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Thesis - faculty.ait.ac.th - Asian Institute of Technology

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The yeast sludge was collected from <strong>th</strong>e bottom sediments <strong>of</strong> a pond from <strong>th</strong>e<br />

Non<strong>th</strong>aburi landfill site, Thailand. A two-liter container was used for enrichment and was<br />

done using fill-and-draw process. The wastewater feed (having glucose as substrate) was<br />

mixed wi<strong>th</strong> a diffused aeration system. The pH was adjusted to 3.5 which is optimum for<br />

yeast grow<strong>th</strong> and can prevent b<strong>ac</strong>terial contamination (Elmaleh, et al., 1996). After 24<br />

hours <strong>of</strong> aeration, <strong>th</strong>e biomass suspension was allowed to settle for 10 hours. Yeast cells,<br />

normally, settle in <strong>th</strong>e bottom, whereas <strong>th</strong>e <strong>ac</strong>id-tolerant b<strong>ac</strong>teria and filamentous fungi<br />

would remain in <strong>th</strong>e suspension. The b<strong>ac</strong>teria and fungi present in <strong>th</strong>e supernatant were<br />

removed by decanting <strong>th</strong>e supernatant. Around 1.5 liters <strong>of</strong> supernatant was decanted and<br />

fresh medium was added to <strong>th</strong>e next batch. When MLSS <strong>of</strong> <strong>th</strong>e yeast biomass exceeded<br />

3,000 mg/L, <strong>th</strong>e enrichment process was <strong>ac</strong>complished.<br />

b) B<strong>ac</strong>teria Sludge<br />

The b<strong>ac</strong>terial seed sludge was collected from <strong>th</strong>e aeration tank in <strong>th</strong>e <strong>ac</strong>tivated sludge<br />

process <strong>of</strong> a wastewater treatment plant.<br />

3.3.2 Acclimatization<br />

Acclimatization was done in order to obtain a mixed b<strong>ac</strong>terial and yeast culture<br />

which can tolerate le<strong>ac</strong>hate containing low biodegradable organics and high ammonia<br />

concentration. Five-liter batch re<strong>ac</strong>tors were used for <strong>ac</strong>climatization <strong>th</strong>rough fill-and-draw<br />

process. The operating conditions for <strong>th</strong>e re<strong>ac</strong>tors are summarized in Table 3.2.<br />

Table 3.2 Operating Conditions for Yeast and B<strong>ac</strong>teria Acclimatization<br />

Operating Conditions Yeast Re<strong>ac</strong>tor B<strong>ac</strong>teria Re<strong>ac</strong>tor<br />

HRT (h) 24 24<br />

MLSS (mg/L) 10,000 5,000<br />

COD (mg/L) 8,000±1,000 8,000±1,000<br />

Temperature ( O C) 25 to 30 25 to 30<br />

pH 3.5 to 3.8 6.8 to 7.0<br />

Bo<strong>th</strong> <strong>th</strong>e re<strong>ac</strong>tors were aerated by a diffused aeration system and <strong>th</strong>e pH was adjusted<br />

to 3.5 - 3.8 for yeast grow<strong>th</strong> and 6.8 - 7.0 for b<strong>ac</strong>terial grow<strong>th</strong>, respectively. After 24 hours<br />

<strong>of</strong> aeration, <strong>th</strong>e biomass was allowed to settle for 3 hours. After 3 hours <strong>of</strong> settlement, <strong>th</strong>e<br />

supernatant was collected and centrifuged at 4000 rpm for 15 minutes. The experiment was<br />

repeated for <strong>th</strong>e next batch under <strong>th</strong>e same conditions until a COD removal <strong>of</strong> 70% could<br />

be <strong>ac</strong>hieved. Once <strong>th</strong>e COD removal efficiency re<strong>ac</strong>hed a value greater <strong>th</strong>an 70%, <strong>th</strong>e<br />

<strong>ac</strong>climatization was presumed to be complete.<br />

3.4 Toxicity Studies<br />

The toxicity studies were done wi<strong>th</strong> yeast and b<strong>ac</strong>terial culture. The toxicity <strong>of</strong> <strong>th</strong>e<br />

culture was tested for different concentrations <strong>of</strong> ammonia and lead.<br />

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