Search
Search Funnelback University
- Refined by:
- Date: 2004
1 -
10 of
27
search results for KaKaoTalk:ZA31 24 24 |u:www.itg.cam.ac.uk
where 0
match all words and 27
match some words.
Results that match 2 of 3 words
-
flm608.dvi
www.itg.cam.ac.uk/people/heh/Paper177.pdf9 Mar 2004: 6.3 6.3 24.3 5.89 1.00 3.86 9.6 6.1 3.8 0.7417 6.3 6.3 24.3 10.71 1.00 ... 86 9.6 8.2 5.2 0.8118 6.3 6.3 24.3 20.37 1.00 3.86 9.6 11.3 7.1 0.8919 13.2 -
jb002019 1..16
www.itg.cam.ac.uk/people/heh/Paper176.pdf9 Mar 2004: are captured by Figure 4.[24] The calculations in Figure 4 illustrate that volcanic. -
Theoret. Comput. Fluid Dynamics (1998) 10: 201–212Theoretical and…
www.itg.cam.ac.uk/people/heh/Paper140.pdf9 Feb 2004: r = (F/πV )1/2. (2.24)In contrast to the instantaneous, fixed volume release of the last section, there is not a finite radius at whichthe mass of particulate matter ... Applying these concepts to the relationship for the density of deposit for a single -
PII: S0301-9322(98)00062-7
www.itg.cam.ac.uk/people/heh/Paper151.pdf9 Mar 2004: rNt 0 rN0 24. M. Ungarish, H.E. Huppert / International Journal of Multiphase Flow 25 (1999) 715737 725. ... For this case. the box model yields [rN/rN(0)]max=[8Fr/(3 b)]1/4. (This is by about 24% smaller than for. -
PHYSICS OF FLUIDS VOLUME 13, NUMBER 12 DECEMBER 2001 ...
www.itg.cam.ac.uk/people/heh/Paper167.pdf9 Feb 2004: H 0 1!5 2F P12 f P1 1! 4.24! FIG. 2. ... On applicationthe boundary conditions4.23! and 4.24!, we find that. a 5 4.523 102 3, F P15 2 8.42 for Fr5 11.9. -
Using PHF format
www.itg.cam.ac.uk/people/heh/Paper150.pdf9 Feb 2004: The volume fration of particles in suspension evolves as23,24. df. dt5. ... X5 x/l , 24! T5 t/ v sl /q!1/ a 2 1!, 25! -
Tuesday Informal Lunch Seminars
www.itg.cam.ac.uk/seminars/tue_1.10/lent_2004.html10 Feb 2004: 24 February. Steve Roper. (ITG). Magma fracture in tough materials. 2 March. -
J. Fluid Mech. (2000), vol. 418, pp. 1–23. Printed ...
www.itg.cam.ac.uk/people/heh/Paper155.pdf9 Mar 2004: Indeed, for most of the experimentsdiscussed by TML λ was in the range 0.02–0.24. ... tr dr rN. drNdthN. (2.24). We eliminate h/t with the aid of (2.12) and, after some rearrangement, we againobtain the result (2.22). -
J. Fluid Mech. (1997), vol. 344, pp. 291–316. Printed ...
www.itg.cam.ac.uk/people/heh/Paper139.pdf9 Mar 2004: 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. -
J. Fluid Mech. (2002), vol. 472, pp. 333–371. c© ...
www.itg.cam.ac.uk/people/heh/Paper172.pdf9 Mar 2004: Sm =. 0. (ni=1. ψi(0) exp (2Viy))1/2. dy. (2.24). Recall thatn. ... 1 = 2/H0. (3.24)Hence from (3.16), by forming an expansion for ϕi, we find that.
Search history
Recently clicked results
Recently clicked results
Your click history is empty.
Recent searches
Recent searches
Your search history is empty.