Startseite Two phase flow analysis of micro channel evaporator to investigate effect of geometry on pressure and heat transfer coefficient with respect to volume of fraction
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Two phase flow analysis of micro channel evaporator to investigate effect of geometry on pressure and heat transfer coefficient with respect to volume of fraction

  • Pradipkumar M. Gavali ORCID logo EMAIL logo , Sanjay D. Yadav ORCID logo und Prateek D. Malwe ORCID logo EMAIL logo
Veröffentlicht/Copyright: 1. August 2024
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Abstract

Pressure and heat transfer coefficient (HTC) are parameters used to measure the performance of microchannel evaporators (MCE). By keeping the same overall dimensions, optimised hydraulic diameters of three different port shapes, square, rectangle and trapezoid, are analysed using CFD software to study the effect of geometry on the performance characteristics of MCE. The number of square, rectangle, and trapezoid channels is 580, 986, and 812, respectively. CFD analysis of the evaporator using R134a refrigerant is performed using the Volume of Fluid (VOF) with the SST k-ω model and Lee model for interphase mass transfer trace. Variation of pressure and HTC concerning volume of fraction liquid refrigerant (α) is compared for these three port structures. The trapezoid port microchannel evaporator (MCE) exhibits the highest pressure drop compared to square and rectangular port MCEs. The rectangular port MCE demonstrates the highest heat transfer coefficient among the configurations studied. The rectangular port MCE outperforms both square and trapezoid port MCEs in overall performance.


Corresponding authors: Pradipkumar M. Gavali, Department of Technology, Shivaji University, Kolhapur, Maharashtra 416004, India; and Rajarambapu Institute of Technology, Rajaramnagar, Islampur, Maharashtra 415414, India, E-mail: ; and Prateek D. Malwe, Dr. D. Y. Patil Institute of Technology, Pimpri, Pune, Maharashtra 411018, India; and Walchand College of Engineering, Sangli, Maharashtra 416415, India, E-mail:

  1. Research ethics: Not applicable.

  2. Author contributions: All authors have equal contributions. P. M. G.: Conceptualization; S. D. Y.: Manuscript evaluation and validation; P. D. M.: Manuscript editing.

  3. Competing interests: The authors state no conflict of interest.

  4. Research funding: None declared.

  5. Data availability: Not applicable.

Nomenclature

u

velocity

p

pressure

F

surface tension and gravity source term

t

time

k

kinetic energy

τ

viscosity stress tensor

α

volume fraction

P

turbulent production term

ω

specific rate of dissipation

b *

model constant

s k

model constant

η

dynamic viscosity

η t

turbulent viscosity

s ω

model constant

S

absolute vorticity

β

model constant

F 1

blending function for transition between k-ε model and k-ω model

m ˙

mass transfer

ξ

time relaxation coefficient

T

temperature

Suffix

vl

vapour to liquid

lv

liquid to vapour

v

vapour phase

l

liquid phase

sat

saturation

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Received: 2024-03-03
Accepted: 2024-07-08
Published Online: 2024-08-01
Published in Print: 2024-08-27

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