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FINAL REPORT Evaluation of Seawater Desalination Projects ...

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EVALUATION OF SEAWATER DESALINATION PROJECTS<br />

PROPOSED FOR THE MONTEREY PENINSULA<br />

surface discharge from a sinking plume than from a bottom plume. However, all else is<br />

rarely equal and much more information about discharge and receiving water characteristics<br />

is required to ensure protection <strong>of</strong> aquatic organisms. Near- and far-field dilution <strong>of</strong><br />

discharged effluents are impacted by many additional factors, such as initial discharge<br />

velocity, discharge and receiving water density, near- and far-field water currents and<br />

flushing, angle <strong>of</strong> discharge relative to currents and other physical features. The proponent<br />

states that the discharge would be a low-velocity discharge <strong>of</strong> diluted brine to near-ambient<br />

density and would remove many <strong>of</strong> the features that enhance far-field dilution. Instead, the<br />

proponent’s approach would leave a “plume <strong>of</strong> effluent” in surface waters (typically<br />

considered some <strong>of</strong> the most sensitive areas <strong>of</strong> a water body) that would have reduced<br />

tendencies to disperse by forces other than far-field advection. This goes against most<br />

accepted regulatory policies and criteria for designing an outfall.<br />

The proposed brine discharge system could be modified for a high-velocity discharge without<br />

dilution in the Salinity Plume Deterrent Systems. Initial velocity would create dilution and<br />

the density could cause a sinking plume (assuming temperatures were controlled so as to not<br />

neutralize the effect <strong>of</strong> density on far-field dilution). However, the potential for recirculation<br />

between the discharge and the intake system under a variety <strong>of</strong> sea conditions is a<br />

concern. A considerable amount <strong>of</strong> design, impact evaluations, and operational controls are<br />

likely to be required to create an acceptable discharge system.<br />

The desalination treatment process proposed to be implemented in the Water Standard<br />

Company <strong>Seawater</strong> <strong>Desalination</strong> Vessel consists <strong>of</strong> the use <strong>of</strong> commercially available<br />

treatment components. The overall treatment process is based on the use <strong>of</strong> reverse osmosis<br />

to accomplish the desalination treatment objectives <strong>of</strong> the project. A low-pressure membrane<br />

pretreatment system (micr<strong>of</strong>iltration) has been included to provide suitable feed water to the<br />

RO process and post-treatment is provided to condition the product water to meet aesthetic,<br />

compatibility and regulatory objectives. Documentation <strong>of</strong> the Water Standard Company<br />

project has been provided to the reviewer under the terms <strong>of</strong> a Non-Disclosure Agreement.<br />

Certain observations presented here cannot be explained in complete detail without violating<br />

this Agreement.<br />

Pretreatment System<br />

Water Standard Company has provided a general description and process flow diagram <strong>of</strong> the<br />

proposed pretreatment process, which indicates the use <strong>of</strong> Pall micr<strong>of</strong>iltration. As discussed<br />

regarding the Coastal Water Project, the use <strong>of</strong> membrane filtration is considered an<br />

appropriate selection for an open intake seawater supply. While existing full-scale<br />

implementation <strong>of</strong> this technology on seawater is not extensive, the track record as RO<br />

pretreatment on other challenging source waters (e.g., municipal wastewater) is substantial.<br />

Additionally, several long-term seawater pilot studies have provided strong indication <strong>of</strong><br />

successful application <strong>of</strong> membrane filtration on seawater. However, it is still standard<br />

practice that membrane pretreatment (micr<strong>of</strong>iltration or ultrafiltration) be pilot tested on local<br />

Monterey Peninsula Water Management District 3-22

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