Synergistic extraction equilibrium of p-aminobenzoic acid by the mixture extractant of di-2-ethylhexyl phosphoric acid (D2EHPA) and tri-n-butylphosphate (TBP) in heptane was investigated at various initial pH values and D2EHPA
TBP concentrations
and a mathematical model was proposed to describe the extraction equilibrium.The results showed that the extraction of p-aminobenzoic acid with the mixed solvent presented synergistic effect by TBP bonded to —NH2 on p-aminobenzoic acid and D2EHPA associated with —COOH on p-aminobenzoic acid
and the synergistic effect was more obvious when D2EHPA concentration was close to TBP concentration.The apparent extraction equilibrium constants were obtained by fitting the experimental data to the models proposed in this paper
and the apparent extraction equilibrium constants for the mixture solvent of D2EHPA and TBP were much higher than those for D2EHPA and TBP solvent alone.
Multi objective optimization of flow and heat transfer characteristics of modified manifold microchannel heat sink based on machine learning
Controlled synthesis of Bi2MoO6/MoO3 composite fibers via in-situ hydrothermal method and their high-efficiency photocatalytic hydrogen production performance
Identification of gas-liquid two-phase flow patterns in a riser based on recursive characteristics and CNN
Study on microwave enhanced removal performance of organic matter in coking waste salt
Heat transfer mechanisms, bottleneck identification and optimization in heat exchanger networks under variable operating conditions