摘要
用NO_2氧化二甲基硫醚(DMS)是合成二甲基亚砜(DMSO)的主要方法,反应过程受气液相传质影响很大.采用反应体积为120 mL的连续搅拌釜式反应器,对该反应的宏观动力学进行了研究.在温度为30~60℃、NO_2 和DMS进料流量分别为0.01~0.10 mol/min和0.005~0.05 moL/min的范围内,考查了反应速率的变化,并测定了不同温度下NO_2在DMSO中的饱和浓度.在热力学和动力学分析的基础上,推导出反应宏观动力学模型,由实验数据拟合出模型中的各参数.结果表明,该反应的活化能为21.64 kJ/mol,液相组成变化时反应速率存在极大值,且模型计算值与实验值相吻合.
Dimethyl sulfide (DMS) oxidation with NO2, which is a primary technique for the production of dimethyl sulfoxide (DMSO), is influenced intensively by mass transfer of gas-liquid phase. The reaction rates of this reaction were investigated in a 120 mL continuous stirred tank reactor at reaction temperature of 30-60 ℃ ,with NO2 and DMS feeding flow rates of 0.01-0.10 mol/min and 0. 005-0.05 mol/min respectively.The concentrations of saturated NO2 in DMSO at various temperatures were also measured. Based on thermodynamic and kinetic analyses, a macrokinetic model was established and its parameters were obtained from experimental data by using fitting method. Results show that the activation energy of the reaction is 21.64 kJ/mol, the reaction rates calculated from the model agree with the experimental values and have a maximum value when the liquid compositions are changed.
出处
《天津大学学报》
EI
CAS
CSCD
北大核心
2006年第4期414-417,共4页
Journal of Tianjin University(Science and Technology)
关键词
二甲基亚砜
二甲基硫醚
宏观动力学
二氧化氮
氧化
dimethyl sulfoxide
dimethyl sulfide
macrokinetics
nitrogen dioxide
oxidation