CN111470954A - 一种原羧酸酯的合成方法 - Google Patents

一种原羧酸酯的合成方法 Download PDF

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CN111470954A
CN111470954A CN202010282325.9A CN202010282325A CN111470954A CN 111470954 A CN111470954 A CN 111470954A CN 202010282325 A CN202010282325 A CN 202010282325A CN 111470954 A CN111470954 A CN 111470954A
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谭昊明
付其璋
陈和粲
刘雨阳
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Shanghai Taichu Chemical Technology Co ltd
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    • C07C41/00Preparation of ethers; Preparation of compounds having groups, groups or groups
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Abstract

一种原羧酸酯的合成方法,其特征在于用羧酸酯与醚在催化剂催化下在一定的温度下,一定的压力下反应一定的时间制备:

Description

一种原羧酸酯的合成方法
技术领域
本发明属于精细化学品绿色合成领域,具体地涉及到一种原羧酸酯的合成方法。
背景技术
原羧酸酯在精细化学品的合成中有着广泛的应用,其中比较有代表性的产品为原甲酸三甲酯、原甲酸三乙酯、原甲酸三异丙酯等等。
传统的原羧酸酯的合成是通过如下几条反应路线制备:
1、腈类与醇类在通入氯化氢气体条件下反应是目前世界上常用的原羧酸酯的生产方法,比较有代表性的产品为原甲酸三甲酯、原甲酸三乙酯。该方法是通过腈与甲醇(或者乙醇)、氯化氢反应,生成氢卤酸亚胺盐,然后醇解、纯化得到原羧酸酯产品;其中的纯化步骤是对醇解反应液进行纯化,具体是分别进行一级蒸馏、纯化处理及二级蒸馏,其中一级蒸馏主要包括初馏、一级精馏、溶剂回收步骤。但是,这种方法得到的产品液中,含有三氮杂苯(三嗪)等含氮杂质是不可避免的。极少量该杂质的存在,会严重干扰和限制了原羧酸酯的应用,比如,以原甲酸三甲酯为原料生产嘧菌酯时,即使原料中含有0.1%的三嗪,也将大大降低嘧菌酯收率。
Figure BDA0002447167730000011
2、同原子的三氯烷烃与醇钠反应缩合制备。如原甲酸三甲酯的合成,用氯仿与甲醇钠缩合制备。这种反应首先制备醇钠,而醇钠的制备往往是通过钠与甲醇反应制备。在制备甲醇钠的过程中,会产生大量的氢气,对于生产安全产生巨大威胁。
Figure BDA0002447167730000012
2、酯交换法
如用原甲酸三甲酯与乙醇反应制备原甲酸三乙酯,或者原甲酸三甲酯与异丙醇制备原甲酸三异丙酯。
Figure BDA0002447167730000013
3、酰氯法
如原甲酸三乙酯的制备,用苯甲酰氯与甲酰胺和乙醇制备原甲酸三乙酯。
Figure BDA0002447167730000021
4、二烷氧基醇钠法
这种方法通过羧酸酯与醇钠反应后与卤代烷缩合制备。
Figure BDA0002447167730000022
发明内容
为了满足绿色生产的需要,为了更好地减少化工生产对于自然界产生的污染和危害,本发明提供了一种原羧酸酯的合成方法。其优点为,用羧酸酯与醚在催化剂催化下一步合成出原羧酸酯。
其反应式如下,
Figure BDA0002447167730000023
其反应过程如下:用催化剂催化羧酸酯与醚在一定的反应温度、一定的反应压力下反应一定的时间直接制得原羧酸酯。
在反应式中:
