UNIFIED CORRELATION FOR OVERALL GAS HOLD-UP IN BUBBLE COLUMN REACTORS FOR VARIOUS GAS-LIQUID SYSTEMS USING HYBRID GENETIC ALGORITHM-SUPPORT VECTOR REGRESSION TECHNIQUE

被引:14
作者
Gandhi, Ankit B. [1 ]
Joshi, Jyeshtharaj B. [1 ]
机构
[1] Inst Chem Technol, Bombay 400019, Maharashtra, India
关键词
bubble column reactor; overall gas hold-up; genetic algorithm; support vector regression; MASS-TRANSFER COEFFICIENT; NON-NEWTONIAN SOLUTIONS; HIGH-PRESSURE; INTERFACIAL AREA; FLOW CHARACTERISTICS; ELEVATED PRESSURES; HEAT-TRANSFER; SCALE-UP; PHASE; HYDRODYNAMICS;
D O I
10.1002/cjce.20296
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The objective of this study is to collect the data on overall gas hold-up (epsilon(G)) for bubble column reactors handling various gas-liquid systems and further develop a unified data-driven model for the estimation of the same. In this work, around 3300 experimental points for epsilon(G) have been collected from 85 open sources spanning the years 1963-2008. The data-driven model for overall gas hold-up has been established using hybrid Genetic Algorithm-Support Vector Regression (GA-SVR)-based methodology. In the present study, GA has been used for nonlinear rescaling of the parameters. These exponentially scaled parameters are subsequently subjected for SVR training. The technique is an extension of conventional SVR technique, showing relatively enhanced results. The proposed hybrid model is based on various prominent design and operating parameters (15 in number) which includes superficial gas velocity, superficial liquid velocity, gas density, molecular weight of gas, sparger type, sparger hole diameter, number of sparger holes, liquid viscosity, liquid density, liquid surface tension, ionic strength of liquid, operating temperature, operating pressure, liquid height, and the column diameter. The estimations made by the SVR-based unified model for epsilon(G) shows an excellent agreement with actual values with estimation accuracy of 98.5% and % AARE of 9.32%. For ease in applicability and ready reference of the practicing engineers, the hybrid GA-SVR-based model in the form of software and the entire database for epsilon(G) has been uploaded on the link www.esnips.com/web/UICT-NCL.
引用
收藏
页码:758 / 776
页数:19
相关论文
共 106 条
[1]   GAS HOLDUP AND VOLUMETRIC MASS-TRANSFER COEFFICIENT IN BUBBLE COLUMNS - EFFECTS OF LIQUID PROPERTIES [J].
AKITA, K ;
YOSHIDA, F .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1973, 12 (01) :76-80
[2]   Hydrodynamic studies in both bi-dimensional and three-dimensional bubble columns with a single sparger [J].
Anabtawi, MZA ;
Abu-Eishah, SI ;
Hilal, N ;
Nabhan, MBW .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2003, 42 (05) :403-408
[3]   Effect of liquid height on flow characteristics in bubble column using highly viscous liquid [J].
Bando, Y ;
Chaya, M ;
Hamano, S ;
Yasuda, K ;
Nakamura, M ;
Osada, K ;
Matsui, M .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2003, 36 (05) :523-529
[4]   Novel correlations for gas holdup in large-scale slurry bubble column reactors operating under elevated pressures and temperatures [J].
Behkish, A ;
Lemoine, R ;
Oukaci, R ;
Morsi, BI .
CHEMICAL ENGINEERING JOURNAL, 2006, 115 (03) :157-171
[5]  
BEHKISH A, 2005, INT J CHEM REACT ENG, V3, P1
[6]   GAS HOLDUP IN A BUBBLE COLUMN CONTAINING ORGANIC LIQUID MIXTURES [J].
BHAGA, D ;
PRUDEN, BB ;
WEBER, ME .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1971, 49 (03) :417-&
[7]   INFLUENCE OF COLUMN DIAMETER AND HIGH GAS THROUGHPUTS ON OPERATION OF A BUBBLE COLUMN [J].
BOTTON, R ;
COSSERAT, D ;
CHARPENTIER, JC .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1978, 16 (02) :107-115
[8]   MASS TRANSFER IN A SPARGED CONTACTOR .I. PHYSICAL MECHANISMS AND CONTROLLING PARAMETERS [J].
BRAULICK, WJ ;
FAIR, JR ;
LERNER, BJ .
AICHE JOURNAL, 1965, 11 (01) :73-&
[9]  
BUCHHOLZ R, 1983, GER CHEM ENG, V6, P105
[10]  
BUCHHOLZ R, 1978, GER CHEM ENG, V2, P105