THERMAL EFFECT ON BUBBLE RISE – AN EXPERIMENTAL STUDY

Authors:

Kishore Kumar Dhar,Asish Mitra,Paritosh Bhattacharya,

DOI NO:

https://doi.org/10.26782/jmcms.2022.03.00002

Keywords:

Bubble,Temperature Gradient,Rise Velocity,Water ,

Abstract

This paper presents the findings of an experimental study on the effect of temperature gradient on bubble rise velocity in water. At the bottom of the chamber holding water, a bubble (equivalent diameter, req 1 mm) is created and rises through it. At a height of 60 cm from the chamber's bottom, a high-speed camera (1000 fps, Kodak, Model 1000 HRC) is mounted with a 90 mm Macro lens. It is connected to a computer. For image capture and processing, the commercial tools Sigma Scan Pro 5.0 and Adobe Photoshop are used. The chamber can be heated with infrared light, resulting in a constant temperature gradient of 1.10C/cm between 30 and 40 cm above the needle in the water. Bubble rise characteristics, such as bubble size and rise velocity, are determined both in the presence and absence of a temperature gradient. The current study clearly demonstrates that this gradient causes an additional increase in terminal rise velocity.

Refference:

I. Arnold, K. and M. Stewart, Surface production operations. 3rd ed. Vol. 1. 2008, Amsterdam: Elsevier. 768 p.
II. Abdel-Aal, H.K., M. Aggour, and M.A. Fahim, Petroleum and gas field processing. 2003, New York: Marcel Dekker. XII, 364 p.
III. A. Mitra, T K Dutta & D N Ghosh, Natural Convective Heat Transfer in Water Enclosed Between Pairs of Differentially Heated Vertical Plates, Heat and Mass Transfer, 45, 2008, 187-192.
IV. A. Mitra, T K Dutta & D N Ghosh, Augmentation of Heat Transfer in a Bubble-agitated Vertical Rectangular Cavity, Heat and Mass Transfer, 48, 2012, 695-704.
V. Bybee, K., Production of heavy crude oil: Topside experiences on Grane, Journal of petroleum technology, 2007. 59(4): p. 86-89.
VI. Baker, A.C. and J.H. Entress, The VASPS subsea separation and pumping system.Chemical engineering research & design, 1992. 70(1): p. 9-16.
VII. Cohen, D.M. and P.A. Fischer, Production systems hit the seafloor running, World Oil, 2008. 229(1): p. 71-8.
VIII. CDS engineering and FMC Technologies, CDS StatoilHydro Degasser. [cited 2009 March 23]; Available from: http://www.fmctechnologies.com/upload/factsheet_cds_degasser.pdf.
IX. Clift, R., J.R. Grace, and M.E. Weber, Bubbles, drops, and particles. 1978, New York: Academic Press, xiii, 380 p.
X. Gjerdseth, A.C., A. Faanes, and R. Ramberg. The Tordis IOR Project, in Offshore technology conference, 2007. Houston.
XI. Grace, J.R., Shapes and velocities of bubbles rising in infinite liquids, Transactions of the Institution of Chemical Engineers, 1973. 51(2): p. 116-120.
XII. Grace, J.R., Shapes and velocities of single drops and bubbles moving freely through immiscible liquids, Transactions of the Institution of Chemical Engineers, 1976. 54(3): p. 167-173.
XIII. Haugan, J.A., Challenges in heavy crude oil – Grane, an overview, Journal of petroleum technology, 2006. 58(6): p. 53-54.
XIV. Lima Ochoterena, R. and Zenit, R., 2003, Visualization of the flow around a bubble moving in a low viscosity liquid, Revista Mexicana De Fisica 49, 348-352.
XV. Mitra A, Bhattacharya P, Mukhopadhyay S, Dhar K K, “Experimental Study on Shape and Path of Small Bubbles using Video-Image Analysis,” 2015 Third International Conf. On Computer, Communication, Control And Information Technology, 7 – 8 February 2015, Academy of Technology, Hooghly, West Bengal, India
XVI. Speight, J.G., The chemistry and technology of petroleum. 1999, New York: Marcel Dekker. xiv, 918 p.
XVII. Shoham, O. and G.E. Kouba, State of the art of gas/liquid cylindrical-cyclone compact-separator technology, Journal of petroleum technology, 1998. 50(7): p. 58-65.
XVIII. Schinkelshoek, P. and H.D. Epsom, Supersonic gas conditioning – Commercialisation of Twister technology, in GPA conference. 2008: Grapevine, Texas, USA.

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