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Investigation on pressure drop characteristic and mass transfer performance of gas–liquid flow in micro-channels

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Abstract

Pressure drop characteristics and mass transfer performance of gas–liquid two-phase flow in micro-channels with different surface wettabilities were experimentally investigated. Side-entry T micro-channel mixers made of glass and polydimethylsiloxane were tested. Frictional pressure drop was found to decrease as the hydrophobicity of the channel surface increased. The flow patterns observed in the experiment were classified as slug flow and continuous gas phase flows. The modified Hagen–Poiseuille equation and Lockhart–Martinelli model were developed to predict the pressure drop for these two types of flow, respectively. The effect of surface wettability was heuristically incorporated in the present models which can correlate well the experimental results. Mass transfer performance was studied by the physical absorption of oxygen into de-ionized water. The results show that the volumetric mass transfer coefficients in hydrophobic micro-channels are generally higher than those in hydrophilic ones. The empirical correlations of overall volumetric mass transfer coefficients were proposed.

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Abbreviations

a :

Half width of the duct (m)

C :

Chisholm factor, dimensionless

Ca :

Capillary number in Eq. (4), dimensionless

Ca GL :

Capillary number based on liquid phase properties and sum of superficial gas and liquid phase, dimensionless

\( C_{{{\text{O}}_{ 2} }} \) :

Concentration of oxygen (mg/L)

\( C_{{{\text{O}}_{2} }}^{ * } \) :

Equilibrium concentration of dissolved oxygen (mg/L)

\( C_{{{\text{O}}_{ 2} }}^{\text{in}} \) :

Inlet concentration of dissolved oxygen (mg/L)

\( C_{{{\text{O}}_{ 2} }}^{\text{out}} \) :

Outlet concentration of dissolved oxygen (mg/L)

D H :

Hydraulic diameter defined by Eq. (2) (m)

d :

Depth of the micro-channel (m)

f :

Fanning friction factor, dimensionless

k L a :

Liquid side volumetric mass transfer coefficient (s−1)

L :

Length of the channel (m)

ΔP :

Total pressure drop (Pa)

ΔP a :

Acceleration pressure drop (Pa)

ΔP g :

Static pressure drop (Pa)

ΔP f :

Friction pressure drop (Pa)

Q :

Volumetric flow rate (m3/s)

R :

General dependent variable

Rs :

Channel resistance (Pa s/m3)

Re :

Reynolds number in Eq. (3), dimensionless

u :

Superficial velocity (m/s)

w :

Width of the micro-channel (m)

We :

Weber number in Eq. (5), dimensionless

X i :

General independent variable

x :

Gas mass flow rate to total mass flow rate in Eq. (13), dimensionless

α :

Void fraction of gas phase, dimensionless

β :

Duct aspect ratio (depth/width), dimensionless

γ :

Surface tension (N/m)

θ :

Contact angle of liquid phase on solid surface (°)

μ :

Viscosity (Pa s)

ρ :

Density (kg/m3)

τ :

Residence time (s)

C:

Continuous gas flow

G:

Gas phase

GL:

Gas–liquid interface

GS:

Gas–solid interface

L:

Liquid phase

LS:

Liquid–solid interface

S:

Slug flow

TP:

Gas–liquid two phase

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Acknowledgments

Financial supports from 973 Program (2009CB623406), the National Natural Science Foundation of China (20990224, 21206166), the National Science Fund for Distinguished Young Scholars (21025627), 863 Project (2012AA03A606) and CAS Program for Cross & Cooperative Team of the Science & Technology Innovation are gratefully acknowledged. The authors thank Professor Xiaolong Yin at Colorado School of Mines for his useful discussions on this work.

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Correspondence to Chao Yang.

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Wang, X., Yong, Y., Yang, C. et al. Investigation on pressure drop characteristic and mass transfer performance of gas–liquid flow in micro-channels. Microfluid Nanofluid 16, 413–423 (2014). https://doi.org/10.1007/s10404-013-1226-5

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  • DOI: https://doi.org/10.1007/s10404-013-1226-5

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