Bioremediation
of Acid Drainage by Means of a Passive Treatment System
Stoyan
N. Groudev, University of Mining and Geology, Sofia,
Bulgaria
Plamen S. Georgiev, University of Mining and Geology,
Sofia, Bulgaria
Irena I. Spasova, University of Mining and Geology, Sofia,
Bulgaria
Marina V. Nicolova, University of Mining and Geology,
Sofia, Bulgaria
Ludo
Diels, VITO, Mol, Belgium
Restoration
of Ecosystems and Long-Term Stabilization of Initially
Acidic Pit Lakes with a case study at the Gilt Edge Mine
Superfund Site, South Dakota
Joseph
G. Harrington, ARCADIS, Inc., Highlands Ranch CO
Kenneth Wangerud, EPA Region VIII Superfund Group, Denver,
CO
Steven
D. Fundingsland, CDM Federal Programs Corp., Denver, CO
A
Geochemical overview of the Berkeley pit-lake, Butte,
Montana, USA
C.
H. Gammons, Montana Tech of the University of
Montana, Butte, MT
D.
A. Pellicori, Montana Tech of the University of
Montana, Butte, MT
S. R. Poulson, University of Nevada-Reno, Reno, NV
J. Madison, Montana Bureau of Mines and Geology,
Butte, MT
P. Reed, Montana Bureau of Mines and Geology,
Butte, MT
Treatment
of Acid Mine Drainage Wastes in a Membrane Bioreactor
Henry
H. Tabak, USEPA, Environmental Research Center,
Cincinnati, OH
Rakesh Govind, University of Cincinnati, Cincinnati, OH
Use
of SRB in a Gravel Bed Reactor for Treatment of Acid Mine
Drainage Water
John
D. Sheppard, Ph.D., McGill University, Quebec, Canada
Darwin Lyew, Ph.D., Biotechnology Research Institute,
Montreal, Quebec, Canada
Algal
Bioremediation of the Berkeley Pit Lake System-and an In
Situ Test Using Limnocorrals
Dr. Grant G. Mitman, Montana Tech of The University of
Montana, Butte, MT
The Effect of
Drainage Flow and Saturation Conditions on Microbial
Pyrite Oxidation in Mine Waste Rock
Joy
Jenkins and JoAnn Silverstein, Department of Civil,
Environmental and Architectural
Engineering,
University of Colorado, Boulder, CO
Bioremediation
of Acid Drainage by Means of a Passive Treatment System
Stoyan
N. Groudev, Department of Engineering Geoecology,
University of Mining and Geology, Studentski grad –
Durvenitza, Sofia 1700, Bulgaria, Tel: +359 2 687396, Fax:
+ 359 2 687396, Email: groudev@mgu.bg
Plamen S. Georgiev, Department of Engineering Geoecology,
University of Mining and Geology, Studentski grad –
Durvenitza, Sofia 1700, Bulgaria, Tel: +359 2 687396, Fax:
+ 359 2 687396, Email: ps_georgiev@mgu.bg
Irena I. Spasova, Department of Engineering Geoecology,
University of Mining and Geology, Studentski grad –
Durvenitza, Sofia 1700, Bulgaria, Tel: +359 2 687396, Fax:
+ 359 2 687396, Email: spasova@mgu.bg
Marina V. Nicolova, Department of Engineering Geoecology,
University of Mining and Geology, Studentski grad –
Durvenitza, Sofia 1700, Bulgaria, Tel: +359 2 687396, Fax:
+ 359 2 687396, Email: mnikolova@mgu.bg
Ludo
Diels, VITO, 2400 Mol, Belgium, Hoofd
Milieu- en Procestechnologie
, Vlaamse
instelling voor technologisch onderzoek (Vito),
Boeretang
200
, B
- 2400 Mol, België,
Tel:
+ 32 (0)14 33 51 00,
Fax.
+ 32 (0)14 58 05 23, Email:
ludo.diels@vito.be
Acid
drainage waters generated in a uranium deposit were
treated by means of a pilot-scale passive system
consisting of an alkalizing limestone drain, an anoxic
barrier for microbial dissimilatory sulphate reduction and
an aerobic rock filter for manganese and organics removal,
connected in a series. The waters had a pH in the range of
about 2.7 – 3.2 and contained radionuclides (uranium,
radium), heavy metals (copper, zinc, cadmium, lead,
cobalt, nickel, iron, manganese), arsenic and sulphates in
concentrations usually much higher than the relevant
permissible levels for waters intended for use in the
agriculture and/or industry. The water flow rate through
the system varied in the range of about 0.1 – 0.3 l/s.
