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GPS-X Technical Reference

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163 Suspended Growth Models<br />

where:<br />

qperm<br />

= permeate flow rate (m 3 /d)<br />

xliq = concentration of solids in bulk liquid phase within the MBR (kg/m 3 )<br />

fcapture<br />

= solids capture rate or fraction (dimensionless)<br />

qbackw = backwash flow rate (m 3 /d)<br />

xcake<br />

= mass of solids in cake layer (kg)<br />

fbw = backwash solids removal rate (1/m 3 )<br />

qcross<br />

= crossflow or air scour flow rate (m 3 /d)<br />

Am = total membrane surface area (m 2 )<br />

fcross<br />

= cross-flow solids removal rate (kg/m)<br />

Ks,cake = half-saturation coefficient for cross-flow air (kg)<br />

The cake layer mass balance considers the bulk convection of solids to the surface of the<br />

membrane, the solids removed due to backwashing, and the solids removed due to crossflow<br />

aeration. Equation 6.45 ignores the diffusion away from the cake layer into the<br />

bulk liquid as this term is assumed to be small compared to the other terms in the mass<br />

balance. The half-saturation coefficient for cross-flow air and the switching function<br />

based on the mass of cake solids is used to smoothly stop the solids removal as the cake<br />

layer disappears.<br />

The default density of a cake layer particle (see Equation 6.44) is equal to the density of<br />

dry biofilm already used in the <strong>GPS</strong>-X fixed-film reactors. The default porosity of the<br />

cake layer (see Equation 6.44) is given in the<br />

Input Parameters > Physical – Membrane > More… form and is estimated using<br />

information given in Chang et al. (1999). The membrane surface area (see Equation<br />

6.44) is site-specific and should be selected to achieve a flux within the range normally<br />

recommended by the manufacturer (e.g. a typical range for hollow fiber membranes is 17<br />

to 25 L/m 2 /h; see Wallis-Lage et al., 2005).<br />

The backwash solids removal rate (see Equation 6.45) is specified in the<br />

Input Parameters > Physical – Membrane > More … form. It is multiplied in<br />

Equation 6.45 by the backwash flow and the cake solids mass (term 2 in Equation<br />

6.45) to give the mass of solids removed from the filter cake per unit time. The default<br />

backwash solids removal rate was calibrated using data from Garcia and Kanj (2002).<br />

The default backwash flow (see Equation 6.45) is entered in the Input Parameters ><br />

Operational – Membrane form and is based on data provided by Garcia and Kanj<br />

(2002).<br />

<strong>GPS</strong>-X <strong>Technical</strong> <strong>Reference</strong>

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