NCG510002_Application_20180503

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May 3, 2018
RECEIVEDIDENRIDW
North Carolina Department of Environmental Quality MAY 11 2.018
Division of Water Resources
1617 Mail Service Center Water Resources
Raleigh, North Carolina 27699-1617 permitting Section
Attention: Mr. Derek Denard
Reference: Blue Ridge Hospital Spruce Pine Discharge Permit
Blue Ridge Hospital—Spruce Pine
125 Hospital Drive
Spruce Pine, Mitchell County, North Carolina
NCDEQ, UST Incident No. 3659
S&ME Project No.4305-17-109E
Dear Mr. Denard:
S&ME, Inc. (S&ME) is submitting the attached application for coverage under general permit NCG510000
(Attachment I). An existing groundwater remediation system (previously covered under permit NCG510002) is
currently in operation at the subject property to remove petroleum free product and petroleum-impacted
groundwater stemming from a leak from an underground storage tank(UST) system. S&ME is currently under
contract with the North Carolina Department of Environmental Quality UST Section to perform the operations and
maintenance of the groundwater remediation system. This permit application is being submitted on behalf of the
responsible party, Blue Ridge Hospital, at the request of the NCDEQ UST Section. On April 19, 2018, via electronic
mail, Mr.Jeff Dulaney, representative of Blue Ridge Hospital,Inc., authorized S&ME to submit this permit
application on behalf of Blue Ridge Hospital, Inc. The documentation of authorization is included in Attachment
H.
4 Importance of the Treatment System
As will be summarized in greater detail in the attached specification package, the current groundwater treatment
system removes petroleum free product and petroleum-impacted groundwater that is present just west of the
hospital structure. The continued operation of the system is imperative to remediate the contaminated
groundwater and, more importantly, to reduce the potential for petroleum-impacted groundwater to discharge
aboveground at the toe of the slope adjacent to Highway 19E. This occurrence would lead to surface migration of
petroleum contaminants via stormwater management features— meaning the contaminants would be directly
discharged to nearby surface water bodies, such as Beaver Creek and the North Toe River.
Effluent Discharge Options
In an effort to determine if there is an alternative method to discharge the system effluent, S&ME contacted the
Spruce Pine Wastewater Treatment plant to determine the feasibility of sending the treated system effluent to the
S&ME,Inc.144 Buck Shoals Road,Suite C-3 I Arden, NC 28704 I p 828.687.9080 I www.smeinc.com

NCG510000 New Application
8) Treatment system components: [Required by 15A NCAC 02H .0105(c)(3)]
Please note: Final design specifications for the actual system that will be installed must be included in this section.
Do not submit this application if only bid specifications are known.
Check all of the following that apply:
® Oil/Water Separator ® Air Stripper ® Carbon Adsorption ® Filters
❑ Other:
a) If an Oil/Water separator is present,please provide the following information:
i) Rated flow capacity of the unit(in GPM): 34 Rpm(a,20 microns to 77 Rpm(aii 30 microns
ii) Volume of unit(gal): 56-gallon sludge collection chamber
iii) Detention time(min): Unknown
iv) Free product disposal method: Gravity to an AST
b) If an air stripper is present,please provide the following information:
i) Rated flow capacity of the unit(in GPM): 1 - 125
ii) Air provided for stripping(in CFM): 900
iii) Air to Water ratio: 135:1
iv) Number of trays(if applicable): 3
(Removal efficiencies for all chemicals of concern should be included in this submittal. Efficiencies should
be expressed as a percentage,i.e.98%or 0.98)
c) If carbon adsorption is present,please provide the following information:
i) Rated flow capacity of the unit(s)(in GPM): 75
ii) Number of carbon units and arrangement if number exceeds one(i.e.,in parallel or in series): 2,series
iii) Pounds of carbon in each unit: 1,000
iv) Specify carbon breakthrough time: Unknown
(The method used to calculate breakthrough time must included in the submittal.)
d) If filters are used,please provide the following information:
i) Rated flow capacity of each unit(s)(in GPM): Up to 220 gpm
ii) Arrangement of particulate filters within the system: ❑ Parallel ® Series
e) Solids disposal method:
0 If other components to be included,please specify: See description of process.
9) Receiving waters: [Required by 15A NCAC 02H .0105(cX 1)1
a) What is the name of the body or bodies of water (creek, stream, river, lake, etc.) that the facility wastewater
discharges into? If the wastewater discharge is to a separate storm sewer system(4S),name the operator of the 4S
(e.g.City of Raleigh). Beaver Creak[Stream Index 7-2-41-(2)j
b) Stream Classification(i.e.WS-IV,C,SA,etc): C; Tr,
10) Alternatives to direct discharge:
[Evaluation required by G.S. § 143-215.1(b)(5)(a)and 15A NCAC 02H.0105(c)(2)]
Address the feasibility of implementing each of the following non-discharge alternatives:
a) Connection to a Municipal or Regional Sewer Collection System
b) Subsurface disposal(including nitrification field,infiltration gallery,injection wells,etc.)
c) Spray irrigation
Page 3 of 5 Revised 9/1/13

NCG510000 New Application
The alternatives to discharge analysis should include boring logs and/or other information indicating that a subsurface
system is neither feasible nor practical as well as written confirmation indicating that connection to a POTW is not an
option. It should also include a present value of costs analysis as outlined in the Division's "Engineering Alternatives
Analysis(EAA)Guidance Document".
Additional Application Requirements:
For new or proposed discharges,the following information must be included in triplicate with this application or it will be
returned as incomplete;per 15A NCAC 02H .0105(c).
a) 7.5 minute series USGS topographic map(or a photocopied portion thereof)with discharge location clearly indicated.
b) A site map clearly tracing the pathway of the discharged water from the site to its discharge point,if the discharge is
not directly to a stream.
c) If the discharge will cross or empty into any easements, right-of-ways, or other public/private property, i.e. DOT,
utilities, ditches, etc., before entering the permitted discharge stream, proof that approval was received from the
appropriate landowners and/or agencies must be provided prior to issuance of the permit.
d) If this application is being submitted by a consulting engineer(or engineering firm),include documentation from the
applicant showing that the engineer (or firm) submitting the application has been designated an authorized
representative of the applicant;per 15A NCAC 02H.0138(b)(1).
e) Final plans for the treatment system(if application is for a new or modified permit). The plans must be signed and
sealed by a North Carolina registered Professional Engineer and stamped-"Final Design-Not released for
construction;"per 15A NCAC 02H.0139.
f) Final specifications for all major treatment components (if application is for a new or modified permit). The
specifications must be signed and sealed by a North Carolina registered Professional Engineer and shall include a
narrative description of the treatment system to be constructed,per 15A NCAC 02H .0139.
g) Site map identifying the location of the monitoring wells,the recovery wells,and the treatment system unit.
h) Analytical monitoring data which sufficiently characterizes the type and concentration of contaminants on site. This
includes a listing of any chemicals found with the maximum observed concentrations reported. The data provided
must be no older than one year prior to the date of this application. At a minimum,the following parameters must
be reported: Benzene,Toluene,Ethylbenzene,Xylene,Lead,Phenol,MTBE,and 1,2-Dichlorethane.
Page 4 of 5 Revised 9/1/13

NCG510000 New Application
CERTIFICATION
I certify that I am familiar with the information contained in this application and that to the best of my knowledge
and belief such information is true, complete, and accurate.
Printed Name of Person Signing: David R. Loftis,P.E.
Title: Senior Engineer
(Please review 15A NCAC 02H .0106(e)for authorized signing officials)
f1�J e0 May 3,2017
(Signature of Applicant) (Date Signed)
North Carolina General Statute$ 143-215.6B provides that:
Any person who knowingly makes any false statement representation, or certification in any application, record,report,
plan, or other document filed or required to be maintained under this Article or a rule implementing this Article; or who
knowingly makes a false statement of a material fact in a rulemaking proceeding or contested case under this Article;or
who falsifies,tampers with,or knowingly renders inaccurate any recording or monitoring device or method required to be
operated or maintained under this Article or rules of the Commission implementing this Article,shall be guilty of a Class
2 misdemeanor which may include a fine not to exceed ten thousand dollars($10,000). 18 U.S.C. Section 1001 provides
a punishment by a fine or imprisonment not more than 5 years,or both,for a similar offense.
• • • • •
This application must be accompanied by a check or money order for$100.00 1per G.S.$143-215.3(a)(1b)l
made payable to:
NCDENR
• • • • •
Mail this application and one copy of the entire package (with check) to:
NC DENR/DWR/Water Quality Permitting Section
1617 Mail Service Center
Raleigh, North Carolina 27699-1617
Attn: Charles Weaver
Final Checklist
This application will be returned as incomplete, as allowed by 15A NCAC 02H .0107(b),unless all of the
following items have been included:
['Complete application with all supporting documents(plus one copy of entire package)
❑ Check or money order for$100.00, payable to NCDENR w/ DEC. Z.o n fl �G o tV�
2/3 copies of county map or USGS quad sheet with location of facility clearly marked on map
2/3 sets of plans and specifications signed and sealed by a North Carolina P.E. (if new or modified permit)
2/Thorough responses to items 1-11 on this application
DI/Alternatives analysis including present value of costs for all alternatives
Note: The submission of this document does not guarantee the issuance of an NPDES permit.
Page 5 of 5 Revised 9/1/13

Attachment II - Blue Ridge Hospital, Inc. Authorization Email

Archived:Thursday,April 26,2018 2:0134 PM
From:Jeff Dulaney
Sent:Thursday,April 19,2018 5:19:43 PM
To:Bradley S.Keyse
Cc:David Loftin;Michael Mace
Subject:RE:Blue Ridge Hospital Permit
Importance:Normal
Yes please submit permit application. I am unaware of other NPDES permits associated with this facility. Thanks
From:Bradley S.Keyse[mailto:[e-mail]]
Sent:Thursday,April 19,2018 1:36 PM
To:Jeff Dulaney<[e-mail]>
Cc:David Loftis<[e-mail]>
Subject:[EXTERNAL]Blue Ridge Hospital Permit
Jeff,
Will you confirm that the Blue Ridge Hospital,Inc.authorizes S&ME to submit the NPDES permit application for the groundwater remediation system at 125 Hospital
Drive in Spruce Pine, NC on behalf of Blue Ridge Hospital,Inc.?
Also do you know of any other NPDES permits associated with the hospital?
Thank you,
Bradley S.Keyse, E.I.
Environmental Staff Professional
S&ME
& 44 Buck Shoals Road,Suite C-3
Arden,NC 28704 map
_
0:828.483.3013
III M:828.329.3367
www.smeinc.com
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Attachment III — Groundwater Remediation System Specifications

II _
Groundwater Remediation System Specifications
Blue Ridge Hospital — Spruce Pine
NCDEQ Incident No. 3659
125 Hospital Drive 0`\`,►CR,,,,�
Spruce Pine, Mitchell County, North Car : 4.ssio' ' ';
S&ME Project No. 4305-17-109E ,� �� /1_
_ • 183.5
9 �
111
PREPARED FOR'
NCDEQ, UST Section
1646 Mail Service Center
Raleigh, NC 27699
DPF-DAPEn P Y:
S&ME, Inc.
44 Buck Shoals Road, Suite C-3
Arden, NC 28704
May 3, 2018

Groundwater Remediation System Specifications
MI/ft &
Blue Ridge Hospital-Spruce Pine, NCDEQ Incident No. 3659
Spruce Pine, Mitchell County, North Carolina
S&ME Project No.4305-17-109E `
Table of Contents
1.0 Description of Groundwater Remediation System 1
1.1 Background 1
1.2 Recovery Wells 1
1.3 Interceptor Trench 2
1.4 Flow Origin and Volume 2
1.5 Wastewater Characterization 2
2.0 System Design 3
2.1 Oil/Water Separator 3
2.2 Shallow Tray Air Stripper 4
2.3 Filters 5
2.3.1 50 Micron Bag Filters 5
2.3.2 10 Micron Bag Filters 5
2.4 Activated Carbon Units 5
2.5 Other Major Components 6
2.5.1 Batch Tank 6
2.5.2 Batch Tank Transfer Pump 6
2.5.3 Shallow Tray Stripper Transfer Pump 6
2.5.4 Air Compressor 7
2.6 Controls and Alarms 7
Appendices
Appendix I-Figures
Appendix II-Site Photographs
Appendix III-Pneumatic Pumps Specifications
Appendix IV-System Influent Laboratory Report
Appendix V-Oil/Water Separator Specifications
Appendix VI-Shallow Tray Air Stripper Software Output
Appendix VII-Shallow Tray Air Stripper Specifications
Appendix VIII-Particulate Filter Specifications
Appendix IX-Carbon Vessel Specifications
Appendix X-Specification of Other Components
May 3, 2018 ii

Nam
Groundwater Remediation System Specifications
Blue Ridge Hospital—Spruce Pine, NCDEQ Incident No. 3659 amp
Spruce Pine, Mitchell County, North Carolina I
maw
S&ME Project No. 4305-17-109E
1.0 Description of Groundwater Remediation System
1.1 Background
The UST system installation contractor failed to connect the excess fuel return line from the exterior foundation
wall of the boiler room (part of the main hospital building at that time) to the 20,000-gallon UST. Excess fuel not
used by the boiler discharged to the subsurface rather than returning to the UST system. The release was
discovered in May 1988. From 1988 to 2007, soil and groundwater assessment activities were conducted to
determine the extent of the release to the soil and groundwater. The groundwater beneath the hospital
historically flows to the northwest toward Beaver Creek, a tributary of the North Toe River, along with the
petroleum free product and petroleum-impacted groundwater. The impacted area is located on a localized
topographic high and there is a relatively steep gradient from the source area to the northern property boundary
along Highway 19E.
In 1994, a remediation system consisting of a groundwater and free product recovery system was installed and
began operation. The existing system was designed to induce hydraulic control over the groundwater
contaminant plume by reducing the migration rate of the plume as it travels northwest towards Highway 19E and
then to Beaver Creek. A portion of the system was also designed to capture shallow, contaminated groundwater
in the vicinity where the contaminant plume intersections the right-of-way associated with Highway 19E.
The remediation system removes both No. 2 fuel oil and dissolved petroleum hydrocarbons from groundwater
that is extracted from the subsurface. The existing pump and treat system consists of 16 recovery wells and 11
trench wells (located along the North Carolina Department of Transportation right-of-way for Highway 19E)
equipped with total fluid pneumatic pumps, associated piping, an oil/water separator, air stripper, bag filters, and
carbon vessels. Treated water from the remediation system discharges to an unnamed tributary of Beaver Creek
(Class C, Trout water), which flows to the North Toe River within the French Broad River basin.
The system components are depicted in the figures in Appendix I. Site photographs are included in Appendix II.
The major components of the system are listed below:
1.2 Recovery Wells
A total of 16 recovery wells are installed at various locations across of the contaminated site to remove free
product and petroleum-impacted groundwater. All recovery wells consist of either a four or six inch well with an
installed pneumatic pump. The pumps installed are either a QED Hammerhead or AP-4 top loading pumps
capable of extracting both free product and petroleum-impacted groundwater. A copy of the specification sheets
for both pneumatic pumps used at the site have been included in Appendix III.
May 3, 2018 1

Groundwater Remediation System Specifications &
Blue Ridge Hospital—Spruce Pine, NCDEQ Incident No. 3659
Spruce Pine, Mitchell County, North Carolina I
S&ME Project No.4305-17-109E
1.3 Interceptor Trench
An interceptor trench consisting of 11 recovery wells to prevent the downward migration of the product plume.
The purpose of the interceptor trench is to prevent migration of the free product plume towards the North Toe
River.
Again, the pumps installed into the interceptor trench are either QED Hammerhead or AP-4 top loading pumps.
The interceptor trench was installed using pea gravel and coarse sand. The recovery wells located in the trench
are six inch in diameter and constructed of stainless steel casing.
1.4 Flow Origin and Volume
Original conception of the system estimated that approximately 1 gallon per minute would be produced from
each well associated with the treatment system. Under normal operating conditions, the average influent flow
(between March 15 and March 29, 2018) was measured at approximately 10 gallons per minute (gpm) or 14,400
gallons per day(gpd). Over the course of operations, heavy rainfall event have shown to temporarily increase the
influent flow to approximately 20 gpm (28,800 gpd). Therefore, for system design/modification purposes we have
assumed a flowrate of 20 gpm.
The current system as currently designed is able to handle an influent flow rate of at least 40 gpm (57,200 gpd).
The system was originally designed with the assumption that additional recovery wells/trenches may be required
to prevent migration of free product and groundwater contamination. However, since additional expansions have
not taken place, the system is operating at about 50%of its design capacity.
1.5 Wastewater Characterization
A groundwater sample was collected on March 30, 2018 from the sample port located after the confluence of the
oil/water separators, but prior to treatment of the influent groundwater by the air stripper and filtration units. The
groundwater sample was analyzed for the following:
4 benzene, toluene, ethylbenzene, total xylenes (BTEX), methyl tert-butyl ether (MTBE), naphthalene, and
1,2-Dichloroethane by Method 6200;
« lead by Method 6010;
total suspended solids (TSS) by Method 2540;
e oil &Grease by Method 1664; and
phenol by Method 420.1.
The laboratory report associated with the influent sample is included in Appendix IV. The results of the influent
sample analysis is summarized in Table 1-1 below
May 3, 2018 2

Groundwater Remediation System Specifications
Blue Ridge Hospital—Spruce Pine, NCDEQ Incident No. 3659
Spruce Pine, Mitchell County, North Carolina I I =
S&ME Project No. 4305-17-109E
Table 1-1 — Influent Data
Constituent Concentration
Benzene 46 pg/L
Ethylbenzene 18 pg/L
Toluene 13 pg/L
Total Xylenes 84 pg/L
MTBE <1.0 pg/L
Naphthalene 76 pg/L
Lead <0.010 mg/L
1,2-dichloroethane <2.0
Phenol 0.077 mg/L
TSS 2.2 mg/L
Oil &grease <1.4 mg/L
pg/L= micrograms per liter
mg/L=milligrams per liter
2.0 System Design
As the system was originally designed in 1993 and installed in 1994, the treatment system components are
present and are in operation at the facility. The information that is provided below details each major piece of
equipment associated with the groundwater treatment system and provides confirmation that the existing system
is still effective at reducing contaminant concentrations found at the site.
2.1 Oil/Water Separator
There are currently two oil/water separators installed at the site. The first oil/water separator receives
groundwater recovered from the recovery wells located across the site. The second oil/water separator receives
groundwater recovered from the recovery wells associated with the interceptor trench. Influent flow from each
individual recovery well is combined into three trunk lines that enter the treatment system building. The oil/water
separators that were installed are Hydro-Flo Technologies (Model No. DP-24). The following are the specifications
associated with the two oil/water separators:
Manufacturer: Hydro-Flo Technologies Inc.
Overall Dimensions: Approximately 9 feet long by 3 feet wide by 5.5 feet tall
Design Flow Rate: 34 gpm @ 20 microns to 77 gpm @ 30 microns
Oil Droplet Removal Rate: 10 mg/L of oil droplets > 20-30 microns
Coalescing Media Pack Size: 48 inches long by 24 inches wide by 36 inches tall
Minimum Coalescing Surface Area: 1,632 square feet
Maximum Cross-sectional Velocity: 0.75 to 1.72 feet per minute
Minimum Separation Retention Time: 7.48 to 1.0 minutes
May 3, 2018 3

MIMI
Groundwater Remediation System Specifications
Blue Ridge Hospital—Spruce Pine, NCDEQ Incident No. 3659
Spruce Pine, Mitchell County, North CarolinaI ' ItilMMIF
S&ME Project No.4305-17-109E
Emir
mom
Sludge Chamber Capacity: 56 gallons
Device for Oil Removal: Rotary Pipe Skimmer
Specification sheets for each oil/water separator have been included in Appendix V.
2.2 Shallow Tray Air Stripper
The influent groundwater contaminant data collected in March 2018 was used to confirm the system design
capacity for the air stripper. For reference, the original design characteristics from 1993 are included. Software
was utilized from Northeast Environmental Products (NEEP-Shallow Tray) who designed the shallow tray stripper
system currently on site. The software computes the shallow tray air stripper outlet concentrations of select
contaminants of concern based on the system's configuration, flow rate, water temperature, and measured
influent concentrations. The software output is included in Appendix VI. The estimated concentrations of the
effluent exiting the shallow tray stripper are summarized below:
Table 2-1 — Air Stripper Evaluation
Air Air
Influent Effluent Influent Effluent
Effluent Effluent
Conc. Conc. Removal Conc. Conc. Removal
Constituent Conc. Conc.
(ppb) - (ppb) - Efficiency (ppb) - (ppb)— Efficiency
1993 1993 (ppmv) 2018 2018 (ppmv)
1993 2018
Benzene 4,600 <1 8.30 99.99% 46 <1 0.04 100%
Toluene 3,900 <1 5.96 99.99% 13 <1 0.01 100%
Ethyl 3,400 <1 4.51 100% 18 <1 0.01 100%
benzene
Total 13,000 <1 17.28 99.99% 84 <1 0.06 100%
Xylenes
Naphthalene 4,600 6 5.05 99.86% 76 <1 0.04 99.97%
MTBE 10* <1 0.02 96.43% 1* <1 0.00 99.76%
1,2-DCA 10* <1 0.01 99.10% 1* <1 0.00 99.99%
*-MTBE and 1,2-DCA concentrations are assumed. They were not sampled in 1993 and were below laboratory detection limits in
2018.
ppb= parts per billion
ppmv= parts per million by volume
May 3, 2018 4

Groundwater Remediation System Specifications
Blue Ridge Hospital—Spruce Pine, NCDEQ Incident No. 3659 IMP
Spruce Pine, Mitchell County, North Carolina III
S&ME Project No. 4305-17-109E
Following are the specifications for the Shallow Tray Stripper:
Manufacturer: Northeast Environmental Products Inc. (NEEP)
Model Number: 3631
Air Flow Rate: 900 cubic feet per minute
Water Flow Rate: 1-125 gpm
Air/Water Ratio: 134.6 cubic feet per minute of air per cubic feet per minute of water
Number of Trays: 3
Overall Dimensions: 6.17 feet long by 5 feet wide by 6.5 feet tall
Specification sheets for the shallow tray stripper have been included in Appendix VII.
2.3 Filters
Two sets of bag filters were installed to allow for filtration of solids that may be in the influent groundwater
stream. The first set of filters were installed prior to the shallow tray air stripper and is capable of capturing
contaminants/solids greater than 50 microns. The second set of filters were installed prior to the carbon filtration
units and is capable of capturing contaminants/solids greater than 10 microns. Both sets of filters are in a parallel
configuration to allow the water to take the path of least resistance. The following are the specifications for the
two sets of bag filters:
2.3.1 50 Micron Bag Filters
Manufacturer: FSI
Model Number: BFN 12
Filter Bags: 1— 50 Micron
Surface Area per Bag: 4.4 squre feet
Maximum flow: Up to 220 gpm
2.3.2 10 Micron Bag Filters
Manufacturer: Krystil Klear
Model Number: 88
Filter Bags: 1- 10 Micron
Surface Area per Bag: 4.4 square feet
Maximum flow: Up to 220 gpm
Specification sheets for each filter have been included in Appendix VIII.
2.4 Activated Carbon Units
Two activated carbon units will receive the effluent from the shallow tray air stripper. The carbon units are meant
as a polishing step prior to the discharge point. The units are meant to capture some of the more difficult
contaminants (such as naphthalene) that were not completely stripped. Based on the calculations above, it is not
May 3, 2018 5

NMI
Groundwater Remediation System Specifications P
Blue Ridge Hospital-Spruce Pine, NCDEQ Incident No. 3659 moor
Spruce Pine, Mitchell County, North Carolina
S&ME Project No.4305-17-109E / I I
anticipated that elevated concentrations of the contaminants of concern are expected to reach and be removed
by the carbon system. The carbon units are setup in series to allow effluent water to flow through both carbon
vessels prior to discharge. Following are the specifications for the carbon units currently installed at the site:
Manufacturer: Carbonair
Model Number: PC7F
Carbon Capacity: 1,000 pounds each
Design Flow Rate: 75 gpm
li Design Pressure: 90 pounds per square inch (psi)
Bed Area: 7 square feet
Dimensions: 3 feet diameter by 6 feet tall
Specification sheets for the carbon vessels have been included in Appendix IX.
2.5 Other Major Components
Other major components of the treatment system include two transfer pumps, a batch settlement tank, and an air
compressor. The pumps allow for the transfer of water between the batch tank and the shallow tray stripper and
between the shallow tray stripper and the carbon vessels. The air compressor provides the pneumatic power for
the recovery well pumps. The following are the specifications for the batch tank, transfer pumps, and air
compressor:
2.5.1 Batch Tank
Manufacturer: Chemtainer Industries
Capacity: 500 gallons
Dimensions: 5 feet diameter by —3.5 feet tall
2.5.2 Batch Tank Transfer Pump
Manufacturer: Price Pumps
Model Number: EC150
Flow: 60-80 gpm (based on pump curve)
Horsepower: 1.5 horsepower
2.5.3 Shallow Tray Stripper Transfer Pump
Manufacturer: Grundfos
Model Number: CRN-8-40
Flow: 30-40 gpm (based on pump curve)
Horsepower: 3 horsepower
May 3, 2018 6

Groundwater Remediation System Specifications
Blue Ridge Hospital-Spruce Pine, NCDEQ Incident No. 3659 azior
Spruce Pine, Mitchell County, North Carolina ' I
S&ME Project No.4305-17-109E
MEV
MINIM
2.5.4 Air Compressor
Manufacturer: Ingersoll-Rand
Model Number: U25HE-SP
Capacity: 100 cubic feet per min
Operating Press.: 125 psi
Horsepower: 25 horsepower
A specification sheet for the air compressor could not be provided by Ingersoll-Rand as it is obsolete and the
manufacturer no longer supports this model. A specification sheet was not provided for the batch tank as it is a
general water holding tank and dimensions are widely available. Specification sheets for the two transfer pumps
listed are included in Appendix X.
2.6 Controls and Alarms
The followingtable describes the system controls and alarms that have been installed on the treatment system:
Y Y
Table 2-2— Summary of Controls and Alarms Features
Item Type Location Control
Batch Transfer Pump Float switch Within Batch Tank Low and Hi float switch turns
the transfer pump on/off
Within Batch
Batch Tank Alarm Float switch Wi t atc Tank Hi-Hi float switch shuts the
treatment system off when
activated
Shallow Tray Transfer Float switch Within Shallow Tray Low and Hi float switch turns
Pump Sump the transfer pump on/off
Shallow Tray Stripper Float switch Within Shallow Tray Hi-Hi float switch shuts the
Alarm Sump treatment system off when
activated
Shallow Tray Stripper Pressure Switch Within Shallow Tray Shuts down the treatment
Alarm Stripper system due to pressure
buildup/fouling of trays
Product Storage Tank Float Switch Within Tank Hi-Hi float switch shuts down
Alarm the treatment system when
activated
May 3, 2018 7

