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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-III-10SIMULTANEOUS HYDROGENATION OF SULFUR, NITROGEN ANDAROMATIC COMPOUNDS IN HEAVY PETROLEUM FRACTIONSOVER NiMo/γ-Al 2 O 3 CATALYSTSF. Jiménez 1 , V. Kafarov 1 , M. Nuñez 2 , R. Maciel Filho 31 Industrial University <strong>of</strong> Santander, Kra 27 Calle 9, Tel.: +57 +76344746,Fax: +57 +76344684, Bucaramanga, Colombia. E-mail: kafarov@uis.edu.co2 Colombian Petroleum <strong>Institute</strong> - ICP, Piedecuesta, Colombia3 Campinas State University, Campinas, S.P, BrazilHydrotreating processes (HDT) have long been broadly investigated for upgrading <strong>of</strong>petroleum fractions all over world, and its role grew in importance recently because <strong>of</strong> <strong>the</strong> use<strong>of</strong> heavier feedstocks as a consequence <strong>of</strong> decreasing in light reserves and international pricesincreasing. Particularly, hydrodesulfurization (HDS) and more recently hydrodenitrogenation(HDN) and hydrodearomatization (HDA) are becoming a key target for <strong>the</strong> research inspecialized scientific community [1, 2]. The three processes have been separately matter <strong>of</strong>many investigations, and <strong>the</strong>refore many phenomena seem clear for <strong>the</strong> scientists [3].However, no extensive work has been done in research <strong>of</strong> simultaneous HDS, HDN and HDAcarried out in heavy feeds at industrial process condition. To respond to this situation, thiswork deals with <strong>the</strong> analysis <strong>of</strong> <strong>the</strong> simultaneous behavior <strong>of</strong> sulfur, basic nitrogen, non-basicnitrogen and aromatic families compounds, in real heavy feeds oils during <strong>the</strong> hydrotreatingprocess [4]. In this research, heavy vacuum gas oil (VGO) and demetalized oil (DMO) wereselected as main feedstocks. By fractioned distillation, each one <strong>of</strong> <strong>the</strong> feeds were split in fourfractions (lowest to heaviest) and each fraction was analyzed and underwent to <strong>the</strong> HDTprocess in a pilot plant, employing a combination <strong>of</strong> catalysts NiMo/γ-Al 2 O 3 and undertemperatures <strong>of</strong> 330, 350 and 370 °C, pressure <strong>of</strong> 10 MPa, liquid hourly space velocity <strong>of</strong>1.1 h –1 , and gas/oil ratio <strong>of</strong> 6.24 [5]. The employed methodology is shown in Figure 1. Thehydrotreating <strong>of</strong> full VGO and DMO was denominated «Direct Pathway», whereas <strong>the</strong>hydrotreating by cuts was denominated «Indirect Pathway». The analytical techniques used inthis work were: ultraviolet-visible spectroscopy for analysis <strong>of</strong> aromatics families, nuclearmagnetic resonance (H-NMR) for total aromatic hydrogen content, and standard methods(ASTM) for <strong>the</strong> determination <strong>of</strong> total sulfur, total nitrogen, basic nitrogen, boiling pointdistribution, density, API, refraction index, and distribution in saturates, aromatics, resins.321

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