Methane activation without using oxidants over supported Mo catalysts

被引:54
作者
Wong, ST [1 ]
Xu, YD [1 ]
Liu, W [1 ]
Wang, LS [1 ]
Guo, XX [1 ]
机构
[1] 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
methane activation; shape-selectivity; alkali metal doping;
D O I
10.1016/0926-860X(95)00260-X
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The catalytic properties of Mo/HSAPO-34, Mo/H-ZSM-5 and Mo/HY catalysts for methane conversion without using oxidants were compared. Mo/H-ZSM-5 catalyst has the best performance in terms of catalytic activity and stability. This catalyst is very selective for benzene production and the benzene yield is the highest of the three catalysts studied. The catalytic activity and benzene selectivity over the Mo/HSAPO-34 catalyst, however, decreased with increasing time on stream. As the catalyst deactivated, the selectivity to ethene increased. The Mo/HY catalyst is active for methane conversion but rapid deactivation of the catalyst resulted in negligible product yield. These results are discussed in terms of the shape-selectivity effect of the support taking into consideration the high reaction temperature. Preliminary studies on alkali metal doped Mo/HSAPO-34 catalysts showed no observed effect on catalyst deactivation.
引用
收藏
页码:7 / 17
页数:11
相关论文
共 15 条
[1]   INSITU SOLID-STATE NMR-STUDIES OF THE CATALYTIC CONVERSION OF METHANOL ON THE MOLECULAR-SIEVE SAPO-34 [J].
ANDERSON, MW ;
SULIKOWSKI, B ;
BARRIE, PJ ;
KLINOWSKI, J .
JOURNAL OF PHYSICAL CHEMISTRY, 1990, 94 (07) :2730-2734
[2]  
Breck D.W, 1974, ZEOLITE MOL SIEVES
[3]   HYDROCARBONS FROM METHANOL [J].
CHANG, CD .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1983, 25 (01) :1-118
[4]   ON THE REACTION-MECHANISM FOR HYDROCARBON FORMATION FROM METHANOL OVER SAPO-34 .1. ISOTOPIC LABELING STUDIES OF THE CO-REACTION OF ETHENE AND METHANOL [J].
DAHL, IM ;
KOLBOE, S .
JOURNAL OF CATALYSIS, 1994, 149 (02) :458-464
[5]   THERMAL-DESORPTION OF C6-C9N-ALKENES FROM THE SURFACE OF ZEOLITE HY [J].
JASRA, RV ;
BHATT, BD ;
GARG, VN ;
BHAT, SGT .
APPLIED CATALYSIS, 1988, 39 (1-2) :49-60
[6]   OXIDATIVE COUPLING OF METHANE TO HIGHER HYDROCARBONS [J].
LEE, JS ;
OYAMA, ST .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1988, 30 (02) :249-280
[7]  
Meier W. M., 1978, ATLAS ZEOLITE STRUCT
[8]   EFFECT OF HEAT-TREATMENT ON THE CHARACTER OF COKE DEPOSITED ON HZSM-5 AND HY ZEOLITES IN ACETONE CONVERSION [J].
NOVAKOVA, J ;
KUBELKOVA, L ;
BOSACEK, V ;
MACH, K .
ZEOLITES, 1991, 11 (02) :135-141
[9]   HYDROGEN CHEMISORPTION ON POTASSIUM-PROMOTED SUPPORTED RUTHENIUM CATALYSTS [J].
UNER, DO ;
PRUSKI, M ;
GERSTEIN, BC ;
KING, TS .
JOURNAL OF CATALYSIS, 1994, 146 (02) :530-536
[10]  
Wang D., 1992, CHINESE J CATAL, V13, P234