Effects of light rare earth on acidity and catalytic performance of HZSM-5 zeolite for catalytic cracking of butane to light olefins

被引:0
作者
Wang Xiaoning [1 ]
Zhao Zhen [1 ]
Xu Chunming [1 ]
Duan Aijun [1 ]
Zhang Li [1 ]
Jiang Guiyuan [1 ]
机构
[1] China Univ Petroleum, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
基金
中国国家自然科学基金;
关键词
light rare earth; HZSM-5; zeolite; catalytic cracking; butane; acidity;
D O I
10.1016/S1002-0721(07)60430-X
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The effects of rare earth (RE) on the structure, acidity, and catalytic performance of HZSM-5 zeolite were investigated. A series of RE/HZSM-5 catalysts, containing 7.54 % RE (RE = La, Ce, Pr, Nd, Sm, Eu or Gd), were prepared by the imp regriation of the ZSM-5 type zeolites (Si/Al = 64:1) with the corresponding RE nitrate aqueous solutions. The catalysts were characterized by means of FT-IR, UV-Vis, NH3-TPD, and IR spectroscopy of adsorbed pyridine. The catalytic performances of the RE/HZSM-5 for the catalytic cracking of mixed butane to light olefins were also measured with a fixed bed microreactor. The results revealed that the addition of light rare earth metal on the HZSM-5 catalyst greatly enhanced the selectivity to olefins, especially to propylene, thus increasing the total yield of olefins in the catalytic cracking of butane. Amongthe RE-modified HZSM-5 samples, Ce/HZSM-5 gave the highest yield of total olefins, and Nd/HZSM-5 gave the highest yield of propene at a reaction temperature of 600 degrees C. The presence of rare earth metal on the HZSM-5 sample, not only modified the acidic properties of HZSM-5 including the amount of acid sites and acid type, that is, the ratio of L/B (Lewis acid/Bronsted acid), but also altered the basic properties of it, which in turn promoted the catalytic performance of HZSM-5 for the catalytic cracking of butane.
引用
收藏
页码:321 / 328
页数:8
相关论文
共 20 条
[1]  
AOLEWUYI YG, 1995, APPL CATAL A-GEN, V131, P121
[2]  
Argauer R.J., 1972, US Pat., Patent No. [3702886, US3702886A]
[3]   Spectroscopic characterization of the acid properties of metal oxide catalysts [J].
Busca, G .
CATALYSIS TODAY, 1998, 41 (1-3) :191-206
[4]   DETERMINATION OF INTEGRATED MOLAR EXTINCTION COEFFICIENTS FOR INFRARED-ABSORPTION BANDS OF PYRIDINE ADSORBED ON SOLID ACID CATALYSTS [J].
EMEIS, CA .
JOURNAL OF CATALYSIS, 1993, 141 (02) :347-354
[5]   Enhanced para-selectivity by selective coking during toluene disproportionation over H-ZSM-5 zeolite [J].
Fang, LY ;
Liu, SB ;
Wang, I .
JOURNAL OF CATALYSIS, 1999, 185 (01) :33-42
[6]   Modified zeolites as catalysts in the Friedel-Crafts acylation [J].
Gaare, K ;
Akporiaye, D .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 1996, 109 (02) :177-187
[7]   LANTHANUM ION-EXCHANGE ON H-ZSM-5 [J].
HARTFORD, RW ;
KOJIMA, M ;
OCONNOR, CT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (12) :1748-1752
[8]   A highly efficient catalytic C4 alkane cracking over zeolite ZSM-23 [J].
Ji, D ;
Wang, B ;
Qian, G ;
Gao, Q ;
Lü, GM ;
Yan, L ;
Suo, JS .
CATALYSIS COMMUNICATIONS, 2005, 6 (04) :297-300
[9]  
Li B, 2005, CHINESE J CATAL, V26, P301
[10]   FeHZSM-5 molecular sieves - Highly active catalysts for catalytic cracking of isobutane to produce ethylene and propylene [J].
Lu, JY ;
Zhao, Z ;
Xu, CM ;
Zhang, P ;
Duan, AJ .
CATALYSIS COMMUNICATIONS, 2006, 7 (04) :199-203