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13 Jul 2009: Fluids, 9 (1966) 1929. 24 T. Kowalski and E. Brundrett, Proc.

10 Jul 2009: C = 0.25χ′′u(0). ,µ. λ= 1.167, ν. λ= 3.00 (24). as |χ′′u(0)| , while for p = 2/3 and µs = 2 these coefficients are 0.24, ... 24) and (dash-dot) 13.0|C|3/2 from Eq. (21), with a numerical fit to thecoefficient.

13 Jun 2009: The the extension to bivariate functions was developed, without analysis,in [24, 25, 27]. ... The bivariate version of this method wasoriginally developed, without analysis, in [24, 25, 27].

23 Jul 2009: Rallison and E. J. Hinch. Without H I 1 84 1 1-24 - a9 With accurate HI 11.474 1-1.814 1-2.064 -2.224 Batchelor (1976, 1983) 1 ... pO as r / a c o , (3.24). and P-D;Vp = ikD,.P on r = 2a.

10 Jul 2009: J. Fluid Mech. (2002), vol. 452, pp. 371–404. c 2002 Cambridge University PressDOI: 10.1017/S0022112001007017 Printed in the United Kingdom. 371. Constitutive laws in liquid-fluidized beds. By P A U L D U R U 1, M A X I M E N I C O L A S1, J O H N

8 Jul 2009: 2004) find. R R0R0. {. 1.24 a, a 1.7. 1.6 a1/2, a 1.7,. ... 24 L. Staron and E. J. Hinch. f of the aspect ratio such that.

21 Jul 2009: py/e K u Ge(b,,, b:,) K E V , , -py/e, 24, v, = 0,.

3 Sep 2009: Despite the numerous results already obtained in thefield, therearestillmanyopenproblemsandtherehasbeenaburstof new experimental results in the last few years [24,25,29,31]. ... and also between solitons [24,25,39] still clearly have a lot

23 Jul 2009: 4 ) gives in ( 3. 8 ) a contribution. 24 AT3 = $ K - = , q 5 ” 0 ( $ ) as # O , ( 3. ... 24 AT3 = = q5 - 89 O(q53ln q5) as q5 0.

3 Sep 2009: R1. 2r0R2. 2. R12. r0 R1 , 24. where a sign has been added to indicate the circulationof the vortex.

26 May 2009: http://journals.cambridge.org Downloaded: 26 May 2009 IP address: 172.16.219.19. J. Fluid Mech. (2008), vol. 611, pp. 395–426. c 2008 Cambridge University Pressdoi:10.1017/S0022112008002942 Printed in the United Kingdom. 395. Very viscous

10 Jul 2009: 0.637, which gives a phase velocity by7!, cr /U l5 2.24, i.e., cr /Vl 5 1.83.

21 Jul 2009: http://journals.cambridge.org Downloaded: 21 Jul 2009 IP address: 131.111.16.227. J. Fluid Mech. (1993), 001. 256, p p. 561-605 Copyright @ 1993 Cambridge University Press. 561. The hydrodynamic force on a rigid particle undergoing arbitrary

13 Jul 2009: x(tj-(O)]=n6D,Ati=2D,t, (24). where the factor l/3 represents the variance of a random number chosen uniformly on [ - 1, 11. ... Res. 24, 2 0 3 3 (1988). L. D e Arcangelis, J.

18 Jul 2009: 578–594. 24.

10 Jul 2009: inside plugs = 54.5%,average particle fraction = 24%, minimum particle fraction inside bubbles = 8.5%.

31 Jul 2009: The interpolations both have the correct qualitative behaviour. The cruder interpolation ( 1 7) is amazingly accurate for the first normal-stress difference, within 24 % for y / D < 20, whereas the inter-

10 Jul 2009: 24)It has been studied by Hooper & Boyd (1983) for unbounded fluid layers (α1 = α2 =) from an asymptotic analysis for β1 1 of the exact dispersion relationship.

14 Jul 2009: J. Fluid Mech. (2009), vol. 630, pp. 391–411. c 2009 Cambridge University Pressdoi:10.1017/S002211200900682X Printed in the United Kingdom. 391. Lagrangian drift near a wavy boundaryin a viscous oscillating flow. E. LARRIEU1, E. J. HINCH2 AND F.

21 Jul 2009: 2.24). terms vanish for the mean. (2.25). (2.26). Relying on the decomposition (2.9) we now write the velocity field V as the sum of two contributions,. ... Ci = Ai Bi, (3.24). Here (O) denotes the semi-infinite fluid domain on one side, either right or

6 May 2009: 1–24 of the Collected Papers, Vol. 3, M. Y. Hussaini, Ed., Oxford.

28 Sep 2009: ui, j =1. rz. ri1/2. ri1/2 z j1/2. z j1/2. ur, zdrdz , 24. ... 24, pp. 273–285. 25J. Li, “Calcul d’interface affine par Morceaux piecewise linear interfacecalculation,” Acad.

13 Jul 2009: TL F r o m all local velocities 0.33 f0.04 0.35 to.05 0.32 20.04 0.24 20.03 0.24 20.03 0.19 ... 1122 1222 24-t-4 173 2023 2324 method.

13 Jul 2009: Received October 24, 1991; in revised form January 13, 1992). Abstract. ... D-2 2 1 and 6 = 4 - -. ( ) 4-D i?L3’ (24).

13 Jul 2009: ELSEVIER Journal of Contaminant Hydrology 16 (1994) 87-108. JOURNAL OF. Contaminant Hydrology. Echo tracer dispersion in model fractures with a rectangular geometry. I. I p p o l i t o a, G. D a c c o r d b, E.J. Hinch e, J.P. H u l i n a

10 Jul 2009: Received 24 January 2002; accepted 11 September 2002; published online 7 March 2003.

30 Nov 2009: The. 24. cubature points are indicated by dots. Derivatives of increasing order are indicated by cir-cles with increasing radius.

8 Jul 2009: Received 18 May 2007; accepted 24 January 2008; published online 29 February 2008.

13 Jul 2009: ARTICLES. Hydrodynamic interactions in deep bed filtrationClaude GhidagliaLaboratoire de Physique et Mecanique des Milieux Hetérogènes, URA 857 au CNRS, ESPCI, 10 rueVauquelin, 75231 Paris Cedex 05, France. Lucilla de ArcangelisLaboratoire de

14 Jul 2009: http://journals.cambridge.org Downloaded: 14 Jul 2009 IP address: 131.111.16.227. J. Fluid Mech. (1996), t d 308, p p. 255-288 Copyright @ 1996 Cambridge University Press. 255. Computer simulations of polymer chain relaxation via Brownian motion. By

10 Jul 2009: B. PerrinLaboratoire de Physique de la Matiere Condensee, UMR 8551, CNRS, Ecole Normale Superieure,Département de Physique, 24 rue Lhomond, 75231 Paris Cedex 05, France.

23 Jul 2009: http://journals.cambridge.org Downloaded: 23 Jul 2009 IP address: 131.111.16.227. J. Fluid Mech. (1977), vol. 83, part 4, p p. 695-720. Printed in Great Britain 695. An averaged-equation approach to particle interactions in a fluid suspension. By E.