HomeMy WebLinkAboutBUSINESS PLAN 8/27/2004 (COPY)
{\\~J' ,~~ -4
.~.~ " Tanlmo/ogy
8501 N. MoPac Expressway, Suite 400
Austin, Texas 78759
Phone: (512) 451-6334
Fax: (512) 459-1459
Date Printed and Mailed: 09/08/2004
BAKERSFIELD FIRE DEPARTMENT
OFFICE OF ENVIRONMENTAL SERVICES
INSPECTOR STEVE UNDERWOOD
900 TRUXTUN AVE., STE. 210
BAKERSFIELD, CA. 93301
Test Date: 08/27/2004
Order Number: 3136161
Dear Regulator,
Enclosed are the results of recent testing performed at the following facility:
. CHEVRON 206561
3360 PANAMA LN.
BAKERSFIELD, CA. 93304
Testing performed:
Leak detector tests
Monitor Certification
Secondary Containment-Spill Container
Sincerely,
-:D~ k'~
Dawn Kohlmeyer
Manager, Field Reporting
ì
t~ DJnknology
CLIENT: CHEVRON U.S.A.
P.O. BOX 2292
145 S. STATE COLLEGE BLVD.
BREA, CA 92822-2292
SAM STEVENSON
(909)765-6536
TANKNOLOGY CERTIFICATE OF TESTING
8900 SHOAL CREEK, BUILDING 200 AUSTIN, TEXAS 78757
TELEPHONE (512) 451-6334 FAX (512) 459-1459
TEST RESULT SUMMARY REPORT
WORK ORDER NUMBER: 3136161
CUSTOMER PO:
SITE: CHEVRON 206561
3360 PANAMA LN.
BAKERSFIELD, CA 93304
PURPOSE: COMPLIANCE
TEST DATE: 08/27/04
MANAGER
(661 )396-7047
TEST TYPE: TLD-1
1
2
3
1 SUPREME
2 PLUS
3 UNLEADED
DW FIBERG
DW FIBERG
DW FIBERG
PRESSURE
PRESSURE
PRESSURE
y
y
y
1
2
3
1 FE PETRO
2 RED JACKET
3 FE PETRO
MLD
FX1V
MLD
BJ255 P
10401-8864 P
BJ2 5 6 P
For owner detailed report information, visit www.tanknology.com and select On-Line Reports-WRAP, or contact your local Tanknology office.
Tester Name: ALBERT J. QUEIROS
Technician Certification Number:91-1448
t1d//~
Printed 09/08/2004 09:43 SBOWERS
INDIVIDUAL TANK INFORMATION AND TEST RESULTS
r., Tånknology
8900 SHOAL CREEK, BUILDING 200
AUSTIN, TEXAS 78757 (512) 451-6334
. i
.;-
TEST DATE:08/27 104
CLIENT: CHEVRON U. S . A.
WORK ORDER NUMBER3136161
SITE:CHEVRON 206561
Tank lD: 1 1
Product: SUPREME
Capacity in gallons: 11,849
Diameter in inches: 120.00
length in inches: 245
Material: DW FIBERG
COMMENTS
Tank manifolded: NO
Vent manifolded: YES
Vapor recovery manifolded: YES
Overfill protection: YES
Overspill protection: YES
Installed: ATG
CP installed on: 1 1
¿l~~J1;II;flJØ1'~'I!~!11~t~(}ä~:V~2§.íé~¡
Start (in) End (in)
'X0~lLg~Ip,'~qìoR;!~~ì,ß~{ØIm "
Dipped Water level:
Dipped Product level:
Probe Water level:
Ingress Detected: Water
Test time:
Inclinometer reading:
VacuTect Test Type:
VacuTect Probe Entry Point:
Pressure Set Point:
Tank water level in inches:
Water table depth in inches:
Determined by (method):
Result:
COMMENTS
Bubble
Ullage
Make:
Model:
SIN:
Open time in see:
Holding psi:
Resiliency cc:
Test leak rate ml/m:
Metering psi:
Calib. leak in gph:
Results:
Bottom to top fill in inches:
Bottom to grade in inches:
Fill pipe length in inches:
Fill pipe diameter in inches:
Stage I vapor recovery:
Stage II vapor recovery:
168.5
176.0
45.0
4.0
DUAL
BALANCE
NOT
TESTED
COMMENTS
New/passed Failed/replaced New/passed Failed/replaced
L.D. #1 L.D. #1 L.D. #2 L.D. #2
FE PETRO
MLD
BJ255
9.00
28
240
189.0
10
3.00
PASS
NOT
TESTED
Material:
Diameter (in):
Length (ft):
Test psi:
Bleedback cc:
Test time (min):
Start time:
End time:
Final gph:
Result:
Pump type:
Pump make:
COMMENTS
DW FIBERG
2.0
175.0
NOT
TESTED
NOT
TESTED
PRESSURE
FE PETRO
NOT
TESTED
NOT
TESTED
Impact Valves Operational: YES
Printed 09/08/2004 09:43
INDIVIDUAL TANK INFORMATION AND TEST RESULTS
TrÞ Dlnknology
8900 SHOAL CREEK, BUILDING 200
AUSTIN, TEXAS 78757 (512) 451-6334
(.
