NCG510549_More Information Received _20180511

May 3, 2018
North Carolina Department of Environmental Quality
Division of Water Resources
1617 Mail Service Center
Raleigh, North Carolina 27699-1617
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:
RECEIVEDIDENRIDWR
MAY 11 2018
Water Resources
Permitting Sectton
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
II.
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. 1 44 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
O Other:
® Carbon Adsorption ® Filters
a) If an Oil/Water separator is present, please provide the following information:
i) Rated flow capacity of the unit (in GPM): 34 gpm 20 microns to 77 gpm 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 apm
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(c)(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)1
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)
Yd2ee0
(Signature of Applicant)
May 3, 2017
(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 Iper G.S. 4 143-215.3(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 (S .tom w' 1 G. zo f1 p�, 1C., r ow
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, April26, 2018 2:0134 PM
From: Jeff Dulaney
Sent: Thursday, April 19, 2018 5:19:43 PM
To: Bradley S. Keyse
Cc: David Loftis; 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, 20181:36 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
imorr
s
S&ME
44 Buck Shoals Road, Suite C-3
Arden, NC 28704 map
0: 828.483.3013
M: 828.329.3367
www.smeinc.com
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Attachment III — Groundwater Remediation System Specifications

Groundwater Remediation System Specifications
Blue Ridge Hospital — Spruce Pine
NCDEQ Incident No. 3659
125 Hospital Drive ��,►��Ai ++
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Spruce Pine, Mitchell County, North Car, .ss,o'!,
S&ME Project No. 4305-17-109E = L .IP
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///14.1%%0
PREPARED FOR
NCDEQ, UST Section
1646 Mail Service Center
Raleigh, NC 27699
PRFPARFD BY
S&ME, Inc.
44 Buck Shoals Road, Suite C-3
Arden, NC 28704
May 3, 2018

Groundwater Remediation System Specifications
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
AMMINI
Mina
Ifl
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

Groundwater Remediation System Specifications
Blue Ridge Hospital — Spruce Pine, NCDEQ Incident No. 3659
Spruce Pine, Mitchell County, North Carolina
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
S&ME Project No. 4305-17-109E
MEM
IMP
III Er
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:
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;
• 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
S&ME Project No. 4305-17-109E
Table 1-1— Influent Data
Constituent
Concentration
Benzene
46 µg/L
Ethylbenzene
18 µg/L
Toluene
13 µg/L
Total Xylenes
84 µg/L
MTBE
<1.0 µg/L
Naphthalene
76 µg/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
µg/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:
Overall Dimensions:
Design Flow Rate:
Oil Droplet Removal Rate:
Coalescing Media Pack Size:
Minimum Coalescing Surface Area:
Maximum Cross -sectional Velocity:
Minimum Separation Retention Time:
Hydro -Flo Technologies Inc.
Approximately 9 feet long by 3 feet wide by 5.5 feet tall
34 gpm @ 20 microns to 77 gpm @ 30 microns
10 mg/L of oil droplets > 20-30 microns
48 inches long by 24 inches wide by 36 inches tall
1,632 square feet
0.75 to 1.72 feet per minute
7.48 to 10 minutes
May 3, 2018 3

Groundwater Remediation System Specifications
Blue Ridge Hospital — Spruce Pine, NCDEQ Incident No. 3659
Spruce Pine, Mitchell County, North Carolina
S&ME Project No. 4305-17-109E
III Ei
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
Constituent
Influent
Conc.
(ppb) -
1993
Effluent
Conc.
(ppb) -
1993
Air
Effluent
Conc.
(ppmv)
1993
Removal
Efficiency
Influent
Conc.
(ppb) -
2018
Effluent
Conc.
(ppb) —
2018
Air
Effluent
Conc.
(ppmv)
2018
Removal
Efficiency
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
benzene
3,400
<1
4.51
100%
18
<1
0.01
100%
Total
Xylenes
13,000
<1
17.28
99.99%
84
<1
0.06
100%
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
Spruce Pine, Mitchell County, North Carolina
S&ME Project No. 4305-17-109E
Following are the specifications for the Shallow Tray Stripper:
Manufacturer:
Model Number:
Air Flow Rate:
Water Flow Rate:
Air/Water Ratio:
Number of Trays:
Overall Dimensions:
Northeast Environmental Products Inc. (NEEP)
3631
900 cubic feet per minute
1-125 gpm
134.6 cubic feet per minute of air per cubic feet per minute of water
3
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
P11 AIMPV
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:
Model Number:
Filter Bags:
Surface Area per Bag:
Maximum flow:
FSI
BFN 12
1— 50 Micron
4.4 squre feet
Up to 220 gpm
2.3.2 10 Micron Bag Filters
Manufacturer:
Model Number:
Filter Bags:
Surface Area per Bag:
Maximum flow:
Krystil Klear
88
1- 10 Micron
4.4 square feet
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

Groundwater Remediation System Specifications
Blue Ridge Hospital - Spruce Pine, NCDEQ Incident No. 3659
Spruce Pine, Mitchell County, North Carolina
S&ME Project No. 4305-17-109E
MIMI
MEI
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
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
Spruce Pine, Mitchell County, North Carolina
S&ME Project No. 4305-17-109E
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 following table describes the system controls and alarms that have been installed on the treatment system:
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
Batch Tank Alarm
Float switch
Within Batch Tank
Hi -Hi float switch shuts the
treatment system off when
activated
Shallow Tray Transfer
Pump
Float switch
Within Shallow Tray
Sump
Low and Hi float switch turns
the transfer pump on/off
Shallow Tray Stripper
Alarm
Float switch
Within Shallow Tray
Sump
Hi -Hi float switch shuts the
treatment system off when
activated
Shallow Tray Stripper
Alarm
Pressure Switch
Within Shallow Tray
Stripper
Shuts down the treatment
system due to pressure
buildup/fouling of trays
Product Storage Tank
Alarm
Float Switch
Within Tank
Hi -Hi float switch shuts down
the treatment system when
activated
May 3, 2018 7

Appendices

Appendix I - Figures

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MeupoK c L' B
/a.y D e ..o r S
ace s u ' C E�
Deed per. ,� e 1 d° a 4
' a. 1.. t o o6r•oo $ �arrgr
a. Q �. A O @u� $ !no
?' Ao O''r -Ler`ace a Spruce Pin. Pine Ave i rc 0
e Walnut Ave o
04,
'ock Pvc
5 s�
8 air°4 tree
grad Regan
f, Mammal
Fan !
English Rd
V,anl� 40
u0
4-d
fit
unra *ao
ep
r
Oe Rd are0 Bata Dr henry
Y tr Fairway L,, e'+
Y
�
..aF
ti >
U �000'
r.1 r.
Roogera S
O
Qc
1 Ica Od4 ha
lgke 4ve aS
wor,a.,o„ r:a aRa
2,000
a
Rock/
4,000e, u�
(FEET)
pteefy C,tat
C/ine 0 9ra
ed
Ca /era Rr6Oe Rtl Dr
�ounte`P La Gain,
REFERENCE:
BASE MAPPING OBTAINED FROM ESRI. THIS MAP IS FOR INFORMATIONAL PURPOSES
ONLY. ALL FEATURE LOCATIONS DISPLAYED ARE APPROXIMATED. THEY ARE NOT BASED ON
CIVIL SURVEY INFORMATION, UNLESS STATED OTHERWISE.
0
er in Sun
t.D
P
Ftp+avy
0
O
0
O
u d
u
r
Nteieteerr
r.�n�r tea
High*" to `
?� 4 Pe
`r Isl'a<'ap as e
en o 'Sy2 P
490rhe
< a
Wyatt`
w Or
Wy4r id®e
Cook Ln
* Project Location
NMI
IIIFE
SITE VICINITY MAP
SCALE:
1n=2,000r
BLUE RIDGE HOSPITAL
125 HOSPITAL DRIVE
SPRUCE PINE, MITCHELL CO., NORTH CAROLINA
DATE:
10-24-17
PROJECT NUMBER
405-17-109
FIGURE NO.
1

1-1
0
a
E
0
E
1-4
rn
REFERENCE:
GIS BASE LAYERS WERE OBTAINED FROM NC ONEMAP AND MITCHELL COUNTY GIS DEPARTMENT.
THIS MAP IS FOR INFORMATIONAL PURPOSES ONLY. ALL FEATURE LOCATIONS DISPLAYED ARE
APPROXIMATED. THEY ARE NOT BASED ON CIVIL SURVEY INFORMATION, UNLESS STATED OTHERWISE.
RW-10
RW-12" ® MW=4R
•
RW-11 MW-4
RW=6
MW-10'
;4 J,
IMW-9
WR-21
OW-4 MW-1
MW-8 ,
31XMW-3
RW-8 ❑ MW-2
MW-14
4 NC OneMa
® Monitoring Wells (Located)
IN Monitoring Wells (Unconfirmed)
X Monitoring Wells (Abandoned / Not Located)
F Recovery Wells
A Observation Wells
—►Recovery Lines
Approximate UST Locations
III E.
BLUE RIDGE HOSPIT
125 HOSPITAL DRIVE
SCALE:
1"=80'
DATE:
10-24-17
SPRUCE PINE, MITCHELL COUNTY, NORTH CAROLINA
PROJECT NUMBER
4305-17-109
FIGURE NO.
2

Drawing path: C:\Users\jnyvall\Desktop\Spruce Pine Information\SP with Plot Styles.dwg
1
0 4 8
GRAPHIC SCALE (IN FEET)
`
3,000 Gallon Free Product
Storage Tank w/ Secondary
Containment
Steel Tank Institute Model F911
Batch Transfer Pump
Price Pump Model EC150
Influent from recovery wells
(3 hoses)
500 Gallon Poly
Batch Tank
Chemtainer Ind.
Oil/Water Separator #1
Hydro Flo Technologies Model DP-24
Treating Recovery Wells 1-16
f
Shallow Tray Air Stripper
Skid w/supporting
equipment
NEEP Shallow Tray Model
3631
-4811
Transfer Pump
Grundfos Model CRN-8-40
2-10 Micron Bag Filters
Krystal Klear Model 88-30 Vessel Backwashing
Oil/Water Separator #2
Hydro Flo Technologies Model DP-24
Treating Trench Recovery Wells 17-27
2 50 Micron Bag Filters
FSI Model BFNP-12 (304SS)
2-1,000 lb Carbon Vessels
CarbonAir Model PC7F
c
w
0
0
0
z
Discharge from system
to NPDES point
Groundwater Treatment Building
LEGEND
WATER FLOW PATH (Dashed where below ground)
AIR FLOW PATH (Dashed where below ground)
PRODUCT FLOW PATH
Notes:
1) Dimensions of equipment are approximate based on
cut sheets for models shown.
2) Piping between equipment consists of Sch. 40 PVC of
various sizes as well as flexible piping (either HDPE or
hose).
3) Valving and sample ports have not been included on
this figure.
Controls and Compressed Air
Building
Service Entrance
Air Supply to
Recovery Wells
Treatment System Layout
SCALE:
As Shown
DATE:
PROJECT NUMBER
4305-17-109J
FIGURE NO.

Discharge to
tributary
BEAVER
N.
1^n
SEABOARD SYSTEM
RAILROAD
i
7
/
7
7
/
7
•
REFERENCE:
Figure from S&ME's October 1998 Site Map for Engineering Drawings
cpt-
/
Underground
Piping
•
Q1,//
Remediation
S stem
Effluent Sample Location
in the S stem
r
Solid
Underground
Pipe
yS.W.D.I.
•
i
•
•
♦
♦
\\
S.W.D-I
Effluent Discharge
from Remediation
System to Storm
Water System
Hospital
SPRUCE PINE
HOSPITAL
SITE MAP — DISCHARGE PATH
SCALE:
NTS
BLUE RIDGE HOSPITAL
125 HOSPITAL DRIVE
SPRUCE PINE, MITCHELL COUNTY, NORTH CAROLINA
DATE:
10-31-2017
PROJECT NUMBER
4305-17-109E
FIGURE NO.
3

1
Drawing Path: C:\Users\jnyvall\Desktop\Spruce Pine Information\SP with Plot Styles.dwg
Influent From
Recovery Wells
i
OIL/WATER SEPARATOR
(Original)
To Recovery Wells
I
2 HP
AIR COMPRESSOR
C.-BATCH TANK
TRANSFER PUMP
1
2- 50 MICRON
BAG FILTERS
(TURBINE FLAW METER(
Influent From
Recovery Wells
i
OIL/WATER SEPARATOR
(Supplemental)
3-TRAY SHALLOW
AIR STRIPPING
SYSTEM
AIR STRIPPER
TRANSFER PUMP
2- 10 MICRON
BAG FILTERS
1000 LB GRANULAR
ACTIVATED CARBON P
VESSEL
1000 LB GRANULAR
ACTIVATED CARBON
VESSEL
its
V_-0
Discharge from system to NPDES point
under gravity flow conditions
3,000 GALLON
PRODUCT HOLDING TANK
WITH SECONDARY
CONTAINMENT
LEGEND
WATER FLOW PATH
AIR FLOW PATH
PRODUCT FLOW PATH
0 BALL VALVE
VACUUM RELIEF VALVE
SAMPLE POINT
-0 PRESSURE GAUGE
NOTE:
ALARMS HAVE BEEN INSTALLED AS FOLLOWS:
1) HI LEVEL IN TRAY STRIPPER SUMP
2) HI PRESSURE IN TRAY STRIPPER
3) HI LEVEL IN PRODUCT AST
4) HI LEVEL IN BATCH TANK
ANY OF THE ALARMS ACTIVATED ABOVE WILL SHUT
SYSTEM DOWN TO PREVENT OVERFLOW CONDIITON.
Treatment System Flow Diagram
Blue Ridge Hospital
125 Hospital Drive
Spruce Pine, North Carolina
SCALE:
Not to Scale
DATE:
4-9-18
PROJECT NUMBER
4305-17-109J
FIGURE NO.
4

Appendix II - Site Photographs

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

0-micron filters plumbed in parallel
Blue Ridge Hospital — Groundwater Treatment System
Spruce Pine, NC
S&ME Project 4305-18-109J
Taken by: GS
I Date Taken: 4/9/18

9
11
10-micron filters plumbed in parallel
it compressor located in secondary treatment building
wo 1,000 lb carbon vessels plumbed in series
Electrical panel located inside secondary treatment building
Blue Ridge Hospital — Groundwater Treatment System
Spruce Pine, NC
S&ME Project 4305-18-109J
Taken by: GS
I Date Taken: 4/9/18

Appendix III - Pneumatic Pumps Specifications

V QED
Specifications - Top Inlet, Long
Environmental Systems
Max. Flow 10 gpm (38 Ipm)
O.D. 3.6 in (91 mm)
Length 56.7 in. (144 cm)
Advantages
1. The original automatic air -
powered well pump, proven
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
Description
The AP4+ Top Inlet Long AutoPump provides maximum
capabilities and flow in a top inlet pump for 4" diameter
and larger wells needing an elevated inlet, such as pumping
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
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-
tors, wellhead caps and accessories to help your installa-
tion go smoothly. This superior pumping heritage, applica-
tion experience and support back up every AutoPump you
put to work on your project.
33

V QED
Specifications - Top Inlet, Long
Environmental Systems
Pump Dimensions
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
Specifications & Operating Requirements
Model
Liquid Inlet Location
O.D.
Overall Length (Pump & Fittings)
Weight
Maximum Flow Rate
Pump Volume/Cycle
Minimum Accuation Level
Standard Pump
Maximum Depth
Air Pressure
Air Usage
High Pressure Pump
Maximum Depth
Air Pressure
Minimum Liquid Density
Standard Construction Materials'
Pump Body
Pump Ends
Internal Components
Tube & Hose Fittings
Fitting Type
Tube & Hose Options
Tubing Materials'
Sizes - Liquid Discharge
Pump Air Supply
Air Exhaust
Hose Material
Sizes - Liquid Discharge
Pump Air Supply
Air Exhaust
Applies to QED supplied tubing;
other tubing sources may not
conform to QED fittings.
4" - Long AP4+ Top Inlet
Top
3.6 in. (91 mm)
56.7 in. (144 cm)
16.5 lbs. (7.6 kg)
10 gpm (38 Ipm)' - See Flow Rate Chart
0.58 - 0.78 gal (2.2 - 3L 1
53.3 in. (135 cm)
250 ft. (76 m)
5 -120 psi (0.4 - 8.4 kg/cm2)
0.35 -1.1 scf / gal. (3.0 - 8.4 liter of air /
fluid liter) - See air usage chart
425 ft. (130 m)
5 - 200 psi (0.4 -14.1 kg/cm2)
0.7 SpG (0.7 g/cm3)
Fiberglass or Stainless Steel
Stainless Steel
Stainless Steel, Viton, PVDF, Hastelloy-C
Brass or Stainless Steel
Barbs, Quick Connects or Easy Fittings
Nylon
1 in. (25 mm) or 1-1/4 in. (32 mm) OD
1/2 in. (13 mm) OD
5/8 in. (16 mm) OD
Nitrile
3/4 in. (19 mm) or 1 in. (25 mm) ID
3/8 in. (9.5 mm) ID
1/2 in. (13 mm) ID
Long and short AP4+ AutoPumps are warranted for
five(5) years: Low-Drawdown AP4+ AutoPumps are
warranted for one (1) year.
34

