HomeMy WebLinkAboutUST-REPORT 12/1/2005If ~, ~ (ENVIRONMENTAL ASSESSMENT] - --"
('/ ~ CHEVRON STATION #98109 ~ +,
~ ~ 1131 OAK STREET
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8501 N. MoPac Expressway, Suite 400
Austin, Texas 78759
Phone: (512) 451-6334
Fax: (512) 459-1459
BAKERSFIELD FIRE DEPARTMENT
OFFICE OF ENVIRONMENTAL SERVICES
INSPECTOR STEVE UNDERWOOD
900 TRUXTUN AVE., STE. 210
BAKERSFIELD, CA. 93301
Test Date: 11 /21 /2005
Order Number: 3143833
Dear Regulator,
Date Printed and Mailed: 12/01/2005
Enclosed are the results of recent testing performed at the following facility:
CHEVRON 98109
1131 OAK ST. X/ST CALIFORIA AVE
BAKERSFIELD, CA. 93304
Testing performed:
Leak detector tests
Monitor Certification
Secondary Containment-Spill Container
Sincerely,
Dawn Kohlmeyer
Manager, Field Reporting
Tan
PURPOSE: COMPLIANCE
TEST DATE: 71/21105
CLIENT: CHEVRON PRODUCTS COMPANY
P.O. BOX 6004
L-237561
SAN RAMON, CA 94583
BRETT BONACCI
(925)842-5047
TANKNOLOGY CERTIFICATE OF TESTING
8501 N MOPAC EXPRESSWAY, SUITE 400 AUSTIN, TEXAS 78759
TELEPHONE (512) 451-6334 FAX (512) 459-1459
TEST RESULT SUMMARY REPORT
WORK ORDER NUMBER: 3143833
CUSTOMER PO: 4658495
SITE: CHEVRON 98109
1131 OAK ST. X/ST CALIFORIA AVE
BAKERSFIELD, CA 93304
MANAGER-JALED
(661)324-7621
Product Pi a Ti htness Test Results
LINE LINE LINE DELIVERY
TEST RESULT
iD PRODUCT MATERIAL NpE A B C D A
1 1 SIIPRSME DW FIBSRG PRSSSIIRS
2 2 PLIIS DW FIBSRG PRSSSIIRS
3 3 RSGIILAR DW FIBSRG PRSSSIIRS
4 4 DISSSL DW FIBSRG PRSSSIIRS
TEST TYPE: TLD-1
IMPACT
FINAL LEAK RATE (gph) VALVE
B C D FUNCTIO
LINE
ID MANUFACTURER MODEL # SERIAL # RESULT MANUFACTURER MODEL # SERIAL # RESULT
1 VSSDSRROOT SLSCTRONI 014690 P
2 VSSDSRROOT SLSCTRONI 001106 P
3 VSSDSRROOT SLSCTRONI 001095 P
4 VSSDSRROOT SLECTRONI 001107 P
New Replacement Line Leak DPter_tnr Test
REP LA ED LE° D TE 1 REPL ~~E K DE E T R'#2
LINE MANUFACTURER MODEL # SERIAL # RESULT MANUFACTURER MODEL # SERIAL # RESUL
ID
rvr owner oeeaneo repon miormanon, nsii www.eanicnoiogy.com aria se~ec~ vn-Lme xepons-wrcHC-, or contact your local ranimoiogy orrice.
