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

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Table 3.7 Char<strong>ac</strong>teristics <strong>of</strong> Ultrafiltration Membrane<br />

UF Membrane Types MWCO (kDa)<br />

Koch membrane, M-100 50<br />

Koch membrane, K-131 10<br />

Koch membrane, K-328 5<br />

3.6.5 Sludge Char<strong>ac</strong>terization<br />

The variation in sludge char<strong>ac</strong>teristics was estimated in bo<strong>th</strong> <strong>th</strong>e re<strong>ac</strong>tors. The<br />

YMBR and BMBR systems can be divided into <strong>th</strong>ree zones based on <strong>th</strong>e membrane cycle.<br />

Based on <strong>th</strong>e membrane fouling, <strong>th</strong>e sludge was sampled for analysis. Sludge properties<br />

which were determined in bo<strong>th</strong> <strong>th</strong>e re<strong>ac</strong>tors were <strong>th</strong>e extra cellular polymer substances<br />

(EPS), sludge volume index (SVI), capillary suction time (CST), MLSS and viscosity.<br />

3.7 Ammonia Stripping Coupled Membrane Biore<strong>ac</strong>tor<br />

The membrane biore<strong>ac</strong>tor was coupled wi<strong>th</strong> ammonia stripping to find out <strong>th</strong>e<br />

treatment efficiency <strong>of</strong> <strong>th</strong>is combined treatment system. The experimental set-up consists<br />

<strong>of</strong> two treatment systems, namely: ammonia stripping and membrane biore<strong>ac</strong>tor (MBR) as<br />

shown in Figure 3.5. Figure 3.7 show <strong>th</strong>e procedure <strong>of</strong> <strong>th</strong>e coupling ammonia stripping<br />

wi<strong>th</strong> MBR.<br />

The operating conditions for ammonia stripping process were based on <strong>th</strong>e results<br />

obtained from <strong>th</strong>e previous experiment. Mean velocity gradient, pH and <strong>th</strong>e mixing time<br />

were based on <strong>th</strong>e experimental results obtained after optimization <strong>of</strong> <strong>th</strong>e ammonia<br />

stripping conditions. The ammonia stripped le<strong>ac</strong>hate was used as a feed in bo<strong>th</strong> <strong>th</strong>e YMBR<br />

and BMBR re<strong>ac</strong>tors. The design <strong>of</strong> <strong>th</strong>e re<strong>ac</strong>tors used for <strong>th</strong>e experiment was similar to<br />

biore<strong>ac</strong>tor as described 3.6.2.<br />

The HRT used in <strong>th</strong>is experiment are from <strong>th</strong>e results obtained after performing <strong>th</strong>e<br />

parametric studies as described in session 3.6.3. The excess sludge was periodically<br />

wi<strong>th</strong>drawn to maintain a mean biomass <strong>of</strong> 10,000 to 12,000 mg/L <strong>of</strong> MLSS. The biore<strong>ac</strong>tor<br />

was assessed in terms <strong>of</strong> <strong>th</strong>e membrane performance in le<strong>ac</strong>hate treatment and sludge<br />

char<strong>ac</strong>teristics.<br />

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