HomeMy WebLinkAboutFMC 2008 _ MONITORING SYSTEM CERTIFICATION
For Use By All Jurisdictions Within the State of California \0
Authority Cited: Chapter 6.7, Health and Safety Code; Chapter 16, Division 3, Title 23, California Code of Regulations 8�
This form must be used to document testing and servicing of monitoring equipment. A separate certification or report must be prepared for each �\
monitoring system control panel by the technician who performs the work. 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 IIIIIIIIIIIIIIIIIIII 47
Facility Name: ARCO AM/PM IE Bldg.No.:
Site Address: 900 MONTEREY ST. City: BAKERSFIELD Zip: 93305
Facility Contact Person: ALONDRA Contact Phone No.: (661) 835-8044
Make/Model of Monitoring System: VR-TLS-350 Date of Testing/Servicing: 10/15/2008
B. Inventory of Equipment Tested/Certified
Check the a ro riate boxes to indicates iiic ui ment ins ted/serviced:
Tank ID: T-1 87 SYPHON Tank ID: T-2 87 MAIN TANK
®In-Tank Gauging Probe. Model: 847390-109 ®In-Tank Gauging Probe. Model: 847390-109
®Annular Space or Vault Sensor. Model: 794390-407 ®Annular Space or Vault Sensor. Model: 794390-407
®Piping Sump/Trench Sensor(s). Model: 794380-208 ®Piping Sump/Trench Sensor(s). Model: 794380-208
�I' Fill Sump Sensor(s). Model: 794380-208 Fill Sump Sensor(s). Model: 794380-208
❑Mechanical Line Leak Detector. Model: ❑Mechanical Line Leak Detector. Model:
®Electronic Line Leak Detector. Model: ®Electronic Line Leak Detector. Model:
®Tank Overfill/High-Level Sensor. Model: ®Tank Overfill/High-Level Sensor. Model:
❑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: T-3 91 Tank ID:
®In-Tank Gauging Probe. Model: 847390-109 ❑In-Tank Gauging Probe. Model:
®Annular Space or Vault Sensor. Model: 794390-407 ❑Annular Space or Vault Sensor. Model:
®Piping Sump/Trench Sensor(s). Model: 794380.208 ❑Piping Sump/Trench Sensor(s). Model:
®Fill Sump Sensor(s). Model: 794390-208 ❑Fill Sump Sensor(s). Model:
❑Mechanical Line Leak Detector. Model: ❑Mechanical Line Leak Detector. Model:
®Electronic Line Leak Detector. Model: ❑Electronic Line Leak Detector. Model:
®Tank Overfill/High-Level Sensor. Model: ❑Tank Overfill/High-Level Sensor. Model:
❑Other(specify equipment type and model in Section E on Page 2). ❑Other(specify equipment type and model in Section E on Page 2).
Dispenser ID: 1-2 Dispenser ID: 3-4
®Dispenser Containment Sensor(s). Model:.208 ®Dispenser Containment Sensor(s). Model: 208
®Shear Valve(s). ®Shear Valve(s).
❑Dispenser Containment Float(s)and Chain(s). ❑Dispenser Containment Float(s)and Chain(s).
Dispenser ID: 5$ Dispenser ID: 7-8
ED.Dispenser Containment Sensor(s). Model: 208 ®Dispenser Containment Sensor(s). Model: 208
®Shear Valve(s). ®Shear Valve(s).
Dispenser Containment Float(s)and Chain(s). ❑Dispenser Containment Float(s)and Chain(s).
Dispenser=ID: 9-10 Dispenser ID: 11-12
®Dispenser Containment Sensor(s). Model: 208 ®Dispenser Containment Sensor(s). Model: 208
®Shear Valve(s). ®Shear Valve(s).
