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PFAS Leachate Removal Pilot Equipment & Testing

Sector: Water Supply and Storage • Location: New Hampshire, United States of America

Source: New Hampshire Purchasing Group

Tender
Closed

The selected vendor will provide equipment , labor , and materials for an on - site FF pilot study to remove PFAS from the Facility ’ s leachate . The vendor will contract directly with the City under the oversight of Sanborn Head , the City , and the New Hampshire Department of Environmental Services ( NHDES ).

Status
Closed
Sector
Water Supply and Storage, Waste Processing and Treatment
Location
New Hampshire, United States of America
Updated
3 Nov 2026
Source
New Hampshire Purchasing Group

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The tender “PFAS Leachate Removal Pilot Equipment & Testing” is a tender record in Taiyo, linked to the Water Supply and Storage sector. It is issued for works, goods, or services related to New Hampshire, United States of America.

Participants

Not available for this record.

Status

Original status

closed

Taiyo status

Closed

Taiyo last update

2026-11-03

Contact

Not available for this record.

Description

Description

The selected vendor will provide equipment , labor , and materials for an on - site FF pilot study to remove PFAS from the Facility ’ s leachate . The vendor will contract directly with the City under the oversight of Sanborn Head , the City , and the New Hampshire Department of Environmental Services ( NHDES ). The objectives of the pilot study are to 1 ) evaluate PFAS removal in landfill leachate , and 2 ) develop design parameters for a full - scale treatment system that can effectively remove PFAS from landfill leachate . Leachate is currently discharged to the City ’ s sewer system and treated as wastewater at the City ’ s wastewater treatment plant ( WWTP ). The goal is to remove PFAS regulated by the NHDES including the following compounds ( and precursor compounds that could transform into the four regulated compounds ) which have Maximum Contaminant Levels as indicated below following the compound name : • Perfluorooctanoic acid ( PFOA )– 12 ppt • Perfluorooctane sulfonic acid ( PFOS ) – 15 ppt • Perfluorohexane sulfonic acid ( PFHxS ) – 18 ppt • Perfluorononanoic acid ( PFNA ) – 11 ppt The pilot study will consist of three phases , as outlined below . The combined timeframe of the three phases is estimated to be six weeks . The pilot study system should have the capacity to operate at or above the current average flow conditions ( 16 , 400 gpd ). When excess leachate flow is generated , beyond the capacity of the pilot system , the excess leachate will go through a bypass to the WWTP without PFAS treatment . The conceptual layout of the pilot study site is shown in the figure in Attachment B . Sanborn Head will be responsible for analytical sampling and coordinating with analytical labs during the study . Phase I : Concept Confirmation and Efficiency Evaluation The PFAS treatment efficiency will be initially assessed under the most robust ( i . e ., conservative ) treatment conditions for 24 to 48 hours . This assessment will provide a baseline starting point for optimization testing . One set of leachate samples will be collected for PFAS and geochemical analysis . Phase II : Operation Optimization Robust treatment conditions often entail longer treatment residence time , frequent changeout , and / or high energy consumption . During Phase II , variable conditions will be tested by the vendor to evaluate PFAS removal efficiency . The goal of this test is to identify the operating parameters that are the most sensitive to PFAS treatment efficiency . The vendor should consider the most sensitive parameters based on the leachate characteristics included in Attachment A and include an explanation in the proposal . Different combinations of operating parameters will be tested to identify the conditions that can successfully achieve the desired treatment efficiencies and result in the lowest operation costs . Each of the combinations will be tested for 24 to 48 hours , during which one set of leachate samples will be collected for PFAS and geochemical analysis . The PFAS analysis for the system influent ( untreated leachate ) and system effluent ( treated leachate ) will be expedited to allow the on - time evaluation of the results . Phase I and Phase II should be completed in 1 to 1 . 5 weeks . The correlation among operational conditions , treatment efficiency , and waste generation should be evaluated and established during Phase II . Phase III : Long - Term Operation The optimal operating parameters identified during Phase II will be tested for a longer treatment duration up to 3 weeks . Various samples will be collected to confirm the repeatability and consistency of this treatment . The primary goal is to confirm the removal efficiency and system operation metrics including waste generation rates . The secondary goal is to evaluate potential scaling and clogging conditions that can affect system operation . System pressure and flow rate will be closely monitored during this phase .

Location

Country

United States of America (USA)

State

New Hampshire

Source

Source

New Hampshire Purchasing Group

URL

More Details

Record type

Tender

Sector

Water Supply and Storage, Waste Processing and Treatment

Article published date

2026-04-28

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