Experimental study of an ammonia loop heat pipe with a flat plate evaporator. (November 2016)

• Record Type: Journal Article
• Authors: Song, He; Zhi-chun, Liu; Jing, Zhao; Chi, Jiang; Jin-guo, Yang; Wei, Liu
• Is Part Of: International journal of heat and mass transfer. Volume 102(2016:Nov.)
• Page Start: 1050
• Page End: 1055
• Publication Date: 2016-11
• Subjects: Loop heat pipe -- Flat plate evaporator -- Secondary wick -- Biporous wick -- Thermal characteristics; Heat -- Transmission -- Periodicals; Mass transfer -- Periodicals; Chaleur -- Transmission -- Périodiques; Transfert de masse -- Périodiques; Electronic journals; 621.4022
• DOI: 10.1016/j.ijheatmasstransfer.2016.07.014
• Languages: English
• ISSNs: 0017-9310

Abstract

Highlights: An ammonia-304L stainless steel flat loop heat pipe with a secondary wick was designed, fabricated and tested. A new type structure for liquid-returning line was designed. The loop could start successfully and operated stably under heat load range from 20 W to 110 W. The system could rapidly respond to the heat load cycle. Abstract: In the present paper, the combination of a primary wick and a secondary wick was put forward and applied to the loop heat pipe. The evaporator was constructed from 304L stainless steel, and anhydrous ammonia with a purity of 99.995% was selected as the working fluid. A secondary wick made of 400-mesh stainless steel wire mesh was inserted into the evaporator, and a blind hole was made in its radial direction. Some partial grooves at the end of liquid line served as the returning liquid exit, and it was wrapped by the blind hole for fear that it be directly exposed to the compensation chamber, potentially causing it to be blocked by the vapor. The experimental results demonstrated that the loop could start up successfully and operated without temperature oscillations under the given heat load range from 20 W to 110 W in the horizontal orientation. In addition, the system rapidly responded to heat load cycle. The thermal resistance of the loop and the evaporator heat-transfer capacity were analyzed, and two operation modes existed because of the different distributions of the operating temperature with the evaporator wall temperature above or below 60 °C.