CN109516967A - 一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法 - Google Patents

一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法 Download PDF

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CN109516967A
CN109516967A CN201811410249.4A CN201811410249A CN109516967A CN 109516967 A CN109516967 A CN 109516967A CN 201811410249 A CN201811410249 A CN 201811410249A CN 109516967 A CN109516967 A CN 109516967A
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tetraethyl ammonium
ammonium fluoride
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李虎
余钊卓
杨松
徐复生
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Guizhou University
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Abstract

本发明公开了一种温和、简便的芳香醇的制备方法。包括:将反应物溶液、硅氢和催化剂四乙基氟化铵混合置于封闭的反应容器中于25‑60℃下反应0.5‑2 h后即可得到芳香醇。硅氢用量相对于芳香醛的用量为2~4倍当量,芳香醛在有机溶剂中的浓度为2~4 wt%,催化剂四乙基氟化胺相对于芳香醛的含量为5~10 mol%。本方法能有效克服传统催化体系危险性高、污染环境、工艺复杂和副产物含量高的不足。

Description

一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的 方法
技术领域
本发明涉及由四乙基氟化胺为催化剂催化芳香醛还原为芳香醇的方法,具体地说就是用四乙基氟化铵为催化剂在硅氢作为氢供体的条件下催化以芳香醛转化为芳香醇。
背景技术
芳香醇作为一种带有芳香味的化合物被广泛的应用于植物精油香水、精油等香味物质的制备当中。其次,芳香醇还作为一种药物中间体在医药合成方面也起着很大的作用。其中以糠醇为代表的芳香醇还可以用于生产糠醛树脂、呋喃树脂和酚醛树脂等。
传统的芳香醇化合物制备方法采用的是以相应的芳香醛为原料,催化体系多基于以Pd、Cu、Ni、Pt和Mg等金属的氧化物或与其他酸性有机配体结合而成的金属有机框架材料,并以氢气、醇和甲酸为氢供体[3-7]。虽然上述体系能够得到较高的芳香醇产率,但是该反应体系中,由于贵金属和金属有机框架的使用会有成本增高、制备工艺复杂的缺陷。除此之外,将醇、酸和氢气作为氢供体会有以下两个缺点:一是由于氢气的使用以及所使用的高温高压的反应条件增加了反应过程中的危险性减缓了该反应体系工业化的进程。二是将醇和酸作为氢供体的同时也会使得体系中的副产物的含量急剧上升。这也使得后面的产物分离提纯的工作难度又提升了一个台阶。
因此,如何降低反应温度,提高体系的安全性,减少副产物的含量成为该体系工业化进程上亟需解决的问题。
发明内容
本发明的目的在于提供一种有效的芳香醇化合物的制备方法,该方法反应条件温和,反应速率快,选择性高并且十分安全,以克服已有技术反应条件苛刻、选择性差、危险和成本高等缺陷。
为实现上述目的,本发明采用的技术方案为:一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,包括以下步骤:
步骤一:将芳香醛加入有机溶剂中,配置成反应物溶液。
步骤二:将反应物溶液、硅氢和催化剂四乙基氟化铵混合置于封闭的反应容器中于25-60 ℃下反应0.5-2 h后即可得到芳香醇。
所述的芳香醛包含糠醛、对茴香醛、吡啶甲醛和5-溴-2呋喃甲醛。
所述的有机溶剂为N,N-二甲基甲酰胺、乙腈或乙酸乙酯。
所述的有机溶剂优选N,N-二甲基甲酰胺。
所述的硅氢为三乙氧基硅烷、三乙基硅烷、四甲基二硅氧烷、七甲基三硅氧烷、苯基硅烷、二苯基硅烷或聚甲基氢硅氧烷。
所述的硅氢优选聚甲基硅氧烷。
所述的硅氢用量相对于芳香醛的用量为2~4倍当量。
所述的芳香醛在有机溶剂中的浓度为2~4 wt%。
所述的催化剂四乙基氟化胺相对于芳香醛类的含量为5~10 mol%。
和现有技术相比,本发明的益处在于:
(1)本发明以聚甲基氢硅氧烷为氢源,从而避免使用危险性高的H2作为氢源,大大地增加了醛还原反应体系的安全性,并且使得该体系的加氢效果更好,收益更高。
(2)本发明中的整个加氢体系高效绿色、条件温和、产物选择性高并且工艺操作简单安全。
具体实施方式
实施例1
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10 mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应0.5 h得到糠醇,转换率94.9%,产率92.3%。
实施例2
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10 mg四乙基氟化铵和68 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应0.5 h得到糠醇,转换率63.0%,产率61.7%。
实施例3
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10 mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,25 ℃下反应0.5 h得到糠醇,转换率85.4%,产率81.9%。
实施例4
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10 mg四乙基氟化铵和102 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,25 ℃下反应0.5 h得到糠醇,转换率71.1%,产率65.8%。
实施例5
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10 mg四乙基氟化铵和68 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,25 ℃下反应0.5 h得到糠醇,转换率52.5%,产率47.8%。
实施例6
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入5 mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应0.5 h得到糠醇,转换率89.5%,产率86.3%。
实施例7
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入5 mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,30 ℃下反应0.5 h得到糠醇,转换率89.5%,产率86.3%。
实施例8
将48 mg糠醛加入到2 mL 乙腈中,再加入5 mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,30 ℃下反应0.5 h得到糠醇,转换率63.8%,产率55.8%。
实施例9
将48 mg糠醛加入到2 mL 乙酸乙酯中,再加入5 mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,30 ℃下反应0.5 h得到糠醇,转换率62.6%,产率49.7%。
实施例10
将48 mg糠醛加入到2 mL 正丁醇中,再加入5 mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,30 ℃下反应0.5 h得到糠醇,转换率39.6%,产率48.7%。
实施例11
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应1 h得到糠醇,转换率99.0%,产率92.1%。
实施例12
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应1.5 h得到糠醇,转换率94.9%,产率92.3%。
实施例13
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和328 mg三乙氧基硅烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应0.5 h得到糠醇,转换率99.3%,产率48.6%。
实施例14
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和232 mg三乙基硅烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应0.5 h得到糠醇,转换率77.1%,产率74.1%。
实施例15
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和134 mg四甲基二硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应0.5 h得到糠醇,转换率99..2%,产率89.4%。
实施例16
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和134 mg七甲基三硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应0.5 h得到糠醇,转换率99.1%,产率89.4%。
实施例17
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和72 mg苯基硅烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应0.5 h得到糠醇,转换率99.4%,产率99.2%。
实施例18
将48 mg糠醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和184 mg二苯基硅烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,35 ℃下反应0.5 h得到糠醇,转换率99.0 %,产率91.4%。
实施例19
将53 mg苯甲醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,60 ℃下反应1 h得到苯甲醇,转换率99.5%,产率99.0%。
实施例20
将68 mg对茴香醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和136mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,60 ℃下反应1 h得到对茴香醇,转换率99.5%,产率99.0%。
实施例21
将68 mg吡啶甲醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和136mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,60 ℃下反应1 h得到吡啶甲醇,转换率99.9%,产率99.9%。
实施例22
将68 mg 5-溴-2呋喃甲醛加入到2 mL N,N-二甲基甲酰胺中,再加入10mg四乙基氟化铵和136 mg聚甲基氢硅氧烷混合至于封闭的50 mL聚氯乙烯塑料反应管中,60 ℃下反应1h得到5-溴-2呋喃甲醇,转换率99.8%,产率99.0%。

