Search

23 Jul 2009: The differential equation can be integrated directly taking Po = 24 to produce an implicit expression for the shape. ... z = 0s-1 F 24( 1 - F2). which when substituted in the volume constraint yields.

10 Jul 2009: For A60,with an initial capillary pressure of 0.76 times the total elastic modulus, a pre-stretch of 3 anda finite extension of L1 = 24 (cf. ... The continuous curves are (a) for A40,L1 = 77 and P = 5; (b) for A60, L1 = 24 and P = 3; (c) for A80 L1 = 4.5

10 Jul 2009: π2/24, 24/π) (0.4112, 7.639), although the numerical results suggestthat the analysis of 4 requires β 1 101 rather than β 1. ... 24/(βT ) (lower), wherein the factor 2 has been included to translate the lines.

8 Jul 2009: σtotn = 1Ca. κn, on ΓM(t). (24). Since there is no fixed boundary in this problem, the purely.Lagrangian approach is well adapted to it. ... Non-Newtonian Fluid Mech. 110 (2–3)(2003) 77–102. [24] R.F. Liang, M.R. Mackley, Rheological

23 Jul 2009: 7 2 13.3 19.7 34.0 % / a , 1.33 1.64 2.13 2-55 3.63 4.24 5. ... Even for r = 30 a 24 Yo variation from axisymmetry produces a drift in 6 from &7r to approximately.

8 Jul 2009: B. PerrinLaboratoire Pierre Aigrain, UMR 8551, CNRS, Ecole Normale Supérieure, Département de Physique,24 rue Lhomond, 75231 Paris Cedex 05, France.

13 May 2009: Van,cn(α, β, nz) =. 0(t α)a(t β)cenφ(t) dt, (4.23). withφ(t) = zt log(t α) log(t β) (4.24). ... Iserles (DAMTP, University of Cambridge). 24. References. [1] Milton Abramowitz and Irene A.

8 Jul 2009: 2 a1.02r30. In both geometries, the final slope at the front is much lower than the slope thatwould be given by an internal angle of friction δ = tan1(µ) = 24.

14 Jul 2009: Phys. Fluids A 5, 13-24. SMART, J. R. & LEIGHTON, D.

1 Dec 2009: 3.24). The corresponding result is the following. Theorem 2 Let f(y) be constant, then we have θ0 = 0, θ1 = ̺ and. ... θs = (s 1)̺, s 2.Proof We shall use formula (3.24) and proceed along the lines of theproof of Theorem.

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,.

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: 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

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