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
References
Aubin J, Ferrando M, Jiricny V (2010) Current methods for characterising mixing and flow in microchannels. Chem Eng Sci 65:2065–2093
Barajas AM, Panton RL (1993) The effects of contact angle on two-phase flow in capillary tubes. Int J Multiph Flow 19:337–346
Beattie DRH, Whalley PB (1982) A simple two-phase flow frictional pressure drop calculation method. Int J Multiph Flow 8:83–87
Bretherton FP (1961) The motion of long bubbles in tubes. J Fluid Mech 10:166–168
Chasanis P, Lautenschleger A, Kenig EY (2010) Numerical investigation of carbon dioxide absorption in a falling-film micro-contactor. Chem Eng Sci 65:1125–1133
Chen IY, Yang K-S, Wang C-C (2002) An empirical correlation for two-phase frictional performance in small diameter tubes. Int J Heat Mass Transf 45:3667–3671
Cheng J, Zhang Y, Pi PH, Lu LS, Tang Y (2011) Effect of gradient wetting surface on liquid flow in rectangular microchannels driven by capillary force and gravity: an analytical study. Int Commun Heat Mass Transf 38:1340–1343
Chisholm D (1967) A theoretical basis for the Lockhart–Martinelli correlation for two-phase flow. Int J Heat Mass Transf 10:1767–1778
Cho J-H, Law BM, Rieutord F (2004) Dipole-dependent slip of Newtonian liquids at smooth solid hydrophobic surfaces. Phys Rev Lett 92:166102
Choi C-H, Westin KJA, Breuer KS (2003) Apparent slip flows in hydrophilic and hydrophobic microchannels. Phys Fluids 15:2897
Churaev NV (1995) Contact angles and surface forces. Adv Colloid Interface Sci 58:87–118
Commenge J-M, Saber M, Falk L (2011) Methodology for multi-scale design of isothermal laminar flow networks. Chem Eng J 173:541–551
Dangla R, Lee S, Baroud CN (2011) Trapping microfluidic drops in wells of surface energy. Phys Rev Lett 107:124501
Dukler AE, Wicks M III, Cleveland RG (1964) Frictional pressure drop in two-phase flow: B. An approach through similarity analysis. AIChE J 10:44–51
Hibara A, Iwayama S, Matsuoka S, Ueno M, Kikutani Y, Tokeshi M, Kitamori T (2005) Surface modification method of microchannels for gas–liquid two-phase flow in microchips. Anal Chem 77:943–947
Huh D, Kuo C-H, Grotberg JB, Takayama S (2009) Gas–liquid two-phase flow patterns in rectangular polymeric microchannels: effect of surface wetting properties. New J Phys 11:075034
Kashid MN, Renken A, Kiwi-Minsker L (2011) Gas–liquid and liquid–liquid mass transfer in microstructured reactors. Chem Eng Sci 66:3876–3897
Kawahara A, Chung PM-Y, Kawaji M (2002) Investigation of two-phase flow pattern, void fraction and pressure drop in a microchannel. Int J Multiph Flow 28:1411–1435
Kreutzer MT, Kapteijn F, Moulijn JA, Kleijn CR, Heiszwolf JJ (2005) Inertial and interfacial effects on pressure drop of Taylor flow in capillaries. AIChE J 51:2428–2440
Lee HJ, Lee SY (2001) Pressure drop correlations for two-phase flow within horizontal rectangular channels with small heights. Int J Multiph Flow 27:783–796
Lee CY, Lee SY (2008a) Pressure drop of two-phase plug flow in round mini-channels: influence of surface wettability. Exp Therm Fluid Sci 32:1716–1722
Lee CY, Lee SY (2008b) Influence of surface wettability on transition of two-phase flow pattern in round mini-channels. Int J Multiph Flow 34:706–711
Li HW, Zhou YL, Sun B, Yang Y (2010) Multi-scale chaotic analysis of the characteristics of gas–liquid two-phase flow patterns. Chin J Chem Eng 18(5):880–888
Lin S, Kwok CCK, Li R-Y, Chen Z-H, Chen Z-Y (1991) Local frictional pressure drop during vaporization for R-12 through capillary tubes. Int J Multiph Flow 17:95–102
Liu DS, Wang SD (2008) Flow pattern and pressure drop of upward two-phase flow in vertical capillaries. Ind Eng Chem Res 47:243–255
Lockhart RW, Martinelli RC (1949) Proposed correlation of data for isothermal two-phase, two-component flow in pipes. Chem Eng Prog 45:39–48
Ma YG, Ji XY, Wang DJ (2011) Measurement and correlation of pressure drop for gas–liquid two-phase flow in rectangular microchannels. Chin J Chem Eng 18(6):940–947