R选自C1-C6烷基,C2-C6炔基,C3-C8环烷基,每个可用以下基团任意选择取代:(卤素,CN,NO2,C1-C6烷硫基,C1-C6烷基亚磺酰基,C1-C6烷基磺酰基;C3-C6三烷基甲硅烷基,或苯基,苯氧基或5元或6元杂芳环,每个环可用以下的基团任意选择取代:(C1-C6烷基,,C2-C6炔基,C3-C8环烷基,C1-C6卤烷基,C2-C6卤炔基;C3-C8卤环烷基,卤素,CN,NO2,C1-C6烷硫基,C1-C6烷基亚磺酰基,C1-C6烷基磺酰基,C2-C6烷基羰基));或为苯基,苄基,五元或六元杂环,每个可用以下基团任意选择取代:(C1-C6烷基,C2-C6炔基,C3-C8环烷基,C1-C6卤烷基,C2-C6卤炔基,C3-C8卤环烷基,卤素,CN,NO2,C1-C6烷硫基,C1-C6烷基亚磺酰基,C1-C6烷基磺酰基,C2-C6烷基羰基,或C1-C6三烷基甲硅烷基)。
R1、R2和R3分别独立地选自:C1-C6烷基,C2-C6烯基,C2-C6炔基,C3-C8环烷基。
在上述的反应中,所述的催化剂为酸性催化剂,选自:1)路易斯酸,包括BF3、BCl3、AlBr3、CbCl3、TiCl4、ZrCl4、FeCl3、FeBr3、SbCl5、SbF5、AsF5、MbCl3、BeCl3、UCl4、WCl4、ZnCl2、CuCl2、HgCl2、SnCl4、TeCl4、AuF5、TaF5、NbF5;2)质子酸,包括氯化氢、氟化氢、发烟硫酸、硫酸、磷酸、过磷酸、三氟乙酸、高氯酸;3)液体超强酸,包括HSO3Cl、HSO3F、HSO3CF3;4)无机固体超强酸,包括TiO2·H2SO4、SbF5-SiO2-Al2O3、SbF5-TiO2-SiO2、SO4 -/Fe2O3、SO4 -/TiO2、SO4 -/ZnO2、SO4 -/SnO2、SO4 -/Al2O3、SO4 -/Al2O3-ZnO2、SO4 -/TiO2-ZnO2、SO4 -/WO3-ZnO2;5)有机高分子超强酸,包括DSFB(制备方法见《离子交换与吸附》1995,11(4),363-367)6)无机杂多酸,包括H3PW12O40、H4SiW12O40-H4GeW12O40、H5BW12O40、H6P2W18O62、H6CoW12O40;其中的任意一种或者两种以上。
在上述反应中,所述的羧酸酯和醚的比例在1:100-100:1(摩尔比);优选范围在1:1-1:10;
在上述反应中,可以选用非质子有机溶剂作为溶剂,选自1)芳香烃如苯、甲苯、氯苯、二甲苯,2)烷烃或者环烷烃如环己烷、正庚烷、正辛烷;3)氯代烃如二氯甲烷、二氯乙烷、氯仿、四氯化碳中的一种或两种以上。
在上述反应中,所述的溶剂可以用反应物本身。
在上述反应中,所述的反应时间从0.1小时-144小时。
在上述反应中,所述的反应压力在0.01Mpa-100Mpa之间。
在上述反应中,所述的反应温度在0-200℃之间。
具体实施方式:
下面结合实施例来说明本发明的内容,但是本发明保护范围绝对不仅仅局限在实施例的范围。
实施例1、原苯甲酸三乙酯制备
Figure BDA0002447167730000031
在50ml带有磁力搅拌子的不锈钢高压釜里,加入1.50g(10mmol)苯甲酸乙酯,0.1g正十六烷(内标)以及含有0.068g(1mmol)三氟化硼的7.40g(100mmol)乙醚溶液中,升温到110℃反应6.0小时,待反应结束后,降温到0-5℃。样品用气相分析,得到苯甲酸乙酯的转化率98%,原苯酸三乙酯收率95%。
实施例2-40
根据实施例-1的反应条件,选用不同的羧酸酯和醚类化合物,以及不同的反应条件,可以得到相应的原羧酸酯类。实施例1-40的结果见表1
表1
Figure BDA0002447167730000041
Figure BDA0002447167730000051
实施例41-60
根据实施例1的反应过程,把催化剂调整为三氯化铝、三溴化铝、SO4 -/TiO2、SbF5、HSO3F、DSFB、SO4 -/Al2O3-ZnO2、H3PW12O40、HF-SbF5等催化剂(其中催化剂当量和三氟化硼相同)。其结果见表2
表2
Figure BDA0002447167730000061

