Development of a Computer-Aided Process for Recovering and Purifying 2-Methyl-2-Cyclopentenone Based on Measured Phase Equilibrium Data

2-Methyl-2-cyclopentenone (MCP) is the main by-product of the newly developed heterogeneous catalysis process for producing crotonaldehyde, which serves as an important intermediate for drug synthesis. However, how to recover and purify MCP from the product mixture is not known. To decipher this, a computer-aided process based on the measured phase-equilibrium data was developed. The improved Rose–Williams equilibrium kettle was used to measure the vapor–liquid equilibrium data for MCP–crotonaldehyde and MCP–water. Surprisingly, MCP and water formed a minimum azeotrope, which aided its own recovery from its dilute solution. The mole fraction of MCP in the azeotrope was 9.1%, the mole fraction of water was 90.9%, and the azeotropic temperature was 96.8 °C. Equilibrium data from the two binary systems were correlated using the Wilson and NRTL activity coefficient models. The NRTL-RK model was selected to simulate the process for recovering and purifying MCP. A two-column process was developed and optimized in this study, and the aim of effectively utilizing the by-product MCP was achieved with this process.

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Publication Details

Journal
Processes
Published
2025-05-08
DOI
https://doi.org/10.3390/pr13051435
Primary Topic
Process Optimization and Integration
Type
article
Field-Weighted Citation Impact
0.00

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article

Development of a Computer-Aided Process for Recovering and Purifying 2-Methyl-2-Cyclopentenone Based on Measured Phase Equilibrium Data

Zhongfeng Geng, Yunfei Bai, Ke Zhang, Feng Shi
Processes
Process Optimization and Integration
article

Development of a Computer-Aided Process for Recovering and Purifying 2-Methyl-2-Cyclopentenone Based on Measured Phase Equilibrium Data

Zhongfeng Geng, Yunfei Bai, Ke Zhang, Feng Shi
article en

Abstract

2-Methyl-2-cyclopentenone (MCP) is the main by-product of the newly developed heterogeneous catalysis process for producing crotonaldehyde, which serves as an important intermediate for drug synthesis. However, how to recover and purify MCP from the product mixture is not known. To decipher this, a computer-aided process based on the measured phase-equilibrium data was developed. The improved Rose–Williams equilibrium kettle was used to measure the vapor–liquid equilibrium data for MCP–crotonaldehyde and MCP–water. Surprisingly, MCP and water formed a minimum azeotrope, which aided its own recovery from its dilute solution. The mole fraction of MCP in the azeotrope was 9.1%, the mole fraction of water was 90.9%, and the azeotropic temperature was 96.8 °C. Equilibrium data from the two binary systems were correlated using the Wilson and NRTL activity coefficient models. The NRTL-RK model was selected to simulate the process for recovering and purifying MCP. A two-column process was developed and optimized in this study, and the aim of effectively utilizing the by-product MCP was achieved with this process.

ProcessesVol. 13(5)
Tianjin University (CN)
National Natural Science Foundation of China
Openalex Percentile: Top 90%
Process Optimization and Integration
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