In selective hydrogenation of pyrolysis gasoline, Pd/Al2O3 is often deposit
ed with iron species due to corrosion of equipment. The impact of deposited
iron on the Pd/Al2O3 is examined. TPR (temperature-programmed reduction) r
esults suggest that the clusters of deposited iron remain segregated from P
d clusters. By use of a model of Fe2O3-Pd/Al2O3 in hydrogenation of pyrolys
is gasoline, the deposited iron is shown to increase isoprene conversion, o
lefin selectivity, and coke formation. TPD (temperature-programmed desorpti
on) of NH3 and TPR results indicate that the deposited iron is in the form
Fe2O3, which increases the acidity of the catalyst. The increased acidity p
romotes coke formation. Excess coke formation leads to high-pressure drops
and eventually bed plugging.