Microconvective Thermal Conductivity in Disperse Two-Phase Mixtures as Observed in a Low Velocity Couette Flow Experiment

1981 ◽  
Vol 103 (1) ◽  
pp. 47-51 ◽  
Author(s):  
C. W. Sohn ◽  
M. M. Chen

Eddy transport associated with microscopic flow fields in shearing two-phase flows was investigated. Although such microconvective effects are expected to be present in all disperse two-phase flows, usually they are masked by other collateral mechanisms and could not be studied critically. In the present study, effective thermal conductivities of neutrally buoyant solid-fluid mixtures were measured in a rotating Couette flow apparatus. Low Reynolds numbers were used to avoid the effects of turbulence. Significant enhancement in effective thermal conductivity was observed when the Ped were high. Here Ped = ed2/αf where e is the local mean shear rate, d is the particle diameter, and αf is the thermal diffusivity of the fluid. Volume fractions employed were φ = 0.15 and 0.30 for polyethylene beads (2.9 mm in diameter) in a mixture of silicone oil and kerosene, and φ = 0.15 for polystyrene particles (0.3 mm in diameter) in a mixture of silicone oil and Freon-113. Single-phase liquid mixtures were also measured in various shear rates to show that the thermal conductivity was independent of shear rate and hence the observed phenomenon was not an instrumental artifact. The dependence of conductivity on particle Peclet number appeared to approach a power law relationship ke ∝ Ped1/2 for high Peclet numbers (300 < Ped < 2000).

2016 ◽  
Vol 65 (7) ◽  
pp. 1690-1697 ◽  
Author(s):  
Zhongke Gao ◽  
Yuxuan Yang ◽  
Lusheng Zhai ◽  
Ningde Jin ◽  
Guanrong Chen

2001 ◽  
Author(s):  
Kendra V. Sharp ◽  
Ronald J. Adrian

Abstract Despite the growing interest in microfluidic systems, the study of two-phase flows in such systems thus far has been somewhat limited in scope. Examples of recent studies of two-phase flows in microchannels include flows containing liquid and gas (Tran, 1998; Stanley, 1997), the dispersion of laminar fluid streams (Galambos, 1998), and the flow of very dilute particle suspensions through micropumps (Jang et al., 1999). The present experiments identify ‘shear-induced arching’ as a new mechanism causing microtube blockage. This mechanism is most likely to occur when 0.33D &lt; dp &lt; 0.46D, where dp is the particle diameter and D is the microtube diameter, and was observed for flows of particle-laden fluids with concentration, ϕ, as low as 0.5%. Following a simple geometrical analysis, for 0.33D &lt; dp &lt; 0.46D, it can be shown that once the particles are in the arching configuration, lateral forces induced by the shear on the arch can hold the particles in place and stabilize the arch. Experiments were performed over a range of particle-to-rube diameter ratios. As predicted, if enough of the particles in any given experiment had a diameter of 0.33D–0.46D, blockages occurred in the microtube.


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