Propuesta para la mejora integral de la seguridad y operatividad en columnas de destilación batch de acetato de etilo y n-hexano: Un enfoque HAZOP

Abstract

Abstract: This work proposes a comprehensive improvement in the safety and operability of the batch distillation process of ethyl acetate and hexane, widely used chemical compounds, but with high associated risks. Ethyl acetate, being highly flammable, can cause fires or explosions if overheated, while hexane, in addition to being toxic, also presents similar risks due to its explosive capacity upon contact with air in the event of leaks or spills. To address these risks, the HAZOP (Functional Analysis of Operability) methodology was used, a systematic analysis tool that identifies the specific hazards and risks present in the batch distillation process, developing preventive and corrective measures designed to mitigate the hazards associated with both compounds, promoting a safer and more efficient work environment. This approach not only helps minimize the possibility of incidents but also optimizes the operation of distillation columns. The main contribution lies in ensuring a controlled, safe, and reliable process, responding to the need to manage risks in critical industrial activities.