HomeMy WebLinkAbout3221 TAFT HWY AST 2013HOODS ALARMS SPRINKLER SYSTEMS SPRAY BOOTHH AST
Permit No. Permit No. Permit No. Permit No. Permit No.
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Permit No.
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File Number: ?71 Address: 3 ;Zz ( d41- -Lj y
Bakersfield, CA 933
Date Received: - a _ ,'3
Business Name: d1m,,o
SYSTEM: BUILDING SQUARE FEET: INSPECTION LOCH
New Mod.
Commercial Hood System
Fire Alarm System
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minor
modification
removal
Fire Sprinkler System
Spw-ay Finish Sy%% em
Aboveground Storage Tank
Underground Storage-Tank
Underground Storage Tank
Underground Storage Tank
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Building Sq. Feet:
Calculation Bldg. Sq. Ft:
Comments: a - -T;&.rj << S `iarC L-e
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Date Time
Signature
Signature
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UNDERGROUND STORAGE TANK
PERMIT APPLICATION
TO CONSTRUCT- INSTALL NEW TANK (NEW FACILITY) /NEW
TANK INSTALL (EXISTING FACILITY) /MOD -MINOR MOD
Permit #
TYPE OF APPLICATION
CHECK ONE ONLY)
NEW TANK INSTALL /NEW FACILITY
MODIFICATION OF FACILITY
NEW TANK INSTALVEXISTING FACILITY
MINOR MODIFICATION OF FACILITY
STARTING DATE/ +
BAKERSFIELD FIRE DEPARTMENT
FACILITY NAME
Prevention Services
EXISTING FACILITY PERMIT #
1600 Truxtun Ave., Suite 401ADAUEeFInBakersfield, CA 93301
FIRN Phone: 661- 326 -3979 • Fax: 661- 852 -2171
ARTII f
TANK OWNER M/
Page 1 of 1
NEW TANK INSTALL /NEW FACILITY
MODIFICATION OF FACILITY
NEW TANK INSTALVEXISTING FACILITY
MINOR MODIFICATION OF FACILITY
STARTING DATE/ + PROPOSED COMPLETION DATE ' f4 _
FACILITY NAME EXISTING FACILITY PERMIT #
FACILITY ADDRESS goz 1 ,4FT' CITY t / ZIP CODE /jf
7
TYPE OF BUSINESS ' w w' APN
TANK OWNER M/ PHONE # - rf
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ADDRESS , rig, ^ A`
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CITY y rim
ENSE
ZIP CODE
CONTRACTOR J' 1
CAf'
JLIC # ICC #
Z55177/
71
ADDRESS .3 "rte d /
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CITY ,)% ` ZIP CODY0.6JS/
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PHONE # ' ) BAKIE`iRSFIELD CITY SINS CENSE # WORK/MAaN/5` COMP
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INSURER
BRIEFLY DESCRIBE THE WORK TO BE DONE: lam` i o4
II T utc,s I we, SseS II
WATER TO FACILITY PROVIDED BY
DEPTH TO GROUND WATER 1 0 SOIL TYPE EXPECTED AT SITE
CO'UNTERMOFTANKSTOBEINSTALLED2iARETHEYFORMOTORFUEL?
ES Cl NO
SPILL PREVENTION CONTROL AND URES PLAN ON FILE?
P—YES NO
THIS SECTION IS FOR MOTOR FUEL STORAGE TANKS
TANK # VOLUME UNLEADED REGULAR PREMIUM DIESEL AVIATION
IZ o Gay
A00 GAL.
THIS SECTION IS FOR NON -MOTOR FUEL STORAGE TANKS
TANKS # VOLUME UNLEADED REGULAR PREMIUM DIESEL AVIATION
FOR OFFICIAL USE ONLY
APPLICATION DATE FACILITY # OF TANKS FEES $
THE APPLICANT HAS RECEIVED, UNDERSTANDS, AND WILL COMPLY WITH THE ATTACHED CONDITIONS OF THIS PERMIT AND ANY OTHER STATE,
LOCAL, AND FEDERAL REGULATIONS. THIS FORM HAS BEEN COMPLETED UNDER PENALTY OF PERJURY, AND TO THE BEST OF MY KNOWLEDGE IS
TRUE AND CORRECT.
AP V,ED BY APPLICANT NAME (PRINT) APPLICANT SIGNATURE
THIS APPLICATION BECOMES A PERMIT WHEN APPROVED
FD2086 (Rev 06/07)
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UNDERGROUND STORAGE TANKS
APPLICATION
TO PERFORM ELD /LINE TESTING/
SB989 SECONDARY CONTAINMENT
TESTING/TANK TIGHTNESS TEST AND
FUEL MONITORING CERTIFICATION
PERMIT #
ENHANCED LEAK DETECTION
TANK TIGHTNESS
a e R a
P/RL
Rru r
BAKERSFIELD FIRE DEPARTMENT
Prevention Services
1600 Truxtun Ave., Suite 401
Bakersfield, CA 93301
Phone: 661-326-3979 • Fax: 661-852-2171
Page 1 of 1
LINE TESTING SB -989 SECONDARY CONTAINMENT
FUEL MONITORING CERTIFICATION
SITE INFORMATION
FACILITY / NAME & PHONE # OF CONTACT PERSON
ADDRESS /7// I CR- EICJ I I.D CA
OWNER NAME bFyAI
OPERATOR NAME PERMIT TO OPERATE #
OF TANKS TO BE TESTED: IS PIPING GOING TO BE TESTED? YES NO
TANK # VOLUME CONTENTS
C I Z o0o raq PW MNU .
TANK TESTING COMPANY
TESTING COMPANY- /- y_ %,/d//
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NAME & PH3 E ?
4
CONTACT PE /'.
4V ` VV
MAILING ADDRESS' . P4 VGN Uv o5 -7r e
NAME HONE # OF TESTER R SPECIAL INSPECTOR CERTIFICATION # *
44 I
DATE & TIME TEST TO BE CONDUCTED ICC # "/77&q TEST METHOD
APPLICANT SIGNATURE
lb
DATE
4HIS APPLICATION BECOMES A PERMIT WHEN APPROVED
VED BY DATE
FD2095(Rev 06/07)
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Page 1 of 2
ahLEAK DETECTION
TECHN0L0G1ESLLC
Exclusive Providers for MDleak® and
PHDleak® Testing Technologies
Facility Certification CONFIDENTIAL
Test Type: California ELD New Construction Test Express Final Test
Facility Name: Happy Gas Job #: 2666
Prepared For: DNJ Construction, Inc
Site Address: 3221 Taft Hwy
City: Bakersfield Primary Test Leak Rate: 0.005 eah
State and Zip: Ca 93313 Secondary Test Leak Rate: 0.1 gph
Start Date: 4/17/2013 End Date: 4/17/2013
SYSTEM Tk -1 87 TK -2 91 TK -3 DSL
Product Primary: PASS PASS PASS
Product Secondary: PASS PASS PASS
Vent Primary: PASS PASS PASS
Vent Secondary: PASS PASS PASS
VR Primary: PASS PASS NA
VR Secondary: PASS PASS NA
Tank: PASS PASS PASS
Turbine Sump: PASS PASS PASS
Turbine Sump Elect: PASS PASS PASS
Turbine Head: PASS PASS PASS
FilWapor Sump: PASS PASS PASS
Fill Sump ect: P PASS PASS
Pill & Vapor Poppet: PASS PASS PASS
UDC's: PASS PASS PASS
Fill Spill Bucket: PASS PASS PASS
Vapor Spill Bucket: PASS PASS NA
Certifying Field Technician: Ken Huey State Lie. # : 01 -1620
Certification Leak Rate: 0.005 gph
Certifying Technician Signature: Date: 4/17/2013
This is a statement to confirm that the components listed above, at the time of testing, have been tested to a leak
sensitivity listed above using the MDleak® and PHDleak® Method. The MDleak® and PHDleak® Method is one of the
most versatile and comprehensive testing procedure offered to the petroleum industry. All petroleum owners and
contractors which utilize the MDleak® and PHDleak® Method can be assured that their facility has passed the Nation's
highest standard in preventative leak detection.
I declare under penalty of perjury that I am a licensed tank tester in the MDleak® and PHDleak@ method, a method
listed by the NWGLDE organization and that the information contained in this report is true and correct to the best of
my knowledge.
If you have any questions on the testing please do not hesitate to call. @ 520- 2074878.
Office use only
Statement Confirmed by: Date: 4/17/2013
e
3221 Taft Hwy
n L DETECTION
N0L0GIESLLc
Exclusive Providers for MDleak® and
PHDleak® Testing Technologies
Page 2 of 2
Log of Repaired Leaks
Tank Information CONFIDENTIAL
Tk -1 87 TK -2 91 TK -3 DSL
12000 3000 5000
Fill Bucket Riser Top Steel Pipe - Single Wall
2783 4/16/13 17:09 Leak Final
Modem Modern Modem
2801 4/16/13 18:16 Leak Final Tk -187 Product Union
Vacuum Vacuum Vacuum
58 58 58
8 f 8 f 811
Tank Sump Boots Turbine
Bravo Smith Red Jacket
UDC/Dis erasers Information
It
Gilbarco
OPW
Smith
IN in Information
Manufacture
Smith
Smith
Fire -Flex
Phil -Tite
Heal
Reference #
Log of Repaired Leaks
Date Time Status System Component Manufacture
2782 4/16/13 17:06 Leak Final TK -3 DSL Fill Bucket Riser Top Steel Pipe - Single Wall
2783 4/16/13 17:09 Leak Final TO 87 VR Bucket Swivel OPW
2801 4/16/13 18:16 Leak Final Tk -187 Product Union Unknown
Log of Unrepaired Leaks
Reference # Date Time Status System Component Manufacture
Page 1 of 1
ahLEAK DETECTION
TECH NOLOGIESLLc
Exclusive Providers for MDleak® and
PHDleak® Testing Technologies
3221 Taft Hwy Reference Addendum CONFIDENTIAL
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SWRCB, January 2002 Page of
Secondary Containment Testing Report Form
Thisform is intendedfor use by contractors performingperiodic testing of USTsecondary containment systems. Use the
appropriate pages ofthisform to report resultsfor all components tested. The completedform, written test procedures, and
printoutsfrom tests (ifapplicable), should be provided to the facility owner /operatorfor submittal to the local regulatory agency.
1. FACILITY INFORMATION
Facility Name: Happy Gas Date ofTesting: 4/13/2013
Facility Address: 3221 Taft Hwy. Bakersfield, Ca.
Facility Contact: Phone:
Date Local Agency Was Notified of Testing :
Name of Local Agency Inspector (ifpresent during testing):
2. TESTING CONTRACTOR INFORMATION
Company Name: Advanced Compliance
Pass
Technician Conducting Test: Bruce W. Hinsley
Not
Tested
Credentials: X CSLB Licensed Contractor SWRCB Licensed Tank Tester
License Type: C61 /D40 License Number: 971259
Manufacturer Training
Manufacturer Component(s) Date Training Expires
Incon TS -STS 9/17/2014
X
3. SUMMARY OF TEST RESULTS
Component Pass Fail Not
Tested
Repairs
Made Component Pass Fail Not
Tested
Repairs
Made
87 UL Fill Sump X
87 UL STP Sump X
91 UL Fill Sump X
91 UL STP Sump X
Diesel Fill Sump X
Diesel STP Sump X
Vent Sump X
UDC 1 -2 X
UDC 3 -4 X
UDC 5 -6 X
UDC 7 -8 X
If hydrostatic testing was performed, describe what was done with the water after completion of tests:
Startup testing prior to the first drop of fuel into new tanks. All containments were new and clean.
Water was clean when removed from sumps. There was no power to the monitor or STPs yet.
CERTIFICATION OF TECHNICIAN RESPONSIBLE FOR CONDUCTING THIS TESTING
To the best ofmy knowledge, thefacts stated in this document are accurate and infull compliance with legal requirements
Technician's Signature: Date: 4/13/2013
SWRCB, January 2002 Page of
4. TANK ANNULAR TESTING
Test Method Developed By: Tank Manufacturer Industry Standard Professional Engineer
Other (Spec)
Test Method Used: Pressure Vacuum Hydrostatic
Other (Specify)
Test Equipment Used: Equipment Resolution:
Is Tank Exempt From Testing ?'