Appendices

Appendix I - Figures

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P'''':# �/
o. 'O
off. se" Q ;Spruce PIOea'rgL Pine Ave i '+ Y
a Walnut Ave O
C%4O
a/ e r Ave `Y
, a°,s „ O
Dy a Ct
u e�ock Ave L a4po'St d I •2,
5 na° e F , S
Bal,., use.
tee English Rd p , ^Qhs1 Si a C.
°
j c i J, a
e S
0
'5
,a t`s b - - .._3 to/D,
.1'4 a4 ,'C Rd : t .� O i
&ant 4' 3 u 3
i n o o 4i P,..
t ace. 5 d'D e'-'1.=1:::, O e tauoa
c;.
FF c• e,,,. Ist'dn0'-PG as �b
orad a y It,.
^ t e Si
of Regain 5 hlarnorel4 ,S B,fa1 i u P 0`dd
Pr Farkn � a `i,' n Carpenter Rd
r
o (� ,a s,
N atria _. 'hi
ry G
O
tin,-; .
c _ Z
o44 ROd9ery o
O -e
> �o p e 'Y C,••v .. I
4 S
d -`
2 10b'ROck Rd
e
H ^ea Ga{
-
•`,o o'
are
areO
ill'',
n4040 da'
.'
�‘ BarrV D, henry
c�' b Fairway Ln t'+ ad o
C aye p• t _c nt D
a v S'7ci C/ine G gra U Wyatt` Fain,R
O e • ea Dr
m Z.
..
J.
Ca very Rr64n"g V
a y6�H
m woodland Rd o. �p m
✓ a 2 ''•,n,s C.,,., Cook In
tG
O ^Lau\ 0 6
.::,Cce�I� �Ounta' Gato o °O
m ,;1,iortnnJ Q
!'0un,rn'_srtl +0
Rock/
0 2,000 4,000e, as d
• t I(FEET) t :'Qe ?'
d
.rru, '0
0'
r REFERENCE:
v\
a BASE MAPPING OBTAINED FROM ESRI. THIS MAP IS FOR INFORMATIONAL PURPOSES °ot4std®e
• ONLY. ALL FEATURE LOCATIONS DISPLAYED ARE APPROXIMATED.THEY ARE NOT BASED ON y Project Location
0
CML SURVEY INFORMATION,UNLESS STATED OTHERWISE.
SCALE: FIGURE NO.
a SITE VICINITY MAP 1 " = 2,000 '
MEMDATE:
"I . BLUE RIDGE HOSPITAL 10-24-17 1
125 HOSPITAL DRIVE PROJECT NUMBER
SPRUCE PINE, MITCHELL CO., NORTH CAROLINA 405-17-109

'•
."*n
.,.,:".:1,4'
. a • t 1
) + Es. / of 11 16 t; ; ,,4,..-74....11:4?t.ft., rl ,,, � v „ ; 3x
fil
Ni , ( . 1f �rw
`; • r ! 'N
&
'$04
A .„ Y}• t ' •* T - ,! ...ii.!' ` w . .'I•' MW-9 4 : . t -, ,i• i ,, j4 J,T �•
I A� ' vOC
V' A
lit* l� '"I',;:;-;* y .( RW-26 i ")'4 '..f 1.A•R p I r`�� +
1 ;+ , + •'may p OW-11 ,, (lam
RW-25-
\\ •s >r jr `1® ,❑ OW-10 I it ` TREATMENT �ee
�, p ,..-.. 4 SYS •
TEM -4 v
;�4k • ❑ BUILDING
y, � .4 • (c-‘'''
w RW-23 a JQC r
7Z RW-22 13 Mg)
RW 21WRA OW-6 r •y • ;
41.
RW 20 - .� I 1P/7PP/I�� ��. . Z
13 OW-5 --',;..4-44r-- 4. RW-1. .i.►• "' A� O
„..,-.
as RW 19G Q, 11
+• t �f**4 cc
Q
y - 9 9 i2W 18 OW-4 MW 1 WR[fie
1N }� i '" •4. V
' !T p WR 22 • 2
OW-3
�. , •s? gssy RW-17 ♦ ►I RW-2 1 Z +
Ect
!y�- G OW-2 ^ i 9 Q
M 1 WR 23 ;Pt.... > z
a 7a
•OW-1 Q t v) H-
�� �� MW-6 I .itCO Z
r' 0 RW-3 w C O
r MW-8 /�OK � ' r RW-7 _ ► ,� 1 •`• / N J
&If. I*/'. 7 K
---it co '-I 5
CI
�.' r aj`l + RW 16 RW-9 ❑ ,:1, p' RW-6I • Z
; r v RVU-13 ® . a
MW-10' 1441110 U
i 1 1 S�;'If 9�l HOSPITAL QR •� ' ! / t ' D
ce
Z.-, -', • . V:.• N II , .. ¢ .• _ .. 90 RW-14 • :4
N " - '.- , RW-10 p r \ vii
f .. .� r .r p :0 -
N a
ti ! m �1 RW-15 i RW 12 ® )N • ,
T. ,, ,t , -j, CI 7
E * .7.,-;,,W ►1 •
+ RW 11 MW-4 �� '^)
efit
"V, MW-13 / _ ,.
5)
'' „..siiiihm.4.___-_,,,,,.,‘;. ...,
}
n4 ..' • ``.. 'A s ',-.'t ,,, ''., P°;# „ . .. - 1 i
o r.' ,. a ,•• , ) ' ' SCALE:
F ),'' ter \' . t 1 ' = 80
62 ,: a '• e k • Monitoring Wells (Located)
�, �y9Q \tr / '� •- if .�� IN Monitoring Wells (Unconfirmed) DATE:
A MW-14 ` i r i Hs 10-24 17
y
,� c \I Ak.j d ® 4' rt h ' '� X Monitoring Wells (Abandoned /Not Located) PROJECT NUMBER
o F:r, ,, , Y .0, 4305-17-109
, , A. _0 f r. N• ' a Recovery Wells
a REFERENCE: 1 e• ,y
V-", A Observation Wells FIGURE NO.
, \ it
GIS BASE LAYERS WERE OBTAINED FROM NC ONEMAP AND MITCHELL COUNTY GIS DEPARTMENT. 0 80 160 P ` ` 011.r\I\ -►Recovery Lines
I THIS MAP IS FOR INFORMATIONAL PURPOSES ONLY. ALL FEATURE LOCATIONS DISPLAYED ARE i
a • APPROXIMATED.THEY ARE NOT BASED ON CML SURVEY INFORMATION,UNLESS STATED OTHERWISE. ._� _ (FEET) )Ni ., .. .111 Approximate UST Locations 1
< j a ' 1 ••�*1,tt NC OneMa

c
3,000 Gallon Free Product
Storage Tank w/Secondary
Containment
Steel Tank Institute Model F911
Batch Transfer Pump I
Price Pump Model EC150A Influent from recovery wells
ow hoses)
I
A
Oil/Water Separator#1 / /
/500 Gallon Poly1111: Hydro Flo Technologies Model DP-24 -f--
Batch Tank Treating Recovery Wells 1-16
Chemtainer Ind. ► LEGEND
(TYF) /
\ // A
A
WATER FLOW PATH(Dashed where below ground)
AIR FLOW PATH(Dashed where below ground)
APRODUCT FLOW PATH
`4‘
et Oil/Water Separator#2 — C
Hydro Flo Technologies Model DP-24 (13
Treating Trench Recovery Wells 17-27
a N O
> m
Q 'C u
Shallow Tray Air Stripper 2-50 Micron Bag Filters
Notes:
Dimensions of equipment are approximate based on CU -
Skid w/supporting FSI Model BFNP-12(304SS)
equipment cut sheets for models shown. w O
2) Piping between equipment consists of Sch.40 PVC of tT . Z
NEEP Shallow Tray Model — various sizes as well as flexible piping(either HDPE or -0 'O C
3631 hose). E _ _
3) Valving and sample ports have not been included on CIJ N i6--
this figure. E7 N UJ
Et) e--I v
7
A Q
1.4
cc [ I V1
2 CV
Transfer Pump
Grundfos Model CRN-8-40 0
C0
Controls and Compressed Air
2-1,000 lb Carbon Vessels
a CarbonAir Model PC7F vl
w
_2 Building
N a
Ace
I OP 21) o
s Air Supply to
3
Recovery Wells
N • Service Entrance
o ) i=
q 2-10 Micron Bag Filters 4
E Krystal Klear Model 88-30 Vessel Backwashing
TE 0
v
m
c
T A
dtil
Discharge from system c —
2
N to NPDES point E w
E ,
o ° SCALE:
Groundwater Treatment Building o As Shown
DATE:
N a o:
a, a0 4-9-18
a oPROJECT NUMBER
To S
- 4305-17-109J
a V
al v
0 4 8 FIGURE NO.
I ,
GRAPHIC SCALE (IN FEET)
1

c
/ �
Discharge to / �o Ste ' �\
tributary /=�oo. . `mo/
/
/ , �� 00 \sem `•
1 / / BEAVER C%. / IV 00<\ \\<z5, /
�' / /
/ ,' o,, , `\ \ Remediation /
`♦\ ♦ System
ti , / •
♦♦\♦\ \ / /
r/ / SEABOARD SYSTEM 1 \ ` Effluent Sample Location
J RAILROAD \♦\\ in the S stem
/1
•Q / •
Off/
?.(,.()q,,-0'jso
00 ♦ Solid
II 0000 / s.rr.D.l`c Underground
T-
••
Pipe
lNi
04 0,:
i •\�,� ♦`•
/ yS.W.D.I.
2 / / \
I / — / \\
t4
/ \
›. / / S.W.D.I.
// // Underground
/ / \ Piping i J SPRUCE PINE
/ / ,„, ,,I
HOSPITAL
/ / Effluent Discharge
i� / from Remediation t
System to Storm a
/ Water System, c\
' a D
Imo '
v------1-''<-->''''' ' - '''''' ''''''''- *
F-7
` Hospital --..„1-7--.1 \ ' ' \, \------- - -”-, .
L ti
I . ,
A \ `, \
, \ \
REFERENCE:
Figure from S&ME's October 1998 Site Map for Engineering Drawings
SCALE: FIGURE NO.
SITE MAP-DISCHARGE PATH NTS
DATE: 3
: BLUE RIDGE HOSPITAL 10-31-2017
125 HOSPITAL DRIVE PROJECT NUMBER
SPRUCE PINE, MITCHELL COUNTY, NORTH CAROLINA 4305-17-109E

Influent From Influent From
Recovery Wells Recovery Wells
OIL/WATER SEPARATOR OIL/WATER SEPARATOR 110(Original) (Supplemental)
- V
To Recovery Wells ® V
3,000 GALLON
25 HP 500 GALLON PRODUCT HOLDING TANK
WITH SECONDARY
AIR COMPRESSOR BATCH TANK CONTAINMENT
1.I
( BATCH TANK
TRANSFER PUMP
LEGEND
V
2-50 MICRON WATER FLOW PATH
BAG FILTERS
rr���f AIR FLOW PATH
(TURBINE FLOW METER) PRODUCT FLOW PATH
BALL VALVE
3-TRAY SHALLOW VACUUM RELIEF VALVE
AIR STRIPPING
SYSTEM
SAMPLE POINT
-0 PRESSURE GAUGE
V
AIR STRIPPER
TRANSFER PUMP
2-10 MICRON
BAG FILTERS
3
w
>
a
1000 LB GRANULAR
-c ACTIVATED CARBON
3 VESSEL
0
E:
o
S
y
c
a NOTE:
2 1000 LB GRANULAR ALARMS HAVE BEEN INSTALLED AS FOLLOWS:
a ACTIVATED CARBON 0 1) HI LEVEL IN TRAY STRIPPER SUMP
VESSEL 2) HI PRESSURE IN TRAY STRIPPER
o \ 3) HI LEVEL IN PRODUCT AST
Y \ 4) HI LEVEL IN BATCH TANK
Cl
ANY OF THE ALARMS ACTIVATED ABOVE WILL SHUT
SYSTEM DOWN TO PREVENT OVERFLOW CONDITION.
V
Discharge from system to NPDES point
under gravity flow conditions
SCALE: FIGURE NO.
Treatment System Flow Diagram Not to Scale
DATE:
Blue Ridge Hospital 4-9-18
125 Hospital Drive PROJECT NUMBER
Spruce Pine, North Carolina 4305-17-109J I

Appendix II - Site Photographs
I

'`
1
A `
ri
to
v
., umm i
`—lir1
1 Oil/Water Separator within treatment building receiving recovery 2 •il/Water Separator within treatment building receiving recovery
ells located throughout the site. ells associated with the interceptor trench.
1 41 INV
� B.grcH
1 ` TiMrK
.R
3 Product storage AST with secondary containment located 00 gallon batch tank located within treatment building.
outside of the primary treatment building.
Blue Ridge Hospital —Groundwater Treatment System S&ME Project 4305-18-109J
1 1 Spruce Pine, NC Taken by: GS I Date Taken:4/9/18

„. r. ..\ ,
i P
7 Ir .. . t - -
.'i.-7,'',,,,.
= jw, r: Y
IIP
flifi it �►,�r
5 Batch tank transfer pump 6 0-micron filters plumbed in parallel
tl
//41 , _. 4.-,- -
is•
.' t.. I 1 4'( r I y '.
ir
,,
,,, ,
,, i
, 1, _
,, ... ,
,-,,,,„..,-, ; , 4.' IN i
.41111,
': "Iii '-'-ammix t'''
ill II
.141, i ii i
r
7 Shallow Tray Air Stripper system 8 Shallow Tray transfer pump
`� Blue Ridge Hospital - Groundwater Treatment System S&ME Project 4305-18-109J
7 Spruce Pine, NC Taken by: GS I Date Taken:4/9/18

_ i
l
._ L -.1,
MC
ti
g
illk . iIli'
,..
-: , 1:-. '
9 10-micron filters plumbed in parallel 10 Two 1,000 lb carbon vessels plumbed in series
{
ii
i
c.
Ev^ w~�
11 'it compressor located in secondary treatment building 12 Electrical panel located inside secondary treatment building
Blue Ridge Hospital —Groundwater Treatment System S&ME Project 4305-18-109J
Spruce Pine, NC Taken by: GS I Date Taken:4/9/18

Appendix III - Pneumatic Pumps Specifications

V QED Specifications - Top Inlet, Long
Environmental Systems
Description
Max. Flow 10 gpm (38 Ipm)
The AP4+ Top Inlet Long AutoPump provides maximum
O.D. 3.6 in (91 mm) ui
capabilities and flow in a top inlet pump for 4" diameter
= and larger wells needing an elevated inlet, such as pumping
Length 56.7 in. (144 cm) total fluids from wells contaminated with LNAPLs. It is
offered in optional versions to handle even the most severe
remediation and landfill pumping applications, and delivers
flow rates up to 10 gpm*. The AP4+ Long Top Inlet
111 AutoPump is complemented by the most comprehensive
selection of accessories to provide a complete system to
meet site specific requirements. Call QED for prompt, no-
obligation assistance on your pumping project needs.
The AutoPump Heritage
The AP4+ Top Inlet Long AutoPump is part of the famous
AutoPump family of original automatic air-powered pumps,
developed in the mid 1980s specifically to handle unique
pumping needs at remediation and landfill sites. Over the
years they've proven their durability at thousands of sites
worldwide. AutoPumps are designed to handle difficult
pumping challenges that other pumps can't, such as
hydrocarbons, solvents, suspended solids, corrosives,
temperature extremes, viscous fluids and frequent start/
stop cycles. Beyond just the pump, AutoPump systems
offer the most complete range of tubing, hose, connec-
Advantages tors, wellhead caps and accessories to help your installa-
tion go smoothly. This superior pumping heritage, applica-
1. The original automatic air- tion experience and support back up every AutoPump you
powered well pump, proven put to work on your project.
worldwide over 23 years
2. The highest flow rates and
deepest pumping capabilities in
the industry
3. Patented, proven design for
superior reliability and
durability, even in severe
applications
4. Handles solids, solvents,
hydrocarbons corrosive
conditions, viscous fluids and
high temperatures beyond the
limits of electric pumps
5. Five-year warranty
33

V QED Specifications - Top Inlet, Long
Environmental Systems
Pump Dimensions Specifications & Operating Requirements
Liquid Discharge Model 4"-Long AP4+Top Inlet
Liquid Inlet Location Top
0.D. 3.6 in.(91 mm)
I I(
Inlet Overall Length(Pump&Fittings) 56.7 in.(144 cm)
Weight 16.5 lbs.(7.6 kg)
Maximum Flow Rate 10 gpm(38 Ipm)*-See Flow Rate Chart
Pump Volume/Cycle 0.58-0.78 gal (2.2-3L)
Air Supply Minimum Accuation Level 53.3 in.(135 cm)
(lpo Exhaust
Standard Pump
Maximum Depth 250 ft.(76 m)
Air Pressure 5-120 psi(0.4-8.4 kg/cm2)
• Air Usage 0.35-1.1 scf/gal.(3.0-8.4 liter of air/
fluid liter)- See air usage chart
High Pressure Pump
Maximum Depth 425 ft.(130 m)
Air Pressure 5-200 psi(0.4-14.1 kg/cm2)
Minimum Liquid Density 0.7 SpG(0.7 g/cm3)
•• Standard Construction Materials,
M Pump Body Fiberglass or Stainless Steel
LL7, Pump Ends Stainless Steel
I° o Internal Components Stainless Steel,Viton,PVDF,Hastelloy-C
Tube&Hose Fittings Brass or Stainless Steel
Fitting Type Barbs,Quick Connects or Easy Fittings
� a
Tube&Hose Options
Tubing Materials, Nylon
Sizes-Liquid Discharge 1 in.(25 mm)or 1-1/4 in.(32 mm)OD
Pump Air Supply 1/2 in.(13 mm)OD
Air Exhaust 5/8 in.(16 mm)OD
Hose Material Nitrile
Sizes-Liquid Discharge 3/4 in.(19 mm)or 1 in.(25 mm)ID
Pump Air Supply 3/8 in.(9.5 mm)ID
Air Exhaust 1/2 in.(13 mm)ID
i Applies to QED supplied tubing;
other tubing sources may not
conform to QED fittings.
- - O 13 3 6' (91 nun,
Long and short AP4+ AutoPumps are warranted for
five(5) years: Low-Drawdown AP4+ AutoPumps are
Application Limits (Base model) warranted for one (1) year.
AP4+ AutoPumps are designed to handle
the application ranges described below.
For applications outside these ranges,
consult QED about AP4+ upgrades.
Maximum Temperature: 180°F (82°C)
pH Range: 4-9
Solvents and Fuels: diesel, gasoline,
JP1-JP6,#2 heating oils, BTEX, MTBE,
landfill liquids
*Consult QED for higher flow requirements
34

V QED Specifications - Top Inlet, Long
Environmental Systems
Flow Rates'
3/4 inch (19 mm) 1 inch (25.4 mm)
Inside Diameter Discharge Hose Inside Diameter Discharge Hose
(Equivalent to 1-Inch O.D.Tubing) (Equivalent to 1.25-Inch O.D.Tubing)
6-INCH(15 cm) SUBMERGENCE OF PUMP HEAD 6-INCH(15 cm) SUBMERGENCE OF PUMP HEAD
18 68.1 18 I I I I I I I 68.1
16 - 60.6 16 I AIR INLET PRESSURES 1 60.6
GALLONS
14 S3 14 53
APPROXIMATE GALLONS APPROXIMATE
PER 12 1 AIR INLET PRESSURES - 45.4 LITERS PER 12 45.4 LITERS
MINUTE10 37.9 PER MINUTE 10 379 PER
WITH MINUTE WITH MINUTE
3/4-INCH 8 303 WITH 1-INCH 8 30.3 WITH
I.D.HOSE 6 22.7 19mm I.D.HOSE 6 i00 PS 22.7 25.4mm
4 \
100
0 PS 15.1 LD.HOSE 4 7 Kg/cm` 15.1 I.D.HOSE
Kg
/cm'
- 40 PSI 7.6 2 40 PSI 70 PSI 7.6
70 PSIME
0 _ 3 Kg/cm2 5 Kg/cm2 0 0 3 Kg/cm 2 5 Kg/cm 2 0
O 20 40 60 80 100 120 14r7617111-6 200 FT. DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters I IN WELL 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters ]IN WELL
2 FT.(60 cm) SUBMERGENCE OF PUMP HEAD 2 FT.(60 cm) SUBMERGENCE OF PUMP HEAD
18 68.1 18 68.1
16 60.6 16 60.6
14 - 53 14 AIR INLET PRESSURES t- 53
GALLONS APPROXIMATE GALLONS APPROXIMATE
PER 12 AIR INLET PRESSURES 45.4 LITERS PER 12 45A LITERS
MINUTE 10 37.9 PER MINUTE PER
10 37.9
WITH MINUTE WITH MINUTE
3/4-INCH 8 30.3 WITH 1-INCH 8 30.3 WITH
I.D.HOSE 622.7 19 mm 100 PSI
0 PSI I.D.HOSE 6
1022.7 25.4 mm
7 Kg/cm 2 I 15 1 I.D.HOSE 7Kg/crr I.D.HOSE
4 4 15.1
40 PSI
2 - 40 PSI 70 PSI 7.6 2 ' 3 K/cm 2 70 PSI 7.6
0 3 Kg/cm' 5 Kg/cm 2 0 0 9 1 5 Kg/cm 2 0
O 20 40 60 80 100 120 140 160 180 200 FT. 1 DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters j IN WELL
10 FT.(300 cm)) SUBMERGENCE OF PUMP HEAD 10 FT.(300 cm) SUBMERGENCE OF PUMP HEAD
18 68.1 18 68.1
16 60.6 16 - 60.6
GALLONS 14 53 APPROXIMATE GALLONS 14 AIR INLET PRESSURES 53 APPROXIMATE
PER 12 AIR INLET PRESSURES 45.4 LITERS PER 12 - 45 4 LITERS
MINUTE 10 37.9 PER MINUTE 10 379 PER
WITH MINUTE WITH MINUTE
3/4-INCH R - 7 30.3 WITH 8 30.3 WITH
l 1-INCH
I.D.HOSE 6 100 PSI 22.7 19 mm I.D.HOSE 6 22.7 25.4 mm
4 7Kg/cm 2 15.1 I.D.HOSE 4 151 I.D.HOSE
2 - 40g PSI 2 70g PSI 2 7.6 2 - 40 PSI I-,I 70 PS 100 PSI 7.6
0 3 K/cm 5 K/cm 0 0 3 Kg/cm 2 ILII 5 Kg/cm 2 I��IIUUII 7Kg/cm 2 0
O 20 40 60 80 100 120 140 160 180 200 FT. 1 DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. �I DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters J IN WELL
'FLOW RATES MAY VARY WITH SITE CONDITIONS. CALL QED FOR TECHNICAL ASSISTANCE.
35

1
V QED Specifications - Top Inlet, Long
Environmental Systems
Air Consumption
1 6 12
3/4 inch (19 mm)
12 Inside Diameter Discharge Hose
10.5 (Equivalent to 1-Inch O.D. Tubing)
1.3 9.7
1.2 9.0
100 PSI
STANDARD 71'9 82 APPROXIMATE
CUBIC FEET OF AIR STANDARD
PER o 7.5 LITER OF AIR
70 PSI PER
GALLON PUMPED 516g/cm 7
(SCF/GAL) 9 6.7 LITER PUMPED
77
(STD ULITER)
[1,
u�> 7 5.2
e
Y
6 4.5
Irl 40 PSI
�' 3 Kq/cm-
5 / 3.7
q / 3.0
3 2.2
2 1.5
20 40 60 80 100 120 140 160 180 200 FT. ]DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
16 12
1.5 11.2 1 inch(25.4 mm)
Inside Diameter Discharge Hose
1.4 10.5 (Equivalent to 1.25-Inch O.D.Tubing)
1 3 9.7
1.2 9.0
100 PSI
1.1 7 Kg/an 2 , 8.2
STANDARD / APPROXIMATE
CUBIC FEET OF AIR STANDARD
PER 10 7 5 LITER OF AIR
GALLON PUMPED PER
(SCF/GAL) .9 6.7 LITER PUMPED
70 PSI (STD ULITER)
5 Kg/cm'
8 6.0
7 5.2
6 4.5
40 PSI
3 Ky/cn
.5 3.7
4 3.0
3 2.2
2 1.5
20 40 60 80 100 120 140 160 180 200 FT, DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters_I IN WELL
36

QED Specifications - Top Inlet, Short
Environmental Systems
Description
Max. Flow 9 gpm (34 Ipm)
The AP4+ Top Inlet Short AutoPump provides maximum
111 capabilities and flow in a top inlet pump for 4" (100 mm)
O.D. 3.6 in (91 mm) diameter and larger wells with shorter water columns and
the need for an elevated inlet, such as pumping total fluids
Length 45 in. (110 cm) from wells contaminated with LNAPLs. It is offered in
(_r=o optional versions to handle even the most severe
remediation and landfill pumping applications, and delivers
flow rates up to 9 gpm (34 Ipm)` The AP4+ Short Top Inlet
AutoPump is complemented by the most comprehensive
selection of accessories to provide a complete system to
meet site specific requirements. Call QED for prompt, no-
obligation assistance on your pumping project needs.
The AutoPump Heritage
The AP4+ Top Inlet Short AutoPump is part of the famous
AutoPump family of original automatic air-powered pumps,
developed in the mid 1980s specifically to handle unique
pumping needs at remediation and landfill sites. Over the
years they've proven their durability at thousands of sites
worldwide. AutoPumps are designed to handle difficult
pumping challenges that other pumps can't, such as
hydrocarbons, solvents, suspended solids, corrosives,
temperature extremes, viscous fluids and frequent start/
stop cycles. Beyond just the pump, AutoPump systems
offer the most complete range of tubing, hose, connectors,
Advantages wellhead caps and accessories to help your installation go
smoothly. This superior pumping heritage, application
1. The original automatic air- experience and support back up every AutoPump you put to
powered well pump, proven work on your project.
worldwide over 23 years
2. The highest flow rates and
deepest pumping capabilities in
the industry
3 Patented, proven design for
superior reliability and
durability, even in severe
applications
4.Handles solids, solvents,
hydrocarbons corrosive
conditions, viscous fluids and
high temperatures beyond the
limits of electric pumps
5.Five-year warranty
37

