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up-front orders of magnitude reduction and accelerated bio-destruction using a dispersive injectable reagent Webinar: “Case studies and first EU projects” broadcast live on 3 November 2015 To watch the webinar recording visit regenesis.com/gb/webinars/
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Page 1: up-front orders of magnitude reduction and accelerated bio ... · up-front orders of magnitude reduction and accelerated bio-destruction using a dispersive injectable reagent Webinar:

up-front orders of magnitude reduction and accelerated bio-destruction using a dispersive injectable reagent

Webinar: “Case studies and first EU projects”broadcast live on 3 November 2015

To watch the webinar recording visit regenesis.com/gb/webinars/

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Principal  technology  features  • Rapid  reduc5on  of  groundwater  concentra5ons  •  Mul%ple  order  of  magnitude  concentra%on  reduc%ons  in  days  /  weeks  

• Accelera5on  of  contaminant  biodegrada5on  •  Elimina%on  of  low-­‐concentra%on  performance  tailing  •  Ability  to  secure  stringent  clean-­‐up  targets  

• Wide  subsurface  dispersion    •  Efficient  fieldwork  •  Ability  to  address  areas  of  restricted  access,  deep  plumes  etc.      

• Long-­‐term  efficacy  •  The  reagent  is  not  consumed  –  it  regenerates  in  situ  

 

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•  A  highly  dispersive,  injectable  sorbent  and  microbial  growth  matrix  

•  Sorbent  •  Rapid  drop  in  dissolved-­‐phase  contaminant  concentra%on  •  Immediate  risk-­‐reduc%on  

•  Microbial  growth  matrix  •  Accelerated  bio-­‐destruc%on  of  sorbed  mass  •  Ability  to  secure  clean-­‐up  to  much  lower  targets  

What  it  is  

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•  A  highly  dispersive,  injectable  sorbent  and  microbial  growth  matrix  

•  Sorbent  •  Rapid  drop  in  dissolved-­‐phase  contaminant  concentra%on  •  Immediate  risk-­‐reduc%on  

•  Microbial  growth  matrix  •  Accelerated  bio-­‐destruc%on  of  sorbed  mass  •  Ability  to  secure  clean-­‐up  to  much  lower  targets  

What  it  is  

How does this work?

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Bio Basics: Availability and Threshold Concentrations

•  Bacteria live on surfaces – biofilms •  Think ‘sink plug-hole slime’ or ‘dental plaque’ rather than ‘tadpoles’

•  They have to wait for their growth substrate (food) to come to them – they do not hunt•  They must therefore either sit on / in the food source (rotting vegetables)

•  Or wait for it to dissolve and come to them in solution (groundwater bioremediation)

•  As the plume is progressively cleaned up, the contaminant concentration drops•  The rate that substrate comes to the bacteria reduces

•  The rate that bacteria can therefore degrade it reduces – first order kinetics / half-life degradation

•  Furthermore, below a certain concentration, the rate can slow dramatically•  Threshold concentrations (Smin) for microbial growth – sufficient energy for activity – ‘starvation’ boundary

•  The threshold is variable but typically in the low µg/L range – therefore not relevant for every site

•  This step change slow-down is in addition to first-order diminishing returns

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6,000 µg/L removed in first week

3,000 µg/L removed in second week

1,500 µg/L removed in third week

750 µg/L removed in fourth week 12.5% of initial weekly mass removal

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6,000 µg/L removed in first week

3,000 µg/L removed in second week

1,500 µg/L removed in third week

750 µg/L removed in fourth week 12.5% of initial weekly mass removal

What if this (linear) rate could continue at this lower concentration….?

