Improving Both the Activity and Selectivity of CoMo/δ-Al2O3 by Phosphorous Modification for the Hydrodesulfurization of Fluid Catalytic Cracking Naphtha

被引:6
作者
Zhang, Cen [1 ,2 ]
Zhang, Yicen [1 ]
Zheng, Huiting [1 ]
Xu, Jundong [1 ,2 ]
Liu, Xinyi [3 ]
Cao, Jing [1 ,2 ]
Zhou, Congshan [1 ,2 ]
机构
[1] Hunan Inst Sci & Technol, Dept Chem & Chem Engn, Yueyang 414006, Hunan, Peoples R China
[2] Key Lab Fine Petrochem Catalysis & Separat Hunan, Yueyang 414006, Hunan, Peoples R China
[3] Chinese Acad Sci, Dalian Inst Chem Phys, State Key Lab Catalysis, Dalian 116023, Peoples R China
基金
中国国家自然科学基金;
关键词
DIFFERENT CRYSTAL FORMS; FCC GASOLINE; COMO/GAMMA-AL2O3; CATALYSTS; COMO/AL2O3; CATALYST; PERFORMANCE; HDS; MORPHOLOGY; ENHANCEMENT; SULFIDE; ALUMINA;
D O I
10.1021/acs.energyfuels.1c04164
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
Developing CoMo/Al(2)O(3 )catalysts with both high hydrodesulfurization (HDS) activity and selectivity is of great importance in the HDS of fluid catalytic cracking (FCC) naphtha. However, most of the reported studies achieved improved selectivity at the expense of HDS activity. Herein, we report a phosphorous modification method to improve the HDS activity and selectivity of CoMo/delta-Al2O3 at the same time. The enhanced HDS performance for CoMoP(2.9)/delta-Al(2)O(3 )was attributed to appropriately weakened metal-support interaction, which resulted in a large amount of the (Co)MoS2 active phase with a higher stacking and Co promotion degree (type II Co-Mo-S). The improved Co promotion degree promotes the HDS activity, and increased stacking decreases the ratio of rim sites, which is beneficial for lowering the olefin hydrogenation activity. When dealing with a real FCC naphtha, the sulfur content could be reduced to 5.4 ppm while achieving a total research octane number loss of only 0.7 units. This work provides a rational catalyst design for FCC naphtha hydrorefining to meet the stringent environmental regulations of the future.
引用
收藏
页码:3825 / 3834
页数:10
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