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Pilot Study to Evaluate H2 Injection for S i l i d i d bili i fStimulating Reduction and Immobilization of
Uranium in Groundwater at an ISR Site
L Cl J C b Y th G bLee Clapp, Jose Cabezas, Yaneth Gamboa, Waldy Fernandez, Revathi Eti, Dayo Ogungbe,
Uche Eziukwu, Daniel Heuston, , ,Muhammad Ibrahim, Ashutosh Deshpande,
Denis Guleiof, Geraldo Carmona
Department of Environmental EngineeringInstitute for Energy & the Environment
1
st tute o e gy & t e o e tTexas A&M University‐Kingsville
Uranium in the Natural Environment• “Primordial” element part of Earth’s formation 4.5 billion years
ago (originated in supernovas).g ( g p )
• Deposited on land by volcanic action over geologic time.
• Dissolved by rainfall and carried into underground formations.
• Chemical conditions in some locations resulted in concentration into “ore bodies.”
• Fairly common element in Earth’s crust (soil, rock) at about 2‐4 mg/kg and in groundwater and seawater (at about 3 µg/L) ‐ as common as tin tungsten molybdenum etccommon as tin, tungsten, molybdenum, etc.
• A square mile of earth, one foot deep, will typically contain over a ton of uranium; one acre of land, one foot deep, typically has 3 ‐ 4 lbs.
2
Uranium in Groundwater
3
Sources of Radiation to Humans
Update from NCRP Report 160, National Council on Radiation Protection and Measurements Ionizing Radiation Exposure of the Population of the United States, 2006
4
ISR Uranium Mining in South Texas
5http://www.uraniuminfo.org
Survey of U and Rn in Groundwaterin Kleberg and Kenedy Countiesin Kleberg and Kenedy Counties
6
Field Sampling Locations
7
U and Rn Concentrations in Private Wells
Kingsville
UraniumU_ppb
< 1010.01-30.00
30.01 - 100.00
Kingsville
_p< 300301 - 1000
1001- 4000
RadonRn (pCi/L)
30.01 100.00
> 100
1001 4000
> 4001
8
What is uranium used for?
• One pound of yellowcake has energy equivalence of 35 barrels of oil and one 7‐gram (1/4‐ounce) uranium fuel pellet g ( ) phas an energy‐to‐electricity equivalent 17,000 cubic feet of natural gas or 1,780 pounds of coal.
• Nuclear energy provides about 20% of the electricity generated in the U.S.
9
What is “In‐Situ Recovery” Mining?
10http://www.curnamona-energy.com.au/figure5.html
How is Groundwater Currently Restored?
~25% rejection~25% rejection
11www.uraniumresources.com/photos.htm
Effectiveness of Current Restoration Methods
12USGS (2009). Groundwater Restoration at Uranium In-Situ Recovery Mines, South Texas Coastal Plains.
Better Methods for Groundwater Restoration at ISR Sites?
• RO alone does not return the ore zone to its original bi diti
Restoration at ISR Sites?
anaerobic condition.
• Another restoration method that can complement RO treatment is in‐situ reduction and immobilization.
• This involves injecting reductants (e.g., organic j g ( g , gsubstrates, reduced sulfur compounds, H2 gas) to return the aquifer to an anaerobic condition.
• Once the aquifer is anaerobic, dissolved uranium precipitates back into an immobile solid phase.
13
p p p
Eh‐pH‐log PEh pH log PCO2Stability Diagram for
U SpeciesU Species
U(VI) solubility decreases with:U( ) so ub ty dec eases t
Decreasing Eh
Increasing pHIncreasing pH
Decreasing PCO2
14
Research Objective
To evaluate the feasibility of injecting H2 to restore anaerobic conditions and stimulate esto e a ae ob c co d t o s a d st u atein‐situ microbial reduction of uranium.
H th i d th t H i j ti ill ti l t th fHypothesized that H2 injection will stimulate growth of autotrophic IRB and SRB.