V QED
Specifications - Top Inlet, Long
Environmental Systems
3/4 inch (19 mm)
Inside Diameter Discharge Hose
(Equivalent to 1-Inch O.D.Tubing)
6-INCH (15 cm)
GALLONS
PER
MINUTE
WITH
3/4-INCH
I.D. HOSE
18
16
14
12
10
8
6
4
2
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
00 PSI
40 P51 70 PSI
0 - 3Kg/cm2 5Kg/cm2 0
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
SUBMERGENCE OF PUMP HEAD
Flow Rates'
2 FT. (60 cm)
GALLONS
PER
MINUTE
WITH
3/4-INCH
I.D. HOSE
18
16
14
12
10
8
6
4
2
0
7 Kg/cm
AIR INLET PRESSURES
0
Kg PSI Kg/cm/cm 7
40 PSI 70 P51
Kg/ m ° 5 Kg; crn
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
0
APPROXIMATE
LITERS
PER
MINUTE
WITH
19 mm
I.D. HOSE
APPROXIMATE
LITERS
PER
MINUTE
WITH
19 mm
I.D. HOSE
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
10 FT. (300 cm)
GALLONS
PER 12
MINUTE 10
WITH
3/4-INCH 8
I.D. HOSE 6
18
16
14
4
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
2 - 40 P51
3Kgcm 2
0
0 20 40 60 80 100 120 140 160 180
6.1 12.2 18.3 244 30 5 366 42 748.8 54.9
00 PSI
7 Kg/cm 2
70'
5 Kg/cm 2
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
APPROXIMATE
LITERS
PER
MINUTE
WITH
19 mm
I.D. HOSE
0
200 FT. 1 DEPTH
61 Meters IN WELL
1 inch (25.4 mm)
Inside Diameter Discharge Hose
(Equivalent to 1.25-Inch O.D.Tubing)
6-INCH (15 cm)
GALLONS
PER
MINUTE
WITH
1-INCH
I.D. HOSE
18
16
14
12
10
8
6
4
2
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
I 40 PS
3 Kg/cm 2
0
100 PSI
7 Kg/cm
70 PSI
5 Kg/cm
20 40 60 80 100 120 140 160 180
6.1 12.2 183 244 305 366 427 48.8 54.9
2FT.(60cm)
GALLONS
PER
MINUTE
WITH
1-INCH
I.D. HOSE 6
2
18
16
14
12
10
SUBMERGENCE OF PUMP HEAD
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
0
00 FT. DEPTH
61 Meters IN WELL
APPROXIMATE
LITERS
PER
MINUTE
WITH
25.4 mm
I.D. HOSE
AIR INLET PRESSURES H
40 PS
3 Kg/cm 2
I I
68 1
60.6
APPROXIMATE
45.4 LITERS
PER
37.9
MINUTE
30.3 WITH
100 PSI 22.7 25.4mm
7 Kg/cm
15 1 I.D. HOSE
70 PSI 7.6
5 Kg/cm 2 0
0 20
6.1
10 FT. (300 cm)
GALLONS
PER
MINUTE
WITH
1-INCH
I.D. HOSE
18
16
14
12
10
6
4
2
00
53
40 0 80 100 120 140 160 180 00 FT. DEPTH
12.2 183 244 30.5 36.6 427 48.8 54.9 61 Meters IN WELL
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES I-
\\N\\'
40 PSI il 70 PS � 100 PSI
3 Kg/cm 5 Kg/cm 2 IlllllI 7Kg/cm 2
0 40 60 80 100 120 140 160
6.1 12.2 18.3 24.4 30.5 36.6 42 7 48.8
(FLOW RATES MAY VARY WITH SITE CONDITIONS. CALL QED FOR TECHNICAL ASSISTANCE.
68.1
60.6
53
APPROXIMATE
45.4 LITERS
37.9 PER
MINUTE
30.3 WITH
22.7 25.4 mm
I.D. HOSE
15.1
7.6
0
180 200 FT. DEPTH
54.9 61 Meters IN WELL
35

V QED
Specifications - Top Inlet, Long
Environmental Systems
STANDARD
CUBIC FEET OF AIR
PER
GALLON PUMPED
(SCF/GAL)
STANDARD
CUBIC FEET OF AIR
PER
GALLON PUMPED
(SCF/GAL)
1.0
Air Consumption
70 PSI
5Kg/ mt
40 P51
31, On
12
3/4 inch (19 mm)
11.2 Inside Diameter Discharge Hose
,05 (Equivalent to 1-Inch O.D. Tubing)
9.7
9.0
8.2
APPROXIMATE
STANDARD
7.5 LITER OF AIR
PER
6.7 LITER PUMPED
(STD L/LITER)
6.0
5.2
4.5
3.0
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
1.6
1.5
14
1.3
1.2
1.0
.9
.8
7
.6
.5
.4
.3
100 PSI
7 Kg/cm
70 PSI
5 Kg/ m
40 PSI
3 Kg/cm
11.2 1 inch (25.4 mm)
Inside Diameter Discharge Hose
10.5 (Equivalent to 1.25-Inch O.D. Tubing)
9.7
9.0
8.2
APPROXIMATE
STANDARD
7.5 LITER OF AIR
PER
6.7 LITER PUMPED
(STD L/LITER)
6.0
5.2
4.5
3.7
3.0
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
36

� QED
Specifications - Top Inlet, Short
Environmental Systems
Max. Flow 9 gpm (34 Ipm)
0.D. 3.6 in (91 mm)
Length 45 in. (110 cm)
Advantages
1. The original automatic air -
powered well pump, proven
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
Description
The AP4+ Top Inlet Short AutoPump provides maximum
capabilities and flow in a top inlet pump for 4" (100 mm)
diameter and larger wells with shorter water columns and
the need for an elevated inlet, such as pumping 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 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,
wellhead caps and accessories to help your installation go
smoothly. This superior pumping heritage, application
experience and support back up every AutoPump you put to
work on your project.
37

V QED
Specifications - Top Inlet, Short
Environmental Systems
i
Pump Dimensions
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
Specifications & Operating Requirements
Model
Liquid Inlet Location
O.D.
Overall Length (Pump & Fittings)
Weight
Maximum Flow Rate
Pump Volume/Cycle
Minimum Accuation Level
Standard Pump
Maximum Depth
Air Pressure
Air Usage
High Pressure Pump
Maximum Depth
Air Pressure
Minimum Liquid Density
Standard Construction Materials
Pump Body
Pump Ends
Internal Components
Tube & Hose Fittings
Fitting Type
Tube & Hose Options
Tubing Materials'
Sizes - Liquid Discharge
Pump Air Supply
Air Exhaust
Hose Material
Sizes - Liquid Discharge
Pump Air Supply
Air Exhaust
1 Applies to QED supplied tubing;
other tubing sources may not
conform to QED fittings.
4" - Short AP4+ Top Inlet
Top
3.6 in. (91 mm)
45 in. (110 cm)
15.8 lbs. (7.2 kg)
9 gpm (34 Ipm)* - See Flow Rate Chart
0.22 - 0.36 gal (.83-1.36L)
41.6 in. (106 cm)
250 ft. (76 m)
5.120 psi (0.4 - 8.4 kg/cm2)
0.35.1.5 scf / gal. (2.4 - 8.4 liter of air /
fluid liter) - See air usage chart
425 ft. (130 m)
5 - 200 psi (0.4 -14.1 kg/cm2)
0.7 SpG (0.7 g/cm3)
Fiberglass or Stainless Steel
Stainless Steel
Stainless Steel, Viton, PVDF, Hastelloy-C
Brass or Stainless Steel
Barbs, Quick Connects or Easy Fittings
Nylon
1 in. (25 mm) or 1-1/4 in. (32 mm) OD
1/2 in. (13 mm) OD
5/8 in. (16 mm) OD
Nitrile
3/4 in. (19 mm) or 1 in. (25 mm) ID
3/8 in. (9.5 mm) ID
1/2 in. (13 mm) ID
Long and short AP4+ AutoPumps are warranted for
five(5) years: Low-Drawdown AP4+ AutoPumps are
warranted for one (1) year.
38

V QED
Specifications - Top Inlet, Short
Environmental Systems
3/4 inch (19 mm)
Inside Diameter Discharge Hose
(Equivalent to 1-Inch O.D.Tubing)
6-INCH (15 cm)
GALLONS
PER
MINUTE
WITH
3/4-INCH
I.D. HOSE
18
16
14
12
10
8
6
4
2 -
0 0
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
40 PSI
3 Kg/cm 2
20 40
6.1 12.2
2 FT. (60 cm)
GALLONS
PER
MINUTE
WITH
3/4-INCH
I.D. HOSE
8
2
100 PSI
7 Kg/cm 2
60
18.3
70PSI ,
5 Kg/cm
80 100 120 140 160 180
24.4 30.5 36.6 42.7 48.8 54.9
SUBMERGENCE OF PUMP HEAD
68 1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
Flow Rates'
APPROXIMATE
LITERS
PER
MINUTE
WITH
19 mm
I.D. HOSE
0
200 FT. DEPTH
61 Meters IN WELL
AIR INLET PRESSURES
10
8
6
4
2 40 PSI
0 r 3 Kg/cm
0 20 40 60 80 100 120 140
6.1 12.2 18.3 244 30.5 36.6 427
10 FT. (300 cm)
GALLONS
PER
MINUTE
WITH
3/4-INCH
I.D. HOSE
16
14
2
10
6
4
0 0
00 PSI
7 Kg/cm 2
70 PSI
5 Kg/cm 2
68.1
60.6
53
APPROXIMATE
45.4 LITERS
9 PER
MINUTE
30.3 WITH
22.7 19 mm
I.D. HOSE
15.1
7.6
0
160 180 200 FT. DEPTH
48.8 54.9 61 Meters IN WELL
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
20 40 60
40 PSI
3 Kg/cm 2
80 100 120
100 PSI
7 Kg/cm 2
70 PSI
5 Kg/cm
68.1
60.6
53
APPROXIMATE
45.4 LITERS
PER
37.9
MINUTE
30.3 WITH
227 19mm
I.D. HOSE
15.1
7.6
0
140 160 180 200 FT.
6.1 12.2 18.3 244 30.5 36.6 42.7 48.8 54.9 61 Meters
DEPTH
IN WELL
1 inch (25.4 mm)
Inside Diameter Discharge Hose
(Equivalent to 1.25-Inch O.D.Tubing)
6-INCH (15 cm)
18
16
GALLONS
PER 12
MINUTE 10
WITH
1.25-INCH 8
O.D. TUBING 6
4
2
14
0
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
100 PSI
7 Kg/cm
40 PSI
3 Kg/cm 2
70 P51
5 Kg/cm 2
0
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
0
APPROXIMATE
LITERS
PER
MINUTE
WITH
31.75 mm
O.D. TUBING
20 40 60 80 100 120 140 160 180 200 FT. DEPTH
6.1 12.2 18.3 244 305 366 42748.8 54.9 61 Meters IN WELL
2FT.(60cm)
GALLONS
PER
MINUTE
WITH
1.25-INCH
O.D. TUBING
GALLONS
PER 12
MINUTE
WITH
1.25-INCH
O.D. TUBING
18
16
14
12
10
8
6
4
2
0
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
100 PSI
7 Kg/cm
40 PSI
3 Kg/cm 2
70 P51
5 Kg/cm
0 20 40 60 80 100 120 140 160
6.1 12.2 18.3 244 305 366 42748.8
10 FT. (300 cm)
18
16
14
0
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
APPROXIMATE
LITERS
PER
MINUTE
WITH
31.75 mm
O.D. TUBING
0
180 200 FT.
54.9 61 Meters
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
68.1
60.6
53
45.4
37.9
g 4410114
Kg/cm 2
30.3
6 100 PSI 22.7
q , 15.1 40 PSI
2
0 7.
. 3Kg/ccm2 ,■■■ 5K9Pml ' 06
0 20 40 60 80 100 120 140 160 180 200 FT. DEPTH
6.1 12.2 18.3 24430536642748.854.9 61 Meters 1 IN WELL
DEPTH
IN WELL
IFLOW RATES MAY VARY WITH SITE CONDITIONS. CALL QED FOR TECHNICAL ASSISTANCE.
APPROXIMATE
LITERS
PER
MINUTE
Wrm
31.75 mm
O.D. TUBING
39

V QED
Specifications - Top Inlet, Short
Environmental Systems
STANDARD
CUBIC FEET OF AIR
PER
GALLON PUMPED
(SCF/GAL)
STANDARD
CUBIC FEET OF AIR
PER
GALLON PUMPED
(SCF/GAL)
1.5
14
1.3
1.2
10
.9
8
7
.6
.5
4
Air Consumption
100 PSI
g;cm 2
70 PSI
5 Kg/ m
40 P51
Kgl,t,
12
3/4 inch (19 mm)
71.2 Inside Diameter Discharge Hose
10.5 (Equivalent to 1-Inch O.D. Tubing)
9.7
9.0
8.2
APPROXIMATE
STANDARD
7.5 LITER OF AIR
PER
67 LITER PUMPED
(STD L/LITER)
6.0
5.2
4.5
3.7
30
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
1.6
1.5
14
1.3
1.2
1.0
.9
8
7
.6
.5
4
.3
00 P51
Kg/cm
70 P51
5 Kg/cm
40 PSI
3 Kg .m
2
11.2 1 inch (25.4 mm)
Inside Diameter Discharge Hose
10.5 (Equivalent to 1.25-Inch O.D. Tubing)
9.7
9.0
8.2
APPROXIMATE
STANDARD
75 LITER OF AIR
PER
6.7 LITER PUMPED
(STD L/LITER)
60
5.2
4.5
37
3.0
2.2
.2 1.5
20 40 60 80 100 120 140 160 180 200 F1.
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters
DEPTH
IN WELL
40

VQED Specifications - Low-Drawdown Top Inlet
Environmental Systems
Max. Flow 6.4 gpm (24 Ipm)
0.D. 3.6 in (91 mm)
Length 30.75 in. (78 cm)
Advantages
1. The original automatic air -
powered well pump, proven
worldwide over 23 years
2. The highest flow rates and
deepest pumping capabilities in
the industry in a low drawdown
top -fill pump
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
Description
The Low-Drawdown AP4+ Top Inlet AutoPump provides
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
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 -
obligation 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
of sites worldwide. AutoPumps are designed to handle
difficult pumping challenges that other pumps can't, such
as 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, caps and
accessories to help your installation go smoothly. This
superior pumping heritage, application experience and
support back up every AutoPump you put to work on
your project.
41

V QED
Specifications - Low-Drawdown Top Inlet
Environmental Systems
Pump Dimensions
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
Specifications & Operating Requirements
Model
Liquid Inlet Location
O.D.
Overall Length (Pumps & Fittings)
Weight
Maximum Flow Rate
Pump Volume/Cycle
Minimum Accuation Level
Maximum Depth
Air Pressure
Air Usage
Minimum Liquid Density
Standard Construction Materials'
Pump Body
Pump Ends
Internal Components
Tube & Hose Fittings
Fitting Type
Tube & Hose Options
Tubing Materials'
Sizes - Liquid Discharge
Pump Air Supply
Air Exhaust
Hose Material
Sizes - Liquid Discharge
Pump Air Supply
Air Exhaust
1 Applies to QED supplied tubing;
other tubing sources may not
conform to QED fittings.
4" - Low Drawdown AP4+ Top Inlet
Top
3.6 in. (91 mm)
30.75 in. (78 cm)
9.8 lbs. (4.4 kg)
6.4 gpm (24 Ipm)
0.11 - 0.16 gal (.42 .61 L1
27.4 in. (70 cm)
250 ft. (76 m)
5 - 120 psi (0.4 - 8.4 kg/cm2)
.31- 2.85 scf/gal. (2.2 - 21.5 liter of air /
fluid liter) - See air usage chart
0.7 SpG (0.7 g/cm3)
Fiberglass or Stainless Steel
Stainless Steel
Stainless Steel, Viton, PVDF, Hastelloy-C
Brass or Stainless Steel
Barbs, Quick Connects or Easy Fittings
Nylon
1 in. (25 mm) or 1-1/4 in. (32 mm) 0D
1/2 in. (13 mm) 0D
5/8 in. (16 mm) OD
Nitrile
3/4 in. (19 mm) or 1 in. (25 mm) ID
3/8 in. (9.5 mm) ID
1/2 in. (13 mm) ID
Low-Drawdown AP4+ AutoPumps are warranted for
one (1) year.
42

VQED Specifications - Low-Drawdown Top Inlet
Environmental Systems
3/4 inch (19 mm)
Inside Diameter Discharge Hose
(Equivalent to 1-Inch O.D.Tubing)
6-INCH (15 cm)
GALLONS
PER
MINUTE
WITH
3/4-INCH
I.D. HOSE
9
8
7
6
5
4
3
2
1
0
0
SUBMERGENCE OF PUMP HEAD
I I I I I I I
AIR INLET PRESSURES
I-
100 PSI
7 Kg; cm
4( P5I
70 PSI
-
3 1: ; cm •
- 5 Kg 'cm
1 1
1 1
34.1
30.3
26.5
22.7
18.9
15.1
11.4
7.6
3.8
0
Flow Rates '
APPROXIMATE
LITERS
PER
MINUTE
WITH
19 mm
I.D. HOSE
20 40 60 80 100 120 140 160 180 200 FT. 1 DEPTH
6.1 12.2 18.3 244 30.5 36.6 42.7 48 8 54.9 61 Meters IN WELI
2FT. (60cm)
GALLONS
PER
MINUTE
WITH
3/4-INCH
I.D. HOSE
9
8
7
6
5
4
3
2
1
0
SUBMERGENCE OF PUMP HEAD
I--
AIR
INLET PRESSURES
00Kg PSI
7Kgcm,
- 40 PSI
3 Kg/cm 2
70 P51
��
5 Kg/cm 2
0 20 40 60 80 100 120 140 160
6.1 122 183 244 30.5 36.6 427488
10 FT. (300 cm)
GALLONS
PER
MINUTE
WITH
3/4-INCH
I.D. HOSE
9
8
7
6
5
4
3
2
1
0
0
SUBMERGENCE OF PUMP HEAD
34.1
30.3
26.5
APPROXIMATE
22.7 LITERS
18.9 PER
MINUTE
15.1 WITH
11.4 19mm
I.D. HOSE
7.6
3.8
0
180 200FT. DEPTH
54.9 61 Meters IN WELI
AIR INLET PRESSURES
40 PSI
Kg cm^
100 PSI
70 PSI
Kg; n
34.1
30.3
26.5
22.7
18.9
15.1
11.4
7.6
3.8
0
20 40 60 80 100 120 140 160 180 200 FT. ] DEPTH
6.1 12218324430.536.642.748854.9 61 Meters IN WELL
APPROXIMATE
LITERS
PER
MINUTE
WITH
19 mm
I.D. HOSE
1 inch (25.4 mm)
Inside Diameter Discharge Hose
(Equivalent to 1.25-Inch O.D.Tubing)
6-INCH (15 cm)
GALLONS
PER
MINUTE
WITH
1-INCH
I.D. HOSE
9
8
7
6
5
4
3
2
1
0
SUBMERGENCE OF PUMP HEAD
I I I I I I I
AIR INLET PRESSURES H
0
00 PSI
7 Kg/cm
40 PSI
3 Kg/cm 2
70 PSI
5 Kg/cm 2
34.1
30.3
26.5
22.7
18.9
15.1
11.4
7.6
3.8
0
20 40 60 80 100 120 140 160 180 200 FT. DEPTH
6.1 12.2 18.3 244 30.5 36.6 42.7 488 54.9 61 Meters IN WELL
APPROXIMATE
LITERS
PER
MINUTE
WITH
25.4 mm
I.D. HOSE
2 FT. (60 cm)
GALLONS
PER
MINUTE
WITH
1-INCH
I.D. HOSE
8
7
6
5
4
3
2
1
0
lI
SUBMERGENCE OF PUMP HEAD
H
AIR INLET PRESSURES
\�
100
7Kgcm2
P521
-
40 PSI
Kg cm'
70 PSI
I5IKg/c12
34.1
30.3
26.5
22.7
18.9
15.1
11.4
7.6
3.8
0
APPROXIMATE
LITERS
PER
MINUTE
WITH
25.4 mm
I.D. HOSE
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
10 FT. (300 cm)
GALLONS
PER
MINUTE
WITH
1-INCH
I.D. HOSE
9
8
7
6
5
4
3
2
1
0
0
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES -
100P`_I
40 PSI
3 Kg/cm 2
70 PSI
5 Kg/cm
1 I
20 40 60 80 100 120 140 160 180
6.1 12 2 18.3 24.4 30 5 36 6 42.7 48.8 54.9
'FLOW RATES MAY VARY WITH SITE CONDITIONS. CALL QED FOR TECHNICAL ASSISTANCE.
34.1
30.3
26.5
22.7
18.9
15.1
11.4
7.6
3.8
0
200 FT. DEPTH
61 Meters IN WELL
APPROXIMATE
LITERS
PER
MINUTE
WITH
25.4 mm
I.D. HOSE
43

