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 ...

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

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>.

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