HomeMy WebLinkAbout1203_Burke_CDLFOverMSWLF_CAPAddendum_DIN28743_20180212
PREPARED FOR:
BURKE COUNTY
P. O. BOX 1486
MORGANTON, NC 28680-1486
BURKE COUNTY – JOHN’S RIVER WASTE MANAGEMENT FACILITY
PERMIT NUMBER 12-03
ADDENDUM TO CORRECTIVE ACTION PLAN
AUGUST 2013
REVISED JANUARY 2018
PREPARED BY:
2211 WEST MEADOWVIEW ROAD, SUITE 101
GREENSBORO, NORTH CAROLINA 27407
NC LICENSE NUMBER C-0782
PHONE: (336) 323-0092
FAX: (336) 323-0093
PROJECT NO. 2180038
ADDENDUM TO CORRECTIVE ACTION PLAN
Johns River Waste Management Facility, Permit No. 12-03
Table of Contents
Addendum to Corrective Action Plan Joyce Engineering
Johns River Waste Management Facility, Permit 12-03 August 2013, Rev. January 2018
i
1.0 INTRODUCTION ...........................................................................................................1
1.1 Site Background ...............................................................................................................1
1.2 Corrective Actions to Date...............................................................................................2
1.3 Gas Impacts and GPS Exceedances Northeast of the Landfill ........................................3
2.0 ADDITIONAL REMEDY - CONTROL OF LANDFILL GAS .....................................5
2.1 Landfill Gas Impact on Groundwater ..............................................................................5
2.2 Passive LFG Control Mechanism ....................................................................................5
2.3 GEU Pilot Tests ...............................................................................................................6
2.4 Active LFG Control Mechanisms ....................................................................................6
2.4.1 GEU ..................................................................................................................6
2.4.2 Wells ..................................................................................................................7
2.4.3 HDPE Pipe & Fittings ..........................................................................................7
2.4.4 Condensate Removal ...........................................................................................7
2.4.5 Operation and Maintenance .................................................................................8
2.4.6 Odor Control ........................................................................................................8
3.0 REMEDY EVALUATION FACTORS ...........................................................................8
3.1 Long-Term and Short-Term Effectiveness ......................................................................8
3.1.1 Magnitude of Reduction of Existing Risks ..........................................................8
3.1.2 Magnitude of Residual Risks in terms of Likelihood of Further Releases due to
Wastes Remaining Following Implementation of a Remedy ..........................................9
3.1.3 Type and Degree of Long-term Management Required, including Monitoring,
Operation, and Maintenance ............................................................................................9
3.1.4 Short-term Risks that Might be Posed to the Community, Workers, or the
Environment during Implementation of such a Remedy, including Potential Threats to
Human Health and the Environment Associated with Excavation, Transportation, and
Redisposal or Containment; .............................................................................................10
3.1.5 Time until Full Protection is Achieved; ...............................................................10
3.1.6 Potential for Exposure of Humans and Environmental Receptors to Remaining
Wastes, Considering the Potential Threat to Human Health and the Environment
Associated with Excavation, Transportation, Redisposal, or Containment; ....................10
3.1.7 Long-term Reliability of the Engineering and Institutional Controls ..................11
3.1.8 Contingency Plans and Potential need for Replacement of the Remedy. ............11
3.2 Controlling the Source .....................................................................................................11
3.2.1 The Extent to which Containment Practices will Reduce Further Releases ........12
3.2.2 The Extent to which Treatment Technologies may be Used ...............................12
Table of Contents (continued)
Addendum to Corrective Action Plan Joyce Engineering
Johns River Waste Management Facility, Permit 12-03 August 2013, Rev. January 2018
ii
3.3 Remedy Implementation ..................................................................................................12
3.3.1 Degree of Difficulty Associated with Constructing the Technology ...................12
3.3.2 Expected Operational Reliability of the Technologies ........................................12
3.3.3 Need to Coordinate with and Obtain Necessary Approvals and Permits from
Other Agencies; ...............................................................................................................13
3.3.4 Availability of Necessary Equipment and Specialists .........................................13
3.3.5 Available Capacity and Location of Needed Treatment, Storage, and Disposal
Service ..................................................................................................................13
3.4 Owner/Operator Capability ..............................................................................................13
3.5 Community Concerns ......................................................................................................13
4.0 WATER QUALITY MONITORING PLAN ..................................................................14
5.0 EVALUATION OF EFFECTIVENESS AND REPORT SUBMITTALS .....................15
5.1 Physical and Chemical Changes in Aquifer Conditions ..................................................15
5.2 Physical and Chemical Changes in Plume Characteristics ..............................................15
5.3 Refining the Site Conceptual Model ................................................................................15
5.4 Evaluation of Remedy Effectiveness ...............................................................................15
5.5 Corrective Action Program Reporting .............................................................................16
6.0 SCHEDULE AND MAINTENANCE .............................................................................17
6.1 Schedule Considerations ..................................................................................................17
6.2 Timeline ..................................................................................................................17
6.2.1 Monitoring Schedule ............................................................................................17
6.2.2 Active GEU Implementation Schedule ................................................................17
6.3 Operations and Maintenance (O&M) ..............................................................................18
6.4 Safeguards and Safety ......................................................................................................18
6.5 Modification of Corrective Action or Schedule ...............................................................18
7.0 FINANCIAL ASSURANCE ...........................................................................................18
8.0 COMPLETION OF CORRECTIVE ACTION ...............................................................18
9.0 REFERENCES ................................................................................................................19
Table of Contents (continued)
Addendum to Corrective Action Plan Joyce Engineering
Johns River Waste Management Facility, Permit 12-03 August 2013, Rev. January 2018
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TABLES
Table 1 Detected VOCs - February & July 2013 Piezometer Sampling
Table 2 Detected VOCs - December 2012 Compliance Sampling
FIGURES
Figure 1 Site Location Map
Figure 2 COCs in MW-36 and MW-38 vs. Time
DRAWINGS
Drawing 1 Groundwater Potentiometric Surface Map (December 2012)
Drawing 2 LFG Delineation Study
Drawing 3 Total VOC Isoconcentration Map
Drawing 4 Cross Section C-C’
Drawing 5 Proposed Active LFG System Layout and Details
Drawing 6 Proposed Active LFG System Details
APPENDICES
Appendix A Gas Vent Construction Logs
Appendix B GEU Pilot Test Data
Appendix C LFG Control Construction Specifications
Appendix D KYGAS Modeling Output
ADDENDUM TO CORRECTIVE ACTION PLAN
Johns River Waste Management Facility, Permit No. 12-03
Addendum to Corrective Action Plan Joyce Engineering
Johns River Waste Management Facility, Permit 12-03 August 2013, Rev. January 2018
1
1.0 INTRODUCTION
On behalf of Burke County, Joyce Engineering (JOYCE) prepared this second Addendum to the
Corrective Action Plan (CAP Addendum #2) for the Johns River Waste Management Facility
(facility). This is the second addendum since the original CAP was submitted in June 2008. The
first CAP Addendum, dated August 2013, was prepared in in response to the Groundwater
Protection Standard (GPS) exceedances of volatile organic compounds (VOCs) in piezometers on
the northeast side of the landfill. VOCs in exceedance of GPS include: 1,1-dichloroethane; 1,2-
dichloroethane; 1,4-dichlorobenzene; benzene; methylene chloride; tetrachloroethene;
trichloroethene; and vinyl chloride. The impacted piezometers are located upgradient of the
existing waste unit and the exceedances are believed to be the result of cross-media impact to the
groundwater by migrating landfill gas (LFG).
The 2013 Addendum added control of migrating LFG as a remedial method for the area northeast
of the active landfill. The 2013 Addendum proposed installation of several passive gas vents and
included as a contingency the option to add a gas extraction unit (GEU) to convert the passive
vents into an active gas extraction system. This Addendum #2 has been prepared in response to a
March 27, 2017, letter from the North Carolina Department of Environmental Quality (NCDEQ),
Division of Waste Management (DWM), Solid Waste Section (SWS), which requested that Burke
County implement the contingency. This CAP Addenda has been prepared in accordance with
15A NCAC 13B.1636 of the North Carolina Solid Waste Management Rules (NCSWMR).
Note: the NCDEQ was formerly called the Department of Environment and Natural Resource
(DENR), and is referenced as such in some parts of this report.
1.1 Site Background
The Johns River Waste Management Facility is located in the north-central portion of Burke
County, north of Morganton, North Carolina. The 318-acre landfill property is bounded by Lower
Creek to the north and east, and the Catawba River to the south. The Johns River flows into the
Catawba River near the southwest corner of the landfill property. The Catawba River forms the
upper reaches of Lake Rhodhiss along the southeastern property line. The property boundaries are
indicated on an excerpt from the USGS topographic quadrangle for Morganton, North Carolina
(Figure 1). The site has rolling topography with elevations ranging from 995 feet to 1,160 feet
above mean sea level (AMSL). The central portion is generally gently sloping and contains the
higher elevations; relatively steep slopes and significant drainage features are located around the
perimeter. Properties within 2,000 feet of the landfill boundary are covered by surface water or
are heavily wooded.
The unlined waste disposal unit consists of 28 acres in the southwest corner of the landfill property.
The municipal solid waste (MSW) Landfill began operation in April 1988, but was closed to
comply with Rule .1627(c)(10)(A) of the NCSWMR, a regulation governing MSW Landfills units
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that were not designed with a base liner and leachate collection system. Burke County operated a
permitted Construction and Demolition (C&D) disposal area on top of the closed portions of the
MSW landfill between 1998 and 2015 under Permit # 1203-CDLF-1998. Closure construction for
the C&D area was completed in 2016, and the closure was certified by the DEQ in February 2017.
A MSW transfer facility is located in the eastern half of the property. The transfer station has
operated since 1998 under permit #1205T-TRANSFER-1998.
In 2012, JOYCE submitted a Site Plan Application and a Permit to Construct Application for an
expansion of the C&D landfill to new cells located northeast of the existing landfill. A Permit to
Construct for Phase 1A was issued in March 2014 and the County completed construction of Phase
1A of the C&D landfill expansion in July 2014. A Permit to Operate for Phase 1A was issued to
the County by the North Carolina Department of Environment and Natural Resources, now the
Department of Environmental Quality (NCDEQ), on August 14, 2014. The C&D Expansion
operates under Permit # 1203-CDLF-2014.
A site plan showing all the pertinent features of the existing and proposed landfills and associated
facilities, as well as the December 2012 groundwater potentiometric contours and flow directions,
is provided as Drawing 1.
1.2 Corrective Actions to Date
In February 2005, in response to Groundwater Protection Standard (GPS) exceedances of several
volatile organic compounds (VOCs), including benzene,1,4-dichlorobenzene, methylene chloride,
tetrachloroethylene, and trichloroethylene at the facility, Burke County submitted an Assessment
of Corrective Measures (ACM) for the Johns River Landfill to the DENR. The ACM presented
an analysis of the effectiveness, performance, reliability, ease of implementation, and potential
environmental impacts of potential remedies, including safety impacts, cross-media impacts, and
residual contamination exposure control. The ACM also addressed the time required to implement
and complete the remediation, the costs of implementation and maintenance, and the institutional
requirements such as State or local permit requirements or other environmental or public health
requirements that may substantially affect the implementation of the potential remedies. Based on
the ACM, four remedial alternatives were selected for further consideration. The four selected
remedies were:
• Monitored Natural Attenuation with Phytoremediation;
• Control of Decomposition Gases (LFG);
• Enhanced Bioremediation; and
• Soil Vapor Extraction (SVE).
In June 2008, the County submitted a Corrective Action Plan (CAP) for the facility, which
proposed Monitored Natural Attenuation and Phytoremediation as the selected remedies for the
site. The CAP was approved by DENR in a letter dated January 29, 2009. The first Corrective
Action Evaluation Report (CAER) for the facility was submitted to DENR in May, 2011.
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The Facility entered the Corrective Action Program following the correspondence received from
the DENR Solid Waste Section (SWS) dated August 18, 2003. An Assessment of Corrective
Measures (ACM) was submitted to NCDEQ in February 2005. A public meeting was held on May
16, 2006 in order to receive public comments regarding the ACM as required by NCSWMR §.1635
(d). A Corrective Action Plan (CAP) was submitted to DENR in June 2008 and revised in
November 2008. The CAP was approved by DENR in a letter dated January 29, 2009. An
addendum to the facility’s CAP was submitted to the DENR in August 2013, adding control of
landfill gas as a remedy for groundwater impacts on the northeastern side of the landfill between
the old landfill and the new C&D expansion area.
The 2013 CAP Addendum proposed installation of eight passive gas vents in the MSW waste
along the northeast side of the old C&D-over-MWS landfill, between the old landfill and the C&D
Expansion Area. In November 2013, JOYCE installed seven passive gas vents at the locations
shown on Drawing 5. One of the originally-proposed eight vents turned out to be located on C&D
waste and could not be installed. In September 2015, four additional passive gas vents were
installed along the top of the landfill as part of closure construction for the C&D portion of the old
landfill. The locations of these vents are also shown on Drawing 5.
In a letter dated March 27, 2017, the NCDEQ-SWS requested implementation of the County’s
corrective action contingency plans, and asked for a proposed alternate remedy and
implementation schedule within 90 days. We requested an extension of the due date for our
response to July 25, 2017, which was approved in an email dated June 12, 2017. A Proposed
Alternate Remedy and Schedule for implementation of an active landfill gas control system was
submitted to NCDEQ on July 25, 2017. After reviewing it, the NCDEQ requested some changes
to the schedule, and a revised Proposed Alternate Remedy and Schedule was submitted on
August 15, 2017.
1.3 Gas Impacts and GPS Exceedances Northeast of the Landfill
LFG monitoring has been performed quarterly at the Johns River Landfill since 1993. Since 1994,
there have been notable exceedances of the lower explosive limit (LEL) for methane in gas probe
GP-2. Gas monitoring probes GP-2S, GP-2I, and GP-2D are nested probes in a single boring that
are jointly referred to as GP-2. GP-2 is located near the northeastern corner of the existing landfill,
less than 100 feet from the limits of waste and far from any property boundary. Probe GP 1
adequately monitors the nearest property boundary to GP-2, and all other property boundaries are
over 2000 feet away and/or are bounded by surface water. The DENR has previously agreed that
the exceedances at GP-2 do not indicate methane migrating across or toward a facility boundary
(see correspondence between JOYCE and the DENR dated October 6, 2011). There have never
been any methane exceedances at any other gas probes or in any structures at the Johns River
facility.
Concern about LFG exceedances in the vicinity of GP-2 were elevated during the DENR review
of the County’s permit application for the C&D expansion to the northeast of the existing landfill.
At the DENR’s request, JOYCE conducted a LFG delineation study in the vicinity of GP-2 in
November 2012. The results of the LFG delineation study are shown in Drawing 2. The area of
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Johns River Waste Management Facility, Permit 12-03 August 2013, Rev. January 2018
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methane concentrations above the LEL extends 200-350 feet from the edge of waste northeast of
the existing landfill, which includes the southwestern portions of the proposed expansion area
Phases 1, 2, and 3.
LFG is typically composed of roughly 55% methane, 44% carbon dioxide, and 1% other VOCs.
It is not uncommon for VOCs in LFG to partition into the ground water where the migrating gas
comes into contact with the groundwater. This can happen inside wells, in the vadose zone, or at
the groundwater surface. LFG impacts to groundwater have been suspected at the Johns River
Landfill in the past. Former upgradient background monitoring wells MW-9 and MW-17, located
north of existing waste unit, both exhibited detections of VOCs that were attributed to LFG prior
to their being removed from service as background wells.
In February 2013, at the DENRs request, JOYCE sampled existing piezometers in the vicinity of
the area of methane migration northeast of the existing landfill to determine the extent of
groundwater impacts in this area. JOYCE sampled Piezometers PZ-30S, PZ-35, PZ-36, PZ-37,
and PZ-38. PZ-36 and PZ-38 are located between the old waste unit and Phase 1 of the proposed
C&D expansion. PZ-38 has been designated to become compliance monitoring well MW-23
under the Water Quality Monitoring Plan (WQMP) submitted in August 2012 with the permit-to
–construct application for the C&D expansion. PZ-30S, and PZ-35, and PZ-37 are located with
the proposed footprint of the C&D expansion. The results of the February 2013 piezometer
sampling event were submitted to the DENR in a letter report dated April 23rd, 2013.
Results of the February 2013 piezometer sampling indicated several VOCs in exceedance of their
respective GPS, including: 1,1-dichloroethane; 1,2-dichloroethane; 1,4-dichlorobenzene; benzene;
methylene chloride; tetrachloroethene; trichloroethene; and vinyl chloride. The exceedances were
in piezometers PZ-36 and PZ-38, which are located between the existing waste unit and the
proposed expansion unit. No VOCs were detected in any of the piezometers located within the
footprint of the proposed expansion unit.
After reviewing the results of the February 2013 piezometer sampling, the DENR requested two
more piezometers be sampled. JOYCE sampled Piezometers PZ-31 and PZ-34 on July 18, 2013.
PZ-31 and PZ-34 are located between the piezometers with exceedances (PZ-36 and PZ-38) and
the piezometers that were clean (PZ-30S, PZ-35, and PZ-37). The results of the July 2013
piezometer sampling event were submitted to the DENR in a letter report dated July 29th, 2013.
Table 1 presents the detected VOCs from the February 2013 and July 2013 piezometer sampling
events. Table 2 presents the detected VOCs from the December 2012 semiannual compliance
monitoring event. These combined results were used to create the Total VOC Isoconcentration
Map shown in Drawing 3. Drawing 4 shows a cross-sectional view of the Total VOC plume.
Drawings 3 and 4 show that the highest concentrations of VOCs in the groundwater are in PZ-36,
the piezometer closest to GP-2, where the highest methane concentrations are. The VOC plume
extends beneath a portion of the Phase 1 footprint in the vicinity of PZ-31. In general, the
concentrations of VOCs to the northeast of the existing landfill closely mimic the concentrations
of methane in the subsurface. This supports the contention that the VOCs in the groundwater in
this area are primarily due to partitioning from the LFG.
Addendum to Corrective Action Plan Joyce Engineering
Johns River Waste Management Facility, Permit 12-03 August 2013, Rev. January 2018
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Figure 2 presents a series of charts showing the concentrations of the constituents of concern in
MW-36 and MW-38 vs. time from February 2013 through December 2016. The charts show
decreasing trends in the concentrations of the COCs since the installation of the gas vents in
November 2013. There is evidence that the remedy is reducing the concentrations of COCs in
MW-36 and MW-38; therefore, the remedy is working effectively as designed.
2.0 ADDITIONAL REMEDY - CONTROL OF LANDFILL GAS
2.1 Landfill Gas Impact on Groundwater
Typically, LFG is made up of approximately 55% methane, 44% carbon dioxide, and 1% other
VOC’s, including vinyl chloride and benzene (Allen, et al, 1997; Deipser and Stegmann, 1994;
Cowie, 2004). Numerous studies have established that VOC’s present in LFG can readily partition
into groundwater. Transfer of VOC’s from gas to groundwater can occur both in the monitor well
and/or outside the monitor well. LFG is the most likely source of VOC detections in groundwater
located cross-gradient from the landfill
The 2005 ACM for this facility concluded that control of decomposition gas (LFG) was an
appropriate and viable remedy for groundwater impacts at the Johns River Facility. It is likely
VOC exceedances northeast of the existing landfill are related to LFG; therefore, control of LFG
migration is an appropriate remedy to address groundwater impacts for this area.
2.2 Passive LFG Control Mechanism
The proposed mechanism for control of LFG in the 2013 CAP addendum was installation of
passive gas vents in the MSW waste along the northeastern portion of existing landfill, spaced
approximately 100 feet apart. The old waste unit consists of a closed MSW landfill with C&D
waste on top of it. Seven vents were installed in November 2013 in the MSW waste just beyond
the limits of the C&D waste. Locations of the vents are shown on Drawing 5. The vents were
installed to the base of waste as determined during drilling. The following table summarizes the
total depths (in feet below grade) for each of the seven gas vents installed in 2013:
Gas Vent: GV-1 GV-2 GV-3 GV-4 GV-5 GV-6 GV-7
Total Depth: 25.5’ 35.0’ 43.0’ 43.0’ 45.0’ 47.0’ 36.0’
The vents were constructed of perforated 6 inch PVC well screen and riser screened from 5 feet
below grade to total depth. The borings were back-filled with gravel to 1 foot above the top of
screen, and a minimum 2-foot bentonite seal was placed above the gravel pack. The vents were
completed approximately feet above grade and topped with solar turbine heads. Vent construction
logs for the seven vents installed in 2013 are included in Appendix A.