V QED Specifications - Top Inlet, Short
Environmental Systems
Pump Dimensions Specifications & Operating Requirements
Model 4"-Short AP4+Top Inlet
Liquid Inlet Location Top
O.D. 3.6 in.(91 mm)
Overall Length(Pump&Fittings) 45 in.(110 cm)
Weight 15.8 lbs.(7.2 kg)
Liquid Discharge Maximum Flow Rate 9 gpm(34 Ipm)`-See Flow Rate Chart
Pump Volume/Cycle 0.22-0.36 gal (.83-1.36 L)
Minimum Accuation Level 41.6 in.(106 cm)
I Inlet
Standard Pump
Maximum Depth 250 ft.(76 m)
Air Pressure 5-120 psi(0.4-8.4 kg/cm2)
Air supply Air Usage 0.35.1.5 scf/gal.(2.4-8.4 liter of air/
.44 Exhaust fluid liter)- See air usage chart
I
High Pressure Pump
Maximum Depth 425 ft.(130 m)
Air Pressure 5-200 psi(0.4-14.1 kg/cm2)
Minimum Liquid Density 0.7 SpG(0.7 g/cm3)
a
"TT, Standard Construction Materials
LL >
Pump Body Fiberglass or Stainless Steel
Pump Ends Stainless Steel
Internal Components Stainless Steel,Viton,PVDF,Hastelloy-C
Tube&Hose Fittings Brass or Stainless Steel
Fitting Type Barbs,Quick Connects or Easy Fittings
Tube&Hose Options
Tubing Materials' Nylon
Sizes-Liquid Discharge 1 in.(25 mm)or 1-1/4 in.(32 mm)OD
Pump Air Supply 1/2 in.(13 mm)OD
Air Exhaust 5/8 in.(16 mm)OD
Hose Material Nitrile
Sizes-Liquid Discharge 3/4 in.(19 mm)or 1 in.(25 mm)ID
Pump Air Supply 3/8 in.(9.5 mm)ID
Air Exhaust 1/2 in.(13 mm)ID
O.D.3.6"(91 mm)
I Applies to QED supplied tubing;
other tubing sources may not
conform to QED fittings.
Long and short AP4+ AutoPumps are warranted for
five(5) years: Low-Drawdown AP4+ AutoPumps are
Application Limits (Base model) warranted for one (1)year.
AP4+ AutoPumps are designed to handle
the application ranges described below.
For applications outside these ranges,
consult QED about AP4+ upgrades.
Maximum Temperature: 180°F (82°C)
pH Range: 4-9
Solvents and Fuels: diesel, gasoline,
JP1-JP6,#2 heating oils, BTEX, MTBE,
landfill liquids
*Consult QED for higher flow requirements
38

V QED Specifications - Top Inlet, Short
Environmental Systems
Flow Rates'
3/4 inch (19 mm) 1 inch (25.4 mm)
Inside Diameter Discharge Hose Inside Diameter Discharge Hose
(Equivalent to 1-Inch O.D.Tubing) (Equivalent to 1.25-Inch O.D.Tubing)
6-INCH(15 cm) SUBMERGENCE OF PUMP HEAD 6-INCH(15 cm) SUBMERGENCE OF PUMP HEAD
18 68.1 18 68.1
16 60.6 16 • 60.6
GALLONS 14 53 APPROXIMATE GALLONS 14 •
53
APPROXIMATE
1 PER 12 AIR INLET PRESSURES - 45.4 LITERS PER 12 -I AIR INLET PRESSURES 45.4 LITERS
MINUTE 10 379 PER MINUTE 10 379 PER
WITH MINUTE WITH MINUTE
8 30.3 WITH 1.25-INCH 8 30.3
3/4-INCH WITH
I.D.HOSE 6 22.7 19 mm O.D.TUBING 6 100 PSI 22.7 31.75 mm
4 100 PSI 15.1 I.D.HOSE 4 7 Kg/cm 2 O.D.TUBING
15.1
7 Kg/cm 2
2 40 PSI 7.6 2 40 PSI 70 PSI , 7.6
0 3 Kg/cm 2 57K cmSIm 2 0 0 _ 3 Kg/cm 2 i 5 Kg/cm 2 _ 0
0 20 40 60 80 100 120 140 160 180 200 FT. DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. j]DEPTH
6.1 12.2 183 244 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
2 FT.(60 cm) SUBMERGENCE OF PUMP HEAD 2 FT.(60 cm) SUBMERGENCE OF PUMP HEAD
18 68.1 18 68.1
16 - 60.6 16 .. 60.6
14
GALLONS 14 53 APPROXIMATE GALLONS - 53
APPROXIMATE
PER 12 AIR INLET PRESSURES - 45.4 LITERS PER 12 AIR INLET PRESSURES - 45.4 LITERS
MINUTEPER MINUTE 10 37.9 PER
10 37.9
WITH MINUTE WITH MINUTE
6 30.3 WITH 1.25-INCH 8 30.3 WITH
3/4-INCH
I.D.HOSE 6 22.7 19 mm O.D.TUBING 6 100 PSI 22.7 31.75 mm
100 PSI 7Kg/cm 2 O.D.TUBING
4 7Kg/cm 2 t s.l W.HOSE 4 156
2 - 40 PSI - 7.6 2 40 PSI 70 PSI - 7'6
2 70 PSI 0 3 Kg/cm 2 _ 5 Kg/cm _ 0
0 3Kg/cm SKg/cm 2 0 0 20 40 60 80 100 120 140 160 180 200 FT. DEPTH
0 20 40 60 80 100 120 140 160 180 200 FT. .J DEPTH 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
6.1 12.2 18.3 24.4 30.5 36.6 427 48.8 549 61 Meters IN WELL
10 FT.(300 cm) SUBMERGENCE OF PUMP HEAD 10 FT.(300 cm) SUBMERGENCE OF PUMP HEAD
18 68.1
18 68.1
16 60.6
16 60.6
14 . 53 GALLONS 14 AIR INLET PRESSURES 53 APPROXIMATE
GALLONSAPPROXIMATE
PER 12 AIR INLET PRESSURES - 45.4 LITERS PER 12 45.4 LITERS
MINUTEPER MINUTE 10 37.9 PER
81 37.9 WITH MINUTE
WITH MINUTE 8 30.3
3/4-INCH & 303 WITH 1.25-INCH WITHO.D.TUBING 6 100 PSI 22.7 31.75 mm
I.D.HOSE 6 100 PSI 22.7 19 mm 1 Kg/cm 2 O.D.TUBING
I.D.HOSE 4 15.1
4 761 2 - 40 PSI 70 PSI - 7.6
2
40 PSI 70 PSI 0 3 Kg/cm 2 5 Kg/cm _ 0
0 3 Kg/cm 2 - 5 Kg/cmz_ 0 0 20 40 60 80 100 120 140 160 180 200 FT. 7 DEPTH
0 20 40 60 so 140 160 180 200 FT. •J DEPTH 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
6.1 122 18.3 24.4 30.5 36.6 42.7 48.8 549 61 Meters IN WELL
1FLOW RATES MAY VARY WITH SITE CONDITIONS. CALL QED FOR TECHNICAL ASSISTANCE.
39

V QED Specifications - Top Inlet, Short
Environmental Systems
Air Consumption
12
100 P51 3/4 inch (19 mm)
5 Kg°° 12 Inside Diameter Discharge Hose
14 10.5 (Equivalent to 1-Inch O.D. Tubing)
1.3 9 7
70 PSI
/Cm]
1.2 5 K 9.0
8.2 APPROXIMATE
STANDARD
CUBIC FEET OF AIR STANDARD
PER 1 6 45.2
il 41
o zs LITER OF AIR
GALLON PUMPED PER
(SCF/GAL) 9 g
6.7 LITER PUMPED
(STD L/LITER)
6.0
•
40 PSI
�>p
i ID
q .5
d
5
q
.2
3.7
30
3 2.2
1.5
20 40 60 80 100 120 140 160 180 200 F7, DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters 1 IN WELL
1.6 12
1.5
'4 3
11.2
10.5
1 inch(25.4 mm)
I00 P51
hgm: Inside Diameter Discharge Hose
(Equivalent to 1.25-Inch O.D.Tubing)
9.7
12 70 PSI 9.0
5 Kg/cm,
1.1 82
STANDARD APPROXIMATE
CUBIC FEET OF AIR STANDARD
PER 1.0 7 5 LITER OF AIR
GALLON PUMPED PER
(SCF/GAL) .9 6.7 LITER PUMPED
(STD L/LITER)
8 6.0
40 PSI
7 3 Kg cm- 5.2
.6 4.5
.5 37 I
.4 30
3 22
2 1.5
20 40 60 80 100 120 140 160 180 200 F7, 1 DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
40

VQED Specifications - Low-Drawdown Top Inlet
Environmental Systems
Description
Max. Flow 6.4 gpm (24 Ipm) The Low-Drawdown AP4+Top Inlet AutoPump provides
O.D. 3.6 in (91 mm) maximum capabilities and flow in a top inlet pump for 4"
(100 mm) diameter and larger wells with very short water
columns and/or the need to pump down to as low as 27.4
Length 30.75 in. (78 cm) inches (70 cm) above the bottom. It is offered in optional
versions to handle even the most severe remediation and
landfill pumping applications, and delivers flow rates up to
6.4 gpm(24 Ipm). The Low Drawdown AP4+ Top Inlet
AutoPump is complemented by the most comprehensive
selection of accessories to provide a complete system to
meet site specific requirements. Call QED for prompt, no-
tobligation assistance on your pumping project needs.
The AutoPump Heritage
The Low-Drawdown AP4+Top Inlet AutoPump is part of the
famous AutoPump family of original automatic air-powered
pumps, developed in the mid 1980s specifically to handle
unique pumping needs at remediation and landfill sites.
Over the years they've proven their durability at thousands
Advantages of sites worldwide. AutoPumps are designed to handle
difficult pumping challenges that other pumps can't, such
1. The original automatic air- as solvents, suspended solids, corrosives, temperature
powered well pump, proven extremes, viscous fluids and frequent start/stop cycles.
worldwide over 23 years Beyond just the pump, AutoPump systems offer the most
complete range of tubing, hose, connectors, caps and
2. The highest flow rates and accessories to help your installation go smoothly. This
deepest pumping capabilities in superior pumping heritage, application experience and
the industry in a low drawdown support back up every AutoPump you put to work on
top-fill pump your project.
3. Patented, proven design for
superior reliability and
durability, even in severe
applications
4. Handles solids, solvents,
corrosive conditions, viscous
fluids and high temperatures
beyond the limits of electric
pumps
5. One-year warranty
41

P
VQED Specifications - Low-Drawdown Top Inlet
Environmental Systems
Pump Dimensions Specifications & Operating Requirements
Model 4"-Low Drawdown AP4+Top Inlet
Liquid Inlet Location Top
O.D. 3.6 in.(91 mm)
Overall Length(Pumps&Fittings) 30.75 in.(78 cm)
Weight 9.8 lbs.(4.4 kg)
Maximum Flow Rate 6.4m
gP (24 Ipm)
)
Pump Volume/Cycle 0.11-0.16 gal (.42-.61 L1
Minimum Accuation Level 27.4 in.(70 cm)
Maximum Depth 250 ft.(76 m)
Air Pressure 5-120 psi(0.4-8.4 kg/cm2)
Air Usage .31-2.85 scf/gal.(2.2-21.5 liter of air/
fluid liter)- See air usage chart
Liquid Discharge Minimum Liquid Density 0.7 SpG(0.7 g/cm3)
' 11
Inlet Standard Construction Materials'
Pump Body Fiberglass or Stainless Steel
Pump Ends Stainless Steel
Internal Components Stainless Steel,Viton,PVDF,Hastelloy-C
Kir Supply Tube&Hose Fittings Brass or Stainless Steel
o f_am4 Exhaust
Fitting Type Barbs,Quick Connects or Easy Fittings
z --
Tube&Hose Options
N
Tubing Materials' Nylon
Sizes-Liquid Discharge 1 in.(25 mm)or 1-1/4 in.(32 mm)OD
Pump Air Supply 1/2 in.(13 mm)OD
Air Exhaust 5/8 in.(16 mm)OD
Hose Material Nitrile
Sizes-Liquid Discharge 3/4 in.(19 mm)or 1 in.(25 mm)ID
Pump Air Supply 3/8 in.(9.5 mm)ID
Air Exhaust 1/2 in.(13 mm)ID
O.D.3.6"(91 mm)
I Applies to QED supplied tubing;
other tubing sources may not
conform to QED fittings.
Low-Drawdown AP4+ AutoPumps are warranted for
one (1) year.
Application Limits (Base model)
AP4+ AutoPumps are designed to handle
the application ranges described below.
For applications outside these ranges,
consult QED about AP4+ upgrades.
Maximum Temperature: 180°F (82°C)
pH Range: 4-9
Solvents and Fuels: diesel, gasoline,
JP1-JP6,#2 heating oils, BTEX, MTBE,
landfill liquids
*Consult QED for higher flow requirements
42

VQED Specifications - Low-Drawdown Top Inlet
Environmental Systems
Flow Rates '
3/4 inch (19 mm) 1 inch (25.4 mm)
Inside Diameter Discharge Hose Inside Diameter Discharge Hose
(Equivalent to 1-Inch O.D.Tubing) (Equivalent to 1.25-Inch O.D.Tubing)
6-INCH(15 cm) SUBMERGENCE OF PUMP HEAD 6-INCH(15 cm) SUBMERGENCE OF PUMP HEAD
9 I I I I I I I 34.1 9 l l l l 1 34.1
8 -I AIR INLET PRESSURES I-- 30.3
8 AIR INLET PRESSURES E-- 30.3
7 26.5 GALLONS 7 26.5 APPROXIMATE
GALLONS APPROXIMATE 1
PER 6 22.7 LITERS PER 6 22.7 LITERS
MINUTEPER MINUTE 5 18.9 PER
5 18.9
WITH MINUTE WITH MINUTE
15.1 1-INCH 4 100 PSI 15.1 WITH
3/4-INCH 4 100 PSI WITH
7 Kg/cm^ 11.4 19 mm I.D.HOSE 3
7 Kg/cm 2 11.4 25.4 mm
LD.HOSE 3 \` I.D.HOSE
2 •`� 7.6 I.D.HOSE 2 40 PSI 7 7.6
40 P>I 70 PSI 1 _ 3 Kg/cm 2 5gl2 _ 3.
1 - 3Kgcm% - 5Kg/cm2 3.8
8
0 1 I I I I 0 0 I I I Kg/cmI I 0
O 20 40 60 80 100 120 140 160 180 200 FT. DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. 1 DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELT 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
2 FT.(60 cm) SUBMERGENCE OF PUMP HEAD 2 FT.(60 cm) SUBMERGENCE OF PUMP HEAD
9 34.1 9 34.1
8 - 30.3 8 30.3
7 AIR INLET PRESSURES F- 26.5GALLONS 7 --IAIR INLET PRESSURES H 26.5
GALLONS APPROXIMATE APPROXIMATE
PER
6 22.7 LITERS PER 6 - 22.7 LITERS
MINUTE5 . PER MINUTE 5 18.9 PER
18.9
WITH MINUTE WITH MINUTE
15.1 WITH 1-INCH 4 700 P51 15'' WITH3/4-INCH 4 -' 100 PSI
I.D.HOSE 37 Kg, 11.4 19 mm LD.HOSE 3
7Kg/cm2 11.4 25.4 mm
\\�� - I.D.HOSE
2 - 40 PSI 7.6 LD.HOSE 2 - 40 PSI 70 PSI >``. 7.6
3 Kg/cm2 70 PSI ._- 1 Kg/cm' 5Kg/cm2 3.8
1 - 5Kg/cm2 3.8
0 I I 0 0 I I 10
O 20 40 60 80 100 120 140 160 180 200 FT. 7 DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. DEPTH
6.1 12.2 183 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELT
10 FT.(300 cm) SUBMERGENCE OF PUMP HEAD 10 FT.(300 cm) SUBMERGENCE OF PUMP HEAD
9 34.1 9 34.1
8 - 303 8 30.3
AIR INLET PRESSURES - 26.5
AIR INLET PRESSURES - 26.5
GALLONS 7 APPROXIMATE GALLONS APPROXIMATE
PER 6 22.7 LITERS PER 6 22.7 LITERS
MINUTEPER MINUTE 5 . 18 9 PER
5 18.9
WITH MINUTE WITH 100 FSI MINUTE
q 15.1 WITH 1-INCH
4 -K r. - 15.1 WITH
3/4-INCH lOC PSI 11.4 25.4 mm
11.4 19 mm I.D.HOSE 3
LD.HOSE 3 ?Egan' - I.D.HOSE
d 40 PSI 7.6 I.D.HOSE 2 40 PSI
3Kg'cm` 3 Kg/cm 1� 7.6
2 70PSI -4.,-4., 2 ( 1 70PSI 1
3.8
1 5Kg/cm2 3.8 1 S Kg/cm 2
0 I I I o 0 I I I I o
O 20 40 60 80 100 120 140 160 180 200 FT. -I DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. 1 DEPTH
J IN WELL 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters
FLOW RATES MAY VARY WITH SITE CONDITIONS.CALL QED FOR TECHNICAL ASSISTANCE.
43

VQED Specifications - Low-Drawdown Top Inlet
Environmental Systems
Air Consumption
2.9 217 3/4 inch (19 mm)
2.8
00 PSI
7Kgkm2 20.9
27 ._ 20.2 Inside Diameter Discharge Hose
2.6 19.4 (Equivalent to 1-Inch O.D. Tubing)
2.5 18.7
2.4 18.0
1 MN 2.3 17.2
2.2 16.5
2.115.7
2.0 15
ill STANDARD19 142 APPROXIMATE
FEET OF AIR STANDARD
CUBIC
PER 1.8 13.5 LITER OF AIR
GALLON PUMPED 1.7 12.7 PER
(SCF/GAL) 1.6 12 LITER PUMPED
1.5 11.2 (STD L/LITER)
70 PSI
1.4 5 Kg/cm' 10.5
1.3 9.7
;>1
>1 1.2 9.0
6 la 1.1 8.2
4'1- ,.0 7.5
.9 6.7
+' .8 40 PSI 6.0
.
{ •
7 5.2
.6 4.5
.5 3.7
.4 3.0
I .3 2.2
.2 1.5
20 40 60 80 100 120 140 160 180 200 FT. DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
2
21.7
z 8• 20.9 1 inch (25.4 mm)
2.7 . 100 PSI / 20.2 Inside Diameter Discharge Hose
7Kgkm2
2.6 19.4 (Equivalent to 1.25-Inch O.D.Tubing)
2.5 18.7
2.4• 18.0
2.3 17.2
2.2• 16.5
2.1 15.7
2.0• / 15 APPROXIMATE
STANDARD 19 14.2
CUBIC FEET OF AIR STANDARD
PER 1.8• 13.5 LITER OF AIR
GALLON PUMPED 1.7 12.7 PER
(SCF/GAL) 1.6 12 LITER PUMPED
15 11.2 (STD L/LITER)
10PSI
1.4 , 10.5
1.3 9.7
1.2• 9.0
1.1 8.2
1.0• 7.5
.9 6.7
8 4 40 PSI 6.0
3 Kg/cm
.7 5.2
6 / 4.5
.5 / 3.7
.4 > 3.0
.3 2.2
.2 1.5
20 40 60 80 100 120 140 160 180 200 Fr. DEPTH
6.1 12.2 18.3 244 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
44

A uto ' umpo _a
., _ , . : ,. ,
HHP4T Top Inlet HammerHead Pro
Description
Max. Flow 9.8 gpm (37.1 Ipm)[.,
The HammerHead Pro HHP4T Top Inlet AutoPump
provides economy and high flow in a top inlet pump for 4"
iiiiI!
O.D. 3.5 in (8.9 cm) (100 mm)wells for applications requiring an elevated inlet,
such as pumping total fluids from wells contaminated with
Length 56 in. (142.2 cm) I� LNAPLs, and delivers flow rates up to 9.8 gpm (37.1 Ipm).
11 The HHPro Top Inlet AutoPump is complemented by the
lir most comprehensive selection of accessories to provide a
complete system to meet site specific requirements. Call
QED for prompt, no-obligation assistance on your pumping
project needs.
The AutoPump Heritage
The HammerHead Pro HHP4T Top Inlet AutoPump is part
of the famous AutoPump family of original automatic air-
powered pumps, developed in the mid 1980s specifically
to handle unique pumping needs at remediation and landfill
sites. Over the years they've proven their durability at
thousands of sites worldwide. AutoPumps are designed to
handle difficult pumping challenges that other pumps can't,
such as hydrocarbons, solvents, suspended solids,
corrosives, temperature extremes, viscous fluids and
frequent start/stop cycles. Beyond just the pump,
AutoPump systems offer the most complete range of
Advantage tubing, hose, connectors, wellhead caps and accessories
to help your installation go smoothly. This superior
1. Delivers higher flow rates than pumping heritage, application experience and support
all competitive pumps back up every AutoPump you put to work on your project.
2. Outstanding value in a high
reliability, high durability pump
3. Easier to service and lighter
weight than other 4" pumps
4. Handles solids, solvents,
corrosive conditions, viscous
fluids and high temperatures
beyond the limits of electric
pumps
5. Three-year warranty
V QED
fi.r.ni+:l tn.r
38

AutoPump°
Pro HHP4T
Top Inlet HammerHead
Pump Dimensions Specifications & Operating Requirements
Model 4"HammerHead Pro Top Inlet
Liquid Inlet Location Top
OD 3.5 in.(8.9 cm)OD
Length Overall(pump&fittings) 56 in.(142.2 cm)OD
Weight 16.5 lbs.(7.5 kg)
Inlet Max. Flow Rate 9.8 gpm(37.1 Ipm)-See Flow rate chart
Pump Volume/Cycle 0.58-0.66 gal(2.2-2.5L)
' Liquid Discharge Standard Model
Max. Depth 250 ft.(76 m)
air supply Air Pressure Range 5-120 psi(0.35-8.4kg/cm2)
Min.Actuation Level 53 in.(134.6 cm)
Exhaust Air Usage 0.34-1.13 scf/gal.
(2.24-8.23 liters of air/fluid liter)
See air usage chart
E Min. Liquid Density 0.7 SpG(0.7 g/cm3)
Standard Construction Materials
Pump Body Fiberglass
;g A Pump Ends Stainless Steel,Brass,Acetal
c k Internal Components Stainless Steel,Viton
Tube&Hose Fittings Brass
LL Fitting Type Barb or Quick Connect
0
0. g
2 Tube&Hose Options
t Tubing Material Nylon
cp
a Sizes'-Liquid Discharge 1 in.(25 mm)or 1-1/4 in.(32 mm)OD
Pump Air Supply 1/2 in.(12 mm)OD
Air Exhaust 5/8 in.(16 mm)OD
Hose Material Nitrile
Sizes-Liquid Discharge 3/4 in.(19 mm)or 1 in.(25 mm)ID
Pump Air Supply 3/8 in.(9 mm)ID
Air Exhaust 1/2 in.(12 mm)ID
'Applies to QED supplied tubing;
other tubing sources may not
conform to QED fittings.
t
O.D.3.5"(89 mm)
Application Limits HammerHead Pro Pumps are warranted for three (3)
The HHP4T Top Inlet HammerHead Pro AutoPump years: 100% materials and workmanship.
is designed to handle the application ranges
described below. For applications outside
this range, choose the appropriate AP4 model.
Maximum Temperature: 150° F (65° C)
pH Range: 4-9
Solvents and Fuels: diesel, gasoline, JP1-JP6,
#2 heating oil, BTEX, MTBE, landfill liquids
39
P.O.Box 3726 Arm Arbor,MI 48106-3726 USA 1.800.624.2026 F 1.734.995.1170 [e-mail] www.qedenv.com

AutoPump®
HP4T Top Inlet HammerHead Pro
Flow Rates'
1.00 inch (25.4 mm) 0.D. 1.25 inch (32 mm) 0.D.
Fluid Discharge Tubing Fluid Discharge Tubing
(Equivalent to 3/4-inch. (19 mm) Hose) (Equivalent to 1- inch. (25.4 mm) Hose)
6-INCH(15 cm) SUBMERGENCE OF PUMP HEAD 6-INCH(15 cm) SUBMERGENCE OF PUMP HEAD
18 68.1 18 68.1
16 60.6 16 - 60.6
14 AIR INLET PRESSURES 53 14 53
GALLONS APPROXIMATE GALLONS APPROXIMATE
PER 12 45.4 LITERS PER 12 -I AIR INLET PRESSURES 45.4 LITERS
MINUTE - 37 9 PER MINUTE 10 37 9 PER
WITH MINUTE WITH MINUTE
1-INCH 8 30.3 WITH 1.25-INCH 8
30.3 WITH
O.D.TUBING 6 _ 22.7 25.4 mm O.D.TUBING 6 100 P51 22.7 31.75 mm
100 PSI 15.1 O.D.TUBING 4 \' 7Kg/cm 2 151 O.D.TUBING
4 Kglcm
2 40 PSI ' 7.6 2 - 40P51 . 70 PSI '' 7.6
70 PSI
0 3 Kg:mac. S Kg-cm 2 0 0 3 Kg'cm- 5 Kg/cm 2 0
01 20 40 60 80 100 120 140 160 180 200 FT. 1 DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. -I DEPTH
6.1 12.2 183 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL 6.1 12.2 183 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
2 FT.(60 cm) SUBMERGENCE OF PUMP HEAD 2 FT.(60 cm) SUBMERGENCE OF PUMP HEAD
18 68.1 18 68.1
16 - - 60.6 16 - . 60.6
14 - 53
GALLONS 14 53 APPROXIMATE GALLONS APPROXIMATE
PER 12 AIR INLET PRESSURES - 45.4 LITERS PER 12 AIR INLET PRESSURES 45.4 LITERS
MINUTE 10 , 37.9 PER MINUTE 10 , , 37.9
PER
WITH MINUTE WITH MINUTE
8 30.3 WITH 1.25-INCH 8 30.3
1-INCH WITH
O.D.TUBING 6 100 PSI 223 25.4 mm O.D.TUBING 6 - 100 PSI 22.7 31.75 mm
\� 0.D.TUBING 7Kg/cm2 O.D.TUBING
4 \ 7Kg/cm 2 1.6 4 15.1
2 40 PSI \ 70 PSI 76 2 40 PSI 70 PSI 7'6
0 3 K y'cm= 5Kg/cm 2 0 0 13 Kg cm _ 0
0 20 40 60 80 100 120 140 160 180 200 FT. 7 DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. DEPTH
6.1 12.2 18.3 24.4 303 36.6 42.7 48.8 54.9 61 Meters IN WELL 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters 1 IN WELL
10 FT.(300 cm) SUBMERGENCE OF PUMP HEAD 10 FT.(300 cm) SUBMERGENCE OF PUMP HEAD
18 68.1 18 68.1
16 - 60.6 16 60.6
14 53 14 N'II' 'I f 77 ,JkeS 53
GALLONS APPROXIMATE GALLONS APPROXIMATE
PER 12 -I AIR INLET PRESSURES 45.4 LITERS PER 12 4S.4 LITERS
MINUTE 10 - 37.9 PER MINUTE 10 37.9
PER
WITH MINUTE WITH MINUTE
1-INCH 8 - 30.3 WITH 1.25-INCH 8
30.3 WITH
O.D.TUBING 6 - 100 PSI 22.7 25.4 mm O.D.TUBING 6 100 PSI 22.7 31.75 mm
7 Kg/cm 2
4
7 15.7 O.D.TUBING 4 15.1 O.D.TUBING
2 40 PSI 70 PSI 7.6 2 - 40 PSI '- - 70 PSI 7'6
0 3 Kg/cm 2 5Kg-cm 2 0 0 3 Kg/cm 2 5 Kg/cm 2 r 0
02'040-7-.80-100-1-2 -0-1W217)0 0 14FT. -1 DEPTH 0 20 40 60 80 100 120 140 160 180 200 FT. -1 DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL 6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
'FLOW RATES MAY VARY WITH SITE CONDITIONS. CALL QED FOR TECHNICAL ASSISTANCE.
♦QED
5nfonne I-I,
40