❑Dispenser Containment Float(s)and Chain(s). ❑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 Plot Plan showing the layout of monitoring equipment. For any equipment capable of generating such reports,I have also
attached a copy of the report;(check aU that apply): ® System set-up ®Alarm history report
Technician Name(print): MICHAEL MOORE Signature:
how
Certification No.: VR A28078/ICC#5249074-UT License.No.: 532878 A-haz
Testing Company Name: Redwine Testing Services, Inc. Phone No.:(661) 834-6993
Site Address: 900 MONTEREY ST Date of Testing/Servicing: 10/15/2008
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UN-036—1/4 www.unidocs.org IIIIIIIIIIIIIIIIIIII 48 Rev.01/26/06
IE
Monitoring System Certification
D. Results of Testing/Servicing
Software Version Installed: VR TLS 350
Complete the following checklist:
® Yes ❑.No* Is the audible alarm operational?
® Yes ❑ No* Is the visual alarm operational?
® Yes ❑ No* Were all sensors visually inspected,functionally tested,and confirmed operational?
® Yes ❑ No* Were all sensors installed at lowest point of secondary containment and positioned so that other equipment will
not interfere with their proper operation?
❑ Yes ❑ No* If alarms are relayed to a remote monitoring station, is all communications equipment (e.g., modem)
® N/A operational?
® Yes ❑ No* For pressurized piping systems, does the turbine automatically shut down if the piping secondary containment
❑ N/A monitoring system detects a leak, fails to operate, or is electrically disconnected? If yes: which sensors initiate
positive shut-down? (Check all that apply) ® Sump/Trench Sensors; ®Dispenser Containment Sensors.
Did you confirm positive shut-down due to leaks and sensor failure/disconnection? ®Yes; ❑No.
® Yes ❑ No* For tank systems that utilize the monitoring system as the primary tank overfill warning device (i.e., no
❑ N/A mechanical overfill prevention valve is installed), is the overfill warning alarm visible and audible at the tank
fill point(s)and operating properly? If so,at what percent of tank capacity does the alarm trigger? 90%
❑ Yes* ® No 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.
❑ Yes* ® No Was liquid found inside any secondary containment systems designed as dry systems? (Check all that apply)
❑Product; ❑ Water. If yes,describe causes in Section E,below.
® Yes ❑ No* Was monitoring system set-up reviewed to ensure proper settings?Attach set up reports, if applicable
® Yes ❑ No* Is all monitoring equipment operational per manufacturer's specifications?
*In Section E below,describe how and when these deficiencies were or will be corrected.
E. Comments:
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Monitoring System Certification
F. In-Tank Gauging/SIR Equipment: ® Check this box if tank gauging is used only for inventory control.
❑ 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:
[�Ees ❑ No* Has all input wiring been inspected for proper entry and termination, including testing for ground faults?
® Yes ❑ No* Were all tank gauging probes visually inspected for damage and residue buildup?
• Yes ❑ No* Was accuracy of system product level readings tested?.
® Yes ❑ No* Was accuracy of system water level readings tested?
® Yes ❑ No* Were all probes reinstalled properly?
®.Yes ❑ No* Were all items on the equipment manufacturer's maintenance checklist completed?
* In the Section H,below,describe how and when these deficiencies were or will be corrected.
G. Line Leak Detectors (LLD): ❑ Check this box if LLDs are not installed.
Complete the folio win checklist:
• Yes ❑ No* For equipment start-up or annual equipment certification, was a leak simulated to verify LLD performance?
❑ N/A (Check all that apply) Simulated leak rate: ®3 g.p.h.; 1-10.1 g.p.h; [10.2 g.p.h.
• Yes ❑ No* Were all LLDs confirmed operational and accurate within regulatory requirements?
• Yes ❑ No* Was the testing apparatus properly calibrated?
❑ Yes ❑ No* For mechanical LLDs,does the LLD restrict product flow if it detects a leak?
® N/A
® Yes ❑ No* For electronic LLDs,does the turbine automatically shut off if the LLD detects a leak?
❑ N/A
• Yes ❑ No* For electronic LLDs, does the turbine automatically shut off if any portion of the monitoring system is disabled
❑ N/A or disconnected?
• Yes ❑ No* j For electronic LLDs,does the turbine automatically shut off if any portion of the monitoring system malfunctions
❑ N/A I or fails a test?
