Based on the kinetic and thermodynamic equations

a comprehensive mathematical model for the continuous esterification process of polyester polyols was developed

which was carried out in an innovational bubbling reactive distillation tower (BRDT) at atmospheric pressure. In this new type of reactor

direct esterification between ethylene glycol and adipic acid was accomplished efficiently and rapidly. A bench BRDT with the height of 2 m was applied for the esterification process of poly (ethylene adipate) (PEA). In the continuous operation

linear oligomers were discharged from the bottom of the column

while water passed a few column trays and a packing section as a condensation byproduct. The influence of major operating conditions on reactor performance was also simulated. Simulation results were in good agreement with experimental data

providing a strategy for developing and optimizing this process.