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Bioremediation
Presentation Authors
Caren Caldwell
Leslie Thompson
Pintail Systems, Inc. was founded in 1987 by
Leslie Thompson
Primary focus was on cyanide detoxification in
gold and silver heap leach pads using native
bacteria cultures.
Bioremediation is not new. Traditionally, nutrients
are added to the contamination site and everyone
hopes for the best. This is very slow if it works at all.
What Makes PSI’s bioremediation process
successful where others fail?
WE OPTIMIZE THE PROCESS
PSI’s Bio-Augmentation Process Traditional Bio-Stimulation
Active Process Passive Process
Use bacteria cultures isolated from the
contaminated site.
Assume that there are effective bacteria
colonies at the site
Isolated cultures are tested for treatment
efficiency in the lab before application at the
site. Nutrients are also optimized for culture
growth.
Nutrients are added to the site and the
assumption is that those nutrients will
stimulate the growth of effective bacteria
cultures.
Effective cultures are grown to high
concentrations using optimized nutrient
formulations and applied to the
contaminated site.
Added nutrients stimulate growth of both
potentially effective bacteria colonies as
well as ineffective colonies. That causes
competition for nutrients and limits the
growth of effective colonies.
New cultures are added to the site on a
regular basis improving treatment
efficiency.
Fast and highly efficient Slow if it works at all
38.4 40.3 32.4 38.4
24
38.4
0.11
0.08
0.01
0.1
1
10
100
0.1 0.3 0.5 0.6 0.7
MG/LTotalCyanide
Tons of Solution per Ton of Ore
Nutrient Stimulation PSI's BioAugmentation
In microbial detoxification of
heap leach pads, cultures can
be applied directly to the heap
in the same way cyanide was
added during production.
The cultures are set up in a
staged culturing system
located at the site
Staged culturing system
inside the “Bug Ranch” at the
Yellow Pine Mine
Cultures are monitored on a
regular basis for culture health
and effectiveness. Adjustments
are made as necessary.
0
5
10
15
20
25
30
35
40
45
50
1
29
25
50
59
71
85
94
107
114
121
128
136
146
155
WADCyanide
Time, Days
Heap Bio-Detox
WAD Cyanide in Heap Effluent Solutions
1.3 million ton heap detox at the
Yellow Pine Mine. WAD cyanide
Located in Idaho with Alpine
Conditions. Environmentally
sensitive area.
1.2 million ton heap detox at
Cyprus Copperstone. WAD
cyanide and total cyanide.
Located in the Arizona desert.
Treatment
Type
Ionic
Cyanide
WAD
Cyanide
Ferro
Cyanide
Thiocyanate
Alkaline
Chlorination
Yes Partial No Partial
Peroxide Yes Yes Partial No
Ion Exchange No Yes Yes Possible
Natural
Degradation
Yes Partial No No
PSI Bio-
Processes
Yes Yes Yes Yes
Sulfur
Dioxide
Yes Yes Partial No
Ref. Cyanide From Mineral Processing
J.L. Huiatt, ET AL. Editors
Volunteer revegetation on the Ortiz
waste rock dump after bio-treatment
Desert climate
Volunteer revegetation on the sides of the
Yellow Pine Mine after bio-treatment.
Alpine climate.
Bugs the Ultimate Solution
Bioremediation in Mining: Remediation
0.622
0.398
0.105
0.488
0.005
0.247
0.046 0.054
0
0.2
0.4
0.6
0.8
Cadmium Chromium Selenium Silver
MG/L
Before Treatment
After Treatment
0.978
2.07
0.186
0.005
0
0.5
1
1.5
2
2.5
Iron Mercury
MG/L
9.15
4.16
0.334 0.007
0
5
10
Copper Zinc
MG/L
Reduction of metals in heap leachate solution in a 2.5 million ton heap before and after
Bio-treatment.
0.35
0.12 0.18
0.0003
0.059 0.07
0
0.1
0.2
0.3
0.4
Mercury Arsenic Copper
MG/L
Before Treatment
After Treatment
0.94
2.44
0.7
0.38
0.01 0.12
0
0.5
1
1.5
2
2.5
3
Zinc Silver Selenium
MG/L
Reduction in metals in heap leachate solution from a 140,000 ton heap near Gabbs, Nevada
In analytical work done by Dr. Jeffrey Steiner at City College of New York, it was
found that bacteria cultures catalyze the formation of minerals in Bio-treated
heaps or process solutions. Mineral formation “locks up” leachable metals. Dr.
