A. Francesconi

发表

Experimental Study of the Excess Molar Volumes of Binary and Ternary Mixtures Containing Water + (1,2-Ethanediol, or 1,2-Propanediol, or 1,3-Propanediol, or 1,2-Butanediol) + (1-n-Butyl-3-methylimidazolium Bromide) at 298.15 K and Atmospheric Pressure

M. Rodrigues, A. Francesconi, 2011 .

Experimental Study of the Excess Molar Enthalpy of Ternary Mixtures Containing Water + (1,2-Propanediol, or 1,3-Propanediol, or 1,2-Butanediol, or 1,3-Butanediol, or 1,4-Butanediol, or 2,3-Butanediol)+Electrolytes at 298.15 K and Atmospheric Pressure

R. F. Checoni, A. Francesconi, 2009 .

Application of the Prigogine–Flory–Patterson model to excess molar enthalpy of binary liquid mixtures containing acetonitrile and 1-alkanol

A. Francesconi, A. Galvão, 2008 .

Measurements of the Molar Heat Capacities and Excess Molar Heat Capacities for Acetonitrile + Diethylamine or sec-Butylamine Mixtures at Various Temperatures and Atmospheric Pressure

R. F. Checoni, A. Francesconi, 2007 .

ERAS modeling of the excess molar enthalpies of binary liquid mixtures of 1-pentanol and 1-hexanol with acetonitrile at atmospheric pressure and 288, 298, 313 and 323 K

A. Francesconi, A. Galvão, 2006 .

Volumetric properties of binary mixtures of acetonitrile and alcohols at different temperatures and atmospheric pressure

A. Francesconi, P. Volpe, R. B. Torres, 2007 .

Salt effect on phase equilibria by a recirculating still

A. Francesconi, R. Zemp, 1992 .

The effect of [bmim][Br] on the solubility of carbon dioxide and methane in glycols at pressures up to 14 MPa and temperatures ranging from 303 to 423 K

A. Francesconi, A. Galvão, 2014 .

Solubility of methane and carbon dioxide in ethylene glycol at pressures up to 14 MPa and temperatures ranging from (303 to 423) K

A. Francesconi, A. Galvão, A. Francesconi, 2010 .

Methane and carbon dioxide solubility in 1,2-propylene glycol at temperatures ranging from 303 to 423 K and pressures up to 12 MPa

A. Francesconi, A. Galvão, 2010 .

Experimental study of methane and carbon dioxide solubility in 1,4 butylene glycol at pressures up to 11 MPa and temperatures ranging from 303 to 423 K

A. Francesconi, A. Galvão, 2009 .

Application of the Prigogine–Flory–Patterson model to excess molar enthalpy of binary liquid mixtures of 1-nonanol or 1-decanol with acetonitrile at atmospheric pressure and 298.15, 303.15 and 308.15 K

A. Francesconi, Dimas Henrique Lanfredi Viola, 2014 .

A model for excess volumes of salty water–acetonitrile mixtures at 298.15 K

A. Francesconi, S. Morrone, 2012 .

Measurement and correlation of the excess molar enthalpy of (1-nonanol, or 1-decanol + acetonitrile) mixtures at (298.15, 303.15, and 308.15) K and atmospheric pressure

A. Francesconi, Dimas Henrique Lanfredi Viola, 2012 .

Measurement and correlation of excess molar enthalpy for (1,2-propanediol, or 1,3-propanediol, or 1,4-butanediol+water) at the temperatures (298.15, 323.15, and 343.15) K

A. Francesconi, M. Nagamachi, A. Z. Francesconi, 2006 .

Experimental study and modelling using the ERAS-Model of the excess molar volume of acetonitrile–alkanol mixtures at different temperatures and atmospheric pressure

A. Francesconi, P. Volpe, R. B. Torres, 2003 .

Application of the ERAS-Model to binary mixtures of diethylamine and s-butylamine with acetonitrile in the temperature range (288.15–303.15) K

