1986
DOI: 10.1051/jphys:019860047060100100
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Scaling analysis of convective solute transport and segregation in Bridgman crystal growth from the doped melt

Abstract: To cite this version:D. Camel, J.J. Favier. Scaling analysis of convective solute transport and segregation in Bridgman crystal growth from the doped melt. Journal de Physique, 1986, 47 (6)

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Cited by 60 publications
(13 citation statements)
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References 22 publications
(22 reference statements)
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“…It therefore has to be assumed that the flow cannot be laminar, in which case the proportionality constant between u N (d) and d 2 is given as the ratio of the bulk velocity u B to the square of the hydrodynamic boundary layer d H . Invoking again the scaling arguments developed in Camel and Favier [28] the ratio d H /h should scale as Re À1/2 . Setting h = 600 lm and m = 4 Â 10 À7 m 2 s À1 , the resulting algebraic equation yields a value for u B of about 0.35 m s À1 , which results in a Reynolds number slightly above 500, confirming that the flow in the drop is indeed inertial.…”
Section: Control By Si Transportmentioning
confidence: 97%
See 1 more Smart Citation
“…It therefore has to be assumed that the flow cannot be laminar, in which case the proportionality constant between u N (d) and d 2 is given as the ratio of the bulk velocity u B to the square of the hydrodynamic boundary layer d H . Invoking again the scaling arguments developed in Camel and Favier [28] the ratio d H /h should scale as Re À1/2 . Setting h = 600 lm and m = 4 Â 10 À7 m 2 s À1 , the resulting algebraic equation yields a value for u B of about 0.35 m s À1 , which results in a Reynolds number slightly above 500, confirming that the flow in the drop is indeed inertial.…”
Section: Control By Si Transportmentioning
confidence: 97%
“…Therefore, consistency arguments require the bulk velocity to be much larger than the above mentioned 2-5 Â 10 À3 m s À1 . More precisely, as the tangential component of the convective velocity is expected to increase linearly with the distance to the solid front d, continuity arguments developed for a related solidification problem by Camel and Favier [28] show that the normal velocity should scale with d 2 . In laminar flows, the proportionality coefficient between u N (d) and d 2 is given as the ratio of the bulk velocity u B to the square of the smallest macroscopic dimension of the drop, here its height h. Even with conservative estimates h = 600 lm, d = 2 lm and u N (d) = 2 Â 10 À3 m s À1 would result in a u B value of 180 m 2 s À1 .…”
Section: Control By Si Transportmentioning
confidence: 98%
“…Indeed, it is mainly the flow in the solute boundary layer that, by penetrating into a thin region of the mush beneath the envelope of the cell/dendrite tips, also washes nickel out of the mush. Knowing Dh, estimates can be obtained for the radial temperature gradient, G R ¼ G Dh=R, and the Grashoff number which gives the strength of thermal convection [23], Gr ¼ b T gG R R 4 =n 2 with b T ( ¼ 1 Â 10 À4 /K) the coefficient of thermal expansion of the melt, g the acceleration of gravity and n (¼ 4 Â 10 À7 m 2 =s) the kinematic viscosity. For G ¼ 25 K=cm, G R ¼ 1:7 K=cm and Gr ¼ 650, so that the order of magnitude of the flow velocity in the bulk nGr 1=2 =R ¼ 0:2 cm=s.…”
Section: Article In Pressmentioning
confidence: 99%
“…[46] Experimental minimum values of the melt height (5 mm) and liquid temperature gradient (10 K/ cm) give an experimental lower limit for Gr of 4.0 · 10 4 . This indicates that convection was present during the growth, supporting the smaller boundary layers calculated with the FR analysis.…”
Section: B Analysis Of Experimental Resultsmentioning
confidence: 99%