Optimization of heat transfer and pressure drop of the channel flow with baffle

被引:4
|
作者
Ghobadi, Behzad [1 ]
Kowsary, Farshad [1 ]
Veysi, Farzad [2 ]
机构
[1] Islamic Azad Univ, Fac Ind & Mech Engn, Dept Mech Engn, Qazvin Branch, Qazvin, Iran
[2] Razi Univ, Dept Mech Engn, Kermanshah, Iran
关键词
heat transfer enhancement; k-omega SST; periodic boundary condition; genetic algorithm; Nusselt number; TURBULENT-FLOW; NANOFLUID FLOW; WATER-AL2O3; NANOFLUID; WATER/TIO2; SINGLE-PHASE; FLUID-FLOW; ENHANCEMENT; EXCHANGER; RIB; TUBE;
D O I
10.1515/htmp-2021-0030
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
In this article, the numerical analysis has been carried out to optimize heat transfer and pressure drop in the horizontal channel in the presence of a rectangular baffle and constant temperature in two-dimension. For this aim, the governing differential equation has been solved by computational fluid dynamics software. The Reynolds numbers are in the range of 2,000 < Re < 10,000 and the working fluid is water. While the periodic boundary condition has been applied at the inlet, outlet, and the channel wall, axisymmetric boundary condition has been used for channel axis. For modeling and optimizing the turbulence, k-omega SST model and genetic algorithm have been applied, respectively. The results illustrate that adding a rectangular baffle to the channel enhances heat transfer and pressure drop. Hence, the heat transfer performance factor along with maximum heat transfer and minimum pressure drop has been investigated and the effective geometrical parameters have been introduced. As can be seen, there is an inverse relationship between baffle step and both heat transfer and pressure drop so that for p/d equal to 0.5, 1, and 1.25, the percentage of increase in Nusselt number is 141, 124, and 120% comparing to a simple channel and the increase in friction factor is 5.5, 5, and 4.25 times, respectively. The results of modeling confirm the increase in heat transfer performance and friction factor in the baffle with more height. For instance, when the Reynolds number and height are 5,000 and 3 mm, the Nusselt number and friction factor have been increased by 35% and 2.5 times, respectively. However, for baffle with 4 mm height, the increase in the Nusselt number and friction factor is 68% and 5.57 times, respectively. It is also demonstrated that by increasing Reynolds number, the maximum heat transfer performance has been decreased which is proportional to the increase in p/d and h/d. Moreover, the maximum heat transfer performance in 2,000 Reynolds number is 1.5 proportional to p/d of 0.61 and h/d of 0.36, while for 10,000 Reynolds number, its value is 1.19 in high p/d of 0.93 and h/d of 0.15. The approaches of the present study can be used for optimizing heat transfer performance where geometrical dimensions are not accessible or the rectangular baffle has been applied for heat transfer enhancement.
引用
收藏
页码:286 / 299
页数:14
相关论文
共 50 条
  • [41] Numerical Investigation of the Effect of Baffle Orientation on Heat Transfer and Pressure Drop in a Shell and Tube Heat Exchanger With Leakage Flows
    Mohammadi, Koorosh
    Heidemann, Wolfgang
    Mueller-Steinhagen, Hans
    HEAT TRANSFER ENGINEERING, 2009, 30 (14) : 1123 - 1135
  • [42] Numerical modeling and optimization of pressure drop and heat transfer rate in a polymer fuel cell parallel cooling channel
    Seyed Amir Hosseini Baboli
    Ahmad Arabkoohsar
    Iman Seyedi
    Journal of the Brazilian Society of Mechanical Sciences and Engineering, 2023, 45
  • [43] Numerical modeling and optimization of pressure drop and heat transfer rate in a polymer fuel cell parallel cooling channel
    Baboli, Seyed Amir Hosseini
    Arabkoohsar, Ahmad
    Seyedi, Iman
    JOURNAL OF THE BRAZILIAN SOCIETY OF MECHANICAL SCIENCES AND ENGINEERING, 2023, 45 (04)
  • [44] Baffle structure effects on mass transfer and pressure drop of HT-PEMFC with orientated flow channels
    Ye, Lihua
    Cheng, Xing
    Shi, Yefan
    Li, Zekai
    Ke, Chenglong
    He, Zhou
    Shi, Aiping
    AIP ADVANCES, 2024, 14 (01)
  • [45] Influence of baffle configurations on flow and heat transfer characteristics of trisection helical baffle heat exchangers
    Dong, Cong
    Chen, Ya-Ping
    Wu, Jia-Feng
    ENERGY CONVERSION AND MANAGEMENT, 2014, 88 : 251 - 258
  • [46] Flow boiling heat transfer and pressure drop of pure HFC-152a in a horizontal mini-channel
    Hamdar, M.
    Zoughaib, A.
    Clodic, D.
    INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2010, 33 (03): : 566 - 577
  • [47] EFFECT OF LIQUID SOLIDIFICATION IN A PARALLEL PLATE CHANNEL UPON LAMINAR-FLOW HEAT TRANSFER AND PRESSURE DROP
    LEE, DG
    ZERKLE, RD
    JOURNAL OF HEAT TRANSFER, 1969, 91 (04): : 583 - &
  • [48] NUMERICAL DETERMINATION OF HEAT-TRANSFER AND PRESSURE-DROP CHARACTERISTICS FOR A CONVERGING-DIVERGING FLOW CHANNEL
    FAGHRI, M
    ASAKO, Y
    JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1987, 109 (03): : 606 - 612
  • [49] Investigation of flow boiling heat transfer and pressure drop of R134a in a rectangular channel with wavy fin
    Raju, M. Amaranatha
    Babu, T. P. Ashok
    Ranganayakulu, C.
    INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2020, 147 (147)
  • [50] The difference in flow pattern, heat transfer and pressure drop characteristics of mini-channel flow boiling in horizontal and vertical orientations
    Saisorn, Sira
    Wongpromma, Pakorn
    Wongwises, Somchai
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2018, 101 : 97 - 112