Abstract
Alkaline hydrolysis of fenitrothion (F), at 26°C, over the pH range 9.5–14, was described by ‐d ln[F]/dt = 0.17 [‐OH] + 6.4 x 104 [HO1 ‐]. The peroxide concentration equalled [total peroxide] [‐OH], provided that the hydroxide concentration was taken as 0.0044 M for all pH values in excess of 11.8. Energies of activation, measured over the range ll‐30°C, were 16.3 kcal mole‐1, for alkaline hydrolysis, and 7.8 kcal mole‐1, for peroxide‐catalyzed hydrolysis.
Appropriate regimes for decontamination of fenitrothion wastes can be calculated from the above data. Two regimes that are relatively safe and inexpensive are decontamination in a saturated aqueous solution of calcium hydroxide and decontamination in a solution of “1% w/v”; sodium carbonate plus 1–2 x 10‐4 M total peroxide. The latter method is especially appropriate for cold temperatures, because of the low energy of activation of peroxide‐catalyzed hydrolysis.