NCD095458527_20001108_FCX Inc. (Statesville)_FRBCERCLA RA_O & M Manual for the Air Sparging and Soil Vapor Extraction System OU-3 Volume I - Text-OCR

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O&M Manual for the
Air Sparging and
Soil Vapor Extraction System
FCX-Statesville Superfund Site OU3
Statesville, North Carolina
November 2000
Volume I
27-18895.014
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O&M Manual for the
Air Sparging and Soil Vapor Extraction System
FCX-Statesville Superfund Site OU3
Statesville, North Carolina
Volume I
Prepared For:
EL PASO ENERGY CORPORATION
1001 Louisiana Street
Houston, Texas
Prepared By:
BROWN AND CALDWELL
227 French Landing Drive
Nashville, Tennessee 37228
( 615) 255-2288
November 2000
27-18895.014
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Environmental Engineering & Consulting
227 French Landing Drive Suite 500
Nashville, TN 37228-1605
Tel: [phone]
Fax: [phone]
November 8, 2000
Mr. McKenzie Mallary
North Site Management Branch
EPARegion4
Atlanta Federal Center
61 Forsyth Street
Atlanta, GA 30303
RE: O&M Manual for the AS/SVE System
FCX-Statesville Superfund Site OU3, Statesville, North Carolina
Dear Ken:
-
27-18895.014
Enclosed are three copies of Volume I and one copy each of Volumes II, III, and IV of the document entitled "O&M Manual for the Air Sparging and Soil Vapor Extraction System, FCX-Statesville Superfund Site OU3, Statesville, North Carolina". For your convenience, one copy of Volume I is provided unbound.
If you have any questions or comments regarding this document, please call me at [phone] or call Mr. Roger Towe of El Paso at [phone].
Sincerely,
Brown and Caldwell
Kenton H. Oma, P.E.
Assistant Technical Director
Design and Solid Waste
cc: N. Testerman, NCDENR
R. Towe, El Paso
H Mitchell, Jr., Beaunit
M. Garlick, Burlington
N. Prince, ESC
( 1 copy Vols. I, II, III, and IV)
(2 copies Vol. I and 1 copy Vols. II, III, and IV) (1 copy Vol. I)
(1 copy Vol. I)
(1 copy Vol. I)
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VOLUME I
LETTER OF TRANSMITTAL
CONTENTS
LIST OF TABLES
LIST OF FIGURES
1.0 Introduction
CONTENTS
IV
V
1-1
1.1 Background Information............................................................................... 1-2
2.0
3.0
4.0
5.0
6.0
1.1.1 Site Location and Description............................................................ 1-2
1.1.2 Site Conditions.................................................................................. 1-3
1.2
1.3
1.4
Description of Air Sparging/Soil Vapor Extraction System .. . ... . .. . . .. . . ... . . .. . . .. . . 1-3
Responsibilities and Contacts........................................................................ 1-5
Organization of O&M Manual...................................................................... 1-5
System Description and Process Flow ...................................................................... .
Functional Description of AS/SVE System .............................................................. .
3.1 Soil Vapor Extraction (SVE) System Operations ........................................... .
3.2 Air Sparging System Operations ................................................................... .
3.3 SCADA System Operations ......................................................................... .
Operations of System Controls ................................................................................ .
4.1 Main Electrical Disconnect Panel ................................................................. .
4.2 Control Panel CPl000 ................................................................................. .
4.3 Computer Cabinet ....................................................................................... .
4.4 Remote Computer ....................................................................................... .
Operating Procedures .............................................................................................. .
5.1 System Startup
5.1.1 Set Process Valve Positions for Startup ............................................. .
5.1.2 Activate SCADA System (Automatic System Startup) ........................ .
5.1.3 Start AS/SVE Process Equipment (Manual System Startup) ............... .
5.2 System Shutdown ........................................................................................ .
5.2.1 Shutdown AS/SVE Process Equipment (Manual System Shutdown) .. .
5.2.2 Deactivate SCADA System (Automatic System Shutdown) ................ .
5.2.3 dose Selected Process Valves ........................................................... .
System Monitoring and Maintenance ........................................................................ .
2-1
3-1
3-1
3-6
3-8
4-1
4-1
4-1
4-2
4-3
5-1
5-1
5-2
5-3
5-4
5-4
5-4
5-4
6-1
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CONTENTS (continued)
6.1 Health and Safety ........................................................................................ .
6.2 Routine Monitoring of AS/SVE System ....................................................... .
6.3 Maintenance of AS/SVE System .................................................................. .
6.3.1 Routine Calibration of Instrumentation ............................................. .
6.3.2 Particulate Filter Replacement ........................................................... .
6.3.3 GAC Media Replacement ................................................................. .
6.3.4 Other Maintenance .......................................................................... .
7.0 Equipment Specifications ........................................................................................ .
6-1
6-2
6-3
6-3
6-3
6-3
6-4
7-1
7.1
7.2
7.3
7.4
SVE Blowers................................................................................................ 7-1
Heat Exchanger............................................................................................ 7-1
Air Compressor............................................................................................ 7-2
GAC System................................................................................................ 7-2
APPENDICES
VOLUME II
Appendix A. Record Drawings
Drawing 18895-Cl
Drawing 18895-C2
Drawing 18895-Pl
Drawing 18895-P2
Drawing 18895-Ml
Site Plan
Piping and Equipment Layout
Piping and Instrumentation Diagram
Piping and Instrumentation Diagram
Well Construction Details
Appendix B.
AppendixC.
GAC Vessels and Air Compressor Documentation by Carbonair
SVE Blower Package and Heat Exchanger Documentation by J.E. Gasho and
Associates
AppendixD. Overhead Coiling Door Documentation
VOLUME III
Appendix E. SCADA System Documentation by Revere Control Systems
Section A -Equipment Startup and Shutdown Instructions
Section B -Engineer's Manual
Section C -Programmer's Manual
Section D -Equipment Manufacturer's User Manuals
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CONTENTS ( continued)
VOLUME IV
Appendix E. SCADA System Documentation by Revere Control Systems (continued)
Section D -Equipment Manufacturer's User Manuals (continued)
Section E -Drawings
Section F -Loop Diagrams
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LIST OF TABLES
No.
Follows
Page
1-1 Responsibilities and Contact List for the AS/SVE System........................................ 1-5
3-1 SCADASystemTagListfortheAS/SVESystem ................................................... 3-1
5-1 Valve Positions for Operation of the AS/SVE System............................................. 5-1
6-1 Maintenance Schedule for the AS/SVE System....................................................... 6-1
6-2 Summary of Chemical Analyses and Analytical Method References for
Groundwater Sampling........................................................................................... 6-2
6-3 Quality Assurance/Quality Control Samples for Groundwater Sampling Events....... 6-2
6-4 Inspection/Maintenance Documentation Form for the AS/SVE System.................. 6-4
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LIST OF FIGURES
No. Follows
Page
1-1 Site Location Map ... ... ... .. . .. ... .. .. ... .. ..... .. ... .. .. . .. . .. . .. . .. . ... .. . .. . . .. .. . ... . .. ... ... . ... . .. . .. . . . .. . . . 1-2
1-2 Site Layout............................................................................................................. 1-2
2-1 Piping and Equipment Layout................................................................................ 2-1
2-2 Piping and Instrumentation Diagram...................................................................... 2-1
2-3 Piping and Instrumentation Diagram...................................................................... 2-1
5-1 Valve and Piping Layout for GAC Vessels............................................................... 5-1
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1.0 INTRODUCTION
The United States Environmental Protection Agency (USEPA), United States Department
of Justice, Beaunit Corporation, Burlington Industries, Inc., and El Paso Natural Gas d/b/ a
El Paso Energy Corporation (El Paso) have entered into an agreement (Consent Decree) for
the performance of response work at the FCX-Statesville Superfund Site (Site) Operable
Unit 3 (OU3) in Statesville, North Carolina consistent with the National Contingency Plan.
lbis response work includes performance of a Remedial Action (RA) for soil and
groundwater at the Site.
The RA is being performed by El Paso to implement the response actions selected for the
Site. The RA Work Plan Quly 2000) provided a plan of action for completing the RA
activities and presented a discussion of the tasks to be performed, a Project Delivery
Strategy, a Construction Management Plan, and a Construction Quality Assurance Plan
(CQAP). The RA Work Plan addressed the technical requirements of the September 30,
1996 Record of Decision (ROD) issued by the USEPA and incorporated work elements and
deliverables previously specified in the Consent Decree, Statement of Work, and in the
approved Remedial Design (RD) Work Plan.
The RA for the treatment of groundwater and soil contamination at the Site is an arr
sparging/ soil vapor extraction (AS/SVE) system with monitored natural attenuation for
areas down gradient of the AS/SVE system. An observational approach has been
incorporated into the RD and RA for implementation of the AS/SVE system due to the
heterogeneity of the soil at the Site as identified during the Pre-Design Investigation. The
observational approach calls for a Phase I AS/SVE design, construction, and testing and
allows for a Phase II design, construction, and operation at a later time if determined
appropriate. The construction of the Phase I AS/SVE system has been completed and is
documented in the report entitled "Construction Completion Report for the Phase I Air
Sparging and Soil Vapor Extraction System, FCX-Statesville Superfund Site OU3, Statesville,
North Carolina" dated November 2000 by Brown and Caldwell (hereafter referred to as the
Construction Completion Report). If the Phase I AS/SVE system is found to be adequate
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without modification, the system will be operated to address the groundwater and soil
contamination in the source area without the need to implement Phase II.
1bis Operations and Maintenance (O&M) Manual presents the procedures and information
for operating and maintaining the Phase I AS/SVE system.
1.1 BACKGROUND INFORMATION
The following includes a brief description of the Site as well as Site conditions.
