1963
DOI: 10.1016/0017-9310(63)90055-3
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A note on heat transfer between spherical particles and a fluid in a bed

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Cited by 8 publications
(3 citation statements)
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“…Prediction of steam explosions requires accounting for the multiphase heat transfer between the volcaniclastic particles and liquid water. Several multiphase heat transfer models have been advanced in the fields of chemical and nuclear engineering over the last 30 years [ Gunn , 1978; Zabrodsky , 1963]. These approaches commonly develop an empirical heat transfer coefficient for the mean heat transfer from the dispersed phase to the fluid.…”
Section: Introductionmentioning
confidence: 99%
“…Prediction of steam explosions requires accounting for the multiphase heat transfer between the volcaniclastic particles and liquid water. Several multiphase heat transfer models have been advanced in the fields of chemical and nuclear engineering over the last 30 years [ Gunn , 1978; Zabrodsky , 1963]. These approaches commonly develop an empirical heat transfer coefficient for the mean heat transfer from the dispersed phase to the fluid.…”
Section: Introductionmentioning
confidence: 99%
“…For an assemblage of particles, such as a fixed bed, the lower limiting value for the Sherwood or Nusselt numbers has been calculated by theory to be 2 or somewhat above 2, depending on the bed voidage (Rowe, 1963;Rowe and Claxton, 1965;Zabrodsky, 1963). In direct opposition to these theoretical predictions, the measured Sherwood and Nusselt numbers of over a dozen investigators (Kunii and Suzuki, 1967) do not level off but keep falling continuously as the Reynolds number is lowered.…”
Section: Gas-solid Mass Transfermentioning
confidence: 99%
“…The theories which predict a leveling off of Sherwood or Nusselt numbers concern local coefficients; the coefficients reported by experiment are those measured in beds with their bypassing and channeling but which assume plug flow of gas through the bed. Zabrodsky (1963) recognized that the large extent of by- passing of solids by bubbling gas could be the reason for the lowered observed coefficients, and he proposed a model which viewed that the surplus gas beyond that needed for minimum fluidization bypassed one or more rows of solids, then mixed completely with the percolating gas. This process is repeated throughout the bed.…”
Section: Gas-solid Mass Transfermentioning
confidence: 99%