AutoPum °
Top Inlet t HammerHead Pro HHP4T
Air Consumption
1.6 12 1.00 inch (25.4 mm) 0.D.
1.5
1.4
1.3
11.2
,0.5
Fluid Discharge Tubing
( (Equivalent to 3/4-inch.
- (19 mm) Hose)
9.7
1.2 9.0
STANDARD 1.1
82 APPROXIMATE
CUBIC FEET OF AIR STANDARD
PER 1.0 7.5 LITER OF AIR
70 PH PER
GALLON PUMPED
(SCF/GAL) .9 6.7 LITER PUMPED
(STD ULITER)
6.0
5.2
4.5
3.7
.4 3.0
3 2.2
2' 1.5
20 40 60 80 100 120 140 160 180 200 FT.
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters DEPTH
IN WELL
1.6 12
1.5 11.2 1.25 inch (32 mm) 0.D.
Fluid Discharge Tubing
1.4. 10.5 (Equivalent to 1- inch.
•
13 97 (25.4 mm) Hose)
1.2 9.0
100 P51
1.1 7 Kg/cm 8.2
STANDARD APPROXIMATE
CUBIC FEET OF AIR STANDARD
PER 1.0 7.5 LITER OF AIR
GALLON PUMPED PER
(SCF/GAL) .9 - 6.7 LITER PUMPED
(STD ULITER)
.8 6.0
.7 5.2
.6 4.5
40 PSI
3 Kg/cm 2
5 / 3.7
.47.- 3.0
.3 2.2
.2 1.5
20 40 60 80 100 120 140 160 180 200 FT. 1DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
41
P.O.Box 3726 Ann Arbor,MI 48106-3726 USA 1.800.624.2026 F 1.734.995.1170 [e-mail] www.qedenv.com

Appendix IV - System Influent Laboratory Report

I dUIC UI 1,UIIL I IL
con-test®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone]*TEL.[phone]
April 9,2018
Bradley Keyse
S&ME,Inc-Arden,NC
44 Buck Shoals Road C-3
Arden,NC 28704
Project Location: 125 Hospital Drive,Spruce Pine,NC
Client Job Number:
Project Number:4305-17-109H
Laboratory Work Order Number: 18C1284
Enclosed are results of analyses for samples received by the laboratory on March 30,2018.If you have any questions concerning
this report,please feel free to contact me.
Sincerely,
tan) ArAte.
Kerry K.McGee
Project Manager
Page 1 of 16 J

I dUtG UI VUI ILCIIL
Table of Contents
Sample Summary 3
Case Narrative 4
Sample Results 5
18C1284-01 5
Sample Preparation Information 8
QC Data 9
Volatile Organic Compounds by GC/MS 9
B200229 9
Metals Analyses(Total) 10
B200353 10
Conventional Chemistry Parameters by EPA/APHA/SW-846 Methods(Total) 11
B199948 11
B200134 11
B200328 11
Flag/Qualifier Summary 12
Certifications 13
Chain of Custody/Sample Receipt 14
Page 2of16

Id..., L UI IteI ILJ
itig) comitESt®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone]*TEL.[phone]
S&ME,Inc-Arden,NC
44 Buck Shoals Road C-3 REPORT DATE: 4/9/2018
Arden,NC 28704 PURCHASE ORDER NUMBER:
ATTN:Bradley Keyse
PROJECT NUMBER: 4305-17-109H
ANALYTICAL SUMMARY
WORK ORDER NUMBER: I 8C1284
The results of analyses performed on the following samples submitted to the CON-TEST Analytical Laboratory are found in this report.
PROJECT LOCATION: 125 Hospital Drive,Spruce Pine,NC
FIELD SAMPLE# LAB ID: MATRIX SAMPLE DESCRIPTION TEST SUB LAB
Influent 18C1284-01 Ground Water EPA 1664B
EPA 420.1
SM21-22 2540D
SM21-22 6200B
SW-846 6010C-D
Page 3 of 16
I

I dUIC UI I,UI ILCI ILS
ton-test®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone]'TEL.[phone]
CASE NARRATIVE SUMMARY
All reported results are within defined laboratory quality control objectives unless listed below or otherwise qualified in this report.
For method 6200B elevated reporting limits for samples 18C1284-01 due to high concentrations of target compounds. Only a select list of analytes was
requested and reported.
SM21-22 6200B
Qualifications:
RL-11
Elevated reporting limit due to high concentration of target compounds.
Analyte&Samples(s)Qualified:
18C1284-01[Influent]
SW-846 6010C/D SW-846 6020A/B
For NC,Metals methods SW-846 6010D and SW-846 6020B are followed,and for all other states methods SW-846 6010C and SW-846 6020A are followed.
II
The results of analyses reported only relate to samples submitted to the Con-Test Analytical Laboratory for testing.
I certify that the analyses listed above,unless specifically listed as subcontracted,if any,were performed under my direction according to the approved methodologies listed
in this document,and that based upon my inquiry of those individuals immediately responsible for obtaining the information,the material contained in this report is,to the
best of my knowledge and belief,accurate and complete.
r)/1/46 .
.
Lisa A.Worthington
Project Manager
Page 4 of 16 ,

I dUlt;UI l,UI ltl;l It,
con-test®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone]*TEL.[phone]
Project Location: 125 Hospital Drive,Spruce Pine, Sample Description: Work Order: 18C1284
Date Received: 3/30/2018
Field Sample#: Influent Sampled: 3/29/2018 14:30
Sample ID: 18C1284-01
Sample Matrix: Ground Water
Sample Flags:RL-11 Volatile Organic Compounds by GC/MS
Date Date/Time
Analyte Results RL DL Units Dilution Flag/Qual Method Prepared Analyzed Analyst
Benzene 46 1.0 0.24 µg/L 2 SM21-22 6200B 4/5/18 4/6/18 10:38 EEH
1,2-Dichloroethane ND 2.0 0.39 µg/L 2 SM2I-22 6200B 4/5/18 4/6/18 10:38 EEH
Ethylbenzene 18 1.0 0.26 sg/L 2 SM2I-22 6200B 4/5/18 4/6/18 10:38 EEH
Methyl tert-Butyl Ether(MTBE) ND 1.0 0.18 µg/L 2 SM2I-22 6200B 4/5/18 4/6/18 10:38 EEH
Naphthalene 76 10 0.24 tsg/L 2 SM2I-22 6200B 4/5/18 4/6/18 10:38 EEH
Toluene 13 1.0 0.34 µg/L 2 SM2I-22 6200B 4/5/18 4/6/18 10:38 EEH
m+p Xylene 43 2.0 0.51 AWL 2 SM21-22 6200B 4/5/18 4/6/18 10:38 EEH
o-Xylene 41 1.0 0.26 µg/L 2 SM2I-22 6200B 4/5/18 4/6/18 10:38 EEH
Xylenes(total) 84 3.0 µg/L 2 SM21-22 6200B 4/5/18 4/6/18 10:38 EEH
Surrogates %Recovery Recovery Limits Flag/Qual
1,2-Dichloroethane-d4 93.2 70-130 4/6/18 10:38
Toluene-d8 98.5 70-130 4/6/18 10:38
4-Bromofluorobenzene 98.0 70-130 4/6/18 10:38
Page 5 of 16

I dull~UI IiUI IICI Ilb
COfltESt®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone]*TEL.[phone]
Project Location: 125 Hospital Drive,Spruce Pine, Sample Description: Work Order: 18C1284
Date Received: 3/30/2018
Field Sample#: Influent Sampled: 3/29/2018 14:30
Sample ID: 1801284-01
Sample Matrix: Ground Water
Metals Analyses(Total)
Date Date/Time
Analyte Results RL DL Units Dilution Flag/Qual Method Prepared Analyzed Analyst
Lead ND 0.010 0.0044 mg/L 1 SW-846 6010C-D 4/6/18 4/6/18 18:55 QNW
Page 6 of 16

I dUIC UI UI ILLI IL,
conotEst®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone]*TEL.[phone]
Project Location: 125 Hospital Drive,Spruce Pine, Sample Description: Work Order: 18C1284
Date Received: 3/30/2018
Field Sample#: Influent Sampled: 3/29/2018 14:30
Sample ID: 18C1284-01
Sample Matrix: Ground Water
Conventional Chemistry Parameters by EPA/APHA/SW-846 Methods(Total)
Date Date/Time
Analyte Results RL DL Units Dilution Flag/Qual Method Prepared Analyzed Analyst
Phenol 0.077 0.050 0.047 mg/L 1 EPA 420.1 4/4/18 4/5/18 14:00 MMH
Total Suspended Solids 2.2 1.0 0.61 mg/L 1 SM21-22 2540D 4/2/18 4/2/18 13:10 LL
Oil&Grease(HEM) ND 1.4 0.99 mg/L I EPA 1664B 4/6/18 4/6/18 13:00 LL
Page 7 of 16

414.) o
I du.,,. ..,,.....,....b
®
1
ANALYTICAL LABORATORY
39 Spruce Street'East Longmeadow,MA 01028*FAX [phone]'TEL.[phone]
Sample Extraction Data
EPA 1664B
Lab Number[Field ID] Batch Initial]mL] Date
18C1284-01[Influent] B200328 1000 04/06/18
EPA 420.1
Lab Number[Field ID] Batch Initial[mL] Final[mL] Date
18C1284-01[Influent] B200134 50.0 50.0 04/04/18
SM21-22 2540D
Lab Number[Field ID] Batch Initial[mL] Date
18C1284-01[Influent] B199948 500 04/02/18
Prep Method:SW-846 5030B-SM21-22 6200B
Lab Number[Field ID] Batch Initial[mL] Final[mL] Date
18C1284-01[Influent] B200229 2.5 5.00 04/05/18
Prep Method:SW-846 3005A-SW-846 6010C-D
Lab Number[Field ID] Batch Initial[mL] Final[mL] Date
18C1284-01[Influent] B200353 50.0 50.0 04/06/18
Page 8 of 16

I dL)IC UI L.UIIWIILS
4 Con-test®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone]*TEL.[phone]
QUALITY CONTROL
Volatile Organic Compounds by GC/MS-Quality Control
Reporting Spike Source %REC RPD
Analyte Result Limit Units Level Result %REC Limits RPD Limit Notes
Batch B200229-SW-846 5030B
Blank(B200229-BLKI) Prepared:04/05/18 Analyzed:04/06/18
Benzene ND 0.50 µg/L
1,2-Dichloroethane ND 0.50 µg/L
Ethylbenzene ND 0.50 µg/L
Methyl tert-Butyl Ether(MTBE) ND 0.50 µg/L
Naphthalene ND 0.50 µg/L
Toluene ND 0.50 µg/L
m+p Xylene ND 1.0 µg/1-
o-Xylene ND 0.50 µg/L
Xylenes(total) ND 1.5 µg/L
Surrogate:1,2-Dichloroethane-d4 23.1 µg/L 25.0 92.4 70-130
Surrogate:Toluene-d8 24.9 µg/L 25.0 99.5 70-130
Surrogate:4-Bromofluorobenzene 24.0 µg/L 25.0 96.1 70-130
LCS(B200229-BSI) Prepared&Analyzed:04/05/18
Benzene 10.1 0.50 µg/1. 10.0 101 70-130
1,2-Dichloroethane 8.73 0.50 µg/L 10.0 87.3 70-130
Ethylbenzene 10.2 0.50 µg/L 10.0 102 70-130
Methyl tert-Butyl Ether(MTBE) 9.43 0.50 µg/L 10.0 94.3 70-130
Naphthalene 9.26 0.50 µg/L 10.0 92.6 70-130 t
Toluene 9.73 0.50 µg/L 10.0 97.3 70-130
m+p Xylene 20.4 1.0 µg/1. 20.0 102 70-130
o-Xylene 10.1 0.50 µg/L 10.0 101 70-130
Surrogate:1,2-Dichloroethane-d4 23.3 µg/1. 25.0 93.4 70-130
Surrogate:Toluene-d8 24.6 µg/L 25.0 98.3 70-130
Surrogate:4-Bromofluorobenzene 24.6 µg/L 25.0 98.4 70-130
LCS Dup(8200229-BSDI) Prepared:04/05/18 Analyzed:04/06/18
Benzene 10.0 0.50 µg/L 10.0 100 70-130 0.894 25
1,2-Dichloroethane 8.83 0.50 µg/L 10.0 88.3 70-130 1.14 25
Ethylbenzene 10.2 0.50 µg/L 10.0 102 70-130 0.295 25
Methyl tert-Butyl Ether(MTBE) 9.61 0.50 µg/L 10.0 96.1 70-130 1.89 25
Naphthalene 8.93 0.50 µg/L 10.0 89.3 70-130 3.63 25 t
Toluene 9.63 0.50 µg/L 10.0 96.3 70-130 1.03 25
m+p Xylene 20.0 1.0 µg/L 20.0 99.8 70-130 2.03 25
o-Xylene 10.0 0.50 µg/1. 10.0 100 70-130 0.895 25
Surrogate:1,2-Dichloroethane-d4 23.8 11g/1. 25.0 95.2 70-130
Surrogate:Toluene-d8 24.7 µg/L 25.0 98.8 70-130
Surrogate:4-Bromofluorobenzene 24.4 µg/L 25.0 97.8 70-130
Page 9 of 16

I GUIC UI liUI!Lel Ilb
con-tEst®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone]*TEL.[phone]
QUALITY CONTROL
Metals Analyses(Total)-Quality Control
Reporting Spike Source %REC RPD
Analyte Result Limit Units Level Result %REC Limits RPD Limit Notes
Batch B200353-SW-846 3005A
Blank(B200353-BLK1) Prepared&Analyzed:04/06/18
Lead ND 0.010 mg/L
LCS(B200353-BSI) Prepared&Analyzed:04/06/18
Lead 0.501 0.010 mg/L 0.500 100 80-120
LCS Dup(B200353-BSDI) Prepared&Analyzed:04/06/18
Lead 0.494 0.010 mg/L 0.500 98.9 80-120 1.44 20
Page 10 of 16

1

I dUIC UI I,UI ILLI Ilb
ODcon-test®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone]'TEL.[phone]
QUALITY CONTROL
Conventional Chemistry Parameters by EPA/APHA/SW-846 Methods(Total)-Quality Control
Reporting Spike Source %REC RPD
Analyte Result Limit Units Level Result %REC Limits RPD Limit Notes
Batch B199948-SM21-22 2540D
Blank(B199948-BLK1) Prepared&Analyzed:04/02/18
Total Suspended Solids ND 2.5 mg/L
LCS(8199948-BSI) Prepared&Analyzed:04/02/18
Total Suspended Solids 176 20 mg/L 200 88.0 66.7-117
Batch B200134-EPA 420.1
Blank(B200134-BLK1) Prepared:04/04/18 Analyzed:04/05/18
Phenol ND 0.050 mg/L
LCS(B200134-BSI) Prepared:04/04/18 Analyzed:04/05/18
Phenol 0.53 0.050 mg/L 0.500 107 71.1-117
LCS Dup(B200134-BSDI) Prepared:04/04/18 Analyzed:04/05/18
Phenol 0.55 0.050 mg/L 0.500 110 71.1-117 2.81 9.35
Batch B200328-EPA 1664B
Blank(B200328-BLKI) Prepared&Analyzed:04/06/18
Oil&Grease(HEM) ND 1.4 mg/L
Blank(B200328-BLK2) Prepared&Analyzed:04/06/18
Oil&Grease(HEM) ND 28 mg/L
LCS(B200328-BSI) Prepared&Analyzed:04/06/18
Oil&Grease(HEM) 16 mg/L 20.0 79.0 78-114
LCS(B200328-BS2) Prepared&Analyzed:04/06/18
Oil&Grease(HEM) 380 mg/L 400 94.0 78-114
Page 11 of 16

I dUIC UI VUI IICI ILb
t ri".4
con tEst®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028'FAX [phone]*TEL.[phone]
FLAG/QUALIFIER SUMMARY
* QC result is outside of established limits.
t Wide recovery limits established for difficult compound.
$ Wide RPD limits established for difficult compound.
# Data exceeded client recommended or regulatory level
ND Not Detected
RL Reporting Limit is at the level of quantitation(LOQ)
DL Detection Limit is the lower limit of detection determined by the MDL study
MCL Maximum Contaminant Level
Percent recoveries and relative percent differences(RPDs)are determined by the software using values in the
calculation which have not been rounded.
No results have been blank subtracted unless specified in the case narrative section.
RL-11 Elevated reporting limit due to high concentration of target compounds.
1
Page 12 of 16

I i1UIC UI 1rV111C111J
ton-test®
ANALYTICAL LABORATORY
39 Spruce Street*East Longmeadow,MA 01028*FAX [phone] TEL.[phone]
CERTIFICATIONS
Certified Analyses included in this Report
Analyte Certifications
EPA 1664E in Water
Oil&Grease(HEM) CT,MA,NH,NY,RI,NC,ME,VA
EPA 420.1 in Water
Phenol CT,MA,NH,NY,RI,NC,ME,VA
SM2I-22 2540D in Water
Total Suspended Solids CT,MA,NH,NY,RI,NC,ME,VA
SM2I-22 6200B in Water
Benzene NC
1,2-Dichloroethane NC
Ethylbenzene NC
Methyl tert-Butyl Ether(MTBE) NC
Naphthalene NC
Toluene NC
m+p Xylene NC
o-Xylene NC
SW-846 6010C-D in Water
Lead CT,NH,NY,ME,VA,NC
The CON-TEST Environmental Laboratory operates under the following certifications and accreditations:
Code Description Number Expires
AIHA AIHA-LAP,LLC-IS017025:2005 100033 03/1/2020
MA Massachusetts DEP M-MA100 06/30/2018
CT Connecticut Department of Publilc Health PH-0567 09/30/2019
NY New York State Department of Health 10899 NELAP 04/1/2019
NH-S New Hampshire Environmental Lab 2516 NELAP 02/5/2019
RI Rhode Island Department of Health LA000112 12/30/2018
NC North Carolina Div.of Water Quality 652 12/31/2018
NJ New Jersey DEP MA007 NELAP 06/30/2018
FL Florida Department of Health E871027 NELAP 06/30/2018
VT Vermont Department of Health Lead Laboratory LL015036 07/30/2018
ME State of Maine 2011028 06/9/2019
VA Commonwealth of Virginia 460217 12/14/2018
NH-P New Hampshire Environmental Lab 2557 NELAP 09/6/2018
VT-DW Vermont Department of Health Drinking Water VT-255716 06/12/2018
NC-DW North Carolina Department of Health 25703 07/31/2018
Page 13 of 16

1

I `-"-C— bLi http://www.contesttabs.com Doc#379 Rev 1.03242017
1.,..,_.•.+ Con—test' Phone:[phone] CHAIN OF CUSTODY RECORD(North Carolina) 39 Spruce Street Page 1_of_1_
ANALYTH LARORATO«- East Longmeadow,MA 01028
Fax:[phone] Requested Turnaround Time
Email:infotzcontestlabs.com 7-Day 0 10-Day 0 6 1 1 2 1 II of Containers
Company Name: S&ME,Inc. -Asheville Due Date: HUNNH 2 Preservation Code
Address: 44 Buck Shoals Road,C-3,Arden,NC 28704 Rush-Approval Required VP A AP 1 Container Code
Phone: 828-483-3013 1-Day 0 3-Day ❑ p ANALYSIS REQUESTED Dissolved Metals Samples
Project Name: TF-3659 Blue Ridge Hospital-Spruce Pine 2-Day 0 4-Day ❑ ❑ Field Filtered
Project Location: 125 Hospital Drive,Spruce Pine,NC Data Delivery 1LI Lab to Filter
Project Number: 4305-17-10911 Format: PDF 0 EXCEL 0v
,o
Project Manager: Bradley Keyse Other: a Orthophosphate Samples
Con-Test Quote Name/Number: CLP Like Data Pkg Required: Li z - 0 al Field Filtered
Invoice Recipient: Email To: bkeVSe(@,,SrrleinC.COf11 os
c CI to Filter •
Sampled By: Gary Simcox Fax To tl: Fs A
Con-Test 13eglnning Ending Y146atrax *Inc °c i
ClientSample10/Description Composite` Grab ,n 9
-Work Corded/ late/Time Date/Time I- H a O Matrix Codes:
Code GW=Ground Water
� � WW=Waste Water
.
- ii Influent 3/29/2018 1430 x GW U X X XX. X DW=Drinking Water
A=Air
- S=Soil
SL=Sludge
.- -' — - SOL=Solid
0=Other(please
. define)
2 Preservation Codes:
I=Iced
-HCl
. _. M=Methanol.
N=Nitric Acid
S=Sulfuric Acid
B=Sodium Bisulfate
... ..... : X-Sodium Hydroxide
T=Sodium
Comments: Thiosulfate
0=Other(please
Please use the following codes to indicate possible sample concentration define)
within the Conc Code column above:
H-High;M-Medium;L-Low; C-Clean; U-Unknown a Container Codes:
' A=Amber Glass
Relinquished by:(signature) Date/Time:
3/29/18 2130 Li North Carolina Detection Limit Requirements Program Information G=Glass
2L IIDSCA ❑ UST/Trust Fund P=Plastic
Received by:(s nature) Date/Time: CIGWPC ❑ SWS Landfill ❑ REC SZ'=Sterile
V=Vial
A_t '1 X ,/ UCJ ' ,yam/,e /c,,22;' SWSL • ❑ IHSB Orphaned Landfill S=Summa Canister
Relin fished by: ignatu ) Date/Time: J *HSB s'. : Q State Lead T=Tedlar Bag
J /yg� // RM!R
4.,.;--':-/r\- 1,1„,/ / cL '� -�t`l'c.C� /& ❑ MSCC Z.0111111 ❑Other O=Other(please
ted by (sl. atu e)` , l �- 3 3 Date/Time: Other: — define) _
co K4L.,1,4fit 431118i0 co nquished by:(signature) to/Time: Project Entity Other PCB ONLY c_
4, ❑ Government ❑ Municipality ❑ Chromatogram ❑ Soxhlet
C
0 dived by: (signature) Date/Time: 0 Federal ❑ Brownfield 0 AIHA-LAP,LLC ❑ Non Soxhlet c
❑ City ❑ School R
cov

I dUIC UI liUIILCI Iib
3/31/2018 Track your package or shipment with FedEx Tracking
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I cdUIC UI L,UI I1 I I1J
(Mr-) CC" Ili—tEt
ANALYTICAL LABOR.TORY
:: Doc#:27 7:•Rev.B:2017
Login Sample Receipt Checklist -(Rejection Criteria Listing - Using Acceptance Policy) Any False
Statement will be brought to the attention of the Client - State True or False
Client ) nil ,;
Received By ' L_:� Date --;.:1--)13t l 1E-; Time t( )-_)1
How were the samples In Cooler ---\-- No Cooler On Ice mf No Ice
received? Direct from Sampling Ambient Melted Ice
Were samples within
By Gun# 5-17 Actual Temp- -_�.->> C..
Temperature? 2-6°C By Blank# Actual Temp-
Was Custody Seal Intact? k_ r- , Were Samples Tampered with? 1-kA
Was COC Relinquished ? ._1 Does Chain Agree With Samples? j
Are there broken/leaking/loose caps on any samples? I
Is COC in ink/ Legible? j Were samples received within holding time? T
Did COC include all Client 1 Analysis -T Sampler Name
pertinent Information? Project ID's t Collection Dates/Times --
Are Sample labels filled out and legible? T
Are there Lab to Filters? j= Who was notified?
Are there Rushes? Who was notified?
Are there Short Holds? 1— Who was notified?
Is there enough Volume? rt
Is there Headspace where applicable? 1-- MS/MSD? {.--
Proper Media/Containers Used? `t' Is splitting samples required? TT--
Were
-Were trip blanks received? - a— On COC?
Do all samples have the proper pH? Acid l 1 � Base yj-�
Unp- 1 Liter Amb. 1 Liter Plastic 16 oz Amb.
HCL- K 500 mL Amb. t 500 mL Plastic l 8oz Amb/Clear
Meoh- 250 mL Amb. 250 mL Plastic , 4oz Amb/Clear
Bisulfate- Col./Bacteria Flashpoint 2oz Amb/Clear
DI- Other Plastic Other Glass Encore
Thiosulfate- SOC Kit Plastic Bag Frozen:
Sulfuric- Perchlorate Ziplock
Unused Media', ;.
llnalla # r6 # ._ ES MMS__ _, _, , : : wa
Unp- 1 Liter Amb. 1 Liter Plastic 16 oz Amb.
HCL- 500 mL Amb. 500 mL Plastic 8oz Amb/Clear
Meoh- 1 250 mL Amb. 250 mL Plastic 4oz Amb/Clear
Bisulfate- Col./Bacteria Flashpoint 2oz Amb/Clear
DI- Other Plastic Other Glass Encore .
Thiosulfate- SOC Kit Plastic Bag Frozen:
Sulfuric- Perchlorate Ziplock _
Comments:
Page 16 of 16

