Malonic
acid is an essential carboxylic acid that is used as a
backbone reactant in deriving multiple higher-order carboxylic compounds.
The successful attempt of producing malonic acid from a biological
route has attracted the scientific community to extract malonic acid
from a fermentation broth or dilute aqueous stream. Experimental study
on the recovery of malonic acid by reactive extraction was performed,
and the effects of TBP concentration, diluents (alkane, ketone, and
alcohol), and malonic acid concentration were investigated. The equilibrium
models (relative basicity and mass action law models) and the number
of theoretical units (NTU) were also evaluated. Fourier transform
infrared spectroscopy provided evidence for the formation of significant
bonds among extractant–diluent–acid complexation systems
which support the experimental outcomes. The results of extraction
equilibrium are discussed regarding dimerization constant (D
MA), partition coefficient (P
MA), extraction efficiency (E
MA%), distribution coefficient (K
D(MA)), overall extraction complexation equilibrium (K
E(MA)), and loading factor
(Z
MA). The highest reactive extraction
efficiency was 73.5% with 0.5962 mol·kg–1 TBP
used in MIBK. The distribution coefficient (K
D(MA)) of malonic acid in various diluents
exhibited the trend MIBK > octanol > heptane. The comparison
between
values predicted by the equilibrium model and experimental outcomes
shows that the relative basicity models predicted better results than
the mass action law for reactive extraction of malonic acid. The NTU
was calculated to be 2, which was estimated by the modified Kremser
equation for designing a countercurrent reactive extraction column.