1.1.1 Site Location and Description
The OU3 Site is located in Iredell County approximately 1.5 miles west of downtown
Statesville, North Carolina (see Figure 1-1). The Site consists of the soil, groundwater,
sediment, and surface water contamination emanating from the textile plant property
currently owned by Burlington. The property is approximately 15 acres in size. Two large
buildings consisting of a warehouse (approximately 60,000 square feet in size) and a textile
plant building (approximately 275,000 square feet in size) are located on the Burlington
property (see Figure 1-2).
Land immediately surrounding the Site is predominantly industrial with a variety of other
uses ranging from commercial to 'residential with associated school and church facilities.
Farther from the Site, rural land in the Statesville area is used for timber farming, grain crops
farming, and dairy farming.
The Site lies within the geologic belt known as the Blue Ridge-Inner Piedmont Belt, which is
situated in the Inner Piedmont Physiographic Province in western-central North Carolina.
1bis province is characterized as gently rolling slopes. The Blue Ridge-Inner Piedmont Belt
consists of metamorphic rocks including gneisses and schists. These rocks have weathered
to form a relatively thin overburden of saprolite, which is observed throughout the Site.
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! SOURC~ U.S.G.S. TOPOGRAPHIC MAP, STATESVILLE WEST QUADRANGL£, NC
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FIGURE 1 -1
SITE LOCATION MAP
FCX-STATESVILLE SUPERFUNO SITE
STATESVILLE, NORTH CAROUNA
18895.013 2/00
BROWN AND
CALDWELL Nuihrillo, TflD..DttlllllH
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FIGURE 1-2
SITE LAYOUT
I I
ERFUND SITE, OU3 FCX-STATESVILLE SNU6RTH CAROLINA 2/00 STATESVILLE,
18895.013
Nashville. Tennessee
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Groundwater at the Site is observed within the saprolite and underlying bedrock. Saprolite
forms the uppermost hydrogeologic unit. Groundwater occurs within the pore spaces of the
saprolite under water table conditions. Groundwater within the fractured bedrock unit
occurs under unconfined or semi-confined conditions. Site information indicates that the
two units are in hydraulic communication. Groundwater gradients observed on-Site indicate
that groundwater in the saprolite and bedrock appears to be flowing both to the north and
to the south from the textile plant.
1.1.2 Site Conditions
Several media and constituents of interest are associated with OU3. The pnmary
constituents of interest present within OU3 include perchloroethylene (PCE), also called
tetrachloroethene, and other chlorinated hydrocarbons. The groundwater contains primarily
PCE and other volatile organic compounds (VOCs). On-Site soil contains primarily VOCs
and to a lesser extent, inorganics and polynuclear aromatic hydrocarbons (P AHs).
Groundwater and soil contamination are being remediated by AS/SVE with monitored
natural attenuation for areas down gradient of the AS/SVE system. Surface water and
sediment associated with an intermittent stream originating from a seep to the north of the
Burlington textile plant also contain some inorganic constituents, polychlorinated biphenyls
(PCBs), and VOCs; however, it was determined that the constituent concentrations posed
no risk and no remediation is required.
1.2 DESCRIPTION OF AIR SPARGING/SOIL VAPOR EXTRACTION SYSTEM
The AS/SVE process that was installed during the Phase I construction consists of
the following components:
• twenty-five triple-purpose wells
• SVE system
• air sparging system
• Supervisory Control and Data Acquisition System (SCAD A) system_
• security measures.
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While each of the triple-purpose wells has a specific function now, the wells were designed
and constructed so that any of them can be used for SVE, air sparging, monitoring, or any
combination of the three. The above-ground piping and instrumentation have been installed
so that the wells can be used as follows:
• two wells for both air sparging and SVE
• eight wells for SVE
• fifteen wells for monitoring probes.
The SVE system consists of the SVE wells, SVE header piping, a packaged blower system, a
heat exchanger, and two granular activated carbon (GAC) vessels. The piping includes a
6-inch diameter common extraction header and 2-inch diameter connecting pipe branches to
the SVE wells. The SVE header and branch piping are fabricated from high-density
polyethylene (HDPE). The SVE blower system is skid-mounted and includes a liquid
separator, a particulate filter, an inlet filter and silencer for bypass air, and two blowers piped
to operate individually or in parallel. The blowers operate to draw the soil gas out of the
selected SVE wells, through the heat exchanger, and through two GAC vessels that are
operated in series to capture organic vapors before the exhaust gas is discharged to the
atmosphere. The heat exchanger reduces the vapor temperature to about 90°F or less,
which improves the GAC absorptive capacity for the Site volatile organic compounds
(VOCs). The GAC in the vessels can be exchanged when the carbon in one vessel reaches
its adsorptive capacity. The treated air is checked by an in-line gas analyzer and subsequently
exits the carbon vessels and the building through a 6-inch vent pipe that extends above the
roof.
The air sparging system consists of an oil-free air compressor. The air sparging piping
consists of 1-inch HOPE, which is rated for compressed air. The piping runs from the air
compressor to the two air sparging wells. The system forces air into groundwater through
the screened section of the air sparging wells. Solenoid valves located in the air piping to
each of the air sparging wells allow for the sparged air to be injected in pulses at desired
frequencies and durations.
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The SCADA system consists of instrumentation connected to the process piping and
equipment. These instruments provide necessary operation data to a programmable logic
controller (PLC). The controls for the system are housed in two cabinets located in the
same area as the equipment. One cabinet houses the motor starters, PLC, hand switches,
alarm lights and other process electrical components. The other houses a computer that
enables an operator to monitor and control the AS/SVE process. Data acquisition and
system operation can also be accomplished from a remote computer via a modem.
The AS/SVE process equipment and control cabinets are located within an equipment area,
which is secured inside an eight-foot tall chain-link fence with locking gates. The equipment
area is accessible from the outside of the textile plant using a key-operated, overhead coiling
door. The AS/SVE wells and piping are protected by bollards that are set into the concrete
floor or asphalt pavement.
The City of Statesville provides electric service to the AS/SVE system that is independent of
the building's main power. BellSouth provides telephone service using a telephone line from
a terminal outside the building to allow remote access to the SCAD A system via modem.
1.3 RESPONSIBILITIES AND CONTACTS
A list of the responsibilities and contacts for the AS/SVE system is presented in Table 1-1.
1.4 ORGANIZATION OF O&M MANUAL
This O&M manual has been organized into two volumes containing the seven sections and
five appendices The organization is as follows:
Volume I
• Section 1.0 -Introduction
• Section 2.0 -System Description and Process Flow
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Responsibility
Site Holder
System Owner
System Manager
System Monitoring ·
System Maintenance
Process and Effluent Sampling
Waste Disposal
USEP A Remedial Manager
NCDENR Remedial Manager
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Table 1-1. Responsibilities and Contact List for the AS/SVE System
FCX-Statesville Superfund Site OU3
Company/Firm Contact Telephone Number(s)
Burlington Industries Mike Garlick [phone]
Neil Baker [phone]
El Paso Energy Corporation Roger Towe [phone]
Brown and Caldwell Ken Oma [phone]
Jonathan Miller [phone]
Brown and Caldwell Will Raines [phone]
Brown and Caldwell Ken Oma [phone]
Brown and Caldwell Maria Megehee [phone]
Brown and Caldwell Greg Christians [phone]
USEP A Region IV MacKenzie Mallary [phone]
NCDENR Nile Testerman [phone] X 350
Page I of I
October 2000
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• Section 3.0 -
• Section 4.0 -
• Section 5.0 -
• Section 6.0 -
• Section 7.0 -
Volume II
Functional Description of AS/SVE System
Operation of System Controls
Operating Procedures
System Monitoring and Maintenance
Equipment Specifications
• Appendix A -Record Drawings
• Appendix B -GAC Vessels and Air Compressor Documentation by Carbonair
• Appendix C -SVE Blower Package and Heat Exchanger Documentation by
J.E. Gas ho and Associates
• Appendix D -Overhead Coiling Door Documentation
Volume III
• Appendix E -SCAD A System Documentation by Revere Control Systems
Section A -Equipment Startup and Shutdown Instructions
Section B -Engineer's Manual
Section C -Programmer's Manual
Section D -Equipment Manufacturer's User Manuals
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Volume IV
• Appendix E -SCADA System Documentation by Revere Control Systems
(continued)
Section D -Equipment Manufacturer's User Manuals (continued)
Section E -Drawings
Section F -Loop Diagrams
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2.0 SYSTEM DESCRIPTION AND PROCESS FLOW
The AS/SVE system described in this manual is used to remediate VOC-contaminated
groundwater and soil at the FCX-Statesville Superfund Site OU3. Figure 2-1 shows a plan
view of the site with locations of the piping, equipment, wells, and monitoring probes.
Figures 2-2 and 2-3 present a piping and instrumentation diagram for the AS/SVE system.
Appendix A presents full-size record drawings of the piping and equipment layout and the
piping and instrumentation diagram.
The SVE blower package draws the vapors from the SVE wells; which are screened in the
vadose zone, using Ametek Rotron regenerative blowers. The two blowers can be operated
together or one at a time depending on the achievable vapor flow rate from the SVE wells.
The SVE package also includes a moisture separator tank, a particulate filter, silencers on the
discharge of each blower, and a silencer on the bleed-in line. The SVE package pulls vapors
from the extraction wells through the blowers and discharges into the GAC vessels. A heat
exchanger cools the vapor as it passes from the blowers into the GAC vessels.
During air sparging, an air compressor supplies air to the groundwater under the site at the
two sparging well locations. The air is carried through a 1-inch I-IDPE pipe to the well
casings and disperses into the groundwater. The compressor is an oil-free, tank-mounted
model manufactured by Gardner-Denver. The air pressure is controlled by a pressure
regulator located on the discharge line from the compressor and by control valves located on
the air line at each sparging well. Electrically activated solenoid valves are also located on
the air line at each sparging well and allow the air to be injected in pulses that are controlled
by a timing function in the SCAD A system.
There are two GAC vessels, each containing 2000 pounds of carbon. A piping manifold,
mounted adjacent to the GAC vessels, allows for series flow, parallel flow, or independent
flow through the GAC vessels by manually changing the valve positions. The primary mode
of operation is series flow through both GAC vessels.