Tester Name: PATRICK M PFRANG
~~
Technician Certification Number:1590
Printed 12/01/2005 08:02 SBOWERS
INDIVIDUAL TANK INFORMATION AND TEST RESULTS
i TanlQ~ology
TEST DATE:11/21/05 8501 N MOPAC EXPRESSWAY, SUITE 400 WORK ORDER NUMBER3143833
CLIENT:CHEVRON PRODUCTS AUSTIN, TEXAS 78759 (512) 451-6334 SITE:CHEVRON 98109
TANK INFORMATION
Tank ID: i i Tank manifolded: No Bottom to top fill in inches: 156. o
Product: sUPRErIE Vent manifolded: Yss Bottom to grade in inches: 161. o
Capacity in gallons: 9, b42 Vapor recovery manifolded: YES Fill pipe length in inches: 56. o
Diameter in inches: 91. oo Overfill protection: YES Fill pipe diameter in inches: 4 • o
Length in inches: 354 Overspill protection: YES Stage I vapor recovery: DUAL
Material: Dw FIBERG Installed: ATG Stage II vapor recovery: BALANCE
CP installed on: / /
COMMENTS
TANK TEST'RESULTS`Test MethGd: VacuTect LEAK DETECTOR TEST RESULTS Test mcthv~: FTA
Start (in) End (in)
Dipped Water Level: New/passed Failed/replaced New/passed Failed/replaced
Dipped Product Level: L.D. #1 L.D. #1 L.D. #2 L.D. #2
Probe Water Level: Make: vEEDERROOT
Ingress Detected: Water Bubble Ullage MOdel: ELECTRONIC
Test time: S/N: oi.cso
Open time in sec:
Inclinometer reading: Holding psi: 21
VacuTect Test Type: NoT Resiliency cc: NOT
TESTED
VacuTect Probe Entry Point: est leak rate ml/m: lag . o TESTED
Pressure Set Point: Metering psi:
Tank water level in inches: Calib. leak in gph: 3.00
Water table depth in inches: Results: PASS
Determined by (method):
Result:
COMMENTS
COMMENTS
LINE TEST RESULTS Test type: TLD-i
LINE A B C D
Material: DW FIBERG
Diameter (in): 3.0
Length (ft): 250.0
Test psi:
Bleedback cc:
Test time (min): NOT NOT NOT NOT
Start time: TESTED TESTED TESTED TESTED
End time:
Final gph:
Result:
Pump type: PRESSURE ,
Pump make: FE PETRO
COMMENTS Impact Valves Operational: UNKNOWN
Printed 12/01/2005 08:02
INDIVIDUAL TANK INFORMATION AND TEST RESULTS
,I- Tan
TEST DATE:il/21/05 8501 N MOPAC EXPRESSWAY, SUITE 400 WORK ORDER NUMBER3143833
CLIENT:CHEVRON PRODIICTS AUSTIN, TEXAS 78759 (512) 451-6334 SITE:CHEVRON 98109
TANK INFORMATION
Tank ID: 2 2 Tank manifolded: No Bottom to top fill in inches: 155. o
Product: Pzvs Vent manifolded: YES Bottom to grade in inches: 160. o
Capacity in gallons: 9, s42 Vapor recovery manifolded: YES Fill pipe length in inches: 55.5
Diameter in inches: 91. oo Overfill protection: YES Fill pipe diameter in inches: 4 • o
Length in inches: 354 Overspill protection: YES Stage I vapor recovery: DIIaz
Material: DW FIBERG Installed: ATG Stage II vapor recovery: BALANCE
CP installed on: / /
COMMENTS
TANK TEST=RESULTSTest Method:VacuTect
W _. LEAK DETECTOR TEST RESULTS Tesltnetho~~.FTA
.,,w_
Start (in) End (in)
Dipped Water Level: New/passed Failedlreplaced New/passed Failed/replaced
Dipped Product Level: L.D. #1 L.D. #1 L.D. #2 L.D. #Z
Probe Water Level: Make: vsfiDaRROOT
Ingress Detected: Water Bubble Ullage Model: anrcxROxxc
Test time: S/N: ooiioe
Open time in sec:
Inclinometer reading: Holding psi: z4
VacuTect Test Type: NOT NoT
Resiliency cc:
VacuTect Probe Entry Point: T ESTED Test teak rate ml/m: lag . o TESTED
Pressure Set Point: Metering psi:
Tank water level in inches: Calib. leak in gph: 3.00
Water table depth in inches: Results: Pass
Determined by {method):
Result:
COMMENTS
COMMENTS
__
LINE TEST RESULTS Test type: TLn-1
L1~1E A B C D
Material: Dw FIBERG
Diameter (in): 3.0
Length (ft): 250. o
Test psi:
Bleedback cc:
Test time (min): NOT NOT NOT NOT
Start time: TESTED TESTED TESTED TESTED
End time:
Final gph:
Result:
Pump type: PRESSURE
Pump make: FE PETRO
COMMENTS Impact Valves Operational: IINKNOWN
Printed 12/01/2005 0$:02
INDIVIDUAL TANK INFORMATION AND TEST RESULTS
~ Tan
TEST DATE: it/21/05 8501 N MOPAC EXPRESSWAY, SUITE 400 WORK ORDER NUMBER3143833
CLIENT:CHEVRON PRODUCTS AUSTIN, TEXAS 78759 (512) 451-6334 SITE:CHEVRON 98109
TAf~K I~tFORMATt2)N
Tank ID: 3 3 Tank manifolded: No Bottom to top fill in inches: 155.0
