Thermo-hydraulic performance of concentric tube heat exchangers with turbulent flow: Predictive correlations and iterative methods for pumping power and heat transfer

被引:0
|
作者
Ali, Samer [1 ]
Nohra, Chadi [2 ]
Faraj, Jalal [3 ,4 ]
Dbouk, Talib [5 ]
Khaled, Mahmoud [4 ,6 ]
机构
[1] Univ. Lille, Institut Mines-Télécom, Univ. Artois, Junia, ULR 4515 – LGCgE, Laboratoire de Génie Civil et géo-Environnement, Lille,F-59000, France
[2] Beirut Arab University, BAU, Lebanon
[3] Energy and Thermo-Fluid Group, The International University of Beirut BIU, Beirut, Lebanon
[4] Energy and Thermo-Fluid Group, Lebanese International University LIU, Bekaa, Lebanon
[5] CORIA, UMR 6614, CNRS, Normandy Univ., UNIROUEN, Rouen,76000, France
[6] GUST Center for Sustainable Development, Gulf University for Science and Technology, Kuwait
来源
关键词
Air conditioning - Firedamp - Heat pump systems - Heat transfer performance - Newton-Raphson method - Synthesis gas - Turbulence - Turbulent flow;
D O I
10.1016/j.ijft.2024.100898
中图分类号
学科分类号
摘要
This research addresses the problem of predicting the thermo-hydraulic performance of concentric tube heat exchangers (CTHE) under turbulent flow conditions, a critical aspect in energy-efficient industrial systems such as HVAC, power generation, and chemical processing. Existing studies often lack accurate predictive methods for balancing heat transfer performance with pumping power requirements. To tackle this issue, novel correlations and an iterative Newton–Raphson method were developed for predicting pumping power and heat transfer rates. Three-dimensional CFD simulations of a water-to-water counter-flow CTHE were conducted, with Reynolds numbers ranging from 4000 to 8000 for both the hot and cold fluids. The simulations employed the Reynolds-Averaged Navier–Stokes (RANS) equations with the k−ω SST turbulence model. The results demonstrated that increasing the Reynolds number enhances both heat transfer rates and pumping power, with the cold fluid requiring consistently higher pumping power. New correlations were developed to predict pumping power, capturing the impact of both entry and fully developed flow regions. These correlations showed an average error of less than 2.33% when compared with the CFD data. The iterative Newton–Raphson method for predicting heat transfer rates demonstrated high accuracy, with an average error of 0.66% for heat transfer rate, 0.03% for hot fluid outlet temperature, and 0.01% for cold fluid outlet temperature. Additionally, we identified optimal operating conditions for efficient cooling and heating based on the heat capacity ratio (Cr). The novelty of this work lies in the development of new, highly accurate predictive correlations and iterative methods for optimizing CTHE performance, going beyond existing literature by providing comprehensive insights into the relationship between pumping power, heat transfer efficiency, and flow conditions. © 2024 The Authors
引用
收藏
相关论文
共 50 条
  • [21] Thermo-Hydraulic Performance of Pillow-Plate Heat Exchangers with Secondary Structuring: A Numerical Analysis
    Afsahnoudeh, Reza
    Wortmeier, Andreas
    Holzmueller, Maik
    Gong, Yi
    Homberg, Werner
    Kenig, Eugeny Y.
    ENERGIES, 2023, 16 (21)
  • [22] Parametric effect of diverging perforated cones on the thermo-hydraulic performance of a heat exchanger tube
    Gaurav Prakash Srivastava
    Anil Kumar Patil
    Manoj Kumar
    Heat and Mass Transfer, 2021, 57 : 1425 - 1437
  • [23] Thermo-hydraulic Performance and Optimization Design of a Louvered Fin-And-Tube Heat Exchanger
    Wu, Jia-Feng
    Liu, Zhi-Chun
    Liu, Wei
    Kung Cheng Je Wu Li Hsueh Pao/Journal of Engineering Thermophysics, 2021, 42 (07): : 1821 - 1826
  • [24] Parametric effect of diverging perforated cones on the thermo-hydraulic performance of a heat exchanger tube
    Srivastava, Gaurav Prakash
    Patil, Anil Kumar
    Kumar, Manoj
    HEAT AND MASS TRANSFER, 2021, 57 (09) : 1425 - 1437
  • [25] Developed correlations for heat transfer and flow friction characteristics of louvered finned tube heat exchangers
    Sadeghianjahromi, Ali
    Kheradmand, Saeid
    Nemati, Hossain
    INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2018, 129 : 135 - 144
  • [26] An investigation of the thermo-hydraulic performance of the smooth wavy fin-and-elliptical tube heat exchangers utilizing new type vortex generators
    Lotfi, Babak
    Sunden, Bengt
    Wang, Qiuwang
    APPLIED ENERGY, 2016, 162 : 1282 - 1302
  • [27] Heat transfer and performance analysis of nanofluid flow in helically coiled tube heat exchangers
    Bahrehmand, S.
    Abbassi, A.
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2016, 109 : 628 - 637
  • [28] Flow Field Structure, Characteristics of Thermo-Hydraulic and Heat Transfer Performance Analysis in a Three Dimensions Circular Tube with Different Ball Turbulators Configurations
    Al-Obaidi, Ahmed Ramadhan
    Chaer, Issa
    ARABIAN JOURNAL FOR SCIENCE AND ENGINEERING, 2021, 46 (12) : 12253 - 12282
  • [29] Flow Field Structure, Characteristics of Thermo-Hydraulic and Heat Transfer Performance Analysis in a Three Dimensions Circular Tube with Different Ball Turbulators Configurations
    Ahmed Ramadhan Al-Obaidi
    Issa Chaer
    Arabian Journal for Science and Engineering, 2021, 46 : 12253 - 12282
  • [30] Intensification of thermo-hydraulic performance in heat exchanger tube inserted with multiple twisted-tapes
    Piriyarungrod, N.
    Kumar, Manoj
    Thianpong, C.
    Pimsarn, M.
    Chuwattanakul, V
    Eiamsa-ard, S.
    APPLIED THERMAL ENGINEERING, 2018, 136 : 516 - 530