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 ...
Appendix B Conference Paper B.IO A test set conducted using
Appendix B Conference Paper B.Il through conducting clear water pipeline tests. Mean velocity and wall shear stress were measured for velocities over
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Appendix B C<strong>on</strong>ference Paper B.IO<br />
A test set c<strong>on</strong>ducted using <str<strong>on</strong>g>the</str<strong>on</strong>g> facility is defined as a set <str<strong>on</strong>g>of</str<strong>on</strong>g> tests using <str<strong>on</strong>g>the</str<strong>on</strong>g> four different<br />
pipe diameters but <str<strong>on</strong>g>the</str<strong>on</strong>g> same slurry.<br />
3.1 Test Facility<br />
Slurry to be used for a test run is collected in a steel hopper which has a capacity 2m 3 •<br />
From <str<strong>on</strong>g>the</str<strong>on</strong>g>re it is pumped by a four bladed Ma<str<strong>on</strong>g>the</str<strong>on</strong>g>r and Plat! 8x6 solids handling pump,<br />
which is driven by a variable speed hydraulic drive, through <str<strong>on</strong>g>the</str<strong>on</strong>g> pipe circuit. Directly<br />
after <str<strong>on</strong>g>the</str<strong>on</strong>g> pump <str<strong>on</strong>g>the</str<strong>on</strong>g> l50mm line splits up into a 90mm and l50mm pipeline. These two<br />
pipelines have a vertical inverted "U" secti<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> l7m, <str<strong>on</strong>g>the</str<strong>on</strong>g> flowrate being measured in<br />
both downcomer secti<strong>on</strong>s by means <str<strong>on</strong>g>of</str<strong>on</strong>g> magnetic flux flow meters. A horiz<strong>on</strong>tal secti<strong>on</strong><br />
<str<strong>on</strong>g>of</str<strong>on</strong>g> approximately 30m follows with <str<strong>on</strong>g>the</str<strong>on</strong>g> return pipelines passing through an in-line heat<br />
exchanger and pneumatic diverter valve before being re-routed back into <str<strong>on</strong>g>the</str<strong>on</strong>g> hopper.<br />
The l50mm horiz<strong>on</strong>tal return pipeline splits into a l50mm line and a 200mm pipeline<br />
<str<strong>on</strong>g>the</str<strong>on</strong>g> two joining toge<str<strong>on</strong>g>the</str<strong>on</strong>g>r after l2m. The 80mm and 150mm pipelines are PVC with clear<br />
viewing and test secti<strong>on</strong>s located in <str<strong>on</strong>g>the</str<strong>on</strong>g> horiz<strong>on</strong>tal return pipelines. The 200mm line is<br />
steel.<br />
Flowrate can be calibrated by diverting <str<strong>on</strong>g>the</str<strong>on</strong>g> slurry using <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> pneumatic diverter valve<br />
into <str<strong>on</strong>g>the</str<strong>on</strong>g> weigh tank which is located al<strong>on</strong>gside <str<strong>on</strong>g>the</str<strong>on</strong>g> hopper. The weigh tank, which has<br />
a capacity <str<strong>on</strong>g>of</str<strong>on</strong>g> 1,5m 3 and is placed <strong>on</strong> a 1750kg mass scale, is used to calibrate <str<strong>on</strong>g>the</str<strong>on</strong>g><br />
magnetic flux flow meters. After flowrate determinati<strong>on</strong>s <str<strong>on</strong>g>the</str<strong>on</strong>g> slurry is directed back into<br />
<str<strong>on</strong>g>the</str<strong>on</strong>g> looped circuit.<br />
In order to accurately determine <str<strong>on</strong>g>the</str<strong>on</strong>g> rheology <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> slurry a 25mm tube was used. A<br />
tapping is taken from <str<strong>on</strong>g>the</str<strong>on</strong>g> l50mm horiz<strong>on</strong>tal return pipeline and using <str<strong>on</strong>g>the</str<strong>on</strong>g> back pressure,<br />
slurry was circulated through <str<strong>on</strong>g>the</str<strong>on</strong>g> 25mm pipeline into <str<strong>on</strong>g>the</str<strong>on</strong>g> weigh tank. The flowrate was<br />
measured using a 25mm nominal bore Altometer magnetic flux flowmeter. The flowrate<br />
<str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> slurry was checked by doing a calibrati<strong>on</strong> using <str<strong>on</strong>g>the</str<strong>on</strong>g> weigh tank during a 25mm<br />
pipe test.<br />
No external agitati<strong>on</strong> was required to maintain solids suspensi<strong>on</strong> in <str<strong>on</strong>g>the</str<strong>on</strong>g> hopper for <str<strong>on</strong>g>the</str<strong>on</strong>g><br />
slurries which were tested.<br />
3.2 Measured Variables<br />
Readings <str<strong>on</strong>g>of</str<strong>on</strong>g> head loss were taken at varying velocities and <str<strong>on</strong>g>the</str<strong>on</strong>g> data obtained was used<br />
to plot a pseudo-shear diagram.<br />
3.3 Water Tests<br />
The hydraulic pipe roughness for each <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> four pipe <str<strong>on</strong>g>size</str<strong>on</strong>g>s was first determined