First and second law multidimensional analysis of a triple absorption heat transformer (TAHT)

被引:34
作者
Donnellan, Philip [1 ]
Byrne, Edmond [1 ]
Oliveira, Jorge [1 ]
Cronin, Kevin [1 ]
机构
[1] Natl Univ Ireland Univ Coll Cork, Dept Proc & Chem Engn, Cork, Ireland
关键词
Absorption heat transformer; Triple stage heat transformer; Water-lithium bromide; Exergy analysis; Factorial analysis; WATER-PURIFICATION; SINGLE-STAGE; EXERGY ANALYSIS; WASTE HEAT; ENERGY; PERFORMANCE; INCREASE; SYSTEMS; DESIGN; BEHAVIOR;
D O I
10.1016/j.apenergy.2013.06.049
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
In this paper, a rigorous multi-dimensional analysis is conducted upon a triple absorption heat transformer (TAHT) using the working fluids water and lithium bromide (LiBr). A full factorial design is created which determines the most influential factors affecting the system's coefficient of performance (COP), exergetic coefficient of performance (ECOP), flow ratio (FR) and total exergy destruction (E-D). The aim is to draw general conclusions which may be adopted into any such TAHT cycle and not simply be specific to any one scenario. Accordingly the paper analyses the position of each variable across its thermodynamically available range instead of the traditional selection of arbitrary temperatures. It is found that in general the condensation temperature and the pinch heat transfer gradient selected have the greatest effect, and that these should be minimised in all situations. There exist points of optimum for the temperatures of the two absorber-evaporators within the cycle, however the evaporation temperature has conflicting effects for different dependent variables, and must therefore be selected based on an economic analysis. The results of this study also show that the generator is the source of the largest exergy destruction in the cycle, followed by the two absorber-evaporators. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:141 / 151
页数:11
相关论文
共 36 条
[1]   DESIGN AND EXPERIMENTAL PERFORMANCE EVALUATION OF AN ABSORPTION HEAT TRANSFORMER WITH SELF-CIRCULATION [J].
ABRAHAMSSON, K ;
GIDNER, A ;
JERNQVIST, A .
HEAT RECOVERY SYSTEMS & CHP, 1995, 15 (03) :257-272
[2]  
Abrahamsson K, 1997, INT J ENERG RES, V21, P631
[3]  
Cabin RJ, 2000, Bulletin of the ecological society of America, V81, P246
[4]   Optimal operation conditions for a single-stage heat transformer by means of an artificial neural network inverse [J].
Colorado, D. ;
Hernandez, J. A. ;
Rivera, W. ;
Martinez, H. ;
Juarez, D. .
APPLIED ENERGY, 2011, 88 (04) :1281-1290
[5]   Error propagation on COP prediction by artificial neural network in a water purification system integrated to an absorption heat transformer [J].
Colorado, D. ;
Hernandez, J. A. ;
El Hamzaoui, Y. ;
Bassam, A. ;
Siqueiros, J. ;
Andaverde, J. .
RENEWABLE ENERGY, 2011, 36 (05) :1315-1322
[6]   Exergetic and exergoeconomic optimization of a cogeneration pulp and paper mill plant including the use of a heat transformer [J].
Cortes, E. ;
Rivera, W. .
ENERGY, 2010, 35 (03) :1289-1299
[7]   Integration of absorption heat pumps in a Kraft pulp process for enhanced energy efficiency [J].
Costa, Andrea ;
Bakhtiari, Bahador ;
Schuster, Sebastian ;
Paris, Jean .
ENERGY, 2009, 34 (03) :254-260
[8]  
Design Institute for Physical Properties, 2012, DIPPR PROJ 801 FULL
[9]  
DONG F, 1993, STAT SINICA, V3, P209
[10]   Comparison of energy, exergy, and entropy balance methods for analysing double-stage absorption heat transformer cycles [J].
Fartaj, SA .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2004, 28 (14) :1219-1230