Numerical investigation of the electric double-layer effect on the performance of microchannel heat exchanger at combined electroosmotic and pressure-driven flow

Abstract EN

Numerically investigated the electric double layer (EDL) Effects on the performance of the square microchannel heat exchanger (MCHE) at combined electro-osmotic and pressure-driven flow with compared pure pressure-driven with a hydraulic diameter (10 – 50) μm.

We defined at any size (Dh) of microchannel heat exchanger become the impact of EDL very slight with the studied effect of electric double layer thickness λ.

The diluted water 1: 1 potassium chloride (KCl) solution is used as a working fluid at an ionic concentration, , silicon microchannel at zeta potential of surface -0.2 volt.

A three-dimensional (3D) Poisson-Boltzmann equations and Naiver-stoke equations with applied electric field solved by using the finite volume scheme in this work.

The results show an increase in pressure drop of the microchannel heat exchanger at combined flow electroosmotic and pressure-driven flow with a percentage of 31.09 % at an ionic concentration and 42.71 % at increase in pumping power, especially at low ionic concentration.

Slight enhancement in average heat transfer rate and effectiveness due to an increase in average temperature difference.

Decrease in overall performance at combined electroosmotic and pressure-driven flow compared with pure pressure Effects on the performance of the square microchannel heat exchanger (MCHE) at combined electro-osmotic and pressure-driven flow with compared pure pressure-driven with a hydraulic diameter (10 – 50) μm.

We defined at any size (Dh) of microchannel heat exchanger become the impact of EDL very slight with the studied effect of electric double layer thickness λ.

The diluted water 1: 1 potassium chloride (KCl) solution is used as a working fluid at an ionic concentration, , silicon microchannel at zeta potential of surface -0.2 volt.

A three-dimensional (3D) Poisson-Boltzmann equations and Naiver-stoke equations with applied electric field solved by using the finite volume scheme in this work.

The results show an increase in pressure drop of the microchannel heat exchanger at combined flow electroosmotic and pressure-driven flow with a percentage of 31.09 % at an ionic concentration and 42.71 % at increase in pumping power, especially at low ionic concentration.

Slight enhancement in average heat transfer rate and effectiveness due to an increase in average temperature difference.

Decrease in overall performance at combined electroosmotic and pressure-driven flow compared with pure pressure driven.