Tank # Tank # Tank # Tank #
Yes No Yes No Yes No Yes No
Tank Capacity:
Tank Material:
Tank Manufacturer:
Product Stored:
Wait time between applying
pressure /vacuum /water and
starting test:
Test Start Time:
Initial Reading (Ri):
Test End Time:
Final Reading (RF):
Test Duration:
Change in Reading (RF -Rj):
Pass/Fail Threshold or Criteria:
Test Result: Pass Fail Pass Fail Pass Fail Pass Fail
Was sensor removed for testing? Yes No NA Yes No NA Yes []No NA Yes No NA
Was sensor properly replaced and
verified functional after testing? Yes No NA Yes No NA Yes No NA Yes No NA
Comments — (include information on repairs made prior to testing, and recommendedfollow -upforfailed tests)
Secondary containment systems where the continuous monitoring automatically monitors both the primary and secondary
containment, such as systems that are hydrostatically monitored or under constant vacuum, are exempt from periodic containment
testing. {California Code of Regulations, Title 23, Section 2637(a)(6)1
SWRCB, January 2002
5. SECONDARY PIPE TESTING
Page of
Test Method Developed By: Piping Manufacturer Industry Standard Professional Engineer
Other (Specify)
Test Method Used: X Pressure Vacuum Hydrostatic
Other (Spec)
Test Equipment Used: Nitrogen / Pressure Gauge Equipment Resolution:
Piping Run # Piping Run # Piping Run # Piping Run #
Piping Material:
Piping Manufacturer:
Piping Diameter:
Length ofPiping Run:
Product Stored:
Method and location of
piping-run isolation:
Wait time between applying
pressure /vacuum /water and
starting test:
Test Start Time:
Initial Reading (R,):
Test End Time:
Final Reading (RF):
Test Duration:
Change in Reading (RF -R,):
Pass/Fail Threshold or
Criteria:
Test Result: Pass Fail Pass Fail Pass Fail Pass Fail
Comments — (include information on repairs made prior to testing, and recommendedfollow -upforfailed tests)
SWRCB, January 2002 Page of
6. PIPING SUMP TESTING
Test Method Developed By: Sump Manufacturer X Industry Standard Professional Engineer
Other (Specify)
Test Method Used: Pressure Vacuum X Hydrostatic
Other (Specify)
Test Equipment Used: Incon TS -STS
Sump # 87 STP Sump # 91 STP
Equipment Resolution: 0.002
Sump # Diesel STP Sump # Vent
Sump Diameter: 48" 48" 48" 24"
Sump Depth: 48" 48" 48" 24"
Sump Material: FRP FRP FRP FRP
Height from Tank Top to Top of
Highest Piping Penetration:
9" 9" 9" 7"
Height from Tank Top to Lowest
Electrical Penetration: 6" 6" 6" N/A
Condition of sump prior to testing: Clean Clean Clean Clean
Portion of Sump Tested' 60% 60% 60% 70%
Does turbine shut down when
sump sensor detects liquid (both
and water)?*
Yes No NA Yes No NA Yes No NA Yes No NA
product
Turbine shutdown response time
Is system programmed for fail -safe
shutdown ?*
Yes No NA Yes No NA Yes No NA Yes No NA
Was fail -safe verified to be
operational?* Oyes No NA Yes No NA Yes No NA Yes No NA
Wait time between applying
pressure /vacuum /water and starting
test:
12 Hrs. 12 Hrs. 12 Hrs. 12 Hrs.
Test Start Time: 09:11/9:27 08:28/08:45 08:28/08:45 09:11/9:27
Initial Reading R 5.3706 "/5.3710" 5.6809 "/5.6808" 6.7365 "/6.7365" 6.0790 "/6.0803"
Test End Time: 09:26/09:42 08:44/09:00 08:44/09:00 09:26/09:42
R) Final Readin g( F 5.3711 "/5.3710" 5.6807 "/5.6806" 6.7364 "/6.7366" 6.0802 "/6.0813"
Test Duration: 30 Min. 30 Min. 30 Min. 30 Min.
Change in Reading (RF -R,): 0.0005 "10.0000" 0.0002 " /- 0.0002" 0. 0001 "/+0.0001" 0.0012" /+0.0010"
Pass/Fail Threshold or Criteria: 0.002" 0.002" 0.002" 0.002"
Test Result: X Pass Fail X Pass Fail X Pass Fail X Pass Fail
Was sensor removed for testing? Yes No NA Yes No NA Yes No NA Yes No NA
Was sensor properly replaced and
verified functional after testing? Yes No NA X Yes No NA Yes No NA Yes No NA
Comments — (include information on repairs made prior to testing, and recommendedfollow -upforfailed tests)
If the entire depth of the sump is not tested, specify how much was tested. If the answer to any ofthe questions indicated with an
asterisk(*) is "NO" or "NA ", the entire sump must be tested. (See SWRCB LG -160)
SWRCB, January 2002 Page of
7. UNDER- DISPENSER CONTAINMENT (UDC) TESTING
Test Method Developed By: UDC Manufacturer Industry Standard Professional Engineer
Other (Specify)
Test Method Used: Pressure Vacuum Hydrostatic
Other (Specie)
Test Equipment Used: Incon TS -STS
UDC # 1 -2 UDC # 3-4
Equipment Resolution: 0.002
UDC # 5-6 UDC # 7 -8
UDC Manufacturer: Bravo Bravo Bravo Bravo
UDC Material: FRP FRP FRP FRP
UDC Depth: 24" 24" 24" 24"
Height from UDC Bottom to Top
of Highest Piping Penetration:
10" 10" 10" 10"
Height from UDC Bottom to
Lowest Electrical Penetration:
N/A N/A N/A N/A
Condition of UDC prior. to
testin :
Clean Clean Clean Clean
Portion of UDC Tested 75% 75% 75% 75%
Does turbine shut down when
UDC sensor detects liquid (both
product and water)?*
Yes No NA Yes No NA Yes No NA Yes No NA
Turbine shutdown response time
Is system programmed for fail-
safe shutdown ?* Yes No NA Yes No NA Yes No NA Yes No NA
Was fail -safe verified to be Yes No NA Yes No NA Yes No NA Yes No NA
operational?'
Wait time between applying
pressure /vacuum /water and
starting test
12 Hrs. 12 Hrs. 12 Hrs. 12 Hrs.
Test Start Time: 10:10/10:26 10:10/10:26 10:10/10:26 10:10/10:26
Initial Reading (Rj): 4.0442 "/4.0435" 5.3185 "/5.3182" 6.1870 "/6.1869" 4.8380 "/4.8377"
Test End Time. 10:25/10:42 10:25/10:42 10:25/10:42 10:25/10:42
Final Reading (RF): 4.0436 "/4.0430" 5.3182 "/5.3181" 6.1868 "/6.1867" 4.8380 "/4.8375"
Test Duration: 30 Min. 30 Min. 30 Min. 30 Min.
Change in Reading (RF -R,): 0.0006 " /- 0.0005" 0.0003 " /- 0.0001" 0.0002 " /- 0.0002" 0.0000 " /- 0.0002"
Pass/Fail Threshold or Criteria:
Test Result: X Pass Fail X Pass Fail X Pass Fail X Pass Fail
Was sensor removed for testing? Yes No NA Yes No NA Yes No NA Yes No NA
Was sensor properly replaced and
verified functional after testing? Yes No NA Yes No NA Yes No NA Yes No NA
Comments — (include information on repairs made prior to testing, andrecommendedfollow -upforfailed tests)
Ifthe entire depth of the UDC is not tested, specify how much was tested. Ifthe answer to any ofthe questions indicated with an
asterisk(*) is "NO" or "NA ", the entire UDC must be tested. (See SWRCB LG -160)
SWRCB, January 2002
8. FILL RISER CONTAINMENT SUMP TESTING
Page of
Facility is Not Equipped With Fill Riser Containment Sums
Fill Riser Containment Sumps are Present, but were Not Tested
Test Method Developed By: Sump Manufacturer X Industry Standard Professional Engineer
Other (Specify)
Test Method Used: Pressure Vacuum X Hydrostatic
Other (Spec)
Test Equipment Used: Incon TS -STS Equipment Resolution: 0.002
Fill Sump # 87 UL Fill Sump # 91 UL Fill Sump # Diesel Fill Sump #
Sump Diameter: 42" 42" 42"
Sump Depth: 48" 48" 48"
Height from Tank Top to Top of
Highest Piping Penetration:
N/A N/A N/A
Height from Tank Top to Lowest
Electrical Penetration:
8" 8" 8"
Condition of sump prior to
testing:
Clean Clean Clean
Portion of Sump Tested 60% 60% 60%
Sump Material: FRP FRP FRP
Wait time between applying
pressure /vacuum /water and
starting test:
12 Hrs. 12 Hrs. 12 Hrs.
Test Start Time: 08:28/08:45 08:28/08:45 09:11/09:27
Initial Reading (R,): 3.8545 "/3.8545" 4.3776 "/4.3772" 5.2844 "/5.2842"
Test End Time: 08:44/09:00 08:44/09:00 09:26/09:42
Final Reading (RF): 3.8547'/3.8555" 4.3774 "/4.3776" 5.2842 "/5.2840"
Test Duration: 30 Min. 30 Min. 30 Min.
Change in Reading RF -R,): 0.0002 " / +0.0010" 0.0002 "/+0.0004" 0.0002 " /- 0.0002"
Pass/Fail Threshold or Criteria: 0.002" 0.002" 0.002"
Test Result: X Pass Fail X Pass Fail X Pass Fail Pass Fail
Is there a sensor in the sump? Yes No Yes No Yes No Yes No
Does the sensor alarm when
either product or water is
detected?
Yes No NA Yes No NA Yes No NA Yes No NA
Was sensor removed for testing? Yes No NA Yes No NA Yes No NA El Yes 11 No El NA
Was sensor properly replaced and
verified functional after testing? yes No NA Yes No NA Yes No NA Yes No NA
Comments — (include information on repairs made prior to testing, andrecommendedfollow -upforfailed tests)
SWRCB, January 2002 Page of
9. SPILLJOVERFILL CONTAINMENT BOXES
Facility is Not Equipped With Spill/Overfill Containment Boxes
SpillJOverfill Containment Boxes are Present, but were Not Tested
Test Method Developed By: Spill Bucket Manufacturer Industry Standard Professional Engineer
Other (Specify)
Test Method Used: Pressure Vacuum Hydrostatic
Other (Spec)
Test Equipment Used: Equipment Resolution:
Spill Box # Spill Box # Spill Box # Spill Box #
Bucket Diameter:
Bucket Depth:
Wait time between applying
pressure /vacuum /water and
test: starting
Test Start Time:
Initial Reading (R,):
Test End Time:
Final Reading (RF):
Test Duration:
Change in Reading (RF -R,):
Pass/Fail Threshold or
Criteria:
Test Result: Pass Fall Pass Fail Pass Fail Pass Fail
Comments — (include information on repairs made prior to testing, and recommendedfollow -upforfailed tests)
TAFTHAPPYGAS
3221 TAFT HWY.
i
HAPPY GAS
3221 HWY.
BAKERSFIELD CA
BAKERSFIELD CA 3221 TAFT HWY.
