Hydrodynamics of a centrifugal separator for separating a gas-liquid stream

1979 ◽  
Vol 15 (2) ◽  
pp. 118-120
Author(s):  
V. G. Sister ◽  
M. M. Veviorovskii ◽  
V. I. Chernyshev
2000 ◽  
Author(s):  
H. J. Kang ◽  
B. Zheng ◽  
C. X. Lin ◽  
M. A. Ebadian

Abstract The velocity distributions inside a centrifugal separator with outside and inside diameters of 152.4 mm (6″) and 76.2 mm (3″), respectively, have been investigated experimentally and numerically to obtain optimum separation efficiency. Two 12.7 mm (1/2-inch) holes were drilled on the external surface of the separator to measure the velocity distribution in the separator. Two direction velocities (tangential direction along the cylinder surface and axial along the vertical direction) were measured to compare with the numerical simulation results. A 6060P Pitot probe was employed to obtain the velocity distribution. The dust samples (a mixture of steel particle and dust) from the dust collection box were analyzed using a Phillips XL30 Scanning Electron Microscope. FLUENT code is used as the numerical solver for this fully three-dimensional problem. The fluid flow in the separator is assumed to be steady and incompressible turbulent flow. The standard k–ε model was employed in this study. Non-uniform, unstructured grids are chosen to discretize the entire computation domain. Almost 100,000 cells are used to discretize the whole separator. The constant velocity profile is imposed on the inlet plane. The pressure boundary condition is adopted at outlet plane. Comparing the velocity distribution and separation efficiency from the experiment and the numerical modeling shows that the experimental results and the estimated data agree fairly well and with a deviation within ±10%.


2016 ◽  
Vol 4 (1) ◽  
pp. 7
Author(s):  
Siney Viana

Mineral processing plants make use of several types of equipments for size separation (size classification) to segregate ore particles by size. A particular type of such equipments is the centrifugal separator, which is intended to receive an input stream of ore slurry to be partitioned into two output streams: a coarse and a fines one. The coarse stream contains most of the coarse solids particles of the slurry, whereas the fines stream contains most of the fine particles. Although a centrifugal separator intends to perform a physical segregation of the solids particles by their size, a chemical segregation also results, in such a way that the chemical content of the coarse and the fines streams are normally different from the content of the input stream. When evaluating the performance of the separation process, three fundamental aspects should be analyzed: 1) the size distribution of the solids particles in each stream; 2) the amount of solids mass from the input stream that goes to the coarse stream and to the fines stream, that is, the mass partition; and 3) the chemical content of each stream. This work presents the application of the Least Squares method of optimization to calculate the mass partition, based on the measured chemical content of the streams, and on the metallurgical balance equations of the separation process.


AIChE Journal ◽  
2016 ◽  
Vol 62 (6) ◽  
pp. 2213-2226 ◽  
Author(s):  
H. E. M. Ninahuanca ◽  
H. Stel ◽  
R. E. M. Morales ◽  
C. Ofuchi ◽  
M. J. da Silva ◽  
...  

2020 ◽  
Vol 55 (8) ◽  
pp. 1012-1028
Author(s):  
Z. M. Malikov ◽  
M. E. Madaliev

2020 ◽  
Author(s):  
Ramsey White ◽  
Simone Mulas ◽  
Ahmed Al-Jughayman

2004 ◽  
Vol 40 (1) ◽  
pp. 59-61 ◽  
Author(s):  
V. G. Chekmenev ◽  
Yu. N. Lebedev ◽  
V. D. Kos' min

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