So this is the general idea – although the top end is accelerated too

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•  Colloidal  ac%vated  carbon  (1  –  2  µm)  •  Size  of  a  bacterium  –  suspends  as  ‘liquid’  •  Huge  surface  area  –  extremely  fast  sorp%on  

•  Proprietary  an%-­‐clumping  /  distribu%on  suppor%ng    surface  treatment  (patent  applied  for)  •  Core  innova%on  •  Enables  wide-­‐area,  low-­‐pressure  distribu%on  through  the  soil  matrix  without  clogging  

•  Low-­‐solubility  /  controlled  availability  matrix  nutrients  •  Support  in-­‐matrix  contaminant  biodegrada%on  •  Does  not  impact  groundwater  /  eutrophica%on  

What the reagent is

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Fracture-emplaced PAC Dispersion-emplaced LAC

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Example in Use- Mixed Solvents -

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Case  Study  –  Mixed  VOC’s  

•  Former  electronics  facility  •  TCE      1,390  µg/L  •  TCA      3,550  µg/L  

•  Sand  to  silty-­‐sand    •  Depth  to  groundwater  3  –  4  m  •  Seepage  velocity  3.7  m/yr  to  the  southwest    

•  Test  site  injec%on  of  PlumeStop™  and  HRC®    

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10  x  reduc%on  

100  x  reduc%on  

non-­‐detect   1  year  and  coun%ng…  

projected  sorp%ve  satura%on  from  influx  

1000  x  reduc%on  

prolifera%on  of  VOC-­‐degrading  microflora    -­‐  dissolved-­‐phase  VOC  at/close  to  ND  -­‐    

18  months  and  coun%ng…  

now >2 years…

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- Distribution through Soil -

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PlumeStop™: reagent distribution

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PlumeStop   Powdered  Ac%vated  Carbon  

PlumeStop™: reagent distribution

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PlumeStop   Powdered  Ac%vated  Carbon  

PlumeStop™: reagent distribution

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PlumeStop   Powdered  Ac%vated  Carbon  

PlumeStop™: reagent distribution

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PlumeStop   Powdered  Ac%vated  Carbon  

PlumeStop™: reagent distribution

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PlumeStop™: reagent distributionSEM image of sand particles without PlumeStop

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PlumeStop™: reagent distributionSEM image of sand particle coated with PlumeStop

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PlumeStop™: reagent distribution

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PlumeStop  Distribu5on  (Field-­‐Prac5cal  Distances)  

•  Long  Column  Study    –  16  foot  length  (5m)  (ID  2”;  5  cm)  –  Fine  to  medium  silica  sand  (210  –  420  µm)  

–  20%  porosity  (est.)  (pore  volume  0.5  gal;  2  L)      

•  Breakthrough  dynamics  •  Retained  carbon  mass-­‐balance  

Influent

Effluent

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Front progresses through dispersive flow

Post-flush residual coating visibly apparent

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Clean chase-water Breakthrough at 1.2 PV

PlumeStop travelling >5 m

back-pressure / flow static – no permeability impact

PlumeStop  applica5on  (start/finish)  

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PlumeStop  Distribu5on  –  wash-­‐out?    

•  Aggressive  chase-­‐water  flushing  –  Nine  pore  volumes  immediately  post-­‐applica%on  

(PlumeStop  dispersive  treatment  s%ll  ac%ve)  

–  Equivalent  seepage  velocity  of  35  km/year  (22  miles/year)  

•  Sacrificial  dissec%on  of  column  –  Broken  into  lengths  and  analyzed  for  elemental  carbon  

(corrected  against  clean-­‐sand,  pre-­‐applica%on  baseline)  

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Influent

Effluent

Total mass retained within column < 0.1% of pore volume 1-2 µm coating on sand particles

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PlumeStop  Distribu5on  –  Laboratory  

Extreme-­‐Case  Test:    •  Low  surface  charge,  low  surface  area  matrix  

–  LAC  reten%on  on  charged  aquifer  fines  will  be  greater    •  High  wash-­‐out  flux    

–  Volume  and  flow-­‐rate  >>  field  condi%ons  –  PlumeStop  dispersive  treatment  longevity  ca.  1  –  3  months  

•  Field-­‐applica%on  control  opportuni%es  –  Volume,  flow-­‐rate,  dilu%on,  chase-­‐water,  injec%on  spacing,  dispersion  adjustment….  

