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In-Situ Groundwater Nitrification and De-Nitrification Remediation Processes
Presented by Steve Mailath, EBA Engineering Consultants
Ltd.Phone: 403.723.6898
Problems with Ammonia and Nitrate
• Over fertilization (eutrophication) of surface waters with N
• Ammonia toxic to animal species – fish and invertebrates
• Nitrate contamination of drinking water– blue baby syndrome – methemoglobinemia
• Discounted value of brown-field development
Environmental and Regulatory Issues
• Environmental regulations are becoming more stringent with time– Environmental enforcement orders
• Growing public concern of environmental management
• Restricted land use
Where is the Problem – Who is responsible
• Fertilizer manufacturing and storage facilities– Brown-field developer
• Sewage treatment facilities– City of Calgary
• Agricultural areas– Farmers
• Airports– Calgary airport authority
Problems with Existing Solutions
• Expense– Treatment facilities– Piping– Operating
• Large footprint, need to close site
In-Situ Groundwater Nitrification andDe-Nitrification Remediation Processes
In-situ nitrification:• Extracting groundwater• Adding oxygen and nutrients• Injection of amended groundwater
In-situ de-nitrification• Extracting groundwater• Adding carbon and nutrients• Injection of amended groundwater
By: Steve Mailath, EBA Engineering Consultants Ltd.Patent Pending: David Reese, University Technologies International, Phone: 270.2434
Dr. Angus Chu, U of C, Phone: 220.8987Steve Mailath, EBA, Phone: 723.6898
Advantages
• Performs as well as best in class solutions at less than half the cost
• Full mass removal - nitrates reduced to N gas• Small footprint and less intrusive than most
solutions• Requires fewer wells and piping• Year round treatment• Free bio-reactor (in situ)
Options
Options Main Limitations Capital($ Million)
Operating
($/year)
Present Value Cost1
($ million)1. Groundwater Extraction and Irrigation Summer
treatment$0.85 $57,000 $1.4
2. Groundwater Extraction and Discharge to City Sanitary Sewer
Removal of ammonia only
$0.69 $50,000 $1.2
3. Groundwater Extraction and Electrochemical Treatment
High cost $3.1 $155,000 $4.7
4. Groundwater Extraction and Biological Treatment (Nitrification)
High cost $1.6 $100,000 $2.6
5. Groundwater Extraction and Wetlands Disposal
Summer treatment, low N
$0.64 $51,000 $1.2
6. In-Situ Electrochemical Treatment Low perm soils $2.8 >$35,000 >$3.0
7. On-Site Ex-Situ Biological Treatment High cost $5.0 to $7.0
>$35,000 >$5.0
8. In-Situ Nitrification and High perm soils $0.2 $30,000 $0.5
De-Nitrification $0.1 $25,600 $0.41 Present value based upon 15 year life and 5% rate of return.
Nitrate Plume
Ammonia Plume
Site Plot Plan
Cross-Section A-A’
Cross-Section D-D’
Typical Gravel
Hydraulic Parameters
• Section length 425 m (perpendicular to flow • Section thickness 3.0 m• Hydraulic conductivity 49 m/day• Hydraulic gradient 0.0023• Groundwater velocity 0.3 – 0.5 m/day• Groundwater flux 144 m3/day (22 igpm)• Ammonia concentration 63.2 mg-N/L• Nitrate concentration 94 mg-N/L (i.e., 31 mg-N/L
in-situ plus 63 mg-N/L generatedby nitrification)
In-Situ Nitrification
Pilot Test Site
Test Site
GROUNDWATER FLOW
Test Site
INJECTIONWELL
EXTRACTION WELL
Installing Monitoring Wells
Test Site
TREATMENT SHED
Nitrification
TREATMENT SHED
Oxygen Addition
OXYGEN SOURCE
Amendment Addition
GAS LIQUID REACTOR
NUTRIENT DELIVERY
OXYGEN DELIVERY
Amendment Addition
VENTURI
Nitrification Results
0.00
20.00
40.00
60.00
80.00
100.00
120.00
1 5 9 13 17 21 25 29 33 37 41 45 49 53 57 61 65 69 73 77 81 85 89 93 97 101
105
109
113
117
121
125
129
133
137
141
145
149
Days
DO
, Am
mon
ia,
Nitr
ate
- N C
once
ntra
tion
(mg/
L)
0.00
0.20
0.40
0.60
0.80
1.00
1.20
Phos
phat
e - P
Con
cent
ratio
n (m
g/L)
TH13 NH4TH13 NO3TH13 DOTH13 PO44 per. Mov. Avg. (TH13 NH4)4 per. Mov. Avg. (TH13 NO3)4 per. Mov. Avg. (TH13 DO)
66 – 89 % AMMONIA REDUCTION
In-Situ De-Nitrification
Pilot Test Site
Amendment Addition
NUTRIENT DELIVERY
NO OXYGEN DELIVERY
De-Nitrification
NUTRIENT DELIVERY CARBON
DELIVERY
Field Lab
De-Nitrification Results
0.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
3 4 5 6 7 8 9 10 11 12 13 14 15 16 17
Days
DO
, A
mm
onia
, Nitr
ate
- N C
once
ntra
tion
(mg/
L)
4 per. Mov. Avg. (TH1 DO)4 per. Mov. Avg. (TH1 NH4)4 per. Mov. Avg. (TH1 NO3)
Nitrate
Ammonia
Dissolved oxygen
78 – 99 % NITRATE REDUCTION
Options
Options Main Limitations Capital($ Million)
Operating($/year)
Present Value Cost1
($ million)1. Groundwater Extraction and Irrigation Summer treatment $0.85 $57,000 $1.4
2. Groundwater Extraction and Discharge to City Sanitary Sewer
Removal of ammonia only
$0.69 $50,000 $1.2
3. Groundwater Extraction and Electrochemical Treatment
High cost $3.1 $155,000 $4.7
4. Groundwater Extraction and Biological Treatment (Nitrification)
High cost $1.6 $100,000 $2.6
5. Groundwater Extraction and Wetlands Disposal
Summer treatment, low N
$0.64 $51,000 $1.2
6. In-Situ Electrochemical Treatment Low perm soils $2.8 >$35,000 >$3.0
7. On-Site Ex-Situ Biological Treatment High cost $5.0 to $7.0 >$35,000 >$5.0
8. In-Situ Nitrification and High perm soils $0.2 $30,000 $0.5
De-Nitrification $0.1 $25,600 $0.41 Present value based upon 15 year life and 5% rate of return.
Questions
In-Situ Groundwater Nitrification andDe-Nitrification Remediation Processes
By: Steve Mailath, EBA Engineering Consultants Ltd.Patent Pending: David Reese, University Technologies International,
Phone: 270.2434Dr. Angus Chu, U of C, Phone: 220.8987Steve Mailath, EBA, Phone: 723.6898
QUESTIONS