Experimental investigation and parametric analysis of a solar thermal dish collector with spiral absorber

被引:66
|
作者
Pavlovic, Sasa [1 ]
Bellos, Evangelos [2 ]
Le Roux, Willem G. [3 ]
Stefanovic, Velimir [1 ]
Tzivanidis, Christos [2 ]
机构
[1] Univ Nis, Dept Energet & Proc Tech, Fac Mech Engn, Nish, Serbia
[2] Natl Tech Univ Athens, Dept Mech Engn, Heroon Polytech 9, Athens 15780, Greece
[3] Univ Pretoria, Dept Mech & Aeronaut Engn, Pretoria, South Africa
关键词
Dish; Exergetic efficiency; Solar collector; Spiral; Absorber; PERFORMANCE ASSESSMENT; FINANCIAL EVALUATION; OPTICAL-PERFORMANCE; PARABOLIC DISH; OPTIMIZATION; CAVITY; EFFICIENCY; RECEIVER; EXERGY; SYSTEM;
D O I
10.1016/j.applthermaleng.2017.04.068
中图分类号
O414.1 [热力学];
学科分类号
摘要
Solar-tracking dish collectors are a potential alternative to fossil fuels because of their high concentration ratios. Important considerations for solar collectors are manufacturing costs, complexity, efficiency, uniform flux distribution and working fluid selection. In this study, a simple, low-cost solar dish collector with a spiral absorber and lightweight structure is examined. Experiments were performed with water as working fluid where the volumetric flow rate, inlet and outlet temperatures, ambient temperature, air velocity and solar irradiation were measured. Experimental results were used to validate a numerical model developed in Engineering Equation Solver, where three working fluids (water, thermal oil and air) were considered in various operating conditions. According to the thermal analysis, water is the most appropriate working fluid for low-temperature applications and thermal oil the most appropriate for higher-temperature applications. The exergetic analysis, however, shows that air is the most appropriate for low-temperature applications and thermal oil the most appropriate for higher-temperature applications. The highest exergetic efficiency was observed for thermal oil with inlet temperature of 155 degrees C. The system can be feasible in areas with solar potential of more than 1600 kW h/m(2) and where the cost of heating is more than 0.15 E/kW h. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:126 / 135
页数:10
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