WQ0006373_Complete File - Historical_20171231

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Permits and Engineering Unit
Water ualit Section
o
Date: April 30, 1992
NON -DISCHARGE SA `F REPORT AND RECOMMENDATION
County: Mecklenburg
Permit No. WQ 0 373
9' - 7
PART I - GENERAL INFORMAT10N
I. Facility and Address: Fehr Property -Infiltration Gallery
Martin Marietta Corporation
7921 Southpark Plaza, Suite 210
Littleton, Colorado 80120
a Date of Investigation.- Aril 30, 199
33. Report Prepared T. Chen
. Persona Contacted and, Telephone Nu r: Chalam V. Pakala,
E. I .T. , Laws Environmental, Inc. 7 4 3 7 1747
. Directions to Site; From the junction of Highway 27 and
Mt* H lly Hunt ra ill.a Road H 1666) approximately 2.
miles northwest of the Charlotte City Limits, travel south-
east on Highway 7 about 0.5 mile. The proposed site is on
the right (southwest) aide of the road approximately 150
feet after crossing the bridge over Long, Creek.
6. Size (land available for expansion and upgrading)*- Adequate
land area: available for expansion/upgrading
7. Topography (relationship to 100 year fled plain included):,
The site was graded and. level; and is not in a flood plain.
. Disposal Sites, list for all disposal sites.
-
Latitude: 35 171 Longitude: 80 0 58, 4511
Attach a U.S.G.S. map extract and indicate facility site.
USGS Quad No.: F 15 SW USGS Quad Name: Mtn. Island Lake
9: Location of Nearest Dwelling and;; Water Supply Well: One
dwelling with water supply well is approximately 250 feet
northwest st of the proposed groundwaterre : diati n site.
10. Watershed Stream Basin Information:
ation
a. watershed 1 aaifi atien:

+� r �• • • F
',.
PART II -DESCRIPTION DISCHARGE AND TREATMENT T WORKS
1. Type of wastewater, sludge or contaminated soil:
Domestic
1 Industrial
*Pretreated petroleum contaminated groundwater
aVolume: 0.00720 MGD (Design Capacity)
. Types and quantities of industrial wastewater:
Wastewater is to be venerated from a groundwater
recovery system The groundwater is contaminated
with petroleum products,.
C. Prevalent toxic constituents in wastewater: The
retreated groundwater may contain trace amount of
petroleum products and metals (Lead).
dPretreatment Program (POTWs only): A
in development approved
should be required not needed
2. Production Rates ( industrial discharges oil ►) in Rounds Per
Zia RA
. Description of Industrial Process (for industries only) and
Applicable CFR Part and Subpart: N/A
. Type of Treatment (specify whether proposed or existing):
The groundwater recovery system is proposed d to consist of an
oil/water separator, Pero idation infiltration gallery,
and a number of monitoring and recovery wells ,
5, Sludge handling and disposalscheme: /
. Treatment Plant Classification. Proposed facility, no rating
determined.
SIC Code(s
Wastewater cad+ (s): N
Primary: Pretreated petroleum contaminated groundwater
Secondary:
Main Treatment Unit Code: N

PART III - OTHER PERTINENT INFORMATION
1. Is this facility being constructed with Construction Grant
Funds (municipals only) N
. Special monitoring requests:
3. Air Quality and/or Groundwater concerns or hazardous
materials utilized at this facility that may impact water
uality, air quality, or groundwater? The proposed waste -
flow is to be generated from a a groundwater recovery
system. The groundwater in the area of a gasoline station,,
which ceased operation in May, 1 83, was contaminated with
petroleum products. Prosper treatment to remove contaminants
from recovered groundwater for to re -injection into the
aquifer may prevent any impact on groundwater. Also no
hazardous materials will be utilized at this facility. No
detrimental impact to the environment is anticipated from
this operation
4. Other: `/
PA.
It Is recommended that a Nbnttrischarge Permit be issued for
the groundwater

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State of North Carolina t3rv�a.�)r��r.
_. TY
Department of .nviron -,e t, Health and Nato Source's
Division of Environmental Management ement WIR 2 '1992
512 NorthSalisbury Street - Raleigh, North Carolina 27604
J rnes G. Martin, Governor George Ti
William W. Cobey, Jr., Secretary
April 1, 199
MR LLIAM ARTICOLA
MARTIN MARIETrA AGGRIGATES
71 SOUTTIPARK PLAZA; SUITE 210
uhJ t; Application No. WQ0006373
purr Property
Subsurface Disposal Facility
Mecklenburg County
Dear MR AR I LA.
TheDivision's Permits and Engineering Unit acknowledges receipt of your permit application and
supporting materials on April 7, 1992. This application has been assigned the number shown above..
Please refer to this number when making inquiries on this project.
Your project has been assigned to John Seymour for a detailed engineering review. A technical,
acknowledgement will be forthcoming.
e aware that theDivision's regional office, copied below, must provide recommendations from the
Regional Supervisor or a Procedure Four evaluation for this project, prig to final action by the
f you have any questions, please contact John Seymour at 1 733-5083.
Sincere y,
t
CDonald a P.E.
Supervisor, rinits and Engineering Unit
cc: Mooresville Regional Office
Law Environmental'
Pollution Prevention Pays
P.Oox 29535, Raleigh, North Carolina 27626--0535 Telephone 919-73 -"7ilt
An Equal Opportunity Affirmative ct on Employer

LAW ENVIRONMENTAL, INC.
4333 WILMONT ROAD, SUITE 300
CHARLOTTE, NORTH CAROLINA 26217
RU. BOX 246674
CHARLOTTE, NORTH 6ARGUNA 26224-0674
704-35 -1747 704-357-1622 (FAX)
April 2, 19
. c
ou
North Carolina Department rent; 1991
and Natural Resources
Division of Environmental Management t w s
Permits and Engineering Unit
P.O. Box 7687
Raleigh, NC 27611
n
Attention: Mr. John Seymour
Engineer
ubj t: Non -Discharge Permit Application ,
urr Property
C" Highway 27 at Long Creek
Mecklenburg ;County, North Carolina
LEI Jon No. 5 - 5 -U 5
{gentlemen:
n behalf of Martin Marietta o tion, Law Environmental is pleased to submit the attached
non -discharge permit application. This submittal is in response to the North Carolina Division
of Environmental Management E letter dated February 14, 19-0 The purpose f the
proposed system is to recover ground water at the referenced site that has been impacted by the
apparent leakage or spillage of fuel oil. Recovery of the ground water from three -wells -1,
l - d l -) will reduce the size of the contaminant plume in both the vertical and lateral
dimensions, minimizing the potential for off -site migration and reducing concentrations o
contaminants present in the shallow aquifer.
Although'the '"-Pero idati n system has been designed for a 3.8 gallons per minute (gpm) flow
rate, a 1 gpm flow rate is being utilized until an optimum infiltration rate is determined from
onsite field tests The treatment system is designed to reduce the concentrations of dissolved
volatile organic compounds in the recovered ground water, The treatment system will
employ UV -Pero idation to produce effluent acceptable for re -injection into the aquifer
through an infiltration gallery in accordance th the North Carolina Division of Environmental
Management's (1' guidelines.
s 5-AMT1
"rPrmte'don R sgd'd apt!

Carolina Department of Health
[ Natural Resources
2, 1992
Action Plan was submitted to NCDEM on January 16, 1992. This permit is one of the
requirements 1r► the SOC which,will be issued by the Mooresville
appreciateWe our consideration of our application. Please contact us if you have any
comments or questions.
Sincerely,
LAW ENVIRONMENTAL, INC.
ANMVY . McCormick, E.I.T.
Staff Engineer
Chal*am. Pakala, E.I.T.
Pro ect Engineer
C
KeithA. Anthony, P.E.
Principal
cfm
cc: Mr. William Articola
Martin Marietta Corporation
Littleton, CO
AllenSchiff
MooresvilleNCDEM
ff
5 TIO

TABLEOF CONTENTS
1.0
NON -DISCHARGE PERMIT APPLICATIONFORM
SUBSURFACEA . . .................
1_1
2.0
DESCRIPTION OF THE ORIGIN, TYPE AND FLOW OF WASTE
TO BE TREATED AND WASTE ANALYSIS....... ... ..........�2-1
.0
FOLLOW-UP EVALUATION ............
3-1
.0
SOILS AND HYDROGEOLOGICI .... ...............
4-1
.1 Soils Description ........., .............. ... ...... .... ....
4.2 Hydrogeologic Desciiption ..... _ ....... a........ ...........
- ;
5.0
FIGURES ....... .......... ......... — .,
_1
Figure1- Site Location
Site Plan
Pi - OperationalSchematic of Proposed Treatment System
Figure - Typical Recovery Well
Figure -' y o loie Profiles
Proposed'Infiltration Chile - Plan and Section Details
6.0
SOILS SCIENTIST'SEVALUATION
RECOMMENDATIONS....... .. ... ....... .. .... ........ ,
_ 1
7.O
TECHNICALP CI A A AC' ' LITERATURE-1
.+
.... ... ... ...
Drawing I - Site Plan
DrawingUtility Trench Plan and Sections
Treatment y tetEquipment Plan
APPENDICES
Appendix I w Test Boring Records
Appendix H - Infiltration Gallery Design Calculations
A - Laboratory Analysis

Department of Environment, Health, anNatural Resources
Division ofEnvironmental Management
Non -Discharge it Application
(THISAI* BE PHOTOCOPIEDFOR USE AS AN O
SEPTICE PIPE / GRAVITY
SUBSURFACE SYSTEMS
IFOR MECHANICAL TREATMENT Y
SUBSURFACE DISPOSAL USE FORM MTDS1
(THE DIVISION of ENVIRONMENTAL MANAGEMENT HAS JURISDICTION IF THE SYSTEM
TREATS INDUSTRIAL WASTEWATER OR IF THE SYSTEM IS OWNED BY A SANITARY
DISTRICT, A METROPOLITAN SEWAGE DISTRICT, A WATER & SEWER AUTHORITY, A
COUNTY, A MUNICIPALITY, OR A PUBLIC VTILITY. THE DIVISION OF ENVIRONMENTAL
HEALTH HAS JURISDICTION FOR OTHER DOMESTIC SUBSURFACE SYSTEMS)
L GENERAL INFORMATION:
1. Applicant'(o gyration individual, or otherMARTIN t RI TT . CORPORATION
TON
. Print Owners or Signing ffi i l's Name and Title (the person Who is legally
responsible for the facility and its compliance): NCR WILLf ART COL
F Mailing Address:tTI=R I't At rr
City: _ LITTLETON State: C 0 Zip* 80120
Telephone o.: 303 971-1885
4. Project Name (subdivision, facility, or establishment name - should be consistent with
project name on plans/specs., letters of flow acceptance; Operational Agreements, etc,):
FURR Ptr z TI
5. Application ate; 4-3-92 6. Fee Submitted: ` � 0-0
7. County where project is located: MECKL ` %3UR
8. Address of treatment and subsurface facility; NC HIGHWAY 7 AT LONG CREEK
(ERR FIGURE ; FOR SITE PLAN)
9. Latitude: 35' 1 7' 5 " Longitude: 0° S « " of subsurface fields
FORM: LPPG 4/91 Page 1 of 1

PAGE 2 (4/9 1)
!L PERMIT INFORMATION:
1. Permit No. (will be completed by DEM):
If this application is being submitted as a retolt of a renewal or modification to an
ttistingi;trai� list the exisfingpetmitournbor N��.Ahaissutdate,-Lx
4. Spocifywitetherthoapplitahtis,,'' —private,
poblk or X
S. Spe.64 whether applicant is* _ sanitary distritt._� metropolitan sewage district;
wate+ oeityl -- county; public ufifiry;
am) tQZ= �,A�QLI�t STATION ZELL
3
1. Nat= of Wislt*Ote� Dotnestic-, % Com�l
% Industrial; —iu % Other waste (specify): TMPkL=, L2jJJJJJL IJ4%TR'R
2,. please provide a one or two word description specifying the Origin of the wa=water�
4 industria�
such as scho6l, siIMVisidb n, hospital, cmth6176 In
11��ACTED LLIU� �61111 , -- I — I
3. If wastewater is not domestic in nature, what level of pretreatment has been provided
J-IAJ�Kr�()R �,IILL REMOVE FU,,E
to ensure protection of the receiving treatment system: —0 —IL—,A—qA —rE L —SE� OPERAT""NA
PRODUC 'SIGN 7200 gallons per daSCH'MATI'
4. Volume of wastewec
ater, generated by this projt: y
5. Exp Ian and of how w ast to water volume was Bete in �PT �:s 1 �tNq ', 0 N �x c'-' '�LOVERY
DA'1 - A PICA 1,1)1 "ATEI'l A KA,11M PUMP �1ICIM �11'-Mrillxl �111111-11-1 �011-11 �11Y'11�1;11-
on
Brief project description: IMPACTEI) GROUND WATER IS PUMPED TO AN 0,1L/WA'rER SEPARATOR. WIIER,-r.A..
rf7V DDtIrITTOT IV vT?P(z4'VT1 LYTTT R.V.�VPARATFI") F'ROM TTIT' RECOVERED CROUND WATER. ALL WTAT]"'R
FROM
IV. DESIGN INFORMATION:
1 Specify the type of system that is being installed: low pressure',
FATL�R STE ik I
gravity; L
other TOTAL ITX0VERY SYSTEM,-IIIPACTED GROUND Ga�F , �T,'
77 1 7, 7; -c7 V - 11 F] < 0'X I NE 717 ,1-.,,jT'.DMiN'r FOLLOWED BY AN 17NFILTRIMON
GAM LEIRY
2 of 10
*SYSTEII. HOWEVER, 11202 INCREASES THE OXYCEN CONTENT IN THE TREATED EFFLUENTS FR01M THE UV-PE11,0XID1,
UNIT, TITUS, ENIHM'41.NG CONTAMINANT DECRADAIA,ON, IN TITS AQUIFFR.

LOW PRESSURF-/GRAVITy
PAGE 3 (4/9 1) ',
*2. Provide a brief listing of the compot"ents of this treatment and disposal system (if not
covered by specific questions below), including dimensions, capacities, loading rates,
and detention times of tanks, Pumping facilities (duplex pumps), high water alarms,
filters (specify type), ponds, lagoons, disinfection facilities, subsurface fields. etc--
7. The fDIlOwing criteria should be used for the sizing of residential septic tanks:
a- three bedrooms or less, use minimum 900 gallons;
b. four bedrooms, use minimum 1000 gallons;
C. five bedrooms, use minimum 1250 gallons.
8. For businesses with a design flow less than 600 GPD, the minimum tank capacity shall
be twice the flow.
3 of 10

LOW PRESS URF,(GRAVITY
PAGE 4 (4/91)
9. - The following criteria should be used for the sizing of septic tanks for residences with
more than five bedrooms, multiple family residences, tanks serving two or more
residences*, or establishments with a flow between 600 GPD and 1500 GPD:
Septic Tank Volume = (L 17) (daily sewage flow) + 500 gallons
*Minimuna septic tank capacity shall be 1500 gallons
10. For design flows between 1500, GPD and 4500 GPD, the following criteria shall be
used: Septic Tank Volume = (0.75) (daily sewage flow) + 1125 gallons
11. For design flows which exceed 4500 GPD, use a septic tank capacity equal to the flow.
12. Specify the septic tank Volume: _ NZA gallons
13. Specify the pump tank volume:, NA gallons
14. Specify the number of pumps and their capacity- --I— pumps at —aL---L-OGPM
15. Specify the high water a ETA BI,Eaidable & visual; sFF,_UW.L_I_ auto dialer
16. Name, of closest downstlope surface waters: .. U i.oN,, . cF�F _c_ Y�
17. Classification of closest downslope surface waters: C (as established
by the Environmental Management Commission and specified on page 7 of this
application).
18. If a power failure at the facility could impact waters classified as WS, SA, B, or
SB, describe which of the measures are being implemented to prevent such impact, as
required in 15 NCAC 2H.0200: THE SYSTEM IS EQUIPPED WITF A SAFETY FEATURE
. SUCH THAT DURING A POWER FAILURE THE ENTIRE SYSTEM WIIJ, BE SHUT DOWIN
19. The different disposal fields, laterals, or groups of laterals in a subsurface system are
typically designed to be dosed at different rates or volumes from one another. Explain
the method that will be used to ensure that the proper dosing rates and volumes occur:
20. The project must conform to the following buffers:
a) 100 feet between the disposal area and any public or private water supply
including wells;
b) 50 feet between disposal area and waters classified as WS-1, S-II, WS-Ill
or B; and 100 feet between the disposal area and the normal high water
level of waters classified as SA or SB;
c) 50 feet between any the disposal area and any stream, lake, river, or
natural drainage way;
d) 50 feet between the treatment/disposal systems and property lines;
4 of 10

LOW PRESSUREIGRAVITY
PAGE 5 '
(4 1
10 feet between the disposal area and any surface water interceptor drains
or diversions (ups o e
feet between the disposal area and any surface water intercepter drains
or diversions (downslo d any groundwater drainage systems;
feet between disposal area and any other subsurface disposal area
except the repair
1+ If any of the applicable buffers are are not being met, please explain how e proposed
buffers 1 provide equal or better protection of the Waters of the State with n
increased potential for nuisance conditions: THE INFILTRATION CALLER' IS DESIGNED
SUCH THAT IT IS ENTIRELY WITHIN THE CAPTURE ONE OF THE RECOV S
THEREBY CREATING A CLOSED LOOP HYD IILZC a TES T TII +

LOW P tT
h. For systems "
g industrial waste or any system with a design flow greater than
GPD ahYdrOgeOlOgic and soils description of the subsurface to a depth of twenty
feet Or bedrock, whichever ;is less. The number of rings shall be sufficient to
determine significant changes in lithly, the vertical permeability of the unsaturated
zone and the hydraulic conductivity of the saturated n , depth to the mean season
al
high water table, and a dete ination of transmissivity and specific yield of the
unconfinedaquifer,
i. Proposal for groundwater monitoring.
. Information on the location, construction details, and primary usage of all wells within
500 feet of the treatment/disposal facilities.
k. dr industrial caste a complete chemical analysis Of the typical wastewater to include but
not be limited to Total Organic Carbon,
Chlorides, Phosphorus, Ammonia,
Nitrates, Phenol, Total Trihalom thanes, Tonicity 'Vest Parameters, Total Halogenated
Compounds, Total COlifOrms, and Total Dissolved lids.
cf 1

LOW PRESSURF
PAGE 7 (4/91) JGRAVITy
TO: REGIONAL WATER QUALITY SUOERVISOR
Please provide me with the classification of the surface waters identified in number 5
below and on the attached map segment:
Name of stitface, waters:
Classification (as established by the Environmental Management Commission):
Proposed Classification, if applicable:
Signatum of regional office personnel: Date:
gy
INSTRUCTIONS TO ENGINEER
I. Applicant (corporation, individual, or other): MARTIN MARIETTA CORPORATION
2. Nam and Complete Address of Engineering Firm: LAW _ENVIRON`MENTAL, INC.
4333 WILMONT ROAD, SUITE 300
City: ----CHARLOTTE--. State: NC Zip: 28208
Telephone No.
3. Project Name: EE BEET
4. Facility design flow TtGPD
5. Name of closest downslopo surface waters: L_0NG CIEEK
6. County(s) where project and surface waters are located: MECKLENBURG
7. Map name and dittv, AD-7.5 MIN, 1969.
8. North Carolina Professional Engineer's Registration No.
9. Print Name of Engineer MR. KEITH A. ANTHONY
10. See and Signature (specify date): "o' "
CAqo
V/",

ENVIRONMENTALN.
DIVISION OF
A
Asheville1 n
59 Woodfin
Washington 'n 'u
F 0 Box
Raleigh Regional wQ Super.
Asheville, NC 28802Washington.
1507
NC 27889
1)ra, Suite 10 1
7 1 2
9194 1
Ralcigh, NC 27609
919/733-2314
Avery n
Buncombe Madison
Beaufort
Chatham Nash
Burke McDowell
Berde s>e'
Camden Martin
Durham Northampton
MitchellCherokee
hts ;Pamlico
rn be Orange
Polk
Clay Ruthoerford
Craven unPerson
Currituck
Franklin
Granville Vance
Graham Swain
Perquimans
Date Fitt
Halifax Wake
HaYWOW l
Henderson yancyGreene
11
Johnston
Wilson
Jackson
Washington
Herdord Wayne
Hyde
Fayetteville a Super.
" oil71
WaChovFayetteville,
M00resville, Regional WQ Su
919 Nn its
Wilmington Region. super
NC 2S301
Mooresville, NC 28115127
Cardinal Drive Extension
91 /4 1541
/ 5-1 99
Wilmington, NC 0 - S
`
919/395-3900Anson
Moore
Robeson
Al"ander
MecklenburgBladen
Csbanus
New+ yr
Cumberland Richmond
Rowan
Catawba Stanly
CmImet. Onslow
Hamett
e Sampsonl+ln
Union
Columbus
ulin
ntutxt
Cleveland
Lincoln
Winston-Salem egi Super,
8025 North Point Boulevard,Suite 100
Winston-Salem, NC 27106
919/7 1-2 51
RockinghamAlamance
Alleghany Randolph
StokesAshe
Caswell Suiry
Davidson Watauga
Davie Wilkes
Forsyth n;
Guilford
8 Of 1

LOW PRESSLTREIGRAVTI'Y
Page
Name and Complete Address of Engineering Fi m LAW ENVIRONMENTAL
City.- CRARLOTTE State: NC Zip: 28208
«'rohssjonal Efioneer's Ceitificttion..
w �rw w r w . w � _w, .•. �w .� .w �
w«,. w � w ws °• w.
w M
Applicant's Certification:
attest that this application for MARTIN MARIETTA
has been reviewed by tie and is accurate and complete to the best of my knowledge. 1 understand
that if all required parts of this application are not completed and that if all required supporting
information and attachments aTe not included, this application package will be retumed as
incomplete. P
/f .
Signature _ � ateTHE COMPLETED APPLICATION PACKAGE, INCLUDING ALL SUPPORTING
INFORMATION AND MATEPJALS, SHOULD BE SEND' TO THE FOLLOWING
NORTH CAROLINA; i i V MANAGEMENT
WATER QUALITY SECTION
PERMITS AND ENGINEERING UNIT
POST OFFICE
512 NORTH SALISBURY STREET
RALEIGH,NORTH CAROLINA 27626-0535
TELEPHONE NUMBER: 9191733-5083 1

LOW PRESSUREIGRANTrY
Page 10 (41)
PERMIT APPLICATION PROCESSING FEES
(effective etber 1, 1
MODTICAMNS
MODIRCATIONS
1
dtts
$300
10,001 - 1
Industrial
DomesWCoolingat
1
1,001 - 1,
Industrial
Domestic/Cooling Water,
or = 1,
Single Family Dwelling
$4$120
Sludge < or = 300 Actes
4'
Sludge > 300 Acres
Sewer Extensions
o dele
Seweract sip
(delegated)
Closed -Loop Recycle
Evaporativeor
NOTE: The Fees for Soil Remediation Projects are
the same as for Sludges.
Underthe Sewer Extension
Fee, "delegated
tomunicipalities"' applies
only to those governmental
jurisdictions .
that have specific delegation
review tort , as granted by the
Division of Environmental
Management.
10 of 1

