• Asian Journal of Turfgrass Science
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• v.20 no.1
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• pp.47-55
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• 2006

Golf course community has always been concerned about water quality regarding to pesticide and fertilizer managements. This study conducted to investigate sorption and leaching behavior of common pesticides used for golf course in granular activated carbon I (GAC 1), granular activated carbon II(GAC II), and charcoal. We used batch study to investigate the influence of concentrations of Smithion and Folicur and particle sizes of GAC I, GAC II, and charcoal on sorption. Also, column study was used to investigate the leaching effect of Smithion in GAC I and charcoal. We found that sorption of Smithion and Folicur were higher in less $45{\mu}m$ of particle size for GAC I, GAC II, and charcoal compared to $1.7{\sim}2.0mm$ size, and the sorption of Smithion and Folicur in less $45{\mu}m$ of particle size ranged from 90 to 99%. In the column study, there was no difference in leaching effect between GAC I and charcoal. Overall, we found that charcoal might offer a cost effective adsorbent as a pesticides in leachate.

• Journal of Environmental Health Sciences
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• v.5 no.1
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• pp.58-60
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• 1978

This experiment was carried out to determine the amount of organophosphorous pesticides accumulated in farmer's blood during the farming season. The Blood had been collected for about 5ml from farmer's, and extraction was purified on a Avicel/Darco G-Co (1:10) column and determined by Gas Chromatography using AFID supported on 2% EGA. The Gas chromatographic detection yielded recoveries from the blood of 88% for smithion 94% for malathion. The amount of average contamination shows 0.045ppm for smithion. 0.054ppm for malathion.

• Journal of Korean Society of Environmental Engineers
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• v.33 no.3
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• pp.157-161
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• 2011

This study investigated decomposition the pathway and characteristics of fenitrothion, which is applied on the golf course for pesticide, by ZVI in batch reactor. The removal efficiencies of the pure fenitrothion and the commercial fenitrothion in Smithion by ZVI were compared. The fenitrothion was converted to 3-Methyl-4-nitrophenol and 4-Amino-m-cresol by ZVI. The fenitrothion decomposition rate by ZVI could be expressed by the first order reaction. As increasing the ZVI dosages, the first order rate constants and removal efficiencies increased. The surface area normalized rate constants for the pure fenitrothion and the commercial fenitrothion were 0.0398 and 0.1312 ($L/m^2{\cdot}hr$), respectively. The decomposition of the commercial fenitrothion in Smithion was faster than that of the pure fenitrothion by ZVI, the surfactant in Smithion lead to enhances solubility of fenitrothion and disperse ZVI.