WEBVTT

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Hello , everyone and welcome to the

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video recording for the uh former PS

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Air Force lab meeting to be held on the

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first of November . This is a partial

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recording of all of the materials that

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will be presented on that day . Uh We

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are limited to our site eight and a MS

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update for this recording . And our

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discussion of eggs and other human

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health risk assessment topics will be

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done in person on the first . Uh with

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me is Haley Plant and Jack Bessy to ,

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to give you this recording next slide ,

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please . All right , this will be the

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agenda once we get to the rab on the

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first . So we will start off with the ,

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you know , of course , playing this

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video and then we'll jump into our

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welcome introductions and rab business

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as we always do and then we'll talk

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about , we'll hit up our other um

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basically talking points so that we'll

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get an update on your task contract as

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well as a human health risk assessment

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update uh to include some egg data .

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And then I believe the city of

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Portsmouth has a really nice

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presentation for everybody . And uh of

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course , everybody's eagerly looking

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forward to the dod policy update ,

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particularly the data sharing . And so

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I'll be uh , I'll be presenting on that

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and we can have uh an open discussion

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and what we're gonna do to implement uh

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that policy therapies . All right ,

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without further ado , I'm gonna kick

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this over to Hayley Plant to start on

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our technical presentations . Thank you .

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Sorry for the delay . Thanks , Chris .

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Uh My name is Haley Plant . I'm a

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project hydro geologist for WSP and

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I'll be presenting updates for the aims ,

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the A MS or the airfield interim

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mitigation system . So to start , um

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this figure on the right shows the

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components of the aims which includes

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the cut off and extraction walls at the

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northern extent of the figure and the

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interim mitigation well or IMW area

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which is indicated by the red box . So

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we'll start with the IMW um update the

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IMW as you probably know is a key

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component of the aims . It was

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installed immediately upgrading from

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the Haven . Well , and its design

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mimics the installation of the Haven .

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Well , in order to remove PFAS impacted

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groundwater and reduce the amount of

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PFAS in the supply . Well , the

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operational extraction capacity of the

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area around the IMW and Haven Mall is

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300 gallons per minute . During the AES

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design modeling demonstrated that

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extraction above 300 G PM from this

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area result in contaminants bypassing

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the upgrading and cut off extraction

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wells which compromises the overall

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effectiveness of the aims . The IMW was

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designed to run concurrently with the

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hewell at a combined extraction rate of

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300 gallons per minute . So under

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current operations , the Haven well is

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run at a maximum of 200 gallons per

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minute , which then allows the IMW to

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run at a minimum of 100 gallons a

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minute . Extraction operations are

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co-ordinated by WSP the Air Force and

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the city of Portsmouth to balance

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extraction from this area . It's

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important to note that when the IMW is

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running concentration of PFAS in the

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Haven . Well decrease when the haven

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well was turned back online . Um In

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July 2021 PFAS concentrations in the

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haven well were over 75% lower than the

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initial concentrations that were

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identified in 2014 , which clearly

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demonstrates the effectiveness of the

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interim mitigation . Well ,

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the aims also utilizes um five

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extraction wells north of the IMW that

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were on the the figure on the last

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slide , these wells function , they cut

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off groundwater flow um going south

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along the airfield in October 2021

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during routine cleaning of one of the

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aims extraction wells . Ew one WSP

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identified a vertical break near the

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top of the wells screen that was

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allowing filter pack material to enter

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the well . And as an interim remedy , a

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temporary seal was placed to support

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the wells screen . This vertical break

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is pictured in the top photo um and the

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filter pack material pictured on the

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bottom left since then . In October

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2021 capacity of the uh the well has

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declined overall because of its limited

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capacity . Replacement of EW one was

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initially scheduled for the spring of

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2024 . However , during routine

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maintenance activities on Wednesday ,

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August 9th , an additional screen break

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was identified and the well filled with

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sediment resulting in ultimate failure

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of the well due to the well's failure

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and the importance of keeping all the

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extraction walls online . The schedule

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for replacement of EW one was expedited

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and this replacement is currently

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underway

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on August 18th . WSP drilled a pilot

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boring for the replacement of ew one .

