HDS of straight-run gas oil at various nitrogen contents.: Comparison between different reaction systems

被引:14
作者
Alvarez, A. [1 ]
Escobar, J. [1 ]
Toledo, J. A. [1 ]
Perez, V. [1 ]
Cortes, M. A. [1 ]
Perez, M. [1 ]
Rivera, E. [1 ]
机构
[1] Inst Mexicano Petr, Prog Ing Mol, Mexico City 07730, DF, Mexico
关键词
hydrodesulfurization; HDS inhibition; low-nitrogen gas oil; LIGHT CYCLE OIL; DEEP HYDRODESULFURIZATION; DIBENZOTHIOPHENE; PERFORMANCE; CATALYST; REMOVAL; 4,6-DIMETHYLDIBENZOTHIOPHENE; 4-METHYLDIBENZOTHIOPHENE; DESULFURIZATION; KINETICS;
D O I
10.1016/j.fuel.2006.08.001
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The effect of removal extent of nitrogen-containing species on the hydrodesulfurization (HDS) of straight-run gas oil from a Mexican refinery over a NiMo-based catalyst was studied. The original middle distillate (similar to 360 ppm N) was subjected to N-compounds removal by contacting with a proprietary adsorbent. By varying contact time, feedstocks of similar to 234 and similar to 137 ppm N were obtained. Progressive improvement on HDS over NiMo catalyst was observed by decreasing concentration of organo-N compounds in the gas oils tested in batch reactor. However, this behavior seemed to depend on the severity of the operation. By increasing operating temperature, the enhanced desorption rate of N-compounds relieved their poisoning effect, making less pronounced the benefit of low-nitrogen feedstocks. The HDS activity data from batch reactor were compared to those found when equivalent experiments were carried out in a fixed-bed up-flow reactor under conditions similar to those used in industrial facilities. (C) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1240 / 1246
页数:7
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