2524-04-1Relevant articles and documents
Distribution and elimination of 14C-ethion insecticide in chamomile flowers and oil
Abdel-Gawad,Abdelhameed,Elmesalamy,Hegazi
, p. 2122 - 2134 (2011)
The residual fate of 14C-ethion labeled at the ethyl group in chamomile flowers and oil was studied. 14C-ethion and some of its degradation products have been prepared for the present investigation. 14C-residues in its flowers and oil were determined at different time intervals. Chromatographic analysis of chamomile oil extracts revealed the presence of the parent compound together with four metabolites, which were identified as ethion monooxon, ethion dioxon, O,O-diethyl phosphorothioate, and O-ethyl phosphorothioate. Effect of drying on ethion residues in chamomile flowers was investigated. Ethion residues were decreased by sun drying of chamomile flowers. The percentage of removal was 18%-47%. Effect of using low cost adsorbents for removal of ethion residues from chamomile oil was investigated. The removal percentage due to adsorption was 100% for CaO and saw dust adsorbers and for watermelon peels, bagass, and rice bran adsorbers were 36%, 41%, and 90%, respectively. Our results proved that the addition of CaO saw dust and rice bran reduced the pesticide residues, so we recommend the addition of these adsorbents during the extraction process to reduce the risk of pesticide residues on chamomile oil. Copyright Taylor & Francis Group, LLC.
EFFECTS OF SUBSTITUENTS IN REACTIONS OF SULFENYL CHLORIDES WITH DERIVATIVES OF PHOSPHONALLENIC ACIDS
Khusainova, N. G.,Berdnikov, E. A.,Naumova, L. V.,Pudovik, A. N.
, p. 1677 - 1683 (1983)
-
Green synthesis technology of O,O-diethyl thiophosphoryl chloride
-
Paragraph 0029; 0032-0036; 0039-0043; 0046-0050; 0053-0056, (2019/03/06)
The invention provides a green synthesis technology of O,O-diethyl thiophosphoryl chloride and relates to the field of chemical synthesis. The green synthesis technology comprises the following steps:taking O,O-diethyl dithiophosphate to react with chlorine gas at low temperature, so as to obtain a crude product of the O,O-diethyl thiophosphoryl chloride; then transferring the crude product to react at high temperature; enabling the residual O,O-diethyl dithiophosphate to further completely react with the chlorine gas. Meanwhile, in a high-temperature reaction process, a polymeric compound isprevented from being generated when a compound catalyst is used and sulfur monochloride impurities are completely removed through reaction, so that a byproduct sulfur has a crystalline state and a product more easily separated and purified. Moreover, HCl and sulfur-containing odorous gas are pumped away through applying negative pressure and the tail gas is absorbed to prevent air pollution. In awhole reaction process, technological water does not need to be added, so that wastewater is not generated and the treatment cost of sulfur-containing and phosphorus-containing wastewater is reduced.The technology has the advantages of simplicity in operation, easiness for obtaining raw materials, moderate reaction conditions, small pollution and environment friendliness.
Production method for O,O-dialkyl thiophosphoryl chloride
-
Paragraph 0023; 0024; 0026, (2017/08/27)
The invention relates to a production method for O,O-dialkyl thiophosphoryl chloride, and belongs to the field of manufacturing of O,O-dialkyl thiophosphoryl chloride through a chemical method. Raw materials comprise dialkyl phosphite, sulfur or sulfide, chlorine or a chlorinating agent and the like. The production method comprises the steps: carrying out a reaction of dialkyl phosphite and sulfur or sulfide in a synthesis kettle for 2 hours, then chloridizing by chlorine or the chlorinating agent to obtain an O,O-dialkyl thiophosphoryl chloride crude product, and then washing with water to obtain the product O,O-dialkyl thiophosphoryl chloride. The total yield can reach 98%-99%, the content of O,O-dialkyl thiophosphoryl chloride can reach more than or equal to 99.5%, the product quality is good, and the purity of the product can reach 99-99.9%; and the production method has the advantages of simple production process, safe production, low energy consumption, and no pollution. The problems in the prior art that a large amount of alcohol is needed to be recycled, consumption of steam is high and energy consumption is high are solved; and the problems that all the process routes need freezing, a large amount of freezing energy and circulating water is needed and the electric energy consumption is high are solved.