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 c...

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description 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.
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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. 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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.</abstract><oa>free_for_read</oa></addata></record>
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subjects CHEMISTRY
CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS
DERIVATIVES THEREOF
GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS
METALLURGY
NUCLEIC ACIDS
NUCLEOSIDES
NUCLEOTIDES
ORGANIC CHEMISTRY
SUGARS
TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE
title Method for recycling organic tin in sucralose production
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