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Very viscous horizontal convection
www.damtp.cam.ac.uk/user/hinch/publications/JFM611_395.pdf26 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 -
PHYSICS OF FLUIDS VOLUME 14, NUMBER 3 MARCH 2002 ...
www.damtp.cam.ac.uk/user/hinch/publications/PhysFluids_14_922.pdf10 Jul 2009: 0.637, which gives a phase velocity by7!, cr /U l5 2.24, i.e., cr /Vl 5 1.83. -
The hydrodynamic force on a rigid particle undergoing arbitrary…
www.damtp.cam.ac.uk/user/hinch/publications/JFM256_601.pdf21 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 -
Tracer dispersion in 2-D fractures with flat and rough walls in a…
www.damtp.cam.ac.uk/user/hinch/publications/PoF_5_1952.pdf13 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. -
Powder flow down a vertical pipe: the effect of air flow
www.damtp.cam.ac.uk/user/hinch/publications/JFM459_317.pdf10 Jul 2009: inside plugs = 54.5%,average particle fraction = 24%, minimum particle fraction inside bubbles = 8.5%. -
CondonDeanoIserles.dvi
www.damtp.cam.ac.uk/user/na/NA_papers/NA2009_05.pdf18 Jul 2009: 578–594. 24. -
‘Phase diagram’ of interfacial instabilities in a …
www.damtp.cam.ac.uk/user/hinch/publications/JFM414_195.pdf10 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. -
http://journals.cambridge.org Downloaded: 31 Jul 2009 IP address:…
www.damtp.cam.ac.uk/user/hinch/publications/JFM76_187.pdf31 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- -
Lagrangian drift near a wavy boundary in a viscous oscillating flow
www.damtp.cam.ac.uk/user/hinch/publications/JFM630_391.pdf14 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. -
Nonlinear drift interactions between fluctuating colloidal particles: …
www.damtp.cam.ac.uk/user/hinch/publications/JFM256_343.pdf21 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
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