Phase equilibrium measurements and thermodynamic modeling of {CO2 + Diethyl succinate (cas 123-25-1) + cosolvent} systems

Add time:09/07/2019    Source:sciencedirect.com

This work reports experimental phase equilibrium data for the binary systems {CO2(1) + Diethyl succinate (cas 123-25-1)(2)} and {CO2(1) + ethyl acetate(2)}, and for the ternary systems {CO2(1) + diethyl succinate(2) + ethanol(3)} and {CO2(1) + diethyl succinate(2) + ethyl acetate(3)}. The experiments for the binary system {CO2(1) + diethyl succinate(2)} were carried out at temperatures ranging from 308 K to 358 K, and temperatures ranging from 303 K to 343 K for {CO2(1) + ethyl acetate(2)} as well as for all ternary systems. Only vapor-liquid equilibria were observed for all systems. The experimental measurements were carried out in a high-pressure variable-volume view cell containing a movable piston, which allows pressure control inside the cell. Binary and ternary systems were modeled with the Peng-Robinson cubic equation of state with the van der Waals quadratic mixing rule (vdW2). The presence of a cosolvent (ethanol and ethyl acetate) decreased the saturation pressures of either bubble or dew points compared to the binary system CO2 + diethyl succinate, increasing the solubility of diethyl succinate in CO2.

We also recommend Trading Suppliers and Manufacturers of Diethyl succinate (cas 123-25-1). Pls Click Website Link as below: cas 123-25-1 suppliers

Prev:Thermochemical pretreatments for enhancing succinic acid production from industrial hemp (Cannabis sativa L.)
Next:Performance evaluation of CO2 capture with Diethyl succinate (cas 123-25-1))