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- W2389590395 abstract "By setting a Kenics static mixer into the device of horizontal liquid-solids two-phase fluidized bed heat exchange tube,experiment was performed using saturated calcium sulfate solution as working medium. The pressure drop results of the horizontal liquid-solids fluidized bed heat exchange tube with a Kenics static mixer were presented. The effects of working fluid velocity,Kenics static mixer twist ratio,solids volume fraction and size on pressure drop were discussed,and compared with the variation of pressure drop in cold state. The pressure drop of setting the Kenics static mixer in heat exchange tube was found to be about 20%—140% over the case without setting the Kenics static mixer under the same operation conditions. Pressure drop increased with increasing Reynolds number and decreased with increasing twist ratio. Moreover,pressure drop was found to increase with increasing volume fraction,but the effect was not significant. On the basis of experiment data,an empirical equation for pressure drop was established. It provides some theoretical information for the optimal design of the liquid-solids two-phase fluidized bed." @default.
- W2389590395 created "2016-06-24" @default.
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- W2389590395 date "2013-01-01" @default.
- W2389590395 modified "2023-09-28" @default.
- W2389590395 title "Researches on pressure drop of horizontal liquid-solids two-phase fluidized bed heat exchang tube with Kenics static mixer" @default.
- W2389590395 hasPublicationYear "2013" @default.
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