j BAKERSFIELD CA 04/13/2013 9:27 AM
04/13/2013 8:44 AM 04/13/2013 9:00 AM SUMP LEAK TEST REPORT
SUMP LEAK TEST REPORT
SUMP LEAK TEST REPORTj VENT
87 FILL
7 FILL TEST STARTEDI 9:11 AM
TEST STARTED 8:28 AM
TEST STARTED 04/13/2013 TEST STARTED 8:45 AM TEST STARTED 04/13,-2013
7NBEGINLEVEL
BEGIN LEVEL 3.8545 IN TEST STARTED 04 /13/2013 END TIME 9:26 AMENDDATEENDTIME8:44 AM
END DATE 04/13/2013
BEGIN LEVEL 3.8545 IN
END TIME 9:00 AM 0443/2013ENDLEVEL6.0802 IN
END LEVEL 3.8547 IN END DATE 04/13/2013 LEAK THRESHOLD 0.002 IN
LEAK THRESHOLD 0.002 IN END LEVEL 3.8555 IN TEST RESULT PASSED
TEST RESULT PASSED LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
UDC 3 -4
91 STP 91 STP TEST STARTED
TEST STARTED 8:28 AM
TEST STARTED 04/13/2013 TEST STARTED 8:45 AM TEST STARTED 04/13/2013BEGINLEVEL6.7022 IN
BEGIN LEVEL 5.6809 IN j TEST STARTED 04/13/2013 END TIME 9.26 RM
END TIME 8:44 AM BEGIN LEVEL 5.6808 IN END DATE 04/13/2013i
END DATE 04/13/2013 END TIME 9:00 AM END LEVEL 6.7208 IN
END LEVEL 5.6807 IN END DATE 04/13/2013 LEAK THRESHOLD 0.002 IN
LEAK THRESHOLD 0.002 IN END LEVEL 5.6806 IN TEST RESULT INCREASED
TEST RESULT PASSED LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
87 STP
91 FILL
91 FILL TEST STARTED 9:11 AM
TEST STARTED 8:28 AM TEST STARTED 04/13/2013
TEST STARTED 04/13/2013 TEST STARTED 8:45 AM BEGIN LEVEL 5.3706 IN
BEGIN LEVEL 4.3776 IN TEST STARTED 04 /13/2013 END TIME 9;26 AM
END TIME 8:44 AM j BEGIN LEVEL 4.3772 IN END DATE 04/13/2013
END DATE 04/13/2013 I END TIME 9:00 AM END LEVEL 5.3711 IN
END LEVEL 4.3774 IN END DATE 04/13/2013 LEAK THRESHOLD 0.002 IN
LEAK THRESHOLD 0.002 IN END LEVEL 4.3776 IN TEST RESULT PASSED
TEST RESULT PASSED LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
DSL FIL
DSL STP
DSL STP TEST STARTED 9:11 AM
TEST STARTED 8:28 AM TEST STARTED 04/13/2013
TEST STARTED 04/13/2013 TEST STARTED 8:45 AM BEGIN LEVEL 5.2844 IN
BEGIN LEVEL 6.7365 IN TEST STARTED 04/13/2013 END TIME 9 :26 AM
END TIME 8:44 AM BEGIN LEVEL 6.7365 IN END DATE 04/13/2013
END DATE 04/13/2013 END TIME 9:00 AM END LEVEL 5,2842 IN
END LEVEL 6.7364 IN END DATE 04/13/2013 LEAK THRESHOLD 0.002 IN
LEAK THRESHOLD 0.002 IN END LEVEL 6.7366 IN EST RESULT PASSED
TEST RESULT PASSED LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
HAPPY GAS
3221 TAFT HWY.
BAKERSFIELD CA
04/13/2013 9:43 AM
SUMP LEAK TEST REPORT
VENT
TEST STARTED 9:27 AM
TEST STARTED 04 /13/2013
BEGIN LEVEL 6.0803 IN
END TIME 9:42 AM
END DATE 04/13/2013
END LEVEL 6.0813 IN
LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
UDC 3 -4
TEST STARTED 927 AM
TEST STARTED 04/13/2013
BEGIN LEVEL 6.7187 IN
END TIME 9:42 AM
END DATE 04/13/2013
END LEVEL 6.7213 IN
LEAK THRESHOLD 0.002 IN
TEST RESULT INCREASED
87 STP,
TEST STARTED 9:27 AM
TEST STARTED 04/13/2013
BEGIN LEVEL 5.3710 IN
END TIME 9:42 AM
END DATE 04/13/2013
END LEVEL 5.3710 IN
LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
DSL FIL
TEST STARTED
TEST STARTED
BEGIN LEVEL
END TIME
END DATE
END LEVEL
LEAK THRESHO'.
TEST RESULT
9:27 AM
04/13/2013
5.2842 IN
9:42 AM
04/13/2013
5.2840 IN
D 0.002 IN
PASSED
HAPPY GAS
3221 TAFT HWY. HAPPY GASBRKERSFIELDCA3221TAFTHWY.
BAKERSFIELD CA
04/13/2913 19:26 AM
04/13/2013 10:42 AM
SUMP LEAK TEST REPORT
SUMP LEAK TEST REPORT
UDC 1 -2
UDC 1 -2
TEST STARTED 10:10 AM
TEST STARTED 04/13/2013 TEST STARTED 10:26 AM
BEGIN LEVEL 4.0442 IN TEST STARTED 04/13/2013
END TIME 10:25 AM BEGIN LEVEL 4.0435 IN
j END DATE 04/13/2013 END TIME 10:42 AM
END LEVEL 4.0436 IN END DATE 04/13/2013
LEAK THRESHOLD 0.002 IN END LEVEL 4.0430 IN
y TEST RESULT PASSED LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
UDC 3-4
UDC 3 -4
TEST STARTED 10:10 AM
TEST STARTED 04/13/2013 TEST STARTED 10:26 AM
BEGIN LEVEL 5.3185 IN TEST STARTED 04/13/2013
END TIME 10:25 AM BEGIN LEVEL 5.3182 IN
END DATE 04/13/2013 END TIME 10:42 AM
END LEVEL 5.3182 IN END DATE 04/13/2013
LEAK THRESHOLD 0.002 IN END LEVEL 5.3181 IN
TEST RESULT PASSED LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
UDC 5 -6
UDC 5-6
TEST STARTED 10:10 AM 1
TEST STARTED 04/13/2013 TEST STARTED 10:26 AM
BEGIN LEVEL 6.1870 IN TEST STARTED 04/13/2013
END TIME 10:25 AM BEGIN LEVEL 6.1869 IN
END DATE 04/13/2013 END TIME 10:42 AM
END LEVEL 6.1868 IN END DATE 04/13/2013
LEAK THRESHOLD 0.002 IN END LEVEL 6.1867 IN
TEST RESULT PASSED LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
UDC 7 -8
UDC 7 -8
TEST STARTED 10:10 AM
TEST STARTED 04/13/2013 TEST STARTED 10:26 AM
BEGIN LEVEL 4.8380 IN TEST STARTED 04/13/2013
END TIME 10:25 AM BEGIN LEVEL 4.8377 IN
END DATE 04/13/2013 END TIME 10:42 AM
END LEVEL 4.8380 IN END DATE 04 /13/2013
LEAK THRESHOLD 0.002 IN END LEVEL 4.8375 IN
TEST RESULT PASSED LEAK THRESHOLD 0.002 IN
TEST RESULT PASSED
MONITORING SYSTEM CERTIFICATION
For Use By All Jurisdictions Within the State ofCalifornia
Authority Cited: Chapter 6 7, Health and Safety Code; Chapter 16, Division 3, Title 23, California Code ofRegulations
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 ofthis 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: Happy Gas & Mini Mart Bldg. No.:
Site Address: 3221 Taft Highway City: Bakersfield Zip: 93313
Facility Contact Person: Amita Contact Phone No.: (661) 831 -2323
Make /Model of Monitoring System: Veeder -Root TLS 350 Date of Testing/Servicing: 4/24/2013
B. Inventory of Equipment Tested /Certified
Check the appropriate boxes to indicate specific equipment inspected /serviced:
Tank ID: 12000 gal. Regular Tank ID: 3000 gal. Super
Z In -Tank Gauging Probe. Model: 847390 -107 In -Tank Gauging Probe. Model: 847390 -107
Z Annular Space or Vault Sensor. Model: 794390 -420/ Vacuum Z Annular Space or Vault Sensor. Model: 794390 -420/ Vacuum
Z Piping Sump / Trench Sensor(s). Model: 794380 -208 / 794390 -304 Z Piping Sump / Trench Sensor(s). Model: 794380 -208 / 794390 -304
Z Fill Sump Sensor(s). Model: 794380 -208 / 794390 -304 Z Fill Sump Sensor(s). Model: 794380 -208 / 794390 -304
Mechanical Line Leak Detector. Model: Mechanical Line Leak Detector. Model:
Z Electronic Line Leak Detector. Model: PLLD Z Electronic Line Leak Detector. Model: PLLD
Z Tank Overfill / High -Level Sensor. Model: 847390 -107 Z Tank Overfill / High -Level Sensor. Model: 847390 -107
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: 3000 gal. Diesel Tank ID:
Z In -Tank Gauging Probe. Model: 847390 -107 In -Tank Gauging Probe. Model:
Z Annular Space or Vault Sensor. Model: 794390 -420/ Vacuum Annular Space or Vault Sensor. Model:
Z Piping Sump / Trench Sensor(s). Model: 794380 -208 / 794390 -304 Piping Sump / Trench Sensor(s). Model:
Z Fill Sump Sensor(s). Model: 794380 -208 / 794390 -304 Fill Sump Sensor(s). Model:
Mechanical Line Leak Detector. Model: Mechanical Line Leak Detector. Model:
Z Electronic Line Leak Detector. Model: PLLD Electronic Line Leak Detector. Model:
Z Tank Overfill / High -Level Sensor. Model: 847390 -107 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
Z Dispenser Containment Sensor(s). Model: 794380 -208 / 794390 -304 Z Dispenser Containment Sensor(s). Model: 794380 -208 / 794390 -304
Z Shear Valve(s). Z Shear Valve(s).
Dispenser Containment Float(s) and Chain(s). Dispenser Containment Float(s) and Chain(s).
Dispenser ID: 5-6 Dispenser ID: 7-8
Z Dispenser Containment Sensor(s). Model: 794380 -208 / 794390 -304 Z Dispenser Containment Sensor(s). Model: 794380 -208 / 794390 -304
Z Shear Valve(s). Z Shear Valve(s).
Dispenser Containment Float(s) and Chain(s). Dispenser Containment Float(s) and Chain(s).
Dispenser ID: Vent Box Dispenser ID:
Z Dispenser Containment Sensor(s). Model: 794380 -208 / 794390 -304 Dispenser Containment Sensor(s). Model:
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 - 1 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 all that apply): ® System set -up Z Alarm history report
Technician Name (print): _ Kristopher Karns Signature: -el. _
Certification No.: B34106 License. No.: 804904
Testing Company Name: Confidence UST Services, Inc. Phone No.: (800) 339 -9930
Site Address: 3221 Taft Highway, Bakersfield, CA 93313 Date of Testing/Servicing: 4124/2013
Page 1 of 3
Monitoring System Certification
D. Results of Testing/Servicing
Software Version Installed: 333.02
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)
E 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 oftank 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. Ifyes, 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: Replaced Overfill Alarm light bulb.
Page 2 of 3
Monitoring System Certification
F. In -Tank Gauging / SIR Equipment: ® Check this box iftank 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:
Yes 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 1 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):
Complete the following checklist:
Check this box if LLDs are not installed.
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.; 0.1 g.p.h ; 0.2 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 ifthe 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* For electronic LLDs, does the turbine automatically shut off if any portion of the monitoring system malfunctions
N/A 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:
Page 3 of 3
Monitoring System Certification Form: Addendum for Vacuum/Pressure Interstitial Sensors
I. Results of Vacuum/Pressure Monitoring Equipment Testing
This page should be used to document testing and servicing of vacuum and pressure interstitial sensors. A' copy of
this form must be included with the Monitoring System Certification Form, which must be provided to the tank
system owner /operator. The owner /operator must submit a copy of the Monitoring System Certification Form to the
local agency regulating UST systems within 30 days oftest date.
Manufacturer: Veeder Root Model: 330020 -463 System Type: Pressure; ® Vacuum
Sensor ID
Component(s) Monitored by this Sensor: 87 Vent
S -1
Sensor Functionality Test Result: ® Pass; Fail Interstitial Communication Test Result: ® Pass; Fail
Component(s) Monitored by this Sensor: 87 Vapor
S -2
Sensor Functionality Test Result: ® Pass; Fail Interstitial Communication Test Result: ® Pass; Fail
Component(s) Monitored by this Sensor: 87 Product
S -3
Sensor Functionality Test Result: ® Pass; Fail Interstitial Communication Test Result: ® Pass; Fail
Component(s) Monitored by this Sensor: 87 Annular
S-4
Sensor Functionality Test Result: ® Pass; Fail Interstitial Communication Test Result: ® Pass; Fail
Component(s) Monitored by this Sensor: 91 Vent
S -5
Sensor Functionality Test Result: ® Pass; Fail Interstitial Communication Test Result: ® Pass; Fail
Component(s) Monitored by this Sensor: 91 Product
S-6
Sensor Functionality Test Result: ® Pass; Fail Interstitial Communication Test Result: ® Pass; Fail
Component(s) Monitored by this Sensor: Diesel Vent
S -9
Sensor Functionality Test Result: ® Pass; Fail Interstitial Communication Test Result: ® Pass; Fail
Component(s) Monitored by this Sensor: Diesel Product
S -10
Sensor Functionality Test Result: ® Pass; Fail Interstitial Communication Test Result: ® Pass; Fail
Component(s) Monitored by this Sensor: Diesel / 91 Annular
S -11
Sensor Functionality Test Result: ® Pass; Fail Interstitial Communication Test Result: ® Pass; Fail
Component(s) Monitored by this Sensor:
Sensor Functionality Test Result: Pass; Fail Interstitial Communication Test Result: Pass; Fail
How was interstitial communication verified?