In September 2015, four additional passive gas vents were installed along the top of the landfill
as part of closure construction for the C&D portion of the old landfill. These vents are only in
C&D waste and do not penetrate to the MSW waste beneath it. They were not installed as part
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Johns River Waste Management Facility, Permit 12-03 August 2013, Rev. January 2018
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of the remedy for groundwater impacts by landfill gas; however, they may provide some
additional gas control that is beneficial to groundwater corrective action. The locations of these
vents are also shown on Drawing 5, and their total depths are summarized below:
Gas Vent: GV-8 GV-9 GV-10 GV-11
Total Depth: 34.0’ 24.0’ 24.0’ 24.0’
2.3 GEU Pilot Tests
GEU pilot tests were conducted on September 25-26, 2017, to determine the optimal vacuum and
flow rates for the proposed permanent GEU. Tests were conducted independently on three of the
seven original passive gas vents, GV-4, GV-2, and GV-6. A 2.0 HP portable GEU was used for
the pilot tests, with vacuums ranging from -10 to -25 inches of water column (in-wc). A GEM-
2000 was used to measure gas concentrations, pressures, etc., on the tested vent throughout each
test, and manual measurements were made periodically at the vents on either side of the tested
vent (i.e., on GV-3 and GV-5 for the test on GV-4). The data from the pilot tests was used to
constraining the design of the active gas extraction system. The data from the pilot test are
presented in Appendix B.
2.4 Active LFG Control Mechanisms
In order to control landfill gas migration and lessen cross-media impacts to the groundwater, the
passive vents will be converted to an active LFG system with the installation of a gas extraction
unit (GEU) and connected to the existing passive vents through a below grade piping system. The
proposed layout and details for the GEU and piping system are shown on Drawings 5 and 6, and
specifications are included in Appendix C.
2.4.1 GEU
The gas extraction unit (GEU) will be a prefabricated, skid mounted unit including: centrifugal
blower, condensate knockout tank and air filter. A flare will be installed if odor or emissions
control is determined to be necessary. Sufficient area will be left on the skid to allow for flare
installation at a later date. Design specifications for the GEU are provided in Appendix C. The
GEU shall have a design rating of 140 SCFM at -15 in. w.c, corresponding to an average of 20
SCFM per vent. Typically a system pressure of approximately -10 to -15 in. w.c is desired
throughout the collection piping.
The gas extraction system was modeled using KYGAS Pipe2018 Gas Network Analysis
Software by KYPIPE LLC to determine the necessary vacuum to be supplied by the blower to
maintain between -10 and -15 in. w.c at each well. Landfill gas input parameters such as specific
gravity, absolute viscosity, density, and molecular weight were estimated by averaging the
corresponding values for methane and carbon dioxide assuming a 50%-50% composition in
landfill gas. Standard pipes with 4” and 8” internal diameters were used in the model for laterals
and header pipes, respectively and assigned a length corresponding to the plan view of the gas
extraction system shown on Drawing 5. A default pipe roughness value of 120 millifeet was
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assigned to the modeled pipes. Fittings (elbows, tees, valves) and entrances were incorporated
into the model to account for additional losses. Each well node was assigned a flow demand of
20 SCFM. The model demonstrated that -15 in. w.c being supplied at the blower was sufficient
to maintain between -10 and -15 in. w.c at each of the wells with the lowest well vacuum value
being -14.1 in. w.c. The output report from the KYGAS modeling is provided in Appendix D.
A variable frequency drive (VFD) rated electric motor capable of operating with the available
single-phase power at the site may be used. If an electric motor requiring 3-phase power is
selected, power will need to be brought in to the proposed GEU location from elsewhere on site,
or from off-site, if necessary.
2.4.2 Wells
Wells will be connected to the gas system using 2” flex hose. A 2” ball valve will be installed
between the well head and the flex hose in order to control flow and isolate the wells. A detail
showing this well configuration is shown on Drawing 5.
2.4.3 HDPE Pipe & Fittings
The gas collection piping shall include an 8” diameter header and 4” diameter lateral lines
connecting the header to each gas vent. The header and lateral lines shall be SDR 17 HDPE. The
proposed generalized layout of the pipe system is shown on Drawing 5. A detail of the trenching
of the landfill gas pipes is also provided on Drawing 5. If the header must cross beneath any roads
or areas where vehicles or equipment may need to drive over it, the HDPE pipe shall be encased
in a corrugated metal protective sleeve. A cleanout is provided at the end of the header line to
allow access to flush or camera the pipes if necessary in the future. Connections of the collection
pipe to the wells shall be accomplished with flexible fittings and flex hose, as shown in the detail
on Drawing 5. Specifications for the piping, trenching, and connections are included in Appendix
C.
2.4.4 Condensate Removal
The pipe system shall have a minimum slope of 2% for drainage of condensate to a single
condensate trap/sump at the northern, or low, end of the header. A 4” HDPE drain line allows
condensate to gravity drain from the header to the trap/sump, with a “J” trap in the sump to
maintain the vacuum on the header. The sump will consist of a buried HDPE tank of
approximately 4’ diameter by 10’ deep (930 gallons). Based on a conservative condensate
generation rate of 0.77 gallons per 1000 CFM of raw landfill gas (Municipal Landfill Gas
Condensate, EPA/600/S2-87/090, 1988) and an expected gas system flow rate of 140 CFM, the
930 gallon tank will have a storage capacity of approximately 5.8 days. The tank will have access
from the surface for periodic pumping out of the condensate, and for maintenance. Condensate
from the knockout pot of the GEU will be designed to gravity drain back to the condensate sump.
A detail drawing of the condensate sump is provided Drawing 6 and specifications are included in
Appendix C.
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2.4.5 Operation and Maintenance
Operation and maintenance of the active LFG system will include: 1) “wellfield”; 2) the GEU; and
3) the condensate sump. The wellfield will be balanced by adjusting the flow at each well to
provide an even distribution of flow and maintain appropriate vacuum throughout the system. The
well field will be balanced at startup and as necessary thereafter to achieve and maintain optimum
system performance.
The GEU will be designed to run 24 hours per day, 7 days per week in an outdoor setting. The
GEU will require periodic lubrication of the blower, replacement of the air filter, and inspection
of the knockout tank to insure proper functioning. The GEU should be checked daily for the first
week of operation, and at a minimum, weekly thereafter. A maintenance log for the GEU should
be maintained on site.
The condensate sump should be checked weekly, at a minimum, and more often if necessary, to
gauge the level of condensate in the tank, and be sure the tank remains in good condition is
operating properly. When the condensate sump is approaching capacity, the condensate should be
pumped out and transported to an appropriate facility for proper disposal.
2.4.6 Odor Control
If odor from the landfill gas becomes an issue, a utility flare may be added to the GEU to
combust the landfill gas. In the event this becomes necessary, the County will submit details for
the design and installation of the flare to DEQ for approval prior to proceeding.
3.0 REMEDY EVALUATION FACTORS
3.1 Long-Term and Short-Term Effectiveness
According to 15A NCAC 13B.1636(c)(1), the County is required to evaluate the long-term and
short-term effectiveness and protectiveness of the potential remedy, along with the degree of
certainty that the remedy will prove successful based on consideration of several factors. These
factors are addressed below.
3.1.1 Magnitude of Reduction of Existing Risks
Existing risk at the facility is limited to environmental professionals and/or County employees
participating in compliance groundwater or LFG monitoring activities. Specifically, the sampling
and handling of contaminated groundwater from within groundwater contamination plumes
beneath the facility creates risk. Natural attenuation lowers this risk by reducing concentrations
of constituents-of-concern (COCs) within the contaminant plume, and the control of LFG will
further reduce the COCs, and therefore, the risk.
The presence of LFG, especially methane, produces some risk. Methane is migrating in the
subsurface in the vicinity of the northeast portion of the existing landfill at concentrations above
the lower explosive limit (LEL), so there is some risk of explosion where people and/or equipment
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are disturbing the ground surface; therefore, special care should be taken in conducting any such
activities within the area of LFG migration. Once the methane migrates out of the soil into the
atmosphere, it is very quickly dissipated and does not pose a significant risk. Control of LFG will
significantly reduce the risk from migrating methane.
3.1.2 Magnitude of Residual Risks in terms of Likelihood of Further Releases due to Wastes
Remaining Following Implementation of a Remedy
The cap above the closed MSW landfill is expected to limit percolation of water through the MSW
waste, therefore limiting leaching of waste constituents into the groundwater. Once the C&D unit
on top of the closed MSW is closed and capped, this will further reduce water infiltration. Natural
attenuation appears to be occurring beneath the facility at a rate that will prevent migration of the
COCs beyond the property boundary at concentrations exceeding their respective GPS. In
addition, control of LFG will reduce the risk associated with any continued release, either from
landfill leachate of from LFG.
Wastes anticipated to be produced under the current remedies are limited to purge water associated
with performing groundwater monitoring events at the facility. The purge water will be discharged
to the ground surface and allowed to naturally infiltrate to the water table. Current impacts to the
groundwater are believed to be at least partially from LFG. The proposed LFG control mechanism
will reduce potential impacts to the groundwater on the northeast side of the landfill.
Wastes associated with implementation of the active LFG control remedy will small amounts of
soil during trenching to install pipelines from the existing gas vents to the proposed GEU, and
installation and connections for the condensate sump. It is not anticipated that any waste will need
to be excavated; however, should any waste be encountered, the waste will be taken to the on-site
MSW transfer facility for disposal off site. Soil removed during vent installation or trench
excavation is not expected to be contaminated, and will be disposed of on site, possibly as daily
cover material. No residual risk is anticipated. After installation of the active LFG control is
implemented, condensate from the active LFG system will be an additional waste, which will be
pumped out and properly disposed off-site by the County as needed.
3.1.3 Type and Degree of Long-term Management Required, including Monitoring, Operation,
and Maintenance
MNA will not require long-term operation and maintenance activities; however, long-term
monitoring of facility compliance wells and performance/sentinel wells will be required. The
Corrective Action Monitoring Plan (CAMP) included in the 2008 CAP will continue until no
NCSWMR Appendix II constituents have been detected in groundwater above GPS for three
consecutive years.
The current passive LFG control mechanism is a passive system which requires little or no
maintenance. Once the active LFG system is implemented, significantly more operation and
maintenance will be needed, as described in Section 2.3.5. The LFG system will be inspected
regularly to be sure that the system has not been damaged and is operating as designed.
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3.1.4 Short-term Risks that Might be Posed to the Community, Workers, or the Environment
during Implementation of such a Remedy, including Potential Threats to Human Health and the
Environment Associated with Excavation, Transportation, and Redisposal or Containment;
Short-term risk associated with MNA is limited to environmental professionals and/or County
employees participating in MNA groundwater monitoring activities. Specifically, the sampling
and handling of contaminated groundwater from monitoring wells constructed within groundwater
contamination plumes create risk; however, the potential for human exposure to landfill
contaminants by environmental personnel and/or County employees will be low as long as
standard health and safety procedures are followed.
Short-term risks associated with the implementation of the LFG control mechanism include
potential exposure to organic gases, including methane and hydrogen sulfide. The methane could
be vented at possibly explosive concentrations. There may also be physical risks associated with
trenching and construction of the LFG system. Gas monitoring will be performed during
construction activities to insure worker safety. A site-specific health and safety plan (HASP) will
be implemented to insure adherence to OHSA safety standards and related regulations during
construction and other phases of this project.
3.1.5 Time until Full Protection is Achieved;
A schedule for achievement of the final remedial objective (COC levels below the GPS at all points
within the plume beyond the point of compliance) is dependent upon independent factors within
the uppermost aquifer that were measured during the NES activities. Any prediction of a
timeframe for achievement of concentration levels below the GPS at this time would be an estimate
based on available data and professional judgment. Groundwater quality will be monitored in
accordance with the facility’s CAMP, and will be completed when no NCSWMR Appendix II
constituents have been detected in groundwater above GPS for three consecutive years.
3.1.6 Potential for Exposure of Humans and Environmental Receptors to Remaining Wastes,
Considering the Potential Threat to Human Health and the Environment Associated with
Excavation, Transportation, Redisposal, or Containment;
Water quality and LFG monitoring will be performed by environmental personnel trained to
minimize their exposure to COCs by using appropriate personal protective equipment and by
avoiding contact with contaminated groundwater, vapors, and gas.
Wastes associated with implementation of the LFG control mechanism will include soil removed
during trench excavation, which is not expected to be contaminated or to contain any solid waste
material. It will be disposed of on site, possibly as daily cover material. No exposure potential is
anticipated.
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Facility workers do not come in contact with contaminated media during day-to-day landfill
operations. The general public is not expected to come in contact with contaminated media since
access to the contaminated media is restricted.
3.1.7 Long-term Reliability of the Engineering and Institutional Controls
Natural attenuation is a proven remedy for facilities similar to the Johns River Landfill (i.e., a
facility with low contaminant concentrations and low risk associated with the delineated
contamination). In addition, results from the biodegradation screening suggest that natural
attenuation is occurring at a rate that will prevent further off site migration of the delineated
contaminant plume, and will begin reducing concentrations of constituents-of-concern to
concentrations below their respective GPS. Therefore, MNA is considered a reliable remedy to
meet clean-up goals at the facility.
The current control mechanism for LFG is a passive system that requires little or no maintenance
and will continue to intercept gas migrating from the landfill for several decades. It is considered
to have excellent long-term reliability. If the contingency active LFG system is implemented,
more maintenance will be required, and mechanical components of the system may need repair or
replacement every few years; however, active LFG systems have well-established long-term
reliability.
3.1.8 Contingency Plans and Potential need for Replacement of the Remedy.
Replacement of MNA and/or the LFG control mechanism as part of the facility remedy will be
performed upon determining that they are not preventing migration of constituents-of-concern
beyond the property boundaries. This will be determined by monitoring groundwater sampling
locations downgradient of the impacted monitoring wells within the plume of contamination in
accordance with the facility’s CAMP. In the event that monitoring indicates that natural
attenuation is inadequate for controlling the plume, enhanced bioremediation may be implemented
to accelerate the rate of attenuation/mitigation, as described in the 2008 CAP.
If the proposed active LFG system is demonstrated to be ineffective at controlling LFG migration
and reducing LFG impacts to groundwater on the northeast side of the existing landfill, a new
contingency action may be implemented. The new contingency may include installation of
additional gas vents or a gas intercept trench between the active gas vents and the C&D expansion
area, which could them be connected to the active gas extraction system. If LFG is demonstrated
to be a significant source of groundwater impacts for other areas of the landfill away from the
proposed LFG system, the proposed system may be extended, and/or additional vents may be
installed.
3.2 Controlling the Source
According to 15A NCAC 13B.1636(c)(2), the County is required to evaluate the effectiveness of
the remedy in controlling the source to reduce further releases based on consideration of the
following factors.
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3.2.1 The Extent to which Containment Practices will Reduce Further Releases
The closed Johns River MSW landfill is unlined; however, it was closed with a low-permeability
soil cap, which acts as a base to the active C&D landfill. The low-permeability cap is expected to
limit percolation of water through the MSW, therefore limiting leaching of waste constituents into
the groundwater. Furthermore, upon closure, the C&D landfill will also be capped with a cap of
equal or lower permeability. The installation of an LFG vents will not affect generation of
additional LFG by the landfill, but it will prevent it from migrating away from the landfill and it
will reduce LFG impacts to groundwater.
3.2.2 The Extent to which Treatment Technologies may be Used
MNA and Phytoremediation use natural processes to treat releases of solid waste constituents to
the groundwater. The LFG control system will not treat the groundwater directly, but will prevent
or lessen future cross-media impacts to the groundwater by LFG.
3.3 Remedy Implementation
According to 15A NCAC 13B.1636(c)(3), the County is required to evaluate the ease or difficulty
of implementing a potential remedy based on consideration of the following types of factors.
3.3.1 Degree of Difficulty Associated with Constructing the Technology
Installation of the proposed active LFG control mechanism will be a relatively easy and routine
construction project involving purchase and installation of a turn-key GEU, installation of a
condensate sump, and installation of piping to connect the existing passive gas vents to the GEU
and to the condensate sump.
3.3.2 Expected Operational Reliability of the Technologies
Natural attenuation is considered a reliable remedy for facilities that have contaminant plumes
that: 1) have low level concentrations of organic solid waste constituents; 2) are contained within
the facility boundary; 3) are stable or shrinking in size; and/or 4) have low levels of risk. The
contaminant plume at this facility has all of these characteristics; therefore, MNA is a reliable
remedy for reported contamination at the landfill.
The proposed control mechanism for LFG is a passive system that will require little or no
maintenance and will continue to intercept gas migrating from the landfill for several decades. It
is considered to have excellent operational reliability. If the contingency active LFG system is
implemented, more maintenance will be required, and mechanical components of the system may
need repair or replacement every few years; however, active LFG systems have well-established
reliability.
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3.3.3 Need to Coordinate with and Obtain Necessary Approvals and Permits from Other
Agencies;
None of the proposed remediation activities will require approvals or permits from other agencies
at this time.
3.3.4 Availability of Necessary Equipment and Specialists
Natural attenuation processes and LFG control are monitored by readily available laboratory and
field procedures and equipment. The monitoring may be conducted by any properly-trained
environmental field technicians or consultants. Installation of the LFG vents may be accomplished
by any licensed driller a bucket rig, or with an auger rig, for vents outside of waste. If the
contingency active LFG system is implemented, there are several venders who build turn-key
GEUs that will be acceptable for this application, and any construction contracting firm
experienced in trenching and pipe installation will be able to do the installation work.
3.3.5 Available Capacity and Location of Needed Treatment, Storage, and Disposal Services
No treatment, storage, or disposal services are required to implement the proposed corrective
actions.
3.4 Owner/Operator Capability
According to 15A NCAC 13B.1636(c)(2), the County is required to evaluate the practicable
capability of the owner or operator, including a consideration of the technical and economic
capability of the owner/operator, to construct and/or maintain the proposed remedy.
The County anticipates continuing its use of a qualified environmental consulting firm to perform
and/or coordinate implementation of the proposed corrective actions and monitoring and reporting
activities associated with the landfill. In addition, the County has budgeted for additional
monitoring requirements associated with this remedy; therefore, the County is capable of
performing the proposed remedy. The financial assurance mechanism for this work will be or has
been submitted under separate cover.
3.5 Community Concerns
According to 15A NCAC 13B.1636(c)(5), the County is required to evaluate the degree to which
community concerns raised as the result of the public meeting are addressed by the potential
remedy. In accordance with 15A NCAC 13B.1635(4)(d), Burke County held a public meeting on
May 16, 2006 to discuss the results of the ACM. The proposed remedies, including control of
LFG, were discussed in the public meeting. The County did not receive any comments during the
required public meeting and public comment period; therefore, there were no community concerns
to address.
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4.0 WATER QUALITY MONITORING PLAN
Groundwater was formerly monitored in accordance with the September 1996 Water Quality
Monitoring Plan (WQMP), and the Corrective Action Monitoring Plan (CAMP) included in the
2008 CAP. In August 2012, the County submitted a new WQMP as part of the Permit to Construct
Application for the C&D expansion. The 2012 WQMP covers both the existing landfill and the
proposed C&D expansion and replaced the previous WQMP and CAMP. In the 2012 WQMP,
piezometer PZ-38 was designated to be converted to a compliance monitoring well to monitor
Phase 1 of the C&D expansion after it was constructed.
The 2013 CAP Addendum added provisions to monitor and evaluate the effectiveness of the
proposed control of LFG remedy. Under the 2013 CAP addendum, piezometers PZ-36 and PZ-38
were converted to permanent monitoring wells MW-36 and MW-38 to act as performance wells
for the control of LFG remedy for the northeastern part of the existing landfill. MW-38 now plays
a duel role as a compliance well and a performance well. MW-36 and MW-38 are located
between the existing landfill and Phase 1 of the C&D Expansion, within the zone of methane
migration. Groundwater from these two piezometers show GPS exceedances believed to be due to
LFG impacts.
After installation of the passive LFG vents, MW-36 and MW-38 have been sampled semiannually
in conjunction with the routine semiannual water quality sampling, for the COC list, plus dissolved
methane and dissolved carbon dioxide. It was expected that the gas vents would decrease the
LFG impacts to groundwater beneath the northeastern portion of the landfill, and with time, the
concentrations of VOCs and dissolved gases in MW-36 and MW-38 will decrease. Such a
decrease was to be considered evidence of the effectiveness of the passive vents at remediating the
groundwater impacts. If after an extended period of monitoring, no significant decrease in
concentrations of COCs was observed in MW-36 and MW-38, recommendations were to be made
to implement the contingency active LFG remedy.