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- Post-Sorption Degradation -- Bio-Regeneration -

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PlumeStop  Bioregenera5on  -­‐  Laboratory  

   

   

   

Contaminant    sorbs  to  sites    available  on  PlumeStop  par%cle    

Microbes  biodegrade  sorbed  

contaminants  

Sorp%on  sites  become  available  for  addi%onal  contaminant  

Principle:  

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•  Microcosm  study  (8  oz.;  230  ml)  –  Test:  water,  lactate,  soil,  PlumeStop,  inoculum  (live)  –  Control:  water,  lactate,  soil,  sodium  azide  (sterilized)  –  Set-­‐up:  Equal  volumes,  no  headspace,  27  reps.  each  

–  Loading:  10  mg/L  PCE  (net)  added  every  two  weeks  –  Study  period:  10  weeks  

•  Dissolved-­‐phase  analysis  (water  only)  •  Total  system  analysis  (water  and  soil  combined)  

PlumeStop  Bioregenera5on  -­‐  Laboratory  

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PlumeStop treatment: capture of spiked PCE – aqueous-phase protected

Control system: PCE concentrations in water climb with each injection

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PlumeStop    bio-­‐regenerated  

capacity  

sorp%on  onto  soil   Sorp%on  onto  soil  plus  PlumeStop  

Theoretical aqueous-phase concentration without sorption

Theoretical aqueous-phase concentration soil + PlumeStop

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PlumeStop treatment: Total PCE mass drops back to baseline between each spike –

Control system: Total PCE mass climbs with each injection

Sorption + degradation ∴  consistent with bio-regeneration  

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PlumeStop  Bioregenera5on  -­‐  Results  

•  PCE  rapidly  captured  by  PlumeStop    –  Same  day  capture  –  aqueous  phase  (groundwater)  cleaned  up  

•  Complete  PCE  degrada%on  post-­‐sorp%on  –  PlumeStop  treatment:  PCE  declines  to  zero  between  each  spike  (whole  system)  

•  Aqueous  phase  protec%on  exceeds  sorp%on  capacity  –  Evidence  of  sorp%on-­‐site  bio-­‐regenera%on  

•  Func%onal  longevity  extended  (indefinitely)  –  Significant  opportuni%es  for  migra5ng  plume  capture  –  back-­‐diffusion  management  

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Q: Does biodegradation proceed post-sorption? A: Yes it does. Q: Is net contaminant degradation rate enhanced, inhibited or unaffected by

sorption into the biomatrix?

PlumeStop™: post-sorption biodegradation

Benzene Degradation Batch-Equilibrium Study•  Soil-water slurry microcosms

–  Treatment 1: with PlumeStop (live)–  Treatment 2: with PlumeStop (sterile)–  Treatment 3: no PlumeStop (sterile)–  Treatment 4: no PlumeStop (live)

•  Sampled destructively in triplicate–  Days 1, 7, 14, 21, 28

•  Water concentration monitored by head-space analysis•  Total benzene mass monitored by whole-system extraction

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PlumeStop™: post-sorption biodegradation

Rapid sorption in both PlumeStop treatments <1 day Ongoing drop in live PlumeStop and live soil control ∴ likely to be bio But could it be a sorption artifact?

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PlumeStop™: post-sorption biodegradation

Total system extract – soil and water No net loss in either sterile system, with or without PlumeStop Both non-sterile systems show benzene reduction Degradation significantly faster in the PlumeStop system

Howard  et  al  (1991)    “Handbook  of  Environmental  Degrada:on  Rates.”  Lewis  Publishers  Inc.    ISBN  0-­‐87371-­‐358-­‐3    

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What if this (linear) rate could continue at this lower concentration….?

