Zobrazeno 1 - 10
of 19
pro vyhledávání: '"Fernando Espiau"'
Publikováno v:
Fluid Phase Equilibria. 363:167-179
This work presents experimental mixing properties, hE and vE, at several temperatures and the isobaric vapor–liquid equilibria (iso-p VLE) at 101.32 kPa for four binaries containing pentane and four alkyl (methyl to butyl) methanoates. Particular c
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::30e1b8901fe28c24b1bb7af6d901cc98
https://doi.org/10.1016/j.fluid.2013.11.026
https://doi.org/10.1016/j.fluid.2013.11.026
Publikováno v:
Industrial & Engineering Chemistry Research. 50:12259-12270
Experimental solubility data are presented for a set of binary systems composed of ionic liquids (IL) derived from pyridium, with the tetrafluoroborate anion, and normal alcohols ranging from ethanol to decanol, in the temperature interval of 275–4
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::dd8aed8a8250b39557876aca28200b87
https://doi.org/10.1021/ie201551w
https://doi.org/10.1021/ie201551w
Publikováno v:
Industrial & Engineering Chemistry Research. 49:9548-9558
This work analyzes the utility of a new model to correlate thermodynamic properties of solutions, the foundations of which have been published in a previous study. The model is applied to a set of experimental data for several properties of binary sy
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::334d96f30999929a0dca780ab327e707
https://doi.org/10.1021/ie101165r
https://doi.org/10.1021/ie101165r
Publikováno v:
Industrial & Engineering Chemistry Research. 49:406-421
A new empirical mathematical model for the Gibbs excess function, gE = ψ(p,T,x), is presented for a multicomponent system. Dependence on the composition is achieved through the so-called active fra...
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::80ee6c2ae29ce6c0314c097806d724a8
https://doi.org/10.1021/ie900898t
https://doi.org/10.1021/ie900898t
Publikováno v:
Industrial & Engineering Chemistry Research. 46:7353-7366
This work shows the utility of a parametric model, as a function of concentration and temperature, to correlate isobaric vapor−liquid equilibrium data and other themodynamic properties of solutions. With the model proposed here, a procedure can be
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::719764e4accaa6b6ae81fbcccaab9ba7
https://doi.org/10.1021/ie0707366
https://doi.org/10.1021/ie0707366
Publikováno v:
Journal of Chemical & Engineering Data. 51:730-742
In this work, the experimental values for excess quantities and are presented at two temperatures and the isobaric vapor−liquid equilibrium data (VLE) at 101.32 kPa for binary systems comprised of the first four propyl alkanoates with tert-butyl al
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::8e68b3da280f247c83a7ceff89044210
https://doi.org/10.1021/je060003c
https://doi.org/10.1021/je060003c
Publikováno v:
Journal of Chemical & Engineering Data. 50:444-454
This work shows the experimental values of excess properties and at two temperatures and the isobaric vapor−liquid equilibria at 101.32 kPa for binary systems composed of the first four butyl alkanoates with tert-butyl alcohol. None of the mixtures
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::17bf6290b5c7724a657651f6d3f08173
https://doi.org/10.1021/je0497350
https://doi.org/10.1021/je0497350
Publikováno v:
Journal of Chemical & Engineering Data. 49:1602-1612
This article presents the experimental values obtained for excess properties and at two temperatures and vapor−liquid equilibria at 101.32 kPa for a group of four binary mixtures composed of four methyl alkanoates (methanoate to butanoate) with ter
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::a03e98582e1cd7245160da02455490a9
https://doi.org/10.1021/je034290l
https://doi.org/10.1021/je034290l
Publikováno v:
Fluid Phase Equilibria. 215:175-186
This article is a theoretical–experimental study on the binary systems ethyl methanoate+alkanes (hexane to decane). Vapour–liquid equilibrium (VLE) data at a pressure of 101.32 kPa are presented for the five systems studied and all were consisten
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::663b8496dd47a604be0c23d62351147c
https://doi.org/10.1016/j.fluid.2003.08.003
https://doi.org/10.1016/j.fluid.2003.08.003
Autor:
Fernando Espiau, Juan Ortega
Publikováno v:
Scopus-Elsevier
This study has used a new polynomial expression with temperature-dependent coefficients as a function based on the so-called active fraction of the mixture components, z(xi), which enabled the thermodynamic vapor−liquid equilibrium quantities, the
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::28d21e98c69e4514a55832eb7796b596
https://doi.org/10.1021/ie030327j
https://doi.org/10.1021/ie030327j