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- W2141039778 abstract "Thermochemical energy storage process in inorganic oxides systems are considered to possess great potential for utilising residual heat. H owever number of technical and scientific problems such as inadequate heat and mass transfers associated with thermochemical energy reactors remain to be overcome. In the past various studies such as integrated metal foam reaction bed system, impreg nation of reactants in consolidated blocks of natural graphite and different configurations of reaction beds have been carried out but dynamic limitations of heat and mass transfers have been observed. Though the intrinsic chemical reaction of working mate rials must be good, the effectiveness of a thermochemical reactor largely depends on excellent rates of heat and mass transfers from the reactor to the external heat transfer fluid since most exothermic reactions are rapid and instantaneous. Fluidised beds are considered to be favourable for rapid exothermal reactions due to the large specific surface area available for reaction and short residences times for gas or solids. To this end, an agitated fluidised bed thermochemical reactor system has been propos ed and investigated with the model results showing enhanced adsorption capacities and heat transfer rates during adsorption process. There is however the need to optimise the thermophysical parameters that affect the minimum fluidising velocity (mfv) in th e adsorption column." @default.
- W2141039778 created "2016-06-24" @default.
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- W2141039778 date "2004-08-16" @default.
- W2141039778 modified "2023-10-16" @default.
- W2141039778 title "Modelling of an Agitated Fluidised Bed Thermochemical Energy Storage System" @default.
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- W2141039778 doi "https://doi.org/10.2514/6.2004-5707" @default.
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