Leak Introduced at Far End of Interstitial Space;' Gauge; Visual Inspection; Other (Describe in Sec. J, below)
Was vacuum /pressure restored to operating levels in all interstitial spaces? ® Yes No (Ifno, describe in Sec. J, below)
J. Comments:
Page 4 of 4
If the sensor successfully detects a simulated vacuum/pressure leak introduced in the interstitial space at the furthest point from the
sensor, vacuum/pressure has been demonstrated to be communicating throughout the interstice.
UN -036A -1 /1 www.unidoes.org Rev. 01/26/06
SOFTWARE REVISION LEVEL
VERSION 333.02
SOFTWAREO 346333 -100 -C
CREATED - 12.08.10- II -.22
S- MODULE0.330160 -0047a
SYSTEM:FEATURES:
PERIODIC IN- TANK'TESTS
ANNUAL IN -TANK TESTS
1SD /APM
SYSTEM SETUP
APR 24, 2013 9:27 AM
SYSTEM UNITS
U.S.
SYSTEM LANGUAGE
ENGLISH
SYSTEM DATE /TIME FORMAT
MON DD YYYY HH : MM : SS. xM
HAPPY GAS.
3221 T,AFT HWY
BAKERSFIELD CA
93313
SHIFT TIME 1 DISABLED
SHIFT TIME 2 :.DISABLED
SHIFT TIME 3 DISABLED
SHIFT TIME 4 DISABLED
TANK PER TST NEEDED_ WRN
DISABLED
TANK ANN TST NEEDED WRN
DISABLED
LINE RE- ENABLE METHOD
PASS LINE TEST
LINE PER TST NEEDED WRN
DISABLED'
LINE ANN TST NEEDED WRN
DISABLED,
PRINT TC VOLUMES
ENABLED
TEMP COMPENSATION
VALUE (DEG .F ): 60.0
STICK HEIGHT OFFSET
DISABLED.
ULLAGE: 90:
H- PR6TOCOL DATA FORMAT
HEIGHT
PRECISION TEST DURATION
HOURS: I 1
DAYLIGHT SAVING TIME
DISABLED
RE- DIRECT LOCAL PRINTOUT
DISABLED
EURO PROTOr:OL PREFIX
S
SYSTEM.SECURITY
CODE .000000
MAINTENANCE °,HISTORY
DISABLED
TANK CHART, SECURITY,
J D -1 SABLED
CUSTOM ALARMS
DISABLED
SERV 1CE' NOT ICE
DISABLED
ISO 3166' COU14TRY
CODE:
VAPOR_HONITORING TYPE
GARB, I SD
MASS /DENSITY,
DISABLED
FISCAL'HEIGHT SECURITY
DISABLED
INVENTORY ALARMS U14ITS
C014F I G : STANDARD
MAX OR LABEL: VOLUME
HIGH. PRODUCT'. %; MAX`
OVERFILL ,: X MAXDELIVNEEDED: P. MAX
LOW PRODUCT': VOLUME
ALARM REDUCTION!
ENABLED
COMMl1141CAT'IONS SETUP.
PORT SETTINGS':
COMM BOARD' 1 (RS -232).
BAUD' RATE, 1200'
PARITY_ : ODD
STOP BIT 1 STOP
DATA LENGTH: 7 DATARS -'M SECUR.1TY
CODE: DISABLED
COM1'BOARD, : 2 (EDIM )
RB -232 SECURITY
CODE 'DISABLED
AUTO TRANSMIT SETTINiZ
AUTO LEAK ALARM LIMITDISABLED -
AUTO: HI.Gh WATER LIMIT
DISABLED
AUTO OVERFILL LIMIT
DISABLED.
AUTO LOW. PRODUCT
DISABLED
AUTO THEFT LIMIT
DISABLED
AUTO DELIVER`; START
DISABLED
AUTO DELIVERY END
DISABLED
AUTO- EXTERNAL .INPUT ON
DISABLED
AUTO EXTERNAL INPUT OFF
DISABLED.
AUT.O.SENSOR FUEL ALARM
D,I,SABLED
AUTO 'SENSOR WATER- ALARM
DISABLED
AUTO.SENSOR OUT ALARM
DISABLED.
RS -232 END OF MESSAGE
DISABLED
I N -TANK SETUP T 2: PRE111,011 1
PRODUCT CODE 2' T 3:DlESEL
T I: REGULAR
THERMAL.COEFF :.00U700ITANK.` D I AMETER' ,98,.00. THERMAL ,COEFF s .000470
PRODUCT CODE I TANK :PROFILE" I .PT= TANK 96.00-
THERMAL COEFF :,000700 FULL VOL 3008 1 TANK PROFEL ' I PT
TANK DIAMETER 94,50 FULL VOL 3008.
TANK PROFILE 1 PTFULLVOL1200212002, FLOAT. SIZE: 4:0 IN.
WATER H I N I;MUM .0..000 FLOAT SIZE: 3.0 IN.
FLOAT SIZE : WATER WARN'i "NG 2.0 I JATER .M I N`1MUM" 0.000.
4 0 11VWATERM1NIIJUh10. [
N. z- HIGH WATER•.LIMIT -:: 3.0
FI
a WATER - WARNING 2.0WATER .ALARM LTER?: L,'Ou{ HIGH WATER. LIMIT : 3.0
WATER WARNING 2,0 4JATER ALARM FILTER.: LOW
HIGH WATER LIMIT:. 3,0WATERALARMFILTER: LOW III OR -LABEL
VOLUME 3008 MAX' OR 'LABEL
MAX OR LABEL HIGH PRODUCT; VOLUME 30Q8.
VOLU1hE 1 2002 MAX 90. 9 PRHIGHODUCT. GALLONS) 2707 Y.; MAX 90.1
HIGH PRODUCT GALLONS) 2707
MAX 90.1 OVERFILL ,L 11111 T
GALLONS) 10802 MAX ::,. 95. i OVERFILL LIMITI,GA.LLONS) 2Ba8 MAX 95.1
OVERFILL L 1r1 J,T GALLONS) 2,858
MAX 95,1 DELIVERY LIMIT
iGALLONS) 11402 V. MAX.: 15.1 DELIVERY LIMITGALLONS) 451 r f 5'. I
DELIVERY LIMIT LOW. PRODUi 'T,
MAX
GALLONS), :. 451
MAX : 15-.1GALLONS) 1 800 VOLUME :. 300: LOIJ ,PODUCF 'f-
LOW PRODUCT LEAK "-ALARM LIMM 99. VOLUME 300
VOLUME : 500 SUDDEN LOSS LIMIT: 99. LEAK. ALARM 'LI MI T : 99
TANK TILT' 0.00 SUDDEN LOSS LIMIT: 99
LEAK ALARM LIMIT: PROBE OFFSET 0.00 TANK TILT 0.00
SUDDEN LOST LIMIT.: 99 PROBE OFFSET 0.00
TANK TILT 0.00PROBEOFFSET0OQ SIPHON MAN,I;FOLDED• TANKS
T>t:''1VONE.,
FOLDED SIPHON;.MAN,1FOLDED TANKSLI,NE•MA.N1 TANKS 7q;. NONE
SIPHON MANIFOLDED TANKS To': NONE LANE MAN,1_FOLDED TANKSTO: NONE TO: N014ELINEMANIFOLDED:TANKSTO: NONE LEAK,MIN,PERIODIG:
0 LEAK ,M1 N .PER IODIC:: 0%
LEAK MIN PERIODIC: LEA *: MIN ANNUAL (r4 0
0 0 LEAK- ,MIN:ANNUAL 0%
0
LEAK III ANNUAL Q7. PERIODIC TEST TYPE. 0 STANDARD PERIODIC. TEST TYPE
PERIODIC TEST TYPE. ANNUAL TEST FAIL - STANDARD
STANDARD ALARM DISABLED ANNUAL TEST.FA "I'L,
ANNUAL TENT FAIL ERI OD l TEST; :FAIL ALARM'•DISABLED
ALARM - DISABLED ALARM D1SFiBLED PER I:ODIC TEST, FAIL
PERIODIC TEST .FAIL ROSS "TEST FAIL ALARM DISABLED
ALARM DISABLED ALARM 'D I SABLED GROSS, TEST FA 1',1:.
GROSS TEST FAIL, ANN' TEST AVERAG I NG.: ' OFF ALy i1?hl DISABLED
ALHRM;DISABLED P. ER TEST AVERAG 1 NG :; OFF ANN TEST AVERAGING: OFF
FINN TEST AVERAGING: TANK. TEST 'NOTIFY. OFF PER TEST AVERAGING: OFF
OFFPERTESTAVERAGING: OFF TNK TST S P'HON bl ?ip .:OFF TANK ,TEST' NOT 1 F`!: OFF
TANK TEST NOTIFY:' OFF DELI VERY• DELA! 1 -0. M I N TNK.TS'T•'SLPHON BREAK:OFF
TNK TST SIPHON BREAK :OFF PUMP'THRESHOLD 1,0;'00;:: DELIVERY DELAY : 10 M114
PUNP._THRESHOLD 10.00X
DELJVEkY DELAY :,10'MINPIMPTHRESHOLD
LEAK TEST METHOD
TEST WEEKLY :! ALL. TANK
SUN
START TIME : 2:00 AM,
TEST. RATE 0..20 ,GAL/HR
DURATION 2 HOURS -
TST EARLY STOP:DISABLED
LEAK TEST REPORT FORMAT"
NORMAL
PREFiSURE LINE-LEAK ETUP'
d I:REGULAR 1
TYP :2.Oi3.01N FIBERGLASS
2.01N DIA LEN: 139 FEET
3.01N DIA LEN: 139 FEET
SHUTDOWN RATE: 3.0 GPH -"
LOW PRESSURE SHUTOFF,' :NO
LOW PRESSURE O -PSI
T I:REGULAR
DISPENSE MODE:
STANDARD
SENSOR: 14ON- VENTED
PRESSURE OFFSET: O.OPS1,
1
MECHANICAL BLENDER: NO
0 2:PREMIUM,
TYP :.2.Oi3 ..01 N. F I BERr3LASS
2.01'N D i A LEN: 13`1 FEET
3.01 N D'1 A ,LEN.: 1:35 FEET
SHUTDOWN RATE: 3.0 GPH
LOW PRESSURE SHU_TOFF:NO
LOW PRESSURE 0 PS.1
T 2 : PRE11 I UM
DISPENSE MODE ".
