Shapes and terminal velocity of a drop rising in stagnant liquids

In this project, the effects of the density ratio ?, the viscosity ratio ?, the inverse viscosity number ? ?, and the Eötvös number Eo on the shapes and terminal velocities of a drop rising in stagnant liquids are studied numerically using a front tracking method. It is found that mild variation...

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Main Author: Liu, Lili.
Other Authors: School of Mechanical and Aerospace Engineering
Format: Final Year Project
Language:English
Published: 2012
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Online Access:http://hdl.handle.net/10356/49435
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Institution: Nanyang Technological University
Language: English
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spelling sg-ntu-dr.10356-494352023-03-04T19:27:17Z Shapes and terminal velocity of a drop rising in stagnant liquids Liu, Lili. School of Mechanical and Aerospace Engineering Tang Hui DRNTU::Engineering::Mechanical engineering::Fluid mechanics In this project, the effects of the density ratio ?, the viscosity ratio ?, the inverse viscosity number ? ?, and the Eötvös number Eo on the shapes and terminal velocities of a drop rising in stagnant liquids are studied numerically using a front tracking method. It is found that mild variation of ? barely changes the drop shape or terminal velocity, whereas ?, ? ? and Eo significantly affect the drop dynamics. With the increase of ?, ? ?, or Eo, the drop becomes either more dimpled or more crescent. When the drop is dimpled or ellipsoidal-cap, there is no recirculation flow in its rear. The recirculation zone appears and becomes larger when ? decreases or Eo increases. From the simulation results, the relationships between Fr, the non-dimensional terminal velocity of the drop, and ?, ? ? and Eo are determined. For the correlation between Fr and ?, it is found that Fr= ?(1+ ?1 ?)/(2+ ?2 ?) for 5< ? ?<38, where ?1 = 1.245±0.165, and ?2 = 3.43±0.35, whereas Fr is a constant around 0.602 for 50< ? ?<100. The correlation between Fr and ? ? follows a logarithmic trend for ? ?<50. And Fr is also found to decrease with the increase of Eo. Bachelor of Engineering (Mechanical Engineering) 2012-05-18T07:16:59Z 2012-05-18T07:16:59Z 2012 2012 Final Year Project (FYP) http://hdl.handle.net/10356/49435 en Nanyang Technological University 42 p. application/pdf
institution Nanyang Technological University
building NTU Library
continent Asia
country Singapore
Singapore
content_provider NTU Library
collection DR-NTU
language English
topic DRNTU::Engineering::Mechanical engineering::Fluid mechanics
spellingShingle DRNTU::Engineering::Mechanical engineering::Fluid mechanics
Liu, Lili.
Shapes and terminal velocity of a drop rising in stagnant liquids
description In this project, the effects of the density ratio ?, the viscosity ratio ?, the inverse viscosity number ? ?, and the Eötvös number Eo on the shapes and terminal velocities of a drop rising in stagnant liquids are studied numerically using a front tracking method. It is found that mild variation of ? barely changes the drop shape or terminal velocity, whereas ?, ? ? and Eo significantly affect the drop dynamics. With the increase of ?, ? ?, or Eo, the drop becomes either more dimpled or more crescent. When the drop is dimpled or ellipsoidal-cap, there is no recirculation flow in its rear. The recirculation zone appears and becomes larger when ? decreases or Eo increases. From the simulation results, the relationships between Fr, the non-dimensional terminal velocity of the drop, and ?, ? ? and Eo are determined. For the correlation between Fr and ?, it is found that Fr= ?(1+ ?1 ?)/(2+ ?2 ?) for 5< ? ?<38, where ?1 = 1.245±0.165, and ?2 = 3.43±0.35, whereas Fr is a constant around 0.602 for 50< ? ?<100. The correlation between Fr and ? ? follows a logarithmic trend for ? ?<50. And Fr is also found to decrease with the increase of Eo.
author2 School of Mechanical and Aerospace Engineering
author_facet School of Mechanical and Aerospace Engineering
Liu, Lili.
format Final Year Project
author Liu, Lili.
author_sort Liu, Lili.
title Shapes and terminal velocity of a drop rising in stagnant liquids
title_short Shapes and terminal velocity of a drop rising in stagnant liquids
title_full Shapes and terminal velocity of a drop rising in stagnant liquids
title_fullStr Shapes and terminal velocity of a drop rising in stagnant liquids
title_full_unstemmed Shapes and terminal velocity of a drop rising in stagnant liquids
title_sort shapes and terminal velocity of a drop rising in stagnant liquids
publishDate 2012
url http://hdl.handle.net/10356/49435
_version_ 1759857436121890816