H i j ti l d b t t tiH2 injection may also decrease carbonate concentrations, and thus inhibit formation of highly soluble uranyl‐carbonate complexes. p
Autotrophic bacteria also have lower growth yields than heterotrophic bacteria, and are thus less likely to cause
15
heterotrophic bacteria, and are thus less likely to cause bioclogging problems.
Main Redox Reactions
• Uranium oxidation+ +21UO O 2H UO H O
• Uranium reduction
( ) ( )+ ++ + → +2
2 2 2 2s aqUO O 2H UO H O2
www.ch.man.ac.uk/centreforradiochemistryresearch/
( ) ( )+ ++ → +2
2 2 aq 2 sH UO UO 2H
• Ferric iron reductionwww.ch.man.ac.uk/centreforradiochemistryresearch/
( ) ( ) ( ) OH3FeH2OHFeH21
22aqs32 +→++ ++
• Sulfate reduction
( ) ( ) ( )2 2aqs32
3 1 1
1616
− + −+ + → + +22 4 2 2
3 1 14H SO H H S HS 4H O2 2 2
Bottle Sediment Donor Initial pH
Microcosm ExperimentsBottle Sediment Donor Initial pH
1 Mesteña H2 6.52 Mesteña H2 6.53 Mesteña H2 6.54 Mesteña H2 8.55 Mesteña H2 8.56 Mesteña H2 8.57 Mesteña Acetate 6.58 M t ñ A t t 6 58 Mesteña Acetate 6.59 Mesteña Acetate 6.510 Mesteña Acetate 8.5 11 Mesteña Acetate 8.512 Mesteña Acetate 8.513 URI H2 6.514 URI H2 6.515 URI H2 6.516 URI H2 8.517 URI H2 8.518 URI H2 8.519 URI Acetate 6.520 URI Acetate 6.521 URI Acetate 6.522 URI Acetate 8.523 URI Acetate 8.524 URI Acetate 8.525 None None 7.426 None None 7.4
-0.63812-0.46559
Cube Plot for Change in Log U
Acetate0.568750.88581
17
URI
MestenaH28.56.5
Sediment
Reductant
Initial pH
-1.86726-1.65236
-0.70697-0.27857
Microcosm Experiments Comparing H2 and Acetate
Comparing H2 and Acetate
http://www.biocomplexity.usf.edu/pages/pichler_photos.htm
Photographs of the microcosm bottles after one month (top) and two months (bottom) of
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incubation (1st row: Mesteña sediments amended with H2; 2nd row: Mesteña sediments amended with acetate; 3rd row: URI sediments amended with H2; 4th row: URI sediments amended with acetate; two control bottles with groundwater only are at back in lower photo).
Microcosm Study Results
C
2.11
A Initial pHB ReductantC Sediment
Factor Name
Pareto Chart of Standardized Effects for U(95% Confidence Level)
AB
AC
A
B
Term
0.00
-0.25
Init ial pH Reductant
Main Effects Plot for Change in Log UData Means
BC
2520151050Standardized Effect
8.56.5
-0.50
-0.75
-1.00
AcetateH2
0.00
Mea
n
Sediment
URIMestena
-0.25
-0.50
-0.75
-1.00A cetateH2 URIMestena
0
1Initial pH
6.58.5
Initial pH
Interaction Plot for Change in Log UData Means
-1
-2
0
-1
-2
Reductant
H2Acetate
Reductant
19
Sediment
Follow‐up Microcosm Studies
1 2 3 4 5 6
2 5 4 31 43 2 12 5 4 31 43 2 1
20
Column Studies
21
Column Studies Results
4 0 l
3.0
3.5
4.0Ethanol ColumnControl Column
on (p
pm)
2 5
3.0
3.5
4.0 Hydrogen ColumnControl Column
ation (ppm
)
1.5
2.0
2.5
umCo
ncen
tratio
1 0
1.5
2.0
2.5
nium
Concen
tra
0.0
0.5
1.0
1 MOD1 2 3 4 5 MOD2 6 7 8 9Uraniu
0.0
0.5
1.0
1 MOD1 2 3 4 5 MOD2 6 7 8 9
Ura
Sampling PortSampling Port
Hydrogen Column Uranium Concentrations (February 2011)
Ethanol Column Uranium Concentrations (February 2011)( y ) ( y )
22
Pilot Field Study
23
N2
PLC 15’ high vent line In-line
filtersFlow
tFlow
t
2-in ID HDPE hose
NaBr 40% injection
Sampling valve
Choke valve
H2 Control box
metermeter
O2 sensor
LEL sensor
1.25-inch x 200 ft coiled tubing110 ft deep static
water level
multistage ESP at 300 ft deep
¼-inch injection hose
5.5 in PVC casing
1” ID tubing (sparger)
Injection well Extraction well
Goliad Fm C sand
550 ftWell screen
24
Injection well Extraction well
Groundwater Restoration System Schematic 24
Mining Site History
• 1986‐1988: Well drilling and completion.