TABLE I
TREATMENT/DISPOSAL SYSTEM
FURR PROPERTY
MECKLIMURG COUNTY, NORTH CAROLINA
LE[ JOB .-
Equipment
Loading Rate (Q) Dimensions Volume
Detention
LxWxH
Time t
t
Oil/Water
t ft x 1.75 If x 1.42 ft 7.46 fe
14.63 min.
Separator
(0.51 fe/ in
UV -Peroxide
3.8 gpm 3 ft x 4 ft x 5 ft 60 ft'
117.65 thin.
Treatment Unit
f
Infiltration
3.8 glint 100 ft x 20 ft x 4 ft
Gallery
fete rest
Oil/water separator:
high level shut off switch
Product storage
high level shut off switch
Equalization k::
low level shut off switch
high level system on switch
h
high -high level shut off switch
UV-P,eroxidation unit
auto dialer is installed
alarm and/or automatic system shutdown for flow conditions
out of range
alarm and shutdown on lamp failure
alarm n lamp overheating
alarm d shutdown n n reactor high temperature
alarm d shutdown on UV access covers
alarm when transmittance controller fails to operate
alarm and shutdown, can lower air pressure
8 55 : .T1

ORIGIN,2.0 DESCRIPTION OF THE TYPE L
TO BE TREATED AND WASTE ANALYSIS
o property wasleased and operated as a gasoline service station. gasoline station ceased
operations in ay 18. The generalsite location and site I shown on :figures
respectively.
Law Environmental (and previously Law Engineering) has been providing assessment services
at the subject site since 1986. or r initiated following apparent leakage from underground
gasoline and other petroleum product r piping at the site. The tanks have since been
removed eight monitoring wells and; one recovery well have been installed on -site. The
locations of the swells are shown on Figure 2. after several phases of assessment, the extent of
petroleum contamination in ground water has been reasonably defined. Quarterly monitoring
at selected wells has been conducted for almost two years. A summary of the most -recent test
results indicating the presence of NME, Benzene, Toluene, Fthylb n ono, Chloride and Total
Suspended Soli SS is shown on Table(Waste nalysis
o proposed location of recovery wells RW-2 and R`W-3 are shown on Figure 2, if free
product is present in any of the recovery ells, it will be separated from the ground water and
recovered in the oillwater separator. Effluent from the oil/water separator will be discharged
to an equalization,It to achieve a constant flow to a -Peroxide treatment system for volatile
organic compound removal. Effluent from the UV-Peroxidetreatment will be reinjected
into the underlying shallow aquifer via an infiltration gallery. The operational floe rate is not
expected o exceed
s 5- M

TABLE 2
SUMMARY
A" l A TES -MG
FURR PROPERTY
CIIARtMIE, NORTH CAROLINA
LER 3
l.ab ratory
tory
Laboratory
detection limit
detection
-1
MW- Mir"- M -
-
-6
-7
-
Rom'-
Parameter
(n /l
limit ( /1
(n /1
(Lt /1 (d /l) (n /l
C /l�
n /l '
�t fly
(��1�/l
(n€1/l
( /1)
(MW-1, 2,, 3, ,
d
6, i°, Q)..
—I a
_.
Date
1 /30/ 2
1 /3t / 2 1130/ 2 1 /3 / -2
1 /30/92
1 /30/
1 /30/ 2
1 /301 2
1/30/92
MTBE
5.0
25
430 553
NOD 6.5 800
NTH
18
47
Ni
70
Benzene
Lo
5.0
30.3 8A
ND 1.3 160
Nib
ND
ND
N1
60
Toluene
1,0
5,O
1.6 1.5
ND 3A Nip
N13
NO
Nib
ND
1
Ethylbenzene
Lo
5.0
11.3 L2
Nil ND 40
ND
NOD
ND
NO
30
yl n , Total
2
10.0
24.7 O3
ND, 9,5 70
NOD
ND
ND
ND
60
COD
5 mg1l
5 ni d,
NA
NA NA NA
N.A
NA
NA
NA
NCB
Chloride rid
Oi 2 rngll
02 mg, /I
NA
NA NA NA
NA
NA.
NA
NA
l l ntS/l
TSS
111-mg/l
10 cell/l
I NA
NA, NA NA
NA
NA
NA
NA
490 K /l
ND , Not detects above laboratory detection limit
NA - Not analyzed
*Constituent etmeentrations are based pan triplicate analyses for 141'? -la
'nie values in the table represent the average the standard deviation,

TABLE 3
REMOVAL EFFICIENCY OFUV-PEROXIDATION
FURR PROPERTY
MECKLENBURG COUNTY, NORTH CAROLINA
L1 JOB NO.56-8555-005
Influent Concentration Effluent Percent Removal
Constituent (u /L) Concentration efficiency
(u/L)
Benzene 60 < 1 > 99.9
`toluene 1. < 1 > 99.9
Ethylbenzene 30 < 1 > 99.9
r 3
Recovery well (R d-1) data, from January 30, 1992, water sampling al s s. Laboratory
and chain -of -custody records `are provided in Appendix 11.
U -Pero i l Lion system is designed to remove above 99.9% for benzene, toluene,
ethylbenzene and xylenes and above 93 for MTBE.
95s - .TI

3.0 FOLLOW-UP SITE MONITORING AND PLAN EVALUATION
A monitoring program will be initiated after activation of the recovery and treatment systems
to assess its effectiveness. The monitoring program will include:
I. Quarterly field measurements of ground -water levels in the monitoring wells to verify the
dimensions of the ground -water capture one.
2. Measurements of flow rate from the recovery wells to the treatment system to check the
placement and efficiency of the recovery pumps, and measurements of the effluent flow to
from the treatment system. The measurements will be performed in accordance with the
requirements of the discharge permit.
3. Quarterly sampling and laboratory testing of ground water from selected plume perimeter
and inside -perimeter monitoring wells to document recovery of the ground -water
contamination plume. Laboratory testing will be performed for Class I petroleum -related
ground -water contaminants, specifically benzene, ethyl benzene, toluene, xylenes, and
MTBE. All parameters that show positive identification will be reported. The laboratory
test will be performed using EPA Methods 601 and 602 or comparable documented
methods; the report will include method detection limits.
4. Sampling of the water treatment system influent and effluent to document effectiveness of
the system in removing the ground -water contaminants. The sampling will be performed
for the parameters and at the frequency required by the non -discharge permit.
The remediation program will be re-evaluated after each sampling and testing episode to monitor
the effectiveness of the ground -water recovery system and of the water treatment system.
Adjustments to the recovery pump flow rates and of the operation of the water treatment system
likely will be necessary to obtain the optimum contaminant capture and contaminant removal
efficiencies.
8555-AIMMO 3-1

4.0 SOILS AND HYDROGEOLOGIC: DESCRIPTIONS
4.1 Solis Description
Three soil test borings, B-1, B-2 and B-3, were drilled at the site on May 16, 1991, to explore
potential soil contamination in the vicinity of the previous kerosene -tank and gasoline -tank pit
areas. These borings were drilled to depths of approximately 15 ft below the existing ground
surface. The general subsurface conditions encountered in the borings are indicated in the Test
Boring Records provided in Appendix 1. The locations of the borings are noted on Figure 2.
Fill material was encountered at boring B-1 to near the termination depth of about 16.4 feet.
Fill material extended to an approximate depth of 10 ft in borings B-2 and B-3. Alluvium was
encountered beneath the fill material in those borings to a depth of 15 feet (termination depth).
The fill material encountered consisted of sandy silts, silty sands and silty clays, The alluvium
encountered in borings B-2 generally consisted of silty clay. The Test Boring Records represent
our interpretation of soil, conditions at the borings based on our "animation of the soil samples.
The lines designating the interfaces between the various strata represent approximate boundaries
and the transition between strata may be gradual.
Eight monitoring wells were also installed on -site. The general subsurface conditions
encountered in the wells are illustrated in profile on Figure 5. The locations of the profile lines
are shown on Figure 2.
' ^ ,''"' 4°1
`

4.2 Hydrogeologic Description
Inflow permeability tests were performed at wells MW- I and MW-3 to estimate the hydraulic
conductivity of the formation materials exposed to the screened interval at each well location.
Hydraulic conductivity (K) is a constant of proportionality relating to the ease of which fluid
passes through a porous medium. Theflield procedure used to measure hydraulic conductivity
is as follows:
* measure the stabilized water level in the well:
a remove water from the borehole by bailing; and
# measure the ground -water level as it recovers to the static level.
The data were reduced and saturated hydraulic conductivity of the screened interval was
calculated using a computer program based on the variable -head method (NAVFAC DM-7. 1).
The average horizontal saturated hydraulic conductivity (KO for MW-1 and MW-3 was
determined to be 3.0 x 101 cm/sec (Report of Continued Assessment and Quarterly Sampling,
dated July 19, 1991). The vertical permeability (Kj was estimated from the field horizontal
saturated hydraulic conductivity data by employing the following ratio:
5: 1 = Kl,:K, (from Walton; Freeze and Cherry).
The infiltration gallery design calculations using the above vertical and horizontal permeability
are provided in Appendix 11 of this application. An average & value (1.8 x 10' ft/min)
obtained from the Soil Conservation Service (SCS) data for Mecklenburg County was used to
verify the estimated average K, value (1.2 x 10' ft/min). Although the values were not
significantly different, the K, value obtained from SCS data was less conservative than the
estimated value. Thus, the estimated K, was utilized in the design of the infiltration gallery.
8555-AIM,TIO 4-2

Water levels at this site were measured during the quarterly sampling episodes for about 3 years.
The approximate depth to high water level at this site was found to be feet.
soil evaluation of the site conducted by Mr. Fred Smith, a ails scientist with Law, is included
in Section 6.0 of the Application. This comprehensive soil evaluation includes field descriptions
of soil and hydrogeologic characteristics, d infiltration gallery recommendations.
8555-A M,TI 4-

1

ENGINEERINGla
LAW
GEOTECHNICAL, ENVIRONMENTAL
CON TRUCT�ON MATERIALS
CONSULTANTS
March 31, 1992
Law Environmental
P. 0. Box 240674
Charlotte, N.C. 28224-0674
Attention: mr. Chalam Pakala
SUBJECT:
LAW PURR PROPERTY
ENGINEERINGLAW J' - " 1
Dear Mr. Pakala:
Law Engineering had completed the soil testing and groundwater
mounding l ulati a for the project described above. Our report
includes our understanding of the preset; information, study
methods, a description of the site and soils, the results of our
testing and our recommendations for the design loading rate.
We have appreciated bein r l to u in the exploration
phase of this project and are re ar d to assist you further.if
you have any questionsconcerning this is si ` or any of our
testing, inspection, design_and consultingservices, l a e do not
hesitate to contact
Very truly yours ' 0; `r,�!
w
w.qt g# i
LAW ENGINEERING
.m r
V I. t u �t5i' niA�
d Zle,
Fred D. Smith
+�'yn may. y�,���yTM per, �pr� �Wl. i. 'w�rt ` P.E.i. .b�A
Principal Soil ienti f Principal'°€ eot hn . al Engineer
Certified No. 2312 Registered, N. C. 11285
FDS/BCH/pap
Attachments
3301 <ATLANTIC AVE.
P.OOX 18288
RAEEGH, NC 27619
91 .876-0416

Ak
PROJECT INFORMATION

� Vk
., results
in
sampling "ted
i�aodrted to

we compute an average transmissivitY of the aquifer to be 11.91,
ft2/day using an aquifer thickness of 14 feet.
We -
calculated the maximumheight of the groundwater mound under the
infiltration gallery using Recharge Groundwater Model. The
Recharge l data r rcvi e n the Appendix.
following parameters
0 a loading rate of .096 f / y 1 gallon/minute or
1,440 gallons/day),
91 ft d
' tran;� is iv /
r
depth to the bottom of the gallery of 4 feet
low the existingsurface,
depth to groundwater of 8 feet from the bottomof
the gallery,
the model lculate as maximum groundwater ound height of
approximately 2.5 feet as shown in Drawing No.
3.
CONCLUSIONS
Based our soil evaluation and the results of the permeability
tests, a expect treated groundwater to infiltrate the saprolite
sails at a rate of 3x104 cm/sec and to percolate downwardto the
groundwater aquifer. in addition, we expect e lateral movement
of water in the unsaturated ne toward n Creek. The movement
f treated water through the soil will provide additional treatment
of the contaminated water. Increased rates of flow might
be
achievable if the actual saturated thickness is greater and/or if
the actual transmia i ity is higher than the value used for tress
calculations.
s

RECHARG
TRANSMIS
SPECIFIC
BEGINNIFi
FINA
TIME INC
TIME F C
BEGINNING I
FINAL DI
DISTANCE IC
STREAM 1
MOUND
STREAM I
TIME
(DAYS),
5
5
5
5
5
5
5
5
5
%too
%100
%100
%too
%100
10
%100
%100
%150
%150
%am^'15
%
V
150
%150
%150
15
%150
%200
pg:
420
%200
%200
%200
%200
%200
%200
%250
25
%250
RATE =
. AY
IVITY =
11.91 .FT Y
YIELD =
.15
TIME
50 DAYS
TIME =
350 DAYS
�EMENT =
50 DAYS
350 DAYS
TANCE =
100 FT
XMENT=
25 F
DEPTH
F
WIDTH20
FT
,ENGTH =
100 FT
DEGREES
;TANCE = 10 FEET
t FIL YES
YES
DISTANCE HEIGHT
FT FT
0
3.904
25
3.496
5
3.33
0
2.25
50
2.4'
75
0.843
75
1.264
100
Q.
100
0.742
4.464
25
4.019
25
4.252
50
2.630
50
3.220
75
1.127
75
1.943
100
0.000
100
1.265
0
4.741
25
4.255
25
4.555
50
2.914
50
3.43
75
1.224
5
2.251
100
0.000"
100
1.605
5.043
25
4.5�� 2
25
.04
50
3.017
so
3.2
75
1.277
75
2.355
100
0.000
100
1.671
_
5.13
25
4.15
25
5.15

%250
__
5="
3
%250
50
3.74
%250
75
1.31
%250
75
2.489
%250
100
0.000
%250
100
1.800
,%300
0
5.247
%300
25
,
4.681
%300
25"
5.115
%300
50
3.129
%300
50
4.027
%300
75
`
1.,334'
%300
75
2.593
%300
100
0.000
%300
100
1.`'91
%350
0
5.31
%350
25,
4.3'
%350
25
5.19
%350
50
3.162
%350
50
4.111
%350
75
1.351
%-350
75
2.5
%350
100
0.000
%350
100
1.984
DISCHARGEO
STREAM
DISTANCE5
GEC
ALONG1
STREAM
1 FOOT
LENGTH
(FT)
T
. . /DAY)
50 DAYS
0.0342
.4
5
0.0338
0.4
10
0.0333
0.4
20
0.0309
0.4
40
0.0246
0.3
so
0.0120
0.1
160
0.0000
0.0
DISCHARGETOTAL
+5.7772+1
CUBIC FT./DAY
100
DAB'
4
0.0430
.5
5
0.0426
0.5<
10
0.0420
0.5
20
0.0395
0.5
40
0.0325
o.4
0
0.0181
0.2
160
0.0054
0.1
320
0.0000
0.0
TOTAL
DISCHARGE=
+9.3
10
+ 1 CUBIC FT./DAY
150
DAYS

0
0.0470
0.
5
0.0465
0.
10
0.0459
0.
20
0.044
0.;
40
0..062,
0.4
0
0.0214
0.
160
0.0000
0.;
TOTAL
DISC 8.85680E+01
CUBIC
FT./DAY
200
DAYS
0
0..041
0.6
5
0.0457
0.
10>
0.0481
0.6
20
0.0455
0.
40
0.0383
0.5
so
0.024
0.
160
0.0077
0.1_
20
0.0008
0.
640
0.0000
0.
TOTAL
DISC 1.21161 02 CUBIC
FT./DAY'
250
DAYS
6
0.0505
0.6
5
0.0501
0.6
10
0.044
0.
20
0.0469
0.'
40
0.07
0.5
0
0.024
0.
160
0.0087
0.1
20
0.0019
0.
640
0.0000
0.0
TOTAL
+ I
DISCHARGE -�1:.56_ 02
. AY
00
DAPS
0
0.0514
0.6
0.0510
0.
10
0.0504
0.6
20,
0.047
0.6
40
0.0406
0.5
80-
0.0255
0.
160
0.0094
0.1
20
0.002`6
0.
640
0.0000
0.
TOTAL
DISC = +1.42 86 02
CUBIC
FT./DAY
350
DAYS
0
0.0521
0.6
5
0.0517
0.6

RECHARGE.13
FT/DAY
TRANSMISSIVITY=
11.91 . F AY
SPECIFIC YIELD
= .15
BEGINNING I
0 DAYS
FINAL TIME
350 DAYS
TIME INCREMENT
= 50 DAYS
TIME OF CUT OFF
= 350 DAYS
BEGINNING DISTANCE
FINAL I
100 FT
DISTANCEINCREMENT
= 25 FT
F
WIDTH20
F'
LENGTH100
F
,
ANGLE0
DEGREES
STREAM DISTANCE
= 100 FEET
MOUNDPROFILE
F
STREAM DISCHARGE
YES
TIME DISTANCEHEIGHT
(DAYS)
)
FT
50
0
5.274
50
25
4.71
so
25
4.905
50
50
3.046
50
5o
3.369
so
75
1.13
50
75
1.70E
so
100
0.00
50
100
1.001
%loo
%loo
25
5.426
%loo
25
5.740
%100
50
3.551
%100
50_
4.347
*100
75
1.521
too
75
2.623
%100
100
0.000
l q
100
1.70
%150
0
5.400
150
25
5.745
%150
25
6.149
%150
50
3.933
%150
50
4.641
tiso
75'
1.52
%150
75
3.080
%150
100
2.166
%2,006.807
%200
25
5.11

%200
25
6.399
%200
50
4.073
%200
50
4.86
%200
75
1.724
%200
75
3.17
,%200
1
%200
100
2.255
%250
0
6.7
%250
25
6.3
%250
25
6.772
%250
50
4.162
,%250
50
-
5.081
%250
75
1.77
%250
75
3.36
%250
100
0.000
%2
100
2.43
%300
0
7.4
%300
25
6.31
%300
25
6.906
%300
50
4.224
%300
50
5.436
%300
75
3.501
%300
100
0.000
%300
100
2.566
350
0
7..16
-%350
25
6.385
%350
25
76
%350
50
4.26
%350
50
5.54
-%350
75
1..624
%350
75
3.847
%350
100
0.000
%350
100
267
DISCHARGE TO STREAM
DISTANCE5
GEC
ALONG
AT
T
STREAM
1 FOOT
ZIT
"
FT (
Y )'
50 DAYS
0.0462
0.6
.456
0.5
10
0.0449.5
20
0.0417
0.5
40
0.0332
80
0.0162
o.2
160
0.0000.
TOTAL
DISC = +7.798E+ 1 CUBIC FT./DAY
100
DAYS
0.0581
0.7
5
0.0575
0.7
10
0.0567
0.7
20
0.0533
o.6

40
0 0438
0.5'
80
0.0244
0.>'
160
0.0073
0.1
320
00000
0.
TOTAL
DISCHARGE+1. 2663 +0
CUBICFT./DAY
150
DAYS
.0634
0.
5
0.0628
0.
10
0.060
0.7
20
0.0585
0.7
40
0.0489
0.
80
0.0289
0.3
160
0.0000
0.
TOTALDISC
- 1.15 +02 CUBIC
FT./DAY
200
DAYS
0
0.0663
0.
5
0.0657
0.8
10
0.0649
0.8
20
0.0614
0.7
40-
0.0518
0.6
0
0.0315
0.4_
160`
0.0104
0.1
320
0.0011.
0.0
640"
0.0000
0.0
TOTAL
DISCHARGE
= +1.. 15 1 +0 OFT./DAY
250
DAYS
0
0.0681
0.
5
0.0676,
0.
10
0.0667
0.
20"
0.0633
0.
40
0.0536
0.
80
0.0332
0.4
160
0.0117
0.1
320
0.0025
0.0
640,
.0000
0.0
TOTALDISCHARGE
+1 .80334 +02
CUBIC
FT./DAY
300
DAYS
0
0.0694
0.
5
0.0688
0.
10'
0.0680
0.
20
0.0645
0.
40
0.0548
0.
0;
0.0344
0.4
160
0.016
0.

