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

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le<strong>ac</strong>hate in municipal wastewater treatment plants. A combined treatment may provide a<br />

better effluent quality as a result <strong>of</strong> <strong>th</strong>e maintenance <strong>of</strong> a more heterogeneous population,<br />

increased availability <strong>of</strong> nutrient and possible dilution <strong>of</strong> potential inhibitors. Ano<strong>th</strong>er<br />

advantage <strong>of</strong> co-treatment <strong>of</strong> le<strong>ac</strong>hate wi<strong>th</strong> domestic sewage is <strong>th</strong>at le<strong>ac</strong>hate contains<br />

excess <strong>of</strong> nitrogen while sewage contains excess <strong>of</strong> phosphorus which eliminates <strong>th</strong>e need<br />

for addition <strong>of</strong> nutrients. However, <strong>th</strong>e main disadvantage is <strong>th</strong>e high concentrations <strong>of</strong><br />

organic and inorganic components contributed by bo<strong>th</strong> young and old le<strong>ac</strong>hate.<br />

To review <strong>th</strong>e <strong>of</strong> co-treatment <strong>of</strong> le<strong>ac</strong>hate in MWW plants, Qasim and Chiang (1994)<br />

summarized research conducted by various researchers (Chian and DeWalle, 1977; Henry,<br />

1985; Raina and Mavinic, 1985). From <strong>th</strong>e review, it was evident <strong>th</strong>at a disagreement arose<br />

as to whe<strong>th</strong>er <strong>th</strong>is option was viable and under what conditions. Whilst Raina and Mavinic<br />

(1985) successfully treated le<strong>ac</strong>hate-MWW combinations <strong>of</strong> 20 to 40 %, Henry (1985),<br />

Chian and DeWalle (1977) and o<strong>th</strong>ers reported poor performance in <strong>th</strong>e co-treatment for<br />

le<strong>ac</strong>hate to MWW a ratio <strong>of</strong> less as 10 %. Since, <strong>th</strong>ere are contradicting results from<br />

various researchers, it is unknown whe<strong>th</strong>er <strong>th</strong>is treatment option is suitable under pr<strong>ac</strong>tical<br />

application. Al<strong>th</strong>ough BOD5, COD and heavy metal reduction is well established, <strong>th</strong>e<br />

relative proportions <strong>of</strong> le<strong>ac</strong>hate effectively treated is effected by ammonia conversions,<br />

temperature, sludge production, foaming, poor solids settleability, heavy metal<br />

<strong>ac</strong>cumulation and precipitate formation.<br />

2.9 Combined Treatment F<strong>ac</strong>ility<br />

A single treatment technology is not efficient in <strong>th</strong>e le<strong>ac</strong>hate treatment due to <strong>th</strong>e<br />

complexity involved in treating le<strong>ac</strong>hate having a varied composition and char<strong>ac</strong>teristic.<br />

Le<strong>ac</strong>hate treatment entails <strong>th</strong>e integration <strong>of</strong> several treatment processes. The coupling <strong>of</strong><br />

units for <strong>th</strong>e development <strong>of</strong> treatment sequences should be modular to allow maximum<br />

flexibility in order to vary <strong>th</strong>e order <strong>of</strong> arrangement and for addition/removal <strong>of</strong> unit<br />

operations. This effectively creates different treatment lines and <strong>th</strong>us better adapted to <strong>th</strong>e<br />

changing qualitative conditions <strong>of</strong> <strong>th</strong>e le<strong>ac</strong>hate (Qasim and Chiang, 1994; Bressi and<br />

Favali, 1997).<br />

Physical-chemical treatment processes for le<strong>ac</strong>hate from young landfills are not as<br />

effective as biological processes, whereas <strong>th</strong>ey are extremely efficient for stabilized<br />

le<strong>ac</strong>hate. COD/TOC and BOD/COD ratios, absolute COD concentration and age <strong>of</strong> <strong>th</strong>e<br />

landfill are necessary determinants in <strong>th</strong>e le<strong>ac</strong>hate char<strong>ac</strong>teristics for selection <strong>of</strong><br />

appropriate treatment system. In treating le<strong>ac</strong>hate, <strong>th</strong>e treatment sequence should be able to<br />

meet ei<strong>th</strong>er <strong>th</strong>e standards for discharge in receiving water bodies or an <strong>ac</strong>ceptable limit for<br />

discharge into water treatment works. To review <strong>th</strong>e treatment sequences prior to<br />

development <strong>of</strong> optimum treatment sequence, few treatment combinations have been<br />

reviewed.<br />

2.9.1 Biological Treatment and Reverse Osmosis<br />

A treatment sequence <strong>th</strong>at is capable <strong>of</strong> removing mineralized material should<br />

include anaerobic digestion, suspended grow<strong>th</strong> biological waste treatment, partial s<strong>of</strong>tening,<br />

filtration and reverse osmosis (RO). The anaerobic digester stabilizes <strong>th</strong>e waste while <strong>th</strong>e<br />

aeration system degrades <strong>th</strong>e biological matter. The effluent could be polished in a gravity<br />

filter and demineralised in a RO unit, <strong>th</strong>us <strong>ac</strong>hieving an effluent devoid <strong>of</strong> dissolved salts<br />

and low in organics. The process train is as shown in Figure 2.7(a). Wi<strong>th</strong> increase in age,<br />

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