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17 May 2006: 4Laboratoire de Physique Statistique, UMR 8550 CNRS, Ecole Normale Supérieure, 24,rue Lhomond, 75231 Paris cédex 05, France. ... 1. 2. –12. 3. 10. G. I. IG. (ν. /g2 ). 1/3. ̂. H(g/ν2)1/3 Ĥ. ̂ (Ĥ/)10/3Π15/9. Π15/24. Π15/96. Π1–1/6

9 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

26 Mar 2023: 1r. rrp1r. n2. r2p1 = 0. (4.24). The solution, finite at r = 0, is p1(r, t) = k(t)rn, so that now p(r, θ, t) = p0(r, t)

7 Aug 2008: Uc ={. (3 2M)1/4β, for M 2D 3/24/3 3,(3/24/3 2D M.

30 May 2006: Stability of a large gas bubble rising through liquid 417. 24. ... 1. oo 1.712 1.26 1.42 1.10 1.24. 13.61 1.200 0.79 1.06 1.

11 Apr 2013: 2 2 2. 24/.467. 35.1 Introduction.

1 Jun 2006: 0.01 (for Ra, = lo@), convection continues in the melt until t = 0.24, by which time the system is about 40% solidified.

18 May 2017: on the y-axis,with τ of (a) 0.085, (b) 0.24, (c) 0.39, (d) 0.55, (e) 0.71, ( f ) 0.87, (g) 1.00 and ... mUmH. 3F10 , (4.23). q= UmH2. sin2/3 θE2/3eq D1F1/30 , (4.24).

10 Mar 2011: Hr XNn1. dhndx. dxnd1. XNn1. hn! 3XNn1. h3n. 24. 35, ð61aÞ.

26 Apr 2006: e-mail: grae@esc.cam.ac.uk; heh1@esc.cam.ac.uk. (Received 24 July and in revised form 27 March 1997). ... 24/3λRa1/3 (3.1). between the Nusselt number Nu for thermal convection in the liquid region and theRayleigh number.