UPP Piping - Franklin Fueling Systems
Contents
1. Recommended Monthly Inspection Verify sump lids are tight and sealed Inspect sumps for dirt debris liquid or any physical cracks or holes that would allow leakage Check for evidence of staining or new staining Verify penetration boots are in good condition and the pipe entry into the sump is positioned properly near perpendicular entry Verify sump liquid sensors are positioned correctly if installed Verify the piping and other equipment in the sump are in good condition Record any faults on this Sump Inspection Register and have the fault s corrected at the time found Additional copies of this form can be downloaded from the FFS website www franklinfueling com End user proprietary inspection check register log formats or any form to record these inspections is acceptable Franklin Fueling Systems 3760 Marsh Rd Madison WI 53718 USA Tel 1 608 838 8786 800 225 9787 Fax 1 608 838 6433 e www franklinfueling com 10 Page Intentionally Blank 11 FFS 2011 408001016 Rev 1 e Franklin Fueling9 Systems www franklinfueling com 3760 Marsh Road Madison WI 53718 USA Tel 1 608 838 8786 Fax 1 608 838 6433 USA amp Canada Tel 1 800 225 9787 M xico Tel 001 800 738 7610 Brazil Tel 55 11 3395 0606 UK Tel 44 1473 243300 Franklin Fueling Systems Gmbh Rudolf Diesel Strasse 20 54516 WITTLICH Germany Tel 49 6571 105 380 Fax 49 6571 105 510 France Tel 49 6 57 11 05 380 China Tel 86 102. 8565 4566 Fax 86 10 8565 4766 A802 ChaowaiMEN Center No 26 Chaowai Street Chaoyang District Beijing 100020 China
3. to Table 1 for allowable bend radius of UPP Pipe Figure 8 Using Temporary Stakes to Snake Pipe Generally any thermal expansion will be accounted for by following our guidelines for spacing backfilling and ensuring runs are snaked Pipes should be separated from each other by at least the diameter of the largest pipe Important Completion Records On completion of UPP installation make an as constructed drawing showing the exact location of all below ground lines It is also recommended that fpipe runs cross each other they must be separated by in addition a photographic record is preserved at least as much backfill material as the diameter of the largest pipe or protected using at least 1 25 mm of Styrofoam Pipe Bend Radius Single Wall Pipe Temperature 4 32mm 4 50mm 2 63mm 3 90mm 4 110mm gt 59 F gt 15 C 1 ft 7 0 5m 2ft 6 0 75m 3ft 0 9 m 7ft 4 2 25 m 9ft 2 75 m 32 59 F 0 15 C 2ft 7 0 8m Aft 1 1 25m 5ft 2 1 58m 10ft 4 3 15m 12ft 8 3 85m lt 32 F lt 0 C 3ft 8 1 12m 5ft 9 1 75m 7ft 3 2 2m 13ft 2 4m 16ft 4 9 m Double Wall Pipe 1 1 1 2 2 3 4 40 32mm 63 50mm 75 63mm 110 90 mm 125 110 mm gt 59 F gt 15 C 2ft 0 6m 3ft 0 9m 3ft 8 1 12m 9ft 2 75 m 10ft 2 3 1 m Temperature 32 59 F 0 15 C 3 ft 3 1m 4ft 11 1 5m 1 88 m 6 ft 2 3 85 m 12ft 8 4 4 m 14 ft 5 lt 32 F
4. with soapy water to check for leaking Caution To avoid explosion hazards nitrogen or an inert gas from a pressure cylinder should be used in place of compressed air for tightness testing if fuel has been used to ballast underground storage tanks or if pipe work has previously contained petroleum Pipe work should be disconnected isolated from underground storage tank prior to commencing tightness testing e Any water used for testing should be disposed of through the oil water separator or by a specialist contractor and in accordance with any local environmental health and safety requirements and regulations There are three tightness testing methods suitable for use with UPP systems Pneumatic Vacuum and Hydrostatic any of these methods can be used to prove the tightness of a line Tightness testing using a Hydrostatic method is suitable for testing at high pressures The UPP pneumatic and vacuum tightness tests should both be carried out to ensure confidence in the installation at lower pressures UPP Recommended Pipe Test Procedure During the test period of 90 minutes the pressure Primary Pipe Hydrostatic Pressure Testing should be recorded with the frequency shown below Method Test period Frequency of Number of Equipment mins readings mins readings e Hydrofor reservoir or pressure tank 10 30 Two pressure gauges rated for 174 psig 12 bar min 30 90 DM reading 2 psig 0 1 bar Table 2 Recording Tes
