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601 S. Madison Avenue, Suite 60
Monroe, GA 30655
Office: 678-635-7360/Cell: 770-241-6176
Prepared by:
Eden Remediation Services Kenneth Summerour, P.G.
www.edenremediation.com
Overview of Remedial Technologies
Chemical Oxidation (ISCO)
Chemical Reduction (ISCR)
Enhanced Bioremediation (ISB)
Surfactant Applications
Chemical Oxidation (ISCO)
4
Breaking bonds of organic
molecules and inserting oxygen
End products are carbon
dioxide, water, and harmless
salts
ISCO applied via direct push
rod train, injection wells,
or blending methods
Useful on source areas or full scale treatments
Success requires
contact with contaminated media (both
saturated soils and impacted groundwater)
Common Chemical Oxidants
Fenton’s Reagent – H2O2 + Fe+2 OH- + OH- + Fe+3
Catalyzed Hydrogen Peroxide (iron chelation)
Calcium Peroxide/Modified Fenton’s (iron chelation + acidic modifier)
Sodium Persulfate – S2O8-2 + activator SO4
.- + (SO4 .- or SO4
-2)
Sodium and potassium permanganate (ideal for chlorinated ethenes)
Ozone (gas, requires ozone generator)
Chemical Reduction (ISCR)
6
ISCR involves the addition of electrons-
mirror image of
ISCO
Abiotic reactions usually
result in less daughter product
formation
Used on chlorinated plumes, metals, explosives,
etc. Applied via direct injection and solid phase PRBs (goal of developing
reducing zones)
Examples: ZVI, nZVI,
iron sulfides, polysulfides, dithionites,
etc.
Enhanced Bioremediation (ISB)
7
ISB involves the injection or addition of nutrients to stimulate microbial
degradation
Petroleum hydro-
carbons commonly reduced
aerobically
“Treatment Train”: ISCO +
aerobic bio-stimulation
Sulfate reducing bacteria - petroleum
fuels or add iron for
treatment of chlorinated
VOCs
Chlorinated VOCs treated
anaerobically reductive de-chlorination
(lactate, soybean oils,
etc.)
Surfactant Treatments
8
Surfactants are soluble in both oil (fuel) and
water
Used for NAPL
removal by creation of emulsions
Extraction required following emulsifi-cation
Variety of surfactant products available
depending on type of
NAPL
Follow-up monitoring needed to
ensure surfactant impact & removal
Comparison of Remedial Technologies
Speed of reaction: ISCO – ISCR – ISB
Source area treatments: ISCO or surfactants
ISCO can treat NAPL and higher dissolved
Large plumes – ISCR/ISB more cost effective
Treatability testing aids in comparison
Consider multiple technologies
Subsurface Injection Technologies
Direct Push Injection
Target discrete zones
Allows higher pressure injection (ZVI/slurries)
Difficult in “tight” formations/surfacing
Additional wells often needed for monitoring
Injection Wells
Constructed with PVC, CPVC, Stainless Steel
Grout seals – better in “tight” formations
Easier geochemical monitoring
Facilitates multiple point injection
Cost savings with multiple injections
Successful Injections Require:
Source area characterization/vertical contaminant profile
Good estimate of pore treatment volume
Direct contact (especially ISCO/surfactants)
Delivery method suited to site conditions
Sufficient delivery volume/don’t under dose
Measure contact in the field!
