Management of Mining- Impacted Groundwater, Bingham Canyon ...€¦ · Picture of NSB. Management...
Transcript of Management of Mining- Impacted Groundwater, Bingham Canyon ...€¦ · Picture of NSB. Management...
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Management of Mining- Impacted Groundwater, Bingham Canyon Mine, Utah, USA
Kelly PaynePrincipal Advisor, Closure & RemediationKennecott Utah Copper LLC
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This Morning’s Discussion
• Nature of Problem
• Regulatory Framework
• Containment and Remediation
• Water Treatment
– Acidic Water
– Neutral Water
• Cleanup Timeframe
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Acknowledgements
Technology & Innovation
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5 October 2009 Remediation of ARD-Contaminated Groundwater 4
Site Location
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Nature of Problem
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Source Controls
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Regulatory Framework
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Comprehensive Environmental Response, Compensation, and Liability Act (CERCLA)
• 1986 — EPA begins Preliminary Site Investigation
• 1994 — Site proposed for NPL listing
• 1995 — MOU between EPA, State of Utah, and KUC
• 1998 — RI/FS completed
• 2000 — ROD issued
• 2002 — RDRA completed
• 2008 — Consent Decree entered
• 2008 — NPL proposal withdrawn
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Natural Resource Damage
• 1986 — State of Utah files Natural Resources Damage (NRD) claim
• 1992 — Initial settlement rejected, Jordan Valley Water Conservancy District (JVCWD) intervenes
• 1995 — NRD settlement approved, KUC provides $37M to “restore, replace, or acquire equivalent”
• 2004 — State approves a joint Kennecott/JVWCD project
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Remedies
• EPA through CERCLA authority for Zone A:
– Maintain source controls
– Contain the plume through pumping
– Remediate the aquifer through pumping and monitored natural attenuation
– Treat extracted groundwater and dispose of treatment residuals
• UDEQ through Natural Resources Damage claim settlement:
– KUCC to construct and operate a RO treatment plant
– KUCC to fund construction of a second RO plant to be owned and operated by local water district
– Each plant to produce 3,500 ac-ft per year for 40 years
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Containment and Remediation
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Acidic Groundwater Well
Sulfate Groundwater Well
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Acidic Groundwater Wells
ECG1146 BSG1201 BSG2784
Installed 1995 2003 2008
Material Stainless Steel Stainless Steel Stainless Steel
Diameter 18-inch 18-inch 18-inch
Total Depth 760 ft bgs 752 ft bgs 870 ft bgs
Screen Intervals 500-700 ft bgs 500-740 ft bgs 490-600 ft bgs700-850 ft bgs
Static Water Level 380 ft bgs 450 ft bgs 410ft bgs
Pumping System 250 HP SS Submersible
200 HP SS Submersible
200 HP SS Submersible
Average Pumping Rate
850 gpm 600 gpm 600 gpm
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Sulfate Groundwater Wells
BFG1200 B2G1193 LTG1147
Installed 2001 1998 1995
Material Stainless Steel Stainless Steel Carbon/Stainless
Diameter 18-inch 18-inch 16-inch
Total Depth 820 ft bgs 1070 ft bgs 605 ft bgs
Screen Intervals 420-800 ft bgs 450-1060 ft bgs 400-590 ft bgs
Static Water Level 420 ft bgs 450 ft bgs 420 ft bgs
Pumping System 350 HP SS Sumbersible
350 HP Booster
350 HP SS Sumbersible
350 HP Booster
200 HP SS Sumbersible
250 HP Booster
Average Pumping Rate
1400 gpm 1400 gpm 600 gpm
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0
600
1200
1800
2400
3000
BSG27 84 1 7 06
BSG1201 551 1282 1292 1300 869 927
ECG1146 7 1 223 337 464 6 496 1022 954 1115 1527 1495 1419 947
T otal 7 1 223 337 464 6 496 1022 1505 2397 2819 27 96 2289 2,580
96 97 98 99 00 01 02 03 04 05 06 07 08
Acidic Water Extraction
Acr
e-F
ee
t p
er
Ye
ar
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1996 1997 1998 1999 2000 2001 2002 2003 2004 2005 2006 2007 2008
Sulfa
te (m
g/l)
0
5000
10000
15000
20000
25000
30000
35000
40000
45000
50000
ECG1124A ECG1124B ECG1124C ECG1146 DTW ECG1124B
Screened Intervals and D
