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flm903.dvi
www.itg.cam.ac.uk/people/heh/Paper180.pdf10 Jun 2004: a. r – riri. sandsaltricecouscoussugar slope 1.24. Figure 9. The non-dimensional radial excursion, (r ri )/ri , as a function of the aspect ratioa with a < 1.7 for sand, salt, ... A straight line through the origin atslope 1.24 has a regression -
PII: S1359645497004692
www.itg.cam.ac.uk/people/heh/Paper144.pdf12 Mar 2004: requires. P q02pd. : 24. Equation (24) thus links the dendrite tip radius to. ... This solution has a scaled tip radius P = 10.8. and a scaled tip position Z 2:24. -
59576 479..507
www.itg.cam.ac.uk/people/heh/Paper173.pdf9 Mar 2004: H.) 3–24 (Springer, Berlin, 1990). 5. Nakada, S., Shimizu, H. & Ohta, K. -
flm608.dvi
www.itg.cam.ac.uk/people/heh/Paper177.pdf9 Mar 2004: 6.3 6.3 24.3 5.89 1.00 3.86 9.6 6.1 3.8 0.7417 6.3 6.3 24.3 10.71 1.00 ... 86 9.6 8.2 5.2 0.8118 6.3 6.3 24.3 20.37 1.00 3.86 9.6 11.3 7.1 0.8919 13.2 -
PII: S0301-9322(98)00062-7
www.itg.cam.ac.uk/people/heh/Paper151.pdf9 Mar 2004: rNt 0 rN0 24. M. Ungarish, H.E. Huppert / International Journal of Multiphase Flow 25 (1999) 715737 725. ... For this case. the box model yields [rN/rN(0)]max=[8Fr/(3 b)]1/4. (This is by about 24% smaller than for. -
J. Fluid Mech. (2002), vol. 458, pp. 283–301. c© ...
www.itg.cam.ac.uk/people/heh/Paper171.pdf9 Mar 2004: These substitutions transform (2.24) into. uN = I(hN) = Fr(hN) h1/2N. ... Appendix. The functions I and χA.1. The function I(hN). From the definitions (2.19), (2.24) and (2.25) we obtain. -
J. Fluid Mech. (2001), vol. 432, pp. 201–217. Printed ...
www.itg.cam.ac.uk/people/aa/JFM1.pdf9 Mar 2004: 15 P 24.2 P25.2 L25.2 P25.2 P30.2 L. T (C) T (C). -
J. Fluid Mech. (2001), vol. 432, pp. 201–217. Printed ...
www.itg.cam.ac.uk/people/heh/Paper159.pdf9 Mar 2004: 15 P 24.2 P25.2 L25.2 P25.2 P30.2 L. T (C) T (C). -
J. Fluid Mech. (2000), vol. 418, pp. 1–23. Printed ...
www.itg.cam.ac.uk/people/heh/Paper155.pdf9 Mar 2004: Indeed, for most of the experimentsdiscussed by TML λ was in the range 0.02–0.24. ... tr dr rN. drNdthN. (2.24). We eliminate h/t with the aid of (2.12) and, after some rearrangement, we againobtain the result (2.22). -
J. Fluid Mech. (2001), vol. 447, pp. 1–29. c© ...
www.itg.cam.ac.uk/people/heh/Paper164.pdf9 Mar 2004: 0.9993 4.81 0 1.52 – –S3 0 45.8 79.80 0.574 1.375 1.0192 0.9996 19.24 0 1.36 – –S7 0 45.2 ... 19.24 0.0282 1.37 550 0.100R10 0.0500 46.3 79.97 0.579 1.390 1.0107 1.0007 9.80 0.0551 0.99 450
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