So this is the general idea – although the top end is accelerated too

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–performance –

chlorinated solvents – post-sorption degradation – lines of evidence

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Background•  Groundwater bioremediation progress

–  Typically monitored in the dissolved phase

–  Lines of evidence approach – multiple parameters

•  PlumeStop™ - sorption precedes degradation–  Contaminant and daughter products drop to below detection limits

–  What verification lines of evidence for degradation remain open?

•  Case study example –  Geochemical and microbial diagnostic lines of evidence

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California Site

•  Pilot test – single well•  Former dry cleaners•  Modest µg/L PCE residue

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California Site•  ‘Dune Sand’ formation

•  10 m/year groundwater flow

•  High redox conditions (aerobic)

•  No attenuation evident

•  PCE 550 µg/L

•  No daughter products

•  PlumeStop™

•  Electron donor and bacteria

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Pilot Test Arrangement

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Historic Data

Steadily increasing PCE

No daughter products

(aerobic conditions)

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(<0.5µg/L)  

>99.9%  reduc5on  

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Redox ‘sweet spot’ establishes Competing TEA’s decline

(note zero on 2o axis)

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PCE immediately ⬇︎ to ND (<5µg/L) Micro parameters increase post-app then decrease after ~two months

225%

541%676%

(init. ND)3,000 x

(no methanogenesis)

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<  MQL  (5  µg/L;  0.5µg/L)  through  7  consecu%ve  sampling  rounds  –  451  days  (15  months)  and  coun%ng…  

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Data Summary•  >99% (two OOM) PCE concentration reduction within 14 days

–  550 µg/L to non-detect (<5 µg/L)

•  Optimal dehalorespiration conditions established–  Redox from +254 mV to -150 mV (±30 mV) ‘sweet spot’

–  Competing electron acceptors depleted

•  Post-inoculation microbial trends–  Increase then decrease in dechlorination species and enzymes

–  Consistent with solvent metabolism and depletion

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Specifics•  DHC enzyme activity – provides strong indicator of degradation

–  Increase in tceA reductase and vinyl chloride reductase post-application

–  TCE and VC remain below detection limits in groundwater (<5µg/L)

•  Dechlorination species proliferate post-application–  Dehalococcoides spp., Dehalobacter spp., Dehalogenimonas spp. ⬆︎⬆–  Reasonable to assume they are growing on H2(aq) and solvent

•  Geochemical status favourable for dehalorespiration–  but not favourable for competing methanogenesis

–  therefore optimal for bioremediation performance and efficiency

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Conclusions

•  PlumeStop™ - depletion of GW solvents to n/d within 19 days

•  Lines of evidence for post-sorption degradation secured

•  All data obtainable from groundwater samples alone

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- commercial projects -

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Case Study- Manufactured Gas Plant / PAHs -

Richmond  IN  

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PlumeStop™  MGP  

•  Silty  clay  loam  transi%oning  to  sand  and  gravel    

•  Globules  of  oil-­‐like  material  in  pore  space  

•  Injec%on  4.0  –  6.7  mbgl    •  PlumeStop™  •  ORC-­‐Advanced®  

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Average dissolved-phase reduction 95% (to reporting limit)

Post-treatment concentrations all below RISC residential and/or 0.5 µg/L

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Case Study- Migrating Plume – Barrier Application -

North  Carolina  

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PlumeStop™  -­‐  Migra5on  Cut-­‐off  Barrier  

•  Former  Industrial  Dry  Cleaner  •  PCE  residues  •  Pilot  Barrier  •  Mul%ple  targeted  forma%ons  •  2.75  –  12.5  mbgl  

•  Silty  Sand  (ca.  1.4  to  5.3x10-­‐4  cm/sec)  

•  Seepage  Velocity  ca.  22  m/year  

•  HRC®  BDI®  PlumeStop™  

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99.7%  reduc%on   94.2%  reduc%on  

[DEGRADATION  TREND  EXAMPLE]  

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Case Study- Deep Plume Treatment -

