Search Results - "Follegatti–Romero, Luis A."

Measurement and prediction of speeds of sound of fatty acid ethyl esters and ethylic biodiesels by Freitas, Samuel V.D., Santos, Ângela, Moita, Maria-Luísa C.J., Follegatti-Romero, Luis A., Dias, Telma P.V.B., Meirelles, Antonio J.A., Daridon, Jean-Luc, Lima, Álvaro S., Coutinho, João A.P.

“…► Measurement of speed of sound for several fatty acid ethyl esters was carried. ► Speed of sound data for ethylic biodiesels is reported for the first time. ►…”
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Low pressure vapor–liquid equilibria modeling of biodiesel related systems with the Cubic–Plus–Association (CPA) equation of state by Oliveira, Mariana B., Follegatti–Romero, Luis A., Lanza, Marcelo, Batista, Fabio R.M., Batista, Eduardo A.C., Meirelles, Antonio J.A.

“…•CPA was applied to predict VLE of 8 binary systems composed of FAEs and tetradecane.•No binary interaction parameters were used for the binary systems.•CPA…”
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Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K by Cavalcanti, Kyriale V.M., Follegatti-Romero, Luz M., Dalmolin, Irede, Follegatti-Romero, Luis A.

“…•Liquid-liquid equilibrium was measured for water + HMF + alcohols at 298.15 K.•1-Pentanol can be suitable for HMF removal from water.•NRTL and UNIQUAC models…”
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Supercritical CO2 extraction of omega-3 rich oil from Sacha inchi (Plukenetia volubilis L.) seeds by Follegatti-Romero, Luis A., Piantino, Carla R., Grimaldi, Renato, Cabral, Fernando A.

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Liquid-liquid equilibrium in systems used for the production of 5-hydroxymethylfurfural from biomass using alcohols as solvents by Dalmolin, Irede, Pinto, Rafaela R., de Oliveira, Leonardo H., Follegatti-Romero, Luis A., Costa, Aline C., Aznar, Martín

“…•New LLE data were determined for the systems containing water+5-HMF+alcohols.•5-HMF distributed similarly for 1-butanol and 2-pentanol but little in…”
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Liquid-liquid equilibria for ternary systems containing ethylic palm oil biodiesel + ethanol + glycerol/water: Experimental data at 298.15 and 323.15 K and thermodynamic modeling by DE AZEVEDO ROCHA, Enio G, FOLLEGATTI-ROMERO, Luis A, DUVOISIN, Sérgio, AZNAR, Martin

“…Several plant species have been proposed as source of oil for the transesterification reaction that generates the mixture of esters known as biodiesel; this…”
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A new distillation plant for neutral alcohol production by Batista, Fabio R.M., Follegatti-Romero, Luis A., Meirelles, Antonio J.A.

“…•New distillation plant for high quality bioethanol production.•Simulations considering 19 components on fermented must (wine).•Use of experimental design…”
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Liquid-liquid equilibria for ternary systems containing ethyl esters, ethanol and glycerol at 323.15 and 353.15 K by FOLLEGATTI-ROMERO, Luis A, OLIVEIRA, Mariana B, BATISTA, Fabio R. M, BATISTA, Eduardo A. C, COUTINHO, Joao A. P, MEIRELLES, Antonio J. A

“…The knowledge and the capacity to describe the phase equilibria of systems composed by transesterification products are very important for an adequate design…”
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Computational simulation applied to the investigation of industrial plants for bioethanol distillation by Batista, Fabio R.M., Follegatti-Romero, Luis A., Bessa, L.C.B.A., Meirelles, Antonio J.A.

