Catalyst deactivation caused by coking
has always been a concern
in the aldol condensation reaction. In this work, Ba–La-modified
alumina has been characterized and tested as a catalyst in the vapor-phase
aldol condensation process. The coke formation, acid–base properties,
and deactivation behavior of the spent catalysts were studied through
a series of characterization techniques: N2 adsorption–desorption,
pyridine FT-IR, TG-DTA, TPO-MS, as well as NH3, CO2-TPD, and UV Raman spectroscopy. It was found that the main
components of coke are polycyclic aromatic hydrocarbons, which can
be removed by high-temperature roasting under an air atmosphere. The
overactivation of formaldehyde accelerates the rate of coke deposition
and ultimately aggravates the decrease in the stability of the catalyst.
Furthermore, adding a proper amount of methanol to the reactants can
greatly inhibit the hydrolysis of esters and improve the selectivity
of the catalyst for the target reaction. Under the optimum reaction
condition of Ma/FA/CH3OH = 6:2:8, the pairs of medium acidic
and weakly basic sites enable Ba–La/Al2O3 to achieve the highest yield of methyl acrylate.