A. Francesconi, R. B. Torres, A. Francesconi, 2002 .

New applications of the ERAS-Model: excess volumes of binary liquid mixtures of 1-alkanols with acetonitrile

A. Francesconi, C. G. Pina, 1998 .

Volumetric Properties of Binary Mixtures of Acetonitrile and Chloroalkanes at 25°C and Atmospheric Pressure

A. Francesconi, P. Volpe, R. B. Torres, 2003 .

Measurements of excess molar enthalpy and excess molar heat capacity of (1-heptanol or 1-octanol)+(diethylamine or s-butylamine) mixtures at 298.15 K and 0.1 MPa

R. F. Checoni, A. Francesconi, 2009 .

Measurement and correlation of excess molar enthalpy at various temperatures acetonitrile + diethylamine or s-butylamine mixtures

R. F. Checoni, A. Francesconi, 2005 .

Application of the Prigogine-Flory-Patterson theory to excess molar volume of binary mixtures of acetonitrile with 1-alkanols

A. Francesconi, C. G. Pina, R. B. Torres, 2003 .

Partial molar enthalpy properties and correlation of excess molar enthalpy data of acetonitrile + diethylamine or S-butylamine mixtures at various temperatures and atmospheric pressure

R. F. Checoni, A. Francesconi, 2006 .

Experimental study and ERAS modeling of the excess molar enthalpy of (acetonitrile+1-heptanol or 1-octanol) mixtures at (298.15, 313.15, and 323.15)K and atmospheric pressure

R. F. Checoni, A. Francesconi, Luciane D’Agostini, 2008 .

Excess Gibbs free energies of (n-hexane + propan-1-ol) at 338.15 and 348.15 K and of (n-hexane + propan-2-ol) at 323.15, 338.15, and 348.15 K

M. Maciel, A. Francesconi, 1988 .

Excess molar volumes of binary mixtures of acetonitrile and chloroalkanes at 298.15 K and atmospheric pressure with application of the ERAS-Model

A. Francesconi, P. Volpe, R. B. Torres, 2002 .

Phase equilibriums and PVT data for the methane-methanol system to 300 MPa and 240.degree.C

A. Francesconi, E. U. Franck, H. Lentz, 1981 .

Values of (p, Vm, T) for methane in the range 15 to 270 MPa and 323 to 723 K

A. Francesconi, 1984 .

Excess volumes of (hexane or cyclohexane + propan-2-ol or butan-2-ol) at the temperatures (288.15 and 298.15) K

A. Francesconi, S. Morrone, 1996 .

(1-n-Butyl-3-methylimidazolium Bromide) at 298.15 K and Atmospheric Pressure

A. Francesconi, M. Rodrigues, 2011 .

Excess Gibbs free energies of (hexane + butan-2-ol) and of (cyclohexane + butan-2-ol) at the temperatures (323.15, 338.15, and 348.15) K

M. E. Araújo, M. Maciel, A. Francesconi, 1993 .

Vapor—liquid phase equilibrium measurements for the n-hexane—1-butanol system at 323.15,338.15 and 348.15 K

M. Maciel, A. Francesconi, 1989 .

PHASE EQUILIBRIUMS AND PVT DATA FOR THE METHANE-METHANOL SYSTEM TO 300 MPA AND 240°C

A. Francesconi, E. U. Franck, H. Lentz, 1982 .

Kashagan Field Approaching Production Start-Up: Insight Into Reservoir Characteristics

G. Leoni, V. Tarantini, A. Francesconi, 2013 .

An alternative CFD tool for gas dispersion modelling of heavy gas

Sávio Souza Venâncio Vianna, Juliane Fiates, Vinicius Simoes, 2016 .

Gas−Liquid Solubility of Hydrogen in n-Alcohols (1 ⩽ n ⩽ 4) at Pressures from 3.6 MPa to 10 MPa and Temperatures from 298.15 K to 525.15 K

A. Francesconi, José Vicente H. d‘Angelo† and, 2001 .