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INSTALL_2004
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2300 - Underground Storage Tank Program
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PR0521537
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INSTALL_2004
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Last modified
2/28/2020 10:41:34 PM
Creation date
2/27/2020 3:48:11 PM
Metadata
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Template:
EHD - Public
ProgramCode
2300 - Underground Storage Tank Program
File Section
INSTALL
FileName_PostFix
2004
RECORD_ID
PR0521537
PE
2371
FACILITY_ID
FA0014623
FACILITY_NAME
WEST VALLEY AUTO SERVICE LLC
STREET_NUMBER
2615
Direction
W
STREET_NAME
GRANT LINE
STREET_TYPE
RD
City
TRACY
Zip
95304
APN
21229017
CURRENT_STATUS
01
SITE_LOCATION
2615 W GRANT LINE RD
P_LOCATION
03
P_DISTRICT
005
QC Status
Approved
Scanner
KBlackwell
Tags
EHD - Public
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Ameron Dualoy° Pipe Monitoring System <br /> Based on these two tests the maximum combined brine level change for a <br /> temperature differential of 63 deg F was 0.37 inches or 0.0059 in/deg for the 21 ft test <br /> line. The worst-case condition, however, gives a change of 0.0076 in/deg. If the worst- <br /> case results are extrapolated to a 300 ft line with a temperature change of 30 deg F, the <br /> effect would be around 3.26 inches. <br /> The total temperature range of 63 deg F achieved in this evaluation far exceeds <br /> the range of temperatures that are expected for a typical service station. If the initial <br /> brine level is correctly set and the reservoir size is correctly designed, a level range of <br /> 3.26 inches should not be a problem. A high/low sensor spacing of 12 inches would <br /> require a level change of±6 inches in order to trigger an alarm. In addition, dual-point <br /> sensors can be custom designed to further minimize the probability of false alarm for <br /> any site. The manufacturer can design the reservoir to service a site of a defined <br /> length. The reservoir would then be suitable for any installation at or below the design <br /> length. <br /> Temperature Test With Trapped Vapor <br /> This testing was conducted with 300 ml of air trapped in the pipeline interstitial <br /> space. The same type of testing was conducted with the trapped air as was conducted <br /> for the pipeline without trapped air. <br /> Two tests were conducted with trapped air. These tests included the following. <br /> 1. One 2 hour circulation with cold liquid at constant temperature through the <br /> primary pipe; <br /> 2. One 2 hour circulation with hot liquid at constant temperature through the <br /> primary pipe; <br /> The first test involved circulation of cold water at a temperature of 32 Deg F <br /> through the primary pipe for 2 hours at a rate of 6 gal/min. The initial interstitial <br /> temperature was 70 deg F at the start of the circulation and decreased to 39 deg F. <br /> The results show a change in level from 7.94 inches to 7.56 in after 2 hours with a <br /> temperature change of 31 deg F. This effect is shown in Figure D-4 in Appendix D. <br /> The second temperature test involved circulation of hot liquid through the primary <br /> pipe at a constant temperature of 100 deg F for 2 hours with the brine reservoir level <br /> again measured at periodic intervals until a steady level was achieved. The interstitial <br /> temperature was at 66 deg F at the start of circulation and increased to 97 deg F after <br /> circulation. The initial brine reservoir was 7.78 inches at the beginning of the circulation <br /> and increased to 8.25 inches at the end of the circulation for a level change of 0.47 <br /> inches. The temperature change was 32 deg F. This effect is shown in Figure D-5 in <br /> Appendix D. <br /> Based on the two trapped air tests, the maximum combined brine level change <br /> for a temperature differential of 57 deg F was 0.69 inches or 0.0120 in/deg for the 21 ft <br /> test line. The worst-case conditions, however, resulted in a level change of 0.0148 <br /> Page 10 of 13 <br />
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