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.
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.
| № | Муаллифнинг исми | Лавозими | Ташкилот номи |
|---|---|---|---|
| 1 | Maksudov .R. | Researcher, | Tashkent State Technical University |
| 2 | Norkobilov A.T. | Associate professor | Shahrisabz branch of the Tashkent Institute of Chemical Technology, Shahrisabz city |
| 3 | Bakhtiyorov A. . | Bachelor student | Shahrisabz branch of the Tashkent Institute of Chemical Technology |
| 4 | Zaripov O.. | DSc, Professor | Tashkent State Technical University |
| № | Ҳавола номи |
|---|---|
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