Mishima K, Hibiki T (1996) Some characteristics of air–water two-phase flow in small diameter vertical tubes. Int J Multiph Flow 22:703–712
Moffat RJ (1988) Describing the uncertainties in experimental results. Exp Therm Fluid Sci 1:3–17
Morris CJ, Forster FK (2004) Oscillatory flow in microchannels: comparison of exact and approximate impedance models with experiments. Exp Fluids 36:928–937
Nghe P, Terriac E, Schneider M, Li ZZ, Cloitre M, Abecassis B, Tabeling P (2011) Microfluidics and complex fluids. Lab Chip 11:788–794
Niu HN, Pan LW, Su HJ, Wang SD (2009) Flow pattern, pressure drop, and mass transfer in a gas–liquid concurrent two-phase flow microchannel reactor. Ind Eng Chem Res 48:1621–1628
Owen WL (1961) Two-phase pressure gradient. Int Dev Heat Transf Pt II. ASME, New York
Pehlivan K, Hassan I, Vaillancourt M (2006) Experimental study on two-phase flow and pressure drop in millimeter-size channels. Appl Therm Eng 26:1506–1514
Pohorecki R (2007) Effectiveness of interfacial area for mass transfer in two-phase flow in microreactors. Chem Eng Sci 62:6495–6498
Roudet M, Loubiere K, Gourdon C, Cabassud M (2011) Hydrodynamic and mass transfer in inertial gas–liquid flow regimes through straight and meandering millimetric square channels. Chem Eng Sci 66:2974–2990
Shao N, Gavriilidis A, Angeli P (2010) Mass transfer during Taylor flow in microchannels with and without chemical reaction. Chem Eng J 160:873–881
Sobieszuk P, Pohorecki R (2010) Gas-side mass transfer coefficients in a falling film microreactor. Chem Eng Process 49:820–824
Su HJ, Niu HN, Pan LW, Wang SD, Wang AJ, Hu YK (2010) The characteristics of pressure drop in microchannels. Ind Eng Chem Res 49:3830–3839
Tan J, Lu YC, Xu JH, Luo GS (2012) Mass transfer performance of gas–liquid segmented flow in microchannels. Chem Eng J 181–182:229–235
Tostado CP, Xu JH, Luo GS (2011) The effects of hydrophilic surfactant concentration and flow ratio on dynamic wetting in a T-junction microfluidic device. Chem Eng J 171:1340–1347
Tretheway D, Meinhart C (2002) Apparent fluid slip flows at hydrophobic microchannel walls. Phys Fluids 14:L9
Triplett KA, Ghiaasiaan SM, Abdel-Khalik SI, LeMouel A, McCord BN (1999) Gas–liquid two-phase flow in microchannels. Part II: void fraction and pressure drop. Int J Multiph Flow 25:395–410
Ungar EK, Cornwell JD (1992) Two-phase pressure drop of ammonia in small diameter horizontal tubes. AIAA 17th Aerospace Ground Testing Conference. Nashville, TN, July 6–8
van Baten JM, Krishna R (2004) CFD simulations of mass transfer from Taylor bubbles rising in circular capillaries. Chem Eng Sci 65:2535–2545
Wang X, Yong YM, Fan P, Yu GZ, Yang C, Mao Z-S (2012) Flow regime transition for concurrent gas–liquid flow in micro-channels. Chem Eng Sci 69:578–586
Warnier MJF, de Croon MHJM, Rebrov EV, Schouten JC (2010) Pressure drop of gas–liquid Taylor flow in round micro-capillaries for low to intermediate Reynolds numbers. Microfluid Nanofluid 8:33–45
Whitesides GM (2011) What comes next? Lab Chip 11:191–193
Yamada T, Hong C, Greroty OJ (2011) Experimental investigations of liquid flow in rib-patterned microchannel with different surface wettability. Microfluid Nanofluid 11:45–55
Yue J, Chen GW, Yuan Q (2004) Pressure drops of single and two-phase flows through T-type microchannel mixers. Chem Eng J 102:11–24
Yue J, Chen GW, Yuan Q, Luo LA, Gonthier Y (2007) Hydrodynamics and mass transfer characteristics in gas–liquid flow through a rectangular microchannel. Chem Eng Sci 62:2096–2108
Yue J, Boichot R, Luo LA, Gonthier Y, Chen GW, Yuan Q (2010) Flow distribution and mass transfer in a parallel microchannel contactor integrated with constructal distributors. AIChE J 56:298–317
Zhao C-X, Middelberg APJ (2011) Two-phase microfluidic flows. Chem Eng Sci 66:1394–1411
Zhao YC, Su YH, Chen GW, Yuan Q (2010) Effect of surface properties on the flow characteristics and mass transfer performance in microchannels. Chem Eng Sci 65:1563–1570
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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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