TEST DATE:08/27 104
CLlENT:CHEVRON U. S .A.
WORK ORDER NUMBER3136161
SITE:CHEVRON 206561
Tank 10: 2 2
Product: PLUS
Capacity in gallons: 11,849
Diameter in inches: 120 . 00
Length in inches: 245
Material: DW FIBERG
COMMENTS
Tank manifolded: NO
Vent manifolded: YES
Vapor recovery manifolded: YES
Overfill protection: YES
Overspill protection: YES
Installed: ATG
CP installed on: 1 1
Bottom to top fill in inches:
Bottom to grade in inches:
Fill pipe length in inches:
Fill pipe diameter in inches:
Stage I vapor recovery:
Stage II vapor recovery:
172.0
176.0
49.0
4.0
DUAL
BALANCE
:!~t<J)'E~.'Í'i,RÞ~,í.!!i,.js+;t4'~~t"
Start (I n)
Dipped Water Level:
Dipped Product Level:
Probe Water Level:
Ingress Detected: Water
Test time:
Inclinometer reading:
VacuTect Test Type:
VacuTect Probe Entry Point:
Pressure Set Point:
Tank water level in inches:
Water table depth in inches:
Determined by (method):
Result:
COMMENTS
New/passed Failed/replaced New/passed Failed/replaced
L.D. #1 L.D. #1 L.D. #2 L.D. #2
Bubble
Ullage
Make:
Model:
SIN:
Open time in sec:
Holding psi:
Resiliency cc:
Test leak rate ml/m:
Metering psi:
Calib. leak in gph:
Results:
NOT
TESTED
RED JACKET
FXJ.V
10401-8864
4.00
32
200
J.89.0
J.5
3.00
PASS
NOT
TESTED
COMMENTS
Material:
Diameter (in):
Length (ft):
Test psi:
Bleedback cc:
Test time (min):
Start time:
End time:
Final gph:
Result:
Pump type:
Pump make:
COMMENTS
DW FIBERG
2.0
175.0
NOT
TESTED
NOT
TESTED
NOT
TESTED
NOT
TESTED
PRESSURE
FE PETRO
Impact Valves Operational: YES
Printed 09/08/2004 09:43
.. .
INDIVIDUAL TANK INFORMATION AND TEST RESULTS
~~ Dlnknology
8900 SHOAL CREEK, BUILDING 200
AUSTIN, TEXAS 78757 (512) 451-6334
TEST DATE:08/27 /04
CLIENT: CHEVRON U. S . A.
Tank ID: 3 3
Product: UNLEADED
Capacity in gallons: 11,849
Diameter in inches: 120.00
length in inches: 245
Material: DW FIBERG
COMMENTS
Jl~('~iQRM~'11IÐ~
Tank manifolded: NO
Vent manifolded: YES
Vapor recovery manifolded: YES
Overfill protection: YES
Overspill protection: YES
Installed: ATG
CP installed on: / /
Dipped Water level:
Dipped Product level:
Probe Water level:
Ingress Detected: Water
Test time:
Inclinometer reading:
VacuTect Test Type:
VacuTect Probe Entry Point:
Pressure Set Point:
Tank water level in inches:
Water table depth in inches:
Determined by (method):
Result:
COMMENTS
Bubble
Make:
Model:
SIN:
Open time in see:
Holding psi:
Resiliency cc:
Test leak rate mllm:
Metering psi:
Calib. leak in gph:
Results:
WORK ORDER NUMBER3136161
SITE:CHEVRON 206561
Bottom to top fill in inches:
Bottom to grade in inches:
Fill pipe length in inches:
Fill pipe diameter in inches:
Stage I vapor recovery:
Stage II vapor recovery:
176.0
182.0
52.0
4.0
DUAL
BALANCE
Ullage
NOT
TESTED
COMMENTS
:!e"ª$riEsØì..~~....~
New/passed Failed/replaced New/passed Failed/replaced
L.D. #1 L.D. #1 L.D. #2 L.D. #2
FE PETRO
MLD
BJ3S6
8.00
30
240
189.0
10
3.00
PASS
NOT
TESTED
Material:
Diameter (in):
length (ft):
Test psi:
Bleedback cc:
Test time (min):
Start time:
End time:
Final gph:
Result:
Pump type:
Pump make:
COMMENTS
DW FIBERG
2.0
1'15.0
NOT
TESTED
NOT
TESTED
PRESSURE
FE PETRO
NOT
TESTED
NOT
TESTED
Impact Valves Operational: YES
Printed 09/08/2004 09:43
MONITORING SYSTEM CERTIFICATION
For Use By All Jurisdictions Within the State of California
Authority Cited: Chapter 6. 7, Health and Safety Code; Chapter 16, Division 3 Title 23, California Code of Regulations
This form must be used to document testing and servicing of monitoring equipment. If more than one monitoring system control panel is installed at the facility, a separate
certification or report must be prepared for each monitorinQ system control panel by the technician who performs the worle A copy of this form must be provided to the tank
system owner/operator. The owner/operator must submit a copy of this form to the local agency regulating UST systems within 30 days of test date.
