Residue Reviews 1969
DOI: 10.1007/978-3-662-40395-2_8
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Chemical and thermal methods for disposal of pesticides

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Cited by 16 publications
(14 citation statements)
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“…KENNEDY et al (1969 and were able to degrade 15 of 19 examined pesticides using a liquid ammonia-metalic sodium solution, while treatment with sodium biphenyl, hydrogen peroxide, or metalic lithium-liquid ammonia was not as successful. LEIGH (1969) examined the degradation of lindane, heptachlor, DDT, and endrin at water-soluble concentrations by chlorine, potassium permanganate, and potassium persulfate and reported that except for heptachlor degradation by potassium permanganate, only minor chemical degradation occurred after 48 hr of treatment with 50 ppm of reactants.…”
Section: B) Oxidation and Reductionmentioning
confidence: 84%
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“…KENNEDY et al (1969 and were able to degrade 15 of 19 examined pesticides using a liquid ammonia-metalic sodium solution, while treatment with sodium biphenyl, hydrogen peroxide, or metalic lithium-liquid ammonia was not as successful. LEIGH (1969) examined the degradation of lindane, heptachlor, DDT, and endrin at water-soluble concentrations by chlorine, potassium permanganate, and potassium persulfate and reported that except for heptachlor degradation by potassium permanganate, only minor chemical degradation occurred after 48 hr of treatment with 50 ppm of reactants.…”
Section: B) Oxidation and Reductionmentioning
confidence: 84%
“…Although the uses of ozone or ultraviolet light are individually not extremely successful in oxidizing organic compounds in wastewaters, MAUK and PRENGLE (1976) reported that combined ozone and ultraviolet light treatment greatly improved the chemical oxidation of refractory organic compounds in wastewaters. Although the agents examined by KENNEDY et al (1969 and were generally able to effect a chemical change in the parent pesticide molecule, the chemical by-products and the added reactants must still be considered hazardous, the reactions themselves are dangerous, and thus these chemical treatment systems cannot be recommended as disposal procedures for use by the layman ( LAWLESS et al 1975, SHIH andDEL PORTO 1975) and would increase the chemical wastewater load if applied to industrial situations without producing compensating benefits. MELNIKOV et al (1958), however, recommended the use of 45 kg of bleaching power or its chlorine equivalent, along with 40 kg of sodium hydroxide for the detoxification of one cu m of industrial wastewater derived from the production of parathion.…”
Section: B) Oxidation and Reductionmentioning
confidence: 97%
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