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Alexander Szabo and Oscar Engle - Svenskt Vatten

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value of 4:1 in length/width ratio. Within each case it was reported that increasing the<br />

length/width ratio <strong>and</strong> introducing baffles slightly increases the water velocity <strong>and</strong> DO in the<br />

effluent water (Abbas et al., 2006). The conclusion drawn from these data simulations is that a<br />

pond should have a length/width ratio of 4:1 <strong>and</strong> at least two baffles.<br />

5.2 Facultative <strong>and</strong> maturation ponds in Sri Pulai, Johor Bahru,<br />

Malaysia.<br />

An analysis of the performance of a waste water stabilization pond in Sri Pulai, Johor Bahru was<br />

done in 2002. The treatment system uses a primary facultative pond followed by a maturation<br />

pond (Ujang et al., 2002). This is the same pond arrangement as used at UTM. The system in Sri<br />

Pulai serves a population equivalent (P.E.) of 10 327 from a residential area of approximately 0.7<br />

km 2 . The ponds together cover an area of 17.725 m 2 , with pond volumes of 16.275 m 3 for the<br />

facultative pond <strong>and</strong> 10 115 m 3 for the maturation pond. The volume of the facultative pond<br />

should result in a retention time of about 30 days. Around 40 % of the incoming water is assumed<br />

to origin from infiltrating ground water (Ujang et al., 2002).<br />

Table 5.2: Average waste water characteristics at Sri Pulai WSP. The influent results is based on 24<br />

samples, the results from the effluent facultative pond <strong>and</strong> the effluent maturation pond is based on<br />

14 respectively 7 samples. (re-drawn from Ujang et al., 2002)<br />


 COD (mg O 2 / SS (g/l) NH 4 -N (mg/l) NO 3 -N (mg/l)<br />

l)<br />

Influent<br />

Effluent facultative pond<br />

446<br />

139<br />

146<br />

48<br />

23.1<br />

19.7<br />

1.5<br />

1.6<br />

Effluent maturation pond<br />

114<br />

41 16.8<br />

1.2<br />

Removal in entire pond<br />

system<br />

74% 72% 27%<br />

20%<br />

Removal in facultative pond<br />

Removal in maturation pond<br />

69%<br />

18%<br />

67%<br />

15%<br />

15%<br />

15%<br />

- 7%<br />

25%<br />

Compared with the effluent st<strong>and</strong>ard for Malaysia, the treatment process was not sufficient, since<br />

the total COD concentration of the effluent was on average 114 mg O 2 /l (see Table 5.2). The<br />

Malaysian effluent st<strong>and</strong>ard B is set to 100 mg COD/l (Ujang et al., 2002).<br />

The authors´ conclusion of the unexpected low treatment efficiency (the pond should be able to<br />

meet st<strong>and</strong>ard B) could partly be caused by hydraulic short-circuiting. The low treatment<br />

efficiency could also be caused by the specific growth rates of biological degrading bacteria not<br />

being so temperature dependent as expected. The authors recommended aeration <strong>and</strong> installation<br />

of baffles to improve the treatment.<br />


<br />

25


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