Feasibility analysis of a hot water solar system coupled to an absorption crossMark heat transformer

被引:7
|
作者
Ibarra-Bahena, J. [1 ]
Dehesa-Carrasco, U. [2 ]
Montiel-Gonzalez, M. [3 ]
Romero, R. J. [1 ]
Venegas-Reyes, E. [4 ]
机构
[1] Univ Autonoma Estado Morelos, Ctr Invest Ingn & Ciencias Aplicadas, Av Univ 1001, Cuernavaca 62209, Morelos, Mexico
[2] Inst Mexicano Tecnol Agua, Catedrat CONACyT, Paseo Cuauhnahuac 8532, Jiutepec 62550, Morelos, Mexico
[3] Univ Autonoma Estado Morelos, Fac Ciencias Quim & Ingn, Av Univ 1001, Cuernavaca 62209, Morelos, Mexico
[4] Ctr Invest Mat Avanzados CIMAV, Catedrat CONACyT, Victoria 147 Nte, Zona Ctr 34000, Durango, Mexico
关键词
Parabolic Trough Collectors; Absorption Heat Transformer; Thermal energy recovery; Water/Carrol mixture; SINGLE-STAGE; WASTE HEAT; PURIFICATION SYSTEM; COGENERATION SYSTEM; PRESSURE-DROP; GENERATOR; TEMPERATURE; DESALINATION; CYCLE; CONFIGURATIONS;
D O I
10.1016/j.applthermaleng.2016.05.140
中图分类号
O414.1 [热力学];
学科分类号
摘要
Parabolic Trough Collectors (PTC) provides thermal solar energy at medium temperature, and in order to increase the thermal level, the solar system can be coupled to upgrading-devices, such as Absorption Heat Transformers (AHT). In this paper, a feasibility analysis of the PTC system operating as thermal source of an AHT is described. The PTC and AHT units were tested and, based on the experimental data of each system, a heat transfer analysis was carried out in order to propose a single system. Two case studies were analysed: In the first, the evaporator temperature was close to the generator temperature (84.6 and 85.2 degrees C respectively) and a simultaneous flow from the heat source was used; in the second case, the evaporator temperature was lower than the generator temperature (79.6 and 86.7 degrees C respectively) and a serial flow from the heat source was proposed. Results show that, for the absorber temperature of 101 C, the calculated generator and evaporator heat loads were 1.50 and 1.34 kW respectively in Case 1, and 0.86 kW for both components in Case 2. For Case 1, the PTC system required 6.0 m(2) in order to provide two mass flows of 6.00 x 10(-02) and 535 x 10-02 kg/s for generator and evaporator at 89 C. For Case 2, one mass flow of 6.60 x 10(-02) kg/s at 89 C for generator and evaporator must be satisfied by a 3.7 m(2) PTC system. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1176 / 1185
页数:10
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