® Yes ❑ No* For electronic LLDs,have all accessible wiring connections been visually inspected?
❑ N/A
• Yes ❑ No* Were all items on the equipment manufacturer's maintenance checklist completed?
* In the Section H,below,describe how and when these deficiencies were or will be corrected.
H. Comments:
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UN-036—1/4 www.unidocs.org Rev.01/26/06
SWRCB,January 2006
Spill Bucket Testing Report Form
This form is intended for use by contractors performing annual testing of UST spill containment structures. The completed form and
printouts from tests(f applicable), should be provided to the facility owner/operator for submittal to the local regulatory agency.
1. FACfLITY INFORMATION
Facility Name: ARCO AM/PM Date of Testing: 10/15/08
Facility Address: 900 MONTEREY ST BAKERSFIELD,CA.
Facility Contact: ALONDRA Phone: 835-8044
Date Local Agency Was Notified of Testing: 10/03/08
Name of Local Agency Inspector(f present during testing): BAKERSFIELD FIRE DEPT.
2. TESTING CONTRACTOR INFORMATION
Company Name: Redwine Testing Services Inc.
Technician Conducting Test: MICHAEL MOORE
Credentials: ❑CSLB Contractor X ICC Service Tech. ❑SWRCB Tank Tester ❑Other(Spec)
License Number(s): ICC 5249074-OT / VR#A28078
3. SPILL BUCKET TESTING INFORMATION
Test Method Used: X Hydrostatic ❑Vacuum ❑Other
Test Equipment Used: MEASURING TAPE Equipment Resolution: MARK
Identify Spill Bucket(By Tank 1 T-1 SYPHON OPW 2 T-2 MAIN 87 OPW 3 T-3 91 OPW 4
Number, Stored Product, etc.
Bucket Installation Type: ❑Direct Bury ❑Direct Bury ❑Direct Bury ❑Direct Bury
X Contained in Sump X Contained in Sump X Contained in Sump ❑Contained in Sum
Bucket Diameter: 12" 12" 12"
Bucket Depth: 12" 12" 12"
Wait time between applying 5 MIN 5 MIN 5 MIN
vacuum/water and start of test:
Test Start Time(TI): 11:30 AM 11:30 AM 11:30 AM
Initial Reading(R[): 12" 12" 12"
Test End Time(TF): 12:30 PM 12:30 PM 12:30 PM
Final Reading(RF): 12" 12" 12"
Test Duration(TF—Tj): 1 HR 1 HR 1 HR
Change in Reading(RF-RO: NO NO NO
Pass/Fail Threshold or PASS PASS PASS
Criteria:
TestResult X Pass ❑F
ail X,Pass 'O Fails,` X Pass v;.❑Fall:'
Lip,
ass;`• ❑F`ail ' .."
Comments—(include information on repairs made prior to testing, and recommended follow-up for failed tests)
CERTIFICATION OF TECHMCIAN RESPONSIBLE FOR CONDUCTING THIS TESTING
I hereby certify that all the information contained in this report is true,accurate,and in fuU compliance with legal requirements.
Technician's Signature: ► " V MjA-1 Date: 10/15/08
State laws and regulations do not currently require testing to be performed by a qualified contractor.However,local requirements
may be more stringent.
MECHANICAL LEAK DETECTOR TEST
WORK SHEET.
W/O# :
Facility Name: ARCO AM/PM
Facility Address: 900 MONTEREY ST. BAKERSFIELD,CA. 93305
Product Line Type (Pressure, Suction, Gravity) PRESSURE
PRODUCT LEAK DETECTOR TYPE TEST TRIP PASS
SERIAL# BELOW PSI OR
3 GPM FAIL
T-1 L/D TYPE RED JACKET YES PASS
SYPHON 87 SERIAL# 244-006-5 5 PSI
T-2 L/D TYPE RED JACKET YES PASS
MAIN 87 SERIAL# 244-006-5 5 PSI
T-3 L/D TYPE RED JACKET YES PASS
91 SERIAL# 244-006-5 2 PSI
L/D TYPE
SERIAL#
I certify the above tests were conducted on this date according to Red Jacket Pumps
field test apparatus testing procedure an limitations
The Mechanical Leak Detector Test pass / fail is determined by using a low flow
threshold trip rate of 3 gallon per hour or les at 10 PSI
I acknowledge that all data collected is true and correct to the best of my knowledge.