5. 0 C Aft 7 1 4 m Tft 3 2 2m 8ft 6 2 6m 16 ft 4 9 m 18 ft 4 5 6 m UL971 Pipe 2 3 11 2 2 3 4 63mm 90mm 63 50mm 75 63mm 110 90mm 125 110mm Table 1 Allowable Bend Radius Temperature Pipe Detector Tape UPP Detectable tape is used to allow the piping location to be found after it has been covered The tape is installed below ground at 9 8 inches 250mm height directly above pipe runs to indicate the position of each pipe Detector Tape Max Depth Detection 3 m Pea Gravel or San 250 mm Subsoil ULT YS UPP Pipe Figure 10 Detector Tape Installation Both ends of the tape should be grounded during installation End of Tape Must be Grounded in Sumps Figure 11 Detector Tape must be Grounded When using a detection tool the near end of the detectable tape should be disconnected from the grounding point to allow the red cable from the transmitter to be connected to the tape and the black cable from the transmitter to be connected to the grounding point The far end of the tape should remain grounded to give the highest signal strength and the earth spike should be as far away from the trace path as possible at a 90 degree angle Use the lowest frequency possible from the transmitter around 577 Hz or 8KHz to eliminate coupling to other grounded cables Use the receiver to follow the path of the tape to locate the buried pipe Follow dir
6. bags of sand or pea gravel or use the hook end to your advantage when turning direction into a chamber or pump sump Site Preparation Site inspection Make sure the site is prepared and ready The tanks and sumps should be in place IMPORTANT The site should be free from previous fuel contamination Pipe Burial Guidelines Recommended burial depth of UPP pipe is a minimum of 12 300 mm All trenches should be sloped back towards the storage tanks The fall back slope for all pipework to the tank chambers should be a minimum of 1 8 per foot or 1 m every 100 m Figure 7 This may vary to meet local requirements The position of the entry fittings at the furthest dispenser sump away from the tank chambers may be considerably higher than that of the entry fittings on the closest dispenser sump Vapor return lines should have a slope of 1 4 per foot and never less than 1 8 per ft back towards the tank farm unless in line joints such as elbows are to be used Trench corners should have a radius of 5ft 1 5 m A recommended 6 15cm bed of backfill material should be laid underneath the pipe prior to installation and there must never be voids under or around the pipe Acceptable backfill materials are Well rounded pea gravel size 1 8 3mm to 3 4 20 mm Crushed rock size 3 4 3mm to 16mm Clean washed sand e Backfill material must not be contaminated with any petroleum product or other contam
7. different applications and to meet various engineering and legal requirements e UPP Extra lined primary pipe with 100 nylon barrier for product suction pressure vapor vent and fill lines e UPP Integral Secondary Containment pipe for pressure systems or environmentally sensitive sites UPP electrical conduit pipe for underground electrical wiring protection UPP piping systems are designed in various diameters from 32 160 mm l 6 for the transfer of fuels in filling station fore courts marinas and airports UPP systems are also used for government and military installations as well as many industrial sites such as mines and rail depots There is no requirement for a concrete trench because fusion welded HDPE pipe is structurally resistant to weight of backfill material and dynamic traffic loads Over 20 years experience show no failures in underground fuel pipe systems and no loss into the ground Underground Fuel Pipe Construction Black outer structural layer of the pipe is High Density Polyethylene HDPE grade PE80 or PE100 which allows the use of electrofusion couplers and fittings to construct a variety of pipeline configurations HDPE PE80 and PE100 has well proven resistance to stress cracking puncture scratch impact microbial and rodent attack The intermediate layer is a tie layer adhesive which permanently bonds the polyethylene layer to the barrier layer The yellow inner barrier layer of UPP Ex
