Abstract
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 important—while 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...
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.