Back to results

University of Houston

Fluids Viscosity Effect on Non-Isothermal Buoyancy-Driven Exchange Flow in Inclined Pipes

Abstract

dc:description.abstract

Buoyancy-driven exchange flow is studied experimentally for different Atwood numbers, inclination angles and fluid pairs. The density difference drives the flow, that is achieved through added salinity for isothermal case and temperature difference for the non-isothermal case. Detailed benchmarking experiments were run for isothermal and non-isothermal cases. The degree of flow instability and mixing was found to increase as the inclination angle moves towards vertical, in both isothermal and non-isothermal experiments. The influence of temperature in the non-isothermal experiments caused a significant increase in the flow instability and diffusion. The rate of fluids interpenetration was measured showing an asymmetry from the observed non-isothermal results. The heavy cold finger advances at a faster rate compared to the light hot fluid finger. This phenomenon was quantified for the full range of inclination angles and Atwood numbers. The effect of temperature-viscosity relation on the dynamics of the flow was studied experimentally. Each fluid phase was viscosified separately, maintaining the same density difference. The viscosities were varied by adding Xanthan gum. The effect of viscosity ratio was quantified by measuring the front velocity of the fluid fingers over the full range of inclination angles. Same density difference was maintained in both isothermal and non-isothermal experiments. The fluids interpenetration rate was maximum for intermediate inclination angles and was observed in both isothermal and non-isothermal (without Xanthan gum) cases. The overall observed asymmetry for visosified experiments was found to be less compared to the non-isothermal experiments (without Xanthan gum) at any given Atwood number.

Degree

thesis:*
Name thesis:degree_name
Master of Science
Level thesis:degree_level
Masters
Discipline thesis:degree_discipline
Engineering Technology
Grantor
University of Houston
Year dc:date.issued
2019

Author and committee

dc:creator, dc:contributor.*
Author dc:creator
  • Ravichandran, Gaarthick
Advisor dc:contributor.advisor
  • Alba, Kamran
Committee members dc:contributor.committeemember
  • Singh, Navdeep
  • El Nahas, Medhat

Subjects

dc:subject × 1

Rights

dc:rights
Statement dc:rights
  • The author of this work is the copyright owner. UH Libraries and the Texas Digital Library have their permission to store and provide access to this work. Further transmission, reproduction, or presentation of this work is prohibited except with permission of the author(s).
Language dc:language.iso
eng

Identifiers

dc:identifier.*
Handle dc:identifier.uri
https://hdl.handle.net/10657/5637
OAI identifier oai:identifier
oai:uh-ir.tdl.org:10657/5637

Chain of custody

source
Harvested from
University of Houston
Base URL
uh-ir.tdl.org/server/oai/request
Last updated
2026-07-24
Source record
OAI-PMH GetRecord
citation

Ravichandran, Gaarthick. Fluids Viscosity Effect on Non-Isothermal Buoyancy-Driven Exchange Flow in Inclined Pipes. Masters thesis, University of Houston, 2019. https://hdl.handle.net/10657/5637