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Dive into the research topics where Dilek Özmen is active.

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Featured researches published by Dilek Özmen.


Brazilian Journal of Chemical Engineering | 2004

Liquid-liquid equilibria of propionic acid - water - solvent (n-hexane, cyclohexane, cyclohexanol and cyclohexyl acetate) ternaries at 298.15 K

Dilek Özmen; Umur Dramur; Beşir Tatlı

The experimental liquid-liquid equilibrium data on propionic acid-water-solvent ternary mixtures at a temperature of 298.15 K are presented. The solvents are n-hexane, cyclohexane, cyclohexanol and cyclohexyl acetate. The distribution coefficients and separation factors are reported. The tie line data are correlated using the methods of Othmer-Tobias and Hand. The experimental results are compared with the values predicted by the UNIFAC group-contribution method.


Journal of Dispersion Science and Technology | 2018

Design of Optimum Response Surface Experiments for Adsorption of Acetic, Butyric, and Oxalic Acids on Amberlyst A21

Sezin Kalyoncu Sarı; Dilek Özmen

ABSTRACT In this study the adsorption equilibria of acetic, butyric, and oxalic acids onto Amberlyst A21 were investigated experimentally at 25°C. The process was optimized using response surface methodology (RSM). The time to reach the equilibrium state, effects of adsorbent amount, and initial acid concentrations on adsorption efficiency were investigated. Freundlich, Langmuir, and Temkin isotherms were applied to experimental data. The Freundlich isotherm revealed better results than the others. In addition to the main aim of this research, a statistical/mathematical approach – RSM – was utilized to simulate and determine the optimum conditions of acetic, butyric, and oxalic acids removal by Amberlyst A21 using three selected parameters (adsorbent dose, initial dye concentration, and type of acids). The significance of independent variables and their interactions were tested by the analysis of variance (ANOVA). The optimum acid concentration, amount of adsorbent, type of acid, and removal of acid (%) were found by desirability function to be 0.199 mol/L, 1.999 g, butyric acid, and 84.537%, respectively. GRAPHICAL ABSTRACT


Fluid Phase Equilibria | 2008

Determination and correlation of liquid–liquid equilibria for the (water+carboxylic acid+dimethyl maleate) ternary systems at T =298.2K

Dilek Özmen


The Journal of Chemical Thermodynamics | 2005

(liquid + liquid) equilibria of (water + propionic acid + dimethyl phthalate) at several temperatures

Dilek Özmen; Süheyla Çehreli; Umur Dramur


The Journal of Chemical Thermodynamics | 2007

(liquid + liquid) equilibria of (water + propionic acid + dipropyl ether or diisopropyl ether) at T = 298.2 K

Dilek Özmen


The Journal of Chemical Thermodynamics | 2005

(Liquid + liquid) equilibria of (water + propionic acid + diethyl phthalate) at several temperatures

Süheyla Çehreli; Dilek Özmen; Beşir Tatlı


Fluid Phase Equilibria | 2006

(Liquid + liquid) equilibria of (water + 1-propanol + solvent) at T = 298.2 K

Siiheyla Cehreli; Dilek Özmen; Umur Dramur


Fluid Phase Equilibria | 2006

(Liquid + liquid) equilibria of (water + propionic acid + methyl isoamyl ketone or diisobutyl ketone or ethyl isoamyl keton) at T = 298.2 K

Dilek Özmen


Fluid Phase Equilibria | 2007

Phase equilibria of water + 1-propanol + solvent (n-amyl acetate, cyclohexanol, and cyclohexyl acetate) at T = 298.2 K

Dilek Özmen; Süheyla Çehreli


Fluid Phase Equilibria | 2010

Liquid + liquid equilibria for the quaternary systems of (water + acetic acid + mixed solvent) at 298.2 K and atmospheric pressure

Dilek Özmen; M. İmge Şenoymak

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