Kinetic modeling of liquid‐phase esterification of acetic acid with n‐butanol using heterogeneous poly(o‐methylene p‐toluene sulfonic acid) as catalyst

Abstract

AbstractLiquid‐phase esterification of acetic acid with n‐butanol to n‐butyl acetate is studied in the presence of a polymeric catalyst, that is, poly(o‐methylene p‐toluene sulfonic acid). The performance of the proposed catalyst is compared with the other commercially available homogeneous and heterogeneous catalysts in terms of its activity. Experiments are conducted in an isothermal stirred batch reactor to study the effects of speed of agitation, temperature, and catalyst loading on the rate of reaction. A concentration‐based pseudo‐homogeneous (PH) kinetic model and activity‐based kinetic models such as PH, Eley‐Rideal (ER), and Langmuir‐Hinselwood‐Hougen‐Watson (LHHW) models are developed. All the models considered in this study resulted in similar percentage deviation close to 4%. Further, kinetic models are validated through additional experiments, and it is observed that the simple concentration‐based PH model is able to predict experimental data with least deviation compared to activity‐based PH, ER, and LHHW models. The developed kinetic models are also tested using the Fisher‐Snedecor test (F‐test) and are found to be acceptable. By incorporating both modeling data and validation data, the overall absolute average deviations of different models are found to be concentration‐based PH model 4.354%, activity‐based PH model 5.006%, ER I model 5.189%, ER II model 5.403%, ER III model 5.437%, and LHHW model 6.104%, illustrating the superiority of the simple concentration‐based PH model.