Claims (8)

1.一种原羧酸酯的合成方法,其特征在于用羧酸酯与醚在催化剂催化下在一定的温度下,一定的压力下反应一定的时间制备:
Figure DEST_PATH_IMAGE001
式中:
R选自C1-C6烷基,C2-C6炔基,C3-C8环烷基,每个可用以下基团任意选择取代:(卤素,CN,NO2,C1-C6烷硫基,C1-C6烷基亚磺酰基,C1-C6烷基磺酰基;C3-C6三烷基甲硅烷基,或苯基,苯氧基或5元或6元杂芳环,每个环可用以下的基团任意选择取代:(C1-C6烷基,C2-C6炔基,C3-C8环烷基,C1-C6 卤烷基,C2-C6卤炔基;C3-C8卤环烷基,卤素,CN,NO2,C1-C6烷硫基,C1-C6烷基亚磺酰基,C1-C6 烷基磺酰基,C2-C6烷基羰基));或为苯基,苄基,五元或六元杂环,每个可用以下基团任意选择取代:(C1-C6烷基,C2-C6炔基,C3-C8环烷基,C1-C6卤烷基,C2-C6卤炔基,C3-C8卤环烷基,卤素,CN,NO2,C1-C6烷硫基,C1-C6烷基亚磺酰基,C1-C6烷基磺酰基,C2-C6烷基羰基,或C1-C6三烷基甲硅烷基);
R1、R2和R3分别独立地选自:C1-C6烷基,C2-C6烯基,C2-C6炔基,C3-C8环烷基。
2.根据权利要求1所述的一种原羧酸酯的合成方法,其特征在于所述的催化剂选自:1)路易斯酸,包括BF3、BCl3、AlBr3、CbCl3、TiCl4、ZrCl4、FeCl3、FeBr3、SbCl5、SbF5、AsF5、MbCl3、BeCl3、UCl4、WCl4、ZnCl2、CuCl2、HgCl2、SnCl4、TeCl4、AuF5、TaF5、NbF5;2)质子酸,包括氯化氢、氟化氢、发烟硫酸、硫酸、磷酸、过磷酸、三氟乙酸、高氯酸;3)液体超强酸,包括HSO3Cl、HSO3F、HSO3CF3;4)无机固体超强酸,包括 TiO2·H2SO4、SbF5-SiO2-Al2O3、SbF5-TiO2-SiO2、SO4 -/Fe2O3、SO4 -/TiO2、SO4 -/ZnO2、SO4 -/SnO2、SO4 -/Al2O3、SO4 -/Al2O3-ZnO2、SO4 -/TiO2-ZnO2、SO4 -/WO3-ZnO2;5)有机高分子超强酸,包括DSFB(制备方法见《离子交换与吸附》1995,11(4),363-367)6)无机杂多酸,包括H3PW12O40、H4SiW12O40-H4GeW12O40、H5BW12O40、H6P2W18O62、H6CoW12O40;其中的任意一种或者两种以上。
3.根据权利要求1所述的一种原羧酸酯的合成方法,其特征在于所述的羧酸酯和醚的比例在1:100-100:1(摩尔比);优选范围在1:1-1:10。
4.根据权利要求1所述的一种原羧酸酯的合成方法,其特征在于可以选用非质子有机溶剂,选自1)芳香烃如苯、 甲苯、氯苯、二甲苯,2)烷烃或者环烷烃如环己烷、正庚烷、正辛烷;3)氯代烃如二氯甲烷、二氯乙烷、氯仿、四氯化碳中的一种或两种以上。
5.根据权利要求1所述的一种原羧酸酯的合成方法,其特征在于所述的溶剂可以用反应物本身。
6.根据权利要求1所述的一种原羧酸酯的合成方法,其特征在于所述的反应时间从0.1小时-144小时。
7.根据权利要求1所述的一种原羧酸酯的合成方法,其特征在于所述的反应压力在0.01Mpa-100Mpa之间。
8.根据权利要求1所述的一种原羧酸酯的合成方法,其特征在于所述的反应温度在0-200℃之间。
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