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

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Figure 4.39 Molecular Weight Cut-<strong>of</strong>f <strong>of</strong> Raw Le<strong>ac</strong>hate, Stripped Le<strong>ac</strong>hate, B<strong>ac</strong>terial<br />

and Yeast Effluents<br />

COD<br />

COD (mg/L)<br />

8000<br />

7000<br />

6000<br />

5000<br />

4000<br />

3000<br />

2000<br />

1000<br />

0<br />

Raw<br />

Le<strong>ac</strong>hate<br />

Stripped<br />

Le<strong>ac</strong>hate<br />

Figure 4.40 Percent Contribution <strong>of</strong> Various Molecular Weight Compounds to <strong>th</strong>e<br />

Total<br />

The compounds greater <strong>th</strong>an 50 k molecular weight contributed almost 80% <strong>of</strong> <strong>th</strong>e<br />

raw le<strong>ac</strong>hate COD. It could be found <strong>th</strong>at some portion <strong>of</strong> <strong>th</strong>e > 50 k compounds is broken<br />

down into < 5 k after ammonia stripping. This is indicated by <strong>th</strong>e increase <strong>of</strong> < 5 k<br />

compounds. The > 5 k fr<strong>ac</strong>tion in <strong>th</strong>e raw le<strong>ac</strong>hate after stripping increased from 0 to 17%,<br />

while <strong>th</strong>e > 50 k fr<strong>ac</strong>tion reduced from 87 to 65%. The 10-50 k and 5-10 k fr<strong>ac</strong>tion did not<br />

increase significantly. The increase in 10-50 k and 5-10 k fr<strong>ac</strong>tions was from 5 to 6% and 8<br />

to 11%, respectively. Yoon, et al. (1998) showed <strong>th</strong>at about 72-89% <strong>of</strong> <strong>th</strong>e organics greater<br />

<strong>th</strong>an MW 500 could be removed and 42% <strong>of</strong> <strong>th</strong>e organics wi<strong>th</strong> less <strong>th</strong>an MW 500 could be<br />

removed from <strong>th</strong>e le<strong>ac</strong>hate using Fenton’s process. However, it was noticed <strong>th</strong>at Fenton’s<br />

process was not effective in removing organics less <strong>th</strong>an MW <strong>of</strong> 500.<br />

The MWCO after MBR treatment indicated notable reduction in > 50 k fr<strong>ac</strong>tion. The<br />

> 50 k fr<strong>ac</strong>tion reduced to 3% in <strong>th</strong>e yeast effluent and 7% in <strong>th</strong>e b<strong>ac</strong>terial system. The<br />

lower molecular weight compounds wi<strong>th</strong> MW 10-50 k, 5-10 k and >5 k in <strong>th</strong>e yeast<br />

effluent increased by 3 to 9%, 7 to 19% and 18 to 65%, respectively. These fr<strong>ac</strong>tions<br />

increased from 6 to 12%, 11 to 31% and 18 to 69%, respectively in <strong>th</strong>e b<strong>ac</strong>terial system.<br />

Using <strong>th</strong>e aerated lagoon for <strong>th</strong>e treatment <strong>of</strong> le<strong>ac</strong>hate, it was found <strong>th</strong>at only 19-28% <strong>of</strong><br />

<strong>th</strong>e total le<strong>ac</strong>hate organics was composed <strong>of</strong> organics less <strong>th</strong>an MW 500 in <strong>th</strong>e effluent<br />

111<br />

Yeast<br />

Effleunt<br />

B<strong>ac</strong>terial<br />

Effluent<br />

MW>50k MW 10k-50k MW 5k-10k MW

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