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The MBR Book: Principles and Applications of Membrane

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neo-exponential increase at fluxes closer to the notional critical flux (Fig. 2.14,<br />

10 LMH line). Sub-critical fouling is discussed further along with <strong>MBR</strong> membrane<br />

fouling mechanisms in Section 2.3.8.<br />

2.2 Biotreatment<br />

2.2.1 Biotreatment rationale<br />

Biological treatment (or biotreatment) processes are those which remove dissolved<br />

<strong>and</strong> suspended organic chemical constituents through biodegradation, as well as<br />

suspended matter through physical separation. Biotreatment dem<strong>and</strong>s that the appropriate<br />

reactor conditions prevail in order to maintain sufficient levels <strong>of</strong> viable (i.e.<br />

living) micro-organisms (or, collectively, biomass) to achieve removal <strong>of</strong> organics. <strong>The</strong><br />

latter are normally measured as biochemical or chemical oxygen dem<strong>and</strong> (BOD <strong>and</strong><br />

COD, respectively); these are indirect measurements <strong>of</strong> organic matter levels since both<br />

refer to the amount <strong>of</strong> oxygen utilised for oxidation <strong>of</strong> the organics. <strong>The</strong> microorganisms<br />

that grow on the organic substrate on which they feed derive energy <strong>and</strong><br />

generate cellular material from oxidation <strong>of</strong> the organic matter, <strong>and</strong> can be aerobic<br />

(oxygen-dependent) or anaerobic (oxygen-independent). <strong>The</strong>y are subsequently separated<br />

from the water to leave a relatively clean, clarified effluent.<br />

<strong>The</strong> most attractive feature <strong>of</strong> biological processes is the very high chemical conversion<br />

efficiency achievable. Unlike chemical oxidation processes, aerobic processes<br />

are capable <strong>of</strong> quantitatively mineralising large organic molecules, that is, converting<br />

them to the end mineral constituents <strong>of</strong> CO 2, H 2O <strong>and</strong> inorganic nitrogen products, at<br />

ambient temperatures without significant onerous byproduct formation. In doing so<br />

a variety <strong>of</strong> materials are released from the biomass in the reactor which are collectively<br />

referred to as extracellular polymeric substances (EPS) <strong>and</strong> which contain a<br />

number <strong>of</strong> components which contribute to membrane fouling in an <strong>MBR</strong> (Section<br />

2.3.6.1). <strong>The</strong> relative <strong>and</strong> overall concentrations <strong>of</strong> the various components are<br />

determined both by the feed characteristics <strong>and</strong> operational facets <strong>of</strong> the system, such<br />

as microbial speciation. Anaerobic processes generate methane as an end product, a<br />

possible thermal energy source, <strong>and</strong> similarly generate EPS. Biotreatment processes<br />

are generally robust to variable organic loads, create little odour (if aerobic) <strong>and</strong> generate<br />

a waste product (sludge) which is readily processed. On the other h<strong>and</strong>, they are<br />

slower than chemical processes, susceptible to toxic shock <strong>and</strong> consume energy associated<br />

with aeration in aerobic systems <strong>and</strong> mixing in all biotreatment systems.<br />

2.2.2 Processes<br />

Fundamentals 37<br />

Processes based on biodegradation can be classified according to the process configuration,<br />

feeding regime <strong>and</strong> oxidation state (Table 2.3). Process configuration defines<br />

the way in which the water is contacted with the biomass, which can form a layer on<br />

some supporting media to form a fixed bi<strong>of</strong>ilm or be suspended in the reactor, or<br />

sometimes a combination <strong>of</strong> these. Suspended growth systems provide higher mass

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