West  Allis,  WI  

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PlumeStop™  -­‐  Deep  Plume  Treatment  

•  Former  Dry  Cleaner  •  PCE  residues  •  Vadose  soil  mixing  •  RegenOx®  ISCO  •  Deep  plume  treatment  •  24  –  27  mbgl  

•  HRC®,  BDI®,  PlumeStop™    

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98.6%  reduc%on   99.7%  reduc%on  99.8%  reduc%on  

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Case Study- Filling Station – BTEX Residues -

Pennsylvania  

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PlumeStop™  -­‐  Filling  Sta5on  

•  Former  Filling  Sta%on  •  BTEX  residues  •  Pilot  Applica%on  •  Tight  forma5on  •  2.75  –  4.5  mbgl  

•  Clay  with  Sand  (ca.  3.53x10-­‐7  cm/sec)  

•  Seepage  Velocity  Zero  •  ORC-­‐Advanced®,  PlumeStop™  

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<0.5  µg/L  >98.3%  reduc%on  

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Case Study- Inner-City Development / Time Pressure -

Downtown  Chicago  

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•  Neighborhood  of  McCormick  Place  –  Central  Chicago  –  New  Sports  Stadium  –  New  Hotel  Complex  

•  Solvent  residues  •  Tight  5me  window  •  High  cost  implica5ons  of  delay  •  Key  remedia5on  requirement:  FAST  

Case  Study:    Inner  City  Development  –  Time  Pressure  

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Case  Study:    Inner  City  Development  –  Time  Pressure  

•  Why  the  5ght  5me  window?  – Weren’t  the  solvent  residues  known?    

•  Access  restric5ons  –  historic  buildings  –  Precluded  early  start    

•  Problem  was  moved  aside  

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Case  Study:    Inner  City  Development  –  Time  Pressure  •  PCE  and  TCE  residues  –  up  to  7,440  µg/L  •  Sand  forma%on  over  clay    

–  Treatment  area  300  m  x  500  m  –  (1,000’  x  1,600’)  –  Treatment  Zone  3  –  7  mbgl  -­‐  (10’  –  22’)    

•  Enhanced  bio:  HRC®,  BDI®    –  Sufficient  to  address  the  contamina%on  

•  PlumeStop™    –  Rapid  risk  reduc%on  and  bio  process  accelera%on    –  Take  the  bio  process  out  of  the  groundwater  phase    

•  19  days’  fieldwork  on  site  (Chicago  winter)  –  138  direct-­‐push  injec%ons  –  no  resident  equipment  

 

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96.9%  reduc%on  Total  VOC  

96.5%  reduc%on  Total  VOC  92.3%  ∑  VOC  MCL  567  µg/L  

TCE  MCL  242  µg/L  (site  works  /  access  restric%ons  –  no  groundwater  data)  

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96.9%  reduc%on  Total  VOC  

96.5%  reduc%on  Total  VOC  

Compositional changes consistent with biodegradation

92.3%  ∑  VOC  MCL  567  µg/L  

TCE  MCL  242  µg/L  (site  works  /  access  restric%ons  –  no  groundwater  data)  

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83%  reduc%on  Total  VOC  

84%  reduc%on  Total  VOC  

Compositional changes consistent with biodegradation

79%  

TCE  MCL  242  µg/L  

∑  VOC  MCL  567  µg/L  

(site  works  /  access  restric%ons  –  no  groundwater  data)  

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Chicago  Site  -­‐  Status  •  Rapid  reduc%on  in  groundwater  contamina%on  

–  80  –  97%  from  first  sampling  interval  (total  solvents)  

•  Bio  condi%ons  established  (redox,  TOC,  microbial  numbers)  –  Parent/daughter  compound  ra%o  shivs  (dissolved  phase)    –  (consistent  with  biodegrada%on)    

•  ∑VOC  targets  met  –  from  first  sampling  round  (through  all  rounds)  •  TCE  targets  met  –  from  second  sampling  round  (and  degrading  fast)  •  Comple%on  report  submiwed  (June  2015)  •  No  further  ac%on  required  