V QED
Specifications - Low-Drawdown Top Inlet
Environmental Systems
STANDARD
CUBIC FEET OF AIR
PER
GALLON PUMPED
(SCF/GAL)
STANDARD
CUBIC FEET OF AIR
PER
GALLON PUMPED
(SCF/GAL)
2.9
2.8
2.7
2.6
2.5
2.4
2.3
2.2
2.1
2.0
1.9
1.8
1.7
1.6
1.5
1.4
1.3
1.2
1.1
1.0
.9
.8
.7
.6
.5
.4
.3
Air Consumption
100 PSI
7 Kg/cm 2
70 PSI
5 Kg/an
40 PSI
21.7
20.9
20.2
19.4
18.7
18.0
17.2
16.5
15.7
15
14.2
13.5
12.7
12
11.2
10.5
9.7
9.0
8.2
7.5
6.7
6.0
5.2
4.5
3.7
3.0
2.2
3/4 inch (19 mm)
Inside Diameter Discharge Hose
(Equivalent to 1-Inch O.D. Tubing)
APPROXIMATE
STANDARD
LITER OF AIR
PER
LITER PUMPED
(STD L/LITER)
.2 1.5
20 40 60 80 100 120 140 160 180 200 Fr. DEPTH
6.1 12.2 18.3 24.4 30.5 36.6 42.7 48.8 54.9 61 Meters IN WELL
2.9
2.8
2.7
2.6
2.5
2.4
2.3
2.2
2.1
2.0
1.9
1.8
1.7
1.6
1.5
1.4
1.3
1.2
1.1
1.0
.9
.8
.7
.6
.5
.4
.3
1
1 PSI
7 Kg/cm 200
/
70 PSI
5 Kg/cm
'
40 PSI
3 Kg/cmm
21.7
20.9
20.2
19.4
18.7
18.0
17.2
16.5
15.7
15
14.2
13.5
12.7
12
11.2
10.5
9.7
9.0
8.2
7.5
6.7
6.0
5.2
4.5
3.7
3.0
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 IN WELL DEPTH
1 inch (25.4 mm)
Inside Diameter Discharge Hose
(Equivalent to 1.25-Inch O.D. Tubing)
APPROXIMATE
STANDARD
LITER OF AIR
PER
LITER PUMPED
(STD L/LITER)
44

HHP4T
AutoPump®
Top Inlet HammerHead Pro
Max. Flow 9.8 gpm (37.1 Ipm)
O.D. 3.5 in (8.9 cm)
Length 56 in. (142.2 cm)
Advantage
1. Delivers higher flow rates than
all competitive pumps
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
11
Description
The HammerHead Pro HHP4T Top Inlet AutoPump
provides economy and high flow in a top inlet pump for 4"
(100 mm) wells for applications requiring an elevated inlet,
such as pumping total fluids from wells contaminated with
LNAPLs, and delivers flow rates up to 9.8 gpm (37.1 Ipm).
The HHPro 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 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
tubing, hose, connectors, wellhead caps and accessories
to help your installation go smoothly. This superior
pumping heritage, application experience and support
back up every AutoPump you put to work on your project.
QED
hrwmnental%stem5
38 -

AutoPump®
Top Inlet HammerHead Pro
Pump Dimensions
Application Limits
The HHP4T Top Inlet HammerHead Pro AutoPump
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
HHP4T
Specifications & Operating Requirements
Model
Liquid Inlet Location
OD
Length Overall (pump & fittings)
Weight
Max. Flow Rate
Pump Volume / Cycle
Standard Model
Max. Depth
Air Pressure Range
Min. Actuation Level
Air Usage
Min. Liquid Density
Standard Construction Materials
Pump Body
Pump Ends
Internal Components
Tube & Hose Fittings
Fitting Type
Tube & Hose Options
Tubing Material
Sizes' - Liquid Discharge
Pump Air Supply
Air Exhaust
Hose Material
Sizes - Liquid Discharge
Pump Air Supply
Air Exhaust
'Applies to QED supplied tubing;
other tubing sources may not
conform to QED fittings.
4" HammerHead Pro Top Inlet
Top
3.5 in. (8.9 cm) 0D
56 in. (142.2 cm) 0D
16.5 lbs. (7.5 kg)
9.8 gpm (37.1 Ipm) - See Flow rate chart
0.58 - 0.66 gal (2.2 - 2.5L )
250 ft. (76 m)
5 - 120 psi (0.35 - 8.4kg/cm2)
53 in. (134.6 cm)
0.34-1.13 scf / gal.
(2.24-8.23 liters of air / fluid liter)
See air usage chart
0.7 SpG (0.7 g/cm3)
Fiberglass
Stainless Steel, Brass, Acetal
Stainless Steel, Viton
Brass
Barb or Quick Connect
Nylon
1 in. (25 mm) or 1-1/4 in. (32 mm) OD
1/2 in. (12 mm) 0D
5/8 in. (16 mm) OD
Nitrile
3/4 in. (19 mm) or 1 in. (25 mm) ID
3/8 in. (9 mm) ID
1/2 in. (12 mm) ID
HammerHead Pro Pumps are warranted for three (3)
years: 100% materials and workmanship.
P.O. Box 3726 Ann Arbor, MI 48106-3726 USA 1.800.624.2026 F 1.734.995.1170 [e-mail]
www.qedenv.com
39

HHP4T
AutoPum p°
Top Inlet HammerHead Pro
1.00 inch (25.4 mm) 0.D.
Fluid Discharge Tubing
(Equivalent to 3/4-inch. (19 mm) Hose)
6-INCH (15 cm)
18
16
GALLONS
PER 12
MINUTE 10
WITH
1-INCH 8
O.D. TUBING 6
14
4
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
2 40 PSI`
3 Kg/cm
0
0 20 40 60 80 100 120 140 160
6.1 12.2 18.3 24.4 30.5 36.6 42 7 48.8
100 PSI
Kg/cm
2 FT. (60 cm)
GALLONS
PER
MINUTE
WITH
1-INCH
0.D. TUBING
GALLONS
PER 12
MINUTE 10
WITH
1-INCH 8
0.D. TUBING 6
4
2
0
0
18
16
14
12
10
8
6
4
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
Flow Rates'
APPROXIMATE
LITERS
PER
MINUTE
WITH
25.4 mm
O.D. TUBING
0
180 200 FT. I DEPTH
549 61 Meters J IN WELL
SUBMERGENCE OF PUMP HEAD
2 -
0
0 20
6.1
AIR INLET PRESSURES
40 P51
Kg/cm 2
00 PSI
\ ` 70 PSI
5 Kg/cm 2
40 60 80 100 120 140 160
12.2 18.3 244 30 5 36 6 42 7 48.8
10 FT. (300 cm)
18
16
14
70 PS
5 Kg/cm 2
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
0
180 200 FT. DEPTH
54.9 61 Meters IN WELL
APPROXIMATE
LITERS
PER
MINUTE
WITH
25.4 mm
0.D. TUBING
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
100 PSI
7 Kg/cm
20
6.1
40 PSI
3 Kg 'cm
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
7.6
0
40 60 80 100 120 140 160 180 200 FT. -1 DEPTH
12.2 18.3 24 4 30.5 36 6 42.7 48.8 54.9 61 Meters IN WELL
APPROXIMATE
LITERS
PER
MINUTE
WITH
25.4 mm
0.D. TUBING
70 PSI
5 Kg/cm 2
1.25 inch (32 mm) 0.D.
Fluid Discharge Tubing
(Equivalent to 1- inch. (25.4 mm) Hose)
6-INCH (15 cm)
18
16
GALLONS
PER 12
MINUTE 10
WITH
1.25-INCH 8
O.D. TUBING 6
14
4
2
0
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSUF1 5
100 PSI
7 Kg/cm 2
40 PSI
70 PSI
3 Kg/cm 2 5 Kg/cm 2 0
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
-2 7.6
0
APPROXIMATE
LITERS
PER
MINUTE
WITH
31.75 mm
O.D. TUBING
20 40 60 80 100 120 140 160 180 200 FT.
6.1 12.2 18.3 244 305 366 42748.8 54.9 61 Meters
2FT.(60cm)
GALLONS
PER
MINUTE
WITH
1.25-INCH
0.D. TUBING
18
16
14
12
10
8
6
4
SUBMERGENCE OF PUMP HEAD
AIR INLET PRESSURES
2 -
0
0
20
6.1
100 PSI
Kg/cm 2
68.1
60.6
53
45.4
37.9
30.3
22.7
15.1
- 7.6
0
40 60 80 100 120 140 160 180 200 FT. DEPTH
12.2 18.3 24430536642748.8 54.9 61 Meters IN WELL
DEPTH
IN WELL
APPROXIMATE
LITERS
PER
MINUTE
WITH
31.75 mm
O.D. TUBING
10 FT. (300 cm
18
16
70 PSI
5 Kg/cm 2
SUBMERGENCE OF PUMP HEAD
68.1
60.6
GALLONS 14 AIR INLET PRESSURES 53 APPROXIMATE
PER 12 45.4 LITERS
MINUTE 10 37.9 PER
WITH MINUTE
1.25-INCH 8 30.3 WITH
0.D.TUBING 6 100I St 22.7 31.75mm
7 Kgcm O.D. TUBING
4 15.1
2 - 40 PSI 70 PSI - 7.6
0 3 Kg/cm e 5 Kg..cm' _ 0
0 20 40 60 80 100 120 140 160 180 200 FT. 1 DEPTH
6.1 12.2 18.3 24.4 30536642748.8 54.9 61 Meters IN WELL
' FLOW RATES MAY VARY WITH SITE CONDITIONS. CALL QED FOR TECHNICAL ASSISTANCE.
QED
rnrwonnem.l System,
40

AutoPu m p®
Top Inlet HammerHead Pro
STANDARD
CUBIC FEET OF AIR
PER
GALLON PUMPED
(SCF/GAL)
STANDARD
CUBIC FEET OF AIR
PER
GALLON PUMPED
(SCF/GAL)
1.6
1.5
1.4
1.3
1.2
1.0
.9
8
.7
.6
.5
.4
.2
20
6.1
Air Consumption
t00 PS
1.6
1.5
1.4
1.3
1.2
1.0
.9
.8
.7
.6
.5
.4
.3
40 60 80 100 120 140 160
12.2 18.3 24.4 30.5 36.6 42.7 48.8
12
HHP4T
1.00 inch (25.4 mm) O.D.
11.2 Fluid Discharge Tubing
(Equivalent to 3/4-inch.
10.5 (19 mm) Hose)
9.7
9.0
8.2
APPROXIMATE
STANDARD
7.5 LITER OF AIR
PER
6.7 LITER PUMPED
(STD ULITER)
6.0
5.2
4.5
3.7
3.0
2.2
1.5
180 200 FT.
54.9 61 Meters 1 DEPTH
IN WELL
100 Pi!
71,g.m7
12
11.2
10.5
9.7
9.0
8.2
1.25 inch (32 mm) 0.D.
Fluid Discharge Tubing
(Equivalent to 1- inch.
(25.4 mm) Hose)
APPROXIMATE
STANDARD
7.5 LITER OF AIR
PER
6.7 LITER PUMPED
(STD L/LITER)
6.0
5.2
4.5
3.7
3.0
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
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 L 0IIL l ILb
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,
liti.O;Atet
Kerry K. McGee
Project Manager
Page 1 of 16 J

1 dUIC VI I.UI ILt l It
Table of Contents
Sample Summary 3
Case Narrative 4
Sample Results 5
18C 1284-01 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 2 of 16

ANALYTICAL LABORATORY
0
con•itest®
1 dUle UI VUIItCI ILJ
S&ME, Inc - Arden, NC
44 Buck Shoals Road C-3
Arden, NC 28704
ATTN: Bradley Keyse
39 Spruce Street * East Longmeadow, MA 01028 * FAX [phone] * TEL. [phone]
PURCHASE ORDER NUMBER:
PROJECT NUMBER: 4305-17-109H
ANALYTICAL SUMMARY
REPORT DATE: 4/9/2018
WORK ORDER NUMBER:
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 #
I8C1284
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 dUIC UI l,UIlLC11W
con -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 18C 1284-01 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:
18C 1284-01 [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.
The results of analyses reported only relate to samples submitted to the Con -Test Analytical Laboratory for testing.
1 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.
rX/46-141-k---
Lisa A. Worthington
Project Manager
L Page 4 of 16 A

I dUlr UI l,U !Lee Ilb
con-stest®
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
Analyte
Date Date/Time
Results RL DL Units Dilution Flag/Qual Method Prepared Analyzed Analyst
Benzene 46 1.0 0.24 µg/L 2 SM2I-22 6200B 4/5/18 4/6/18 10:38 EEH
1,2-Dichloroethane ND 2.0 0.39 µg/L 2 SM21-22 6200B 4/5/18 4/6/18 10:38 EEH
Ethylbenzene 18 1.0 0.26 µg/L 2 SM21-22 6200B 4/5/18 4/6/18 10:38 EEH
Methyl tert-Butyl Ether (MTBE) ND 1.0 0.18 µg/L 2 SM21-22 6200B 4/5/18 4/6/18 10:38 EEH
Naphthalene 76 10 0.24 µg/L 2 SM21-22 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 µg/L 2 SM21-22 6200B 4/5/18 4/6/18 10:38 EEH
o-Xylene 41 1.0 0.26 µg/L 2 SM21-22 6200B 4/5/18 4/6/18 10:38 EEH
Xylenes (total) 84 3.0 µg/L 2 SM2I-22 6200B 4/5/18 4/6/18 10:38 EEH
Surrogates % Recovery Recovery Limits Flag/Qual
1,2-Dichloroethane-d4
Toluene-d8
4-Bromofluorobenzene
93.2
98.5
98.0
70-130
70-130
70-130
4/6/18 10:38
4/6/18 10:38
4/6/18 10:38
Page 5 of 16

I dUle UI tj0I ILeIItJ
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: 18C1284-01
Samnle Matrix: Ground Water
Analyte
Metals Analyses (Total)
Results RL DL Units Dilution Flag/Qual
Method
Date Date/Time
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 dine VI lrul Ile! Ilw
con -test®
ANALYTICAL LABORATORY
39 Spruce Street * East Longmeadow, MA 01028 * FAX [phone] `TEL. [phone]
Project Location: 125 Hospital Drive, Spruce Pine,
Date Received: 3/30/2018
Field Sample #: Influent
Sample ID: 18C1284-01
Sample Matrix: Ground Water
Sample Description: Work Order: 18C1284
Sampled: 3/29/2018 14:30
Analyte
Conventional Chemistry Parameters by EPA/APHA/SW-846 Methods (Total)
Results RL DL Units Dilution Flag/Qual
Method
Date Date/Time
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

to
ANALYTICAL LABORATORY
COfl tESt®
dUIC UI I,UtIlei Itb
39 Spruce Street * East Longmeadow, MA 01028 * FAX [phone] * TEL. [phone]
Sample Extraction Data
EPA 1664E
Lab Number [Field ID] Batch Initial ImLI Date
18C1284-01 [Influent] B200328 1000 04/06/18
EPA 420.1
Lab Number [Field ID]
Batch Initial ImLI Final [mL1 Date
18C1284-01 [Influent]
B200134 50.0 50.0 04/04/18
SM21-22 2540D
Lab Number [Field ID]
Batch
Initial ImLI Date
18C1284-01 [Influent] B199948 500 04/02/18
Prep Method: SW-846 5030B-SM21-22 6200B
Lab Number [Field ID]
18C1284-01 [Influent]
Batch Initial ImLI Final [mL] Date
B200229 2.5 5.00 04/05/18
Prep Method: SW-846 3005A-SW-846 6010C-D
Lab Number ]Field ID]
Batch Initial ImLI Final ImLI Date
18C1284-01 [Influent] B200353 50.0 50.0 04/06/18
Page 8 of 16

ANALYTICAL LABORATORY
limi)
con -test®
I dUIC UI I.UIILelILS
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
1,2-Dichloroethane
Ethylbenzene
Methyl tert-Butyl Ether (MTBE)
Naphthalene
Toluene
m+p Xylene
o-Xylene
Xylenes (total)
ND
ND
ND
ND
ND
ND
ND
ND
ND
0.50 µg/L
0.50 µg/L
0.50 µg/L
0.50 µg/L
0.50 µg/L
0.50 µg/L
1.0 µg/L
0.50 µg/L
1.5 µg/L
Surrogate: 1,2-Dichloroethane-d4
Surrogate: Toluene-d8
Surrogate: 4-Bromofluorobenzene
LCS (B200229-BSI)
23.1 14/1-• 25.0 92.4 70-130
14.9 µg/L 25.0 99.5 70-130
24.0 µg/L 25.0 96.1 70-130
Prepared & Analyzed: 04/05/18
Benzene 10.1 0.50 µg/L 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
Toluene 9.73 0.50 µg/L 10.0 97.3 70-130
m+p Xylene 20.4 1.0 µg/L 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/L 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 (B200229-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
Toluene 9.63 0.50 µg/L 10.0 96.3 70-130 1.03 25
m+p Xylene 20.0 1.0 Itg/L 20.0 99.8 70-130 2.03 25
o-Xylene 10.0 0.50 µg/L 10.0 100 70-130 0.895 25
Surrogate: 1,2-Dichloroethane-d4
Surrogate: Toluene-dR
Surrogate: 4-Bromofluorobenzene
f
23.8 141- 25.0 95.2 70-130
24.7 1Ig/L 25.0 98.8 70-130
24.4 µg/L 25.0 97.8 70-130
t
Page 9 of 16

