the effect of the particle size distribution on non-newtonian turbulent ...
the effect of the particle size distribution on non-newtonian turbulent ...
the effect of the particle size distribution on non-newtonian turbulent ...
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Chapter 2 Literature Review Page 2.35<br />
I<br />
Pipe wall<br />
Sheared<br />
annulus<br />
The Reyno1ds number is given by<br />
where<br />
and<br />
D ohear = D - D p,ug •<br />
Annular<br />
velocity<br />
Figure 2.14: Unsheared plug geometry<br />
Plug diameter<br />
Pipe diameter<br />
Slatter (1994) used <str<strong>on</strong>g>the</str<strong>on</strong>g> following precepts as <str<strong>on</strong>g>the</str<strong>on</strong>g> basis <str<strong>on</strong>g>of</str<strong>on</strong>g> his <strong>turbulent</strong> flow model:<br />
(2.69)<br />
(2.70)<br />
(2.71)<br />
• The velocity <str<strong>on</strong>g>distributi<strong>on</strong></str<strong>on</strong>g> is logarithmic and similar to <str<strong>on</strong>g>the</str<strong>on</strong>g> classic Newt<strong>on</strong>ian<br />
<strong>turbulent</strong> velocity <str<strong>on</strong>g>distributi<strong>on</strong></str<strong>on</strong>g> over <str<strong>on</strong>g>the</str<strong>on</strong>g> entire core regi<strong>on</strong>.<br />
• A roughness <str<strong>on</strong>g>effect</str<strong>on</strong>g> is caused by <str<strong>on</strong>g>the</str<strong>on</strong>g> solid <str<strong>on</strong>g>particle</str<strong>on</strong>g>s.