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 ...
Preamble LIST OF TABLES Page xvi Page 3.1 Pipeline diameters 3.12 3.II Pipeline roughness 3.13 3.III d S5 Sizes for
Preamble NOMENCLATURE Svrnbol Description Unit a constant A constant cross sectional area m2 A, area ratio b constant B constant roughness function c constant C concentration CD drag coefficient d
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- Page 5 and 6: Preamble ACKNOWLEDGEMENrS Page v I
- Page 7: Preamble Page vii CHAPTER 1: INTROD
- Page 10 and 11: Preamble 3.8 Experimental Procedure
- Page 12 and 13: Preamble Page xii LIST OF FIGURES P
- Page 14: Preamble Page xiv 4.5 Optimum repre
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Preamble<br />
NOMENCLATURE<br />
Svrnbol Descripti<strong>on</strong> Unit<br />
a c<strong>on</strong>stant<br />
A c<strong>on</strong>stant<br />
cross secti<strong>on</strong>al area m2 A, area ratio<br />
b c<strong>on</strong>stant<br />
B c<strong>on</strong>stant<br />
roughness functi<strong>on</strong><br />
c c<strong>on</strong>stant<br />
C c<strong>on</strong>centrati<strong>on</strong><br />
CD drag coefficient<br />
d <str<strong>on</strong>g>particle</str<strong>on</strong>g> diameter !Lm<br />
D internal pipe diameter m<br />
E error functi<strong>on</strong><br />
rheological parameter<br />
f Fanning fricti<strong>on</strong> factor<br />
F force N<br />
k c<strong>on</strong>stant<br />
hydraulic roughness !Lm<br />
K fluid c<strong>on</strong>sistency index Pa.s·<br />
K' apparent fluid c<strong>on</strong>sistency index Pa.s·'<br />
I average amplitude <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> liquid oscillati<strong>on</strong><br />
:£ PrandtI mixing length m<br />
L pipe length m<br />
m slope<br />
rheological parameter<br />
M mass kg<br />
n flow behaviour index<br />
Page xvii
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