Product: REGULAR Vent manifolded: YES Bottom to grade in inches: 160. o
Capacity in gallons: 9, 842 Vapor recovery manifolded: YES Fill pipe length in inches: 55.5
Diameter in inches: 91. oo Overfill protection: YES Fill pipe diameter in inches: 4. o
Length in inches: 354 Overspill protection: YES Stage I vapor recovery: DUAL
Material: Dw FIBERG Installed: ATG Stage II vapor recovery: BALANCE
CP installed on: / /
COMMENTS
TANK TEST RESULTS Test P/lethod: VacuTec t LEAK DETECTOR'TEST RE5ULT5 Test method: FTA
Start (in) End (in)
Dipped Water Level: New/passed Failed/replaced New/passed Failed/replaced
Dipped Product Level: L.D. #1 L.D. #1 L.D. #2 L.D. #2
Probe Water Level: Make: vssnsRROOT
Ingress Detected: Water Bubble Ullage Model: sLSCTRONic
Test time: S/N: ooioss
Open time in sec:
Inclinometer reading: Holding psi: 21
VacuTect Test Type: NoT NoT
Resiliency cc:
VacuTect Probe Entry Point: T ESTED Test leak rate ml/m: 189. o TESTED
Pressure Set Point: Metering psi:
Tank water level in inches: Calib. leak in gph: s. 00
Water table depth in inches: Results: Pass
Determined by {method}:
Result:
COMMENTS
COMMENTS
LINE TEST RESULTS Test type: TLD-i
LINE A B C D
Material: Dw FIBSRG
Diameter (in): 3.0
Length (ft): 250. o
Test psi:
Bleedback cc:
Test time (min): NOT NOT NOT NOT
Staff time: TESTED TESTED TESTED TESTED
End time:
Final gph:
Result:
Pump type: PRSSSURE
Pump make: FE PETRO
COMMENTS Impact Valves Operational: UNxNOwN
Printed 12/01/2005 08:02
INDIVIDUAL TANK INFORMATION AND TEST RESULTS
i Tan
TEST DATE:11/21/05 8501 N MOPAC EXPRESSWAY, SUITE 400 WORK ORDER NUMBER3143833
CLIENT:CHEVRON PRODUCTS AUSTIN, TEXAS 78759 (512) 451-6334 SITE:CHSVRON 98109
TANK INFORiVIATIt7N
Tank ID: 4 4 Tank manifolded: No Bottom to top fill in inches: 155.5
Product: DIESEL Vent manifolded: No Bottom to grade in inches: 160.5
Capacity in gallons: 9, s42 Vapor recovery manifolded: No Fill pipe length in inches: 57 . o
Diameter in inches: 91. oo Overfill protection: YES Fill pipe diameter in inches: 4.0
Length in inches: 354 Overspill protection: YES Stage I vapor recovery: NONE
Material: DW FIBERG Installed: ATG Stage II vapor recovery: NONE
CP installed on: / /
COMMENTS
TANK TEST RESULTS Test Method:vacuTect LEAK DETECTOR TEST-.RESULTS rest method: FTA
Start (in) End (in)
Dipped Water Level: New/passed Failed/replaced New/passed Failed/replaced
Dipped Product Level:
L.D. #1 L.D. #1 L.D. #2
L.D. #2
Probe Water Level: Make: vasnsxROOx
Ingress Detected: Water Bubble Ullage Model: ELSCTROrrxc
Test time: SIN: ooiio~
Open time in sec:
Inclinometer reading: Holding psi: 21
VacuTect Test Type: NoT
Resiliency cc: NoT
VacuTect Probe Entry Point: T ESTED Test leak rate ml/m: 1s9. o TESTED
Pressure Set Point: Metering psi:
Tank water level in inches: Calib. leak in gph: s . 00
Water table depth in inches: Results: Pass
Determined by {method):
Result:
COMMENTS
COMMENTS
LINE TEST RESULTS Test type: TLn-i
LINE A B C D
Material: Dw FIBERG
Diameter (in}: 3 . o
Length {ft}: 250.0
Test psi:
Bleedback cc:
Test time (min}: NOT NOT NOT NOT
Start time: TESTED TESTED TESTED TESTED
End time:
Final gph:
Result:
Pump type: PRESSURE
Pump make: FE PETRO
COMMENTS Impact Valves Operational: UNKNOFTN
Printed 12/01/2005 08:02
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 monitoring svstem 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
Facility Name: CHEVRON 98109
Site Address: 1131 OAK ST. X/ST CALIFORIA AVE
Facility Contact Person: MANAGER - JALED
Make/Model of Monitoring System:TLS-350
B. Inventory of Equipment Tested/Certified
Check the appropriate boxes to indicate specific equipment inspected/serviced
Tank ID: T-1 SUP Tank ID: T-2 PLUS
X In-Tank Gauging Probe. Model: MAG X 1n-Tank Gauging Probe. Model: MAG
X Annular Space or Vault Sensor. Model: 409 Annular Space or Vault Sensor. Model: 409
~( Piping Sump/Trench Sensor(s). Model: 208 Piping Sumplfrench Sensor(s). Model: 208
Fill Sum Sensors
X p ()~ Model: 208
Fill Sump Sensor(s).
