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Recycling Treated Municipal Wastewater for Industrial Water Use

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TM3: Recycled <strong>Wastewater</strong> System Components and Costs<br />

<strong>Recycling</strong> <strong>Treated</strong> <strong>Municipal</strong> <strong>Wastewater</strong> <strong>for</strong> <strong>Industrial</strong> <strong>Water</strong> <strong>Use</strong><br />

dissolved salts. The sedimentation process would be followed by filtration and<br />

disinfection. Another alternative is a microfiltration process followed by membrane<br />

softening, which could also serve industries that need nearly complete removal of<br />

dissolved salts, as with boiler feed water. Removal of dissolved salts can also be<br />

handled with an ion exchange unit process after a softening/filtration process.<br />

A secondary membrane WWTP (membrane bioreactor) would be an option <strong>for</strong> a new<br />

or expanding WWTP that expects a significant reclaimed water use. Disinfection<br />

requirements would be less and the majority of other constituents are markedly lower<br />

than with conventional secondary treatment. Trace constituent removal can also be<br />

achieved with carbon adsoprtion and advanced oxidation processes, as discussed in<br />

subsequent sections.<br />

If Minnesota continues to adhere to the Title 22 Cali<strong>for</strong>nia <strong>Water</strong> <strong>Recycling</strong> Criteria<br />

and the reuse application requires a recycled tertiary water (<strong>for</strong> potential human<br />

contact uses such as recycle water in cooling towers), most existing WWTPs would<br />

need to add a filtration process to supply reclaimed water. The requirement <strong>for</strong> a<br />

chemical addition/flocculation/ sedimentation process will be site-specific and in<br />

some cases will depend on the types and size of particles in the secondary effluent<br />

and effectiveness of the disinfection process. Some facilities may include the chemical<br />

addition process system to meet phosphorus removal goals <strong>for</strong> both the NPDES<br />

permit and specific reclaimed water requirements <strong>for</strong> the industry served. The<br />

treatment technologies approved to meet the Title 22 criteria are listed in Appendix A,<br />

Exhibit 2.<br />

The following subsections provide an introduction to unit processes to remove<br />

specific categorical constituents. The technologies presented are principally <strong>for</strong><br />

applications onsite at WWTPs. However, the processes could be used alone or in<br />

combination with treatment facilities on the industrial site, particularly where a single<br />

user has a unique water quality. Package systems (multiple process units) supplied by<br />

manufacturers, applicable to industries with smaller demands and/or to target<br />

specific constituents, are not identified in this study. Some proprietary processes are<br />

identified <strong>for</strong> specific unit processes to present the variety of technologies available.<br />

3.2.2 Enhanced Suspended and Dissolved Solids Removal (Chemical<br />

Addition/Softening)<br />

With hard, high salt waters common in Minnesota, treatment may be required to<br />

lower hardness and dissolved solids in the reclaimed supply to an industry.<br />

Traditional chemical addition/coagulation/flocculation/sedimentation processes can<br />

be used to reduce dissolved solids, as well as remove suspended solids in the effluent.<br />

In addition, a coagulation process may be required to meet the Title 22 regulations <strong>for</strong><br />

process requirements.<br />

If the industrial water demand uses the majority of the municipal effluent generated,<br />

it may be cost-effective to locate the treatment process at the WWTP. Additional<br />

benefits can also be realized by the municipality if the planning <strong>for</strong> a reclaimed<br />

supply coincides with expansion and/or improvements planning to meet new<br />

Craddock Consulting Engineers 9<br />

In Association with CDM & James Crook<br />

TM3-Component&Costs_0707

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