Analysis of hydrodynamic phenomena in a fluidized bed for thermochemical hydrogen production
type: CreativeWork
description: This thesis examines transport phenomena of cupric chloride (CuCI2) hydrolysis within a fluidized bed. Conversions of CuCi2 and steam as a fluidizing gas are numerically investigated using a new non-catalytic gas-solid reaction model, proposed in the literature but here updated for the purposes of the present study. The results are illustrated considering two cases of kinetics for the consumption of particles: Volumetric Model and Shrinking Core Model. Consistent results in terms of the conversion of reactants versus superficial velocity, bed inventory and bed temperature are obtained by developing new solution algorithms abased on each of the above kinetic models.
abstract: This thesis examines transport phenomena of cupric chloride (CuCI2) hydrolysis within a fluidized bed. Conversions of CuCi2 and steam as a fluidizing gas are numerically investigated using a new non-catalytic gas-solid reaction model, proposed in the literature but here updated for the purposes of the present study. The results are illustrated considering two cases of kinetics for the consumption of particles: Volumetric Model and Shrinking Core Model. Consistent results in terms of the conversion of reactants versus superficial velocity, bed inventory and bed temperature are obtained by developing new solution algorithms abased on each of the above kinetic models.
author: Haseli, Yousef
language: en
keywords: Cupric Chloride, Fluidized bed, Transport phenomena, Hydrodynamics
date published: 2008-04-01
date modified: 2026-07-24T05:35:28Z
provider: Ontario Institute of Technology
publisher: Networked Digital Library of Theses and Dissertations
type: WebPage
source organization: University of Ontario Institute of Technology

PropertyValue
property ID: Handle
value: https://hdl.handle.net/10155/7