Tech: Michael Moore
Signature: Date: 10/15/2008
I
Monitoring System Certification
UST Monitoring Site Plan
Site Address:
9 3 30 A
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Ts- 7 7 37
Date map was drawn. _jC5 T
Instructions
If you already have a diagram that shows all required information, you may include it, rather than this page,. with
he general. 1_1
your Monitoring System Certification. On your site plan, shots t raJ layout of tanks and plpin�,,, (ean-
i'dent' I
ify locations of the following equipment, if installed: munitunng systern control panels sensors monitoring
g
tank annular spaces, sumps., dispenser pans, spill containers, or other secondary containment areas, mechanical of
electronic line leak detectors; and in-tank liquid level probes (if used for leak detection,). In the space provided,
note the date this Site Plan was prepared.
---- IN-TANK ALARM
---- IN-TANK ALARM ----- T 3:PREMIUM
-- SENSOR ALARM ----- I T 3:PREMIUM MAX PRODUCT ALARM
'-;L 7:9REMIUM ANNULAR I PROBE OUT F . OCT 15. 2008 11 :43 AM
, 'ANNULAR SPACE OCT 15, 2006 11 :40 AM
FUEL ALARM
OCT 15, 2008 11 :30 AM
+
ARCO 05526 ARCO 05526
900 MONTEREY ST 900 MONTEREY ST
BAKERSFIELD CA 93305
----- SENSOR ALARM ----- BAKERSFIELD CA 93305
805-8b1 . 1972
L B:PREMIUM FILL SUMP 805-861 .1972
OTHER SENSORS r- OCT 15, 2008 11 :45 AM
FUEL ALARM OCT 15, 2008 11 :42 AM
OCT 15, 2008 11 :34 AM
' IN-TANK ALARM ----- SYSTEM STATUS REPORT
T3:PREMIUM SYSTEM STATUS REPORT - - _ - _ _
LOW PRODUCT ALARM - - - - - - - - - - T 3:OVERFILL ALARM
OCT 15, 2008 11 :40 AM T 3:LOW PRODUCT ALARM
T 3:DELIVERY NEEDED T 3:HIGH PRODUCT ALARM M
Z i ARCO 05526
900 MONTEREY ST
BAKERSFIELD CA 93305
805-861 . 1972
OCT 15, 2008 11 :46 AM
-- IN-TANK ALARM------
T 3:PREM I UP$
DELIVERY NEEDED ' ' SYSTEM STATUS REPORT
OCT 15, 2008 11 :40 PJW IN-TANK ALARM ----- - - - - - - - - - - - -
.� T 3:PREMIUM
T 3:OVERFILL ALARM
OVERFILL ALARM
OCT 15, 2008 11 :42 AM T 3:HIGH PRODUCT ALARM
INVENTORY REPORT
1 T 1-,UNLEADED SYPHON
-- IN-TANK ALARM ----- VOLUME = 3083 GALS
T 3:PREMIUM , I ULLAGE = 8544 GALS
INVALID FUEL LEVEL 90% ULLAGE= 7381 GALS
OCT 15 2008 11 :40 AM TC VOLUME = 3050 GALS
---- IN-TANK ALARM ----- , ;
.--,� HEIGHT = 29. 11 INCHES
T 3:PREMIUM WATER VOL = 0 GALS
