Viscous flow model for particle trajectories and deposition efficiency on a single rectangular fibre in an electric field

Author(s):  
K. Adamiak
1981 ◽  
Author(s):  
Yaakov Shima ◽  
Gabor Kalman ◽  
Paul Carini

2004 ◽  
Vol 43 (9A) ◽  
pp. 6020-6025 ◽  
Author(s):  
Won-Young Chung ◽  
Tai-Kyung Kim ◽  
Yero Lee ◽  
Jin-Young Yoon ◽  
Hyun-Woo Kim ◽  
...  

Author(s):  
Won-young Chung ◽  
Tai-kyung Kim ◽  
Young-tae Kim ◽  
Byung-joon Hwang ◽  
Young-kwan Park ◽  
...  

Author(s):  
C. Y. Cheong ◽  
P. T. Ireland ◽  
S. Ashforth-Frost

Theoretical predictions have been compared with experiment for a single semi-confined impinging jet. The turbulent air jet discharged at Re = 20 000 and impinged at nozzle-to-plate spacings (z/d) of 2 and 6.5. Experimental velocity profiles were obtained using hot-wire anemometry. Theoretical velocity profiles were derived using stagnation three-dimensional flow model and viscous flow model for an axisymmetric case. For z/d = 2, velocity profiles in the inviscid region of the near wall flow can be predicted accurately using the stagnation flow model. As the edge of the jet is approached, the flow becomes complex and, as expected, cannot be predicted using the model. Prediction of boundary layer profiles using the viscous flow solution for an axisymmetric case is also reasonable. For z/d = 6.5, the developing impinging jet is essentially turbulent on impact and consequently predictions of near wall flow field, using both the theoretical models, are inappropriate.


SPE Journal ◽  
2012 ◽  
Vol 18 (01) ◽  
pp. 38-49 ◽  
Author(s):  
Mohammad R. Rahmanian ◽  
Roberto Aguilera ◽  
Apostolos Kantzas

Summary In this study, single-phase gas-flow simulation that considers slippage effects through a network of slots and microfractures is presented. The statistical parameters for network construction were extracted from petrographic work in tight porous media of the Nikanassin Group in the Western Canada Sedimentary Basin (WCSB). Furthermore, correlations between Klinkenberg slippage effect and absolute permeability have been developed as well as a new unified flow model in which Knudsen number acts implicitly as a flow-regime indicator. A detailed understanding of fluid flow at microscale levels in tight porous media is essential to establish and develop techniques for economic flow rate and recovery. Choosing an appropriate equation for flow through a single element of the network is crucial; this equation must include geometry and other structural features that affect the flow as well as all variation of fluid properties with pressure. Disregarding these details in a single element of porous media can easily lead to flow misinterpretation at the macroscopic scale. Because of the wide flow-path-size distribution in tight porous media, a variety of flow regimes can exist in the equivalent network. Two distinct flow regimes, viscous flow and free molecular flow, are in either side of this flow-regime spectrum. Because the nature of these two types of flow is categorically different, finding/adjusting a unified flow model is problematic. The complication stems from the fact that the viscosity concept misses its meaning as the flow regime changes from viscous to free molecular flow in which a diffusion-like mechanism dominates. For each specified flow regime, the appropriate equations for different geometries are studied. In addition, different unified flow models available in the literature are critically investigated. Simulation of gas flow through the constructed network at different mean flow pressures leads to investigating the functionality of the Klinkenberg factor with permeability of the porous media and pore-level structure.


Author(s):  
Kai Zhang ◽  
Jianzhong Lin ◽  
Mingzhou Yu

The flow and electric field are simulated numerically with finite volume method first, then large number of nanoparticles and microparticles are injected into the microchannel separately, and these particles are traced with the Lagrangian method. It has been found that particle deposition efficiency in the bend usually decreases first then increases with particle size increasing, and there usually exists a minimum value and it corresponds to the particle diameter of about 3μm, which means that kind of particle can transport longer distance. The electric field doesn’t affect that specified value. This conclusion is helpful to the optimization of the design of microchips.


Fuel ◽  
2016 ◽  
Vol 181 ◽  
pp. 887-894 ◽  
Author(s):  
Lidong Geng ◽  
Gensheng Li ◽  
Pacelli Zitha ◽  
Shouceng Tian ◽  
Mao Sheng ◽  
...  

2015 ◽  
Vol 23 (1) ◽  
pp. 312 ◽  
Author(s):  
G. T. Jasion ◽  
J. S. Shrimpton ◽  
Y. Chen ◽  
T. Bradley ◽  
D. J. Richardson ◽  
...  

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