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The Use of Permanganate at Two Chlorinated Ethene Sites
Michael F. Dacey,
GeoInsight, Inc., Manchester, NH
A “Green Oxidant” for In-Situ Chemical Oxidation for the
Treatment of Contaminated Soils
Maureen Dooley,
Regenesis, Wakefield, MA
Ben Mork, Regenesis, San Clemente, CA
Micro-Encapsulated Oxidant Technology: Enhancing
In Situ
Chemical Oxidation (ISCO) with Selective Oxidation and
Controlled-Release Permanganate
Pamela J. Dugan,
Carus Corporation, Peru, IL
Beth Vlastnik,
Carus Corporation, Peru, IL
Sheryl Ivy,
Carus Corporation, Peru, IL
Lindsay Swearingen, Specialty Earth Sciences, New
Albany, IN
Jason
Swearingen, Specialty Earth Sciences, New Albany, IN
Aggressive Remediation of NAPL and Coal Tar Impacted
Sites Using Ozone and Hydrogen Peroxide Injection
Charles
Whisman, Groundwater & Environmental Services, Inc.,
Exton,
PA
The Use of Permanganate at Two Chlorinated Ethene Sites
Michael F.
Dacey,
GeoInsight, Inc., 25 Sundial Ave. Suite 515 West,
Manchester, NH 03103, USA, Tel: 603-314-0820, Fax:
603-314-0821, Email: mfdacey@geoinc.com
Single and multiple in-situ
applications of sodium and potassium permanganate were
completed at two sites in Massachusetts and New
Hampshire and monitored for short- and long-term impacts
to chlorinated ethene concentrations in ground water.
Concentrations of the primary constituents,
tetrachloroethene and trichloroethene, were observed to
be significantly reduced in target monitoring wells, but
post-injection response times varied from one week to
over one year.
Injection result variability is attributed to
various factors including injection quantity/volume,
number of injections, rate of injection, and
geology/hydrogeology of the receiving formation.
Permanganate reacts almost
instantaneously to cleave the
carbon-carbon double bond in chlorinated ethene
compounds.
However, matrix heterogeneities result in preferential
permanganate loading in higher permeability zones.
Post-injection permanganate distribution to lower
permeability zones is accomplished primarily by
diffusion and advection and results in longer time
frames to treat some target areas.
Significant post-injection rebound occurred at
one site that was attributed to re-equilibration between
the treated dissolved phase and the adsorbed phase.
In this case, multiple targeted applications were
successful in treating both the dissolved- and adsorbed
contaminant phases, and resulted in long-term
(permanent?) dissolved-phase contaminant concentration
reductions.
Treatment in the overburden smear zone was effected by
low water table position at the time of treatment with
residual rebound attributed to permanganate depletion
prior to achieving complete contact with the full smear
zone thickness.
To avoid displacement of source
area contaminants, applications were refined to use a
minimum volume of permanganate and carrier liquid.
Minimally diluted sodium permanganate was
injected at very low rates and solid potassium
permanganate granules were placed within a smear zone
trench. In
both instances contaminant displacement and downgradient
migration was minimized by using focused applications of
concentrated permanganate.
Based upon the results from these
two sites, multiple smaller permanganate applications
over a longer time frame are recommended to better
evaluate the full effect of each application and enable
more targeted follow-up applications.
This approach potentially reduces chemical costs,
but should be weighed against labor costs and other time
related factors.
A “Green Oxidant” for In-Situ Chemical Oxidation for the
Treatment of Contaminated Soils
Maureen Dooley,
Regenesis, 19 Belmont Rd, Wakefield, MA 01880, USA, Tel:
781-245-1320, Email: mdooley@regenesis.com
Ben Mork Ph.
D., Regenesis, 1011 Calle Sombra, San Clemente, CA
92673, USA, Tel: 949-366-8000, Email: mork@regenesis.com
A variety of oxidants have been
used to degrade organic contaminants in industrial
wastes, soil and groundwater, including percarbonate,
perborate, peracetic acid, nitric acid, persulfate,
permanganate, and ozone.
Sodium percarbonate (SPC) is often cited as a
powerful, but safe, environmental benign (“green”)
oxidant for these applications. In fact, SPC has been
used in numerous industrial and household products (e.g.
detergent bleaches) since the 1960’s replacing oxidants
like perborate because SPC has less environmental
concerns.
However, proper activation of SPC is important to its
efficiency, especially in in-situ applications for the
purpose of transforming groundwater or soil contaminants
into less harmful chemical species. Catalyzed SPC
systems, like RegenOx™, have been shown to be very
effective in oxidizing a wide range of contaminants.