Appendix V - Oil/Water Separator Specifications

. ,
..
DYNA- PAK
1. OIL/WATER SEPARATORS
'
For the Removal of Both Dispersed Oils & Settleable Solids
I
11
- ; -
iC. - r .'f .�� '(: F' -:) .fir• �• �L,``' _
,.....::•:::.I.::.:.::".:.4%...: • .:-4.•:••..:/1,....: :*•••:).••. ei:•:-• INN. - •.. •.•••••SO. •.
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•, 7- •••••V r...4!•...a•L„..c--C1.__:__.,----
F .. '11'. , ...oil/.g-ge.„tii-lt t%ie.,Tr•4
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= : : H N . .':'-'• •- •' . ' � •1-'66... '•- ,''•1. .•'-_ .I.r •l. ' .' - 'h',::f. r' - 'i 1•':z:�•:♦ b • a' _ �_;- r . i . - r..
T• i I N-L O,_-G I� . C
MASTERING THE ART OF OIL/WATER SEPARATION

HYDRO-FLO'S
Dyna-Pak oil/water
j separators provide
maximum efficiency and
t
! higher capacities in a
4111114111°.
l compact, cost effective
package.
QS
I i
I-` BASIC CONCEPTS
The basic concept used by ..
-10.
S.t
manufacturers'of gravity type oil water of the
1 separators is that materials of different velocity and direction plates. Solids
specific gravities will rise and settle at of flow, material of an entering the pack
predictable rates. By using the basic construction, and solids 4.,160 encounter a 60 degree
formulas, as outlined in Stokes Law, we handlingcapabilities.AtHydro- angle of inclination which
can predict the retention time necessary to Flo we usea proprietary Dyna-Pak is optimum for solids settling.
separate oil of any specific gravity and cross corrugated coalescing media. The solids slide down the plates
droplet size,from any given waste stream at The Dyna-Pak media was designed with gathering both mass and velocity as they
the desired flow rate.The problem is that a consideration of all these factors. The near the bottom of the pack and drop into
separator based solely on retention time specific shape and spacing of the Dyna-Pak the sludge collection chamber.
cannot effectively separate oil particles plates provides greater coalescing
smaller than 150 microns,and if they could performance than any other media available, C)
they would be prohibitively large. while also assuring maximum protection SLUDGE COLLECTION
from blinding. The Dyna-Pak media is CHAMBER:
By placing certain materials in the waste moldedofahighlyoleophilic(oil attracting) The sludge collection chamber is located
stream,the efficiencies of oil/watersepara- material which greatly enhances our oil- directly beneath the Dyna-Pak and pro-
don can be greatly improved due mainly to water separation capabilities. vides ample volume for the settled sludge.
The sides of the chamber are sloped at 45
OPERATION degrees to insure easy and complete re-
WITH DYrrA-PAx moval of the sludge. .
1 pr
COALESCING INFLUENT DIFFUSION
CHAMBER:
OIL REMOVAL:
Flow enters the inlet chamber where it is The separated oil accumulates at the sur-
evenly dispersed through a non-clog cid- face of the separation chamber where it
411 ..1:==-1---1----
wrrHOUT DYNA-PAK ! fuser across the width and depth of the displaces the water, as the oil layer in-
COALESCING MEDIA Dyna-Pak.Large solids fall out of suspen- creases, oil automatically spills over an
sion here before entering the separation adjustable oil skimming weir into an into-
' impingement on their surfaces.As fine oil i chamber. grad oil reservoir where it can either flow by
droplets impinge upon the plate surfaces ' gravity or be pumped automatically to
they coalesce,or merge,with previous drop- SEPARATION CHAMBER: remote storage tanks.
lets to produce much larger droplets.There I The separation chamber is filled with the
they continue to Brow in size until they are Dyna-Pak coalescing media.The pack cre-
large enough to break free and rapidly rise ates a uniform cross-sectional resistance EFFLUENT CHAMBER:
to the surface where they are skimmed or which further helps disperse the flow ThecleanwaterleavingtheDyna-Pakflows
decanted. This coalescing action allows throughout the separation chamber. The under the oil reservoir and up over the ad-
removal of smaller droplets than is possible I sinuosidial flow of wastewater through the justable effluent weir,which maintains the
with a standard gravity separator. pack serves to promote intimate contact liquid level throughout the separator. .s
between the oil droplets and the plate sur- the clean water passes over the effluent
The effectiveness of any coalescing media faces. The coalesced oil has the least re-_ weir it enters the effluent or clean water
is governed by several critical variables, stricted path to exit the waste scream, and chamber where itcan either flow by gravity .
shape, density, available surface area, slides to the top of the pack on the surfaces or be pumped automatically.•

LARGE
DROPLETS ". . .OveralI effluent oil
VENT
OUT
* content has been
MIXTURE __ _ reported
OF OIL ' y- ti ti, _ _= � .. . beto 60°
WATER .i uni _ . �-�: .. __ awl [� CLEAN t oup /O lower
&SOLIDSla ...1,!-;',. ....„1-1_-1:-H-:-1• ---2-.:-1.--.:-.7.-•.:-_-- - - WATER
• • w. for parallel plate
-„-_,-;22.:.. .:-.:--_-.-1---::-.:-:-:-. '. .. '
•- � �- • =--__:-, . systems, with a higher
SMALL tip, z��:�-�==-==- = •'
DROPLETS proportion
L\ 'N';:;>; ;.(11;;,.,x: of small oil droplets
.t,,- OIL
K.�.�.: .M recovered"
* Shown with Design & Operation of
• SOLIDS optional oil Oil-Water Separators
•
{ reservior API Publication 421, Feb. 1990
' Note:Any reference to
the API is not meant as an
MAJOR SECTION endorsement by the
American Petroleum Institute.
❑ Removes both dispersed oil(down to 10
0 PPM@ 20 microns)and settleable solids
MATERIALS OF I 0 Sludge pump out package ❑ Custom designs for specialized
0 Recovered oilpackageapplications-no matter what your
CONSTRUCTION: pumpout
❑ Effluent oil content monitor requirements are,Hydro-Flo is your best
Standard materials of construction include, choice for oilywaste solutions
but are not limited to,carbon steel,stainless ❑ Heater package for freeze protection
i
steel, PVC, neoprene, schedule 40 pipe, 0 Hazardous environment upgrades
' 15N ANSI flanges, and grade 5 stainless available APPLICATIONS:
steel fasteners, 0 All stainless steel construction 0 Automotive Maintenance Facilities
as ers all water tight weld Joints
g 0 Elevated temperature protection (For 0 Airports
are double welded and tested either hydro-
staticalI , magnafluxed, d Y e- ne[rant or applications over 140 Degrees F.) 0 Bus terminals
Y gn
l�
0
Special coating systems for severe 0 Bulkplants NDE methods in accordance with
current military specifications. interior/exterior environments 0 Chemical plants -
❑ Sludge auger package 0 Cosmetic industry
COATINGS: ❑ Oil drag skimmer package 0 Electro chemical plants
0 Chemical pre and post treatment for 0 Fabricated metal plant
Above grade carbon steel tanks have an complex emulsions. 0 Glass factories
exterior surface that is prepared to a SSPC- 0 Grinding and honing operations
SP6,commercial blast, and given one(1) 0 Lens grinding and polishing
coat of self priming epoxy paint(6DMT). FEATURES:
O Military bases
All steet tanks have an interior surface that ❑ Sizes from 2 GPM to 3000 GPM 0 Oil fields&Refineries
is prepared to a SSPC-SP10, near white O Sludge collection chamber-keep media 0 Petroleum plants
metal blast,and given two(2)coats of coal maintenance free 0 Pulp and paper mills
tar epoxy(16 DMT). As a standard on all ❑ Compactdesign-takes up less space than 0 Railroad yards i
buried equipment, Hydro-Flo will supply competitive units 0 Rolling mill quench oil
dielectric insulators and anodes to insure ❑ Best possible oil removal without 0 Steam cleaning facilities
state-of-the-art corrosion protection for chemical treatment 0 Textile mills
years of trouble free operation. 0 Fast and easy installation 0 Tramp oil separation
O Fast delivery ❑ Truck maintenance terminals
AVAILABLE OPTIONS: 0 High quality-we can compare every 0 Utility companies
❑ Flow control packages aspect of our equipment against any of 0 Wire drawing operation
O Influent pump package the competition 0 Wash racks

Mastering the Art of Oil/water beparazzo""
.
DP-211/STI,/1:15/0 design info
Designed flow rate = 15 GPM a 70 microns to 34 GPM a 30 microns
Specific gravity of the wastewaters aqueous phase = 1 .0
Specific gravity of the oil phase = .8Z
Oil droplet removal rate = 10 mg/1 of oil droplets > 20 to 30 microns
Media pack size to be 24"W x 36"0 }: 4U"L
Minimum projected surface area = 360 square feet
Minimum coalescing surface area = 720 square feet
Ma;:i m.cm crass sectional velocity = .37 to .76 f eel'/min
29 to 10 ruin
-
Minimum separation chamber retention time -
Minimum sludge chamber capacity = 36 gallons
device for oil removal = Integral oil reservoir with adjustable 011
skimming weir
DP--24/STL/1121/0 design iiifo
Designed flow rate = 21 GPM a 20 microns to 47 GPM a 30 microns
Specific gravity of the wastewaters aqueous phase = 1.0
Specific gravity of the oil phase = .85
Oil droplet removal rate = 10 mg/1 of oil droplets > 20 to 30 microns
Media pack size to be 24"W tc 36"D x 48"L
Minimum projected surface area = 504 square feet
Minimum coalescing surface area = 1008 square feet
Maximum crass sectional velocity = .47 to 1.15 feeo t/min
Minimum separation chamber retention time
Minimum sludge chamber capacity = 56 gallons
device for oil removal = Integral oil reservoir with adjustable oil
skimming weir
There are two oil/water separators at the site. Both are the same model listed below-
•
DP-24/STL/*34/0 design info
Designed flow rate = 34 GPM 2 20 microns to 77 GPM a 30 microns i
Specific gravity of the wastewaters aqueous phase = 1.0
Specific gravity of the oil phase = .85
- Oil droplet removal rate = 10 mg/1 of oil droplets > 20 to 30 micro
Media pack size to be 24"W x 36''D x 48"1.
Minimum projected surface area = G16 square feet
Minimum coalescing surface area = 1632 squo are feett
min
Maximum cross sectional velocity = .75
Minimum separation chamber retention time = 10 to 7.4G min
Minimum sludge chamber Capacity = 56 gallons
device for oil removal = Integral oil reservoir with adjustable oil
skimming weir
"DP" SERIES COALESCING TYPE
Cross Corrugated Plate 0il/Water Separators Page 01
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Appendix VI - Shallow Tray Air Stripper Software Output

1
1
i
1

an
low profile f t r l p p e f s Original Design Criteria from 1993
System Performance Estimate Series chosen: 3600 3600
Client and Proposal Information: Water Flow Rate: 40.0 GPM US 9.1 m3/hr
Air Flow Rate: 900 CFM 1529 m3/hr
Blue Ridge Hospital Water Temp: 55°F 12.8°C
125 Hospital Drive Air Temp: 59°F 15.0°C
Spruce Pine,NC A/W Ratio: 168:1 168:1
S&ME Project 4305-17-1097 Safety Factor: 10% 10%
Water Discharge Temp. 55.2°F 12.9°C :IUCED DRI'
Model 3611 Model 3621 Model 3631 Model 3641 Model 3651 Model 3661
Untreated Influent Effluent Effluent Effluent Effluent Effluent Effluent
Contaminant Effluent Target ppmv , hr ppmv Lbs/hr ppmv Lbs/h: ppmv Lbs/hr ppmv Lbs/hr ppmv
%removal %removal %removal %removal %removal %removal
Benzene 4600 ppb 185 ppb 7 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 1,780 ppm ppb .. 7.96 8.28 0.09 8.30 n ie< 8.30 0.09 8.30 0.09 8.30
Mwt 78.12 71-43-2 r 95.99% 99.84% 99.99% 100.00% 100.00% 100.00%
Toluene 3900 ppb 185 ppb 9 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 515 ppm ppb o? 5.68 0.00 5.95 0.08 5.96 0.115 5.96 0.08 5.96 0.08 5.96
Mwt 92.13 108-88-3 95.25% 99.77% 99.99% 100.00% 100.00% 100.00%
Ethyl Benzene 3400 ppb 118 ppb 4 ppb <I ppb <1 ppb <1 ppb <I ppb
Solubility 152 ppm ppb 0.07 4.36 0.0' 4.51 0.07 4.51 0.07 4.51 0.07 4.51 0.07 4.51
Mwt 106.16 100-41-4 96.51% 99.88% 100.00% 100.00% 100.00% 100.00%
Xylenes 13000 ppb 502 ppb 19 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 175 ppm ppb :[, 16.61 0.26 17.25 0.26 17.28 0.26 17.28 0.26 17.28 0.26 17.28
Mwt 106 1330-20-7 96.14% 99.85% 99.99% 100.00% 100.00% 100.00%
Naphthalene 4600 ppb 516 ppb 58 ppb 6 ppb <1 ppb <1 ppb <1 ppb
Solubility 30 ppm ppb 4.49 4.99 0.09 5.05 0.09 5.06 0.09 5.06 0.09 5.06
Mwt 128.16 91-20-3 88.79% 98.74% 99.86% 99.98% 100.00% 100.00%
1,2-Dichloroethane 10 ppb 2 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 550 ppm ppb '!00 0.01 0.00 0.01 0.00 0.01 0.00 0.01 0.00 0.01 0.00 0.01
Mwt 98.96 107-06-2 79.23% 95.68% 99.10% 99.81% 99.96% 99.89%
MTBE 10 ppb 3 ppb 1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 43,000 ppm ppb 0.01 0.00 0.01 0.00 0.02 0.00 0.02 0.00 0.02 0.00 0.02
Mwt 88.15 1634-04-4 67.08% 89.16% 96.43% 98.83% 99.61% 99.87%
Total ppb 29520 ppb 1512 ppb 99 ppb 9 ppb 1 ppb 0 ppb 0 ppb
Total VOC Lbs/hr - ppmv 0.56 39.13 0.59 41.02 0.59 41.13 0.59 41.14 0.59 41.14 0.59 41.14
Total 94.88% 99.66% 99.97% 100.00% 100.00% 100.00%
This report has been generated by ShallowTray Modeler software version IMP.This software is designed to assist a skilled operator in predicting the performance of a ShallowTray air stripping
system.Hydro Quip,Inc.is not responsible for incidental or consequential damages resulting from the improper operation of either the software or the air stripping equipment.This software is
Copyright Hydro Quip,Inc.,2015.
Report Generated:4/17/2018 Modeler VIMP SEPT 2015

Shad Design Based on March 29, 2018
low profile a.r strippers - Influent Sample Data
System Performance Estimate Series chosen: 3600 3600
Client and Proposal Information: Water Flow Rate: 14.0 GPM US 3.2 m3/hr
Air Flow Rate: 900 CFM 1529 m3/hr
Blue Ridge Hospital Water Temp: 55°F 12.8°c
125 Hospital Drive Air Temp: 59°F 15.0°C
Spruce Pine,NC A/W Ratio: 481:1 481:1
S&ME Project 4305-17-109H Safety Factor: 10% 10%
Water Discharge Temp. 55.6°F 13.1°C INDUCED DRAF
Model 3611 Model 3621 Model 3631 Model 3641 Model 3651 Model 3661
Untreated Influent Effluent Effluent Effluent Effluent Effluent Effluent
Contaminant Effluent Target .l.t;hr ppmv Lbs/hr ppmv Lbs/hr ppmv Lbs/hr ppmv LI. ppmv ppmv
%removal %removal %removal %removal %removal %removal
Benzene 46 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 1,780 ppm ppb 0.00 0.03 0.00 0.03 0.00 0.03 0.00 0.03 0.03 0.00 0.03
Mwt 78.12 71-43-2 99.56% 100.00% 100.00% 100.00% 100.00% 100.00%
Toluene 13 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 515 ppm ppb 1.00 0.01 0.00 0.01 0.00 0.01 0.00 0.01 0.00 0.01 0.00 0.01
Mwt 92.13 108-88-3 99.42% 100.00% 100.00% 100.00% 100.00% 100.00%
Ethyl Benzene 15 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 152 ppm ppb 0.01 0.00 0.01 0.00 0.01 0.00 0.01 0.01 0.00 0.01
Mwt 106.16 100-41-4 99.65% 100.00% 100.00% 100.00% 100.00% 100.00%
Xylenes 84 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 175 ppm ppb '100 0.04 0.00 0.04 0.00 0.04 0.00 0.04 0.00 0.04 0.00 0.04
Mwt 106 1330-20-7 99.59% 100.00% 100.00% 100.00% 100.00% 100.00%
Naphthalene 76 ppb 4 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 30 ppm ppb n0 0.03 O..'' 0.03 0.00 0.03 0.00 0.03 a.n0 0.03 0.00 0.03
Mwt 128.16 91-20-3 94.31% 99.68% 99.99% 100.00% 100.00% 100.00%
1,2-Dichloroethane 1 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
Solubility 550 ppm ppb on 0.00 0.Of` 0.00 0.00 0.00 0.00 0.00 0.0n 0.00 0.00 0.00
Mwt 98.96 107-06-2 97.66% 99.95% 100.00% 100.00% 100.00% 100.00%
MTBE 1 ppb <1 ppb <1 ppb <I ppb <1 ppb <1 ppb <1 ppb
Solubility 43,000 ppm ppb 00 0.00 0.00 0.00 0.00 0.00 0.00 1.0c, 0.00 0.00 0.00
Mwt 88.15 1634-04-4 90.84% 99.16% 99.92% 99.99% 100.00% 100.00%
Total ppb 239 ppb 5 ppb 0 ppb 0 ppb 0 ppb 0 ppb 0 ppb
Total VOC Lbs/hr - ppmv 0.00 0.11 0.00 0.11 0.00 0.11 0.00 0.11 0.00 0.11 0.00 o.11
Total 97.65% 99.69% 99.99% 100.00% 100.00% 100.00%
This report has been generated by ShallowTray Modeler software version IMP.This software is designed to assist a skilled operator In predicting the performance of a ShallowTrey air stripping
system.Hydro Quip,Inc. is not responsible for incidental or consequential damages resulting from the improper operation of either the software or the air stripping equipment.This software is
Copyright Hydro Quip,Inc.,2015.
Report Generated:4/17/2018 Modeler VIMP SEPT 2015

Appendix VII — Shallow Tray Air Stripper Specifications

NOV-18-93 THU 15:38 North East Env Prod FAX NO, 16032987063 P. 02
low profile air strippers
System Performance Estimate
Clio..t A t,upwatl h.rv.nial4H I_ rvwur. CI wsr.I. .,o u.,.
National Environmental 'Centrations have been updated using ave bAicf Tamp: 50..0 '
` from actual influent concentrations Air temp: 50.0 =
collected March 30, 2018. Model 3631 is A/W Ratio: 134 J cu.ft/Cu.ft
currently installed at site. Safety Factor Nc le
Untreated. Model 9611 Model 3621 odel 3631 / lode) 3641
Contornlnont Influent Effluent Effluent ffluent Effluent
Water Water Water Water
Air(lbs/hr) Air(lbs/hr) Air(lbs/hr) Air(lbs/hr)
75 removal %removal •• removal %removal
Bonzono 4600 ppb 378 ppb 32 ppb 3 ppb <1 ppb
0.105596 0,114250 114978 0.115045
91.7862% 99.3253% • 9446 _ 99.9954%
Ethyl Benzene 3400 ppb 248 ppb 19 ppb <1 ppb
0.078810 0.084562 0.• 0.085 35
92.6785% 99.464U% 39. 1 • 99.99%1%
Naphthalene 4900 ppb 3060 ppb 2329 ppb 148 944 ppb
f0,023510 0.056800 0.0 0.091440
20.4507% 09.3752%, 117 79.4971%
p-Xylene 13000 ppb 905 ppb b9 ppb - P. 1 ppb
0.302509 0.323567 950 0.325119
03.0440% 00.6161% 0.0669 00.0077%
Talueno 3000 ppb 050 ppb 05 ppb 4 ppb I ppb
0.088339 0.096668 0.097443 0.097519
90.5784% 99.1123% 99.9164% 99.9921% '
I -
I
As requested, listed above is the modeling for the Model 3631. Bis (2-ethyl Hexyl Phthalate),
Phenanthrene, and phenol are difficult to strip and will not see much or any removal with air
stripping. Bis(2-ethyl Hexyl Phthalate) is not water soluable and has a low vapor pressure,
Phenol Is water soluable with a low vapor pressure and phenanthrene, in best case, will strip
apporximately 40%.
, i .
t '
This report has been generated by ShallowTray Modeler software version 1.4.1.This software is designed to assist a skilled operator
in prodding the performance of a ShalbwTray air stripping system.The software wil accurately predict the system performance
when both the equipment and the software are operated according to the written documentation and standard operation.
North East Environmental Products,inc.cannot be responsible for incidental or consequential damages resulting from the improper
operation of either the software or the air stripping equipment Report generated:11/18/93
®Copyright 1992 North East Environmental Products, Inc.• 17 Technology Drive,West Lebanon,NH 03784
Voice:603-298-7061 FAX:[phone]•All Rights Reserved.

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AllE1111111111111/11111111111111111Mii=iiiMffiallin
L o w Profile be easily cleaned through ports using a washing
'y"he discreet size of a ShallowTray„ air stripper does wand and pressure washer. Trays can also be easily
-nor advertise a contamination sire. It is easily removed for a thorough inspection and cleaning.
accessed for maintenance and can be installed inside
a building.The system is also ideal as a trailer- Full Range Turndown
mounted, portable stripper for pump rests, pilot Not only are ShallowTray systems forgiving of
studies, short-term cleanup, or emergency response. "surprise" inorganics in the water, they also allow
There is no tower. operation anywhere within the rated flow range. In
fact, as the flow rate is
Treatment reduced, performance
The airforms afroth of bubbles approximately- increases. Also as demands
The ShallowTray process 6 inches deep on the aeration tray,generating a Also,
uses forced draft, large mass transfer surface area where the change (stricter effluent
countercurrent air stripping contaminants are volatilized. contaminant levels) so can
through baffled aeration the ShallowTray system. Its
p:::—..,_ ' ••.: modular design allows for
trays to remove volatile ;i► ''' �'
-r `�J:2;.;'f E .-f;�r f.:"r,' �f �.-,1 ,r,--,&!;,:i1.-,f4. the addition of trays which
organic compounds -2:-,,,k-i:,-,i4-,/,5,..,-;41.,-i-�a . �i•r`:1;� -f;.
from water. - f jl�} ..;,..•."4-4-%2 . 0!'i •ll v S y �s ' �. 1', increase the percent removal
r � , ' ,;1„i.r ". a t r ` t 10.4% of contaminants.
1 f, 3 Tt � :
Contaminated water is 1;x,11.-,:.9•,,1-JJ .-`.../' t:-,,-.2.,-., '� -.�r,;,. f a
sprayed into the inlet t'ii 1- h l �r;G.lr JI�, .-�Z-) -- ;; .
f: ).( �, ,;�,f1 rel,? ii '= 71 No Disposal
chamber through a coarse *-.. 3,;r z'`r 5 ; t '� '1 Q�` ' )-, x
1 i „^� ShallowTra systems have
mist spray nozzle.The .1.?'-i , . • ',, it_F, t si,4�- t ,z4"-.1-.V.-.'' Y Y
9 --.!,....,-.;.•.,..s - •. • ,,i`.. ? 1�.ir -, no packing or diffusers to
Darer flows over a flow .�•.� ;,',., .,, _, ?- N.i ,‘, �3' '' Zr '
,;_:-t.'•�- az ,,f',..;: � ;''...,`=� ,;.�:.t -;.� ` contend with and no costs
distribution weir and along `c _'.:`_,.t;'• . • :4.::".:.-- . _-;,:,,
the baffled aeration tray. associated with GAC
Air, blown up through breakrbrough, fouling or
disposal and replacement.
3/ib" diameter holes in the Air is blown up through hundreds of i/6'diameter
aeration tray, forms a froth holes in the aeration tray.
of bubbles generating a System Size
large mass transfer surface To determine the system
area where the contaminants are volatilized.The size required for your site, first identify the flow
necessary contact or residence time to reach rate. This guides you to the ShallowTray Series
required volatilization is achieved through model needed. As an example, with a flow rate of 30gpm,
size, addition of trays, and flow rate selection. select the 2600 Series,which is rated for flows from
1 to 50gpm.
Resistant to Fouling -
ShallowTray systems are resistant to fouling Next, identify the contaminants present and the
//b" diameter removal requirement. Generally, this determines the
problems. Treatment trays have large 3
aeration holes. In addition, the turbulent action of number of trays required. However, the graphs in
the froth scours the surfaces of the tray reducing this brochure should be used as a guideline only.
build-up of oxidized iron. For a proposal, send us or your representative the
specifications.Request for Quotation-sheets are
If, under extreme conditions, oxidized iron available.
' accumulates or hardness begins to scale up, trays can
Ji.