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NOTICE
• Thi• pk,t wa• prspar•d for th• v,c:Ju•lw ., .. of lh• party nam,d h,,-on. Said ~rllflcatu do not Hf•nd to any unnamed p•f'S{)n without an upr-.u ree,rlffl~tlon by /11, .surv.ror
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,xcNd.s th, min/mum r.q11/r,mwits of Cl claH B •urv.y In
ar:cardanc• with lh• Stondorda of Procllt:e for Land Surv.ylng
In North Carol/no.
• Th• ratio of p,nh,fon ~,a,.. any ad/ustm,nfs Is I ; 27,09 I.
• This Is not a boundary survey.
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t----------------1 DIIA"L. ___ .,!LJ __
x -·-• -.... ,., • --~ -DAlE:
---·I DESIGNED JPM
----1QfEQCED__JQ1Q __
a<EO<a>
A ! 8 I C I D
AS-BUILT ORA'MNCS 10/le/2000
E F G H
FCX-STATESVILLE SUPERFUND SITE
OPERABLE UNIT THREE (OU3)
STATESVILLE, NORTH CAROLINA
J i( L
,...
N
t ---111-..E
L£G£ND
0 sw ....... AS/SVE WELL
EB EW ....... SV£ WELL
,.-MP ....... MONITORING PROBE
$ MW ....... EXISTING MONITORING WELL
I) SSMH •.•. SANITARY SEWER MANHOLE
6" SVE PIPING
2" SVE PIPING
1" AIR SPARGING PIPING
CHAIN LINK F£NC£
.. $ .. fl
'°"·77' -i!H$ ....,,. ..
OOORIJIK'-rr TA81...E FOR WEU.. LOCAOONS
O<S<IW'TIOH -""""" rw-,,,__, 48n.9T 48QJ.7T
EW-2/SW-2 .., . .,.,. 5017.79'
tw-3 ...,_.,, ..,. ....
tw • 40.55.88' 493$.10'
tw-, 4058.43' ""'-2T
tw-• 4875.99' ,,,.,.,.,
tw-, 4774.75' 5QU.91'
tw-• 4757.83' 4937.7J'
tw-• 477a..98' ..,,.,.,
EW-10 4880.08' 4775.94' .,,_, 4957.98' 513".ff'
MP-2 ..,,,_,,. 4llle..5e'
MP-3 4773.75' 51:s1.1e· ...... ..... ,. . 4924.7J'
MP-5 4779.52' 481:17.M' .,,_, 4777.M' 49!1Q..3SI'
MP-7 4879.91' 49$3.93' .. _. ....... , !liOUl.50'
WP-& 4827.~· """-n'
MP-10 4927.48' ~Cl..55'
MP-11 .....,.. 4i75.34'
MP-12 4911&.38' 4-UJ.94'
MP-13 .,...,.. ..,,..,,
MP-14 =· ~16.95'
WP-15 48&4.211' 48$3.95'
W-11 4871.$7' 52<10.&3'
w-,s
_ _...
5229.99'
W-0 4-M0.19' 4748.11" .... ....... 4r.,o.19'
W-lel 41135.72' 4811.24'
W-1$5 4'135.51' 4815.15'
SYE-2 4'13U12' 4-elJ..5.2' ,_,. 5192.'9' 4ffl.eo'
" " "
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FIGURE 2-1 DRA'MNG NUMBER
PIPING AND EQUIPMENT LAYOUT 1B895
SHEET NUMBER
2.-1
M I N 0 I p
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9
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INTERLOCK fROM SVE BLOWER r--------------7----------
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----1 Q£CKED KHO
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EW-J
CE!-1 COMMON EXlRACTION HEADER
CSH COMMON SP.-.RGE HEADER
EH1 EXTRACTION HEADER 1
EH2 EXTRACTION HEADER 2
EH3 EXTRACTION HEADER 3
EH4 EXlRACTlON HEADER 4
EH5 EXTRACTION HEADER 5
EH8 EXlRACTION HEADER 6
EH7 EXlRACTION HEADER 7
EH8 EXlRACTION HEADER 8
EH9 EX1RACTlON HEADER 9
EH10 EXlRACTlON HEADER 10
EFF TREATED EFFLUENT OFF-GAS
SHl SPARGE HEADER 1
SH2 SPARGE HEADER 2
EW-<
EQUIPMENT LEGEND·
AS AIR SPARGING B-1 BLOWER 1
B-2 BLOWER 2 GAC GRANULAR ACTIVA TEO CARBON
SVE SOIL VAPOR EX1RACT10N EV EXlRACTION HEADER VALVE
SV SPARGE HEADER VALVE AV AIR COMPRESSOR VALVE
CV COMMON HEADER VALVE
OV ORAIN VAL VE
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FT FLOW TRANSMlnr:R
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HV HAND-VAL\'E
IE CURRENT ELEMENT
U CURRENT INOICATOO IT CURRENT l'RANSMITTER U L.EVEl lNOICA TOR LT LEVEL TRANSMITJr:R
Pl PRESSURE INDICATOO
PT PRESSURE TRANSMITTER
MS MOTOR STARTER (RELAY)
PA PRESSURE ALARM
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TE l'EMPERATURE ELEMENT
Tl TEMPERATURE INDICATOR
TT l'EMPERATURE lRAHSMITTrn
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OORACTED V.4.POR FLOW
INJECTED AIR FLOW
ELECTRICAL SIGNAL
MANUALLY ACTIVATED BI.JTTERFL Y VALVE
SOLENOID VfJJ...VE
MANUALLY ACTUATED GLOBE VALVE (LOCKABLE)
MANUAlLY ACn.1'.TED BALL VALVE (LOCKABLE)
VACUUM RELIEF VALVE
PRESSURE REGULATOR
SAMPLE PORT
EV 10
TO
PACKAGED SVE
SYSTEJj
BLIND Fl..ANGES FOR
CONTINGENT WELLS
EW-10
C:t LOCAU.Y MOUNTED EQUIPMENT
(PSI-INSTRUMENT READING)
Et PANEL MOUNTED EQUIPMENT
(HAND/OFF/AUTO)
~ PROGRAMMABLE LOGIC
CONTROLLER (MOTOR STARTER)
~ PIPE SIZE IDENTIFIER
----ll BLJND FlANGE FOR CONTINGENT WEU.
□ CONDENSATION DRIP 1RAP
~ BLOWER
PRo..ECT NUMBER
ZONE R[V. """"'""" B'I' DATE AP9. EL PASO ENERGY CORPORATION 18895.014
F G H
rcX-STATESVILLE SUPERrlJND SITE
OPERABLE UNIT THREE (OU3)
STATESVILLE, NORTH CAROLINA
J K L
flGURE 2-2 DRA'MNG NUMBER
PIPING AND INSTRUMENTATION DIAGRAM 18895
SHEET NUMBER
2-2
M N 0 p
1(
9
8
7
6
5
3
2
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TO SPAR'GE WEU. VALVES -----7---------------------------------------------------------------------------7
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Pa:i.o:TW-DESICNED JPM
DATE: ---O<ECkED __ KHO __
DAm CHECkED
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,~51\JRE -CV-2
SEPARATOR
DV-1
UOUto DRAIN
{NORMAU 'I' LOCKED CLOSED)
PIPING l EGEND·
CEH COMMON tx1RACTION HEADER
CSH COMMON SPARGE HEADER
EH I (XTRACTIDN HEADER 1
EH2 EXTRACTION HEADER 2
EHJ EXTRACTION HEADER .3
EH4 EXTRACTION HEADER 4
EHS EXTRACTION HEADER 5
EH6 EXTRACTlON HEADER 6
EH7 EXTRACTlON HEADER 7
EH8 EX1RACTlON HEADER 8
EH9 EXTRACTlON HEADER 9
EH10 EXTRACTION HEADER 10
EFF lREATED EFFWENT OFF-GAS
SH1 SPARGE HEADER 1
SH2 SPARGE HEADER 2
EQUIPMENT I EGEND·
AS AIR SPARGING 8-1 BLOWER 1
8-2 BLOWER 2
GAC GRANULAR ACTIVATED CARBON
SVE SOIL VAPOR EX1RACTlON EV EXTRACTlON HEADER VALVE SV SPARCE HEADER VALVE
AV AIR COMPRESSOR VAL'.-£
CV COMMON HEADER VALVE
OV DRAIN VAL VE
SVE BLOWER SYSTEM
CONTROi l EGEND·
FE Fl.OW El...EMENT
Fl Fl.OW INDICATOff
FT Fl.OW lRANSl,CllTER
HOA HANO/al'" /AUTO HS HANO-S'MTCH
HV HANO-VAL~
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II CURRENT INDICATOR IT CURRENT TRANSMITTER
LI LEVEL INDICATOR
LT lE\IEL 1RANSMITT£R
pt PRESSURE INOICATOO
PT PRESSURE lRANSMITTER
MS MOTOR STARlER (RELAY)
PA PRESSURE Al.ARM
pt PRESSURE INOICA TOR
TE TEMPERATURE EUMENT
TI TEMPERAT1JRE INDICATOR
TT TEMPERATURE lRANSMITTER
RE\'lSIONS
ZOE REV. """""""' BY DAlE J,PP,
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1/1
£
AFTERCQQLER
EXTRACTED VAPOR FLOW
INJECTED AIR flOW
ELECTRICAL SIGNAL
MANt.W..l'I' ACTIVATED BLJTTERfl'I' VALVE
SOLENOID VN....VE
tOl
~
MANt.W..l'I' ACTUATED GLOBE VAi.VE (LOCKABLE)
MANt.W..l'I' ACTUATED BAU. VALVE (LOCKABLE)
~
~
VACUUM RELIEF VALVE
PRESSURE REGULATOR
SAMPLE PORT
EL PASO ENERGY CORPORATION
F'CX-STATESVILLE SUPERF'UND SITE
. OPERABLE UNIT THREE (OU3)
STATESVILLE, NORTH CAROLINA
J K L
OAC-1 GAC-2
GRANULAR ACTIVATED
CARBON APSQRBERS
(SEE OPERATION ANO MAINTEPW4CE MANUAL
f"OR EXM::T PIPING ANO VALVE LAYOUT)
TO AIR SPAAGE WELLS
---11
LOCAU.Y MOUJ'ITEO EQUIPMENT (PSI-INSTRUMENT READING)
PANEL MOUNTED EQUIPMENT
(HANO/OFF/AUTO)
PROGRAMMABLE LOGIC
CONTROUER (MOTOR STNITT:R)
PIPE SIZE tDENllFlER
BLIND Fl.ANGE FOR CONTINGENT WELL
CONDENSATION DRIP TRAP
BLOWER
F'IGURE 2-3
TREATED OFF GAS
EXHAUST STACK
PRO..ECT NUMBER
18895.014
DRAWING HUMBER
PIPING AND INSTRUMENTATION DIAGRAM 18895
SH£ET NUMBm
2-3
M N 0 p
!(
9
8
7
6
5
4
3
2
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When the primary or lead GAC vessel in the series requires a carbon change-out, it can be
manually isolated with the valving while the secondary GAC vessel stays on-line to treat
mcorrung vapors. The valving is adjusted after change-out has occurred so that the
secondary GAC vessel becomes the primary GAC vessel in the series and the changed-out
GAC vessel becomes the secondary vessel. This rotation is repeated as the GAC is spent in
each vessel. There is no requirement for moving vessels or disconnecting piping to rotate
primary and secondary positions in the series.
