(56e) Flow Analysis of an Atypical Cylindrical Cyclone Separator with a Large Ratio of Length to Diameter | AIChE

(56e) Flow Analysis of an Atypical Cylindrical Cyclone Separator with a Large Ratio of Length to Diameter

Authors 

GAO, Z. - Presenter, China University of Petroleum, Beijing
WANG, J., China University of Petroleum, Beijing
WANG, J., China University of Petroleum, Beijing
MAO, Y., China University of Petroleum, Beijing
Wei, Y., China University of Petroleum
This study presents a flow analysis on an atypical cylindrical cyclone separator with a large ratio of length to diameter. Due to the distribution of the flow field determines the merits of separation performance, the aim is to optimize the flow. The Phase Doppler Particle Analyzer (PDPA) is used to measure the gas flow, and the numerical simulation is carried out by using the Reynolds Average Navier-Stokes (RANS) equation, the Reynolds stress model (RSM). Since the model is validated by good agreement between the numerical results and experimental data, and then the tangential velocity is analyzed from the transient flow field and dynamic performance.

The results showed that the tangential velocity of the transient flow field existed a non-axisymmetric phenomenon in the cross section, which was mainly presented as asymmetric distribution of the contours. The zero location of tangential velocity value was not coincide with the geometric center, where the tangential velocity was larger near the zero location. In addition, the dynamic character of tangential velocity was high-speed pulsating, with quasi-periodic characteristic. The structure or operation optimization could change the pulsation frequency and reduce the industrial vibration, which is highly significant.

Meanwhile, a parameter of RMS was used to identify the degree of turbulence velocity deviating from mean velocity. The RMS data showed that the flow instability gradually increased with the fluid flowing into the cyclone separator from the inlet section, until reached a peak value at the position about 2.0 times the length to diameter. And then the flow instability gradually decreased, with the fluid energy dissipated.

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