6
0 0 Series ,.:
.,r
le _
._..,
1 . r
' .�
a . '0_ -pl---0-1 . IF ,� ,� }F. "_ Model Pictured: 3631
vs ~-a^o« r �' Options chosen for system pictured:
mrALr- p
�, ,3d as -r+r� . t0 ® �Ti- C
1� y 4� ` �, :. 1 :. tf' l'EXP Feed and Discharge pumps
®� °' 4} ,` i✓' Two NEMA 7 control panels with
O1!� ,, az. k ' f alarm interlocks,motor starters and
• r ,, ,i €� I —r i: •ti intrinsically safe relays for the
I I' I , i I Pl. it-' i
I „ 1�: ShallowTray system,as well as
��• 1 pl EXP controls for two well pumps,
1 =� =: i •
an oil water separator and surge
- tank
=__,.. . ��;<;~ iiNEMA 7 main disconnect switch
r +1 C�Low air pressure alarm switch
• ` ` ' fK1
< ..1. [if High water level alarm switch
. iDischarge pump level switch
f`; ;_ ki Water pressure gauges
t � ,r �- z I'. ' -7=:'
P
' g'Digital water flow indicator and
. B
,� 1 totah7er
i Air flow meter
q ! ifTemperature gauges
— _ ` - '' • �' [ Line sampling ports
ypical 3641 Configuration*
AIR EXHAUST 70-SSB In.OD
t 1 I (PRESSURE GAGE I I
Ibk? SAMPLE PORT I TEMPERATURE GAGE
FLOW METER I
'
I
12 in.
AIR FLOW GAGE AERATION TRAY
AIR PRESSURE GAGE 1:=2=1
I AIR PRESSURE SWITCH 12 m.
' 1 O 6 1AEPATtON TRAY
ICS-) G�
o _ f
CONTROL MAIN 121n,
' PANEL BBox- AERATION TRAY
c�
000 _ I 121n. 99 in.
4'CLEANOUT PORTS ' AERATION TRAY
HANDLES - n C
QALARM HORN
.---
WATER-LEVEL
BLOWER
B'INSPECTION PORT I WATER-LEVEL / ("�^
SIGHT TUBE -
AIR
INTAKE INLET HOLDING TANK
HIGH LEVEL ALARM FLOAT HIGHLEVGLBMFLOATSWCH i BLOWER
0
SAMPLE PORT
PRESSURE GAGE O __—.4TEMPERATURE GAGE 0
FLOW CONTROL VALVE
OUTLET PUMP FLOAT SWITCH I O VALVE
OL OP ul=O DRAIN
1
( SKID MOUNT FRAME 1 SKID MOUNT FRAME IJ,
I
i...----— —Ta In — RIGHT SIDE VIEW
FRONT VIEW
'Use these drawings as a guideline only.Systems are built to your project's specifications.
-

, 1
r Percent Removal vs. Flow Rate
TCE
mo-
1 /11 SU— ..••••••,,... Benzene
••
flow # min. approx.
Models, rate trays width length height cfm lbs. NS--, .•
\•
OS
- 3611 1-75gpm 1 5' 6'2" 5'3" 900 1240 .. MTBE
se- ...„.,.,
1 3621 1-75gpm 2 5' 6'2" 6'3" 900 1440 N "..,.
...,....
1 , —
N-
3631 1-75gpm 3 5' 6'2" r3" 900 1640
m-
3641 1-75gpm 4 5' 6'2" 8'3" 900 1840
3D- Four Trays
TCE '
MO
US— __—NU....•.....
Benzene .•••
SU— .....
'•
, 10 — %...
'•
N— N.,•
1
_ '‘,.... .
N— ,
,%,MTBE
ss-
. ...,
''.
so- - ..„----7
,.,...,............,.
so- I
i I
Shall
so._
low pro ile air strippers lir
"- Three Trays'
TCE i I
NS—
.6".'" Irlr6.—•
ft
NO— ft
•
. •
. N.31— •....
. Benzene
..
N "."--..
3600 AERATION TRAY ... ....,.
as- •...
WATER L c 0,1 .
GRUNER 10 '• MTBE
so- .411.41.••••...i.....,
Utm.U1=1,1m1.m.wiftdM00.I.,
. .. . . .. le 33..
........ ...,-.......... .....
' .. ...... '.'...'.....:........... ...... ). Two Trays
. •..... •.. •...•...••.. .. • ... 0 0
. ... ... ...-.--• .-.
.. .......... .-.....-.-......• .... E too_
. . ... ..... .. ......... .. ....
. ....... .
. . ... .
. ... ..... . ..
, ......... . .
OnT
. . .
C.
' ' .• '—" .
. . . .......... . ...
••• ..... . ...-.
I V
... .
.. .... . ..
. . ... . . ..... . . 1.. 96_ ...
0.1
.,.. ..... ..... . ., ,...... .. . . ..... ...
..:..,..:........:...••......:....:..:\-..:.......s......s.*........:...'.....,...:......-:........-...:.....::...........:......:...:...::......:............. ...............:
Ieso
-' .,.,-,. . ..-.. ,.....,,.,.
...
......
•.•.•
M•I•ft..M..
.ImitBeOWnIftzefft-
..... .. . .. . ., „ MTBE
...:.... 10—
..e-
.
,
.. ... __ -.- . . ... 3OneTray
. . .... . ...... . ... .
.......• ..• .....••...........•......-. ..:. o 16 26 oh ih 66 oh- A do sh 'do '
') ' "... .', .' ".." ..•'•"... ... . ..•-• •• ' "•
.. ......... Percent of Rated GPM
, . 3600
TOP VIEW GPM 0 10 20 30 40 50 60: 75
The graphs represent approximate removal efficiencies.Use the
• ShallOwTrapt modeling program to calculate expected performance.
-'
A .A1.116.

Appendix VIII — Particulate Filter Specifications
Pp P

FSI
Bag
Filter Vessels
..b.
a
0
4
1.41111111111111

FSI Advanced Design
FSI Bag Filter Vessels are designed,built and stamped to meet code requirements in our own
FSPN-2500 Shown with ► ', - ASME code manufacturing facilities.Features like the single-gasket seal,permanent piping and
Clam Shell Pneumatic =`•r, sturdy perforated metal baskets as standard equipment provide durable and consistent
Lid Lifter ............. • , '1, performance.Positive bag hold down is an integral part of the lid.Our advanced basket design
..�. ,
1 ,, ^ eliminates the need for under-basket gaskets.Swing-out cover bolts with eyenuts simplify the
' ' r bag changing operation,while our(optional)Displacement Floats reduce spillage and ensure
-.. proper seating of the bag.
.. Of course,all FSI Bag Filter Vessels are fully compatible with conventional ring type bags as well
:' as FSI Polyloc®bags,which feature the most advanced sealing device on the market today.
...:
4~'..... Standard Features Options
It- • Completely cleanable;easy cleaning access • Titanium,Hastelloy B&C,and Alloy 20
11,. • Full ports for unrestricted flow available on request
4 • Sturdy baskets standard(no gasket required) • Coatings available
# �• • Single gasket lid seal • Heavy duty baskets available
• Positive bag sealing • Additional connections including
'
304Ilir•H'
housing standard; SanitaryFittings and Socket Weld
II � Carbon Steel or SS ous g s a g
,�, -1 r -, 316 SS available on request are available
--
' r 1 i
STANDARD FILTER VESSELS
Model No. No.of Gags Gag Situ.No. Surface Area Surface Area Inlet S Max f low
Pr,r Gag.FL' Pot Vessel.Ft.' Outlet Sire Rate,GPM
FSPN-20 1 3 0.5 0.5 r 25
FSPN-35 1 4 1.0 1.0 1" 45
FSPN-40 1 1 2.0 2.0 2' 90 •
FSPN-85 1 2 4.4 4.4 2" 200
FSPN-250 2 2 4.4 8.8 3"-4" 400
FSPN-252 2 2 4.4 8.8 3"-4" 400
FSPN-355 3 2 4.4 13.2 3'-6" 600
FSPN-800 4 2 4.4 17.6 4"-6" 800
F5194-1000 5 2 4.4 22.0 4"-8" 1000
Polyloc snap tight bag seal F5PN-1100 6 2 4.4 26.4 4"-8" 1200
F5194-1300 7 2 4.4 30.8 6'-8" 1400
Permanent piping FSPN-2000 8 2 4.4 35.2 6"•8' 1600
F5191-2200 9 2 4.4 39.6 6"-8" 1800
(in-line models available) FSPN-2500 10 2 4.4 44.0 6"-8" 2000
. FSPN-3000 12 2 4.4 52.8 8"-10" 2400
F5494-3500 14 2 4.4 61.6 10--12" 2800 1
FSPN-4000 16 2 4.4 70.4 10"-12" 3200
_FSPN-4200 18 2 4.4 79.2 10"-14' 3600
FSPN-4500 20 2 4.4 88.0 10"-14" 4000
FSPN-4800 22 2 4.4 96.8 10"-14" 4400
^ FSPN-5000 24 2 4.4 105.6 10"-14" 4800
7,7714
*Maximum flow rate is based on aqueous flaw at 10 PSI AP clean.Inlet and outlet pipe sizes can be changed to meet customer requirements.
I STANDARD EASY OPEN LID VESSELS
Hinged cover and swing- Model No. No.of Bugs Bag Size No. Soria,c Area Surface Area Inlet& Max Flow
out bolts with eyenuts - Pur Gag,It.' Pat Vessol,Fl: Outlet Sire Rafu,GPM'
` FSPZ-800 4 2 4.4 17.6 4"-6" B00
g; FSPZ-1000 5 2 4.4 22.0 4"-8" 1000
- F502-1100 6 2 4.4 26.4 4"-8" 1200
FSPZ-1300 7 2 4.4 30.8 6"-8" 1400
F54PZ-2000 8 2 4.4 35.2 6"-8" 1600
FSPZ-2200 9 2 4.4 39.6 6"-8" 1800
•r FSPZ-2500 10 2 4.4 44.0 6"-8" 2000
FSP2-3000 12 2 4.4 52.8 8"-10" 2400
1•• FSPZ-3500 14 2 4.4 61.6 10"-12" 2800
FSPZ-4000 16 2 4.4 70.4 10"-12" 3200
FSPZ-4200 18 2 4.4 79.2 10"-14" 3600 •
FSPZ-4500 20 2 4.4 88.0 10"-14" 4000
FSPZ-4800 22 2 4.4 96.8 10"-14" 4400
I FSPZ-5000 24 2 4.4 105.6 10"-14" 4800
'Maximum flow rate is based on aqueous flow at 1.0 PSI AI'clean.Inlet and outlet pipe sizes can be changed to meet customer requirements.

<<
1 iiNilL 161.000, . .woFSPN-3500 Available in standard in-line configuration
4 (shown)or side outlet.Custom styles available on
request.Features single-gasket seal,easy access
- • I II I Ii . cleaning and sturdy baskets.Uses 14 size 2 filter bags.
– Hydraulic lid lifter is recommended on 14 bag vessels
y " h and larger.
%/ FSPN-250 Features single-gasket seal and sturdy
[1 baskets.Uses two size 2 filter bags.
- I r / FSPN-85 Uses one size 2 bag. Our most popular vessel.
" h,
- ' • . - Ideal for batch or continuous applications in paint and
. ' rOP I resin plants.
Y'
M
bI ¢ FSPN-40 Up to 4"full port that permits non-restricted
I ' 1
r
I. U. _ fF�- flow.Side in,bottom out design shown;other outlet
1. I ..• — f configurations available.Designed for continuous flow or
small batch operations.Uses one size 1 filter bag.Shown
•
`'`d with optional legs.
P adjustable
.: FSPN-35 Miniature single bag filter vessel designed for
Icontinuous flow or small batch operations.
Uses one size 4 bag.
See back cover for ordering information.
BFN Vessels: Your Cost Effective Alternative _
INLET/OUTLET CONFIGURATIONS AVAILABLE
n
FSI,the acknowledged leader in liquid bag filtration equipment,is pleased to lam;
offer its new BFN Series bag filter vessels for quality filtration in `�«
economical applications. ■
BFN vessels are available in Carbon Steel and 304 SS;316 SS available on request. c it 4'1
. ■ +
Standard Features _.-• STYLE 6 STYLE 2
• Maximum working pressure BFN 11,12-150 PSI,BFN 13,14-150 and 300 PSI 1 r? SIDE IN/SIDE OUT SIDE IN/BOTTOM OUT
• Single gasket cover seal OFFSET
• Gasket materials available include BUNA N,Neoprene EPR,Viton,Viton Teflon ''., : It)
Encapsulated (others on request) - ion
• 304 SS perforated basket for up to 75 PSI differential . - BNP
• Two inlet/outlet configurations 1
• Same side inlet/outlet for easy manifolding LI
• Low pressuredrops
.__.
co
• Variety of connections available in either NPT or flange
BFN 11, 12-1",1 1/4",1 1/2",2",2 1/2",3",4" l 0 _,..1---•
BFN 13, 14-1", 1 1/4",1 1/2",2"
• Permanently piped housing - -�'
• Available with extra length legs,evacuation float
Options iiI
• Heavy duty baskets available
• Additional connections including Sanitary Fittings and
Socket Weld are available -1 • t
• BFNC 11,12 ASME code versions available I1
og
11;mi
BFN VESSELS -
Model No. No of Bags Bag Size No. Surface Area Standard Max GPM'
Per Bag,Ft.2 Inlet/Outlet
BFN 11 _ 1 1 2.0 2" 1001111
Bf N 12 1 2 4.4 r 220
BFN 13 1 3 0.5 1" 25 `
BFN 14 1 4 1.0 1" 45 0
'Maximum flow rate is based on aqueous flow at 1 0 PSI Ti'clean Through vessel only without bags installed.

II
i
I I

Ordering Information
To order,use the abbreviations from the charts shown on this page.
The charts are color coded for your convenience.
Single Bag Example
— 5 6
FSPN-85 304 150 2FLG 2 COATED
These codes describe the following vessel:FSPN-85 Model No.-304 SS construction-150 PSI pressure rating-2"flange connection-Inlet/Outlet Style 2,
Side in/Bottom out-Coated
Multi Bag Example
MIIIII 1.111111 4 IIIIIIMIIIII 6
FSPN-2500 CS 150 8 INLINE 1/16 CA
These codes describe the following vessel:FSPN-2500 Model No.-Carbon Steel construction-150 PSI pressure rating-8"flange connection-Inline Inlet/
Outlet-1/16"corrosion allowance
BFN Example
2 5 6
BFN P 12 304 150 2FLG 6
These codes describe the following vessel:BFN model series-Polyloc bag style-holds one size 2 bag-304 SS construction-150 PSI pressure rating-
2"flange connection- Inlet/Outlet Style 6,Side in/Side out,offset
SINGLE BAG MULTI BAG BFN
5 Inlet/Outlet Configuration 4 Connection Size 2 Bag Style
FSPN-20 1-Side In/Side Out-Inline FSPN-250 3"-4"FLG BFN P-Polyloc
FSPN-35 2-Side In/Bottom Out FSPN-252 3"-4"FLG S-Snap Ring
6-Side In/Side Out-Offset FSPN-355 3"-6"FLG
FSPN-40 1-Side In/Side Out-Inline —._...__ FSPN-800 4"-6"FLG
FSPN-85 2-Side In/Bottom Out FSPN-1000 4"-8"FLG 11=(1)it 2-Side In/Bottom Out
3-Side In/Bottom Out-90' FSPN-1100 4"-8"FLG 12=(1)12 6-Side In/Side Out-Offset
ESPN-1300 6"-8"FLG
Elbow — 13=(1)13
FSPN-2000 6"-8"FLG 14=(1)14
FSPN-2200 6"-8"FLG
FSPN-2500 8"-10"FLG
CS-Carbon Steel 150-150 PSI _ FSPN-3000 8"-10"FLG 5 Pressure Rating
304-304 Stainless Steel 300-300 PSI _ FSPN-35D0 10"-12"FLG CS-Carbon Steel 150-150 PSI
316-316 Stainless Steel XXX _-Customer Specified FSPN-4000 10"-12"FLG 304-304 Stainless Steel 300-300 PSI
__ FSPN-4200 10"-14"FLG 316-316 Stainless Steel
FSPN-4500 10"-14"FIG
FSPN-20&FSPN-35 fSPN-4800 10"-14"FLG 6 Connection Size and Type
1 NPT 11Iz NPT FSPN-5000 10"-14"FIG 1 NPT 1 FLG
1 1/4 NPT 2 NPT 11/4 NPT 11/4 FLG
FSPN-40&FSPN-85 1 V2 NPT 142 FLG
1 NPT 1 FIG CS-Carbon Steel 100-100 PSI 2 NPT 2 FLG
1 1/4 NPT 11/4 FLG 304-304 Stainless Steel 150-150 PSI 21/2 NPT 21/2 FLG
1 1/2 NPT 11/2 FLG 316-316 Stainless Steel 300-300 PSI 3 NPT 3 FIG
2 NPT 2 FIG XXX-Customer Specified 4 FIG
2 1/2NPT 21/2 FLG
3 NPT 3 FLG k1, s comedian Type 11 6 Options
4 FLG Inline CA-Corrosion Allowance FSt's"comprehensive manufacturing control'philosophy ensures that
Side Out Coated we will maintain our status as the industry leader in all phases of the
6 Options PSI-Partial Jacket filter business.For more information,technical consultation or details
CA-Corrosion Allowance FSJ-Full Jacket about our design capability,contact your FSI representative or our
Coated headquarters in Michigan City.Indiana.
PSI-Partial Jacket —
FSl-Fulllacket
rie Dii I ISO CERTIFIED
Filter Specialists,Inc.
TO LEARN MORE ABOUT FILTER SPECIALISTS PRODUCTS, CONTACT ONE OF THE OFFICES OR VISIT OUR WEBSITE AT: http://www.fsifilters.com
USA Europe Central America South America
FILTER SPECIALISTS,INC. FILTER SPECIALISTS INTERNATIONAL GMBH FSI de MEXICO FSI SUL AMERICANA INDUSTRIAS
SHIP:100 Anchor Road Balterweg 3.1 S. de R.L. de C.V. Rua Oneda
Michigan City,IN 46360 D-65817 Eppstein-Bremthal Centeno 119-A 671 Bairro Planalto
MAIL:P.O.Box 735 Germany Granjas Esmerelda Sao Bernardo Do Campo
Michigan City,IN 46361 Phone: [phone] Iztapalapa,Mexico D.F.C.P.09810 Sao Paulo, Brazil
Phone: [phone] Fax: [phone] Phone: [phone] Cep 09895-280
800-348-3205 Fax: [phone] Phone: [phone]
Fax: [phone] Fax: [phone]
There are no expressed or implied warranties,including the implied warranty of merchantability and fitness for a particular purpose not specific herein respecting this agreement or the product being sold hereunder or the service provided herein
BFV-015-1001
M....kiln•oku 0n.o

I

Model 88 Single Liquid Bag
Housing
flow rates to 220 g.p.m.
Krystil Klear's model 88 Single Series of Liquid Bag
Housings offer two depths, a 15" and a 30" housing
depending upon the needed surface area and volume of _ ,
fluid to be filtered.
FEATURES
► Carbon, 304, or 316 stainless steel material •
► 150 PSI pressure rating
► Low pressure drop
► Quick swing closure with eye nuts
► Viton seals - lid & basket
► Differential, drain, and vent ports
► Adjustable support legs
► 316 stainless steel strainer basket
► 2-part epoxy paint finish on carbon vessels •
Our 88 series effectively removes dirt, pipe scale, and other
contaminants from process liquids such as water,chemical and
E_,
petroleum products. Quality construction and design assure
protection for all down-stream equipment.
VESSEL CONSTRUCTION: Our model 88 single vessels are
designed for operating up to 150 PSI at 300°F.The housing design
provides a large sump area at the bottom of the basket for
particulate accumulation. This design utilizes the filter more
efficiently and prolongs the element life.
The 316 S.S. basket seals onto a viton o-ring to eliminate particulate bypass between the basket and seat. Optional
mesh-lined strainer baskets and o-rings are available. Please refer to their individual brochures in our liquid
catalog.
A vent in the housing lid and a drain port in the housing speed evacuation and filling. Gauge ports are located
on the body of the housing to install gauges for monitoring the differential pressure across the bag. Permanently
piped housings are opened with simple tools without disturbing the piping. Swing bolts with eye-nuts allow easy
opening and closing of the swing-lid.No need to remove any hardware.
As a standard finish, all vessels are blast cleaned and painted inside and out with a 2-part epoxy. Stainless steel
vessels are supplied with a satin finish.

Threaded Flanged Threaded Flanged Threaded Flanged
(NPT) (1501b,A.N,S.1.1 (NPT) (150 Th.A,N.S.1.) (NPT) Vcns (ISO lb.A.N.S.I.
A--, .„;'-ti' B1 [441A �� °` r.B-1 ]'A-1• B
IN
I
rt ROILJT
fF
K I K i
r .. .. Idra�ni . L
‘41/14
L-- K'u..r.ni - J t^'OUT H t.- OUT
OUT OUT
NH Style A"
w rah custnrner's elbow
All dimensions are approximate
to 1111111111111111111111111117111iiwuuwuui o nwMwo uwuu®®
'� 2 ; ' 6 7 24 7 5'1'7 0 24 7 26.2 3.4 25 7 P7 2 5 3 6.7 36? 37.4 7.0 36.2 37.7 3 4 37.2 2.3 125.
04 3 5 a 26 5 7.0 24.7 26.5 5.0 26 3 10003 5 4 7-I 36.2 38.0 7.0 36.2 39.2 5 0 38 7 3 1 I 145"
00 71 24.7 .ud
4 54 7,1 24 7 26,6 74) 24 7 29 163 26-9 4 5 4 7 I 36.2 38.1 7.0 36 2 40.6 6.3 38.9 3.8 Nt _
Adjustable support legs have 12"bolt circle and a 16"height adjustment.
Easy access vent Poet
swing boltsp
Housing Operation:
Unfiltered liquid enters the housing above the filter bag or strainer
---- /J1fif/f .o-r�og basket; flows down into the housing; and continues through the
f� Seal element. Solids arc trapped inside the filter bag or strainer and
easily removed when the housing is serviced- Our standard o-ring
Contaminated ,: "f'e t ter: seal between the basket and the housing ensures a positive seal to
Liquid prevent bypass.
-t s saaket aging
- - sevBasket data for Model 88 with flow rates to 220 ,,tri
a -s
�� I :v Pi. a I)�ptII \oniii1 t)tit ctu s,urtao: ' . \cJunx
Inlet g '{ , Liquid Inich�SI linche.) (sq II ,cu In I
3165.3. __.i • T „,..,
''a IS 6 7 2.3 500
sv,iner 30 6.7 4.4 1000
Baakel ; I ; u r
Howlett -4 :� ::: ; :
F ,. .•. ; CAMIeI
• • Building a Part Number:
188 15 2 N A C is
ii.„,„,m,\IMILA 4. 13a43.cI ')I/ Iin4 OM SI/.Ctins Conn Iype. Out lel Loctilioit Material PSI
2 Style A Carbon=C
1_sx
15 3 NE'I13 304SS=-4 150=15
+n 1 LANtGF=F
4 C 316SS=-6
SPECIFICATIONS
Housing lid has a 3-bolt swing closure with a vent port. Connections are( ) inch(NPT)(FLC) with a(side inlet and bottom
outictxsidc inlet and side outletXside inlet and 90° bottom outlet). Housing is supplied with two differential prcssurc ports to
measure the differential pressure across the filter bag. A two-part epoxy finish is applied on the carbon steel vessels to maximize
the life of the housing;stainless steel vessels are supplied with a satin finish. Basket material is constructed of 316 stainless steel
with 9164"perforations to act as a strainer or to accept a #1 or#2 size liquid bag. Basket seals onto a Viton o-ring in the basket
support. Adjustable tripod leg assembly is supplied with housing. Vessels are rated at a 150 pounds per square inch design.
Distributed by:
P
i 'sti1' P.Xleari ration v'�R""'�o
tA Pyramid Technologies
Div.Of Geyer's Mfg. & Design, Inc. r 467 Forrest Park Cir
9449 S. 550 W. Phone: [phone] Am. Franklin,TN 37064
Winamac, IN 46996 Fax: [phone] X14° 615-599-419(1
[e-mail] web site: KrystilKlear.com

Appendix IX — Carbon Vessel Specifications

CIRBONAIR
Temporary Water Treatment Services Carbon • Rental • Service
7500 Boone Ave N, Suite 101,Brooklyn Park,MN 55428 Ph: 800-526-4999 Fax: [phone] www.carbonair.com
Virgin Granular Coal Based Carbon (Liquid Phase)
Carbonair's virgin granular coal based carbon is manufactured from selected grades of
bituminous coal which give high adsorption surface area with a broad pore size distribution
(micropore, mesopore, and macropore). This carbon is recommended for a variety of organic
hydrocarbons in molecular size.
Typical Applications
Groundwater, wastewater, potable water, liquid process purification, decolorization, and
dechlorination.
Typical Contaminants
Petroleum hydrocarbons such as MTBE, BTEX (benzene, toluene, ethylbenzene, xylenes),
butylbenzene, isopropylbenzene, isopropylether,propylbenzene, styrene,trimethylbenzene,
tetraethyl lead(TEL), low molecular weight PAHs (polyaromatic hydrocarbons such as
naphthalene, methylnaphthalene) and high molecular wieght PAHs (fluoranthene, phenanthrene,
and pyrene).
Chlorinated and brominated hydrocarbons such as bromoform, bromodichloromethane,
carbontetrachloride, chlorodibromomethane, chloroform, dibromochloropropane, dichloroethene
(DCE), dichloroethane (DCA), ethylenedibromide, trichloroethane (TCA), trichloroethene
(TCE),tetrachloroethane, and tetrachloroethene (PCE), and polychlorinated biphenyls (PCBs).
Other organic compounds such as dyes,pesticides, herbicides, insecticides, explosives,phenols,
pentachlorophenols, and PCBs.
Inorganic compounds such as chlorine and chloramines.
Typical Physical Properties*
Iodine Number 900 (minimum)
Molasses Number 200 (minimum)
Apparent density (dense packing) 27-31 lbs/ft3
Abrasion Number(Ro-Tap) 75 (minimum)
Moisture Content(as packed) 2% (maximum)
Mesh Size 8x30, 12x40
* Please consult with Carbonair for your specific application.

