Numerical and experimental investigations were carried out to improve the knowledge of the flow field in solid/liquid suspensions in agitated vessels and to examine the ability of the commercial CFD, code CFX 4.2, for this application. The numerical results were compared with our own experimental re
Power consumption in the agitation of solid-liquid suspensions
β Scribed by R. H. Kohler; Joseph Estrin
- Publisher
- American Institute of Chemical Engineers
- Year
- 1967
- Tongue
- English
- Weight
- 301 KB
- Volume
- 13
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
β¦ Synopsis
AH = enthalpy change, cal./g.-mole psoz = partial pressure of sulfur dioxide, atm. poa = partial pressure of oxygen, atm. R = universal gas constant, 1.98 cal./(g.-mole) ( O K . ) ro = initial reaction rate, 1b.-moles sulfur dioxide/ (hr.) AS = entropy change, cal./ (g.-mole) ( O K . ) T = absolute temperature, O K . n = total pressure, atm.
π SIMILAR VOLUMES
The onset speed of gas induction and the power consumption after gas induction were studied in a gas-induced type agitated tank. In such an agitated tank, four unique baffles which were shorter and narrower than the conventional ones were adopted. Two 45Β‘ downward pitched blade turbines (PBT) in ser