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Abstract

This paper presents a comprehensive study on the synthesis of ethyl acetate through the esterification of acetic acid with ethanol using a continuous stirred tank reactor (CSTR). Ethyl acetate is a significant solvent in various industries due to its eco-friendly characteristics and economic efficiency. The study develops a detailed mathematical model focusing on the operating of the CSTR to enhance the understanding of the reaction kinetics and thermodynamics in a continuous processing environment. The reactor model was validated with experimental data to optimize process parameters, aiming to improve yield and selectivity. Key variables such as reactant ratios, and operational temperatures were methodically varied to study their effects on the esterification process. Results indicated that optimal conditions achieved a significant yield improvement while maintaining process sustainability. This research not only advances the operational efficiency of ethyl acetate synthesis but also supports the broader application of CSTR in similar chemical processes.

First Page

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Last Page

47

References

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