Sizing and selection of heat exchanger at defined saving-investment ratio

被引:12
作者
Agra, Ozden [1 ]
机构
[1] Yildiz Tech Univ, Dept Mech Engn, TR-34349 Istanbul, Turkey
关键词
Effectiveness; NTU; Heat exchangers; Economical optimization; Saving-investment ratio; GENETIC ALGORITHMS; DESIGN; OPTIMIZATION; COST;
D O I
10.1016/j.applthermaleng.2010.10.013
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this study, a new model was developed to determine the size and the best type of heat exchanger for waste-heat-recovery systems at desired saving-investment ratio. The savings investment ratio is obtained as a function of the three dimensionless numbers: effectiveness, Number of Transfer Units and investment to saving potential ratio which is a function of technical and economical parameters. Rearranging the saving-investment ratio relation and multiplying investment to saving potential ratio and saving-investment ratio, a new dimensionless number which is called saving effectiveness was obtained as a function of effectiveness and Number of Transfer Units. This second dimensionless number was plotted on effectiveness and Number of Transfer Units charts which are available in the literature. Heat exchanger size at desired saving-investment ratio can be determined from the obtained charts or the correlation given as table. When desired saving-investment ratio is given saving effectiveness can be calculated than the effectiveness and Number of Transfer Units values cart be read from the charts or calculated for all types of heat exchangers. Afterwards, investment cost and saving can also be calculated easily. The best heat exchanger type is determined by comparing savings of different heat exchanger types for the same saving-investment ratio value. In addition, the model is explained using two case studies. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:727 / 734
页数:8
相关论文
共 18 条
[1]   COST OPTIMUM HEAT-EXCHANGER NETWORKS .2. TARGETS AND DESIGN FOR DETAILED CAPITAL-COST MODELS [J].
AHMAD, S ;
LINNHOFF, B ;
SMITH, R .
COMPUTERS & CHEMICAL ENGINEERING, 1990, 14 (07) :751-767
[2]   Optimal geometry and flow arrangement for minimizing the cost of shell-and-tube condensers [J].
Allen, Benoit ;
Gosselin, Louis .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2008, 32 (10) :958-969
[3]   Heat exchanger design based on economic optimisation [J].
Caputo, Antonio C. ;
Pelagagge, Pacifico M. ;
Salini, Paolo .
APPLIED THERMAL ENGINEERING, 2008, 28 (10) :1151-1159
[4]   Heat exchanger optimization for geothermal district heating systems: A fuel saving approach [J].
Dagdas, Ahmet .
RENEWABLE ENERGY, 2007, 32 (06) :1020-1032
[5]   Design optimization of shell and tube heat exchangers using global sensitivity analysis and harmony search algorithm [J].
Fesanghary, M. ;
Damangir, E. ;
Soleimani, I. .
APPLIED THERMAL ENGINEERING, 2009, 29 (5-6) :1026-1031
[6]   Approximate design and costing methods for heat exchangers [J].
Hewitt, Geoff F. ;
Pugh, Simon J. .
HEAT TRANSFER ENGINEERING, 2007, 28 (02) :76-86
[7]  
Incropera F., 2007, FUNDAMENTALS HEAT MA, P670
[8]   Effectiveness-ntu computation with a mathematical model for cross-flow heat exchangers [J].
Navarro, H. A. ;
Cabezas-Gómez, L. C. .
BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, 2007, 24 (04) :509-521
[9]   A new approach for thermal performance calculation of cross-flow heat exchangers [J].
Navarro, HA ;
Cabezas-Gómez, L .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2005, 48 (18) :3880-3888
[10]  
Ponce JM, 2006, COMPUT-AIDED CHEM EN, V21, P985