MAX PRODUCT ALARM WATER 0.00 INCHES
t OCT 15, 2008 11 :42 AM TEMP 75.2 DEG F
T 2:UNLEADED MAIN
VOLUME = 3265 GALS
ULLAGE = 8362 GALS
RCO 05526 90% ULLAGE= 7199 GALS
00 MONTEREY ST TC VOLUME = 3223 GALS
AKERSFIELD CA 93305 HEIGHT = 30.30 INCHES
05-861 .1972 - WATER VOL 0 GALS
-- IN-TANK ALARM ----- WATER =—""0.00 INCHES
CT 15, 2008 11 :40 AM 1 T3:PREMIUM f TEMP = 78.1 DEG F
' HIGH PRODUCT ALARM
OCT 15. 2006 11 :42 AM
T 3:PREMIUM
SYSTEM STATUS REPORT VOLUME = 11137 GALS
ULLAGE 490
3:LOW PRODUCT ALARM 1 90% ULLAGE= 0 GALS
TC VOLUME = 1OB95 GALS
3:INVALID FUEL LEVEL HEIGHT = 83.52 INCHES
WATER VOL = 126 GALS
3:DELIVERY NEEDED WATER 3.53 INCHES
---- IN-TANK ALARM -----
TEMP __ 90.9 DEG F
T 3:PREMIUM
HIGH PRODUCT ALARM
OCT 15, 2008 11 :43 AM
ARCO 05526:, ARCO 05526" ---- IN-TANK ALARM --
900 MONTEREY ST - 900 MONTEREY ST T 2:UNLEADED MAIN
HAKERSFIEi D` CA"93305 I BAKERSFTEILD CA 93305 ! PROBE OUT
805-861 .19 72 805-861 . 1972 } ( OCT 15, 2008 12:08 PM
OCT. 15, 2008 11 :47.AM OCT ,15, 2008 11 :54 AM _
SYSTEM STATUS REPORT SYSTEM. STATUS REPORT'
-
- - - - - - - - - - -
T 3:OVERFILL ALARM ALL FUNCTIONS NORMAL
---- 1N-TANK ALARM -----
- - T 2:UNLEADED MAIN
° OVERFILL ALARM
... i 1
OCT 15, 2008 12:10 PM
----- SENSOR ALARM ------
L ,4tANNULAR MAIN UNL 4
T 3:PREMIUM ANNULAR.,SPAC_E
hMtEEtPQI .1?' FUEL ALARM
OCT 1,5. 2008 12:02411
INCREASE START s j ---- IN-TANK ALARM
---=-
:OCT 15, 2008 11 :40 AM T 2:UNLEADED MAIN
T 3:INVALID:FUEL LEVEL= ' MAX PRODUCT ALARM
VOLUME = 630 GALS � OCT 15. 2008 12:10 PM
HEIGHT - 9.99 INCHES
`
.WATER °_ 0.00 LNCHES -
TEMP 97.2-,DEG'F
----- SENSOR ALARM -----
INCREASE END L 5:MAIN UNL FILL .
OCT 15, 2008 11 :48 AMA' OTHER SENSORS
y " FUEL ALARM
VOLUME = 11627 GALS j OCT 15. 2008 12:05 PM r ---- 'IN-TANK ALARM -----
HEIGHT = 95.94 INCHES T 2:UNLEADED MAIN
} WATER = 0.95 INCHES ;HIGH PRODUCT ALARM
} TEMP
93.9.-DEG F : ' E OCT 15. 2008 12: 10 .PM
GROSS INCREASE= 10997 ! g
TC NET INCREASE= 10737 f
:, 1 ---- "I IV-TANK ALARM ----- - -
i T 2:UNLEADED MAIN , -
'LOW PRODUCT ALARM ----
j . OCT 15, 2008 12:07 PM i ---- IN-TANK ALARM
T 2:UNLEADED MAIN
PROBE OUT
OCT 15, 2008 12:11 PM
---- IN-TANK ALARM
T 3:PREMIUM
PROBE OUT
OCT 15, 2008 11 :48 AM P ---- IN-TANK,ALARM. -----
T 2:UNLEADED MAIN
DELIVERY NEEDED