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Case Study- Rail Terminal – Solvent Residues -

Bologna,  Italy  

•  

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Two  components  

•  Laboratory  tests  –  basic  principles  –  Dispersion    –  Contaminant  capture  

•  Field  Pilot  –  real-­‐world  prac%cality    – Method  of  applica%on  –  Placement  valida%on  

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Laboratory  Test  Program  –  University  of  Rome  Sapienza  

•  Dispersion  of  PlumeStop  through  columns  –  Sand  column  –  Sand  and  clay  column  

•  Contaminant  capture  by  residual  coa%ng  –  Sand  column  –  Sand  and  clay  column  

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Laboratory  Test  Program  –  Dispersion  

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Sand  Column   Clay  and  Sand  Column  

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Laboratory  Test  Program  –  Capture  

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Laboratory  Test  Program  –  Capture  

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  •  Major  rail  sta%on  upgrade  •  Solvent  residues  (ca.  100  µg/L)  •  Pilot  Applica%on  

•  Complex  alluvial  forma5on  –  Fine  Sand  +  Silt  (ca.  7.5  x10-­‐4  cm/sec)  

•  6.0  –  8.0  mbgl  •  5.0  m/year  seepage  velocity  

–  Fine  to  Med  Sand  (ca.  7.5x10-­‐3  cm/sec)  •  17  -­‐  19  mbgl  •  50  m/year  seepage  velocity  

•  HRC®,  PlumeStop™  •  Field  applica5on  tests  

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Field  Applica5on  

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Field  Applica5on  

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Placement  Valida5on  

Entry into monitoring wells: - Weak evidence of placement

Confirmatory soil coring: - Strong evidence of placement

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Placement  Valida5on  

•  Fine  Sand  +  Silt  (ca.  7.5  x10-­‐4  cm/sec)  •  6.0  –  8.0  mbgl  •  5.0  m/year  seepage  velocity  

post-­‐applica%on   pre-­‐applica%on  Visual indications of evenly dispersed dark material No visible fracture or ‘soil parting’ placement

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Placement  Valida5on  

Visual indications of evenly dispersed dark material No visible fracture or ‘soil parting’ placement

•  Fine  Sand  +  Silt  (ca.  7.5  x10-­‐4  cm/sec)  •  8.0  –  9.0  mbgl  •  ca.  5.0  m/year  seepage  velocity  

post-­‐applica%on   pre-­‐applica%on  

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Placement  Valida5on  

Visual indications of evenly dispersed dark material No visible fracture or ‘soil parting’ placement

•  Sand  and  gravel  layer    •  9.0  –  10.5  mbgl  

post-­‐applica%on   pre-­‐applica%on  

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Placement  Valida5on  

post-­‐applica%on   pre-­‐applica%on  

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Placement  Valida5on  

post-­‐applica%on   pre-­‐applica%on  

“Effective foc” – activated carbon sorption >> organic carbon sorption Plots show factor of 50 – 100 x The factor estimated for TCE is significantly higher

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Sorp5ve  Efficacy  

post-­‐applica%on   pre-­‐applica%on  

•  Soil  from  cores  tested  for  contaminant  capture  in  lab  

•  Batch-­‐equilibrium  study  •  20  g  water;  5.0  g  core  soil  •  Triplicate  samples    

•  PCE:  2,800  µg/L  •  TCE:  7,100  µg/L   ca. 100 x site concentrations

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PlumeStop™  -­‐  Bologna  Rail  Sta5on  –  Retained  Sorp5ve  Efficacy  

 -­‐  preliminary  data  -­‐    PCE: 100% capture in all samples (2,800 µg/L)

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Bologna  Centrale:    Status  

•  Field  Pilot  –  real-­‐world  prac%cality    – Method  of  applica%on    ☑︎  –  Placement  valida%on        ☑︎  

