COMPARISON OF THE EFFECT OF VARIOUS NANOPARTICLE SHAPES ON OPTIMAL DESIGN OF PLATE HEAT EXCHANGER

被引:5
|
作者
Hajabdollahi, Hassan [1 ]
Ataeizadeh, Mohammad [1 ]
Masoumpour, Babak [1 ]
Dehaj, Mohammad Shafiey [1 ]
机构
[1] Vali E Asr Univ Rafsanjan, Fac Engn, Rafsanjan, Iran
关键词
plate heat exchanger; different shapes of nanoparticles; Boehmite alumina nanoparticles; thermoeconomic optimization; SHELL-AND-TUBE; BOEHMITE ALUMINA NANOFLUID; THERMAL PERFORMANCE; HYDRAULIC OPTIMIZATION; FLUID; FLOW; ENHANCEMENT; BEHAVIOR; CHANNEL; SURFACE;
D O I
10.1615/HeatTransRes.2021036994
中图分类号
O414.1 [热力学];
学科分类号
摘要
In the present study, the thermoeconomic aspects of gasket-plate heat exchangers (GPHE), using the Boehmite alumina as nanoparticles, are studied. Four different nanoparticle shapes including platelet, brick, cylinder, and blade are investigated. Effectiveness and total annual cost (TAC) are chosen as two objective functions, and the results of optimal Pareto fronts are compared with the case of a base fluid. Eight design parameters including particle volumetric concentration as well as some heat exchanger geometrical parameters are considered, and optimization is performed for various sets of cold-side mass flow rates. The results indicate a considerable improvement in both the effectiveness and TAC for all the cases studied as compared with the case of a base fluid. The optimum results show that the best studied shape of nanoparticles for thermoeconomic improvement is cylinder, followed by platelet, brick, and blade shapes. For example, the effectiveness is improved by 19.95%, 18.26%, 18.12%, and 16.54%, respectively, in the cases of cylinder, platelet, brick, and blade shapes as compared with the base fluid for the final optimum solution. The optimum results also demonstrate the lower heat exchanger volume in the case of nanofluid for all the shapes studied as compared with the base fluid case. Finally, optimum values of some important parameters such as pressure drop and particle volumetric concentration are discussed in all the cases studied and results are reported.
引用
收藏
页码:29 / 47
页数:19
相关论文
共 50 条
  • [41] COMPUTER-AIDED DESIGN OF OPTIMAL PLATE CAM SHAPES
    FELDMANN, JU
    ANGEWANDTE INFORMATIK, 1977, (04): : 164 - 170
  • [42] Optimal design of bypass location on heat exchanger networks
    Luo, Xionglin
    Sun, Lin
    Zhang, Junfeng
    Huagong Xuebao/Journal of Chemical Industry and Engineering (China), 2008, 59 (03): : 646 - 652
  • [43] Optimal design of tests for heat exchanger fouling identification
    Palmer, Kyle A.
    Hale, William T.
    Such, Kyle D.
    Shea, Brian R.
    Bollas, George M.
    APPLIED THERMAL ENGINEERING, 2016, 95 : 382 - 393
  • [44] Optimal Design of Heat Exchanger Network in Oil Refineries
    Al-Mutairi, Eid M.
    PRES 2010: 13TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, 2010, 21 : 955 - 960
  • [45] Optimal Design of Double Pipe Heat Exchanger Structures
    Peccini, Alice
    Lernos, Julia C.
    Costa, Andre L. H.
    Bagajewicz, Miguel J.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2019, 58 (27) : 12080 - 12096
  • [46] Use of Algorithm of Changes for Optimal Design of Heat Exchanger
    Tam, S. C.
    Tam, H. K.
    Chio, C. H.
    Tam, L. M.
    ISCM II AND EPMESC XII, PTS 1 AND 2, 2010, 1233 : 857 - +
  • [47] Influence of availability costs on optimal heat exchanger design
    Witte, L.C.
    Journal of Heat Transfer, 1988, 110 (04): : 830 - 835
  • [48] Design of Optimal Fuzzy Controller for Heat Exchanger Temperature
    Abdullah A.A.
    Khalaf A.N.
    Bachache N.
    Journal of Engineering Science and Technology Review, 2022, 15 (05) : 153 - 157
  • [49] Performance comparison of the plate heat exchanger using different nanofluids
    Tiwari, Arun Kumar
    Ghosh, Pradyumna
    Sarkar, Jahar
    EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2013, 49 : 141 - 151
  • [50] Optimal shape and arrangement of staggered pins in the channel of a plate heat exchanger
    Lee, KS
    Kim, WS
    Si, JM
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2001, 44 (17) : 3223 - 3231