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

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(a)<br />

(b)<br />

(c)<br />

Nitrate conc.<br />

(mg NO 3 - -N/L)<br />

Effluent nitrite conc.<br />

(mg NO -<br />

2 -N/L)<br />

Denitrification<br />

efficiency (%)<br />

12<br />

9<br />

6<br />

3<br />

1.0<br />

0.8<br />

0.6<br />

0.4<br />

0.2<br />

100<br />

80<br />

60<br />

40<br />

20<br />

0<br />

0 10 20 30<br />

Operating periods (day)<br />

R-1(o ppt)<br />

R-2(7.5 ppt)<br />

R-3(15 ppt)<br />

R-4(30ppt)<br />

Fig. 1. Operation of denitrifying reactor with<br />

immobilized denitrifier ; Nitrate nitrogen<br />

concentrations of <strong>the</strong> influents and effluent of<br />

reactors (a), nitrite nitrogen concentrations of <strong>the</strong><br />

effluent of reactors (b) and denitrification<br />

efficiency(c) with different salinity<br />

Influent R-1(●) Effluent R-1(❍) ; 0ppt of salinity<br />

Influent R-2(▲) Effluent R-2(u) ; 7.5ppt of salinity<br />

Influent R-3(■) Effluent R-3(y) ; 15ppt of salinity<br />

Influent R-4(▼) Effluent R-4(v) ; 30ppt of salinity<br />

The effect of acclimation method on <strong>the</strong> denitrification process.<br />

Fig. 2. shows nitrate removal rates and nitrite nitrogen concentrations of <strong>the</strong><br />

acclimation method from <strong>the</strong> fresh water denitrification system to <strong>the</strong> marine system.<br />

R-1 was maintained to <strong>the</strong> fresh water system as <strong>the</strong> control reactor to correct changes<br />

in cultivation conditions, for example temperature, pH and DO, because all reactors<br />

were operated at room temperature and 4 months were required for <strong>the</strong> operation.<br />

In <strong>the</strong> control reactor, R-1, <strong>the</strong> nitrate nitrogen removal rates were reduced to 18.5,<br />

13.3 and 8.6 g NO3 - -N/m 3 /day at each step and <strong>the</strong> nitrite nitrogen concentration was<br />

lower than 0.05 mg NO2 - -N/L during operating periods and temperatures in <strong>the</strong><br />

reactor were measured 27~28, 20~23 and 17~18 o C at each step, respectively.<br />

Decrease in room temperature might cause reductions of nitrate nitrogen removal<br />

rates[3]. In R-2, <strong>the</strong> salinity was increased to 30 ppt by 3 steps, and <strong>the</strong> nitrate<br />

removal rates were 18.2, 12.6 and 7.9 g NO3 - -N/m 3 /day and <strong>the</strong> rates were reduced on<br />

salinity, however, <strong>the</strong>se were 98.4, 94.7 and 91.5 % compared to <strong>the</strong> control of <strong>the</strong><br />

same periods, respectively. Nitrite nitrogen concentration was 0.05, 0.15 and 0.27 mg<br />

NO2 - -N/L, respectively. In R-3, salinity was increased to 30 ppt by 2 steps nitrate<br />

nitrogen removal rates were 16.3 and 11.9 g NO3 - -N/m 3 /day and nitrite nitrogen<br />

concentrations were 0.68 and 0.70 mg NO2 - -N/L. As <strong>the</strong> nitrate nitrogen removal rate<br />

was compared to <strong>the</strong> same method of R-2, <strong>the</strong>se were 88.1 and 89.5 %. In R-4 with<br />

seawater, <strong>the</strong> nitrate nitrogen removal rate was 17.4 g NO3 - -N/m 3 /day and it was 94.1<br />

% compared to <strong>the</strong> control and nitrite nitrogen concentration was 0.69 mg NO2 - -N/L.<br />

Therefore, direct acclimation was more efficient than stepwise acclimation when <strong>the</strong><br />

freshwater denitrification system was converted to <strong>the</strong> marine system, although <strong>the</strong><br />

nitrite nitrogen concentration showed 0.69 mg NO2 - -N/L. However, nitrite<br />

concentrations could be maintained within <strong>the</strong> criteria in <strong>the</strong> marine system[9]. Also,<br />

<strong>the</strong> direct acclimation method required less time periods to convert <strong>the</strong> fresh water<br />

system to <strong>the</strong> marine system.<br />

3

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