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

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HTC, kW/m2K<br />

5<br />

4.5<br />

4<br />

3.5<br />

3<br />

2.5<br />

2<br />

0 8 16 24 32 40 48 56 64 72<br />

0.4<br />

FF, m2K/kW<br />

0.3<br />

0.2<br />

0.1<br />

0<br />

0 8 16 24 32 40 48 56 64 72<br />

Hours<br />

Figure 3. The <strong>impact</strong> <strong>of</strong> sudden cutting <strong>of</strong> phosphonate based<br />

<strong>antiscalant</strong> <strong>dosing</strong> at TBT 100 o C and 1.0 ppm with<br />

continuous cycling <strong>of</strong> <strong>cleaning</strong> <strong>balls</strong> on the perf<strong>or</strong>mance<br />

<strong>of</strong> MSF pilot plant<br />

5<br />

4.5<br />

HTC, k W /m2K<br />

4<br />

3.5<br />

3<br />

2.5<br />

2<br />

0 8 16 24 32 40 48 56 64<br />

0.4<br />

FF, m2K/kW<br />

0.3<br />

0.2<br />

0.1<br />

0<br />

0 8 16 24 32 40 48 56 64<br />

Hours<br />

Figure 4. The <strong>impact</strong> <strong>of</strong> sudden cutting <strong>of</strong> polycarboxylate based<br />

<strong>antiscalant</strong> <strong>dosing</strong> at TBT 100 o C and 1.0 ppm with<br />

continuous cycling <strong>of</strong> <strong>cleaning</strong> <strong>balls</strong> on the perf<strong>or</strong>mance <strong>of</strong><br />

MSF pilot plant

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