• 1989‐1998: ISR (oxidation and dissolution of uraninite).
• 1999 2004: Water restoration by RO & permeate reinjection• 1999‐2004: Water restoration by RO & permeate reinjection.
• 2005‐2009: Water stabilization & monitoring (no pumping).
25
H2 Injection Groundwater Restoration:5 Stages5 Stages
• Stage 1 ‐ Equilibration (Jan‐March 2009): GW circulation at 40 gpm without amendments.
• Stage 2 ‐ H2 & Br‐ injection (March‐May 2009): GW circulation at 40 gpm with H2 and Br‐.
• Stage 3 ‐ Stabilization (May‐Nov 2009):No pumping.
• Stage 4 – Reverse flow (Nov 2009‐Oct 2010):g f ( )Reverse GW circulation at 6 gpm without amendments.
• Stage 5 – Stabilization Nov 2010‐June 2011
26
Stage 5 Stabilization Nov 2010 June 2011No pumping.
27
Field Monitoring
28
N1.9 acre within circle
130 ft between injection & extraction
Injection well
Extraction well
Injection well
23
4141
29
Groundwater Restoration: 41-day flow pathlines at 40 gpm
x ?x ? N
xx
41Br-
??XBr-
No Br-
x x?
x x?
30
Detection of Bromide Tracer in Swept Wells
Bromide ConcentrationGroundwater Stabilization Phase
180180w-51
Bromide (ppm)
140
160
7
140
160
w-50w-49
Bromide (ppm)
120
nort
hing
4
5
6
120
w 49
w-53w-46
80
100
y (m
)
2
3
80
100
I-9w-44w-43
41
40
60
0
1
40
60
w-25
w-41
3140 60 80 100 120 140 160
x (m) easting40 60 80 100 120 140 160
w-27 w-28
Modeled vs Measured Br‐ Concentrations
32
Modeled vs Measured Br‐ Concentrations
33
U(VI) ConcentrationGroundwater stabilization phase
180180w-51
U VI (ppm)
140
160
2.8
3.2
140
160
w-50w-49
(pp )
100
120
m) n
orth
ing
1.6
2
2.4
100
120 w-47w-53
w-46
80
y (m
0 4
0.8
1.2
80 w-43I-9
w-44
w-41
40
60
0
0.4
40
60
w-25
34
40 60 80 100 120 140 160
x (m) easting40 60 80 100 120 140 160
w-27 w-28
Sulfate ConcentrationGroundwater stabilization phase
180180w-51
Sulfate (ppm)
p
140
160
780140
160
w-50w-49
100
120
) nor
thin
g
620
700
100
120w-53
w-46
w-47
80
100
y (m
)
460
540
80
100
w-44
w-41I-9
w-43
40
60
380
40
60
w-25
35
40 60 80 100 120 140 160
x (m) easting40 60 80 100 120 140 160
w-28w-27
14Bromide
stop f lowand H2
start H2/Br
stop Br
start reversegw f low12
Stop reversegw f low
8
10
c (p
pm) Estabilization
(without pumping) Estabilization(without pumping)
6Con
c Well 23
Well 41
2
4
0
36
Date
stop flow start reverse6
Uranium
stop reversestart H2stop flow and H2
start reversegw flow
5
U) Stabilization
(without pumping)Stabilization
(without pumping)
stop reversegw flow
4
(ppm
as
U
Well 23
Well 41
( p p g) ( p p g)
2
3
Con
c
1
0
37
Date
38
39
40
start stop H2300
