Excess molar enthalpies for mixtures of supercritical CO2 and ethyl acetate and their role in supercritical fluid applications

[Display omitted] ► {CO2+ethyl acetate (EA)} mixtures are studied under conditions of T and P used in supercritical fluid applications. ► (CO2+EA) mixtures exhibit exothermic to very exothermic mixing. ► Very exothermic mixing results when low-density supercritical CO2 is mixed with the liquid EA. ►...

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Veröffentlicht in:The Journal of chemical thermodynamics 2012-08, Vol.51, p.59-64
Hauptverfasser: Zahran, Fouad, Pando, Concepción, Renuncio, Juan A.R., Cabañas, Albertina
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Pando, Concepción
Renuncio, Juan A.R.
Cabañas, Albertina
description [Display omitted] ► {CO2+ethyl acetate (EA)} mixtures are studied under conditions of T and P used in supercritical fluid applications. ► (CO2+EA) mixtures exhibit exothermic to very exothermic mixing. ► Very exothermic mixing results when low-density supercritical CO2 is mixed with the liquid EA. ► Thermal effects are shown to have an effect in supercritical CO2 applications such as SAS precipitations. Mixtures of supercritical CO2 and ethyl acetate (EA) are very often involved in supercritical fluid applications and their thermodynamic properties are required to understand and design these processes. Excess molar enthalpies (HmE) for (CO2+EA) mixtures were measured using an isothermal high-pressure flow calorimeter under conditions of temperature and pressure typically used in supercritical processes: pressures from (9.00 to 18.00)MPa and temperatures from (313.15 to 333.15)K. Mixtures showed exothermic mixing; excess molar enthalpies exhibited a minimum in the CO2-rich region. The effects of pressure and temperature on the excess molar enthalpy of (CO2+EA) are large. The most exothermic HmE values were observed for a coincident CO2 mole fraction value of 0.737 at T/K=(323.15 and 333.15) and P/MPa=9.00: (−4489 and −4407)J·mol−1, respectively. Two-phase splitting was observed in the CO2-rich region at T/K=333.15 and P/MPa=9.00; in this region HmE varies linearly with CO2 mole fraction. For a given mole fraction and temperature, mixtures become more exothermic as pressure decreases. These trends were analyzed in terms of molecular interactions, phase equilibria, density and critical parameters previously reported for (CO2+EA). Excess molar enthalpies here reported were correlated using the Soave–Redlich–Kwong and Peng–Robinson equations of state, and the classical mixing rule with two binary interaction parameters. The influence of the thermal effects on the phase behavior of (CO2+EA) mixtures formed in supercritical antisolvent precipitation experiments was discussed.
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Mixtures of supercritical CO2 and ethyl acetate (EA) are very often involved in supercritical fluid applications and their thermodynamic properties are required to understand and design these processes. Excess molar enthalpies (HmE) for (CO2+EA) mixtures were measured using an isothermal high-pressure flow calorimeter under conditions of temperature and pressure typically used in supercritical processes: pressures from (9.00 to 18.00)MPa and temperatures from (313.15 to 333.15)K. Mixtures showed exothermic mixing; excess molar enthalpies exhibited a minimum in the CO2-rich region. The effects of pressure and temperature on the excess molar enthalpy of (CO2+EA) are large. The most exothermic HmE values were observed for a coincident CO2 mole fraction value of 0.737 at T/K=(323.15 and 333.15) and P/MPa=9.00: (−4489 and −4407)J·mol−1, respectively. Two-phase splitting was observed in the CO2-rich region at T/K=333.15 and P/MPa=9.00; in this region HmE varies linearly with CO2 mole fraction. For a given mole fraction and temperature, mixtures become more exothermic as pressure decreases. These trends were analyzed in terms of molecular interactions, phase equilibria, density and critical parameters previously reported for (CO2+EA). Excess molar enthalpies here reported were correlated using the Soave–Redlich–Kwong and Peng–Robinson equations of state, and the classical mixing rule with two binary interaction parameters. 