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Co-Conspirators: S. Busler, T. Danehy,
M. Dunn, D. Guy, R.Mahony, C. Neely
Presenter: Cliff Denholm
 <300 publicly funded PTS in PA1
 >77 billion gal/yr of AMD treated in PA alone1
 >16 Million Pounds of Iron removed/year
 >3 Million Pounds of Aluminum removed/year
1www.datashed.org
 We all know that Passive Systems Don’t Work
 Passive Systems require too much maintenance
 Vertical Flow Ponds Don’t Work
 You can’t passively treat High Aluminum AMD
 You can’t passively treat High Iron AMD
 Active Treatment is the only answer
 Watershed Groups are failing
 Watershed Groups are not maintaining systems
 Treatment Technology ~30 years old
◦ Developed over time
◦ Still developing
 Mistakes had to be made to learn
 Early excitement & funding availability allowed for
experimentation
◦ Sometimes it worked, Sometimes it didn’t
 Do something or do nothing
Yes and No
Point
Flow
(GPM) pH
Alk
mg/L
Acid
mg/L
T. Fe
mg/L
T. Al
mg/L
T. Mn
mg/L
SO4
mg/L
In 34 2.9 0 258 22 19 6 516
Out NA 3.3 0 154 15 14 6 519
Point
Flow
(GPM) pH
Alk
mg/L
Acid
mg/L
T. Fe
mg/L
T. Al
mg/L
T. Mn
mg/L
SO4
mg/L
In NA 3.3 0 NA 81 21 9 691
Out 24 6.3 177 NA 62 <1 9 680
Point
Flow
(GPM) pH
Alk
mg/L
Acid
mg/L
T. Fe
mg/L
T. Al
mg/L
T. Mn
mg/L
SO4
mg/L
Raw 20 3.0 NA 261 34 14 14 693
WL4 33 6.5 48 -2 <1 <1 6 642
 VFPs  Chemical
Plants
 Refuse
Removal &
CFB Plants
 Land
Reclamation
 Aquafix
 Coal Ash
 ALDs
 Wetlands
 Lime
dosers TIFs
 HFLBs
Why Do Passive Systems “Fail”?
•Design - undersized, wrong application/developing technology, etc.
•Construction - sloppiness, short-cuts, accidental errors
•Site conditions - not enough room, something vs. nothing
•Unanticipated issues - water quality or quantity changes
•Design life met and/or treatment media spent
•Lack of O&M
Passive Treatment
Systems
Are
LOW Maintenance
Not
NO Maintenance
Flow pH Acid Alk Fe Mn Al
Raw 36 4.1 319 NA 82 55 12
Constructed 1999 (16 Years Old)
Cost $391,000
Upgrades Cost ~$10,000
O&M Costs ~$8,000
Volunteer = $?
O&M Annualized ~$500
Flow pH Acid Alk Fe Mn Al
Raw 36 4.1 319 NA 82 55 12
Treated 44 6.6 -2 81 1 31 <1
Flow pH Acid Alk Fe Mn Al
Raw 36 4.1 319 NA 82 55 12
Forbay N 10 3.3 201 NA 20 40 11
Forbay S 21 3.4 228 NA 48 42 10
Upgrades
◦ Installed Forebay
◦ Replaced VFP Outlet Pipes to adjustable peri-pipes