STANDARD'
SENSOR: NON - VENTED
PRESSURE OFFSET:.O.OPSI.;
PECHANICAL BLENDER: NO
0 3:DSL t
TYP.:2:0 3:0 "IN FI:BERGI ASS2.a]14 DIA' LEN,: 04: EET
3 ..0,114 01 A LEN 94 ,FEET
SHUTDOWN RATE: 3:0 GPH-
LOW PRESSURE - SHUTOFF': NO
LOW. PRESSURE..:, 0—PSi'
T 3 :DIESEL ,
DISPENSE 'MODE:,
STANDARD'
SENSOR: NON - VENTEDPRESSUREOFFSET: 'O,-0PS1
MECHANI CAL .13[:>r,NDER : NO
LINE LEAK LOCKOUT SETUP
LOCKOUT SCHEDULE
DA1LY
START TIME : - DISABLED
STOP TIME' DISABLED
i LIQUID 'SENSOR 'SETUP
1.:87- TURBINEDWSUMP- "2 -I
CATEGORY STP SUMP
L.2:87 FiLL
DW SUMP; "2 -1CATEGORY 'PIP1, SUMP
L 3E9l. TURBINE
DW,SUMP 2 -1
CATEGORY STp.SUMP
L 4:91 FILL
DW SUMP, 2 -1
CATEGORY.: PIPING SUMP
L 5:DSL'TURBINEDW - SKIP 2 -1
CATEGORY P -1 PING SUMP
L-6 :DSL FILL
DW :SUMP- '2 -1
CATEGORY : Pl "PING SUMP
L ,7T: VENT
DW 'SUMP' 2 -1
CATEGOR;' : OTHER. SENSORS
L 9:D.ISP'1 -2' DW SUh10 2' -1 _
CATEGORY; : D'I SPENSER .PAN
LIO :DISP 3 -4
DW. SKIP 2 -1
CATEGORY :DISPENSER PAN
L'1 I : DI'SP. 5 -6
DW SUh1P, 2 =1
CATEGORY DISPENSER PAN
L12 :DISP, 7 -8_
DW SUMP,2 -1
CATEGORY-: DISPENSER PAN
sl3:FM 3 =4
CATEGORY AIR FLOW METER
s.1,4cFhf 5 -6'
CATEGORY AIR FLOW METER
51.5:FM 7 -8
CATEGORY AIR FLOW METER
s16:PRESSURE SENSOR
CATEGORY VAPOR-PRESSURE
ri
Q 2 : PREM I_UM` SMARTSENSOR .SETUP
OUTPUT RELAY SETUP I IN-TANK ALARMS
T 2,: LEAK 'ALARM... _ s 1:87 VENT
R 1.:OVERFI LL T 2 : COW'. PRODUCT- ALARM CATEGORY VAC .SENSOR
TYPE: - PUMP a:
STANDARD LIQUID SENSOR'ALMS Q'1 :REGULAR
NORMALLY' OPEN L 3: FUEL ALARM VOLUME: 25.3' GALLONS
L. 41FUEL ALARM' RELIEF VALVE: : NO
TANK 0: NONE L 9-:FUEL ALARM
LIO :FUEL .ALARM s 2.:87 VAPOR
L 1 1 :FUEL 'ALARM CATEGORY. VAC_ . SENSOR
IN -TANK: ALARMS L12: FUEL ,ALARM' PUMP o:
ALL:OVERFILL ALARM L I:SENSOR.;OUT ALARM Q !:REGULAR'
L 4 :SENSOR OUT - ALARM; VOLUME: -15:A GALLONS
L 9:SENSOR OUT ALARM RELIEF VALVE: NO-
L10:SENSOR OUT ALARM
LI`I :SENSOR! OUT ALARM s ;3 :87 PRODUCT
L12:SENSOR,OUT'ALARM CATEGORY VAC. SENSOR
L ' 3 : SHORT , AL:ARM ` PUMP 0:
L '4 :SHORT ALARM Q, ; l : REGULAR
L_9 :SHORT ALARM VOLUME: 32._0 GALLONSL10 :SHORT'AL:ARM RELIEF. VALVE: :'NO
L1'I:SHORT ALARM
L 12:SHORT ALARM s '4:87 ANNULAR
PLLD LINE DISABLE SETUP CATEGORY VAC`SENSOR
I _SITE,ALARMS" PUMP d:
1-SD GROSS-PRES FAIL I : REGUL•,AR ,
0 !:REGULAR ISD DEGRD PRES'FA1L
Q
rVOLOME: 32.0:GALLONS
ISD'VAPOR_ LEAK.FAIL RELIEF VALVE: :' NO
1N -TANK ALARMS
T i : LEAK ALARM J SD• HOSE ALARMS . s 5:91 .VENT'
T ):LOW PRODUCT +ALARM ALL:GROSS COLLECT FAIL CATEGORY VAC SENSOR
ALL : DEGRD, FAIL PUMP 0:
LIQUID SENSOR AUDIS
COLLECT'
ALL : FL014: COLLECT FAIL, Q .2 : PREh K UM
L 1:FUEL ALARM -. VOLUME: 25.1 GALLONS
L 2:FUEL ALARM Q. 3':.DSL RELIEF .VALVE:- : _NO
L 9:FUEL ALARM
LIO:FUEL ALARM 1A. -TANK ALARMS s 6:91 PRODUCT
ALLI1:FUEL ARM T 3: LEAK- ALARM CATEGORY VAC SENSOR
L IC" FIJI ALARM T 3 : LOW PRODUCT ALARM, PUMP P:
L I : SE;N _'. -k OUT ALARM ' Q 2; PREMIUM
L 2:SENSOR OUT ALARM LIQUID SENSOR ,ALMS• VOLUME: 30'.l.GALLONS
L 9:SENSOR OUT ALARM L 5 :FUEL - ALARM) RELIEF VALVE: NO
L 10 : SENSOR OUT- AL AI?M L 6 : FUEL ALARM
L 1 1 :SENSOR OU'I fa.ftiktl L10 : FUEL ALARM s Q: ATM .
L12:SENSOR; oUT iiLr•,RM. L1 I :FUEL -ALARM CATEGORY: -.ATM •P SENSOR
L I:SHORT ALARM L 5:SENSOR OUT,HL:ARM
L 2:SHORT ALARM L` 6 :BENSOR OUT 'ALARM 5,',g': DSL VENT.
L 9:SHORT ALARM L10,SENSOR'OUT -ALARM CATEGORY VAC SENSOR
LLO:SHORT ALARM L'1d :SENSOR OUT ALARM PUMP,d:
L1I:SHORT ALARM L SISHORT-ALARM Q 3::DSL
L12 :SHORT'ALARM L 6:SHORT ALARM VOLUME;: 25..3 GALLONS
LI.O:SHORT,ALARM RELIEF.VALVE: : NO
ISO SITE ALARMS fLII:SHORT ALARM
ISD GROSS PRES FAIL s10:DSL;PRODUCT, ISD
DEGRD PRES FATL CATEGORY 'VAC SENSOR
ISO VAPOR LEAK.FAIL PUMP,":
Q 3:DSL
ISO HOSE ALARMS VOLUME: 11.6'GALLONS
ALL:GROSS COLLECT FAIL RELIEF VALVE; : NO
ALL:DEGRD COLLECT.FAIL
ALL:FLOW COLLECT FAIL 511:DSL ANNULAR.
CATEGORY vH ' : L-msOR
PUMP 0,:
A ,3 : DSL
VOLUME: 32.0 - GALLONS
RELIEF.VALVE: : NO
a1,2 :fM 1 -2
CATEGORY. AIR FLOW METER
sl3:FM 3 =4
CATEGORY AIR FLOW METER
s.1,4cFhf 5 -6'
CATEGORY AIR FLOW METER
51.5:FM 7 -8
CATEGORY AIR FLOW METER
s16:PRESSURE SENSOR
CATEGORY VAPOR-PRESSURE
EVRi1SD SETUP
EVR.TYPE: BALANCE
BALANCE NOZZLE TYPE
VST
VAPOR PROCESSOR TYPE
NONE
ANALYSIS TIMES
TIME: 1.1:59 PM
DELAY MINUTES: 1
ACCEPT HIGH ORVR:
MAP
DISABLED
SERIAL NUM LABEL
1 58891 - - -
1SD HOSE TABLE
2 58886
ID FP FL HL AA RR
01 01 01 02 01 00
02 02 02 02 01 OG'
03 03 03 02 02 00
04 04 04 02 02 00'
05 05 05 02 03 00
06 06 06 02 03 00
07 07 07 02 04 00
08 08 08 • 02 04 00
ISD AIRFLOW METER MAP
ID SERIAL NUM LABEL
1 58891 - - - FM- 1 =2 - - --
2 58886 FM 3 -4
3 59646 FM 5 -6
4 58895 FM 7 -8
ISD FUEL GRADE HOSE MAP
1 .2 3 4
FP MHH MHH MHH MHH AA
01 201 901 101 U U 1
02 202 902 1"02 U U 1
03 203 903 103 U 'U '2
04 204 904 104 U U .2.
05 205 905 105 U U 3
06 206 906 106 U U 3
07 207 907 107 U U 4
08 208 908 108 U U, 4,
LABEL TABLE
1: UNASSIGNED
2: BLEND3
3: REGULAR
4: MID GRADE
5: PREMIUM
6: GOLD
7: BRONZE
8: SILVER
9: BLEND2
10: BLEND4-
D,ISPENSER.' ALARE. I:. M - - -- } ; ALARM 'HTSTOR;' REPORTt
COMMUN I CATION ALARMAPR' 24..2013 9.:33 AM E I:87 TURBINE.- --
1 STP ;SUMP
T T:REGULAR,..
I NVENTO ', 1'PICREASE
INCREASE,START
APR '24 -. 201-3 a 9-: '22 AM
VOLUME . 7084 -GAL9HEIGHT' 53,:97 'INCHES
WATER
0:75 INCHES
78':0 DEG'--F
1 NOREASE END
APR-24: 2013 9:33 AM
VOLUME _ 7264.4GALSHEIGHT. _ 55'..09. 1 NCHESWATER1. 77 1NCHESTEMP478.3'DEG F
GROSS INCREASE- l00TCNET1Nc;REASE. 176
ALARM HISTORY-REPORT
I,N —TAk ALARM - - - --
T'1•:REGULAR
r 1- n END X X x 3s w
x s END ,X .N
ALARM H,ISTQRY REPORT
SENSOR,ALARM'-----
L 2 :87 FILL
P I P.I NG SUMP
END
ALARM.HISTORY REPORT
SENSOR ALARM - - - --
L 3:91 TURB I IqE
STP SUMP
s ; .x END X X X ?i x
ALARM HISTORY REPORT
SENSOR ALARM - - - --
L 4:91 FILL
P I P•1 NG, SUMP
x x x x t END r x* x x
ALARM HISTORY'REPORT
SENSOR ALARM - - - --
L 5:DSL TURBINE
PIPINGiSUMP
xxx XENDxx - xx
ALARM HISTORY REPORT
SENSOR ALARM -
L 6:DSL FILL
PIPING SUMP
ALARM H I STORY REPORT
ALARM HISTORY REPORT - - - -- SENSOR ALARM ° - --
SENSOR ALARM - - -= + LI'I:DISP 5 -6-
L 7: VENT, j DISPENSER -'PAN
OTHER•SENSORS.
END
ALARM HISTORY REPORT
SENSOR, ALARM =-- --
L '9:DISP 1' -2
DISPENSER PAN
x x A x x END. N ,'x _x: X x
ALAR11 HI STOP.Y• REPORT
SENSOR ALARM-- -- ---
LI0:DISP 5 -4'
D I SPENSER, PAN
x ;o W x .x END r r_ W k,;( x ri x e 3. END rt x x x A
X, X' x m - x END *;rt x h, x
ALARM-HISTORY .REPORT
SENSOR ALARM - - - --
L-12:DISP ? =B` _
DISPENSER PAN:
x :x'i(kENDxx w A W
ALARM HISTORY REPORT
SENSOR ALARM - - - --
0.4:REGULAR
t
xxrxEND~rx .
ALARM HISTORY.REPORT
SENSOR ALARM - - - --
p 2:PREMIUM
cxxx'AE14DX 'A x #X
ALARM HISTOR`. REPORT
SENSOR ALARM
0 3:DSL
x x x,x END .A ii A 'A A
ALARM HISTORY REPORT
SMARTSENSOR ALARM --
s 1:87 VENT
x w x' END A; x x ),
a. ALARM .H I STORY :REPORT
SMARTSENSOR ALARM --
s - 2:,8 ?; VAPOR
SETUP, :DATA' WARNING
APR 23. .2013 3 :.11'1. Pll.
x * ^ x x EI4D x k- x x x
ALARM H'1 STOR`l' • REPORT
SHARTSENSOR ALARM --
s 3:87 PRODUCT
NO VACUUM ALARM
APR 23. 201.31c 1:25 ,PM
t
NO VACUUM ALARM
APR ,23. _2013' 3:1,2-'PM
NO VACUUM'ALARM
APR 23. 20.13 -3:.'i--1 'PM
3i -x t Z: X END .x 'X X
ALARM . H l S-rORY REPORT
SMARTSENSOR ALARM --
s 4 :67 ANNULAR
140 VACUUH ALARM
APR 24. 201'3 9:20.AM
140 VACUUM ALARM
APR 24• '201.3 - 6:46 AM
NO VACUUM ALARM,
APR -24. 2013 8•:43 -AM
ALARM Hi STORY REPORT
SMARTSENSOR -ALARM --
i- s:591 VENT,.
SETUP DATA WARNING"
APR: 23. 2013 '3:11 PM
N X)0 W X END x k*O H
ALARM HISTORY'REPORT
SMARTSENSOR ALARM --
s'6:91µPRODUCT
SETUP DATA•WARNING
APR -23, 2013 3:I1 PM
END x w x x x
ALARM HISTORY REPORT
SMARTSENSOR ALARM --
s 9': DSL VENT
NO VACUUM ALARM
APR. 23. 2013 3:11 PM
s j X 'k END. X ;. x x ;:
HAPPY GAS
ALARM H I STORY "REPORT' 4 3221, TAFT' HWY ,
BAKERS_F:IELD CA
SMARTSENSOR, ALARM. -- 933b3
s10 :D$L PRODUCT ; APR. 2.4,. 2013 = 10:06 AM
xxxxA END x9xX..x
ALARM Hi STORY 'REP,ORT
SMARTSENSOR ALARM. - -
sII:LSL ANNULAR
NO VACUUM ALARM
APR 23: 2013 5:1.6 PM
c x x x x END *.* x x .
HAPPY GAS
3221 TAFT HW`!
BAKERSFIELD CA
93313
APR 24, 2013 10:02.AM
SYSTEM'STATUS REPORT
ALL.FUNCTIONS NORMAL
DISPENSER ALARM - - --
E I. - ,
COMHUNI'CATION ALARM.
AP,R'2Q 201- 11.0:12,AM
PRESSURE' L -I NE LEAK-ALARM
6 1:REGULAR
PLLD SHUTDOWN;ALARM
APR '24. 201.3 10: 15.'AM.
