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K L a, min -1<br />

50<br />

40<br />

30<br />

20<br />

10<br />

(a)<br />

Reference<br />

K L a<br />

0<br />

90<br />

0 2 4 6 8 10<br />

Hydraulic residence time, min<br />

Saturation<br />

100<br />

98<br />

96<br />

94<br />

92<br />

DO saturation, %<br />

Chen, S. “Modeling surfactant removal in foam fraction I, II”. Aquacultural Engineering<br />

13(1994) 13: 163-200.<br />

Suh, K.H. and Lee, M.G.. “ Treatment of Aquacultural Recirculating Water by Foam Separation -<br />

I. Characteristics of Protein Separation” J. Korean. Fish. Soc., 28(1995). 599-606.<br />

4<br />

K L a, min -1<br />

25<br />

20<br />

15<br />

10<br />

5<br />

K L a<br />

0<br />

90<br />

0.0 0.5 1.0 1.5 2.0 2.5<br />

Superficial air velocity, cm/sec<br />

Saturation<br />

Fig. 5. The effect of hydraulic residence time (a) and superficial air velocity (b) on DO transfer.<br />

(b)<br />

100<br />

98<br />

96<br />

94<br />

92<br />

DO saturation, %

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