In the alkalizing drain the pH of the waters was increased
to values higher than 7 and as a result of this most of
the iron was precipitated as hydroxides. A portion of
arsenic was also removed mainly by sorption on these
hydroxides. The permeable barrier had a volume of 12.5 m3
and was filled by a mixture of solid biodegradable organic
substrates (cow manure, plant compost, hydrolysate of
rich-in-cellulose wastes from the paper industry, hay).
The barrier was inhabited by a microbial community
consisting mainly of sulphate-reducing bacteria and other
metabolically interdependent microorganisms. In the
barrier the non-ferrous metals were precipitated mainly as
the relevant insoluble sulphides, and uranium was
precipitated mainly as uraninite (UO2) as a
result of the prior reduction of the hexavalent uranium to
the tetravalent form. Radium was removed mainly as a
result of its sorption by the solid organic matter present
in the barrier. Portions of the other metals were also
removed in this way. The effluents from the barrier were
enriched in dissolved organic compounds and usually still
contained manganese in concentrations higher than the
relevant permissible level. These effluents were treated
in the rock filter where the Mn2+ ions were
oxidized by different aerobic heterotrophic bacteria to Mn4+,
which were precipitated as MnO2. The dissolved
organic compounds were removed as a result of their
oxidation by the heterotrophs inhabiting the filter.
Restoration
of Ecosystems and Long-Term Stabilization of Initially
Acidic Pit Lakes with a case study at the Gilt Edge Mine
Superfund Site, South Dakota
Joseph
G. Harrington, ARCADIS, Inc., 630 Plaza Drive, Suite 200,
Highlands Ranch CO 80129-2379, Tel: 720 344-3500, Fax:
720-344-3535, Email: jharrington@arcadis-us.com
Kenneth Wangerud, EPA Region VIII Superfund Group, 999 18th
Street, Suite 500, Denver, CO
80202-2466, Email: wangerud.ken@epa.gov
Steven D. Fundingsland, CDM Federal Programs Corp., 1331
17th Street, Suite #1050, Denver, CO 80202, Email: fundingslandsd@cdm.com
EPA
NRMRL Mine Waste Technology Program and Region VIII
Superfund office have jointly conducted an in-situ
remediation and restoration technology demonstration and
Treatability Study at the Anchor Hill Pit Lake, Gilt Edge
Mine Superfund site.
The treatability study project has been quite
successful to date. The
pit lake originally contained 77,000,000 gallons of pH 3
water with elevated heavy metals, sulfate, and nitrate.
The Green World Science® patented process for in
situ treatment of metals and other contaminants
(exclusively licensed to ARCADIS) was implemented to
encapsulate metals; create stable long-term water quality
and restore a sustainable ecosystem.
This technology allows for ecosystem restoration in
situ and is substantially more cost-effective than
treatment through ex situ water treatment facilities.
Concentrations
of dissolved COCs have decreased more than 99%, and
aquatic standards (cold water biota under chronic
exposure) for heavy metals were attained.
Discharge of remediated water from the pit lake to
nearby Strawberry Creek began in June, 2004.
Site stakeholders are considering a site-wide water
treatment system whereby acidic waters are collected in
the pit from across the site (at a rate of up to 150 gpm),
treated in the pit lake in a somewhat “batch” mode,
and then subsequently discharging these waters to the
creek following a pre-filtration step.
This innovative approach, creating a long-term
stable ecosystem with low anticipated maintenance
requirements for further treatment of acid migration and
drainage, has substantial implications on closure
strategies for operating and closed pits such as form or
may form at mine closures elsewhere throughout the United
States.
Results
from successful treatment of a uranium mine pit lake in
Sweetwater county, WY and a molybdenum mine pit lake in
Tonopah, NV will also be presented.
A
Geochemical overview of the Berkeley pit-lake, Butte,
Montana, USA
C.
H. Gammons, Dept. of Geological Engineering,
Montana Tech of The University of Montana, Butte, MT
59701, Tel: 406-496-4763, Email: cgammons@mtech.edu
D.
