Effect of 2-hexanol and methanol on the one-pot process of dehydration and alkoxycarbonylation for the synthesis of esters

N. Sevostyanova, S. Batashev, A. S. Rodionova, D. K. Kozlenko
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Abstract

Objectives. To study the possibility of one-pot synthesis (combination of two processes in one reactor) for the following pairs of processes: (1) dehydration of 2-hexanol and isomerizing alkoxycarbonylation of the resulting 2-hexene, in order to obtain 2-hexyl heptanoate, and (2) dehydration of 2-hexanol and isomerizing methoxycarbonylation of the resulting 2-hexene, in order to obtain methyl esters of C7 carboxylic acids. To investigate the effect of the concentrations of 2-hexanol and methanol on the rate of the one-pot synthesis.Methods. One-pot synthesis was studied in a toluene medium in a steel batch reactor designed to operate at elevated pressure and equipped with a glass insert, a magnetic stirrer, a sampler, and gas input and discharge devices. Samples of the reaction mass were taken during the combined process and were analyzed by means of gas–liquid chromatography with a flame ionization detector.Results. The possibility of one-pot combination was demonstrated for 2-hexanol dehydration catalyzed by methanesulfonic acid, as well as for the isomerizing alkoxycarbonylation of the resulting 2-hexene with 2-hexanol and CO, catalyzed by the Pd(PPh3)2Cl2–XANTPHOS–methanesulfonic acid system. The dependencies of the rates of the dehydration of 2-hexanol and the formation of esters of C7 carboxylic acids on the concentration of 2-hexanol were shown to pass through a maximum. The possibility of the one-pot process was proved for the synthesis of esters from 2-hexanol, methanol, and CO with the predominant formation of heptanoic acid esters in the presence of the above catalytic system. The rates of dehydration of 2-hexanol and the formation of 2-hexyl esters of C7 carboxylic acids were found to decrease with increasing the concentration of methanol in the reaction mass. Under mild conditions (temperature 115°C, CO pressure 3 MPa) with the addition of methanol, the total fraction of 2-hexyl and methyl heptanoic acid esters among C7 carboxylic acid esters was determined to be 85.5%.Conclusions. The reactions of intramolecular acid–catalytic dehydration of 2-hexanol and isomerizing alkoxycarbonylation of the resulting 2-hexene, catalyzed by the Pd(PPh3)2Cl2–XANTPHOS–methanesulfonic acid system, can be performed as a one-pot process. Methanesulfonic acid simultaneously functions as a catalyst for the dehydration of 2-hexanol and a cocatalyst for the palladium–phosphine system for the alkoxycarbonylation of hexenes. In the presence of the Pd(PPh3) 2Cl2–XANTPHOS–methanesulfonic acid catalytic system, processes for the synthesis of heptanoic acid esters from 2-hexanol, methanol, and CO can be combined within one reactor. An increase in the methanol concentration negatively affects the rate of the dehydration of 2-hexanol and the formation of 2-hexyl esters of C7 carboxylic acids. A small amount of methanol in the reaction mass leads to an increase in the fraction of heptanoic acid esters among C7 carboxylic acid esters.
2- 己醇和甲醇对脱水和烷氧羰基化一步法合成酯的影响
目标: 研究以下几种工艺的单锅合成(在一个反应器中结合两种工艺)的可能性研究以下几种工艺进行一次合成(在一个反应器中结合两种工艺)的可能性:(1) 2-己醇脱水,并对生成的 2-己烯进行异构化烷氧基羰基化反应,以获得庚酸 2-己酯;(2) 2-己醇脱水,并对生成的 2-己烯进行异构化甲氧基羰基化反应,以获得 C7 羧酸甲酯。研究 2-己醇和甲醇的浓度对单锅合成速率的影响。单锅合成是在甲苯介质中,在钢制间歇反应器中进行的,该反应器设计为在高压下运行,并配备了玻璃插件、磁力搅拌器、取样器以及气体输入和排放装置。在组合过程中对反应物进行取样,并通过带有火焰离子化检测器的气液相色谱法进行分析。甲磺酸催化的 2- 己醇脱水以及 Pd(PPh3)2Cl2-XANTPHOS-Methanesulfonic acid 系统催化的 2- 己烯与 2- 己醇和 CO 的异构化烷氧基羰基化反应都证明了单锅组合的可能性。结果表明,2-己醇的脱水速率和 C7 羧酸酯的生成速率与 2-己醇浓度的关系达到了最大值。在上述催化体系存在的情况下,证明了以 2-己醇、甲醇和 CO 为原料合成酯类的单锅工艺的可能性,并主要生成了庚酸酯。研究发现,随着反应物中甲醇浓度的增加,2-己醇的脱水率和 C7 羧酸 2-己酯的生成率都会降低。在加入甲醇的温和条件下(温度 115°C,CO 压力 3 兆帕),C7 羧酸酯中 2-己基和甲基庚酸酯的总比例为 85.5%。在 Pd(PPh3)2Cl2-XANTPHOS-甲磺酸体系的催化下,2-己醇的分子内酸催化脱水反应和生成的 2-己烯的异构化烷氧基羰基化反应可作为一锅工艺进行。甲磺酸既是 2-己醇脱水的催化剂,又是钯膦体系进行己烯烷氧基羰基化的助催化剂。在 Pd(PPh3) 2Cl2-XANTPHOS-Methanesulfonic acid 催化体系存在的情况下,从 2-己醇、甲醇和 CO 合成庚酸酯的过程可在一个反应器中进行。甲醇浓度的增加会对 2-己醇的脱水速率和 C7 羧酸 2-己酯的生成产生负面影响。反应物中少量甲醇会导致 C7 羧酸酯中庚酸酯的比例增加。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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