I GUIC VI l,0Illel 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-BLKI)
Lead
LCS (B200353-BSI)
Lead
Prepared & Analyzed: 04/06/18
LCS Dup (B200353-BSDI)
Lead
ND 0.010 mg/L
Prepared & Analyzed: 04/06/18
0.501 0.010 mg/L 0.500 100 80-120
Prepared & Analyzed: 04/06/18
0.494 0.010 mg/L 0.500 98.9 80-120 1.44 20
Page 10 of 16

IdUIC VI \-41ILClIL,
con -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
Analyte
Result
Reporting
Limit
Spike Source
Units Level Result %REC
%REC
Limits
RPD
RPD Limit Notes
Batch B199948 - SM21-22 2540D
Blank (B199948-BLK1)
Total Suspended Solids
LCS (B199948-BSI)
Total Suspended Solids
Batch B200134 - EPA 420.1
ND
176
2.5 mg/L
20 mg/L
Prepared & Analyzed: 04/02/18
Prepared & Analyzed: 04/02/18
200 88.0 66.7-117
Blank (B200134-BLK1)
Phenol
LCS (B200134-BSI)
Phenol
LCS Dup (B200134-BSDI)
Phenol
Batch B200328 - EPA 1664B
Prepared: 04/04/18 Analyzed: 04/05/18
ND
0.050 mg/L
Prepared: 04/04/18 Analyzed: 04/05/18
0.53 0.050 mg/L 0.500
107 71.1-117
Prepared: 04/04/18 Analyzed: 04/05/18
0.55 0.050 mg/L 0.500 110 71.1-117 2.81 9.35
Blank (B200328-BLK1)
Oil & Grease (HEM)
Blank (B200328-BLK2)
Oil & Grease (HEM)
LCS (B200328-BSI)
Prepared & Analyzed: 04/06/18
ND
1.4 mg/L
ND
28 mg/L
Prepared & Analyzed: 04/06/18
Prepared & Analyzed: 04/06/18
Oil & Grease (HEM)
LCS (B200328-BS2)
16
Oil & Grease (HEM)
mg/L 20.0
79.0 78-114
Prepared & Analyzed: 04/06/18
380 mg/L 400 94.0 78-114
Page 11 of 16

dune UI lrurltelltb
conotest®
ANALYTICAL LABORATORY
39 Spruce Street * East Longmeadow, MA 01028 * FAX [phone] * TEL. [phone]
FLAG/QUALIFIER SUMMARY
• QC result is outside of established limits.
fi 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.
r Page 12 of 16

I dUIC UI L 0I ttC1Ilb
con -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)
EPA 420.1 in Water
CT,MA,NH,NY,RI,NC,ME,VA
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
AII-IA 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
N 1-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

lEcobL
http://www.contestlabs.com Doc # 379 Rev 1_03242017
can_ tEst'
ANALYTCM
Company Name:
Address:
Phone:
Project Name:
Project Location:
Project Number:
Phone: [phone]
Fax: [phone]
Email: infoicontesttabs.com
S&ME, Inc. - Asheville
44 Buck Shoals Road, C-3, Arden, NC 28704
CHAIN OF CUSTODY RECORD (North Carolina)
Requested Turnaround Time
7-Day
Due Date:
10-Day
Rush -Approval Required
828-483-3013
TF-3659 Blue Ridge Hospital - Spruce Pine
1-Day ❑ 3-Day ❑
2-Day ❑ 4-Day ❑
125 Hospital Drive, Spruce Pine, NC
4305-17-109H
Project Manager:
Bradley Keyse
Con -Test Quote Name/Number:
Invoice Recipient:
Sampled By:
Con -Test
'Work Oitler#
Gary Simcox
Client Sample iD ',Description
Influent
Beginning
Date/Time`
3/29/2018
Data Delivery
Format: PDF Q EXCEL
Other:
CLP Like Data Pkg Required: ❑
Email To: bkeyse a(�smeinc.com
Fax To #:
1430
x
GW
U
39 Spruce Street
East Longmeadow, MA 01028
Page 1_ of _1
2
1
H
X
U N
N
A
H
P
# of Containers
2 Preservation Code
Container Code
X
X
ANALYSIS REQI IFSTED
X
X
❑ Field Filtered
❑ Lab to Fitter
Orthophosphate Samples
❑ Field Filtered
❑ Lab to Filter
Comments:
Relinquished by: (signature) Zii
Received by: (s'gnature)
Relinq'Iah - . by: ignatu )
'J,-1`-j
Date/Time:
3/29/18 2130
Date/Time:
vl, /c672;•
Date/Time:
,3/3%
Please use the following codes to indicate possible sample concentration
within the Conc Code column above:
H - High; M - Medium; L - Low; C - Clean; U - Unknown
North Carolina Detection Limit Requirements
GWPC
Lf SWSL
U
IHSB
❑ MSCC
v
co nquished by: (signature)
rn
77/
3 .3 -C Date/Time:
��31II81CL)
D to/Time:
eived by: (signature)
Date/Time:
Other:
Project Entity
❑ Government 0 Municipality
❑ Federal ❑ Brownfield
❑ City ❑ School
Program Information
❑ DSCA 0 UST/Trust Fund
❑ SWS Landfill ❑ REC
❑ IHSB Orphaned Landfill
• State Lead
❑ Other:
Other
❑ Chromatogram
❑ AIHA-L4P,LLC
' Matrix Codes:
GW = Ground Water
WW = Waste Water
OW = Drinking Water
A=Air
5=Soil
SL = Sludge
SOL = Solid
0 = Other (please
define)
2 Preservation Codes:
I = Iced
H = HCL
M = Methanol
N = Nitric Acid
S = Sulfuric Acid
B = Sodium Bisulfate
X = Sodium Hydroxide
T = Sodium
Thiosulfate
0 = Other (please
define)
3 Container Codes:
A = Amber Glass
G = Glass
P = Plastic
ST = Sterile
V = Vial
5 = Summa Canister
T = Tedlar Bag
0 = Other (please
define)
PCB ONLY
❑ Soxhlet
❑ Non Soxhlet
c1II 1Iin'N 10 I11PI

3/31/2018 Track your package or shipment with FedEx Tracking
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I dUIC UI lAJIIICI IW
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771882256414
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x3Pad )ISV
FedEx Compatible
https://www.fedex.comlapps/tedextracknaction=track&tracknumbers=771882256414&locale=en_US&cntry_code=us
Page 15 of 16

I clUIC UI I.VI IICIIIJ
Is COC in ink/ Legible? j
Did COC include all Client
pertinent Information? Project
Are Sample labels filled out and legible?
Are there Lab to Filters?
Are there Rushes?
Are there Short Holds?
Is there enough Volume?
Is there Headspace where applicable?
Proper Media/Containers Used?
Were trip blanks received?
Do all samples have the proper pH?
1111111411 ANALYTICAL LA13ID UID Ft Y
con aim tEstci°
Doc# :211: Rev:5 2 17
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
Received By
How were the samples In Cooler
received?
Were samples within
Direct from Sampling
Date
No Cooler
t hE>
By Gun # L5 1
Time
On Ice
Ambient
Actual Temp -
No Ice
Melted Ice
Temperature? 2-6°C By Blank # Actual Temp -
Was Custody Seal Intact? Were Samples Tampered with? } .�
Was COC Relinquished ? Does Chain Agree With Samples? 1
Are there broken/leaking/loose caps on any samples?
Were samples received within holding time? -T
1 Analysis -7 Sampler Name
ID's Collection Dates/Times -- -
Acid
Who was notified?
Who was notified?
Who was notified?
MS/MSD?
Is splitting samples required?
On COC? '�--
Base
._
Unp-
1 Liter Amb.
1 Liter Plastic
16 oz Amb.
HCL-
lc_
500 mL Amb.
t
500 mL Plastic
1
8oz Amb/Clear
Meoh-
250 mL Amb.
250 mL Plastic
1
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
Unp-
1 Liter Amb.
1 Liter Plastic
16 oz Amb.
HCL-
500 mL Amb.
500 mL Plastic
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
Comments:
Iv
Page 16 of 16

Appendix V - Oil/Water Separator Specifications

DYNA-PAK
I - OIL/WATER SEPARATORS
For the Removal of Both Dispersed Oils & Settleable Solids
MASTERING THE ART OF OIL/WATER SEPARATION

HYDRO-FLO'S
Dyna-Pak oil/water
separators provide
maximum efficiency and
higher capacities in a
compact, cost effective
package.
BASIC CONCEPTS
The basic concept used by most
manufacturers' of gravity type oil water
separators is that materials of -different
specific gravities will rise and settle at
predictable rates. By using the basic
formulas, as outlined in Stokes Law, we
can predict the retention time necessary to
separate oil of any specific gravity and
droplet size, from any given waste stream at
the desired flow race. The problem is that a
separator based solely on retention time
cannot effectively separate oil particles
smaller than 150 microns, and if they could
they would be prohibitively large.
By placing certain materials in the waste
stream, the efficiencies of oil/water separa-
tion can be greatly improved due mainly to
WITH DYNA-PAK
COALESCING
MEDIA
WITHOUT DYNA-PAK
COALESCING MEDIA
impingement on their surfaces. As fine oil
droplets impinge upon the plate surfaces
they coalesce, or merge, with previous drop-
lets to produce much larger droplets. There
they continue to grow in size until they are
large enough to break free and rapidly rise
to the surface where they are skimmed or
decanted. This coalescing action allows
removal of smaller droplets than is possible
with a standard gravity separator.
The effectiveness of any coalescing media
is governed by several critical variables,
shape, density, available surface area,
velocity and direction
of flow, material of
construction, and solids
handling capabilities. At Hydro -
Flo we use a proprietary Dyna-Pak
cross corrugated coalescing media.
The Dyna-Pak media was designed with
consideration of all these factors. The
specific shape and spacing of the Dyna-Pak
plates provides greater coalescing
performance than any other media available,
while also assuring maximum protection
from blinding. The Dyna-Pak media is
molded of ahighly oleophilic (oil attracting)
material which greatly enhances our oil -
water separation capabilities.
OPERATION
INFLUENT DIFFUSION
CHAMBER:
Flow enters the inlet chamber where it is
evenly dispersed through a non -clog dif-
fuser across the width and depth of the
Dyna-Pak. Large solids fall out of suspen-
sion here before entering the separation
chamber.
SEPARATION CHAMBER:
The separation chamber is filled with the
Dyna-Pak coalescing media. The pack cre-
ates a uniform cross -sectional resistance
which further helps disperse the flow
throughout the separation chamber. The
sinuosidial flow of wastewater through the
pack serves to promote intimate contact
between the oil droplets and the plate sur-
faces. The coalesced oil has the least re- _
stricted path to exit the waste stream, and
slides to the top of the pack on the surfaces
of the
plates. Solids
entering the pack
encounter a 60 degree
angle of inclination which
is optimum for solids settling.
The solids slide down the plates
gathering both mass and velocity as they
near the bottom of the pack and drop into
the sludge collection chamber.
SLUDGE COLLECTION
CHAMBER:
The sludge collection chamber is located
directly beneath the Dyna-Pak and pro-
vides ample volume for the settled sludge.
The sides of the chamber are sloped at 45
degrees to insure easy and complete re-
moval of the sludge.
OIL REMOVAL:
The separated oil accumulates at the sur-
face of the separation chamber where it
displaces the water, as the oil layer in-
creases, oil automatically spills over an
adjustable oil skimming weir into an inte-
gral oil reservoir where it can either flow by
gravity or be pumped automatically to
remote storage tanks.
EFFLUENT CHAMBER:
The clean water leaving the Dyna-Pakflows
under the oil reservoir and up over the ad-
justable effluent weir, which maintains they
liquid level throughout the separator. As
the clean water passes over the effluent
weir it enters the effluent or clean water
chamber where it can either flow by gravity
or be pumped automatically.

MIXTURE
OF OIL,
WATER
& SOLIDS
SMAr T
DROPLETS
L.
0
LARGE
DROPLETS
OUT
• SOLIDS
VENT
OIL
* Shown with
optional oil
reservior
MAJOR SECTION
MATERIALS OF
CONSTRUCTION:
Standard materials of construction include,
but are not limited to, carbon steel, stainless
steel, PVC, neoprene, schedule 40 pipe,
150# ANSI flanges, and grade 5 stainless
steel fasteners, all water tight weld joints
are double welded and tested either hydro-
statically, magnafluxed, dye -penetrant or
other NDE methods in accordance with
current military specifications.
COATINGS:
Above grade carbon steel tanks have an
exterior surface that is prepared to a SSPC-
SP6, commercial blast, and given one (1)
coat of self priming epoxy paint (6DMT).
A11 steet tanks have an interior surface that
is prepared to a SSPC-SP10, near white
metal blast, and given two (2) coats of coal
tar epoxy (16 DMT). As a standard on all
buried equipment, Hydro -Flo will supply
dielectric insulators and anodes to insure
state-of-the-art corrosion protection for
years of trouble free operation.
AVAILABLE OPTIONS:
❑ Flow control packages
❑ Influent pump package
.Overall effluent oil
content has been
reported
b CLEAN to be up to 60% lower
WATER for parallel plate
systems, with a higher
proportion
of small oil droplets
recovered"
❑ Sludge pump out package
❑ Recovered oil pump out package
❑ Effluent oil content monitor
❑ Heater package for freeze protection
O Hazardous environment upgrades
available
❑ All stainless steel construction
Cl Elevated temperature protection (For
applications over 140 Degrees F.)
❑ Special coating systems for severe
interior/exterior environments
❑ Sludge auger package
❑ Oil drag skimmer package
0 Chemical pre and post treatment for
complex emulsions.
FEATURES:
❑ Sizes from 2 GPM to 3000 GPM
❑ Sludge collection chamber -keep media
maintenance free
O Compact design -takes up less space than
competitive units
O Best possible oil removal without
chemical treatment
❑ Fast and easy installation
O Fast delivery
❑ High quality -we can compare every
aspect of our equipment against any of
the competition
CS
Design & Operation of
Oil -Water Separators
API Publication 421, Feb. 1990
Note: Any reference to
the API is not meant as an
endorsement by the
American Petroleum Institute.
❑ Removes both dispersed oil (down to 10
PPM@ 20 microns) and settleable solids
❑ Custom designs for specialized
applications -no matter what your
requirements are, Hydro -Flo is your best
choice for oily waste solutions
APPLICATIONS:
❑ Automotive Maintenance Facilities
Cl Airports
❑ Bus terminals
❑ Bulk plants
❑ Chemical plants
❑ Cosmetic industry
❑ Electro chemical plants
❑ Fabricated metal plants
❑ Glass factories
❑ Grinding and honing operations
❑ Lens grinding and polishing
❑ Military bases
0 Oil fields & Refineries
❑ Petroleum plants
❑ Pulp and paper mills
❑ Railroad yards
❑ Rolling mill quench oil
❑ Steam cleaning facilities
❑ Textile mills
❑ Tramp oil separation
❑ Truck maintenance terminals
❑ Utility companies
❑ Wire drawing operation
0 Wash racks

Mastering the Art of Oil/water 5eparamia"
DP-2'/STL/1115/0 design info
Designed flow rate = 15 GPM a 7.0 micrnne to 34 GPM a 30 microns
Specific gravity of the wastewaters aqueous phase = 1.0
Specific gravity of the oil phase = . 13'S
Oil droplet removal rate = 10 mg/1 of oil droplets > 20 to 30 microns
Media pack size to be 24"W x 36"D }: 4U"L
Minimum projected surface area = 360 square fer_=t
Minimum coalescing surface area = 720 square feet
Ma;: i mum cross sectional velocity = .37.7. to .76 feet/min
29 to 10 rein
-
Minimum separation chamber retention time -
Minimum sludge chamber capacity = J6 gallons
device for oil removal = Integral oil reservoir with adjustable 0l1
skimming weir
DP--24/STL/1121/0 design ilifo
Designed flow rate = 21 GPM a 20 microns to 47 G1'M a 30 microns
Specific gravity of the wastewaters aqueous phase = 1.0
Specific gravity of the oil phase = .85
011 droplet removal rate = 10 mg/1 of oil droplets > 20 to 30 microns
Media pack size to be 24"W x 36"D x 4©"L
Minimum projected surface area = 504 square feet
Minimum coalescing surface area = 1008 square feet
Maximum cross sectional velocity = .47 to 1.05 feet/mto >inmin
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- s
y w`
DP 4/STL/#34/0 design info
Designed flow rate = 34 GPM a 20 microns to 77 GPM a 30 microns
Specific gravity of the wastewaters aqueous phase = 1.0
Specific gravity of the oil phase = .05
Oil droplet removal rate = 10 mg/1 of of 1 droplets > 20 to 30 micro
Media pack size to be 24"W x 36''D x 48"L
Minimum projected surface area = 016 square feet
Minimum coalescing surface area ==1632 square feet
Maximum cross sectional velocity
Minimum separation chamber retention time = 10 to 7.40 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 Oil/Water Separators
q(7' ri SM' oN st7 : ni CF,' 77. da44bst7Rt7n) I ' oN -n I
Page t#1
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Appendix VI - Shallow Tray Air Stripper Software Output

low profile air strippers
System Performance Estimate
Client and Proposal Information:
Blue Ridge Hospital
125 Hospital Drive
Spruce Pine, NC
S&ME Project 4305-17-109J
Original Design Criteria from 1993
Model 3611 Model 3621
Untreated Influent Effluent Effluent
Contaminant Effluent Target ppmv Lbs/1- ppmv
%removal %removal
Benzene 4600 ppb 185 ppb 7 ppb
Solubility 1,780 ppm ppb 7.96 O.8 8.28
Mwt 78.12 71-43-2 95.99% 99.84%
Toluene 3900 ppb 185 ppb 9 ppb
Solubility 515 ppm ppb 1.07 5.68 0 OF 5.95
Mwt 92.13 108-88-3 95.25% 99.77%
Ethyl Benzene 3400 ppb 118 ppb 4 ppb
Solubility 152 ppm ppb 0.07 4.36 0 07 4.51
Mwt 106.16 100-41-4 96.51% 99.88%
Xylenes 13000 ppb 502 ppb 19 ppb
Solubility 175 ppm ppb 0.25 16.61 0.26 17.25
Mwt 106 1330-20-7 96.14% 99.85%
Naphthalene 4600 ppb 516 ppb 58 ppb
Solubility 30 ppm ppb 0.08 4.49 4.99
Mwt 128.16 91-20-3 88.79% 98.74%
1,2-Dichloroethane 10 ppb 2 ppb <1 ppb
Solubility 550 ppm ppb 0.00 0.01 0.00 0.01
Mwt 98.96 107-06-2 79.23% 95.68%
MTBE 10 pPb 3 ppb 1 ppb
Solubility 43,000 ppm ppb 0.00 0.01 0.00 0.01
Mwt 88.15 1634-04-4 67.08% 89.16%
Series chosen: 3600 3600
Water Flow Rate: 40.0 GPM US 9.1 m3/hr
Air Flow Rate: 900 CFM 1529 m3/hr
Water Temp: 55 °F 12.8 °C
Air Temp: 59 °F 15.0 °C
A/W Ratio: 168 :1 168 :1
Safety Factor: 10% 10 %
Water Discharge Temp. 55.2 °F 12.9 °C
Model 3631
Effluent
Lbs/hr ppmv
%removal
<1 ppb
0.09 8.30
99.99%
<1 ppb
0.08 5.96
99.99%
<1 ppb
0.07 4.51
100.00%
<1 ppb
0.26 17.28
99.99%
6 pp6
0.09 5.05
99.86%
<1 ppb
0.00 0.01
99.10%
<1 ppb
0.00 0.02
96.43%
Model 3641 Model 3651
Effluent Effluent
Lbs/h, ppmv ppmv
%removal %removal
<1 ppb <1 ppb
0.09 8.30 8.30
100.00% 100.00%
<1 ppb <1 ppb
0.08 5.96 0.08 5.96
100.00% 100.00%
<1 ppb <1 ppb
0.07 4.51 0.07 4.51
100.0004 100.00%
<1 ppb <1 ppb
0.26 17.28 0.26 17.28
100.00% 100.00%
<1 ppb <1 ppb
0.09 5.06 0.09 5.06
99.98% 100.00%
<1 ppb <1 ppb
0.00 0.01 0.00 0.01
99.81% 99.96%
<1 ppb <1 ppb
0.00 0.02 0.02
98.83% 99.61%
Model 3661
Effluent
Lbs/hr ppmv
%removal
<1 ppb
0.09 8.30
100.00We
<1 ppb
0.08 5.96
100.00%
<1 ppb
0.07 4.51
100.00%
<1 ppb
0.26 17.28
100.00%
<1 ppb
0.09 5.06
100.00%
<1 ppb
0.00 0.01
99.99%
<1 ppb
0.00 0.02
99.97%
Total ppb 29520 ppb 1512 ppb 99 ppb 9 ppb 1 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
Total 94.6856 99.66% 99.97% 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
0 ppb
0.59 41.In
100.00%