When the clean air passes out of the GAC vessels, it is vented above the roof of the
building.
The operation of AS/SVE is controlled using a SCADA system, which enables the operator
to control the process operations locally from a desktop computer or remotely via a modem ..
The SCADA system consists of the following equipment: a programmable logic controller
(PLC), desktop computers (on-Site and remote), an alarm printer, a report printer, and an
auto-dialer. The PLC receives process information from the instrumentation that is located
throughout the AS/SVE system. The process information can be monitored and controlled
from the local desktop computer or from a remote computer. The SCADA system alerts
the operator in the event of selected alarm conditions with a local panel alarm and an auto-
dial for remote notification of the alarm condition.
\ \BCNSHOJ\PROJECTS\PROJ\18895\ 18895.014\0&MS02.doc 2-2
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3.0 RJNCTIONAL DESCRIPTION OF AS/SVE SYSTEM
This section presents a functional description of the AS/SVE system. A listing of the
instrument tag identification numbers that are utilized by the SCAD A system are provided in
Table 3-1 for reference. The following sections describe the functions of the major
equipment comprising the system as well as the instrumentation that allows the operator to
control and monitor the system.
3.1 SOIL VAPOR EXTRACTION (SVE) SYSTEM OPERATION
The SVE system extracts soil vapor from the SVE wells. The two SVE blowers can be
activated and deactivated using three position hand/ on/ auto (HOA) switches mounted on
the CPlOO0 panel. The blower run indicator lights are located on the CPlO00 panel. The
HOA switches allciw the operator to manually tum the blowers on and off or to allow them
to operate in the automatic mode controlled by PLC. In the automatic mode, the blowers
will shut off when the high-high liquid level alarm on the moisture separator is activated and
when the blower discharge pressure is out of normal range. The operator can select the
blower operating mode (on/off/ auto) and monitor the blower status (off/on) from the
SCADA system (MS0201 and MS0202). The SCADA system records the blower process
data and alarm history as information is received from the following instruments:
• Pressure element PE0203 monitors the vacuum on the suction side of the blower.
The PLC is programmed to have a low and high pressure set point. The low-
pressure (LP) set point deactivates the blowers and activates an alarm (P A0203)
which in tum activates an alarm light on the CPlOO0 panel and activates the
autodialer notifying the operator that the blower is not running properly. A high-
pressure (HP) set point deactivates the blowers and activates an alarm (P A0203)
which in tum activates an alarm light on the CPl000 panel and activates the
autodialer notifying the operator that the blower is not running properly. After
either an LP or HP alarm, reactivation of the blower requires an operator
command through the SCADA system. The pressure output is displayed on the
SCADA system in inches of water column (in.W.C.) vacuum. The operator can
\ \BCNSH03\FROJECTS\FROJ\18895\18895.0!4\0&MS03.doc 3-1
•
D Table 3-1. SCADA System Tag List for the AS/SVE System
FCX-Statesville Superfund Site OUJ
D
Instrument Range u Tag ID Description Location Unit Low High Alarm Set Point
FE0101 Differential Pressure, Pilot Tube EW-1 in.WC. 0 2 I PE0101 Vacuum EW-1 in.WC. 0 100 TE0101 Temperature EW-1 F 19 120 Fl8101 Flow, Calculated EW-1 scfm FE0102 Differential Pressure, Pilot Tube EW-2 in.WC. 0 2 I PE0102 Vacuum EW-2 in.WC. 0 100 TE0102 Temperature EW-2 F 19 120 Fl8102 Flow, Calculated EW-2 scfm I FE0103 Differential Pressure, Pilot Tube EW-3 in.WC. 0 2 PE0103 Vacuum EW-3 in.WC. 0 100 TE0103 Temperature EW-3 F 19 120 Fl8103 Flow, Calculated EW-3 scfm I FE0104 Differential Pressure, Pilot Tube EW-4 in.WC. 0 2 PE0104 Vacuum EW-4 in.WC. 0 100 TE0104 Temperature EW-4 F 19 120 I Fl8104 Flow, Calculated EW-4 scfm FE0105 Differential Pressure, Pitot Tube EW-5 in.WC. 0 2 PE0105 Vacuum EW-5 in.WC. 0 100 TE0105 Temperature EW-5 F 19 120 I FI8105 Flow, Calculated EW-5 scfm FE0106 Differential Pressure, Pilot Tube EW-6 in.WC. 0 2 PE0106 Vacuum EW-6 in.WC. 0 100 TE0106 Temperature EW-6 F 19 120 I Fl8106 Flow, Calculated EW-6 scfm FE0107 Differential Pressure, Pilot Tube EW-7 in.WC. 0 2 PE0107 Vacuum EW-7 in.WC. 0 100 TE0107 Temperature EW-7 F 19 120 I Fl8107 Flow, Calculated EW-7 scfm FE0108 Differential Pressure, Pitot Tube EW-8 in.WC. 0 2 PE0108 Vacuum EW-8 in.W.C. 0 100 I TE0108 Temperature EW-8 F 19 120 FI8108 Flow, Calculated EW-8 scfm · FE0109 Differential Pressure, Pilot Tube EW-9 in.WC. 0 2 PE0109 Vacuum EW-9 in.WC. 0 100 I TE0109 Temperature EW-9 F 19 120 FI8109 Flow, Calculated EW-9 scfm FE0110 Differential Pressure, Pitot Tube EW-10 in.WC. 0 2 PE0110 Vacuum EW-10 in.WC. 0 100 I TE0110 Temperature EW-10 F 19 120 Fl8110 Flow, Calculated EW-10 scfm TM0401 Valve Closing Timer SW-1
I FE0401 Differential Pre·ssure, Pitot Tube SW-1 in.WC. 0 2 PE0401 Pressure SW-1 in.WC. 0 60 TE0401 Temperature SW-1 F 19 120 Fl8401 Flow, Calculated SW-1 scfm I TM0402 Valve Closing Timer SW-2 FE0402 Differential Pressure, Pitot Tube SW-2 in.WC. 0 2 PE0402 Pressure SW-2 in.WC. 0 60
I TE0402 Temperature SW-2 F 19 120
I P:\PROJ\18895\18895.014\T0301.xls
1 of 2
D
0 Table 3-1. SCADA System Tag List for the AS/SVE System
FCX-Statesville Superfund Site OU3
D
Instrument Range
I Tag 10 Description Location Unit Low High Alarm Set Point
Fl8402 Flow, Calculated SW-2 scfm
I MS0301 Motor Starter Air Compressor
TE0901 Temperature, Ambient Air Wall between compressor F 19 120
and disconnect panel
PE0901 Pressure, Atmospheric Wall between compressor psi 0 30
I and disconnect panel absolute
PE0301 Pressure Air Compressor Discharge psi 0 100
PA0301 Alarm Air Compressor Discharge psi 15 L 25 H
I FE0201 Differential Pressure, Pitot Tube CEH SVE Inlet in.WC. 0 2
TE0201 Temperature CEH SVE Inlet F 0 300
PE0201 Vacuum CEH SVE Inlet in.WC. 0 100
Fl8201 Flow, Calculated CEH SVE Inlet scfm
I AE0201 Gas Analyzer CEH SVE Inlet ppm 0 200
PE0202 Differential Pressure Particulate Filter in.WC. 0 40
PAH0202 Alarm for Differential Pressure Particulate Filter in.WC. 10 H
I LI0201 Water Level Moisture Separator inches 24 24
AL0201 Alarm for Water Level Moisture Separator inches 24 H
LI0202 Water Level Moisture Separator inches 28 28
AL0202 Alarm for Water Level Moisture Separator inches 28 HH
I FE0202 Differential Pressure, Pitot Tube Air Bleed-in Line in.WC. 0 2
Fl8202 Flow, Calculated Air Bleed-in Line scfm
FE0203 Differential Pressure, Pitot Tube Blowers Inlet in.WC. 0 2
TE0203 Temperature Blowers Inlet F 0 300
I PE0203 Pressure Blowers Inlet in.WC. 0 100
Fl8203 Flow, Calculated Blowers Inlet scfm
PA0203 Pressure Alarm Blowers Inlet in.WC. 30 L 80 H
MS0201 Motor Starter Blower 1 I IE0201 Current Blower 1 Amp
IAH0201 Current Alarm Blower 1 Amp . 44 H
MS0202 Motor Starter Blower 2
I IE0202 Current Blower 2 Amp
IAH0202 Current Alarm Blower 2 Amp 44 H
TE0204 Temperature Blower Outlet F 0 300
TAH0204 Alarm for Temperature Blower Outlet F 250 H
I PE0204 Pressure Blower Outlet in.WC. 0 40
PE0205 Differential Pressure GAG 1 in.WC. 0 10
PDAH0205 Alarm for Differential Pressure GAG 1 in.WC. 8H
AE0202 Gas Analyzer Gas Analyzer ppm I AAH0202 Concentration Alarm Gas Analyzer ppm SH
TE0205 Temperature Line Between GACs 1 & 2 F 0 212
TAH0205 Temperature Alarm Line Between GACs 1 & 2 F 100 H
I PE0206 Differential Pressure GAC2 in.WC. 0 10
POAH0206 Alarm for Differential Pressure GAC2 in.WC. 8H
FE0207 Differential Pressure Treated Off Gas in.WC. 0 2
TE0207 Temperature Treated Off Gas F 0 212
I PE0207 Pressure Treated Off Gas in.WC. 0 10
Fl8207 Flow, Calculated Treated Off Gas scfm
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monitor pressure readings and set points and can change set points through the
SCADA system.
