Study on Hydrodesulfurization of L/W Coexistence Zeolite Modified by Magnesium for FCC Gasoline

被引:15
作者
Fan, Jiyuan [1 ]
Yang, Xu [2 ]
Zhao, Zhen [1 ]
Duan, Aijun [1 ]
Xu, Chunming [1 ]
Zheng, Peng [1 ]
Wang, Xilong [1 ]
Jiang, Guiyuan [1 ]
Liu, Jian [1 ]
Wei, Yuechang [1 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[2] SINOPEC, Inst Dalian, Res Inst Petr & Petrochem, Dalian 116041, Liaoning, Peoples R China
基金
中国国家自然科学基金;
关键词
HYDRO-UPGRADING PERFORMANCE; HDS CATALYSTS; SILICA FOAMS; MG; COMPOSITE; DESULFURIZATION; AROMATIZATION; SELECTIVITY; MOLYBDENA; MO/AL2O3;
D O I
10.1021/acs.energyfuels.7b03072
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
L/W coexistence zeolite was synthesized with low-cost silica-alumina microspheres via an in situ hydrothermal method and modified by Mg as catalyst additive for FCC gasoline hydro-upgrading. The physicochemical properties of the supports and corresponding catalysts were characterized by means of XRD, SEM, N-2 adsorption-desorption, NH3-TPD, Py-IR, H-2-TPR, HRTEM, and Raman spectroscopy. The characterization results demonstrated that the L/W composite possessed the typical characteristics of L and W zeolites and that the morphology of L/W coexistence zeolite was completely different from that of the mechanical mixed zeolite. NH3-TPD and Py-IR results showed that the amount of acid sites decreased with an increase in Mg incorporation. Moreover, H-2-TPR profiles indicated that Mg regulated the metal-support interaction, which was conducive to the formation of type-II CoMoS phase. With the promoting effects of Mg, Cat-2Mg catalyst exhibited a good balance between hydrodesulfurization (HDS) efficiency (91.4%) and the preserving ability of the octane number (the decrease in research octane number (Delta RON) = 0.8 units), which could be attributed to the synergy effects of proper texture property, suitable acidity, and moderate MoS2 slab distribution.
引用
收藏
页码:777 / 786
页数:10
相关论文
共 48 条
[1]  
[Anonymous], 2017, CHINA VEHICLE ENV MA
[2]   Dehydrogenation of propane over Pt/KL catalyst Investigating the role of L-zeolite structure on catalyst performance using isotope labeling [J].
Azzam, Khalid G. ;
Jacobs, Gary ;
Shafer, Wilson D. ;
Davis, Burtron H. .
APPLIED CATALYSIS A-GENERAL, 2010, 390 (1-2) :264-270
[3]  
Bai Y, 2006, CHINESE J CATAL, V27, P275
[4]   Improved hydrogenolysis (C-S, C-M) function with basic supported hydrodesulfurization catalysts [J].
Caloch, B ;
Rana, MS ;
Ancheyta, J .
CATALYSIS TODAY, 2004, 98 (1-2) :91-98
[5]   Effect of Mg addition on the structure and performance of sulfide Mo/Al2O3 in HDS and HDN reaction [J].
Chen, Wenbin ;
Nie, Hong ;
Li, Dadong ;
Long, Xiangyun ;
van Gestel, Jacob ;
Mauge, Francoise .
JOURNAL OF CATALYSIS, 2016, 344 :420-433
[6]   Alumina-supported cobalt-molybdenum sulfide modified by tin via surface organometallic chemistry:: application to the simultaneous hydrodesulfurization of thiophenic compounds and the hydrogenation of olefins [J].
Choi, JS ;
Maugé, F ;
Pichon, C ;
Olivier-Fourcade, J ;
Jumas, JC ;
Petit-Clair, C ;
Uzio, D .
APPLIED CATALYSIS A-GENERAL, 2004, 267 (1-2) :203-216
[7]   STUDIES ON MOLYBDENA-ALUMINA CATALYSTS .7. EFFECT OF COBALT ON CATALYST STATES AND REDUCIBILITY [J].
CHUNG, KS ;
MASSOTH, FE .
JOURNAL OF CATALYSIS, 1980, 64 (02) :320-331
[8]  
Cordero RL, 2000, APPL CATAL A-GEN, V202, P23
[9]   Glycerol steam reforming over Ni/γ-Al2O3 catalysts, modified with Mg(II). Effect of Mg (II) content [J].
Dieuzeide, M. L. ;
Jobbagy, M. ;
Amadeo, N. .
CATALYSIS TODAY, 2013, 213 :50-57
[10]   Synergisms between matrices and ZSM-5 in FCC gasoline non-hydrogenating upgrading catalysts [J].
Ding, Yihui ;
Liang, Jifeng ;
Fan, Yu ;
Wang, Yonggang ;
Bao, Xiaojun .
CATALYSIS TODAY, 2007, 125 (3-4) :178-184