A. General Information
Facility Name: CHEVRON 206561
Site Address: 3360 PANAMA LN.
City: BAKERSFIELD
Contact Phone No: 396-7047
Date of Testing/Service: 08/27/2004
CA
Zip: 93304
Facility Contact Person: MANAGER
Make/Model of Monitoring System:VEEDEROOTTLS350 Work Order Number: 3136161
B. Inventory of Equipment Tested/Certified
Check the appropriate boxes to indicate specific equipment inspected/serviced
Tank lD: 1-91 Tank ID: 2-89
X In-Tank Gauging Probe. Model: MAG-2 X In-Tank Gauging Probe, Model: MAG-2
= 409 Ixl Annular Space or Vault Sensor,
X Annular Space or Vault Sensor. Model: Model: 409
== 352 .-
X Piping SumpfTrench Sensor(s). Model: ~ Piping SumpfTrench Sensor(s). Model: 352
= Fill Sump Sensor(s). 352
X Model: 1'1{ Fill Sump Sensor(s). Model: 352
:=::
X Mechanical Line Leak Detector. Model: MLD Ix Mechanical Line Leak Detector. Model: FX1V
= Electronic Line Leak Detector. Model: ;;;;;:
Electronic Line Leak Detector, Model:
X Tank Overfill/High-Level Sensor, Model: MAG-2 ex Tank Overfill/High-Level Sensor. Model: MAG-2
= Other (specify equipment type and model in Section E on page 2), Other (specify equipment type and model in Section E on page 2).
'-
Tank ID: :1-11f TanklD:
:RJ In-Tank Gauging Probe. Model: MAG-2 r- In-Tank Gauging Probe. Model:
X Annular Space or Vault Sensor, Model: 409 Annular Space or Vault Sensor. Model:
X Piping SumpfTrench Sensor(s). Model: 352 Piping SumpfTrench Sensor(s). Model:
X Fill Sump Sensor(s), Model: 352 Fill Sump Sensor(s). Model:
x= Mechanical Line Leak Detector. Model: MLD .- Mechanical Line Leak Detector. Model:
= Electronic Line Leak Detector. Model: .-
= Electronic Line Leak Detector. Model:
X Tank Overfill/High-Level Sensor. Model: MAG-2 Tank Overfill/High-Level Sensor, Model:
=
Other (specify equipment type and model in Section E on page 2). r- Other (specify equipment type and model in Section E on page 2).
- '-
ulspenser IU: 1/2 Dispenser ID: 3/4
~ Dispenser Containment Sensor(s) Model: 322 !xl Dispenser Containment Sensor(s) Model: 322
Œ] Shear Valve(s). ŒJ Shear Valve(s)
D Dispenser Containment Float(s) and Chain(s). n Dispenser Containment Float(s) and Chain(s),
Dispenser ID: 5/6 Dispenser ID: 7/8
ŒJ Dispenser Containment Sensor(sJ Model: 322 rxJ Dispenser Containment Sensor(s). Model: 322
o ShearValve(s). ~ Shear Valve(s).
n Dispenser Containment Float(s) and Chain(s). D Dispenser Containment Float(s) and Chain(s).
Dispenser ID: Dispenser ID:
D Dispenser Containment Sensor(s) Model: o Dispenser Containment Sensor(s), Model:
D Shear Valve(s). o Shear Valve(s).
D Dispenser Containment Float(s) and Chain(s), o Dispenser Containment Float(s) and Chain(s),
. If the facility contains more tanks or dispensers, copy this form. Include information for every tank and dispenser at the facility.
