Gallic Acid Separation by DES-Based Aqueous Biphasic Systems: Experimental, ePC-SAFT, and Classical Thermodynamic Study

Gallic acid (GA) is considered a representative polyphenol derived from natural sources. The partitioning behavior of GA can reveal how the polyphenol compounds in fruit residue would separate in techniques such as aqueous biphasic systems (ABS). In recent years, modern ABSs have used deep eutectic solvents (DES) that known as green solvents. In this work, aqueous biphasic systems (ABS) have been utilized to study the partitioning of GA. This study investigates the liquid–liquid equilibria (LLE) of ABS composed of DES and a solution of inorganic salts (K2HPO4 and K3PO4) at a temperature of 298.15 K and atmospheric pressure. The DES used consists of choline chloride (ChCl) as the hydrogen bond acceptor and 1,4-butanediol as the hydrogen bond donor in a 1:3 molar ratio. LLE tie-lines were determined and analyzed, and the partitioning coefficients of GA (KGA) and its extraction efficiency (EGA%) were calculated for each tie-line. The partition coefficient of GA was consistently greater than 1 across all samples, with maximum values of 2.95 and 2.74 for K2HPO4 and K3PO4, respectively. The thermodynamic behavior of the pseudoternary system (salt, DES, and water) was examined using electrolyte solution models by incorporating extended NRTL, extended UNIQUAC, and ePC-SAFT models. Comparisons of the RMSD indicated that these models show good agreement with the experimental data when regressing the binary interaction parameters in the ternary system. These binary interaction parameters were then used to predict additional tie-lines and the continuation of the binodal curves with good accuracy. Based on the predicted tie-lines, the partitioning behavior of GA was regressed, and the highest predicted value of KGA, 3.44, was achieved using an ABS with weight fractions of 0.35 DES, 0.3 K3PO4, and 0.35 water in feed. The RMSD values for ternary systems containing K3PO4 were 0.0086 for the extended NRTL model, 0.0219 for the extended UNIQUAC model, and 0.0506 for the ePC-SAFT model.

Authors

Institutions

Publication Details

Journal
Industrial & Engineering Chemistry Research
Published
2024-10-31
DOI
https://doi.org/10.1021/acs.iecr.4c03399
Citations
2
Primary Topic
Chemical and Physical Properties in Aqueous Solutions
Type
article
Field-Weighted Citation Impact
0.85

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Gallic Acid Separation by DES-Based Aqueous Biphasic Systems: Experimental, ePC-SAFT, and Classical Thermodynamic Study

Sanaz Edrisi, Hamid Bakhshi
2 citations
Industrial & Engineering Chemistry Research
Chemical and Physical Properties in Aqueous Solutions
0.85
article

Gallic Acid Separation by DES-Based Aqueous Biphasic Systems: Experimental, ePC-SAFT, and Classical Thermodynamic Study

Sanaz Edrisi, Hamid Bakhshi
article en
2 citations

Abstract

Gallic acid (GA) is considered a representative polyphenol derived from natural sources. The partitioning behavior of GA can reveal how the polyphenol compounds in fruit residue would separate in techniques such as aqueous biphasic systems (ABS). In recent years, modern ABSs have used deep eutectic solvents (DES) that known as green solvents. In this work, aqueous biphasic systems (ABS) have been utilized to study the partitioning of GA. This study investigates the liquid–liquid equilibria (LLE) of ABS composed of DES and a solution of inorganic salts (K2HPO4 and K3PO4) at a temperature of 298.15 K and atmospheric pressure. The DES used consists of choline chloride (ChCl) as the hydrogen bond acceptor and 1,4-butanediol as the hydrogen bond donor in a 1:3 molar ratio. LLE tie-lines were determined and analyzed, and the partitioning coefficients of GA (KGA) and its extraction efficiency (EGA%) were calculated for each tie-line. The partition coefficient of GA was consistently greater than 1 across all samples, with maximum values of 2.95 and 2.74 for K2HPO4 and K3PO4, respectively. The thermodynamic behavior of the pseudoternary system (salt, DES, and water) was examined using electrolyte solution models by incorporating extended NRTL, extended UNIQUAC, and ePC-SAFT models. Comparisons of the RMSD indicated that these models show good agreement with the experimental data when regressing the binary interaction parameters in the ternary system. These binary interaction parameters were then used to predict additional tie-lines and the continuation of the binodal curves with good accuracy. Based on the predicted tie-lines, the partitioning behavior of GA was regressed, and the highest predicted value of KGA, 3.44, was achieved using an ABS with weight fractions of 0.35 DES, 0.3 K3PO4, and 0.35 water in feed. The RMSD values for ternary systems containing K3PO4 were 0.0086 for the extended NRTL model, 0.0219 for the extended UNIQUAC model, and 0.0506 for the ePC-SAFT model.

Industrial & Engineering Chemistry ResearchVol. 63(45)
Babol Noshirvani University of Technology (IR)
Babol Noshirvani University of Technology
Clean water and sanitation
Openalex Percentile: Top 28%
Chemical and Physical Properties in Aqueous Solutions
0.85
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.