G. Malmary et al., MEASUREMENT OF PARTITION-COEFFICIENTS OF CARBOXYLIC-ACIDS BETWEEN WATER AND TRIISOOCTYLAMINE DISSOLVED IN VARIOUS DILUENTS, Journal of chemical and engineering data, 43(5), 1998, pp. 849-851
Tertiary amines dissolved in organic diluents are attractive extractan
ts for the recovery of carboxylic acids from dilute aqueous solutions.
This paper reports experimental results for liquid-liquid equilibrium
in organic/aqueous two-phase systems containing a tertiary amine (tri
isooctylamine) and five carboxylic acids, aconitic, citric, lactic, ma
lic, and oxalic acid. Triisooctylamine (tris[6-methylheptyl]amine) was
dissolved in various diluents such as chloroform, a mixture (heptane
(50 vol %) + 1-hexanol (50 vol %)), and l-octanol. Partition coefficie
nts for individual acids were determined at a temperature of 25 degree
s C over a range of amine concentration in each diluent between 2.5 vo
l % and 60 vol %. Thus, for aconitic, citric, lactic, malic, and oxali
c acid the maximum values of partition coefficient were found to be 92
.7, 47.0, 28.2, 65.2, and 76.0, respectively. For dilute solutions con
taining less than 3 mass % of acid, it is energetically preferable to
remove the solute from the water through liquid-liquid extraction. Owi
ng to the significant partition coefficients obtained with amine dilue
nt systems, the process generates a small extract stream for subsequen
t regeneration processing. On the other hand, the recovery of solute b
y evaporation requires the energy intensive vaporization of water. Liq
uid-liquid extraction can be considered as an effective process for th
e recovery organic acids present in wastewater from industries such as
distilleries, canneries, and wineries.