SENSOR ALARM
L 1:87 •TURBINE .
STP 'SUMP'
FUEL'•ALARM
APR 24 2013 10:I51,AM
SENSOR ALARM
a -- SENSOR ,ALARM - - - --
L 5:DSL TURBINE,'
PIPING SUMP"
FUEL ALARM
J : APR: 24. 20,13 f_0 16 AM
SENSOR 'ALARM.:--- -
L 5:DSL TURBINE -
PIPING SUMP
LOW, L I CCU 1 D• ALARM
APR 24: 2013 '10:16.AM
PRESSURE LINE LEAK ALARM
0 2 c PREM 1 UM .'
PLLD.SHUTDOWN - ALARM
APR :24. 2013' 10: 11 AM
SENSOR ALARM - - ---
L 3 : 91 TURBINE
STP SUMP.
FUEL-ALARM
APR, 24, ' 20.13 1;0 : 17 AM
SENSOR ALARM
L 3-:'.91 ;TURBI NE
STP, 'SUMP
LOW'LIOUID ALARM
APR 24. 20.13.10 :17 AM
L_1 87 TURBINE
S`-S 'EM STATUS. REPORT STP': SUMP, `?-
LOW LIQUID ;ALARM
ALL-FUNCTIONS NORMAL APR 24.. 2013 10::15.f1M
PRESSURE LINE LEAK ALARM
W (:REGULAR
PLLi) SHUTDOWN ALARM
APR 24-:2013,10:.18 AM'
PRESSURE LINE,LEAR ALARM' -
QP 3 : DSL .
PLL:D ,SHUTDOWN •ALARM
APR 24. 2013` .1.0::1,6 NM
T
SENSOR ALARM - - - -- 1SENSORALARM - - - -- + L. 6:LiL FILLL2:87 FILL P 1 P 1 Nc:' Sump' PIPING SUMP FUEL-ALARM- FUEL ALARP) - y
APR 24. 2013 10: l8 AM APR. 24, 2013 10;20, AM
SENSOR ALARhI - - - -- PRESSURE LINE LEAK ALARM
L 2:87 FILL. Q 2 :,PREM 1 UI °)
PLLD SHUTDOWN ,ALARM
LOWTLGQU MPALARM APR 24 201"3 10:21 A14
APR 24: 2013 10:18.AM
SENSOR, ALAR11 . - - - --
PRESSURE LINE LEAK ALARM L 4:;91
h1r; ,
F1
0 3: DSL P I P l SUPM
PLLD-SHUTDOWN ALARM FUEL ALARM
APR 24, 2013 10:f9 AM APR 24. 201,3 70:21 kM
SENSOR ALARMSENSORALARM - -_-
L n : DSL FILL L 4 19 I. F!FLL
PIPING SUMP LOW LIQUID
SUMP
FUEL ALARM LOW LIQUID ALARM,_
APR 24;.2013 10:19 AM APR „24. 2013 10.2.1 HM
SENSOR ALARM SENSOR ,ALARIl - - - --
L 7: :VENT - L IDSL FILL 'OTHER! SENSORSPIPINGSUMPFUEI;'AL-ARM; LOW L I OU 1 D ALARM APR 24 . '2613 I 0:-22 AI-LAPR24, 2013 . 10:19 AM,
PRESSURE L I NE LEAK ALARM - - - -- SER8OR ALAR-11 - - - --
Q 3:6SL :L 7 tVENT
PLLD SHUTDOWN ALARM. OTI:IEP..SE11GORS
APR 24, 2013 10:20 AM LOW LIOUID'ALARM,
APR 24. 201.3 10 :26 'AM
P.RESSURE-.LINE. LEAK ALARM
Q (,.:REGULAR
PLLD SHUTDOWN ALARM,
APR '24 2013 10:27 AM
PRESSURE' L 1 NE LEAK ALARM
0 2':PREMlUll .
PLLD.SHUTDOWN ALARM
APR 24, 2013 10:27 AM
SENSOR ALARM
L 9:DISP l -2
DISPENSER PAN
FUEL ALARM
APR 24 2013.10:27 AM
SE1413OR ALARM
L 9:DISP 1 -2
DISPENSER PAN
LOW,LIQU1D,ALARM
APR 24, 2013 .10:28 AM
PRESSURE 'L l NE. LEA): ALARM
0 1'.: REGULAR
PLLD SHUTDOWN ALARM
APR 24, 201. 3.10:28 AM
1
PRESSURE LINE LEAK ALARM
0 2: PREhi YUM .
PLLD SHUTDOWN ALARM
APR' 24: 2013,..10:28 .AM
PRESSURE,LINE LEAK ALARMSENSOR _ALAi?M - - - -- ;.Q f :REGULARPRESSURELINELEAKALARM: LII:DIiSP 5-6. SHUTDOWN ALARM03: ESL A fSP.I;NSER PAN .- . APR 2q. •2013 10:37 AMPLLDSHUTDOWN-ALARM _ FUEL ALARM
APR 24, 2013,10:28 AN I APR,24: 2013 10:29 AM'
I,
PkESSURE'LINE LEAK. ALARM
SENSOR ALARM - - - -- - -- -- SENSOR ALARM - - - -- G 2:PREMIUM
LIO:D.ISP 3 -4 L11:DISP 5 -6' PLLD SHUTDOWN ALARM
DISPENSER PAN DISPENSEP, APR'24, 2013 10:37 AM
FUEL ALARM LOW LIQUID ALARM
APR 24. 2013 10:28 AM APR 24, 201.: 10:30 AM.
SENSOR ALARM - -- --
L 9:DISP 1=2
SENSOR ALARM - -_ -- PRESSURE ;LI1NE'_LEAK'ALARM DISPENSER PAN
L1D:DISP 3 -4 0 I:REGULAR SENSOR 020131 0:
DISPENSER PAN PLLD' SHUTDOWN ALARM APR 24. 2013 10 37 W1
LOW LIQUID ALARM APR,-24, 2013,"10"31 AJ
APR 24, 2013 10:29 AN
PRESSURE.LINE LEAK ALARM
PRESSURE LINE LEAK- ,ALARM W 3 : DSL
PRESSURE LINE. LEAK ALARM 0 2:PREMIUM PLLD SHUTDOWN ALARM
0 1:REGULAR PLLD.SHUTDOWN - ALOM APR 24, 2013.10:37 AM
PLED SHUTDOWN ALARht APR '24, 2013 10:31 -AM
APR 24 2013 10:29 AM
SENSOR. ALARM -- - --
SENSOR `HLaRN _ - - - =- LID DISP 3 -4
PRESSURE LINE LEAK ARM L12 :DISP 7 -8 DISPENSER PANLASENSOR. OUT ALARM02 :PREMIUM DISPENSER -PAN, APR 24': 2013 10:37 AMPLLDSHUTDOWNALARMFUELALARM
APR 24, 2013.10 :29'AM APR 24. 2013 1,0:31 Am
1I
SENSOR ALARM - - - --
PRESSURE LINE LEAK ALARM -- - -- SENSOR ALARM - - -- L'I1 :DISP;.5 -6 .
Q 3:DSL L12:DISP 7 -8 DISPENSER PAN
PLLD SHUTDOW14 ALARM D-ISPENSER. PAN' SENSOR .OUT ALARM
APR 24. 2013 10:29 AM LOW .L IGUI D, ALARM APP. 24 , 2013' 10:37 AM,
APR 24. 2013 10:31 AM
IN-TANX ALARM
T 3.:D.IOUT PRESSURE. LINE LEAN ALARMPROBEOUTU:I:REGULAR
SENSOR ALARM -- APR 24. X113 10:,4Q AM; ROSS .L' I NE FAIL
L 6:DSL FILL APR 24,'M13 10:58 AM
PIPING SUMP
SENSOR. OUT ALARM
APR 24, 2013 10:38 All
IN -TANK ALARM - - - --
T - i : REGULAR , -
SENSOR ALARM -" - --
SENSOR ALARM - - - -- f INVENTORY INCREASE
SENSOR ALARM -- - -- L 7 :VENT '' L12 DISP 7-8 OTHER SENSORS. INCREASE START.
DISPENSER.PAN SENSOR-OUT ;ALRRM APR. 24. 2013 1.0:40 AM
SENSOR OUT ALARM
APR 24. 2013 10;37 AM APR 24. 20I3.10:38:AO
VOLUME a 7273 GALS
HEIGHT o 55.1.6 INCHES
WATER - 0.00 INCHES
TEMP = 87. -5 DEG ;F
INCREASE ENDrAPR24, 2013 10:53 AM
SENSOR : ALARM - - --- VOLUME - 1.1119 GALS
SENSOR ALARM --- -- L 2 :87 FILL HEIGHT - 82.53 INCHES
L 5 :DSL TURBINE P'I PIING, SUMP WATER = 0.00 INCHES
PIPING SUMP SE08OR OUT ALARM TEMP = 87.6 DEG F
SENSOR OUT ALARM APR :24.- 2013 {10: 38 -AM iAPR24. 2013 10:372AI1
INCREASE END
APR 24, 20.13 10:36 Al"
GROSS INCREASE- 3846
TO. NET, INCREASE- 3771.
IN-TANX ALARM
T 3.:D.IOUT PRESSURE. LINE LEAN ALARMPROBEOUTU:I:REGULAR
SENSOR ALARM -- APR 24. X113 10:,4Q AM; ROSS .L' I NE FAIL
L 6:DSL FILL APR 24,'M13 10:58 AM
PIPING SUMP
SENSOR. OUT ALARM
APR 24, 2013 10:38 All
IN -TANK ALARM - - - --
SENSOR ALARM -" - -- T I :RE(;ULAR
L 3:91 TURBINE OVERFILL ALARM
5TP SUMP APR 24. 2013 10: 41 ,AM
SENSOR OUT ALARM
APR 24. 2013 10:38 AM
T 3:DIESEL'
INVENTORY INCREASE
INCREASE START
APR 24. -2013 10.:43 AM
VOLUME 230% GALS
IN -TANK ALARM - -r -- HEIGHT 68.87 INCHES
T (:REGULAR WATER '0.00 INCHES
SENSOR ALARM --- -- PROBE; 00T, TEMP 86.1 DEG F
L 4:91 FILL APR -24., 2013 16:41 AM.
PIPING SUMP
SENSOR OUT ALARM INCREASE END
APR 24, 20.13 10:36 Al" r, APR 24, 2013 10:55 AM
VOLUME = 2773 GALS
HEIGHT - 83.34 INCHES
WATER _ O.OG INCHES
TEMP a 86 -.2 DEG F
IN -TANK ALARM -- - --
T 3:DIESEL. GROSS . INCREASE- 464
OVERFILL ALARM TO NET•:INCREASE- 458
SENSOR,ALARM -'- -- APR 24,'2013-10:44 AK
L 1:87 TURBINE
STP SUMP
SENSOR OUT ALARM
APR 24. 2013 10:3Ei AM
t
IN-TANX ALARM
T 3.:D.IOUT PRESSURE. LINE LEAN ALARMPROBEOUTU:I:REGULAR
SENSOR ALARM -- APR 24. X113 10:,4Q AM; ROSS .L' I NE FAIL
L 6:DSL FILL APR 24,'M13 10:58 AM
PIPING SUMP
SENSOR. OUT ALARM
APR 24, 2013 10:38 All
PRESSURE LINE LEAK ALARM PRESSURE-LI:NE'LEAK' 'ALARM - -` SMARTSENSOR ALARM,- -
1Q' 3:DSG s :87' VENT
0 i:REGULAR NO VACUUM ALARM
PLLD SHUTDOWN ALARM PLLD :SHUTDOWN" ALARM APR 24, 2013.14:.39'AM.