1 ar 1
t
d r " I „e-�..,.,w �.� p +, a � '� � ,,`, ate, S�"m •���' "� �" , � "�
*
�cp
to
y M: (d"a�"`t"`-�.a� �, , � "`e� �, ea � ��w�. � `� � ��w P°x�,j •q � � '"• pr � R_..,�� 't
�, �, ......" ''� . °tea.. `��' < '`�`*'„a w. a ° *�°" ' y �"-•� r .�'.'
� s,.,,,�,,.. `wM r^ p°.="'\.r� tit '� '�� � �`'ae"`: '�a ��� ��"" ,•. j' e!
t..
}r
y V
_
R
OWN
wrwwuuw
CHARLOTTE,LAW ENVIRONMENTAL, INC.
SITE LOCAMM MAP
11W
409
w 944MM
FIGURE

i
ui
G
h
TABLE10
GROUND-WATERLAW
I E I
PROPERTYFURR
L I
LI N
CHARLOTTE, NORTLI
DRAWN.-
ENGCiEC
FEB. 1 :
°i
4- -1
`T :
SCALE: NOT TO SCALE DWG:
3
EE E E: FIELD
NOTES

CompactThe can t ` r developed
to measure the saturatedhydraulic conductivity (R.) of the
v do (unsaturated) zone. The instrument determines
utilizing per techniques su the shallow well n method,
borehole t r, or borehole infiltration test. Thesemethods
are describedin many publications including it
Analysis" published by the aerie oci ty of Agronomy.
The ccHP measures -to a depth of two teas below the soil
surface. Measurementdepth can be increased y additional sets of
constant head tubes and a portablepressure measuring device.
The measures the in - situ K, of a soil layer by creating
constant n head of water at the selected s th of measurement by a
series of pressure regulatingl of water called constant head
tubes. Basedon a steady state flow rate from e cylindrical auger
hole under a constant head of water, the Glover solution can be
used to calculateKsat. The tion is
Ksat
flow of water
The Glover solution sn n the depth of water in the hole ( �
the radius of the hole(r) , and thesteady tad flow rat ( .
1

PROCEDURE
. Select the landscape where e` ur f Y.. is desired.
» Describe the soil profile.
» Bore a 6-cm diameter hole to desired
» Plane andclean the bottom of the augerl i the n
laver»
5. Measure and recordthe distancechole to
LEVELthe REFERENCE on the permeameter.
. Connect the constant head tubesit tubes as directed
the manual and turn the eameter on to fill; the hole it
water.
7. Allow the permeameter to achieveconstant of t r i
the hole. This providesto i ; of the it at the depth
measured.to be
Start8. nt of flow rates to determineif steadystate
conditions hav en accomplished.
9. After t .nin three steady flow rates, a r nrecord
the depthwater in the cl .
10Record all field ata and calculate K»

TECHNICAL SPECIFICATIONS
AND
MANUFACTURER'S LITERATURE
GROUND -WATER RECOVERY/TREATMENT SYSTEM
AT FURR PROPERTY
MECKLENBURG COUNTY, NORTH CAROLINA
FOR
MARTIN MARIETTA CORPORATION
LITTLETON, COLORADO '00'04 11
Ro
j /6k tssfo s
%
Al
APRIL 1992 427G i N
A
.. tilt,
04,41soolit'
OWNER: MARTIN MARIETTA CORPORATION
ENGINEER: LAW ENVIRONMENTAL, INC.
4333 WILMONT ROAD, SUITE 300
CHARLOTTE, NORTH CAROLINA 28217
LEI JOB NO. 568655005

CONSIRUCnON SPECIFICAnONS
MIO Stttnm� 4 Work
The scope of work includes trenching, furnishing and installing subgrade PVC piping and
associated fittings, including unions and valves, installing recovery vaultsfor the ground water
recovery system, and installing treatment system equipment on the pad including mechanical and
electrical hook-up. Also included are steel piping inside the building among treatment system
components.
The treatment system equipment is to be connected to 2-inch PVC total fluids and discharge
pipes described on Drawing 2 of 3. The connection between the recovery system (PVC pipes)
and the treatment system components (steel pipe) is the responsibility of the contractor,
Future work (not included in this contract) includes connecting pneumatic ground -water pump
system to control panel and air compressor and installing pneumatic hose and regulator for air
lift.
Law Environmental will furnish the following treatment system equipment components: a 5-hp
air compressor, an oil/water separator, a product storage tank, an equalization tank, a
UV -Peroxide unit, a hydrogen peroxide storage tank, transfer pumps, vaults, a flow meter, an
air conditioning unit, a heater, and a vent fan.
The contractor will be responsible for posting local permits necessary to perform the work.
Permits required by the North Carolina Division of Environmental Management (NCDEM)
Authorization -to -Construct and non -discharge will be provided by the owner.
Soil sampling and testing will be performed by a qualified testing contractor. Costs for testing
are to be borne by the Contractor. Copies of the test results will be forwarded to Law
Environmental. Based on the test results, Law will either accept or reject the work.
Temporary electrical power, water and sanitation facilities will be the responsibility of the
Contractor. Security of Contractor's equipment and tools will also be the responsibility of the
Contractor.
Upon completion and final acceptance of the work by the Field Representative, the Contractor
shall clean the work area to match preexisting conditions.
DIMION 2: SITEWORK
02100 Site Prepa-Ation
PULL__QLnZBI
This section includes utility locating and trench lay -out, for the recovery system.
SM.FMCON&SM

p —PrQdugcU
Not applicable.
_' ut
.1. Contact a utility locating service. Locations of underground utilities must be clearly
marked prior to initiation of trenching activities.
3.2 Lay out proposed nches from recovery wells to the treatment system pad.
10 Piping Fittings
:part 1 dnc
This section includes installation of PVC pipes and conduits in the trench but not inside of the
building
1.1 Comply with all laws, ordinances, codes, rules and regulations of local, stud and
federal authorities having jurisdiction; over any of the work specified herein.
RMLZ_PIMQcts
.1; Pipes, and fittings for ®inch hose conduits, -inch total fluids pipe and -inch PVC
discharge pipe shall be Schedule 40 Type 1 Grade 1 PVC and shall be pressure rated.
4-inch hose conduits shall include "sweep" DWV fittings.
2.2 The vaults shall be provided by owner:
2.3 Concrete used for the s' urexent of recovery well vaults shall consist of Type I
Portland -cement concrete, minimum 3000 PSI compressive strength at 28 days.
Part.3 E uiifon
3.1 The contractor responsible for this performance shall employ personnel who have been
qualifiedy training and experience for executing this Work.
3.2 Piping shall be aligned, connected, and properly supported. Install piping in longest
practical lengths, avoiding insofar as possible the use of short lengths and couplings,
Remove scale, dirt, grease, oil and debris from all pipes before installation. Pipe
connections shall be properly primed and glued with PVC cement. Construct pipelines
with as fear joints as possible. Piping shall stub -up into vaults as shown on drains.
Cap or plug open ends of all pipes and valves until final connections are made.;
.3 Ropes to be used later to pull hoses for pneumatic ground -water pumps will be installed
in the -inch diameter hose conduits Enos of ropes will be tied off to stub -ups inside
e recovery well vaults and on the treatment system equipment pad.
s ms

3.4 Backfill, trench with compacted crushed stone for pipe bedding.
3.5 Upon completion of the 2-inch to fluids pipe installation, a 75 psi pressure test shall
be conducted as directed by the Law Environmental representative before the trench is
backfilled. Seal ends of PVC pipes in vaults with duct tape.
3.6 Recovery well vaults and covers shall be installed as shown on drawings,
17 Exterior steel surfaces which will be in contact with grout shall be coated with a
grouting adhesive.
3.8 Clean crushed stone shall be placed in a 2-inch layer at the base of the vault excavation.
3.9 Portland -cement concrete shall be placed at the sides of the excavation to the top of the
vault. The concrete around the vault shall be at least 4 inches thick. Taper concrete
down away from vault to drain away surface water.
4,0 Concrete used in vaults shall be kept moist by spraying or by covering with moist
burlap or plastic for at least 14 days after initial placement. The finished concrete
surface shall be level with a smooth surface.
4.1 An additional 2-inch layer of crushed stone shall be placed at the base of the vault.
DWISIGN 11: EQUIPM[ENT
11300 Fluid Waste Treatment and Dispo&-d Equipment
Part I General
L)= 2 ErQd=
2.1 Four (4) 2-inch x 2-inch x 1/4-inch thick angle steel tabs for anchoring UV -Peroxide
unit,
12 Twelve (12) Phillips Red -Head Self -Drilling Anchors A307 to equivalent) with single
cone expander made from heat treated steel.
2.3 Two (2) 2-inch steel valves.
2.4 Two (2) 3/4-inch steel spigots.
2.5 One-way flap -type check valve for horizontal installation.
SMFURRCONSAM

2.6
Two (2) 1/4-inch mate -threaded hose barbs for air lifts.
Part 3
Engution
3.1
Position air compressor, oil/water separator, product storage tank, equalization tank and
UV -Peroxide treatment unit as shown on Drawing 3.
3.2
Weld anchor tabs on frame of UV -Peroxide unit.
3.3
Shim up and level UV -Peroxide unit before anchoring.
3.4
Anchor air compressor, product storage tank, equalization tank, and UV -Peroxide
treatment unit to equipment pad.
A. Anchors shall have: It diameter = 3/8-inch
Anchor diameter = 9/16-inch
Minimum embedded depth = 1.5-inch
B. Anchors shall be used as drill bit and holes should be drilled until chuck holder
is flush with the surface.
C. The anchor hole shall be cleaned of loose material.
D. Plug shall be inserted in the anchor.
E. Anchor shall be expanded by inserting it into hole and driving it in until the
chuck holder is flush with the top of the concrete.
F. Equipment shall be bolted to complete the anchoring work.
3.5
Install air lift "wye" connection on the influent and effluent pipe of oil/water separator
as shown on Drawing 3. Install 2-inch x 1/4-inch bushing with 1/4-inch female
threads. Install 1/4-inch threaded hose barb in 1/4-inch threaded bushing.
3.6
Install flow meter using neoprene boots for ease of disconnecting flow meter for
cleaning and servicing. Connections are to be located 1-foot from both sides of the
flow meter.
11370
Compm=rs
Part I General
Installation of air compressor.
Part 2
Prodg-cla
2.1
Air system shall have:
A. Air supply tubing: Nylon UV protected, 1/2".
B. Logic tubing: 1/4" nylon UV protected.
CLevel controller: QED or equivalent Well Master Level Controller.
D. Main controller: QED or equivalent Pulse Sender Main Controller.
E. Remote Well Operator: QED 2" or equivalent Remote Well Operator.
SM-FMCOM-sm

FAII-I—En"tLM
.1 Install air supply components in accordance with manufacturer's instructions.
II
FAr1j--Q0z9
Installation of oil/water separator unit.
p Iruets
2.1 AFL Industries Vertical Tube Coalescingfor 5 gpm..
A. Flow Capacity: 5 gpm.
power source required.
C. EquipmentEnvelope: old corrosion -resistant fiberglass.
. Equipment Dimension: ' - J " long by I'+- wide by IA - 511 " high.
2.2 Flow Failsate Features.
A. Provide automatic system shutdown for flow conditions out of .' high level
shut off switch.
2.3 piping.
A. Inlet: M flanged.
B. Outlet: "
C. OilOutlet: " flanged.
.4 Stage for oil/water separator.
A. Concrete blocks, d mortar.
I'
3.1 Performe Work in accordance with applicable local, state and federal codes, latest
editions.
3.2 Install treatment unit in complete accordance th e manufacturer's instructions.
3.3 Construct a '-5" tall stage for the oil/water separator using concrete blocks and mortar.
,4 Provide all required connections indicated on the Drawings.
3.5 Protect Work from theft, vandalism and unauthorized entry throughout the construction
period.
S

11337 ua a
La-qj--D&nsnj
Installation of 'Equalization Tank.
2.1 Delta CoolingTowers Storage Tank.
StorageA. K 500 gpm.
B. Equipment Envelope: polyethylene:
C. Equipment Dimension: 4' - " diameter, ' - 3" height.
2.2 Flora Failsafe to
A. Provide automatic system shutdown for floc conditions out of g low level
shutoff switch, high level turn on switch, and high -high hovel shutoff switch.
2.3 Piping.
A. Inlet: 3'" fi
B. Outlet: 3" flanged.
C. Overflow: " flanged.
Drain:D. 2" Hang
Part 3 Ex=lfio
3.1 Perform or in accordance with all applicable local, state and federal codes, latest
editions.
3.2 Install treatment unit in complete accordance with themanufacturer's instructions.
3.3 Provide all required connections indicated on the Drawings.:'
3.4 Protect t or :from theft, vandalism and unauthorized entry throughout the construction
11377 UV -Peroxide Treatment Systetn
F
Installation of UV -Peroxide treatment systems.
RW12--PBQd=
2.1 Rayox System, Model101-1 1.
A. Flow Capacity: 3.8 gallons per minute.
B. Pipe Diameter: 3 4" 316L stainless steel, Schedule 10
C. Netted Materials: 316 or 31 L stainless steel, quartz, t flon, viton.
SM.PMRCONSAM

D.
Sample Points: Provide sample port on system discharge line.
E.
Hydraulic System Pressure Requirements: 25 psig.
F.
UV Reactor: One 4 kw Sol them Lamp, UV shielded, with high temperature
shutdown.
G.
Transmittance Controller: Pneumatic drive with adjustable action cycle.
Controller to have automatic action for cleaning UV
reactor quartz sleeve.
H.
Hydrogen Peroxide System: Capable of providing 35% hydrogen peroxide at a
flow rate of 4 gallons per day.
1.
Equipment Envelope: 3 feet wide by 4 feet long by 5 feet high.
J.
Sldd Material: Structural steel with acid wash primer chemical resistant enamel
paint.
2.2
High Voltage System.
A.
Enclosure: NEMA 1, ventilated, drip proof.
B.
480 VAC.
C.
One 4 kw lamp power supply.
D.
480/120 VAC transformer.
E.
Power Factor: Better than 0.9 at
2.3
Low Voltage Control System.
A.
120 VAC, 24 VDC, NEMA 12 enclosure.
2.4
System and Process Control.
A.
Provide system control via programmable logic controller by Texas Instruments.
B.
Fault Annunciator: Message system on control panel
C.
Temperature: Reactor high temperature switches.
2.5
Flow Failsafe Features.
A.
Provide alarm and/or automatic system shutdown for flow conditions out of
range.
2.6
Lamp Failsafe Features.
A.
Provide alarm and shutdown on lamp failure.
B.
Provide alarm on lamp overheating.
C.
Provide power interlock on HV cabinet door.
D.
Provide alarm and shutdown on reactor high temperature.
E.
Provide alarm and shutdown on LTV access covers.
2.7
Transmittance Controller Failsafe Features.
A.
Provide alarm on failure to operate.
B.
Provide alarm and shutdown on low air pressure.
18
Feed Pump.
A.
Capable of delivering I to 5 USGPM.
SM-FURRCOMAM

2.9 Piping.
A. Inlet: 3/4" flanged.
B. Outlet: 3/4" flanged.
Part 3 EXWdM
3.1 Perform the Work in accordance with all applicable local, state and federal codes, latest
editions.
3.2 Install treatment unit in complete accordance with the manufacturer's instructions.
3.3 Provide all required connections indicated on the Drawings.
3.4 Protect Work from theft, vandalism and unauthorized entry throughout the construction
period-
DIMION It ME.CFUMCAL
15050 Basic Mechanical Materials and Methods
Bart-L—fkllml
This section includes installation of steel piping between treatment system components,
installation of steel piping for the exposed influent and discharge pipes including steel/PVC
connection in the ground outside the treatment system building, and installation of valves,
spigots, air lifts and flow meters.
Part 2 g[Qdj=
2.1 All pipes and fittings inside the building shall be steel.
12 Steel union joints, check valves and other valves are the responsibility of the contractor.
2.3 All steel pipes shall be threaded.
RaA2--E—XM1l1ffl
11
3.2
All steel piping shall be aligned, connected and properly supported. No sharp bends
or elbows shall be used at the change of direction, instead long 900 sweeps shall be
used.
Steel union joints shall be installed on either end of the treatment system components.
SM-YU"CONSAM

DIVISIONI: ELECIRICAL
Distribution16400 Service and
Part l jat&
Is section applies to installation, and hook-up of electrical power to treatment system control
panel located inside the
.1 Contractor shall furnish Pratt hour meter bass and switch capable of 120/480 VAC,
single phase/three phase100 amp application. Products and workmanship shall meet
or exceed NEC or local codes (the strictest code shall apply).
Part 3 `Q
.1 Install a main disconnect switch under'the watt hour meter. Switch shall be housed In
heavy duty outdoor elosu i identifiable lever switch to controlon/off
status from the outside. . s l a watt hour meter base to existing electric pole.
3.2 Hook up electrical to each system neat as specified in the manufacturers
specifications.

TMSOLO is an intelligent,h igh -rate pneumatic mp for total OU Js applications.
It runs itself,with an internal float system and a magnetic "brain"cartridge.
The brain senses liquid level in the pump, turning the air supply on when the
pump is full,and turning s off as soon as the pump empties. With its bulk- in
za brain, SOLO doesn't require air cycle or ` -tiff level control at the well heed,
simplifying system design. AJI you need above the well cap is a compact air
filter/speed control. SOLO is easy to Install -just nun air to each well. Continued operation is truly hands-off.SOLO constantly
reacts to changes in well recovery rate, so Ws always pumping t the highest rate possible. It also shuts down automatically
ter in the well drops below pumping l a SOLO requires a minimum of 3.5 feet of liquid in order to pump.) because
cycling is controlled at the pump, SOLO is either refilling or discharging of the time. `here's no waiting between active
phases of the cycle for the entire length of air supply tubing to re -pressurize. This operating efficiency enables SOLO to delver
pumping rates of up to 6 gallons per minute while also saving on air supply requirements. The pumping mechanism in SOLO
uses the same high-dearance design that has made PULSE FRUMP the standard for field performance without clogging or
breakdowns. All parts, including the magnetic brain cartridge, are rated for at least 5,000,000 cycles and are field-replacable
if necessary.
TABLE OF CONTENTS_
GE
2. HOW SOLO WORKS 2
3. INSTALLATION
A.
HOSE/TUBING ATTACHMENT TO TOP OF PUMP-,-----,- 3
B. CAP AND TUBING/HOSE:
1. PUMPS WITH ALL NYLON TUBING -4
;. PUMPS WITH HOSES AND NYLON TUBING,- 5

HOW THE SOLO PUMP WORKS
E SOLO PUMP REQUIRES A MINIMUM OF . ' F LIQUID TO PUMP.
THE SOLO PUMP AUTOMATICALLY SHINS OFF WHEN THE LIQUID
LEVEL IS PUMPED DOWN.
E
THE SILO PUMP WILL AUTOMATICALLY BEGIN PUMPING AGAIN ONCE
WELL LEVEL HAS RE O EREI
TOP CHECK
...
BALL
r
iNITI aL STATIC
j .- •+ { � 4
AIRPORTAL r
yy "�'g-�'g
WATER E:::t-i LEVEL
t"1fEi 1"� L:✓I-iTTi.,: }
HERE CAR HIGHER
PUMP
�
„^
DILL
TUBE
FLOAT WITH PUMP FULL.
FLO AT IN THIS POSITION SLICES THE ACTUATOR ROD UPWARD
CAUSING AIR TO ENTER THE PUMP. THE AIR PRESSURE FORCES
ITHE INLET CHECK BALL TO SEAT KEEPING ANY MORE LIQUID
FROM ENTERING THE PUMP. THE LIQUID IN THE PUMP'S BODY IS
EN FORCED INTO THE PUMP'S PILL TUBE AND UP THE
II; fl DISCHARGE LIFE TO THE SURFACE. THE TOP CHECK BALL IS
I 1 UNSEATED BY THE UPWARD FORCE OF THE DISCHARGED LIQUID,
ACTUATOR ROD
FLOAT WITH PUMP EMPTY
FLOAT AT IN IS POSITION SLIDES ACTUATOR ROD DOWNWARD
ALLOWING THECOMPRESSED AIR IN THE PUMP TO VENT. THE
INLET CHECK BALL UNSEATS (NO LONGER HAVING ANY AIR
AIR PRESSURE HOLDING IT DO N ) WHICH ALLOWS THE NEXT
VOLUME OF LIQUIDIN THE WELL INTO THE PUMP. AS THE LIQUID
REFILLS THE PUMP THE FLOAT RISES BACK LIP INTO THE
POSITION MENTIONED ABOVE AND THE PUMPING PROCESS
IS REPEATED. THE TOP CHECK BALL IS SEATED BY THE WEIGHT
F ANY LIQUID IN THE DISCHARGE E LINE ABOVE IT PREVENTING
THAT LIQUID FROM RE-ENTERINGTHE PUMP BODY,
INLET CHECK BALL
PUMP INLEr

HOSE/TUBING ATTACHMENTS TO TOP OF SOLO PUMP
PUMP DISCHARGE
FITTING
BRAIN EXHAUST
FITTING
PUSH HOSEj
FLJ81NG
DOWNIO
-nitsb BARB
PUSH
ENOAG&
TUBING DOWN
MENT (MINIMUM)
FLUSH WITI 4
TH8 VillINGS
NUT
CLAMP
t
I PLACEMENT
Pu Mp
EXHAust
lFif TING
PUMP
D[S�NAAOE
01
�CLAMP
1 1
V
I I
EYELET HOLE
FOR ROPE
ATTACHMENT
PUMP EXHAUST
FITTING
PUMP AIR SUPPLY
PUSH HOSE1
FLUSH WITH
THE FITTJN6rs
PUMP AIR
SOPPLY
CLAMP
--, I PLACEMENT
413ARBS (TAPERED)
713AR1ST APER ED) 3 BARBSHAPERED)
-AMPS PLACE CLAMP TOOL OVER THE
DIMPLED EAR PORTION OFTI-IE
CLAMP AND SQUEEZE EAR
TOGETHER { AS SHOWN BELOW),
A B
A. CLAMP IN CLOSED POSITION
B. CLAMP IN OPEN POSITION

ALL NYLON TUBING
496, 8" CAPS
18 LOWER PUMP TO DESIREDDEPTH.
. ICI
ww DETER-
MINED, MEASURE OFF APPROXIMATELY
OF TUBING LENGTH
PUMP TOP OF WELL CASING) FROM BOTH THE
EXHAUSTLINE BRAIN
DEFLECTOREXHAUSTLINE.*
3. CUT BOTH I
4. ATTACH THE PUMP EXHAUST DEFLECTOR
: CLAMP TO THE PUMP EXHAUST LINE.
FOR CLAMP INSTRUCTIONS)
. TIE STRAP ALL TUBING INTO
,qq ,p^�. PUMP
p P DISCHARGE
{7 � LONE I TLC
w. " BELOW WHERE YOU CLIP`
OFF YOUR EXHAUST LINES.
6. PASS PUMP DISCHARGE AND
.D. PUMP AIR SUPPLY
AIR SUPPLY LINES
THE WELL .
T 7. RE -ADJUST DESIRED
DEPTH.
1
8. I LL I I
/ " .5 . PUMP EXHAUST DOWN ONTO AIR/DISCHARG
LINES.
NOTE: EXHAUST TUBING
OUTLETS SHMD BE
LOCATED AO . V
BELOW WELL CAP OR IN A TOPMEW PUMP
LOCATION CIt TO THE AIR
CAP BB THEY WU NOT
BECOME SLINE
UBMERGED-
w
PLUG
(PROBE
HOLE) t
DISCHARGE LINE

IP

-----------
Itom all At
12 ZAN rMixt-i
KIM"
HOSE&
04000F
spi0o"
TUSIUG
SPOT SPIDOT

Pulse Pump
-) D Environmental Systems, Inc, (QED)
warrants to the original purchaser of lis
products that, subject to the limitations and
conditions provided below, the products,
materials and/or 'workmanship shall'
reasonably conform to descriptions of the
products and shall be free of defects in
materials and workmanship. Any failure of
the products to conform to this warranty will
be remedied by QED in the manner provided
herein,
This warranty shall be limited to the duration
and the conditions set forth below. All
warranty durations are calculated from the
original date of purchase.
t , Liquid uid contacting equipment (including
pumps), tubing; liquid contacting supplies
and Ilow totali ation equipment are
warranted for t year;
. Control devices, control device mounting,
and surface air supply hose are warranted
l for t year.
i
Separately sold parts and spare parts hits
are warranted for ninety ff days.
4. Repairs performed by QED are warranted
i for ninety f days from date of repair or for
:ire full terra of the original warranty,
wnioliever is longer.
r
Buyer's exclusive remedy for breach of said
warranty shall be as follows: if, and only if,
QED is notified in writing within the
:applicable warranty period of the existence
of any such defects in the said products„ and
QED upon examination of any such defects,
shall find the same to be within the terra of
i and covered by the warranty running from
QED to Buyer, QED will, at its option, as
soon as reasonably possible, replace or
!ny such product, without charge tuyer. If CE for are reason, cannot repair
TM Warranty
ra product covered hereby within four f
weeks after receipt of the original Pur-
chaser'sl uyer's notification of a wairranty
claim, then Et 's sole responsibility shall
be, at its option, either to replace the
detective product with za comparable new
unit at no charge to the Buyer, or to refund
the full purchase price. In no event shall
such allegedly detective products be
returned to QED without its consent, and
C Ef 's obligations of repair, replacement or
refund are conditioned upon the Buyers
return of the defective product to QED.
IN NO EVENT SMALLCOED
ENVIRONMENTAL T, L ,Y TE@ , ENC. BE
LIABLE FOR CONSEQUENTIAL OR
INCIDENTAL DAMAGES FOR B EA IA iF
SAID WARRANTY.
The foregoing warranty does not apply to
major subassemblies and other equipment,
accessories, and other parts manufactured
by others, and such other parts, accessories,
and equipment are subject only to the
warranties, it any, supplied by their
respective manufacturers. QED makes no
warranty concerning products or accessories
not manufactured, by QED. In the event of
failure of any such product or accessory,
QED will dive reasonable assistance to
Buyer in obtaining from the respective
manufacturer whatever adjustment cs
reasonable in light of the manufacturer's
oven warranty.
THE FOREGOING WARRANTY IS IN LIEN
F ALL OTHER WARRANTIES,
TIE: ,.
EXPRESSED, IMPLIED OR STATUTORY
(INCLUDING BUT NOT LIMITED TO THE
WARRANTIES OF MERCHANTABILITY ' AN
FITNESS FOR A PARTICULAR PURPOSE),
WHICH OTHER WARRANTIES ARE
EXPRESSLY EXCLUDED HEREBY, Y, and of
any other obligations or liabilities on the part
of QED, and QED neither assumes nor
r

authorizes any person to assume for it any
other obligation or liability in connection with
said products, materials and/or workman-
ship.
aship.
It is understood and agreed that QED shelf in
no event be liable for incidental or cdnse-
gUential damages resulting from its breach.
f any of the terms of this agreement, nor for
special damages, nor for improper selection
of any product described or referred to for
particular application
This warranty will be void in the event of
unauthorized disassembly of component
assemblies. Defects in any equipment that
result from abuse, operation in any manner
outside the recommended procedures, use
and applications other than for intended use,
or exposure to chemical or physical environ-
ment beyond the designated' limits of
materials and cuntruction will also void this
warranty.
Chemical attack to liquid contacting equip-
ment and supplies shall not be covered by
this warranty. A range of materials is avai-
lable from QED and it is [lie Buyer's respon-
sibility to select materials to fit the Buyer's
application, QED will only warrant that the
supplied liquid contacting materials will
conform to published f. specifications
and generally accepted standards for that
particular material.
D shall be released from all obligations
under all warranties if any product covered
hereby is repaired or modified by persons
other than Q 's service "personnel unless
such repair by others is made with the writ-
len consent of QED. If any product covered
hereby is actually defective within (lie terms
of this warranty, Purchaser must contact
Vnasknng •Sga1
QED for determination of warranty coverage.
If the return of a component is determined to
be 'necessary, QED will authorize the return,
of the component, at owner's expense, if the
product proves not to be defective within tale
terms of this warranty, then all costs and ex-
penses in connection with the; processing of
the Purchaser's claims and all costs for repair,
parts and labor as authorized by owner
hereunder shall be borne by the Purchaser.
The original Purchaser's sole responsibility
in the instance of a warranty claim shalt be to
notify QED of the defect, malfunction, ' or
other manner in which the terms of this war-
ranty are believed to be violated. You may
secure performance of obligations here- i
under by contacting the Customer Service
Department of QEDand:
1 Identifying the product involy d by model
or serial number or other sufficient descrip-
tion that will allow QEDAo determine which
product is defective.
2. Specifying where, when, and from whom
the product was purchased.
3. Describing the nature of the defect o
malfunction covered by this warranty.
a Sending' the malfunctioning component,
after authorization by QED to
D Environmental Systems Inc.
6155 Jackson load
Aran arbor, MI51 g
Telephone: [phone]
-tl-S-5
1-51 - .5-g g (Canada)
1- 1 d®g 5--11(Fax)
Environmental
QED Systems, Inc.,
RO, Box 3726, Ann Mar, MI 48106
3001624 -2026 In McJiizg n, 3131 - 547 In Canada, 5 M85-0290
2
Fax [phone]