Shal
low p r o f i l e a r r strippers
System Performance Estimate
Client and Proposal Information:
Blue Ridge Hospital
125 Hospital Drive
Spruce Pine, NC
S&ME Project 4305-17-109H
Contaminant
Benzene
Solubility 1,780 ppm
Mwt 78.12 71-43-2
Toluene
Solubility 515 ppm
Mwt 92.13 108-88-3
Ethyl Benzene
Solubility 152 ppm
Mwt 106.16 100-41-4
Xylenes
Solubility 175 ppm
Mwt 106 1330-20-7
Naphthalene
Solubility 30 ppm
Mwt 128.16 91-20-3
1,2-Dichioroethane
Solubility 550 ppm
Mwt 98.96 107-06-2
MTBE
Solubility 43,000 ppm
Mwt 88.15 1634-04-4
SO
Untreated Influent
Effluent Target
Design Based on March 29, 2018
Influent Sample Data
Series chosen:
Water Flow Rate:
Air Flow Rate:
Water Temp:
Air Temp:
A/W Ratio:
Safety Factor:
Water Discharge Temp.
3600 3600
14.0 GPM US 3.2 m3/hr
900 CFM 1529 m3/hr
55°F 12.8°C
59 °F 15.0 °C
481 :1 481 :1
10% 10%
55.6 °F 13.1 °C
Model 3611 Model 3621 Model 3631 Model 3641 Model 3651
Effluent Effluent Effluent Effluent Effluent
...s:nr ppmv Lbs/hr ppmv Lbs/hr ppmv Lbs/h. ppmv ppmv
%removal %removal %removal %removal %removal
46 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
ppb ":0 0.03 0.0C 0.03 0.00 0.03 0.00 0.03 0.03
99.56% 100.00% 100.00% 100.00% 100.00%
13 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
ppb 10 0.01 0.00 0.01 0.00 0.01 0.00 0.01 0.00 0.01
99.42% 100.00% 100.00% 100.00% 100.00%
18 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
ppb 1.00 0.01 0.00 0.01 0.00 0.01 0.00 0.01 0.00 0.01
99.65% 100.00% 100.00% 100.00% 100.00%
84 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
ppb 0.04 0.00 0.04 0.00 0.04 0.00 0.04 0.00 0.04
99.59% 100.00% 100.00% 100.00% 100.00%
76 ppb 4 ppb <1 ppb <1 ppb <1 ppb <1 ppb
ppb 0.00 0.03 0.00 0.03 0.00 0.03 0.00 0.03 0.00 0.03
94.31% 99.68% 99.98% 100.00% 100.00%
1 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
ppb '.n0 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
97.66% 99.95% 100.00% 100.00% 100.00%
1 ppb <1 ppb <1 ppb <1 ppb <1 ppb <1 ppb
ppb n!'- 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
90.84% 99.16% 99.92% 99.99% 100.00%
INDUCED DRAF
Model 3661
Effluent
ppmv
%removal
<1 ppb
0.00 0.03
100.00%
<1 ppb
0.00 0.01
100.00%
<1 ppb
0.00 0.01
100.00%
<1 ppb
0.00 0.04
100.00%
<1 ppb
0.00 0.03
100.00%
<1 ppb
0.00 0.00
100.00%
<1 ppb
0.00
100.00%
Total ppb
Total VOC Lbs/hr - ppmv
Total
239 ppb
5 ppb
0.00 0.11
97.65%
0 ppb
0.00 0.11
99.89%
0 ppb
0.00 0.11
99.99%
0 ppb
0.00 0.11
100.00%
0 ppb
0.00 0.11
100.00%
0 ppb
0.00 0.11
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

Appendix VII — Shallow Tray Air Stripper Specifications

NOV-18-93 THU 15:38
North East Env Prod FAX N0, 16032987063
P, 02
Naphthalene
low profile
System Performance Estimate
Cite. et a 1 141l I.. u, era llu, a_
National Environmental Concentrations have been updated using
modeling based on design in 1993 and
from actual influent concentrations
collected March 30, 2018. Model 3631 is
currently installed at site.
Untreated
Contaminont Influent
Bonzono 4600 ppb
Ethyl Benzene 3400 ppb
KOO ppb
Model 3611
Effluent
Water
Air(lbs/hr)
% removal
378 ppb
0.105596
91.7862%
249 ppb
0.078810
92.6785%
3660 ppb
0.023510
20.4507%
p-Xylene 13000 ppb 905 ppb
0.302508
03.0440%
Teluono 3000 ppb
060 ppb
0.088339
90.5784%
Model 3621
Effluent
Water
Air(Ibs/hr)
removal
32 ppb
0,114250
99.3253%
19 ppb
0.084562
99.4640%
2329 ppb
0.056800
49.3752%
b3 ppb
0.323567
00.5181 %
35 ppb
0.096668
99.1123%
Nluaad, ClItJUW
Water Flow Rate: 50.0 gr .n
Air Flow Rate: 900 cf .1
Writer Temp: 50.0 '
Air temp: 50.0
ANV Ratio: 134 .i cu. ft/ cu. ft
Safety Factor Nc ,e
°del 3621
ffluent
Water
Air(lbs/hr)
removal
/ode) 3641
Effluent
Water
Air(lbs/hr)
% removal
<1 ppb
0.115045
99.9954%
ppb
0.085035
99.9w / 1 %
944 ppb
0.091440
79.4971%
1 ppb
0.325118
00.0077%
1 ppb
0.09751 A
99.9921 %
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%.
This report has been generated by ShalbwTray Modeler software version 1.4.1. This software is designed to assista skilled operator
in predcting the performance of a ShalbwTray air stripping system. The software will accurately predict the system performance
when both the equipment and the software am operated a cordng to the written documentation and standard operation.
North feast 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: 11/1893
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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.(arras HIV uop ut Atunio{Jrt{s r 3o uofoas ssolo :IaAoo sprq uo o70t�d
motor to Liz uonraaE sauaS OOci 3o mwadot sanoa 2u013 uo ozot;d
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1T9z japopir ��Cvc�rzollvgS agfo aapvwuasacdaz sr uol, v. snip nqj
•.IlElo, at{a 017! sajotq
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•aauraJo LiantssaJ old
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atp 3o tpouaJ IJrt3 atp
punolr sJanrn IaIEJ
-010t40 30 auurat:ala asEtid
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•3finn autp{otq ozut
sur3 IaaEm paaraii
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uotzvar atp moos pur
uonrzrEpr{on sazttutseur
aunpo.r} ruajnginl,

Low Profile
he discreet size of a ShallowTray„ air stripper does
-not advertise a contamination site. It is easily
accessed for maintenance and can be installed inside
a building. The system is also ideal as a trailer -
mounted, portable stripper for pump tests, pilot
studies, short-term cleanup, or emergency response.
There is no tower.
Treatment
The ShallowTray process
uses forced draft,
countercurrent air stripping
through baffled aeration
trays to remove volatile
organic compounds
from water.
Contaminated water is
sprayed into the inlet
chamber through a coarse
mist spray nozzle. The
eater flows over a flow
distribution weir and along
the baffled aeration tray.
Air, blown up through
3/16" diameter holes in the
aeration tray, forms a froth
of bubbles generating a
large mass transfer surface
area where the contaminants are volarili7ed. The
necessary contact or residence time to reach
required volatilization is achieved through model
size, addition of trays, and flow rate selection.
Resistant to Fouling
ShallowTray systems are resistant to fouling
problems. Treatment trays have large 3/16" diameter
aeration holes. In addition, the turbulent action of
the froth scours the surfaces of the tray reducing
build-up of oxidized iron.
If, under extreme conditions, oxidized iron
ccumulates or hardness begins to scale up, trays can
The airforms afroth of bubbles approxiinately.
6 inches deep on the aeration tray, generating a
large mass transfer surface area where the
contaminants are volatilized.
Air is blown up through hundreds of diameter
holes in the aeration tray.
be easily cleaned through ports using a washing
wand and pressure washer. Trays can also be easily
removed for a thorough inspection and cleaning.
Full Range Turndown
Not only are ShallowTray systems forgiving of
"surprise" inorganics in the water, they also allow
operation anywhere within the rated flow range. In
fact, as the flow rate is
reduced, performance
increases. Also, as demands
change (stricter effluent
contaminant levels) so can
the ShallowTray system. Its
modular design allows for
the addition of trays which
increase the percent removal
of contaminants.
No Disposal
ShallowTray systems have
no packing or diffusers to
contend with and no costs
associated with GAC
breakthrough, fouling or
disposal and replacement.
System Size
To determine the system
size required for your sire, first identify the flow
rate. This guides you to the ShallowTray Series
needed. As an example, with a flow rate of 30gpm,
select the 2600 Series, which is rated for flows from
1 to 50gpm.
Next, identify the contaminants present and the
removal requirement. Generally, this determines the
number of trays required. However, the graphs in
this brochure should be used as a guideline only.
For a proposal, send us or your representative the
specifications. Request for Quotation -sheets are
available.

ypical 3641 Configuration*
AIR EXHAUST
Ijill,
4 AIR FLOW GAGE
AIR PRESSURE GAGE
AIR PRESSURE SWITCH
�o(t)
4' CLEANOUT PORTS
HANDLES
B' INSPECTION PORT
HIGH LEVEL ALARM FLOAT SWITCH
SAMPLE PORT
PRESSURE GAGE
TEMPERATURE GAGE
FLOW CONTROL VALVE
OUTLET PUMP FLOAT SWITCH
CONTROL
PANEL
000
MAIN
DISC.
BOX
ALARM HORN
AIR INTAKE
0
of
NLET
BLOWER
WATER -LEVEL
SIGHT TUBE $
3
SAMPLE PORT
PRESSURE GAGE
TEMPERATURE GAGE
FLOW METER
Model Pictured: 3631
Options chosen for system pictured:
'EXP Feed and Discharge pumps
gTwo NEMA 7 control panels with
alarm interlocks, motor starters and
intrinsically safe relays for the
ShallowTray system, as well as
EXP controls for two well pumps,
an oil water separator and surge
tank
NEMA 7 main disconnect switch
g Low air pressure alarm switch
1 'High water level. alarm switch
itDischarge pump level switch
t Water pressure gauges
gDigital water flow indicator and
totah7er
Air flow meter
gTemperature gauges
[Line sampling ports
10-5/9 H. OD
� I
12 M.
AERATION TRAY
c=== cm=
12 In.
AERATION TRAY
121n
AERATION TRAY
*In
AERATION TRAY
INLET BLOWER
�1 �c
DRAIN
0 VALVE
HOLDING TANK
C j 1SKID MOUNT FRAME SKID MOUNT FRAME
74 In. I1 5:, in.
FRONT VIEW RIGHT SIDE VIEW
*Use these drawings as a guideline only. Systems are built to your project's specifications.
- i
99 in.
i

flow it min. approx.
Models. rate trays width length height cfm
Ibs.
3611
1-75gpm
1
5'
6'2"
5'3"
900
1240
3621
1-75gpm
2
5'
6'2"
6'3"
900
1440
3631
1-759pm
3
5'
6'2"
73"
900
1640
3641
1-75gpm
4
5'
6'2"
8'3"
900
1840
Scow profile air strippers
I
3600 AERATION TRAY
M E-70
r
TOP vaw
36
Percent Removal vs. Flow Rate
,..-
ua—
TCE
Benzene
s
,
es
�'•. MTBE
.....
3°-
Four Trays
°
IX-
u-
-
�_
TCE '
---ti---`. ---_
Benzene ..-
•,
.,
�_
_
•, i
•
••, MTBE
-
Three Trays
°
..-
LI-
...-
-
e.
�_
.-- TCE
--- _ ..........
�.
......Benzene
-
`•,
•
.` MTBE
-
Two Trays
°
00-
w-
°B
-
TCE
•
'•.- Benzene
-
MTBE
One Tray
° .
)0
,b 4 36 4 4 .b 76 e6 .b 40
Percent of Rated GPM
0. 10 20 30 40 50 60: 75
The graphs represent approximate removal efficiencies. Use the
ShaifowTrayTM modeling program to calculate expected performance.

Appendix VIII — Particulate Filter Specifications

FSI Advanced Design
FSPN-2500 Shown with
Clam Shell Pneumatic
Lid Lifter
FSI Bag Filter Vessels are designed, built and stamped to meet code requirements in our own
ASME code manufacturing facilities. Features like the single -gasket seal, permanent piping and
sturdy perforated metal baskets as standard equipment provide durable and consistent
performance. Positive bag hold down is an integral part of the lid. Our advanced basket design
eliminates the need for under -basket gaskets. Swing -out cover bolts with eyenuts simplify the
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.
Standard Features Options
• Completely cleanable; easy cleaning access • Titanium, Hastelloy B&C, and Alloy 20
• Full ports for unrestricted flow available on request
• Sturdy baskets standard (no gasket required) • Coatings available
• Single gasket lid seal • Heavy duty baskets available
• Positive bag sealing • Additional connections including
• Carbon Steel or 304 SS housing standard; Sanitary Fittings and Socket Weld
316 SS available on request are available
Polyloc snap tight bag seal
Permanent piping
(in -line models available)
Hinged cover and swing -
out bolts with eyenuts
STANDARD FILTER VESSELS
Model No. No. of Bags Bag Size No. Surface Area Surface Area Inlel & Max Flow
Per Baq. Ft ' Pnl Vnsvrl_ Ft. Outlet Size Rate, GPM'
FSPN-20
3
0.5
0.5
1"
25
FSPN-35 1
4
1.0
FSPN-40 1
2.0
FSPN-85 1
FSPN-250 2
FSPN-252 2
FSPN-355 3
2 4.4
2 4.4
2 4.4
2 4.4
1.0
2.0
4.4
8.8
8.8
13.2
45
2"
90
2" 200
400
400
600
FSPN-800 4 2 4.4 17.6 4"-6" 800
FSPN-1000 5 2 4.4 22.0 4"-8" 1000
FSPN-1100 6 2 4.4 26.4 4"-8" 1200
FSPN-1300 7 2 4.4 30.8 6"-8" 1400
FSPN-2000 8 2 4.4 35.2 6"-8" 1600
FSPN-2200 9 2 4.4 39.6 6"-8" 1800
FSPN-2500 10 2 4.4 44.0 6"-8" 2000
FSPN-3000 12 2 4.4 52.8 8"-10" 2400
FSPN-3500 14 2 4.4 61.6 10'-12' 2800
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
4.4 105.6 10"-14" 4800
'Maximum flow rate is based on aqueous flow at 10 PSI AP clean. Inlet and outlet pipe sizes can to changed to meet customer requirements.
STANDARD EASY OPEN LID VESSELS
Madill No. No. of Bags Bag Size. No. Surfarr. Area Surface Area Inlet & Max Flow
Pur Bag, Ft.' Per Vessel, FL Outlet SIN Rale, GPM'
FSPZ-800
FSPZ-1000 5
4
FSPZ-1100 6
FSPZ-1300 7
FSPZ-2000 8
FSPZ-2200 9
FSPZ-2500 10
FSPZ-3000 12
FSPZ-3500 14
FSPZ-4000 16
FSPZ•4200 18
FSPZ-4500 20
FSPZ-4800 22
FSPZ-5000 24
2
2
2
2
2
2
2
2
2
2
4.4
4.4
4.4
4.4
4.4
4.4
17.6
22.0
26.4
30.8
35.2
39.6
800
1000
1200
1400
1600
1800
4.4 44.0 6"-8" 2000
4.4 52.8 8"-10" 2400
4.4 61.6 10"-12' 2800
4.4 70.4 10"-12' 3200
4.4 79.2 10"-14" 3600
4.4 88.0 10"-14" 4000
4.4 96.8 10"-14" 4400
4.4 105.6 10"-14" 4800
'Maximum flow rate is based on aqueous flaw at 1 0I'SI AI' clean. Inlet and outlet pipe sizes can be changed to meet customer requirements.