C. Certification
I certify that the equipment identified in this document was inspected/serviced in accordance with the manufacturers' guidelines.
Attached to this certification is information (e.g manufacturers' checklists) necessary to verify that this information is correct.
and a Site Plan showing the layout of monitoring equipment. For any equipment capable of generating such reports, I have also attached
a copy of the (Check all that apply): [l System set-up ~ Alarm history report
tW/rt--
Technician Name (print): ALBERT J. QUEIROS
Certification No.: 000-00-2808
Signature:
License. No.:
Testing Company Name: Tanknology
Site Address: 8900 Shoal Creek, Bldg. 200 Austin, TX 78757
Phone No.: (800) 800-4633
Date of Testing/Servicing: 08/27/2004
Monitoring System Certification
Page 1 of 3
Based on CA form dated 03/01
Monitoring System Certification
~
Site Address: 3360 PANAMA LN.
Date of Testing/Service: 08/27/2004
D. Results of Testing/Servicing
Software Version Installed: 112.02
Complete the following checklist:
o Yes DNo· Is the audible alarm operational?
o Yes DNo· Is the visual alarm operational?
o Yes DNo· Were all sensors visually inspected, functionally tested, and confirmed operational?
o Yes DNo' Were all sensors installed at lowest point of secondary containment and positioned so that other equipment will not
interfere with their proper operation?
o Yes nNO· nN/A If alarms are relayed to a remote monitoring station, is all communications equipment (e.g. modem) operational?
o Yes DNo· DN/A For pressurized piping systems, does the turbine automatically shut down if the piping secondary containment
monitoring system detects a leak, fails to operate, or is electrically disconnected? If yes: which sensors initiate positive
shut-down? (check all that apply) ŒJ SumpfTrench Sensors; ŒJ Dispenser Containment Sensors.
Did you confirm positive shut-down due to leaks and sensor failure/disconnection? ŒJ Yes DNo
o Yes DNo· DNJA For tank systems that utilize the monitoring system as the primary tank overfill warning device (i.e.: no mechanical
overfill prevention valve is installed), is the overfill warning alarm visible and audible at the tank fill points(s) and operating
properly? If so, at what percent of tank capacity does the alarm trigger? 95 %
DYes· 0NO Was any monitoring equipment replaced? If yes, identify specific sensors, probes, or other equipment replaced and list the
manufacturer name and model for all replacement parts in Section E, below.
DYes' 0NO Was liquid found inside any secondary containment systems designed as dry systems? (check all that apply) D Product;
D Water. If yes, describe causes in Section E, below.
o Yes DNo· Was monitoring system set-up reviewed to ensure proper settings? Attach set-up reports, if applicable.
o Yes DNo· Is all monitoring equipment operational per manufacturers' specifications?
. In Section E below, describe how and when these deficiences were or will be corrected.
E. Comments:
Page 2 of 3
Based on CA form dated 03/01
Monitoring System Certification
Site Address: 3360 PANAMA LN.
Date of Testing/Service: 08/27/2004
F. In-Tank Gauging I SIR Equipment
o Check this box if tank gauging is used only for inventory control.
o Check this box if no tank gauging or SIR equipment is installed.
This section must be completed if in-tank gauging equipment is used to perform leak detection monitoring.
Complete the following checklist:
0ves DNo' Has all input wiring been inspected for proper entry and termination, including testing for ground faults?
0ves DNo' Were all tank gauging probes visually inspected for damage and residue buildup?
o Yes DNo' Was accuracy of system product level readings tested?
0ves DNo' Was accuracy of system water level readings tested?
[5<] Yes DNo' Were all probes reinstalled properly?
0ves DNo' Were all items on the equipment manufacturers' maintenance checklist completed?
* In the Section H, below, describe how and when these deficiencies were or will be corrected.
G. Line leak Detectors (llD) :
D Check this box if LLDs are not installed.
Complete the following checklist:
0ves ONO' ONtA For equipment start-up or annual equipment certification, was a leak simulated to verify LLD performance?
(Check all that apply) Simulated leak rate: 0 3 g.p,h 0 0.1 g.p.h 00.2 g.p.h
Œ]Ves ONo' Were all LLDs confirmed operational and accurate within regulatory requirements?
Œ]ves ONO' Was the testing apparatus properly calibrated?
Œ]Ves ONO' ONtA For mechanical LLDs, does the LLD restrict product flow if it detects a leak?
DVes ONo' 0NtA For electronic LLDs, does the turbine automatically shut off if the LLD detects a leak?
Dves ONo' 0NtA For electronic LLDs, does the turbine automatically shut off if any portion of the monitoring system is disabled or disconnected?
