• Title/Summary/Keyword: 휜-관열교환기

Search Result 2, Processing Time 0.017 seconds

Performance Evaluation of a Fin-Tube Heat Exchanger Using One-Dimensionalized Refrigerant Circuit (냉매유로를 1차원 배열화한 휜-관 열교환기 성능해석)

  • Kim, Doo-Hwan;Ye, Huee-Youl;Lee, Kwan-Soo;Cha, Woo-Ho
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
    • /
    • v.20 no.12
    • /
    • pp.833-843
    • /
    • 2008
  • A new method is presented for developing a simulation program which can analyze the heat transfer characteristics of fin-tube heat exchanger. This method is able to describe several types of refrigerant circuit arrangement. The delivery path of air and refrigerant properties is simplified by transforming three-dimensional array into one-dimensional array. By comparing simulated results with experiment results, the deviation was 8.2%. Several fin-tube heat exchangers of different design factors and operating conditions were simulated using this program. It was shown that this program could be used for designing practical fin-tube heat exchangers.

Prediction and Experiment of Pressure Drop of R22 and R134a on Design Conditions of Condenser (응축기의 설계조건에서 R22와 R134a의 압력강하 예측 및 실험)

  • Kang, Shin-Hyung;Byun, Ju-Suk;Kim, Chang-Duk
    • Journal of Energy Engineering
    • /
    • v.15 no.4 s.48
    • /
    • pp.243-249
    • /
    • 2006
  • An experimental study on the refrigerant-side pressure drop of slit fin an tube heat exchanger has been carried out. A comparison was made between the predictions of previously proposed empirical correlations and experimental data for the pressure drop on design conditions of condenser in micro-fin tube for R22 and Rl34a. Experiments were carried out under the conditions of inlet refrigerant temperature of $60^{\circ}C$ and mass fluxes varying from $150\;to\;250\;kg/m^{2}s$ for R22 and Rl34a. The inlet air conditions are dry bulb temperature of $35^{\circ}C$, relative humidity of 40% and air velocity varying from 0.68 to 1.43 m/s. Experiments show that pressure drop for R134a was $22{\sim}22.6%$ higher than R22 for the degree of subcooling $5^{\circ}C$ For the mass fluxes of $200{\sim}250\;kg/m^{2}s$, the deviation between the experimental and predicted values for the pressure drop was less than ${\pm}20%$ for R22 and Rl34a.