Suspending solid particles in an agitated conical-bottom tank
โ Scribed by L. Musil; J. Vlk
- Publisher
- Elsevier Science
- Year
- 1978
- Tongue
- English
- Weight
- 744 KB
- Volume
- 33
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
โฆ Synopsis
An investigation of the critical impeller speed at which particulate solnds become fully suspended in the hquid by mechanical sturring has been carried out Based on balances of kinetic energy, two theoretical equations were denved gaving the cntical impeller speed as a function of physical properties of the mixed slarry as well as of several selected geometrical parameters of the mixing device
Both theoretical equations were employed for the treatment of results obtained by experimentation
(\rightarrow) the first one which was derived under the assumption of no loss of energy correlated well data obtained in the experimental region where impeller clearance had no effect upon the critical impeller speed
(\rightarrow) the second one which includes loss of energy due to its viscous dissipation agreed well with the experimental results showing a linear dependence of the critical impeller speed upon the impeller clearance
๐ SIMILAR VOLUMES
A diffusion-reaction model is presented for describing noncatalytic fluid-solid reaction in an agitated slurry where the solid particles are polydisperse. The model equations consist of a composite of subsystems each described by a distinct Thiele modulus and collectively coupled through the bulk ph
measurement of density and gas hold-up in a three-phase Hydrodynamics of Fischer-Tropsch synthesis in slurry catalytic reactor. Brit. Chem. Engng 9, 83G832. bubble column reactors. Proc. Fifth DOE Indirect Farley, R. and Ray, D. J., 1964b, The design and operation of a Liquefaction Contractors' Meet