The air compressor and electrically actuated solenoid valves at the sparging points
are interlocked with the blower so that if the blower is not running, the arr
compressor will not run, and the solenoid valves will be automatically closed.
• Flow element FE0202 is located on the air bleed-in line before the blower. This
element displays the flow rate in cfm through this portion of the system and
transmits signals to the PLC to display and record flow via the SCAD A system.
• Pressure element PE0201 is located on the common suction header before the
moisture separator. This element displays pressure as in.W.C. through this portion
of the system and transmits signals to the PLC to display and record pressure via
the SCADA system.
• Temperature element TE0201 on the common suction header before the moisture
separator sends a signal to the PLC to display and record temperature via the
SCADA system.
• Flow element FE0201 on the common suction header before the moisture
separator displays flow rate in cfm through this portion of the system and
transmits signals to the PLC to display and record flow via the SCADA
system. The PLC calculates and displays the standard flow rate in scfm
(FI8201) using the actual pitot tube differential pressure, temperature, and
pressure inputs (FE0201, TE0201, and PE0201).
• Level control element LE0201 indicates the condensate level in the moisture
separator. The level control system consists of a level transmitter (L 1) and a level
switch (LS). The level indication system has high water level and high-high water
level set points. The high water level (HWL) set point activates an alarm (AL0201)
which in turn activates an alarm light on the CPlO00 panel and activates the
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autodialer notifying the operator that the moisture separator needs to be drained.
The high-high water level (HHWL) set point activates an alarm (AL0202) which in
turn activates an alarm light on the CPl000 panel, activates an autodialer, and
deactivates the AS/SVE system. Once the water level in the moisture separator
falls below HHWL deadband, reactivation of the air sparging and SVE systems
requires an operator command through the SCADA system.
• Differential pressure indicator PE0202 located on the particulate filter before the
blower indicates the pressure drop across the filter. It displays the pressure
differential in in.W.C. and transmits signals to the PLC to display and record the
pressure differential via the SCADA system. A high-pressure differential activates
an alarm (P AH0202) located on the SCADA system and the autodialer to notify
the operator of the high-pressure differential. The operator can change the alarm
set point through the SCADA system.
• Temperature element (fE0203) is located on the suction line after the
suction header and bleed-in line. This element transmits a signal to the
PLC to display and record the temperature via the SCADA system.
• Flow element FE0203 is located on the suction line after the particulate
filter and before the blowers. This element transmits a signal to a locally
mounted flow differential pressure gage. The gage displays the picot tube
differential pressure in in.W.C. and transmits a signal to the PLC to display
and record the flow rate via the SCADA system. The PLC calculates and
displays the standard flow rate in scfm (FI8203) using the actual picot tube
differential pressure, temperature, and pressure inputs (FE0203, TE0203,
and PE0203).
• Electric current elements IE0201 and IE0202 are located in CPl000
measure the electrical current for each of the SVE blowers and transmit
signals to the PLC to display as amperage. An out-of-range current
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activates an alarm (IAH0201 and IAH0202) on the SCADA system and
autodialer, and deactivates the blower.
• Temperature element TE0204 is located on the blower discharge pipe and
transnuts a signal to the PLC to display and record the discharge
temperature via the SCADA system. An out-of-range temperature
activates an alarm (TAH0204) on the SCADA system.
• Pressure element PE0204 is located on the blower discharge pipe and
transmits a signal to a locally mounted pressure indicator. This indicator
displays pressure in in.W.C. through this portion of the system and
transmits signals to the PLC to display and record the pressure via the
SCADA system.
• Two direct reading differential pressure elements, PE0205 and PE0206, are located
on the GAC vessels down stream from the blowers to monitor pressure drops
across each of the vessels. Pressure indicators display the pressure differential in
in.W.C. and transmit signals to the PLC to display and record the differential via
the SCADA system. The operator can monitor and set differential set points
through the SCADA system. An out-of-range pressure differential activates an
alarm (PDAH0205 and PDAH0206) which in turn activates an alarm light on
CPl000 and activates the autodialer, notifying the operator.
• Temperature element TE0205 is located between the GAC vessels and
transmits a signal to the PLC to display and record the temperature via the
SCADA system. An out-of-range temperature activates an alarm
(TAH0205) on the SCADA system.
• Temperature element TE0207 is located on the GA C effluent header
downstream from the GAC vessels. This element transmits a signal to the
PLC to display and record the temperature via the SCADA system.
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• Pressure element PE0207 is located on the GAC effluent header
downstream from the GA C vessels. This element displays pressure in
in.W.C. through this portion of the system and transmits a signal to the
PLC to display and record the pressure via the SCADA system.
• Flow element FE0207 is located on the GAC effluent header downstream
from the GAC vessels. This element displays the pitot tube differential
pressure in in.W.C. through this portion of system and transmit a signal
to the PLC. The PLC displays and records the flow rate via the SCADA
system by calculating and displaying the standard flow rate in scfm
(FI8207) using the actual pitot tube differential pressure, temperature, and
pressure inputs (FE0207, TE0207, and PE0207). An out-of-range flow
activates an alarm on the SCADA system and the autodialer and
deactivates the blowers.
• Temperature element TE0901 located in the equipment area is used to
monitor the ambient air temperature in that area. It transmits a signal to
the PLC to display and record the temperature via the SCADA system.
• Pressure element PE0901 is located in the equipment area and is used to
monitor the ambient barometric pressure in the area. It transmits a signal
to the PLC for use in standard flow rate calculations.
• The extraction header from each extraction well (EW-1 through EW-10) has a
pressure element for monitoring each extraction well vacuum. Each pressure
element (PE0101 through PEOllO respectively) has a local pressure indicator
display and sends a signal to the PLC. The operator can monitor the extraction
well vacuum readings using the SCADA system.
• The extraction header from each extraction well (EW-1 through EW-10)
has a temperature element (TE0101 through TEOllO respectively) for
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morutonng temperature. They transmit signals to the PLC to display and
record the temperature via the SCADA system.
• The extraction header from each extraction well (EW-1 through EW-10)
has a flow element (FE0l0l through FE0ll0 respectively) for monitoring
SVE system performance. They transmit signals to the PLC to display
and record the flow rate via the SCADA system. The PLC calculates the
standard flow rate in scfm (FI8101 through FI8110) using the actual picot
tube differential pressure, temperature, and pressure inputs (FE0101,
TE0101, and PE0l0l through FE0llO, TE0ll0, and PE0ll0
respectively).
• Gas analyzers AE0201 and AE0202 are located at the blower inlet pipe
and between the GAC vessels, respectively. The analyzers transmit signals
to the PLC to display and record the PCE concentration via the SCADA
system.
3.2 AIR SP ARGING SYSTEM OPERA TIO NS
The packaged air sparging system will supply air to sparging wells SW-1 and SW-2. The
compressor's run indicator light and hand/ off/ auto (HOA) switch are located on the
instrument control panel (identified as CPl000). The HOA switch allows the operator to
manually tum the compressor on and off or operate it in the automatic mode where it is
controlled by the PLC. The compressor is electrically interlocked with the extraction
blowers so that the compressor can not operate unless at least one of the extraction blowers
is also operating. The operator is able to select the compressor operating mode
(on/off/auto) and monitor compressor status (off/on) from the SCADA system. The
SCADA system records the compressor process data and alarm history as information is
received from the following instruments:
• Pressure element PE0301 monitors the discharge pressure at the compressor. The
compressor is deactivated by both a LP set point and a HP set point. The two set
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points (P A0301) define the operating range of the packaged air sparging system.
The output from the element is displayed on the SCADA system in pounds per
square inch (psi). The operator can monitor the pressure readings, monitor set
points, and change set points through the SCADA system.
• The influent air line to each sparging well has a solenoid valve for pulsing airflow
to the two sparging wells. Each solenoid valve is controlled by the PLC (1M0401
and TM0402). The airflow to each well can be pulsed on and off independently by
an adjustable timed function that is controlled by the PLC. The operator can
monitor the valve status (open/closed) and set the pulse cycle as well as monitor
and change set points from the SCADA system. The PLC will automatically close
the valves whenever the SVE system is not operating.
• The influent air line to each sparging well has a pressure element for monitoring
spargmg pressure. Each pressure element (PE0401 and PE0402) has a local
pressure indicator (PI) display and sends a signal to the PLC. The operator can
also monitor sparging well pressure readings from the SCAD A system.
• A temperature element (TE0401 and TE0402) is provided on the influent
air line to each sparging well for monitoring sparging air temperature. The
output is transmitted to the PLC to display the instantaneous temperature
via the SCADA system.
• A flow element (FE0401 and FE0402) is provided on the influent air line
to each sparging well for monitoring the actual flow rate in cubic feet per
minute (cfm). The instrument will transmit signals to the PLC to display
both the instantaneous flow rate and the daily cumulative flow via the
SCADA system. The PLC calculates the flow in standard cubic feet per
minute (scfm) (FI8401 and FI8402) using actual pitot tube differential
pressure, temperature, and pressure inputs (FE0401, TE0401, PE0401,
and FE0402, TE0402, PE0402 respectively).