APR 24, 2013 10:58 AM j APR 24. 2013. 1110 AM
T 2:PREMIUII - SMARTSENSOR ALARM --
1N -TANK ALARM --- -- INV:PREMI'
INCRIA6E s 1 87 VENT
T 2:PREMIUM HIGH_ LlOUID'ALARM
OVERFILL ALARM APR 24.201.3 11:34 AM
APR 24, 2013 i1:00 AM INCREASE START__
ApR'.24, 20.13 1.0:59 AM
VOLUME F 1978,GALSHEIGHT - .60.00'INCHE8
WATER e' 0.:00 jNCHES
TEMP 89.4 DEG'F
INCREASE END
IN-TANK ALARM - - APR , 24 , 2013, 1.1 : 1 1 AM
T BI UM VOLUME 2768-GALSPROBEOUTHEIGHT = 83.15,'1NGHE.SAPR24. 2013 I1:00,AM WATER - 0.00 INCHESTEMP, - 89.13; DEC' "F
GROSS INCREASE- 7.90
TC, NET -INOREASE=• 773
IN -TANK ALARM --- --
T 2:PREMIUM
LOW TEMP WARNI.NG
APR 24, 2013 11:01 AM
PRESSURE LINE LEAK .ALARM,
0 2:PREMIUM
GROSS LINE FAIL
APR 24, 2013 11:04'AM
SMARTSENSOR ALARM --
s 3:87•PRODUGT
NO VACUUM ALARM. APR24,. 201 3 11:34 AM
SI'1ARTSENSOR ALARM'--
s 2:87 'VAPOR''
NO VACUUM ALARM
APR 24. 2013 11:34 AM
PRESSURE LINE.L•EAK ALARM'
0 2 :PREMIUM
PLLD SHUTDOWN ALARM
APR 24. 2013 11:04,AM
SIYIARTSENSOR ALARM --
s 3: Q7• P.RODUCT
NIGH' L'IOU1Fi •ALARil
APR. 24 - '200 .11 : 34 AM
PRESSURE LINE LEAI( ALARM
0 3:DSL
GROSS LINE FAIL
APR 24. 2013 11 10 AM
4
HAPPY GAS
3221 TAFT HWY
BAKERSF I ELD CA
93313
APR 24, 2013,11:37 AM
SYSTEM STATUS REPORT
E I:COMMUNICATION ALARM
9 I:GROSS LINE FAIL .
0 1:PLLD SHUTDOWN.ALARM
C 2:GROSS LINE FAIL
G 2:PLLD SHUTDOWN ALARM
0 3:GROSS LINE FAIL
Q 3:PLLD SHUTDOWN ALARM
s ):NO VACUUM ALARM
3 2:NO VACUUM ALARM
s 3:NO VACUUM ALARM
INVENTORY REPORT
T I:REGULAR
VOLUME - 5299 GALS
ULLAGE = 6703 GALS;
901. ULLAGE-- 5502 GALS
TC VOLUME - 5255- GALS
HEIGHT - 42.90 INCHES
WATER VOL = 0 GALS
WATER - 0.00 INCHES
TEMP - 71.9 DEC F
T 2:PREM CUM
VOLUME 698 GALS
ULLAGE = 2110-GALS
90% ULLAGE- 1009 GALSTOVOLUME - 888 GALS
HEIGHT' - 32.53 INCHES
WATER VOL - 0 GALS
WATER - 0.00 INCHES
TEMP - ` 73.9 'DEG F,
T 3:DIESEL
VOLUME _ 900' GALS
ULLAGE. _ 2108 GALS
90% ULLAGE!- 807 GALS
TC VOLUME - 894 GALS
HEIGHT = 32:60 INCHES
WATER VOL - 0 'GALS
WATER - 0 -.00 INCHES
TEMP - 73.7 DEG F
A ii x x x E14D N ** x W
Sh1ARTSEN50R ALARM --
s 9.: DSL VENT .
P!0 ACUUVM ALARM 49 AMHAPPYGASAM24, 2013 1.1:
3221 TAFT• WY
BAKERSF I ELD• Cr:
93313
APR -24, _2013 11:41 AM
S`fSTEM `STATUS . REPORT
SMARTSENSOR ALARM. --
E 1 =1111IUN I CATION ALARM
l
G 4 : GROSS, L I.14E FAIL
s10:DSL PRODUCT
Or I:PLLD- SHUTDOWN ALARM
J NO- VACUUM ALARM ; AM
AP;R.24. 201,3 1L.45
HAPPY GAS
SYSTEM ;STATUS- REPOR`f -
3221 TAFT.HWY
E 1 : COhll`1UN I CAT.1(iN. ALARM
BAKERSF :I ELD CA
1:GROS9 LINE FAIL
1 :PLLD SHUTDOWN ALARM
93313
L) 2: GROSS: LINE FAIL
r, 2 ,.PLED .SHUTDOWNI ALARM
APR 24. 201,3 11:39 HM
3:GROSS LINE FAIL
SMARTSENSOR ALARM.'__
SYSTEM STATUS. REPORT t 10:DSL PRODUCT
NO VACUUM ALARMl :45 AME: I :COMMUNICATION, ALARhI APR 24. 2013 I
0 1iGROSS LINE FAtIL
Q" 1 :,PLLD - SHUTDOWN ,ALARM
G 2:GROSS-LINE FAIL
0,2:PLLD,SHUTD04JN ALARM
Q 3:GROSS LINE.FAIL SMARTgENSOR,ALARM --
0.3 :PLLD SHUTDOWN ALARM S g:pSL.VENT
HIGH LIQUID
APR 24, 2013 1l:
NLAR
6
s 2.:NO VACUUM ALARM
Sh1ARTSEN50R ALARM --
s 9.: DSL VENT .
P!0 ACUUVM ALARM 49 AMHAPPYGASAM24, 2013 1.1:
3221 TAFT• WY
BAKERSF I ELD• Cr:
93313
APR -24, _2013 11:41 AM
S`fSTEM `STATUS . REPORT
E 1 =1111IUN I CATION ALARM
l
G 4 : GROSS, L I.14E FAIL
HAPPY GAS
TAFT . 3221
AI'ERSF LELD ^,A
9331.3
Or I:PLLD- SHUTDOWN ALARM APR: 24, 2013;1 :50'AM
0 2 :GR0SS LIN FAIL
G 2:PLLD, SHUTDOWN 'ALARM SYSTEM ;STATUS- REPOR`f -
0. 3: GROSS * LI NE FA, I L, E 1 : COhll`1UN I CAT.1(iN. ALARM
G 3:PLLD SHUTDOWN NL iRhl- 1:GROS9 LINE FAIL
1 :PLLD SHUTDOWN ALARM
L) 2: GROSS: LINE FAIL
r, 2 ,.PLED .SHUTDOWNI ALARM
3:GROSS LINE FAIL
3 3:.PLLD' SHUTDOWN ALARM
SMARTSENSOR.ALARM --
s '9: DSL..VENT,. .
5.'9:NO VACUUM ALARM
NO VACUUM'ALARM
APR. -241. ,20.13 1'1 :45'AM
SMARTSENSOR.ALARM --
s 5:91 VENT
NO VACUUM ALARM
APR 24. 2013 1 l :'S3 ,AM
SMARTSENSOR ALARM -=
s 6:91 PRODUCT
NO VACUUM ALARM
APR 24. 2013. 11:53 -AM
SMARTSENbSOR:'ALARM --
s 6 :91 PRODUCT
HIGH LIQUID ALARM
APR 24, 2013 11:54 AM
SMARTSENSOR ALARM -
s 5 :91 VENT
HIGH LIQUID ALARM'
APR 24.. 2013 11:55 AM
SMARTSENSOR ALARM --
s 5:91 VENT
NO VACUUM ALARM
APR 24, 2013 11 :56 AM
SPIARTSENSOR,ALARM --
s 6:91 PRODUCT "
NO VACUUM ALARM
APR 24. 2013 11 :56 Ali
SRARTSENSOR "ALAP.W
elI:DSL'ANNULAR
NO VACUUM' ALARM , .
APR 24.. 20,13' 12:05 PM
SMARTSENSOR,ALARM --
s1, f ;.DSL "ANNULAR' '
N0. VACUUM ALARM
APR 24: t_2013 .12:05 PIN
SMARTSENSOR•'ALARM --
s 4:'87 ANNULAR
NO VACUUM ALARM
APR 24. '2013 12:08' PM
SMART: Liv:3GR' ALARM --
sl.1:DSLrANNUL•AE
HIGH'LIQUID°ALARM
APR. 24. `200.12• :.13 'PM
SMARTSENSOR ALARM
s'4:.87 ANNULAR
HIGH LIQUID ALARM
APR '24 2013 12:22 .PM
1 HAPPY GAS
3221 TAFT,HWY
BAKERSFIELD CA
93313
APR _24.. ,20;03' 12: 33 PM
SYSTEM STATUS REPORT
E 'I: COMMUNICATION ALARM
QA :GROSS LIME FAIL
Q J:PLLD SHUTDOWN ALARK
0 2: GROSS L 1 NE , FA I L
Q 2:PLLD SHUTDOWN ALARM
0 3:GROSS LI:NE'FAI
0' 3 : PLM SHUTDOWN, ALARM.
s 4:140 VACUUM.ALARM
5.11:NO VACUUM'ALARM
HAPPY GAS'
3221 TAFT HWY
BAKERSFIELD CA.
933.1.3.
APR: 24 2013, 12:.34 PM
SYSTEM STATUS REPORT
E L :COMMUNICATI'ON, ALARM
Q ,1:GROSS LINE, 1=AIL
0 1 :PLLD SHUTDOWN. ALARM
Q 2: GROS'S L I PIE FAIL
0 2:PLLD SHUTDOWN ALARM
3 -3:GROSS LINE FAIL
G' 3 : PLLD 'SHUTDOWN' ALARM
s 4: NO VACUUM`ALARM
s III :NO VACUUM ALARM
HAPPY GAS - -- SMARTSENSOR ALARM' -- 1 HAPPY' GAS
3221 TAFT HWY s 5:9C VENT'. 3221,TAFT HWY
BAKERSFIELD CA NO VACUUM ,ALARM BAKERSF.IELD CA93313 -APR :24. 2013 '.l 2:56 PM 9.3313 -
APR 24, 2013 12:37•'PM
SYSTEM STATUS,REPORT
E I:COMMUNICATION ALARM
s 4:NO VACUUM ALARM
s11:N0 VACUUM. ALARM
HAPPY GAS
3221 TAFT HWY
BAKER8F.1 ELD 'CA
93313
APR. 24, 2013 12:38 PM
SYSTEM STATUS.REPORT
a 4:NO VACUUM ALARM -
511:,NO VACUUM ALARM
SMARTSENSOR DIAGNOSTIC
APR 24. 2013 12:50 PM
s 5:91 VENT
VAC SENSOR.
SERIAL NUMBER 1.2370020COMPENSATEDPRESSURE:
6.227 PSIUNCOMPENSATEDPRESSURE:
EVACUATION STATE :4 PSI
VACUUM :OKFLUIDSTATUS: NORMALVCV: CLOSED
4 -24 -13 12:34PM
LEAK RATE: 3.468 GPHTIMETONOVAC:
0:181 HHHH : MM .
1-24-13 1.2 : 50PPI
EVAC RAT10:2.9 @ - 6.2PS1SENSORFAULTS:
NONE
SMARTStN,50R' b l'AGNOST I C
APR, 24. 20'13' 1 :O1.,PM
s 4 :87 .ANNU' t:AR
VAC SENSOR
SERIAL NUMBER 13030003
COMPENSATED, PRESSURE:
6.000 PSI
UNCOMPENSATED PRESSURE:
6.256r PSI.
EVACUATION - STATE:
EVAC ACTIVE MANUAL
FLUID ,STATUS'.- NORMAL
VCV :. OPEN'
4 -24 -13 '12:51PM
LEAK RATE: O:OOO GPH
Ti Mt TO' NO-VAC: -
0 :,00 HHHH:MM,
4 -24 -13 I:OOPM _
EVAC. RATIO: '10 e - 6.OPSj,
SENSOR FAULTS:
NONE
SMARTSEPSOR ,ALARM --
sII:DSL ANNULAR.
VACUUM .WARNI'NG
APR 14 2013 ':l :031, PM.
APR. 24 r -2013 1:12. PM
SYSTEM.:STATUS REPORT
ALL,FUNCTIONS NORMAL.
INVENTORY REPORT
T I:REGULAR
VOLUME - 5299.GALS
ULLAGE - 6703 GALS
90% ULLAGE- 5502 GALS
TC VOLUME- 5255 GALS
HEIGHT - 42.91' INCHES
WATER VOL - O GALS
WATER =. 0.00 INCHES
TEMP- - 71.8 DEG F'
T 2:PREMIUM
VOLUME 898 GALS
ULLAGE 21-10 GALS
90% ULLAGE_- 1809 GALS
TC VOLUME 888 GALS
HEIGHT' - 32.53 INCHES
WATER VOL 0 GALS
WATER• - 0.00'INCHES
TEMP 74.2 DEG F
T 3:DIESEL
VOLUME - 900 GALS
ULLAGE - 2.108 GALS
90% ULLAGE- 1807 GAES
TC VOLUME` 894 GALS
HEIGHT a 32.60 INCHES
WATER VOL -- ` 0 GALS.
