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Optimizing Radiochemistry Lab Performance in Decommissioning David - - PowerPoint PPT Presentation

Optimizing Radiochemistry Lab Performance in Decommissioning David A. Montt, CHP Sherman the resident bald eagle at Yankee Rowe Associate & Senior Health Physicist Dade Moeller and Associates, Inc. 1 Acton Place, Suite 201 Acton,


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Optimizing Radiochemistry Lab Performance in Decommissioning

David A. Montt, CHP Sherman the resident bald eagle at Yankee Rowe Associate & Senior Health Physicist Dade Moeller and Associates, Inc. 1 Acton Place, Suite 201 Acton, Massachusetts 01720

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Optimizing Radiochemistry Lab Performance in Decommissioning

  • Achieved Initial Criticality—1960
  • Began Commercial Operation—1961
  • Upgrade to 600 MWth—1963
  • Decision to Cease Operations—2/1992
  • Possession Only Status—8/1992
  • Decommissioning Activities—1992 - 2006
  • Fuel Movement to ISFSI (Begin)—6/2002
  • Fuel Movement to ISFSI Completed—6/2003
  • Decommissioning Complete---10/2006
  • ISFSI & GW Monitoring Continue to Present

YNPS History

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  • http://www.yankeerowe.com/decommis

sioning_dismantle.html - web page for video of

demolition progression from March 2003 to December 2003

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Optimizing Radiochemistry Lab Performance in Decommissioning

  • Optimization of Radiochemistry Lab Performance becomes a

critical necessity.

  • Examples Follow and Include:
  • Developing a process to maintain effective control of effluents

in a construction environment in a rapidly changing environment

  • Identifying the critical stakeholders/customers & work in
  • advance. Know your current and future clients.
  • Identifying the analyses needed going forward,
  • Of those needed, identifying those that can most realistically

be performed on site recognizing resource constraints (personnel, utilities and budget)

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  • Differences between Operating and Decommissioning Chemistry

Needs

– Operating

  • Union/Management Environment – can be contentious and inefficient by

nature.

  • On site staff can be large – 10 to 25+ depending on number of units on site
  • Extensive Analytical capabilities, even with corporate lab capabilities.

– Ion Analysis (Dionex analyzer, or equivalent) – Graphite Furnace (metals) – Atomic Absorption (metals) – Total Organic Compounds (TOC) – Gross Beta – Gamma spectroscopy optimized for operating plant radionuclide levels (plant

  • perational levels)

– Tritium, C-14, low energy beta analyses using liquid scintillation technology – Boron analyses by titration or automated instrument analyses – Sediment, – pH, – conductivity, – Oil and Grease

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Optimizing Radiochemistry Lab Performance in Decommissioning – Decommissioning

  • Union Essentially Non Entity; Workforce essentially becomes
  • ne. Contract workforce becomes more prominent.
  • Staff can be small – 2 to 5 depending on number of units on

site

  • Limited Analytical capabilities solidify, and production and

turnaround time becomes the driver.

– Gamma spectroscopy optimized for operating plant radionuclide levels (focused environmental levels) – Tritium, C-14, low energy beta analyses using liquid scintillation technology – Sediment, – pH, – Conductivity – Oil & Grease

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  • Type of work that needs to be supported

– Final Status Survey (FSS)

  • Structures
  • Soil/Biota
  • Surface water/storm water runoff
  • Surface Water/Sediment

– Groundwater Monitoring

  • D&D operations can impact adversely – will increase your

workload unexpectedly

  • Presents challenges requiring an effective interface with non

radiological environmental

– Unusual, one-of-a-kind operations (examples at end) – Effluents

  • Nature of Effluents changes over time
  • Easy to lose sight of important elements of program
  • Make sure program remains current with reality
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  • Likely Customers must be anticipated early on.

Need to make Sure Radiochemistry is effectively integrated into all Scheduling.

– FSS – Groundwater Group – Effluents Program – Remediation Group (sample analysis) – Non Radiological

  • Shipment of actual/potentially contaminated samples off site
  • Actual on site analyses (PCB and Screening Lab)

– Unique Problem Solving Campaign Leaders – Construction personnel/contractors with little to no radiological background – Regulators – Other stakeholders (public)

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  • Likely and most cost effective analyses

must be anticipated early on.. and justified.