DVes ONo' 0NtA For electronic LLDs, does the turbine automatically shut off if any portion of the monitoring system malfunctions or fails a test?
DYes ONO' Œ]NtA For electronic LLDs, have all accessible wiring connections been visually inspected?
ŒJves ONo' Were all items on the equipment manufacturers' maintenance checklist completed?
* In the Section H, below, describe how and when these deficiencies were or will be corrected.
H. Comments:
Page 3 of 3
Based on CA form dated 03/01
;::
58-989 SECONDARY CONTAINMENT SUMMARY RESULTS
1"", Tanknology
TEST DATE:08/27 /2004
BREA
SAM STEVENSON
909-765-6536
CA
92822
WORK ORDER NO.: 3136161
SITE: CHEVRON 206561
3360 PANAMA LN.
BAKERSFIELD CA 93304
CLIENT: CHEVRON U.S.A.
P.O. BOX 2292
145 S. STATE COLLEGE BLVD.
Tank Interstital Tests
Piping Interstital Tests
1
2
3
OPW
OPW
OPW
Pass
Fail
Pass
Tanknology representative: JERRY BELLOLl
Services conducted by: ALBER7 J. QUEIROS
~
æt/J~
:t. TánknoIogy Test Date: 08/27/2004
Work Order: 3136161
SECONDARY CONTAINMENT TEST RESULTS
SUMP TESTS
Type Tank or Disp Manufacturer Model or Diam,/Widthllength Depth Test Method Start Initial level Finish Final Pass/
# Material (") (") Time level Change Time Result Fail
Spill Container 1 OPW Plastic 12" 5 GAL 10:50 8" FROM NONE 11:20 8" FROM Pass
Spill Container 2 OPW Plastic 12" 5 GAL 10:50 8" FROM 7" 11:20 1"FROM Fail
Spill Container 3 OPW Plastic 12" 5 GAL 10:50 8" FROM NONE 11:20 8" FROM Pass
/
I
I
Comments: SUSPECT PLUS BUCKET IS NOT TIGHT WHERE PLASTIC FLEX, BOLTS TO BOTTOM PLASTIC DISH.
!
I
0::.
.-
TEST DATE: 08/27/04
CLIENT: CHEVRON U. S . A.
SITE DIAGRAM
-~ Tånknology
8900 SHOAL CREEK, BUILDING 200
AUSTIN, TEXAS 78757
(512) 451-6334
FAX (512) 459-1459
WORK ORDER NUMBER3136161
SITE: CHEVRON 206561
o::D VENTS
§ § § (c::;) c::;) )
PLU UL SUP
S
~ ~ ~ ( )
CD CD CD c::;) c::;)
E
N<ts CHEVRON
#206561
Printed 09/08/2004 09:43 SBOWERS
¡.
Work Order:
31.361.61.
CHEvRO" USA CSI-la4~
3360 PANAMA lANE
ÐAKERSl"IEL.P CA. 93304
SS-20&5IPH-396-7047
AUG 27. 2004 0:02 AM
SVSTÐ'I STATue 1lEPæJ'
- - - - - - -- - - - - -
ALL FUNCTIONS i'tG~"
----- SENSOR ALARM -----
L 3: 92-5TP SlI"\P
8TP 9LtIP
J.IQUID WARN I I«;
AOO 27. 2004 9:54 N1
----- SENSOR AlARM -----.
L 3:92-m'P BLtIP .."
8TP SI.J'IP
L I QU I Ð I.Lì\RIIIl NG
RUG 27. 2004 8:54 AM
----- SENSOR ~ -----
L 1: 92-ANNULAR
ANNIJl.AR SPACE
FUEL ~
AUG 27. 2004 8:56 m
----- sœHSOR ~ -----
L 2:92-FI[l. SLt1P
PIPIt«; SlttP
HIGH LIQU1D ALARM
AUG 27. 2D04 8;59 N1
----- SENSOR ALARM -----
L 2:92-FILL SUMP
PIPI ~ SlJ'1P
HIGH LIGUID ALARM
AUG 27. 2004 8:59 AM
----- SENSOR ALARM -----
L 2:92-FIlJ.. SlJ1P
PIPI NG SlJ1P
HIGH LIQUID AI.F\RM
AUG 21. 2004 a:59 AM
----- DENSOR ALARM -----
L 2:9;?-f'ILL SlJt1Þ
P I.Þ I tK: Blt1l'
LIQUID IoW!Nr~
A~ 27. :~004 . 9:00 P.H
,----- SENSOr;! AlARM -----
L 2:92-FILL SUMP
PIPING Slt1P
HIGH LIQUID ALARM
. AlJG 27. 2004 9:00 N1
----- SENSOR Al.AAt1
L ?:B7-ANNUL.AR
ANNl.Il.AR SPI-ICE
FUEl. ALAAM
1\00 27. 2004 9: 01 N1
----- SENSOR AlARI'I ----
L 8:B7-FILL SlI1P
PIPlOO SLtIP
HIGH LIQUID ALARM
Aue 27. '~004 9:02 AM
-
I
L----- SENSO~ ALARM -----
8:f37-FILL 5L11P
PIPING SlNP
LIQUID WARNI~
AUG 27. 2004 9:03 AM
----- S£~R ALARM -----
L e:87-FILL SUMP
PIPING SlJ1P
HIGH LIQUID ALARM
AUG 27. 2004 9: 03 ÞI1
---- IN-TANK ALARM ---__
T I :SlIPREI'If.:
PROBE OUT
AUG 27. 2004 9:04 ~
---- IN-TANK ALARM ----_
T J :SUPREHE'
I NVALID FUEL LEVEL
AUG 27. 20D4 9:04 AM
- ---- SEttiOR AlAI\'M
L 4:eg-ANNULAR ---~.
