Thesis - faculty.ait.ac.th - Asian Institute of Technology
Thesis - faculty.ait.ac.th - Asian Institute of Technology
Thesis - faculty.ait.ac.th - Asian Institute of Technology
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4.2 Biokinetic Studies<br />
Bio-kinetic experiments are important in any biological treatment systems. A<br />
biological system consists <strong>of</strong> a mixture <strong>of</strong> organisms wi<strong>th</strong> different grow<strong>th</strong> patterns and<br />
degradation rates. The overall grow<strong>th</strong> and degradation rate is important for <strong>th</strong>e degradation<br />
<strong>of</strong> <strong>th</strong>e pollutants present in <strong>th</strong>e waste. Therefore, bio-kinetic studies were conducted to get<br />
an overall picture <strong>of</strong> <strong>th</strong>e degradation potential and grow<strong>th</strong> <strong>of</strong> <strong>th</strong>e microorganisms used in<br />
<strong>th</strong>e degradation pattern.<br />
4.2.1 Acclimatization <strong>of</strong> Mixed Yeast and B<strong>ac</strong>terial Sludge<br />
Prior to <strong>th</strong>e biokinetic study, it is necessary to <strong>ac</strong>climatize <strong>th</strong>e organisms to <strong>th</strong>e<br />
prevailing toxic conditions <strong>of</strong> <strong>th</strong>e le<strong>ac</strong>hate having high COD and ammonia concentrations<br />
along wi<strong>th</strong> o<strong>th</strong>er humic organic components. After <strong>ac</strong>climatization <strong>of</strong> <strong>th</strong>e culture to be used,<br />
a rich mixture <strong>of</strong> resistant le<strong>ac</strong>hate degrading organisms could be obtained. In <strong>th</strong>e present<br />
experiment, b<strong>ac</strong>terial and yeast culture were used to degrade <strong>th</strong>e le<strong>ac</strong>hate in <strong>th</strong>e membrane<br />
biore<strong>ac</strong>tors. Preceding <strong>ac</strong>climatization <strong>of</strong> <strong>th</strong>e yeast culture, to obtain a wide range <strong>of</strong> <strong>th</strong>e<br />
yeast species, yeast was enriched using <strong>th</strong>e standard enrichment technique. The enrichment<br />
was completely <strong>ac</strong>complished once <strong>th</strong>e yeast re<strong>ac</strong>hed a MLSS concentration <strong>of</strong> 3,000 mg/L.<br />
The <strong>ac</strong>climatization and <strong>th</strong>e enrichment <strong>of</strong> <strong>th</strong>e b<strong>ac</strong>terial and yeast culture was done as<br />
described in section 3.3.2. The pH <strong>of</strong> <strong>th</strong>e yeast culture was maintained at around 3.5 as<br />
yeast <strong>ac</strong>tivity is pronounced at low pH and <strong>th</strong>is would also help in preventing b<strong>ac</strong>terial<br />
contamination.<br />
(1) Organic Removal<br />
The <strong>ac</strong>climatization <strong>of</strong> <strong>th</strong>e b<strong>ac</strong>terial and yeast culture were done as described in<br />
section 3.3.2 wi<strong>th</strong> <strong>th</strong>e simulated medium-aged landfill le<strong>ac</strong>hate having char<strong>ac</strong>teristic given<br />
in section 3.2 wi<strong>th</strong> variation in COD load, which was step-wise increased to finally obtain<br />
an <strong>ac</strong>climatized culture. The operation conditions for <strong>th</strong>e <strong>ac</strong>climatization process are<br />
mentioned in <strong>th</strong>e Table 3.2. The organic load while <strong>ac</strong>climatizing was step wise increased<br />
from 3,800 to 7,300 for b<strong>ac</strong>terial as well as yeast culture. The <strong>ac</strong>climatization was done<br />
step-wise until a COD removal approximately 70% could be <strong>ac</strong>hieved. The changes in <strong>th</strong>e<br />
biomass concentration along wi<strong>th</strong> <strong>th</strong>e F/M ratio and COD removal efficiencies were<br />
noticed. These measured parameters are given in Table B-2 and B-3 <strong>of</strong> Appendix B.<br />
Acclimatization <strong>of</strong> yeast and b<strong>ac</strong>terial culture took about 67 days. The change in <strong>th</strong>e<br />
COD removal efficiency and <strong>th</strong>e F/M ratio is given in Figure 4.1 and 4.2. It was found <strong>th</strong>at<br />
after 67 days, <strong>th</strong>e COD removal efficiency wi<strong>th</strong> yeast culture was higher <strong>th</strong>an <strong>th</strong>at <strong>of</strong><br />
b<strong>ac</strong>terial culture. The COD removal efficiency re<strong>ac</strong>hed 75% in yeast sludge compared to<br />
66% in <strong>th</strong>e b<strong>ac</strong>terial sludge. This indicates <strong>th</strong>at, yeast culture could probably be more<br />
effective in le<strong>ac</strong>hate treatment <strong>th</strong>an <strong>th</strong>e b<strong>ac</strong>terial culture. However, as <strong>th</strong>e results obtained<br />
are not sufficient to conclude <strong>th</strong>at yeast system has a better performance <strong>th</strong>an b<strong>ac</strong>teria<br />
system, fur<strong>th</strong>er investigation is necessary. F/M ratio decreased from 1.01 to 0.62 kg<br />
COD/kg SS.d in <strong>th</strong>e yeast culture and from 1.45 to 1.14 kg COD/kg SS.d in <strong>th</strong>e b<strong>ac</strong>terial<br />
sludge. The difference between <strong>th</strong>e F/M ratios in <strong>th</strong>e b<strong>ac</strong>terial culture was not as much as<br />
<strong>th</strong>e yeast culture. This suggests <strong>th</strong>at <strong>th</strong>e grow<strong>th</strong> <strong>of</strong> <strong>th</strong>e yeast culture was more prominent<br />
<strong>th</strong>an <strong>th</strong>e b<strong>ac</strong>terial culture. Lower <strong>th</strong>e F/M ratio, <strong>th</strong>e better is <strong>th</strong>e le<strong>ac</strong>hate treatment cap<strong>ac</strong>ity<br />
<strong>of</strong> <strong>th</strong>e system. This could be <strong>th</strong>e reason for <strong>th</strong>e better removal efficiency <strong>of</strong> COD by <strong>th</strong>e<br />
yeast culture.<br />
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