4.7 Article

Evaporation heat transfer characteristics of falling film in small diameter fabricated tubes of absorption refrigeration system: An experimental investigation

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijheatmasstransfer.2020.120618

关键词

Absorption refrigeration system; Falling film; Small diameter evaporator tubes; Outside heat transfer coefficient

资金

  1. Korea Institute of Energy Technology Evaluation and Planning (KETEP)
  2. Ministry of Trade, Industry, and Energy (MOTIE) of the Republic of Korea [20192010107020, 20172010105860, P00 02131]
  3. National Research Foundation of Korea - Korean Government [2019R1A2C2010607]
  4. Leaders in Industry-university Cooperation + Project - Ministry of Education of Korea [20 01000783]
  5. Leaders in Industry-university Cooperation + Project - National Research Foundation of Korea [20 01000783]
  6. Korea Evaluation Institute of Industrial Technology (KEIT) [20172010105860] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

向作者/读者索取更多资源

The absorption refrigeration system is being optimized with a focus on the evaporator, where improvements in wettability and reduction of liquid film uneven distribution are key targets. Using smaller diameter tubes to optimize performance shows a peak heat transfer coefficient at the transition Reynolds number. Experimental correlations were developed to predict data within +/- 20% accuracy.
Absorption refrigeration system is going through optimization. The evaporator is one of the core components of the absorption refrigeration system, and its optimization can be done by improving the wettability and reducing the uneven distribution of liquid film. Enhanced tubes are often helpful in mitigating the film thickness and ensuring proper wetting of the tubes, thus enhancing the heat transfer performance. Using a smaller tube diameter also significantly affects the heat transfer performance because of the increasing ratio of the developing boundary layer to the fully developed boundary layer. In this study, seven small-diameter (12.7 mm) tubes were used to optimize the performance of the evaporator. The parameters observed are as follows: falling-film Reynolds number (10-100), wall superheat (2.2-5.1 degrees C), and saturation pressure (0.9-1.20 kPa). The heat transfer coefficient exhibited a peak point at a falling-film Reynolds number, called transition Reynolds number (Re-transition ) mostly at a value of similar to 42. The wall superheat is increased by increasing the wall temperature and, as a result, the heat transfer coefficient remains unchanged; however, the heat flux increases almost linearly. The heat transfer coefficient increases with the increase in the saturation pressure. One of the fabricated tubes was tested with corrosion, and a negligible change in the heat transfer coefficient was observed when compared with the uncorroded tube. Both droplet and jet modes are observed when viewing the falling-film phenomena through a glass window. Smooth tube data reveal a reasonable comparison with the jet and droplet mode of Hu et al. Of all the tubes, the heat transfer coefficient of Tube_Z is the highest. Tube_Y1 exhibited the highest heat flux; however, Tube_Z exhibited the highest ratio of heat flux to friction factor. Empirical correlations were developed based on the current experimental perimeters, and correlations predicted the data within +/- 20%. (C) 2020 Elsevier Ltd. All rights reserved.

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