Calcium
stop reversestartH2
stop H2and f low start reverse
gw f low
250 stabilization (without pumping)
stabilization(without pumping)
stop reversegw f low
200
pm)
100
150
Con
c (p
W ll 23
50
Well 23
Well 41
0
41
Date
8 1
pH
start H2stop H2and f low
start reversegw f low
7.9
8.1
t bili ti
stop reversegw f low
7.5
7.7
Well 23
Well 41
stabilization(without pumping)
stabilization(without pumping)
7.1
7.3
pH
6.7
6.9
6.5
42Date
600
Bicarbonate
startH2
stop H2and f low
start reversegw f low
450
500
550
stabilization(without pumping)
stabilization(without pumping)
stop reversegw f low
300
350
400
(ppm
)
200
250
300
Con
c
50
100
150Well 23
Well 41
0
43
Date
300
Chloride
start H2stop H2and f low
start gwreverse f low
250 stabilization(without pumping)
stop reversegw f low
stabilization(without pumping)
200
ppm
)
100
150
Con
c (
50
100Well 23
Well 41
0
44
Date
220Redox Potential
stop H2and f low
startH2
start reversegw f low
140
160
180
200
Well 23stabilization
(without pumping)
stop reversegw f low
stabilization(without pumping)
80
100
120
140
(mV)
Well 23
Well 41
( g)( g)
20
40
60Eh
60
-40
-20
0
-80
-60
45
Date
0 7
Manganese
startH2
stop H2and f low
start reversegw f low
0.6
0.7
stabilization( i h i )
stabilization
stop reversegw f low
0.4
0.5
ppm
)
(without pumping)(without pumping)
0.3
Con
c (p
0.1
0.2Well 23
Well 41
0.0
46
Date
50
Magnesium
startH2
stop H2and f low
start reverse gw f low
40
50
stabilization( ith t i )
stop reversegw f low
30
0
m)
(without pumping)stabilization(without pumping)
20
Con
c (p
pm
Well 23
10
C Well 23
Well 41
0
47Date
0.0010
0.0012
)
Oxidized Species in Solution
Fe(3)
U(6)0.0010
0.0012
L)
Reduced Species in Solution
Fe(2)
U(4)
a b
0.0004
0.0006
0.0008
oncentration (mole/L
S(6)
0.0004
0.0006
0.0008
oncentration (mole/ S(‐2)
0.0000
0.0002
0.000 0.001 0.002 0.003 0.004 0.005 0.006
Co
Moles of hydrogen added per liter of groundwater
0.0000
0.0002
0.000 0.001 0.002 0.003 0.004 0.005 0.006
Co
Moles of hydrogen added per liter of groundwater
Moles of hydrogen added per liter of groundwater
0.0010
0.0012
L)
Solid‐Phase Species
8
10pe and pH of Solutionc d
0.0004
0.0006
0.0008
ncentration (mole/L
0
2
4
6
or pH
pH
pe
0.0000
0.0002
0.000 0.001 0.002 0.003 0.004 0.005 0.006
Con Ferrihydrite, Fe(OH)3(s)
Uraninite, UO2(s)
Pyrrhotite, FeS(s)
‐6
‐4
‐2
00.000 0.001 0.002 0.003 0.004 0.005 0.006p
e
Changes in (a) oxidized species in solution, (b) reduced species in solution, (c) solid‐phase species, and (d) Eh and pH with increasing addition of H2.