Steiner’s work was done on Bio-treated ore from the Summitville Mine. This
explains the reduction in leachable metal from heaps treated with PSI’s Bio-
Processes.
23
6.31.27 0.3
0
10
20
30
Nitrate Flouride
MG/L
100,000 ton heap located in South Dakota. Leachate solution before and after Bio-treatment
420
120
2.5 0.52
0
100
200
300
400
500
Arsenic Copper
MG/L
17.9
14.6
3.740.11 0.05
0.01
0
5
10
15
20
Total Cyanide WAD Cyanide Mercury
MG/L
Before Treatment
After Treatment
1800 TON PILOT HEAP
CYANIDE IN HEAP LEACHATE SOLUTIONS
Total CN WAD CN
time, days
0
7
14
21
28
35
41
53
63
74
84
95
105
116
127
137
0.01
0.1
1
10
100
1000
1800 Ton Test Heap
Nitrates vs Time
nitrate
time, days
0
7
14
21
28
35
41
53
63
74
84
95
105
116
127
0
20
40
60
80
100
120
140
1800 Ton Test Heap
Copper in Leachate Solutions
copper
time, days
0
7
14
21
28
35
41
53
63
74
84
95
105
116
127
137
0
0.5
1
1.5
2
2.5
3
3.5
4
4.5
5
The McCoy Cove Mine was used as an EPA/MWTPP test site to demonstrate the
removal of cyanide and leachable metals from mine water using a filtration system with
immobilized bacteria.
Pintail
332
179
255
882
46.8 5.1
84.9
15.4
0
200
400
600
800
1000
Arsenic Mercury Selenium Silver
UG/L
Untreated Influent
Treated Effluent
233
25
0
100
200
300
WAD Cyanide
MG/L
Simultaneous Denitrification and Cyanide Detoxification of process solution in a bio-reactor
246 254
33
0
50
100
150
200
250
300
WAD Cyanide
MG/LWADCyanide
Influent Preg Solution Untreated Preg Control
Treated Preg Solution
30.4 30.5
1.63
0
5
10
15
20
25
30
35
Nitrate
MG/LNitrate
All of the data in this presentation is the result of using
bacteria native to the contaminated site. By using native
bacteria adapted to the conditions at the site, we have been
able to conduct successful bioremediation projects located in a
wide variety climates, from alpine to desert.
We have also been able to remediate a wide range of
contaminants with one treatment, saving time and money.

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  • 3. Pintail Systems, Inc. was founded in 1987 by Leslie Thompson Primary focus was on cyanide detoxification in gold and silver heap leach pads using native bacteria cultures.
  • 4. Bioremediation is not new. Traditionally, nutrients are added to the contamination site and everyone hopes for the best. This is very slow if it works at all. What Makes PSI’s bioremediation process successful where others fail? WE OPTIMIZE THE PROCESS
  • 5. PSI’s Bio-Augmentation Process Traditional Bio-Stimulation Active Process Passive Process Use bacteria cultures isolated from the contaminated site. Assume that there are effective bacteria colonies at the site Isolated cultures are tested for treatment efficiency in the lab before application at the site. Nutrients are also optimized for culture growth. Nutrients are added to the site and the assumption is that those nutrients will stimulate the growth of effective bacteria cultures. Effective cultures are grown to high concentrations using optimized nutrient formulations and applied to the contaminated site. Added nutrients stimulate growth of both potentially effective bacteria colonies as well as ineffective colonies. That causes competition for nutrients and limits the growth of effective colonies. New cultures are added to the site on a regular basis improving treatment efficiency. Fast and highly efficient Slow if it works at all
  • 6. 38.4 40.3 32.4 38.4 24 38.4 0.11 0.08 0.01 0.1 1 10 100 0.1 0.3 0.5 0.6 0.7 MG/LTotalCyanide Tons of Solution per Ton of Ore Nutrient Stimulation PSI's BioAugmentation
  • 7. In microbial detoxification of heap leach pads, cultures can be applied directly to the heap in the same way cyanide was added during production. The cultures are set up in a staged culturing system located at the site
  • 8. Staged culturing system inside the “Bug Ranch” at the Yellow Pine Mine Cultures are monitored on a regular basis for culture health and effectiveness. Adjustments are made as necessary.
  • 9. 0 5 10 15 20 25 30 35 40 45 50 1 29 25 50 59 71 85 94 107 114 121 128 136 146 155 WADCyanide Time, Days Heap Bio-Detox WAD Cyanide in Heap Effluent Solutions 1.3 million ton heap detox at the Yellow Pine Mine. WAD cyanide Located in Idaho with Alpine Conditions. Environmentally sensitive area. 1.2 million ton heap detox at Cyprus Copperstone. WAD cyanide and total cyanide. Located in the Arizona desert.
