Stochastic axial dispersion model for tubular equipment

被引:2
作者
Nakama, C. S. M. [1 ]
Siqueira, A. F. [2 ]
Vianna, A. S., Jr. [1 ]
机构
[1] Univ Sao Paulo, Escola Politecn, Dept Engn Quim, Sao Paulo, Brazil
[2] Univ Sao Paulo, Escola Engn Lorena, Dept Ciencias Basicas & Ambientais, Sao Paulo, Brazil
关键词
Stochastic modeling; Simulation; Axial dispersion model; Milli-reactor fluid dynamics; RESIDENCE TIME DISTRIBUTION; RANDOM-WALK SIMULATION; POROUS-MEDIA; FLOW; DISTRIBUTIONS; REACTORS;
D O I
10.1016/j.ces.2017.05.024
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A stochastic model based on the axial dispersion model was proposed for the mathematical representation of the fluid dynamics of tubular equipment with irregular behavior. The differential equation was built by inserting randomness in the dispersion coefficient, which added a stochastic term to the model. This term was capable of simulating fluctuations that may arise in the characterization of tubular equipment using the stimulus-response technique. The model was validated by comparing sample paths and computational confidence intervals with three experimental data sets of a tubular milli-reactor for polystyrene production with different configurations. A convergence analysis was carried out in order to determine the number of elements needed for time discretization. An estimator function was developed to calculate the parameter of the stochastic term, while the parameter of the deterministic term was estimated by the least squares method. The stochastic differential equation was discretized and solved by the Euler-Maruyama method. The computational confidence intervals were calculated using the Monte Carlo method. The results were considered satisfactory, once the model was capable of representing the irregular fluid dynamics of a tubular reactor. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:131 / 138
页数:8
相关论文
共 29 条
[1]   Hydrodynamics and residence time distribution of liquid flow in tubular reactors equipped with screen-type static mixers [J].
Abou Hweij, K. ;
Azizi, F. .
CHEMICAL ENGINEERING JOURNAL, 2015, 279 :948-963
[2]  
[Anonymous], 1998, CHEM REACTION ENG, DOI DOI 10.1002/AIC.690190143
[3]  
[Anonymous], 1997, HDB STOCHASTIC METHO
[4]   Low-dimensional models for describing mixing effects in laminar flow tubular reactors [J].
Chakraborty, S ;
Balakotaiah, V .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (13) :2545-2564
[5]  
Chen Z., 2012, J MATH CHEM, P451
[6]   CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES [J].
DANCKWERTS, PV .
CHEMICAL ENGINEERING SCIENCE, 1953, 2 (01) :1-13
[7]   Modeling ion channel dynamics through reflected stochastic differential equations [J].
Dangerfield, Ciara E. ;
Kay, David ;
Burrage, Kevin .
PHYSICAL REVIEW E, 2012, 85 (05)
[8]   STOCHASTIC MODELING OF TRANSIENT RESIDENCE-TIME DISTRIBUTIONS DURING START-UP [J].
FAN, LT ;
SHEN, BC ;
CHOU, ST .
CHEMICAL ENGINEERING SCIENCE, 1995, 50 (02) :211-221
[9]   Random walk simulation of miscible flow through heterogeneous 2D porous media considering dispersion tensor [J].
Fayazi, Amir ;
Ghazanfari, Mohammad Hossein .
CHEMICAL ENGINEERING SCIENCE, 2015, 132 :81-92
[10]  
Gaines J.G., 1995, STOCHASTIC PARTIAL D, P55