Raghvendra Gupta

Dr. Raghvendra Gupta


Research Focus & Metrics

Academic Career Length

19Years (2008-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 June 2009 in Chemical Engineering Science
Verified
Journal Article
Closed access
RGRaghvendra Gupta
Raghvendra Gupta
DFDavid F Fletcher
David F Fletcher
BHBrian S. Haynes
Brian S. Haynes

1 March 2010 in The Journal of Computational Multiphase Flows
Verified
Journal Article
Open access
RGRaghvendra Gupta
Raghvendra Gupta
DFDavid F Fletcher
David F Fletcher
BHB.S. Haynes
B.S. Haynes
Over the past few decades an enormous interest in two-phase flow in microchannels has developed because of their application in a wide range of new technologies, ranging from lab-on-a-chip devices used in medical and pharmaceutical applications to micro-structured process equipment used in many modern chemical plants. Taylor flow, in which gas bubbles are surrounded by a liquid film and separated by liquid plugs, is the most common flow regime encountered in such applications. This review introduces the important attributes of two phase flow in microchannels and then focuses on the Taylor flow regime. The existing knowledge from both experimental and computational studies is presented. Finally, perspectives for future work are suggested.

1 March 2010 in Chemical Engineering Science
Verified
Journal Article
Closed access
RGRaghvendra Gupta
Raghvendra Gupta
DFDavid F Fletcher
David F Fletcher
BHBrian S. Haynes
Brian S. Haynes

1 November 2011 in Chemical Engineering Science
Verified
Journal Article
Closed access
AAAzadeh N. Asadolahi
Azadeh N. Asadolahi
RGRaghvendra Gupta
Raghvendra Gupta
DFDavid F Fletcher
David F Fletcher
BHBrian S. Haynes
Brian S. Haynes

1 March 2014 in Physics of Fluids
Verified
Journal Article
Closed access
PDF file
EKEvert Klaseboer
Evert Klaseboer
RGRaghvendra Gupta
Raghvendra Gupta
RMRogerio Manica
Rogerio Manica
When (long) bubbles are transported in tubes containing a fluid, the presence of a thin film of fluid along the tube walls causes the velocity of the bubble to be different from the average fluid velocity. Bretherton [“The motion of long bubbles in tubes,” J. Fluid Mech. 10, 166 (1961)] derived a model to describe this phenomenon for pressure driven flows based on a lubrication approach coupled with surface deformation of the bubble. Bretherton found that the parameter governing the physics involved is the capillary number (Ca) which expresses the relationship between speed of the bubble, surface tension, and viscosity of the liquid. The results of Bretherton are here re-derived and analyzed in a slightly more perspicuous manner. Incorporating the condition that the bubble-film combination should fit inside the tube results in an expression very similar to the one found empirically by Aussillous and Quéré [“Quick deposition of a fluid on the wall of a tube,” Phys. Fluids 12, 2367 (2000)] of the Taylor [“Deposition of a viscous fluid on the wall of a tube,” J. Fluid Mech. 10, 161 (1961)] experimental data. Our expression is valid for Ca values up to Ca = 2.0, but approaches Bretherton's result for low values of Ca. The analysis is done in terms of the pressure buildup which originates from the interplay between surface tension and lubrication due to the thin layer of fluid near the tube wall.

1 February 2012 in Chemical Engineering Science
Verified
Journal Article
Closed access
AAAzadeh N. Asadolahi
Azadeh N. Asadolahi
RGRaghvendra Gupta
Raghvendra Gupta
SLShui Yee Leung
Shui Yee Leung
DFDavid F Fletcher
David F Fletcher
BHBrian S. Haynes
Brian S. Haynes