– Value of time savings for on site analyses

  • vs. off site lab vendor
  • Time savings – analyses w/in 24 hours a +
  • Cost savings – minimum $100,000/day
  • Permits timely decision making
  • Timely response to unplanned events
  • Rapid control of situations involving

Regulators

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  • Analyses typically selected may be obvious

– Gamma Spectroscopy – Liquid Scintillation counting

  • Will be H3 most likely, but may need to look as C14, and

possibly others

– Oil and Grease – pH, Sediment – Particle size analysis (0.5u, 1.0u, and up filters) – Boron titration (early on if primary water tank leaks during plant history – Look at on case by case basis; know your plant history

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  • Perhaps not so obvious

– Want NIST Traceable calibration sources

  • Anticipate geometries and media needed
  • 13 gamma spectroscopy geometries

– 4 liter M water, 4 Liter M soil, I liter M water, 1 liter M soil, LSC vial, Planchets w/filters and soil – Non Rad: 100 ml jar soil, 100 ml jar water/gel, 20 ml bottle PCB swipes, etc.

  • Want NIST Source in correct activity range

– Environmental levels for Gamma Spectroscopy – Environmental levels for LSC (H3, C14, etc.)

– May want NIST traceable check sources

  • Gamma scans of soil
  • Gamma spectroscopy of soil

– Anticipate unusual Regulator special requests (total uranium, e.g.)

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  • Understand Lab will move from historical facility to

smaller temporary facility

  • Understand utilities cannot be taken for granted

(electricity, water, temp control, waste)

  • Understand Lab waste will need to be dealt with

and plan in advance

  • Production and results turnaround will be driver
  • Cannot sacrifice quality program, but can optimize

it.

  • You will own and be held accountable for

performance – take control early on before problems arise – have solution implemented.

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  • FSS will be slow and clumsy early on. Will not last. Be ready.
  • Ground water will be similar
  • Understand elements of MARLAP of greatest value and

incorporate early on.

  • Special projects – hard to anticipate all, stay plugged in by

attending daily and special meetings

  • Effluents you will have full control of, So….

– integrate with Non-Rad Environmental early on, – update programs early on to ensure these are in place and work – long lead time especially with FSAR, QAPP, RECP, NPDES, TSCA – Liquid Effluents can be challenging if not addressed effectively early on – understand what you need & want to do. – Remediation Group will be closely tied to, or part of, HP – establish link early on in programs and people

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EXAMPLE

  • FSS Sample Throughput Maximized

– Initially, following movement of Chemistry Lab to a Trailer to support of the Primary Auxiliary Building (PAB) demolition, three HpGe’s were installed leaving a footprint for a 4th. – Based on counting times necessary to meet DCGL’s (30 min/sample) and implementation of MARLAP protocols, a though put of 100 samples per day could be processed – Understanding the necessity to dry samples, the existing methodology created a bottleneck.

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  • FSS Sample Throughput Maximized (Cont.)

– No one owned the Sample prep trailer at that point, so Chemistry took ownership realizing it needed to maintain full control to optimize sample throughput and control prioritization requirements of stakeholders. – 2 drying ovens capable of drying in open pans limited sample production to 70 samples in 24 hours. 2 additional

  • vens were procured as backup in the event of failures of

the older ovens. – A method tried at Maine Yankee was tested and implemented at Yankee Atomic. – Samples were dried in plastic Marinellis in the ovens with the covers off at 130 degrees C. The melting limit was 150

  • degrees. Except for one occasion, this process worked

well, permitting up to 112 samples to be prepped in a 24 hour period and meshed well with lab production capacity.

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  • Other enhancements (from Changes in Sample

collection, prep & drying)

– Moved sifting of samples to the field

  • Eliminated need to deal with large quantities of soil and

rock in trailer

  • Supported 24 hour turn around from receipt to reviewed

and signed results.

  • Supported streamlining of COC

– Permitted use of closed loop sample hood – Enhanced housekeeping of Sample Prep Trailer – Greatly minimized potential for cross contamination of samples

  • Sample drying changes implemented and

basis (next page)

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  • Additional advantages to this methodology included:

– Eliminating at least 2 handling steps, – 2 potential cross contamination opportunities – The need to weigh each Marinelli and cover (the weights between batches did not vary by more than 1%) – The opportunity to introduce bar code scanning of samples for COC simplification through analysis – Elimination of large volumes of soil in the prep facility as the samples were sifted in the field for > 90% of the samples – Chemists who understood lab operations and prep

  • perations worked both facilities alternatively.

