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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 />

effluent quality and type of membrane selected. Pretreatment processes can be<br />

required <strong>for</strong> iron and manganese removal (to avoid scaling on the membranes),<br />

disinfection to avoid biofouling (some membranes are sensitive to chlorine), pH<br />

adjustment to avoid scale <strong>for</strong>mation, and antiscalants. ED membranes have the least<br />

pretreatment requirements, with cartridge filtration recommended.<br />

In addition to pretreatment considerations, there is the management and disposal of<br />

the waste streams. The amount of product water resulting from the treatment of the<br />

incoming water, also called recovery, can range from 50-85 percent <strong>for</strong> RO, 70-90<br />

percent <strong>for</strong> NF facilities, and 80-90 percent <strong>for</strong> ED. Disposal options <strong>for</strong> the<br />

concentrated waste streams vary from energy intensive thermal evaporation<br />

processes to ocean discharge. As concern <strong>for</strong> trace constituents grows, surface water<br />

discharges may be less likely. Concentrate disposal and flexibility of options should<br />

be incorporated in the planning stages to assure it is the optimum choice <strong>for</strong> a specific<br />

site and application.<br />

VRTX Technologies has a product that prevents scale and biofouling in cooling water<br />

systems without the use of chemicals. It relies on localized effects of hydrodynamic<br />

cavitation to create high temperatures and pressures that break the bonds between the<br />

dissolved mineral and water. Minerals (including calcium) are precipitated out of the<br />

water stream as solids <strong>for</strong> disposal. Most microbiological cells are also destroyed at<br />

these extreme temperatures and pressures and dissolved gases leading to corrosion<br />

are stripped away. This technology may be an appropriate application <strong>for</strong> reclaimed<br />

waters where hardness is an issue; but may not apply to high dissolved salt waters.<br />

This unit process will likely be located on the industry site. A major benefit of the<br />

technology is the reduction in chemical use. If it is at the WWTP site, then disinfectant<br />

may need to be added <strong>for</strong> transmission to the industry, which may not be costeffective<br />

or meet other industry goals.<br />

3.2.5 Residual and Specific Trace Constituent Removal (Multiple Processes)<br />

Residual amount of organic and inorganic constituents can still remain after reverse<br />

osmosis and may need to be removed <strong>for</strong> specific industrial applications. Other<br />

constituents occur in trace amount in conventionally treated secondary effluent. These<br />

trace constituents are of concern because of known or suspected toxicity. Of<br />

heightened interest, is the environmental impact of several emerging contaminants of<br />

concern, such as:<br />

pharmaceutically active chemicals (PhACs)<br />

endocrine disrupting compounds (EDCs)<br />

disinfection by products (DBPs) such as N-nitrosodimethylamine (NDMA)<br />

a host of groundwater supply contaminants such as 1,4-dioxane and methyl<br />

tertiary-butyl ether (MTBE)<br />

new and reemerging pathogenic microorganisms such as Legionella pneumophila,<br />

Cryptosporidium, and Giardia<br />

Craddock Consulting Engineers 15<br />

In Association with CDM & James Crook<br />

TM3-Component&Costs_0707

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