◦ Inlet & Outlet pools in HFLB
O&M
 Flushing/Backflushing
 Cleaning out low pH iron from pipes
 Removed low pH iron from top of VFPs
 Stirred top layer of VFP treatment media
 Stir HFLB
Remaining O&M Needs
◦ Stir HFLB
162-
2162-8
162-
3
CC
1
162-6
& 162-
10
OPC
Moa
t
VFP
1
SB1
AL
D
CC
1
CC
1
CC
1
162-6
& 162-
10
CC
1
SB1
162-6
& 162-
10
CC
1
Moa
t
SB1
162-6
& 162-
10
CC
1
VFP
1
Moa
t
SB1
162-6
& 162-
10
CC
1
VFP
1
Moa
t
SB1
162-6
& 162-
10
CC
1
OPC
VFP
1
Moa
t
SB1
162-6
& 162-
10
CC
1
AL
D
OPC
VFP
1
Moa
t
SB1
162-6
& 162-
10
CC
1
AL
D
OPC
VFP
1
Moa
t
SB1
162-6
& 162-
10
CC
1
162-8
AL
D
OPC
VFP
1
Moa
t
SB1
162-6
& 162-
10
CC
1
162-
2162-8
AL
D
OPC
Moa
t
SB1
162-6
& 162-
10
CC
1
162-
3
162-
2162-8
AL
D
OPC
Moa
t
SB1
162-6
& 162-
10
CC
1
Forebay
162-3162-2
162-8
ALD
OPC
VFP1
Moat SB1
162-6 &
162-10
CC1
Aka TIFs
HFLB
SP/WL
VFP2B
OPC3
SB1
Flow
GPM pH
Alk
mg/L
Acid
mg/L
T. Fe
mg/L
T. Al
mg/L
T. Mn
mg/L
SO4
mg/L
5-10 2.67 0 1385 304 142 20 2620
Flow
GPM pH
Alk
mg/L
Acid
mg/L
T. Fe
mg/L
T. Al
mg/L
T. Mn
mg/L
SO4
mg/L
3.12 0 512 28 83 26 2130
Avg 80%
Fe Loading Removed
In ~600 Feet!!!
Winter Solstice
12/21/09
<0°C
pH ~3
pH
~ 5
pH
~~7
Flow
GPM pH
Alk
mg/L
Acid
mg/L
T. Fe
mg/L
T. Al
mg/L
T. Mn
mg/L
SO4
mg/L
46 7.51 214 -180 0.1 0.2 5.3 1097
Vegetation in Channels and Spillways
 Box outlet clogged
 Vegetation removed,
outlet depth increased
 2008-Site constructed
Hydraulic issues noted
Flow pH Acid Alk Fe Mn Al
Raw 135 3.2 257 NA 26 55 10
Treated 135 6.3 0 74 <1 25 <1
Source: www.datashed.org
 2000-Site constructed
 2012- decreased
treatment performance
noted
 VFP East Stir
 Forebay inlet and
outlet cleaned
 WL outlet cleared of
vegetation
 HFLB stone re-leveled
 VFP outlet spillway
cleared of vegetation
buildup
 Multiple issues noted
during site visit by SRWC
 Forebay pipe inlet clogged
 VFP performance
decreased
Pre- and Post- O&M Effluent
Field Water Quality Data
Parameter Pre-
O&M
Post-
O&M
pH 6.0 6.9
alkalinity 20 ~70
Fe (mg/l) 4-8 0.5 - 1
Total metals mg/L, acidity and
alkalinity as CaCO3 mg/L
Flow pH Acid Alk Fe Mn Al
Forebay 12 3.1 509 NA 107 107 29
Treated 13 6.9 30 64 <1 53 <1
Source: www.datashed.org
 Replace baffle curtains
 Removed Fe off of VFP & stirred VFP
 Backflushed & Stirred HFLB
 Fixed access road entry
 Assist PA watershed groups, non-profits,
conservation districts, etc.