– Electric Sifter Carts were designed and successfully field tested, but never gained popularity. – In both the lab and prep facility, the move to self contained ductless hoods was implemented, greatly improving

  • perations.
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  • MARLAP

– Did not mandate percentage of moisture to dry samples to, only that it be minimized – Guidance would lead you to believe must be no more than a small fraction of 1% – Indicated need to individually weigh each sample container and cover – Recommended removal of all extraneous material from sample > 3/4” in dimension except

  • rganic material.

– With +25% agreement between split samples at DCGL level (e.g.), 1% error seemed overkill. – Evaluate and develop technical basis document.

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  • MARLAP

– Electrical supply (current and voltage) fluctuations were not uncommon. – Impacted some of the more sensitive instrumentation – e.g., LSC – Vibration of large trucks moving on road had similar impact

  • n LSC and Gamma spectroscopy.

– Value to counting no more than 20 samples per run with NIST source, blank, followed by spike and blank at end.

  • Provided nice tight QC package with each run of 20 samples.
  • Permitted for identification of bad runs resulting form any one
  • f a multitude of problems
  • Minimized volume of samples needing recount/re-analysis.

– Maintained 2 sigma criteria historically used on site, but flagged data at 3 sigma for further investigation. – Co-located FSS air and water samples with historical environmental sample locations to permit scaling to historical data collected over 30+ years for trend analysis.

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  • Conclusions

– Anticipate your customers early on – Anticipate the analyses plant will most likely need and that provide the greatest benefit – Campaign early on, get buy in and get to work – Set goal of never being the bottle neck in any effort Chemistry/Radiochemistry will be supporting – Figure out what you need to achieve goal – Get Upper management buy in – Get to work – Make sure you have the right team in place – Need good mix of regimented regulars and non-regimented problem solvers – Communication internal to the group and external to the group are critical. (seems obvious but practiced sparingly – not a commodity to be rationed) – There is no avoiding the marriage of non-radiological and radiological effluents in decommissioning.. – Groundwater will most likely be the first opportunity for this. – Hydrogeology will be a good second major for RETS/REMP engineers and scientists…. – As will Non Radiological Environmental Science

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The End!

(of Main Presentation – examples of Unique, One of a Kind Evolutions Typical of Decommissioning Follow for Future Reference)

QUESTIONS?

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Addendum

Unique, One of a Kind Evolutions Typical of One Decommissioning Plant

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  • Examples of Unique, One of a Kind

Operations

– PCB Thermal Desorption – Using Thermal Desorption to Remove Tritium from Concrete – Developing a Flexible Effluents Program to Permit Rapid Adaption to Changing Conditions – Spent Fuel Pool Drain Down & Direct Discharge – Extensive Use of Bench Testing – Effective Integration of Non Radiological Environmental Program in to Radiological

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Chemistry Opportunities in Decommissioning

  • Effluent Monitoring for a Thermal Desorption Unit

– History

  • The Exterior of the Vapor Container (white ball) had been painted with a custom paint

made with PCB oil to maximize its ability to move with the steel as it expanded and contracted with temperature changes

  • Over time, with exposure to the sun, and temperature extremes ranging from -15’F and

+105 ‘F during 30+ years, the paint matrix started to physically degrade, releasing PCB oil, and PCB paint chips to the environment under the VC, in storm drains and in Sherman Pond sediment.

  • These PCBs were discovered in 2001, and remaining PCB’s on the Ball were fixed by

painting over the contaminated paint on the Ball to contain the source.

  • Initially, with an established remediation level of 2 ppm in soil in Massachusetts, the site

was looking at having to ship about 25% of the surface soil in the industrial area off site.

  • With a newly imposed limit of 1 ppm in 2003, the amount of soil involved in remediation

tripled (increased by 300%).

– Remediation Method Chosen

  • Shipping soil off site is now cost prohibitive
  • Methods to remediate soil on site and re-use as fill are searched for and explored.
  • Thermal Desorption is the Method chosen
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  • System Description

– Processing Rate was Impressive – The Unit took soil feed in batches – Samples were taken at predetermined rates (1 sample per cubic yards) at feed and processed soil ends. – Remediated soil was consistently < 1.0 ppm PCB – Soil was run through the system by auger, heated to 725 degrees, volatizing the PCB, which was subsequently condensed and captured in a vessel for recovery/disposal.

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  • System Description (cont.)