Soil Blending Methods: In-Situ
In-Situ blending performed using excavators or augers
Offers maximum contact
Eliminates waste generation
Treat soils AND groundwater together
Allows treatment of low permeability soils
“Green friendly” alternative to off-site land filling
Soil Blending Methods: Ex-Situ
Ex-situ blending involves removal prior to treatment
Soils typically screened and blended in a pug mill
Soils can be stabilized after treatment for re-use
Lower cost alternative to hazardous waste landfilling
Select Case Studies
1) VCP Soil Blending Site (AL)
2) Dry Cleaner – Texas
3) Wood Treatment Facility
(South GA)
4) Industrial Site (Atlanta area)
5) Former Lagoon (Upstate NY)
6) Former Auto Dealer (NW GA)
Alabama VCP Site – Soil Blending Overview
Releases - former paint solvent ASTs
Assessment identified LNAPL and
VOCs (naphthalene and toluene)
Highest total VOCs: 1,000-5,000 ppm
ADEM required haz disposal- blending
offered as an alternative
Treatability study identified CHP +
sodium persulfate + iron chelate
Treatment performed on 300+ tons of
soil from 2-10’
Confirmatory sampling indicated VOC
reduction to below risk target levels
No costly offsite removal required
Cost < $75,000, NFA received
VCP Site (cont.) Soil Blending Results
0
100
200
300
400
500
600
700
800
900
1,000
Baseline Post Blending
So
il C
on
ce
ntr
ati
on
s (
mg
/kg
)
PRE AND POST SOIL BLENDING RESULTS
4-Methyl-2-Pentanone
Ethylbenzene
Isopropylbenzene
Methylcyclohexane
Naphthalene
Tetrachloroethene
Toluene
Xylenes (total)
Former Dry Cleaner - Montgomery Co., Texas
• Release of PCE and daughters, max VOCs >1,000 ppb
• DTW 20-30 ft-bgs, water bearing silty-sand confined by
SC/clay
• PCE degradation products suggested past reductive
de-chlorination
• Risk based treatment goal: < PCLs (protective
concentration limits)
Overview
Former Dry Cleaner - Montgomery Co., Texas
• ISCO treatment designed utilizing iron activated
sodium persulfate (15-20% solution)
• Three injection treatments performed targeting
source area and down-gradient
• Confirmatory sampling indicated results <PCLs
• A NFA later received allowing redevelopment
Results
Wood Treatment Facility Overview
Site in Coastal Plain Province
near Okefenokee Swamp
Creosote and penta-
chlorophenol (PCP) impact in
surface impoundment
NAPL present & dissolved
PAHs to 45-55’
Proposed Corrective action
includes ISCO-soil blending &
down-gradient PRB
Former
Impoundment
Site
Wood Treatment Facility (cont.) Treatability Approach
0
50,000
100,000
150,000
200,000
250,000
300,000
350,000
Control 15% H2O2 15% H2O2 and 0.1% PMG
TREATABILITY RESULTS Anthracene
Benzo(a)pyrene
Chrysene
Fluoranthene
A treatability study indicated either soil blending or ISCO
would be most effective using CHP followed by potassium
permanganate
Wood Treatment Facility (cont.) Soil Blending
An initial soil blending pilot in 2010 resulted in NAPL removal from
CHP-permanganate oxidation
Follow-up pilot in 2012 used high volume dose of CHP only with
significant reduction observed < target goals
Full scale treatment pending following PRB installation
Industrial Facility Overview
22
A small PCE solvent plume was identified in
an industrial park outside Atlanta, GA
Maximum PCE concentrations - 260 ppb
Iron-rich saprolite at a depth of 15-25 feet
Goal was PCE reduction < MCL (5 ppb)
Treatability study indicated sodium
persulfate with natural iron activation
most effective
Injection performed into 15 delivery
wells
Industrial Facility (cont.) Treatment Results
Post Injection Pre Injection
Confirmatory sampling conducted 45, 90, and 120 days
post injection indicated non-detect concentrations of
PCE and degradation products after a single injection
Former Lagoon, Upstate NY Overview
IW
-1
IW
-2
IW
-3
IW
-5
IW
-4
Lagoon
Well 2
Lagoon
Well 1
Site contains two former solvent
disposal lagoons (1,1,1-TCA, DCE
etc.)
Limited soil excavation performed in
the source area
Groundwater pump-and-treat
system installed
VOCs detected in alluvial sediment
and fractured sandstone formation
(15-20 feet)
Former Lagoon (cont.) Treatment Process
25
ISCO treatment performed
using alkaline activated
persulfate to lower source
area VOCs (1,000-5,000 ppb)
Geochemical monitoring
indicated significant oxidant
impact (see graph)
Confirmatory sampling
indicated VOC reduction
Further treatment is pending
Former Auto Dealer Overview
Auto dealership constructed in low lying swamp
Valley and Ridge Province, Conasauga Formation
(limestone)
Groundwater depth 4 -13 ft-bgs in silty-clay/sandy-silt soils
Site
Separate releases of
gasoline and waste
oil/chlorinated VOCs
discovered, plume >200’
LNAPL detected in 22
wells, thicknesses >1’
Former Auto Dealer (cont.) ISCO Treatment Summary
ISCO injections performed using CHP and activated persulfate
Separate ISCO injection performed using potassium
permanganate to treat vinyl chloride
Results indicated complete LNAPL removal and desired
reduction in dissolved phase
Leading edge of plume
treated/controlled
Vinyl chloride eliminated
with one injection
NFA achieved allowing
sale of the property
Subsurface Remediation is Attainable! Keep at it, and remember to:
Start with a good estimate of clean-
up mass and volume
Choose the right chemistry –
treatability testing is always
recommended
Design a “best-fit” strategy
(i.e. soil blending, injection, and
down-gradient PRB)
Measure contact in the field
Follow a performance monitoring plan to expedite site
closure