Conditions of Non-uniform Fluidization in an Auto-oscillating Mode

Korniyenko, Bogdan; Kornienko, Yaroslav; Haidai, Serhii; Liubeka, Andrii; Huliienko, Serhii

doi:10.1007/978-3-031-03877-8_2

Cited by 4 publications

(3 citation statements)

References 22 publications

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“…For the case of flat slits through which gas jets are supplied, the diameter of the formed bubble at the top of the gas jet, which has a cylindrical shape, is calculated by the equation [4]:…”

Section: Presentation Of the Main Materialsmentioning

confidence: 99%

“…Works [1,4,5] show that the use of IJPF in the process of production of granulated organic-mineral fertilizers with an equivalent diameter of granules of 2.5÷4.0 mm by dewatering 50%(wt.) of the aqueous composite liquid phase achieved the specific load of the surface of the fluidized bed by moisture, which accounts for 1°C of driving force, exceeds by 1.55 times the similar indicator in the bubbling mode.…”

Section: Presentation Of the Main Materialsmentioning

confidence: 99%

“…For a better distribution of working liquid phase, the authors [2][3][4] proposed the introduction of liquid heterogeneous system during granulation into the middle of the fluidized bed using a mechanical disperser.…”

Section: Introductionmentioning

confidence: 99%

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