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The replacement well is EW one R and

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it's located 20 ft west of the original

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ew one location data collected during

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drilling was used to develop the design

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of a new extraction well um which will

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maximize extraction capacity for the

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surrounding material . And as of the

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date of this recording WSP has

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completed the well designed with

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concurrence from the Air Force U SEPA

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and New Hampshire Des . Looking ahead

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the installation of EW one R is

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expected in November 2023 which will be

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followed by well development

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installation of the well pump and

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related infrastructure and connections

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to the existing um AMES electrical and

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water lines . Currently WSP is

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continuing coordinate with the PD A and

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civil contractors to finalize the

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construction details . Uh Next up will

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be Jack Desy . We'll present an update

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on site .

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Thank you , Hayley . Hello everyone .

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My name is Jack Bessie . I'm an

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engineer with WSP who spent the last

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three plus years working on optimizing

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the site eight interim mitigation

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system . I want to start by explaining

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what I mean by optimization . Since I

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know it's a term we throw around a lot ,

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but I think is worth clarifying both

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treatment systems were designed and

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built as interim response actions in a

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very short period of time with the

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understanding that they wouldn't

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operate perfectly immediately after

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they started up . But that through a

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step by step process of identifying and

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correcting problems or choke points in

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the process , they would get optimal

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and reach the goals set by the hydro

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geologist to us . Optimization is about

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constant learning to identify new

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limitations in the process . Come up

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with new ideas to address those

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limitations , implement those ideas to

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see if it worked as intended and then

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start looking for the next limitation

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at site . Eight iron fouling is shown

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in the two pictures on the right of the

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screen continues to be the primary

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challenge and is the main limitation

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for increasing extraction rates and

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treatment flow rates . The pictures uh

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on the top right show a pipe filled

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with iron build up which dramatically

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reduces the flow capacity through the

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pipe . On the bottom , right , an

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extraction pump fed with iron which

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reduces the maximum flow that a well

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pump can produce . Operators are

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performing additional cleaning and

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maintenance to limit the extraction

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capacity reductions from this type of

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fouling . And through their step by

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step , optimization processes have been

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able to dramatically improve the

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handling of iron within the site .

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Eight building and treatment process

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allowing more contaminated groundwater

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to be treated . The picture in the

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center bottom of the screen uh shows

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the Lamela clarifier , the primary iron

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removal tool , we have uh producing

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basically iron free water flowing

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through that top channel uh as it's

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intended to do . Despite the challenges

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with fowling , the incremental

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improvement has resulted in capacity

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increases with decreasing system

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downtime . However , operators are

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running out of avenues for significant

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improvement without major changes to

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the equipment in the facility and are

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approaching their maximum capacity with

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the existing equipment which is uh

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still below the overall target .

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Operators have been increasing . Uh The

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site eight treatment flow through the

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series of improvements . Uh We're

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discussing um they've been identifying

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specific limitations , applying the

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corrective measures and then re

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evaluating to identify the next . Since

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the last rab update on the site , eight ,

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average operating flow has increased

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notably and we're now able to run all

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10 extraction wells , albeit not quite

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at full speed . The chart here shows

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the daily average flow rates in gallons

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per minute and really , I think

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demonstrates the progress made uh

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throughout this last year

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to address uh the capacity limitations ,

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an optimization plan has been developed

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to bring the site eight I MS treatment

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capacity to match the extraction while

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pumping capacity and goals of the

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Hydroge Hydro Geological team . The

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first step in this plan was to remove

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the regenerative ion exchange resin and

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replace it with single use ion exchange

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resin is used at the games . The new

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resin was put in the same treatment

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tanks uh which are shown in the picture

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here . This was completed this past

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spring and the new resin is performing

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well as expected . Uh This step was one

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of the many iterative steps taken uh

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this past year to improve treatment

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capacity .

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The next step in the optimization plan

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is to test an additional an additional

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type of filtration that will improve

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metals and solids removal . Prior to

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phos treatment , the drawing on the

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right of this screen uh represents that

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type of filter . This test is

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anticipated to begin early this winter

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and will inform fu future changes to

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the process that will improve treatment

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capacity .

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The core of the optimization plan we've

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developed is to make use of the space

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freed up by removing the regeneration

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support equipment and replace and

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upsize a number of key process units

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that have been determined to be

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undersized for the dynamic and

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challenging groundwater conditions .

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The site eight I MS must treat the plan

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assumes a new filter similar to the one

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being pilot tested this winter would be

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installed along with several major

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process units that would be replaced or

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upsized to remove limitations within

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the process to increase treatment flow .