“…► An alcoholic wine containing ethanol, water and seventeen other congeners was considered in the simulations. ► A validation of simulations against…”
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Liquid−Liquid Equilibrium for Ternary Systems Containing Ethyl Esters, Anhydrous Ethanol and Water at 298.15, 313.15, and 333.15 K by Follegatti-Romero, Luis A, Lanza, Marcelo, Batista, Fabio R. M, Batista, Eduardo A. C, Oliveira, Mariana B, Coutinho, João A. P, Meirelles, Antonio J. A

“…The most common method used for purifying biodiesel is washing with water. During the biodiesel washing process, two phases are formed, a water-rich phase and…”
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Liquid–liquid equilibria for ethyl esters+ethanol+water systems: Experimental measurements and CPA EoS modeling by Follegatti-Romero, Luis A., Oliveira, Mariana B., Batista, Eduardo A.C., Coutinho, João A.P., Meirelles, Antonio J.A.

“…► Water washing of biodiesel is a very effective process to remove ethanol from ester phase. ► LLE data of water systems are important for design and operation…”
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Mutual Solubility for Systems Composed of Vegetable Oil + Ethanol + Water at Different Temperatures by da Silva, César A. S, Sanaiotti, Guilherme, Lanza, Marcelo, Follegatti-Romero, Luis A, Meirelles, Antonio J. A, Batista, Eduardo A. C

“…This study presents liquid−liquid equilibrium data for systems of interest in biodiesel production and the refining of edible oils by liquid−liquid extraction…”
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Mutual Solubility of Pseudobinary Systems Containing Vegetable Oils and Anhydrous Ethanol from (298.15 to 333.15) K by Follegatti-Romero, Luis A., Lanza, Marcelo, da Silva, César A. S., Batista, Eduardo A. C., Meirelles, Antonio J. A.

“…The two-phase base-catalyzed transesterification of vegetable oils with short chain alcohols is common in the production of biodiesel. The reactants (vegetable…”
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Modelling thermophysical properties of mixtures of 2-hydroxyethyl ammonium-based ionic liquids + water, methanol, or ethanol with the electrolyte-cubic plus association equation of state by Follegatti-Romero, Luis A., Liang, Xiaodong

“…This work presents a theoretical study using the electrolyte Cubic-Plus-Association (e-CPA) equation of state combined with quantum chemistry computations, for…”
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Predicting imidazolium ionic liquid properties with a simple molecular volume-based SAFT-VR Mie approach by Beraldo, Cleiton S., Liang, Xiaodong, Follegatti-Romero, Luis A.

“…[Display omitted] •The extrapolation power of a novel parametrization method is evaluated.•The parametrization assumes a strong correlation between the COSMO…”
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Predicting the solubility of gases in imidazolium-based ionic liquids with SAFT-VR Mie EoS by a novel approach based on COSMO by Beraldo, Cleiton S., Liang, Xiaodong, Follegatti-Romero, Luis A.

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Density, viscosity, and thermal stability of alkanolamine-based ionic liquids by Bressan, Gabriel L., Alcantara, Murilo L., Follegatti-Romero, Luis A.

“…•The density, viscosity, and excess volume of three alkanolammonium-based PILs were measured and modeled.•VFT and Redlich-Kister models accurately described…”
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Modelling mixtures of ammonium and pyridinium-based ionic liquids and carbon dioxide with the Cubic Plus Association Equation of state by Frias, Renan M., Follegatti-Romero, Luz M., Follegatti-Romero, Luis A.

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Liquid–Liquid Equilibrium for 2‑Methylfuran (Biofuel) + Alcohols + Water Systems: Experiments and Thermodynamic Modeling by Moreira, Leila C., de Araújo, Paulo C. C., Soares, Rafael de P., Follegatti-Romero, Luis A.

“…Purification requirements for 2-methylfuran (MF), a new furan biofuel, have increased the demand for experimental liquid–liquid equilibrium (LLE) data and the…”
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Modelling acid gas mixtures of polar aprotic solvents and CO2 with the Cubic Plus Association equation of state by Follegatti-Romero, Luis A., Oller do Nascimento, Cláudio A., Liang, Xiaodong

“…[Display omitted] •Mixtures relevant to CO2 capture applications from atmospheric to supercritical conditions were investigated.•CPA results for physical…”
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