Claims (9)

1.一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,其特征在于:包括以下步骤
步骤一:将芳香醛加入有机溶剂中,配置成反应物溶液;
步骤二:将反应物溶液、硅氢和催化剂四乙基氟化铵混合置于封闭的反应容器中于25-60 ℃下反应0.5-2 h后即可得到芳香醇。
2.根据权利要求1所述的一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,其特征在于:所述的芳香醛包含糠醛、对茴香醛、吡啶甲醛和5-溴-2呋喃甲醛。
3.根据权利要求1所述的一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,其特征在于:所述的有机溶剂为N,N-二甲基甲酰胺、乙腈或乙酸乙酯。
4.根据权利要求3所述的一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,其特征在于:所述的有机溶剂优选N,N-二甲基甲酰胺。
5.根据权利要求1所述的一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,其特征在于:所述的硅氢为三乙氧基硅烷、三乙基硅烷、四甲基二硅氧烷、七甲基三硅氧烷、苯基硅烷、二苯基硅烷或聚甲基氢硅氧烷。
6.根据权利要求5所述的一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,其特征在于:所述的硅氢优选聚甲基硅氧烷。
7.根据权利要求1所述的一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,其特征在于:所述的硅氢用量相对于芳香醛的用量为2~4倍当量。
8.根据权利要求1所述的一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,其特征在于:所述的芳香醛在有机溶剂中的浓度为2~4 wt%。
9.根据权利要求1所述的一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法,其特征在于:所述的催化剂四乙基氟化胺相对于芳香醛类的含量为5~10 mol%。
CN201811410249.4A 2018-11-23 2018-11-23 一种低温下四乙基氟化铵选择性催化芳香醛还原为芳香醇的方法 Pending CN109516967A (zh)

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