Figure 2 presents a series of charts showing the concentrations of the constituents of concern in
MW-36 and MW-38 vs. time from February 2013 through December 2016. The charts show
decreasing trends in the concentrations of the COCs since the installation of the gas vents in
November 2013. This constitutes evidence that the remedy is reducing the concentrations of
COCs in MW-36 and MW-38; therefore, the remedy is working effectively as designed.
However, in a letter dated March 27, 2017, the NCDEQ-SWS requested implementation of the
County’s corrective action contingency plans, and asked that the proposed alternate remedy be
implemented.
After implementation of the active gas extraction alternate remedy, the GWMP will remain the
same. MW-36 and MW-38 will continue to be monitored as performance wells for the control of
landfill gas remedy. Continued decreases in the concentrations of VOCs and dissolved gases in
MW-36 and MW-38 will be considered evidence of the effectiveness of the active gas extraction
system at remediating the groundwater impacts.
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5.0 EVALUATION OF EFFECTIVENESS AND REPORT SUBMITTALS
5.1 Physical and Chemical Changes in Aquifer Conditions
Data obtained from the semiannual sampling events, including groundwater elevation and flow,
groundwater field and indicator parameters, and constituent concentrations will be evaluated with
regard to the physical and chemical conditions in the uppermost aquifer at the site. Any significant
changes in the conditions in the aquifer will be reported with recommendations on corrective
actions, changes in the monitoring program, or other appropriate responses.
5.2 Physical and Chemical Changes in Plume Characteristics
Data obtained from semiannual water quality sampling will be used to re-evaluate the risk posed
by the residual plume in accordance with the CAMP included in the 2008 CAP. If COC
concentrations are observed to be less than the established GPS in sentinel wells, no action will be
required, and the routine compliance and corrective action monitoring will continue until the
remedial objective is achieved and the Corrective Action Program is suspended.
Performance wells MW-36 and MW-38 will be sampled semiannually in conjunction with the
routine semiannual water quality sampling for the COC list, plus dissolved methane and dissolved
carbon dioxide. Observed decreases in VOC concentrations and/or decreases in dissolved methane
and carbon dioxide will constitute evidence that the control of LFG remedy is effectively
controlling gas migration and reducing gas impacts to groundwater. Increases in concentrations
of VOCs or methane and carbon dioxide will be considered evidence that the remedy is not
effective.
5.3 Refining the Site Conceptual Model
Any new information that comes to the attention of the facility, either from the data collected on
site or other sources, which impacts the site conceptual model will be reported and evaluated. This
includes data on site or regional geology, hydrogeology, or other aspects of the site conceptual
model. The site conceptual model will be refined in response to the new information as needed
and appropriate.
5.4 Evaluation of Remedy Effectiveness
The MNA plus phytoremediation remedy will be evaluated based on analytical results obtained
from the performance wells MW-11, MW-12, MW-16S, and MW-17, and sentinel wells MW-18
and MW-19, in accordance with the CAMP. Data obtained from these wells will be tracked using
moving average concentration trend graphs to evaluate the effectiveness of the MNA remedy. The
concentration trend graphs will provide a visual means for evaluating the effectiveness of the MNA
plus phytoremediation remedy. In addition, evaluation of MNA indicator parameters will be used
to evaluate the natural attenuation process.
Evaluation of the control of LFG remedy will be based primarily on semiannual sampling of
MW-36 and MW-38 as performance wells. Observed decreases in VOC concentrations and/or
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decreases in dissolved methane and carbon dioxide in PZ-36 and PZ-38 will constitute evidence
that the control of LFG remedy is effectively controlling gas migration and reducing gas impacts
to groundwater. Increases in concentrations of VOCs or methane and carbon dioxide will be
considered evidence that the control of LFG remedy is not effective.
In addition, methane, carbon dioxide, and oxygen concentrations will be monitored at the existing
permanent and temporary gas probes in the vicinity of the passive gas vent system. This will
include GP-2S, GP-2M, & GP-2D, TGP-1, TGP-2, TGP-3, TGP-4, TGP-6, TGP-7, and TGP-9.
These probes will be monitored prior to installation of the passive gas vents, approximately one
month after installation of the gas vents, and quarterly after that. The temporary gas vents will be
monitored quarterly until they need to be abandoned for construction of the C&D landfill
expansion, or until the NCDEQ agrees that they no longer need to be monitored. The LFG
monitoring data will be used to supplement the groundwater data in evaluation of the effectiveness
of the passive vent remedy.
The data from the two performance wells (MW-36 and MW-38) will be evaluated to determine
the effectiveness of the passive vent system in the CAER for the preceding CAER period. If the
CAER concludes that the control of LFG remedy is not effectively controlling gas migration and
reducing gas impacts to groundwater, the CAER may recommend modifications to the existing
remedy to improve its effectiveness. For example, the CAER may recommend hooking gas vents
GV-8 through GV-11 to the active system, or it may recommend installation of additional vents
or gas intercept trenches. If necessary, the CAER may recommend that new or additional remedies
be evaluated, and if appropriate, implemented.
5.5 Corrective Action Program Reporting
The routine compliance monitoring for this site shall continue to be reported semiannually in
accordance with NCSWMR §1634 (Assessment Monitoring Program) and the WQMP and CAMP
for the facility. The additional data gathered for the performance wells and sentinel will be
included in the semiannual Water Quality Monitoring Reports (WQMRs).
In addition to the semiannual WQMRs, the performance criteria for the groundwater corrective
action remedies will be evaluated and presented to the NCDEQ every five years in a Corrective
Action Evaluation Report (CAER). The first CAER for the facility was submitted to NCDEQ in
May 2011 and covered the MNA and phytoremediation remedies. The second CAER for the
facility was submitted to NCDEQ in April 2016 and covered the MNA and phytoremediation
remedies as well as the passive control of LFG remedy. The April 2016 CAER was approved by
the NCDEQ in a letter dated April 19, 2016. The next CAER is due after the second semiannual
sampling event of 2020 and will also include evaluation of the active control of LFG remedy.
The CAER may provide recommended modifications to the CAP, recommendations to initiate
alternative remedies, recommendations to suspend CAP monitoring, or other actions, as
appropriate. The CAER shall include, at a minimum, a summary report, data tables, laboratory
reports (if not previously submitted), groundwater elevation contour maps, isoconcentration
contour maps, cross sections showing groundwater elevations and isoconcentration contours, an
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evaluation of the effectiveness of the corrective action, and graphs illustrating trends of key
indicator parameters and/or constituents from key/representative monitoring stations.
In the event that a GPS exceedance is confirmed in one or more sentinel well samples based on
routine MNA monitoring results pursuant to the CAP, Burke County will notify NCDEQ in writing
of: (1) the confirmed exceedance; and (2) the County’s intended course of action to address the
GPS exceedance.
After the remedial objectives of the CAP have been obtained for the required time period, Burke
County will notify the NCDEQ of its intent to suspend the monitoring requirements of the CAP
and of its intent to revert to Assessment or Detection Monitoring, as appropriate, in accordance
with the NCSWRM and the facility’s WQMP.
6.0 SCHEDULE AND MAINTENANCE
6.1 Schedule Considerations
According to 15A NCAC 13B.1636(d), the owner/operator is required to specify, as part of the
selected remedy, a schedule for initiating and completing remedial activities. Such a schedule
shall require the initiation of remedial activities within a reasonable period of time, taking into
consideration the factors set forth in §.1637(d).
6.2 Timeline
6.2.1 Monitoring Schedule
Upon considering the factors set forth in §.1637(d), and based on the results of the natural
attenuation scoring results, natural attenuation is occurring at a rate that will prevent the migration
of solid waste constituents beyond the landfill property boundary at concentrations exceeding the
GPS. This portion of the proposed remedy is already in place at the landfill. Monitoring and
reporting will proceed semiannually in accordance with the CAP and the CAMP. Similarly,
monitoring for the passive control of LFG remedy has been ongoing in accordance with the 2013
CAP Addendum, and this revised addendum does not add any additional monitoring requirements.
6.2.2 Active GEU Implementation Schedule
The following timeline is proposed for implementation of the active control of LFG remedy:
Activity Schedule
Prepare construction plans and bid documents for
purchase and installation of the active GEU
system.
Within 60 days of approval of
the CAP Addendum by the
NCDEQ
Obtain approval of Burke County Board of
Commissioners to go to bid
Within 120 days of approval of
the CAP Addendum by the
NCDEQ
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Obtain bids for purchase and installation of the gas
extraction system
Within 45 days of Board
approval
Select contractor, negotiate contract, and get
Board of Commissioners' approval of the contract Within 45 days of obtaining bids
Begin construction/installation of the system Within 60 days of Board
Approval
Complete construction/installation of the system
and bring online
Within 45 days of beginning
Construction
Prepare Gas Extraction System Construction
Report with construction drawings and
specifications and submit to NCDEQ
Within 30 days of completing
Construction
6.3 Operations and Maintenance (O&M)
The facility shall establish a site-specific, routine inspection schedule, the frequency of which shall
be appropriate for the maintenance requirements of the monitoring network and the LFG control
system. Inspection results shall be recorded and placed in the facility’s Operating Record.
6.4 Safeguards and Safety
The facility shall establish a site-specific health and safety guidelines for the monitoring system
and monitoring activities, including installation of gas vents, sampling of monitoring wells, and
monitoring of LFG. The guidelines shall include appropriate security for the monitoring wells and
vents, such as locked protective casings and/or access restrictions, as well as descriptions of
appropriate personal protective equipment for routine and anticipated activities.
6.5 Modification of Corrective Action or Schedule
Any requests for modifications of the approved corrective action and/or the implementation
schedule must be submitted in writing to the Solid Waste Section, and the requested modifications
may not be implemented until approved in writing by the Division of Waste Management.
7.0 FINANCIAL ASSURANCE
Burke County’s financial assurance information has or will be submitted under separate cover.
8.0 COMPLETION OF CORRECTIVE ACTION
Once concentrations of the constituents of concern are below established GPS at and beyond the
relevant point of compliance as defined in 15A NCAC 13B.1631(a)(2) for three consecutive years,
the corrective action will be considered complete. If the facility is in the post-closure care period
at the end of the Corrective Action Program, Assessment Monitoring will be continued. After the
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remedial objectives of the CAP have been obtained for the required time period, Burke County
will notify the DEQ of its intent to suspend the monitoring requirements of the CAP and of its
intent to revert to Assessment or Detection Monitoring, as appropriate, as defined in the facility’s
Transition Plan and WQMP. In accordance with 15A NCAC 13B.1637(f), a certification that
corrective action has been completed in compliance with the requirements of 15A NCAC
13B.1637(e) will be submitted to NCDEQ.
9.0 REFERENCES
The references cited below were used to prepare this document and may or may not be cited in
the text of this report.
Allen, M.R., Braithwaite, A., and Hills, C.C. (1997). Trace Organic Compounds in Landfill Gas
at Seven U.K. Waste Disposal Sites. Environmental Science and Technology. v. 31, p.
1054-1061.
Cowie, S. (2004). Emission of Non-methane Organic Compounds (NMOCs) and hazardous air
Pollutants (HAPs) from Decomposing Refuse and Individual Waste Components and
Under Different Conditions. Master’s Thesis, North Carolina State University.
Deisper, A. and Stegmann, R. (1994). The Origin and Fate of Volatile Trace Components in
Municipal Solid Waste Landfills. Waste Management & Research. v. 12, p. 129-139.
Joyce Engineering, Inc. (JEI), 1994. Transition Plan, Johns River Waste Management Facility.
April 1994.
JEI, 1996. Water Quality Monitoring Plan, Johns River Waste Management Facility.
September, 1996.
JEI, 1998. Water Quality Assessment Plan, Johns River Waste Management Facility. May
1998.
JEI, 2000. Water Quality Assessment Report, Johns River Waste Management Facility. January
2000.
JEI, 2004. Update on Groundwater Assessment Activities, Johns River Waste Management
Facility. October 2004.
JEI, 2005a. Assessment of Corrective Measures Report, Johns River Waste Management
Facility. February 2005.
JEI, 2005b. Quantitative Risk Assessment, Johns River Waste Management Facility. February
2005.
JEI, 2008. Corrective Action Plan, Johns River Waste Management Facility. June 2008.
Addendum to Corrective Action Plan Joyce Engineering
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JEI, 2011. Second Semiannual Groundwater Monitoring Report of 2010 and
Corrective Action Evaluation Report, Johns River Waste Management Facility. May 2011.
JEI, 2012. C&D Landfill Expansion - Volume 2: Permit to Construct, Johns River Waste
Management Facility. August 2012.
JEI, 2013a. 2012 Landfill Gas Delineation Study, Johns River Waste Management Facility.
January 2013.
JEI, 2013b. Piezometer Sampling Report, Johns River Waste Management Facility. April 2013.
North Carolina Department of Environment, Health, and Natural Resources (NC-DENR), 1997
& 2011. North Carolina Solid Waste Management Rules. 15 NCAC 13B. January 1997,
Revised April 2011.
NC-DENR, 2007. North Carolina Solid Waste Section Guidelines for Corrective Action at Solid
Waste Management Facilities. March 2007.
TABLES
Table 1: Detected VOCs ‐ February and July 2013 Piezometer Sampling EventsCONSTITUENT PZ‐30S PZ‐31 PZ‐34 PZ‐35 PZ‐36 PZ‐37PZ‐38 (MW‐23)UNITS MDL SWSLNC2L / *GWPSSample Date:2/18/13 7/18/13 7/19/13 2/18/13 2/18/13 2/18/13 2/18/131,1‐Dichloroethane ND 11.3 ND ND7.9ND9.1µg/L 0.32 5 61,2‐Dichloroethane ND 0.54 J ND ND1ND 0.59 J µg/L 0.12 1 0.41,2‐Dichlorobenzene ND 0.61 J ND ND 0.44 J ND ND µg/L 0.3 5 201,4‐Dichlorobenzene ND 6.5 ND ND18ND7.8µg/L 0.33 1 64‐Methyl‐2‐pentanone (MIBK) ND ND ND ND 2.1 J ND ND µg/L 0.33 100 560*Acetone ND ND ND ND 19.8 J ND ND µg/L 10 100 6000Benzene ND 7.6 ND ND8ND3.8µg/L 0.25 1 1Chlorobenzene ND 0.48 J ND ND 0.76 J ND 0.38 J µg/L 0.23 3 50Chloroethane ND ND ND ND 1.1 J ND ND µg/L 0.54 10 3000cis‐1,2‐Dichloroethene ND 19.3 ND ND 21 ND 15.6 µg/L 0.19 5 70Ethylbenzene ND 0.94 J ND ND 23.2 ND 1.4 µg/L 0.3 1 600Methylene Chloride ND 16.4 ND ND17.9ND ND µg/L 0.97 1 5Tetrachloroethene ND 7.8 ND ND5.5ND ND µg/L 0.46 1 0.7Toluene ND 1.5 ND ND 44.1 ND 0.77 J µg/L 0.26 1 600Trichloroethene ND 5.8 ND ND3.6ND 2.7 µg/L 0.47 1 3Trichlorofluoromethane ND 0.89 J ND ND 0.65 J ND ND µg/L 0.2 1 2000Vinyl Chloride ND ND ND ND1.2ND ND µg/L 0.62 1 0.03Xylene (Total) ND 92.5 ND ND 295 ND 1.7 J µg/L 0.66 5 500Total VOCs:ND172.16ND ND471.25ND43.84µg/LMDL = Method Detection Limit. SWSL = Solid Waste SWSL = Solid Waste Section Reporting Limit.NC2L = Groundwater Standard from 15 NCAC 2L.0202. *GWPS = Solid Wast*GWPS = Solid Waste Section Groundwater Protection Standard for constituent with no NC2L.ND = Not detected above the MDL. J = Estimated concenJ = Estimated concentration below the SWSL. Shaded values indicate exccedance of the NC2L or GWPS.John's River Landfill, Burke Co., NCJoyce Engineering
Table 2: Detected VOCs ‐ December 2012 Compliance SamplingBackgroundSampleConstituent NC2L /GWPS MW‐20 MW‐10 MW‐11 MW‐12 MW‐13 MW‐16S DateBenzene 1 ND 0.830 J 4.10 2.80 14.9 1.60 12/4‐5/2013Chlorobenzene 50 ND ND 0.700 J 0.620 J 0.540 J 0.650 J 12/4‐5/2013Chloroethane 3,000 ND ND ND 1.80 J 2.70 J 1.90 J 12/4‐5/2013Chloroform 70 ND ND ND ND 0.140 J ND 12/4‐5/20131,2‐Dichlorobenzene 20 ND ND 0.390 J ND 0.570 J ND 12/4‐5/20131,4‐Dichlorobenzene 6 ND ND 15.0 4.40 9.70 6.00 12/4‐5/20131,2‐Dichloroethane 0.4 ND ND 0.670 J 0.790 J 1.70 1.30 12/4‐5/20131,1‐Dichloroethylene 7 ND ND ND 0.660 J 0.580 J ND 12/4‐5/2013cis‐1,2‐Dichloroethylene 70 ND 3.30 J 9.10 9.40 25.4 6.60 12/4‐5/20131,2‐Dichloropropane 0.6 ND ND ND 0.370 J 0.650 J 0.590 J 12/4‐5/2013Ethylbenzene 600 ND ND 0.320 J 1.10 2.10 ND 12/4‐5/2013Methylene Chloride 5 ND ND ND ND 174 ND 12/4‐5/2013Tetrachloroethylene 0.7 ND ND ND ND 7.30 ND 12/4‐5/2013Toluene 600 ND ND ND 0.330 J 10.7 0.450 J 12/4‐5/2013Trichlorofluoromethane 2000 ND ND ND ND 0.650 J ND 12/4‐5/2013Trichloroethylene 3 ND 0.530 J 2.30 3.30 11.2 0.670 J 12/4‐5/2013Xylenes (total) 500 ND ND ND 2.4 J J 43.6 ND 12/4‐5/2013Naphthalene 21 ND ND ND ND 1.50 J ND 12/4‐5/2013Total VOCs 4.66 33 26 308 20Tetrahydrofuran NE ND ND ND ND 6.90 ND12/4‐5/2013Total Organic Carbon NE ND NM 13,100 8,750 NM 16,00012/4‐5/2013Methane NE ND NM 2,070 2,050 NM 4,91012/4‐5/2013Concentrations in µg/L. J = Estimated Concentration below the SWSL. ND = Not detected above the method detection Limit.Downgradient WellsJohn's River Landfill, Burke Co., NCJoyce Engineering
FIGURES
FIGURE 2: Constituents of Concern in MW‐36 and MW‐38 vs. Time
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
8.0
9.0
10.0
Feb‐13Jun‐13Oct‐13Feb‐14Jun‐14Oct‐14Feb‐15Jun‐15Oct‐15Feb‐16Jun‐16Oct‐16µg/lBenzene
MW‐36
MW‐38
0.0
2.0
4.0
6.0
8.0
10.0
12.0
14.0
16.0
18.0
20.0
Feb‐13May‐13Aug‐13Nov‐13Feb‐14May‐14Aug‐14Nov‐14Feb‐15May‐15Aug‐15Nov‐15Feb‐16May‐16Aug‐16Nov‐16µg/l1,4‐DCB
MW‐36
MW‐38
0.0
2.0
4.0
6.0
8.0
10.0
12.0
14.0
Feb‐13Jun‐13Oct‐13Feb‐14Jun‐14Oct‐14Feb‐15Jun‐15Oct‐15Feb‐16Jun‐16Oct‐16µg/l1,1‐DCA
MW‐36
MW‐38
0.0
0.2
0.4
0.6
0.8
1.0
1.2
Feb‐13May‐13Aug‐13Nov‐13Feb‐14May‐14Aug‐14Nov‐14Feb‐15May‐15Aug‐15Nov‐15Feb‐16May‐16Aug‐16Nov‐16µg/l1,2‐DCA
MW‐36
MW‐38
0.0
5.0
10.0
15.0
20.0
25.0
30.0
Feb‐13Jun‐13Oct‐13Feb‐14Jun‐14Oct‐14Feb‐15Jun‐15Oct‐15Feb‐16Jun‐16Oct‐16µg/lMethylene Chloride
MW‐36
MW‐38
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
8.0
9.0
Feb‐13May‐13Aug‐13Nov‐13Feb‐14May‐14Aug‐14Nov‐14Feb‐15May‐15Aug‐15Nov‐15Feb‐16May‐16Aug‐16Nov‐16µg/lPCE
MW‐36
MW‐38
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
Feb‐13Jun‐13Oct‐13Feb‐14Jun‐14Oct‐14Feb‐15Jun‐15Oct‐15Feb‐16Jun‐16Oct‐16µg/lTCE
MW‐36
MW‐38
0.0
0.2
0.4
0.6
0.8
1.0
1.2
1.4
Feb‐13May‐13Aug‐13Nov‐13Feb‐14May‐14Aug‐14Nov‐14Feb‐15May‐15Aug‐15Nov‐15Feb‐16May‐16Aug‐16Nov‐16µg/lVinyl Chloride
MW‐36
MW‐38
0.0
10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0
Feb‐13Apr‐13Jun‐13Aug‐13Oct‐13Dec‐13Feb‐14Apr‐14Jun‐14Aug‐14Oct‐14Dec‐14Feb‐15Apr‐15Jun‐15Aug‐15Oct‐15Dec‐15Feb‐16Apr‐16Jun‐16Aug‐16Oct‐16Dec‐16µg/lSum of COCs
MW‐36
MW‐38
Burke Co. ‐ Johns River Waste Management Facility, Permit No. 12‐03 Joyce Engineering
DRAWINGS
SMP-5 SURFACE MONITORING POINT LOCATION AND IDENTIFICATION
NOT MEASURED
LEGEND
PROPERTY LINE
EXISTING ROAD
EXISTING 25' TOPOGRAPHIC CONTOUR
EXISTING 2' TOPOGRAPHIC CONTOUR
GROUNDWATER SURFACE CONTOUR [FEET
ABOVE MEAN SEA LEVEL (AMSL)]
APPROXIMATE LIMITS OF WASTE
CENTERLINE OF STREAM
GAS PROBE LOCATION AND IDENTIFICATION
PIEZOMETER LOCATION AND IDENTIFICATION
COMPLIANCE WELL LOCATION AND IDENTIFICATION WITH STATIC
WATER LEVEL ELEVATION (FEET AMSL)
(NM)
GP
1050
1020
MW-13
1009.52
PZ-9D
GMP-3
TOPOGRAPHIC CONTOUR INTERVAL = 2 AND 10 FEET.
