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Kinetics of hydrodenitrogenation of SRC-II liquids and synfuel-simulating blends

✍ Scribed by Joseph Shabtai; Gene J.C. Yeh; Chris Russell; Alex G. Oblad


Publisher
Elsevier Science
Year
1988
Tongue
English
Weight
819 KB
Volume
67
Category
Article
ISSN
0016-2361

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✦ Synopsis


The kinetics of hydrodenitrogenation (HDN) of two blended feeds (blend A, a SRC-II middle-heavy distillate blended with 4.76 wt % of l,lO-phenanthroline and blend B, a synfuel-simulating reference blend containing tetralin, 85.5, phenanthrene, 3.5, and l,lO-phenanthroline, 11.0 wt %), were measured in an autoclave reactor at four temperatures between 30&375"C, using sulphided 3Co-8Mo and 3Ni-8Mo catalysts prepared by stepwise addition of the Co or Ni promoter to MO-impregnated y-A&O,. Linear increase in nitrogen removal as a function of time was found at each reaction temperature, indicating pseudo-zero-order HDN kinetics for both feeds. Faster hydrogen consumption is observed with both catalysts in the early stage of the HDN process, in agreement with previous kinetic studies of isomeric benzoquinolines, phenanthridine and carbazoles, showing rapid initial hydrogen consumption by hydrogenation of both N-heterocyclic and carbocyclic aromatic rings prior to the less-consuming CN hydrogenolysis steps. The hydrogen consumption for HDN of blend A at 35&375"C is in the range of S&10.3 moles of H, per N g atom removed. This is drastically higher than the ideal H, consumption of 34 moles H, per N g atom removed, calculated on the basis of selective hydrogenation of N-heterocyclic rings only, followed by C-N hydrogenolysis. Results obtained indicate the need for catalysts of augmented C-N hydrogenolysis selectivity for more efficient HDN of heavy oils and synfuels.


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Catalytic hydrodenitrogenation of an SRC
✍ Albert S. Hirschon; Richard M. Laine πŸ“‚ Article πŸ“… 1985 πŸ› Elsevier Science 🌐 English βš– 338 KB

The addition of hydrogen sulphide to an SRC-II coal liquid under hydrodenitrogenation conditions resulted in a significant decrease in the nitrogen content of the product. The reaction was run in a batch reactor for 1 h at 400Β°C with a presulphided Harshaw CoMo catalyst and at l2OOpsig (8.39 MPa) in