ANHULAR SPACE
FUEL AtARt1
AUG 2.. 2004 9:08 AM
----- SENSOR ALARM -----.
L 5:89-FILL SUMP
PIPI~ SlJ1P
HIGH LIQUID ALARM
AUG 27. 2004 ~:10 AM
Tanknology-NDE 8900 Shoal Creek, Building 200 Austin, Texas 78757
Work Order:
3136161
þ:l
----- SENSOR ALARM -----
. L 5: a9-FU-L 8\W
1'1 P HG BltIP
LIQUID IoIARNING
AUG 27. 2004 ~:10 AM
----- SGNSOR ALARM -----
L 5:89~FJLL SLt1P
PIPIOO SLI1P
HIGH LIQUID ALARM
AUG 27. 2004 9:10 AM
."
IN-TANK ALARM -----
T 3: UNLEADED
PTtOBE our
AUG 27. 2004 9:l4 AM
. ---~ IN-TAHI( ALARM -~--
T 2:PLlB '
DELIVER't l E£DEÐ
AUG 27. 2004 9:15 AM
---- IN-TANK ALARM -----
.1 2:PLlJS
LOU PRODUCT ALMt1
,AUO'2? 2004 9:15 AM
'."
---- I~-TANK ALARM -----
T 2:PLUS
I NVAL I D FUEL LEVEL
AUO 27. 2004 9:15 AM
.:-::-_lrof-TAÑK ALMI1 -----
---- IN-TANK ~ -----
T :3: UNLEADED
, HIGH WAtER ALARM
AUG 27. 2004 9:19 AM
---- I~-TANK ALARM -----
T I :SUPRFJ1E
HIGH WATER WARNHIG
AUG 27. 2004 ~:25 AM
IN-TANK ALARM -----
T ;): UNLf'ADED
HIGH WATER WARNING
AUG 27. 2004 9:18 AM
---- IN-TANK ALARM -----
T 2:PLUS .
HIGH WATER ALARM
AUG 27. 2004 9:25. AM
---- IN-TANK ALARM -----
T :3: UNLFADED
HIGH .PRODUCT ALAJm
AUG 27. 2004 9:19 AM
---- IN-TANK ALARM -----
T 2:PLlB
HIGH ~T£R IrI'iRNl NG
AUG 27. 2004 9:25 AM
T I :SUPRÐ1E
J NVENTORV ] NC'RE'ASE
J I«:REASE: START
AUG 27. 20D4 9:04 AM
VOLlI'1E .. 188J GAlS
WATER = 0.00 f NCHES'
TEMP ~ 86.2 DEG F
---- IN-TAN!( ALARM -0----
T 1 :SUPREME
HIGH PRODOOT ALARM
AUG 21. 2004 9:31 AM
1~ END
AUG 27. 2004 9:;?2 ~
VOLU1E .. 10025 GALS
WATER = 8.16 I~HES
Tf.11P .. 86.1 DEe F
1" 3: UNLFADED
I NVENTOR'r' I tcREASE
I NCREASE START
AuG 21. 2004 ~:J9 AM
VOLUME . 9978 GALS
WATER .. 6.15 ItcHES
TÐ1J> .. 85.8 DEG F
GROOS J NORF.AS£- 81 44
TO NET I NCREASE- 7995
I NCREAaF. EIIII>
AUG 27. 2004 9:39 AM
---- IN-TANK ALARM -----
T 1: SUPRf.1'If:
tUGH ~TER Al.AÐ1
AUG 27. 2004 9:25 AM
VOLlJ'IE
~TER
TI?11P
.. 10907 GALS
.. 0.00 INCHES
II< 91.6 DEG F
GROSS INCREASE- 929
TC NET {NcREA9E- a9B
Tanknology-NDE 8900 Shoal Creek, Building 200 Austin, Texas 78757
"
Work Order:
31.361.61.