GROUNDWATER SURFACE CONTOUR INTERVAL = 10 FEET.
STATIC WATER LEVELS WERE MEASURED ON DECEMBER 4, 2012.
GROUNDWATER CONTOURS BASED ON LINEAR INTERPOLATION BETWEEN AND
EXTRAPOLATION FROM KNOWN DATA, TOPOGRAPHIC CONTOURS, AND KNOWN
FIELD CONDITIONS.
MW-16D GROUNDWATER ELEVATION WAS NOT USED IN CALCULATING
GROUNDWATER CONTOURS.
NOTES
EXISTING 5' TOPOGRAPHIC CONTOUR
EXISTING 10' TOPOGRAPHIC CONTOUR1080
T1 TEMPORARY WELL
APPROXIMATE LOCATION OF SPRING HEAD
1.
2.
3.
4.
5.
JE-0020 CONTROL POINT LOCATION AND IDENTIFICATION
SENTINEL WELL LOCATION AND IDENTIFICATION WITH STATIC
WATER LEVEL ELEVATION (FEET AMSL)
MW-18
GROUNDWATER FLOW PATHWAY USED TO
CALCULATE HYDRAULIC GRADIENT
i 1
SEGMENT USED FOR GRADIENT CALCULATION
MW-9 ABANDONED OR UNUSED MONITORING WELL
NM
1
0
1
0
1130
113
0
113
0
10
6
0
107010
8
0
107010601050
1040
10
3
0 10201060
1050
1040103010201010
1020
10
4
0
10
3
0
10
2
0
10101010100010
7
0
10
5
0
106
0 11001110
1090
1080109011001130
1110
11201100 1110
1120
1110
1120
1110
1100
1090
108010701
0
1
0
1020
1030
1040
1050
1060
1070
1080
1090
1050
1060107010601050 104010301020101
0
10
3
0
10
5
0
10
4
0
102
0
10
6
0108010701
0
6
0
10
50
10401020103010701060105010401020103010
5
0
105010601070108
0
1
0
9
0
1
1
0
0
1
1
1
0
1
1
2
0
1
1
3
0
1
1
4
0
1
1
5
0
1
1
6
0
1
1
5
0
1
1
4
0
1
1
3
0
1
1
2
0
1
1
1
0
1
1
0
0
1
0
9
0
1
0
8
0
1
1
7
0
11
1
0
10
9
0
108
01070 10601050 1040E 1213000E 1214000E 1215000E 1216000E 12170001050
1040
1030
1020
1010
10
0
01060105010401030
10201010
1000
JE-0019
HV-1
AS-10
HV-2
JE-0020
JE-0018
JE-0023
JE-0024
GMP-2
GMP-3
GMP-41070
1070i1
i2
i 3
i 4
1060
(ABANDONED)
PZ-2S
(ABANDONED)
PZ-2D
(NM)
PZ-23
(NM)
PZ-15
(NM)
PZ-22D(NM)
PZ-22S
(NM)
PZ-16D
(NM)
PZ-16S
(NM)
PZ-12
(NM)PZ-27
(NM)
PZ-14
(NM)PZ-13
(ND)PZ-9D
(NM)
PZ-9S
GP-2
1009.52
MW-13
SMP-6
993.46
MW-12
992.94
MW-11
993.43
MW-16D 992.05
MW-16S
999.04
MW-10
SMP-5
(ABANDONED)
MW-9
(NM)MW-14
(NM)MW-15S
(NM)
MW-15D
(NM)MW-8
(NM)
MW-1
(FORMERLY PZ-4)
MW-20
NMMW-17
SHOOTING
RANGE
MULCHING
AREA
L
O
W
E
R
C
R
E
E
K
JOH
N
S
R
I
V
E
R
CATAW
B
A
R
I
V
E
R
PROTECTED AREA
PROTECTED AREA
WETLAND
WETLAND
EXISTING TRAIL
EXISTING SEDIMENT BASIN
APPROX. LIMIT OF
EXISTING WASTE
TRANSFER FACILITY
BOUNDARY
EXISTING
SEDIMENT
BASIN
T1
T2
T3 T4
T5
(NM)
(NM)(NM)
(NM)
EXISTING WASTE
DISPOSAL AREA
(NM)
CURRENT BACKGROUND WELL
FORMER BACKGROUND WELL
MW-18 MW-19
NMNM
1053.51
OFFICE
AND
GARAGE
1040105010701080109011001060PROJECT NO.APPROVEDCHECKEDDRAWNDESIGNEDDATEDATEREVISIONS AND RECORD OF ISSUEBYNOAPPCKSCALE All rights reserved.Ó Joyce Engineering, Inc.DRAWING NO.L:\Burke County\2013 CORRECTIVE ACTION\SHEET SET\1 GW-EVENT 12-12.DWG Layout=SHT 012211 W. MEADOWVIEW ROADGREENSBORO, NC 27407PHONE: (336) 323-00920
(FEET)
GRAPHIC SCALE
400200100
277.1301.12JOHNS RIVER, WASTE MANAGEMENT FACILITYBURKE COUNTY, NORTH CAROLINA20181
AS NOTEDGROUNDWATER SURFACE MAPDECEMBER 4, 2012PERMIT NO. 12-03AACRWHAACVB1/16/131/15/18RESUBMITTED FOR CAP ADDENDUM #2
JOHNS
R
IVER
CATA
W
B
A
RI
V
E
R (
L
A
K
E
R
H
O
D
HI
S
S)~STREAM S-2
WETLAND
W1
EXISTING
SEDIMENT BASIN
PROTECTED AREA
STREAM S-4
WETLAND W3
CEMETERY
OFFICE AND
GARAGE
STREAM S-3
100 YR FLOOD LIMIT
ELEV. 1005.0
EXISTING LANDFILL
DISPOSAL AREA
EXISTING
WASTE LIMITS
SCALEHOUSE~PROTECTED AREA
SHOOTING
RANGE
JE-0022
JE-0018
JE-0024
JE-0020
JE-0019
AS-10
HV-1
JE-0023
CARDBOARD
BATTERIES
CARDBOARD
RECYCLE DROP OFF
OIL
WHITE GOODS
MULCH AND
YARD WASTE
MULCH AND
PALLETS
WHITE GOODS
FACILITY BOUNDARY /
PROPERTY LINE
(TYP WEST AND SOUTH EDGES)
MW-10
MW-11
MW-12
MW-15D
MW-15S
MW-9
AB
MW-1
MW-2
PZ-6PZ-5
PZ-21
PZ-20
NLEPZ-22D
PZ-22S
PZ-15
NLE
PZ-16D
PZ-16S
PZ-8S
PZ-8DPZ-19
PZ-23
NLE
PZ-12
PZ-17
PZ-14
PZ-13 PZ-18
NLE
PZ-9S
PZ-1
PZ-3
NLE
PZ-24 PZ-11
PZ-10
MW-7
MW-6
AB
MW-3
GMP-7A
GP-3
GMP-4
GMP-3
GMP-2
GP-2
MW-16S
MW-16D
MW-17
PZ-37
PZ-33
PZ-30S
PZ-30D
PZ-31
PZ-34MW-22 PZ-35
MW-23
PZ-2S
NLE
PZ-2D
NLE
PZ-27
MW-20
PZ-7
PZ-25
MW-14
PZ-32
FACILITY LIMIT
CEMETERY
PROPERTY
BUFFER
(TYP)10301050107010901050
1070
1090
1110
1130
1150
1050
1
0
4
0
1
0
2
0
1050
1
0
6
0
107
0
1
0
8
01120
10501030103010
7
0
MW-19MW-18
FUTURE SAND
DREDGING FACILITY
PHASE 1
5.3 AC PHASE 2
5.7 AC
PHASE 3
4.0 AC
PHASE 4
4.0 AC PHASE 5
4.7 AC
PHASE 6
4.9 AC
PHASE 8
4.2 AC
PHASE 7
4.2 AC
200'-0"
STREAM BUFFER 50'-0"
STREAM
S1
BORROW AREA
TRANSFER
STATION
WETLAND
W2
PROPOSED
WASTE LIMIT
GP-4
MW-13
PZ-9D
HV-2
MW-8
GP-1
0%
5%
10%
20%
30%
40%
50%
60%
TGP-6
11.1%TGP-8
0.0%
TGP-2
22.3%
TGP-116.3%
TGP-3
8.3%
TGP-434.2%
(PZ-36)
44.3%
0.1%
0.1%
(PZ-38)
48.2%
S=60.6%
I=60.2%
D=60.4%
0.5%
TGP-7
0.0%
GP-5
TGP-5
0.1%0%5%10%20%30%40%50%19.9%
TGP-9
5.99%60%TGP-10
0.0%
0
(FEET)
GRAPHIC SCALE
400200100
NOTE:
CONTOURS REPRESENT ISOCONCENTRATIONS OF METHANE GAS
IN THE SUBSURFACE IN PERCENT BY VOLUME. CONTOURS BASED ON
NOVEMBER 30, 2012 MONITORING DATA.2211 W. MEADOWVIEW ROADGREENSBORO, NC 27407PHONE: (336) 323-0092NC CORP LIC: C-0782PROJECT NO.APPROVEDCHECKEDDRAWNDESIGNEDDATEDATEREVISIONS AND RECORD OF ISSUEBYNOAPPCKSCALE All rights reserved.Ó Joyce Engineering, Inc.DRAWING NO.L:\Burke County\2013 CORRECTIVE ACTION\SHEET SET\2 LANDFILL GAS DELINEATION STUDY.dwg Layout=Layout1277.1301.12JOHNS RIVER, WASTE MANAGEMENT FACILITYBURKE COUNTY, NORTH CAROLINA20182
AS NOTEDLANDFILL GAS DELINEATION STUDYNOVEMBER 29 - 30 2012GVBRWHGVBGVB07/31/131/15/18RESUBMITTED FOR CAP ADDENDUM #2
JOHNS
R
IVER
CATA
W
B
A
RI
V
E
R (
L
A
K
E
R
H
O
D
HI
S
S
)~STREAM S-2
WETLAND W1
EXISTING
SEDIMENT BASIN
PROTECTED AREA
STREAM S-4
WETLAND W3
CEMETERY
OFFICE AND
GARAGE
STREAM S-3
100 YR FLOOD LIMIT
ELEV. 1005.0
EXISTING LANDFILL
DISPOSAL AREA
APPROXIMATE
EXISTING
WASTE LIMITS
SCALEHOUSE~PROTECTED AREA
SHOOTING
RANGE
CARDBOARD
BATTERIES
CARDBOARD
RECYCLE DROP OFF
OIL
WHITE GOODS
MULCH AND
YARD WASTE
MULCH AND
PALLETS
WHITE GOODS
FACILITY BOUNDARY /
PROPERTY LINE (TYP
WEST AND SOUTH EDGES)
MW-10
4.66
MW-11
33
MW-12
26
MW-13
308
MW-15D
MW-9
AB
MW-1
MW-2
PZ-6PZ-5
PZ-21
PZ-20
NLEPZ-22D
PZ-22S
PZ-15
NLE
PZ-16D
PZ-16S
PZ-8S
PZ-8DPZ-19
PZ-23
NLE
PZ-12
PZ-17
PZ-14
PZ-13 PZ-18
NLE
PZ-9D
PZ-9S
PZ-1
PZ-3
NLE
PZ-24 PZ-11
PZ-10
PZ-26
MW-7
MW-6
AB
MW-3
GMP-7A
GP-1 GP-3
GMP-4
GMP-3
GMP-2
GP-2
MW-16S
20
MW-16D
ND
MW-17
PZ-37
ND
PZ-33
PZ-30S
ND
PZ-30D
PZ-34
ND
PZ-36
471.25 PZ-35
ND
PZ-38
43.84
PZ-2S
NLE
PZ-2D
NLE
PZ-27
MW-20
ND
PZ-7
PZ-25
MW-14
PZ-32
FACILITY LIMIT
CEMETERY
MW-19
.19J - 5/13
MW-18
.16J-5/13
FUTURE SAND
DREDGING FACILITY
PHASE 1
5.3 AC PHASE 2
5.7 AC
PHASE 3
4.0 AC
PHASE 4
4.0 AC
PHASE 5
4.7 AC
PHASE 6
4.9 AC
PHASE 8
4.2 AC
PHASE 7
4.2 AC
STREAM S1
TRANSFER
STATION
WETLAND W2
PROPOSED
WASTE LIMIT
0+001+002+003+004+005+006+007+008+009+0010+0011+0012+0013+0014+0015+0016+0017+0018+0
0
19+0
0
20+0
0 21+0022+0023+0024+0025+0026+0027+0028+0029+00ND
100200300400MW-15S
MW-8
PZ-31
172.16
0
(FEET)
GRAPHIC SCALE
400200100AB = ABANDONED
NLE = NO LONGER EXISTING
(PRESUMED DESTROYED)2211 W. MEADOWVIEW ROADGREENSBORO, NC 27407PHONE: (336) 323-0092NC CORP LIC: C-0782PROJECT NO.APPROVEDCHECKEDDRAWNDESIGNEDDATEDATEREVISIONS AND RECORD OF ISSUEBYNOAPPCKSCALE All rights reserved.Ó Joyce Engineering, Inc.DRAWING NO.L:\Burke County\2013 CORRECTIVE ACTION\SHEET SET\3 AND 4 TOTAL VOC MAP AND PROFILE.dwg Layout=PROFILE A-A277.1301.12JOHN'S RIVER WASTE MANAGEMENT FACILITYBURKE COUNTY, NORTH CAROLINA20183
AS SHOWNTOTAL VOCISOCONCENTRATION MAPGVBRWHGVBGVB06.26.13VOC CONCENTRATIONS IN ug/L FROM
THE FOLLOWING DATES:
5/30/12 FOR MW-18 AND MW-19
12/5/12 FOR MW-10, MW-11, MW-12, MW-13,
MW-16S, MW-16D, AND MW-20
2/18/13 FOR PZ-30S, PZ-35, PZ-36, PZ-37 AND PZ-28 1/15/18RESUBMITTED FOR CAP ADDENDUM #2
PROFILE A-A
980
990
1000
1010
1020
1030
1040
1050
1060
1070
1080
1090
1100
1110
1120
1130
1140
1150
1160
1170
1180
980
990
1000
1010
1020
1030
1040
1050
1060
1070
1080
1090
1100
1110
1120
1130
1140
1150
1160
1170
1180
0+00 1+00 2+00 3+00 4+00 5+00 6+00 7+00 8+00 9+00 10+00 11+00 12+00 13+00 14+00 15+00 16+00 17+00 18+00 19+00 20+00 21+00 22+00 23+00 24+00 25+00 26+00 27+00 28+00 29+00
MW-10
PZ-36
PZ-31 PZ-30S PZ-30D
MW-20
GROUND WATER
BEDROCK
SCREENED INTERVAL (TYP)
PROPOSED PHASE 1 C & D EXPANSION LIMITS
EDGE OF WASTE
EDGE OF WASTE
ESTIMA
T
E
D
B
A
S
E
O
F
W
A
S
T
E
4.66
172.16
ND
471.25
400
300
100
ND
200
ND
AB = ABANDONED
NLE = NO LONGER EXISTING
(PRESUMED DESTROYED)2211 W. MEADOWVIEW ROADGREENSBORO, NC 27407PHONE: (336) 323-0092NC CORP LIC: C-0782PROJECT NO.APPROVEDCHECKEDDRAWNDESIGNEDDATEDATEREVISIONS AND RECORD OF ISSUEBYNOAPPCKSCALE All rights reserved.Ó Joyce Engineering, Inc.DRAWING NO.L:\Burke County\2013 CORRECTIVE ACTION\SHEET SET\3 AND 4 TOTAL VOC MAP AND PROFILE.dwg Layout=TOTAL VOC277.1301.12JOHN'S RIVER WASTE MANAGEMENT FACILITYBURKE COUNTY, NORTH CAROLINA20184
AS SHOWNTOTAL VOCPROFILE A-AGVBRWHGVBGVB06.26.130
(FEET)
GRAPHIC SCALE
0(FEET)VERTICAL
EXAGGERATION =
50 100 200
10
20
40
5:1 1/15/18RESUBMITTED FOR CAP ADDENDUM #2
PZ-34
1090
CLOSED LANDFILL
HV-1
MW-15D
MW-15S
MW-9
PZ-15
PZ-23
GP-2
MW-17 PZ-30S
PZ-30D
PZ-31
MW-22
PZ-35
MW-23
PHASE 1
5.3 AC
PHASE 2
5.7 AC
GP-4
MW-13
TGP-6
11.1%
TGP-8
0.0%
(PZ-36)
44.3%
0.1%
0.1%
(PZ-38)
48.2%
S=60.6%
I=60.2%
D=60.4%
0.5%
TGP-7
0.0%
19.9%
TGP-9
5.99%
CLEANOUT C
5
APPROXIMATE
LOCATION OF GAS
EXTRACTION
BLOWER SKID
A6
CONVERT EXISTING
PASSIVE GAS VENT
TO ACTIVE (TYP. OF 7)
A
5
8" HDPE GAS
PIPE
B
5
TGP-2
22.3%
TGP-1
16.3%
TGP-5
0.1%
4" HDPE GASLATERAL (TYP.)B
5
CONDENSATE
COLLECTION
B
6
GV-01
GV-02
GV-03
GV-04
GV-05
GV-06
GV-07 GGGGGGTGP-3
8.3%
TGP-4
34.2%
EXISTING WASTELIMITS (APPROX.)
GV-08
GV-09
GV-10
GV-11
ADETAILGAS VENT
N.T.S.
WELLBORE SEAL
(LANDTEC OR EQUAL)
EXISTING 6" Ø SCH80 PVC PIPE
STAINLESS STEEL CLAMP
FERNCO 6"x2" REDUCER2" KANAFLEX HOSE
FERNCO 4"x2" REDUCER
HDPE PIPE(SEE PLAN FOR SIZE)4'5'-0" (MAX)
DO NOT ALLOW
SAG IN HOSE
PROTECTIVE
COVER
REMOVE EXISTING
CANDY-CANE TOP
2" BALL VALVE
18" MIN.BDETAILLFG PIPE TRENCH
N.T.S.12" MIN24"COVER
SYSTEM
18" MIN
MAGNETIC TRACING TAPE
FILL
FILL (IF NEEDED)
SDR 17 HDPE PIPE
(DIAMETER VARIES)
NOTE:
1.RESTORE GROUND AND DITCH
TO EXISTING CONDITION
2.MAINTAIN A MINIMUM SLOPE OF2% DURING CONSTRUCTIONFOR LANDFILL GAS PIPING
GROUND SURFACE
6" SDR 17 HDPE FLANGE
ADAPTOR WITH STEEL BACKING
RING AND RUBBER GASKET
6" SDR 17 HDPE LID, 1"
THICK BOLTED TO FLANGEADAPTOR
CLEANOUT, TYP.
1'
DIRECTION OFCONDENSATE FLOW
NOTE: ANGLE
CLEANOUT FOR
PIPE ACCESS IN
DOWNSLOPEDIRECTION
CPIPE CLEANOUT (TYP.)
