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INDIVIDUA' ANK/LINE/LEAK DETECTOR TE REPORT <br /> TEST DATE: 03/10/98 WORK ORDER NUMBER: 2203787 <br /> CLIENT: SHELL OIL COMPANY SITE: SHELL 204-7524-0402 <br /> Tank ID: 2 Material:STEEL Bottom to top fill in inches: 134.0 <br /> Product:PLUS Tank manifolded:No Bottom to grade fill in inches: 142.0 <br /> Capacity in gallons: 9,987 Vent manifolded:No Fill pipe length in inches: 37.5 <br /> Diameter in inches: 96.00 Vapor recovery manifolded:YES Fill pipe diameter in inches: 4.0 <br /> Length in inches: 323 Impact Valves Operational: Y Stage I vapor recovery: DUAL <br /> Tank age (years): Overfill protection: No Stage II vapor recovery: BALANCE <br /> Fuel pure rating: Overspill protection: No Installed: ATG <br /> COMMENTS CP installed on: <br /> Start m n in New/passed Failed/replaced New/passed Failed/replaced <br /> Dipped Water Level: L.D.#1 L.D.#1 L.D.#2 L.D.#2 <br /> Dipped Product Level: Make:vApoRLEss <br /> Probe Water Level: Model: LD2000 <br /> Ingress Detected: Water Bubble Ullage S/N: 32301 <br /> Test time: Open time in sec: 3.00 <br /> VacuTect Test Type: Holding psi: 16 <br /> VacuTect Probe Entry Point: Resiliancy cc: 150 <br /> Pressure Set Point: Test leak rate ml/m: 189.0 <br /> Tank water level in inches: Metering psi: 10 <br /> Water table depth in inches: Calib. leak in gph: 3.00 <br /> Determined by (method): Results: PASS <br /> Result: <br /> COMMENTS COMMENTS <br /> $ e5 pe: TLD <br /> g ' C D <br /> Material: STP FIBERG <br /> Diameter(in): 2.0 <br /> Length (ft): 80.0 <br /> Test psi: 50 <br /> Bleedback cc: 90 <br /> Test time(min): 30 <br /> Test 1: Start time: 12:01 <br /> Finish psi: so <br /> Vol change cc: 12 <br /> Test 2:Start time: 12;11 <br /> Finish psi: so <br /> Vol change cc: 3 <br /> Test 3:Start time: 12:21 <br /> Finish psi: so <br /> Vol change cc: o <br /> Final gph: 0.008 <br /> Result: PASS <br /> Pump type: PRESSURE <br /> COMMENTS Pump make: RED JACKET <br /> 8900 SHOAL CREEK, BUILDING 200,AUSTIN,TEXAS 78757(512)451-6334 Draft 03/11/98 14:46 MSHAW <br />