Design of a software application for the simulation and control of continuous and batch crystallizer circuits

被引:1
作者
Bennett, MK [1 ]
Rohani, S [1 ]
机构
[1] Univ Western Ontario, Fac Engn Sci, Dept Chem & Biochem Engn, London, ON N6A 5B9, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
object oriented programming; graphical user interface; dynamic simulation; industrial crystallizers; batch; continuous; single and multiple effect;
D O I
10.1016/S0965-9978(02)00022-4
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
A computer application was developed for the simulation of industrial crystallizers, including the draft-tube baffled, forced-circulation, and Oslo crystallizers. The application enables the design and control of single and multiple effect, batch and continuous crystallizer circuits. C++ classes that dynamically simulate several batch and continuous industrial crystallizers, auxiliary vessels such as mixers and pumps, and controllers, are coupled with a graphical user interface. The flowsheet-style interface facilitates the configuration and interconnection of various components. Graphs for the dynamic display of simulation data were created and an example simulation illustrates the use of the program. (C) 2002 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:365 / 374
页数:10
相关论文
共 14 条
[1]  
Bennett AK, 2001, CHEM ENG SCI, V56, P6623
[2]  
BENNETT RC, 1993, HDB IND CRYSTALLIZAT
[3]   Influence of crystal habit on the compression and densification mechanism of ibuprofen [J].
Di Martino, P ;
Beccerica, M ;
Joiris, E ;
Palmieri, GF ;
Gayot, A ;
Martelli, S .
JOURNAL OF CRYSTAL GROWTH, 2002, 243 (02) :345-355
[4]   Effect of cooling mode on product crystal size in seeded batch crystallization of potassium alum [J].
Doki, N ;
Kubota, N ;
Sato, A ;
Yokota, M .
CHEMICAL ENGINEERING JOURNAL, 2001, 81 (1-3) :313-316
[5]   EVALUATION OF CRYSTAL-GROWTH KINETICS FROM A DESUPERSATURATION CURVE USING INITIAL DERIVATIVES [J].
GARSIDE, J ;
GIBILARO, LG ;
TAVARE, NS .
CHEMICAL ENGINEERING SCIENCE, 1982, 37 (11) :1625-1628
[6]   NUCLEATION, GROWTH, AND AGGREGATION RATES FROM STEADY-STATE EXPERIMENTAL-DATA [J].
HOUNSLOW, MJ .
AICHE JOURNAL, 1990, 36 (11) :1748-1752
[7]  
Jancic S., 1984, IND CRYSTALLIZATION
[8]   OPTIMAL OPERATION OF A BATCH COOLING CRYSTALLIZER [J].
JONES, AG .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (05) :1075-1087
[9]  
*OLI SYST TECHN IN, 2001, CRYSPII
[10]  
Ranodolph A., 1988, THEORY PARTICULATE P