| 催化反应精馏法制D-乳酸的研究 |
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| 引用本文： | 李泽壮,刘经伟,方晓江.催化反应精馏法制D-乳酸的研究[J].精细石油化工,2020,37(2):21-24. |
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| 作者姓名： | 李泽壮 刘经伟 方晓江 |
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| 作者单位： | 中国石化扬子石油化工有限公司南京研究院,江苏南京210048;中国石化扬子石油化工有限公司南京研究院,江苏南京210048;中国石化扬子石油化工有限公司南京研究院,江苏南京210048 |
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| 摘 要： | 筛选了SHY树脂作为D-乳酸甲酯的水解树脂,考察了树脂水解动力学性能。根据推导的水解动力学方程求取水解、酯化反应的指前因子和活化能。运用Aspen Plus软件对D-乳酸产量为1 kt/a的反应精馏塔进行模拟,发现精馏塔反应段需要9块理论板,其中进料位置以上需3块理论板,进料位置以下需6块理论板。
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| 关 键 词： | D-乳酸 指前因子 活化能 催化反应精馏 理论板 |
RESEATCH OF REACTIVE DISTILLATION PROCESS FOR THE SYNTHESIS OF D-LACTIC ACID |
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| Li Zezhuang,Liu Jingwei,Fang Xiaojiang.RESEATCH OF REACTIVE DISTILLATION PROCESS FOR THE SYNTHESIS OF D-LACTIC ACID[J].Speciality Petrochemicals,2020,37(2):21-24. |
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| Authors: | Li Zezhuang Liu Jingwei Fang Xiaojiang |
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| Affiliation: | (Nanjing Research Institute of Sinopec Yangzi Petrochemical Limited Company, Nanjing 210048, Jiangsu, China) |
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| Abstract: | SHY resin was selected as the hydrolysis resin of methyl D-lactate,and its hydrolysis kinetics was investigated.According to the derived hydrolysis kinetics equation,the pre-exponential factors and activation energies were calculated.Aspen Plus software was used to simulate the reaction distillation column with D-lactic acid output of 1 kt/a.It was found that 9 theoretical plates were needed in the reaction section of the distillation column,including 3 theoretical plates above the feed position and 6 theoretical plates below the feed position. |
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| Keywords: | D-lactate activation energy pre-exponential factors catalytic reaction distillation theoretical plates |
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