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 ...
Chapter 3 Experimental Work Page 3.16 The following procedure was undertaken for calibrating
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Chapter 3 Experimental Work Page 3.16<br />
The following procedure was undertaken for calibrating <str<strong>on</strong>g>the</str<strong>on</strong>g> magnetic flow meters.<br />
I. The pump speed was set to <str<strong>on</strong>g>the</str<strong>on</strong>g> desired speed.<br />
2. The weigh tank scale reading was noted (Ml)'<br />
3. The data logger was first started and <str<strong>on</strong>g>the</str<strong>on</strong>g>n <str<strong>on</strong>g>the</str<strong>on</strong>g> diverter valve was opened and <str<strong>on</strong>g>the</str<strong>on</strong>g><br />
stopwatch started at <str<strong>on</strong>g>the</str<strong>on</strong>g> same time.<br />
4. The diverter valve was closed and <str<strong>on</strong>g>the</str<strong>on</strong>g> stopwatch stopped at <str<strong>on</strong>g>the</str<strong>on</strong>g> same time when<br />
sufficient slurry had been collected. The data logger ran for a pre-set time, enough<br />
to cover <str<strong>on</strong>g>the</str<strong>on</strong>g> whole procedure.<br />
5. The weigh tank reading .was noted (M,).<br />
The flow rate for each reading is given by <str<strong>on</strong>g>the</str<strong>on</strong>g> equati<strong>on</strong>:<br />
(3.9)<br />
The average transducer reading cannot be used for calibrati<strong>on</strong> purposes as it is not accurate.<br />
In order to obtain <str<strong>on</strong>g>the</str<strong>on</strong>g> correct transducer reading for each point a graph <str<strong>on</strong>g>of</str<strong>on</strong>g> current signal vs<br />
time was plotted. Figure 3.13 shows a typical output.<br />
As can be seen from <str<strong>on</strong>g>the</str<strong>on</strong>g> graph <str<strong>on</strong>g>the</str<strong>on</strong>g> current signal drops sharply after <str<strong>on</strong>g>the</str<strong>on</strong>g> diverter valve is<br />
opened (point A) before c<strong>on</strong>stantly decreasing (point B to point C). After <str<strong>on</strong>g>the</str<strong>on</strong>g> diverter valve<br />
is closed (point C) <str<strong>on</strong>g>the</str<strong>on</strong>g> current signal reading returns to <str<strong>on</strong>g>the</str<strong>on</strong>g> original value (point D). The<br />
slope <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>the</str<strong>on</strong>g> line BC remains c<strong>on</strong>stant at <str<strong>on</strong>g>the</str<strong>on</strong>g> varying pump speeds. The transducer reading<br />
is thus read by extending a line EF from <str<strong>on</strong>g>the</str<strong>on</strong>g> slope <str<strong>on</strong>g>of</str<strong>on</strong>g> line BC halfway during <str<strong>on</strong>g>the</str<strong>on</strong>g> time taken<br />
to divert <str<strong>on</strong>g>the</str<strong>on</strong>g> slurry to <str<strong>on</strong>g>the</str<strong>on</strong>g> weigh tank (point A to point C).<br />
The calibrati<strong>on</strong> equati<strong>on</strong> is <str<strong>on</strong>g>the</str<strong>on</strong>g>n derived by performing a linear regressi<strong>on</strong> <strong>on</strong> <str<strong>on</strong>g>the</str<strong>on</strong>g> flow rate<br />
and <str<strong>on</strong>g>the</str<strong>on</strong>g> transducer readings in each case.<br />
No difference was found between <str<strong>on</strong>g>the</str<strong>on</strong>g> laminar and <strong>turbulent</strong> flow data when calibrated in this<br />
Way, as indicated by Fig 3.14 showing a typical calibrati<strong>on</strong>.