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San Joaquin Valley Unified Air Pollution Control District` <br /> Pressure Decay Test TP201.3 <br /> Confirmation No_: Testing Company: <br /> Permit No.: Address: - <br /> Site Name: r4 an�Lr••� L f.. ._ <br /> Address- 2 S, y.qm Te-r,s c Phone.- <br /> Phone: <br /> hone:Phone: <br /> Phase I System? 2 p,a/Coaxial Tanks Manifolded? <br /> Phase 11 System? a e Assist/Other: <br /> Total Number of Nozzles � <br /> Nozzles for Tank#1 Nozzles for Tank 93 <br /> Nozzles for Tank#2 J Nozzles for Tank#4 <br /> Balance"Nozzle End"hoses must be drained prior to test. Number of hoses over 100mi: <br /> Tank Information 2 3 4 ALL <br /> 1. Product Grade {7 �y <br /> 2.Actual Tank Capacity, gallons G/6 W% <br /> U. Gasoline Volume, gallons <br /> 4. Ullage, (v) gallons (line#2 minus line#3) <br /> Test Information 1 2 3 4 5 <br /> 5. Start Time f (4 <br /> 6. Initial Test Pressure, inches H2O <br /> 7. Pressure after 1 minute, inches H2O f <br /> 8. Pressure after 2 minutes, inches H2O <br /> 9. Pressure after 3 minutes, inches H2O <br /> 10. Pressure after 4 minutes, inches H2O <br /> 11_ Pressure after 5 minutes,inches H2O <br /> 12 Allowable Final Pressure <br /> 13, Pass/Fail (Enter"GF"for Gross failure) ;+L <br /> Nitrogen introduction point, Phase I vapor coupler or Phase 11 vapor riser. <br /> I > <br /> Record Vapor Coupler Integrity Test Assembly pressure after 1 - <br /> Type of pressure device used: 1�ic�lne Mianomnere- ar;r�ai ,-i <br /> p !�i�li�l- C,iL�Si�n t: i test <br /> I ��`fEnter Calibration date for pressures)device (90 days) <br /> — Enter initial tank uliage pressure (Vent if over 0.5 in.w.c.) <br /> Enter flowmeter rate, F (Must be 1 to 5 CFM) <br /> Enter calculated ullage fill-time-tz t2= V <br /> Enter actual fill-time [1522]F <br /> U Enter ending value of drift test(Must be 0.01 in,w.c. or less) <br /> Tester: t- e�f A f Tester 10: i t <br /> 1-. — <br /> Signature: � Test Cate; q /13 stct <br />