N.T.S.2211 W. MEADOWVIEW ROADGREENSBORO, NC 27407PHONE: (336) 323-0092NC CORP LIC: C-0782PROJECT NO.APPROVEDCHECKEDDRAWNDESIGNEDDATEDATEREVISIONS AND RECORD OF ISSUEBYNOAPPCKSCALE All rights reserved.Ó Joyce Engineering, Inc.DRAWING NO.L:\Burke County\JOHNS RIVER EXPANSION 2011\2013 CAP ADDENDUM\Drawing 5 (Passive Active Vent Plan).dwg Layout=5-Plan218008JOHNS RIVER WASTE MANGEMENT FACILITYBURKE COUNTY, NORTH CAROLINA20185
AS SHOWNPROPOSED ACTIVELFG SYSTEM LAYOUT & DETAILSMAHCADDLBBLBB12/12/170
(FEET)
GRAPHIC SCALE
1206030 1/15/18SUBMITTED FOR CAP ADDENDUM #2
2'-0"10'4'
6'
6" HDPE
(PUMP HOSE ACCESS)
4"
HDPE
DRAIN
TRAP
2" HDPE LID
2'-0"4" HDPEBAND TANK DETAIL
CONDENSATE TRAP
N.T.S.
4" HDPE
(CLEANOUT)PIPE SUPPORT3'-6"NOTES:
1.EQUIPMENT INSTALLED WITH REQUIRED CLEARANCE
PER MANUFACTURER'S RECOMMENDATIONS AND
LOCAL BUILDING CODES.
2.FINAL SKID LAYOUT TO BE DETERMINED BY
MANUFACTURER.
3.IT IS THE CONTRACTOR'S RESPONSIBILITY TO INSTALL
THE APPROPRIATE ELECTRICAL COMPONENTS TO
PROVIDE A FULLY OPERATIONAL SYSTEM.
4.FLARE TO BE INSTALLED IF ODOR OR EMISSIONS
CONTROL IS DETERMINED TO BE NECESSARY.
5.AT A MINIMUM, THE GAS EXTRACTION UNIT WILL BE
EQUIPPED W/ A CENTRIFUGAL BLOWER, CONDENSATE
KNOCKOUT TANK, AND AIR FILTER. SPACE SHALL BE
LEFT AVAILABLE FOR INSTALLATION OF A FLARE.
AGAS EXTRACTION UNIT SKID
N.T.S.
5'
MIN.
5'
MIN.5' MIN.5' MIN.STEEL BLOWER
FLARE SKID
(SEE NOTES)
1" HDPE GRAVITYCONDENSATE DRAIN
LINE TO VACUUM
SIDE OF TRAP
8"x8"x4"
TEE
JUNCTION BOX
CONTRACTOR IS RESPONSIBLE FOR
ARRANGING, COORDINATING,
INSTALLING AND CONNECTING TO THE
POWER SOURCE AT THE NEAREST
POWER POLE.
UGE
930 GALLON MIN.
CONDENSATE
TRAP & TANKTO CONDENSATEKNOCK-OUT POTFROM CONDENSATE
KNOCK-OUT POT
B
6 2211 W. MEADOWVIEW ROADGREENSBORO, NC 27407PHONE: (336) 323-0092NC CORP LIC: C-0782PROJECT NO.APPROVEDCHECKEDDRAWNDESIGNEDDATEDATEREVISIONS AND RECORD OF ISSUEBYNOAPPCKSCALE All rights reserved.Ó Joyce Engineering, Inc.DRAWING NO.L:\Burke County\JOHNS RIVER EXPANSION 2011\2013 CAP ADDENDUM\Drawing 5 (Passive Active Vent Plan).dwg Layout=6-Details218008JOHNS RIVER WASTE MANGEMENT FACILITYBURKE COUNTY, NORTH CAROLINA20186
AS SHOWNPROPOSED ACTIVELFG SYSTEM DETAILSMAHCADDLBBLBB12/12/171/15/18SUBMITTED FOR CAP ADDENDUM #2
Appendix A
Gas Vent Construction Logs
Appendix B
GEU Pilot Test Data
Appendix B: GEU Pilot Test Data
Table B2: GEU Test of GV-2
Device ID: GEM™2000; Version 2_41 - 08/01/14; LSGAM:6_0_20150403; {2038000911074}
Date/Time CH4 CO2 O2 Balance "AIR"VFD Set GV-1 GV-3 Date Time Vel Flow P T BP
% % % %in.-H2O PSI in.-H2O PSI in.-Hg PSI
CFM Hz In-Wc In-Wc ft/min cfm in.-H2O º F in.-Hg
GV-2 9/26/2017 11:46 60.3 35.6 0.2 3.9 2.8 0.101 0.22 0.008 28.87 1.043 0.4 1.3
GV-2 9/26/2017 11:48 58.6 37.4 0 4 2.8 0.101 0.205 0.007 28.88 1.043 9/26/2017 11:48:35 56 1.23 0.001 92.8 28.94
GV-2 9/26/2017 12:02 59.4 40.5 0 0.1 2.7 0.098 0.213 0.008 28.88 1.043 9/26/2017 11:50:35 56 1.23 0.002 93.4 28.94
GV-2 9/26/2017 12:04 58.3 41.6 0 0.1 2.7 0.098 0.217 0.217 28.89 1.044 20 0.3 1.5 9/26/2017 11:52:35 58 1.27 0.001 93.9 28.94
GV-2 9/26/2017 12:06 58.5 41.4 0 0.1 2.8 0.101 0.222 0.222 28.87 1.043 9/26/2017 11:54:35 60 1.3 0.002 94.2 28.94
GV-2 9/26/2017 12:08 58.9 41 0 0.1 2.7 0.098 0.219 0.219 28.87 1.043 9/26/2017 11:56:35 60 1.32 0.002 94.7 28.93
GV-2 9/26/2017 12:10 58.5 41.4 0 0.1 -0.5 -0.018 -3.084 -3.084 28.87 1.043 9/26/2017 11:58:35 61 1.33 0.002 94.2 28.93
GV-2 9/26/2017 12:12 58.2 41.7 0 0.1 -0.7 -0.025 -3.35 -3.35 28.87 1.043 9/26/2017 12:00:35 61 1.32 0.002 94 28.94
GV-2 9/26/2017 12:14 58.2 41.7 0 0.1 -0.9 -0.033 -3.463 -3.463 28.89 1.044 9/26/2017 12:02:35 60 1.31 0.002 94.2 28.93
GV-2 9/26/2017 12:16 57.6 42.3 0 0.1 -0.9 -0.033 -3.53 -3.53 28.88 1.043 20 9/26/2017 12:04:35 61 1.32 0.002 94.6 28.93
GV-2 9/26/2017 12:18 57.4 42.5 0 0.1 -1.0 -0.036 -3.585 -3.585 28.88 1.043 9/26/2017 12:06:35 62 1.36 0.002 94.8 28.93
GV-2 9/26/2017 12:20 57.7 42.2 0 0.1 -1.0 -0.036 -3.613 -3.613 28.87 1.043 9/26/2017 12:08:35 222 4.84 0.002 93.4 28.93
GV-2 9/26/2017 12:22 57.8 42.1 0 0.1 -1.1 -0.040 -3.642 -3.642 28.87 1.043 9/26/2017 12:10:35 328 7.16 0.002 91 28.93
GV-2 9/26/2017 12:24 57.8 41.6 0 0.6 -1.1 -0.040 -3.676 -3.676 28.88 1.043 9/26/2017 12:12:35 325 7.09 0.002 89.4 28.93
GV-2 9/26/2017 12:26 57.6 41.4 0 1 -1.1 -0.040 -3.714 -3.714 28.88 1.043 9/26/2017 12:14:35 323 7.04 0.002 88.8 28.93
GV-2 9/26/2017 12:28 58.1 41.8 0 0.1 -1.1 -0.040 -3.756 -3.756 28.88 1.043 9/26/2017 12:16:35 321 7 0.002 90.6 28.93
GV-2 9/26/2017 12:30 57.6 41.7 0 0.7 -1.2 -0.043 -3.763 -3.763 28.88 1.043 9/26/2017 12:18:35 318 6.93 0.002 92.1 28.93
GV-2 9/26/2017 12:32 57.5 42.4 0 0.1 -1.2 -0.043 -3.783 -3.783 28.88 1.043 9/26/2017 12:20:35 314 6.85 0.002 92.3 28.93
GV-2 9/26/2017 12:34 58.2 41.6 0 0.2 -1.2 -0.043 -3.802 -3.802 28.87 1.043 0 1.5 9/26/2017 12:22:35 311 6.78 0.002 92.5 28.92
GV-2 9/26/2017 12:36 57.6 42 0 0.4 -1.2 -0.043 -3.809 -3.809 28.89 1.044 9/26/2017 12:24:35 309 6.75 0.002 93.8 28.93
GV-2 9/26/2017 12:38 57.5 42.1 0 0.4 -1.3 -0.047 -3.839 -3.839 28.87 1.043 9/26/2017 12:26:35 308 6.73 0.002 93.7 28.93
GV-2 9/26/2017 12:40 57.9 42 0 0.1 -1.3 -0.047 -3.855 -3.855 28.87 1.043 9/26/2017 12:28:35 309 6.75 0.002 93.1 28.92
GV-2 9/26/2017 12:42 57.1 41.6 0 1.3 -1.3 -0.047 -3.859 -3.859 28.87 1.043 9/26/2017 12:30:35 307 6.71 0.002 93.5 28.92
GV-2 9/26/2017 12:44 57.9 41.4 0 0.7 -1.3 -0.047 -3.901 -3.901 28.89 1.044 9/26/2017 12:32:35 314 6.85 0.002 96 28.92
GV-2 9/26/2017 12:46 57.5 42 0 0.5 -1.4 -0.051 -3.928 -3.928 28.87 1.043 9/26/2017 12:34:35 315 6.88 0.002 96 28.92
GV-2 9/26/2017 12:48 57.4 42.5 0 0.1 -1.4 -0.051 -3.926 -3.926 28.87 1.043 9/26/2017 12:36:35 314 6.86 0.002 95.6 28.92
GV-2 9/26/2017 12:50 56.9 41.7 0 1.4 -1.3 -0.047 -3.929 -3.929 28.88 1.043 9/26/2017 12:38:35 314 6.86 0.002 95.2 28.91
GV-2 9/26/2017 12:52 57.8 42.1 0 0.1 -1.4 -0.051 -3.923 -3.923 28.87 1.043 9/26/2017 12:40:35 313 6.83 0.002 95.4 28.91
GV-2 9/26/2017 12:54 57.7 41.3 0 1 -1.4 -0.051 -3.925 -3.925 28.88 1.043 9/26/2017 12:42:35 312 6.81 0.001 94.9 28.91
GV-2 9/26/2017 12:56 57.6 41.5 0 0.9 -1.4 -0.051 -3.911 -3.911 28.87 1.043 9/26/2017 12:44:35 311 6.78 0.002 94.8 28.91
GV-2 9/26/2017 12:58 57.4 41.8 0 0.8 -1.3 -0.047 -3.924 -3.924 28.87 1.043 0 1.5 9/26/2017 12:46:35 310 6.77 0.002 94.3 28.91
GV-2 9/26/2017 13:00 57.1 41.5 0 1.4 -1.3 -0.047 -3.927 -3.927 28.88 1.043 9/26/2017 12:48:35 310 6.76 0.002 94.6 28.91
GV-2 9/26/2017 13:02 57.7 41.8 0 0.5 -1.3 -0.047 -3.92 -3.92 28.86 1.043 40 0 1.6 9/26/2017 12:50:35 311 6.78 0.002 94.6 28.9
GV-2 9/26/2017 13:04 57.2 41.8 0 1 -1.3 -0.047 -3.926 -3.926 28.88 1.043 0 1.5 9/26/2017 12:52:35 312 6.81 0.002 94 28.9
GV-2 9/26/2017 13:06 57.1 42 0 0.9 -7.5 -0.271 -9.958 -9.958 28.88 1.043 9/26/2017 12:54:35 311 6.79 0.002 94.8 28.9
GV-2 9/26/2017 13:08 57.2 42 0 0.8 -8.1 -0.293 -10.592 -10.592 28.88 1.043 9/26/2017 12:56:35 311 6.79 0.002 95.6 28.9
GV-2 9/26/2017 13:10 57.4 41.8 0 0.8 -8.4 -0.303 -10.858 -10.858 28.87 1.043 9/26/2017 12:58:35 311 6.78 0.003 95.6 28.89
GV-2 9/26/2017 13:12 56.8 42.3 0 0.9 -8.5 -0.307 -11.025 -11.025 28.87 1.043 9/26/2017 13:00:35 311 6.78 0.003 95.9 28.89
GV-2 9/26/2017 13:14 57.5 41.6 0 0.9 -8.6 -0.311 -11.196 -11.196 28.87 1.043 <0 1.8 9/26/2017 13:02:35 309 6.74 0.002 96.6 28.89
GV-2 9/26/2017 13:16 56.8 42.2 0 1 -8.7 -0.314 -11.266 -11.266 28.87 1.043 9/26/2017 13:04:35 642 14.02 0.003 97.1 28.89
GV-2 9/26/2017 13:18 57.3 41.5 0 1.2 -8.7 -0.314 -11.295 -11.295 28.87 1.043 9/26/2017 13:06:35 1075 23.45 0.002 96.5 28.89
GV-2 9/26/2017 13:20 57.3 42.2 0 0.5 -8.9 -0.322 -11.369 -11.369 28.87 1.043 40 <0 1.8 9/26/2017 13:08:35 1064 23.22 0.002 96.7 28.89
GV-2 9/26/2017 13:22 57.3 42.2 0 0.5 -8.9 -0.322 -11.406 -11.406 28.86 1.043 9/26/2017 13:10:35 1057 23.07 0.003 96.7 28.88
GV-2 9/26/2017 13:24 56.9 42.2 0 0.9 -9.0 -0.325 -11.467 -11.467 28.86 1.043 9/26/2017 13:12:35 1037 22.62 0.003 97.1 28.89
GV-2 9/26/2017 13:26 57.1 42 0 0.9 -9.0 -0.325 -11.518 -11.518 28.86 1.043 9/26/2017 13:14:35 1037 22.63 0.002 98.6 28.89
GV-2 9/26/2017 13:28 56.5 41.7 0 1.8 -9.0 -0.325 -11.588 -11.588 28.87 1.043 9/26/2017 13:16:35 1033 22.54 0.002 98.1 28.89
GV-2 9/26/2017 13:30 56.5 41.6 0 1.9 -9.0 -0.325 -11.586 -11.586 28.86 1.043 9/26/2017 13:18:35 1030 22.48 0.002 97.2 28.89
GV-2 9/26/2017 13:32 56.4 41.4 0 2.2 -9.1 -0.329 -11.58 -11.58 28.87 1.043 9/26/2017 13:20:35 1027 22.41 0.002 97.2 28.89
GV-2 9/26/2017 13:34 56.9 43 0 0.1 -9.2 -0.332 -11.675 -11.675 28.87 1.043 9/26/2017 13:22:35 1031 22.5 0.002 97.5 28.89
GV-2 9/26/2017 13:36 56.8 41.6 0 1.6 -9.2 -0.332 -11.696 -11.696 28.87 1.043 9/26/2017 13:24:35 1022 22.31 0.002 96.6 28.89
GV-2 9/26/2017 13:38 56.4 41.7 0 1.9 -9.2 -0.332 -11.717 -11.717 28.85 1.042 43004 0.560127 1021 22.28 0.002 96.7 28.89
GV-2 9/26/2017 13:40 56.4 42 0 1.6 -9.2 -0.332 -11.755 -11.755 28.85 1.042 43004 0.561516 1020 22.25 0.002 97.2 28.89
GV-2 9/26/2017 13:42 56.9 40.9 0 2.2 -9.2 -0.332 -11.778 -11.778 28.86 1.043 43004 0.562905 1021 22.27 0.003 96.5 28.89
GV-2 9/26/2017 13:44 56.6 41.3 0 2.1 -9.3 -0.336 -11.796 -11.796 28.85 1.042 9/26/2017 13:32:35 1019 22.24 0.002 95.8 28.89
GV-2 9/26/2017 13:46 56.8 41.8 0 1.4 -9.3 -0.336 -11.844 -11.844 28.86 1.043 9/26/2017 13:34:35 1021 22.28 0.002 96.2 28.89
GV-2 9/26/2017 13:48 56.5 41.8 0 1.7 -9.4 -0.340 -11.833 -11.833 28.86 1.043 9/26/2017 13:36:35 1016 22.16 0.003 97.8 28.89
GV-2 9/26/2017 13:50 56.4 41.7 0 1.9 -9.4 -0.340 -11.901 -11.901 28.86 1.043 9/26/2017 13:38:35 1014 22.12 0.003 98 28.89
GEM Data Log Velocicalc Manual Velocicalc Log
Static Press. Diff. Press. Baro. Press.Temp.
(°F)
Burke Co., Johns River Landfill, Permit 12-03
CAP Addnedum Page 1 of 3 Joyce Engineering
Appendix B: GEU Pilot Test Data
Table B2: GEU Test of GV-2
Device ID: GEM™2000; Version 2_41 - 08/01/14; LSGAM:6_0_20150403; {2038000911074}
Date/Time CH4 CO2 O2 Balance "AIR"VFD Set GV-1 GV-3 Date Time Vel Flow P T BP
% % % %in.-H2O PSI in.-H2O PSI in.-Hg PSI
CFM Hz In-Wc In-Wc ft/min cfm in.-H2O º F in.-Hg
GEM Data Log Velocicalc Manual Velocicalc Log
Static Press. Diff. Press. Baro. Press.Temp.
