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 ...

digitalknowledge.cput.ac.za
from digitalknowledge.cput.ac.za More from this publisher
03.07.2013 Views

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

Appendix B Conference Paper B.Il through conducting clear water pipeline tests. Mean velocity and wall shear stress were measured for velocities over ong>theong> test range and roughness was determined using ong>theong> Colebrook / White (1939) equation. 3.3 Material Used The solids material used for testing purposes was kaolin clay and sand. Tests were conducted using kaolin clay and ong>theong>n a mixture ong>ofong> kaolin clay and No. 2 Foundry Sand from Consol at varying concentrations. - Kaolin Clay Kaolin clay was obtained from ong>theong> Serina Kaolin (Pty) Ltd which is currently mining a kaolin deposit at Brakkekloong>ofong>, Fish Reek, Cape Town, South Africa. The kaolin was delivered in ong>theong> form ong>ofong> pellets and filter cakes. To obtain a homogenous slurry ong>theong> pellets or filter cake was thoroughly mixed with water using a recirculating pipe after ong>theong> pump back into ong>theong> hopper before circulating ong>theong> slurry through ong>theong> pipelines. - Sand Sand was obtained from Consol in 25kg bags called No. 2 Foundry Sand. The ong>particleong> ong>sizeong> ong>ofong> ong>theong> sand was between 75 and 350 I'm. 3.3.1 Mixtures ong>ofong> Kaolin Clay and Sand The sand used was found to form a settling slurry with water. In order to obtain a homogeneous slurry, kaolin clay was used as a suspending agent for ong>theong> sand. Tests were ong>theong>refore conducted to determine ong>theong> amount ong>ofong> kaolin clay needed to suspend ong>theong> sand. It was found that kaolin clay at a concentration ong>ofong>at least Cv = 5% was required. 3.4 Particle Size Distribution The ong>particleong> ong>sizeong> ong>distributionong> ong>ofong>ong>theong> kaolin clay/sand mixture was obtained by combining ong>theong> PSD ong>ofong>ong>theong> kaolin clay (determined using a Malvern 2600/3600 Particle Sizer VF.6) and ong>theong> PSD ong>ofong> ong>theong> sand determined through sieving. The dS5 was ong>theong>n obtained from ong>theong> combined PSD's as shown below in Figure 1. 4. ANALYSIS & RESULTS The measured variables ong>ofong> head loss and velocity were used to plot pseudo-shear diagrams ie wall shear stress vs pseudo-shear rate. A typical pseudo-shear diagram is shown in Figure 2 and ong>theong> improvement obtained using ong>theong> new model, is clearly visible, as opposed to ong>theong> oong>theong>r ong>theong>oretical models.

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

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!