 2011-Current (multiple grants)
 Technical assistance & water sampling
 Funding Sources
◦ PA DEP Growing Greener Program
◦ Foundation for PA Watersheds
◦ In-kind/match watershed groups
Construction Cost = $200,000
Annual O&M = 1%
Need = ~$40,000 to invest
Replacement Cost every 20 Years
Need = ~$60,000 to invest
If provide an extra $100,000 at time of grant
to the watershed group, they could maintain
treatment for “perpetuity”
 High Risk (High Metal) AMD can be
passively treated IF
◦ Good Design
◦ Sufficient Site Conditions
 Area
 Elevation Change
◦ Proper Construction
◦ Maintained
Require Sufficient Funding At All Stages:
◦ Design
◦ Construction
◦ Monitoring
◦ Maintenance
Watershed Groups Can and Should be part of the
long-term plan to maintain treatment systems as
they can do it cheaper but they need:
◦ Support
◦ Funding
 Lab Samples
 Field Equipment
 Travel Expenses
◦ Maintenance
◦ Technical Assistance like SRI’s O&M TAG
 Passive treatment is not maintenance free;
 Like a car, regular inspections and occasional
maintenance are needed for a treatment system
to reach it’s design life;
 Poor water quality does not always mean the system
is a failure or has reached its design life;
 Treatment performance can often be restored
through maintenance activities that rejuvenate the
system instead of replacing the treatment media or
rebuilding the system and thus saving money;
 Most sites require
maintenance over time
 Regular site visits and
observations allow
many problems to be
addressed quickly and
efficiently
 PA PTS Snapshot
 Passive is the only answer
 All of our systems work 100%, 100% of the
time
 Passive systems don’t require maintenance
 All watershed groups are fine
 Slippery Rock Watershed Coalition 1994
 Stream Restoration Incorporated 1996
 BioMost, Inc 1998
 Designed over 60 Passive Treatment Systems
 Designed/modified a handful of Active Systems
 Maintained/repaired numerous systems
 Inspected & evaluated >100 systems
 Managed Statewide AMD Treatment Snapshots
in 2009, 2010, 2012, 2015
 Created & Manage Datashed (www.datashed.org)
BEFORE
Flow
GPM pH
Alk
mg/L
Acid
mg/L
T. Fe
mg/L
T. Al
mg/L
T. Mn
mg/L
SO4
mg/L
69 3.0 0 498 51 26 21 1340
AFTER
Flow
GPM pH
Alk
mg/L
Acid
mg/L
T. Fe
mg/L
T. Al
mg/L
T. Mn
mg/L
SO4
mg/L
319 6.0 22 12 4 4 13 830
 Don’t let the perfect get in the way of the
good
 Need to fund maintenance not just the design
& construction to ensure long-term treatment
Cliff  Denholm, Stream Restoration Incorporated,  "Passive Treatment of Acidic High-Metal Discharges Part 1"

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Cliff Denholm, Stream Restoration Incorporated, "Passive Treatment of Acidic High-Metal Discharges Part 1"

  • 1. Co-Conspirators: S. Busler, T. Danehy, M. Dunn, D. Guy, R.Mahony, C. Neely Presenter: Cliff Denholm
  • 2.  <300 publicly funded PTS in PA1  >77 billion gal/yr of AMD treated in PA alone1  >16 Million Pounds of Iron removed/year  >3 Million Pounds of Aluminum removed/year 1www.datashed.org
  • 3.
  • 4.  We all know that Passive Systems Don’t Work  Passive Systems require too much maintenance  Vertical Flow Ponds Don’t Work  You can’t passively treat High Aluminum AMD  You can’t passively treat High Iron AMD  Active Treatment is the only answer  Watershed Groups are failing  Watershed Groups are not maintaining systems
  • 5.
  • 6.
  • 7.  Treatment Technology ~30 years old ◦ Developed over time ◦ Still developing  Mistakes had to be made to learn  Early excitement & funding availability allowed for experimentation ◦ Sometimes it worked, Sometimes it didn’t  Do something or do nothing Yes and No
  • 8.
  • 9.
  • 10. Point Flow (GPM) pH Alk mg/L Acid mg/L T. Fe mg/L T. Al mg/L T. Mn mg/L SO4 mg/L In 34 2.9 0 258 22 19 6 516 Out NA 3.3 0 154 15 14 6 519
  • 11. Point Flow (GPM) pH Alk mg/L Acid mg/L T. Fe mg/L T. Al mg/L T. Mn mg/L SO4 mg/L In NA 3.3 0 NA 81 21 9 691 Out 24 6.3 177 NA 62 <1 9 680
  • 12. Point Flow (GPM) pH Alk mg/L Acid mg/L T. Fe mg/L T. Al mg/L T. Mn mg/L SO4 mg/L Raw 20 3.0 NA 261 34 14 14 693 WL4 33 6.5 48 -2 <1 <1 6 642
  • 13.
