Freeze drying process: real time model and optimization

被引:58
作者
Boss, EA [1 ]
Filho, RM [1 ]
de Toledo, ECV [1 ]
机构
[1] Univ Estadual Campinas, Fac Chem Engn, Chem Proc Dept, Lab Optimizat Design & Adv Control, BR-13081970 Campinas, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
freeze-drying; dynamic process; mathematical model; optimization;
D O I
10.1016/j.cep.2004.01.005
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
Freeze drying is a separation process based on the sublimation phenomenon. This process has the following advantages compared to the conventional drying process: the material structure is maintained, moisture is removed at low temperature (reduced transport rates), product stability during the storage is increased, the fast transition of the moisturized product to be dehydrated minimizes several degradation reactions. Freeze drying process has not been studied well enough. In order to put it to practice, a mathematical model based on fundamental mass and energy balance equations has been developed, based on a deterministic mathematical model proposed by Liapis and Sadikoglu [Drying Technol. 15 (3-4) (1997) 79 1], and used to calculate the amount of removed water and amount of residual water. The proposed model contains the freeze drying equations, which are solved by the orthogonal collocation and polynomial approximation-Jacobi method. The results show that the dynamic mathematical model represents well the process and is especially well suited for real time optimization. As a case study to illustrate the model utilization in a real time optimization procedure, the freeze drying process was optimized by the method of Successive Quadratic Programming (SQP) used for solution of non-linear equations, for skimmed milk and soluble coffee. The optimization procedure showed to be an important tool to improve the process performance since lower energy consumption and hence lower cost has been achieved to obtain the product with the same quality. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:1475 / 1485
页数:11
相关论文
共 7 条
[1]   DUSTY-GAS PARAMETERS OF ACTIVATED CARBON ABSORBENT PARTICLES [J].
GLOOR, PJ ;
CROSSER, OK ;
LIAPIS, AI .
CHEMICAL ENGINEERING COMMUNICATIONS, 1987, 59 (1-6) :95-105
[2]   Research and development needs and opportunities in freeze drying [J].
Liapis, AI ;
Pikal, MJ ;
Bruttini, R .
DRYING TECHNOLOGY, 1996, 14 (06) :1265-1300
[3]  
LICHTFIELDS RJ, 1979, CHEM ENG SCI, V34, P1085
[4]   AN ANALYSIS OF THE LYOPHILIZATION PROCESS USING A SORPTION-SUBLIMATION MODEL AND VARIOUS OPERATIONAL POLICIES [J].
MILLMAN, MJ ;
LIAPIS, AI ;
MARCHELLO, JM .
AICHE JOURNAL, 1985, 31 (10) :1594-1604
[5]  
PLACKETT RL, 1946, BIOMETRIKA 4, V33, P305, DOI [DOI 10.2307/2332195, DOI 10.1093/BIOMET/33.4.305]
[6]   Mathematical modelling of the primary and secondary drying stages of bulk solution freeze-drying in trays: Parameter estimation and model discrimination by comparison of theoretical results with experimental data [J].
Sadikoglu, H ;
Liapis, AI .
DRYING TECHNOLOGY, 1997, 15 (3-4) :791-810
[7]  
Schittkowski K., 1986, Annals of Operations Research, V5, P485, DOI 10.1007/BF02739235