(°F)
GV-2 9/26/2017 13:52 56.5 42.1 0 1.4 -9.4 -0.340 -11.916 -11.916 28.86 1.043 9/26/2017 13:40:35 1019 22.22 0.003 97.9 28.89
GV-2 9/26/2017 13:54 56.5 41.6 0 1.9 -9.4 -0.340 -11.937 -11.937 28.86 1.043 9/26/2017 13:42:35 1016 22.16 0.003 99 28.89
GV-2 9/26/2017 13:56 56.4 42.1 0 1.5 -9.4 -0.340 -11.947 -11.947 28.86 1.043 <0 1.8 9/26/2017 13:44:35 1014 22.11 0.003 98.3 28.89
GV-2 9/26/2017 13:58 56.2 41.4 0 2.4 -9.4 -0.340 -11.972 -11.972 28.84 1.042 9/26/2017 13:46:35 1018 22.21 0.003 98.4 28.89
GV-2 9/26/2017 14:00 56.4 41.3 0 2.3 -9.5 -0.343 -11.995 -11.995 28.84 1.042 9/26/2017 13:48:35 1019 22.22 0.002 99 28.89
GV-2 9/26/2017 14:02 56.6 42 0 1.4 -9.5 -0.343 -11.985 -11.985 28.84 1.042 9/26/2017 13:50:35 1022 22.3 0.002 99.5 28.89
GV-2 9/26/2017 14:04 56 41.5 0 2.5 -15.2 -0.549 -17.582 -17.582 28.86 1.043 60 9/26/2017 13:52:35 1019 22.23 0.002 99 28.89
GV-2 9/26/2017 14:06 56.3 41.9 0 1.8 -15.8 -0.571 -18.307 -18.307 28.86 1.043 9/26/2017 13:54:35 1015 22.14 0.002 98.9 28.89
GV-2 9/26/2017 14:08 55.8 41.4 0 2.8 -16.0 -0.578 -18.486 -18.486 28.84 1.042 9/26/2017 13:56:35 1017 22.18 0.002 98.6 28.89
GV-2 9/26/2017 14:10 56.4 41.9 0 1.7 -16.1 -0.582 -18.459 -18.459 28.85 1.042 9/26/2017 13:58:35 1015 22.15 0.003 97.5 28.88
GV-2 9/26/2017 14:12 55.8 41.9 0 2.3 -16.2 -0.585 -18.551 -18.551 28.84 1.042 9/26/2017 14:00:35 1013 22.11 0.003 96.9 28.88
GV-2 9/26/2017 14:14 56 41.4 0 2.6 -16.2 -0.585 -18.613 -18.613 28.85 1.042 9/26/2017 14:02:35 1141 24.9 0.003 96.9 28.89
GV-2 9/26/2017 14:16 56.3 42 0 1.7 -16.2 -0.585 -18.629 -18.629 28.84 1.042 60 9/26/2017 14:04:35 1673 36.5 0.003 97.6 28.88
GV-2 9/26/2017 14:18 56 41.5 0 2.5 -16.3 -0.589 -18.71 -18.71 28.85 1.042 60 <0 1.6 9/26/2017 14:06:35 1653 36.06 0.003 96.7 28.88
GV-2 9/26/2017 14:20 55.7 40.8 0 3.5 -16.3 -0.589 -18.786 -18.786 28.84 1.042 9/26/2017 14:08:35 1640 35.77 0.003 97.1 28.88
GV-2 9/26/2017 14:22 56.3 42 0 1.7 -16.3 -0.589 -18.809 -18.809 28.84 1.042 9/26/2017 14:10:35 1627 35.49 0.003 98.1 28.88
GV-2 9/26/2017 14:24 56 41.1 0 2.9 -16.2 -0.585 -18.802 -18.802 28.85 1.042 9/26/2017 14:12:35 1625 35.45 0.003 98.7 28.88
GV-2 9/26/2017 14:26 55.6 41 0 3.4 -16.3 -0.589 -18.846 -18.846 28.85 1.042 9/26/2017 14:14:35 1615 35.24 0.003 99.9 28.88
GV-2 9/26/2017 14:28 56.2 41.8 0 2 -16.4 -0.592 -18.791 -18.791 28.84 1.042 9/26/2017 14:16:35 1614 35.2 0.003 100 28.88
GV-2 9/26/2017 14:30 55.8 41.3 0 2.9 -16.4 -0.592 -18.868 -18.868 28.84 1.042 9/26/2017 14:18:35 1607 35.07 0.003 100.4 28.88
GV-2 9/26/2017 14:32 56.5 41.5 0 2 -16.2 -0.585 -18.738 -18.738 28.84 1.042 9/26/2017 14:20:35 1613 35.18 0.003 99.9 28.87
GV-2 9/26/2017 14:34 55.6 41.2 0 3.2 -16.3 -0.589 -18.853 -18.853 28.85 1.042 9/26/2017 14:22:35 1617 35.27 0.003 98.8 28.87
GV-2 9/26/2017 14:36 55.8 40.9 0 3.3 -16.4 -0.592 -18.85 -18.85 28.85 1.042 9/26/2017 14:24:35 1611 35.15 0.003 98.5 28.87
GV-2 9/26/2017 14:38 55.5 42.2 0 2.3 -16.4 -0.592 -18.821 -18.821 28.84 1.042 9/26/2017 14:26:35 1617 35.28 0.003 99.7 28.87
GV-2 9/26/2017 14:40 56.3 40.9 0.1 2.7 -16.4 -0.592 -18.88 -18.88 28.85 1.042 9/26/2017 14:28:35 1714 37.39 0.003 102.5 28.87
GV-2 9/26/2017 14:42 56.4 41 0 2.6 -16.5 -0.596 -18.909 -18.909 28.85 1.042 9/26/2017 14:30:35 1714 37.39 0.003 100.9 28.87
GV-2 9/26/2017 14:44 56.8 41.2 0.1 1.9 -16.6 -0.600 -18.957 -18.957 28.85 1.042 9/26/2017 14:32:35 1737 37.91 0.003 97.3 28.87
GV-2 9/26/2017 14:46 0.2 4.6 18.8 76.4 1.4 0.051 -1.029 -1.029 28.84 1.042 0 9/26/2017 14:34:35 1737 37.9 0.003 96.8 28.86
GV-2 9/26/2017 14:48 0 0.9 20.1 79 1.8 0.065 -0.604 -0.604 28.84 1.042 9/26/2017 14:36:35 1741 37.98 0.003 98 28.86
GV-2 9/26/2017 14:50 0 0.3 20.3 79.4 2.0 0.072 -0.41 -0.41 28.84 1.042 9/26/2017 14:38:35 1742 38.01 0.003 97.2 28.86
GV-2 9/26/2017 14:52 0 0.1 20.4 79.5 2.1 0.076 -0.287 -0.287 28.84 1.042 9/26/2017 14:40:35 1741 37.98 0.003 97.3 28.86
GV-2 9/26/2017 14:54 0 0 20.4 79.6 2.2 0.079 -0.194 -0.194 28.84 1.042 9/26/2017 14:42:35 1724 37.62 0.003 101.3 28.86
GV-2 9/26/2017 14:56 24.4 8.9 13.3 53.4 -12.7 -0.459 -14.259 -14.259 28.84 1.042 9/26/2017 14:44:35 435 9.49 0.003 103 28.86
GV-2 9/26/2017 14:58 50.5 35.2 2 12.3 -15.5 -0.560 -17.752 -17.752 28.84 1.042 9/26/2017 14:46:35 71 1.54 0.003 99.9 28.86
GV-2 9/26/2017 15:00 53.3 39 0.8 6.9 -15.9 -0.574 -18.248 -18.248 28.85 1.042 9/26/2017 14:48:35 59 1.29 0.004 98.5 28.86
GV-2 9/26/2017 15:02 53.7 39 0.4 6.9 -16.1 -0.582 -18.443 -18.443 28.85 1.042 9/26/2017 14:50:35 51 1.12 0.004 97.1 28.86
GV-2 9/26/2017 15:04 55.2 41.3 0.2 3.3 -16.2 -0.585 -18.618 -18.618 28.85 1.042 9/26/2017 14:52:35 45 0.99 0.004 95.8 28.86
GV-2 9/26/2017 15:06 55.8 40.7 0.2 3.3 -16.3 -0.589 -18.691 -18.691 28.85 1.042 60 9/26/2017 14:54:35 169 3.69 0.004 95.6 28.86
GV-2 9/26/2017 15:08 55.3 41.1 0.1 3.5 -16.5 -0.596 -18.798 -18.798 28.83 1.042 9/26/2017 14:56:35 1696 36.99 0.004 97.1 28.85
GV-2 9/26/2017 15:10 55.8 40.5 0.1 3.6 -16.5 -0.596 -18.908 -18.908 28.83 1.042 9/26/2017 14:58:35 1881 41.04 0.004 96 28.85
GV-2 9/26/2017 15:12 55.9 40.4 0.1 3.6 -16.6 -0.600 -18.96 -18.96 28.83 1.042 9/26/2017 15:00:35 1901 41.47 0.004 97 28.85
GV-2 9/26/2017 15:14 55.9 41.4 0.1 2.6 -16.6 -0.600 -19.029 -19.029 28.84 1.042 9/26/2017 15:02:35 1897 41.39 0.004 95.3 28.85
GV-2 9/26/2017 15:16 55.7 41.4 0.1 2.8 -16.7 -0.603 -19.03 -19.03 28.84 1.042 9/26/2017 15:04:35 1885 41.12 0.004 95.2 28.85
GV-2 9/26/2017 15:18 55.8 40.9 0.1 3.2 -16.7 -0.603 -19.082 -19.082 28.84 1.042 9/26/2017 15:06:35 1876 40.93 0.004 95.7 28.85
GV-2 9/26/2017 15:20 55.9 41.2 0.1 2.8 -16.8 -0.607 -19.155 -19.155 28.83 1.042 9/26/2017 15:08:35 1876 40.92 0.004 97.8 28.85
GV-2 9/26/2017 15:22 55.9 40.5 0.1 3.5 -16.8 -0.607 -19.172 -19.172 28.84 1.042 9/26/2017 15:10:35 1868 40.75 0.004 97.7 28.85
GV-2 9/26/2017 15:24 56.3 41.6 0.1 2 -16.9 -0.611 -19.17 -19.17 28.84 1.042 9/26/2017 15:12:35 1866 40.71 0.004 97.8 28.85
GV-2 9/26/2017 15:26 55.9 41.1 0.1 2.9 -16.8 -0.607 -19.165 -19.165 28.84 1.042 9/26/2017 15:14:35 1865 40.69 0.004 98.4 28.85
GV-2 9/26/2017 15:28 56.1 41.4 0.1 2.4 -16.8 -0.607 -19.203 -19.203 28.84 1.042 9/26/2017 15:16:35 1860 40.58 0.004 99.3 28.85
GV-2 9/26/2017 15:30 55.3 41.1 0.1 3.5 -16.8 -0.607 -19.193 -19.193 28.83 1.042 9/26/2017 15:18:35 1864 40.67 0.004 99.9 28.85
GV-2 9/26/2017 15:32 55.8 41.3 0.1 2.8 -17.0 -0.614 -19.248 -19.248 28.84 1.042 9/26/2017 15:20:35 1861 40.61 0.004 97.3 28.85
GV-2 9/26/2017 15:34 55.1 42.4 0.1 2.4 -17.0 -0.614 -19.249 -19.249 28.84 1.042 9/26/2017 15:22:35 1848 40.31 0.004 97.4 28.85
GV-2 9/26/2017 15:36 56.3 41.7 0.1 1.9 -16.7 -0.603 -19.129 -19.129 28.84 1.042 9/26/2017 15:24:35 1843 40.2 0.004 97 28.85
GV-2 9/26/2017 15:38 55.7 41.1 0.1 3.1 -16.7 -0.603 -19.114 -19.114 28.83 1.042 43004 0.643461 1830 39.93 0.004 96.6 28.85
GV-2 43004.65291 55.9 41.4 0.1 2.6 -16.8 -0.607 -19.145 -19.145 28.83 1.042 43004 0.64485 1826 39.84 0.004 96.8 28.85
GV-2 43004.65429 55.7 41.6 0.1 2.6 -16.8 -0.607 -19.124 -19.124 28.84 1.042 43004 0.646238 1824 39.8 0.004 98.4 28.85
GV-2 43004.65568 56.1 41.5 0.1 2.3 -16.8 -0.607 -19.197 -19.197 28.84 1.042 43004 0.647627 1825 39.82 0.004 99.7 28.85
Burke Co., Johns River Landfill, Permit 12-03
CAP Addnedum Page 2 of 3 Joyce Engineering
Appendix B: GEU Pilot Test Data
Table B2: GEU Test of GV-2
Device ID: GEM™2000; Version 2_41 - 08/01/14; LSGAM:6_0_20150403; {2038000911074}
Date/Time CH4 CO2 O2 Balance "AIR"VFD Set GV-1 GV-3 Date Time Vel Flow P T BP
% % % %in.-H2O PSI in.-H2O PSI in.-Hg PSI
CFM Hz In-Wc In-Wc ft/min cfm in.-H2O º F in.-Hg
GEM Data Log Velocicalc Manual Velocicalc Log
Static Press. Diff. Press. Baro. Press.Temp.
(°F)
GV-2 43004.65707 55.5 41.1 0.1 3.3 -16.8 -0.607 -19.227 -19.227 28.83 1.042 43004 0.649016 1812 39.54 0.004 100.5 28.84
GV-2 43004.65846 55.6 41.1 0.1 3.2 -16.8 -0.607 -19.235 -19.235 28.84 1.042 43004 0.650405 1801 39.3 0.004 99.9 28.84
GV-2 43004.65985 55.7 41.6 0.1 2.6 -16.8 -0.607 -19.243 -19.243 28.83 1.042 43004 0.651794 1802 39.31 0.004 99.2 28.84
GV-2 43004.66124 55.7 40.8 0.1 3.4 -16.9 -0.611 -19.239 -19.239 28.84 1.042 43004 0.653183 1799 39.24 0.004 97.4 28.84
GV-2 43004.66263 55.8 40.9 0.1 3.2 -16.8 -0.607 -19.232 -19.232 28.84 1.042 43004 0.654572 1802 39.31 0.005 100.2 28.84
GV-2 43004.66402 55.1 40.8 0.1 4 -16.9 -0.611 -19.25 -19.25 28.84 1.042 43004 0.655961 1800 39.27 0.004 101.2 28.84
GV-2 43004.66541 55.3 40.4 0.1 4.2 -16.9 -0.611 -19.243 -19.243 28.84 1.042 43004 0.65735 1804 39.35 0.004 100.5 28.84
GV-2 43004.66679 55.6 41.4 0.1 2.9 -16.8 -0.607 -19.179 -19.179 28.84 1.042 43004 0.658738 1796 39.19 0.004 98.3 28.84
GV-2 43004.66818 55.2 40.8 0.1 3.9 -16.8 -0.607 -19.182 -19.182 28.84 1.042 43004 0.660127 1793 39.11 0.005 98.9 28.84
GV-2 43004.66957 55.4 41.5 0.1 3 -16.7 -0.603 -19.157 -19.157 28.84 1.042 43004 0.661516 1786 38.97 0.004 99 28.84
GV-2 43004.67096 55.4 41.3 0.1 3.2 -16.7 -0.603 -19.174 -19.174 28.84 1.042 43004 0.662905 1790 39.05 0.005 100.5 28.84
GV-2 43004.67235 55.6 40.8 0.1 3.5 -16.7 -0.603 -19.069 -19.069 28.84 1.042 43004 0.664294 1784 38.93 0.005 99.3 28.84
GV-2 43004.67374 55 41.8 0.1 3.1 -16.7 -0.603 -19.126 -19.126 28.83 1.042 43004 0.665683 1778 38.8 0.005 100.3 28.84
GV-2 43004.67513 55.7 41.8 0.1 2.4 -16.7 -0.603 -19.081 -19.081 28.83 1.042 43004 0.667072 1782 38.87 0.005 103.9 28.84
GV-2 43004.67652 55.4 41 0.1 3.5 -16.8 -0.607 -19.12 -19.12 28.83 1.042 43004 0.668461 1791 39.06 0.005 103.4 28.84
GV-2 43004.67791 55.4 41.8 0.1 2.7 -16.7 -0.603 -19.124 -19.124 28.84 1.042 43004 0.66985 1783 38.9 0.005 101.3 28.84
GV-2 43004.67929 55.4 41.6 0.1 2.9 -16.8 -0.607 -19.125 -19.125 28.83 1.042 43004 0.671238 1782 38.88 0.005 102.3 28.83
GV-2 43004.68068 55.7 41 0.1 3.2 -16.8 -0.607 -19.142 -19.142 28.84 1.042 43004 0.672627 1770 38.61 0.005 100.8 28.83
GV-2 43004.68207 55.2 41.1 0.1 3.6 -16.8 -0.607 -19.22 -19.22 28.83 1.042 43004 0.674016 1771 38.63 0.005 101.2 28.83
GV-2 43004.68346 55.9 41.2 0.1 2.8 -16.9 -0.611 -19.198 -19.198 28.83 1.042 43004 0.675405 1771 38.64 0.005 102.7 28.83
GV-2 43004.68485 55.8 41.3 0.1 2.8 -16.8 -0.607 -19.202 -19.202 28.84 1.042 43004 0.676794 1773 38.68 0.005 102.5 28.83
GV-2 43004.68624 55.1 41.2 0.1 3.6 -16.8 -0.607 -19.189 -19.189 28.84 1.042 43004 0.678183 1763 38.47 0.005 101 28.83
GV-2 43004.68763 55.3 41.4 0.1 3.2 -16.8 -0.607 -19.197 -19.197 28.84 1.042 43004 0.679572 1764 38.49 0.005 101.1 28.83
GV-2 43004.68902 55.2 41.1 0.1 3.6 -16.8 -0.607 -19.182 -19.182 28.83 1.042 43004 0.680961 1769 38.59 0.005 101.3 28.83
GV-2 43004.69041 55.1 41.2 0.1 3.6 -16.8 -0.607 -19.187 -19.187 28.83 1.042 43004 0.68235 1767 38.54 0.005 100 28.83
GV-2 43004.69179 55.1 40.6 0.1 4.2 -16.8 -0.607 -19.214 -19.214 28.82 1.041 43004 0.683738 1766 38.52 0.005 97.6 28.83
GV-2 43004.69318 55.5 41.9 0.2 2.4 -16.9 -0.611 -19.226 -19.226 28.83 1.042 43004 0.685127 1761 38.42 0.005 100.2 28.83
GV-2 43004.69457 55.2 40 0.1 4.7 -17.0 -0.614 -19.27 -19.27 28.83 1.042 43004 0.686516 1762 38.45 0.005 99.4 28.83
GV-2 43004.69596 55.3 41 0.1 3.6 -16.9 -0.611 -19.316 -19.316 28.84 1.042 43004 0.687905 1757 38.33 0.005 99.9 28.83
GV-2 43004.69735 55.4 40.4 0.1 4.1 -17.0 -0.614 -19.301 -19.301 28.84 1.042 43004 0.689294 1765 38.5 0.005 100.2 28.83
GV-2 43004.69874 55.4 40.6 0.1 3.9 -17.1 -0.618 -19.268 -19.268 28.84 1.042 43004 0.690683 1764 38.48 0.005 100.7 28.83
GV-2 43004.70013 55.6 41.5 0.1 2.8 -17.0 -0.614 -19.347 -19.347 28.82 1.041 43004 0.692072 1764 38.48 0.005 101.5 28.83
GV-2 43004.70152 55.2 41.5 0.1 3.2 -17.0 -0.614 -19.325 -19.325 28.83 1.042 43004 0.693461 1768 38.58 0.005 99.9 28.83
GV-2 43004.70291 55.4 40.6 0.1 3.9 -17.0 -0.614 -19.395 -19.395 28.83 1.042 43004 0.69485 1761 38.41 0.005 96.4 28.83
GV-2 43004.70429 55.7 41.1 0.1 3.1 -17.1 -0.618 -19.368 -19.368 28.83 1.042 43004 0.696238 1761 38.41 0.005 97.4 28.83
GV-2 43004.70568 55.4 41.7 0.1 2.8 -17.1 -0.618 -19.368 -19.368 28.84 1.042 43004 0.697627 1760 38.39 0.005 97.7 28.83
GV-2 43004.70707 55 40.9 0.1 4 -17.1 -0.618 -19.383 -19.383 28.82 1.041 43004 0.699016 1768 38.57 0.005 99.1 28.83
GV-2 43004.70846 55.3 40.5 0.1 4.1 -17.1 -0.618 -19.42 -19.42 28.83 1.042 43004 0.700405 1766 38.53 0.005 99.7 28.83
GV-2 43004.70985 55.7 40.7 0.2 3.4 -17.0 -0.614 -19.399 -19.399 28.83 1.042 43004 0.701794 1767 38.55 0.005 99.2 28.83
GV-2 43004.71124 55.3 40.6 0.2 3.9 -17.0 -0.614 -19.367 -19.367 28.82 1.041 43004 0.703183 1768 38.57 0.005 99.1 28.83
GV-2 43004.71263 55.3 41.3 0.1 3.3 -17.1 -0.618 -19.352 -19.352 28.83 1.042 43004 0.704572 1770 38.62 0.005 98.6 28.83
GV-2 43004.71402 55.3 40.9 0.1 3.7 -17.0 -0.614 -19.367 -19.367 28.82 1.041 43004 0.705961 1763 38.45 0.005 98.2 28.83
GV-2 43004.71541 54.9 40.9 0.1 4.1 -17.0 -0.614 -19.383 -19.383 28.82 1.041 43004 0.70735 1761 38.42 0.005 97.3 28.83
GV-2 43004.71679 55.7 41.2 0.2 2.9 -17.1 -0.618 -19.401 -19.401 28.83 1.042 43004 0.708738 1762 38.45 0.005 97.3 28.83
GV-2 43004.71818 55.2 41.2 0.2 3.4 -17.1 -0.618 -19.406 -19.406 28.82 1.041 43004 0.710127 1759 38.38 0.005 97.4 28.83
GV-2 43004.71957 55.7 41.7 0.2 2.4 -17.2 -0.621 -19.445 -19.445 28.83 1.042 43004 0.711516 1760 38.4 0.005 97.9 28.83
GV-2 43004.72096 0.9 10 16.6 72.5 0.10 0.0036 -2.413 -2.413 28.82 1.041 0 <0 <0 43004 0.712905 1758 38.35 0.005 97.9 28.83
43004 0.714294 1755 38.28 0.005 94.8 28.83
43004 0.715683 1750 38.19 0.005 94.7 28.83
43004 0.717072 1753 38.24 0.005 96.5 28.83
43004 0.718461 1757 38.33 0.005 98.2 28.83
43004 0.71985 1407 30.69 0.005 99.9 28.83
Burke Co., Johns River Landfill, Permit 12-03
