磷(iii)化合物在不同介质中催化合成3-羟基-2-萘酸苯胺

Leon Shteinberg
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引用次数: 0

摘要

在各种介质(甲苯、辛烷、氯苯、对二甲苯、邻二甲苯、邻氯甲苯、三甲甲苯、伪文献烯、n.=德斯兰、邻二氯苯、邻二甲苯和硝基苯的混合物)中苯胺与3=羟基=2=萘酸的酰化反应中,磷(III)化合物(三氯化磷和磷酸)的催化作用使水沸腾和蒸馏后形成3=羟基=2=萘酸苯胺。随着反应温度在111℃(甲苯)至170℃(伪异丙烯)范围内的升高,观察到目标产物的初始生成速率单调增加。在这种情况下,速度对数与温度的关系符合Arrhenius方程,活化能Ea为66.2 kJ/mol。高沸点n =癸烷(175°С)和邻位二氯苯(180°С)脱离了这种依赖关系,其中苯胺3=羟基=2=萘酸的初始生成速率与伪文献烯(170°С)相比降低了。后者可能是由于催化剂在如此高的温度下分解或氧化,P(III)转变为P(V), P(III)不具有催化活性。苯胺与3=羟基=2=环烷酸的相互作用是一系列顺序平行的反应,其中除了3=羟基=2=环烷酸反内酯外,3=苯胺=2=环烷酸及其苯胺作为杂质形成。最可接受的溶剂是邻二甲苯和邻氯甲苯,沸点分别为146℃和156℃,目标产物的收率可达98%。在146℃以下,反应以相对较低的速率进行;156℃以上杂质量明显增加,主要与反应温度的升高平行,3=羟基=2=萘酸苯胺的最大产率降低。这就需要对其进行额外的净化,使工艺过程大大复杂化。邻二甲苯中加入10-20%体积的硝基甲苯,在146-148℃范围内,3=氧=2=萘酸苯胺的产率提高1.25-1.42倍,溶剂极性(ε)分别从2.3提高到7.64。这可能是由于催化剂的单体数量和/或3=氧=2=萘酸和苯胺的反应质量和水分离速度的增加所致。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
SYNTHESIS OF 3-HYDROXY-2-NAPHTHOIC ACID ANILIDE CATALYZED BY PHOSPHORUS (III) COMPOUNDS IN VARIOUS MEDIA
Catalysis with phosphorus P(III) compo­unds (phosphorus trichloride and phospho­rous acid) in the acylation of aniline with 3=hydroxy=2=naphthoic acid in various media (toluene, octane, chlorobenzene, para=­xylene, ortho=xylene, ortho=chlorotoluene, mesitylene, pseudocumene, n.=deсan, ortho= di­chlo­ro­benzene, mixtures of ortho=xylene with nitrobenzene) upon boiling and vigorous distillation of water leads to the formation of 3=hydroxy=2=naphthoic acid anilide. With an increase in the reaction temperature in the range from 111 (toluene) to 170 °C (pseudo cumene), a monotonous increase in the initial rate of formation of the target product is observed. In this case, the temperature depen­dence of the logarithm of the velocity obeys the Arrhenius equation, and the activation energy Ea is 66.2 kJ/mol. Higher-boiling n.=decane (175 °С) and ortho=dichlorobenzene (180 °С) fall out of this dependence, in which the initial rate of formation of anilide 3=hydroxy=2=naphthoic acid, compared with that for pseudocumene (170 °С), decreases. The latter may be due to the decomposition or oxidation of the catalyst at such a high temperature with the transition of P(III) to P(V), which does not have catalytic activity. The interaction of aniline with 3=hydro­xyl=2=naphthoic acid proceeds as a series of sequential and parallel reactions in which, in addition to 3=hydroxyl=2= naphthoic acid ani­lide, 3=aniline=2=naphthoic acid and its anilide are formed as impurities. The most acceptable solvents are ortho=xylene and ortho=chlorotoluene with boiling points of 146 and 156°C, in which the yield of the target product is up to 98%. Below 146 °C the reaction proceeds at a relatively low rate; above 156°C the amount of impurities increases significantly, mainly in parallel with an increase in the reaction temperature, and the maximum yield of 3=hydroxyl=2=naphthoic acid anilide decreases. This requires its additional purification, significantly complicating the technological process. The addition of 10–20% by volume of nit­robenzene to ortho=xylene leads to an increase in the yield of 3=oxy=2=naphthoic acid anilide by 1.25–1.42 times in the temperature range of 146–148°C with increasing solvent polarity (ε), respectively, from 2.3 to 7.64. This may be due to an increase in the quantity of the monomers of the catalyst and/or 3=oxy=2=naphthoic acid and aniline in reaction mass and the speed of water separation.
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