OCT. 15. 2008 12:07 PM k ----- I-,N-TANK-ALARM
t T 3:PREMIUM
OCT 15. 20
p. LOW .PRODUCT ALARM
08 12: 13 PM
_ ----- SENSOR ALARM -----•
L 9:PREMIUM TURBINE SUMP r
STP SUMP
FUEL ALARM ! ---- IN=TANK`ALARM ----- I
OCT 15, 2008,11 :50 AM T 2:UNLEADED MAIN
INVAL.ID .FUEL.LEVEL- - IN-TANK ALARM
OCT• 15. 2008 12:07'PM ---
T 3:PREMIUM
- �- DELIVERY'NEEDED
OCT 15. -2008- 12:13 PM
- T 3:F=F;11:Jf1
I Nl./NT) °' 1 NC-R�,�_E ---- 1 N-TANK. ALARM --
T :PREP i l UM T 1 :UNLEADED SYPHON
INVALID FUEL LEVEL INCREASE START PROBE OUT
OCT 15, 2008 12: 13 PM OCT 15. 2008 12: 13 PM OCT 15, 2008 12:25 PM
'VOLUME 666 GALS
HEIGHT = 10.36 INCHES
WATER = 0.00 INCHES
TEMP = 97.4 DEG F
INCREASE END
----- SENSOR ALARM ----- OCT 15, 2008 12:20 PM ---- IIV-TANK ALARM ---
L 6:MAIN UNL TURBINE VOLUME = 1820 GALS T 1 :UNLEADED SYPHON
STP SUMP HEIGHT = 20.28 INCHES OVERFILL ALARM
FUEL ALARM WATER = 0.76 INCHES OCT 15, 2008 12:27 PM
OCT 15. 2008 12:14 PM TEMP = 97.3 DEG F
GROSS INCREASE= 1154
TC NET INCREASE= 1124
---- IN-TANK ALARM ---
T 2:UNLEADED MAIN T 1 :UNLEADED SYPHON
INVENTORY INCREASE MAX PRODUCT ALARM
OCT 15, 2008 12:27 PM
INCREASE START
OCT 15, 2008 12:08 PM
T 2: INVALID FUEL LEVEL
VOLUME 529 GALS ----- SENSOR ALARM -----
HEIGHT = 8.90 INCHES L 2:SYPHON FILL SUMP
WATER = 0.00 INCHES OTHER SENSORS
TEMP = 78. 1 DEG F FUEL ALARM
OCT 15, 2008 12:22 PM
---- IN-TANK ALARM ---
INCREASE END T I :UNLEADED SYPHON
OCT 15, 2008 12: 17 PM HIGH PRODUCT ALARM
OCT 15, 2008 12:27 PH
VOLUME = 11627 GALS
HEIGHT =108.29 INCHES
WATER = 0.00 INCHES
TEMP = 82.6 DEG F
GROSS INCREASE= 11098
---- IN-TANK ALARM -----
'
TC NET INCREASE= 10920 T 1 :UNLEADED SYPHON LOW PRODUCT ALARM
OCT 15, 2008 12:24 PM
---- IIV-TANK ALARM ----
T 1 :UNLEADED SYPHON
PROBE OUT
OCT 15, 2008 12:28 PM
---- IN-TANK ALARM -----
- SENSOR ALARM ----- T 1 :UNLEADED SYPHON
L 1 :ANNULAR SYPHON DELIVERY NEEDED
OCT 15, 2008 12:24 PM
ANNULAR SPACE ----- SENSOR ALARM ----
FUEL ALARM L 3:SYPHON TURBINE SUMP
OCT 15. 2008 12:19 PM PIPING SUMP
FUEL ALARM
OCT 15, 2000 12:"30 Ptl
---- IIV-TANK ALARM -----
T 1 :UNLEADED SYPHON
INVALID FUEL LEVEL
0(_7T 15, 2008 1 2U PM
'T 1 :UNL.EADEL S-PH';?P.! ----- SENSOR ALA RM ----- - - - --
' I•PlS.+EiY<_>r'`i I Pdi:REASE L 13:D I SP 7.8
T 3:PREP``I Ul'!
