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Study of the simultaneous catalytic hydrogenation of pyridine and hydrodesulfurization of thiophene

Journal Article · · Ind. Eng. Chem. Process Des. Dev.; (United States)
DOI:https://doi.org/10.1021/i260073a027· OSTI ID:5508294

The study of the simultaneous catalytic hydrogenation of pyridine and hydrosulfurization of thiophene, model compounds representing sulfur and nitrogen content in oil shale and coal-derived liquid fuels was extended to higher, industrially relevant pressures, up to 7 MPa. The reactions were carried out in a continuous plug-flow microreactor at 200 to 400C and thiophene and pyridine partial pressures of 12.4 kPa each, over a commercial 3.1% by wt NiO/15% MoO/sub 3//Al/sub 2/O/sub 3/ catalyst. Thiophene hydrodesulfurization was inhibited by pyridine under all the conditions studied. In the absence of thiophene, pyridine reached a thermodynamic equilibrium with piperidine above 350C at all pressures studied (1.1 4 to 7 MPa), but this equilibrium was not reached in the presence of thiophene because of the inhibition of pyridine hydrogenation and enhancement of piperidine hydrogenolysis. The combined conversion of pyridine plus piperidine, i.e., the over-all rate of hydrodenitrification, was enhanced by thiophene at > 300C and > 3.55 MPa.

Research Organization:
Massachusetts Inst. of Technology
OSTI ID:
5508294
Journal Information:
Ind. Eng. Chem. Process Des. Dev.; (United States), Journal Name: Ind. Eng. Chem. Process Des. Dev.; (United States) Vol. 19:1; ISSN IEPDA
Country of Publication:
United States
Language:
English

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