Study on Solvent Recovery of Batch Extractive Distillation for Separation of Ethanol-Water
Yao Jun-feng
Abstract
Yao Jun-feng
Abstract
In this paper, the process of solvent flow velocity choosing and the solvent recovery operation during batch extractive distillation for the separation of ethanol-water azeotropic mixture using glycol as the solvent was studied. The results showed that the relative volatility of ethanol-water azeotropic mixture increased obviously as solvent ratio increased and the slop cut of water-glycol lasted a very short time during which the temperature at the top of the column rose sharply. When the reflux ratio was up to 2:1, the yield percentage of solvent recovery reached the value of 99.33%.
A significance statement is not available in the OpenAlex record.
A contribution statement is not available in the OpenAlex record.
Method details are not available in the OpenAlex metadata.
Findings are not separately available in the OpenAlex metadata.
Limitations are not available in the OpenAlex metadata.
Application details are not available in the OpenAlex metadata.
In this paper, the process of solvent flow velocity choosing and the solvent recovery operation during batch extractive distillation for the separation of ethanol-water azeotropic mixture using glycol as the solvent was studied. The results showed that the relative volatility of ethanol-water azeotropic mixture increased obviously as solvent ratio increased and the slop cut of water-glycol lasted a very short time during which the temperature at the top of the column rose sharply. When the reflux ratio was up to 2:1, the yield percentage of solvent recovery reached the value of 99.33%.
Key concepts: Solvent, Batch distillation, Azeotropic distillation, Extractive distillation, Relative volatility, Chemistry, Chromatography, Fractional distillation