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3.3 SCADA SYSTEM OPERA TIO NS
• System alarms are categorized within the PLC based on the priority level (1-high
and 2-low). Priority levels for each alarm are given below.
Priority
Alarm Tag Name Alarm Description Level
AAH0202 GAC-1 high VOC concentration 1
AL0202 Moisture separator HHWL 1
PDAH0205, PDAH0206 GAC high pressure differential 1
AL0201 Moisture separator HWL 2
PAH0202 Particulate filter high pressure differential 2
IAH0201,IAH0202 Current meter out of range 2
PA0203 Blower LP and HP 2
TAH0204 Blower discharge high temperature 2
TAH0205 Temperature between GAC vessels 1
PA0301 Compressor LP and HP 2
• The PLC samples and stores data items for maintaining records of historical
system performance. The system can archive all the process data at a user-defined
sampling frequency. A sampling frequency of 1 minute was used for the initial
programming of the PLC data collection.
• The operator can input laboratory analytical data into the PLC database.
• The PLC has the ability to generate and print data summary reports. The content
and format of the reports are easily programmable. Reports can be generated on
demand that include the following information:
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• Cwnulative effluent flow volwne measured in 1000 standard cubic feet (kscQ
on daily, weekly, monthly, and yearly (to date) basis.
• Average effluent flow rate (kscQ on a daily, weekly, monthly, and yearly (to
date) basis.
• The PLC continuously generates an alarm report that identifies the alarm, its
time of activation, and the time at which it was acknowledged.
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4.0 OPERATION OF SYSTEM CONTROLS
The controls of the AS/SVE system equipment reside in two control cabinets, CPl 000 and
the computer cabinet. The system can either be controlled locally from these two cabinets
or from a remote computer. There is a main electrical disconnect for the AS/SVE system
where the electrical service enters the building. The following sections provide details about
the components and operations of the aforementioned controls. Detailed documentation on
the instrumentation and controls is provided in Appendix E.
4.1 MAIN ELECTRICAL DISCONNECT PANEL
The main electrical disconnect panel is located in the northwest comer of the equipment
area. Electricity for the system comes into the building to the main electrical disconnect
where it is then routed to the control cabinets. The main disconnect breaker can be used to
shutoff all of the electrical power to the system. The main electrical disconnect panel also
contains breakers for equipment secondary to the AS/SVE system including the overhead
.. , coiling door, the overhead lights, and the 110 VAC utility outlets.
4.2 CONTROL PANEL CP1000
Control panel CPlO00 houses the vital control components for the AS/SVE system. These
components include the PLC, the motor starters, the instrumentation termination blocks,
and the uninterruptable power supply (UPS). The control panel is equipped with a small
heater in order to protect the components from condensation at low temperatures. The
signals from the instrumentation .throughout the AS/SVE process are received by the PLC;
the PLC controls the process equipment by switching on or off the equipment as described
in Section 3 .0. The PLC also communicates with the desktop computer, which provides the
operator interface.
The four motors in the AS/SVE system are controlled by motor starters, each of which has
an HOA switch on CP1000. The HOA switches are three-way selector switches that allow
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for manual or automatic operation of the two blowers, heat exchanger fan, and air
compressor.
• The "Hand" position manually energizes the respective piece of equipment. The
"Hand" position bypasses the automatic PLC function. When operating
equipment in the "Hand" mode, close attention should be given to the system
conditions because the PLC would not have control of the system if an off-normal
or potentially dangerous condition were to occur.
• The "Off" position prevents the device operation.
• The "Automatic" position allows for the operation of the respective equipment by
the PLC. The equipment will start and stop automatically depending on the
information provided by the field instrumentation.
• A green status indicator light below each HOA switch illuminates when the
associated control circuit is energized.
Also located on the front door of CPlO00 are yellow alarm indicator lights and a light test
button. The button should be used periodically to test the bulbs in the alarm indicator
lights.
4.3 COMPUTER CABINET
The computer cabinet houses a desktop computer, a monitor, an alarm printer, a report
printer, and an autodialer. Additionally, the cabinet is equipped with a small air conditioner
and heater in order to maintain an internal temperature that will not damage the cabinet's
contents. The computer enables the operator to interface with the system controls and to
monitor the field conditions at various points in the system. In the automatic mode, the
operator uses the computer to start and stop the system. He or she can also use the
computer to generate cumulative reports using one of the cabinet's printers and the software
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residing on the computer. For more information about these reports, consult Section 3.3 of
this manual.
Some of the components inside the computer cabinet relate to the emergency response
features of the SCADA system. The autodialer will alert the operator in the event of an
alarm condition by playing a computerized, alarm-specific voice message over the pre-
programmed phone number. Whenever an alarm condition is experienced, the system prints
the date, time, and alarm code on the alarm printer inside the computer cabinet.
4.4 REMOTE COMPUTER
The remote computer contains software that allows the operator to interface directly with
the SCADA system over a modem from any off-Site location. Using this remote computer,
the operator can monitor system status, start and stop the system, and download data and
reports.
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5.0 OPERA TING PROCEDURES
This sect10n provides general procedures for the system startup and shutdown. The
procedure has provisions for startup and shutdown with the system while operating either in
the automatic mode or in the manual mode.
5.1 SYSTEM STARTIJP
The following subsections describe the steps in detail that the operator should follow to
startup the AS/SVE system.
5.1.1 Set Process Valve Positions for Startup
Valve positions for process flow should be set at each of the air sparging and SVE wells and
in the equipment area according to Table 5-1. Valve identification numbers and locations
are shown on Figures 2-2, 2-3, and 5-1. Set the valve positions as follows:
1. Open the ten SVE extraction well valves (EV-1 through EV-10).
2. Open air sparging system valve AV-1 at the air compressor and close the control
valves SV-1 and SV-2 at the air sparging wells (the control valves will be opened
after system startup to set the desired air sparging flow rates).
3. Partially open the blower air-bleed valve, CV-2, to position 5 as marked on the
valve handle. After system startup, adjust the valve position to obtain the desired
SVEvacuum.
4. For single blower operation, open the SVE blower system valves CV-1, CV-3,
CV-4, and CV-7. (Note: If two blower operation is desired, also open CV-5 and
CV-6.)
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I Table 5-1. Valve Positions for Operation of the AS/SVE System
I FCX-Statesville Superfund Site OU3
I Valve Position Valve ID Startup Shutdown
I SVE Extraction Wells
EV-1 Open Closed
I EV-2 Open Closed
EV-3 Open Closed EV-4 Open Closed u EV-5 Open Closed
EV-6 Open Closed
EV-7 Open Closed I EV-8 Open Closed
EV-9 Open Closed I EV-10 Open Closed
Air Sparging System
I AV-1 Open Closed SV-1 Closed (Adjust after Startup) Closed
I SV-2 Closed (Adjust after Startup) Closed
Moisture Separator Drain
I DV-1 Closed Closed
SVE Blower System
I CV-1 Open Closed
CV-2 Open to Position 5 Closed
I CV-3 Open
CV-4 Open
CV-5 Closed (for 8-1 only operation) I CV-6 Closed (for 8-1 only operation)
CV-7 Open
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Table 5-1 (Continued). Valve Positions for Operation of the AS/SVE System
FCX-Statesville Superfund Site OU3
Valve Position
Valve ID Startup
GAC Vessels (select one of the following modes of operation)
Series Operation with GAC-1 Primary
CV-8 Open
CV-9 Closed
CV-10 Open
CV-11 Closed
CV-12 Open
CV-13
Series Operation with GAC-2 Primary
CV-8
CV-9
CV-10
CV-11
CV-12
CV-13
GAC-1 Operation Only
CV-8
CV-9
CV-10
CV-11
CV-12
CV-13
GAC-2 Operation Only
CV-8
CV-9
CV-10
CV-11
CV-12
CV-13
\\BCNSH03\PROIECTSIPROJ\\889S\\889S.014\T0S0J.doc
Closed
Closed
Open
Closed
Open
Closed
Open
Closed
Closed
Open
Open
Closed
Closed
Closed
Open
Closed
Closed
Open
Closed
Shutdown
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0 0
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"' r;:
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"' z
3 <{
I "' 0
APROX. a·-1r
APPROX. 8' -0"
CPC-20R
&" PIPING
DISCHARGE
SAMPL£/PR[SSURE CAUCE LOCATION
(TYP. BOTH VESSELS)
INL[T SAMPLE/
PRESSURE C,1..UC[
LOCATION
INLET Fl.ANCE SPOOL
(lYP. 80111 VESSELS)
0 0
0
0
0
0
0
0 0 0 0
GAC-1 Vessel
GAC-1
Vessel
#1
2-4" W. . .',WAY
0 0 0
__ _.... __ -/.~"/0 0
INLEr f'"ROM
SV(
Plan View
Side View
0 0
0 0
,. 0
0 0 0 0 .
GAC-2 Vessel
#2
Vessel
f---------------13'-o·-----------------
SOURCE: OPERATIONS AND MAINTENANCE MANUAL, CARBONAIR ENVIRONMENTAL
SYSTEMS, INC. (SEE APPENDIX B)
FIGURE 5-1
VALVE AND PIPING
LAYOUT FOR GAC VESSELS
18895.014
FCX-STATESVILLE SUPERFUND SITE
STATESVILLE, NORTH CAROLINA
BROWN AND
10/00
CALD"WE LL Nashville, Tennessee
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5. Set process valves for GAC vessels in desired position for normal series operation.
See Table 5-1 for correct valve positions and Figure 5-1 for the GAC vessel valve
locations. System can be operated with GAC-1 vessel as primary or GAC-2 vessel
as primary. (Note that Table 5-1 also provides valve positions for individual GAC
vessel operation that can be used during carbon changeout of the off-line GAC
vessel.)
