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97 results about "Dibutyltin oxide" patented technology

Dibutyltin oxide, or dibutyloxotin, is an organotin compound with the chemical formula (C₄H₉)₂SnO. It is a colorless solid that, when pure, is insoluble in organic solvents. It is used as a reagent and a catalyst.

Method of recycling and reusing of dibutyltin oxide in process of cane sugars manufacturing cane suger-6-ethyl ester

The invention relates to a method of recycling and reusing of dibutyltin oxide in the process of cane sugars manufacturing cane suger-6-ethyl ester. The method of recycling and reusing of the dibutyltin oxide in the process of the cane sugars manufacturing the cane suger-6-ethyl ester comprises the following steps: (1), carrying out the cane sugars manufacturing the cane suger-6-ethyl ester; (2), recycling cyclochexane liquor which contains the dibutyltin oxide; (3), using the recycled and obtained dibutyltin oxide with a moisture percentage of 10%-20% for the step (1) of manufacturing the cane suger-6-ethyl ester. The method of recycling and reusing of the dibutyltin oxide in the process of the cane sugars manufacturing the cane suger-6-ethyl ester is concise, operation is easy, and the obtained dibutyltin oxide which contains water can be directly used for manufacturing the cane suger-6-ethyl ester again. A step of drying the dibutyltin oxide can be saved. Under conditions of not affecting yields generally, production cost is reduced. Safe hidden dangers which exist in the process of drying and dewatering the dibutyltin oxide are completely prevented. The method of recycling and reusing of the dibutyltin oxide in process of the cane sugars manufacturing the cane suger-6-ethyl ester can be suitable for industrial production.
Owner:LIYANG WEIXIN CHEM

Method for recycling organic tin in sucralose production

The invention relates to a method for recycling organic tin in sucralose production. The method includes sucralose esterification reaction, dibutyltin oxide serves as a catalyst to take participate in the reaction to generate a sucrose-6-ester midbody, after a midbody solution is extracted through cyclohexane, organic tin acetic ester is dissolved in an extractant cyclohexane phase, a cyclohexane phase is extracted out, and cyclohexane is obtained through evaporation by means of a distillation still. The method is characterized by including the following steps that a, boiled cooling water is cooled to 50 DEG C, then pure water is added for stirring and washing, and stirring is carried out for one hour; b, bottom water is separated out, residues in the still are recycled organic tin acetic ester, and the residues are returned to an esterification reactor to take participate in the esterification reaction and be used repeatedly. The method has the advantages that the organic tin acetic ester is not degreased or dried and can be directly recycled and used repeatedly, so that zero emission is achieved, production cost is reduced, waste water generated in the organic tin recycling process is eliminated to the largest extent, production efficiency is greatly improved, and economic benefits are remarkable.
Owner:ANHUI JINGHE IND

Method for continuously preparing and supplementing organic tin catalyst in sucralose production

The invention relates to a method for continuously preparing and supplementing an organic tin catalyst in sucralose production. The method comprises the following steps of pumping a cyclohexane phasecontaining organic tin acetate recovered after acylation in the previous batch into a distillation kettle, and supplementing 1-5% of dibutyltin oxide according to the amount of the organic tin acetateadded before esterification, and heating to a certain temperature, keeping the temperature, performing reacting, distilling under reduced pressure to remove the solvent after the reaction, and reusing the prepared organic tin acetate in the sucralose production process. According to the method, the acylation reaction of the dibutyltin oxide is carried out by fully utilizing the acetic anhydride remained in the cyclohexane extraction phase recovered in the previous batch in the production, so that the production device and the production cost of the sucralose catalyst are saved, the process issimplified, the production efficiency is greatly improved, the working intensity of operators is reduced, the pollution is reduced, and the environment is protected. The utilization rate of residualraw material is increased by using a novel process, so that the reaction efficiency and the material utilization rate are optimized in the whole production process, and the economic benefit of an enterprise is obviously increased.
Owner:ANHUI JINGHE IND
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