A. Pellicori, Montana Tech of the University of
Montana, Butte, MT
S. R. Poulson, Dept. of Geological Sciences,
University of Nevada-Reno, Reno, NV
J. Madison, and P. Reed, Montana Bureau of Mines
and Geology, Butte, MT
The
Berkeley pit-lake contains over 100 billion L of highly
acidic (pH 2.6), metal-rich water (Fe ~ 1000 mg/L; Zn ~
600 mg/L; Cu ~ 150 mg/L).
The pit-lake began filling in 1983 when mining of
the Butte ore body temporarily ceased, and is still
filling at a rate of 7 to10 million L/day.
Most of this influent water is deep groundwater
draining ~ 10,000 km of subjacent flooded underground mine
workings. In
the past, an additional source of influent water was the
Horseshoe Bend spring (HBS), a large, acidic (pH 3.1) seep
discharging near the base of a nearby tailings dam. In
2003, a modern lime treatment facility was built to treat
the HBS. The
same facility will eventually treat Berkeley pit-lake
water when the lake reaches a critical elevation, some 10+
years from now.
Two
intriguing aspects of the Berkeley pit-lake are that its
water quality is much worse than all known influent
waters, and that the chemistry of the pit-lake has shown
no improvement with time, whereas the water quality of the
subjacent flooded mine workings has improved dramatically
with time. In
the past 5 years, our research group has combined water
quality monitoring, bench-top experiments, and stable
isotope investigations to attempt to explain these
disparities. The
poor water quality of the pit-lake is attributed to a
combination of several factors, including: 1) leaching of
metal salts from the pit walls as the lake levels rise; 2)
evapo-concentration; and 3) subaqueous oxidation of pyrite
by dissolved ferric iron.
A 4th hypothesis – influx of deep
groundwater of poor quality from the direction of the
active tailings dam – is also possible, but is difficult
to test.
Portions
of this study were funded by the
U.S.
Environmental Protection Agency through its Office of
Research and Development under IAG
DW89938870-01-0 through the U.S. Department of
Energy (DOE) National Energy Technology Laboratory under
Contract DE-AC22-96EW96405.
Treatment
of Acid Mine Drainage Wastes in a Membrane Bioreactor
Henry
H. Tabak, U.S. EPA, Environmental Research Center, ORD,
National Risk Management Research Laboratory, 26 West
Martin Luther King Drive, Cincinnati, OH 45268, Tel:
513-569-7681, Fax: 513-569-7105, Email: tabak.henry@epa.gov
Rakesh Govind, University of Cincinnati, Department of
Chemical Engineering, Cincinnati, OH 45221, Tel:
513-556-2666, Fax: 513-556-0217, Email: rgovind@alpha.che.uc.edu
Acid
mine drainage (AMD) is a severe pollution problem
attributed to past mining activities. AMD is an acidic,
metal-bearing wastewater generated by the oxidation of
metal sulfides to sulfates by Thiobacillus bacteria in
both the active and abandoned mining operations. The
wastewaters
contain substantial quantities of dissolved solids with
the particular pollutants (metal sulfates) dependent upon
the mineralization occurring at the mined rock surfaces.
The exposure of post-mining residuals to water and air
results in a series of chemical and biological oxidation
reactions that produce an effluent which is highly acidic
and contains high concentrations of various metal
sulfates.. The metals (metal sulfates) usually encountered
and considered of concern for human risk assessment are:
arsenic, cadmium, iron, lead, manganese,
zinc
and copper. These metals as well as sulfate are considerd
serious pollutants of the acid mine drainage. The
pollution generated by abandoned mining activities in the
area of Butte, Montana has resulted in the designation of
the Silver Bow Creek-Butte area known as Berkeley Pit, as
the largest superfund (National Protection List) site in
U.S. This
paper reports on bench-scale studies conducted to develop
a biotreatment method for acid mine water (AMW) using
membrane bioreactor systems to maximize the biological
sulfate conversion rate and thus enhance the
bioremediation of acid mine water from Berkeley Pit as
well as other acidic water pit lakes.