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Mixtures of supercritical CO2 and ethyl acetate (EA) are very often involved in supercritical fluid applications and their thermodynamic properties are required to understand and design these processes. Excess molar enthalpies (HmE) for (CO2+EA) mixtures were measured using an isothermal high-pressure flow calorimeter under conditions of temperature and pressure typically used in supercritical processes: pressures from (9.00 to 18.00)MPa and temperatures from (313.15 to 333.15)K. Mixtures showed exothermic mixing; excess molar enthalpies exhibited a minimum in the CO2-rich region. The effects of pressure and temperature on the excess molar enthalpy of (CO2+EA) are large. The most exothermic HmE values were observed for a coincident CO2 mole fraction value of 0.737 at T/K=(323.15 and 333.15) and P/MPa=9.00: (−4489 and −4407)J·mol−1, respectively. Two-phase splitting was observed in the CO2-rich region at T/K=333.15 and P/MPa=9.00; in this region HmE varies linearly with CO2 mole fraction. For a given mole fraction and temperature, mixtures become more exothermic as pressure decreases. These trends were analyzed in terms of molecular interactions, phase equilibria, density and critical parameters previously reported for (CO2+EA). Excess molar enthalpies here reported were correlated using the Soave–Redlich–Kwong and Peng–Robinson equations of state, and the classical mixing rule with two binary interaction parameters. The influence of the thermal effects on the phase behavior of (CO2+EA) mixtures formed in supercritical antisolvent precipitation experiments was discussed.</description><subject>Carbon dioxide</subject><subject>Carbon dioxide-expanded solvent</subject><subject>Chemical thermodynamics</subject><subject>Chemistry</subject><subject>Density</subject><subject>Enthalpy</subject><subject>Ethyl acetate</subject><subject>Exact sciences and technology</subject><subject>Excess molar enthalpies</subject><subject>General and physical chemistry</subject><subject>General. 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Theory</topic><topic>Mixing rules</topic><topic>Moles</topic><topic>Precipitation</topic><topic>Supercritical antisolvent precipitation</topic><topic>Supercritical carbon dioxide</topic><topic>Supercritical fluids</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Zahran, Fouad</creatorcontrib><creatorcontrib>Pando, Concepción</creatorcontrib><creatorcontrib>Renuncio, Juan A.R.</creatorcontrib><creatorcontrib>Cabañas, Albertina</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>The Journal of chemical thermodynamics</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Zahran, Fouad</au><au>Pando, Concepción</au><au>Renuncio, Juan A.R.</au><au>Cabañas, Albertina</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Excess molar enthalpies for mixtures of supercritical CO2 and ethyl acetate and their role in supercritical fluid applications</atitle><jtitle>The Journal of chemical thermodynamics</jtitle><date>2012-08-01</date><risdate>2012</risdate><volume>51</volume><spage>59</spage><epage>64</epage><pages>59-64</pages><issn>0021-9614</issn><eissn>1096-3626</eissn><coden>JCTDAF</coden><abstract>[Display omitted] ► {CO2+ethyl acetate (EA)} mixtures are studied under conditions of T and P used in supercritical fluid applications. ► (CO2+EA) mixtures exhibit exothermic to very exothermic mixing. ► Very exothermic mixing results when low-density supercritical CO2 is mixed with the liquid EA. ► Thermal effects are shown to have an effect in supercritical CO2 applications such as SAS precipitations. 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subjects Carbon dioxide
Carbon dioxide-expanded solvent
Chemical thermodynamics
Chemistry
Density
Enthalpy
Ethyl acetate
Exact sciences and technology
Excess molar enthalpies
General and physical chemistry
General. Theory
Mixing rules
Moles
Precipitation
Supercritical antisolvent precipitation
Supercritical carbon dioxide
Supercritical fluids
title Excess molar enthalpies for mixtures of supercritical CO2 and ethyl acetate and their role in supercritical fluid applications
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