,
:5>
T 1: SUPIID1E
I NVENT~ INCREASE
I ~E START
AUG 27. 20Q4 9:26 AM
VOLUME ~ 10025 GALS
WATER .. 8. 16 I NCIiES
tEMP .. 78.9 PEG F
1 NCREASt; END
AUG 27. 2004 9:51 AM
VOUJ1E - 10a04 GALs
ItM:\TER .. 0.00 INCHæ
TEMP . 80.6 DEG F
GROss I NCRF.ASEz 779
TO 'NET INCREASE= 755
T 3: UHLEADEO
I NVENTOR"l INCREASE
I NCREAS£ START
AUG 27. 2004 ~:52 AM
VOLlJ'Π.. 8R51 GAJ..B
WATER .. 0.00 I NCHEB
TEMP .. 91·.7·DEG F
1 f"£.RE'AaE END
AUG 27. 2004 I Q : 09 AM
VOLlI'1E .. 9203 GALS
WATER · O.DO INCHES
TÐ1P .. 91.9 DEQ F
GROSa t ICRFASE~ 352
TC NET I NCRFASE- 343
--' . ' ~ml'SOR ALARM ----..
L b:~':I-nTP SUMP,
srI' SlI1l'
LIidUl D Wr=INNI NC
AUG 27. 2004 10:23 AM
T 2:PLUS
¡ I'NENTORY [NCREASE
I NCREASE START
AUG 27. 2004 10:07 ~
VOLltΠ"7992 GALS
WATER .. 0.00 I tt:JHES
'1'EI'IP .. 93. I DEG F
I ~REASE ENP
At.(; 27, 2004 10:23 AM
VOLlt1E .. 9536 GAIß
WATER '" 0.00 I NCHæ
TEMP .. 92.8 DEG F
GROSS ItcREASE.. 1544
. TC NET 11'CREASE~ 1509
----- SENSOR ~LA~ -----
1. 6:89-£11> SLMP
8TP SLtIP
LIQUI D WARN I NO
AUG 27. 2004 10:23 AM
---- IN-TANK ALARM -----
T 1 :SUPREME
HIGH PRODLCT ALARM
AUG 27. 2004 10:34 AM
IN-TANK ALARM -----
T 2:PLLB
HIGH PRODOCT AI..AAJ1
AUG 27. 2004 10:40 AM
---- IN-TANK ALARM -----
T 2:~LlJS
OVERFI1.I. ALAJ1M
AUG 27. 2004 10:40 AM
---- IN-TANK ALARM -----
T 1 :SUP'RÐ-IE
OVERF I 1.1. AUlRM
AUG 27. 2004 10:40 AM
---- I N-TANK ALA~ -----
T 3:U~LEADED
HU;;H PRODUCT ALARM .
AUG 27, 2004 10:40 AM
---- IN-TANK ALARH ----
T 3: UNLEADED
OVERPIU. ALARM
AUG 27. 2004 10:41 AM
---- IN-TANK ALARM -----
T 2:PLUB
DELIVER'{ IEEÐED
AOG ~7. 2004 10:44 AM
---- IN-TANK ALARM -----
T 1 :SUPRÐ1E
DELIVERY NEE1)£D
AUG 27. 2004 10:44 AM
Tanknology-NDE 8900 Shoal Creek, Building 200 Austin, Texas 78757
.1'
Work Order:
3136161
..'
----- SENSOR ALARM -----
LI0:D1SÞENBER PAN 1-2
DISPENSER PAN
HIGH LIQUlb ~
AUG 27. 2004 10:46 AM
---- 1 N-TANK ALARI'I ----
T 1 :SUPRÐ1E
LOW PRODUC1' ALMM
AUG 21. 2004 10:49 AM
, .
