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作 者:丁亚伟 张绍勇 杨丙连 DING Ya-wei;ZHANG Shao-yong;YANG Bing-lian(R&D Center of CAC Shanghai International Trading Co.,Ltd.,Shanghai 201612,China;Key Laboratory of Vector Biology and Pathogen Control of Zhejiang Province,College of Life Sciences,Huzhou University,Huzhou 313000,China)
机构地区:[1]上海泰禾化工有限公司,上海201612 [2]湖州师范学院,浙江省媒介生物学与病原控制重点实验室,浙江湖州313000
出 处:《精细化工中间体》2021年第5期27-30,共4页Fine Chemical Intermediates
摘 要:α-乙酰基-γ-丁内酯与氯气在无溶剂条件下发生氯化反应,得到α-氯-α-乙酰基-γ-丁内酯和副产氯化氢,α-氯-α-乙酰基-γ-丁内酯在少量水和氯化氢的存在下进行开环、氯代和脱羧反应得到3,5-二氯-2-戊酮。对氯气投料比、反应温度、氯化氢用量等因素进行优化。优化工艺条件为,第一步反应:氯化温度为0~5℃、n(氯气)∶n(α-乙酰基-γ-丁内酯)=1.07∶1.00;第二步反应:水解、脱羧及氯化温度为90℃、n(氯化氢)∶n(α-氯-α-乙酰基-γ-丁内酯)=0.7∶1.0,n(水)∶n(α-氯-α-乙酰基-γ-丁内酯)=0.8∶1.0,通入氯化氢4 h,此条件下,收率达95.2%。The reaction betweenα-acetyl-γ-butyrolactone and chlorine gas under solvent-free conditions givesα-chloro-α-acetyl-γ-butyrolactone and the by-product hydrogen chloride.Then,α-chloro-α-acetyl-γ-butyrolactone undergoes ring opening reaction and decarboxylation reactions in the presence of a small amount of water and hydrogen chloride to obtain 3,5-dichloro-2-pentanone.The reaction conditions including chlorine feed ratio,reaction temperature,hydrogen chloride dosage and other factors were optimized.The optimized process conditions were as followings:the chlorination temperature was in a range from 0℃to 5℃;the amount of chlorine gas was 1.07 times ofα-chloro-α-acetyl-γ-butyrolactone in molar mass;the temperature of hydrolysis,decarboxylation and chlorination was of 90℃;the amount of hydrogen chloride was 0.7 times ofα-chloro-α-acetyl-γ-butyrolactone in molar mass;the amount of water was 0.8 times ofα-chloro-α-acetyl-γ-butyrolactone in molar mass;and the yield was 95.2%.
关 键 词:α-乙酰基-γ-丁内酯 α-氯-α-乙酰基-γ-丁内酯 3 5-二氯-2-戊酮
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