WATER 0.00 INCHES
TEMP - 73`.7 DEG . F
END k x A
S lARTSENSOR. DIAGNOSTIC
APR 24, 2013 1:12.-PM
s.I: "87 VENT
VAC SENSOR
SERIAL NUMBER 13030002'
COMPENSATED PRESSURE:
7'. 196 PSI
UNCOMPENSATED PRESSURE
7.460 PSI
EVACUATION,STATE;
VACUUM OK
FLUID STATUS: NORMAL
VCV: CLOSED';
4 -24 -13 1:12PM,
LEAK RATE: - 0.031 GPH
TIME TO NO VAC.:
100-00 HHH_H:MM
EVAC RATIO: l; ,NOWW
SENSOR FAULTS:
NONE
s 2:87 VAPOR'
VAC SENSOR
SERIAL NUMBER 13030005
COMPENSATED PRESSURE:'
5.933 PSI
UNCOMPENSATED,PRESSURE:
6:198 PSI
EVACUATION STATE:
EVAC PENDING
FLUID STATUS: NORMAL,
VCV: CLOSED
4 -24 -13 1:12PM
LEAK RATE: 0.220 GPH
TIME TO NO VAC:
23:32 HHHH:MM
EVAC RATIO.: UNKNOWN
SENSOR FAULTS:-
NONE
s 3:67 PRODUCT
VAC SENSOR
SERIAL NUMBER 13030004
COMPENSATED PRESSURE: -, -
6.493 PSI
UNCOMPENSATED PRESSURE,:
76.758• PSI
EVACUATION STATE,:
VACUUM OK
FLUID STATUS: NORMAL
vCV: CLOSED
4 -24 -13 1:12PM
LEAK, RATE:. 0.020 GPH;
TIME TO NO' .VAC :
100:00 HHHH:MM
4 -24 =13 10:57AM
EVAC RATIO :I'.•7 - 6.6PSI
SENSOR FAULTS:
NONE
s 4,:,87' ANNULAR
VAC. :SENSOR.`_
SER i AL NUMBER' .- - 13030003
COMPENSATED - PRESSURE::_ .
3.%15 PSI
UNCOMPENSATEU'PRESSURE
EVACUATION: STATE:
EVAC 'PENDING._ , - .
FLUID. STATUS:" NORMAL
VCV: CLOSED
4-24 -1 ;3'' .I:12PM
LEAK RATE: 24.354 GPH
71 ME - TO Id0 VAC. : C. "I6 1•1HHH'MM
4-24,:713. 'I.1,01w" ._ :
EVAC ' RATIO :10:.;0 'q -6.. OPS
SENSOR ,- FAUL`T$:
NONE_ . , , . .
s 5: 91 TVErJ
VAC SENSOR,
SERIAL 'NUMBER 1,2370020
COMPENSATED VRESOURE: -
5:440_PS'1
UNCOMPENSATED,PRESSURE':
5.705' PST
EVAGUATION: STATE: —
EVAC PEND I,NG'
FLU1D'STATUS: NORMAL
VCV: CLOSED
4 -24 '- 1 3. _I c,1.1.PM -.
LEAK , RATEt 0...077 GP,H
T1 ME T.O 14.0 VAC: . 9,9 :45, HHHH:MM
4- 24-1`2 1.2 :50PM
EVAC' RAT_I.O : Z.9, U 6.2PSl;
SENSOR` FAULI`3
NONE
s 6-:91 PRODUCT
VAC .SENSOR.
SERIAL- NUMBER ! 1237062_I' '
COMPENSATED',;PRESSURE:
7.518 PSI'
UI400MPENSATED ,PRESSURE:
EVACUATION STATE.
VACUUM 0'K .
FLUID STATUS: NORMAL
VCV: CLOSED
4 -24-13 l .: 12PM.
LEAK.'RATE 0.163 GPH
TIME TO NO' VAC :
82 :05 HHHH:MM,
EVAC RAT10: UNKNOWN -
SEPISOR .FAULTS :
NONE
1 s 8; ATM
ATM. P •SENSOR
SERIAL NUMBER; 7259.
1ATM PRESSURE - 0.265. PSI
s -9. :`DSL VENT
VAC SENSOR
SERIALiNUMBER .,, 18B29
COMPENSATED;PRESSURE:
6.216 PSI
UNCOMPENSATED PRESSURE:
5.491 PSI
EVACUATI:ON•STATE:
VACUU11 OK,
FLUID :STATUS: NORMAL,
VCV : - CLOSED
4 -24 -13 1 :12PM
LEAK;RATE: 0.1.26 GPH
T I ME" TO NO VAC:
71:15 HHHH,:Mh1
4L24 -13 I0 19AM
EVAG RATIO.: 10 C 4.7PS1
SENSOR FAULTS:
NONE, -
sl,O:DSL PRODUCT
VAC. SENSOR
SERIAL NUMBER 13020010
COMPENSATED PRESSURE:
9.189 PSI
UNCOMPENSATED'PRESSURE:.
9 .•153, PS
EVACVATION.STATE,:.
VACUUM OK. FLUID STATUS: NORMAL
VCV,: CLOSED
4 -24 -13 1:1.1 PM
LEAK 'RATE:, 0.041 CPH
TIME. TO NO VAC:
100:00 HHHH:MM
EVAC, RATM: UNKNOWN
SENSOR FAULTS::
NONE
sIII ;DSL ANNULAR'
VAC. SENSOR -
SERIAL'NUMBER• 13020002
COMPENSATED PRESSURE:
7.756 PSI
UNrOMPENSATED-PRESSU,RE:
8.021 PSI
EVACUATION STATE:
VACUUM OX,
FLUID STATUS.: NORMAL
VCV.: CLOSED
4-24'—I,3 1 : 1 2PM
LEAK RATE: 7.127 CPH
TIME TG NO VAC:
2:04 HHHH':MM
4—,2,4'— 1 X 1 :OSPM-
EVAC RAT I..6:. 36@ —7.9PS l
SENSOR.FAULTS:.
NONE —
s12 :FM 1 -2
AIR FLOW-METER: '
SERIAL NUMBER 5BB51 HARPY'GAS
3221 'T,AFT' H41,`! BAKERSF'I ELD' CA
933113;
s 13 : FM 3 -4
APR, 24"r "2013 1:29 :PM
AIR ,FLOW METER
SERIAL NUMBER 58886
SYSTEM STATU?_REPORT
sl4:FM 5 -6. AtL FUNCTIONS NORMAL
AIR ,FLOW, METER INVENTORY REPORT
SERIAL NUMBER 59646
T !;:REGULAR 5300 GALE: VOLUME` "
sl5:FM 7 -9 U1,LAGE- . ° 6702; GALS
GALS
AIR FLOW METER:
90?4 ;UL' LAGS° 5501
TG 5256` GALS
SERIAL NUMBER 58895=
VOLUME
HEIGHT. m 42.. 91 INCHES
0 GAL 13WATERVOL
WATER ° 0.00 INCHEa
TEMP; Ti .8 IEr, F
s16 :PRESSURE SENSOR
VAPOR PRESSURE T 2:PREMIUM 898, GALSSERIALNUMBER12805VOLU19E: ° 21,10, GALSULLAGE• °
90%' ULLAGE- I11809 GALS,
TC= VOLUME 888 ;GALS
HEIGHT 53'1NCHES
WATER. "'VOL '- 0 .GALS
17NCHESWATER0.00
TEMP °: 74.2 'DEG 'F
T. 3 : Di ESEL 9f10 C;ALSVOLUME °
ULLAGE' ° 2100 GALS
Son ULLAGE° • 1,807 GALS,
TC VOLUME n' '894 GALS
HEIGHT 32.
E0
INCHES
WATER VOL 0 GALS.
0 I NCHE.S. WATER :0¢
TEMP a 73;.8.DEG F
x: END A ..x
rp
a
J
SWRCB, January 2006
Spill Bucket Testing Report Form
Thisform is intendedfor use by contractors performing annual testing ofUSTspill containment structures. The completedform and
printouts from tests (f applicable), should be provided to thefacility owner /operatorfor submittal to the local regulatory agency.
1. FACILITY INFORMATION
Facility Name: Happy Gas & Mini Mart Date of Testing: 4/24/2013
Facility Address: 3221 Taft Highway, Bakersfield, CA 93313
Facility Contact: Amita I Phone: 661 -831 -2323
Date Local Agency Was Notified of Testing: 4/23/2013
Name of Local Agency Inspector (fpresent during testing): Ernie Medina
2. TESTING CONTRACTOR INFORMATION
Company Name: Confidence UST Services, Inc.
Technician Conducting Test: Kristopher Karns
Credentials: Z CSLB Contractor x ICC Service Tech. 0 SWRCB Tank Tester Other (Spec)
License Number(s): CSLB# 804904 ICC# 5264406 -UT TT# 09 -1743
3. SPILL BUCKET TESTING INFORMATION
Test Method Used: x Hydrostatic Vacuum Other
Test Equipment Used: Lake Test Equipment Resolution: 0.0625"
Identify Spill Bucket (By Tank
Number, Stored Product, etc.
1 Regular 2 Super 3 Diesel 4
Bucket Installation Type: Direct Bury
x Contained in Sump
Direct Bury
x Contained in Sump
Direct Bury
x Contained in Sump
Direct Bury
Contained in Sum
Bucket Diameter: 12.00" 12.00" 12.00"
Bucket Depth: 12.50" 12.50" 12.25"
Wait time between applying
vacuum/water and start oftest: 5 min. 5 min. 5 min.
Test Start Time (Ti): 10:45am 10:45am 10:45am
Initial Reading (Rj): 10.00" 11.25" 10.75"
Test End Time (TF): 11:45am 11:45am 11:45am
Final Reading (RF): 10.00" 11.25" 10.75"
Test Duration (TF — Ti): 1 hour 1 hour l hour
Change in Reading (RF - Rj): 0.00" 0.00" 0.00"
Pass/Fail Threshold or
Criteria: 0.0625" 0.0625" 0.0625"
Test Results Ox. Pass 0 Fail D Pass Fail " t] ,Pass` ?` Fail° Pass Fail `
Comments — (include information on repairs made prior to testing, and recommendedfollow -upforfailed tests)
CERTIFICATION OF TECHNICIAN RESPONSIBLE FOR CONDUCTING THIS TESTING
1 hereby certify that all the Information contained in this report is true, accurate, and in full compliance with legal requirements.
Technician's Signature: , Date:_ 04/24/2013
State laws and regulations do not currently require testing to be performed by a qualified contractor. However, local requirements
may be more stringent.
Happy Gas & Mart
3221 Taft Hwy
Bakersfield, CA
4/24/2013
2= External Overfill Alarm
3= Emergency Shut Off Switch
4= Veeder Root ATG Probe
5= Veeder Root PLLD
6= Veeder Root 208 Sump Sensor
7= Veeder Root 420 Annular Sensor
8= Veeder Root 304 Sump Sensor
9= 12000 Gal. Regular STP Sump
10= Regualr Fill Sump
11= 3000 Gal. Super STP Sump
12= Super Fill Sump
13= 3000 Gal. Diesel STP Sump
14= Diesel Fill Sump
15= Vent Box
Comments: The Diesel and Super are
a Split tank and share one Annular.
2 * 6
Ll '#F1DFh LJ #FIDF
40 @ 40 C%
BUST= UST
4UC10 TIM, Job Order/ Invoice # go 689'
BUILD WITH CONFIDENCE'
Toll Free #: 1- 800 - 339 -9930 Da Call de Time 1017 Station Control Number Repair Da Invoice Date
3ai d
Name Confidence UST Construction Inc. Work performed at Station number: s
Street 16250 Meacham Road Street a a I T%> cuo
city Bakersfield, Ca 93314 City g St to ZipoJU
Total C Mileage
Terms M S tn 2Tl Store number:
Description of work performed:
bVICIAJ& M G i ,o Rll ESTr
Total Amount
Invoice A + B + C
m i . L Tour•
Labor
Date Name / Number Class Hours Hourly Amount
Arrived Departed Labor Travel Total
Handling %
Rate
Tax ( If applicable)
AM
Total B
May we please have your comments regarding service / equipment provided by the above named contractor:
Store Employee Printed Name
Store Employee Signature
PM PM
AM AM
PM PM
AM AM
PM PM
Employee Signature Date Vendor Signature Date
Contractor Supplied - Materials - Rentals Amount Sub -Total
Quantity
Total A Labor
Total B Material
Total C Mileage
Total Amount
Invoice A + B + C
Accounting Breakdown
Mileage
Miles Rate Total Sub Total
Handling %
Tax ( If applicable)
Total C Total B
May we please have your comments regarding service / equipment provided by the above named contractor:
Store Employee Printed Name
Store Employee Signature p
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