•  First  field  sampling  data  imminent    –  (not  quite  in  %me  for  webinar)  

•  Full  scale  applica5on  approved  –  Scheduled  for  January  2016  

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Europe  Status  

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Europe  Status  

•  Eight  further  projects  scheduled  in  next  4  –  5  months    –  United  Kingdom  –  Belgium    –  Italy  

•  30  further  projects  in  design  phase    •  Wide  interest  everywhere  

–  Ireland  to  Poland  –  Scandinavia  to  Mediterranean  

•  Wide  regulatory  acceptance  

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- usage indicators -

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1.  When time is critical

2.  To secure stringent clean-up targets

3.  For passive control of migrating contamination

4.  As a long–term means of addressing matrix back-diffusion

 

PlumeStop™ – product usage indicators

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PlumeStop™ – product usage indicators

1.  When time is critical

The fastest groundwater remediation technology available today?

•  Immediate risk reduction secured through sorption(especially fast due to high relative surface area and wide dispersion)

•  Long-term destruction secured through in-matrix biodegradation(accelerated degradation achieving bio-regeneration of sorption sites)

 

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PlumeStop™ – product usage indicators

2.  For securing stringent clean-up targets

•  Low µg/L targets are challenging for all technologies

•  Bio typically performs comparatively well, but at very low concentrations, substrate availability becomes insufficient to support microbial activity

•  PlumeStop accumulates low-level contaminants into the bio-matrix until concentrations become sufficient within the matrix to support an active microflora while keeping contaminants out of the groundwater

 

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PlumeStop™ – product usage indicators

3.  Passive control of migrating diffuse contamination

Used in barrier formation to capture diffuse contaminants

•  Concentration of contaminants in matrix for locally intensive treatment

•  Tighter capture zone than bio-barriers alone(especially valuable where space is limited and/or groundwater is fast-flowing)

•  Faster destruction rates and greater timing tolerance between (bio) amendment applications – if still needed

 

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PlumeStop™ – product usage indicators

4.  A long–term means of addressing matrix back-diffusion (i.e. diffusion-driven rebound)

•  PlumeStop maintains a concentration gradient out of the immobile porosity

•  Mobile porosity contaminant conc. remains low due to capture by PlumeStop

•  Sorption sites regenerate due to accelerated in-matrix biodegradation

•  The product is not consumed and remains functional – theoretically for decades

 

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Contaminant  diffuses  out  of  

immobile  porosity  

Biodegrada%on    accelerated  within  the  matrix    

Mobile-­‐porosity  concentra%ons  

decline  /  remain  low  

Sorp%on  sites    are  regenerated  

GW  contaminants  par%%on  into  the  

PlumeStop  

Back-­‐diffusion  gradient    

created  /  sustained  

Bacteria  and  substrate  are  concentrated  

together  

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- close -

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PlumeStop – positioning within Regenesis product range

 •  Used to further increase bioremediation performance

•  Reduced treatment times•  Achieve very low target concentrations (low µg/L range)

•  Can be co-applied with electron donor/acceptor technologies•  Aerobic bioremediation – e.g. with ORC-Advanced®

•  Anaerobic bioremediation – e.g. with HRC®

•  Used as a standalone treatment •  Where natural donor/acceptor supply is adequate •  E.g. migrating plume management – back-diffusion management

 

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PlumeStop – further information

•  www.regenesis.com – case studies, tech bulletins, and

•  white Paper – technology detail & supporting science

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Tech  Bulle5ns  –  available  online:  click  here  

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Tech  Bulle5ns  –  available  online:  click  here  

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up-front orders of magnitude reduction and accelerated bio-destruction using a dispersive injectable reagent

Ques5ons?

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www.regenesis.com  

Jeremy  Birns+ngl   Ph.D. B.Sc. MSEE, CEnv

Vice  President

Environmental  Technology  

+44  1225  731  446

Bath,  UK

[email protected]

Thank  You  


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