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Kinetics of Carbon Dioxide (CO2) with DiethylenetriamineinNon-aqueous Solvents using Stopped-flow Technique

机译:二亚乙基亚胺喹啉 - 水溶液的二氧化碳(CO2)的动力学使用停止流动技术

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In this work, the reaction kinetics of carbon dioxide (CO2) with diethylenetriamine (DETA)in methanol and ethanol systems were measured using the stopped flow technique over a temperature range of 293-313K in terms of pseudo first-order rate constant (k0). Concentration in the range of 10 to 50mol/m~3 for diethylenetriamine were studied. The experimental data show that the pseudo first-order rate constants (k0) increase with the increase of both amine concentration and temperature. The zwitterion mechanism and the termolecular mechanism were used to representthe data for DETAinmethanol and ethanol systems with excllent ADDs of 3.5%, 2.4%, respectively. In comparison with EDA and AEEA in terms of k2, DETA exhibits a better reaction kinetics performance for capturingCO2. Those results will be useful in finding an efficient method for the removal of CO2 from industrial gases.
机译:在这项工作中,在伪一阶速率常数(k0)方面,使用停止的流动技术在293-313k的温度范围内测量甲醇和乙醇系统中二氧化二氧化胺(DETA)的二亚甲基三胺(DETA)的反应动力学。 。研究了二亚乙基三胺的10至50mol / m〜3的浓度。实验数据表明,随着胺浓度和温度的增加,伪一阶率常数(K0)增加。两产机机理和前分子机制用于代表丁甲醇和乙醇系统的数据,分别具有3.5%,2.4%的含量增加。与EDA和AEEA在K2方面相比,DETA表现出更好的反应动力学性能,用于Captringco2。这些结果对于找到从工业气体中除去CO2的有效方法。

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