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R(OprtOWAL) OPTIONAL) L AND

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F41 T.T.t bffl* 0'--x
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I Ot -X-tl- bfol. Vlo" 4*4 "J( oo� '#jtrjgA tot
a G.: , t —4, 1, Aft, co#wWotloot to
bqti # too as.* 0.4 t.#t,~ tt of#**
9, 1" 0 all OfOO .:th 01.4 It '04,41 to W"
0#10.0 I-Oiov 000 "A 01014.
I DtAant 'Z
IN" Ik fittoo tt* wk. 40 PM of"�
14" Is C"Stettd of IN 0-094d St.$*
Wood Ift ISAVAIRAlft motic
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AtV NO DATE or
sudustf x-,, w.
SECM01"J 'A-4
RN-2 LER—INGA BEIT!R ENVIRONM=ENT

SYSTEM SPECIFICATION DOCUMENT
RAYOX8 ENHANCED Solarche
201-RB-500085 Rayoxv Flow Schematic
forms part of this Specification
SOLARCIIEM ENVIRONMENTAL S`
DOCUMENTN. —,.
Dmwn y;Wtgg I 1
Wagg
7-D
a
Approved7
By:
It
THESE R1�VfNNS, S=ANS; lESfNSARE `SHE PR PE� EE NM A S'Yti SUBT RETURN�'f NTHEY RS 1 ED 0 THEHA THEYWILL OT E LS EE IN i�WAY i �itJR W"
Page I of

SYSTEM SPECIFICATION 201-RB-000064
SYSTEM OPERATING
DESCRIPTION
page 2 of this document
HYDRAULIC SYSTEM
FWW CAPACITY
3.8 gallons per minute
PIPE DIA.METER
4
3" 316L stainless steel, schedule 0
:,"T
W
316 or 316L Stainless steel, quartz,
teflon, viton
SAMPLE POINTS
0After
reactor(system dish
MAXIMUM SYSTEM PRESSURE
®
25 psi
PUMP
0
Suppliedby customer
UV REACTOR SYSTEM
UV REACPOR
BOnekW
Solarchem
0
UV shielded
0
High Ternpemnue shutdown
TRANSMITTANCE CONTROLLER
*
Automatic action cleaning UV
reactor quartz sleeve
Pneumatic drive
Adjustable action cycle
*
(supplied by cyst
80 to 100 psi, <5 micron filter,
dew pt < 38*17
Page I of

SYSTEM SPECIFICATION 1
DELIVERYLIQUID REAGENT
HYDROGEN PEROXIDE SYSTEM 35%Hydrogen Peroxide
Estimatednt ).
Deliveryvia metering pump
Storage and unloadingothers
EQUIPMENT COPE '
S Strucnirai steel, with acid wash primer
chemical resistant enamel paint
WEIGHT(approximate) 1000 is
ELECTRICAL
• 480VAC, 60 Hz, 3 Phase
Running• nt Full Load
15 Amps+ 10 _
Housed• In k NEMA T
vends drip -proof enclosure
One 4 kW Lamp Poorer Supply
480/120 VAC Transformer
Transfortners in the high voltage
enclosure capable of rugged long term
performance
Power Factor better than 0.9 at 4 k
Page 3 of 6

120 VAC,2 4 VDC, NEMA 12 Enclosure
Contains PLC, metering pump controls
and instrument indicators
Panel r has start/stopstart/stop push buttons,
instrument and alarm annunciators
CSA Special Approval obtained on
finished Systemt Solarchern plant
NTROL
• System Controlvia Programmable
Controller (Texas Instruments)
• _ Message Systemn control panel
• Reactor high temperature switches
and/orAlarm automatic system ; shutdown
on flow out of range
Alarrn d shutdown on iamp failure
Alarm n lamp overheating
Power interlock on HV cabinet door
Alarm and shutdown n reactor high
temperature
Page 4 of

SYSTEM SPECIFICATION 2101-RB-000064
* Alarm and shutdown on UV access
covers
TRANSMITTANCEC n failure to operate
Alarm and shut down on low air pressure
SYSTEM DOCUMENTS d Maintenance
including:
- System Description
Piping and Instrumentation Diagram
- Control Description
Operating Procedure
Set of Drawings
OEM Nbnuals
Fags 5 of 6

SYSTEM SPECIFICATION 201.RB-000064
System Operating Description
Solarchem's Rayox,& Enhanced Oxidation system is designed to treat up to 3.8 U.S,
gallons per minute of contaminated groundwater, pre reated to the influent water
characteristics provided below. A flow schematic of the Rayox* system is shown as
drawing number 201-RB-500085.
The system is designed to run at a steady flow rate between 2.5 and 3 USGPM, dependin
on the rate of groundwater flow and contaminant loading. Before the water enters theg
Rayox-O reactor, up to 200 ppm peroxide is added to the stream barpump. metering
addition rate, and the flow rate, will be adjusted as part of the
This
e system oprison
following commissionin . Steady flow through the reactor is made posib mizati
9 le by an
equalization tank (supplied by customer) which accumulates the irregular groundwater
flow. The Rayoxv system is stopped and started by level switches in the equalization
tank, cycle duration in a function of the groundwater flow rate.
TYPICAL INFLUENT WATER CHEMISTRY:
PH: 60 nommai UV Absorbancr*m:
COD: 50 ppm 280 nm 0.10
260 0.12
[C031: 300 ppm as Na,2 CO, 240 0.15
Tel� <5 pp m 230 0.17
[CII: 50 pm, 220 020
Color p.
<10TCU 210 0.30
Turbiditv: <50 NTU 100 O45
TPH: <20 ppm
The Rayox* reactor is a cylindrical stainless steel vessel at the centre of which is a single
high powolarchem Ultraviolet lamp. A quartz sleeve separates the lamp from the
water. The quartz sleeve is kept clean automatically by an air actuated transmittance
controller that wipes the surface at regular intervals.
The system operates under the control of a PLC (Programmable is Controller). The
main function of the PLC software is to control the process and to monitor the system
status and alert the operator to any fault conditions. The system is failsafe for operator
safety. Alarm and status messages are displayed on a message annunciator on the control
panel.
Four options are offered for this system. The first is a 3-way valve which will allow the
system to recycle water to the equalizing tank during start-up such that no untreated water
will be discharged. The second option is a modem which will allow remote system
monitoring and fault reporting. The third option is an automatic voice dialer which would
warn of system shutdown but could not be accessed from a remote location (option 3 is a
less expensive alternative to option 21. The fourth option allows the use of 220 VAC
instead of 480 VAC.
Pap 6 of 6

ENHANCED OXIDATION SYSTEM So
SITE SERVICE
REQUIREMENTSRAYOX0
TO BE PROVIDED BY M
ENVIRONMENT
Industrial Ind , ""
Seated r Painted Concrete Floor
ELECTRICAL SUPPLY
480 VAC, 60 Hz, 3 phase
Running
l SAmp - 1
INSTRUMENT AIR
3 scfin, 80-100 psi, <5 Micron filter
dew pt
EQUALIZING5K
Recommended volume w high
d low level
e1 switches
FEED PUMP
To deliver 1 to
REAGENT UNLOADING
Hydrogen Peroxide 35% 4 U.&
AND STORAGE
PIPING
t 3/ " Flanged
Outlet 3/4" Flanged
Drain piping
UNLOADING
Requires loading dock and fork lift
INSTALLA'nON LABOR
Unloading, placing, leveling and anchoring
the equipment
Electrical hook-up
Tubing pump and storage
tanks, and between metering pump and
Rayox,&skid
wiringElectrical e metering pump and
aax skid
0EMIZ7101 ENVtRUN__N1_E_N7"XLSYSTENYS-
Dew
DocumentNo.- Z0I-RJB Is By-, L..
Checked By:
Approved By:
THESE DRAWINGS, SPE IFi A _RN97 DYES NS
ARE THE PROPERTY OF SOLARCHEM
ENVIRONMENTAL SYSTEMS, AND, ARE SUBJECT
TO RETURN UPON REQUEST, THEY ARE
SUBMITTED ON THE CONDMON THAT THEY
WILL NOT BE USED OR REPRODUCED LN ANY
WAY WITHOUT OUR WR=N APPROVAL

Section
System overview
General
This section is intended to introduce the reader to thevox
vstern and provide a functional description. of the overall
process.
I r w ' 171-RB-000047 shows a perspective views of the
Ravox Svstem, Model I0 -171.' The system is used to treat
groundwater contaminated with Benizene, Toluene,
Ethvlbenzene,a" vlene, and IMTBE This is accomplished by
means of a single Rayox Reactor () driven by a high voltage
Ravox Power Suppiv (9), All ether equipment is used for
control or system support functions.
Drawings Referenced
i 1-R - 00048: Svstem, Instrumentation Location
irl-RB- 00 1 . P&II
Functional description
Peter to Drawing 11- - 0041 . Groundwater is delivered
by the customer's Process Pump at up to 2.5 USGPMto the
influent point. Influent flow is controlled by a Manual Flow
Control Valve (FV 10 ) located downstream of the
Automatic Shut-off valve (FV 1002),
Addition of Hydrogen Peroxide
Refer to Drawing 171-RB-000048. Hydrogen Peroxide is
injectedintothe influent line at the Peroxide Injection Port
(1) and is mixed into the water by the Static Mixer t20). T lie
delivery rate of Hydrogen Peroxide is controiled by an
adjust ent on the Peroxide Pump t l).
reatment inside the Reactor
Water then enters at the bottom of the I.a rox Reactor () and
flowers up in a turbulent plug -flow p tte for efficient
destruction of contaminants. A UV Lamp situated at the
centre of the Reactor, emits ultra -violet light which is
absorbed by the target the is i(s). After absorption of the
appropriate wavelength th of light, a hiighiv reactive
compound called a radical is produced. liven the right
conditions in the reactor, these radicals are produced very
fast and ww;ill in tan;tiv break -down to carbon dioxide tw#ate ,
and chloride, in the case of chlorinated compounds. These'
products can be safely emitted into the atmosphere.

. x.,
RayoxJ C A do and ,' llaintc &4+nce M4fi\ uai
_147he Reactor Assembly bly
The UT%7 Lamp is pnvsicarly isolated from the Reactor
Chamber by e of a Quartz Tube. The surface of the
Quartz Tube is �,,,riped clean at regular intervals by an air -
actuated Transmittance Controller (2). The pourer required
to drive the LJV Lamp is supplied by a high -voltage Ravox
Power Supply (21). Blower assemblies mounted at the top
() and botto of the Chamber are used to blow cooling air
across the electrical connections to the Lamp, Ultra -violet
shielding is designed into each Reactor assembly,
Sampling
Sampling ports are provided at various points in the syste
to allow for analysis of treated water and ensure that the
water is decontarninated prior to discharging
Draining reactors
The Reactor is also fitted vrith a drain for maintenance
purposes
process control
The Ravox Systemoperates under control of a process
Controller (6). A Programmable Logic Controller (or PLC)
inside the Process Controller, monitors various sensors,
adjusts 'parameters accordingly, and displays status
information. Various interlocks and ala male the syste
tail sate both in terms of operator safety and quality of
discharged water f, for example, a UV La p fails, an al arm
is activated and the syste is automatically shut dawn:
Operation p
minimal can required to run the,
lao�ivste n do-1 e. "he fr
front panel of the process
Controller has various operator controls and displays used
to primarily start-up and shut-dov the system. jOperation
is described in detail in Chapter .
Release 1.0 pat it tion 171-R-

MUM UNE
F➢ OW Ir➢E Ff.1I ,
qq pp qq g ,p+ p
G
PEROME FLOW .� ;PVT
�..ry PROCESS C;CIiiM01l.k @
i
NI,
I' . h l➢I 1A SIC ... �I k�` ''t'CJX Pal, AC I CAI
F2<^�YOX POWER �xt ➢PP1 �`; � .: � — � _ .. )AIR c:OM IEC�T➢C�IJ I�CaF�T
w
r
i
CCONI k�01 E R
,�.� ICI E 1 PORT m� <.:
_ MI5Bi.
C OVL R I='AH i SMICH
111LU II ( f !I!E —__. - A6I BAHK
— YtYON fAwo
l�«A?.r.t
7Gi"f4 Cd0 oANi �
AR PRESSURE. S ➢FcI1 .�
$YCk.`� lYkSY�VJaY�.k@PAC9Utl t{Yi:,is71L�Mp

----
FMURE USE)
PUMP
_._.
Aiw
-:
hEC6F i2 i"BtaG � J Eli VF Ick L [ C' t n 1
COMPRESSOR Mill IAIx W ��J � rr � �°C�� � } 'rx"} 1f L i�f C ���� I� 1
1 i u /V
low
Asa,
Ii`l'
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M-103 -- �
.* SIAM MIXER
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w
PE6wOXIDi. iAPJKMl
d QYN fi0."El 56Gh9t+3 � ;�'� �,r.+aaar
I tip...
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9r�r2. `e:ftf_ a+er fie
AN
1 tt aat�PS-'191 Tar
LAMP POWER SUPPLY N£trAE [[ f7t WiEi *ad3t7d8d A .�"

a
sola"it
SOLARCHEM WARRANTY
arfce '�
Solarchern Enterprises Inc. ("Solarchem") warrants that its Rayoxo water Purification
system ("Rayoxv,) specified in the Rayoxo System Specification document will, if
operated and maintained in accordance wcrion
ith the instr s containin the Sol ed he Operations and Maintenance Manual delivered with u m
Rayox'&, perform in accoarcrdance with
the Rayox,3, performance specifications contained therein. If RayoxO does not perform in
accordance with the specifications contained in the said quotation number and Solarchern is
unable within a reasonable period of time to remedy the defective performance, the Buyer
may remove and return Rayox,& to Solarchem and olarchern will reimburse the Buyer for
the full purchase price of Rayoxo less 25% of the purchase price per year that Rayoxe
was in the Buyer's possession.
M=dalp�
of cheat warrants that for a period of 12 months from delivery FOB Sol arthe m's
warehouse (Incoterms 1980) of Rayox,& to the Buyer, Solarchein will replace or repair
non -consumable parts of RaVoX1& proved to be defective in material or workmanship
provided that the Buyer gives prompt written notice of each defect to Solarchem.
of hem Aifl be liable for the direct labour and material cost;of such repair or replacement
by the Buyer only if Solarchern give prior authorization in writing for the repair or
replacement involved.
There are not representations, warranties or conditions express or implied statutory or
otherwise with respect to Rayoxo or any part thereof except as expressly proved herein.

Solarch
LAMP
SOLARCHEM ENVIRONMENTAL SYSTEMS
SOlarchern lamps are guaranteed at rated destruction perfor-n=ce on the following basis
"" ETA RTC ( "r L I 1
d
Continuous up to 100 Hours
replayed at no charge.
101 _F'rice oursprorated d credit allowed
for unused portion of 3000 hours,
applied to. purchase of snke
Discontinuous 51 to 400
lamps.
100 Tours Lamp replaced at no charge,
101 -2000 Hours Price Prorated and credit allowed
for unused portion of 2000 hours,
applied to purchase of subsequent
lamps.

REACMION RATES OF OZOINEkND
HYDROXYL
RADICALSF ORGANIC
()
Cx
olefins 1 to 450 x 1 10 to I tI t 1
S-contaming 0 to L6 x 103 109 to 10
orgarucs
Phenois109
N�contarmng 10 to i 101 to 11
cry ids
Almancs 1 to f t fly to 1 1t1
Acetyienes .04 to 104
,k1dehydes 10 io
Ketones s 1 to 1o!o
Alcohols itl-Z to 1 10 to 10
A&AM 10-2 104 to 109
Carboxyiid 10-3 to io", 10 to 109
acids
Table
These radicals, once formed, aggressively at=k a waterbome
contaminant and vtpicaily inniate a rapid, oxidative cascade
of reactions, which, in the caw of a fty n or an
�)xygenated hydrocarbon. results uitimatety In C07. and Ham,
xf the cote ut is chlorinated o compound. Lhe
,nine tenon; process will also resuit to the formation of
�diohd (CI-) sore.
appreciationof the reason for the. increased rate of
decontamination obtainable by enhanced oxidation can be
obtamed by reviewing the data in Table 1, above, which his
,Jhe mic constant, k. for the don o e ozone, d the
hydroxvt radical H number of different classes of
organic compounds. These data shoes that the rate constant
for H it on orga= compounds is typically rrrtfiaon
It ) to a billion t 1 tithes faster than molecular ozone -
,,ere nave n a number ofinvesuizattons into the de is o
aloe chemistry invaived in the enhanced oxidation process.
he detailed, step by step chemical s involved in the

Jill"
':ie rate constant for the reacuon between the oxidant and the
R e a s o n s r g
-'OMPOUnd in queSUon. NiAtherrs aticailv this can be expres='
is:
The Proprietary Solarchem Lamps.
A System Design that allows for Variable,
4fetime of contaminant x
Muiti-stage Treatment.
'kx first order rate constant for the decay of x
ki rate constant for the reaction between
gA Unique Reactor Design Wbich
radical oxidizing species Ri
Enhances Mr us and Rad." tion Transfer.
= concentration of the radical oxidizing species present
ENOX Additive&
HO-)
High Efficiency Power Suppfim
For example, even if the by product was relatively refractory
,such as a carboxylic acid (e.g. formic acid) then
Automated Quartz Cleaning Device.
l0iiUmole - s x 10-9 moies iLl-I = IN
Contaminant Photo decomposition
Where the following assumptions have been made:
Proprietary process conditions
107 Lf mole , s �Jrorn Table 1)
HO- I = steady stave concentration of the hvdroxvi maical.
Figure ('21) on page 4, shows that the basic Ravox,& wax
'Which is: (10-9 rnoiesiLi
decontatumation system typically consists of a series c
'a
that the HO- radical is the only oxidant reacting with the
annular reacMs) complete with roprietary Uv jamp,
pq
carboxviic acid in questionve
qua= sleeve to protect the iamp, a trarisnuttance controller c
keep the quartz sleeve clean. a variable length annulus fo
In the above example, the concentration of the carboxviic acid
water flow, and a stainless steel outer shell wail. nus deing,
°,vould decrease by a factor of (1/e) (-0.37) every lifetime. or
f3cilitates variable. multistep treatment and efficient mass an(
every 10 seconds. If the byproduct reacted more quickly (i.e.
radiation transfer.
had a larger raw con with the oxidants in solution, or
Lhe concentration of the oxidizing species were higher, then
RFACID2&
1.he iifedme of the intermediate would be further reduced.
The importance of reactor design on the performance can b
seen from the results shown in Figure 1. From act
F
t-rorn me foregoing discussion, it can be seen that [ne
treatment results, the dioxane concentration
.oncentration of any intermediates or by-products that might
­)c formed -as a result of the 140- anack on the original
xmpound, can be reduced to whatever levels desurd by
-imply ensuring Lhat the contact or residence time Ls
sufficiently long to achieve the target discharge, criteria What
is usually observed in practice, however, given the highly
reactive nature of the radical oxidizing species generated in
." e enhanced oxidation process. is that the contact times
. eacd to rcduce trie concentration ot Lhe mitiai con Luninanu;
to target discharge values, also results in the sausfactonly
complete destruction of any intermediates or by-products,
As a, resuft of this near complete rnineratizauon
"des trucoon ') of any waterbome organic conLunmants, the
use of enhanced oxidation for process and groundwater
-2mediation means that them is vimiailv never a se-condary fir
.ownstrearn aisoosai or handling pronlem. Figure i
SOLARCHEM ENVIRONMENTAL SYSTEMS

i
k%xakL
THREERAYOXRF-ACTORS
R
s
r T r
FIL MW SWITM LW
MOW AIAAX LOW
EFFLUENTrAL
INFLUENT
Drain
Bile
Transmittance
Controders
TEI
63
1p350
[ELRAYOX FLOW' SCHEME
Figure
,
emaining after a dose of three in reactor B is roughly one half
important for iarger throughputs, e.g. > 100 gpM, or for more
hat remaining w Since dose is proporuortairefractory
contaminants such as TCA and methylene chloni t
_ st. it can be seen that the operational costs involved with
which require higher LTV do e&
,,,chieving the discharge concentration obtained with 3 dose
is —0.2 ppm with reactor B wouid beapproxiniatedy 3
The importance of the choice at UV Lamp can be seen b,
more with reactor A (i.e. 4 dose units with A vs 3 units with
:. results , tit i 6�ja drt figure
JQk.Ft reviewingf} qq is
i.results
are shown for the destruction of waterborne dioxane a
a function of dose using two different So
data shoes that the cost of achieving a dischargE
he Solarchern dimps am high intensity broad spectrum UV
concentration of l Mot with lamp 8 would be toughly
�nt v s xhich have particuiariv Szmng output .r s Pe
Lhat for p A with this particular c tt
photo -active absorption bands of most waterborne
c,ontarnmants. Powers to 300 times thm o0mituible with
Generally then. it is important to achieve a judicious m
;ow pressuremercury typical of first genemuon
between the iamp emission d the p tiv
mrianced oxidation systems, am attainame with e
absorption bands of the target con t(s) as this ca-
Solarchern Lamps.
cream a significant new contamintint destruction channel i.c
phoutilvsis or phouidecomposition of the contaminant.
;s �,ubstanuai enhancement in en , fcctive rower -awn !h
i� tip itt Ste€ VS L.anSlaICS Uiiia �;TUUCr, .Aalt)cet K Yti
systerns for a given throughput capacity, resulting in lower
° pital and operaung costs. This. of course. becomes critically

