Determination of Ambient Air Vaporizers' Performance Based on a Study on Heat Transfer in Longitudinal Finned Tubes

被引:0
|
作者
Lisowski, Filip [1 ]
Lisowski, Edward [2 ]
机构
[1] Cracow Univ Technol, Fac Mech Engn, Dept Machine Design & Composite Struct, Al Jana Pawla II 37, PL-31864 Krakow, Poland
[2] Cracow Univ Technol, Fac Mech Engn, Dept Appl Informat, Al Jana Pawla II 37, PL-31864 Krakow, Poland
关键词
ambient air vaporizers; longitudinal finned tubes; forced convection; CFD analysis; LIQUEFIED NATURAL-GAS; FROST FORMATION; EXCHANGERS; CONVECTION; DESIGN;
D O I
10.3390/en17143579
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Ambient air vaporizers (AVVs) are the most commonly used type of heat exchanger for cryogenic regasification stations. The transfer of heat from the environment for heating the liquefied gas and its vaporization is a cost-free and efficient method. Designing ambient air vaporizers for regasification or fueling stations requires accepting the size and related thermal power of the AVV considering the operating conditions and the type of liquefied gases to be vaporized. The nominal capacity of the ambient air vaporizer depends on its design, the frosting of longitudinal finned tubes, and the airflow through the vaporizer structure. This paper presents the results of experimental studies and computational fluid dynamics (CFD) analysis on determining the heat output of AVV longitudinal finned tubes depending on their design. This experiment was conducted in order to establish a numerical model. The relation between the longitudinal finned tubes thermal power and the air flow velocity is demonstrated and the beneficial effect of forced convection is proved. The obtained results are used for verification calculations of ambient air vaporizers' performance depending on the size of the AVV, the profile cross-section, and the airflow velocity for different liquefied gases. Under conditions of forced convection, profiles with 12 equal-height fins were discovered to be the most efficient for higher airflow velocity providing up to 7% higher heat rate than profiles with 8 equal-height fins. However, at low air velocity, profiles with 8 equal-length fins showed a comparable heat output to profiles with 12 equal-length fins. Profiles with 8 and 12 unequal high fins differ in average heat output by about 28%. The profile with 12 unequal high fins turned out to be the least effective when 2D airflow was considered in this analysis.
引用
收藏
页数:20
相关论文
共 50 条
  • [41] Air-side heat transfer characteristics of ambient air vaporizers with various geometric parameters under cryogenic frosting conditions
    Kwon, Junho
    Yun, Sungho
    Lee, Sewon
    Cho, Wonhee
    Kim, Yongchan
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2022, 184
  • [42] Numerical analysis of heat and mass transfer in a compact finned tubes air heat exchanger under dehumidification conditions
    Benelmir, Riad
    Mokraoui, Salim
    HEAT AND MASS TRANSFER, 2012, 48 (04) : 663 - 682
  • [43] Numerical analysis of heat and mass transfer in a compact finned tubes air heat exchanger under dehumidification conditions
    Riad Benelmir
    Salim Mokraoui
    Heat and Mass Transfer, 2012, 48 : 663 - 682
  • [44] Experimental study of the natural convection heat transfer performance for finned oval tubes at different tube tilt angles
    Unger, Sebastian
    Beyer, Matthias
    Thiele, Johanna
    Hampel, Uwe
    EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2019, 105 : 100 - 108
  • [45] Effect of ambient pressure on air side heat transfer and flow characteristics of plain finned tube heat exchanger
    Zhang, Jiawen
    Liu, Jianhua
    Zhang, Liang
    Liu, Qi
    Wu, Qingqing
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2020, 158
  • [46] Heat transfer and fluid flow performance of an internally longitudinal finned tube: Numerical study and experimental validation
    El-Sebaey, Mahmoud S.
    El-Din, Sh Shams
    El-Kholy, Mohamed Kh.
    INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2024, 201
  • [47] Heat transfer enhancement of finned oval tubes with punched wing-type longitudinal vortex generators
    Chen, Y
    Fiebig, M
    Mitra, NK
    HEAT TRANSFER 1998, VOL 5: GENERAL PAPERS, 1998, : 351 - 356
  • [48] Air side performance of finned-tube heat exchanger with combination of circular and elliptical tubes
    Deepakkumar, R.
    Jayavel, S.
    APPLIED THERMAL ENGINEERING, 2017, 119 : 360 - 372
  • [49] Experimental Study on Heat Transfer and Resistance Performance of Elliptical Finned Tube Heat Exchanger with Different Air Entrance Angles
    Du, Xueping
    Zeng, Min
    Wang, Qiuwang
    Dong, Zhaoyi
    PRES 2011: 14TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, PTS 1 AND 2, 2011, 25 : 369 - +
  • [50] INFLUENCE OF LAYOUT OF A BANK OF FINNED ALUMINIUM TUBES ON HEAT TRANSFER
    ZOZULYA, NV
    KALININ, BL
    KHAVIN, AA
    THERMAL ENGINEERING, 1970, 17 (06) : 44 - &