epth to Water (feet below
ground surface)
0
100
200
300
400
500
600
700
800
900
1000
1100
1200
A
B
C
E
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Water Treatment
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Zone A Pump and Treat Strategy
BARRIERWELLS
(~3,300 gpm)
ACID WELLS
(~2,300 gpm)
REVERSE OSMOSISTREATMENT PLANT
HIGH-DENSITY SLUDGELIME TREATMENT
PLANT
TAILINGS LINE
CONCENTRATE
DRINKING WATER(2,400 GPM)
RECYCLE / DISCHARGE
JORDAN VALLEY WATERCONSERVANCY
SOLIDS
AQUEOUS
TAILINGS IMPOUNDMENT
RECYCLE / DISCHARGE
SOLIDS
AQUEOUS
REPOSITORY
DISCHARGEPost mine
closure
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Reverse Osmosis Treatment Plant
Configuration Two 2-stage skids
Feed Rate 3000 gpm to membranes
200 gpm to remineralization
3200 gpm total
Membranes Hydranautics ESPA2
(sprial wound polyamide)
Pressure Vessels Protec and CodeLine
Recovery Rate 71 to 74%
Production 2200 gpm permeate
2400 gpm product
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Zone A Treatment Plant Water Delivery
0
1,000
2,000
3,000
4,000
Annual 3,843 3,299 3,536
Rolling Avg 3,843 3,571 3,559
YE 5/31/07 YE 5/31/08 YE 5/31/09
Acr
e-F
ee
t p
er
Ye
ar
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Picture of RO Scaling
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Picture of dumps/reservoir
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Picture NP5
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Aerial of Tailings System
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Picture of NSB
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Management Criteria
• The neutralization potential (NP) value of samples collected from the tailings North Splitter Box should be either greater than or equal to the NP of Copperton Mill Tailings for the month or at least 5 t CaCO3 eq/kt, using a six-month rolling average.
• Aqueous alkalinity should be greater than or equal to 10 mg CaCO3 eq/L at least 90% of the time. Aqueous alkalinity will be evaluated as a rolling six-month average.
• The aqueous pH at the North Splitter Box should be greater than or equal to 6.7 during at least 90% of the time over a calendar year.
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Tailings Neutralization Potential (t CaCO3/kt)
Monthly 6-Month Average
Date GMT NSB GMT NSB
Jan-08 15 14 25 23
Feb-08 151 147 46 41
Mar-08 31 22 47 40
Apr-08 11 15 44 38
May-08 21 24 46 40
Jun-08 23 21 42 41
Jul-08 149 153 64 64
Aug-08 20 14 43 42
Sep-08 26 30 42 43
Oct-08 104 107 57 58
Nov-08 21 24 57 58
Dec-08 11 15 55 57
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Tailings Aqueous Alkalinity (mg CaCO3/l)
Monthly 6-Month Average
Date GMT NSB GMT NSB
Jan-08 23 47 34 57
Feb-08 17 11 30 45
Mar-08 175 103 54 50
Apr-08 51 34 55 43
May-08 59 98 60 59
Jun-08 29 27 59 53
Jul-08 11 <5 57 55
Aug-08 57 82 64 69
Sep-08 26 84 39 65
Oct-08 27 36 35 65
Nov-08 22 15 29 49
Dec-08 20 76 27 59
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Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec Jan
Tons
Per
Hou
r or G
allo
ns P
er M
inut
e
0
1000
2000
3000
4000
5000
6000
7000
8000
9000
pH
6
7
8
9
10
11
Concentrator Throughput (TPH)Acidic Water Pumping (GPM)Tailings pH at North Splitter Box
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Picture of Scaling
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Cleanup Timeframe
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Column Leaching Study
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Geochemical Models
• Extrapolation based on interpretation of earlier column data
• Extrapolation using data from individual wells that have undergone complete recovery
• Expanded 1D geochemical model
• Empirical rinse curve model
• Extended 1D advection-dispersion model with mass extraction
Acidity comprised mostly of mineral acidity in the form of elevated Al and Fe concentrations
Concentration of acidity estimated for water extracted from the two extraction wells, ECG1146 and BSG1201
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Calculated lime demand
2000 2005 2010 2015 2020 2025 20300
1
2
3
4
5
6
Lim
e de
man
d (t/
ML)
Year
Rinse curve model Extrapolated well data model Advection-dispersion-extraction model Geochemical model (clean) Geochemical model (transition) Upper 95% confidence limit of all models