– Driving of PCBs also drove off moisture content – Soil was also contaminated with licensed material gamma emitters (Co 60, Cs 137, Ag 108m, etc.) and Tritium – The unit temperature was too low to be concerned with metal volatilization, but moisture was driven off, captured by condensation, and re-used to re-hydrate the soil.

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  • System Description (cont.)

– The Oven/Auger discharge contained a bag house to capture soil – The raw condensate was captured, the PCB oil separated from the water, the water was then channeled to a particulate then charcoal filter – Any radioactive effluents present would also show up in the raw condensate – This is what was sampled, vs. using a stack monitor, to check for effluents.

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  • Monitoring Results

– On a few occasions early in the process, tritium was identified at ~1800 pCi/L. – Tritium levels dropped in the following three samples collected every 2 days. – Levels were then non-detect though the rest of the operation which continued for ~ 9 months. – Water was never discharged, as it was continually re-used to hydrate the soil. In fact water had to be added to the system. – The company who owned the technology had a Massachusetts permit allowing them to discharge up to 0.5 ppm PCB in water. – Yankee’s limit for PCB in water discharges was non-detect.

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  • Monitoring Results (cont.)

– During system set up, assembly and operational testing, dust could occasionally be observed leaving the stack, or the tower where the dry soil was he hydrated. – As a result of this, an air sampler was placed in the vicinity of the unit where predominant wind direction moved the dust. – No licensed material was detected on the particulate filters.

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  • Reactor Support Structure (RSS) Demolition

presented some interesting challenges in meeting DCGL’s for concrete mandated by Massachusetts.

– Extensive core sampling of RSS indicated minor levels of tritium and no C14. – Later and more extensive core sampling found higher levels of tritium, challenging the original plan to use significant tonnage of the RSS concrete (containing minimal levels of activation products), as back fill. – Levels as high as 500 pCi/g, averaging 120 pCi/g – State of MA mandated 12 pCi/g – Based on the tritium levels, most of the RSS concrete would not be available for use as fill.

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  • Solution?

– Someone suggested using the PCB Thermal desorption unit to process the concrete to drive the excess moisture and tritium as tritiated water from the concrete. – If concrete levels could be reduced to 10 pCi/g or less, concrete would be processed using this methodology – The concrete was typically 1” in average dimensions. It could be processed, at a slight additional cost, to 3/4” dimensions. – Chemistry was asked to evaluate this on a Thursday morning, and to provide results and conclusions by the following Monday morning, as contract was under negotiation for PCB remediation with vendor and decision on Tritium remediation had to be made that Monday.

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  • The Evaluation and results

– Vendor lab was contacted. – Oven was available at 300 degrees C (~572 degrees F). 2 hour retention time would be simulated. – Procedure and instructions were drafted up and emailed to the lab. – A courier deliver the RSS concrete samples that afternoon. – Test was conducted Friday and Saturday in vendor lab. Results from vendor lab were emailed out Saturday afternoon to Chemistry.

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  • The Evaluation and results (cont.)

– Chemistry evaluated results, and drafted a report for Monday Morning – Average tritium remaining was just over 10%. – Question on cost effectiveness of pulverizing to 1/4” dimension was raised. – Levels of 5-6% of original tritium concentration would have resulted in a go ahead. – Decision was made to not utilize this process. – Results of study follow. – RSS concrete was shipped to Utah for burial.

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  • Water Processing and Discharge in

Rapidly Changing Environment

– Plant liquid wastes still had to be dispensed with. – In plant treatment would not be available for the duration of D&D – Trenches and open foundations were anticipated to fill with water and contain radioactivity – PCBs & RCRA 8 metals were also anticipated – Continuous discharges and batch discharges were expected – pH, sediment were also as potential problems in regards to discharging to Sherman Pond

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  • Strategy

– NPDES permit up for renewal and to include specifics for SFP discharge – Added construction dewatering category – Specified plant and portable skid treatment – EPA & MADEP approach was to focus on quality of water discharged, and pathways with contingencies to use alternate discharge pathways as D&D progressed.

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  • Strategy (cont.)

– ODCM concentrated on in plant systems, and was revised to include portable, temporary skids – Provision was added for continuous and batch discharges from trenches and foundations. – Added sampling using composite samplers and/or grab samples. – Contingencies for loss of composite samplers included hourly grab samples – Continuous sampling included three initial grab samples – if all three results were within a certain level of agreement, continuous discharge with hourly grabs was permitted.