Several
biotreatment techniques for the treatment of sulfate by
sulfate reducing bacteria (SRB) have been proposed in the
past, however few of them have been practically applied to
treat sulfate containing AMD. This research deals with
development of an innovative polypropylene hollow fiber
membrane bioreactor system for the treatment of AMW from
the Berkeley Pit lake using hydrogen consuming SRB
biofilms. The advantages of using the membrane bioreactor
over the conventional tall liquid phase, gas sparged
bioreactor systems are: large microporous membrane surface
to the liquid phase; formation of hydrogen sulfide outside
the membrane thus preventing mixing with pressurized
hydrogen gas
inside the membrane; no requirement for
gas recycle compressor for hydrogen; membrane
surface is suitable for immobilization of active SRB,
resulting in formation of biofilms,
thus preventing
washout problems associated with suspended culture
reactors; and lower operating costs
in membrane bioreactors, eliminating gas
recompression and gas recycle costs. Information will be
provided on sulfate reduction rate studies and on
biokinetic tests with suspended SRB in anaerobic sludge
and sediment source master culture reactors and with SRB
biofilms in bench-scale SRB membrane bioreactors.
Biokinetic parameters have been deterrnined using
biokinetic models for the master culture and membrane
bioreactor systems. Data
will be presented also on the effect of AMW sulfate
loading at 25, 50, 75 and 100 ml/min in scale-up SRB
membrane units, under varied temperatures (25, 35 and
40oC), to determine and optimize sulfate conversion for an
effective AMD biotreatment. Pilot-scale
studies have generated data on the effect of flow rates of
AMW (in MGD) and varied inlet sulfate concentrations in
the influents on the resultant outlet sulfate
concentration in the effluents and on the number of SRB
membrane modules needed for the desired sulfate conversion
rates i. The pilot-scale data indicate that SRB membrane
bioreactor systems can be applied toward field-scale
biotreatment (sulfate conversiuon) of AMW from Berkeley
Pit lake as well as from other acidic water pit lakes and
for a recovery
of high
purity metals and a usable
water
from the AMW wastes.
Use
of SRB in a Gravel Bed Reactor for Treatment of Acid Mine
Drainage Water
John
D. Sheppard, Ph.D., Department of Bioresource Engineering,
McGill University, 21,111 Lakeshore Road, Ste-Anne de
Bellevue, Quebec, Canada H9X 3V9, Tel: 514-398-7967,
Email: john.sheppard@mcgill.ca
Darwin
Lyew, Ph.D., Biotechnology Research Institute, NRCC, 6100
Royalmount Ave., Montreal, Quebec, Canada H4P 2R2, Tel:
514-496-2664, Email: darwin.Lyew@nrc.ca
This
paper summarizes work that was performed in response to
the need by Noranda Technology Inc. to develop alternative
technologies for the treatment of acid-mine drainage being
produced at various mine sites in Canada. It is based on
the use of sulphate-reducing bacteria entrapped in a
submerged gravel bed subjected to AMD. The hydrogen
sulphide resulting from the reduction of the sulphate in
the AMD binds with dissolved metal ions, producing metal
sulphide precipitates in the gravel bed, thus becoming
essentially immobilized. This work focussed on the
relationship between the activity of the SRB and the
physical characteristics of the gravel bed such that a
rational design procedure could be followed for scale-up
from the laboratory to the field. The laboratory
experiments were conducted using plexiglas columns
containing gravel beds of various characteristics. The
reactors had a working volume of 8 L and the AMD was
treated by semicontinuous addition. The scale-up criteria
was based on the development of two dimensionless numbers,
FSRB and DSRB, that accounted for
the volume of AMD entering the bed (Vc), the
total surface area of the gravel in the bed (tSA), the
interfacial or superficial surface area between the bed
and the AMD (sSA) and the void volume in the bed (Vv).
A relationship was shown to exist between the proportion
of sulphate removed by the SRB to the product of the
ratios of Vc/Vv and sSA/tSA (DSRB),
while the rate of sulphate removal was related to the
product of the inverse ratio, Vv/Vc,
and sSA/tSA (FSRB). Based on data from the
laboratory-scale gravel bed reactors, the degree of
sulphate removal was best with a DSRB value
between 0.0075 and 0.015, while the rate of sulphate
removal was inversely proportional to the FSRB
value.
Algal
Bioremediation of the Berkeley Pit Lake System-and an In
Situ Test Using Limnocorrals
Dr.
