Erol İnce
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Research Interests
Erol İnce has a total of 8 co-authors. Here are the top co-authors by number of shared publications:
- Sah Ismail Kirbaslar
Department of Chemical Engineering Faculty of Engineering Istanbul University‐Cerrahpaşa Istanbul Türkiye
4 shared publications Dana Constantinescu
DDBST GmbH, Marie-Curie-Str. 10, D-26129 Oldenburg, Germany
2 shared publications- Melisa Lalikoglu
Engineering Faculty, Chemical Engineering Department, Istanbul University, 34320, Avcilar/Istanbul, Turkey
2 shared publications - Derya Dişpinar
R&D Non-Ferrous Metal Treatment, Enschede, The Netherlands
1 shared publication - Emel Çalışkan
Istanbul University - Cerrahpasa
1 shared publication Sadık Kaan İpek
Teknik Alüminyum San. A.Ş.
1 shared publication
Latest Publications
- Open Access
- 1 January 2022
- Published by Springer Nature
- p. C1
Correction to: Development of Coating Methods of Fiber Reinforced for Different Matrix Composites for Industrial Applications
- 1 January 2022
- Published by Springer Nature
- p. C1
Open AccessCorrection to: Development of Coating Methods of Fiber Reinforced for Different Matrix Composites for Industrial Applications
- 15 October 2014
- Published by American Chemical Society (ACS) in Journal of Chemical & Engineering Data
- Vol. 59 (11) , 3353-3358
Liquid Phase Equilibria of the Water + Acetic Acid + Dimethyl Carbonate Ternary System at Several Temperatures
- 15 October 2014
- Published by American Chemical Society (ACS) in Journal of Chemical & Engineering Data
- Vol. 59 (11) , 3353-3358
Liquid Phase Equilibria of the Water + Acetic Acid + Dimethyl Carbonate Ternary System at Several Temperatures
- 29 August 2014
- Published by American Chemical Society (ACS) in Journal of Chemical & Engineering Data
- Vol. 59 (9) , 2781-2787
Liquid Phase Equilibria of Water + Formic Acid + Dimethyl Carbonate Ternary System at Several Temperatures
- 29 August 2014
- Published by American Chemical Society (ACS) in Journal of Chemical & Engineering Data
- Vol. 59 (9) , 2781-2787
Liquid Phase Equilibria of Water + Formic Acid + Dimethyl Carbonate Ternary System at Several Temperatures
- 1 May 2014
- Published by Elsevier in Fluid Phase Equilibria
- Vol. 370, 19-23
(Liquid+liquid) equilibria of the (water+carboxylic acid+dibasic esters mixture (DBE-2)) ternary systems
- 1 May 2014
- Published by Elsevier in Fluid Phase Equilibria
- Vol. 370, 19-23
(Liquid+liquid) equilibria of the (water+carboxylic acid+dibasic esters mixture (DBE-2)) ternary systems
- 7 August 2007
- Published by American Chemical Society (ACS) in Journal of Chemical & Engineering Data
- Vol. 52 (5) , 1889-1893
Liquid−Liquid Equilibria for Ternary Systems of Water + Formic Acid + Dibasic Esters
- 7 August 2007
- Published by American Chemical Society (ACS) in Journal of Chemical & Engineering Data
- Vol. 52 (5) , 1889-1893
Liquid−Liquid Equilibria for Ternary Systems of Water + Formic Acid + Dibasic Esters
- 1 March 2005
- Published by Elsevier in Fluid Phase Equilibria
- Vol. 230 (1-2) , 58-63
Liquid–liquid equilibria of the ternary system water+acetic acid+dimethyl adipate
- 1 March 2005
- Published by Elsevier in Fluid Phase Equilibria
- Vol. 230 (1-2) , 58-63
Liquid–liquid equilibria of the ternary system water+acetic acid+dimethyl adipate
- 31 December 2004
- Published by Taylor & Francis in Separation Science and Technology
- Vol. 39 (13) , 3151-3162
Liquid–Liquid Equilibria of Water + Ethanol + Dibasic Esters Mixture (Dimethyl Adipate + Dimethyl Glutarate + Dimethyl Succinate) Ternary System
Liquid–liquid equilibrium data for the ternary system water + ethanol + mixture of dibasic esters (dimethyl adipate + dimethyl glutarate + dimethyl succinate) have been determined experimentally at 298.15, 308.15 and 318.15 K. Complete phase diagrams were obtained by determining solubility and tie-line data. Distribution coefficients and separation factors were evaluated for the immiscibility region.
- 31 December 2004
- Published by Taylor & Francis in Separation Science and Technology
- Vol. 39 (13) , 3151-3162
Liquid–Liquid Equilibria of Water + Ethanol + Dibasic Esters Mixture (Dimethyl Adipate + Dimethyl Glutarate + Dimethyl Succinate) Ternary System
Liquid–liquid equilibrium data for the ternary system water + ethanol + mixture of dibasic esters (dimethyl adipate + dimethyl glutarate + dimethyl succinate) have been determined experimentally at 298.15, 308.15 and 318.15 K. Complete phase diagrams were obtained by determining solubility and tie-line data. Distribution coefficients and separation factors were evaluated for the immiscibility region.
- 1 October 2003
- Published by Elsevier in The Journal of Chemical Thermodynamics
- Vol. 35 (10) , 1671-1679
(Liquid+liquid) equilibria of (water+ethanol+dimethyl glutarate) at several temperatures
- 1 October 2003
- Published by Elsevier in The Journal of Chemical Thermodynamics
- Vol. 35 (10) , 1671-1679
(Liquid+liquid) equilibria of (water+ethanol+dimethyl glutarate) at several temperatures
- Open Access
- 1 April 2002
- Published by FapUNIFESP (SciELO) in Brazilian Journal of Chemical Engineering
- Vol. 19 (2) , 243-254
Liquid-Liquid equilibria of the water-acetic acid-butyl acetate system
Experimental liquid-liquid equilibria of the water-acetic acid-butyl acetate system were studied at temperatures of 298.15± 0.20, 303.15± 0.20 and 308.15± 0.20 K. Complete phase diagrams were obtained by determining solubility and tie-line data. The reliability of the experimental tie-line data was ascertained by using the Othmer and Tobias correlation. The UNIFAC group contribution method was used to predict the observed ternary liquid-liquid equilibrium (LLE) data. It was found that UNIFAC group interaction parameters used for LLE did not provide a good prediction. Distribution coefficients and separation factors were evaluated for the immiscibility region
- 1 April 2002
- Published by FapUNIFESP (SciELO) in Brazilian Journal of Chemical Engineering
- Vol. 19 (2) , 243-254
Open AccessLiquid-Liquid equilibria of the water-acetic acid-butyl acetate system
Experimental liquid-liquid equilibria of the water-acetic acid-butyl acetate system were studied at temperatures of 298.15± 0.20, 303.15± 0.20 and 308.15± 0.20 K. Complete phase diagrams were obtained by determining solubility and tie-line data. The reliability of the experimental tie-line data was ascertained by using the Othmer and Tobias correlation. The UNIFAC group contribution method was used to predict the observed ternary liquid-liquid equilibrium (LLE) data. It was found that UNIFAC group interaction parameters used for LLE did not provide a good prediction. Distribution coefficients and separation factors were evaluated for the immiscibility region