  • 10. Treatment Type Ionic Cyanide WAD Cyanide Ferro Cyanide Thiocyanate Alkaline Chlorination Yes Partial No Partial Peroxide Yes Yes Partial No Ion Exchange No Yes Yes Possible Natural Degradation Yes Partial No No PSI Bio- Processes Yes Yes Yes Yes Sulfur Dioxide Yes Yes Partial No Ref. Cyanide From Mineral Processing J.L. Huiatt, ET AL. Editors
  • 11. Volunteer revegetation on the Ortiz waste rock dump after bio-treatment Desert climate Volunteer revegetation on the sides of the Yellow Pine Mine after bio-treatment. Alpine climate. Bugs the Ultimate Solution Bioremediation in Mining: Remediation
  • 12. 0.622 0.398 0.105 0.488 0.005 0.247 0.046 0.054 0 0.2 0.4 0.6 0.8 Cadmium Chromium Selenium Silver MG/L Before Treatment After Treatment 0.978 2.07 0.186 0.005 0 0.5 1 1.5 2 2.5 Iron Mercury MG/L 9.15 4.16 0.334 0.007 0 5 10 Copper Zinc MG/L Reduction of metals in heap leachate solution in a 2.5 million ton heap before and after Bio-treatment.
  • 13. 0.35 0.12 0.18 0.0003 0.059 0.07 0 0.1 0.2 0.3 0.4 Mercury Arsenic Copper MG/L Before Treatment After Treatment 0.94 2.44 0.7 0.38 0.01 0.12 0 0.5 1 1.5 2 2.5 3 Zinc Silver Selenium MG/L Reduction in metals in heap leachate solution from a 140,000 ton heap near Gabbs, Nevada
  • 14. In analytical work done by Dr. Jeffrey Steiner at City College of New York, it was found that bacteria cultures catalyze the formation of minerals in Bio-treated heaps or process solutions. Mineral formation “locks up” leachable metals. Dr. Steiner’s work was done on Bio-treated ore from the Summitville Mine. This explains the reduction in leachable metal from heaps treated with PSI’s Bio- Processes.
  • 15. 23 6.31.27 0.3 0 10 20 30 Nitrate Flouride MG/L 100,000 ton heap located in South Dakota. Leachate solution before and after Bio-treatment 420 120 2.5 0.52 0 100 200 300 400 500 Arsenic Copper MG/L 17.9 14.6 3.740.11 0.05 0.01 0 5 10 15 20 Total Cyanide WAD Cyanide Mercury MG/L Before Treatment After Treatment
  • 16. 1800 TON PILOT HEAP CYANIDE IN HEAP LEACHATE SOLUTIONS Total CN WAD CN time, days 0 7 14 21 28 35 41 53 63 74 84 95 105 116 127 137 0.01 0.1 1 10 100 1000 1800 Ton Test Heap Nitrates vs Time nitrate time, days 0 7 14 21 28 35 41 53 63 74 84 95 105 116 127 0 20 40 60 80 100 120 140 1800 Ton Test Heap Copper in Leachate Solutions copper time, days 0 7 14 21 28 35 41 53 63 74 84 95 105 116 127 137 0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 5
  • 17. The McCoy Cove Mine was used as an EPA/MWTPP test site to demonstrate the removal of cyanide and leachable metals from mine water using a filtration system with immobilized bacteria.
  • 19. 332 179 255 882 46.8 5.1 84.9 15.4 0 200 400 600 800 1000 Arsenic Mercury Selenium Silver UG/L Untreated Influent Treated Effluent 233 25 0 100 200 300 WAD Cyanide MG/L
  • 20. Simultaneous Denitrification and Cyanide Detoxification of process solution in a bio-reactor 246 254 33 0 50 100 150 200 250 300 WAD Cyanide MG/LWADCyanide Influent Preg Solution Untreated Preg Control Treated Preg Solution 30.4 30.5 1.63 0 5 10 15 20 25 30 35 Nitrate MG/LNitrate
  • 21. All of the data in this presentation is the result of using bacteria native to the contaminated site. By using native bacteria adapted to the conditions at the site, we have been able to conduct successful bioremediation projects located in a wide variety climates, from alpine to desert. We have also been able to remediate a wide range of contaminants with one treatment, saving time and money.