2010
DOI: 10.1016/j.ijheatmasstransfer.2010.02.047
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Air-side heat transfer characteristics of flat plate finned-tube heat exchangers with large fin pitches under frosting conditions

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Cited by 56 publications
(17 citation statements)
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“…Therefore, boundary layer interruption between fins can occur theoretically for a fin space of 7.0 mm at an air flow rate of 1.0 m 3 /min. That is, the boundary layer interruption for a fin space of more than 7.0 mm can be avoided under the given conditions because the boundary layer interruption is largely dependent on the fin space [25]. This is consistent with the results of Kim [22].…”
Section: Numerical Resultssupporting
confidence: 90%
“…Therefore, boundary layer interruption between fins can occur theoretically for a fin space of 7.0 mm at an air flow rate of 1.0 m 3 /min. That is, the boundary layer interruption for a fin space of more than 7.0 mm can be avoided under the given conditions because the boundary layer interruption is largely dependent on the fin space [25]. This is consistent with the results of Kim [22].…”
Section: Numerical Resultssupporting
confidence: 90%
“…The result provided by Kim et al [60] also revealed the above conclusion. They measured the change of sessile droplet temperature with time on a cold surface (its static contact angle was 75 ± 1 • ), when the cold surface temperature, the outdoor air temperature (T a ) and relative humidity (RH) were held constant at-10 ± 0.2 • C, 25 ± 1 • C and Energies 2018, 11, 2642 5 of 36 30 ± 3%, respectively, without forced air flow around the cold surface [60]. The results are showed in Figure 3.…”
Section: Figurementioning
confidence: 99%
“…To promote the rapid development of ASHP technology and the successful implementation of Coal to Electricity policy in China, the anti-frosting and defrosting technologies are focused by researchers worldwide in recent years [14]. According to the references, the anti-frosting technologies include changing the characteristics (temperature, velocity [20], humidity [21], pressure [22] and purified air [23]) of inlet ambient air, changing the cold surface temperature [24], surface treatment [25], changing the structure of air heat exchanger (fin-tube geometry [26][27][28], fin spacing [29,30], fin type [31,32]), changing the interaction between air or frost layer and cold surface (electric field [33], ultrasonic wave [34], magnetic field [35] and low frequency mechanical oscillation [36]). And the defrosting technologies mainly have reverse cycle [37], hot gas bypass [38], electrical heating [19,39,40], warm-air defrosting [41], compressor shutdown [42], hot water spray [43], phase change heat storage, electric field [44], ultrasonic wave [45], magnetic field [46], air-particle jet [47], control strategy [48] and waste heat recovery [49,50].…”
Section: Introductionmentioning
confidence: 99%
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“…Their investigations revealed that round tube heat exchanger showed the longest refrigeration time due to its larger surface area. Some other researchers have equally examined the frost formation and effect of frost layer on the performance of fin-tube heat exchanger [21][22][23][24][25][26].…”
Section: Introductionmentioning
confidence: 99%