Phase Equilibrium for Phenol Extraction from Aqueous Solution with 2-Pentanone at Different Temperatures-Reference-Cited by-同舟云学术

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Phase Equilibrium for Phenol Extraction from Aqueous Solution with 2-Pentanone at Different Temperatures

Published:2016-09-07 Issue:10 Volume:45 Page:1414-1424
ISSN:0095-9782
Container-title:Journal of Solution Chemistry
language:en
Short-container-title:J Solution Chem

Author:

Lv Ran,Li Libo,Wang Huimin,Chen Yun

Funder

The Fundamental Research Funds for the Central Universities, SCUT

Guangdong Science Foundation

National Natural Science Foundation of China

Project of the Science and Technology New Star of Pearl River in Guangzhou

Publisher

Springer Science and Business Media LLC

Subject

Physical and Theoretical Chemistry,Molecular Biology,Biochemistry,Biophysics

Link

http://link.springer.com/content/pdf/10.1007/s10953-016-0517-3.pdf

Reference27 articles.

1. Jiang, H., Fang, Y., Fu, Y., Guo, Q.: Studies on the extraction of phenol in wastewater. J. Hazard. Mater. B101, 179–190 (2003)

2. Busca, G., Berardinelli, S., Resini, C., Arrighi, L.: Technologies for the removal of phenol from fluid streams: a short review of recent developments. J. Hazard. Mater. 160, 265–288 (2008)

3. Pinto, R., Lintomen, L., Luz Jr., L., Wolf-Maciel, M.: Strategies for recovering phenol from wastewater: thermodynamic evaluation and environmental concerns. Fluid Phase Equilib. 228–229, 447–457 (2005)

4. Lv, R., Wang, Z., Li, L., Chen, Y.: Liquid–liquid equilibria in the ternary systems water + cresols + methyl butyl ketone at 298.2 and 313.2 K: experimental data and correlation. Fluid Phase Equilib. 404, 89–95 (2015)

5. Luo, L., Liu, D., Li, L., Chen, Y.: Phase equilibria of (water + propionic acid or butyric acid + 2-methoxy-2-methylpropane) ternary systems at 298.2 K and 323.2 K. Fluid Phase Equilib. 403, 30–35 (2015)

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2. Liquid–liquid equilibrium for ternary methyl tert-amyl ether + phenol + water system at 283.15, 298.15, and 313.15 K;Separation Science and Technology;2022-07-14

3. Simulation and dynamic control of removal phenols from coal gasification wastewater by synergistic extraction;Separation and Purification Technology;2022-03

4. Influence of acetone and sodium sulfate impurities on the liquid-liquid equilibrium for the phenol extraction with n-butyl acetate;Separation Science and Technology;2022-02-23

5. Ternary (Liquid + Liquid) Equilibrium Experiment and Thermodynamic Modeling for Isoamyl Alcohol + o-Cresol + Water at 298.2, 308.2 and 318.2 K under 101.3 kPa;Journal of Solution Chemistry;2022-02

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