue
Open Access
Volume 12, Issue 9 - 12(9) Special Issue: Chemistry and Chemical Engineering - Materials
September 2014
Contents
-
May 1, 2014
-
May 1, 2014
Issues in this Volume
-
Issue 12
-
Issue 11
-
Issue 10
-
Issue 912(9) Special Issue: Chemistry and Chemical Engineering - Materials
-
Issue 812(8) Special Issue: Chemistry and Chemical Engineering - Environmental and Biochemistry
-
Issue 712(7) Special Issue: Chemistry and Chemical Engineering - Physical Chemistry
-
Issue 6
-
Issue 5
-
Issue 4
-
Issue 3
-
Issue 2
-
Issue 1
Issues in this Volume
-
Issue 12
-
Issue 11
-
Issue 10
-
Issue 912(9) Special Issue: Chemistry and Chemical Engineering - Materials
-
Issue 812(8) Special Issue: Chemistry and Chemical Engineering - Environmental and Biochemistry
-
Issue 712(7) Special Issue: Chemistry and Chemical Engineering - Physical Chemistry
-
Issue 6
-
Issue 5
-
Issue 4
-
Issue 3
-
Issue 2
-
Issue 1