THE EFFECT OF ISOLARCHEIM
LAIAPS ON DIOXANE REMOVAL
Rayox Dose
Figure
BENZENELTV ABSORPTION PE i
100
o
40
20
ro
46
r
Wavelength, not
Ft
Selecung the appropriate UV lamp is facilitated
anderstanding the Peak abwr&vwe of a particular water
'tmara' nis is accomplished by obtatning a printout of the
dosorbance with respect to the UV wavelengtha
,pectrophotorneter as is shown in figure (4 & 5). Figure 0)
meows the PeA apsorbame of waterborne berztene to be about
:0 nm while that of NDMA to be about 228as shown in
zuret.Jj. It can oe concluded fay utifizing protons of L
to take advantageof the photo chemical destructionof
. , rise contarninarv, in addition to the oxidation way
unitiated by file hydroxyl and perhydroxyt radical 4 wiil
-zsfait in a lower operating and capital cost as wed as smaller
care compact yoprocessing egtu
UV Absorption SPectrum o(NDMA
ca It
7
Wavelength, arn
Figure
in Gmujvwster
i
Ilan
ze
Figure d
Af)f)rrrw.1,9
A further factor contributingto Ray"Iss supenc
pertornunce is the use of o rta`
additives a Process '.know how. These ad&nvp-
enhancethe rate of contartuniant destruction by enhancing th
raw Of r3dicW forniation or the efficiency of radii
utifization. The exnordinary enhancement
decomanimation efficiency obtained by Easing one or met
ENOX additives n from the data an Figures (6 & 7`
wherein die dog of the concentradon of benzene in water
plotted as a function of Ravoxo dose. From Figure(o), it c
be n that the use of ENOENOX 510 resents in a cost one quarte
(11) of that required for UV/peroxide alone to achieve s; f=-
benzene concentration of i ppb franc an initial value of aboL
» "ram
SOLARCHEM ENVIRONMENTAL SYSTEMS

•
�,
�«
��.
�_
,,
ie
a � „� _.
., s i,
ea
e '" � , .,
r � ..
�
t ..
_ « ,
"�
m i �
w .„
,.. i' .
e
�;
ti
�
��
�. �� �
c �� '�
.4� � ;�,;..�^
�� � i V t� i;,
„y,, ,.
. �.
'`""� �#
,u
�
�..,
�,
r ,'
! � ,.
.: ,.
r., �, ....: .., _.
� ..
� ..
w
� 4 �
t-...:
i y
•
�, � - M. .
� a
� �.... r
t ��
,. � � � �;
-... of
. �. .. ,
�.
��
.,

„tt
maatir U.. wood t1t=9 firm has PCP con
'nadenuate"vaste handling Pr3cuceS havein the
90undwater at one of its is in the Soudieastern States,
r. rt t of sod as well as the 3quders undera major`
crag tt of the PCP in the groundwater is about 3
�` se facility in athvsifefi Ontario. e tt rtca
the dISCharge Criteria was set at less than 10 ppb.
Ministry of the Environment wanted to achieve a discharge
results shrswIl in Fig= (li) cttttsrp sftt this ttiret way
sserttsattcttt at l ppt (ttMetft detection limit).
t�assi achtev
The treatment results Shown In Figure ( demonstrate that
the <20 PIX target was readily amune&
REMOVAL OF PENTACHLOROPHENOL t3
CONTAMINATEDO SITE
PCB GROUNDWATER REMEDIATION
I
�
.t
Z
.01 Z. 0
Ptit
t. detection
0.001tt
d t z a
1 3
Rayox Dose
Rayox Dose
Figure 10
Figure1
Dioxane is an excellent, water xmiscible r lv nt mth a
TO illustrate the powerful decontamination tion ility of
range of industrial li o . Unfortunately past
Rayox,9 some typical results for the desauction of Several
process wastewater eut s i.e. Lagoons, have
refractory cart is vets below:
,esufted in Elie contamination of some groundwater aquifers,
- r ux pfe. a Michigan tst inadvertently
pi (13) shrews nits liar reduction of the
yontammawd an aquifer beneath one of its facilities with up to
�hloraform from about 3 0 pput to less than 0. t pprtt._
3.0 ppta of dioxane. The results shown i ; (11)
,ientonstrate that discharge concentranons of <2 ppb
Chloroform Destruction Using Rayox
99.999+% destruction) tip achievable with
t
Dioxane Destruction using Rayox
t
too
x to.
y'y
[
st
0.1
1i
Rayne Dose
k1 ,
Ravox Dose
Figure 11

'igurc d l i 91ves some results for the reducuon of the i '.
a oncentration from atiout 2000 ppb to i ss than 5 ppb.
Using star ox
Degruction of TCAin ` Ci C
t 00
W
,�
ait
10000,
U V/112t
1001,
L 0
sla
t tt EII—
10 E001610
0 2 4 10
Dose
Figure 1-5
FigureRavox
1 4I?
.fit
The effect of y on waterborne - DCA was
Figure 0) presencs results showing the reduction of Freon
evaluated on a groundwaterat the Law7v= Livermore
from about 100 ppb to less than 10 ppb.
National Labomtory on Livermore Califorma to july 199().
Groundwater _ l was transported by uink truck to
For h of the above examples, evert tower discharge criteria
be treated to batch mode by a Rayoxg tivisportableit,
could easily be ,achieved by simply increasing the y
located on the Lawrence Livermore National Laboratory slit,
dose.
This transportable utut was Sunda to that shown in Figure 8.
Ott results of DCA reduction shown to Figure 16 confirm the
capability of Ravos(S to reduce waterhome 1, , DCA from
rntare than 100 ppb to the tow ppb range.
t
KzkWhr�t
HI
Symbol Test So. Destruction
7w8 30 25
3
n+
4.
.6 0 100
6.0 30 12.8
X t oSC07>
7. t o
10so 12.
,gg
4.9 40
scio 3.0 a a.
E
��ryry
40
Energy tkwhtl000 gulonq)
Figured

7o illustrate the Powerful decontamination capability C
PESTICIDES
Two examples of the effect of SoLvtoems Rayinisl
yra . : is for the destruction of sever n-picalon
waterbomex California am worthy of note.
.ontarninants are irivenbelow:
Field tests completed in January 1990 in San Luis Obispo on
Destruction ot Petroleum Hydrocarrons m
pesuciderinsate stream confirm the mpid destruction of
Rauast rater
waterborne Roundup in Figure (19),
lam
Roundup a 'on using Ravox
g xr
t
m
low
ofto
Figure 1
i
Figure (17) shows the results for the reduction of BETX and
in barge ballast wata as a function of Rayov&o t
a site in New York state,
Figure 1
ZENZMM
At a second site near Bakentield California, Solarcherr
Tlie groundwater under a New Brunswick Department of
successfully reduced waterborne DINOSEB. a banned pre
art fueting station in New Brunswick had become
emergence herbicide, it a large quantity of sots wash water
,,ontaminated over the years with BETX, As can be seen from
shown in Figure t 20). rotor reduction from that of s deer
-ke dam in Figure (18), benzene was reduced from about 80
orange to essentudly water white was alsoa riamed
to t ppb.. As benzene is the most refractory of the
t uon. the other contaminants t to even
f
over concentrations. Another point worth noting was that noof
Ptre , r : _ Effect of Rayox on The Destruction
Dinosebin Soil Washwater
,..s ne was used. so there was no tiff gas with s
� t
Lo am In some tim generation enhanced oxidation systems,
is a as a H the nit t o st t
t
,uanutv of any volatile contardinant will be air strip ped due to
ae large gas-houid ratio invoived,,inth such systetras.
Destruction o(BTX In Groundwater at
New k Dept. o(Transport site�
100
i
1
t
1
-rRayox
Dose
0,01
i
RAYOX DOSE
Figure 1

77he man4facttire ai TNT (trinitrowfueftf dith mmits in ibe
OroducUbn of pink waw. contarnmaLed with �50- 1 �25 mg�t of
7�NTSdLg� qxrutd out dtaobifity Saidies wsigned to
find the hld�( cb�t tffks� conftgj� of !Wo� to aeat
77NT to tfie rNU#0 djku3* C-hMrmi of <005 ni*j�. n
tesults a tbi� studitS indir-awd that Ofthwiced oxidithid�*&
MeOd, �* ��ve f0f Oittk water atamem
T*4T Destruction in Water Using Rayox
RAyox Dose
'�t die Indian Hitad M*iand NavAj Ordinahce 8t4oii th�*
a nitmglYtCTtne Contanith4ted wagttwWa, sucani ftoM tl
,extrusion piam F6r this sumam. Lho best approach Usin
�nhanwd oxidaticul: for the destrucla6b Of NO frolll i lba 10P
- WL SOi-kRCHEM ENVIRONMENTAL SYSTUAS

LO < 1 n*L, was a tN*ydwpn pex� symm�k
lestrircuon curve fbf NQ is zurt in
MIMMU."M VWO�M"'Y� -7 U
�drnbioed hydroxyt m� and photdfy�rs based mepnanjsm
"Or the rnaximuru effip�, Wtild ihe o*d 4 trtattatent of
all ihe
dds stream with tieffva• b» » 4re e0foo4ra» ;,
rniugg= in tivour of the 14der ippr�
Other retated ordnance rompounds successfully destroyed by
Ravox,& include:
TNT
PGDN
DNT
TIMETN
Nix
71-:GDN
i4MX
RDX
2 A Y-Q V I
"mfirninary estanates of Capital and (�xratmg cost -ut
available frGm Soiarchern Won receipt of the following
nf6rination:
,nietwin tarninants of coxem & concenuawn
* Desired effluent qUaiitV
* �,Iectric power rnte in c,,kWhr
Very versatile system
cao: d up or dol
ugh Degree of Safety
can be built to UL Standards.
SOLA

erences
;gen ie. 11. .A Hewes, `.%.. Ma , t -E. 1976
Oxidation to Refractory Altatertais by Ozone with L"ltr
:bier Radiation. 1n Proc. C '.nd Internanonai
SYMiPosium on Ozone Technoiogy, Inteernat. Ozone
Institute pp. 224-252
Peyton. Glaze. W,H. 1988. Destrucaon or
Pollutants with Ozone in Combination with Ultra Violet
Radiation 3. Photolysis qf Aqueous Ozone, Environ., S is
Techn. 22, 71 1- 6 :
`. Pailt ra, I1, Brunet, H� Dore, . 1. Conaitions opta s
j*appiicaaon du Systemexi Oro - Perorvae
"'Hydrogene Water Research, Voint 22, N, r Pg. d.
Htinge, 1. et Bader, 11. (1 `6) 7`he Role of 1lv os t
Radical Reacaons in Ozonatian Processes in Aoueous
Solutions. Water lies 10. 3 -S t .
5. Barker, R., Improving the Effleiency o1 Ozone to Odour
Treatment with UV Light Ejecmcay Research Centre
Report M1233 (1979),
6, Dr, P.D. S. Stevens "Application of Rayox3 w'nr the
,emetuarion of contaminated Ciro ester ° HAZ.VAT
Central C nterences* Chicago. IL.Vid 1990.
Dr. Sol Lvandres et at 7reatment of Grounawater
Contammants with ' oldle Or ; n
.'7econd Generadon UV Light Tec` log' ` HALVACON
1. Sama Clara California, April, 1 1
1. P. W. Smith "AOX Reduction in Bleach Plans Effluent',
�Wo e 90 Conii!rence, March 19 to 23,1990,
,
1. Mr. Doug Reed 'Enhanced n Treatment of
Process Wastewater Containing Explosives-, IMZVAT
Conference, June 1990. Atlantic City, , " ,_
-kCKNOWLERUMUM
The author gratefuilyowi the very vaivable
preparanon of thts articie. Without their c ntnbution,
Lhe prepartiaon of the articie would not have been
~passable.
SOLARCHE
ONMENTALSYSTEMS

TEST BORING RECORD
EUVATION D.
NE;S' A[`ION- t o Foat
t (VEM
MICRIPMN
0 1 to 0 :0
40 60 as too
0,
Tod 11
1
[
S r
Fill kFirm to Soft 0(a gs to Tan to Brown
I_
Slightly Clayey Fine to glum Sandy SILT
Hit - Loose to Very Loose Orange to Tan
r a
i 3 i
Slightly Silty Fine to Medium SAND with
Organic Matter and Rock Fragments - Moist
g a
2
s t
t
10.5Fill
- Soft Tan to Gray Fins to Medium
Slightly Sandy Silty CLAY - foist
I
r � � E
1
e
t
4
� A
1
tlee
f 4A
}
Boring Terminated at 16A Feet.
t
No Ground dater Encountered at Time of
REMARKS.,
DRILLED BY LAW ENG.BORINGN
•1
LOGGED BY SBF DATE STARTED
5-14- 1
CHECKEDY CRL- AT MPL T EIS
-1 - 1
JOB NUMBER
56-8555
PAGE t OF 4 Law Environmental

TEST BORING RECORD
UJ-VATION Drfq,
REMARKS:
FENETRATION-BLOWS PFX FAT
DRILLED BY LAW 1BORING NUMBER
B-2
LOGGED BY SBF DATE STARTED
5-14- 1
CHECKED BY CRL DATE O PLET
-1 - 1
JOB NUMBER
56-8555

TEST BORING
ELEVATION DEEM PENETRATION-BLOWSPER FOOT
Lei 100
0.2 Topsoil
Fill - Firms to Soft Tan to Brown to grange
Fine to Medium Slightly Sandy silty CLAY �
s
-0 —IF—UtSoft grange to Brown Fine to lure j P
Slightly saner silty CLAY with Rook
Fragments - Slight Petroleum Odor
1 i1. k
Alluvium .Firsts Orange to Green Fine to }
Medium Slightly sandy Silty LAY - Moist
L i
t �
13.0
Alluvium ;-Firm Brown to Green Fine to
Medium lightly Clayey Silty SAND - Moist
1 ith strong Petroleums Odor
s
_..
Boring Terminated at 15.0 Feet.
No Ground Water Encountered at Time of
Boring.
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REMARKS: DRILLED BY LAW B G BORING NUMBER B_
LOGGED BY SBF GATE STARTED 5-1 - 1
CHECKED BY CRL DATE'COMPLETED 5-14-91
JOB NUMBER - 5
zr
PAGE 1 OF 1 Law nvironrrserstal

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88 SOIL SURVEY
TABLE 14.—ENGINEERING PROPERTIES AND CLASSIFICATION
[The symbol < means leas than,; > means greater than, Absence of an entry means data were not estimated]
C3assi 'lcaticn rag- 1 ercontage passing 4
Sail n e andoC'e�tha USDA texture a f lnches
_.
4U2f1G a
t 4see n4mr-t Liquid I Plas-
map symbol 1 1 Unified AASHiCJ o 1 1 ; limit ticity
a x e a R m e a s__
_ -------------
�n Pet
4p , A DS---..-;,.»---1 0-111 Andy loam--- --ISM, SM-SCIA-1 0 18 -1001 -»1001 -7 15-35 i <
ApplinR 111--4315andy clay, claylMH, CL, 1A-7 1 0-5 1 5-1 1 5-7 04 0-9 1 5- p 1 41-74 1
1 1 bars, clay. 1 ML, SC 1 t 1 t 1 1 1
143-6613andy clay, clayiSC, CL iA-4, --bo O 5 195-100195-100170-90 140-75" + 25-45 1
1 i t.
loam, dandy R
1- clay loaar
1 R d R p f 5 1 R y 1
1 B t 1
C S2, CeD2--..- ---_1 0- bandy clay to 1 �9, , ;A -A A- 1 174-100172-1 i 5-95 138- 1 „ 1-35 1
Cecil t ; CL, ML t
1-531Clay, clay lupin 1M , ML 1A-7 t 0 197-1001 2-100 172-w99 155-95 1 41-81
15 .651 ea herec 1
1 a bedrock. 1 1 1 1 1 1 1 m
11YM'<Ap
x 5 4 ➢ 8 t 1 i i } Y p
Cecil— ----------- 1 0-6 iSandy clay loam 'ISM, 5C 1A--4, A-61 0 174-10I4172-10015- S 38-51 1 21-3.5 ;
1 i i CL, ML I1 1 t
is 6-531 lay, clay loam 'MH, ML to-7 1 0 19-1001192-lGOt 2-99 055-95 1 41 t
15-651Meathered
a
Urban land 1 1 1 1 t t 1
DaS, OaD, DaE------t 0-7 tSandy clay loam 1CL, SC, a A-,6, A-^41 0 i 94_1001 4-.100175y-95 '40_70 1 25-40 1
Davidson 1 i CL-ML,; 1 i 1 1 t 1
1 1 SM-SC; 1
t 7-16tClay loam ------- JCL iA-6 i O 196-100190-1f1o175--95 5t1-75 1 25-40
1 16-99 i C a---_- w--.-.--1 CL, CH, i A-7, -°61 0 196-100195-1001185-100165-85 1 3 «-65
1 F 1 ML, MH
EnB. EnD ----------- 1 0-7 'Sandy Lean ----ISM, iA-2-4, 1 -5 181-100180-1001155-6 125-49'; 1 <3 I
Enon 1 r SM-SC- l A-4 4& 1 1 r 1
m 1 1 Sc l A-,
1. t 1 A--2-x6
7- 61C1ay loam, clay 1C11 1A-7-6 1 0-5 15 100 16-tUI11'75-9 16 -9 1 51-79
1 3 - 6011We t ere „ «- 1 - - t .. - -. - 1 --.- 1 --- t -. - ---
bedrock. 1 1 p ( 1 a
GeB2, GeD2------- --d 0-5 lSilty clay loam 1CL,. ML IA-6, 1 €1-3 195--1Cti3195-100:490-100i65-Kill 30-49
George" l le r t 1 1 A ,7-6
u 5-• 5n5ilty clay,, iMH ML tA•-7— i 40 i3-100'195-1001 0-100 75-98 i 41-75
1 1 silty clay
loam, clay t 1 t k t 1 t
1 t loam- t ► t i t t & 1
1 5--4913ilty clay loam,,MH IA-7-5 It 0 195-100i90-..100165--100I6G-96 1 50-75
t a silt loam, clay,,a 1 1 e 1
1 1" loam. % 1 1
i49-99tS It 1L1ast------- 1ML C& ,' iA 4 1 Ci 5 190-10019U-100165-100160-95 a <30
t 1 1 CL-ML It
Gas, Gn[-------.- 0-6 1Slaty silt loam 1GM, SM iA_4 1 5- 4 t60-&C 155--75 150-70 4�0-60 1 <35
Gc lds ton 1 t ML { 1 1 1 c 1 1
1 GM -GC
t 5-161 1aty silt loam.IGM, OR, ! A«. , 110-30 t55-100150-92 145-90 125-80 1 <45
slaty very fine' ML, 1 A-4 $ B 1 a 1
t 1 sandy loam, 1 GM -GC 1 A-,5 i 1 t 1
116--241 laty silt loam 1GM iA-2 i20-40 125_40 125-40 120-40 115-35 <20
1247-621Weathered
bedrock.
1i S-___ __®®_ -_®__b C®6 o"Sandy loam _ -1SMy ;A-»2, A-41 0 195-100c1 G 100151^8127-46 1 <30
Helena a 1, 1 M-sc, 1 1 1
Sc
1 8-11tSandy clay loam,iC 1A-6; Aa71 0 195-1430t95-100t1'0--90 R55--70 i 30^4:9
1:... clay loamy
{ 11-40JClay loam, sandy,CH, MH 'A-7 1 U 195"100195-100t73-93 156--80 1 50-85
1 , clay, clay. 1 t 1 1 1 1
14U�-6411�eathere
t t bedrock.
Sea footnote at and of table:
NP-5
15-,3or
R-22'
3-15
9--37
3- 1
9-37
5-1d
1 1 -25
15--35
NP-15
25-80
11-24
15-35
15-35
N-10
P'-1G
N - 1 t
NP-3
NP-9
15-25
2 4-5 r1

