USE OF A SATURATED/ UNSATURATED ZONE GROUNDWATER MODEL TO INVESTIGATE SOIL-WATER DYNAMICS IN ON-SITE WASTEWATER TREATMENT SYSTEMS - PowerPoint PPT Presentation

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USE OF A SATURATED/ UNSATURATED ZONE GROUNDWATER MODEL TO INVESTIGATE SOIL-WATER DYNAMICS IN ON-SITE WASTEWATER TREATMENT SYSTEMS

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Title: USE OF A SATURATED/ UNSATURATED ZONE GROUNDWATER MODEL TO INVESTIGATE SOIL-WATER DYNAMICS IN ON-SITE WASTEWATER TREATMENT SYSTEMS


1
USE OF A SATURATED/ UNSATURATED ZONE GROUNDWATER
MODEL TO INVESTIGATE SOIL-WATER DYNAMICS IN
ON-SITE WASTEWATER TREATMENT SYSTEMS
  • Ouro T Koumai
  • James M HassettDepartment of Environmental
    Resources and Forest Engineering, SUNY - ESF,
    Syracuse NY 13210

2
Presentation Outline
  • Project Scope
  • Treatment Data
  • Hydraulic Data
  • Conclusions

3
CWC Septic Rehab/ Replacement and Monitoring
Project (2002- 2007)
  1. Rehabilitate/Replace failing septic system
  2. Investigate the use of Best Alternative
    Technologies (BATs) in sites with less than
    optimal conditions

Jim and Jessica at site M4
Catskill/ Delaware watershed with Monitoring sites
4
Failure criteria
  • Hydraulic failure (Easy to Observe)
  • Breakout
  • Outflow or visible back up to surface
  • Unsuitable soil
  • Treatment failure (Difficult to Observe)
  • Inadequate treatment
  • Unsaturated zone depth lt 2ft.

5
System Design
6
Peat Filter System
7
Hassett Lysimeters
8
Summary Sampling Design
  • 24 sites sampled for one year
  • (4C, 5R, 5A, 5P, 5S) quasi replication, quasi
    random
  • Wide geographic distribution within watershed
  • Multiple engineers and installers
  • QA/QC program showed results adequate for
    purposes of study
  • Sampling locations allowed multiple means of
    quantifying system performance

9
Treatment Results
  • System Operation versus System Design
  • All systems operated at less than design flow
  • Septic Tank Effluent
  • Comparable to other studies
  • Conclusion
  • Differences in system performance attributed to
    differences among systems, and not hydraulic or
    organic loading issues

10
Example Data-TOC at a Conventional Site
11
Median Performance - TOC
12
Overall TOC Removal Septic Tank Effluent to L4
13
Removal of TOC in Pretreatment and Soil Systems
14
Removal of TP in Pretreatment and Soil Systems
15
Average Annual Cost per kg of Constituent Removed
by System Type
C R A P S
TOC 308 347 357 271 232
TP 1,350 1,936 2,391 1,767 1,868
Total Nitrogen 317 510 653 427 487
16
Hydraulic Observations and Considerations

17
Unexpected Flow Patterns
18
Unexpected Degree of Soil Saturation
19
Evidence of Weeping and Breakout
20
Visual Indicators
21
VS2DTI model
Preprocessor
  • Model configured in accordance with site layout,
    topography, stratigraphy and hydrology
  • Initial conditions represented by depth to water
    table and minimum pressure head

Postprocessor
  • Pressure head
  • Moisture content
  • Saturation

22
Modeling Choices
23
Modeling Choices
  • Domain size of leach field or mound
  • Water input flow from septic tank
  • Unsteady flow analysis

24
Pressure head profiles
Example of simulated pressure head profiles at 0
hr (Left) and Time 86400 hr (right) for a
typical conventional SWIS
25
Moisture Content
Example of Simulated moisture content profiles at
0 hr (Left) and Time 86400 hr (right) for a
typical conventional SWIS
26
Percent Saturation
Example of Simulated Saturation profiles at 0 hr
(Left) and Time 86400 hr (right) for a typical
conventional SWIS
27
Site data
  • Perc test results (min/inch)
  • Deep hole observations
  • Soil texture
  • Lot size, slope, etc.

