Hydrocracking of aromatic hydrocarbons over USY-zeolite

被引:72
作者
Chareonpanich, M [1 ]
Zhang, ZG [1 ]
Tomita, A [1 ]
机构
[1] TOHOKU UNIV,INST CHEM REACT SCI,SENDAI,MIYAGI 98077,JAPAN
关键词
D O I
10.1021/ef950238m
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 [动力工程及工程热物理]; 0820 [石油与天然气工程];
摘要
Hydrocracking of 1-butylbenzene, tetralin, diphenylmethane, naphthalene, l-methylnaphthalene, 9,10-dihydroanthracene, anthracene, and phenanthrene was investigated at 400, 500, and 600 degrees C under 5 MPa of hydrogen pressure. With metal-free ultrastable Y-zeolite catalyst and at a severe cracking temperature of 600 degrees C, accumulated yields of benzene, toluene, and xylene (BTX) and C-1-C-3 hydrocarbon gases were nearly 100%. The formation of tar and coke was almost negligible. On the basis of the product distribution pattern, the reaction pathways leading to BTX and light gases were postulated. The reaction for diphenylmethane, n-butylbenzene, and tetralin was initiated by the hydrocracking of a C-C single bond, whereas for other compounds the hydrogenation of the aromatic ring was the initial step followed by the hydrocracking reaction. Even in the case of l-methylnaphthalene, the hydrogenation of the aromatic ring preceded the hydrocracking of the methyl group. The hydrocracking of anthracene and phenanthrene was likely to proceed via the cracking at the outer ring.
引用
收藏
页码:927 / 931
页数:5
相关论文
共 27 条
[1]
HYDROGENATION AND HYDROCRACKING OF A MODEL LIGHT CYCLE OIL FEED .1. PROPERTIES OF A SULFIDED NIMO HYDROTREATING CATALYST [J].
BOUCHY, M ;
DUFRESNE, P ;
KASZTELAN, S .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1992, 31 (12) :2661-2669
[2]
SELECTIVE PRODUCTION OF BTX BY HYDROCRACKING OF COAL VOLATILE MATTER OVER ZEOLITE CATALYST [J].
CHAREONPANICH, M ;
TOMITA, A ;
NISHIJIMA, A .
ENERGY & FUELS, 1994, 8 (06) :1522-1523
[3]
EFFECT OF CATALYSTS ON YIELDS OF MONOCYCLIC AROMATIC-HYDROCARBONS IN HYDROCRACKING OF COAL VOLATILE MATTER [J].
CHAREONPANICH, M ;
ZHANG, ZG ;
NISHIJIMA, A ;
TOMITA, A .
FUEL, 1995, 74 (11) :1636-1640
[4]
CATALYTIC HYDROCRACKING REACTION OF NASCENT COAL VOLATILE MATTER UNDER HIGH-PRESSURE [J].
CHAREONPANICH, M ;
TAKEDA, T ;
YAMASHITA, H ;
TOMITA, A .
FUEL, 1994, 73 (05) :666-670
[5]
DYNAMIC MODIFICATION OF SURFACE ACID PROPERTIES WITH HYDROGEN MOLECULE FOR ZIRCONIUM-OXIDE PROMOTED BY PLATINUM AND SULFATE-IONS [J].
EBITANI, K ;
TSUJI, J ;
HATTORI, H ;
KITA, H .
JOURNAL OF CATALYSIS, 1992, 135 (02) :609-617
[6]
A MOLECULAR ORBITAL THEORY OF REACTIVITY IN AROMATIC HYDROCARBONS [J].
FUKUI, K ;
YONEZAWA, T ;
SHINGU, H .
JOURNAL OF CHEMICAL PHYSICS, 1952, 20 (04) :722-725
[7]
CHEMISTRY OF METHANE FORMATION IN HYDROGASIFICATION OF AROMATICS .1. NON-SUBSTITUTED AROMATICS [J].
GRABER, WD ;
HUTTINGER, KJ .
FUEL, 1982, 61 (06) :499-504
[8]
CATALYTIC CRACKING OF A HYDROCARBON MIXTURE ON COMBINATIONS OF HY AND HZSM-5 ZEOLITES [J].
GUERZONI, FN ;
ABBOT, J .
JOURNAL OF CATALYSIS, 1993, 139 (01) :289-303
[9]
HYDROCRACKING POLYCYCLIC-HYDROCARBONS OVER A DUAL-FUNCTIONAL ZEOLITE (FAUJASITE)-BASED CATALYST [J].
HAYNES, HW ;
PARCHER, JF ;
HEIMER, NE .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1983, 22 (03) :401-409
[10]
HYDROGENATION OF MONONUCLEAR AROMATICS OVER A SULFIDED NIMO/AL2O3 CATALYST [J].
HO, TC .
ENERGY & FUELS, 1994, 8 (05) :1149-1151