BFN Vessels: Your Cost Effective Alternative
FSI, the acknowledged leader in liquid bag filtration equipment, is pleased to
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.
Standard Features
• Maximum working pressure BFN 11,12-150 PSI, BFN 13,14-150 and 300 PSI
• Single gasket cover seal
• Gasket materials available include BUNA N, Neoprene EPR, Viton, Viton Teflon
Encapsulated (others on request)
• 304 SS perforated basket for up to 75 PSI differential
• Two inlet/outlet configurations
• Same side inlet/outlet for easy manifolding
• Low pressure drops
• 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"
BFN 13, 14-1", 1 1/4", 1 1/2", 2"
• Permanently piped housing
• Available with extra length legs, evacuation float
Options
• Heavy duty baskets available
• Additional connections including Sanitary Fittings and
Socket Weld are available
• BFNC 11, 12 ASME code versions available
BFN VESSELS
Model No. Nu of Bags Bag Site No. Surface Area Standard Max GPM
Per Bag, Ft.2 Inlet/Outlet
BFN 11
BFN 12
BFN 13
2
3
4.4
0.5
2"
1"
220
25
BFN 14 1
4 1.0 1" 45
'Maranon flow rate is based on aqueous flow at 1.0 PSI AP clean through vessel only without bags installed.
FSPN-3500 Available in standard in -line configuration
(shown) or side outlet. Custom styles available on
request. Features single -gasket seal, easy access
cleaning and sturdy baskets. Uses 14 size 2 filter bags.
Hydraulic lid lifter is recommended on 14 bag vessels
and larger.
FSPN-250 Features single -gasket seal and sturdy
baskets. Uses two size 2 filter bags.
i FSPN•85 Uses one size 2 bag. Our most popular vessel.
Ideal for batch or continuous applications in paint and
resin plants.
FSPN-40 Up to 4" full port that permits non -restricted
flow. Side in, bottom out design shown; other outlet
configurations available. Designed for continuous flow or
small batch operations. Uses one size 1 filter bag. Shown
with optional adjustable legs.
FSPN-35 Miniature single bag filter vessel designed for
continuous flow or small batch operations.
Uses one size 4 bag.
See back cover for ordering information.
INLET/OUTLET CONFIGURATIONS AVAILABLE
STYLE 6
SIDE INSIDE OUt
OFFSET
4
STYLE 2
SIDE IN/BOTTOM OW

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
FSPN-85 304 150 2FLG
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
6
Multi Bag Example
FSPN-2500
4
2 COATED
6
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
1 Model No.
FSPN-20
FSPN-35
FSPN-40
FSPN-85
CS - Carbon Steel
304 - 304 Stainless Steel
316 - 316 Stainless Steel
5 Inlet/Outlet Configuration
1 - Side In/Side Out - Inline
2 - Side In/Bottom Out
6 - Side In/Side Out - Offset
1 - Side In/Side Out - Inline
2 - Side In/Bottom Out
3 - Side In/Bottom Out - 90'
Elbow
3 Pressure Bating
150 - 150 PSI
300 - 300 PSI
XXX - Customer Specified
4 Connection Size and Type
FSPN-20 & FSPN-35
1 NPT
1 '/4 NPT
FSPN-40 & FSPN-85
1 NPT
1'/4 NPT
1 '/2 NP1
2 NP1
2 V2 NPT
3 NPT
1 '/2 NPT
2 NPT
1 FLG
1V4FLG
1'/z FLG
2 FLG
2 '/, FLG
3 FLG
4 FLG
6 Options
CA - Corrosion Allowance
Coated
PS1- Partial Jacket
FS1- Full Jacket
MULTI BAG
s
1 Model No
FSPN-250
FSPN-252
FSPN-355
FSPN-800
FSPN-1000
FSPN-1100
FSPN-1300
FSPN-2000
FSPN-2200
FSPN-2500
FSPN-3000
FSPN-3500
FSPN-4000
FSPN-4200
FSPN-4500
FSPN-4800
FSPN-5000
CS - Carbon Steel
304 - 304 Stainless Steel
316 - 316 Stainless Steel
5 Connection Type
Inline
Side Out
4 Connection Size
3"- 4" FLG
3"- 4" FLG
3"- 6" FLG
4"- 6" FLG
4"- 8" FLG
4"- 8" FLG
6"- 8" FLG
6"- 8" FLG
6"- 8" FLG
8"-10" FLG
8"- 10" FLG
10"-12" FLG
10"- 12" FLG
10"- 14" FLG
10"- 14" FLG
10"- 14" FLG
10"- 14" FLG
100 - 100 PSI
150-150PSI
300 - 300 PSI
XXX - Customer Specified
6 Options
CA - Corrosion Allowance
Coated
PS1 - Partial Jacket
FS1- Full Jacket
Filter Specialists, Inc.
BFN
BFN
11 = (1) f1
12=(1)62
13=(1)63
14=(1)N4
11111111111111111111111
CS -Carbon Steel
304 - 304 Stainless Steel
316 - 316 Stainless Steel
2 Bag Style
P - Polyloc
S Snap Ring
7 Inlet/Outlet Cot ation
2 - Side In/Battom Out
6 - Side In/Side Out - Offset
5 Pressure Rating
150-150PSI
300 - 300 PSI
6 Connection Size and Type
1 NPT
1'/4 NPT
1'/2 NPT
2 NPT
2'/:NPT
3 NPT
1 FLG
1'/4 FLG
1'/i FLG
2 FLG
2'/2FLG
3 FLG
4 FLG
FSI's "comprehensive manufacturing control" philosophy ensures that
we will maintain our status as the industry leader in all phases of the
filter business. For more information, technical consultation or details
about our design capability, contact your FSI representative or our
headquarters in Michigan City. Indiana.
ISO CERTIFIED
TO LEARN MORE ABOUT FILTER SPECIALISTS PRODUCTS, CONTACT ONE OF THE OFFICES OR VISIT OUR WEBSITE AT: http://www.fsifilters.com
USA
FILTER SPECIALISTS, INC.
SHIP: 100 Anchor Road
Michigan City, IN 46360
MAIL: P. 0. Box 735
Michigan City, IN 46361
Phone: [phone]
800-348-3205
Fax: [phone]
Europe
FILTER SPECIALISTS INTERNATIONAL GMBH
Balterweg 3.1
D-65817 Eppstein-Bremthal
Germany
Phone: [phone]
Fax: [phone]
Central America
FSI de MEXICO
S. de R.L. de C.V.
Centeno 119-A
Granjas Esmerelda
Iztapalapa, Mexico D.F. C.P. 09810
Phone: [phone]
Fax: [phone]
South America
FSI SUL AMERICANA INDUSTRIAS
Rua 0neda
671 Bairro Planalto
Sao Bernardo Do Campo
Sao Paulo, Brazil
Cep 09895-280
Phone: [phone]
Fax: [phone]
There are no expressed or implied warranties, including the implied warranty of merchantability and fortes fora particular purpose not specific herein respecting this agreement or the product being sold hereunder or the service provided herein
BFV-015-1001
n."". us+ • 0411 on/0

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
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.

oa
OUT
()tt'1
Threaded
(NPT)
K +.at
Flanged
(1501h. A,N.S.I.)
IN
il(fatirt
n,t,
1l'
B
All dimensions are approximate
'Pt A
B
C D
E
F (.;
1-1 1 J
l
c ,
6 7'
24.7
25.9
7 0
24 7
26.2
; 4
25 7
2.3
14)i-
3
9 4
7 I
24.7
26.5
7.0
24.7
26.5
5.0
26 3
3,1
125r.
1 skid
4
5 a
7.1
24 7
26.6
7 0
24 7
29 1
6.3
26.9
3.8
Nt.
F access
swing bolts
r
Contaminated
Liquid
yt
31655. _
Strainer
Basket
1,88
15
.0-nng
Seal
1, '
t
outla
2
00
00
I'tix
Sift.
A
53
B
6.7
NP1 Style "A"
N tth cuscu'met's elbow
36.2
37.7
3.4 137.2 2.3
3
54
7.1
36.2 38.0 7.0
36.2
39.2
501387 31 1
4
54
7I
36.2 38.1 7.0
362
40.6
6.3 138.9 3.8
125-
Iaia
skid
mot.
Adjustable support legs have 12" bolt circle and a l6" height adjustment.
Housing Operation:
Unfiltered liquid enters the housing above the filter hag or strainer
basket; flows down into the housing: and continues through the
element. Solids are trapped inside the filter bag or grainer and
easily removed when the housing is serviced. Our standard o-ring
seal between the basket and the housing ensures a positive seal to
prevent bypass.
Basket data for Model 88 with flow rates to 220 ► m
I).1,Ii1 „Its odI
( mcltrs I
15
30
I)t.11t1t..Ici
I uichi:S I
67
6.7
(sq It
23
4.4
500
1000
Building a Part Number:
N A
C
15
I lonNow \Iotkl -,
[task!' 51h:I1t1)
('stun Siir till)
C<Hit1 Iglu:
Oullrt Lv:uliult
\ialertal
PSI
1_sx
liia
i
2
I i AhtGt 1
St}•Ik A
Carbon=C
150=15
3
B
304SS=--t
C
316SS=6
SPECIFICATIONS
Housing lid has a 3-bolt swing closure with a vent port. Connections are ( ) inch (NPTXFLG) with a (side inlet and bottom
outictXsidc inlet and side outictXside inlet and 90° bottom outlet). !lousing is supplied with two differential pressure 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 9/64" 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.
0_7rystil QXear itration
Div. Of Geyer's Mfg. & Design, Inc.
9449 S. 550 W. Phone: [phone]
Winamac, IN 46996 Fax: [phone]
[e-mail] web site: KrystilKlear.corn
Distributed by:
94RAM'O
. Pyramid Technologies
467 Forrest Park Cir
AMMO Franklin, TN 37064
615-599-4190

Appendix IX — Carbon Vessel Specifications

cAR O IAIR
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
dechlorization.
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), tetrachloroethene, 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
Molasses Number
Apparent density (dense packing)
Abrasion Number (Ro-Tap)
Moisture Content (as packed)
Mesh Size
900 (minimum)
200 (minimum)
27-31 lbs/ft3
75 (minimum)
2% (maximum)
8x30, 12x40
* Please consult with Carbonair for your specific application.

Call: 1.877.759.8143
CARBONAIR
Home
Equipment Rentals
Equipment for Sale Services
Products for Sale: Liquid Phase Carbon Vessels
About Carbonair Careers
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
Contact Us
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 AWWA,
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 PCI PC3 PC5
Diameter 1' 2' 2'-6"
-0" -0"
Height (feet) 4' 4' 6'-0"
-4"
Bed Area (Square 1.1 2.4 4.9
Feet)
Nominal Flow 10 20 50
Rate (gpm)
Carbon Capacity 90 250 500
(pounds)
Connections 1" 1" 2"
Design Pressure 150 150 90
(psi)
Weight Empty 23 80 780
(pounds)
Weight Loaded 113 330 1280
(pounds)
Operating Weight 290 805 2670
(pounds)
225 650 1900
PC7
3'
6'-0"
7
75
1000
2"
90
980
1980
3670
3230
PC13 PC20 PC28 PC50 PC78
4' 5' 6' 8' 10'
MPC Series Liquid Phase
Carbon Vessels
8' 4" 8'-5" 12'-5" 13'-3" 17'-7" Carbonair's MPC Series Liquid Phase Carbon
Vessels are high quality filters ideal for
12.6 19.5 28 50 78.5 groundwater remediation, particularly in
applications where the vessels must be moved
periodically. All MPC Carbon Vessels are
equipped with lifting eyes and forklift tubes
allowing for easy movement of these vessels on
site or in a facility. They have a lower profile than
the PC Series vessels making them more compact
3„
and easy to ship. MPC Series carbon vessels have
90 75 75 75 75 pressure ratings ranging from 75 PSI to 90 PSI.
100 150
250
300
550
1500 2500 5000 10,000 20,000
2"
4" 6"
6"
1230 1800 3150 8100 10,900
2730 4300 8150 18,100 30,900
6150 9200 17,450 40,600 75,600
4600 7400 14,400 30,520 55,750
LPC Series Liquid Phase
Carbon Vessels

Carbon Adsorber—Liquid Phase
PC 7
12" x 16"
MAN WAY
42"
6" x 8"
—HAND HOLE
42"
36" O.D.
TOP VIEW
Pressure Drop (psi)
Pressure Drop for PC7
10 15 20 25 30 35 40 45 50
Row Rate (gpm)
3" PIPE COUPLING
(CARBON SLURRY IN)
LIFT LUG (2)
2" PIPE FLANGE
(INFLUENT)
45'
91 1/4"
2" PIPE FLANGE
(EFFLUENT)
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
MOTOR PUMPS
TYPE EC
(ALL IRON & CIBF)
TYPE EIOOB
APPLICATIONS
INDUSTRY —Coolant pumps, hot and cold water
circulating pumps, chemical transfer pumps,
booster pumps.
O.E.M.—Circulating, washers, booster, towers and
evaporating condensers, coolants.
FEATURES
■ Compact close coupled design using standard
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.)
Type EC Features:
• Sizes: 1" x 1%" x 5" (EC100) and 11/2" x 2" x 5"
(EC150).
• Double Type 21 Viton, Neoprene or EPR seals
optional.
• Seal Flush, seal quench optional.
Type EIOOB Features:
IN All cast bronze construction.
• Size: 1" x 11/4" x 5"
■ Seal flush optional.
■ Double Type 21 Viton, Neoprene or EPR
seals optional.
ALSO AVAILABLE AS:
with AIR MOTOR DRIVE
(see Bulletin #127)
(ALL BRONZE)
DOUBLE SEAL OPTION
316 STAINLESS STEEL *A -
Equivalent models.
TYPE SC
(see Bulletin #109)

0
PERFORMANCE CURVES
1800 R.P.M.:
(nominal speed)
4.94" Imp. Dia. ' -
EC100-25
& E100-25B
U.S. GALLONS PER MINUTE
Note Datted, show HP required on 1 0 SG liquid. Pumps with e
1800 R.P.M.
' (nominal speed)
4
■
n
•
1
20 ..•r 40 50 60
U.S GALLONS PER MINUTE
DIMENSIONS —in inches:
AG Dimensions based on '/00-115/230 V motors.
AG 1--C Z
PARTS LIST
3
EC100
Al CIBF
A. Impeller
Sizes: 25 0216
33 0218
50 0220
75 0222
100 0224
150 0216
200
300
8. Volute
C Volute Bolts
0 Pipe Plugs (2 rqd
E Bracket
F. Motor Bolts 14 rqd.)
G. Gasket, Synihe'ic Fiber
N. Shaft with Set Screws
J. Slinger
K. Mechanical Seal
Buna T.6A (Standard)
Viton T.6A
Teflon T.9
Neoprene w/NiResist Seat T.6A
E.P.R.T6A
DOUBLE SEAL
Viton T21 2 rqd.)
Neoprene T.21 (2 rqd.)
E.P.R.T.21(2rqd
)
D.S. Seal Cover
D.S. Seal Cover Gasket
Seal Cover Bolls (3 rqd.)
0217
0219
0221
0223
0225
0217
0214
057314 rqd l
0557
0212
0588
13
4e —
EC150
Al CIBF
(Specify Trim)
0231 0258
0231 0258
0231 0258
0231 0258
0180
05703(8 rqd)
1180
0588
0506
0226-1
0522
0538
0539
1150
0675
0383
0985
0984
1023
0973
0974
0256
80
100 tf 1 H ill
EC100 —4'°4' I ' IN .
..: 'III
cr�nn_�nn .-4 r' 1 RIM
•
40 11111111 "�
.:_■.
.■. agia&i,.
U.S. GALLONS PER MINUTE
* Note: E100-75B and EC100-75CIBF impeller diameter is 4.25.
motors (Except EC100-25 E100 258 and EC150models)
90
Model No.
EC150.300 4.94'
EC150-200 75 4.50 '
60''
EC150-150
:3.75"
30
15
_ Imp. Dia.
11
11
th the next
3600 R.P.M.
(nominal speed)
_IIINSPREPISL
.—.L_ n111;; ;no 1 _
0 20 4 r 60 80 100 120 140 160 180
U S. GALLONS PER MINUTE
W
LL
Z
0
Q
W
Approx. ODP
AG Ship Wght. Disch. Suct. CDL X Y Z
EC100 & E100B
Sizes: 25 73A
33 8'/2
50 8%
75
100 93/4
150 10%2
914
34#
35#
36# 1 114 513/16 3'/e 4%6 3%s 1% 2%
39#
43#
49#
EC150-33
EC150-150
EC150-200
EC150-300
8%2 45#
10'/2 57# 1% 2 6 6 3% 5 3%s 13/a 3%
11% 62#
12% 65#
E1008
0217
0219
0221
0223
0225
0217
0215
376(4rgdl
0558
0213
0592
K Double Seal
A K

VI\VIVVI V-2 1111JIMV‘.IIV1'1J
CR, CRN
GB Installation and operating instructions
CD Montage- and Betriebsanleitung
OF Notice d'installation et d'entretien
0 Istruzioni di installazione e funzionamento
�E Instrucciones de instalacidn y funcionamiento
Instrugoes de instalacao e funcionamento
GR O5rwisc cykcrracrraang KOI i1EIToupy1aq
NL Installatie- en bedieningsinstructies
�S Monterings- och driftsinstruktion
SF Asennus- ja kayttoohjeet
DK Monterings- og driftsinstruktion
_................,.__ .
f:rs• ourib rani C® `/ •

