The Potential of Non-Ionic Surfactants for Extraction of Lactic Acid from Aqueous Solution

Lactic acid, an important commodity chemical for various applications, is mainly produced through fermentation. In this study, the potential of non-ionic surfactants (an alcohol ethoxylate (AE) and two alcohol alkoxylates (AAs)) as solvents for the extraction of lactic acid from aqueous solutions is...

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Main Authors: Remil Aguda, Shayla LeBoeuf, Cody Stelly, Samantha Bonilla, Brandon LeBlanc, William Holmes, Rafael Hernandez, Mark E. Zappi, Emmanuel D. Revellame
Format: Article
Language:English
Published: MDPI AG 2020-07-01
Series:Applied Sciences
Subjects:
Online Access:https://www.mdpi.com/2076-3417/10/15/5315
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author Remil Aguda
Shayla LeBoeuf
Cody Stelly
Samantha Bonilla
Brandon LeBlanc
William Holmes
Rafael Hernandez
Mark E. Zappi
Emmanuel D. Revellame
author_facet Remil Aguda
Shayla LeBoeuf
Cody Stelly
Samantha Bonilla
Brandon LeBlanc
William Holmes
Rafael Hernandez
Mark E. Zappi
Emmanuel D. Revellame
author_sort Remil Aguda
collection DOAJ
description Lactic acid, an important commodity chemical for various applications, is mainly produced through fermentation. In this study, the potential of non-ionic surfactants (an alcohol ethoxylate (AE) and two alcohol alkoxylates (AAs)) as solvents for the extraction of lactic acid from aqueous solutions is reported for the first time. Ternary mixtures containing lactic acid, water, and surfactants were prepared for the assessment. The results indicated that for all the systems, the water–surfactant binary pair exhibits partial immiscibility. Furthermore, the results suggested that with respect to the size of the two-phase region and stability of phases developed, the AE is the suitable solvent for the targeted extraction process. Thus, tie-lines for the system lactic acid + water + AE were then determined to establish the phase diagram of the system at 308.15 K. From the tie-lines, distribution coefficients and separation factors were estimated, which indicated that a compromise between the size and number of extraction units is necessary if AE is to be used as a solvent for lactic acid extraction. The extraction efficiency was estimated to be only about 37–48%. Nevertheless, the biodegradability and non-toxicity of AE makes it a viable solvent for the development of the extractive lactic acid fermentation process.
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spelling doaj.art-3c450e71723e45ab80e818c2e92b81082023-11-20T08:38:31ZengMDPI AGApplied Sciences2076-34172020-07-011015531510.3390/app10155315The Potential of Non-Ionic Surfactants for Extraction of Lactic Acid from Aqueous SolutionRemil Aguda0Shayla LeBoeuf1Cody Stelly2Samantha Bonilla3Brandon LeBlanc4William Holmes5Rafael Hernandez6Mark E. Zappi7Emmanuel D. Revellame8Department of Chemical Engineering, University of Louisiana at Lafayette, Lafayette, LA 70504, USADepartment of Chemical Engineering, University of Louisiana at Lafayette, Lafayette, LA 70504, USADepartment of Chemical Engineering, University of Louisiana at Lafayette, Lafayette, LA 70504, USADepartment of Chemical Engineering, University of Louisiana at Lafayette, Lafayette, LA 70504, USADepartment of Chemical Engineering, University of Louisiana at Lafayette, Lafayette, LA 70504, USAThe Energy Institute of Louisiana, University of Louisiana at Lafayette, Lafayette, LA 70504, USADepartment of Chemical Engineering, University of Louisiana at Lafayette, Lafayette, LA 70504, USADepartment of Chemical Engineering, University of Louisiana at Lafayette, Lafayette, LA 70504, USAThe Energy Institute of Louisiana, University of Louisiana at Lafayette, Lafayette, LA 70504, USALactic acid, an important commodity chemical for various applications, is mainly produced through fermentation. In this study, the potential of non-ionic surfactants (an alcohol ethoxylate (AE) and two alcohol alkoxylates (AAs)) as solvents for the extraction of lactic acid from aqueous solutions is reported for the first time. Ternary mixtures containing lactic acid, water, and surfactants were prepared for the assessment. The results indicated that for all the systems, the water–surfactant binary pair exhibits partial immiscibility. Furthermore, the results suggested that with respect to the size of the two-phase region and stability of phases developed, the AE is the suitable solvent for the targeted extraction process. Thus, tie-lines for the system lactic acid + water + AE were then determined to establish the phase diagram of the system at 308.15 K. From the tie-lines, distribution coefficients and separation factors were estimated, which indicated that a compromise between the size and number of extraction units is necessary if AE is to be used as a solvent for lactic acid extraction. The extraction efficiency was estimated to be only about 37–48%. Nevertheless, the biodegradability and non-toxicity of AE makes it a viable solvent for the development of the extractive lactic acid fermentation process.https://www.mdpi.com/2076-3417/10/15/5315alcohol ethoxylatealcohol propoxylatephase equilibriaextractive fermentationpseudo-ternary system
spellingShingle Remil Aguda
Shayla LeBoeuf
Cody Stelly
Samantha Bonilla
Brandon LeBlanc
William Holmes
Rafael Hernandez
Mark E. Zappi
Emmanuel D. Revellame
The Potential of Non-Ionic Surfactants for Extraction of Lactic Acid from Aqueous Solution
Applied Sciences
alcohol ethoxylate
alcohol propoxylate
phase equilibria
extractive fermentation
pseudo-ternary system
title The Potential of Non-Ionic Surfactants for Extraction of Lactic Acid from Aqueous Solution
title_full The Potential of Non-Ionic Surfactants for Extraction of Lactic Acid from Aqueous Solution
title_fullStr The Potential of Non-Ionic Surfactants for Extraction of Lactic Acid from Aqueous Solution
title_full_unstemmed The Potential of Non-Ionic Surfactants for Extraction of Lactic Acid from Aqueous Solution
title_short The Potential of Non-Ionic Surfactants for Extraction of Lactic Acid from Aqueous Solution
title_sort potential of non ionic surfactants for extraction of lactic acid from aqueous solution
topic alcohol ethoxylate
alcohol propoxylate
phase equilibria
extractive fermentation
pseudo-ternary system
url https://www.mdpi.com/2076-3417/10/15/5315
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