Advanced Oxidative Remediation Technology
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Aztech Technologies has experience utilizing in situ and ex situ oxidative
processes to remediate petroleum contaminated groundwater. Aztech Technologies
has designed, installed and operated remediation systems using advanced oxidative
technology to treat groundwater ex situ in trailer mounted systems. Aztech
has also performed in situ treatment including the injection of oxygen releasing
compounds to stimulate bioremediation and the introduction of hydrogen peroxide
to directly oxidize organic compounds.
Electrochemical Peroxidation
Electrochemical Peroxidation, (ECP), is a patented adaptation of Fenton Reagent
chemistry. The unique process utilizes electrochemically produced ferrous
ions (Fe2+) to catalyze a radical oxidation reaction that degrades
aqueous phase chlorinated and non-chlorinated contaminants to water and carbon
dioxide.
Revolutionary Application of an Established Chemical Reaction
The Fenton Reagent Reaction has been known for more than a
century, Aztech Technologies has engineered a modern day application:
- The contaminated influent is first adjusted to slightly acidic conditions,
pH 3-5, with sulfuric acid to facilitate ferrous ion production.
- Hydrogen peroxide (H2O2) is then
injected into the contaminated influent prior to the reactor.
- A low voltage direct current is applied to parallel sacrificial steel electrodes,
introducing ferrous (Fe2+) ions into solution.
- Ferrous ions instantaneously react with hydrogen peroxide to produce hydroxyl
radicals (OHo).
Fe2+ + H2O2 →
OH- + OHo + Fe3+
Relative Oxidation
Power
Cl2 = 1.0 |
| Fluorine |
2.23 |
| Hydroxyl radical (*OH) |
2.06 |
| Atomic oxygen (singlet) |
1.78 |
| Ozone |
1.50 |
| Hydrogen peroxide |
1.31 |
| Perhydroxyl radical(*OOH) |
1.25 |
| Potassium permanganate |
1.24 |
| Chlorine dioxide |
1.15 |
- Hydroxyl radicals (OHo) instantaneously
and indiscriminately degrade organic contaminants radically oxidizing them
to their inorganic constituents: carbon dioxide, carbon monoxide, and water.
Facilitated Three Phase Remediation:
Three-phase remediation expedites decontamination of petroleum spill sites.
- The primary treatment phase occurs ex situ in the ECP reactor and facilitates
the radical oxidation of organic contaminants in the groundwater recovered
from the impacted aquifer. A stream of clean water carrying trace amounts
of hydrogen peroxide leaves the reactor.
- The second phase involves re-injection of ex situ treated water immediately
up gradient or within the plume of contaminated groundwater. The re-injected
water, oxygenated by the trace hydrogen peroxide, promotes in situ chemical
oxidation.
- The third phase establishes aerobic conditions within the plume. Excess
hydrogen peroxide raises the dissolved oxygen content of the plume, allowing
native microbial populations to thrive, effectively enhancing in situ bioremediation
of the contaminant plume.
The ECP Advantage
When compared to other remediation technologies, ECP presents a clear advantage:
- The inefficiency of current technology is rooted in the cyclic nature of
treating a primary contaminated media in a way that produces a secondary contaminated
media.
- Ground water remediation is currently dominated by air stripping and granular
activated carbon (GAC), technologies that rely on transferring organic contaminants
present in extracted ground water from one phase to another.
- Air stripping transfers organic contaminates from the aqueous phase
to the vapor phase via volatilization. Organic contaminants transferred
to the vapor phase, via the air stripper, are captured, via adsorption,
by GAC.
- Organic contaminants are frequently transferred from the aqueous phase
to the solid phase via adsorption to GAC.
- With both treatment technologies, incineration is necessary to destroy
the extracted organic compounds.
- ECP technology destroys organic contaminants without the
production of a secondary contaminated media, consumes little energy, and
in practice, is more cost-effective than other competitive techniques.
- Contaminants treated by the ECP process are not filtered
or extracted; they are completely degraded to water and carbon dioxide
by the process.
- The ECP process produces no contaminated materials
or hazardous bi-products.
- The ECP process utilizes minimal energy consumption
- Costs for transport and treatment of contaminated secondary media (e.g.
GAC) are eliminated.
- Only small quantities of inexpensive reagents are required.
ECP, the Future of Water Remediation
The ECP process destroys organic contaminants in wastewater
via an advanced oxidative reaction that is cleaner, simpler, and more cost effective
than other current technologies.
ECP efficiently reduces hydrocarbon compounds to non-detectable
levels.
ECP is cost effective, treating water contaminated by hydrocarbons
without producing reaction bi-products, which must be further treated or removed
from the site.
Chart 1 Depicts data from an ECP system test conducted on
July 3, 2000
in Saratoga Springs New York. Samples analyzed by Northeast Analytical
Laboratories using EPA method 502.2. Contaminant concentrations are in
parts per billion (ppb). Total VOC excludes MTBE.
ECP is currently being used for removal of gasoline and fuel
oil contamination from groundwater at a site in Saratoga Springs, NY. The treated effluent stream from the ECP
process, when analyzed per EPA Method 502.2 shows all hydrocarbons at nondetectable
concentrations.
ECP is effective for reduction of MTBE in ground water. MTBE
is a nefarious gasoline additive required by EPA for reduction of air pollution
from automobiles. It is toxic and a suspected carcinogen. MTBE’s high
solubility in ground water makes it more difficult to remove than other hydrocarbon
compounds.
Chart 2 Depicts data from an ECP Pilot test conducted on 8/15/01
in Saratoga Springs New York.
500 gal of groundwater contaminated to an MTBE conc. of 2000ppb was treated
at 2gal/min. resulting in an observed 100% reduction of the compound. Samples
analyzed by Northeast Analytical Laboratories using EPA method 502.2. Contaminant
concentrations are in parts per billion (ppb).
ECP technology is developing at an accelerated rate. Future
engineering advances and refinements to the ECP system promise greater success
in efficiency, application, and cost reduction.
For more data on Electrochemical Peroxidation please consult our paper "Pilot
Scale Demonstration of Electrochemical Peroxidation Process at a Petroleum
Spill Site".