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Formic acid is the simplest yet commercially valuable organic acid. It is widely used as a stabilizer and sterile agent in food industries. Reactive extraction is highly effective and selective technique for the recovery of formic acid from dilute solutions. Kinetics study provide rate controlling step (reaction rate or diffusion) that is required to visualize the intrinsic reactive extraction mechanism. Kinetics study of formic acid (0.1–0.4 kmol/m 3 ) extraction with tri- n- octyl amine (TOA) (0.11–0.67 kmol/m 3 ) in  n -butyl acetate (NBA) was investigated at temperature 308 ± 1 K. Kinetics study was carried out in a Lewis cell. Effect of formic acid concentration, TOA concentration, speed of stirring, and phase volume ratio were investigated to find the reaction regime. Diffusivity coefficient (D A ) of formic acid in NBA was found 3.20 × 10 −7  m 2 /s. Reaction rate constant was evaluated to be 0.616 m 3 /mol s. The physical mass transfer coefficient (k L ) was evaluated to be 0.8278 × 10 −6  ×  N   3.387 . The reaction was independent on hydrodynamic parameters and falls under fast reaction regime. The reaction was found first order with respect to both formic acid as well as TOA, occurring in the diffusion film. The findings of the present work are helpful in the selection of commercially viable extraction system and in the design of extractors.

Kinetics study on reactive extraction of formic acid using tri- n -octyl amine diluted in n -butyl acetate