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Kinetics of the extraction of succinic acid with Tri-n-octylamine in 1-Octanol solutions

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TLDR
In this paper, the intrinsic kinetics of succinic acid from aqueous solution with 1-octanol solutions of tri-n-octylamine (TOA) were carried out using a stirred cell with a microporous hydrophobic membrane.
Abstract
Kinetic studies for the extraction of succinic acid from aqueous solution with 1‐octanol solutions of tri‐n‐octylamine (TOA) were carried out using a stirred cell with a microporous hydrophobic membrane. The interfacial concentrations of species were correlated and thus the intrinsic kinetics was obtained. The overall extraction process was controlled by the chemical reaction at or near the interface between the aqueous and organic phases. The formation reaction of succinic acid‐TOA complex was found to be first order with respect to the concentration of succinic acid in the aqueous phase and the order of 0.5 with respect to that of TOA in the organic phase with a rate constant of (3.14 ± 0.6) × 10−8 m2.5·mol−0.5·s−1. The dissociation reaction of succinic acid‐TOA complex was found to be the second‐order with respect to that of succinic acid‐TOA complex in the organic phase and the order of –2 with respect to that of TOA in the organic phase with a rate constant of (1.44 ± 1.4) × 10−4 mol·m−2·s−1.

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Reactive Extraction as an Intensifying Approach for the Recovery of Organic Acids from Aqueous Solution: A Comprehensive Review on Experimental and Theoretical Studies

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Nanofiltration coupled with vapor permeation-assisted esterification as an effective purification step for fermentation-derived succinic acid

TL;DR: An integrated membrane process that consists of nanofiltration (NF) and vapor permeation (VP) was employed as a series of purification process for fermentation-derived succinic acid.
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Enhanced extraction of 3-demethylated colchicine from fermentation broth of Bacillus megaterium: Optimization of process parameters by statistical experimental design

TL;DR: In this article, a central composite design (CCD) model was employed with three extraction variables (temperature, pH, and process time) for optimization of 3-DMC.
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Selective extraction of maleic acid and phthalic acid by supercritical carbon dioxide saturated with trioctylamine

TL;DR: In this article, a continuous flow apparatus was used to extract maleic acid and phthalic acid from their mixture by supercritical carbon dioxide saturated with trioctylamine (scCO 2 -TOA).
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Equilibria, Kinetics, and Modeling of Extraction of Citric Acid from Aqueous Solutions with Alamine 336 in 1-Octanol

TL;DR: In this article, the mass transfer coefficients of citric acid, Alamine 336, and 1:1 acid-alamine complex in 1-octanol were calculated from acetic acid mass-transfer coefficient, which was determined by measuring its fluxes of simple diffusion from kerosene to water.
References
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Extraction chemistry of fermentation product carboxylic acids

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Extraction of carboxylic acids with amine extractants. 1. Equilibria and law of mass action modeling

TL;DR: In this paper, the results of the extraction of acetic, lactic, succinic, malonic, fumaric, and maleic acids by Alamine 336, an aliphatic, tertiary amine extractant, dissolved in various diluents, were interpreted by a chemical modeling approach, in which the stoichiometries of acid-amine complexes and corresponding equilibrium constants were determined.
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Chemical and Fuel Production by Anaerobic Bacteria

TL;DR: A chronology of key events and events in the history of the United States, as well as some of the key stories and anecdotes, are presented.
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Recovery of carboxylic acids produced by fermentation

TL;DR: In-situ removal of carboxylic acid by extraction during fermentation is the most popular approach, but recovery of the extractant can easily lead to waste inorganic salt formation, which counteracts the advantage of the in-Situ removal.
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Succinic acid production with reduced by-product formation in the fermentation of Anaerobiospirillum succiniciproducens using glycerol as a carbon source.

TL;DR: Succinic acid can be produced with much less by-product formation by using glycerol as a carbon source, which will facilitate its purification, according to the gram ratio of succinic acid to acetic acid.
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