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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0.02, respectively. This can be considered <strong>th</strong>at <strong>th</strong>e slowly degradable components in<br />
<strong>th</strong>e yeast effluent are higher <strong>th</strong>an <strong>th</strong>at in <strong>th</strong>e b<strong>ac</strong>terial effluent.<br />
11. The contribution <strong>of</strong> molecular weight compounds > 50 kDa in <strong>th</strong>e raw le<strong>ac</strong>hate was<br />
greater <strong>th</strong>an 80% in terms <strong>of</strong> BOD and COD concentrations. This found <strong>th</strong>at some<br />
portion <strong>of</strong> <strong>th</strong>e > 50 kDa compounds was broken down into < 5 kDa after ammonia<br />
stripping. The reduction <strong>of</strong> molecular weight compounds > 50 kDa significantly<br />
presented after MBR treatment. This showed <strong>th</strong>at <strong>th</strong>e complex higher molecular<br />
weight compounds could be degraded effectively using membrane biore<strong>ac</strong>tor<br />
systems. Considering <strong>th</strong>e BOD content in <strong>th</strong>e effluent, it was found <strong>th</strong>at in bo<strong>th</strong> yeast<br />
and b<strong>ac</strong>terial effluents, <strong>th</strong>e molecular weight compounds < 5 kDa contributed to <strong>th</strong>e<br />
maximum BOD when compared wi<strong>th</strong> <strong>th</strong>e o<strong>th</strong>er fr<strong>ac</strong>tions. The COD content also<br />
showed a similar trend.<br />
12. For <strong>th</strong>e sludge properties, <strong>th</strong>e bound and soluble EPS <strong>of</strong> <strong>th</strong>e yeast and b<strong>ac</strong>teria<br />
systems are measured. In comparison between yeast and b<strong>ac</strong>teria systems, bound<br />
EPS concentration in terms <strong>of</strong> TOC was not different while soluble EPS <strong>of</strong> mixed<br />
b<strong>ac</strong>terial sludge was higher <strong>th</strong>an <strong>th</strong>at <strong>of</strong> mixed yeast sludge. Also, <strong>th</strong>e protein to<br />
carbohydrate ratio in <strong>th</strong>e soluble EPS was higher. This indicated <strong>th</strong>at soluble EPS<br />
could be <strong>th</strong>e f<strong>ac</strong>tor which affected <strong>th</strong>e membrane fouling.<br />
13. The b<strong>ac</strong>terial sludge showed a better dewatering quality <strong>th</strong>an <strong>th</strong>at <strong>of</strong> <strong>th</strong>e yeast sludge.<br />
The viscosity <strong>of</strong> <strong>th</strong>e b<strong>ac</strong>terial system was higher <strong>th</strong>an <strong>th</strong>e yeast system.<br />
14. Ammonia stripping pretreatment wi<strong>th</strong> MBR was effective in treating le<strong>ac</strong>hate wi<strong>th</strong><br />
high ammonium nitrogen concentration but <strong>th</strong>e effluent still contained a large<br />
quantity <strong>of</strong> refr<strong>ac</strong>tory organic compounds. This might be due to <strong>th</strong>e contribution <strong>of</strong><br />
<strong>th</strong>e slowly biodegradable organics and non-biodegradable organics containing in <strong>th</strong>e<br />
le<strong>ac</strong>hate. Therefore, it should be fur<strong>th</strong>er treated in a post treatment, elevating <strong>th</strong>e<br />
water quality <strong>of</strong> <strong>th</strong>e final effluent or even increasing <strong>th</strong>e biodegradable organics<br />
5.2 Recommendations for Future Work<br />
Based on <strong>th</strong>e extensive experimental results <strong>of</strong> <strong>th</strong>is study, <strong>th</strong>e following<br />
recommendations are proposed.<br />
1. For MBR system, membrane fouling is a common problem but it is made more<br />
difficult to predict and control in <strong>th</strong>e MBR. This might be due to <strong>th</strong>e effects <strong>of</strong> <strong>ac</strong>tive<br />
microorganisms generating EPS. The EPS is <strong>of</strong> key significance wi<strong>th</strong> respect to<br />
fouling <strong>th</strong>at is dependent on <strong>th</strong>e EPS concentrations and chemical components <strong>of</strong><br />
EPS. Fouling is also affected by <strong>th</strong>e floc size and particle size distribution correlated<br />
wi<strong>th</strong> membrane permeability. It is recommended <strong>th</strong>at future work should be focused<br />
on <strong>th</strong>e contributions <strong>of</strong> <strong>th</strong>e various particle fr<strong>ac</strong>tions (suspended particles, colloidal,<br />
soluble solids), presenting in <strong>th</strong>e sludge on <strong>th</strong>e mechanisms <strong>of</strong> membrane fouling.<br />
More laboratory and pilot scale experiments are needed to estimate membrane<br />
fouling and <strong>th</strong>e influences <strong>of</strong> operating parameters.<br />
2. In MBR system, <strong>th</strong>e various soluble organic substances could be retained wi<strong>th</strong>in <strong>th</strong>e<br />
biore<strong>ac</strong>tor. The components <strong>of</strong> soluble organic compounds are complex and may<br />
include humic substances, fluvic <strong>ac</strong>ids, polys<strong>ac</strong>charides, proteins, etc. Therefore, <strong>th</strong>e<br />
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