Title: Evaluation of Passive Nitrogen Removal Systems
1Evaluation of Passive Nitrogen Removal Systems
- Daniel P. Smith, PhD, P.E.
- Applied Environmental Technology
- Tampa, FL 33592-2250
AET
2Acknowledgements
- Florida Department of Health
- Elke Ursin, Eberhard Roeder, Paul Booher
- Dick Otis
- Mark Flint
- Damain Anderson
- Hillsborough County, Florida
3Florida Passive Nitrogen Removal Study
- Objective evaluate enhanced nitrogen removal
from on-site wastewater using passive systems - Influent septic tank effluent
- Goal reduce total nitrogen
4Florida Passive Nitrogen Removal Study Tasks
- Literature review and database
- Experimental evaluation
- Feasibility
- Economic analysis
5Passive Definition
- A type of onsite sewage treatment and disposal
system that excludes the use of aerator pumps and
includes no more than one effluent dosing pump in
mechanical and moving parts and uses a reactive
media to assist in nitrogen removal
6Technology Constraints
- No aerators unsaturated filter for Stage 1
- One pump otherwise gravity flow
- where to place?
- Reactive media
- electron donor for denitrification
- alkalinity
- ion exchange
7Two Stage Processfor TN Reduction
- Stage 1 unsaturated filter
- aerobic Organic N and ammonia
- produce low effluent TKN
- Stage 2 saturated
- anoxic oxidized N
- electron donor for denitrification produce
low effluent NOx
8Pump Before Stage 1 Filter
- Allows timed dosing
- Nitrification performance of Stage 1 filter
- Potential for Stage 1 recycle
- Flow equalization to entire treatment train
- Gravity flow through second stage filter to
dispersal field
9Media Evaluation System
10Passive Nitrogen Removal StudyApplied
Environmental Technology
Stage 1 (unsaturated)
Stage 2 (saturated)
11Media Selection Factors Stage 1 Aerobic
Unsaturated
- Particle size
- Specific surface area
- External porosity
- Air filled porosity
- Water retention capacity
- Cation Exchange Capacity (CEC)
12Stage 1 Media (nitrification)
Expanded clay
Zeo-Pure clinoptilolite
Tire crumb
13Media Selection Factors Stage 2 Anoxic
Saturated
- Reactivity electron donor release rate
- Longevity
- Alkalinity supply
- Anion Exchange Capacity (AEC)
14Stage 2 Media (denitrification)
Expanded shale
Elemental sulfur
Oyster shell
15Autotrophic Nitrogen Reduction
16Filter Media
17Expanded shale/oyster shell/elemental sulfur
18Test Site Flatwoods Park, Hillsborough County,
Florida
19Test Site Flatwoods Park, Hillsborough County,
Florida
20Operating Features (one pass)
21Nitrogen Loading
22Feed Septic Tank Effluent
232 Stage System Effluent TN
24Nitrogen Average (n5)
25Two Stage Removal Efficiency
26Total NitrogenRemoval Efficiency
27Stage 2 Effluent LDO and pH Probes
28Results Field Parameters
29Stage 1 Removal Efficiency
30Example System
- Stage 1 Aerobic
- 100 ft2 x 24 in. expanded clay
- Stage 2 Anoxic
- Sulfur/oyster/shale 60/20/20 volume Vanoxic
1/4 Vaerobic - Media cost Stage 1 700 / Stage 2 825
31Theoretical Longevity of Electron Donor4 persons
_at_ 13 gram N/capita-day
32Conclusions
- Proof of Two Stage Filter concept for Passive N
Removal - Single pass at 3 gal./ft2-day
- Total N removal of 97
- Total N reduced from 77 to 2 mg/L
- Longer term operation needed
33Conclusions
- Stage 1 aerobic 99 NH4 reduction with
clinoptilolite and expanded clay - Stage 2 anoxic NOxlt0.5 mg/L and 99 reduction
with sulfur-based denitrification - Need to verify longevity of performance and media
34(No Transcript)
35Biochemical Transformations
- Organic N NH4 NO2- NO3-
N2
Nitrification (Aerobic)
Denitrification (Anoxic)
Ammonification
36Results Stage 1 Effluent NH4
37Stage 1 TN Removal Efficiency
38Florida Passive Nitrogen Removal Study Tasks
- Literature review and database
- Experimental evaluation
- Feasibility
- Economic analysis
39Obligatory Biochemical Sequence for TN Reduction
- Aerobic Organic N ? NH4
- NH4 ? NO3
- Anoxic NO3 ? N2
40Example On-Site Configuration
41Media Selection Factors Stage 1 Aerobic
Unsaturated
- Particle size
- Specific surface area
- External porosity
- Air filled porosity
- Water retention capacity
- Cation Exchange Capacity (CEC)
42Total Inorganic Nitrogen Removal Efficiency