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Membrane and Desalination Technologies - TCE Moodle Website

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

Disposal options for MF/UF backwash residuals are similar to those for conventional water<br />

treatment plants, <strong>and</strong> typically include the following:<br />

1. Discharge to a suitable surface water body<br />

2. Discharge to the sanitary sewer<br />

3. Treatment with supernatant recycle <strong>and</strong> solids disposal<br />

The discharge of backwash residuals to surface water bodies or the sanitary sewer is likely<br />

to be subject to state <strong>and</strong>/or local regulations <strong>and</strong>, in the case of surface water discharge, to<br />

require a permit. Moreover, the potential to utilize one of these options may be complicated if<br />

the residuals include chemical wastes. In addition to the use of coagulants added to the feed,<br />

some backwash procedures utilize chlorine or other chemicals. Small amounts of chlorine<br />

may be quenched <strong>and</strong> acids or bases can be neutralized prior to discharge, although larger<br />

amounts or other types of chemicals added to the backwashing processes may require<br />

additional treatment or preclude discharge to a surface water body or sanitary sewer.<br />

On-site treatment options for MF/UF backwash residuals are also similar to those that<br />

might be used with conventional media filtration, <strong>and</strong> include clarification, sedimentation<br />

lagoons, gravity thickening, centrifuging, belt filter presses, or a combination of these<br />

processes (26). A second stage of MF or UF may also be utilized to further concentrate<br />

residuals <strong>and</strong> increase process recovery. If a sedimentation process is used to treat MF/UF<br />

backwash residuals, the addition of a coagulant may be necessary to improve the settling<br />

characteristics of the solids if coagulant is not already applied in the MF/UF pretreatment<br />

process. With on-site treatment, the supernatant is generally recycled to the treatment plant<br />

influent while the concentrated solids are transported off site for l<strong>and</strong>filling or other means<br />

of disposal. As with discharging, the addition of chlorine or other chemicals to the<br />

backwash process may complicate residuals treatment. It is important to note that backwash<br />

residuals concentrate any pathogenic organisms that are present in the feed water, as well as<br />

other suspended solids. Although the control of such concentrated pathogens in filter<br />

backwash residuals is largely unregulated, the potential treatment of this stream should be<br />

taken into consideration if these residuals are to be discharged into a surface water receiving<br />

body.<br />

6.2. Chemical Cleaning Residuals<br />

Both MF/UF <strong>and</strong> NF/RO membranes undergo periodic chemical cleaning, <strong>and</strong> thus both<br />

types of systems generate spent chemical waste as a byproduct of these processes. As with the<br />

backwashing process for MF/UF, the frequency of chemical cleaning varies on both a site<strong>and</strong><br />

system-specific basis. Although chemical cleaning is conducted much less frequently<br />

than backwashing, the frequency is also more difficult to predict. Generally, MF/UF systems<br />

are cleaned no more frequently than once every month for efficient operation <strong>and</strong> the<br />

minimization of system downtime, although it is not uncommon for these systems to operate<br />

for much longer without requiring chemical cleaning. The cleaning frequency for NF/RO<br />

may vary anywhere from 3 months to 1 year, depending on the feed water quality <strong>and</strong> the<br />

effectiveness of feed water pretreatment for minimizing fouling. However, because chemical

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