  • 14.  VFPs  Chemical Plants  Refuse Removal & CFB Plants  Land Reclamation  Aquafix  Coal Ash  ALDs  Wetlands  Lime dosers TIFs  HFLBs
  • 15. Why Do Passive Systems “Fail”? •Design - undersized, wrong application/developing technology, etc. •Construction - sloppiness, short-cuts, accidental errors •Site conditions - not enough room, something vs. nothing •Unanticipated issues - water quality or quantity changes •Design life met and/or treatment media spent •Lack of O&M
  • 17.
  • 18. Flow pH Acid Alk Fe Mn Al Raw 36 4.1 319 NA 82 55 12
  • 19.
  • 20. Constructed 1999 (16 Years Old) Cost $391,000 Upgrades Cost ~$10,000 O&M Costs ~$8,000 Volunteer = $? O&M Annualized ~$500 Flow pH Acid Alk Fe Mn Al Raw 36 4.1 319 NA 82 55 12 Treated 44 6.6 -2 81 1 31 <1
  • 21. Flow pH Acid Alk Fe Mn Al Raw 36 4.1 319 NA 82 55 12 Forbay N 10 3.3 201 NA 20 40 11 Forbay S 21 3.4 228 NA 48 42 10
  • 22.
  • 23. Upgrades ◦ Installed Forebay ◦ Replaced VFP Outlet Pipes to adjustable peri-pipes ◦ Inlet & Outlet pools in HFLB O&M  Flushing/Backflushing  Cleaning out low pH iron from pipes  Removed low pH iron from top of VFPs  Stirred top layer of VFP treatment media  Stir HFLB Remaining O&M Needs ◦ Stir HFLB
  • 24.
  • 25.
  • 26. 162- 2162-8 162- 3 CC 1 162-6 & 162- 10 OPC Moa t VFP 1 SB1 AL D CC 1 CC 1 CC 1 162-6 & 162- 10 CC 1 SB1 162-6 & 162- 10 CC 1 Moa t SB1 162-6 & 162- 10 CC 1 VFP 1 Moa t SB1 162-6 & 162- 10 CC 1 VFP 1 Moa t SB1 162-6 & 162- 10 CC 1 OPC VFP 1 Moa t SB1 162-6 & 162- 10 CC 1 AL D OPC VFP 1 Moa t SB1 162-6 & 162- 10 CC 1 AL D OPC VFP 1 Moa t SB1 162-6 & 162- 10 CC 1 162-8 AL D OPC VFP 1 Moa t SB1 162-6 & 162- 10 CC 1 162- 2162-8 AL D OPC Moa t SB1 162-6 & 162- 10 CC 1 162- 3 162- 2162-8 AL D OPC Moa t SB1 162-6 & 162- 10 CC 1 Forebay 162-3162-2 162-8 ALD OPC VFP1 Moat SB1 162-6 & 162-10 CC1 Aka TIFs
  • 28. Flow GPM pH Alk mg/L Acid mg/L T. Fe mg/L T. Al mg/L T. Mn mg/L SO4 mg/L 5-10 2.67 0 1385 304 142 20 2620
  • 29.
  • 30. Flow GPM pH Alk mg/L Acid mg/L T. Fe mg/L T. Al mg/L T. Mn mg/L SO4 mg/L 3.12 0 512 28 83 26 2130 Avg 80% Fe Loading Removed In ~600 Feet!!!
  • 32.
  • 34.
  • 35.
  • 36.
  • 37.
  • 38. Flow GPM pH Alk mg/L Acid mg/L T. Fe mg/L T. Al mg/L T. Mn mg/L SO4 mg/L 46 7.51 214 -180 0.1 0.2 5.3 1097
  • 39. Vegetation in Channels and Spillways
  • 40.  Box outlet clogged  Vegetation removed, outlet depth increased
  • 41.
  • 42.
  • 44.
  • 45. Flow pH Acid Alk Fe Mn Al Raw 135 3.2 257 NA 26 55 10 Treated 135 6.3 0 74 <1 25 <1 Source: www.datashed.org
  • 46.
