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机构地区:[1]湘潭矿业学院化学工程系,湖南湘潭411201
出 处:《湘潭矿业学院学报》1999年第4期43-46,共4页Journal of Xiangtan Mining Institute
摘 要:对用麦迪霉素为原料直接合成醋酸麦迪霉素的工艺进行研究- 用DMAP作酰化反应催化剂时,可以避免分子内异构化和过度酰化等副反应- 考察了原料配比、反应温度、反应时间等因素对酰化产物收率的影响- 用正交试验发现选择工艺条件为:麦迪霉素与乙酰氯的摩尔比1∶3 .3,反应温度60 ℃,反应时间10 h 时,酰化反应收率为97 .5 % ,经醇解后,反应总收率为84% - 具有良好的工业化前景- 表3,参5-A technological process of direct synthesizing midecamycin acetate from midecamycin and acetyl chloride was studied.The intramoleacular isomerization and excessive acetylation were avoided by using 4 dimethyl amino pyridine as acetyl catalyst.The optimum technological condition was obtained with orthogonal design,and it is as follows:molar ratio of midecamycin to acetyl chloride is 1.0:3.3,reation temperature is 60 ℃,reation time is 10h.Under the optimum condition,the yield of midecamycin acetate is 84%.3tabs.5refs. A technological process of direct synthesizing midecamycin acetate from midecamycin and acetyl chloride was studied.The intramoleacular isomerization and excessive acetylation were avoided by using 4 dimethyl amino pyridine as acetyl catalyst.The optimum technological condition was obtained with orthogonal design,and it is as follows:molar ratio of midecamycin to acetyl chloride is 1.0:3.3,reation temperature is 60 ℃,reation time is 10h.Under the optimum condition,the yield of midecamycin acetate is 84%.3tabs.5refs.
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