Multitechnique characterization of coke produced during commercial resid FCC operation

被引:62
作者
Cerqueira, HS
Sievers, C
Joly, G
Magnoux, P
Lercher, JA
机构
[1] Petrobras SA, Ctr Pesquisas & Desenvolvimento Leopoldo A Miguez, Tecnol FCC Ilha Fundao, BR-21941598 Rio De Janeiro, Brazil
[2] Tech Univ Munich, Inst Tech Chem, D-85748 Garching, Germany
[3] Univ Poitiers, CNRS, UMR 6503, F-86022 Poitiers, France
关键词
D O I
10.1021/ie048963k
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The characterization of industrial coked resid fluid catalytic cracking (RFCC) catalysts is reported. The aim is to provide insight into the coke deposition on commercial resid fluid catalytic cracking catalysts sampled after the stripper of a commercial RFCC unit and to relate it to the potential process chemistry. Physicochemical techniques were used to characterize the used catalysts and the deposited coke. 95% of the coke was insoluble in CH2Cl2. This coke was located in the mesopores of the catalyst matrix. The results suggest the existence of domains of polyaromatic and heterogeneously distributed coke, in which saturated hydrocarbons are trapped. IR spectroscopy of adsorbed pyridine shows that the largest fraction of strong Bronsted acid sites is free after the catalyst has passed the stripper. The results indicate that for RFCC not the local deactivation of the acid sites but rather blocking of domains of the catalyst is the most important mode of deactivation after passing through the riser reactor.
引用
收藏
页码:2069 / 2077
页数:9
相关论文
共 57 条
[1]  
[Anonymous], STUD SURF SCI CATAL
[2]   Elementary reactions and intermediate species formed during the oxidative regeneration of spent fluid catalytic cracking catalysts [J].
Barth, JO ;
Jentys, A ;
Lercher, JA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (12) :3097-3104
[3]   On the nature of nitrogen-containing carbonaceous deposits on coked fluid catalytic cracking catalysts [J].
Barth, JO ;
Jentys, A ;
Lercher, JA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (10) :2368-2375
[4]   Characterization of coke on equilibrium fluid catalytic cracking catalysts by temperature-programmed oxidation [J].
Bayraktar, O ;
Kugler, EL .
APPLIED CATALYSIS A-GENERAL, 2002, 233 (1-2) :197-213
[5]   CATALYST DEACTIVATION BY ACTIVE-SITE COVERAGE AND PORE BLOCKAGE [J].
BEECKMAN, JW ;
FROMENT, GF .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1979, 18 (03) :245-256
[6]  
BEIRNAERT HC, 1994, STUD SURF SCI CATAL, V88, P97
[7]   CHARACTERIZATION OF ACID CATALYSTS BY MEANS OF MODEL REACTIONS .1. ACID STRENGTH NECESSARY FOR THE CATALYSIS OF VARIOUS HYDROCARBON REACTIONS [J].
BOURDILLON, G ;
GUEGUEN, C ;
GUISNET, M .
APPLIED CATALYSIS, 1990, 61 (01) :123-139
[8]   Coke characterisation in aged residue hydrotreating catalysts by solid-state 13C-NMR spectroscopy and temperature-programmed oxidation [J].
Callejas, MA ;
Martínez, MT ;
Blasco, T ;
Sastre, E .
APPLIED CATALYSIS A-GENERAL, 2001, 218 (1-2) :181-188
[9]   Influence of coke on the acid properties of a USHY zeolite [J].
Cerqueira, HS ;
Ayrault, P ;
Datka, J ;
Guisnet, M .
MICROPOROUS AND MESOPOROUS MATERIALS, 2000, 38 (2-3) :197-205
[10]   m-xylene transformation over a USHY zeolite at 523 and 723 K:: Influence of coke deposits on activity, acidity, and porosity [J].
Cerqueira, HS ;
Ayrault, P ;
Datka, J ;
Magnoux, P ;
Guisnet, M .
JOURNAL OF CATALYSIS, 2000, 196 (01) :149-157