5.1.2 Activate SCADA System (Automatic System Startup)
1. At main disconnect panel, check that main disconnect breaker is in the "on"
position and CPl000 breaker is on.
2. Inside CPl000, check that circuit breakers and motor starter breakers are in the
"on" position. Also tum on the UPS.
3. Close the doors to CPl000 and set the disconnect lever on the CPl000 door to the
" ,, .. on posmon.
4. Tum on equipment inside computer cabinet including desktop computer, monitor,
alarm printer, report printer, and autodialer.
5. Once the computer is on and operating, set the applicable HOA switches 0ocated
on front of CPl000 cabinet) to the "auto" position. If air sparging is not to be
performed, tum the compressor HOA switch to "off". If only one blower is to be
operated, turn blower 2 HOA switch to "off".
6. If air sparging is to be performed with SVE, rotate the air compressor disconnect
switch to the "on" position (the switch is mounted locally on the air compressor).
7. Login to the desktop computer as operator or as engineer as directed by system
manager. For the operator level, enter operator and brown. For the engineer
level, enter engineer and caldwell.
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8. Using the mouse in the computer cabinet, select the "SVE System" screen.
9. At the direction of the system manager, start either blower 1, blower 2, or both
blowers (as directed) by dicking the start buttons with the computer mouse.
Starting a blower automatically activates the air compressor so that it will maintain
the system air pressure to the sparging wells. Starting a blower also automatically
activates the fan on the after-cooler to reduce the temperature of the blower
discharge prior to the GAC.
10. Adjust system vacuum using the bleed-in valve CV-2 as directed by the system
manager.
11. Adjust the air sparging flow rate and pressure using the sparging control valves
SV-1 and SV-2 as directed by the system manager.
5.1.3 StartAS/SVE Process Equipment (Manual System Startup)
1. At main disconnect panel, check that main disconnect breaker is in the "on"
position and CPl000 breaker is on.
2. Inside CPlO00, check that circuit breakers and motor starter breakers are in the
"on" position.
3. Oose the doors to CPl000 and set the disconnect lever on the CPlO00 door to the
" ,, .. on posmon.
4. Tum on equipment inside computer cabinet including desktop computer, monitor,
alarm printer, report printer, and autodialer.
5. Set the desired HOA switches 0ocated on front of PLC cabinet) to the "hand"
position. (fhis will manually activate the system equipment selected by the
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operator. Care should be taken by the operator to monitor system conditions since
the system will not provide alarming and automatic control if an off-normal
condition exists.)
5.2 SYSTEM SHUTDOWN
The following steps should be followed to cease operation of the AS/SVE system.
5.2.1 Shutdown AS/SVE Process Equipment (Manual System Shutdown)
Set the desired HOA switches Qocated on front of PLC cabinet) to the "off" position. (This
will deactivate any active system equipment selected by the operator. Care should be taken
by the operator to monitor system conditions if any process equipment is still running since
the system alarms will not be activated if the computer is off.)
5.2.2 Deactivate SCAD A System (Automatic System Shutdown)
1. Login at the desktop computer terminal as operator.
2. Select the "SVE System" screen using the mouse in the computer cabinet.
3. Stop the aftercooler fan by clicking the stop button with the computer mouse.
(This will Stop all four system motors since the blowers are interlocked to run only
with the after cooler fan operating and the air compressor is interlocked to run
only with a blower operating.)
5.2.3 Close Selected Process Valves
1. dose air sparging system valve AV-1 at the air compressor and close the control
valves SV-1 and SV-2 at the air sparging wells.
2. dose the ten SVE extraction well valves (EV-1 through EV-10).
I IBCNSH0JIPROJECTSIPROJ\!8895\18895.014\Q&MSOS.doc 5-4
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3. dose valves CV-1 and CV-2 at the blower package.
4. Other valves may be closed at the discretion of the system manager.
\ \BGJSH0J\PROJECfS\PROJ\18895\18895.014\0&MSOS.doc 5-5
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6.0 SYSTEM MONITORING AND MAINTENANCE
1bis section provides guidance for the routine monitoring and the maintenance of the
AS/SVE system. Table 6-1 provides a schedule of routine tasks related to the system
mamtenance.
6.1 HEAL TH AND SAFETY
The following safety measures should be adhered to by personnel when morutonng,
operating, troubleshooting, or maintaining the AS/SVE system and its related components.
The contaminants contained in the untreated vapor are considered hazardous and proper
steps should be taken to minimize human contact with them. For more detailed health and
safety information, refer to the "Health and Safety Plan for Remedial Action of Operable
Unit Three (OU3) FCX-Statesville Superfund Site" (referred to as the HASP) dated
May 2000 by Brown and Caldwell.
1. Personnel performing maintenance work on this system, where potential exposure
to site contaminates is possible, shall be 40-hour trained under the Occupational
Safety and Health Administration (OSHA) 1910.120 Hazardous Waste Operations
and Emergency Response (HAZWOPER) Standard. This includes: work that
would open SVE piping system, removal of SVE liquid condensate, changeout of
GAC media, and other similar activities.
2. Proper decontamination procedures for personnel and equipment should be
followed to reduce the spread of contamination. The on-site documentation shall
include the site-specific HASP in accordance with 29 CFR 1910.120.
3. Proper Personal Protective Equipment (PPE) should be worn as directed by the
HASP to prevent direct or indirect contact with the contaminants during
monitoring and maintenance activities.
\ \BrnsH0J\PROJECI'S\rROJ\18895\18S95.014\0&MS06.doc 6-1
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Table 6-1. Maintenance Schedule for the AS/SVE System
FCX-Statesville Superfund Site OU3
Maintenance Activity Maintenance Frequency Maintenance Work
Responsibility
Blowers
Replace Particulate Filter on When differential pressure Maintenance Contractor
Blower Package reaches 10 in.W.C.
Replace Bearing in Blowers After 15,000 to 20,000 hours of Maintenance Contractor
operat10n
Inspect Vacuum Relief Valves Periodically Maintenance Contractor
Air Compressor
Drain Moisture from Tank When necessary (Caution: Maintenance Contractor
pressure in tank must be less
than 25 PSIG)
Clean/Replace Intake Air' As necessary (monthly) Maintenance Contractor
Filters
Check V-Belts for Tightness Monthly Maintenance Contractor
Clean Auto Drain Valve Monthly Maintenance Contractor
GACVessels
Replace Carbon As necessary Carbon Vendor
Drain Condensate As necessary at carbon Carbon Vendor
changeout
Other
Test PLC Alarm Circuits and Once every 180 days Maintenance Contractor
Panel Lights
Check Instrument Calibration Once every 180 days Maintenance Contractor
Drain Drip Traps Once every 180 days Maintenance Contractor
\ \BCNSHOJ \PROJECI'S\PR.OJ\ 18 895 \ 18895.014 \ T0601.doc
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4. Maintenance work on electrical, pneumatic, and/ or spring-loaded systems shall be
performed using proper lock-out/tag-out (LOTO) procedures in accordance with
OSHA standards. The LOTO procedures are provided in the HASP.
5. Pneumatic devices should only be removed or serviced after their air supply lines
have been shut off and locked out following equipment-specific LOTO
procedures.
6. Air line valves should be closed when control panel(s) are shut down.
7. Proper respiratory protection should be worn when handling dry GAC to prevent
inhalation. Although virgin GAC is not considered hazardous, it may cause
irritation to the respiratory tract and lungs.
8. Liquid removed from the moisture separator and/ or drip traps should be handled
as a hazardous waste and all environmental regulations regarding its disposal
should be strictly followed.
9. Spent GAC should be handled as a hazardous waste and all environmental
regulations regarding its disposal should be strictly followed.
6.2 ROUTINE MONITORING OF AS/SVE SYSTEM
Routine monitoring of the system will be performed remotely by BC operations
personnel using a computer. Monitoring also includes routine on-Site inspections of
the system, recording system status, scheduling maintenance (if needed), and
scheduling the · sampling of the process. Sampling of groundwater wells will be
performed as directed by the RA Work Plan, the Phase I Performance Test Plan, or
as directed by the System Manager. The reference methods for analysis of
groundwater samples are presented in Table 6-2 and the quality control/ quality
assurance (QA/QC) sampling requirements are presented in Table 6-3.
\ \BCNSH03\PROJECTS\PROJ\18895\18895.014\0&MS06.doc 6-2
Table 6-2. Summary of Chemical Analyses and Analytical Method References for Groundwater Sampling
FCX-Statesville Superfund Site OU3
Sample Evaluation
Field Measurements:
Laboratory Analyses:
Chemical Test/Analyte Parameter
Carbon dioxide
Iron (II)
Manganese (II)
Sulfide
Conductivity
Oxidation-reduction potential (ORP)
pH
Dissolved oxygen (DO)
Temperature
Chloride
Iron (total)
Manganese (total)
Aluminum (total)
Nitrate/nitrite
Sulfate
Ethane. ethene, and methanee
TCL voes
Alkalinity (carbonate/bicarbonate)f
Dissolved total organic carbon (TOC)
Volatile fatty acids
Analytical Reference Methoda
Hach KitC
Hach KitC
Hach KitC
Hach KitC
ASTM Method D-1125-82
ASTM Method D-1498-76
ASTM Method D-1293-84
CHEMETRICS KitC
NAd
USEPA Method 325.2
Aquaterra QAPP Table 3
Aquaterra QAPP Table 3
Aquaterra QAPP Table 3
USEPA Method 353.2
USEPA Method 375.4/9038
USEPA Method 8015-Modified
Aquaterra QAPP Table 2
Standard Methods 2320B
USEPA Method 415.1
Standard Methods 5560C
DQO Levelb
II
I
111
IV
IV
IV
111
111
111
IV
111
111
111
a Sample preservatives, when required by the method, will be added to sample containers at the analytical laboratory prior to sampling. Contract
Required Detection Limits (CRDLs) will be according to the contract laboratory procedure (CLP) methods referenced in the Aquaterra QAPP
Tables 2 and 3.
b DQOs (Data Quality Objectives) and QA/QC frequencies per "Environmental Investigations Standard Operating Procedures and Quality
Assurance Manual", May 1996, USEPA Region 4. Level I= Field Screening; Level II= Field Analyses; Level Ill= Screening Data with Definitive
Confirmation; Level IV = Definitive Data.
c Method will be per manufacture's procedures.
d Not Applicable. .
e Analysis will be subcontracted to Microseeps Incorporated, Pittsburgh, Pennsylvania.
f Samples to be collected in zero headspace containers to prevent exchange of carbon dioxide between the samples and the atmosphere.
