Hydrotreatment and Hydrocracking of Oil Fractions by B. Delmon
By B. Delmon
The 2d overseas Symposium on Hydrotreatment and Hydrocracking of Oil Fractions, that's additionally the seventh within the sequence of ecu Workshops on Hydrotreatment, came about in Antwerpen, Belgium from November 14 to 17.The Symposium emphasised how oil refining faces more and more serious environmental laws. those and the expanding software of heavier crudes containing extra S-, N- and steel parts demand extra effective hydrotreatment and hydrocracking approaches. it's transparent from the keynote lectures, the oral contributions and the posters of this assembly that adapting the working stipulations won't suffice. enough catalysts must be built, with assorted composition and constitution. floor technology strategies and molecular modeling are actually good validated instruments for this type of improvement. they need to be of assist in generally varied features, just like the function of precursors within the education or the variations gone through through the catalyst less than response stipulations. the advance of hydrotreatment and hydrocracking additionally wishes exact modeling of the chemical reactor. This calls for extra consultant hydrodynamics and kinetic types whose validity extends to the very low S- and N-contents. those parts will be vigorously constructed.
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42. , EP 359356 (1990). 43. Standard Oil Co. Ohio, US 4177136 (1979). 44. J. Tuszynski, US 4725571 (1988). J. Tuszynski, US 4725569 (1988). 46 Soc. Nat. Elf Aquitaine, WO 8805338 (1988). 47 Shell Int. Res. Mij. , WO 9748488 (1997). M. van Gestel, J. C. Duchet, J. , 145 (1994) 429. 49 Tricat Ind. , WO 9806493 (1998). 50 Shell Int. Res. Mij. , WO 9834728 (1998) and WO 9748489 (1997). 34 51. E. S. W. Cui, Appl. , 58 (1990) 199. 52. M. A. Louwers and R. Prins, Catal. Today, 10 (1991) 345. 53. A. J.
The amount of pyridine left on B (1540 cm 1) and L (1450 cm "1) sites were 85% and 50% to saturated amount at 423 K. At initial stage of hydrogen introduction, L peak decreased and B peak increased. After B peak reached the saturation level, the peaks assigned to piperidine appeared. The results indicated that when vacant B sites exist, pyridine adsorbed on L site migrated to the B site. Figure l(b) shows the spectra of the sample with very low coverage of pyridine (B:55% and L: 25%). Pyridine migration from L to B was clearly observed and pyridine hydrogenation did not proceed at all even after 150-min hydrogen flow.
Kis, G. Lomic and P. Pavlovic, Appl. Catal. A, 107 (1994) 133. 120. Y. Yoshimura, E. Furimsky, T. Sato, H. Shimada, N. Matsubayashi and A. Nishijima, 9th Int. Catal. Congr. (Calgary 6/26-7/1/88) Proc. 1 (1988) 136. 121. E. Furimsky, Fuel Process. , 27 (1991) 131. 122. Y. Yoshimura, S. Yoshitomi, T. Kameoka, T. Sato, H. Shimada, N. Matsubayashi, M. Imamura, A. Nishijima and H. Yanase, Energy & Fuels, 8 (1994) 435. 123. Y. Noguchi, T. Itoh T, Y. Obayashi and K. Komine, ACS Div. Petr. , 38 (1993) 50.