Call: 1.877.759.8143
30rea.5
C4RBONAIR
Hume Equipment Rentals Equipment for Sale Services About Carbonair Careers Contact Us
Products for Sale: Liquid Phase Carbon Vessels
Carbonair's PC Series,MPC Series,and LPC Series liquid phase carbon vessels are designed for the removal of
dissolved contaminants from liquid streams.With flow ranges up to 550 gpm per unit and carbon capacities up to -
20,000,Carbonair can provide the liquid phase carbon vessel to meet your needs.Click here for specifications
for our fiberglass PC Series,stecl PC Series,MPC Series,and LPC Scrics of liquid phase carbon adsorption .
filters.For more information on Liquid Phase Carbon and Specialty Media available from Carbonair.
PC Series Liquid Phase Carbon Vessels
Carbonair's PC Series Liquid Phase Filter Vessels are designed and manufactured in accordance with engineering standards set forth by the
American Society of Mechanical Engineers(ASME).The materials used in construction are in accordance with standards established by AW WA,
FDA and EPA. The PC Series vessels are ideal for applications that require pressure ratings of greater than 75 PSI. Typical applications for this line
of filters include municipal drinking water treatment,industrial wastewater treatment and groundwater remediation.
Specs
Model PC1 PC3 PC5 PC7 PC13 PC20 PC28 PC50 PC78 MPC Series Liquid Phase
Diameter 1' 2' 2'-6" 3' 4' 5' 6' 8' 10' Carbon Vessels
-0" -0"
Height(feet) 4' 4' 6'-0" 6'-0" 8'-4" 8'-5" 12'-5" 13'-3" 17'-7" Carbonair's MPC Series Liquid Phase Carbon
4" 2" Vessels are high quality filters ideal for
Bed Area(Square 1.1 2.4 4.9 7 12.6 19.5 28 50 78.5 groundwater remediation,particularly in
Feet) applications where the vessels must be moved
Nominal Flow 10 20 50 75 100 150 250 300 550 periodically. All MPC Carbon Vessels are
Rate(gpm) equipped with lifting eyes and forklift tubes
Carbon Capacity 90 250 500 1000 1500 2500 5000 10,000 20,000 allowing for easy movement of these vessels on
(pounds) site or in a facility. They have a lower profile than
the PC Series vessels making them more compact
Connections 1" 1" 2" 2" 2" 3" 4" 6" 6" and easy to ship. MPC Series carbon vessels have
Design Pressure 150 150 90 90 90 75 75 75 75 pressure ratings ranging from 75 PSI to 90 PSI.
(psi)
Weight Empty 23 80 780 980 1230 1800 3150 8100 10,900
(pounds)
Weight Loaded 113 330 1280 1980 2730 4300 8150 18,100 30,900
(pounds) LPC Series Liquid Phase
Operating Weight 290 805 2670 3670 6150 9200 17,450 40,600 75,600 Carbon Vessels
(pounds)
225 650 1900 3230 4600 7400 14,400 30,520 55,750

Carbon Adsorber—Liquid Phase
PC 7
12" x 16" 6" x 8"
MANWAY —HAND HOLE
36=O.D.
$ ,; 1
Vr
Pressure Drop for PC7
42" o O o
1.6
1.4
g 1.2
0 1.0
cl 0.8
5 0.6
n — h 0.4
a. 0.2
--
4--
0
--
0 5 10 15 20 25 30 35 40 45 50
42" Flow Rate(gpm)
TOP VIEW
3" PIPE COUPLING
(CARBON SLURRY IN)
LIFT LUG (2)
opo
0
2" PIPE FLANGE
(INFLUENT)
45"
91 1/4"
2" PIPE FLANGE
,
(EFFLUENT)
oOo
o0
32" �
3" X 150# BLIND FLANGE
3" X 150# STODDING FLANGE
(CARBON SLURRY OUT)
ELEVATION / FRONT VIEW
Sales Drawing #121140
03/22/05
n CARBONAIR 2005

Appendix X - Specification of Other Components

CLOSE COUPLED CENTRIFUGAL
MPS
MO
,,,,,o
e •
TYPE EC
, _
11 ,, Age._ ,
(ALL IRON & CIBF)
Adel" TYPE elooB
(ALL BRONZE)
APPLICATIONS
INDUSTRY—Coolant pumps, hot and cold water 4('----- 41°
circulating pumps, chemical transfer pumps,
booster pumps. - 1 /
,�x
O.E.M.—Circulating, washers, booster, towers and i)) %`-c- sf ., •
evaporating condensers, coolants. S :
1
tl ." 4
FEATURES .�
• Compact close coupled design using standard A
NEMA 56C motors.
• Back pull-out design for easy serviceability. : ., /
• 303 Stainless Steel shaft standard.
• Mechanical Seal: Type 6A Buna. carbon vs
ceramic single seal standard. (75 PSI MAX.)
■ Type 21 Viton and Type 9 Teflon single seals
optional. Other seal faces and elastomers
available. (200 PSI MAX.) s
Type EC Features: ‘ 1
■ Sizes: 1" x VA" x 5" (EC100) and 11/2" x2" x 5" r
(EC150). tel., 'i t'i'
• Double Type 21 Viton, Neoprene or EPR seals I ��
optional. I,
• Seal Flush, seal quench optional.
Type EIOOB Features: DOUBLE SEAL OPTION
■ All cast bronze construction.
• Size: 1" x 11/4" x 5"
IN Seal flush optional.
■ Double Type 21 Viton, Neoprene or EPR
seals optional.
ALSO AVAILABLE AS:
with AIR MOTOR DRIVE 316 STAINLESS STEEL _.,
(see Bulletin #127) °._ Equivalent models.
TYPE SC
." (see Bulletin #109)

PERFORMANCE CURVES
.. ■.c o .. i .. ■■ --■-- •
—
ai••• III:1 ..c 1800 R.P.M. " : ■■ ••••• =•,::..m.•.."i 3600 R.P.M. m "
. 25 • i■■ (nominal speed).� 100 •• •••—••• (nominal speed) —
me
4.84.Imp.DI � � ' ■ EC100-150 4.94'rma.otp_ ■■ 1. __I_ _
20 NNW —. .. -ii. EC100 100 80-4so . . . ..
O■ �i ■ 'ff •1•i• . . . . -4.39' ■ -�■ . . : EC100&E100 8 T.
■ EC100-25 I _ • EC100-75 4.25mkt V■��m. i . . . L� "
F- ■■ �_. . .. r. ■■ EC100 50 60 __ir•bre .��_ ■■■■—
W t .- —••• EC100-33 3.e2 ■■�1*1■.79■-:vu�1'•
IL ,' 111111 ��-�•■�–• tr>nrimirizAcmibaniiiiive`lusrr�crr_•■a.. i ����■. ••. _.■ ++ :
Z ..— ■■■• _■ I11fG!■ I0 5 .' 11111lip
11111_ ilii 1111 20 1 If MOO M1M3 . 1 0
■—■ ■.■■■ ■ - ••• .4, . . `Q
W –■� ■■■■SOME ■ ■■■
Q
0 10 _ •
20 r •'. 0 10 20 30 40 50 80 70 80 90
• U.S. GALLONS PER MINUTE U.S. GALLONS PER MINUTE
*Note:E100-75B and EC100-75CIBF impeller diameter is 4.25!
Note Dotted lines show HP required on '''''""' " . - toned motors(Except EC100-25 E100-25B and EC) r .••.els) - •. ,-
. seem
' I I i --1800 R.R EC150.30090 4.94" ..-_Imp.Dia. �'• •!•3600 R.P.M."�
• '-• (nominal speed) 75 emeeem r_'•.— rr� •• (nominal speed) c
25 i I —•■■••■r_ar�
I I EC150-200 4.50"-I�i.-■■—rr■a711"1"■1 ■Ermine =
4.84"Imp.Dia. , _i: ii . , k3, • --11 ■■-
20 11�illl■s..1,l i� II! 60_ 1lR1111
�- EC150-33 r ! EC150-150 3.75" . ._- 'Mail • �=i-u—
���� 11—
w 15_. . • .Ml��..■ q 1"a FIr 45 miles' =i•IN, puffin.
mamma
z10 �■�� ii. 1� lu
3 i1.. . . I1i1IS�quails!LL
s 1 _ 1:111 - iMill1®mI lig
aro
w1 1irr , (•. , •i f, 11 1U•1=■–■u■–�--■-- W
_ 1=■r■ V ■u■ _
■ o■ 1 t 1
0 10 20 --r 40 50 6,7-47 80 r'. . :: 20 40 60 . 80 100 120 140 160 184
U.S. GALLONS PER MINUTE U.S. GALLONS PER MINUTE
DIMENSIONS—in inches: Approx.ODP
AG Dimensions based on'/60-115/230 V motors. Model No. AG Ship Wght. Desch. Suct. C D L X Y Z
AG C7..it. EC100&E10013Y Sizes: 25 7% 34#
IT
�Jt33 8%2 35#
50 8/ 36# 1 1'/. 513/16 3Y 4'/s 3%z 1% 23/
t • X 75 9'/a 39#
ilW ��1 100 93/, 43#
i�( U, a `� 150 10%2 49#
I 316 D EC150-33 81/2 45#
1
EC150-150 101/2 57# 11/2 2 6% 3% 5 3% 13/4 3%
Lam- F._ 8"
EC150-200 11% 62#
48� EC150-300 12% 65#
PARTS LIST
K Double Seal
rt ,
AlECIOCIBF Al 0 EC150CIBF ElODB ®` "VI�
(Specify Trim) -- SW
) v •
A.Impeller K E F H
Sizes' 25 0216 0217 0217 A
33 0218 0219 0231 0258 0219
50 0220 0221 0221
75 0222 0223 0223
100 0224 0225 0225 6 • 11
150 0216 0217 0231 0258 0217
200 0231 0258 ta , r.41
300 0231 0258 -tc \\
B.Volute 0214 0180 0215 wy �� -
C.Volute Bolls 0573(4 rqd.) 0573(8 rqd I 0376(4 rqd I
0 Pipe Plugs(2 rqd 1 0557 0557 0558 ,
E.Bracket 0212 1180 0213 - 1 / r
F.Motor Bolts(4 rqd.) 0588 0588 0592 C\
G.Gasket,Synthetic Fiber 0506 J
H.Shaft with Set Screws 0226-1
K.Meager 0522 C
K.Mechanical Seal
Buna 1.6A(Standard) 0538 B G
Viton T.6A 0539
Teflon T.9 1150 9
Neoprene w/NiResisl Seat TBA 0675 s\,(13 ,,,D-1-�4
E.PR.T6A 0383 5�t VO AOrp
DOUBLE SEAL
Viton 1:2112 rqd.) 0985 ��r Q O•\ag5aAQ1
NeopE.PR�121(2 rene g2 d.Irgd 1 0984 1023 . 19612 AOtC\gn-' ,0l6a
D.S Seal Cover Gasket 0974 e- Ga`;off\ 38
Seal Cover Bolls(3 rqd.) 0256 So.0O`�e� .(10

VI\VIVVI LI II' JI I% .J .. IIVItlJ
CR, CRN
GB Installation and operating instructions
( Montage-and Betriebsanleitung
ED Notice d'installation et d'entretien
�I Istruzioni di installazione e funzionamento
�E Instrucciones de instalacion y funcionamiento
© Instrucoes de instalacao e funcionamento
GR Oarlyfec cykaraorac Kal Aciroupyiac
NL Installatie-en bedieningsinstructies
CD Monterings-och driftsinstruktion
SF Asennus-ja kayttOohjeet
DK Monterings-og driftsinstruktion
_ .
_ _
It
s -
Lx
cn .
�"'.
imam
CR
O
—,,
..� . _..._.... ._._......_� . rW2 ■A if"141IG' •

Declaration of Conformity Konformitatserklarung
We GRUNDFOS declare under our sole responsibility that the products CR and 'Mr GRUNDFOS erklaren in alleiniger Verantwortung,dab die Produkte CR and
CRN,to which this declaration relates,are in conformity with the Council Direc- CRN,auf die sich diese Erklarung bezieht,mit den folgenden Richtlinien des
tives on the approximation of the laws of the EC Member States relating to Rates zur Angleichung der Rechtsvorschriften der EG-Mitgliedstaaten Uberein-
- Machinery(98/37/EC). stimmen:
Standard used:EN 292. - Maschinen(98/37/EG). I
- Electromagnetic compatibility(89/336/EEC). Norm,die verwendet wurde:EN 292.
Standards used:EN 61 000-6-2 and EN 61 000-6-3. - Elektromagnetische Vertraglichkeit(89/336/EWG).
- Electrical equipment designed for use within certain voltage limits Normen,die verwendet wurden:EN 61 000-6-2 and EN 61 000-6-3.
(73/23/EEC)[95]. - Elektrische Betriebsmittel zur Verwendung innerhalb bestimmter
Standards used:EN 60 335-1 and EN 60 335-2-51. Spannungsgrenzen(73/23/EWG)[95].
Normen,die verwendet wurden:EN 60 335-1 and EN 60 335-2-51.
Declaration de Conform ite Dichiarazione di Conformity
Nous GRUNDFOS declarons sous notre seule responsabilite que les produits Noi GRUNDFOS dichiariamo sotto la nostra esclusiva responsabilita the i pro-
CR et CRN auxquels se Were tette declaration sont conformes aux Directives dotti CR e CRN,ai quali questa dichiarazione si riferisce,sono conformi alle 1
du Conseil concernant le rapprochement des legislations des Etats membres CE Direttive del consiglio concernenti it rawicinamento delle legislazioni degli Stati
relatives a membri CE relative a
- Machines(98/37/CE). - Macchine(98/37/CE).
Standard utilise:EN 292. Standard usato:EN 292.
- Compatibilite electromagnetique(89/336/CEE). - Compatibilita elettromagnetica(89/336/CEE).
Standards utilises:EN 61 000-6-2 et EN 61 000-6-3. Standard usati:EN 61 000-6-2 e EN 61 000-6-3.
- Materiel electrique destine a employer dans certaines limites de - Materiale elettrico destinato ad essere utilizzato entro certi limiti di
tension(73/23/CEE)[95]. tensione(73/23/CEE)[95].
Standards utilises:EN 60 335-1 et EN 60 335-2-51. Standard usati:EN 60 335-1 e EN 60 335-2-51.
Declaration de Conform idad Declaragao de Conformidade
Nosotros GRUNDFOS declaramos bajo nuestra Unica responsabilidad que los Nos GRUNDFOS declaramos sob nossa Unica responsabilidade que os produtos
productos CR y CRN a los cuales se refiere este declaration son conformes con CR e CRN aos quais se refere esta declaragao estao em conformidade com as
las Directives del Consejo relatives a la aproximacion de las legislaciones de los Directives do Conselho das Comunidades Europeias relatives a aproximacao das
Estados Miembros de la CE sobre legislagoes dos Estados Membros respeitantes a
- Maquinas(98/37/CE). - Maquinas(98/37/CE).
Norma aplicada:EN 292. Norma utilizada:EN 292.
- Compatibilidad electromagnetica(89/336/CEE). - Compatibilidade electromagnetica(89/336/CEE).
Normas aplicadas:EN 61 000-6-2 y EN 61 000-6-3. Normas utilizadas:EN 61 000-6-2 e EN 61 000-6-3.
- Material electrico destinado a utilizarse con determinados limites de tension - Material electrico destinado a ser utilizado dentro de certos limites de ten-
(73/23/CEE)[95]. sao(73/23/CEE)[95].
Normas aplicadas:EN 60 335-1 y EN 60 335-2-51. Normas utilizadas:EN 60 335-1 e EN 60 335-2-51.
Ar1Awan FuppdpcpwanS Overeenkomstigheidsverklaring
Eµe(c r)GRUNDFOS SrlXWvouµeµe anoKXeiarixa own mac eu0Uvrl On ra Wij GRUNDFOS verklaren geheel onder eigen verantwoordelijkheid dat de pro-
npotovra CR Kai CRN auppopcpWvovraiµc-my Obrlv(a Tou Eu1113ouMou en( dukten CR en CRN waarop deze verklaring betrekking heeft in overeenstemming
Tic aiiycAiorlc Twv voµwv Twv Kpa'Wv McXWv Trig EupwnatKrjc EvWOTlc ae zijn met de Richtlijnen van de Raad inzake de onderlinge aanpassing van de wet-
oXearlµe ra gevingen van de Lid-Staten betreffende
- MrlXavrjµara(98/37/EC). - Machines(98/37/EG).
flpoTuno nou Xprlaiµononj8nKe:EN 292. Norm:EN 292.
- HXeicrpoµayvrlrLKrj auµ(3arerarra(89/336/EEC). - Elektromagnetische compatibiliteit(89/336/EEG).
flporuna nou XprlarµonoinenKav:EN 61 000-6-2 Kar EN 61 000-6-3. Normen:EN 61 000-6-2 en EN 61 000-6-3.
- HXeKTptKec auaKeuec oXeoiaaµevec via Xprjarl evroc opioµevcov op(wv - Elektrisch materiaal bestemd voor gebruik binnen bepaalde spanningsgren-
rlXei rpiKrjc raorlc(73/23/EEC)[95]. zen(73/23/EEG)[95].
rlporuna nou Xpgaiµonoirj0rlKav:EN 60 335-1 Kai EN 60 335-2-51. Normen:EN 60 335-1 en EN 60 335-2-51.
Ftirsakran om overensstammelse Vastaavuusvakuutus
Vi GRUNDFOS forsakrar under ansvar,att produkterna CR och CRN,som Me GRUNDFOS vakuutamme yksin vastuullisesti,etta tuotteet CR ja CRN,jota
omfattas av denna forsakran,ar i overensstammelse med Radets Direktiv om tame vakuutus koskee,noudattavat direktiiveja jotka kasittelevat EY:n jasenvalti-
inbordes narmande till EU-medlemsstaternas lagstiftning,ayseende oiden koneellisia laitteita koskevien lakien yhdenmukaisuutta seur.:
- Maskinell utrustning(98/37/EC). - Koneet(98/37/EY).
Anvand standard:EN 292. Kaytetty standardi:EN 292.
- Elektromagnetisk kompatibilitet(89/336/EC). - Elektromagneettinen vastaavuus(89/336/EY).
Anvanda standarder:EN 61 000-6-2 och EN 61 000-6-3. Kaytetyt standardit:EN 61 000-6-2 ja EN 61 000-6-3.
- Elektrisk material aysedd for anvandning inom vissa spanningsgranser - Maarattyjen janniterajoitusten puitteissa kaytettavat sahkOiset laitteet
(73/23/EC)[95]. (73/23/EY)[95].
Anvanda standarder:EN 60 335-1 och EN 60 335-2-51. Kaytetyt standardit:EN 60 335-1 ja EN 60 335-2-51.
Overensstem m elseserklmring
Vi GRUNDFOS erklfrer under ansvar,at produkterne CR og CRN,som denne Bjerringbro,1st September 2003
I erklaering omhandler,er i overensstemmelse med Radets direktiver om indbyr-
des tilnaermelse til EF medlemsstaternes lovgivning om
- Anvendt
(98/37/EF).dard: C9 i
Anvendt standard:EN 292. 7 �„�(
- Elektromagnetisk kompatibilitet(89/336/E0F).
Anvendte standarder:EN 61 000-6-2 og EN 61 000-6-3.
I - Elektrisk materiel bestemt til anvendelse inden for visse spaendingsgraenser Jan Strandgaard
(73/23/E0F)[95]. Technical Manager
Anvendte standarder:EN 60 335-1 og EN 60 335-2-51.

CR, CRN
Installation and Page 4 <<B
operating instructions
Montage- and Seite 9 • 71
Betriebsanleitung
Notice d'installation Page 15 ■ F
et d'entretien
Istruzioni di installazione Pag. 21 1.1
e funzionamento
Instrucciones de instalacion Pag. 26 • E I
y funcionamiento
Instrugoes de instalagao Pag. 31 rP
e funcionamento
OanyIcS cykarao-raargS XeXIba 37 .3R1
KQI AcIToupyIac
Installatie- en Pag. 43 ■ NL
bed ien ingsinstructies
Monterings- och Sida 48 • S I
driftsinstruktion
Asennus-ja Sivu 53 • SF
kayttoohjeet
Monterings- og Side 58 • ')K I
driftsinstruktion

CONTENTS 3. Applications
Page GRUNDFOS multistage in-line centrifugal pumps,types CR and
1. Handling 4 CRN, are designed for a wide range of applications.
2. Type designation 4 Pumped liquids
2.1 Pump key for CR, CRN 2,4, 8 and 16 4 Thin, non-explosive liquids, not containing solid particles or fi-
3. Applications 4 bres.The liquid must not attack the pump materials chemically.
4. Technical data 4 When pumping liquids with a density and/or viscosity higher than
4.1 Ambient temperature 4 that of water,motors with correspondingly higher outputs must be
4.2 Liquid temperature 4 used, if required. 1
4.3 Maximum permissible operating pressure and liquid
temperature for the shaft seal 4 CR,CRN
4.4 Minimum inlet pressure 5 For liquid transfer, circulation and pressure boosting of cold or
4.5 Maximum inlet pressure 5 hot clean water.
4.6 Electrical data 5 CRN
4.7 Frequency of starts and stops 5
4.8 Dimensions and weights 5 In systems where all parts in contact with the liquid must be made
4.9 Sound level 5 of stainless steel,CRN pumps must be used.
5. Installation 5
6. Coupling adjustment 6 4. Technical data
7. Electrical connection 6 4.1 Ambient temperature
7.1 Frequency converter operation 6
Maximum +40°C.
8. Start-up 7 If the ambient temperature exceeds+40°C,the motor output(P2)
9. Maintenance 7 must be reduced,see fig. 1.
10. Frost protection 7 Fig. 1
11. Service 8
P2
12. Fault finding chart 8 [°i°] • -
13. Disposal 8 100
90
Before beginning installation procedures,these in- 80
Astallation and operating instructions should be stud- 70
ied carefully.The installation and operation should 60 co
also be in accordance with local regulations and ac- 50 1 1 1 1 I m
cepted codes of good practice. 20 25 30 35 40 45 50 55 60 65 70 75 80 co
cv
t[°C] o
1 .Handling 1000 22502 500 m 1
AThe motors of the CR,CRN 2,4,8 and 16 pumps are 4.2 Liquid temperature
supplied with lifting eyes which must not be used for
lifting the entire pump. Pump type Liquid temperature
When the entire pump is to be lifted, observe the following: CR, CRN 2,4, 8 and 16 -20°C to+120°C
• CR, CRN 2,4, 8 and 16 pumps fitted with GRUNDFOS MG See also fig.A,page 63,which indicates the relationship between
motors should be lifted in the pump head by means of straps liquid temperature and maximum permissible operating pressure.
or the like.
• For other motor makes, it is recommended to lift the pump in Note:The maximum permissible operating pressure and liquid
the pump head by means of straps. temperature ranges apply to the pump only.
4.3 Maximum permissible operating pressure and
2. Type designation liquid temperature for the shaft seal
I
2.1 Pump key for CR, CRN 2, 4, 8 and 16 Fig. 2
Example CR 8-30/2-X- X- X-XXXX
iP ba RN 2,4,8 and 16:
l
Pump range: 30
CR, CRN
25 •
Nominal flow rate in m3/h
Number of stages x 10 20 AUUE/AUUV AUUE•
1 1
Number of impellers(is only used if the
y pum p 15
AUUE/AUUV
has fewer impellers than chambers) 10 W> I I I
RUBE/BURN
D D BUBE $
Code for pump version 5 cc cc a
Code for pipework connection 0 m
Code for materials -40 -20 0 20 40 60 80 100 120 140 160 E.
Code for shaft seal and rubber pump parts t[°C]

4.4 Minimum inlet pressure 4.8 Dimensions and weights
Fig.3 Dimensions: See fig.C, page 65.
Weights: See label on the packing.
4.9 Sound level
r See fig. D, page 66. 40
Hf 5. Installation
t r - The pump can be installed vertically or horizontally,see fig.4.
-� p Ensure that an adequate supply of cool air reaches the motor
H NPSH cooling fan. However,the motor must never fall below the hori-
Pb m zontal plane.
a
N Fig.4
1
V
[ Hv
iIP
Ilii
The maximum suction lift"H"in metres head can be calculated as ,
follows: Si'''.
H=pbx10.2-NPSH-Hf-H„-HS a
Pb = Barometric pressure in bar. -' _- p L El a -
(Barometric pressure can be set to 1 bar). - - m
In closed systems, Pb indicates the system pressure ~
in bar. Arrows on the pump base show the direction of flow of liquid
NPSH = Net Positive Suction Head in metres head through the pump.
(to be read from the NPSH curve on page 69 at the Figure C, page 65,shows the dimensions of the base as well as
highest flow the pump will be delivering). the diameter and the position of the foundation bolt holes.
Hf = Friction loss in suction pipe in metres head at the To minimize possible noise from the pump, it is advisable to fit ex-
highest flow the pump will be delivering. pansion joints either side of the pump and anti-vibration mount-
Hv = Vapour pressure in metres head,see fig. E on page ings between foundation and pump.
66.tm= Liquid temperature. Port-to-port lengths and pipework connections appear from fig.C,
Hs = Safety margin=minimum 0.5 metres head. page 65.
If the calculated"H"is positive,the pump can operate at a suction Isolating valves should be fitted either side of the pump to avoid
lift of maximum "H"metres head. draining the system if the pump needs to be cleaned, repaired or
If the calculated"H"is negative, an inlet pressure of minimum replaced.
"H"metres head is required.There must be a pressure equal to Install the pipes so that air locks are avoided,especially on the
the calculated"H"during operation. suction side of the pump. Correct pipework shown in fig. 5.
Example: Fig. 5
pb= 1 bar.
Pump type: CR 16, 50 Hz.
Flow rate: 16 m3/h.
NPSH (from page 69): 1.5 metres head.
Hf=3.0metreshead.
temperature:Liquidtemperaerature: +60°C.
H„(from fig. E, page 66): 2.1 metres head.
H=pb x 10.2-NPSH-Hf-Hv-Hs[metres head].
H= 1 x 10.2-1.5-3.0-2.1 -0.5=3.1 metres head. E i-
1 This means that the pump can operate at a suction lift of maxi-
mum 3.1 metres head. I 1 2 3
Pressure calculated in bar: 3.1 x 0.0981 =0.30 bar. o
Pressure calculated in kPa: 3.1 x 9.81 =30.4 kPa. .
4.5 Maximum inlet pressure ,U.I�1I I1©1IIIIII�1*N
Figure B, page 64, shows the maximum permissible inlet pres-
sure. However,the actual inlet pressure+pressure when the Pos.
pump is running against a closed valve must always be lower no. Description Function
than the"maximum permissible operating pressure".
If the system and the pumps are to be pressure-tested at a pres- 1 Expansion Reduces noise and absorbs vibra-
sure higher than that stated in fig. B, page 64,the pump shaft joint tions and expansion.
must be locked to prevent axial movement. 2 Isolating valve Enables easy service of the
pump.
4.6 Electrical data Pipe hanger Supports pipe and absorbs distor-
See motor nameplate. 3
tion and strain.
4.7 Frequency of starts and stops Note:The pump must always be protected against backflow by
means of a non-return valve(foot valve).
Motors up to 4 kW: Maximum 100 times per hour.
Other motors: Maximum 20 times per hour.

