Novel equipment for testing catalytic cracking and catalyst regeneration with short contact times

被引:12
作者
Lipiäinen, K
Hagelberg, P
Aittamaa, J
Eilos, I
Hiltunen, J
Niemi, VM
Krause, AOI
机构
[1] Fortum Oil & Gas Oy, FIN-06101 Porvoo, Finland
[2] Helsinki Univ Technol, Dept Chem Technol, FIN-02015 Helsinki, Finland
关键词
catalytic cracking; catalyst regeneration; pulse reactor; short contact time;
D O I
10.1016/S0926-860X(99)00079-4
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
A new piece of equipment was developed for testing catalytic cracking and catalyst regeneration, particularly for short contact times. The gas oil to be cracked is injected into the upper section of the reactor, which can be operated in the temperature range 400-800 degrees C, catalyst-to-oil ratios from 0 to 300 g(cat)/g(oil) and residence times between 0.01 and 2.3 s. The product is led directly into the analysis section where hydrocarbons from C-1 to C-12 (in total 350 compounds) are separated by a capillary column. In catalyst regeneration studies oxygen/nitrogen pulses are fed into the reactor via a gas-loop. The carbon monoxide and carbon dioxide formed are first separated in a packed column after which they are converted to methane by hydrogen on a Ni/gamma-Al2O3 catalyst ensuring the determination of even small amounts of coke. The reproducibility of the experiments has proved to be excellent. With this new reactor system, accurate information can be obtained on the initial activity of the catalyst and product distribution. (C) 1999 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:411 / 421
页数:11
相关论文
共 16 条
[1]  
ANDERSON PC, 1972, J I PETROL, V58, P83
[2]   KINETIC INVESTIGATION OF COMPLEX PSEUDO MASS-ACTION SYSTEMS BY USE OF THE PULSE METHOD [J].
CHRISTOFFEL, EG ;
SURJO, IT ;
ROBSCHLAGER, KH .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1980, 58 (04) :513-516
[3]   MODELING THE KINETICS OF FAST CATALYTIC CRACKING REACTIONS [J].
COLLYER, R ;
LAROCCA, M ;
DELASA, H .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1989, 67 (06) :955-962
[4]   KINETICS OF VACUUM GAS OIL CRACKING ON A ZEOLITIC CATALYST [J].
COOPMANS, JF ;
MARS, P ;
DEGROOT, RL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1992, 31 (09) :2093-2103
[5]   FLUID CATALYTIC CRACKING - SELECTIVITY AND PRODUCT YIELD PATTERNS [J].
HARI, C ;
BALARAMAN, KS ;
BALAKRISHNAN, AR .
CHEMICAL ENGINEERING & TECHNOLOGY, 1995, 18 (05) :364-369
[6]   SIMULTANEOUS MEASUREMENT OF ADSORPTION, REACTION, AND COKE USING A PULSED MICROBALANCE REACTOR [J].
HERSHKOWITZ, F ;
MADIARA, PD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (12) :2969-2974
[7]   CATALYTIC CRACKING OF HEAVY OILS IN COMBINATION WITH PYROLYSIS FOR THE PRODUCTION OF LIGHT OILS [J].
ITOH, M ;
SUZUKI, T ;
TSUJIMOTO, Y ;
TAKEGAMI, Y ;
WATANABE, Y .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1984, 23 (03) :622-625
[8]   FAST CATALYTIC CRACKING OF HEAVY GAS OILS - MODELING COKE DEACTIVATION [J].
LAROCCA, M ;
NG, S ;
DELASA, H .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (02) :171-180
[9]  
Niccum P. K., 1998, NPRA ANN M SAN FRANC
[10]   A novel test method for cracking catalysts [J].
Nokkosmaki, MI ;
Kuoppala, ET ;
Leppamaki, EA ;
Krause, AOI .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1998, 44 (02) :193-204