Declaration of Conformity
We GRUNDFOS declare under our sole responsibility that the products CR and
CRN, to which this declaration relates, are in conformity with the Council Direc-
tives on the approximation of the laws of the EC Member States relating to
- Machinery (98/37/EC).
Standard used: EN 292.
- Electromagnetic compatibility (89/336/EEC).
Standards used: EN 61 000-6-2 and EN 61 000-6-3.
- Electrical equipment designed for use within certain voltage limits
(73/23/EEC) [95].
Standards used: EN 60 335-1 and EN 60 335-2-51.
Konformitatserklarung
Wir GRUNDFOS erklaren in alleiniger Verantwortung, dab die Produkte CR and
CRN, auf die sich diese Erklarung bezieht, mit den folgenden Richtlinien des
Rates zur Angleichung der Rechtsvorschriften der EG-Mitgliedstaaten iiberein-
stimmen:
- Maschinen (98/37/EG).
Norm, die verwendet wurde: EN 292.
- Elektromagnetische Vertraglichkeit (89/336/EWG).
Normen, die verwendet wurden: EN 61 000-6-2 and EN 61 000-6-3.
- Elektrische Betriebsmittel zur Verwendung innerhalb bestimmter
Spannungsgrenzen (73/23/EWG) [95].
Normen, die verwendet wurden: EN 60 335-1 and EN 60 335-2-51.
Declaration de Conformite
Nous GRUNDFOS declarons sous notre seule responsabilita que les produits
CR et CRN auxquels se Were cette declaration sont conformes aux Directives
du Conseil concernant le rapprochement des legislations des Etats membres CE
relatives a
- Machines (98/37/CE).
Standard utilise: EN 292.
- Compatibilita electromagnetique (89/336/CEE).
Standards utilises: EN 61 000-6-2 et EN 61 000-6-3.
- Materiel electrique destine a employer dans certaines limites de
tension (73/23/CEE) [95].
Standards utilises: EN 60 335-1 et EN 60 335-2-51.
Dichiarazione di Conformity
Noi GRUNDFOS dichiariamo sotto la nostra esclusiva responsabilita the i pro-
dotti CR e CRN, ai quali questa dichiarazione si riferisce, sono conformi alle
Direttive del consiglio concernenti it ravvicinamento delle legislazioni degli Stati
membri CE relative a
- Macchine (98/37/CE).
Standard usato: EN 292.
- Compatibilita elettromagnetica (89/336/CEE).
Standard usati: EN 61 000-6-2 e EN 61 000-6-3.
- Materiale elettrico destinato ad essere utilizzato entro certi limiti di
tensione (73/23/CEE) [95].
Standard usati: EN 60 335-1 e EN 60 335-2-51.
Declaration de Conformidad
Nosotros GRUNDFOS declaramos bajo nuestra unica responsabilidad que los
productos CR y CRN a los cuales se refiere esta declaration son conformes con
las Directives del Consejo relatives a la aproximacion de las legislaciones de los
Estados Miembros de la CE sobre
- Maquinas (98/37/CE).
Norma aplicada: EN 292.
- Compatibilidad elettromagnetica (89/336/CEE).
Normas aplicadas: EN 61 000-6-2 y EN 61 000-6-3.
- Material electrico destinado a utilizarse con determinados limites de tension
(73/23/CEE) [95].
Normas aplicadas: EN 60 335-1 y EN 60 335-2-51.
Declarag3o de Conformidade
Nos GRUNDFOS declaramos sob nossa unica responsabilidade que os produtos
CR e CRN aos quais se refere esta declaragao estao em conformidade com as
Directives do Conselho das Comunidades Europeias relatives a aproximagao das
legislagties dos Estados Membros respeitantes
- Maquinas (98/37/CE).
Norma utilizada: EN 292.
- Compatibilidade electromagnetica (89/336/CEE).
Normas utilizadas: EN 61 000-6-2 e EN 61 000-6-3.
- Material electrico destinado a ser utilizado dentro de certos limites de ten-
sao (73/23/CEE) [95].
Normas utilizadas: EN 60 335-1 e EN 60 335-2-51.
nnAwan Iuppop(Pwanc
Eµeik n GRUNDFOS SnXcbvouµe µe anoKXetaTiKa SIK) mac eu0uvn 6Ti ra
npotdvra CR Kai CRN auµµopq bvovrat µe -my Obnyia Tou Euµ(iouXiou eni
Trig oIyKXiafc TON v6µwv TON Kparwv McXwv Trig EupwnatKrjq Evwang ae
axean µe To
- MnXavrjµara (98/37/EC).
flp6Tuno nou Xpnatµonotrl8nxe: EN 292.
- HhcI rpoµayvn-rix j auµpat6Tnra (89/336/EEC).
flp6Tuna nou XpnatµonotnenKav: EN 61 000-6-2 Kai EN 61 000-6-3.
- HXcKrptxec auaKeuec 0Xeotaaµevec yia Xprjarl evr6S opiaµevwv opiwv
nXeKTpLK1'S Taang (73/23/EEC) [95].
flp6runa nou XpnaiµonoinenKav: EN 60 335-1 Kai EN 60 335-2-51.
Overeen komstigheidsverklaring
Wij GRUNDFOS verklaren geheel onder eigen verantwoordelijkheid dat de pro-
dukten CR en CRN waarop deze verklaring betrekking heeft in overeenstemming
zijn met de Richtlijnen van de Raad inzake de onderlinge aanpassing van de wet-
gevingen van de Lid -Staten betreffende
- Machines (98/37/EG).
Norm: EN 292.
- Elektromagnetische compatibiliteit (89/336/EEG).
Normen: EN 61 000-6-2 en EN 61 000-6-3.
- Elektrisch materiaal bestemd voor gebruik binnen bepaalde spanningsgren-
zen (73/23/EEG) [95].
Normen: EN 60 335-1 en EN 60 335-2-51.
Forsakran om overensstammelse
Vi GRUNDFOS ftirsakrar under ansvar, att produkterna CR och CRN, som
omfattas av denna ftirsakran, ar i overensstammelse med Radets Direktiv om
inbordes narmande till EU-medlemsstaternas lagstiftning, ayseende
- Maskinell utrustning (98/37/EC).
Anvand standard: EN 292.
- Elektromagnetisk kompatibilitet (89/336/EC).
Anvanda standarder: EN 61 000-6-2 och EN 61 000-6-3.
- Elektrisk material aysedd for anvandning inom vissa spanningsgranser
(73/23/EC) [95].
Anvanda standarder: EN 60 335-1 och EN 60 335-2-51.
Vastaavuusvakuutus
Me GRUNDFOS vakuutamme yksin vastuullisesti, etta tuotteet CR ja CRN, jota
tams vakuutus koskee, noudattavat direktiiveja jotka kasittelevat EY:n jasenvalti-
oiden koneellisia laitteita koskevien lakien yhdenmukaisuutta seur.:
- Koneet (98/37/EY).
Kaytetty standardi: EN 292.
- Elektromagneettinen vastaavuus (89/336/EY).
Kaytetyt standardit: EN 61 000-6-2 ja EN 61 000-6-3.
- Maarattyjen janniterajoitusten puitteissa kaytettavat sahktiiset laitteet
(73/23/EY) [95].
Kaytetyt standardit: EN 60 335-1 ja EN 60 335-2-51.
Overensstem m elseserklering
Vi GRUNDFOS erklwrer under ansvar, at produkterne CR og CRN, som denne
erklaering omhandler, er i overensstemmelse med Radets direktiver om indbyr-
des tilne rmelse til EF medlemsstaternes lovgivning om
- Maskiner (98/37/EF).
Anvendt standard: EN 292.
- Elektromagnetisk kompatibilitet (89/336/E0F).
Anvendte standarder: EN 61 000-6-2 og EN 61 000-6-3.
- Elektrisk materiel bestemt til anvendelse inden for visse spa ndingsgrmnser
(73/23/E0F) [95].
Anvendte standarder: EN 60 335-1 og EN 60 335-2-51.
Bjerringbro, 1st September 2003
Jan Strandgaard
Technical Manager

CR, CRN
Installation and Page 4
operating instructions
Montage- and Seite 9 •
Betriebsanleitung
Notice d'installation Page 15 F I
et d'entretien
Istruzioni di installazione Pag. 21 ri
e funzionamento
Instrucciones de instalacion Pag. 26 ' E 1
y funcionamiento
Instrugoes de instalagao Pag. 31 rP
e funcionamento
NM
Oanyicc cyKaraoTaaric XEXiba 37 ■ t3J
Kai AcIToupyiau
Installatie- en Pag. 43 ■ lit
bedieningsinstructies
Monterings- och
driftsinstruktion
Asennus- ja
kayttoohjeet
Sida 48 ' S
ION
Sivu 53 ■ SF
1
Monterings- og Side 58 • ')K 1
driftsinstruktion

CONTENTS
1. Handling
2. Type designation
2.1 Pump key for CR, CRN 2, 4, 8 and 16
3. Applications
4. Technical data
4.1 Ambient temperature
4.2 Liquid temperature
4.3 Maximum permissible operating pressure and liquid
temperature for the shaft seal
Minimum inlet pressure
Maximum inlet pressure
Electrical data
Frequency of starts and stops
Dimensions and weights
Sound level
4.4
4.5
4.6
4.7
4.8
4.9
5. Installation
6. Coupling adjustment
7. Electrical connection
7.1 Frequency converter operation
8. Start-up
9. Maintenance
10. Frost protection
11. Service
12. Fault finding chart
13. Disposal
3. Applications
Page GRUNDFOS multistage in -line centrifugal pumps, types CR and
4 CRN, are designed for a wide range of applications.
4 Pumped liquids
4 Thin, non -explosive liquids, not containing solid particles or fi-
4 bres. The liquid must not attack the pump materials chemically.
4 When pumping liquids with a density and/or viscosity higher than
4 that of water, motors with correspondingly higher outputs must be
4 used, if required.
4
5
5
5
5
5
5
5
6
6
6
7
7
7
8
8
8
Before beginning installation procedures, these in-
stallation and operating instructions should be stud-
ied carefully. The installation and operation should
also be in accordance with local regulations and ac-
cepted codes of good practice.
1. Handling
The motors of the CR, CRN 2, 4, 8 and 16 pumps are
supplied with lifting eyes which must not be used for
lifting the entire pump.
When the entire pump is to be lifted, observe the following:
• CR, CRN 2, 4, 8 and 16 pumps fitted with GRUNDFOS MG
motors should be lifted in the pump head by means of straps
or the like.
• For other motor makes, it is recommended to lift the pump in
the pump head by means of straps.
2. Type designation
2.1 Pump key for CR, CRN 2, 4, 8 and 16
Example
Pump range:
CR, CRN
CR8-30/2-X- X- X -XXXX
Nominal flow rate in m3/h
Number of stages x 10
Number of impellers (is only used if the pump
has fewer impellers than chambers)
Code for pump version
Code for pipework connection
Code for materials
Code for shaft seal and rubber pump parts
CR, CRN
For liquid transfer, circulation and pressure boosting of cold or
hot clean water.
CRN
In systems where all parts in contact with the liquid must be made
of stainless steel, CRN pumps must be used.
4. Technical data
4.1 Ambient temperature
Maximum +40°C.
If the ambient temperature exceeds +40°C, the motor output (P2)
must be reduced, see fig. 1.
Fig. 1
P2
[°%°I
100
90
80
70
60
50
20 25 30 35 40 45 50 55 60 65 70 75 80
t t°c]
1000 2250 3500 m
4.2 Liquid temperature
TMOO 2189 4298
Pump type
Liquid temperature
CR, CRN 2, 4, 8 and 16
-20°C to +120°C
See also fig. A, page 63, which indicates the relationship between
liquid temperature and maximum permissible operating pressure.
Note: The maximum permissible operating pressure and liquid
temperature ranges apply to the pump only.
4.3 Maximum permissible operating pressure and
liquid temperature for the shaft seal
Fig. 2
CR, CRN 2, 4, 8 and 16:
p [bar]
30
25
20
15
10
5
0
AUUE
/AUU
AUUE
i
RUDE
RUUV
AUUE/AUUV
I I
BUBE/BUBV
BUBE
l
-40 -20 0 20 40 60 80 100 120 140 160
t [°C]
TMO1 1922 4500

4.4 Minimum inlet pressure
Fig. 3
4.8 Dimensions and weights
Dimensions: See fig. C, page 65.
Weights: See label on the packing.
HI f
Pb
Hv
NPSH
TMO1 1242 4097
The maximum suction lift "H" in metres head can be calculated as
follows:
H=pbx 10.2-NPSH-Hf-Hv-Hs
Pb
= Barometric pressure in bar.
(Barometric pressure can be set to 1 bar).
In closed systems, pb indicates the system pressure
in bar.
NPSH = Net Positive Suction Head in metres head
(to be read from the NPSH curve on page 69 at the
highest flow the pump will be delivering).
Hf = Friction loss in suction pipe in metres head at the
highest flow the pump will be delivering.
Hv = Vapour pressure in metres head, see fig. E on page
66. tm = Liquid temperature.
Hs = Safety margin = minimum 0.5 metres head.
If the calculated "H" is positive, the pump can operate at a suction
lift of maximum "H" metres head.
If the calculated "H" is negative, an inlet pressure of minimum
"H" metres head is required. There must be a pressure equal to
the calculated "H" during operation.
Example:
pb = 1 bar.
Pump type: CR 16, 50 Hz.
Flow rate: 16 m3/h.
NPSH (from page 69): 1.5 metres head.
Hf = 3.0 metres head.
Liquid temperature: +60°C.
Hv (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.
This means that the pump can operate at a suction lift of maxi-
mum 3.1 metres head.
Pressure calculated in bar: 3.1 x 0.0981 = 0.30 bar.
Pressure calculated in kPa: 3.1 x 9.81 = 30.4 kPa.
4.5 Maximum inlet pressure
Figure B, page 64, shows the maximum permissible inlet pres-
sure. However, the actual inlet pressure + pressure when the
pump is running against a closed valve must always be lower
than the "maximum permissible operating pressure".
If the system and the pumps are to be pressure -tested at a pres-
sure higher than that stated in fig. B, page 64, the pump shaft
must be locked to prevent axial movement.
4.6 Electrical data
See motor nameplate.
4.7 Frequency of starts and stops
Motors up to 4 kW: Maximum 100 times per hour.
Other motors: Maximum 20 times per hour.
4.9 Sound level
See fig. D, page 66.
5. Installation
The pump can be installed vertically or horizontally, see fig. 4.
Ensure that an adequate supply of cool air reaches the motor
cooling fan. However, the motor must never fall below the hori-
zontal plane.
Fig. 4
i
TMO1 1241 4097
Arrows on the pump base show the direction of flow of liquid
through the pump.
Figure C, page 65, shows the dimensions of the base as well as
the diameter and the position of the foundation bolt holes.
To minimize possible noise from the pump, it is advisable to fit ex-
pansion joints either side of the pump and anti -vibration mount-
ings between foundation and pump.
Port -to -port lengths and pipework connections appear from fig. C,
page 65.
Isolating valves should be fitted either side of the pump to avoid
draining the system if the pump needs to be cleaned, repaired or
replaced.
Install the pipes so that air locks are avoided, especially on the
suction side of the pump. Correct pipework shown in fig. 5.
Fig. 5
TMO1 0900 3997
Pos.
no.
Description Function
1
Expansion Reduces noise and absorbs vibra-
joint tions and expansion.
2
Isolating valve Enables easy service of the
pump.
3
Pipe hanger Supports pipe and absorbs distor-
tion and strain.
Note: The pump must always be protected against backflow by
means of a non -return valve (foot valve).

In the case of installations in which the discharge pipe slopes
downwards away from the pump and there is a risk of siphon ef-
fect and in installations which must be protected against backflow
of unclean liquids, a vacuum valve must be fitted close to the
pump, see fig. 6.
Fig. 6
TMO1 1240 4097
Minimum flows:
Pump type
Liquid temperature
Up to +80°C
+120°C
+80°C +150°C
+120°C (only spe-
cial version)
CR, CRN 2
0.2 m3/h 0.5 m3/h
CR, CRN 4
0.4 m3/h 1.0 m3/h
CR, CRN 8
0.8 m3/h 2.0 m3/h
CR, CRN 16
1.6 m3/h 4.0 m3/h
Note: The pump must never operate against a closed discharge
valve.
6. Coupling adjustment
For adjustment of coupling in CR, CRN 2 and 4, see fig. F,
page 67.
For adjustment of coupling in CR, CRN 8 and 16, see fig. G,
page 68.
7. Electrical connection
The electrical connection should be carried out by an authorized
electrician in accordance with local regulations.
Before removing the terminal box cover and before
any removal/dismantling of the pump, make sure that
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
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.
Three-phase motors must be connected to a motor starter.
The terminal box can be turned to four positions, in 90° steps:
1. If necessary, remove the coupling guards. Do not remove the
coupling.
2. Remove the bolts securing the motor to the pump.
3. Turn the motor to the required position.
4. Replace and tighten the bolts.
5. Replace the coupling guards.
The electrical connection should be carried out as shown in the
diagram inside the terminal box cover.
7.1 Frequency converter operation
Motors supplied by GRUNDFOS:
All three-phase motors supplied by GRUNDFOS can be con-
nected to a frequency converter.
Dependent on the frequency converter type, this may cause in-
creased acoustic noise from the motor. Furthermore, it may
cause the motor to be exposed to detrimental voltage peaks.
Note: GRUNDFOS motors types MG 71 and MG 80 as well as
MG 90 (1.5 kW, 2-pole), all for supply voltages up to and including
440 V (see motor nameplate), must be protected against voltage
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
Note: Do not start the pump until it has been filled with liquid and
vented.
Pay attention to the direction of the vent hole and
take care to ensure that the escaping water does not
cause injury to persons or damage to the motor or
other components.
In hot-water installations, special attention should be
paid to the risk of injury caused by scalding hot water.
Step Action
1
3
4
6
7
TM01 1403 4497
TM01 1404 4497
TMO1 1405 4497
Close the isolating valve on
the discharge side of the
pump and open the isolating
valve on the suction side.
Remove the priming plug from
the pump head and slowly fill
the pump with liquid.
Replace the priming plug and
tighten securely.
See the correct direction of ro-
tation of the pump on the mo-
tor fan cover.
a Start the pump and check the
direction of rotation.
0
TMO1 1407 4497
TM01 1408 4497
TM01 1409 4497
Vent the pump by means of
the vent valve in the pump
head. At the same time, open
the discharge isolating valve a
little.
Continue to vent the pump. At
the same time, open the dis-
charge isolating valve a little
more.
Close the vent valve when a
steady stream of liquid runs
out of it. Completely open the
discharge isolating valve.
CR 2 and 4,
CRN 2, 4, 8 and 16:
For these pumps, it is advisable to open the bypass valve during
start-up. The bypass valve connects the suction and discharge
sides of the pump, thus making the filling procedure easier. When
the operation is stable, the bypass valve can be closed. When
pumping liquids containing air, it is advisable to leave the bypass
valve open.
Fig. 7
TM01 1243 4097
9. Maintenance
Before starting work on the pump, make sure that all
power supplies to the pump have been switched off
and that they cannot be accidentally switched on.
Pump bearings and shaft seal are maintenance -free.
If the pump is to be drained for a long period of inactivity, remove
one of the coupling guards to inject a few drops of silicone oil on
the shaft between the pump head and the coupling. This will pre-
vent the shaft seal faces from sticking.
Motor bearings:
Motors which are not fitted with grease nipples are maintenance -
free.
Motors fitted with grease nipples should be lubricated with a high -
temperature lithium -based grease, see the instructions on the fan
cover.
In the case of seasonal operation (motor is idle for more than
6 months of the year), it is recommended to grease the motor
when the pump is taken out of operation.
10. Frost protection
Pumps which are not being used during periods of frost should be
drained to avoid damage.
Drain the pump by loosening the vent screw in the pump head
and by removing the drain plug from the base.
Care must be taken to ensure that the escaping water
does not cause injury to persons or damage to the
motor or other components.
In hot-water installations, special attention should be
paid to the risk of injury caused by scalding hot water.
Do not tighten the vent screw and replace the drain plug until the
pump is to be used again.
CR 2 and 4,
CRN 2, 4, 8 and 16:
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.

