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  1. 1 Ιουν 2018 · In this study, residue curve maps of the n-butyl acetate synthesis reaction were calculated based on the Langmuir-Hinshelwood-Hougen-Watson kinetic and UNIQUAC models to calculate the physical...

  2. 17 Αυγ 2022 · The conventional process for BuAc production is both capital and energy intensive. The purification process involves the separation of BuAc from the azeotropic mixture of water and n-butanol, which is difficult to accomplish using a simple distillation unit.

  3. 3 Οκτ 2002 · The development of a heterogeneously catalyzed reactive distillation process for the production of n-butyl acetate by the esterification of n-butanol with acetic acid is presented....

  4. 1 Οκτ 2012 · In this paper, a reactive distillation (RD) column was applied for synthesis n-butyl acetate from n-butanol and acetic acid. The Langmuir-Hinshelwood-Hougen-Watson (LHHW) kinetic model and an equilibrium stage model for separation were employed to study the RD process.

  5. 1 Ιαν 2009 · The production of n -butyl acetate from dilute acetic acid and n -butanol in three reactive distillation systems; i.e., single-column reactive distillation, distillation–reactive distillation hybrid system and pervaporation–reactive distillation hybrid system, was simulated using ASPEN PLUS program.

  6. 11 Σεπ 2023 · Abstract. Experiments are conducted in a lab-scale continuous reactive distillation column (CRDC) for the esterification of acetic acid with n -butanol to produce n -butyl acetate using a poly (o-methylene p-toluene sulfonic acid) (PTSA–POM) catalyst.

  7. Conceptual design of n-butyl acetate synthesis by reactive distillation based on residue curve maps is presented. Based on the simulation results, both the energy consumption and

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