2002
DOI: 10.1016/s0196-8904(01)00136-4
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Air side performance of thermosyphon heat exchanger in low Reynolds number region: with and without electric field

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Cited by 28 publications
(9 citation statements)
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“…Again, at high frontal velocity, the heat transfer coefficients of all cases are nearly the same. The phenomena are similar to the works of Wangnipparnto et al [6,7] who used electric field to enhance heat transfer in thermosyphon heat exchanger. Fig.…”
Section: Performance Analysissupporting
confidence: 85%
See 1 more Smart Citation
“…Again, at high frontal velocity, the heat transfer coefficients of all cases are nearly the same. The phenomena are similar to the works of Wangnipparnto et al [6,7] who used electric field to enhance heat transfer in thermosyphon heat exchanger. Fig.…”
Section: Performance Analysissupporting
confidence: 85%
“…For example, Wangnipparnto et al [6,7] used the electric field to promote the heat transfer rate of the thermosyphon heat exchanger at low Reynolds number. Kui [8] studied the performance of air to air heat pipe under the electric field and developed the heat transfer model for the equipment.…”
Section: Introductionmentioning
confidence: 99%
“…Forced convection enhancement has been studied extensively for both laminar and turbulent internal flows [10][11] [12]. Additionally, ionic-wind-enhanced heat transfer has been investigated by Ohadi et al [13] for a shell-and-tube heat exchanger and by Wangnipparnto et al [14] in a thermosyphon heat exchanger.…”
Section: Introductionmentioning
confidence: 99%
“…The effect of the electro-magnetic forces on the heat transfer and friction factor has been studied for a tube, channel and tube bundles in the past. Yabe et al (1978Yabe et al ( , 1987, Yabe (1991), Kulacki (1983), Poulter & Allen (1986), Nelson et al (1991), Ohadi et al (1991), Ishiguro et al (1991), Ogata et al (1992), Wangnippanto et al (2001), but Lin & Jang (2005) were the first to apply the EHD electrodes on a finned-tube heat exchanger. They studied the effects of different arrangements of electrodes, applied voltage and tube pitch on the streamline, pressure and temperature profile for a finned tube heat exchanger [D = 20 mm, t f = 0.2 mm, f p = 6.2 mm, S l = 34.6 mm (for staggered arrangement), 40 mm (for inline arrangement), and S t = 40 mm].…”
Section: Plate Finsmentioning
confidence: 99%