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The MBR Book: Principles and Applications of Membrane

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2.1.4 <strong>Membrane</strong> process operation<br />

2.1.4.1 Flux, pressure, resistance <strong>and</strong> permeability<br />

<strong>The</strong> key elements <strong>of</strong> any membrane process relate to the influence <strong>of</strong> the following<br />

parameters on the overall permeate flux:<br />

(a) the membrane resistance,<br />

(b) the operational driving force per unit membrane area,<br />

(c) the hydrodynamic conditions at the membrane:liquid interface,<br />

(d) the fouling <strong>and</strong> subsequent cleaning <strong>of</strong> the membrane surface.<br />

<strong>The</strong> flux (normally denoted J) is the quantity <strong>of</strong> material passing through a unit area<br />

<strong>of</strong> membrane per unit time. This means that it takes SI units <strong>of</strong> m 3 /m 2 /s, or simply<br />

ms �1 , <strong>and</strong> is occasionally referred to as the permeate or filtration velocity. Other non-<br />

SI units used are litres per m 2 per hour (or LMH) <strong>and</strong> m/day, which tend to give more<br />

accessible numbers: <strong>MBR</strong>s generally operate at fluxes between 10 <strong>and</strong> 100 LMH. <strong>The</strong><br />

flux relates directly to the driving force (i.e. the TMP for conventional <strong>MBR</strong>s) <strong>and</strong> the<br />

total hydraulic resistance <strong>of</strong>fered by the membrane <strong>and</strong> the interfacial region adjacent<br />

to it.<br />

Although for conventional biomass separation <strong>MBR</strong>s the driving force for the<br />

process is the TMP, for extractive or diffusive <strong>MBR</strong>s (Sections 2.3.2–2.3.3) it is respectively<br />

the concentration or partial pressure gradient. Whereas with conventional<br />

pressure-driven <strong>MBR</strong>s the permeate is the purified product, for extractive <strong>MBR</strong>s the<br />

contaminants are removed from the water across the membrane under the influence<br />

<strong>of</strong> a concentration gradient <strong>and</strong> are subsequently biologically treated, the<br />

retentate forming the purified product. For diffusive bioreactors neither water nor<br />

contaminants permeate the membrane: in this case the membrane is used to transport<br />

a gas into the bioreactor.<br />

Resistance R (/m) <strong>and</strong> permeability K (m/(s bar), or LMH/bar in non-SI units) are<br />

inversely related. <strong>The</strong> resistance is given by:<br />

P<br />

R �<br />

J<br />

�<br />

h<br />

Fundamentals 29<br />

(2.1)<br />

where � is the viscosity (kg/(m s 2 )) <strong>and</strong> �P (Pa) the pressure drop, <strong>and</strong> can refer to<br />

either the TMP (�P m Pa/bar in non-SI units) or individual components which contribute<br />

to the pressure drop. Permeability is normally quoted as the ratio <strong>of</strong> flux to<br />

TMP (hence J/�P m), the most convenient units being LMH/bar, <strong>and</strong> sometimes corrected<br />

for temperature impacts on viscosity.<br />

<strong>The</strong> resistance R includes a number <strong>of</strong> components, namely:<br />

(a) the membrane resistance,<br />

(b) the resistance <strong>of</strong> the fouling layer (adsorbed onto the membrane surface),<br />

(c) the resistance <strong>of</strong>fered by the membrane:solution interfacial region.

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