IN-TANK ALAR1 ----
T 2 ~PLlB
LOW PRODœT AlJW1
Ate 27. 2004 10:49 AM
1 N-TANK AU\RI'1 -----
T : ;) : UNl..EADED
DELIVER'/ NEEDED
AUG 27. 2004 10:49 AM
T 2:PLUB
1 N\1E~R\I 1 HCREASE
I NCREA8E START
Ale 27. 2004 10: 26 AM
VOLlJ'IE . 9536 GAlß
~TER . 0.00 I NCHEB
TEMP . 93.7 DEG F
I t«::R£ASE END
AUG 'J.'l. 2OiJ4 1 0: 56 AM
VOt.tI'IE .. 11706 GAUl
~TER .~ 0.00 INCHES
TEMP . 94.2 DEe F
CROSS INCRPASE- 2170
1'0 NET I~" 2115
T 1: SUPREME
11'NEKrOJl'J I NCREAaE
J t£REASE START
AUG 27. 2004 10:26 AM
VOLlJ'IE - t 0144 CAtS
WATER EO. 00 I NCHæ
TÐ1P .. 79.9 DEG F
I~ END
AUG 27. 2004 10:56 AM
VOLlJ'IE m 11834 GALS
~ .. C.OD I~Hæ
TÐ1P .. 81.8 DEe F
GROSS INCREA9E" 1690
TC I'ŒT I NCR£A8E.. 1651
T 3:UNLEADED
J """EffTO~ ¡ ~REASE
l~ 5fART
AUG 27. 2004 10:40 AM
VOLlJ'IE - ~203 GALS
I..¥rrER .. D . DO 1 NCHES
TEI1J> ~ 95 . 2 DEe F
I NCREASE END
AUG 21. 2004 10:57 AM
VOLlJ'IE .. 1141 4 GALS
~TER .. 0.[1[1 INCHES
TÐ1P = 95.2 DEG F
GROSS I!'CREASE- 2211
TC NET 1 t«::REASE- 2156
---- IN-TANK ALARM -----
T 3:UNJ.EADEI)
LOIoI PRODUCT ALARM
AUG 27. 2004 10:57 AM
---- IN-TANK ALARM -----
T 2:PLLB
PROBE OI1f
AUG 27. 2004 10:51 AM
IN-TANK AIJ\J\'I'I -----
T 2:PLL18
LOW TÐ1P bM\RNJ tÐ
AUG 27. 2004 10:58 AM
----- SENSOR ALARM -----
L 5:a9-FILL SUMP
PIPING SLt1P
SENSOR OUT Al.ARN
AUG 27. 2004 10:59 AM
---- IN-TANK ALARM -----
T I :SUPREI'IE
PROBE OUT
AUO 27# 2004 10:59 AM
---- IN-TANK ALARM -----
T t :SUPREME
J N\IAL I D FUEL 1..E\I£1.
AUG 27. 2004 11:00 AM
----- SENSOR ALARM -----
L 2:92-FILL SUMP
PIPII'«'ò SlI"IP
HIGH LIQUID ALARM
AUG 27. 2004 11:00 AM
cr
Tanknology-NDE 8900 Shoal Creek, Building 200 Austin, Texas 78757
~ 1 ,"'
Work Order:
3:1.36J.6J.
L-279~~~RS~ -----
PIPING SltlP
SENSOR OUT AtARt1
AUG 27. 2004 11:00 AM
---- rN~TANK ALARM ----_
T :3: UNLFAtÆb
PROSE our
AUG 27. 2004 11:05 AM
. ----- S£I't3OR AI.ARt1 -----
L 8:S7-FILL SUMP
PIPIOO SlJ1P
SEI'SOR our A1ARI1
AOO 27, 2004 11 i 07 f¥'I
T 2:PLUS·
[NVENTOR'l' J t«;~
I NCREASE START
AUG 27. 2004 10:57 AM
WLlI'IE ... 707 GALS
~TER .. D.DO l~HEB
TÐ1P .. 97.7 DEG F
INCREASE END
AUG 2~. 2004 11:16 AM
WLI.tI£ ... 3861 GALS
WATER = 0.00 I I'CHES
TB1P s 91.8 DEG F
GROSS r ICJήE- :3154
TC tŒT I~· 3096
?
T I :SUPRE11E
I NV£NTORY t NCREASE
1/'CREAsE fn"ART
AUG 27. 2004 10:59 AM
VOLl.tIë s 633 GALS
~ .. IJ,ßß IOC~
ICIV '" 92.3 DBG F
I NCREAsE Elm
AUG 27. 2Q04 11:16 AM
VOLlME ~ 2714 GALS
ItM\TER ~ 0.00 lOOHEB
TEMP . B2.9 DEG F
CROss INCREASE'" 2081
TC NET I t£RF.ASE.. 204'1
CHEVRON USA CSI-1849
3360 PANAMA U\NE
BAKERSFIELD CA.93304
SS-2065JPH-396-7D47
AUG 27. 2004 11:29 AM
SVSTEJoI STATLS REPORT
- - - - - - - - - - - -
ALL FUJllCTIONS NORI'1Al.
Tanknology-NDE 8900 Shoal Creek, Building 200 Austin, Texas 78757