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  • Results

– For the most part, pH and sediment precluded direct discharge and required the use of temporary processing systems employing Baker Tanks – Radiological constituents were not limiting – Concrete dust and rubble were the source of pH and sediments challenges, and it was ubiquitous. – PCBs also mandated treatment in Baker Tank Systems. 0.5 micron particulate filters were the most effective tool for abating PCB Levels in water – RCRA 8 Metals were not limiting at discharging water with low levels was permissible, and was based on 57 cfs discharge rate from Sherman Dam. If this discharge rate was higher, metal levels could be higher in the effluent, but this flexibility was never necessary.

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  • Operation

– Demolition contractor rented and operated the water processing systems (basis for this) – YAEC provided analytical support, approved discharges,

  • versaw contractor

– Outfalls 003 and 004 were primaries for temporary system discharge points – Processing tanks utilized 120 mesh pre-filter on tank 1, settling tank with recirculation capabilities in tank 2, with the capability for pH adjustment, followed by 1 micron, or 0.5 micron filtration (controlled PCBs and fine sediment) – Fine sediment affected color of the water, was a NPDES permit requirement, and required considerable reprocessing near the end of the project.

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  • Water Processing Under the Vapor

Container During Demolition

– Presented challenges – As steel shell was removed, rain could enter the VC, flush out radionuclides and contaminate the concrete and ground below, increasing the level

  • f remediation required.

– In addition, the paint used to contain the older PCB laden paint, had to be stripped for cut lines to prevent formation of dioxins. – This introduced the potential for PCB contamination in the water, and expansion of affected site areas.

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  • Water Processing Under the Vapor Container During Demolition

– SOLUTION – The solution was a bermed area covered with an impervious barrier to contain the water under the VC – This water was processed through a temporary system located adjacent to the VC (wet side) and positioned to take advantage of gravity flow between tank 1 and tank 2. – Water capacity of the tanks was limiting at times as an EPA certified methodology was required for PCB analysis and RCRA 8 metals analysis and took one week from shipment of samples to receipt of results. – Heavy rains frequently challenged processing capability. – Drops of steel occasionally penetrated the barrier mandating repairs – In one very heavy storm, the berm failed and overflowed, resulting in an estimated loss of ~5000 gallons. ~3000 gallons were captured and pumped back into the berm after the berm was repaired. – Initially water in the berm had levels of PCBs at 2 ppm, and detectable cobalt and cesium. These dropped off as time progressed.

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  • BENCH TESTS

– Bench Testing was an invaluable tool during Decommissioning

  • Examples included pH testing prior to the SFP

discharge

  • Tritium in RSS concrete to determine the validity of

remediation using thermal desorption equipment

  • On site Tritium analysis recovery determination
  • Tritium swipe methodology development at the request
  • f executive management
  • Estimating initial mixes of buffer or acid to adjust pH,

and determine potential for wide swings and at which points when adjusting large volumes for discharge

  • To catch potential problems when changes in work

scope were discovered but not communicated. Screen Well house intake pipe plugging methodology was a good example.

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  • Screen Well House Plugging

– Initially the plan was to plug the discharge line, pump out the water using direct discharge, and fill the pipe with concrete – For reasons still unclear (cost? schedule?), the decision was made to pump the concrete slurry directly into the SWH after the plug was placed by divers without pumping the water out first. – At the request of a conscientious project manager, Chemistry investigated the impact of this change in strategy. – The concrete vendor was contacted and a sample of the mix was

  • btained, with directions mixing ratios.

– 2 gallons of water from the SWH were collected – The concrete was mixed and added to the SWH sample water in proportions based on the volume of water in the SWH and the volume of concrete to be added. – pH was monitored and recorded frequently until readings stabilized. – Initial readings climbed to 12.8 pH units, and stabilized to 12.2 – 12.3 standard units within the first hour. TSS levels, sampled every 15 minutes were high initially, but never exceeded the NPDES limits.

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  • Solution

– A report on the study was penned and widely distributed with recommendations from both Chemistry and the water processing lead. – It was recommended several Baker tanks be leased to permit processing of the water expeditiously, and to provide additional water processing capacity in the future for the increasing number of open pits and open foundations that were challenging the existing system. – The recommendation was not well received initially due to the costs and perceived schedule impacts. However, bench test results left little doubt of impact should recommendations not be implemented. – Following intense negotiations with the demolition contractor, 4 additional baker tanks with processing and recirculation capabilities were placed in service, and except on rare

  • ccasions, were fully utilized continuously.
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END