1996
DOI: 10.1016/0301-9322(95)00071-2
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Flow pattern maps for solid-liquid flow in pipes

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Cited by 161 publications
(90 citation statements)
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References 7 publications
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“…The distribution of the solid volume fraction upstream the step shows the typical trend of the heterogeneous suspension flow in a straight pipe (Doron and Barnea, 1996), and seems not to be affected by the step even at x/D = -1. For x/D between 0 and about 10, the flow recirculates.…”
Section: Solids Volume Fraction Distributionmentioning
confidence: 81%
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“…The distribution of the solid volume fraction upstream the step shows the typical trend of the heterogeneous suspension flow in a straight pipe (Doron and Barnea, 1996), and seems not to be affected by the step even at x/D = -1. For x/D between 0 and about 10, the flow recirculates.…”
Section: Solids Volume Fraction Distributionmentioning
confidence: 81%
“…As the velocity decreases, the solid particles accumulate at the pipe bottom and form a packed bed moving along the pipe. The concentration of this layer is the maximum packing one (Doron and Barnea, 1996;Doron et al, 1987). At last, when the mixture velocity is insufficient to keep all the immersed particles in motion, a stationary deposit is observed at the bottom of the pipe.…”
Section: Introductionmentioning
confidence: 99%
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“…Doron et al [19] and Doron and Barnea [25] mentioned that the mixture viscosity can be assumed as liquid viscosity because the coarse particles do not affect the viscosity of the whole mixture. However, in the applications discussed here the cuttings sizes are very small with larger surface area which makes them much more surface interactive with the mud and cosiness between the particles through large physico-chemical interaction and therefore they will alter the viscosity of the mixture compared to coarser particles.…”
Section: Cuttings Transport In the Annulus Spacementioning
confidence: 99%