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The plan is not final and no formal

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design for this has been completed at

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this time , the core elements of it are

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feasible and based heavily on the

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experience we've gained operating this

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system since it was started up . And

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just as a note , the two units that you

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see the sledge filter press in the

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foreground and the sledge holding tank

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in the background are both units that

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we've identified as key limitations to

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increasing uh flow further and would

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are both likely to be replaced or

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duplicated . Uh through this

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optimization plan .

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I know a number of RB members visited

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the site eight treatment plant this

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summer and likely saw the large number

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of drums and other waste containers

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stored in front of the treatment plant

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building . And we just wanted to

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provide an update on that these process

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generated phos impacted wastes have

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been stored while a new vendor and end

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disposal facility was identified and

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set up . Uh as of the date of the rab ,

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uh The vast majority of this waste will

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have been removed from peas and is

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being transported to an approved

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permitted disposal site in Michigan

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where all phos waste uh from peas will

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be transported . Going forward the

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pictures here uh going clockwise from

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the top left uh show some used ion

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exchange resin uh that's removed a lot

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of the phos from the groundwater there .

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Uh pressed sludge solids , mostly iron

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in the top right and then some used bag

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filters on the bottom there .

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Even with the operational challenges ,

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the C I MS has posed , we've seen

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demonstrated impacts of the treatment

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system in hydraulic capture and water

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quality . The extraction wells continue

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to maintain hydraulic control ,

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preventing the spread of PFAS impact to

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groundwater declines in phos

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concentrations have been observed

12:30.248 --> 12:32.192
across the C eight I MS Monitoring

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network including within the bedrock

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trough where 70% of the wells

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demonstrate decreasing or probable

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decrease in concentrations of phos

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bedrock trough is the area indicated by

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the brown dotted lines on the picture

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on the left here . Uh Outside of the

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bedrock trough , reduced phos

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concentrations as compared to pre I MS

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start up , levels have been observed at

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08-6046 A bedrock monitoring . Well to

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the northwest of the bedrock trough at

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Watering Spring and in Pickering Brook ,

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north of the bedrock trough , that's

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all for uh our update on the two

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treatment plants at peas . And I'll

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pass the presentation back to Chris

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King to wrap up our recording .

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All right . Thank you for that , Jack

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and uh Haley . That's a lot to unpack .

13:28.172 --> 13:30.283
Um Hopefully you'll have some time to

13:30.283 --> 13:32.394
take a look at this a couple of times

13:32.394 --> 13:32.349
and develop any further questions you

13:32.359 --> 13:34.880
might have on site eight or aims . Um

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Otherwise , uh you can , our meeting is

13:37.450 --> 13:39.450
on the first of November at the New

13:39.450 --> 13:41.672
Hampshire Des Building . Uh the address

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is shown on the screen here . Uh We are

13:43.894 --> 13:46.228
looking forward to seeing you in person .

13:46.228 --> 13:45.739
There's a lot more to discuss . We have

13:45.750 --> 13:47.750
some other presentations as well as

13:47.750 --> 13:49.472
mentioned before . The City of

13:49.472 --> 13:51.528
Portsmouth has a lot . Uh They wanna

13:51.528 --> 13:53.639
share about the operations of their ,

13:53.639 --> 13:55.583
their treatment plant as well . Um

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Could you please return on the previous

13:55.609 --> 13:58.030
slide ? So right now , um this is the

13:58.039 --> 14:00.909
presentation schedule that we had . Uh ,

14:01.119 --> 14:03.063
this , this video is , um , it's a

14:03.063 --> 14:05.063
partial recording , so we have much

14:05.063 --> 14:07.175
more to discuss . So please , uh , if

14:07.175 --> 14:09.397
you can arrive by five o'clock and then

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we'll begin our discussions there and

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we'll also have some other materials

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for you to walk around and look at ,

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should you decide to show up early at 4

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30 ? We'll all be there . We'll have

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our experts both in the Air Force and

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uh WSP . And also we'll be saying

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goodbye to Ona Ferguson . So most of

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you all who know her , um , please come

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and wish her well in her new endeavor .

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All right . Until the first , we shall

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see you there . Bye everybody . Thank

14:31.028 --> 14:29.500
you .

