Evidence map›Paper›PMID 40745327›Full record

ArticleJournal of biological engineering2025

Volatile fatty acids recovery from thermophilic acidogenic fermentation using hydrophobic deep eutectic solvents.

Can Liu, Xueyao Zhang, Qi Qiao, Zhiwu Wang, Qing Shao, Jian Shi

Abstract read
In one paragraph

Article in Journal of biological engineering, 2025. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Not yet cited in PubMed.

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1 · What the graph read from it

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3 · Its place in the literature

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4 · The record

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5 · Who and what money

Authors and funding

6 authors.

Can LiuDepartment of Biosystems and Agricultural Engineering, University of Kentucky, Lexington, KY, 40546, USA. canliu.biosysteng@gmail.com.
Xueyao ZhangDepartment of Biological Systems Engineering, Virginia Polytechnic Institute and State University, Blacksburg, VA, 24061, USA.
Qi QiaoDepartment of Chemical and Materials Engineering, University of Kentucky, Lexington, KY, 40506, USA.
Zhiwu WangDepartment of Biological Systems Engineering, Virginia Polytechnic Institute and State University, Blacksburg, VA, 24061, USA.
Qing ShaoDepartment of Chemical and Materials Engineering, University of Kentucky, Lexington, KY, 40506, USA.
Jian ShiDepartment of Biosystems and Agricultural Engineering, University of Kentucky, Lexington, KY, 40546, USA.

Funding

National Institute of Food and Agriculture 1018315
6 · The paper itself

Abstract

backgroundVolatile fatty acids (VFA) derived from acidogenic fermentation can be recovered as precursors for synthesizing value-added chemicals to replace those from fossil fuels. However, separating VFAs from the fermentation broth with complex constituents and a high-water content is an energy-intensive process.

resultsThis study developed an innovative membrane extraction technology, utilizing hydrophobic deep eutectic solvents (HDESs) as the acceptor phase along with an omniphobic membrane contactor for efficient extraction of anhydrous VFAs. All tested HDESs, three terpene-based type V HDESs and two tetraalkylammonium halide-based type III HDESs, were found to effectively extract VFAs at pH 3, with extraction recovery percentages (ERPs) up to 80% and 92% for 4 C- and 5 C- VFAs, respectively. However, the ERP of type V HDESs decreased significantly when the aqueous phase was adjusted to pH 6. Molecular simulations suggest that the VFA-HDES interactions vary with VFA dissociation, where the ion-dipole interactions between VFA conjugate bases and hydrogen bond donors at near-neutral pH conditions may destabilize the type V HDES structure and lead to reduced extraction efficiency. The temperature increases from 25 °C to 55 °C did not significantly impact VFA distribution, but a higher temperature could enhance cross-membrane mass transfer.

conclusionsThis study demonstrated a novel continuous VFA extraction technology based on HDESs and elucidates the impact of temperature, pH, impurities in real fermentate and the applicability of an integrated membrane system through combined experimental and computational approaches.

Indexed as

Arrested methanogenesisDeep eutectic solventMembrane extractionMolecular simulationVolatile fatty acid

Identifiers

PMID40745327
PMCPMC12315322

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Read under generation 80e0d062 · epoch 390. Bibliography from PubMed, PubMed Central and OpenAlex; grants from NIH RePORTER; trial links from ClinicalTrials.gov; estimates, votes and beliefs from the OpenQuestion graph.