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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Air Compressor<br />
Influent<br />
Air Diffuser<br />
Air Outlet<br />
Bio-Re<strong>ac</strong>tor<br />
Return Sludge<br />
Membrane Unit<br />
(a) (b)<br />
Figure 2.10 Schematic Diagrams <strong>of</strong> (a) External Recirculation MBR and (b) Submerged<br />
MBR System<br />
2.11.1 Membrane Configuration<br />
Effluent<br />
Influent<br />
Membrane biore<strong>ac</strong>tor configurations include: extr<strong>ac</strong>tive membrane biore<strong>ac</strong>tors<br />
(EMBR), bubble-less aeration membrane biore<strong>ac</strong>tors (MABR), recycle membrane<br />
biore<strong>ac</strong>tors and membrane separation biore<strong>ac</strong>tors.<br />
Treatment by aerobic processes is <strong>of</strong>ten limited by insufficient oxygen while using<br />
air as an oxygen source. The implementation <strong>of</strong> oxygen as opposed to air as an aeration<br />
medium would increase <strong>th</strong>e degradation rate <strong>of</strong> <strong>th</strong>e system. However, since conventional<br />
aeration devices have high power requirements and a high rate <strong>of</strong> mixing, <strong>th</strong>ese devices<br />
cannot be used wi<strong>th</strong> bi<strong>of</strong>ilm processes. MABR process uses gas permeable membranes to<br />
directly supply high purity oxygen wi<strong>th</strong>out bubble formation in a bi<strong>of</strong>ilm (Stephenson, et<br />
al., 2000). The membranes are generally configured in ei<strong>th</strong>er a plate-and-frame or hollow<br />
fibre module. However, research has focussed on <strong>th</strong>e hollow fibre arrangement wi<strong>th</strong> gas on<br />
<strong>th</strong>e lumen-side and wastewater on <strong>th</strong>e shell-side. The hollow fibre modules are preferred<br />
since <strong>th</strong>e membrane provides a high surf<strong>ac</strong>e area for oxygen transfer while occupying a<br />
small volume wi<strong>th</strong>in <strong>th</strong>e re<strong>ac</strong>tor.<br />
The membrane recycle biore<strong>ac</strong>tor consists <strong>of</strong> a re<strong>ac</strong>tion vessel operated as a stirred<br />
tank re<strong>ac</strong>tor and a membrane module containing <strong>th</strong>e membrane. The substrate and<br />
biocatalyst are added to <strong>th</strong>e re<strong>ac</strong>tion vessel in pre-determined concentrations. Thereafter,<br />
<strong>th</strong>e mixture is continuously pumped <strong>th</strong>rough <strong>th</strong>e membrane. While <strong>th</strong>e biocatalyst adheres<br />
to <strong>th</strong>e membrane surf<strong>ac</strong>e, <strong>th</strong>e medium permeates <strong>th</strong>rough <strong>th</strong>e membrane and is recycled to<br />
<strong>th</strong>e re<strong>ac</strong>tor vessel.<br />
A summary <strong>of</strong> <strong>th</strong>e advantages and disadvantages <strong>of</strong> e<strong>ac</strong>h biore<strong>ac</strong>tor configuration is<br />
presented in Table 2.18.<br />
The versatility and treatment capability <strong>of</strong> membrane biore<strong>ac</strong>tors has catapulted <strong>th</strong>e<br />
technology as a viable alternative in water and wastewater treatment over a short period.<br />
Initial design configurations <strong>of</strong> external loop systems were prone to fouling which<br />
prevented stable operation and hence was confined to small-scale operations wi<strong>th</strong> limited<br />
value and applicability.<br />
42<br />
Feed Tank<br />
Compressed Air Effluent<br />
Level Control<br />
Tank<br />
Membrane<br />
Air Diffuser