28
Engineering design data
  • Flow rate
  • Tank capacity
  • Flow application rate
  • SWIS basal area,
  • field length and
  • number of laterals

29
Raised trench model
Conceptual VS2DT model for S1
  • S1, base model
  • 60 x 31
  • 5 laterals at 0.021 ft/ hr
  • Native soil tight clay
  • Fill clay loam

30
Applications of the VS2DT model to sites in the
Catskill/Delaware
  • M4 Flow simulated to explain the occurrence of
    seeping down slope and the breakout upslope
  • S2 Explain the occurrence of unusual grass
    growth patterns observed on the system
  • C2 Explain the presence of wastewater effluent
    in all 4 lysimeters and consistent soil
    saturation.

31
Raised trench systems
32
Simulated pressure head profiles for typical
raised trench SWIS
Time 0 hr
Time 86400 hr
The profiles show a pressure head increase for
the profile on right as a result of wastewater
disposal
33
Effect of soil textural classpressure head
profiles
Medium sand
Fine sand
Silt loam
Sandy loam
34
M4
35
S2
Grass growth along the pipes
36
C2
Table 3.20 Summary of test pit observations at Site C2 Table 3.20 Summary of test pit observations at Site C2 Table 3.20 Summary of test pit observations at Site C2 Table 3.20 Summary of test pit observations at Site C2 Table 3.20 Summary of test pit observations at Site C2 Table 3.20 Summary of test pit observations at Site C2
Deep test pit Depth to bottom Pit Depth to seasonal ground water Depth to Fragipan Depth to bedrock Approximate slope
DTP1 57 47 35 None 5
DPT2 53 20 N/A None 5
37
Conclusions
  • The applications of the model to the three
    previously mentioned SWISs (M4, S2 and C2) have
    more or less replicated the defects and
    observations made on the field.
  • The VS2DT modeling justified most requirements
    set in appendix 75-A by the NYS DOH.

38
Questions?
39
Recommendations
  • To promote safer designs, installation and
    operation of OWTSs, we would recommend that
  • Sites with slopes be subject to great deal of
    attention during SWIS design and installation.
    Delicate site leveling and stabilization should
    be considered, sides extension slopes for raised
    trench systems should be reduced from 1/3 to 2/3
    if possible.
  • In addition to the NYS DOHs appendix 75-A,
    engineers should consider modeling the flow based
    on design before design is implemented.

40
Recommendations (contd.)
  • Additional deephole tests or other types of soil
    appraisal be required to sufficiently access the
    sites Hydrogeological characteristics.
  • Systems be designed with the provision of worst
    hydrologeologicals conditions possible.
  • The design of raised trench system be mandatorily
    preceded by the use of advanced treatment units
    (peat filters, sand filter etc.).

41
The CWC Septic Program provides reimbursement for
repair or replacement of failing or reasonably
likely to fail residential septic systems located
within 100 feet of a watercourse or 500 feet of a
reservoir or reservoir stem.
42
Goals and Objectives
  • To provide information about the effectiveness of
    alternative onsite wastewater treatment
    technologies under local conditions to help
    designers and regulators select appropriate,
    cost-effective systems in the WOH watershed.

43
Project Scope
  • Can alternative technologies remediate
    substandard absorption areas to an acceptable
    level?
  • What is the performance (i.e., carbon, nutrient
    and pathogen removal) of such systems in real
    world conditions?
  • What is the cost of installation, operation and
    maintenance of various technologies?
  • How well can these systems be maintained over
    time?

44
SUNY-ESF Project Team
  • James Hassett Experience with other septic
    studies, water resources engineer
  • Donald Siegel Experience with other septic
    studies, groundwater hydrology
  • Alvin Chan, Jessica Martin Graduate students
    extraordinaire

45
Sampling Protocol System Types
  • Conventional Systems (C)
  • Raised Bed Systems (R)
  • Aerobic Treatment Units (A)
  • Singular Model 960 by Norweco
  • Peat Moss Filtration Systems (P)
  • Ecoflo STB 650 by Premier Tech Environment
  • Intermittent Sand Filters (S)

