• Title/Summary/Keyword: Parallel Flow 평행류형 열교환기

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Study on the Performance of the Separate type Heat Pipe Using the Parallel Flow type Heat Exchanger (평행류형 열교환기를 이용한 분리형 히트파이프의 성능에 관한 연구)

  • Jeon, Sung-Taek;Cho, Jin-Pyo
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.16 no.8
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    • pp.5045-5050
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    • 2015
  • As modern houses are constructed with high-density and high-insulation, there is benefit to reduce energy consumption, but there are many side effects raised from polluted air. To solve the problem, a ventilation system is used to improve a indoor air quality. In this study, we tested the parallel flow type heat exchanger used in a heat exchanger of an automotive air conditioner. And we experimentally estimate ventilation performance of HRV(heat recovery ventilator) with heat-pipe according to working fluid filling quantity and ventilation. The working fluid was R22, which was filled from 40 to 60 (%vol.) by 10(%vol.). Ventilation based on the front velocity was measured from 0.3 m/s to 1.5 m/s by 0.3 m/s intervals. Refrigerant filling quantity with the highest efficiency was found to depend on the ventilation. From this study the optimal refrigerant filling quantity in accordance with the ventilation of the detachable heat pipes was found experimentally.

Separate type heat pipe performance comparison by the heat exchanger shapes (열교환기 형상에 따른 분리형 히트파이프 성능 비교)

  • Jeon, Sung-Taek;Cho, Jin-Pyo
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.17 no.12
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    • pp.723-729
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    • 2016
  • This study compared fin-tube and parallel-flow heat pipes for their sensible heat exchange rate, heat recovery amount, and air-side pressure drop. Tests were done with different refrigerant charging rates of 40-60% vol. and air flow rates of 300-1,400. The sensible heat exchange rate was highest for both types of heat pipes at a working fluid charge of 40% vol. and low flow rate. For the parallel-flow heat pipe, the 60% vol. charge is too high and results in a low sensible heat exchange rate. The reason is that the thicker liquid film of the tube wall deteriorates the heat transfer effect. Hence, the optimal charging rate is 40 to 50% vol. The evaporator heat pipe has a larger air-side pressure drop than the condenser section heat pipe. The reason is considered to be condensation water arising from the evaporator surface. Compared to the fin-tube heat pipe, the parallel-flow heat pipe showed better performance with a working fluid charging rate of 48%, volume of 41%, and an air-side pressure drop about 37%.

Wet Surface Performance Test of PF Heat Exchanger (PF열교환기의 습표면 성능시험)

  • Cho, J.P.;Kim, N.H.;Choi, K.K.
    • Proceedings of the KSME Conference
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    • 2000.11b
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    • pp.314-320
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    • 2000
  • In this study, the wet surface heat transfer coefficients and friction factors of PF heat exchangers are presented. Two sample with different fin pitch(1.25mm, 1.5mm) were tested. Tests were conducted in a open loop wind tunnel. The wet surface heat transfer coefficient was reduced following the procedure given in ARI 410-81. Results showed that the heat transfer coefficients of the heat exchanger with 1.5mm fin pitch were approximately the same as those with 1.25mm fin pitch, except at low reynolds number(Re<100), where the heat transfer coefficients of 1.5mm fin pitch were slighly higher than those with 1.25mm fin pitch. The friction factors of the 1.25mm fin pitch, however was 120 % to 160 % higher than those of the 1.5mm fin pitch. The wet surface heat transfer coefficients were lower than those of the dry surface. The wet surface friction factors, however, were higher than those of the dry surface.

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Slim Electronic Panel Cooler with Parallel Flow Condenser (PF 열교환기가 적용된 슬림형 중계기 냉각기)

  • Cho, J.P.;Kim, N.H.;Lee, J.H.;Lee, Y.J.;Mook, I.K.;Lim, W.K.;Lim, S.S.
    • Proceedings of the SAREK Conference
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    • 2006.06a
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    • pp.483-488
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    • 2006
  • In this study, newly-developed slim electronic panel cooler with aluminum PF condenser and evaporator was tested and the results are compared with imported panel cooler with fin-tube heat exchangers. The PF heat exchangers significantly (approximately 45%) reduced the refrigerant charge. The air-side pressure drop was also reduced, which resulted in the reduction of the sound level of the panel cooler. The effect of the condenser size was also investigated.

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A Study on the Performance Characteristics of Fin-type Heat Exchanger for the Automobile Air-Conditioners (자동차 공조용 핀형 열교환기의 성능특성에 관한 연구)

  • 홍경한;전상신;이승재;박찬수;권일욱;김재열;김병철;하옥남
    • Transactions of the Korean Society of Machine Tool Engineers
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    • v.13 no.4
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    • pp.100-105
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    • 2004
  • Fin-tube type(Fin-type) heat exchanger has been tested in order to replace the heat exchanger of parallel flow type(P.F -type) which is now widly used in automobile air conditioning system The following conclusions are drawn by the comparison of the characteristics of the heat exchangers. Evaporator and condenser capacities and COP(Coefficience of performance) were varied as with the compressor speed, outdoor air temperature and air flow rate changed, which much influenced on the characteristics of the air conditioning system Evaporator and condenser capacities were increased with increasing compressor speed and outdoor air temperature. Evaporator and condenser pressures of Fin-type were decreased by 7% and 5% respectively compared with those of P.F-type. The COP of Fin-type was decreased with increasing outdoor air temperature and compressor speed. The COP of P.F-type was decreased by 14% compared with that of Fin-type.

Performance evaluation of PF-condenser adapted to Large Size air-conditioner (대형 에어컨에 적용된 PF열교환기의 성능평가)

  • Cho, J.P.;Choi, Y.H.;Kim, J.H.;Kim, N.H.;Kim, J.H.
    • Proceedings of the KSME Conference
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    • 2000.04b
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    • pp.1-6
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    • 2000
  • In this study, We evaluated the Performance of PFC and the system performance of large size air-conditioner applying to outdoor condenser. PFC can meet the same cooling capacity in 40.42% of volume to fin-tube condenser. Although the fin-tube condenser requires 3600g of refrigerant charging, PFC requires 1700g, 1800g, 1900g, 2000g refrigerant charging for each 2.0mm, 2.5mm, 3.0mm and 3.5mm fin pitches. Difference of condensing and evaporation pressure is the biggest point 2.0mm fin pitch and the smallest point 2.5mm fin pitch.

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