CAP Addnedum Page 3 of 3 Joyce Engineering
Appendix B: GEU Pilot Test Data
Table B3: GEU Test of GV-6
Device ID: GEM™2000; Version 2_41 - 08/01/14; LSGAM:6_0_20150403; {2038000911074}
Date/Time CH4 CO2 O2 Balance "AIR"VFD Set GV-5 GV-7 Date Time Vel Flow P T BP
% % % %in.-H2O PSI in.-H2O PSI in.-Hg PSI
CFM Hz In-Wc In-Wc ft/min cfm in.-H2O º F in.-Hg
GV-6 9/27/2017 7:58 63.7 34.6 0.3 1.4 2.9 0.105 0.45 0.016 28.83 14.160
GV-6 9/27/2017 8:00 59.9 38.1 0 2 2.8 0.101 0.466 0.017 28.84 14.165
GV-6 9/27/2017 8:02 59.3 38.5 0 2.2 2.9 0.105 0.467 0.017 28.84 14.165
GV-6 9/27/2017 8:04 58.9 38.6 0 2.5 2.8 0.101 0.464 0.017 28.83 14.160
GV-6 9/27/2017 8:06 59 38.8 0 2.2 2.8 0.101 0.46 0.017 28.82 14.155 0 9/27/2017 8:06:08 184 4.02 0.003 76.8 28.91
GV-6 9/27/2017 8:08 58.6 38.4 0 3 0.9 0.033 1.253 0.045 28.82 14.155 20 0.9 0 9/27/2017 8:08:08 908 19.81 0.003 78.4 28.91
GV-6 9/27/2017 8:10 58.7 38.2 0.1 3 -2.1 -0.076 5.505 0.199 28.82 14.155 9/27/2017 8:10:08 1748 38.13 0.003 79.3 28.91
GV-6 9/27/2017 8:12 56.9 36.2 0.6 6.3 -2.8 -0.101 6.168 0.223 28.82 14.155 9/27/2017 8:12:08 1567 34.2 0.003 80 28.91
GV-6 9/27/2017 8:14 55.4 35.3 1 8.3 -3.1 -0.112 6.496 0.235 28.84 14.165 9/27/2017 8:14:08 1450 31.63 0.002 80.3 28.91
GV-6 9/27/2017 8:16 55 35.5 1.2 8.3 -3.3 -0.119 6.699 0.242 28.84 14.165 9/27/2017 8:16:08 1371 29.9 0.002 81.9 28.92
GV-6 9/27/2017 8:18 55.4 34.6 1.2 8.8 -3.5 -0.126 6.844 0.247 28.84 14.165 9/27/2017 8:18:08 1318 28.75 0.002 83.2 28.92
GV-6 9/27/2017 8:20 54.9 34.4 1.3 9.4 -3.6 -0.130 6.959 0.251 28.82 14.155 9/27/2017 8:20:08 1278 27.88 0.002 83.6 28.92
GV-6 9/27/2017 8:22 54.7 33.9 1.2 10.2 -3.7 -0.134 7.028 0.254 28.82 14.155 9/27/2017 8:22:08 1249 27.24 0.002 84.3 28.92
GV-6 9/27/2017 8:24 54.7 34.1 1.3 9.9 -3.7 -0.134 7.056 0.255 28.84 14.165 9/27/2017 8:24:08 1215 26.5 0.002 84.2 28.92
GV-6 9/27/2017 8:26 54.3 34.2 1.3 10.2 -3.7 -0.134 7.075 0.256 28.84 14.165 9/27/2017 8:26:08 1189 25.95 0.002 85.2 28.92
GV-6 9/27/2017 8:28 54.4 34.2 1.4 10 -3.8 -0.137 7.101 0.257 28.82 14.155 9/27/2017 8:28:08 1175 25.63 0.002 86 28.92
GV-6 9/27/2017 8:30 54.2 33.5 1.4 10.9 -3.8 -0.137 7.131 0.258 28.82 14.155 20 0.6 0 9/27/2017 8:30:08 1156 25.21 0.002 86 28.92
GV-6 9/27/2017 8:32 53.8 33.5 1.4 11.3 -3.8 -0.137 7.173 0.259 28.84 14.165 9/27/2017 8:32:08 1140 24.88 0.002 85.5 28.92
GV-6 9/27/2017 8:34 53.6 33.8 1.5 11.1 -3.8 -0.137 7.163 0.259 28.83 14.160 9/27/2017 8:34:08 1128 24.61 0.002 85.8 28.92
GV-6 9/27/2017 8:36 53.9 33.3 1.5 11.3 -3.9 -0.141 7.192 0.260 28.84 14.165 20 0.6 0 9/27/2017 8:36:08 1121 24.45 0.002 86.9 28.92
GV-6 9/27/2017 8:38 53.5 33.9 1.5 11.1 -3.8 -0.137 7.203 0.260 28.84 14.165 9/27/2017 8:38:08 1108 24.17 0.002 88.7 28.92
GV-6 9/27/2017 8:40 55.8 35 0.8 8.4 -10.3 -0.372 12.923 0.467 28.82 14.155 9/27/2017 8:40:08 2499 54.52 0.002 89.5 28.92
GV-6 9/27/2017 8:42 55.7 34.9 0.7 8.7 -13.6 -0.491 16.782 0.606 28.82 14.155 40 0.6 0 9/27/2017 8:42:08 3474 75.79 0.002 91.4 28.92
GV-6 9/27/2017 8:44 55.8 34.9 0.8 8.5 -15.7 -0.567 18.931 0.684 28.84 14.165 9/27/2017 8:44:08 3276 71.48 0.002 91.5 28.92
GV-6 9/27/2017 8:46 55.1 35.1 0.9 8.9 -16.7 -0.603 19.884 0.718 28.82 14.155 40 0.6 <0 9/27/2017 8:46:08 3154 68.82 0.002 92.1 28.92
GV-6 9/27/2017 8:48 54.9 34 1 10.1 -17.3 -0.625 20.474 0.740 28.82 14.155 9/27/2017 8:48:08 3051 66.57 0.002 93.7 28.92
GV-6 9/27/2017 8:50 54.6 34.4 1.1 9.9 -17.7 -0.639 20.865 0.754 28.82 14.155 9/27/2017 8:50:08 2820 61.53 0.002 93 28.92
GV-6 9/27/2017 8:52 53.9 34.3 1.1 10.7 -17.9 -0.647 21.107 0.763 28.82 14.155 40 0.75 <0 9/27/2017 8:52:08 2661 58.04 0.002 91.5 28.92
GV-6 9/27/2017 8:54 54.1 34.1 1.2 10.6 -18.1 -0.654 21.344 0.771 28.83 14.160 9/27/2017 8:54:08 2609 56.91 0.002 88.7 28.92
GV-6 9/27/2017 8:56 54.1 33.9 1.2 10.8 -18.3 -0.661 21.557 0.779 28.82 14.155 9/27/2017 8:56:08 2564 55.93 0.002 86.7 28.92
GV-6 9/27/2017 8:58 53.4 34.2 1.2 11.2 -18.5 -0.668 21.695 0.784 28.82 14.155 40 0.7 <0 9/27/2017 8:58:08 2511 54.79 0.002 85.8 28.92
GV-6 9/27/2017 9:00 53.4 33.8 1.3 11.5 -18.5 -0.668 21.684 0.783 28.84 14.165 9/27/2017 9:00:08 2458 53.62 0.002 85.3 28.92
GV-6 9/27/2017 9:02 52.6 33.4 1.4 12.6 -18.5 -0.668 21.703 0.784 28.84 14.165 9/27/2017 9:02:08 2420 52.79 0.002 86.4 28.92
GV-6 9/27/2017 9:04 53 33.1 1.4 12.5 -18.5 -0.668 21.734 0.785 28.84 14.165 9/27/2017 9:04:08 2401 52.37 0.002 87.5 28.92
GV-6 9/27/2017 9:06 53.4 33.7 1.3 11.6 -18.6 -0.672 21.812 0.788 28.82 14.155 9/27/2017 9:06:08 2383 51.99 0.002 88.6 28.93
GV-6 9/27/2017 9:08 53 34 1.4 11.6 -18.6 -0.672 21.894 0.791 28.84 14.165 40 0.6 <0 9/27/2017 9:08:08 2365 51.6 0.002 90.6 28.93
GV-6 9/27/2017 9:09 52.6 33.5 1.5 12.4 -18.6 -0.672 21.919 0.792 28.82 14.155 9/27/2017 9:10:08 2350 51.27 0.002 92.7 28.92
GV-6 9/27/2017 9:11 52.2 33.4 1.4 13 -18.8 -0.679 21.945 0.793 28.82 14.155 40 0.5 <0 9/27/2017 9:12:08 2330 50.83 0.002 93.7 28.92
GV-6 9/27/2017 9:13 52.7 33.8 1.4 12.1 -18.8 -0.679 22 0.795 28.82 14.155 9/27/2017 9:14:08 2311 50.41 0.002 93.6 28.93
GV-6 9/27/2017 9:15 52.2 33.3 1.5 13 -18.8 -0.679 22.041 0.796 28.82 14.155 9/27/2017 9:16:08 2294 50.05 0.002 93.3 28.93
GV-6 9/27/2017 9:17 52 33.3 1.4 13.3 -18.9 -0.683 22.095 0.798 28.82 14.155 40 0.5 <0 9/27/2017 9:18:08 2281 49.75 0.002 93.4 28.92
GV-6 9/27/2017 9:19 52.2 33.2 1.5 13.1 -18.9 -0.683 22.13 0.799 28.82 14.155 9/27/2017 9:20:08 2269 49.5 0.002 93.3 28.92
GV-6 9/27/2017 9:21 51.9 33.8 1.5 12.8 -18.9 -0.683 22.162 0.801 28.84 14.165 9/27/2017 9:22:08 2930 63.92 0.002 93.2 28.92
GV-6 9/27/2017 9:23 53.2 34 1.2 11.6 -23.2 -0.838 26.269 0.949 28.84 14.165 60 0.4 <0 9/27/2017 9:24:08 3053 66.6 0.002 93.4 28.92
GV-6 9/27/2017 9:24 52.6 34.5 1.2 11.7 -23.9 -0.863 26.959 0.974 28.82 14.155 9/27/2017 9:26:08 2875 62.72 0.002 92.9 28.92
GV-6 9/27/2017 9:26 52.2 33.5 1.3 13 -24.1 -0.871 27.138 0.980 28.82 14.155 60 0.4 <0 9/27/2017 9:28:08 2779 60.62 0.002 92.2 28.92
GV-6 9/27/2017 9:28 52.3 34 1.3 12.4 -23.8 -0.860 26.951 0.974 28.84 14.165 9/27/2017 9:30:08 2747 59.93 0.002 91.6 28.92
GV-6 9/27/2017 9:30 52.3 33.9 1.4 12.4 -23.9 -0.863 26.985 0.975 28.82 14.155 9/27/2017 9:32:08 2704 59 0.002 92 28.92
GV-6 9/27/2017 9:32 52.1 33.6 1.5 12.8 -23.9 -0.863 27.06 0.978 28.84 14.165 9/27/2017 9:34:08 2677 58.4 0.002 92.6 28.92
GV-6 9/27/2017 9:34 51.5 33.1 1.5 13.9 -24.0 -0.867 27.113 0.980 28.82 14.155 9/27/2017 9:36:08 2657 57.97 0.002 93.3 28.92
GV-6 9/27/2017 9:36 51.5 33.6 1.5 13.4 -24.0 -0.867 27.176 0.982 28.84 14.165 9/28/2017 0.401481 2633 57.45 0.002 93.9 28.92
GV-6 9/27/2017 9:38 51.2 33 1.6 14.2 -24.1 -0.871 27.197 0.983 28.82 14.155 9/29/2017 0.40287 2619 57.13 0.002 93.7 28.92
GEM Data Log Velocicalc Manual Velocicalc Log
Static Press. Diff. Press. Baro. Press.Temp.
(°F)
Burke Co., Johns River Landfill, Permit 12-03
CAP Addnedum Page 1 of 2 Joyce Engineering
Appendix B: GEU Pilot Test Data
Table B3: GEU Test of GV-6
Device ID: GEM™2000; Version 2_41 - 08/01/14; LSGAM:6_0_20150403; {2038000911074}
Date/Time CH4 CO2 O2 Balance "AIR"VFD Set GV-5 GV-7 Date Time Vel Flow P T BP
% % % %in.-H2O PSI in.-H2O PSI in.-Hg PSI
CFM Hz In-Wc In-Wc ft/min cfm in.-H2O º F in.-Hg
GEM Data Log Velocicalc Manual Velocicalc Log
Static Press. Diff. Press. Baro. Press.Temp.
(°F)
GV-6 9/27/2017 9:40 50.7 33.2 1.6 14.5 -24.1 -0.871 27.267 0.985 28.82 14.155 9/30/2017 0.404259 2606 56.86 0.002 93.8 28.92
GV-6 9/27/2017 9:42 50.7 33.1 1.6 14.6 -24.1 -0.871 27.241 0.984 28.82 14.155 60 0.4 <0 9/27/2017 9:44:08 2588 56.47 0.003 94.5 28.91
GV-6 9/27/2017 9:44 50.7 33.2 1.7 14.4 -24.1 -0.871 27.256 0.985 28.82 14.155 9/27/2017 9:46:08 2547 55.57 0.004 94.8 28.91
GV-6 9/27/2017 9:46 50.4 33 1.6 15 -24.1 -0.871 27.23 0.984 28.81 14.150 9/27/2017 9:48:08 2499 54.52 0.004 94.9 28.91
GV-6 9/27/2017 9:48 50.4 32.8 1.7 15.1 -23.9 -0.863 27.031 0.977 28.81 14.150 9/27/2017 9:50:08 2458 53.63 0.004 96.2 28.91
GV-6 9/27/2017 9:50 50 33.1 1.8 15.1 -23.6 -0.853 26.877 0.971 28.82 14.155 9/27/2017 9:52:08 2419 52.77 0.004 96.7 28.91
GV-6 9/27/2017 9:52 49.8 32.2 1.8 16.2 -23.5 -0.849 26.634 0.962 28.81 14.150 9/27/2017 9:54:08 2412 52.63 0.004 97.1 28.9
GV-6 9/27/2017 9:54 49.8 32.5 1.8 15.9 -23.3 -0.842 26.507 0.958 28.83 14.160 60 0.3 <0 9/27/2017 9:56:08 2412 52.63 0.004 98.1 28.9
GV-6 9/27/2017 9:56 50.1 32.6 1.8 15.5 -23.3 -0.842 26.467 0.956 28.83 14.160 9/27/2017 9:58:08 2407 52.52 0.003 99.6 28.9
GV-6 9/27/2017 9:58 49.7 32.4 1.9 16 -23.2 -0.838 26.372 0.953 28.83 14.160 9/27/2017 10:00:08 2402 52.39 0.004 100.5 28.9
GV-6 9/27/2017 10:00 49.5 32.4 1.9 16.2 -23.1 -0.835 26.352 0.952 28.83 14.160 60 0.3 <0 9/27/2017 10:02:08 2393 52.2 0.004 100.8 28.9
GV-6 9/27/2017 10:02 49.5 32.3 1.8 16.4 -23.1 -0.835 26.364 0.952 28.81 14.150 9/27/2017 10:04:08 2382 51.97 0.004 101.1 28.9
GV-6 9/27/2017 10:04 49.4 33 1.8 15.8 -23.2 -0.838 26.352 0.952 28.81 14.150 9/27/2017 10:06:08 2379 51.9 0.004 100.4 28.9
GV-6 9/27/2017 10:06 49.2 32.3 1.9 16.6 -23.2 -0.838 26.334 0.951 28.81 14.150 9/27/2017 10:08:08 2381 51.95 0.005 98.5 28.89
GV-6 9/27/2017 10:08 49.3 32.7 1.8 16.2 -23.2 -0.838 26.385 0.953 28.81 14.150 9/27/2017 10:10:08 2376 51.83 0.005 98 28.89
GV-6 9/27/2017 10:10 49.3 32 1.8 16.9 -23.2 -0.838 26.425 0.955 28.81 14.150 9/27/2017 10:12:08 2355 51.38 0.004 99.4 28.89
GV-6 9/27/2017 10:12 49.2 31.8 1.9 17.1 -23.2 -0.838 26.413 0.954 28.83 14.160 9/27/2017 10:14:08 2356 51.39 0.004 99.7 28.89
GV-6 9/27/2017 10:14 49.3 31.9 1.8 17 -23.2 -0.838 26.414 0.954 28.83 14.160 9/27/2017 10:16:08 2359 51.46 0.004 99.5 28.89
GV-6 9/27/2017 10:16 49.4 32.4 1.8 16.4 -23.3 -0.842 26.432 0.955 28.83 14.160 9/27/2017 10:18:08 2350 51.27 0.004 101.3 28.89
GV-6 9/27/2017 10:18 49.1 32.5 2 16.4 -23.3 -0.842 26.439 0.955 28.81 14.150 9/27/2017 10:20:08 2340 51.05 0.002 103.4 28.89
GV-6 9/27/2017 10:20 48.4 32.3 2 17.3 -23.2 -0.838 26.403 0.954 28.83 14.160 9/27/2017 10:22:08 2340 51.04 0.002 105.2 28.9
GV-6 9/27/2017 10:22 49 32.3 1.9 16.8 -23.2 -0.838 26.37 0.953 28.83 14.160 60 0.3 <0 9/27/2017 10:24:08 2330 50.84 0.001 106.1 28.9
GV-6 9/27/2017 10:24 48.4 32.2 2 17.4 -23.2 -0.838 26.355 0.952 28.81 14.150 9/27/2017 10:26:08 2321 50.64 0.001 106.9 28.9
GV-6 9/27/2017 10:26 48.6 31.6 2 17.8 -23.2 -0.838 26.331 0.951 28.81 14.150 9/27/2017 10:28:08 2311 50.42 0.002 107 28.9
GV-6 9/27/2017 10:28 48 32.8 1.9 17.3 -23.2 -0.838 26.352 0.952 28.81 14.150 9/27/2017 10:30:08 2307 50.34 0.002 106.5 28.9
GV-6 9/27/2017 10:30 47.8 31.9 2 18.3 -23.1 -0.835 26.355 0.952 28.81 14.150 9/27/2017 10:32:08 2357 51.43 0.002 105.4 28.9
GV-6 9/27/2017 10:32 47.5 32.2 1.9 18.4 -23.2 -0.838 26.391 0.953 28.83 14.160 60 0.3 <0 9/27/2017 10:34:08 2017 44 0.002 105.2 28.9
GV-6 9/27/2017 10:34 0.9 9.3 16.9 72.9 -3.5 -0.126 7.196 0.260 28.81 14.150 9/27/2017 10:36:08 1308 28.54 0.002 103.2 28.9
GV-6 9/27/2017 10:36 0 2.1 19.9 78 -0.4 -0.014 3.828 0.138 28.83 14.160 0
Burke Co., Johns River Landfill, Permit 12-03
CAP Addnedum Page 2 of 2 Joyce Engineering
Appendix C
LFG Control Construction Specifications
LFG Control System Trench., Backfill, & Compt for Pipelines Joyce Engineering, Inc.
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SECTION 02221
TRENCHING, BACKFILLING, AND COMPACTING FOR PIPELINES
PART 1 GENERAL
1.01 WORK INCLUDED
A. Excavating Trenches, backfilling and compacting for installation of HDPE Landfill
gas and condensate drainage pipes.
B. Dewatering, protection, and maintenance of trenches, support of existing structures,
sheeting and shoring, hauling and disposal of excess excavated materials and fill.
1.02 REFERENCES
A. OSHA 29 CFR Part 1926, Subpart P, Occupational Safety and Health Standards -
Excavations.
PART 2 PRODUCTS
2.01 BACKFILL MATERIALS
A. Re-use excavated soil for backfill.
PART 3 EXECUTION
3.01 PREPARATION AND RESTORATION
A. Remove sod, topsoil, and other surface treatment and restore to original condition or
better upon completion of the Work.
B. Material from each distinct soil layer should be segregated and stockpiled separately
from other soil layers during excavation.
C. After excavation, all disturbed soil strata should be restored to their original
composition, thicknesses, compaction level and moisture content.
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3.02 PROTECTION
A. Protect excavations by shoring, bracing, sheet piling, or other methods required to
prevent cave-in or loose soil from falling into excavation.
B. Place excavated and other material 2 feet minimum back from edge of trench
excavation.
C. Minimum trench excavation slope to conform with OSHA 29 CFR Part 1926,
Subpart P.
D. Underpin adjacent structures which may be damaged by excavation Work, including
utilities and piping.
E. Notify OWNER and ENGINEER immediately of unexpected subsurface conditions.
F. Protect bottom of excavations from frost.
3.03 TRENCHING
A. Excavate to the required alignment and grade.
B. No adjustment in compensation will be made for grade adjustments not in excess of 1
foot above or below the plan elevations.
C. Remove any water that accumulates in trench, and construct ditches, flumes, and
dams to direct water away from excavation.
D. ENGINEER may limit the amount of open trench where field conditions or plant
operations require.
E. ENGINEER may order additional excavation where unsuitable soil conditions are
encountered.
F. Promptly dispose of excess excavation off-site or in area designated by OWNER.
G. Bottom of trench shall be compacted prior to laying pipe, in accordance with Project
Specifications.
