March 2005
 

Paper:
"Design of a Membrane Filtration System to Meet Operational Criteria"

Author:  
Lori Kappen, EIT

Presented:

New Jersey AWWA
Annual Conference
Atlantic City, NJ

(A similar poster was presented at the AWWA Membrane Technology Conference in Phoenix, AZ)

 
 

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ABSTRACT  

 

The treatment capacity of a 1990's vintage conventional water treatment plant was to be expanded from 20 to 42 mgd.  The owner desired to provide capacity expansion while ensuring the ability to comply with the worst-case disinfection requirements of the proposed Long Term 2 Enhanced Surface Water Treatment Rule (LT2).  The plant's existing treatment process includes pre-ozonation, conventional filtration, post-ozonation, GAC adsorption and chlorine disinfection.

           

Alternatives

Two treatment process options for meeting the owner's requirements were evaluated for cost and effectiveness: 1) adding UV disinfection to the current treatment process; and 2) replacing conventional filtration with membrane filtration.  The membrane filtration option was pilot tested and selected for plant expansion.

 

Warranty Considerations

 

In preparing the specifications and procurement documents for the membrane equipment, strong consideration was given to ensuring the membrane system would meet operational requirements over its entire life.  In order to minimize operational costs and avoid negative impacts on other treatment processes, warranty requirements were developed and negotiated to assure system integrity and to limit wastewater production, chemical cleaning frequencies and upstream and downstream flow variation associated with membrane cleaning. 

 

O&M Considerations

A long-term service agreement was capitalized and stipulated in the warranty to require the manufacturer to provide maintenance and replace the membrane modules upon failure.  The membrane fibers were also required to pass periodic challenge and porosity testing.  Membrane cleaning chemicals were specified to meet NPDES permit requirements, and waste neutralization system redundancies were established to avoid delays in membrane cleaning; or the need to discharge un-neutralized waste to the on-site wastewater handling facilities.

Contact author
for full paper

 

 

 

 

 

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