8. e Franklin Fueling Systems UPP Piping Installation Guide Overview Franklin Fueling Systems 3760 Marsh Rd Madison WI 53718 USA Tel 1 608 838 8786 800 225 9787 Fax 1 608 838 6433 www franklinfueling com Safety Important UPP Systems must only be installed by fully trained and certified installers Failure to follow installation instructions will invalidate warranty and installer certification Piping Installation Safety UPP Welding Units must never be operated in Zone 1 or Zone O areas Hazardous area definitions are from IP Model Code of Safe Practice Part 15 and are available in the APEA Blue Book 2nd Edition Ensure Welding Units are connected to a power supply that meets the requirements detailed in the user manual and are within the requirements of any local authority or regional legislation Important to any type of piping system is to safely connect all metallic components to ground Metallic components and more general conductive materials due to their high capacitance can have the potential to store high amount of electrostatic energy sparks discharge can only be observed over conductive elements All exposed metal parts used in UPP System installations should be adequately grounded to a dedicated earth electrode and brought to a potential equal to that of other metal parts in the close proximity Chemical Safety Where using chemicals such as Acetone during the installation of UPP syste
9. ection included with the receiver and transmitter for detecting buried pipe location Pressure Testing Following inspection and prior to backfilling a tightness test should be carried out by a competent person on each pipe run chamber and sump to verify the integrity of joints and seals This testing should meet the requirements of local officials and engineers and comply with local health and safety regulations The following testing procedure is suggested for guidance only and should in no way override oil companies or local regulator s requirements Testing Guidelines Equipment Target test pressure should be 5096 of scale on gauge e g if the test pressure is 14 5 psi 1 Bar use a 29 psi 2 Bar gauge Gauges should have serial numbers and be tested certificated yearly Pressure testing equipment should have fitted a relief valve set at around 7 25 psi 0 5 bar above the test pressure General Guidelines e When applying pressure from gas cylinders use suitable valves to ensure test pressure is not exceeded e Apply pressure or vacuum slowly to minimise risks e When tightness testing primary pipe the secondary should be open to atmosphere this is critical whenever secondary pipe is filled with liquid Secondary pipe should ideally not be welded prior to testing primary to allow inspection of joints e When tightness testing secondary pipe the primary should be open to atmosphere Wipe each joint
10. for use This is particularly important for electrofusion fittings These must be kept in their packaging until ready for use to prevent any contamination or oxidation Uncoiling Pipe Figure 4 Uncoiling Pipe The pipe can straighten with considerable force Take care when releasing pipe from the coil and secure the straightened pipe Let the pipe rest in its uncoiled state for about eight hours High ambient temperatures can reduce this layout time and low temperatures may increase it Pipe can be laid in its final position to relax before connecting up Caution You need at least two people to uncoil and cut the pipe The coil is taped up in layers to make it easier to uncoil at manageable intervals e The area in which the pipe is uncoiled on site must be clear safe and free of sharp objects Remove the tape around the tail end on the outer winding and secure this end e With the coil in the vertical position roll the coil out cutting and removing tape as you find it ensuring to release only the next turn of pipe in the coil e Do not drag the pipe The natural curves from coiling can be used to change pipe direction and bags of sand pea gravel or stakes can be used to hold it in place until it is ready for connecting One person should hold the pipe whilst another cuts it to the desired length he cut ends will have a prominent hook that can be partially removed when weight is placed on it
11. inant N 1 300mm min 3 12 150mm min 6 150mm min n a 6 Figure 5 Pipe Spacing When laying duct onto a concrete base a 6 150mm thick bed of compacted sand should be laid on the concrete below the duct The minimum amount of sand should be 2 50mm of compacted sand All beds should be laid so that the pipe will not dip or sag when it is installed Laying of pipe should start from the tank farm Underground pipe runs may be continuous or have electrofusion welded joints Any mechanical joints or compression fittings must be located within a containment chamber or sump Welding Connectors Heating Element Figure 6 Electrofusion Welded Fitting Detail Refer to manual FFS 0123 for information about the electrofusion process Figure 7 Fall back slope to Tank UPP pipe exceeding 12m 39ft should be laid in a e f used above ground UPP pipe should be protected series of large snake like curves and not in straight lines against mechanical climatic damage Additional Uncoiled pipe when laid will settle in a natural curve supports and anchor points may also be required Check fire codes for proper installation e Mark positions on the tank access chamber sump for penetration locations and install UPP seals gt Bend Radius The UPP piping systems have a semi rigid construction NG which gives both strength and flexibility ath EER X Ka _ Figure 9 Bend Radius NE Refer