This ISCO technology exhibits many “green”
attributes which make it more environmentally friendly
when compared to other oxidants.
The details of these attributes will be the topic
of this presentation.
Micro-Encapsulated Oxidant Technology: Enhancing
In Situ
Chemical Oxidation (ISCO) with Selective Oxidation and
Controlled-Release Permanganate
Pamela J. Dugan,
Ph.D., Beth Vlastnik, Sheryl Ivy, Carus Corporation,
315 5th Street Peru, IL 61354, Tel: 815-224-6870, Fax:
815-224-6896
Lindsay Swearingen, Jason Swearingen, Specialty Earth
Sciences, New Albany, IN
Controlled-release techniques have
been utilized extensively in diverse fields such as
pharmaceutical and agrochemical technologies. However,
controlled-release of an oxidant during
in situ
chemical oxidation (ISCO) is an emerging concept that is
extremely relevant to the field of environmental
remediation, yet to-date has received little attention.
ISCO with permanganate, persulfate, and catalyzed
hydrogen peroxide has shown great promise for
remediation of many recalcitrant organic contaminants of
concern (COC). Because the oxidant also reacts with
natural organic matter, inorganic soil constituents, and
other reduced compounds, having a protective barrier
that controls the release of the oxidant, and provides a
coating that has an affinity for, and dissolves rapidly
in hydrocarbons, may enhance the efficiency of ISCO.
Micro-encapsulated potassium
permanganate particles (MEPPs) were created and
characterized. Paraffin wax is used as the
environmentally benign matrix material for encapsulating
the sub-micron size solid permanganate particles. The
paraffin matrix not only serves to protect the solid
potassium permanganate particles from fast dissolution
and potentially undesirable nonproductive reactions but
allows for selective release of permanganate in the
presence of dense nonaqueous phase liquids (DNAPL). The
paraffin wax met the following requirements: solid at
room temperature, substantially water-insoluble (i.e.,
hydrophobic), soluble in tetrachloroethene (PCE) DNAPL
(i.e., oleophilic), biodegradable, and resistant to
permanganate oxidation. To evaluate selective and
enhanced-release of permanganate in the presence of
DNAPL, batch tests were conducted in zero headspace
reactors (ZHRs). The goal of these experiments was to
evaluate the rate at which MEPPs were released in
deionized (DI) water and in the presence of PCE DNAPL.
Results indicate accelerated permanganate release
from MEPP's in the presence of DNAPL as compared to
permanganate release in the MEPP reactors containing DI
water. Experimental results reveal that the encapsulated
oxidant technology holds promise enhancing traditional
ISCO through the creation of controlled-release
micro-encapsulated permanganate capable of
selective-release in the presence of DNAPL. Future work
involves investigation into encapsulating other
oxidants, and catalysts.
Aggressive Remediation of NAPL and Coal Tar Impacted
Sites Using Ozone and Hydrogen Peroxide Injection
Charles Whisman,
P.E, Vice President of Engineering, Groundwater &
Environmental Services, Inc., 440 Creamery Way, Suite
500, Exton, PA 19341 Tel: 610-458-1077, Ext. 3008, Fax:
610-458-2300, Email: cwhisman@gesonline.com
This presentation will discuss
innovative ways to aggressively remediate sites with
large NAPL plumes, including diesel fuel, heating oil,
and coal tar impacts.
Case studies will discuss how ozone and hydrogen
peroxide injection systems can reduce volatile organic
compound composition (in NAPL, soil, and groundwater) as
well as the NAPL/coal tar thickness and volume.
The presentation will discuss recent case studies
where ozone and hydrogen peroxide injection systems were
designed and operated to achieve cleanup goals at sites
with NAPL impacts.
This discussion will evaluate tools
that can assist with the evaluation and design of the
chemical oxidation system, including laser induced
fluorescence, enhanced feasibility testing, and the
membrane interface probe.
Case studies include information obtained from
remediating significant NAPL impact at manufactured gas
plant (MGP) facilities, Brownfield sites, heating oil
releases, and petroleum refineries/terminals.
These case studies are completed in-field
projects which utilized chemical oxidation for an
expedition and aggressive remediation of significant
NAPL mass.
The discussion will provide guidance regarding the type
of NAPL that may be suitable for chemical oxidation and
considerations for safely implementing a NAPL
remediation strategy. Case studies will provide a
detailed analysis of the remediation effects on soil,
groundwater, and NAPL during aggressive chemical
oxidation, and evaluate the various investigation and
confirmatory tools were used to assess the remediation
performance.
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