Solid holdup and circulation rate in a liquid-solid circulating fluidized bed with viscous liquid medium

Experiments were conducted in a liquid-solid circulating fluidized bed with different viscous liquids and particles to study the hydrodynamics, average solid hold up and solid circulation rate. The effects of operating parameters, i.e., primary liquid flow rate in the riser, auxiliary liquid flow ra...

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Main Authors: Gnanasundaram, N., Loganathan, M., Perumal, Kumar
Format: Journal Article
Published: Brazilian Journal of Chemical Engineering 2015
Online Access:http://hdl.handle.net/20.500.11937/8358
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author Gnanasundaram, N.
Loganathan, M.
Perumal, Kumar
author_facet Gnanasundaram, N.
Loganathan, M.
Perumal, Kumar
author_sort Gnanasundaram, N.
building Curtin Institutional Repository
collection Online Access
description Experiments were conducted in a liquid-solid circulating fluidized bed with different viscous liquids and particles to study the hydrodynamics, average solid hold up and solid circulation rate. The effects of operating parameters, i.e., primary liquid flow rate in the riser, auxiliary liquid flow rate, total liquid flow rate and viscosity of the liquid were studied for solids of different density and particle size. Results show that the circulating fluidization regime starts earlier for more viscous solutions because of the decrease in critical transitional velocity. The onset of solid holdup increases with an increase in liquid viscosity for sand and for glass beads. The solid circulation rate increases with an increase in total velocity and auxiliary velocity, and also increases with increasing viscosity.
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institution Curtin University Malaysia
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last_indexed 2025-11-14T06:20:29Z
publishDate 2015
publisher Brazilian Journal of Chemical Engineering
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spelling curtin-20.500.11937-83582017-09-13T14:38:33Z Solid holdup and circulation rate in a liquid-solid circulating fluidized bed with viscous liquid medium Gnanasundaram, N. Loganathan, M. Perumal, Kumar Experiments were conducted in a liquid-solid circulating fluidized bed with different viscous liquids and particles to study the hydrodynamics, average solid hold up and solid circulation rate. The effects of operating parameters, i.e., primary liquid flow rate in the riser, auxiliary liquid flow rate, total liquid flow rate and viscosity of the liquid were studied for solids of different density and particle size. Results show that the circulating fluidization regime starts earlier for more viscous solutions because of the decrease in critical transitional velocity. The onset of solid holdup increases with an increase in liquid viscosity for sand and for glass beads. The solid circulation rate increases with an increase in total velocity and auxiliary velocity, and also increases with increasing viscosity. 2015 Journal Article http://hdl.handle.net/20.500.11937/8358 10.1590/0104-6632.20150324s00003026 Brazilian Journal of Chemical Engineering unknown
spellingShingle Gnanasundaram, N.
Loganathan, M.
Perumal, Kumar
Solid holdup and circulation rate in a liquid-solid circulating fluidized bed with viscous liquid medium
title Solid holdup and circulation rate in a liquid-solid circulating fluidized bed with viscous liquid medium
title_full Solid holdup and circulation rate in a liquid-solid circulating fluidized bed with viscous liquid medium
title_fullStr Solid holdup and circulation rate in a liquid-solid circulating fluidized bed with viscous liquid medium
title_full_unstemmed Solid holdup and circulation rate in a liquid-solid circulating fluidized bed with viscous liquid medium
title_short Solid holdup and circulation rate in a liquid-solid circulating fluidized bed with viscous liquid medium
title_sort solid holdup and circulation rate in a liquid-solid circulating fluidized bed with viscous liquid medium
url http://hdl.handle.net/20.500.11937/8358