Catalytic cracking of alkylbenzenes: Modeling the reaction pathways and mechanisms

被引:41
作者
Watson, BA
Klein, MT
Harding, RH
机构
[1] UNIV DELAWARE,DEPT CHEM ENGN,CTR CATALYT SCI & TECHNOL,NEWARK,DE 19716
[2] WR GRACE & CO CONN,COLUMBIA,MD 21044
关键词
fluid catalytic cracking; acid cracking; modeling; mechanism;
D O I
10.1016/S0926-860X(97)00122-1
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 cracking reaction pathways and mechanisms of 1-phenylhexane, 1-phenyloctane and 1-phenyldecane were studied. Experiments at 500 degrees C with a rare earth Y (REY) catalyst indicated that the dominant reactions included dealkylation and cracking in the alkyl side chain. To describe these results, a mechanistic model of the catalytic cracking of 1-phenyloctane was developed using a novel mechanism-based lumping scheme that exploits the chemical similarities within reaction families. The formal application of 17 reaction family matrices, which correspond to 15 reaction family classes, to the matrix representations of the reactants and derived products generated the model. The reaction family concept was further exploited to constrain the kinetics within each reaction family to follow a quantitative structure/reactivity Polanyi relationship. Ultimately, eight Polanyi relationship parameters, one catalyst specific parameter and three coking/deactivation parameters were optimized using experimental data. The resulting model correlations were excellent, as the overall parity between experimental and model values was y(Model)=0.00131+0.994y(Exp) with a correlation coefficient of 0.998.
引用
收藏
页码:13 / 39
页数:27
相关论文
共 30 条
[1]  
[Anonymous], 1992, THESIS U DELAWARE
[2]   THE DELPLOT TECHNIQUE - A NEW METHOD FOR REACTION PATHWAY ANALYSIS [J].
BHORE, NA ;
KLEIN, MT ;
BISCHOFF, KB .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (02) :313-316
[3]   COMPUTER-GENERATED PYROLYSIS MODELING - ON-THE-FLY GENERATION OF SPECIES, REACTIONS, AND RATES [J].
BROADBELT, LJ ;
STARK, SM ;
KLEIN, MT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1994, 33 (04) :790-799
[4]   CRACKING OF LONG-CHAIN ALKYL AROMATICS ON USY ZEOLITE CATALYSTS [J].
CORMA, A ;
MIGUEL, PJ ;
ORCHILLES, AV ;
KOERMER, GS .
JOURNAL OF CATALYSIS, 1992, 135 (01) :45-59
[5]   THE CATALYTIC CRACKING OF CUMENE [J].
CORMA, A ;
WOJCIECHOWSKI, BW .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1982, 24 (01) :1-65
[6]   ZEOLITE EFFECTS ON THE CRACKING OF LONG-CHAIN ALKYL AROMATICS [J].
CORMA, A ;
MIGUEL, PJ ;
ORCHILLES, AV ;
KOERMER, G .
JOURNAL OF CATALYSIS, 1994, 145 (01) :181-186
[7]  
Dumesic J.A., 1993, MICROKINETICS HETERO
[8]   Inertia and driving force of chemical reactions. [J].
Evans, MG ;
Polanyi, M .
TRANSACTIONS OF THE FARADAY SOCIETY, 1938, 34 (01) :0011-0023
[9]  
FROMENT GF, 1990, CHEM REACTOR ANAL
[10]  
Gates B. C, 1992, CATALYTIC CHEM