2014
DOI: 10.1016/j.egypro.2014.03.091
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Experimental Investigation into a Packed Bed Thermal Storage Solution for Solar Gas Turbine Systems

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Cited by 44 publications
(27 citation statements)
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“…These results are successfully simulated thanks to the one-dimensional two-phase model from Mumma and Marvin, 1976, which is used to investigate the most efficient bed configuration to store a given heat power during a given time period. Klein et al, 2014Klein et al, , 2010, studied a 28-kWh packed bed of ceramic beads running up to 900°C. The system suffers from flow channelling near the tank's wall but the phenomenon is taken into account and correctly simulated by a two-dimensional three-phase model.…”
Section: Introductionmentioning
confidence: 99%
“…These results are successfully simulated thanks to the one-dimensional two-phase model from Mumma and Marvin, 1976, which is used to investigate the most efficient bed configuration to store a given heat power during a given time period. Klein et al, 2014Klein et al, , 2010, studied a 28-kWh packed bed of ceramic beads running up to 900°C. The system suffers from flow channelling near the tank's wall but the phenomenon is taken into account and correctly simulated by a two-dimensional three-phase model.…”
Section: Introductionmentioning
confidence: 99%
“…As described by Zanganeh et al (2012), the dominant temperature dependent property is the solid phase heat capacity. The temperature dependent heat capacity of candidate ceramic storage materials is presented by Klein et al (2014b). The materials considered in the current study undergo small changes in heat capacity when the temperature range of analysis is above 350 C. Thus the assumption of constant thermophysical properties improves the simulation time and does not introduce solution errors.…”
Section: Governing Equationsmentioning
confidence: 99%
“…3. Details of the testing programme are provided in Klein et al (2014b). Tests were conducted over the temperature ranges 350-900°C and 600-900°C.…”
Section: Tes Model Validationmentioning
confidence: 99%
“…Achenbach [14] showed that the void fraction is higher in the near-wall region of a PBR due to the stacking of particles, leading to a non-uniform flow resistance across the bed and hence changes in the velocity profile and radial temperature distribution. Klein et al [15] investigated the radial temperature distribution in a high-temperature packed bed, showing that solid particles at the tank wall increased in temperature slower than those in the centre. It was hypothesised this was due to increased heat losses to the wall via radiation and convection.…”
Section: Modelling Of Packed Bed Regeneratorsmentioning
confidence: 99%