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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

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