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Section 5: Limitations

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Permanganate, solid peroxides, activated sodium persulfate can be used to treat ... All hydrocarbon odor eliminated from all wells ... – PowerPoint PPT presentation

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Title: Section 5: Limitations


1
Section 5 Limitations
2
ISCO Limitations
  • Saturated Zone vs Unsaturated Zone
  • Chemistry
  • CoSolvents
  • Geology /Geochemistry/Hydrogeology
  • NAPL

3
ISCO Saturated Zone vs Unsaturated
  • All ISCO are Aqueous Phase Technologies
  • Ozone is also an Unsaturated Zone Technology
  • In order for treatment to occur, both the
    contaminant and the oxidant must be in solution
    together.
  • Permanganate, solid peroxides, activated sodium
    persulfate can be used to treat the unsaturated
    zone if zone or soils are hydrated during
    treatment.
  • Percent saturated is dependent on the contaminant
    and the soil type

4
What about Chemistry
5
What About CoSolvents
  • All organic Mass is addressed by ISCO
  • Chlorinated Solvents dissolved into oils
    generally behave as the oil. ( sink or float)
  • Cosolvent must be oxidized to reduce target
    analytes
  • BETX is only a 20 portion of fuel contamination
    so remaining solvent must be oxidized

6
What About Geology, Geochemistry, and Hydrogeology
  • If you cant contact the contaminant with ISCO
    you can not treat it.
  • Tight Clays require special treatment
  • Heterogeneity requires special consideration for
    well locations and screen intervals.
  • High Flow Aquifers need to use recirculation to
    maintain contact
  • Carbonate formations can be treated but need to
    be tested for best ISCO approach

7
What about NAPL
  • Very rarely does NAPL exist as free floating
    product
  • If NAPL can be recovered effectively, it should
    be
  • NAPL occupies the pore spaces of soil and exists
    in the colloidal spaces in the soil
  • Effective short-term ISCO treatment requires
    dissolution of the sorbed and NAPL phase in the
    colloidal spaces with heat- Only peroxide
    provides that heat in ISCO Treatments
  • NAPL has been and can be effectively and safely
    treated with ISCO using controlled temperatures
    at low pressures
  • NAPL must be treated with Submerged application
    of chemicals below NAPL Zone.

8
Total Mass EvaluationNature of Contamination
  • Contamination mass exists in four phases in the
    contaminated zone
  • Soil gas
  • Sorbed
  • Dissolved
  • Non-aqueous phase liquid (NAPL) or
    phase-separated
  • Geochemistry, partitioning coefficient (Kow)
    determines the relationship between phases in
    the saturated zone
  • Majority of mass (normally gt80) is sorbed and
    phase-separated

Graphic source Suthersan, 1996
9
ISCO Pilot PAH DNAPL SITE, TRENTO, IT
Site information Old Petroleum Tar Chemical
Distillation Plant Contamination from Closed
Treatment Ponds Geology 0 2 m bgs till, stone
and heterogeneous soil with brick fragments 2
-5m silty/sandy soil black color and heavy
hydrocarbon and naphthalene smell, 5 to 14.3 m
sandy, 13.30 to 16.30 colour black w/
hydrocarbon smell. Flowing DNAPL tars are
present in the last 10 cm. Hydrogeology The
water table is 2.7 m bgs but locally confined
10
ISCOPAH DNAPL, TRENTO, IT
Pilot Test Area
Future Treatment Area
11
ISCO PAH DNAPL SITE, TRENTO, IT
AW-03
Creek
Concrete Wall
PZ-01
AW-02
PZ-02
AW-01
12
ISCO PAH DNAPL SITE, TRENTO, IT
DNAPL in AWs prior to Treatment
13
ISCO PAH DNAPL SITE, TRENTO, IT
14
DNAPL Reduction PAH DNAPL SITE, TRENTO, IT
  • Observations
  • Flow was 2 l/min and increased to 5 l/min after
    hydrogen Peroxide application through Concurrent
    Application in All AWs
  • Temperatures were increased to 40 C in all AWs
  • All DNAPL was removed from AW wells and PZ 01
    within 2 days
  • All hydrocarbon odor eliminated from all wells
  • Secondary indications of Sodium Persulfate
    Oxidation Activity for 6 weeks
  • Dissolved concentrations less than 100 ppb and
    no residual sheen or NAPL

15
DNAPL Reduction PAH DNAPL SITE, TRENTO, IT
  • Observations
  • Controlled Applications of Hydrogen Peroxide can
    effectively dissolve large amounts of NAPL and
    Dissolved Mass by agitation and addition of heat
    at low pressure
  • Controlled application at low pressure controls
    migration of NAPL
  • Persistence of Activated Sodium Persulfate
    consumes dissolved organics for over six weeks
    eliminating repartitioning and rebound potential.
  • Augmentation of additional sodium Persulfate
    after initial application can be performed before
    repartitioning of dissolved mass.

16
Conclusions
  • ISCO and the contaminant must be in an Aqueous
    solution for successful Treatment
  • ISCO can treat all organics
  • ISCO is not selective, it treats all organics
    including non-target Cosolvents and Natural
    Occurring Organics
  • ISCO can safely and effectively treat
    non-recoverable NAPL and prevents rebound
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