48
Moles of hydrogen added per liter of groundwater ‐8 Moles of hydrogen added per liter of groundwater
0.0050
0.0060
0.0010
0.0012
le/L)
n (mole/L)
Oxidized Species in Solution
0.0010
0.0012
)
Reduced Species in Solutiona b
0.0020
0.0030
0.0040
0.0004
0.0006
0.0008
(6) Concentration (mo
nd U(6) Concentration
Fe(3)
U(6)
S(6)0.0004
0.0006
0.0008
oncentration (mole/L)
Fe(2)
U(4)
S(‐2)
0.0000
0.0010
0.0000
0.0002
0.0000 0.0005 0.0010 0.0015 0.0020
S(
Fe(3) an
Moles of dithionite added per liter of groundwater
0.0000
0.0002
0.0000 0.0005 0.0010 0.0015 0.0020
Co
Moles of dithionite added per liter of groundwater
0.0010
0.0012
(mole/L)
Solid‐Phase Species
6
8
10pe and pH of Solutionc d
0.0004
0.0006
0.0008
Phase Concentration (
Ferrihydrite, Fe(OH)3(s)
Uraninite, UO2(s)
Pyrrhotite, FeS(s) 0
2
4
6
pe or pH
pH
pe
0.0000
0.0002
0.0000 0.0005 0.0010 0.0015 0.0020
Solid‐P
Moles of dithionite added per liter of groundwater‐6
‐4
‐2
0.0000 0.0005 0.0010 0.0015 0.0020
Moles of diothinite added per liter of groundwater
Changes in (a) oxidized species in solution, (b) reduced species in solution, (c) solid‐phase species, and (d) Eh and pH with increasing addition of Na2S2O4.49
Moles of dithionite added per liter of groundwater Moles of diothinite added per liter of groundwater
Microbial CharacterizationW
ell 4
1
Wel
l 23
50
Microbial Characterization
C-CTC-CT
51
Summary of Key Results
• ~100,000 scf of H2 was dissolved and safely injected into 2.4 million gallons of groundwater.g g
• Br‐ tracer was detected as far as 160 ft from the injection well which was consistent with flow simulationwell, which was consistent with flow simulation.
• >95% reduction in U has been sustained near both well 23 and well 41 for a little over two years23 and well 41 for a little over two years.
52
Summary of Key Results• ~95% removal of Mo was initially observed near the injection well. However, when flow was reversed, Mo has rebounded to ~181% of the baseline concentration.
• Significant reduction of Fe, Mn, and particularly SO42‐
4was been observed.
• Reduction of 350 mg/L of sulfate corresponded toReduction of 350 mg/L of sulfate corresponded to utilization of 29 mg/L of H2, indicating that essentially all of the injected H2 was consumed before reaching the extraction well.
5353
Additional Observations
• DO consistently remained below 0.3 mg/L.
S th f ti b d ll 23• Some methane formation observed near well 23 during H2 injection (~0.7 mg/L).
• Higher soluble sulfide concentrations near well 23 (~1.0 mg/L)
54
Ongoing & Future Work
• MT3DMS modeling of bromide tracer results.
G h i d li• Geochemistry modeling.
• Future research should assess alternative H2 delivery strategies (e.g., pulsing) to minimize sulfate reduction at the injection well.
• Survey of concentrations of U, Rn and other constituents in private wells in region surround the ISR mining area.
55
Acknowledgments
This material is based upon work supported by UraniumThis material is based upon work supported by Uranium Resources, Inc. (URI), in part by the U.S. Department of Energy under Agreement No. DE‐FGO2‐08ER64519, and in part by the National Science Foundation under Agreement No. HRD‐0734850. Any opinions, findings, and conclusions or recommendations expressed in this material are thoseor recommendations expressed in this material are those of the author and do not necessarily reflect the views of the sponsors.p
56
Thank you!
Questions?
57