In the case of installations in which the discharge pipe slopes 7. Electrical connection
downwards away from the pump and there is a risk of siphon ef- The electrical connection should be carried out by an authorized
fect and in installations which must be protected against backflow electrician in accordance with local regulations.
of unclean liquids, a vacuum valve must be fitted close to the
pump, see fig.6. Before removing the terminal box cover and before
® any removal/dismantling of the pump,make sure that
Fig.6 the electricity supply has been switched off.
The pump must be connected to an external mains
switch with a minimum contact gap of 3 mm in all
I poles.
�_ The operating voltage and frequency are marked on the motor
nameplate. Make sure that the motor is suitable for the electricity
supply on which it will be used.
Single-phase GRUNDFOS motors incorporate a thermal switch
and require no additional motor protection.
MI*1111:11.I4I f Three-phase motors must be connected to a motor starter.
The terminal box can be turned to four positions, in 90°steps:
Minimum flows: 1. If necessary, remove the coupling guards. Do not remove the
Liquid temperature coupling.
2. Remove the bolts securing the motor to the pump.
+120°C 3. Turn the motor to the required position.
Pump type 0°C +150°C
Up to+80°C +$0 C (only spe- 4. Replace and tighten the bolts.
cial version) 5. Replace the coupling guards.
The electrical connection should be carried out as shown in the
CR,CRN 2 0.2 m°/h 0.5 m3/h - diagram inside the terminal box cover.
CR,CRN 4 0.4 m°/h 1.0 m°/h -
CR,CRN 8 0.8 m'/h 2.0 m'/h 7.1 Frequency converter operation
CR,CRN 16 1.6 m°/h 4.0 m3/h - Motors supplied by GRUNDFOS:
Note:The pump must never operate against a closed discharge All three-phase motors supplied by GRUNDFOS can be con-
valve. netted to a frequency converter.
Dependent on the frequency converter type,this may cause in-
6. Coupling adjustment creased acoustic noise from the motor. Furthermore, it may
cause the motor to be exposed to detrimental voltage peaks.
For adjustment of coupling in CR, CRN 2 and 4, see fig. F, Note: GRUNDFOS motors types MG 71 and MG 80 as well as
page 67. MG 90(1.5 kW,2-pole),all for supply voltages up to and including
For adjustment of coupling in CR, CRN 8 and 16,see fig.G, 440 V(see motor nameplate), must be protected against voltage
page 68. peaks higher than 650 V(peak value)between the supply termi-
nals.
It is recommended to protect all other motors against voltage
peaks higher than 850 V.
The above disturbances, i.e. both increased acoustic noise and
detrimental voltage peaks,can be eliminated by fitting an LC filter
between the frequency converter and the motor.
For further information,please contact the frequency converter or
motor supplier.
Other motor makes than those supplied by GRUNDFOS:
Please contact GRUNDFOS or the motor manufacturer.

8. Start-up CR 2 and 4,
Note: Do not start the pump until it has been filled with liquid and CRN 2,4,8 and 16:
vented. For these pumps, it is advisable to open the bypass valve during
Pay attention to the direction of the vent hole and start-up.The bypass valve connects the suction and discharge
take care to ensure that the escaping water does not sides of the pump,thus making the filling procedure easier.When
A cause injury to persons or damage to the motor or
other components. the operation is stable,the bypass valve can be closed.WhenCD
pumping liquids containing air, it is advisable to leave the bypass
In hot-water installations, special attention should be valve open.
paid to the risk of injury caused by scalding hot water. Fig.7
Step Action
1
:.......16ILL____ Close the isolating valve on Drain plug
'4' the discharge side of the Bypass valve
o pump and open the isolating
valve on the suction side. � �_
:n -
I- M
2III ; w
Remove the priming plug from :42=1 =:_
r r. the pump head and slowly fill 1 i��
a the pump with liquid. N.
- ° Replace the priming plug and c,
= tighten securely.
lin* E
I-
3
9. Maintenance
", See the correct direction of ro-
tation of the pump on the mo-
4
o Before starting work on the pump, make sure that all
---
IA ,
tor fan cover. power supplies to the pump have been switched off
./ and that they cannot be accidentally switched on.
f//� Ei—
}ffl Pump bearings and shaft seal are maintenance-free.
If the pump is to be drained for a long period of inactivity,remove
4 one of the coupling guards to inject a few drops of silicone oil on
1 the shaft between the pump head and the coupling.This will pre-
it-- , vent the shaft seal faces from sticking.
—' a Start the pump and check the Motor bearings:
i i- - v direction of rotation.
0 Motors which are not fitted with grease nipples are maintenance-
-
free.
I s
I I f Motors fitted with grease nipples should be lubricated with a high-
s temperature lithium-based grease,see the instructions on the fan
cover.
Vent the pump by means of In the case of seasonal operation (motor is idle for more than
w the vent valve in the pump 6 months of the year), it is recommended to grease the motor
N head.At the same time,open when the pump is taken out of operation.
_imi
the discharge isolating valve a
little. 10. Frost protection
i-
Pumps which are not being used during periods of frost should be
6 drained to avoid damage.
Continue to vent the pump.At Drain the pump by loosening the vent screw in the pump head
h.
;,;:z i the same time, open the dis-
.....4.670
and by removing the drain plug from the base.
co charge isolating valve a little Care must be taken to ensure that the escaping water
-Tr
more. does not cause injury to persons or damage to the
A motor or other components.
1- In hot-water installations, special attention should be
7 paid to the risk of injury caused by scalding hot water.
Do not tighten the vent screw and replace the drain plug until the
Close the vent valve when a pump is to be used again.
ivr, a steady stream of liquid runs CR 2 and 4,
0 out of it.Completely open the
discharge isolating valve. CRN 2,4,8 and 16:
1.1..141.64111061111 E Before replacing the drain plug in the base,screw the bypass
valve out against the stop,see fig.7.
Fit the drain plug by tightening the large union nut followed by the
bypass valve.

1
1
11
I

11. Service
Note: If a pump has been used for a liquid which is injurious to
health or toxic,the pump will be classified as contaminated.
If GRUNDFOS is requested to service the pump, GRUNDFOS
® must be contacted with details about the pumped liquid,etc.be-
fore the pump is returned for service.Otherwise GRUNDFOS can
refuse to accept the pump for service.
Possible costs of returning the pump are paid by the customer.
However,any application for service(no matter to whom it may
be made)must include details about the pumped liquid if the
pump has been used for liquids which are injurious to health or
toxic.
12. Fault finding chart
ABefore removing the terminal box cover and before any removal/dismantling of the pump,make sure that the electricity supply
has been switched off and that it cannot be accidentally switched on.
Fault Cause Remedy
1. Motor does not run a) Supply failure. Connect the electricity supply.
when started. b) Fuses are blown. Replace fuses.
c) Motor starter overload has tripped out. Reactivate the motor protection.
d) Main contacts in motor starter are not making Replace contacts or magnetic coil.
contact or the coil is faulty.
e) Control circuit is defective. Repair the control circuit.
f) Motor is defective. Replace the motor.
2. Motor starter overload a) One fuse/automatic circuit breaker is blown. Cut in the fuse.
trips out immediately b) Contacts in motor starter overload are faulty. Replace motor starter contacts.
when supply is
switched on. c) Cable connection is loose or faulty. Fasten or replace the cable connection.
d) Motor winding is defective. Replace the motor.
e) Pump mechanically blocked. Remove the mechanical blocking of the pump.
f) Overload setting is too low. Set the motor starter correctly.
3. Motor starter overload a) Overload setting is too low. Set the motor starter correctly.
trips out occasionally.
b) Low voltage at peak times. Check the electricity supply.
4. Motor starter has not a) Check 1 a), b),d)and e).
tripped out but the
pump does not run.
5. Pump capacity not a) Pump inlet pressure is too low(cavitation). Check the suction conditions.
constant. b) Suction pipe/pump partly blocked by impurities. Clean the pump or suction pipe.
c) Pump draws in air. Check the suction conditions.
6. Pump runs but gives a) Suction pipe/pump blocked by impurities. Clean the pump or suction pipe.
no water. b) Foot or non-return valve blocked in closed po- Repair the foot or non-return valve.
sition.
c) Leakage in suction pipe. Repair the suction pipe.
d) Air in suction pipe or pump. Check the suction conditions.
e) Motor rotates in the wrong direction. Change the direction of rotation of the motor.
7. Pump runs back- a) Leakage in suction pipe. Repair the suction pipe.
wards when switched b) Foot or non-return valve is defective. Repair the foot or non-return valve.
off.
8. Leakage in shaft seal. a) Shaft seal is defective. Replace the shaft seal.
9. Noise. a) Cavitation occurs in the pump. Check the suction conditions.
b) Pump does not rotate freely(frictional resist- Adjust the pump shaft.
ance)because of incorrect pump shaft posi-
tion.
c) Frequency converter operation. See section 7.1 Frequency converter operation.
13. Disposal
Disposal of this product or parts of it must be carried out accord-
ing to the following guidelines:
1. Use the local public or private waste collection service.
2. In case such waste collection service does not exist or cannot
handle the materials used in the product, please deliver the
product or any hazardous materials from it to your nearest
GRUNDFOS company or service workshop. Subject to alterations.

1

Fig.A 1
1
Gg Maximum permissible operating pressure:
O Max.zulassiger Betriebsdruck:
O Pression de fonctionnement maxi autorisee:
O Massima pressione di esercizio possibile:
0 Presion maxima de funcionamiento permitida:
© permissivel:
maxima de funcionamento
GR Meyuorq emrpenrq nIco, Aeiroupyiaq:
Nl. Maximaal toelaatbare werkdruk:
O Max.tillatet driftstryck:
SF Suurin sallittu kayttopaine:
DK Maks.tilladeligt driftstryk:
Frequency Pump type Curve
Frequenz Pumpentyp Kurve p[barj
Frequence Type de pompe Courbe 36
Frequenza Pompa tipo Curva
Frecuencia Tipp de bomba Curva 32
Frequencia Modelo da bomba Curva 28
fuxv6Tgra Tunoc avTAiac Kapn iAq
Frequentie Pomptype Curve 24 �� 3
Frekvens Pumptyp Kurva 20 2
Taajuus Pumpputyyppi Kayra
Frekvens Pumpetype Kurve 16 • 1
CR, CRN 2-20 4 CR, CRN 2-150 1 12
CR, CRN 2-180 4 CR, CRN 2-260 2 8
CR, CRN 4-20/1 4 CR, CRN 4-160 1
CR,CRN 4-190 4 CR, CRN 4-220 2 4 0
50 Hz
CR, CRN 8-20/1 4 CR, CRN 8-120 1 0 I
CR, CRN 8-140 4 CR, CRN 8-200 3 -40 -20 0 20 40 60 80 100 120 140 160 0
CR, CRN 16-30/2 4 CR, CRN 16-80 1 t[C] 0
CR, CRN 16-100 4 CR,CRN 16-160 3
CR, CRN 2-20 4 CR, CRN 2-150 1
CR, CRN 2-180 4 CR, CRN 2-260 2
CR, CRN 4-20/1 4 CR, CRN 4-160 1
CR,CRN 4-190 4 CR, CRN 4-220 2
60 Hz
CR,CRN 8-20/1 4 CR,CRN 8-120 1
CR,CRN 8-140 4 CR, CRN 8-200 3
CR,CRN 16-30/2 4 CR, CRN 16-80 1
CR, CRN 16-100 4 CR,CRN 16-160 3

1

Fig. B
Gg Maximum inlet pressure for CR and CRN:
O Max.Zulaufdruck fur CR and CRN:
Pression maximum d'entree pour CR et CRN:
ED Massima pressione in aspirazione per CR e CRN:
• Presi6n maxima de entrada para CR y CRN:
Pressao maxima de admissao CR e CRN:
GR Ma yiarr)nieaq eiaoSou yia CR Kai CRN:
NL Maximale inlaatdruk m.b.t.type CR en CRN:
O Max.tilloppstryck for CR och CRN:
SF Suurin tulopaine CR ja CRN:
DK Maks.tillebstryk for CR og CRN:
50 Hz 60 Hz
CR,CRN 2
CR, CRN 2-20 6 bar CR, CRN 2-20—> CR, CRN 2-60 10 bar
CR, CRN 2-30 —> CR, CRN 2-110 10 bar CR, CRN 2-70 4 2-180 15 bar
CR, CRN 2-130 —> CR, CRN 2-260 15 bar
CR, CRN 4
CR, CRN 4-20/1 4 CR, CRN 4-20 6 bar CR, CRN 4-20/1 4 CR, CRN 4-20 6 bar
CR,CRN 4-30 4 CR, CRN 4-100 10 bar CR, CRN 4-30 4 CR, CRN 4-80/7 10 bar
CR, CRN 4-120 4 CR,CRN 4-220 15 bar CR, CRN 4-80 4 CR, CRN 4-160 15 bar
CR, CRN 8
CR, CRN 8-20/1 4 CR, CRN 8-60 6 bar CR, CRN 8-20/1 9IR, CRN 8-40 , 6 bar
CR, CRN 8-80 4 CR, CRN 8-200 10 bar CR, CRN 8-50 4 CR, CRN 8-140 10 bar
CR, CRN 16
CR, CRN 16-30/2 4 CR, CRN 16-30 6 bar CR, CRN 16-30/2 4 CR, CRN 16-30 6 bar
CR, CRN 16-40 4 CR, CRN 16-160 10 bar CR, CRN 16-40 4 CR, CRN 16-100 10 bar

C) C) C) f) C) C) C) C)
Z - Z co Z A Z N - -
C) Co A N N 3
T
H
N 3r..
0 0 0 3 r 1.1
�J — v
0o ., a, 3 = z
o 0 0 3
° v
TMOO 2251 3393
H
N N) j j 3
111i_
v
o 0 0 0 3 = I D m
r--I
O O N N 3 0
0) W A -4D. t'�
TMOO 2252 3393
H
N N N N 3 r
E
N o 0 0 3 = D
3
s' v
cm al w w 3 ° 0 ,--
N N) 3
TMOO 2253 3393
H
N) N) � N
a) c o 0 3 r i
co 0o a, a, 3 Z
Z
o 0 0 0 3= O
Z
n) N) N) i) 0 L..q v
TMOO 2254 3393
H
3
o o CO 0 01 01 01 01 3 r ."
I::'
(0 (0 ao 0o v v v v 3 - °
a
o o 0 0 01 01 , 01
3 Z
.,
o
►. .
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v
O O O 0 N N 01 (N), Z z
TMOO 2255 3393
0) 0) 0) 0) 0 0 0 0 3 r
o 0 0 0 0 0 o O 3 -`
-.IT
nigil-
0 0 CO 0 0 V 0 J 3 N ,�' -
v_
3W
01 01 01 0, 0 0 0 01 3
CO144-
N N N N N)_ N_ N_ N 3 co A
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C
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TMOO 2256 3393
0•6ij

Fig. D
GB Airborne noise emitted by pumps with motors fitted by GRUNDFOS:
�D Luftschallemission von Pumpen mit Motoren,die von GRUNDFOS montiert sind:
CF Bruit aerien emis par les pompes avec moteurs montes par GRUNDFOS:
01 Rumore aereo emesso da pompe dotate di motori installati da GRUNDFOS:
0 Nivel de ruido producido por bombas con motores montados por GRUNDFOS:
Ruido emitido pelas electrobombas montadas pela GRUNDFOS:
GR O6pu3oq nou eKnipneTai orov aipa ono avTAicc cq o5iaap*vcc pe Krvrirrjpec ands Tr)GRUNDFOS:
NL Geluidsdruk van pompen met een door GRUNDFOS gemonteerde motor:
OS Ljudtrycksniva fran pumpar med motorer monterade av GRUNDFOS:
SF Ilmassa kantautuva aani GRUNDFOS'in asentamilla moottoreilla:
DK Luftbaren stoj fra pumper med motorer monteret of GRUNDFOS:
50 Hz 60 Hz
Motor
EPA
[kW] pA
[dB(A)] [dB(A)]
0.25 <70 <70
0.37 <70 <70
0.55 <70 <70
0.75 <70 <70
1.1 <70 <70
1.5 <70 <70
2.2 <70 <70
3.0 <70 <70
4.0 <70 <70
5.5 <70 <70
7.5 <70 72
11 80 84
15 72 77
Fig. E
6n Hv
CC/ (ml
150-_45
-40
140-35
-30
130-_25
120120
11015
-12
100110
90-
-6,0
-6,0
80�'S,0
-4,0
703.0
60-2,0
-1,5
50-
1,0
40,0,6
0,6
3010,4 M
0,3 rn
20-02
1
0-
-0,1 1"1
0- O
2
H

CR, CRN 2 and 4
Fig.F
N*1
r
A B
6-__-
2.....4
�,1I I0ithiit .,.
.`��•\ T)IIII r;,, r :I� 4i
.741‘1\--9
I I . •• 10' iiiii0
� o' VIII I,o,f, , ,..„m I ! rnN � N
co,
• G1-
C D
�1 M6 13 Nm(1,3 kpm)
1• ;ij a M8 32 Nm(3,1 kpm)
t1,5 mmj .�01M10 62 Nm(6,2 kpm)
1 �IIIIII�,�r`��`'POI
2
■of ( '
. ate.
O
I i 1 1, 1� �������� ''
0 114 co Vil(W,I. 11
/ N 2 1
Ipoi
N
N `�� , N

CR, CRN 8 and 16
Fig.G
A IB
1 Aiwi
41:11°40
71111II
fi!4
SiIlll�lgl�' .,j; 44 W1--
,
t 9 1111 ' 4 2
le"
-10 8
11111 . C41
Op\, , *11111
%8. i :<-'
"*, >1" 4--
8 `j i
A % i,;-- ii
CD
3 • 4)0
M613Nm1,3kpm)o M632 Nm�3,1kpm)1 t4M10 62 Nm(6,2 kpm)
° O _till
''rte
--16_ � 1
+ LIIIIIIIII1
N ( i(I
r
''‘.5>,-' ,
4 t A\ I
l4 1
49
1001 Oil
• III.j : :;I41110-
4*
�1 ►
1
o 71111
m
_
N N
P O. i, P

NPSH
p H
[kPa] [m] CR 2,CRN 2
9- 60 Hz
80- 8
7
60- 6 •
50 Hz
5
40- 4
3
20- 2
n
1 a,
kr
v
0- 0 (N
N
0.0 0.4 0.8 1.2 1.6 2.0 2.4 2.8 3.2 3.6 Q[m'/h] tD
o
I I I I I I I o
0.0 0.2 0.4 0.6 0.8 1.0 Q Ws] 1-
P H
[kPa] [m] CR 4,CRN 4
•
• 2.8 I
24-2.4 60 HZ
2.0 50 H7
16-
1s
1.2
8-0.8
0.4 �' r-
rn
La
0-0.0 v
CD
DI
0 1 2 3 4 5 6 7 8 Q[m'/h] `O
1 I I I I I I o
0.0 0.4 0.8 1.2 1.6 2.0 2.4 Q[Ifs] i-
P H
[kPa] [m] CR 8 CRN 8
3.6
32-3.2 .............1 4N.
2.8 ............ ..
24-2A MEMMENNEN 5o Hz MIAMI
111........ ,M... Nameplate on
16-21.0 ..... ..rM
.... ... pump indicates 42
1.2 ..........'41.... gpm.
........__ina.....
8-0.8 �M�MINEzi,.......
o-0.o allaill11............ L.
N
O 1 2 3 4 5 6 7 8 9 10 11 12 13 Q[m'/h] t2
11 1 1 1 1 1 I I I I I 0
0.0 0.4 0.8 1.2 1.6 2.0 2.4 2.8 3.2 3.6 Q[IN 1-
P H
[kPa] [m] CR 16,CRN 16
9
80- 8 I 60 Hz
7 50 Hz
60- 6-
5 1 I
40- 4
3-
20- 2
1 rn
CO
N
O 2 4 6 8 10 12 14 16 18 20 22 24Q[V/h) af
I I I I I I I o
O 1 2 3 4 5 6 7Q[Ifs] 1-
1
LIL.. - --- ------- -- - - - - -

f
Denmark Hong Kong Poland
GRUNDFOS DK A/S GRUNDFOS Pumps(Hong Kong)Ltd. GRUNDFOS Pompy Sp.z o.o.
Poul Due Jensens Vej 7A Unit 1,Ground floor ul.Klonowa 23
DK-8850 Bjerringbro Siu Wai Industrial Centre Baranowo k.Poznania
Tlf.:[phone] 29-33 Wing Hong Street& PL-62-081 Przezmierowo
Telefax:[phone] 68 King Lam Street,Cheung Sha Wan Phone:[phone]
E-mail:info [e-mail] Kowloon Telefax:[phone]
www.grundfos.com/DK Phone:[phone] Portugal
Argentina Telefax:[phone] Bombas GRUNDFOS Portugal,S.A.
Bombas GRUNDFOS de Argentina S.A. Hungary Rua Calvet de Magalhaes,241
Ruta Panamericana km.37.500 Lote 34A GRUNDFOS Hungaria Kft. Apartado 1079
1619-Garin Park u.8 P-2770-153 Paco de Arcos
Pcia.de Buenos Aires H-2045 Torbkbalint, Tel.:[phone]
Phone:[phone] Phone:[phone] Telefax:[phone]
Telefax:[phone] Telefax:[phone] Russia
Australia India 000 GRUNDFOS
GRUNDFOS Pumps Pty.Ltd. GRUNDFOS Pumps India Private Limited Shkolnaya 39
P.O.Box 2040 Flat A,Ground Floor RUS-109544 Moscow
Regency Park 61/62 Chamiers Aptmt Phone:[phone]
South Australia 5942 Chamiers Road Telefax:[phone],[phone]
Phone:[phone] Chennai 600 028 e-mail:[e-mail]
Telefax:[phone] Phone:[phone] Singapore
Austria Telefax:[phone] GRUNDFOS(Singapore)Pte.Ltd.
GRUNDFOS Pumpen Vertrieb Ges.m.b.H. Indonesia 24 Tuas West Road
Grundfosstraf6e 2 PT GRUNDFOS Pompa Jurong Town
A-5082 GrOdig/Salzburg JI.Rawa Sumur III,Blok III/CC-1 Singapore 638381
Tel.:[phone] Kawasan Industri,Pulogadung Phone:[phone]
Telefax:[phone] Jakarta 13930 Telefax:[phone]
Phone:[phone] Spain
Belgium Telefax:[phone]/460 6901 p
N.V.GRUNDFOS Bellux S.A. Bombas GRUNDFOS Espana S.A.
1 Boomsesteenweg 81-83 Ireland Camino de la Fuentecilla,s/n
B-2630 Aartselaar GRUNDFOS(Ireland)Ltd. E-28110 Algete(Madrid)
Tel.:[phone] Unit 34,Stillorgan Industrial Park Tel.:[phone]
Telecopie:[phone] Blackrock Telefax:[phone]
Brazil County Dublin Sweden
GRUNDFOS do Brasil Ltda. Phone:[phone] GRUNDFOS AB
Rua Tomazina 106 Telefax:[phone] Box 63,Angeredsvinkeln 9
CEP 83325-040 Italy S-424 22 Angered
Pinhais-PR GRUNDFOS Pompe Italia S.r.l. Tel.:[phone]
Phone:[phone] Via Gran Sasso 4 Telefax:[phone]
Telefax:[phone] 1-20060 Truccazzano(Milano) Switzerland
Canada Tel.:[phone] GRUNDFOS Pumpen AG
GRUNDFOS Canada Inc. Telefax:[phone]/95838461 Bruggacherstrasse 10
2941 Brighton Road Japan CH-8117 Fallanden/ZH
Oakville,Ontario GRUNDFOS Pumps K.K. Tel.:[phone]
L6H 6C9 1-2-3,Shin Miyakoda Telefax:[phone]
Phone:[phone] Hamamatsu City Taiwan
Telefax:[phone] Shizuoka pref.431-21 GRUNDFOS Pumps(Taiwan)Ltd.
China Phone:[phone] 14,Min-Yu Road
GRUNDFOS Pumps(Shanghai)Co.Ltd. Telefax:[phone] Tunglo Industrial Park
22 Floor,Xin Hua Lian Building Korea Tunglo,Miao-Li County
755-775 Huai Hai Rd,(M) GRUNDFOS Pumps Korea Ltd. Taiwan,R.O.C.
Shanghai 200020 6th Floor,Aju Building 679-5 Phone:[phone]
PRC Yeoksam-dong,Kangnam-ku,135-916 Telefax:[phone]
Phone:[phone] Seoul Korea Thailand
Telefax:[phone] Phone:[phone] GRUNDFOS(Thailand)Ltd.
Czech Republic Telefax:[phone] 947/168 Moo 12,Bangna-Trad Rd.,K.M.3,
GRUNDFOS s.r.o. Malaysia Bangna,Phrakanong
Cajkovskeho 21 GRUNDFOS Pumps Sdn.Bhd. Bangkok 10260
779 00 Olomouc 7 Jalan Peguam U1/25 Phone:[phone]...91
Phone:[phone] Glenmarie Industrial Park Telefax:[phone]...6
Telefax:[phone] 40150 Shah Alam Turkey
Finland Selangor GRUNDFOS POMPA SAN.ve TIC.LTD.STI
OY GRUNDFOS Pumput AB Phone:[phone] Bulgurlu Caddesi no.32
Mestarintie 11 Telefax:[phone] TR-81190(Jskiidar Istanbul
Piispankyla Mexico Phone:[phone]
FIN-01730 Vantaa(Helsinki) Bombas GRUNDFOS de Mexico S.A.de C.V. Telefax:[phone]
Phone:[phone] Boulevard TLC No. 15 United Arab Emirates
Telefax:[phone] Parque Industrial Stiva Aeropuerto GRUNDFOS Gulf Distribution
Apodaca,N.L.66600
France P.O.Box 16768
Pompes GRUNDFOS Distribution S.A. Mexico Jebel Ali Free Zone
Parc d'Activites de Chesnes Phone:[phone] Dubai
57,rue de Malacombe Telefax:[phone] Phone:[phone]
F-38290 St.Quentin Fallavier(Lyon) Netherlands Telefax:[phone]
Tel.:[phone] GRUNDFOS Nederland B.V. United Kingdom
Telecopie:[phone] Postbus 104 GRUNDFOS Pumps Ltd.
Germany NL-1380 AC Weesp Grovebury Road
GRUNDFOS GMBH Tel.:[phone] Leighton Buzzard/Beds.LU7 8TL
Schliiterstr.33 Telefax:[phone]/492299 Phone:[phone]
40699 Erkrath New Zealand Telefax:[phone]
Tel.:[phone] GRUNDFOS Pumps NZ Ltd. U.S.A.
Telefax:[phone] 17 Beatrice Tinsley Crescent GRUNDFOS Pumps Corporation
e-mail:[e-mail] North Harbour Industrial Estate 17100 West 118th Terrace
Service in Deutschland: Albany,Auckland Olathe,Kansas 66061
e-mail:[e-mail] Phone:[phone] Phone:[phone]
Greece Telefax:[phone] Telefax:[phone]
GRUNDFOS Hellas A.E.B.E. Norway
20th km.Athinon-Markopoulou Av. GRUNDFOS Pumper A/S
P.O.Box 71 Stremsveien 344
GR-19002 Peania Postboks 235,Leirdal
Phone:[phone] N-1011 Oslo
Telefax:+0030-210-66 46 273 Tlf.:[phone]
Telefax:[phone]

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