MECKLENBURG COUNTY, NORTH CAROLINA 91
TABLE 15.--PHYSICAL AND CHEMICAL PROPERTIES OF SOILS
!The symbol < means less than; > means greater than. The erosion tolerance factor (T) is for the entire
profile. Absence of an entry means data were not available or were not estimated!
rowan
Soil name and e Depth t Permeability i Available !Soil reaction; Shrink-sweli I factors
map symbol ; B water capacity potential 1
AAR, Ape-_.._.:,- --
0-11
f
Appling,
11-43
43-66
CeS2, CeD2 -------
0-6
i
Cecil
6-53
1
53-65
CuB*, CuD*:
Cecil--,.--_-----
Q-6
B.
6-53
1
53-65
1
Urban land.
ti
DaB, DaD, DaE ----
o-7
Davidson
7-16
16-99
En8, EnD --------- f
0-7
Enon
7-36
0
36-60
t
GeB2, Ge112 -------
0-5
Georgeville
5-35
1
35-49
49-99
t
Goldston
8-16
16-24
24-62
HeB --------------
0-8
Helena
8-11
i
11-40
0
40-64
i
HuH*:
Helena-___-.-..__ f
0-8
1
11-40
0
1
40-64
tl
Urban land.
Ire ell 1
6-24
is
24-28
0
28-65
Iredell ---------
o-6
6-24
0
24-28
i 0
28-65
1
Urban land.
LAS --------------
0-5
Lignum
5-37
;
37-50
See footnote at end of table,
In/hr
in/in
4.5-5.5
:Low ------------
0,24
4.5-5.5
:Mader -ate -------
:Low
0.20
0.12-0.16
4.5-5.5
------------
0.24
0.6-2O
A
0.13-0.15
1
4.5-6.0
tl
3Low ------------
0.6-2.0
1
0.13-0-15
4,5-5, ,5
!Moderate -------
0.28
---------------
0.6-2.0
1
0.13-0-15
1
4,5-6,0
!Low ------------
0.28
0.6-2.0
0.13-0-15
1
4.5-5�5
!Moderate -------
0.28
0.6-2.0
Or14-0.18
1
4.5-6,5
:Low ------------
O�28
o.6-2.0
1
0.15-0.18
4x5-6.c
8Low ------------
0.32
O6-2.0
0.12-0,16
4,5-6.o
!Low ------------
Oa24
2.0 -6.0
0�11-0.15
5a1-6�5
tIs
!Low ------------
O.17
6-0.2
0.15-0.20
5.1-7.8
sHigb -----------
0.'32
---------------
o.6-2.0
t
0-13-0a18
4ro5-6.0
fiLow ------------
0.37
0.6-2.0
0.13-0-18
4,5-5.5
trLow ------------
0,37
0.6-2<O
0.13-0-18
i
4.5-5.5
'9Low ------------ f
0.43
o.6�-2 .0
0105-0.10
1
4.5-5.5
ILow ------------ 1
0.43
2.0-6.o
0.10-0115
4.0-6.0
wLow ------------
0.20
2.o-6.o
0.10-0.15
4.0-6.0
tLow -------------
2.o-6.o
005-0.10
4,0-6.G
Mow ------------
0.20
---------------
2.o-6.o
0.10-0.12
d
4
4Low ------------
0.37
0.2-0.6
O,13-01.15
1
4.5-5.5
!Moderate -------
0.37
.06-0.2
1
0.13-0-15
1
4.5-5.5
oHigh....®--------i
0.32
---------------
ry
2,o-6.o
O10-0.12
4.5-6.0
!Low..------_----
0.37
0.2-0.6
1
0-13-0.15
4,5-5.5
!Moderate--------;
0.37
.06-0.2
O13-0-15
4.5-5.5
lHigh -----------
0.32
---------------
2.0-6.0
0.12-0,15
56-7-3
'KLow ------------s
0,32
.06-0.2
0.16-0.22
6.1-7,3
;Very high--- ---
0.20
.06-0.6
5,
0.14-0.18
l
ti
6>1-7.8
thigh -----------
---------------
0.28
2.o-6.o
0.12-0.15
5.6-7.3
!Low----- _--_
0.32
.06-0®2
0.16-0.22
6,1-7t3
flyer y high ------
0.20
,.06-0.6
0.14-0.18
1
6.1-7,8
Nigh-----------
O28
---------------
0.6-2,C
0.11-0.18
4.5-5.5
',Low ------------ c
.43
.,06-0.6
0,10-0.18
4.5-5.5
'Moderate--_.---- f
0.43
-------i.
--------
4
3
3
5
4
2
3
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and basal beds
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,n by an
' ertically
ouifer. Where
e rocks below,
ccurate
main-
ult. Confined
e called ieakv
,,it to analyze
timed aquifer
no a conduit
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and gravel
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N,
OCCURRENCE -AND MOVEMENT OF GROUNDWATER P
Table 3.1 Porosities for Common Consolidated and Unconsolidated Materials
f lav33 [ Sandstone
Silt 3-3
y ; Limestone/dolomite (original
Sand `3d Q secondary porosity
Gravel I , 0 } Shale 1-�0
:Sand & gravel,mixes i 3 Fractured r t litrte rock -i
ilaciai till d
l ll 33 Vesicular basalt
( t0-5
Dense. solid rock
volume of weer an aquifer can hold, it does not indicate how much water the aquifer
will yield,
When 'pater is drained from a saturated material tinder the force of
material releases only he
part of the total volume stored in its pores. Thequantitytof
water that a unit volume of unconfined aquifer gives ups by gravity i called its specific
yield (Figure Specific yields for certain rocks and sediment types are presented
in Table 5,2, Some water is retained in the pores by molecular attraction and captlm laxity, The amount of water that a unit vOlurne of aquifer retains after gravity drainage
is called its specific retention. fhe smaller the average grain size, the greater is the
Percent of retention, the coarser the sediment, the
when comparedtca the greater will be the speciMc yield;
porosity, The surface area for differero size sand grains is
shown in Table 53. Note the large increase in surface area forthe finest sediment.
As the surface area increases, a larger percentage of the; water in the pores is field by
surface tension or other adhesive farces. Therefore -finer sediments have lower specific
yields compared to coarser sediments, even if they both have the same porosity,
Specific yield plus specific retention equals the porosity of an aquifer® Both specific
yield and specific retention are expressed as decrial fractions or percentages. Specific
yields of unconfined aquifers (equivalent to their storage Coefficients*) range from
0.01 to 030. Specific yields cannot be determined for confined aquifers because the
aquifer materials are not dew atered during pumping.
t Storage coefficients cients are much lower in confined aquifers because they are not
drained during pumping- and any water released from storage is obtained primarily
by compression of the aquifer and expansion Of the water when pumped. During
Table S.?. Representative Sp ; 3fic Yield ranges for Selected"Earth Materials
t Sediment
tild 4`inld, % �
Clay 1�3
Sand 10- 0
Gravel
Sand and Gravel 1 5-3f1
25
Sandstone 85-1
t 0.3-3 Y
Shale
Limestone U 3
*The coerricient or storage is Tulip^ defined in Cha ter 4, Bric"Y. it is the volume of water taken into or
releasedfrom storage Per unit change in head per unit area:

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A~ ANNAft
UW M11401WAL,
NATIONAL ORATORIES DIVISION
300 CHAST IN CENTER BLVD. SMITE 31
KENNES W, G OROIA 3014
5 FAX [phone]
February
Lawn Environmental, Inc.
Lake Points office Park
4333 t Road Suite
Charlotte, 28217
Attention: Susan Fadero
LE Jor:6 4.
Subject: l analysis of sa l received n01/31/92.
Dear Ms. Fadero:
Law Environmental National Laboratories has completed
its analysis
of your samplesreports results the following
Theseresults I tonly to the contents of the, samples
submitted. 1 l not be reproduced
except in full
without 1 of Law EnvironmentalNational
Laboratories.
If there arequestions, please do not hesitate
to contact us.
Sincerely,
LAW ENVIRONMENTAL A LL LABS
Linda Harris
Hydrocarbon Laboratory Sa r isor
. tt ut : Data Report
Invoice

LAW ENVIRONMENTAL NATIONAL
LABORATORIES
TEST DATA REPORT
Date 02/07/92
page 1
---
Project Information
---
Lab Number :
62-3726-01
project No. :
56-8555-004.20
Cust. No.
Project Name :
FURR PROPERTY
Manager:
SAS AN FADERO
---
Sample Information
---
Station ID :
RW-1
Sampled
Date/Time
01/30/92 l6i07
Matrix :
W
Received
Date/Time
01/31/92 14:00
Type
GRAB
Received From/By
EES/SN
Collector
WAT
Chain
of Custody
242
Number of
Containers
a 5
Remarks
--- Test Data ---
Parameter. .............................
Method.... Units
PQL .......
Results...
Test Data
Analy
-- SAMPLE PREPARATION RESULTS --
EXT/TPH SEMI-VOLATILE/W
SP 3510
NA
02/04/92
JMK
--- SERIES 16000
TPH-VOLATILE
SPS 5030 mg/l
5
ND
02/06/92
BE
--- SERIES 17000
PH-SEMI-VOL TILE
EPA SFB mg/l
0.5
ND
02/05/92
RD

LAW ENVIRONMENTAL, INC.
NATIONAL LABORATORY
112 TOWNPARK DRIVE SAMPLING NAME OF FACILITY:
ow
ENNE A a', AR IA 0144 INFORMATION
4) 4 1 PI NUMBER STREET ADDRESS'
7
PR=OJEME J, vo
13-
_.. ,
AMPLER $SIG AT RED A� �
SAMPLING DATE�/3 6)
LENL LAD NO
iNMA SAMPLE STATIONDESCRIPTION CODE
DATIE I TIME H lsmw fly y T- Y;,"d
�ela� SIG 11)"e)
NOTE'
ALL OF THE ABOVE INFORMATION HAS BEEN TRANSCRIBED FROM ORIGINAL
L IFAIL 92- /901

LAW IAINC.
11
404-4 w34
Lam Environmental, Inc
L.nint Office Park
4333 Wilmont Road, Suite 300
Charlotte, NC. 282,17
Attention: Susan Fadero
Subject: Chemical analysis of samples received n 01/31/92.
Dear Ms. Fade:r
Law Environmental National Laboratories has completedits analysis
of your samples and reports the results on the following
These results relate only to the o ten f the samples
submitted. hi report shall not be reproduced except in full
without the approval of Lacy Environmental National Laboratories.
If there are any questions, please Rio not hesitate to contact us.
Sincerely
LAW ENVIRONMENTAL 'NATO LABS
Clifford ride
QC Coordinator
Attachment: Data Report
Invoice

CASE NARRATIVE
Project Name: Furr Property Date: 02/17/92
Project Number: 56-8555004 T20
This Narrative pertains to the following sample(s) submitted to Law
Environmental National Labs (LENL Kennesaw) on Ja,nM4ry21_, 1992.
Client ID # Lab Number
Matrix Spike (MW-1) 92-1901-10
Matrix Dup (MW-1) 92-1901-11
The request to utilize sample MW-1 as the matrix spike and matrix
spike duplicate for the Aromatic Volatiles (EPA 602) was accidently
overlooked by the analyst. Sample MW-8 (91-1901-08) was spiked
instead and the results are reported on the MS/MSD summary report.
MW-1 however, was analyzed in duplicate and the results have been
reported in this transmittal. We apologize for this oversight and
do not expect to have a similar reoccurrence.
Signed:
VV

LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Cate 02/ 1/92
Page 1
Lab Number 2-1901-01
Project No. : 56-855SO04 "T20
Project Name : FURR PROPERTY
Manager: SUSAN FACER
Station ID -: -1
Matrix
T S,
Collector z WA
Remarks
--- Project Information ---
Cut;. No.
--- sample Information ---
Sampled Date/Time
01/30/92 15:13,
Received Date/'dime
01/ 1/92 11:40
Received From/By
WA"T/E S
Chain of Custody 'ff
9630
Number of Containers
3
-_ 'feet Data ---
Parameter .......... .......... ........ Method.... Unit ....... Results... Test Date Anal
- CC ORGANIC ANALYSIS RESULTS
Diohl srodifluor meth ne EPA 601 ug/l 18 ND 012/05/92 VZ
Chlordmethan EPA 601 ug/1 0.80 NU 02/05/92 VZ
Vinyl Chlorides EPA 601 ug/l 1.8 NU 02/CS/92 VZ
Bromomethane EPA 601 ug/l 12 ND 02/05/92 VZ
Chloroethane SPA 601 ug/l 5.2 ND 032/05/92 VZ
Sri tlorofluor a th EPA 601 ug/l 3.2 Nth 02/05/92 VZ
1,1-D chloroethene EPA 601 g/l 1.3 ND 2/05/92 VZ
Methylene Chloride EPA 6031 ug/l 2.5 ND 02/05/92 VZ
trans l,2-Dichloroethene EPA 601 ug/l 1.0 N0 02/05/92 VZ
1,1°-Dichloroeth;ane EPA 601 Ug/l 0.70 ND 02/05/92 VZ
Chloroform EPA 601 ug/1 0.50 NC 02/05/`92 VZ;
1, 1, 1-Trichlor ethane EPA 601 Ug/1 0.86 ND 02/05/92 VZ
Carbon Tetrachloride EPA 601 ug/la 1.2 ND 02/05/92 VZ
1,2-Uichl+ roethane EPA 601 ug/l 0.30 ND 602/05/92 VZ
Trichloroethen EPA 601 ug/l 1.2 N 02/05/92 VZ
1,2- ichloropr ane EPA 6031 ug/l 0.40 ND 02/05/92 VZ
Sromod chloromethane EPA 601 ug/I 1.0 NC 2/05/92 VZ
2-ChloroethylvLnyl ether EPA 60ug/l 1 ND 602/035/92 VZ
cis-1,3-C chloro ro ne EPA 601 ug/l 3.4 NU 02/05/92 VZ
trans-1,3-LOichloro o n EPA 601 ug/l, 3.4 ND 02/05/92 VZ
1,1,2-Trichloroethah PA 601 ug/l 0.20 Nei 02/05/92 VZ
Tetra.chlo oethene EPA 601 ug/l 0.96 Nib 2/05/92 VZ
Uihr moth oroc thane EPA 601. ug/1 0.960 N} 02/ OS/92 VZ
ChltrohenZene EPA 601 ug/l 1®C Nil 02/05/92 VZ
Sromofora EPA 601 ug/l 2.0 NU 02/05/92 VZ
1, 1,2, 2--'Tetr c loro th n EPA 601 uq/1 0.30 ND 02/05/92 VZ
1,3-ichloroben ene EPA 601 ug/l 1.0 ND 02/05/92 Vz
1, 'Uichloro en ens EPA 601 ug/1 1 U 02/05/92 VZ
r
Signed

LAW
ENVIRONMENTAL NATIONAL
LABORATORIES
TEST DATA
REPORT
Dare + 2 / 14/92
Page 2
Lab 'Number : -1 1 - 1
Project No. : 56 66550 4 T20
--- Test
data ---
Parameter . ....»........,.........a.»...
Method....
Unit
.....,..
Results,..
'Test Date
Analy
-- GC ORGANIC1 BUNTS --
1,2-Dichlorobenzene
EPA 601
/ 1
1.0
ND
02/ 5/ 2
VZ
Methyl -tertiary -butyl sheer (MTSE)
EPA 602
/l
5.0
440
02/06/ 2
VZ
Benzene
EPA 602
/1
1.0
40
02/05/92
VZ
Toluene
EPA 62
ug/1-
1.0
1.
/66/2
VZ
th l enze e
EPA 602
/l
1.0
10
2/ 6/ 2
VZ
Xylan , "Total
EPA 602
/l
2.0
24
/ / 2
VZ
Signed

Date 2/1/92
Page
LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
--- Project Information --
Lab Number 92-19 1-62
Project No. w 56-8555004 T20 Gust.
Project tams FURR PROPERTY
"tanager SUSAN FADER '
_-- Sample Information ,---
Station I 2 Sampled Date/Tim 11/9 15:30
MatrixReceived Date/'lime 01/31/92 11
Type Received Prom/By AT/EE9
Collector t WAT Chain of custody 963
Number f Containers
Remarks
-- Fast Data ---
Parameter .............. ...t ..#...... Method.... units P L.... A. Results ... Test bats Analy
- cc ORGANIC ANALYSIS RESULTS
Dichloradifluoromethane EPA 601 a /l is NO 02/06/92 VZ
chl rom than EPA 601 u /1 0.80 ND 02/06/92 2
Vinyl chloride EPA 601 Ug/l 1. 02/06/92 VZ
From m th n EPA 601 a/1 12 ND 02/06/92 V
chl rusth n EPA 601. ug/1 5.2 ND 02/06/92 V2
Trichl rcfluor m th n EPA 601 ug/l 3.2 Nib 02/06/92 V
1, 1- ichloro th ne EPA 601 a /l 1..3 NO 02/06/92 V
Methylene Chloride EPA 601 u /l. 2.5 NO 02/06/92 VZ
trans-1, 2 i hl ru th n EPA 601 ug/l 1. 02/06/92 VZ
I,I-Dichloroethane EPA 601 u /l 0.70 NO 2/ 6/92 V
chloroform EPA 601 u9/l 0.50 ND 02/06/92 V
1,1,1-Trschl ru than EPA 601 u /l 0.30 NO 02/06/92 VZ
Carbon Tetrachloride EPA 661 a /l 1. 2/06/92 V
1,2-Dichloroethane EPA 601 ug/l 0.30 ND 02/06/92 VZ
Trichloroethene EPA 601 Ug/l 1.2 ND 02/06/92 VZ-
1,2-Dichlurupr pan EPA 601 ue /1 0.40 NO 02/06/92 VZ
Eromodichloro than EPA 601 u / L 1.0 NO 02/06/92 VZ
2-chloro thy ° inyl ether EPA. 601 u9/1 1.3 ails 02/06/92 V '
ris-1, -Di hl p ° pen EPA 601 ug/1 3.4 02/06/92 VZ
trans-1,3-Di hl r p p n EPA 601. u9/l, 3.4 ND 02/06/92 VZ
1,1,2-Tri:chl r than EPA 601 u9/1 0.20 NO 02/06/92 V
Tetrachloroethene EPA 601 u /l 0.30 STD02/06/92 VZ
Dibromochloromethane EPA 601 u9/ 1 0.90 NO 02/06/92 VZ
Chlorobenzene EPA 601 a /l 1.0 NO 02/06/92 V
Bromoform EPA 661 Ug/l 2.0 ND 02/06/92 V
1, 1, 2, 2-T tra. hloro than EPA 601 ug/1 0.3 2/06/92 V
1,3-Di.chlora n ens EPA 601 ug/lY 1 2/06/92 VZ
1, - ichlorobenzen EPA 601 a /l 1-0 ND 02/06/92 V
Signed

LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Date 1/9
Page
Lab Number : 9 -19 1 02
Project N. s 5 ,-955 T20
--- Test Data ---
Parameter ........ ..................... Method.... emit L ....... Results... Teat Pate Analy
-- GC ORGANIC ANALYSIS RESULTS
,2- i hloro a EPA 601 Ug/1, 1.0 N / 6/9
Methyl -tertiary -butyl. ether { * BEPA 602 ug/1 S.0 N / 6/9
Benzene'PEA 602 Uq/1 1.0 N / 6/9
Toluene EPA 602 Uq/1 1.0 ND 0/ 6/9
Ethylbenzene EPA 602 ug/1 1.0 ND / 6/9
Xylene, 'Total EPA 602 ug/l, ND 0/ 6/9

LAID ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Date 02/14/92
?age 1
Lab Number : 52�190
Project Name - .«
Manager: SUSAN FADERO
Station I -3
Matrix '
Type : GRAB
Collector r WAT
-- Project information --
Cunt* No. .
-_- Sample Information ---
Sampled ile Date/Time 01/30/92 1 z3
Received Date/"ire 1/1/92 11:4
Received Fr m/ AT/EE
Chain of Custody 963
Number of Containers
-- Teat Data
Parameter ..... .......... ......m.., b. Method.... Units P ....... Results... Teat Nate Anal
-- GC. ORGANIC ANALYSIS RESULTS
ichl rod fluor eth n EPA 601 u /1 16 ND 02/06/92 V
hlor meth ne EPA 601 /l 0.80 ND 02/06/92 VZ
Vinyl Chloride EPA 601 /l 1.E ND 02/06/92 VZ
Eromomethane EPA 601 u /1. 12 NO 02/06/92 V
hlo°ethane EPA 61 u/l 6.2 ND 02/06/92 VZ
Trichlorof uoro ethan EPA 601 ug/l 3.2 ND 02/06/92 V
1,1-IDichloroethenEPA 661 a/1 1.3 ND 02/06/92 VZ
Methylene Chloride EPA 601 u /l 2.5 ND 02/06/92 VZ
trans,-1,2-Dichloroethene EPA 601 ug/1 1.0 ND 02/06/92 V
1, 1- Dichlotn th n EPA 601. Ug/l 0.7 ND 02/06/92 VZ
Chloroform EPA 601 uD9/l 0.50 ND 02/06/92 VZ
1, 1.1-Tric lcrc> t,ha¢ EPA 601 u /l 0.30 ND 02/06/92 VZ
Carbon Tetrachloride EPA 611 u /1 1.2 NO 02/06/92 6/92
1,2-Dl chloroethane EPA 661 a /l 030 NO 02/06/92 VZ
Trichlsrc there EPA 601 a /l 1.2 ND 02/06/92
1.,2-Dichl ropr span EPA 601 ug/1 0.40 DAD 02/06/92 V
Promodichloromethan EPA 601 a /l 1. ND 2/06/92 V
2-Chloroethylvinyl ether EPA 601 u /l 1.3 ND 02/06/92 '
cis-1,3-Dichlorop ` n EPA 601 ug/l 3.4 ND 02/06/92 VZ
trans 1, Dichloropropen EPA 601 u9/1 3.4 ND 02/06/92 i
1, 1, `3-Trl.chlor+ ethan EPA 601 a /l 0.20 ND 02/06/92 V
Tetrachloroethen EPA 601 ua3/l 0.30 ND 02/06/92 VZ
Di%romochloromethan EPA 601 uDl/l 6.96 NOD 02/06/92 VZ
hl.oroten ene EPA 631 u /l 1.6 N 2/06/92 VZ
rcm form EPA 601 u+ /l 2.0 ND 02/06/92 VZ
1,1,2,2-Tdtrachloro than EPA 601. Ug/l, 0.30 ND 02/06/92 VZ
1,3-Dichlorobenzens EPA 661 Ug/1 110 ND 02/ 6192 t
1,4-Dichi roben ene EPA 601 u /l 1.0 NO 02/06/92 VZ
Signed

LAW
ENVIRONMENTAL NATIONAL
LABORATORIES
TEST DATA
O T
Date 32/1/2
Page
Lab Number : -1 --0
Project N. : 56«-5555 T2
_-- Test
Data ---
Parameter ...................... ....
.... Method....
Units
P ....*..
Results...
Test Date
Analy
-- GO ORGANIC ANALYSIS RESULTS --
1,2 l lalc r b n n
EPA 601
a/1
1.0
NO
02/ 6 92
VZ
methyl -tertiary -butyl ether ( )
EPA 602
u /l
5.0
6.5
02/ 6/ 2
VZ
Benzene
EPA 602
u /1
1.10
1.3
2/ 6/°2
V
Toluene
EPA 602
u /l
1.0
3.
2/ 6/ 2
V
EthylbenzeneEPA
62
gag/1
1.0
NO
02/06/92
VZ
1. n , Total
EPA 602
u /1
2.0
9.5
2/ 6/ 2
V
Signed

LAW ENVIRONMENTAL NATION 'LABORATORIES
TEST DATA REPORT
2/17/92-
I,
--- Project Information ---
Lab Number ; 92-19 1.- 4
Project No. ; 56-8555004 T20 Cram. No.
Project Name : PURR PROPERTY
Manager:
SUSAN FADERO
Sample Information ---
Station ID :
-4
Sampled Date/Time
1/3 /9 15:37
Matrix :
W
ReceivedDate/Time :
01/31/9 11:40
Type
GRAB
Received,From/ByWAT/EES
Collector
WAT,
Chain of Custody9630
Number of Containers
; 3
Remarks
-- Test data ---
Parameter ................A............Method.... mite
-- GC ORGANIC ANALYSIS RESULTS
Dichlorodifluoromethane
EPA
601
gag/i
Chloromethane
EPA
61
/1
Vinyl Chloride
EPA
601
g/1
Bromomethane
EPA
601
u/ l
hl.nrethn
:PA
61
/ 1
'rihlrflur:ethh
EPA
61
e
1,1-Dichloroethene
EPA
601
u /l
Methylene Chloride
EPA
51
as/l
tr n 2,2 Dich r et ene
EPA
601
t /1
1,1 1 hlor eth ne
EPA
601
a /l-
Chloroform
EPA
601
tag/l.
1, 1,1-Trichl r° th nd
EPA
601
a /l
Carbon Tetrachloride
EPA
601
/l
1, 2--D i. h l methane
EPA
601
u/
Trichloroethene
EPA
601
u /
1,2-'ihlrprdpn
EPA,
661
1
6resdihlerethene,
EPA
61
u/;
2a hleroeth l in l ether
EPA
601
a /l
i s- , 3- irhl r apr pen
EPA
601
a / l:
trans-1, 3- ichlereprn rye
EPA
601
u+ /
1,1,2-Tri hl e th h
SPA
601
ug/1
Tetrachloroethene
EPA
601
u /l
Di. r c e hlar met e
Epp,
601
1
hl r den ene
EPA
601
ug/l
Bromoform
EPA
61
u/.
1,1,2,2-Tetrahlrthend
EPA
61
u9/l
1, 1-tli hlor he rene
EPA
601
u /l
1, - i hl r benzene
EPA
631
/l
PQL ...... Results— Test Date An l
9
/6/92
V"
4.
2/6/92
VZ
9.
2/6/92
V
60
ND
02/06/92
VZ
26
2/6/92
VZ
16
ND
02/06/92
VZ
6.5
ND
02/06/92
VZ
2
ND
02/06/92
VZ
5.0
ND
02/ 6/92
VZ
3.5
ND
02/06/92
V
2.5
ND
2/ 6/92
VZ
1.5
ND
02/ 6/ 2
VZ
6.0
ND
02/06/92
VZ
1.5
ND
02/06/92
VZ
6.o
ND
2/ 6/92
VZ
2.
2/6/92
VZ
5.
2/6/92
VZ.
6.5
ND
02/06/92
VZ
17
ND
02106/92
VZ
17
ND
02/06/92
VZ
1.
2/6/92
VZ
1.5
ND
02/06/92
VZ
4m
2/6/92
VZ
5..
2/6/92
`Z
10
ND
02/06/92
VZ
1.5
ND
02/06/92
VZ
5.0
ND
02/ 6/92
VZ
5.0
ND
02/ 6/92
VZ
SignedXd

