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impact of interruption of antiscalant dosing or cleaning balls ...

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No Ball Cleaning<br />

Fouling Fact<strong>or</strong>, m 2 K /kW<br />

0.35<br />

Ball Cleaning<br />

0.3<br />

No-Ball Cleaning<br />

Resumed<br />

0.25<br />

FF Design = 0.215<br />

0.2<br />

0.15<br />

0.1<br />

0.05<br />

0<br />

0 40 80 120 160 200 240 280 320 360 400<br />

Hours<br />

Figure 5. Balls <strong>cleaning</strong> <strong>interruption</strong> with dose rate <strong>of</strong> 1.0 ppm<br />

<strong>of</strong> phosphonate based <strong>antiscalant</strong> at TBT <strong>of</strong> 90 o C<br />

0.15<br />

0.125<br />

Fouling Fact<strong>or</strong>,<br />

m2K/kW<br />

0.1<br />

0.075<br />

0.05<br />

0.025<br />

No-Ball Cleaning<br />

Ball Cleaning<br />

Resumed<br />

0<br />

0 50 100 150 200 250 300 350 400 450<br />

5<br />

Overall Heat Transfer<br />

Coefficient, kW /m2K<br />

4.75<br />

4.5<br />

4.25<br />

4<br />

3.75<br />

3.5<br />

3.25<br />

3<br />

No-Ball Cleaning<br />

0 50 100 150 200 250 300 350 400 450<br />

Time (hours)<br />

Ball Cleaning<br />

Resumed<br />

Figure 6. Balls <strong>cleaning</strong> <strong>interruption</strong> with dose rate <strong>of</strong> 1.0 ppm <strong>of</strong><br />

polycarboxylate based <strong>antiscalant</strong> at TBT <strong>of</strong> 90 o C

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