Model: 208
Mechanical Line Leak Detector. Model: Mechanical Line Leak Detector. Model:
Electronic Line Leak Detector. Model: PLLD X Electronic Line Leak Detector. Model: PLLD
Tank Overfill/High-Level Sensor. Model: EXTERNAL X Tank Overfill/High-Level Sensor. Model: EXTERNAL
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: - Tank ID:
X In-Tank Gauging Probe. Model: MAG In-Tank Gauging Probe. Model: MAG
X Annular Space or Vault Sensor. Model: 409 Annular Space or Vault Sensor. Model: 409
X Piping Sump/Trench Sensor(s). Model: 208 Piping Sump/Trench Sensor(s). Model: 208
~( FiII Sump Sensor(s). Model: 208 Fill Sump Sensor(s). Model: 208
Mechanical Line Leak Detector. Model: Mechanical Line Leak Detector. Model:
X Electronic Line Leak Detector. Model: PLLD Electronic Line Leak Detector. Model: PLLD
~( Tank Overfill/High-Level Sensor. Model: EXTERANL X Tank Overfill/High-Level Sensor. Model: EXTERNAL
Other (specify equipment type and model in Section E on page 2). Other (specify equipment type and model in Section E on page 2).
Ispenser 1/2 Dispenser ID: 7/8
OX Dispenser Containment Sensor(s) Model: 208 )( Dispenser Containment Sensor(s) Model: 208
X^ Shear valve(s). X Shear Valve(s)
Dispenser Containment Float(s) and Chain(s}. Dispenser Containment Float(s) and Chain(s).
Dispenser ID: 3/4 Dispenser ID: 9/10
X^ Dispenser Containment Sensor(s) Model: 208 Dispenser Containment Sensor(s). Model: 208
X^ Shear Valve(s). Shear Valve(s).
Dispenser Containment Float(s) and Chain(s). Dispenser Containment Float(s) and Chain(s).
DispenserlD: 5/6 DispenserlD:
Dispenser Containment Sensor(s) Model: 208 Dispenser Containment Sensor(s). Model:
^X 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 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): ~ System set-up XD Alarm history report
Technician Name (print): PATRICK M PFRANG Signature: ~~~~
Certification No.: 1862 License. No.:
Testing Company Name: Tanknology Phone No.: (800) 800-4633
Site Address: 8501 N. MoPac Expressway, suite 400, Austin, TX 78759 Date of Testing/Servicing: 11/21/2005
Page 1 of 3 Based on CA form dated 03/01
Monitoring System Certification
City: BAKERSFIELD
CA Zip: 93304
Contact Phone No: 324-7621
Date of TestinglService: 11/21/2005
Work Order Number: 3143833
Monitoring System Certification
Site Address: 1131 OAK ST. X/ST CALIFORIA AVE
Date of Testing/Service: 11 /21 /2005
D. Results of Testing/Servicing
Software Version Installed: 123.02
Complete the following checklist:
X Yes ^ No' Is the audible alarm operational?
O Yes ~ No ` Is the visual alarm operational?
O 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?
0 Yes ~ No ` NIA If alarms are relayed to a remote monitoring station, is all communications equipment (e.g. modem) operational?
Yes
~ No'
~ N1A 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) ^x Sump/Trench Sensors; ^x Dispenser Containment Sensors.
Did you confirm positive shut-down due to leaks 3tld sensor failure/disconnection? ~ Yes ^ No
Yes ~ No ` ~ N/q For tank systems that utilize the monitoring system as the primary tank overfill waming device (i.e.: no mechanical
overfill prevention valve is installed), is the overfill waming 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? so
Yes` ^x 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' XD 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.
OX Yes ~ No ` Was monitoring system set-up reviewed to ensure proper settings? Attach set-up reports, if applicable.
^X Yes ~ No ` 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:
Replaced syphon jet on 91 & DIE
Page 2 of 3 Based on CA form dated 03/01
Monitoring System Certification
Site Address: 1131 OAK ST. X/ST CALIFORIA AVE
Date of Testing/Service: 11 /21 /2005
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:
Q Yes ^ No • Has all input wiring been inspected for proper entry and termination, including testing for ground faults?
