Forero G., Luis A. et al. published their research in Fluid Phase Equilibria in 2014 | CAS: 763-69-9

Ethyl 3-ethoxypropanoate (cas: 763-69-9) belongs to esters. Esters perform as high-grade solvents for a broad array of plastics, plasticizers, resins, and lacquers, and are one of the largest classes of synthetic lubricants on the commercial market. Polyesters are important plastics, with monomers linked by ester moieties. Esters contain a carbonyl center, which gives rise to 120° C–C–O and O–C–O angles. Unlike amides, esters are structurally flexible functional groups because rotation about the C–O–C bonds has a low barrier. Their flexibility and low polarity is manifested in their physical properties; they tend to be less rigid (lower melting point) and more volatile (lower boiling point) than the corresponding amides. Recommanded Product: 763-69-9

A modified Patel-Teja cubic equation of state. Part II: Parameters for polar substances and its mixtures was written by Forero G., Luis A.;Velasquez J., Jorge A.. And the article was included in Fluid Phase Equilibria in 2014.Recommanded Product: 763-69-9 The following contents are mentioned in the article:

In this work, the parameters of the equation of state formed by the Patel-Teja pressure-volume-temperature relationship and the alpha function of Heyen have been estimated for 184 polar substances. To obtain the parameters of the proposed model, pseudo-exptl. data have been generated using the DIPPR correlations for vapor pressure and liquid d. The proposed model in conjunction with the Wong-Sandler mixing rules and the NRTL activity model have been used to describe the vapor liquid equilibrium of some complex mixtures Three kinds of binary systems have been analyzed and they are those of the type: polar substance/aromatic, polar substance/n-alkane and polar substance/n-alkanol. Based on the homologous series concept, generalized expressions for the binary interaction parameters in the Wong-Sandler-NRTL mixing rules were developed in order to correlate vapor-liquid equilibrium at low pressures for the selected mixtures For n-alkanes and aromatic compounds, the acentric factor has been used to generalize the binary interaction parameters for mixtures with a polar substance and these kinds of compounds In the case of systems composed by a polar substance and an alc., the reduced dipole moment of the alcs. is used to develop the generalized expressions. Ninety-two binary mixtures were analyzed and a relative average absolute deviation of 1.21% was estimated for the bubble pressure. Finally, the model was validated by predicting binary vapor-liquid equilibrium at high pressures and for ternary mixtures In both cases, the results are satisfactory. The average absolute deviations in bubble pressure are 2.34% for high pressure predictions and 1.15% for ternary mixtures This study involved multiple reactions and reactants, such as Ethyl 3-ethoxypropanoate (cas: 763-69-9Recommanded Product: 763-69-9).

Ethyl 3-ethoxypropanoate (cas: 763-69-9) belongs to esters. Esters perform as high-grade solvents for a broad array of plastics, plasticizers, resins, and lacquers, and are one of the largest classes of synthetic lubricants on the commercial market. Polyesters are important plastics, with monomers linked by ester moieties. Esters contain a carbonyl center, which gives rise to 120° C–C–O and O–C–O angles. Unlike amides, esters are structurally flexible functional groups because rotation about the C–O–C bonds has a low barrier. Their flexibility and low polarity is manifested in their physical properties; they tend to be less rigid (lower melting point) and more volatile (lower boiling point) than the corresponding amides. Recommanded Product: 763-69-9

Referemce:
Ester – Wikipedia,
Ester – an overview | ScienceDirect Topics