Technique for producing compound of macrolide
A production process, macrolide technology, applied in the field of production of macrolide musk compounds, can solve the problems of rising production costs, environmental pollution, waste of raw materials, etc., to reduce the consumption of raw materials, reduce production costs, and reduce waste discharge Effect
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Embodiment 1
[0037] 45kg fresh ethylene glycol, 80kgC 11 ~C 15 Add the mixed dicarboxylic acid and 2.0kg palmitic acid into the esterification polycondensation reactor, heat the material under the protection of nitrogen, start stirring at 100 ° C, and heat the material to 180 ~ 200 ° C within 4 ~ 6 hours, when the temperature rises When the temperature reaches 150°C, water begins to evaporate. When no water evaporates, the system pressure is slowly reduced to 3mmHg, and the excess ethylene glycol is distilled under reduced pressure. The distilled ethylene glycol is condensed and cooled to 80-90°C before entering Filtration—recycling in the adsorption container. There is a filter bag on the upper part of the container. The adsorption column is filled with granular activated carbon with a particle size of 2-3mm and a pH of 6.3. The bed size is 300×1200mm, and the operating temperature is 80-90°C. The operating pressure is 3mmHg, and the residence time is controlled to 25-30min. The materia...
Embodiment 2
[0040] 20.5kg of reclaimed ethylene glycol, 80kg of tridecanedioic acid and 3.2kg of palmitic acid obtained in 25kg of fresh ethylene glycol and the regeneration treatment in the embodiment are added in the polycondensation reactor, and the method for esterification and polycondensation is carried out according to the method of embodiment 1 Reaction, steaming out excess ethylene glycol, the distilled ethylene glycol is condensed and cooled to 80-90°C and collected in a filter-adsorption container, and the prepared polyester is subjected to depolymerization and cyclization, depolymerization and cyclization and subsequent refining and purification operating conditions With embodiment 1. While the depolymerization and cyclization was carried out, the recovery treatment system used in Example 1 was used to process the gained ethylene glycol solution. The pressure of the processing operation was normal pressure, and finally 21.6 kg of the ethylene glycol solution was obtained. The s...
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