Using hybrid neural networks in scaling up an FCC model from a pilot plant to an industrial unit

被引:46
作者
Bollas, GM
Papadokonstadakis, S
Michalopoulos, J
Arampatzis, G
Lappas, AA
Vasalos, IA
Lygeros, A
机构
[1] Natl Tech Univ Athens, Sch Chem Engn, GR-15780 Athens, Greece
[2] Ctr Res & Technol Hellas, CERTH, CPERI, Thermi 57001, Greece
关键词
fluid catalytic cracking; process modeling; neural networks; hybrid modeling; pilot to commercial unit scale up; riser hydrodynamics; FCC kinetics;
D O I
10.1016/S0255-2701(02)00206-4
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 ; 0820 ;
摘要
The scaling up of a pilot plant fluid catalytic cracking (FCC) model to an industrial unit with use of artificial neural networks is presented in this paper. FCC is one of the most important oil refinery processes. Due to its complexity the modeling of the FCC poses great challenge. The pilot plant model is capable of predicting the weight percent of conversion and coke yield of an FCC unit. This work is focused in determining the optimum hybrid approach, in order to improve the accuracy of the pilot plant model. Industrial data from a Greek petroleum refinery were used to develop and validate the models. The hybrid models developed are compared with the pilot plant model and a pure neural network model. The results show that the hybrid approach is able to increase the accuracy of prediction especially with data that is out of the model range. Furthermore, the hybrid models are easier to interpret and analyze. (C) 2003 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:697 / 713
页数:17
相关论文
共 31 条
[1]   Identification and control of a riser-type FCC unit using neural networks [J].
Alaradi, AA ;
Rohani, S .
COMPUTERS & CHEMICAL ENGINEERING, 2002, 26 (03) :401-421
[2]   DYNAMIC AND CONTROL OF FLUIDIZED CATALYTIC CRACKERS .1. MODELING OF THE CURRENT GENERATION OF FCCS [J].
ARBEL, A ;
HUANG, ZP ;
RINARD, IH ;
SHINNAR, R ;
SAPRE, AV .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (04) :1228-1243
[3]   DEVELOPMENT OF CATALYTIC CRACKING TECHNOLOGY - A LESSON IN CHEMICAL REACTOR DESIGN [J].
AVIDAN, AA ;
SHINNAR, R .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (06) :931-942
[4]   REACTION RATES IN CATALYTIC CRACKING OF PETROLEUM [J].
BLANDING, FH .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (06) :1186-1197
[5]   Modeling small-diameter FCC riser reactors. A hydrodynamic and kinetic approach [J].
Bollas, GM ;
Vasalos, IA ;
Lappas, AA ;
Iatridis, D .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (22) :5410-5419
[6]   Future directions in modelling the FCC process: An emphasis on product quality [J].
Christensen, G ;
Apelian, MR ;
Hickey, KJ ;
Jaffe, SB .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (13-14) :2753-2764
[7]   TOWARDS IMPROVED PENICILLIN FERMENTATION VIA ARTIFICIAL NEURAL NETWORKS [J].
DIMASSIMO, C ;
MONTAGUE, GA ;
WILLIS, MJ ;
THAM, MT ;
MORRIS, AJ .
COMPUTERS & CHEMICAL ENGINEERING, 1992, 16 (04) :283-291
[8]  
DIMITRIS CP, 1992, AICHE J, V38, P1499
[9]   Situating the high-density circulating fluidized bed [J].
Grace, JR ;
Issangya, AS ;
Bai, DR ;
Bi, HT ;
Zhu, JX .
AICHE JOURNAL, 1999, 45 (10) :2108-2116
[10]  
KRAMBECK FJ, 1991, MOB WORKSH CHEM REAC