Thermal-hydraulic performance of a nanofluid in a shell-and-tube heat exchanger equipped with new trapezoidal inclined baffles: Nanoparticle shape effect

2022 ◽  
Vol 395 ◽  
pp. 348-359
Author(s):  
Mehdi Bahiraei ◽  
Mohammad Naseri ◽  
Ali Monavari
Keyword(s):  
Heat Exchanger ◽  
Hydraulic Performance ◽  
Shape Effect ◽  
Tube Heat Exchanger ◽  
Nanoparticle Shape ◽  
Shell And Tube ◽  
Nanoparticle Shape Effect

Shape optimization of segmental porous baffles for enhanced thermo-hydraulic performance of shell-and-tube heat exchanger

2020 ◽  
Vol 180 ◽  
pp. 115835 ◽  
Author(s):  
Hamid Reza Abbasi ◽  
Ebrahim Sharifi Sedeh ◽  
Hossein Pourrahmani ◽  
Mohammad Hadi Mohammadi
Keyword(s):  
Heat Exchanger ◽  
Shape Optimization ◽  
Hydraulic Performance ◽  
Tube Heat Exchanger ◽  
Shell And Tube

scholarly journals Temperature effect on thermal-hydraulic performance of one-pass counter-current flow shell-and-tube heat exchanger and upon its design

2021 ◽  
pp. 349-349
Author(s):  
Elmokhtar Elouardi ◽  
Fatima Yatim ◽  
Hassan Chehouani
Keyword(s):  
Heat Exchanger ◽  
Physical Properties ◽  
Temperature Effect ◽  
Current Flow ◽  
Hydraulic Performance ◽  
Dimensionless Quantity ◽  
Tube Heat Exchanger ◽  
Shell And Tube ◽  
Counter Current ◽  
Thermo Physical Properties

A methodology of design and analysis of thermal-hydraulic performance for a single pass 1-1 counter-current flow shell and tube heat exchanger (CCFSTHE) TEMA E type has been established. The temperature effect on the thermo-physical properties of flowing fluids and on the overall coefficient of heat transfer along the heat exchanger is incorporated in our approach, as well as the coupling between different thermal and hydraulic parameters. It has been noted that the correction factor (F) in the HAUSBRAND formula is not included. Our method brings us to a new dimensionless quantity (MKA) which links the calculation parameters of the heat exchanger to the thermo-physical properties. This dimensionless quantity relates the number of transfer units (NTU) to the heat flow ratio (R). The results based on our models show a pronounced deviation compared to the model reported in the literature (NTU method). This deviation may be related to a temperature effect not included in the literature model. It has been shown that the results derived from our models are in a good agreement with experimental data. Our new method, named MKA - method, could be a useful tool for theoretical and experimental studies of the design and analysis of the single pass 1-1 CCFSTHE thermal and hydraulic performance for 0 ? R ?1.

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