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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.

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

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.

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

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.

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.