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COMPLIANCE INFO 2004 - 2006
Environmental Health - Public
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EHD Program Facility Records by Street Name
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2300 - Underground Storage Tank Program
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PR0231861
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COMPLIANCE INFO 2004 - 2006
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Last modified
10/20/2023 11:39:42 AM
Creation date
3/7/2019 9:33:42 AM
Metadata
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Template:
EHD - Public
ProgramCode
2300 - Underground Storage Tank Program
File Section
COMPLIANCE INFO
FileName_PostFix
2004 - 2006
RECORD_ID
PR0231861
PE
2361
FACILITY_ID
FA0003601
FACILITY_NAME
ARCO STATION #826951*
STREET_NUMBER
130
Direction
S
STREET_NAME
WILSON
STREET_TYPE
WAY
City
STOCKTON
Zip
95205-5561
APN
15502064
CURRENT_STATUS
01
SITE_LOCATION
130 S WILSON WAY
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
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The flow capacity of a piping <br />product is dependent upon several <br />factors including internal diameter <br />(I.D.) and Hazen -Williams flow <br />factor. The flow factors for FRP and <br />thermoplastic pipes are virtually <br />the same except corrugated systems <br />tend to have slightly greater <br />pressure losses. As a rule of thumb, <br />you can compute the internal area <br />of the piping system to compare the <br />flow capacity of different products. <br />The following chart shows the <br />internal area of different sized <br />products on the market. <br />Product Internal area <br />1.5" FLX 11 (1.5" I.D.) 1.77 int <br />2.0" Flex pipe (2.0a I.D. 3.14 int <br />2" Dualoy 3000/L (2.21" I.D.) 3.84 int <br />3" Dualoy 3000/L (3.32" I.D.) 8.66 int <br />Based on the above chart, the <br />following comparisons can be <br />made: <br />1.211 FRP has 117% greater flow <br />capacity than 1.511 flexible pipe <br />(3.84 int vs. 1.77 in') <br />2. 2" FRP has 18% greater flow <br />capacity than 2.0" flexible pipe <br />(3.84 int vs. 3.14 in 2). <br />3. 3t1 FRP has 176% and 389% <br />greater flow capacity than 2" and <br />1.5" flexible pipe, respectively. <br />4. 3" FRP has 126% greater flow <br />capacity than 2" FRP (8.66 int vs. <br />3.84 in). <br />Hazen -Williams Pressure Loss <br />Curves for different diameters of <br />Ameron products, like the picture <br />below, are available upon request <br />The chart is based on water, but can <br />be converted. to gasoline by multi- <br />plying the pressure drop by 0.82. <br />Looking at an example on the chart, <br />50 gpm gasoline flowing through <br />1,511 hose (83 psix 0.82) would lose <br />68 psi pressure over 1,000 feet. This <br />would equate to 6.8 psi per 100 feet. <br />One thousand feet of 2" Dualoy <br />3000/L with 50 gpm gasoline <br />flowing through it(12 psi x 0.82) <br />would lose 10 psi or 1 psi per 100 <br />feet, i.e. 85 % less pressure loss. <br />Given the same flow rate (50 gpm), <br />you can also see that the flow <br />velocity between the two sizes of <br />piping is vastly different. For the Flow Rimes <br />1.5" hose, 50 gpm must travel at <br />about 8.5 ftJsec. (turbulent flow) <br />and the 2" Dualoy 3000/L flow <br />would be less than 4 ftJsec. <br />H&ga yfjwmm Pressure Loss �saul m 2: <br />fl" shows 2500 gallons Pa rnlnirta DmS from the Inter- <br />aec6on of the 12 Inch nomliIaf pip. alze gree, It"."' <br />he prenure <br />lose h shown as 41 pal per 100o feet. To the right. folbwing Na slope of <br />the weer velocity Ones, 1M velodty is Indicated as 6.75 to* per second. <br />The pramrs loaf ter the entire One Is determined by multiptying 1M pres- <br />sure lose per 100 feet dmes the length of the line, divided by 1000 feet. <br />R ee Loy—PO. M P. sfun MN/j-w ' T,K <br />>P_ no N11..", MI <br />Ion <br />KL 411bnla 14"12- paa.tra rii'-"— QV O t2 <br />MUM1,114 The Manning equadan was empufcalfy developed for pipes of all shapes. <br />fug or partldy ful comisying water or sewerage. it Is used In most ODOR <br />channel flow caleulegons. <br />twae>r r <br />• • 1,••• vredn f1eM frw..eabl <br />s - "Y* -N ares 1feM ear r..o <br />(laminar flow). Certain fuel <br />products such as diesel fuel, should <br />not be pumped at excessive flow <br />rates because foaming will occur, <br />causing problems in the lines. <br />As a further example, it would not <br />be possible to substitute 1.5" or <br />even 2" flexible hose for 3" FRP in a <br />nigh volume operation such as a <br />`ruck stop. The hose could not <br />iupply the same volume of product <br />:o the same number of dispensers. <br />kt best, individual lines would have <br />:o be run to each dispenser which <br />vould increase cost drastically and <br />till have reduced flow at the <br />lispenser. <br />For more information, contact <br />Reid Van Cleave In the Houston <br />office. <br />Reference materiaL- <br />PipingFlowRate Design forRetm7 <br />Reftre181gFacMe5 <br />by Sullivan D. Curran, <br />Fiberglass 'Ink & Pipe Institute. <br />0 <br />
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