scholarly journals Vortex precession in thin elliptical ferromagnetic nanodisks

2017 ◽  
Vol 433 ◽  
pp. 59-63 ◽  
Author(s):  
C.E. Zaspel
Keyword(s):  
2010 ◽  
Vol 41 (4) ◽  
pp. 465-478 ◽  
Author(s):  
S. I. Shtork ◽  
Sergei Alekseenko ◽  
V. L. Okulov ◽  
P. A. Kuibin

2000 ◽  
Author(s):  
Xin Fu ◽  
Huayong Yang

Abstract Having the advantages of no motion elements, high reliability, undemanding maintenance and good medium flexibility, the swirl meter has been widely used to measure the gas, liquid and steam in chemical, petroleum as well as processing industries. For the current one-piezoelectric-pressure-sensor swirl meter, however, the measuring error caused by the interference pressure oscillation limits its application in the system where pressure is unsteady, or a noisemaker is nearby. In this paper, the fluid dynamic features inside the channel of the swirl meter are studied numerically and by experiment. The time dependent vortex motions as well as the hydrodynamic vibrations within the channel of the swirl meter are simulated using the CFD approaches of the RNG k-ε model. The computed flow fields indicate that the eccentric motion of vortexes initiates an axisymmetric pressure oscillation within the vortex precession area of the swirl meter. The frequency of the oscillation shifts linearly with volume flow rates. Both the calculated and the measured results prove that the hydrodynamic vibrations on the arbitrary axisymmetric points are equal in amplitude and frequency but with a 180 degree phase difference. By installing differential pressure transducers on such the axisymmetric points, the signals of the vortex pressure oscillations are enhanced, while the interferential signals are suppressed, enabling the anti-interference performance and low-flowrate sensibility of the swirmeter to be effectively improved.


2016 ◽  
Vol 40 (4) ◽  
pp. 1072-1081 ◽  
Author(s):  
Desheng Chen ◽  
Baoling Cui ◽  
Zuchao Zhu

Measurements of flow rates of fluids are important in industrial applications. Swirlmeters (vortex precession meters) are widely used in the natural gas industry because of their advantage in having a large measurement range and strong output signal. In this study, using air as a working medium, computational fluid dynamics (CFD) simulations of a swirlmeter were conducted using the Reynolds-averaged Navier–Stokes (RANS) and renormalization group (RNG) k–ε turbulence models. The internal flow characteristics and the influence of the tube structure (geometric parameter of flow passage) on metrological performance were studied, with a particular focus on the meter factor. Calibration experiments were performed to validate the CFD predictions; the results show good agreement with those from simulations. From the streamline distributions, a clear vortex precession is found in the throat region. At the end of throat, the pressure fluctuation reached a maximum accompanied by the largest shift in the vortex core from the centreline. There exists a large reverse flow zone in the vortex core region in the convergent section. To mitigate the influence of reverse flow on vortex precession, a suitable length of throat is required. For a larger convergent angle, the fluid undergoes higher acceleration leading to an increase in velocity that produces more intensive pressure fluctuations. The minor diameter of the throat also produces a higher velocity and larger meter factor. Compared with both divergent angle and throat length, the convergent angle and throat diameter play a more important role in determining precession frequency.


2000 ◽  
Vol 85 (14) ◽  
pp. 2857-2860 ◽  
Author(s):  
B. P. Anderson ◽  
P. C. Haljan ◽  
C. E. Wieman ◽  
E. A. Cornell

2013 ◽  
Vol 110 (23) ◽  
Author(s):  
Mohamed El Ketara ◽  
Etienne Brasselet

2001 ◽  
Vol 65 (2) ◽  
Author(s):  
L. Hough ◽  
L. A. K. Donev ◽  
R. J. Zieve
Keyword(s):  

2014 ◽  
Vol 9 (3) ◽  
pp. 39-48
Author(s):  
Elizaveta Gesheva ◽  
Sergey Shtork ◽  
Sergey Alekseenko

The work is focused on a detailed study of the characteristics of the vortex flow in the chamber tangential type, modeling, in particular, the common furnace coal-fired boilers. It was shown that the vortex structure formed in the chamber with diaphragm is a vortex filament with the relative radius rm / R = 0,1 and a length of about the size of the camera l / R = 6. During researches it was measured the velocity field and vortices using a static method of diagnosis flow PIV, and performed the verification of calculated data obtained using the LES and DES methods for simulation of turbulent flows in the CFD package Star CCM +. Calculated velocity profiles and vortex precession frequency agree with experimental data, which indicates the correctness of chosen approach of modeling of turbulent swirling flow


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