LAW
ENVIRONMENTAL NATI
PIES
"EST DATA
REPORT
Date 2/1/92
Page 2
Lab Number : 92-1901-04
Project No. z 5 - 55 T20
--- Test
Data ---
Parameter . .... ............... ........
Method....
Units
P L...
4v .
Results...
Test Date
Analy
ORGANIC'5 --
1,2-Dichlorobenzene
EPA 601
/
02/ 6/92
VZ
t -t r r ty ether (M
EPA 602
ug/l
25
800
02/06/92
V
Benzene
EPA 602
u /1
5.0
160.
2/ /92
V
Toluene
EPA 602
u /l
5..0
ND
02/06/92
V
Ethylbenzene
EPA 602
u9/1
5.0
40
02/06/92
VZ
Z l n, Total
EPA 602
a /l
10
70
02/06/92
VZ

LAW ENVIRONMENTAL NATIONAL, LABORATORIES
TEST DATA REPORT
Date2/14/92
Page'
__- Project Information ----
Lab Number ; --19 1- 05
Project No. 56-8555004 T2
Project Name FURR PROPERTY
Manager: SU aAN FADERG
--- Sample Information ---
Station I MW-5 Sampled bate/'Tine 1/3 /92 15:45
Matrix : W Received Late/Time : 01/31/92 11:40
Type Received From/By : WAT/EE
Collector m WAT Chaim of Custody 9636
Number of Containers . Z
Remarks
--- Test Data ---
Parameter ......................... ..... Method.... Units P L— .. Results... 'Peet Date Analy
GG ORGANIC ANALYSIS RESULTS
ichlorodifluoroethane; EPA 61 g/l is ND 02/06/92 VZ
hloromethane EPA 601 ug/l 0.60 ND 02/06/92 VZ
Vinyl Chloride EPA 601 ug/l 1.8 ND 02/06/92 VZ
Eromomethane EPA. 601 ug/l 12 ND 2/06/92 VZ
Ghloroethane, EPA 61: ug/l 5.2 ND 02/06/92 V
"Trichloro'luoremethane EPA 601 ug/l 3.2 NU 02/06/92 VZ
1.,1-Dichloroethene EPA 601 ug/1 1.3 ND 02/06/92 VZ
Methylene Chloride EPA 601 ug/, 2.5 ND 02/06/92 VZ
trans-1,2--Dichloroe hene EPA 6E1 ug/l 1.6 Nib 2/06/92 VZ
1,1-9ichleroethane EPA 601 ug/l 0.70 NO 02/06/92 VZ
Chloroform EPA 601 ug/l 0.50 ND 02/06/92 VZ
1,1,1-Trichloroethane EPA 601 ug/l 0.30 ND 02/06/92 VZ
Carbon Tetrachloride EPA 601 Ug/l 1.2 Nib 02/06/92 VZ
1, 2- Diehl rcet ne EPA. 601 Ug/l 0.302/06/92 VZ
Trichlor°oethen EPA 601 ug/l 1.2 ND 02/06/92 VZ
1 , 2- ichl ro-propane EPA 601 g/l 0.40 ND 02/06/92 VZ
5romodich oromethane EPA 601 ug/l 1..6 ND 02/06/92 VZ
2-Gh oroethylvinyl ether EPA 601 ug/I 1.3 ND 02/06/92 VZ
cis,-1, 3-D chlorc sro ene EPA 661 ug/l 3.4 ND 02/06/92 VZ
trans-1, -Dichloro ropene EPA 601 ug/lu 3.4 NO 02/06/92 VZ
1,1,2-Trichlor ethane EPA, 601 ug/l 0.20 ND 02/06/92 VZ
Tetrachloroethene EPA 601 Ug/1 0.30 ND 02/06/92 VZ
Uibr moch pros ethane EPA: 601 ug/1 0.90 ND 02/06/92 VZ
hl rober ene EPA 601 ug/l 1.0 ND 02/06/92 VZ
Bromoform EPA 601 ug/1 2.0 ND 02/06/92 VZ
1,1,2,2-Tetrachlor ethane EPA 601 ug/1 0.30 ND 02/06/92 VZ
1,3-Dichlorobenzene EPA 60ug/1 1.0 NO 02/06/92 V
1,4-Uichl;oroben ene EPA 601 ug/1 1.0 ND 02/06,/92 VZ
Signed �

LAW ENVIRONMENTAL NATIONAL LABORATORIES
°T DATA REPORT
Data 02/1 /9
Page
Lab Number : 92-1961-05
Project No. : 56 6666 2
- Teat Data ---
Parameter ...................... ....<.. Method.... Units T L........ Results... Teat Date Analy
ORGANIC ANALYSIS RESULTS
1,2-Dichlorobenzene EPA 601 u 1 1. 2/ 6 f 92 V
Methyl -tertiary -butyl ether (ELT EPA 602 ug/1 5.0 TAD /06
Toluene EPA 602 Ug/1 1.0 ITT! 6/92 VZ
i n , Total EPA 602 9/1 2.0 ND 02/06/92 V
r
Signed

LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Date 2/14/92
Page
__- Project Information ®_-
tab Chamber :
2-1901-06
Project No. :
E6-E555 04 T20
Cust. No.
Project Name :
FURR PROPERTY
Manager:
EC16A 1 FADERO
-- sample Information ---
Station bE :
-6
Sampled Date/Time
: 01/9 /92 15:4
Matrix :
W
Received Date/Time
91/ 1/ 11:4'
Type :
GRAB
Received From/By
: WAT/EEE
Collector :
WAT
Chain of Custody
963
Number of Containers
: 3
Remarks
--- 'cat Data. ---
Parameter ................... .................... Method.... Units P T........ Results... Test Date Analy
-- GC ORGANIC ANALYSIS RESULTS;
lrhl r diflu r methane EPA 601 ug/l 1E ND 02/06/92 V
Eh or me hane EPA 601 /1 0.80 ND 02/06/92 VZ
Vinyl Chloride EPA. 601 ug/1 1.E ND 02/06/92 VZ
Er m methane EPA 601 dg/l 12 NE 02/06/92 V
hlor ethane EPA 601 /l 5.2 Nil 02/06/92 V2
richl rofluoro ethane EPA 601 ug 3.2 NCI 02/06/92 V
1,1- 1l hlor ethene EPA 601 ug/1 1.3 ND 02/06/92 VZ
Methylene Chloride EPA 601 ug/1 2.5 ND 2/06/92 vz
trans-1 , 2- Dichler ether EPA 601 ug/1 1.0 ND 02/06/92 VZ
1, 1-Elchlntoethane EPA 601 ug/l 0.70 ND 02/06/92 V
Chloroform EPA 601 ug/l 0.50 ND 02/06/92 V
1, 1-Tri hlor ethane EPA 601 :g/1 0.30 ND 02/06/92 VZ
Carbon Tetrachloride EPA 601 ug/l 1.2 NE 02/06/92 VZ
1,2-Dichloroethane EPA 601 Ug/1 0.30 NE 02/06/92 VZ
Erl hloroethene EPA 601 g/l 1.2 ND 02/06/92 VZ
1, 2-91 hl aropropane EPA. 601 ug/l 1.4E NE 02/06/92 VZ
From dlehl r methane EPA 641 ug/1 1.0 ND 02/06/92 V
2z- hl roethylvinyl. ether EPA 601 ug/1 1.3 Nil 02/06/92 V
la-1 3- 1 hl:a Pr a n EPA 601 ug/l 3.4 ND 02/06/92 V
trans- , 3-Di hl rr P Pens; EPA 601 a /1 3.4 NO 02/06/92 VZ
1,1,2-Trichloroethane EPA 601 ug/l 0.20 ND 02/06/92 VZ
Tetra hl r e hene EPA. 601 ug/1. 0.30 ND 02/06/92 VZ
Dibromo hlbr :methane EPA 601 Ug/1 0.90 NE 02/06/92 V
hlor ben ens EPA 661 ug/l 1.0 NO 02/06/92 V
Bromoform EPA 601 ug/l 2.0 ND 02/06/92 VZ
1,1,2,2RT t.ra hl r e hane EPA 601 ug/1 0.30 ND 02/06/92 VZ
1,3-Di hl robenxene EPA 601 ug/1 1.0 ND 02/06/92 VZ
1,4-E . hlc roben ene EPA 601 ug/l 1.0 ND 02/06/92 V
Signed Eaa�

LAW
ENVIRONMENTAL NATIONAL
LABORATORIES
TEST DATA
REPORT
Date 02/14/92
Page 2
Lab Number : 92-1901-06
Project No. : 56-8555004 T20
--- Test
Data ---
Parameter .................. ............
Method ....
Units
PQL.— ....
Results ...
Test Date
Analy
-- GC ORGANIC ANALYSIS RESULTS --
1,2-Dichlorobenzene
EPA 601
Ug/l
1.0
ND
02/06/92
VZ
Methyl -tertiary -butyl ether (MIRE)
EPA 602
ug/l
5.0
18
02/06/92
VZ
Benzene
EPA 602
Ug/1
1.0
ND
02/06/92
VZ
Toluene
EPP, 602
ug/1
1.0
ND
02/06/92
VZ
Ethylbenzene
EPA 602
fag/1
1.0
ND
02/06/92
VZ
Xylene, Total
EPA 602
Ug/l
2.0
ND
02/06/92
VZ

SAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Date 02/14/92
Page
--- Project Information --
1,ab Num r :-i70.L--
Project No. s: 56-8555004 T2
Project Name ; FURR PROPERTY
Manager: SUSAN FADERO
Station I
Matrix
Tyra R
Collector : DRAT
u t . No.
--- Sample Information ---
Sampled Date/Time w 01./3 /92 16: 6
Received Date/"Time i 01/31/92 11:40
Received Prom/By T/ R6
Chain of Custody 963
Number of Containers m
®-- Teat data ---
Parameter ........... .... ............. Method.... Units P L....... Results... Teat Date Analy
__ GC ORGANIC NALYS S RESULTS
IDichl rr difluor meth n EPA 601 uq/1, 19 ND 02/06/92 ii
hl ar c eth ne EPA 601 ug/l 0.80 ND 02/06/92 VZ
Vinyl Chloride EPA 601 ug/1 1.8 ND 02/06/92 VZ
r mo ethane EPA 601 ug/l 12 ND 2/06/92 VZ
Chloroethane EPA 601 XJg/l 3.2 ND 02/06/92 VZ
Trichlorofluoromethane EPA 601 gag/1 3.2 ND 02/06/92 VZ
1, 1-iDichlor Seth n EPA 601 ug/1 1,3 ND 02/06/92 VZ
Methylene Chloride EPA 601 ug/l 2.6 ND 02/06/92 VZ
trans , 2- ichl aroeth n EPA 601 ug/1 1.0 ND 02/06/92 VZ
, 1-DD chlcr reth n PDT 601 ug/1 0.70 NO 02/06/92 VZ
Chloroform EPA 601 ug/1 0.50 ND 02/06/92 VZ
1, 1, 1 Trichloro than EPA 601 ug/l 0.30 ND 02/06/92 VIZ
Carbon Tetrachloride EPA 601 ug/l 1.2 ND 02/06/92 VZ
1, 2-DDichl :r ethane EPA 601 ug/1 0.30 ND 02/06/92 VZ
Trichlo n +bhene PPP 661 ug/1 1.2 ND 02/06/92 vz
1,2- ichl r pr an EPA 601 ug/l 0.40 ND 02/06/92 VZ
Promodichlorum th n EPA 601 ug/I 1.0 ND 02/06/92 VZ
2-chlornethylvi yl other; EPA 601 rag/1 1.3 ND 02/06/92 V
cis 1,3- ichlor pr pen EPA 601 ug/1 3.4 ND 02/06/92 V
trans- , 3-DDi hl r pene EPA 601 ug/l 3.4 DAD 02/06/92 V
1,1, 2-Tr dhlr r ethan EPA 601 ug/l 0.20 ND 02/06/92 BIZ
Tetr chlor eth n PA 601 ug/1 0.30 ND 02/06/92 VZ
Dibromochlaromethane RPM, 601 ug/l 0.90 ND 02/06/92 VZ
hloroben en EPA 601 ug/1 1.0 ND 02/06/92 BIZ
DDrom form EPA. 601 g/l 2.0 ND 02/06/92 VZ
1, 1, 2, 2-T trachl ro thane EPA 601 ug/ � 39 NO 02/06/92 VZ
1, 3 DDi.chl robenren EPA 661 ug/1 1.0 ND 02/06/92 VE
1,4-Dichlarobenzene EPA 601 ug/1 1.0 ND 02/06/92 VZ;
Signed 4L� -,iu"

LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Date 2/1.4/92
Page
Lab Number ; 92-1901-07
Project No. : 56 855 0 4 T20
a_.. Test Data ---
Parameter....... .... ..... ............. Method.... Emits 9 L, ....... Results... Test Cate Analy
-- CC ORGANIC ANALYSIS RESULTS --
1, 2-Diehl pro n EPA 601 ug/1 1.0 ND / v
Methyl -tertiary -butyl ether (H EPA 602 uq/ 1 5.0 47 2 VZ
Benzene EPA 602 9/l 1. 2/ 6/92 VZ
Toluene ERA 602 is/1 1. 6/92 VZ
thylbenzen ERA 602 + / ,, 1.0 ND 02/06/92 VZ
len , Total EPA 602 '/1_ 2.0 ND 02/ 6/92 VZ
11
Signed

LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Date 2/14/92
Page 1
---- Project Information --
Lab Number ¢-1901-08
Project No. 56-8555004 V23 Cust. No.
Project Name : 'FURR PROPERTY
Manager SUSSUSAN FADERO
. - Sample Information ---
Station ID MW-B Sampled gate/Time : 01/30/92 16.6
Matrix ; W Received Date/`dime : 1/31/92 11:4
Type Received From/By : WAT/EES
Collector : WAT Chain of Custody :: 963
Number of Containers
Pemarl�a
-_- Test Data ---
Parameter .......... ... Method.... Units P T,....... Results... Teat Date ,Deal}
-- GC ORGANIC ANALYSIS RESULTS
Dichlorodifluoromethane EPA 601 ug/1 18 NO 02/06/92 VZ
hl+r urethan EPA 601 ug/1 0.6 02/06/92 VZ
Vinyl Chloride EPA 601 ug/1 1.6 ND 02/06/92 VZ
Sr+ moethan EPA, 601 ug/ L 12 ND 02/06/92 V
hl r ethane EPA 601 ug/1 5.2 NO 02/06/92 V
Trichlorofluoromethane EPA01 ug/ l 3.2 Nth 02/06/92 VZ
i, -ichloroethene EPA 601 ug/1 1.3 NO 02/06/92 VZ
Methylene chloride ERA 661 ug/1 2.3 NO 2/06/92 VZ
trans l,2 i hlar et ens EPA 601 ug/l 1.0 ND 02/06/92 VZ
1, 1.-[Di hl r et ane EPA 601 ug/1 0.70 NO 02/06/92 V -
chloroformEPA 601. Ug/l 0.50 ND 02/06/92 VZ
1,1,1-Trichloroethane SPAS 601 ug/l 0.30 NO 2/06/92 VZ
Carbon Tetrachloride EPA 601 ug/l 1.2; NO 02/06/92 VZ
1,2- i hler ethane EPA 661 ug/l 0.3 02/06/92 VZ
Trichloroethene EPA 601 Ug/1 1.2 ND 2/06/92 VZ
1,2-ichl r pr pane EPA 601 ug/l 0.40 ND 02/06/92 VZ
Bromodichloromethane EPA 601 ug/1 1.0 NO 02/06/92 VZ
2-Chloroethylvinyl ether EPA 601 ug/ . 1.3 NO 02/06/92 V
ci -1,3- 1chl ropr gene EPA 601 ug/l 3<4 ND 02/06/92 V"
t an -1,3 TDichl r p pen EPA 601 g/l 3.4 NO 02/06/92 VZ
1,1,2 ri hl r ethane EPA 661 ug/l 0.20 NO 02/06/92 VZ'
Teti . hlnroeth ne EPA 601 ug/1 6.30 ND 02/06/92 V
Dibromochloromethane EPA 601, ug/1 0.90 ND 02/06/92 VZ
hl r uben ens EPA 601 ug/ 1 1.0 ND 02/06/92 VZ
Bromoform EPA 601 ug/1 2.0 NO 02/06/92 VS
1,1,2,2-Tetra hlar ethane SPA 601 ug/1 0.30 ND 02/06/92`tile
1,3-Dichlorobenzene EPA 661 ug/1 1.0 ND 2/06/92 VZ
1, -Di hl roben ens EPA 601 Uq/1. 1.0 ND 02/06/92 VZ
Signed D

LACE ENVIRONMENTAL NA IONA LABORATORIES
TEST DATA REPORT`
Data 2/14/92
Page 2
Lab Number : 92-1901-08
Project No. : 6-566 Ci4 T20
--- "feat Data ---
Parameter ............. ——............. Method.... Units P L« ...... Results... feat Tate Ahaly
CSC ORGANIC ANALYSIS RESULTS,'
1 2-Di hlo oben EPA 601 Ug/l 1.0 ND 2/06/ 2 VZ
Methyl -tertiary -butyl ether (MTBE) EPA 602 Ug/1 5.02/ 6/ 2 VZ
Benzene RSA 602 /1 1.0 RT 2/06/ 2 VZ
Toluene n SPA 662 /l 1.0 NTH / 6/ 2 VZ
Ethylbenzene EPA 602 /l 1.0 ND 02/06/ 2 VZ
yl en , Total SPA 602 a / l 2.0 D / 6/ 2 y
Signed

LAB ENVIRONMENTAL NATIONAL
LABORATORIES
TEST
DATA
REPORT
Date 02117/92
Wage
_ -
Project
Information ---
Lab Number 2-191-69
Project No. s 56 8555004 120
Cult. No.
Project Name z FURR PROPER'
Manager: SUSAN FADERO
---
Sample Information
---
Station 1 , - l
Sampled
Date/Time
l/ 0 16:07
Matrix "
Received
Date/Time
01/ 1192 11:40
Type GRAS
Received From/By
NA E S
Collector WAS
Chain
of Custody :
9630
Number of
Containers :
6
Remarks
Teat
Data ---
Parameter ....... ..........I ......Method....
units
P 1..... .. Results...
Test Este
A aly
--
-- INORGANIC CHEMISTRY RESULTS
Chemical Oxygen Demand
EPA
410..
mg/1
5
NO
02/07/92
AAT
Chloride
EPA
325.3
a /l
0.2
11
02/ 5/92
EC
Residue, ion Filterable ( SS)
EPA
160.2
m /l
10
490
02/ 1/92
S
True Color
EPA
110.2
P.C.U.
5
ISO
1/31/92
EC
Turbidity
EPA
180.1
U.T.U.
0.7
110
01/31/92
BC
--
-- METALS ANALYSIS - METALS PREP RESULTS
Iron, Dissolved
EPA
6010
m /l
0.1
1.7
02/04,/92
JST
--- SERIES 35000
Dissolved Metals Prep; Aqueous ICP
EPA
3010
N/
2/02 2
HH
-- CC ORGANIC ANALYSIS RESULT ®-
Cichlc°cdifl.umethsne
EPA
61
u/l
90
Nib
2/07/92
V
Chlor methane
EPA
601
u /l
4.0
ND
02/07/92
VZ
Vinyl Chloride
EPA
601
a /l
9.0
NO
92/07 92
V'
P cmdmethane
EPA
601
a/1
60
ND
02/07/92
VZ
Chloroeth ne
EPA
601
a /l
26
ND
02/07/92
VZ
Trichlorofluoromethane
EPA
601.
1,
16
ND
02/07/ 2
VZ
1,1-ichlrethene-
EPA
61
/l
6.5
NO
12/792
V
Keth lease Chloride
EPA
601
a/1
12
ND
12/07/92
VZ
trans-1, 2-Pichlc ° eth e
EPA
601
/l
5.0
ND2/07
92.
VZ
1,1-Dlchld cethane
EPA
601
/l
3.5
ND
02/07/92
V
Chloroform
EPA
601
u /1
2..5
ND
2/ 7/92
VZ
1,1,1 i hlc ethane
EPA
60
a /l:
1.5
NC
2/07/92
V
Carbon Tetrachloride
EPA
601
u9/1
6.0
ND
02/07/92
v72
1,2-Dichloroethane
EPA
601
ug/l
1.5
N}
2/07 2
VZ
Trichlaroethene
EPA
601
a/1
6.0
ND
02/07 92
V

LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Date 02/17/92
Page 2
Lab Number : 92-1901-09
Project No. : 56-8555004 T20
--- Test Data ---
Parameter ....... — ..................... Method .... Units PQL ....... Results... Test Date Analy
-- GC ORGANIC ANALYSIS RESULTS
1,2-Dichloropropane EPA 601 g/l 2.0 ND 02/07/92 VE
Bromoth chloromethane EPA 601 ug/l 5.0 ND 02/07/92 VZ
2-Chloroethylvinyl ether EPA 601 ug/l 6.5 ND 02/07/92 VZ
cis-1,3-Dichloropropene EPA 601 ug/1 17 ND 02/07/92 VZ
tran s-1,3-Dichloropropene EPA 601 ug/1 17 ND 02/07/92 VZ
1,1,2-Trichloroethan e EPA 601 ug/l 1.0 NO 02/07/92 VZ
Tetrachloroethene EPA 601 ug/l 1.5 ND 02/07/92 VZ
Dibromochloromethane EPA 601 ug/l 4.5 ND 02/07/92 VZ
chl,oroben zene EPA 601 Ug/1 5.0 ND 02/07/92 VZ
Bromoform EPA 601 ug/1 10 ND 02/07/92 VZ
1,1,2,2-Tetrachloroethane EPA 601 Ug/l 1.5 ND 02/07/92 VZ
1,3-Dichloroben zene EPA 601 ug/l 5.0 ND 02/07/92 VZ
1,4-Dichloroben zone EPA 601 ug/l, 5.0 ND 02/07/92 VZ
1,2-Dlchlorobenzene EPA 1 ug/l 5.0 ND 02/07/92 VZ
Methyl -tertiary -butyl ether (MTBE) EPA 602 ug/l 25 70 02/07/92 VZ
Benzene EPA 602 ug/1 5.0 60 02/07/92 VZ
Toluene EPA 602 ug/1 5.0 12 02/07/92 VZ
Ethylbenzene EPA 602 ug/1 5.0 30 02/07/92 VZ
Xylene, Total EPA 602 ug/l 10 60 02/07/92 VZ
signed

LAW AL
112TONWWDRK
IA30144-5599
40"21-3400
February 19, 1992
Lam Environmental, Inc.
LakePoint Office Park
333 Wilmont Road, Suite 300
Charlotte, NC 28217
Attention: Susan Fadero
Subject: Revised report of samples received n 01/31/92.
Dear Maw adr
Law Environmental National Laboratories has revisedits chemical
analysis of your samples and reports the results on the following
pages. These results relate only to the contents of the samples
submitted. This report shall not be reproduced except in full
without the approval Laws Environmental National Laboratories.
If there are any questions, please do not hesitate to onta t us.
sincerely,
LAW ENVIRONMENTAL L LABS
Clifford H. McBride
QC/Coordinator
i
Attachment: Data Report

LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Date 02/14/92
Page I
--- Project Information ---
Lab Number ; 92-1901-11
Project No. : 56-8555004 T20 Cust. No. :
Project Name : FURR PROPERTY
Manager: SUSAN FADERO
--- Sample Information ---
Station ID : MW-1 (DUPLICATE) Sampled Date/Time : 01/30/92 15:13
Matrix ; W Received Date/Time : 01/31192 11:40
Type : GRAB Received From/By : WAT/EEs
Collector : WAT Chain of Custody : 9630
Number of Containers : 3
Remarks :
--- Test Data ---
Parameter ..................... Method.... Units PQL ....... Results... Test Date Analy
-- GO ORGANIC ANALYSIS 'RESULTS
Methyl -tertiary -butyl ether (MTBE) EPA 602 Ug/l 5.0 480 02/08/92 VZ
Benzene EPA 602 ug/l 1.0 26 02/06/92 VZ
Toluene EPA 602 ug/l 1.0 3.0 02/06/92 VZ
Ethylbenzene EPA 602 ug/l 1.0 12 02/06/92 VZ
Xylene, Total EPA 602 ug/I 2.0 25 02/06/92 VZ
Signed

LAW ENVIRONMENTAL
IATION
LABORATORIES
"BEST DATA REPORT
Cate 2/1/2
Cage
---
Project
Information
---
Lab Number ,
2 1 01 1
Project No. :
56-8555004 T20
Cust. No.
Project Name
FURR PROPERTY
Manager:
"SUSA FAD Rt
--a
Sample
Information
---
Station I
1 (TRIPLICATE)
Sampled
Date/Tim
1/ / 2 15: 3
Matrix
Received
Date/Time
1/31/ 11:40
Typea
GRAB
Received From/By
AT/R
collector
WAS
Chain
of Custody
9630
Number of
Containers
3
Remy
--- "hest Data ---
Parameter ..........
....................
Method....
Units
P 1.......
Results.,.
Test Date
Analy
ORGANIC ANALYSIS
RESULTS --
Methyl-tertiary-butyl
ether { RS}
EPA 602
ug/1
5.0
37
/ 7/ 2
VZ
Benzene
EPA 602
g/l
1.0
25
02/06/92
VZ
Toluene
EPA 602
/l;
1.0
NO
02/06/92
VZ
Ethylbenzene
EPA 602
/l
1.0
12
2/ «/ 2
VZ
len , Total
EPA 602
a/1
2.0
25
2 / 2
VZ

LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA. REPORT
Data 02114,/92
Page
--- Project Information ---
Lab Number m 92-1901-13
Project No. : 6-8555004 T20
Project Name : FURR PROPERTY'
Manager: SUSAN FAD "NO
-_- Sample Information -- -
Oust. No. .
Station 10 , METHOD BLANK pled Date/Tim /
Matrix $ Received Date/Time- / /
Type Received From/By
Collector Chain of Custody 0
Number of containers 0
Remarks
"Teat Data
---
Parameter..... ..........,.............. Method.... Unit,
Test Date Analy
-- 00 ORGANIC ANALYSIS RESULTS
Oichlorodifluoror than EPA 601 ug/1 16 ND 02/05/92 V
Ohlor m than EPA 601 ug/1 0.80 ND 02/05/92 VZ
Vinyl Chloride EPA 601 ug/1 1.8 NO 02/05/92 V
Bromomethane EPA 601 ug/ l 12; N0 02/05/92 VZ
Ohloro than EPA. 601 Ug/1 5.2 ND 02/05/92 VZ
Trichl rof uor m than EPA 601 Ug/l 3.2. ND 02/05/92
1,1-illchloroath n EPA 601 ug/l 1.3 N0 02/05/92 V
Methylene Chloride EPA 601 ug/l 2..5 NO 02/05/92 VZ
trans-1,2-Dichloro than EPA 601 ug/l 1.0 NO 2/05/92 VZ
1,1 Oichl ro than EPA 601 ug/I 0.70 ND 02/05/92 VZ
Chloroform EPA 601 ug/l 0.50 N0 2/05/92 VZ
1,1.,1-Trtchlord thane EPA 601 Uq/1 0.30 N0 02/05/92 VZ
Carbon Tetrachloride EPA 601 ug/< 1.2 NO 02/05/92 VZ
1,2 ichl ro than EPA 601 ug/1 0.30 N0 02/05/92 Vz
Trichlorothna EPA 601 g/l; 1.2 N7 020592 VZ
1,2-Dichloropr ana EPA 601 ug/I 0.40N0 02/05/92 V
Bran dish orom than EPA 601 ug/I 1.0 N0 02/05/92 VZ
2-hl. ro th 1. i yl ether EPA 601 Ug/11.3 ND 02/05/92
cis-1,3-Dichloro ro n EPA 601 ug/l 3.4 ND 02/05/92 ti
trans-1, 3°-Oichloro ro n EPA 601 ug/l 3.4 N0 02/05/92 VZ
1,1,2-Trichlarnathan EPA 601 ug/1 0.20 NO 02/05/92 VZ
T trachlo o th na EPA 601 ug/1 0.30 ND 02/05/92 VZ
Oibrcmochlorom than EPA 601 ug/1, 0.90 N0 02/05/92 VZ
Ohlo°oh n an EPA 601 ug/l 1.0 ND 02/05/92 V
Bromoform EPA 601 ug/1 2.-0 ND 02/05/92 VZ
1,1,-2,2-Tatrachloroathan EPA 601 ug/l 0.30 N0 02/05/92 VZ
1,3-OichloroL n an EPA 601 ug/l 1.0 ND 02/05/92 VZ
1,4-Dichlarobenzene EPA 601 Ug/1 1.0 N0 02/05/92 VZ
Signed

LAW
ENVIRONMENTAL NATIONAL
LABORATORIES
"BEST DATA
REPORT;
Date /1 /92
Page
Lab Number :-1901-13
Project No. : 56-855500 I"20
--- Test
Data ---
Parameter te.-.....„................,......... Method....
Units
L.....-.
Results....
Test Date
Analy
- - GC ORGANIC N YS RESULTS --
1., -Dick .o enzen
EPA 601
auq/1
1.0
rite
02/05/92
V
methyl -tertiary -butyl ether (MTBE)
EPA 602
. /1
5.0
ND
02/05/92
VZ
Benzene
EPA 602
sag/l
1.0
ND
02/05/92
VZ
Toluene
EPA 602
/1
1..0
ND
02/05/92
V
Ethylbenzene
EPA 602
u9/1
1.0
ND
02/05/92
VZ
ylen , Total
EPA 602
ug/1
2.0
ND
02/05/92
VZ
Signed

LAW ENVIRONMENTAL ATIO LABORATORIES
TEST DATA REPORT
Date 02/1 /92
Page I
I Lab Number : 92-1901-1
Project No. : 56-8555004 T20
Project Name c 'FU R PROPERTY
Manager: SUSAN FAOERO
Station I0 ETli00 BLANK
Matrix : W
Type
collector
Remarks
Project. w
--_ Sample Information
---
Sampled Cate/'dime
Received Date/Time
Received From/By
Chain of custody0
Number of Containers 0
Test Data
---
Parameter ..................... ........ Method.... units P L....... Results... Test Date Analy
-- 00 ORGANIC ANALYSIS RESULTS
Dichldrod fl#unr meth ne EPA 601 ug/l 18 ND 02/06/92 VZ
hl rdmethane EPA 601 ug/l 0.80 ND 02/06/92 V
vinyl Chloride EPA 601 ug/l 1.6 RO02/06/92 VZ
Brcmomethane EPA 601 ug/1 12 ND 02/06/92 V8
hlor etha€e EPA 601; ug/l 5.2 ND 02/'06/92 VZ
Trichlorofluaromethane EPA 601 ug/l 3.2 ND 02/06/92 V
1,1-Dichl roethen EPA 601 ug/l 1>3 ND 02/06/92 V
Methylene chloride EPA 601 ua/1 2.5 R0 2/06/92 V
trans 1,2- ichl r ethen EPA. 601 ug/l 1.0 ND 02/06/92 Vz
1,1Oichlethane EPA 601 ug/l 0.0 M0 02/06/92 VZ
chloroform EPA 601: ug/l 0.50 ill. 02/06/92 VZ:
1,1,1-Trichloroethane EPA 601 ug/l 0.30 ND 02/06/92 VZ
Carbon Tetrachlorides EPA 601: ug/l 1.2 ND 02/06/92 VZ
1,2-Oichlorcet.h ne EPA 601 ug/l 0.30 ND 02/06/92 VZ
Trichloroethene EPA,. 601 ug/l 1.2 ND 02/06/92 VZ
1, 2-Dichloropropan EPA 601 ug/l 0.40 M0 02/06/92 VZ
Brom dichl arum thane EPA 601. ug/l 1.0 ND 02,/06/92 VZ
2-Ohl rceth l inyl ether EPA 601 ug/l 1.3 ND 02/06/92 VZ
cis-1,3-Dichloropropene SPA 601 ug/l 3.4 ND 02/06/92 VZ
trans l,3-Oichldr pr pen EPA 601 ug/l 3.4 ND 02/06/92 VZ
1,1,2-Trichlor ethan EPA 601 ug/l 0.20 ND 02/06/92 VZ
Tetrachloroethene EPA 601 ug/l 0.30 ND 02/06/92 VZ
Oibrcmochlor methane EPA 601 ug/1 0.90 ND 02,/06/"92 VZ
Ohlcrchen ene EPA, 601 ug/1 1.0 ND 02/06/92 VZ
Br m font EPA 601 ug/1 2.0 ND 02/06/92 VZ
1,1,2,2-'T t.rachl. rc h n EPA 601 ug/l 0.30 ND 02/06/92 BIZ
1,3-Dichl.oroben ene EPA 601 uqJ/1 1.0 ND 02/06/92 V
1, 4-Dtchlcrcten ene EPA 601 ug/1 1.0 ND 02/06/92 VZ
Signed 4��k 4't'-�d

LAW ENVIRONMENTAL NATIONAL LABORATORIES
TEST DATA REPORT
Date 2/14/92
Page 2,
Lab tTuMber : 92-19 1-14
Project No. ; S-S5SSCCi4 "T20
--- 'Teat Data --
-- CC ;ORGANIC ANALYSIS RESULTS -
1,2-Tilc lorob nzen
EPA
60
/l
1.
/06/ 2
VZ
Methyl -tertiary -butyl ether (MTBE)
TPA
602
°act/l
5.0
ND
02/ 6/92
VZ
BenzeneEPA
602
ug/1
1.0
TAT?
02/06/92
VZ
Toluene
EPA
60
ug/l
1.0
TAT)
2/06/ 2
V
Ethylbenzene
EPA
602
u /]
1.0
NTH
02/ 6/92
V
Xylene, Total
EPA
602
ug/1
2.0
ND
02/06/92
VZ
Signed _ia,6"t

LAW ENVIRONMENTAL NATIONAL LABORATORIES
'EST DATA REPORT
Date 02/14/9
Page l
--- Project Information -..-
Lab Number : 2-1901-1 ;
Project No. : 56-85550 4 T20
Cust. No.
Project [dame : PURR PROPERTY
Manager: SUSAN FACDERO
---
Sample Information ---
Station IB A METHOD BLANK
pled
Date/Time
Matrix i
Received
Date/Time
Type D
Received
From/By -;
Collector t
Chain
of Custody ;
Number of
Containers z
Remarks
Test
Data
Parameter...... ...> w...................
Method.....
Units
PQL....µ..
Results—
Test Date
Analy
-- GO ORGANIC ANALYSIS RESULTS
Dichlorodifluoromethane
EPA
601
ug/l
18
ND
02/07/92
Chlcromethane
EPA
601
Ug/1
0.80
ND
02/07/92V
Vinyl Chloride
EPA
601
u /l
1.8
ND
02/07/92
V"
Brom meth ne
EPA
601
a /l:
12
ND
02/07/92
V
hlordeth n
EPA
601
u /l
s-2
STD
02/07/92
V
Trichlorofluoromethane
EPA
601
Ug/l
3.2
ND
02/07/922
1, 1-CDichloroeth ne
EPA
601
u9/l
1.3
ND
02/07/92
VE
Methylene Chloride
EPA.
601
a/1
2.5
ND
/07/92
V2
trans-1, 2-Dichldreethene
EPA
601
ug/l
110
STD
02/07/92
V2
1, 1- ichloroet ne
EPA
601
a /l
0.70
PATS
02/07/92
V
Chloroform
EPA
601
Ug/l
6.50
ND
02/07/92
V
1,1,-Trichlcr ethane
EPA
601
u /l
0.30
3.6
2/07/92
V
Carbon Tetrachloride
EPA
601
u /1
1.2
ND
02/07/92
V
1,2-5Dichlorcethan
EPA
601
u /1
0.30
ND
2/07/92
V'
Tricklcroethene
EPA
601
/1
1.2
ED
02/07/92
V2
1,2-Dichl ropr ane
EPA
601
u /l
0.40
ND
2/07/92
V
Bromddichlorom thane
EPA
601
a /l
1.
02/07/92
'V
2-°Chlcroeth lvinyl ether
EPA
601
a /l
1#3
ND
02/07/92
V
cis-1,3®Bichlor pr pene'
EPA
601
ug/l
3.4
ND
2/07/92
VZ
trams-1,3-Dichloro r ene
EPA
661
a /l
3.4
ND
02/07/92
V
1,1,2-Trichlorcethane
EPA
601
u /l
0.20
ND
32/07/92
V
Tetrachlcroethene
EPA
601
u+ /1
0.30
ND
2/07/92
V"
Bibromochloromethane
EPA
601
a /l
0.90
ND
02/07/92
V
Chlcrobenzene
EPA
601
ug/l
1.0
ND
02/07/92
V
Bromofcrtat
EPA
601
u /l
2.0
ND
02/07/92
V
1,1, ,2-Tetrachlcrcethane
EPA
681
Ug/l
0.30
0.31
02/07/92
V
1,3-Bichlcro enzene
EPA
601
ug/1
1.0
MD
02/07/92
V2
1,4-Dichlorobenzene
EPA
601,
a /l
1.0
NO
02/07/92
V2
Signed

LAW
ENVIRONMENTAL NATIONAL
LABORATORIES
TEST DATA
REPORT
Date 02/14/92
Page 2
Lab Number c 92-1901-15
Project No. 56-8555004 T20
--- Test
Data ---
Parameter ..............................
Method....
Units
PQL .......
Results...
Test Date
Analy
-- GC ORGANIC ANALYSIS RESULTS --
1,2-Dichlorobenzene
EPA 601
ug/l
1.0
ND
02/07/92
VZ
Methyl -tertiary -butyl ether (MTBE)
EPA 602
ag/1
5.0
ND
02/07/92
VZ
Benzene
EPA 602
ug/l
1.0
ND
02/07/92
VZ
Toluene
EPA 602
ug/l
110
ND
02/07/92
VZ
Ethylbenzene
EPA 602
ug/l
1.0
ND
02/07/92
VZ
Xylene, Total
EPA 602
Ug/l
2.0
ND
02/07/92
VZ
Signed IW-41

Project
L b Sample ID -
Date
,analyzed-
COMMENTS.
� � .•r s
•
Chloride
56-8555004-T20 Project Name:
92-1901-12 Instrument l
2-5-92 Date Extracted:
Matrix:
Farr Property
Aq X Soil
ZIS

Law Environmental National Laboratories
Ater Matrix Spiker atria Spike Duplicate Recovery
ProjectName:
urr Property Project plumber: 56-8555004-T20
Lab Sample ID:
-158-01 Matrix: X
Soil
MS/MSD Data Apply" to the following samples:
92-1901-09
SPIKE SAMPLE MS Ms
0C
COMPOUND
ADDED
ONCE T TIN
CONCENTRATION
LIMITS
l q LI
t g/Ll
mg L
#
Chloride
30.0 6.28 34,7 95
-11
SPIV
COMPOUND
ADDED CONCENTRATION
LIMITS
(mg L) trng/LD REC #` RPD #
RPD ! REC.
Chloride
d.
-11
#
Column to be used to flag recovery and RPD values with an asterisk.,
Values outside of OC Limit
RP out of 1 outside limits
Spike Recovery , £1 - out of 2 outside limits
COMMENTS:

Project
Lab Sample 1
Date Analyzed?
Law EnvironmentalNational Laboratories
Method Blank Summary
Chemical Oxygen Demand
55-555 -T2 Project me:
92-1901-12 Instrument ID:
2-7-92 Date Extracted:
Matrix:
Purr Property
1

Law Environmental National Laboratories
Water Matrix Spike/Matrix SpIkDuplicate Recovery
Project e;: Furr Property Project Number:56-8555004-T20
Lab Sample ICE: -`i 1 - stria: Aq X Soil
Data ly to a following samples:
92-1901-09
SPIKESAMPLE Ms MS Oc
COMPOUND ADDED CONCENTRATION CONCENTRATION % LI i
coo 40.0 NO 9P78-125
PIKE
COMPOUND ADDED CONCENTRATION % % OC LIMITS
IFCOD 4001 7 �1
Column to be used to flag recovery and RPD values with an asterisk,
* Values outside of QC Limits
out of f _ outside limits
Spike Recovery: out of 2 outside limits
COMMENTS:
APPROVED Y: _.

Project
#-
Lab Sample ID:
Date Analyzed -
i EDITS.
Law
Environmental National Laboratories
Method Blank Summary
Turbidity
5-55FT2 Project arse:
92-1901-10 Instrument 1
1 -1-92 Date Extracted -
Matrix:
m
Farr Property
Sell

Law Environmental National Laboratories

Project
Lab Sample to -
Date
Analyzed-
COMMENTS:
Environmental National Laboratories
Method Blank Summary
Color
- -T 0 Project m Farr Property
92-1901-10 Instrument ID:
1-31-92 Date Extracte&
Matrix: Aq X
_ 1l

Law Environmental National Laboratories
Methodl
l Summary
TSS
I
Project #:
56-5655 -T 6
Project Name.
Farr Property
Lab Sample l
92-1901-10
Instrument ID:
Date Analyzed;
2-1-92
Date Extracted:
Matrix:;
Soil
lint
Ce
-Sample
Lai
ID
Sample ID
Industrial Wastewater
S -1 S -01
6
6
10
11
1
_1
1
1
_1
1

Law Environmental NationalLaboratories
TSS Duplicate Analyses Record
G
Project urr Prra Project 6-8555004-T20
Matrix: AQ X or
SOIL-
PL Iv l Al P
9_1 9-1 17 17,5 9.12.1-921
'.
=L4L
Range' = X, ® 2 Average' ,, + X, }
Relative percent difference'' --- (PF) = P n s x 100
Average
Do not Calculate If results are B L.
.JfV
APPROVED
4

Law Environmental National Laboratories
Water to Method Bleak Summary
Project game : Purr Property Project 66666 6 eT6
Lab Sample l -1 6 -1 atria: Aq X TCLP
Method Blank Date Apply to the following samples.
92-1901-09
RESULT"`
ELEMENT (` L)
1 -Aluminum
Antimony
Arai
Barium

Law Environmental National Laboratories
Water t l atria Spike/Matrix Spike Duplicate Recovery
Mile, VIM`
ow 1W
Project
568555004-TZO Project Name
Furr Property
Lab Sample l
92-1992- 1 Matrix:
Aq x 1
Units
ugll
M$JMSD,Data Apply to the following aamplee:,
9 3-19 1-09
SPIKE
SAMPLEMae
M�
CONTROL
ELEMENT T
ADDED
%Ms CONC.
%M80 RP ITEM
1
Aluminum
1
33 - 162
2
Antimony
12
45. 139
3
Arsenic
3
54 - 132
estrum
i
77 - 122
6
Beryllium
1
67 - 145
6
Cadmium
12
63 a 149
7
Chromium
3
54 - 13
8
Cobalt
1
9 112
9
Copper
1000
85 . 114
10
Iron
1
246 1274 13 1392
16 3 66.129
11
Lead
3+3
49' - 14
12
Manganese nese
1000
7 - 124
13
Mercury
5
57 - 1 9
14
Mickel
1000
62 - 1 95
15
Selenium
30
45 - 127
16
Silver
313
1
Thallium
3
33 - 127
19
Vanadium
1000
9 , 12
19Zinc
500
76-123,
VALUES OUTSIDE OF DO LIMITS
Recovery Outside of Control Limit
N Not Analyzed for Spike
Spike Diluted Out
Precision Outside of Control Limits

»>« Environmental »c::+*«i Laboratories
Gc ::;,»::. Met�hod t:»«< SUZZaty
54-0552004-1<O Project Name
92",190 <<» ±:<e <*
•..:
20:52 »c»»<«
Furr Prpper» 2
COMMENTS:/ \..... .. .. ... . :

Law Environmental ..w.
MethodGC volatile Blank
5 04-T2Project Name
1901 13 Lab File
2-5-92 Date c
12:08 Matrix
99
client
Sample -ID
-1 1 1
3
92-1901-02
3,
_
1 01 3
1
4
4
114
4
1 01.
3 1
1 1 7
1
10
11
1
13
14
1
COMMENTS:

#M R.. e. Lab Vile X:.:
client
SampleID
Sample ID
Analyzed
MW-4
-1 C1- 4
1:31
1 01 !
3 : 26
3
1 01
:1
-138
5
Matrix Spike 1
191121:18
Matrix Dup MW-1
111
:1
1'
1
12
14
C
APPROVED BY-. L� J�� J, ____

Law Environmental National Laboratories
GC Volatile
Method BlankAOM
vow
- -TProject
Lab Sample ID
92-1901-15
Lab File
Date Analyzed
2-7-92
Date Extracted;
Time Analyzed0.03
Matri
i
R
Lab
Time
client
Sample
ID
S M le ID
Analysed
Matrix
Spike 1
92 19 1-1
3
1
1

Law EnvircoMAUtal National Laboratories
Water GC Volatile Surrogate Summary Report
Project art
Project
9010
::
�►
92-19,01-04
92��1400.
nR
52 001�09
p..
q
LIMITSOC
seal ae
P 1 1e D(48-130)
Surrogate# Column to be used to flag recovery values
ute u
Values .dlimit
Volatiles: 0 out of 45 ; outside of QC limits
COMMENTS:

Law Environmental Laboratories
Water GC Volatile Surrogate Summary Report
Pro,j actrc r
Project - 5 04- 2
29
LAB
1 L 3 (ELCD) TOT
T
1
2 190 2
102 87 1.1.4
24
94 88 108
4
2
7
1
2
13
4
LIMITSOC
(FB) =
Fluorobenzene(PID) ( 2 1)
SMC2 ) =
ado-m+ hl than ) 2-1 22
) =
4 h r t 1.0E ) 4 -, )
column
to be usedto flag recovery
Surrogate poursd diluted out
Values outside of OC limits
olati
u ___1_2 outside of QC limits

USTODY RECORD
LAW ENVIRONMENTAL,
jW NATIONAL LABORATORY
1NPARK NAMEFACILITY: DRIVE � ��
EN ESA , GEORGIA 30144 INFORMATION
(404) 4 1- 4 6 NUMBER
STREET S _ _ -_ _ __
PROJECT NAME JOB NCL
7/;
dui
w
ca A+ SAPLE STATIONDESCRIPTION � � � . � Ca ` � L N L LAB NO,
zi
TIME sotm
a CODE
...
of
m
i, y
H I I SY* D 9�C! I TIME RE EBY: CATS I Tilk I HED .' � 1 t
A
A
DISTRIBUTION.* F31GI AL AND YELLOW COPIES ACCOMPANY SAMPLE SHIPMENT EhNT TO LABORATORY,
PINK COPY RETAINED BY SAMPLERS. YELLOW COPY RETAINED BY LABORATORY.; *SOURCE
REMARKSRECOVERY WELL - RW NRDES DISCHARGE - INNS
ell
Rem MONITORING WELL DRINKING WATER - D
SOIL / SEDIMENT HAZARDOUS WASTE - N-iW
SLN E - SL: SURFACE WATER SIN
WAOUE US Y NA