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Gliffy Diagram |
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size | L |
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name | NTU vs Vc |
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page | AGUACLARA:Relations between Vc and NTU |
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pageid | 10945299 |
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align | right |
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space | AGUACLARA |
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If this suspension were in a column that was monitored by a turbidimeter, the fast settling particles would settle past the turbidimeter first and then much later the small particles would settle past the turbidimeter sensor. Thus the turbidity vs time plot is shown below.
Gliffy Diagram |
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size | L |
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name | NTU vs time 2 |
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page | AGUACLARA:Relations between Vc and NTU |
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pageid | 10945299 | align |
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right | space | AGUACLARA |
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The time on the x axis can be converted into a terminal velocity based on the distance between the top of the column and turbidimeter sensor.
Gliffy Diagram |
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size | L |
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name | NTU vs Vc during settle phase |
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page | AGUACLARA:Relations between Vc and NTU |
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pageid | 10945299 | align | right |
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space | AGUACLARA |
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Now we can see that this final figure is actually the integral of the particle size distribution shown in the first Figure. Thus we can move between the trace of turbidity vs time during the sedimentation phase to a particle size distribution. This data transformation could be one of the next steps in analyzing the data from the tube floc apparatus.
We also observe that the initial slope of turbidity vs time is expected to be flat for the first few seconds. I don't think the collected data shows that trend and thus it may be worth investigating why the turbidity was decreasing from the very beginning of the sedimentation phase. An instantaneous decrease in turbidity would require an infinite sedimentation velocity for at least some of the particles in the suspension.
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