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Membrane and Desalination Technologies - TCE Moodle Website

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358 N.K. Shammas <strong>and</strong> L.K. Wang<br />

where mT is the viscosity of water at temperature T, cp, T is the water temperature, C.<br />

Since water temperature can have a significant impact on flux, it is common practice to<br />

“normalize” the flux to a reference temperature during operation for the purposes of monitoring<br />

system productivity independent of changes in water temperature. For MF/UF <strong>and</strong><br />

MCF processes, a reference temperature of 20 C is typically used for convenience, since the<br />

viscosity of water is approximately 1 cp at 20 C. For constant TMP <strong>and</strong> total membrane<br />

resistance, Eq. (9) can be used to illustrate the relationship between the normalized flux <strong>and</strong><br />

viscosity at 20 C <strong>and</strong> the actual flux <strong>and</strong> viscosity at a given temperature of interest T:<br />

J20ðm20Þ ¼JTðmTÞ; (9Þ<br />

where<br />

J20 = normalized flux at 20 C, gal/ft 2 /d<br />

m 20 = viscosity of water at 20 C, cp<br />

J T = actual flux at temperature T, gal/ft 2 /d<br />

m T = viscosity of water at temperature T, cp<br />

Substituting the value of 1 cp for the viscosity at 20 C(m20) <strong>and</strong> Eq. (8) for the viscosity of<br />

water at temperature T (mT), yields an expression for normalized flux at 20 C as a function of<br />

the actual flux <strong>and</strong> the temperature, as shown in Eq. (10):<br />

J20 ¼ JTð1:784 0:0575 T þ 0:0011 T 2<br />

10 5 T 3 Þ; (10Þ<br />

where J20 is the normalized flux at 20 C, gal/ft 2 /d, JT is the actual flux at temperature T,gal/ft 2 /d,<br />

<strong>and</strong> T is the water temperature, C.<br />

It is important to note that the normalized flux (J20) does not represent an actual operating<br />

condition. This term simply represents what the flux would be at 20 C for a constant TMP <strong>and</strong><br />

total membrane resistance. Thus, changes in the value of J 20 during the course of normal<br />

operation are indicative of changes in pressure <strong>and</strong>/or membrane resistance due to fouling. If<br />

values for viscosity are known, the polynomial expression for viscosity as a function of<br />

temperature in Eq. (10) may be simplified to a temperature correction factor (TCF). For a MF,<br />

UF, or MCF process, the TCF is defined as the ratio of the viscosity at temperature T to the<br />

viscosity at 20 C, as shown in Eq. (11):<br />

TCF ¼ mT ; (11Þ<br />

m20 where TCF is the temperature correction factor, dimensionless, mT is the viscosity of water at<br />

temperature T, cp, <strong>and</strong> m 20 is the viscosity of water at 20 C, cp.<br />

Note that the term TCF is often used generically to refer to any type correction factor used<br />

to adjust a parameter for temperature. Thus, the specific equation for the TCF may vary<br />

depending on the parameter to which it is applied. For example, in the context of membrane<br />

filtration, the TCF applied to reference MF, UF, <strong>and</strong> MCF flux to a st<strong>and</strong>ard temperature, as<br />

defined in Eq. (11), is different than that applied to NF <strong>and</strong> RO flux to a st<strong>and</strong>ard temperature,<br />

as shall be shown in Eq. (15). Thus, it is important to always consider the context in which the<br />

term TCF is used.

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