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二甲醚羰基化制醋酸甲酯生产过程中最佳操作条件的研究

Investigation of optimal operating conditions in dimethyl ether carbonylation to methyl acetate production process.

作者信息

Peyman Shadi, Bijani Parisa Moghimpour, Bahadori Fatemeh

机构信息

Faculty of Chemical Engineering, Urmia University of Technology, P.O. Box 57166-17165, Urmia, Iran.

Catalyst Research Group, Petrochemical Research and Technology Company, National Petrochemical Company, P.O. Box 14358-84711, Tehran, Iran.

出版信息

Environ Sci Pollut Res Int. 2023 Oct;30(48):106636-106647. doi: 10.1007/s11356-023-29871-1. Epub 2023 Sep 21.

Abstract

Ethanol production methods are expanding due to the importance of ethanol as a fuel or additive to fuels. One of these methods is converting methanol to ethanol in a three-step process. All of these steps need to deeply study and investigate to develop the process. In this research, the carbonylation of dimethyl ether to produce methyl acetate, which is the intermediate reaction of the three-step process of methanol to ethanol, has been simulated and optimized. The parameters of temperature, pressure, residence time, and feed ratio have been investigated as effective operational parameters of the process. It has been shown that the temperature and pressure of the process are more effective in the ranges of 220-280 °C and 30-50 bar, respectively. The simulation results showed a maximum point in dimethyl ether conversion in the feed ratio of 0.4-0.6, i.e., in temperature of 260 °C, residence time of 5 h, pressure of 45 bar, DME/CO/Ar = 30/67/3, and DME conversion about 22%. Also, it has been shown that increasing the residence time increases the effect of each of the above parameters. Optimization of the dimethyl ether carbonylation process has demonstrated that the combination of different ranges of the above parameters achieves the desired conversion, i.e., in pressure of 48.23 bar, temperature of 259.06 °C, residence time of 3.68 h, and dimethyl ether/feed of 0.461 vol%; conversion of dimethyl ether will be equal to 85.50%.

摘要

由于乙醇作为燃料或燃料添加剂的重要性,乙醇生产方法正在不断扩展。其中一种方法是通过三步过程将甲醇转化为乙醇。为了开发该过程,所有这些步骤都需要深入研究和调查。在本研究中,对二甲醚羰基化生产乙酸甲酯进行了模拟和优化,乙酸甲酯是甲醇制乙醇三步过程中的中间反应。研究了温度、压力、停留时间和进料比等参数作为该过程的有效操作参数。结果表明,该过程的温度和压力分别在220 - 280°C和30 - 50 bar范围内更为有效。模拟结果表明,在进料比为0.4 - 0.6时,即温度为260°C、停留时间为5 h、压力为45 bar、二甲醚/一氧化碳/氩气 = 30/67/3的条件下,二甲醚转化率出现最大值,二甲醚转化率约为22%。此外,研究表明增加停留时间会增强上述每个参数的影响。二甲醚羰基化过程的优化表明,上述参数不同范围的组合可实现所需的转化率,即在压力为48.23 bar、温度为259.06°C、停留时间为3.68 h以及二甲醚/进料为0.461体积%的条件下,二甲醚转化率将等于85.50%。

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