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 Page xii LIST OF FIGURES Page 2.1 illustration
Preamble Page xiii 2.18 Comparison
- Page 1 and 2: THE EFFECT OF THE PARTICLE SIZE DIS
- Page 3 and 4: Preamble DECLARATION Page iii I, Ga
- 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 14: Preamble Page xiv 4.5 Optimum repre
- Page 17 and 18: Preamble NOMENCLATURE Svrnbol Descr
- Page 19 and 20: Preamble T shear stress Pa T y yiel
- Page 23 and 24: Chapter I For example: Introduction
- Page 25 and 26: Chapter 1 Introduction Page 1.5 1.3
- Page 27 and 28: CHAPTER 2
- Page 33: Chapter 2 Literature Review Page 2.
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- Page 46 and 47: Chapter 2 Literature Review Viscous
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Preamble Page xii<br />
LIST OF FIGURES<br />
Page<br />
2.1 illustrati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> Newt<strong>on</strong>'s law <str<strong>on</strong>g>of</str<strong>on</strong>g> viscosity 2.5<br />
2.2 Rheological models for n<strong>on</strong>-Newt<strong>on</strong>ian fluids 2.8<br />
2.3 Forces acting <strong>on</strong> a fluid element in larninar flow 2.12<br />
2.4 Typical pipeline test data for three pipe diameters 2.14<br />
2.5 Graphical representati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> Metzner & Reed approach 2.15<br />
2.6 Magnified view <str<strong>on</strong>g>of</str<strong>on</strong>g> a rough wall pipe showing regi<strong>on</strong>s <str<strong>on</strong>g>of</str<strong>on</strong>g> <strong>turbulent</strong> flow 2.18<br />
2.7 Magnified view <str<strong>on</strong>g>of</str<strong>on</strong>g> a rough wall pipe showing <str<strong>on</strong>g>the</str<strong>on</strong>g> viscous sub-layer<br />
and <str<strong>on</strong>g>the</str<strong>on</strong>g> slurry <str<strong>on</strong>g>particle</str<strong>on</strong>g>s 2.20<br />
2.8 Graphical comparis<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> Blasius, Knudsen & Katz and v<strong>on</strong> Karmen<br />
fricti<strong>on</strong> factor equati<strong>on</strong>s for <strong>turbulent</strong> flow 2.21<br />
2.9 Comparis<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> law <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> wall for smooth and rough pipes 2.25<br />
2.10 Moody diagram 2.28<br />
2.11 The Dodge & Metzner correlati<strong>on</strong> shown <strong>on</strong> a fricti<strong>on</strong> factor-Reynolds<br />
number diagram<br />
2.29<br />
2.12 Comparis<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> Dodge & Metzner predicti<strong>on</strong> curve and Kemblowski &<br />
Kolodziejski experimental data for <str<strong>on</strong>g>the</str<strong>on</strong>g> flow <str<strong>on</strong>g>of</str<strong>on</strong>g> a 30% aqueous kaolin<br />
suspensi<strong>on</strong> at n'=O,39 (taken from Kemblowski & Kolodziejski, 1973) 2.32<br />
2.13 illustrati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> area ratio 2.34<br />
2.14 Unsheared plug geometry 2.35<br />
2.15 Velocity pr<str<strong>on</strong>g>of</str<strong>on</strong>g>ile in <strong>turbulent</strong> flow 2.38<br />
2.16 Comparis<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> <strong>turbulent</strong> velocity <str<strong>on</strong>g>distributi<strong>on</strong></str<strong>on</strong>g> between a n<strong>on</strong>-Newt<strong>on</strong>ian<br />
slurry and air at Re=40600<br />
2.17 Comparis<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> relative turbulence intensities between a n<strong>on</strong>-Newt<strong>on</strong>ian<br />
slurry and air at Re=40600<br />
2.42<br />
2.43