Fig. 4 | Scientific Reports

Fig. 4

From: Intensified process based on reactive distillation for Triacetin production via glycerol esterification with acetic acid

Fig. 4

Kinetic model validation for glycerol esterification using Purolite C160 in a batch reactor (data adapted from15 using an acetic acid to glycerol molar ratio of 6 to 1 at atmospheric pressure. (A) glycerol conversion lines (-) represent simulation results and symbols represent experimental results) and (B) comparison product yields between experimental results and simulation results.

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