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
Before 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
when started.
a) Supply failure. Connect the electricity supply.
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
tripped out but the
pump does not run.
a) Check 1 a), b), d) and e).
5. Pump capacity not
constant.
a) Pump inlet pressure is too low (cavitation). Check the suction conditions.
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
no water.
a) Suction pipe/pump blocked by impurities. Clean the pump or suction pipe.
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-
wards when switched
off.
a) Leakage in suction pipe. Repair the suction pipe.
b) Foot or non -return valve is defective. Repair the foot or non -return valve.
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-
ance) because of incorrect pump shaft posi-
tion.
Adjust the pump shaft.
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.

Fig. A
GB
CD
CD
CD
0
U
CD
NL
0
SF
DK
Maximum permissible operating pressure:
Max. zulassiger Betriebsdruck:
Pression de fonctionnement maxi autorisee:
Massima pressione di esercizio possibile:
Presi6n maxima de funcionamiento permitida:
Pressoo maxima de funcionamento permissivel:
Mtyiorq en rpsrrrrj nfeari Aerroupyfaq:
Maximaal toelaatbare werkdruk:
Max. tillatet driftstryck:
Suurin sallittu kayttopaine:
Maks. tilladeligt driftstryk:
Frequency Pump type Curve
Frequenz Pumpentyp Kurve
Frequence Type de pompe Courbe
Frequenza Pompa tipo Curva
Frecuencia Tipo de bomba Curva
Frequancia Modelo da bomba Curva
iuxv6Tgra Tunoc avrAfaq KapnuAq
Frequentie Pomptype Curve
Frekvens Pumptyp Kurva
Taajuus Pumpputyyppi Kayra
Frekvens Pumpetype Kurve
50 Hz
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
CR, CRN 8-20/1 4 CR, CRN 8-120 1
CR, CRN 8-140 4 CR, CRN 8-200 3
p [bar]
Jv
32
28
24
3
2 --
20
16
1
12
8
4
0
-40 -20 0 20 40 60
80 100 120 140 160
CR, CRN 16-30/2 4 CR, CRN 16-80 1 t [C]
CR, CRN 16-100 4 CR, CRN 16-160 3
60 Hz
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
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
TMO2 7530 3703

Maximum inlet pressure for CR and CRN:
Max. Zulaufdruck fur CR and CRN:
Pression maximum d'entree pour CR et CRN:
Massima pressione in aspirazione per CR e CRN:
PresiOn maxima de entrada para CR y CRN:
Pressao maxima de admissao CR e CRN:
Ma yioTI) rriear9 eiaobou yia CR Kai CRN:
Maximale inlaatdruk m.b.t. type CR en CRN:
Max. tilloppstryck for CR och CRN:
Suurin tulopaine CR ja CRN:
Maks. tillebstryk for CR og CRN:
50 Hz
60 Hz
CR, CRN 2
CR, CRN 2-20
CR, CRN 2-30 —> CR, CRN 2-110
CR, CRN 2-130 —> CR, CRN 2-260
6 bar
10 bar
15 bar
CR, CRN 2-20 4 CR, CRN 2-60
CR, CRN 2 -70 -3 2-180
10 bar
15 bar
CR, CRN 4
CR, CRN 4-20/1 4 CR, CRN 4-20
CR, CRN 4-30 4 CR, CRN 4-100
CR, CRN 4-120 4 CR, CRN 4-220
6 bar
10 bar
15 bar
CR, CRN 4-20/1 4 CR, CRN 4-20
CR, CRN 4-30 - CR, CRN 4-80/7
CR, CRN 4-80 4 CR, CRN 4-160
6 bar
10 bar
15 bar
CR, CRN 8
CR, CRN 8-20/1 4 CR, CRN 8-60
CR, CRN 8-80 4 CR, CRN 8-200
6 bar
10 bar
CR, CRN 8-20/1 �R, CRN 8-40
CR, CRN 8-50 4 CR, CRN 8-140
6 bar
10 bar
CR, CRN 16
CR, CRN 16-30/2 4 CR, CRN 16-30
CR, CRN 16-40 -3 CR, CRN 16-160
6 bar
10 bar
CR, CRN 16-30/2 4 CR, CRN 16-30
CR, CRN 16-40 4 CR, CRN 16-100
6 bar
10 bar

CRN 16
CR 16
0
7J
z
m
CR 8 200 80 1%
CRN 4
CR 4 160 50 1%
CRN 2
CR 2 160 50 1
261 80 60,3
261 80 60,3
210 50 42,4
210 50 42,4
202 90 51
202 80 51
162 50 32
162 50 32
N
co
0
0
N
261 80 2%
210 50 2
210 50 2
300 90 50
300 90 50
280 80 40
280 80 40
250 75 32
250 75 32
250 75 25
250 75 25
130 199 215 247 14
130 190 215 246 13
130 199 215 247 14
130 190 215 246 13
100 150 180 210 13
100 147 180 210 13
100 150 180 210 13
100 147 180 210 13
3
3
3
3
✓
x
Av
v
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
3
✓
x
r
2
v
✓
x
iiv
3
3
3
3
r
x
z
TMOO 2251 3393
H
TMOO 2252 3393
H
TMOO 2253 3393
H
TMOO 2254 3393
H
TMOO 2255 3393
TMOO 2256 3393
z
z
CI)
v
m
z
0
z
v
z
•6i1

Fig. D
Airborne noise emitted by pumps with motors fitted by GRUNDFOS:
Luftschallemission von Pumpen mit Motoren, die von GRUNDFOS montiert sind:
Bruit aerien emis par les pompes avec moteurs montes par GRUNDFOS:
Rumore aereo emesso da pompe dotate di motori installati da GRUNDFOS:
Nivel de ruido producido por bombas con motores montados por GRUNDFOS:
Ruido emitido pelas electrobombas montadas pela GRUNDFOS:
06pu(3oc rrou sKrT pneTai arov aipa ands avrAfcc epobiaap*vcc pe Krvrlrrjpcc ands Tr) GRUNDFOS:
Geluidsdruk van pompen met een door GRUNDFOS gemonteerde motor:
Ljudtrycksniva frail pumpar med motorer monterade av GRUNDFOS:
Ilmassa kantautuva aani GRUNDFOS'in asentamilla moottoreilla:
Luftbaren stir)] fra pumper med motorer monteret of GRUNDFOS:
Motor
[kW]
50 Hz 60 Hz
LpA
[dB(A)]
LpA
[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
(C) (m)
150ti45
-40
140-35
_30
130-_25
120ti20
110-15
-12
100ti10
6,0
90-
-
-6,0
60 5,0
-4,0
70- 3,0
60-2.0
-1,5
-1,0
40,0,6
-0,6
30ti0,4
20- 02
10-
-0,1
0-
TMOO 3037 3493

CR, CRN 2 and 4
Fig. F
a
VIIares
-A-,...:1,,
%r-,,. IlaSV=.-AP
r.
11.1.1h\
ODr___dd
CD
%titi
TMO1 2642 2198
co
94740 4-4
Ns . I" /14—_=.,..Vio r
Ail
Nk.\-
Q
TMO1 2643 2198
C
1,5
mm
---1-1
j
j
ilk
t
D
...Z1
11411.4j
M6 13 Nm (1,3 kpm)
M8 32 Nm (3,1 kpm)
M10 62 Nm (6,2 kpm)
of O
't,
..:(1,,""----("ww4
libill2
./
1
—
4rd e
3
!iII
��T6
;!!!
*:I-i- -lpill1.5,_.,_,,,
—�
-...ii,
,,,,N
'I.N.I 0,
N
It
/I
N
N
��
'
N

CR, CRN 8 and 16
Fig. G
a
.4\ ______ ,04,..r_s_:- arm tA.��0
II____A.
u, \,.....,... __,._==—._‘.
,. sop, ___ ,-A,_—_,_._..
/i< ...
,T72:41
`° SO)
)'
TMO1 2645 2198
W
0 " :, ..,, A r4 Fir
®�:o�-
0
Vk.
dJ:_i*ff*MEW ''''' -NI,
v,®\ /�
TMO1 2646 2198
C
D
411:10M6
*SIM8
13 Nm 1,3 kpm)
32 Nm (3,1 kpm)
M10 62 Nm (6,2 kpm)
a
11
1 1
*--i&I,
4-
Aft
F. )4.1
100
PI
'-
11 I
1°1
Iiie
1

NPSH
p H
[kPa] [m]
CR 2, CRN 2
80 -
60 -
40 -
20 -
0
9
8
7
6
5
4
3
2
1
0
60 Hz
50 Hz
00 04 08 12 16 20 24 28 32 36 Q m'/h
I I I 1
0 0 0.2 0.4 0.6 0.8
p H
[kPa [m]
2.8
24 -
16
8-
0
2.4
2.0
1.6
1.2
0.8
0.4
0.0
10
CR 4, CRN 4
60 Hz
50 H7
0
1
2 3 4 5 6 7 8 Q [m'/h]
I 1 1 1 1 1 I
0.0 0.4 0.8 1.2 1.6 2.0 2.4 Q [Us]
p H
[kPa] [ml
3.6
32 - 3.2
2.8
24 - 2.4
2.0
16 - 1.6
1.2
8-0.8
0.4
0-0.0
p
(kPa
80-
60 -
40 -
20 -
0
CR 8 CRN 8
11111111111112M
■■■■■■■■■ 50 Hz ■II■■
■■■■■■■■■ ,/■■■
■■■■■■■■■■■MME
■■■■■■■■■■RM■■■
■■■■■■■■ina■■■■■
rasso■■■■■■■■■■■■
O 1 2 3 4 5 6 7 8 9 10 11 12 13 Q [m'/h]
I I I I I I I I I I I I
0.0 0.4 0.8 1.2 1.6 2.0 2.4 2.8 3.2 3.6 Q [I/s]
H
m]
9[
8
7
6
5
4
3
2
0
CR 16, CRN 16
60 Hz
50 Hz
O 2 4 6 8 10 12 14 16 18 20 22 24 Q [m'/h)
1 I 1 I I I I 1
O 1 2 3 4 5 6 7Q [I/s]
TMOO 1625 4597
TMOO 1626 4597
Nameplate on
pump indicates 42
gpm.
TMOO 1627 4597
TMOO 1628 4597

Denmark
GRUNDFOS DK A/S
Poul Due Jensens Vej 7A
DK-8850 Bjerringbro
Tlf.: [phone]
Telefax: [phone]
E-mail: [e-mail]
www.grundfos.com/DK
Argentina
Bombas GRUNDFOS de Argentina S.A.
Ruta Panamericana km. 37.500 Lote 34A
1619 - Garin
Pcia. de Buenos Aires
Phone: [phone]
Telefax: [phone]
Australia
GRUNDFOS Pumps Pty. Ltd.
P.O. Box 2040
Regency Park
South Australia 5942
Phone: [phone]
Telefax: [phone]
Austria
GRUNDFOS Pumpen Vertrieb Ges.m.b.H.
Grundfosstralle 2
A-5082 Gr6dig/Salzburg
Tel.: [phone]
Telefax: [phone]
Belgium
N.V. GRUNDFOS Bellux S.A.
Boomsesteenweg 81-83
B-2630 Aartselaar
Tel.: [phone]
Telecopie: [phone]
Brazil
GRUNDFOS do Brasil Ltda.
Rua Tomazina 106
CEP 83325 - 040
Pinhais - PR
Phone: [phone]
Telefax: [phone]
Canada
GRUNDFOS Canada Inc.
2941 Brighton Road
Oakville, Ontario
L6H 6C9
Phone: [phone]
Telefax: [phone]
China
GRUNDFOS Pumps (Shanghai) Co. Ltd.
22 Floor, Xin Hua Lian Building
755-775 Huai Hai Rd, (M)
Shanghai 200020
PRC
Phone: [phone]
Telefax: [phone]
Czech Republic
GRUNDFOS s.r.o.
Cajkovskeho 21
779 00 Olomouc
Phone: [phone]
Telefax: [phone]
Finland
OY GRUNDFOS Pumput AB
Mestarintie 11
Piispankyla
FIN-01730 Vantaa (Helsinki)
Phone: [phone]
Telefax: [phone]
France
Pompes GRUNDFOS Distribution S.A.
Parc d'Activites de Chesnes
57, rue de Malacombe
F-38290 St. Quentin Fallevier (Lyon)
Tel.: [phone]
Telecopie: [phone]
Germany
GRUNDFOS GMBH
Schluterstr. 33
40699 Erkrath
Tel.: [phone]
Telefax: [phone]
e-mail: [e-mail]
Service in Deutschland:
e-mail: [e-mail]
Greece
GRUNDFOS Hellas A.E.B.E.
20th km. Athinon-Markopoulou Av.
P.O. Box 71
GR-19002 Peania
Phone: [phone]
Telefax: +0030-210-66 46 273
Hong Kong
GRUNDFOS Pumps (Hong Kong) Ltd.
Unit 1, Ground floor
Siu Wai Industrial Centre
29-33 Wing Hong Street &
68 King Lam Street, Cheung Sha Wan
Kowloon
Phone: [phone]
Telefax: [phone]
Hungary
GRUNDFOS Hungaria Kft.
Park u. 8
H-2045 Tor6kbalint,
Phone: [phone]
Telefax: [phone]
India
GRUNDFOS Pumps India Private Limited
Flat A, Ground Floor
61/62 Chamiers Aptmt
Chamiers Road
Chennai 600 028
Phone: [phone]
Telefax: [phone]
Indonesia
PT GRUNDFOS Pompa
JI. Rawa Sumur III, Blok III / CC-1
Kawasan Industri, Pulogadung
Jakarta 13930
Phone: [phone]
Telefax: [phone]/460 6901
Ireland
GRUNDFOS (Ireland) Ltd.
Unit 34, Stillorgan Industrial Park
Blackrock
County Dublin
Phone: [phone]
Telefax: [phone]
Italy
GRUNDFOS Pompe Italia S.r.l.
Via Gran Sasso 4
1-20060 Truccazzano (Milano)
Tel.: [phone]
Telefax: [phone]/95838461
Japan
GRUNDFOS Pumps K.K.
1-2-3, Shin Miyakoda
Hamamatsu City
Shizuoka pref. 431-21
Phone: [phone]
Telefax: [phone]
Korea
GRUNDFOS Pumps Korea Ltd.
6th Floor, Aju Building 679-5
Yeoksam-dong, Kangnam-ku, 135-916
Seoul Korea
Phone: [phone]
Telefax: [phone]
Malaysia
GRUNDFOS Pumps Sdn. Bhd.
7 Jalan Peguam U1/25
Glenmarie Industrial Park
40150 Shah Alam
Selangor
Phone: [phone]
Telefax: [phone]
Mexico
Bombas GRUNDFOS de Mexico S.A. de C.V.
Boulevard TLC No. 15
Parque Industrial Stiva Aeropuerto
Apodaca, N.L. 66600
Mexico
Phone: [phone]
Telefax: [phone]
Netherlands
GRUNDFOS Nederland B.V.
Postbus 104
NL-1380 AC Weesp
Tel.: [phone]
Telefax: [phone]/492299
New Zealand
GRUNDFOS Pumps NZ Ltd.
17 Beatrice Tinsley Crescent
North Harbour Industrial Estate
Albany, Auckland
Phone: [phone]
Telefax: [phone]
Norway
GRUNDFOS Pumper A/S
Stromsveien 344
Postboks 235, Leirdal
N-1011 Oslo
Tlf.: [phone]
Telefax: [phone]
Poland
GRUNDFOS Pompy Sp. z o.o.
ul. Klonowa 23
Baranowo k. Poznania
PL-62-081 Przezmierowo
Phone: [phone]
Telefax: [phone]
Portugal
Bombas GRUNDFOS Portugal, S.A.
Rua Calvet de Magalhaes, 241
Apartado 1079
P-2770-153 Paco de Arcos
Tel.: [phone]
Telefax: [phone]
Russia
000 GRUNDFOS
Shkolnaya 39
RUS-109544 Moscow
Phone: [phone]
Telefax: [phone], [phone]
e-mail: [e-mail]
Singapore
GRUNDFOS (Singapore) Pte. Ltd.
24 Tuas West Road
Jurong Town
Singapore 638381
Phone: [phone]
Telefax: [phone]
Spain
Bombas GRUNDFOS Espana S.A.
Camino de la Fuentecilla, s/n
E-28110 Algete (Madrid)
Tel.: [phone]
Telefax: [phone]
Sweden
GRUNDFOS AB
Box 63, Angeredsvinkeln 9
S-424 22 Angered
Tel.: [phone]
Telefax: [phone]
Switzerland
GRUNDFOS Pumpen AG
Bruggacherstrasse 10
CH-8117 Fallanden/ZH
Tel.: [phone]
Telefax: [phone]
Taiwan
GRUNDFOS Pumps (Taiwan) Ltd.
14, Min -Yu Road
Tunglo Industrial Park
Tunglo, Miao-Li County
Taiwan, R.O.C.
Phone: [phone]
Telefax: [phone]
Thailand
GRUNDFOS (Thailand) Ltd.
947/168 Moo 12, Bangna-Trad Rd., K.M. 3,
Bangna, Phrakanong
Bangkok 10260
Phone: [phone] ... 91
Telefax: [phone] ... 6
Turkey
GRUNDFOS POMPA SAN. ve TIC. LTD. STI
Bulgurlu Caddesi no. 32
TR-81190 (Jskiidar Istanbul
Phone: +90 - 216-4280 306
Telefax: +90 - 216-3279 988
United Arab Emirates
GRUNDFOS Gulf Distribution
P.O. Box 16768
Jebel Ali Free Zone
Dubai
Phone: [phone]
Telefax: [phone]
United Kingdom
GRUNDFOS Pumps Ltd.
Grovebury Road
Leighton Buzzard/Beds. LU7 8TL
Phone:[phone]
Telefax: [phone]
U.S.A.
GRUNDFOS Pumps Corporation
17100 West 118th Terrace
Olathe, Kansas 66061
Phone: [phone]
Telefax: [phone]

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