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
You also want an ePaper? Increase the reach of your titles
YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.
From <strong>th</strong>e data obtained above, it can be seen <strong>th</strong>at 5 days BOD contributes to about<br />
67% <strong>of</strong> <strong>th</strong>e 20 days COD present in <strong>th</strong>e raw le<strong>ac</strong>hate, while in <strong>th</strong>e BMBR and YMBR<br />
effluent; <strong>th</strong>e 5 days BOD contributed only 38 and 25% <strong>of</strong> <strong>th</strong>e 20 days BOD. This shows<br />
<strong>th</strong>at compared to <strong>th</strong>at <strong>of</strong> <strong>th</strong>e raw le<strong>ac</strong>hate, <strong>th</strong>e effluents <strong>of</strong> <strong>th</strong>e membrane biore<strong>ac</strong>tors take a<br />
longer time to degrade <strong>th</strong>e organics suggesting <strong>th</strong>e presence <strong>of</strong> greater amount <strong>of</strong> slowly<br />
biodegradable organics. In comparison between YMBR and BMBR effluents, slowly<br />
biodegradable organics in YMBR effluent was higher <strong>th</strong>an <strong>th</strong>at in BMBR effluent.<br />
When <strong>th</strong>e BOD/COD ratio for raw le<strong>ac</strong>hate was considered, it was found <strong>th</strong>at<br />
BOD5/COD was 0.45 which increased to a BOD20/COD <strong>of</strong> 0.68 after 20 days. This<br />
suggests <strong>th</strong>at <strong>th</strong>e degradable component in <strong>th</strong>e raw le<strong>ac</strong>hate is almost 68%. The<br />
BOD5/COD <strong>of</strong> bo<strong>th</strong> <strong>th</strong>e b<strong>ac</strong>terial and yeast effluent was found to be 0.01. Though, <strong>th</strong>e<br />
b<strong>ac</strong>terial and yeast effluent had a similar BOD5/COD ratio, <strong>th</strong>e BOD20/COD ratio <strong>of</strong> <strong>th</strong>e<br />
b<strong>ac</strong>terial and yeast effluent varied wi<strong>th</strong> a ratio <strong>of</strong> 0.02 and 0.04, respectively. This also<br />
suggests <strong>th</strong>at <strong>th</strong>e slowly degradable components are more in <strong>th</strong>e yeast effluent in<br />
comparison wi<strong>th</strong> b<strong>ac</strong>terial effluent.<br />
4.5.2 Molecular Weight Cut-<strong>of</strong>f<br />
The organic matter present in <strong>th</strong>e le<strong>ac</strong>hate varies and is dependent on <strong>th</strong>e waste<br />
composition and degree <strong>of</strong> degradation. The medium molecular weight compounds wi<strong>th</strong><br />
molecular weight (MW) between 500 and 10,000 Da are dominated by carboxylic and<br />
hydroxylic groups wi<strong>th</strong> fulvic <strong>ac</strong>id and humic fr<strong>ac</strong>tion also contributing to <strong>th</strong>is fr<strong>ac</strong>tion in<br />
<strong>th</strong>e le<strong>ac</strong>hate (Chian and DeWalle, 1976; Harmsen, 1983). They are difficult to degrade and<br />
are termed refr<strong>ac</strong>tory. The fulvic and humic-like compounds present in le<strong>ac</strong>hate are formed<br />
from micobiological processes from <strong>th</strong>e intermediate products <strong>of</strong> degradation <strong>of</strong> polymeric<br />
organic compounds such as lignine (Andreux, 1979).<br />
The high molecular weight organics are usually stable to degradation. The<br />
effectiveness <strong>of</strong> a treatment process can be related to <strong>th</strong>e removal <strong>of</strong> specific organic<br />
fr<strong>ac</strong>tion in le<strong>ac</strong>hate. Bo<strong>th</strong> fulvic and humic substances are inert to biological treatment.<br />
Therefore, fr<strong>ac</strong>tionating <strong>th</strong>e COD based on molecular weight can <strong>ac</strong>t as an indicator to <strong>th</strong>e<br />
removal efficiency and degradation potential <strong>of</strong> <strong>th</strong>e biological system.<br />
According to <strong>th</strong>e results, <strong>th</strong>e molecular weight distribution or molecular weight cut<strong>of</strong>f<br />
(MWCO) was computed by measuring <strong>th</strong>e COD concentration <strong>of</strong> e<strong>ac</strong>h fr<strong>ac</strong>tion and <strong>th</strong>e<br />
volume filtered. The transformation <strong>of</strong> organic substances corresponding to <strong>th</strong>e change <strong>of</strong><br />
COD mass is shown in Figure 4.39. Detailed calculation is given in Table H-3 <strong>of</strong> Appendix<br />
H.<br />
As shown in <strong>th</strong>e figure, <strong>th</strong>e raw le<strong>ac</strong>hate contained a higher fr<strong>ac</strong>tion <strong>of</strong> high<br />
molecular weight compounds (> 50 k). The low-molecular weight fr<strong>ac</strong>tions, which include<br />
lower molecular weight compounds, were present at low fr<strong>ac</strong>tion. Figure 4.40 shows<br />
percent COD contribution <strong>of</strong> various molecular weight components to <strong>th</strong>e total COD in<br />
raw le<strong>ac</strong>hate, stripped le<strong>ac</strong>hate, b<strong>ac</strong>terial and yeast effluents.<br />
110