Resumo (PT):
Abstract (EN):
: Fixed-bed reactors for nitrobenzene (NB) hydrogenation into aniline (ANL) in the liquid phase have not
experienced extensive industrial-scale development, mostly due to
difficulties in removing the reaction heat generated. In this work,
NB hydrogenation was performed in a tubular fixed-bed reactor
using a Pd/Al2O3 commercial catalyst. The influence of some
operating conditions was analyzed by assessing catalyst performance
in NB conversion and selectivity toward ANL and secondary
products. It was found that catalyst time of usage is extremely
importantwhile NB conversion remains stable, selectivity toward
the products formed changes (ANL selectivity increases with the
catalyst use but the formation of secondary products decreases until
almost disappearing). It was also found that temperature and
pressure are the most important parameters in the ranges studied
and that NH3, which is a reaction product with potential influence in gas composition, does not affect NB conversion but helps
decreasing secondary products formation.
Language:
English
Type (Professor's evaluation):
Scientific
No. of pages:
12