\\BCNSH03\PROJECTS\PROJ\18895\18895.014\T0602.doc Page 1 Of 1
Sample Evaluation
Field Measurements:
Laboratory Analyses:
Table 6-3. Quality Assurance/Quality Control Samples for Groundwater Sampling Events
FCX-Statesville Superfund Site OU3
Chemical T esU Analyte Parameter
Carbon dioxide
Iron (II)
Manganese (II)
Sulfide
Conductivityb
Oxidation-reduction potential (ORP)
pH'
Dissolved oxygen (DO)
Temperature
Chloride
Iron (total)
Manganese (total)
Aluminum (total)
Nitrate/nitrite
Sulfate
Ethane, ethene, and methane
TCL VOCs
Alkalinity (carbonate/bicarbonate)
Dissolved total organic carbon (TOC)
Volatile fatty acids
QA/QC Samples
1 Duplicate per 20 GW samples (min. 1 per event')
1 Duplicate per 20 GW samples (min. 1 per event)
1 Duplicate per 20 GW samples (min. 1 per event)
1 Duplicate per 20 GW samples (min. 1 per event)
1 Duplicate per 20 GW samples (min. 1 per event)
1 Duplicate per 20 GW samples (min. 1 per day)
1 Duplicate per 20 GW samples (min. 1 per event)
1 Duplicate per 20 GW samples (min. 1 per day)
1 Duplicate per 20 GW samples (min. 1 per event)
1 Duplicate and 1 Equipment Blank per 20 GW samples (min. 1 per event)
1 Duplicate, 1 Equipment Blank, and 1 MS/MSD per 20 GW samples (min. 1 per event)
1 Duplicate, 1 Equipment Blank, and 1 MS/MSD per 20 GW samples (min. 1 per event)
1 Duplicate, 1 Equipment Blank, and 1 MS/MSD per 20 GW samples (min. 1 per event)
1 Duplicate and 1 Equipment Blank per 20 GW samples (min. 1 per event)
1 Duplicate and 1 Equipment Blank per 20 GW samples (min. 1 per event)
1 Duplicate and 1 Equipment Blank per 20 GW samples (min. 1 per event)
1 Trip Blank per 20 GW samples (min. 1 per sample shipment<);
1 Duplicate, 1 Equipment Blank, and 1 MS/MSD per 20 GW samples (min. 1 per event)
1 Duplicate and 1 Equipment Blank per 20 GW samples (min. 1 per event)
1 Duplicate and 1 Equipment Blank per 20 GW samples (min. 1 per event)
1 Duplicate and 1 Equipment Blank per 20 GW samples (min. 1 per event)
'A sampling "event" refers to samples collected on consecutive days over a period of no more than five days.
'Instrument shall be calibrated in accordance with the manufacturer's frequencies and procedures. Calibration records shall be recorded in the field book.
'A "shipment" refers to sending samples from the field to the laboratory.
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6.3 MAINTENANCE OF AS/SVE SYSTEM
System maintenance includes routine calibration of process instruments; change-out of the
GAC Vessels' media; repair of equipment, piping, valves, instruments, etc.; and process
modifications or upgrades. The maintenance personnel who perform work on the AS/SVE
system shall have the 40-hour HAZWOPER training because the system processes
hazardous vapors.
6.3.1 Routine Calibration of Instrumentation
Routine calibration of instrumentation will be performed at regular intervals. Instruments
giving suspect data will be recalibrated as necessary.
6.3.2 Particulate Filter Replacement
Located above the condensate collection tank on the blower package is the blower
particulate filter. There is a differential pressure display located at the filter housing. When a
pressure differential of 10 in.W.C. is reached, the filter should be replaced.
6.3.3 GAC Media Replacement
Since influent contaminant levels to the system may vary from day to day, it is difficult to
project the longevity of the GAC before it will become exhausted and will require a
change-out. When VOC are detected at concentrations of 5 ppm or greater by the gas
analyzer located between the two GAC vessels, then change-out of the spent carbon from
the primary GAC vessel shall be initiated. The secondary GAC vessel will act to adsorb and
remove those contaminants which breakthrough the primary vessel until the primary vessel
can be replenished with virgin carbon. Appendix B contains equipment specifications and
operating instructions, which are further discussed in Section 7.0.
The GAC system should be maintained so that the secondary GAC vessel's effluent quality
always remains below detectable limits for VOCs.
\ \BGJSH03\PROJECI'S\PROJ\ 18895\18895.014\0&MSOb.doc 6-3
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Spent carbon is vacuumed or removed from the respective vessel through the manways
provided, and transferred into drums for off-site disposal. The disposal of spent media will
be managed by the waste disposal contractor. Virgin GAC is then loaded into the vessel
through the same port. Upon completion of this procedure the secondary vessel in the
series shall assume the primary position while the newly loaded vessel takes the secondary
position. This rotation shall be repeated as GAC vessels are exhausted. Refer to the
corresponding valve arrangement specified in Table 5-1 for the rotation of vessels.
6.3.4 Other Maintenance
Other scheduled maintenance activities will be performed in accordance with the frequencies
provided in Table 6-1. All system inspection and maintenance activities should be recorded
on the form provided in Table 6-4,
\ \BCNSH0J\pROJECTS\rRQJ\18895\18895.014\0M.1S06.doc 6-4
Table 6-4. Inspection and Maintenance Documentation Form for the AS/SVE System
FCX-Statesville Superfund Site OU3
Date:
Operator:
Feature Inspected Maintenance Performed Comments
(YIN) (YIN)
SVE Blower System
-particulate filter
-moisture separator
-relief valves
-bearings on blowers
. . -mstrumentatlon
-aftercooler
Air Compressor
-receiving tank
-intake filters
-V-belts
-drum valve
GACVessels
-Carbon
-instrumentation
Drip Traps ( 4 total)
P: \pRQJ\18895\ 18895.014 \ T0604 .doc Page I of2
Table 6-4 (Continued). Inspection and Maintenance Documentation Form for the AS/SVE System
FCX-Statesville Superfund Site OU3
Date:
Operator:
Feature Inspected Maintenance Performed Comments
(Y/N) (Y/N)
AS/SVE Well Instrumentation
-EW-1/SW-1
-EW-2/SW-2
-EW-3
-EW-4
-EW-5
-EW-6
-EW-7
-EW-8
-EW-9
-EW-10
11 /7 /00\00027\P: \PRO J\ 18895 \ 18895.014\ T0604,doc P:i.ge 2 of2
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7.0 EQUIPMENT SPECIFICATIONS
Specifications and operating instructions for selected pieces of equipment are provided in
Appendices B, C, and D. Overviews of the mechanical equipment specifications are
provided below.
7.1 SVE BLOWERS
• Blower Manufacturer:
• Type:
• ModelNo.:
• Construction:
• Suction and Discharge:
• Motor:
• Electrical:
• Installed Accessories:
7.2 HEAT EXCHANGER
• Manufacturer:
• Mode!No.:
• Fluid Circulated:
• Construction:
• Inlet and Outlet Size:
• Motor:
• Electrical:
• Temperature In/ Out:
• Heat Exchanged:
\ \BQ\l'SH03 \FROJECTS\PR.OJ\ 18895\ 18 895.014 \O&.MS07 .doc
Ametek Rotron TMD
Explosion-Proof Regenerative Blower
EN909BG72WL
Cast aluminum housing, cover, impeller, and
manifold; cast iron flanges; Teflon lip seal
4" -F 8 NPSC
15 horsepower explosion proof
208V, 3-Phase, 60 Hz, 44 Amps (maximum)
GX120 Moisture Separator Q.E. Gasho & Ass.)
EMI-6 Inline Filter (EM Products)
EMS-4 Inlet Filter (EM Products)
BIU-4 Absorbtive Silencer (EM Products)
Xchanger, Inc.
AA-500
Air
Aluminum plate fin core; galvanized exhaust
hood; coated carbon steel fan guard and frame
6" flange
1 HP, 1725 RPM, TEFC
208V, 3-Phase, 60 Hz
210°F/109.6°F at 500-scfm air flow
54,237 BTU/hr
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7.3 AIR COMPRESSOR
• Manufacturer:
• ModelNo.:
• Type:
• Outlet Size:
• Motor:
• Electrical:
• Air Displacement:
7.4 GAC SYSTEM
Gardner Denver Machineiy Inc.
12T10VTS35
Oil-less, Tank-Mounted
1 ¼" FNPT
10 HP, 1450 RPM, TEFC
208V, 3-Phase, 60 Hz
57.8CFM
• Manufacturer: Carbonair Environmental Systems, Inc.
• Model No.: GCP 20R
• GAC Vessel Dimensions: 5'-0" OD x 7'-2" H
• Packaged System Dimensions: 8'-6" L x 13'-0" W x 8'-0" H
• Construction:
Vessels:
Piping:
Valves (disc/stem/body):
• BedArea:
• Flow Capacity:
• GACMedia Type:
• GAC Capacity:
Coated Carbon Steel
Carbon Steel
Bronze/ 416 SS/Cast Iron
19.63 sq ft
200-1800 cfm
4x10 mesh virgin bituminous vapor phase carbon
2000 pounds ( each)
Additional product and equipment information is provided in the appendices.
• Appendix B presents information on the GAC system and air compressor;
• Appendix C presents information on the blower package and heat exchanger;
• Appendix D presents information on the overhead door.
\ \BG!SH0J\PROJECTS\PROJ\ 18895\ 18895.014\0&MS07.doc 7-2