12. ms products be sure to follow all safety guidelines given on the chemical containers themselves or on any accompanying literature Confined Space Some installation of UPP products may occur in confined spaces where a lack of oxygen and a concentration of toxic vapors is likely to be experienced Such working conditions are dangerous and all local health and safety guidelines for working in such environments should be followed Material Handling Protective Equipment Ensure the correct personal protective equipment PPE is used at all times in line with local health and safety requirements Material Safety Data Ensure all safety data is accessed and used while installing UPP Systems Material Safety Data Sheets are available in the download area of the UPP website Transport amp Storage UPP products should be transported and stored in accordance with the guidelines contained in this manual Heavy items Heavy items should be handled using suitable lifting equipment operated by authorised personnel Transit On loading and Storage Uncoiling Pipe Site Preparation Pipe Bend Radius Completion Records Pipe Detector Tape Pressure Testing Testing Guidelines 7 UPP Recommended Pipe Test Procedure Hydrostatic Pressure Testing Method Sump Inspection Register Introduction Underground Fuel Pipe Systems Several types of underground fuel pipe are available for
13. t Results Check valve e Ball valve The test is passed if all the readings during the testing cycle are 43 5 psi 3 bar or above Decreasing readings failure of pressure test Note that the readings are likely to increase Pressure relief valve rated for 290 psig 20 bar set at 159 psig 11 bar Conditioning Phase Fillthe pipe work system to be tested with water making sure that any air relief valves are opened while filling the pipe work e After filling the pipe work wait 1 hour for the temperature to stabilize e When the failure point has been located and remedied repeat the full conditioning and testing sequence e Ifthe system fails the pressure test make the following checks e Check all mechanical connections Check welded joints Pressurize the system to 145 psi 10 bar and maintain this pressure for 30 minutes System pressure shall be maintained by means of refilling in order to compensate for the increase in volume due to the expansion of the pipe work At this time the system should be thoroughly inspected for leakage After any such areas have been remedied repeat the conditioning before proceeding to the testing phase Testing Phase Rapidly reduce the system pressure to 43 5 psi 3 bar by bleeding water from the pipe work Due to the visco elastic properties of polyethylene the pipe will contract Pressure PSI bar 0 10 20 300246810 15 20 25 30 40 50 60 70 80 90 Condi
14. tioning Time mins Test Reading Times mins Hydrostatic Testing Graph UPP Pneumatic Tightness Testing Method Procedure Refer to ASTM International Document F2786 10 for overall pneumatic testing information Test Pressure e 50 PSI 3 5 bar for pipe up to 2 Use operating pressure for Piping Fittings over 2 When testing secondary pipe terminated with flexible boot pressure test at 0 5 bar 7 psi for 30 minutes following a 15 minutes conditioning at test pressure Never exceed the maximum pressure rating table 5 Record Temperature and Pressure at start of each test time Condition the piping as below 1 Pressurize the piping to 10 of test pressure Hold pressure for 30 minutes and inspect for leakage or pressure drop 2 Increase pressure to 50 of test pressure and again inspect for leakage while holding pressure for 30 minutes 3 Increase pressure to 100 of test pressure and again inspect for leakage while holding pressure for 30 minutes e Record Temperature and Pressure at end of each test time fresults are within criteria of Table 3 Tightness Test is passed Pressure Testing Safety Follow these guidelines when doing pneumatic testing Wear Safety glasses Relieve air pressure at the completion of each test phase and before any corrective actions are taken Never exceed the pressure rating of components when testing Allow only necessary and authorized persons in the proximit