^x 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?
x Yes ~No • Were all probes reinstalled properly?
O Yes ~ No • 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) : ~ Check this box if LLDs are not installed.
Complete the following checklist:
0 Yes
^ No'
^ NIA 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 ~ 0.1 g.p.h ~0.2 g.p.h
x Yes ~ No • Were all LLDs confirmed operational and accurate within regulatory requirements?
x Yes ~No' Was the testing apparatus properly calibrated?
Yes ~No ~ ^x NIA For mechanical LLDs, does the LLD restrict product flow if it detects a leak?
^x Yes ^No " ^ NIA For electronic LLDs, does the turbine automatically shut off if the LLD detects a leak?
Q Yes ^No' ^ N!A For electronic LLDs, does the turbine automatically shut off if any portion of the monitoring system is disabled or disconnected?
^x Yes ^No' ~ NIA For electronic LLDs, does the turbine automatically shut off if any portion of the monitoring system malfunctions or fails a test?
Yes ^No " ~ NIA For electronic LLDs, have all accessible wiring connections been visually inspected?
Yes ^No' Were atl 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
SB-989 SECONDARY CONTAINMENT SUMMARY RESULTS
. Tanknology
TEST DATE:11/21/2005
CLIENT: CHEVRON PRODUCTS COMPANY
P.O. BOX 6004
L-2375B1
SAN RAMON CA 94583
BRETT BONACCI
925-842-5047
Tank Interstital Tests
TANK
PRODUCT MANUFACTURER RESULTS
WORK ORDER NO.: 3143833
SITE: CHEVRON 98109
1131 OAR ST. X/ST CALIFORIA AV8
BAKERSFIELD CA 93304
Piping Interstital Tests
LINE
PRODUCT MANUFACTURER RESULTS
Sump &Under-Dispenser Containment Tests
Sump/
DISP.#
MANUFACTURER
P/F
91 Phil-Tite Pass
89 Phil-Tite Pass
87 Phil-Tite Pass
DIE Phil-Tite Pass
representative: BRIAN DERGE
Services conducted by: PATRICK M PFRANG
~~!s~~
UMP TESTS y^
~~*~~~
SECONDARY CONTAINMENT TEST RESULTS Test Date:
Work Order: 11/21/2005
3143833
Type Tank or Disp
# Manufacturer Model or
Material Diam./Width/Length
(") Depth
(") Test Method Start
Time Initial
Level Level
Change Finish
Time Final
Result Pass/
Fail
Spill Container 91 Phil-Tite Plastic 11 x 10 10 1253 3 0 1353 3 Pass
Spill Container 89 Phil-Tile Plastic 11 x 10 10 1253 3 0 1353 3 Pass
Spill Container 87 Phil-Tite Plastic 11 x 10 10 1253 3 0 1353 3 Pass
Spill Container DIE Phil-Tite Plastic 11 x 10 10 1253 3 0 1353 3 Pass
Comments:
~ 7anlviology
8501 N MOPAC EXPRESSWAY, SUITE 400
AUSTIN, TEXAS 78759
(512)451-6334
FAX (512) 459-1459
TEST DATE:11/21/05 WORK ORDER NUMBE(3143833
CLIENT:CHSVRON PRODIICTS COMPANY SITE:CHSVRON 98109
COMMENTS
Performed monitor certification, lds, and spill buckets passed. Replaced the siphon jet valve on
the 91 and diesel.
PARTS REPLACED
QUANTITY DESCRIPTION
2 SIPHON JET A33EMBLIES
HELIUM PINPOINT TEST RESULTS (IF APPLICABLE)
ITEMS TESTED
HELIUM PINPOINT LEAK TEST RESULTS
Printed 12/01/2005 08:02 SBOWERS
ITE DIAGRAM
. ~n
8501 N MOPAC EXPRESSWAY, SUITE 400
AUSTIN, TEXAS 78759
(512)451-6334
FAX (512) 459-1459
TEST DATE: 11/21/05 WORK ORDER NUMBER3143833
CLIENT: CHEVRON PRODIICTS COMPANY SITE: CHEVRON 9 810 9
Chevron #98109 STP DSL ~`~~
1131 Oak St. A I
Bakersfield, CA 10K
93304 ~~
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Printed 12/01/2005 08:02 SBOWERS
. Work Order: 3143833
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Tanlaiology Inc. 8501 N. MoPac Expressway, Suite 400, Austin, Texas 78?59
Work~Order:
3143833
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