Simulation of heat integrated multiple effect evaporator system

被引:31
作者
Jyoti, Ghoshna [1 ]
Khanam, Shabina [2 ]
机构
[1] Natl Inst Technol, Dept Chem Engn, Rourkela 769008, Orissa, India
[2] Indian Inst Technol, Dept Chem Engn, Roorkee 247667, Uttar Pradesh, India
关键词
Multiple effect evaporators; Condensate flashing; Vapor bleeding; Pinch analysis; Optimization; SELECTION;
D O I
10.1016/j.ijthermalsci.2013.08.016
中图分类号
O414.1 [热力学];
学科分类号
摘要
In the present work a number of configurations and difficulties of MEE system such as condensate flashing, vapor bleeding, steam splitting, preheating of liquor using condensate, variable physical properties and boiling point rise are taken into consideration to analyze the evaporation system. For this purpose seven effect evaporator system of a typical Indian pulp and paper industry is considered. The model developed is a set of nonlinear algebraic equations that include total and solute mass balances, energy balances, heat transfer rate equations, and the composition and temperature dependence of thermodynamic properties such as vapor pressures and enthalpies. The model is solved using nonlinear equation solver. Economic evaluation to optimize the number of flash tanks is carried out for seven effect evaporator system. The two different types of configurations of vapor bleeding are considered and compared. Considering optimum number of flash tanks and best configuration of vapor bleeding, a system is designed. Further, a modified system is found considering optimum number of flash tanks and preheating of liquor using condensate. This modified design enhances the steam economy by 23.77% and reduces the steam consumption by 36.76% in comparison to base case and thus, it is selected as optimum design. Finally, Pinch analysis of the MEE network has also been carried out and it is found that predicted results are compared well with base case. (C) 2013 Elsevier Masson SAS. All rights reserved.
引用
收藏
页码:110 / 117
页数:8
相关论文
共 23 条
[1]  
Agarwal V.K., 2004, CHEM ENG WORLD, V39, P76
[2]   Selection of optimal feed flow sequence for a multiple effect evaporator system [J].
Bhargava, R. ;
Khanam, S. ;
Mohanty, B. ;
Ray, A. K. .
COMPUTERS & CHEMICAL ENGINEERING, 2008, 32 (10) :2203-2216
[3]  
BREMFORD DJ, 1994, APPITA J, V47, P320
[4]   Chemical process simulation for minimizing energy consumption in pulp mills [J].
Cardoso, Marcelo ;
de Oliveira, Katia Dionisio ;
Avelar Costa, George Alberto ;
Passos, Maria Laura .
APPLIED ENERGY, 2009, 86 (01) :45-51
[5]  
El-Dessouky H, 1998, CHEM ENG TECHNOL, V21, P437, DOI 10.1002/(SICI)1521-4125(199805)21:5<437::AID-CEAT437>3.0.CO
[6]  
2-D
[7]   Multiple effect evaporation - Vapour compression desalination processes [J].
El-Dessouky, HT ;
Ettouney, HM ;
Al-Juwayhel, F .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2000, 78 (A4) :662-676
[8]   Selection of optimum configuration for multiple effect evaporator system [J].
Gautami, G. ;
Khanam, S. .
DESALINATION, 2012, 288 :16-23
[9]   Simultaneous re-design and scheduling of multiple effect evaporator systems [J].
Heluane, Humberto ;
Blanco, Anibal M. ;
Rosa Hernandez, Maria ;
Alberto Bandoni, J. .
COMPUTERS & OPERATIONS RESEARCH, 2012, 39 (05) :1173-1186
[10]   Thermal integration of multiple effect evaporator in sugar plant [J].
Higa, M. ;
Freitas, A. J. ;
Bannwart, A. C. ;
Zemp, R. J. .
APPLIED THERMAL ENGINEERING, 2009, 29 (2-3) :515-522