15. tra pipe is specially formulated fuel proof barrier layer which has exceptional resistance to absorption and permeation of both gasoline and alcohol fuel blends The smooth bore and low friction loss of UPP pipe permits higher fuel and vapor flows when than steel pipe reducing the pumping energy costs UPP underground fuel pipe is pressure rated to 90 psi 6 2 bar according to UL971 Rupture pressure is typically exceeding 580 psi 40 bar providing a large margin of safety Carrier PE Black Tie Layer Liner Nylon Yellow Figure 1 UPP Pipe Structure Figure 2 Installation Overview Transit On loading and Storage Although UPP polyethylene pipe and fittings are extremely hard wearing and resilient it is important to handle and store them with care to prevent scuffing or gouging Any damaged pipes may need to be rejected and not installed UPP products should be transported in a flat bedded vehicle free from sharp objects and projections Wide polypropylene slings must be used when lifting pipe crates by crane Avoid using chains hooks or hawsers A spreading beam should be used when lifting crates containing pipe lengths greater than 19 ft 8 6m Allow for a slight bending of the pipe crates when on and off loading Standard 19ft 8 6m crates may be moved using a forklift A side loader fitted with a minimum of four supporting forks should be used for longer lengths Otherwise use a crane fi
16. tted with a spreader beam e When using a forklift to on or off load coils the forks should be covered to avoid damage to the coiled pipe Figure 3 Moving Coils Storage on site Individual pipe lengths should be stacked not more than 3ft 1m high with the bottom layer fully restrained by wedges The bottom layer of pipes should be laid on timber battens at 3ft 1m centres to avoid any damage from sharp objects lying on the ground Pipe crates should be stored on clear level ground and should never be stacked more than three crates high Coils should be stored on firm level ground that has suitable protection for the bottom of the coil Stacked coils should never exceed three coils high Individual coils should be stacked flat If stored on edge they must be secured against a properly anchored support and stored like this for a short period of time only particularly in warm weather conditions e Badly stacked coils and pipe lengths can slip causing personal injury or damage to the product Facilities for safe lifting and moving must be available Pipes are supplied with distinctive colored end caps to prevent entry of any contamination These end caps must be kept in place during storage e UPP fittings all electrofusion fittings are packed in heat sealed polyethylene bags and delivered in cardboard cartons Fittings should be stored in their packaging and in a dry area away from direct sunlight until ready
17. y of pipe being tested Restrain the movement of connections joints and seals during testing Acceptable Pressure Variation Vacuum Testing Pneumatic Vacuum Tightness Testing Type of Test Conditioning Test Vacuum Test Time Mins Tank Chamber 3 mins 2x 30 mbar 0 44 7 Dispenser Sump Test Vacuum psi 3 kPa Spill Container 3 mins 2x Test 30 mbar 0 44 psi 1 5 Vacuum 3kPa Table 4 Vacuum Testing Pressure Ratings Maximum Pressure Rating UL 971 Pipe type Pressure Pressure Rating Bar Rating PSI UPP Primary 6 90 UPP Secondary 4 58 Table 5 UL971 Pipe Maximum Pressure Rating Maximum Pressure Rating EN14125 Pipe type Pressure Pressure Rating Bar Rating PSI UPP Primary 10 145 UPP Secondary 4 58 Table 6 EN14125 Pipe Maximum Pressure Rating Secondary Pipe Testing Pressure Rating Secondary Test Bar PSI Pressure Rubber boots 0 5 T Welded Boots 9 5 50 Table 7 Secondary Testing Pressures Initial Pressure 3 5 bar Temperature variation AT C Final pressure due to temperature change bar Initial Pressure 50 psi Temperature variation AT F 30 20 10 0 47 2 48 1 49 1 50 Final pressure due to temperature change psi Table 3 Pressure Variation with Temperature Change 10 20 30 90 9 51 9 52 8 Franklin Fueling Systems Sump Inspection Register Date of Inspection or Test Results of Inspection or Test Signature of Inspector or Tester
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