46
Conventional Five Sampling Locations
47
Typical D-Box and Distribution Pipe
48
Lysimeter Schematic
49
Lysimeter Installation
50
Lysimeter Installation
51
Typical Site Layout
52
Sampling from Hassett Lysimeter
53
Sampling from D-Box
54
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55
Raised Bed Five Sampling Locations
56
Sampling from Pump Chamber
57
Aerobic Treatment Units (A) Six Sampling
LocationsSingular Model 960 by Norweco
58
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59
PEAT (P) - Six Sampling LocationsEcoflo STB 650
by Premier Tech Environment
60
Intermittent Sand Filter (S) Six Sampling
Locations
61
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62
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63
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64
Parameters
  • Laboratory analyses
  • TOC, TP, TDP, NH3-N, Nitrate/nitrite-N, fecal
    coliform, conductivity
  • Field measurements
  • Temperature, pH, volume from each lysimeter,
    water meter reading, rain fall data (courtesy of
    NYC DEP)

65
Data Review
  • Data received from lab, merged with field data,
    entered in Excel spreadsheet
  • Data transferred to SAS for data management
  • Graphs generated for each sampling site each
    month
  • Data inspected visually for discrepancies

66
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67
Site S3 Total Phosphorus - Corrected
68
QA/QC Data
  • Field Duplicates Samples obtained and labeled
    appropriately (e.g., S3L4). In addition, samples
    taken from some locations and labeled as DUP 1,
    etc, sent to lab in separate cooler.
  • Equipment Blanks Distilled water run through
    pumps into sampling bottles.

69
Field Duplicate Data - Conductivity
70
Field Duplicate Data - TOC
71
Field Duplicate Data Fecal Coliform
72
Summary Sampling Design
  • 24 sites sampled for one year
  • (4C, 5R, 5A, 5P, 5S) quasi replication, quasi
    randomness
  • Wide geographic distribution within watershed
  • Multiple engineers and installers
  • QA/QC program showed results adequate for
    purposes of study
  • Sampling locations allowed multiple means of
    quantifying system performance

73
Results - I
  • System Operation versus System Design
  • All systems operated at less than design flow
  • Septic Tank Effluent
  • Comparable to other studies
  • Conclusion
  • Differences in system performance attributed to
    differences among systems, and not hydraulic or
    organic loading issues

74
Statistical Summary Septic Tank Effluent
75
Example Data-TOC at a Conventional Site
76
Example Data TOC at a Sand Filter Site
77
Results II Overall System Performance
  • Compare median of all data for each system type
  • Compare septic tank effluent (system input) to L4
    (deepest lysimeter) for each system type

78
Median Performance - TOC
79
Median Performance - TP
80
Median Performance NH3-N
81
Median Performance Nitrate/nitrite - N
82
Median Performance Fecal Coliform
83
Results -Overall Removal Data
  • Compare most upstream data (either P or D) to L4

84
Overall TOC Removal Septic Tank Effluent to L4
85
Overall Total N Removal Septic Tank Effluent to
L4
86
Statistical Summary Unadjusted L4 Data
87
Results III Just What Does Pretreatment Buy?
  • Compare removals in pretreatment unit to removals
    in soil system

88
Removal of TOC in Pretreatment and Soil Systems
89
Removal of TP in Pretreatment and Soil Systems
90
Removal of FC in Pretreatment and Soil Systems
91
The Question of Dilution
  • Conductivity data can be used as a conservative
    tracer to calculate dilution attributed to rain,
    groundwater, etc.

92
Calculation of Per Cent of Effluent in Samples
from L1 through L4
93
Removals of FC at L4 Adjusted for Dilution
94
Statistical Summary L4 Data Adjusted for Dilution
95
Cost-Benefit Analysis Average Annual Cost per
kg of Constituent Removed by System Type
C R A P S
TOC 308 347 357 271 232
TP 1,350 1,936 2,391 1,767 1,868
Total Nitrogen 317 510 653 427 487
96
Conclusions
  • Aerobic Treatment Units are problematic
  • Long term effects of reduced drain field loadings
    from alternative treatment systems unknown, but
    likely to be a positive benefit in terms of
    increased service life

97
Catskill Watershed Corporation
  • 845-586-1400
  • cwconline.org
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