3.04 UTILITY TEST HOLES
A. Where potential utility conflicts are anticipated, uncover utility lines well in advance
of trench excavation.
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B. Determine grade of the utility line.
C. Backfill and restore disturbed area to original condition.
3.05 BEDDING AND HAUNCHING
A. Minimum bedding requirements for pipes: The HDPE pipe shall be placed on
compacted soil bedding as shown on the Contract Drawings. If bedding material is
necessary to obtain grades, it shall be of nature that will not damage the piping during
placement and backfilling.
3.06 BACKFILLING
A. Backfill immediately following completion of pipe installation.
B. Take necessary precautions with backfill and construction operations to protect
completed utility system from damage.
C. Backfill with care around structures.
D. Backfill to the original ground elevation unless shown otherwise on the Contract
Drawings.
E. Place and compact backfill in accordance with Project Specifications.
F. If surveying of pipe spot elevations is not performed prior to backfilling, allow for
access to top of pipe for future surveying.
3.07 FIELD QUALITY CONTROL
A. CONTRACTOR shall be responsible for quality control.
END OF SECTION 02221
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SECTION 02618
HIGH-DENSITY POLYETHYLENE (HDPE) PIPE
PART 1 GENERAL
1.01 WORK INCLUDED
A. Landfill gas (LFG) piping
1.02 REFERENCES
A. ASTM D1248 - High-density polyethylene (HDPE) weight resin for pipes and
fittings.
B. ASTM D2513 - Industrial molded fittings for high-density polyethylene (HDPE)
pipes.
C. ASTM D3261 - Butt fittings for high-density polyethylene (HDPE) pipes.
1.03 DELIVERY, STORAGE, AND HANDLING
A. Protect pipe from sun, elements, and weather changes.
B. Store pipe in areas that are safe from normal daily plant operations and from
construction activities.
1.04 SUBMITTALS
A. Submit product data under provisions of Project Specifications.
B. Include data on pipe materials, pipe fittings, and accessories.
C. Inspect material a minimum of 7 days prior to installation, and indicate in writing any
deficiencies to the OWNER.
LFG Control System HDPE Pipe & Fittings Joyce Engineering, Inc.
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PART 2 PRODUCTS
2.01 ACCEPTABLE MANUFACTURERS
A. Acceptable manufacturers of LFG pipe include, but are not limited to:
1. Spirolite Corporation
4094 Blue Ridge Industrial Parkway
Norcross, GA 30071
2. Plexco
3240 N. Mannheim Road
Franklin Park, IL 60131
3. CRS PolyPipe
Drawer HH
Gainesville, TX 76240
4. Phillips Driscopipe, Inc.
2929 North Central Expressway
Richardson, TX 75083
2.02 MATERIALS
A. Pipe: All HDPE Pipe – SDR 17, PE3408, minimum 2% carbon black, cell
classification 345444C (or other classification approved by the ENGINEER).
B. Joints: Butt, heat fusion process as per manufacturer instruction. Joints at
connections between phases may be electrofusion type couplings. Saddle
connections by sidewall heat plate machine (not by extrusion).
C. Fittings: Fittings may be molded or prefabricated by the manufacturer.
PART 3 EXECUTION
3.01 INSPECTION
A. Inspect pipe, fittings, and other appurtenances before installation to verify quality of
material.
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3.02 PREPARATION
A. Ream pipe and tube ends. Remove burrs.
B. Remove dirt and other contaminants, inside and outside, from pipe and fitting
materials before assembly.
C. Make straight field cuts without chipping or cracking pipe.
3.03 INSTALLATION
A. Make heat fusion joints in accordance with manufacturer’s recommended procedures.
B. Install pipe and fittings to the line and grade specified on the drawings.
C. Verify that installed grades meet requirements by providing a survey as specified in
Project Specifications.
C. The maximum allowable tolerance for grade is 0.10 foot.
D. Construct bedding material and general soils over pipe with care to avoid damage to
pipe. Minimize traffic and turning of traffic over pipe.
E. Backfill pipe in accordance with Project Specifications.
F. Compact pipe trenches by hand or mechanical tamping in 6 in. layers.
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3.04 FIELD QUALITY CONTROL
A. ENGINEER to observe all pipe, joints and fittings prior to backfilling.
B. Flush pipe with sewer cleaning equipment when construction is completed. Submit
details of flushing program to ENGINEER for approval. Provide detail of temporary
flushing method that will allow free flow discharge of flush water from low end of
pipe so that flush water may be observed by the ENGINEER. Flush until water runs
clear. Flushing program is to remove all debris including HDPE cuttings, soil,
gravel, and all contaminants from pipelines. CONTRACTOR to provide all water
and equipment required to complete the flushing.
C. Air testing: Air test the system in accordance with the pipe manufacturer’s
instructions and as follows, and submit all test results to ENGINEER.
1. Pressure-test all pipe, fittings, and appurtenances except piping below landfill
gas well heads. Mechanically plug the ends of pipelines to be tested and
close gate valves at all wells. Apply either a positive or negative gauge
pressure of 2.5 pounds per square inch (psi) or greater. Close the valve on the
pressurizing unit, and monitor the pressure for a minimum of 30 minutes. A
system pressure loss of less than 0.5 psi during the testing period shall be
considered acceptable.
2. Pressure tests shall be performed in the presence of the ENGINEER. Give
48-hour notice to ENGINEER prior to testing. A written report shall be
prepared by the CONTRACTOR for each test and submitted to the
ENGINEER. Provide all gauges, pumps, pipe, connections, and all other
necessary apparatus to conduct tests.
3. If results of tests performed do not conform to requirements as stated herein,
CONTRACTOR shall make the necessary repairs and repeat tests, as required
until satisfactory results are obtained.
END OF SECTION 02618
LFG Control System Gas Extraction Unit Joyce Engineering, Inc.
John’s River Landfill 02900-1 December 2017
Burke County, NC
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SECTION 02900
LANDFILL GAS EXTRACTION UNIT (GEU)
PART 1 GENERAL
1.01 DESCRIPTION OF WORK, DEFINITIONS & RESPONSIBILITIES
A. System Description
Gas Extraction Unit
This specification covers the design and performance requirements for a skid-mounted
landfill gas extraction unit (GEU).
The GEU shall be designed to extract landfill gas at the specified pressure and flow. The
design of the GEU shall strive for efficiency, one that minimizes initial cost, seeks to operate
at the lowest possible horsepower, but meets all required performance and material standards
as described in this specification.
The GEU shall consist of: a blower; electric motor; suction liquid knockout vessel; piping;
air filter; manual butterfly valve; controls; and skid.
The GEU shall be designed for outdoor installation. Design objectives shall strive to avoid
complex control systems, facilitate ease of maintenance and to ensure a high degree of
equipment reliability. Each piece of equipment shall be selected for its performance
characteristics and proven satisfactory operation in landfill gas extraction applications. The
design shall be an efficient system applying proven engineering practices and state-of-the-art
technology. All components shall be new, of high quality, free from defects in manufacture
and workmanship, low in maintenance, and intended for a long service life.
B. Definitions
1. Vendor - Manufacturer/Supplier of the landfill gas GEU skid system or components
thereof.
2. Contractor - General Contractor or his Subcontractor performing installation and
construction work at the jobsite.
C. Contractor Responsibility
Contractor shall be responsible for furnishing all labor, materials, equipment, freight, taxes
and supervision for the design, fabrication, delivery, installation and startup of the
equipment as described herein, with all appurtenances necessary to perform the specified
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function, whether expressly described or not, F.O.B. jobsite. Contractor shall provide all
coordination with Vendor(s) for the GEU system or system component design, manufacture,
delivery, installation and startup.
D. Work By Others
1. Providing power to a utility pole at the GEU location.
1.02 SUBMITTALS
1. Equipment list, specifications and equipment flow charts.
2. Operation and Maintenance Manuals. Provide written instructions to enable
the installation, operation and maintenance of the GEU.
1.03 SITE CONDITIONS
A. The unit will be located at the Johns River Landfill in Burke County, North Carolina.
1.04 GENERAL SERVICE DESCRIPTION
A. Functional Conditions
1. Landfill Gas Inlet Design Conditions
a. Suction Pressure, max. -15 " H20
b. Suction Temperature as produced
c. Design Flow Rate, wet 140 scfm
d. Water Content saturated
2. Suction temperature of the gas may vary between 30oF and 120oF.
PART 2 PRODUCTS
2.01 BLOWER
A. The blower assembly shall be capable of delivering 140 SCFM of landfill gas at
minus 15 in.- w.c. total pressure head at the inlet.
B. The blower must be corrosion resistant and safe to operate with explosive gas, since
the landfill gas that will flow through it is expected to be approximately 50%
methane.
C. Motor and blower housings shall be suitable for exterior service and be provided with
nameplate information including manufacturer, model number, serial number, and
capacity and rating information.
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D. Blower impellers or fan blades shall be made of a non-sparking material such as
aluminum.
E. Motor shall be high efficiency, totally enclosed, and fan cooled (TEFC).
F. Provide expansion/vibration joints between the blower inlet and outlet and connected
piping.
2.02 CONDENSATE KNOCK-OUT POT
A. Condensate knock-out pot complete with the following:
• HDPE vessel.
• Flanged top, inlet and outlet for accessibility and maintenance.
• Manual liquid drain valve and high level shutoff switch.
• Stainless steel wire mesh pad demister.
• Air filter.
• A differential pressure gauge to be mounted on the vessel and connected to taps
on the upstream and downstream side of the mesh pad.
2.03 CONTROL SYSTEM
A. Control System Description
1. Electric blower motor starter ON/OFF switch with either:
a. Explosion proof enclosure, or
b. Mounted at least 10 feet away from blower with NEMA 4 enclosure.
2.04 STEEL SKID
1. Heavy duty AISC designed structural steel skid.
2. Skid to be completely galvanized after fabrication (corrosion resistant).
2.05 MANUAL BUTTERFLY VALVE
1. One (1) manual, lever operated butterfly valves to be located as shown on the Drawings.
Manual butterfly valves shall be Asahi Type 57 (or approved equivalent), lined body
design and bubble-tight seal (meeting or exceeding Class VI as defined by American
National Standard Institute). Liner shall be molded and formed around the body,
functioning as gasket seals with convex ring design on each side of the valve for lower
bolt tightening torque and valve body shall have molded body stops and seat relief area to
prevent over tightening of mating flanges.
2.06 PIPING
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1. All piping to be HDPE or 304 SS Schedule 10S.
2. Gaskets shall be a synthetic fiber type with an NBR binder, Donex 660 or equal for
stainless steel piping or neoprene for HDPE piping.
3. All stainless steel flanges to be 150# RFSO.
4. All piping to be fully assembled, mounted, and supported from the outlet of the knock
out pot to the skid edge.
5. Piping and piping fabrication shall be consistent with recognized industry specifications.
6. Piping wall thickness shall be designed for a minimum of 1.5 times the operating
pressure.
7. Gas piping, where it is possible for liquids to collect, shall have drain connections
(manual ball valves) and shall ensure complete drainage through low points without
disassembly. Low points in gas piping are to be avoided.
2.07 CONSTRUCTION
A. Piping and equipment arrangements shall be designed to provide adequate clearance
areas and safe access for operation and maintenance.
B. The fabrication of the skid shall conform in dimensions for installation on the site
maps.
2.08 INSPECTION AND TESTING
A. The Engineer's representative shall have the right to reject any components that do
not conform with the specifications. The Engineer's acceptance of shop test results
shall not constitute waiver of Vendor's obligation to provide equipment which meets
the design operating requirements of the GEU skid.
PART 3 EXECUTION
3.01 WARRANTY
It shall be the responsibility of the Contractor to design and provide an integrated system
which meets all requirements of the specifications. The GEU shall be supplied as a complete
and operable package and shall be warrantied as a single package for a minimum period of
18 months after shipment and 12 months after start-up.
3.02 INSTALLATION
Contractor will install the GEU in accordance with the installation instructions provided by the
Vendor.
A. Install all equipment in accordance with manufactures requirements, approved
submittals, and the Drawings.
LFG Control System Gas Extraction Unit Joyce Engineering, Inc.
John’s River Landfill 02900-5 December 2017
Burke County, NC
\\JEI-GSO-FS1\Projects\Burke County\Johns River Waste Management Facility\Groundwater\CAP\CAP Revisions\2017 Active Gas Extraction\2017 RIC Office Work\To Submit\02900 LFG Extraction Unit.doc
B. Provide neoprene isolation pads between the blower and the skid base.
C. Provide electrical installation in accordance with electrical codes and manufacturers
requirements. Obtain electric permit, if required.
D. “Danger - No Smoking” signs shall be posted on all four sides of the GEU skid.
E. Touch-up any damaged coatings.
END OF SECTION 02900
Appendix D
KYGAS Modeling Output
burke gas.TXT
* * * * * * * * * * * * * K Y G A S * * * * * * * * * * * * *
* *
* Gas Network Analysis Software *
* *
* CopyRighted by KYPIPE LLC (www.kypipe.com) *
* Version: 9.004 11/15/2017 *
* *
* Interface: Classic *
* Pipe2018 *
* *
* * * * * * * * * * * * * * * * * * * * * * * * * * * * * * *
INPUT DATA FILE NAME FOR THIS SIMULATION = c:\users\MHOFME~1\desktop\burke\BUR
KEG~1.KYP\burke_ga.DAT
OUTPUT DATA FILE NAME FOR THIS SIMULATION = c:\users\MHOFME~1\desktop\burke\BUR
KEG~1.KYP\burke_ga.OT2
DATE FOR THIS COMPUTER RUN : 12‐14‐2017
START TIME FOR THIS COMPUTER RUN : 11:22:10:61
SUMMARY OF DISTRIBUTION SYSTEM CHARACTERISTICS:
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
NUMBER OF PIPES = 15
NUMBER OF JUNCTION NODES = 15
UNITS SPECIFIED = ENGLISH
A CONSTANT DENSITY FLUID IS SPECIFIED ‐ DENSITY = .04POUNDS/CUBIC FOOT
ABSOLUTE VISCOSITY = .275E‐06 POUND SECONDS/SQUARE FOOT
USER SPEC. FLOW UNITS (USFU) = SCF / MIN.
USER SPEC. PRESSURE UNITS(USPU) = INCHES OF WATER (GAUGE)
‐‐‐‐‐‐‐ SUMMARY OF PIPE NETWORK GEOMETRIC AND OPERATING DATA ‐‐‐‐‐‐‐
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
PIPE NODE NODE LENGTH DIAM. ROUGHNESS SUM‐M PUMP ELEVATION
NAME #1 #2 (FT.) (IN.) (MILLIFEET) FACT. ID CHANGE
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
Page 1
burke gas.TXT
P‐1 J2 J3 103.0 8.1 ****** .4 0 ‐2.0
P‐2 J3 J4 102.0 8.1 ****** .4 0 ‐2.0
P‐3 J4 J5 94.0 8.1 ****** .4 0 ‐2.0
P‐4 J5 J6 98.0 8.1 ****** .4 0 ‐2.0
P‐5 J6 J7 90.0 8.1 ****** .4 0 ‐2.0
P‐6 J2 GV6 25.0 4.0 ****** 1.8 0 4.0
P‐7 J7 GV1 116.0 4.0 ****** 1.8 0 24.0
P‐8 J6 GV2 90.0 4.0 ****** 1.8 0 22.0
P‐9 J5 GV3 71.0 4.0 ****** 1.8 0 20.0
P‐10 J4 GV4 60.0 4.0 ****** 1.8 0 16.0
P‐11 J3 GV5 44.0 4.0 ****** 1.8 0 10.0
P‐12 J7 R‐1 51.0 8.1 ****** .5 0 ‐2.0
P‐13 J2 J1 93.0 8.1 ****** .4 0 2.0
P‐14 J1 GV7 5.0 4.0 ****** 1.8 0 .0
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
JUNCTION NODE ELEV DEMAND FPN
NAME TITLE (USFU) PRESSURE
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
GV1 1122.00 ‐20.00
GV2 1122.00 ‐20.00
GV3 1122.00 ‐20.00
GV4 1120.00 ‐20.00
GV5 1116.00 ‐20.00
GV6 1112.00 ‐20.00
GV7 1110.00 ‐20.00
J1 1110.00 .00
J2 1108.00 .00
J3 1106.00 .00
J4 1104.00 .00
J5 1102.00 .00
J6 1100.00 .00
J7 1098.00 .00
R‐1 1096.00 .00 ‐15.00
================================================================================
Set = 0
==================== RESULTS FOR THIS SIMULATION FOLLOW =================
Solution was obtained in 1 trials
Flow Accuracy = .0000E+00[ < .500E‐02]
Page 2
burke gas.TXT
RV Accuracy = .0000E+00[ < .100E‐02]
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
PIPE NODE NODE FLOW LOSS VELOCITY DENSITY FRICTION AREA
NO. #1 #2 (USFU) (USPU) (FT/S) (#/CF ) FACTOR RATIO
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
P‐1 J2 J3 40.000 .03 3.42 .042 .1468
P‐2 J3 J4 60.000 .07 5.12 .042 .1460
P‐3 J4 J5 80.000 .12 6.83 .042 .1456
P‐4 J5 J6 100.000 .20 8.54 .042 .1453
P‐5 J6 J7 120.000 .26 10.25 .042 .1452
P‐6 J2 GV6 ‐20.000 .12 6.87 .042 .2457
P‐7 J7 GV1 ‐20.000 .51 6.87 .042 .2457
P‐8 J6 GV2 ‐20.000 .40 6.87 .042 .2457
P‐9 J5 GV3 ‐20.000 .32 6.87 .042 .2457
P‐10 J4 GV4 ‐20.000 .27 6.87 .042 .2457
P‐11 J3 GV5 ‐20.000 .20 6.87 .042 .2457
P‐12 J7 R‐1 140.000 .21 11.96 .042 .1450
P‐13 J2 J1 ‐20.000 .01 1.71 .042 .1491
P‐14 J1 GV7 ‐20.000 .03 6.87 .042 .2457
R‐1 R‐1 R‐1 ‐139.450 .00 .00 .042********
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
JUNCTION NODE DEMAND PRESSURE PRESSURE PRESSURE DENSITY
NAME TITLE (USFU) (USPU) (PSIA) (PSIG) #/CF
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
GV1 ‐20.00 ‐14.49 14.17 ‐.52 .042
GV2 ‐20.00 ‐14.34 14.18 ‐.52 .042
GV3 ‐20.00 ‐14.23 14.18 ‐.51 .042
GV4 ‐20.00 ‐14.14 14.19 ‐.51 .042
GV5 ‐20.00 ‐14.10 14.19 ‐.51 .042
GV6 ‐20.00 ‐14.12 14.19 ‐.51 .042
GV7 ‐20.00 ‐14.18 14.19 ‐.51 .042
J1 .00 ‐14.21 14.18 ‐.51 .042
J2 .00 ‐14.20 14.18 ‐.51 .042
J3 .00 ‐14.22 14.18 ‐.51 .042
J4 .00 ‐14.28 14.18 ‐.51 .042
J5 .00 ‐14.38 14.18 ‐.52 .042
J6 .00 ‐14.56 14.17 ‐.52 .042
J7 .00 ‐14.81 14.16 ‐.53 .042
R‐1 .00 ‐15.00 14.16 ‐.54 .042
* This designates the use of default density in a low pressure region
Page 3
burke gas.TXT
THE NET SYSTEM DEMAND (USFU) = ‐140.000
SUMMARY OF INFLOWS(+).AND.OUTFLOWS(‐) :
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
NAME FLOW (USFU) FPN TITLE
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
R‐1 ‐139.4 R‐1
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
SUMMARY OF MINIMUM.AND.MAXIMUM VELOCITIES (FT/S)
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
MINIMUM MAXIMUM
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
R‐1 .00 P‐12 11.96
P‐13 1.71 P‐5 10.25
P‐1 3.42 P‐4 8.54
P‐2 5.12 P‐14 6.87
P‐3 6.83 P‐3 6.83
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
SUMMARY OF MINIMUM.AND.MAXIMUM LOSS/1000. (PSI )
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
MINIMUM MAXIMUM
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
R‐1 .00 P‐14 .16
P‐13 .00 P‐11 .16
P‐1 .01 P‐12 .14
P‐2 .03 P‐5 .10
P‐3 .05 P‐4 .07
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
SUMMARY OF MINIMUM.AND.MAXIMUM PRESSURES (USPU)
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
MINIMUM MAXIMUM
‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐
R‐1 ‐15.00 GV5 ‐14.10
J7 ‐14.81 GV6 ‐14.12
J6 ‐14.56 GV4 ‐14.14
GV1 ‐14.49 GV7 ‐14.18
J5 ‐14.38 J2 ‐14.20
************************* END OF KYGAS SIMULATION ************************
Page 4