Grant G. Mitman, Department of Biological Sciences,
Montana Tech of The University of Montana, Butte, MT
59701, Tel: 406-490-3177, Email: gmitman@mtech.edu
The
Berkeley Pit Lake System is one of the largest
contaminated sites in North America and is located near
the headwaters of the largest superfund site in the
U.S. It is
filling at a rate of about 28.7 million liters per day
with metal laden, acidic (pH 2.7) water.
Chlorella ellipsoidea is one of the first
autochthonous species of algae from the Berkeley Pit Lake
System to be tested for its bioremediative potential.
An experimental matrix was designed for this
experiment using a completely randomized design (CRD). The
matrix was set up with tissue culture flasks having the
following treatments:
Na2HPO4 at 0, 25, 50, 75, 100
mg/l, inoculated vs. no- inoculated with algae (187,500
algae/ml final), and filtered (0.2Fm) vs. non filtered pit
water as variables, NaNO3
amount was fixed at53 mg/ml.
Three replicates were made of each and the
experiment lasted 60 days.
The results of this experiment demonstrated
significant remediation of most metals.
These results will be presented.
As a result of the success of these experiments, it
is hypothesized that these same principles should work
(even better) in the Berkeley Pit Lake system if it is
nutrified. In
order to more fully test this hypothesis it is important
to scale up from imhoff cones to more fully represent the
physical and chemical properties of Berkeley Pit Lake
System Water for the test.
Therefore, the experiment should occur in the
Berkeley Pit. This
will be possible by using Limnocorrals.
These enclosures consist of polyethylene in a
cylindrical form (e.g. 1m diameter x 5 m depth) open at
the top with camouflaged flotation collars and anchored to
the bottom. Limnocorrals have been used for about 40 years
for experimental studies in lakes when it is necessary to
test biological, physical and chemical properties in
situ while varying an aspect of the ecosystem on a
small scale to determine the outcome (e.g. nutrients,
algae) (Cruikshank 1983). Preliminary results of this
experiment will also be presented.
The
Effect of Drainage Flow and Saturation Conditions on
Microbial Pyrite Oxidation in Mine Waste Rock
Joy
Jenkins and JoAnn Silverstein, Dept. Civil, Environmental,
and Architectural Engineering
, University
of Colorado, Boulder, CO
Research
on microbial iron and sulfur cycling in the mined rock
subsurface has focused on biogeochemical reactions at the
water-rock interface. A strategy for remediation of acid
mine drainage (AMD) sources is initiation of a shift in
microbial populations from dominance of iron oxidizing
bacteria to iron and sulfur reducing microorganisms by the
addition of biodegradable organic matter.
However, control of AMD formation by organic carbon
addition requires an understanding of the role of
hydrologic and transport conditions in biogeochemical iron
and sulfur transformation. Experiments were conducted
using two 37.8-liter (10 gallon) rock microcosm tanks
packed with 0.1 – 10-cm rock particles obtained from a
mine waste pile near Leadville, CO resulting in 50%
porosity. Filtered
deionized water was recirculated through the tanks with a
10-day average hydraulic residence time. One tank was run
under saturated conditions and the second was run with
trickle flow to achieve 16% saturation. The headspace of
both tanks was sparged with air. Production of soluble
ferric iron (Fe(III)) and sulfate in the unsaturated tank
was significantly higher than in the saturated system, 16
g/L in the unsaturated tank compared with 0.1 g/L in the
saturated tank drainage water. Ferrous iron was negligible
in the unsaturated tank (< 20 mg/L) whereas it
comprised over 75% of the total soluble iron in the
saturate tank drainage water, indicating suppression of
bacterial iron oxidation. This was consistent with
differences in dissolved oxygen, which averaged 4 mg/L in
the unsaturated tank compared with 1 mg/L in the saturated
tank drainage. The drainage water pH in the unsaturated
tank was 1.5, significantly lower than the saturated tank
drainage, which had a pH in the range of 2.5 – 3.
Results indicate that availability of oxygen is critical
to bacterial iron oxidation. Furthermore, significant
formation of oxidized iron and sulfate products may occur
during periods when drainage flow is minimal.
This indicates that methods to inhibit bacterial
pyrite oxidation must be effective during periods of
unsaturated flow, perhaps even under snow cover.
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