DISPENSER PAN VOLUME = 1812 GALS
INCREASE START FUEL ALARM ULLAGE 9815 GALS
OCT 15, 2008 12:25 PM OCT 15, 2008 12:58 PM 90% ULLAGE= 8652 GALS
T 1 :INVALID FUEL LEVEL TC VOLUME = X1764 GALS
VOLUME = 531 GALS HEIGHT • 0.22 INCHE
HEIGHT = 8.92 INCHES WATER VOL = 10 GALS
WATER = 0.75 I fVCHE
WATER = 0.00 INCHES TEMP = 97.6 DEG F
TEMP = 75.3 DEG F
INCREASE END
OCT 15, 2006 12:34 PM ----- SENSOR ALARM -----
L12:DISP 5.6
VOLUME = 11627 GALS DISPENSER PAN r1 A 7 T
HEIGHT = 97.66 INCHES FUEL ALARM C-
WATER = 1 .37 INCHES OCT 15, 2008 1 :01 PM 198949 ARCO AM-PM
TEMP = 81 .1 DEG F 8116 LAMONT AVE
LAMONT CA 93241
GROSS INCREASE= 11096
TC NET INCREASE= 10931 OCT 15, 2008 2:56 PM
SYSTEM STATUS REPORT
ARCO 05526 - - - - - - - - - - - -
900 MONTEREY ST ALL FUNCTIONS NORMAL
BAKERSFIELD CA 93305
805-861 . 1972 INVENTORY REPORT
OCT 15, 2008 1 :04 PM
T 1 :87
VOLUME = 5409 GALS
----- SENSOR ALARM ----- ULLAGE = 14542 GALS
L15:DISP 11 .12 SYSTEM STATUS REPORT 90% ULLAGE= 12546 GALS
DISPENSER PAN - - - - - - - - - - - - TC VOLUME = 5364 GALS
FUEL ALARM ALL FUNCT D--:+)S' i'! MAL HEIGHT = 38.29 INCHES
OCT 15, 2008 12:50 PM WATER VOL = 0 GALS
ARCO i 15526 WATER =
0.00 INCHES
900 MONTEREY ST TEMP = 71 .7 DEG F
BAKERSFIELD CA 93305
805-861 .1972
T 2:92
OCT 15, 2008 1 :04 PM VOLUME = 2599 GALS
ULLAGE = 9274 GALS
90% ULLAGE= 8086 GALS
TC VOLUME = 2569 GALS
----- SENSOR ALARM ----- SYSTEM STATUS REPORT HEIGHT - 33.51 INCHES
L14:DISP 9.10 - - - - - - - - - - - - WATER VOL, = 7 GALS
DISPENSER PAN ALL FUNCTIONS NORMAL WATER = 0.89 INCHES
FUEL ALARM TEMP = 76.5 DEG F
OCT 15, 2008 12:52 PM INVENTORY REPORT
T 3:87 SIPHON
T 1 :UNLEADED SYPHON VOLUME = 2845 GALS
VOLUME = 2860 GALS ULLAGE = 7461 GALS
ULLAGE = 8767 GALS 901 ULLAGE= 6430 GALS
90. ULLAGE= 7604 GALS TC VOLUME = 2814 GALS
TC VOLUME = 2828 GALS HEIGHT = 38.08 INCHES
HEIGHT = 27.63 INCHES WATER VOL = 0 GALS
WATER VOL = 0 GALS WATER = 0.00 INCHES
----- SENSOR ALARM ----- WATER = 0.00 INCHES TEMP = 75.3 DEG F
L11 :DISP 3.4 TEMP = 75.4 DEG F
DISPENSER PAN
FUEL ALARM MANIFOLDED TANKS
OCT 15, 2008 12:54 PM T 2:UNLEADED MAIN INVENTORY TOTALS
VOLUME = 3011 GALS T 1 :87
ULLAGE = 8616 GALS T 3:87 SIPHON
90% ULLAGE= 7453 GALS VOLUME = 8254 GALS
TC VOLUME = 2972 GALS TC VOLUME = 8178 GALS
HEIGHT = 28.64 INCHES
WATER VOL = 0 GALS * END * x
WATER = 0.00 INCHES
TEMP = 70.2 DEG F 161
----- SENSOR ALARM -----
L10:DISP 1 .2
DISPENSER RAN
FUEL ALARM
OCT 15. 200P 12:56 PM