ON REACTIVITY OF PIPERAZINE AMINOGRUPS IN INTERACTION WITH ETHYLENE OXIDE

Yuliya V. Demidova, V. Potekhin, P. A. Demidov
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Abstract

Currently, the main method for producing N-(2-hydroxyethyl) piperazine in industry is the cyclization of ethylene glycols and ethanolamines in the presence of ammonia and hydrogen. The main disadvantage of this method is the production of a wide range of products and, as a consequence, low selectivity for N-(2-hydroxyethyl) piperazine. In this work, the object of study is the piperazine hydroxyethylation reaction in the presence of an “inert” solvent under the reaction conditions, as the most selective way to obtain N-(2-hydroxyethyl) piperazine. The solvent molecule acts as a homogeneous catalyst of the acid type and is characterized by the presence of a mobile proton for opening the oxirane ring of ethylene oxide by the acid-base mechanism. There was studied the dependence of the yield of reaction products on the parameters of the process in the temperature range of 60 - 130 ° C; solvent concentration (water, methylcellosolve) 1 - 75% wt. and molar ratio of reagents (ethylene oxide / piperazine) 0.2 - 1. Analysis of the reaction mass by gas-liquid chromatography showed that the main by-product is N, N'-bis (2-hydroxyethyl) piperazine - the product of the hydroxyethylation of N-(2-hydroxyethyl ) piperazine in the second amino group. The hydroxyl group of hydroxyethylation products are formed in a negligible amount. It was found that the composition and concentration of the solvent, as well as the temperature regime of hydroxyethylation, do not significantly affect the selectivity of the process. It was shown that piperazine hydroxyethylation is described by the kinetics of series-parallel reactions. The results obtained in the study may be of interest for the development of piperazine hydroxyethylation process technology, in terms of simplifying the mathematical model of the reactor unit by excluding from the description factors that do not significantly affect the selectivity of the formation of N-(2-hydroxyethyl) piperazine.
哌嗪胺基与环氧乙烷相互作用的反应性
目前,工业上生产N-(2-羟乙基)哌嗪的主要方法是在氨和氢的存在下,乙二醇和乙醇胺进行环化反应。该方法的主要缺点是生产的产品范围广,因此对N-(2-羟乙基)哌嗪的选择性低。在这项工作中,研究的对象是在“惰性”溶剂存在下的哌嗪羟乙基化反应条件下,作为选择性最强的方法获得N-(2-羟乙基)哌嗪。溶剂分子作为酸型均相催化剂,其特点是存在一个可移动的质子,通过酸碱机制打开环氧乙烷的氧环。研究了反应温度在60 ~ 130℃范围内反应产物产率与工艺参数的关系;溶剂浓度(水,甲基纤维素溶液)1 - 75% wt,试剂摩尔比(环氧乙烷/哌嗪)0.2 - 1。气液色谱法对反应质量的分析表明,主要副产物为N, N′-双(2-羟乙基)哌嗪,是N-(2-羟乙基)哌嗪在第二氨基上发生羟乙基化反应的产物。羟基乙基化产物的羟基形成量可以忽略不计。结果表明,溶剂的组成和浓度以及羟乙基化反应的温度对反应的选择性没有显著影响。结果表明,哌嗪羟乙基化反应可以用串并联反应动力学来描述。通过从描述中排除不显著影响N-(2-羟乙基)哌嗪形成选择性的因素,简化了反应器单元的数学模型,研究结果可能对哌嗪羟乙基化工艺技术的发展有意义。
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