  • 47.  2000-Site constructed  2012- decreased treatment performance noted  VFP East Stir  Forebay inlet and outlet cleaned
  • 48.  WL outlet cleared of vegetation  HFLB stone re-leveled  VFP outlet spillway cleared of vegetation buildup
  • 49.  Multiple issues noted during site visit by SRWC  Forebay pipe inlet clogged  VFP performance decreased
  • 50.
  • 51.
  • 52.
  • 53. Pre- and Post- O&M Effluent Field Water Quality Data Parameter Pre- O&M Post- O&M pH 6.0 6.9 alkalinity 20 ~70 Fe (mg/l) 4-8 0.5 - 1 Total metals mg/L, acidity and alkalinity as CaCO3 mg/L
  • 54. Flow pH Acid Alk Fe Mn Al Forebay 12 3.1 509 NA 107 107 29 Treated 13 6.9 30 64 <1 53 <1 Source: www.datashed.org
  • 55.
  • 56.
  • 57.
  • 58.
  • 59.  Replace baffle curtains  Removed Fe off of VFP & stirred VFP  Backflushed & Stirred HFLB  Fixed access road entry
  • 60.  Assist PA watershed groups, non-profits, conservation districts, etc.  2011-Current (multiple grants)  Technical assistance & water sampling  Funding Sources ◦ PA DEP Growing Greener Program ◦ Foundation for PA Watersheds ◦ In-kind/match watershed groups
  • 61. Construction Cost = $200,000 Annual O&M = 1% Need = ~$40,000 to invest Replacement Cost every 20 Years Need = ~$60,000 to invest If provide an extra $100,000 at time of grant to the watershed group, they could maintain treatment for “perpetuity”
  • 62.  High Risk (High Metal) AMD can be passively treated IF ◦ Good Design ◦ Sufficient Site Conditions  Area  Elevation Change ◦ Proper Construction ◦ Maintained
  • 63. Require Sufficient Funding At All Stages: ◦ Design ◦ Construction ◦ Monitoring ◦ Maintenance
  • 64. Watershed Groups Can and Should be part of the long-term plan to maintain treatment systems as they can do it cheaper but they need: ◦ Support ◦ Funding  Lab Samples  Field Equipment  Travel Expenses ◦ Maintenance ◦ Technical Assistance like SRI’s O&M TAG
  • 65.  Passive treatment is not maintenance free;  Like a car, regular inspections and occasional maintenance are needed for a treatment system to reach it’s design life;
  • 66.  Poor water quality does not always mean the system is a failure or has reached its design life;  Treatment performance can often be restored through maintenance activities that rejuvenate the system instead of replacing the treatment media or rebuilding the system and thus saving money;
  • 67.
  • 68.
  • 69.
  • 70.  Most sites require maintenance over time  Regular site visits and observations allow many problems to be addressed quickly and efficiently  PA PTS Snapshot
  • 71.  Passive is the only answer  All of our systems work 100%, 100% of the time  Passive systems don’t require maintenance  All watershed groups are fine
  • 72.  Slippery Rock Watershed Coalition 1994  Stream Restoration Incorporated 1996  BioMost, Inc 1998  Designed over 60 Passive Treatment Systems  Designed/modified a handful of Active Systems  Maintained/repaired numerous systems  Inspected & evaluated >100 systems  Managed Statewide AMD Treatment Snapshots in 2009, 2010, 2012, 2015  Created & Manage Datashed (www.datashed.org)
  • 73. BEFORE Flow GPM pH Alk mg/L Acid mg/L T. Fe mg/L T. Al mg/L T. Mn mg/L SO4 mg/L 69 3.0 0 498 51 26 21 1340 AFTER Flow GPM pH Alk mg/L Acid mg/L T. Fe mg/L T. Al mg/L T. Mn mg/L SO4 mg/L 319 6.0 22 12 4 4 13 830
  • 74.  Don’t let the perfect get in the way of the good
  • 75.  Need to fund maintenance not just the design & construction to ensure long-term treatment