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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Activated Carbon Adsorption<br />
Granular <strong>ac</strong>tivated carbon in combination wi<strong>th</strong> biological pretreatment is <strong>th</strong>e leading<br />
technology for <strong>th</strong>e treatment <strong>of</strong> landfill le<strong>ac</strong>hate for <strong>th</strong>e removal <strong>of</strong> chemical oxygen<br />
demand (COD), adsorbable organic halogens (AOX) and o<strong>th</strong>er toxic substances. More <strong>th</strong>an<br />
130 different types <strong>of</strong> organics have been identified on spent carbon from le<strong>ac</strong>hate<br />
treatment plants. Granular <strong>ac</strong>tivated carbon is used to remove AOX and COD, bo<strong>th</strong> <strong>of</strong><br />
which are not primary focus <strong>of</strong> biological treatment systems and <strong>th</strong>erefore, <strong>th</strong>e effluent<br />
quality may be found above discharge consent levels from such treatment systems. Wi<strong>th</strong><br />
particularly dilute le<strong>ac</strong>hate, it may be operated wi<strong>th</strong> a plate separator or pressurized sand<br />
filter removing suspended solids from <strong>th</strong>e flow, in order to ensure <strong>th</strong>at <strong>th</strong>e carbon filter is<br />
not blocked wi<strong>th</strong> solids. It is necessary to ensure <strong>th</strong>at <strong>th</strong>ere are no substances in <strong>th</strong>e<br />
le<strong>ac</strong>hate which will damage <strong>th</strong>e carbon prior to selecting such a system.<br />
When Fettig (1996) studied <strong>th</strong>e treatment <strong>of</strong> landfill le<strong>ac</strong>hate by preozonation and<br />
adsorption in <strong>ac</strong>tivated carbon columns, <strong>th</strong>e data evaluation revealed <strong>th</strong>at degradation took<br />
pl<strong>ac</strong>e inside <strong>th</strong>e <strong>ac</strong>tivated carbon beds. Therefore, <strong>th</strong>e total removal efficiency <strong>of</strong> ozonated<br />
le<strong>ac</strong>hate in <strong>ac</strong>tivated carbon columns was found to be higher <strong>th</strong>an <strong>th</strong>e removal efficiency<br />
due to adsorption processes. A review <strong>of</strong> physical-chemical processes done by Qasim and<br />
Chiang (1994) indicated <strong>th</strong>at adsorption by <strong>ac</strong>tivated carbon was more effective in organic<br />
removal from raw le<strong>ac</strong>hate <strong>th</strong>an chemical precipitation wi<strong>th</strong> COD removal efficiencies <strong>of</strong><br />
59 to 94 %. The humic substances remains unaffected by <strong>ac</strong>tivated carbon treatment while,<br />
1,000 MW fluvic substances could be easily removed by <strong>ac</strong>tivated carbon.<br />
Membrane Filtration<br />
A membrane is defined as a material <strong>th</strong>at forms a <strong>th</strong>in wall capable <strong>of</strong> selectively<br />
resisting <strong>th</strong>e transfer <strong>of</strong> different constituents <strong>of</strong> a fluid and <strong>th</strong>us affecting separation <strong>of</strong> <strong>th</strong>e<br />
constituents. The principle objective <strong>of</strong> membrane manuf<strong>ac</strong>ture is to produce a material <strong>of</strong><br />
reasonable mechanical streng<strong>th</strong> <strong>th</strong>at can maintain a high <strong>th</strong>roughput <strong>of</strong> a desired permeate<br />
wi<strong>th</strong> a high degree <strong>of</strong> selectivity (Visvana<strong>th</strong>an, et al., 2000). The optimal physical structure<br />
<strong>of</strong> <strong>th</strong>e membrane material is based on a <strong>th</strong>in layer <strong>of</strong> material wi<strong>th</strong> a narrow range <strong>of</strong> pore<br />
size and a high surf<strong>ac</strong>e porosity. This concept is extended to include <strong>th</strong>e separation <strong>of</strong><br />
dissolved solutes in liquid streams and <strong>th</strong>e separation <strong>of</strong> gas mixtures for membrane<br />
filtration.<br />
The classification <strong>of</strong> membrane separation processes are based on particle and<br />
molecular size. The processes such as reverse osmosis (RO), nan<strong>of</strong>iltration (NF),<br />
ultrafiltration (UF) and micr<strong>of</strong>iltration (MF) do not generally require <strong>th</strong>e addition <strong>of</strong><br />
aggressive chemicals and can be operated at ambient temperature making <strong>th</strong>ese processes<br />
bo<strong>th</strong> an environmentally and economically attr<strong>ac</strong>tive alternative to <strong>th</strong>e conventional<br />
operating units. Table 2.12 summarizes <strong>th</strong>e various membrane processes and its separation<br />
potential. RO membranes can remove more <strong>th</strong>an 99 % <strong>of</strong> organic m<strong>ac</strong>romolecules and<br />
colloids from feed-water and up to 99 % <strong>of</strong> <strong>th</strong>e inorganic ions.<br />
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