Performance analysis and experimental study of heat-source tower solution regeneration

被引:32
作者
Liang, Caihua [1 ]
Wen, Xiantai [1 ]
Liu, Chengxing [1 ]
Zhang, Xiaosong [1 ]
机构
[1] Southeast Univ, Sch Energy & Environm, Nanjing, Jiangsu, Peoples R China
基金
中国国家自然科学基金;
关键词
Solution regeneration; Heat-source tower; Auxiliary heat source; Experiment; INTERNALLY COOLED/HEATED DEHUMIDIFIER/REGENERATOR; COOLING-TOWER; MASS-TRANSFER; LIQUID; RUWCT;
D O I
10.1016/j.enconman.2014.05.020
中图分类号
O414.1 [热力学];
学科分类号
摘要
By analyzing similarities and difference between the solution regeneration of a heat-source tower and desiccant solution regeneration, this paper points out that solution regeneration of a heat-source tower has the characteristics of small demands and that a regeneration rate is susceptible to outdoor ambient environments. A theoretical analysis is performed on the characteristics of a heat-source tower solution in different outdoor environments and different regeneration modes, and an experimental study is performed on variation rules of the solution regeneration rate of a cross-flow heat-source tower under different inlet parameters and operating parameters. The experimental results show that: in the operating regeneration mode, as the air volume was increased from 123 m(3) h(-1) to 550 m(3) h(-1), the system heat transfer amount increased from 0.42 kW to 0.78 kW, and the regeneration rate increased from 0.03 g s(-1) to 0.19 g s(-1). Increasing the solution flow may increase the system heat transfer amount; however, the regeneration rate decreased to a certain extent. In the regeneration mode when the system is idle, as the air volume was increased from 136 m3 h-1 to 541 m(3) h(-1), the regeneration rate increased from 0.03 g s(-1) to 0.1 g s(-1). The regeneration rate almost remained unchanged around 0.07 g s(-1) as the solution flow is increased. In the regeneration mode with auxiliary heat when the system is idle, increasing the air volume and increasing the solution flow required more auxiliary heat, thereby improving the solution regeneration rate. As the auxiliary heat was increased from 0.33 kW to 1.03 kW, the regeneration rate increased from 0.11 g s(-1) to 0.27 g s(-1). That is, increasing the auxiliary heat greatly improves the solution regeneration rate. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:596 / 602
页数:7
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