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TABLE OF CONTENTS Pages Symposium 1 - the National Sea ...

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higher superficial air velocity greatly increased <strong>the</strong> removal rates and removal<br />

efficiencies of protein and TSS in bulk solution. Each substance removal was nearly<br />

proportional to <strong>the</strong> superficial air velocity used. This might be due to <strong>the</strong> increases in <strong>the</strong><br />

area of air-water interface resulted from <strong>the</strong> higher superficial air velocity, which can<br />

cause increasing amount of substances adsorbed.<br />

Protein removal rate, g/m 3 ¡¤min<br />

12<br />

10<br />

8<br />

6<br />

4<br />

In Fig. 4 removal rates and removal efficiencies of protein and TSS were plotted as<br />

function of <strong>the</strong> air distributor pore size. With <strong>the</strong> increasing pore size of air distributor,<br />

removal rates and removal efficiencies of protein and TSS were decreased. When<br />

reducing <strong>the</strong> pore size of air distributor, <strong>the</strong> bubble diameter was diminished. This was<br />

due to <strong>the</strong> increased interfacial area available for protein adsorption, with more protein<br />

and TSS entering <strong>the</strong> foam phase, thus promoting removal.<br />

Protein removal rate, g/m 3 ¡¤min<br />

6<br />

5<br />

4<br />

3<br />

2<br />

1<br />

(a)<br />

Air<br />

stone<br />

(a)<br />

Air distributor<br />

Removal rate<br />

Removal efficiency<br />

2<br />

0<br />

0.0 0.5 1.0 1.5 2.0 2.5<br />

Superficial air velocity, cm/sec<br />

G4 G2 G1<br />

0 30 60 90 120<br />

0<br />

150<br />

Pore size, §­<br />

Removal rate<br />

Removal efficiency<br />

100<br />

80<br />

60<br />

40<br />

20<br />

Protein removal efficiency, %<br />

100<br />

80<br />

60<br />

40<br />

20<br />

Protein removal efficiency, %<br />

To determine <strong>the</strong> effect of a foam separator on dissolved oxygen transfer to sea water,<br />

dissolved oxygen saturation were measured with various hydraulic residence times and<br />

superficial air velocities and calculated out <strong>the</strong> overall mass transfer coefficient. As<br />

shown in Fig. 5, <strong>the</strong> hydraulic residence time for highest overall oxygen mass transfer<br />

coefficient was <strong>the</strong> optimum condition for <strong>the</strong> highest protein removal rate. And <strong>the</strong><br />

higher superficial air velocity substantially increases dissolved oxygen saturation in <strong>the</strong><br />

bulk solution.<br />

3<br />

TSS removal rate, g/m 3 ¡¤min<br />

20<br />

18<br />

16<br />

14<br />

12<br />

10<br />

Air<br />

stone<br />

(b)<br />

Air distributor<br />

G4 G2 G1<br />

Removal rate<br />

Removal efficiency<br />

0 30 60 90 120<br />

0<br />

150<br />

Pore size, §­<br />

Fig. 4. The effect of air distributor pore size on protein (a) and TSS (b) removal.<br />

TSS removal rate, g/m 3 ¡¤min<br />

26<br />

24<br />

22<br />

20<br />

18<br />

Removal rate<br />

Removal efficiency<br />

16<br />

0<br />

0.0 0.5 1.0 1.5 2.0 2.5<br />

Superficial air velocity, cm/sec<br />

Fig. 3. The effect of superficial air velocity on protein (a) and TSS (b) removal.<br />

(b)<br />

100<br />

80<br />

60<br />

40<br />

20<br />

100<br />

80<br />

60<br />

40<br />

20<br />

TSS removal efficiency, %<br />

TSS removal efficiency, %

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