Performance analysis of a dual component generator-condenser of an absorption heat transformer for water desalination

被引:10
作者
Delgado-Gonzaga, J. [1 ]
Juarez-Romero, D. [1 ]
Saravanan, R. [2 ]
Marquez-Nolasco, A. [3 ]
Huicochea, A. [1 ]
Morales, L., I [4 ]
机构
[1] Univ Autonoma Estado Morelos, Ctr Invest Ingn & Ciencias Aplicadas, Cuernavaca 62209, Morelos, Mexico
[2] Anna Univ, Dept Mech Engn, R&AC Div, Chennai 600025, Tamil Nadu, India
[3] Tecnol Monterrey, Sch Engn & Sci, Ave Eugenio Garza Sada 2501, Monterrey 64849, NL, Mexico
[4] Univ Autonoma Estado Morelos, Escuela Estudios Super Xalostoc, Ayala 62715, Morelos, Mexico
关键词
Generator-condenser integration; LiBr-H2O generator dynamics; Helical heat exchange dynamics; Generator-condenser interaction; Generator-condenser heat transfer coefficients; LITHIUM BROMIDE SOLUTIONS; MASS-TRANSFER; TRANSFER COEFFICIENTS; PURIFICATION SYSTEMS; AMMONIA-WATER; INCREASE; COP;
D O I
10.1016/j.tsep.2020.100651
中图分类号
O414.1 [热力学];
学科分类号
摘要
The purpose of this work is to evaluate the behavior of a novel dual component: generator-condenser (GE-CO) applied to a single-stage absorption heat transformer for water desalination (SAHT-WD) by simple evaporation that operates with a LiBr-H2O mixture. The GE-CO consists of two sections located in the same shell, where desorption and condensation occur simultaneously. The evaluation has been divided into an experimental and a theoretical analysis. The experimental analysis is focused on determining the operating conditions that favor the performance of the GE-CO and the overall SAHT-WD. To estimate the heat transfer coefficients and wetting efficiencies based on the experimental results, a mathematical model that considers variation of the inlet absorption mixture stream, the refrigerant, the heating and cooling water was constructed. The results indicate a good coupling between the GE-CO and the AHT, with maximum values of COP and desalinated water flow of 0.49 and 3.91 x 10(-4) kg/s. The maximum specific desalination rate (SDR) of the AHT-WP was 1.10 x 10(-4) kg/s/kW. Both in the GE and CO, the heat transfers of the film of the absorbent mixture and the refrigerant respectively, limit the heat transfer process.
引用
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页数:15
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