A Novel Approach for Detailed Modeling and Optimization To Improve Energy Saving in Multiple Effect Evaporator Systems

被引:7
作者
Bo, Di [1 ]
Yang, Kunru [1 ]
Xie, Qingsong [1 ]
He, Chang [1 ]
Zhang, Bingjian [1 ]
Chen, Qinglin [1 ]
Qi, Zhiwen [1 ]
Ren, Jingzheng [2 ]
Pan, Ming [1 ]
机构
[1] Sun Yat Sen Univ, Sch Chem Engn & Technol, Guangzhou 510275, Guangdong, Peoples R China
[2] Hong Kong Polytech Univ, Dept Ind & Syst Engn, Hong Kong, Peoples R China
基金
中国国家自然科学基金;
关键词
HEAT-EXCHANGER NETWORKS; TRANSFER INTENSIFICATION; SIMULATION; INTEGRATION; EFFICIENCY; SELECTION; PULP;
D O I
10.1021/acs.iecr.9b00449
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The multiple effect evaporator (MEE) system is a typical process for liquor concentration in the energy-intensive industries. Many approaches and commercial software have been widely used for MEE simulation and optimization. However, the existing work usually assumes simplified correlations for material thermodynamic properties and evaporator operations to avoid computational complexity, which may cause a large deviation in results. This Article addresses accurate and detailed unit operations and material properties to model the MEE systems and further heat integration for optimal energy recovery. To deal with the resulting complex mixed integer nonlinear programming (MINLP) problems of MEE systems, an efficient optimization strategy is developed, where the noncritical variables in the MINLP model are initialized as parameters and updated by solving a series of mixed integer linear programming (MILP) problems using a two-stage iterative procedure. An industrial scale problem for concentrating black liquor in a Chinese paper mill is carried out to demonstrate the validity and efficiency of the new approach. On the basis of the conditions of constant heat-transfer coefficients and stream boiling point rises assumed in the well-known commercial software WinGEMS, our method performs identically to WinGEMS in five distinct scenarios. Moreover, our method is more capable of solving industrial problems in practical situations including varying stream thermal properties and evaporator heat-transfer coefficients, achieving up to 25% of energy conservation in a real-world case.
引用
收藏
页码:6613 / 6625
页数:13
相关论文
共 30 条
[1]  
[Anonymous], P 11 C PROC INT MOD
[2]  
[Anonymous], 2009, EN TECHN TRANS IND S, DOI DOI 10.1787/9789264068612-EN
[3]   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
[4]   Modeling and energy reduction of multiple effect evaporator system with thermal vapor compression [J].
Chen, Tianming ;
Ruan, Qi .
COMPUTERS & CHEMICAL ENGINEERING, 2016, 92 :204-215
[5]   Combining pinch and exergy analysis for process modifications [J].
Feng, X ;
Zhu, XX .
APPLIED THERMAL ENGINEERING, 1997, 17 (03) :249-261
[6]   Selection of optimum configuration for multiple effect evaporator system [J].
Gautami, G. ;
Khanam, S. .
DESALINATION, 2012, 288 :16-23
[7]   Indicators for industrial energy efficiency in India [J].
Gielen, Dolf ;
Taylor, Peter .
ENERGY, 2009, 34 (08) :962-969
[8]   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
[9]  
International Energy Agency (IEA), 2011, EN TRANS IND IND GLO
[10]   Simulation and energy optimization of a pulp and paper mill - Evaporation plant and digester [J].
Ji, Xiaoyan ;
Lundgren, Joakim ;
Wang, Chuan ;
Dahl, Jan ;
Grip, Carl-Erik .
APPLIED ENERGY, 2012, 97 :30-37