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¢ AERFORAIANCEPPE
www.performancepipe.com
YELLOWSTRIPEO 8300 Piping Products for
LPG and Propane Gas Distribution
Natural Gas Distribution
Performance P e
PERFORMANCE RMAI CE PIPE is the functional successor to the operations of Plexcoi and Driscopipe . On July
2000, Chevron chemical company and Phillips Chemical.company announced the combination of
their worldwide chemicals businesses into a joint venture, Chevron Phillips Chemical company L.P.
Performance Pipe, a division of chevron Phillips chemical Company LP, succeeds Plexco and
Driscopipe as North America's largest producer of polyethylene piping products for gas, industrial,
municipal, ruining, oilfield, and utility applications.
Performance Pipe offers more than forty years of polyethylene piping system experience, with pipe and
fitting manufacturing facilities throughout the United states and in Mexico.
To enhance the outstanding quality and performance of Performance Pipe polyethylene piping, Chevron
Phillips Chemical company LP further strengthens Performance Pipe with over four decades of duality
products.
A commitment to Qualityand Performance
Performance Pipe YELLOWSTRIPEO 8300 gas piping is a product of choice for premium high-density
polyethylene gas piping ysterr�s.' YELL OWSTRIPE 8300 gas pipe * produced from exceptionally high
performance material which meets all the requirements for PP listing as a PE3 8 1 o PE1 og product.
The pipe is manufactured in accordance with the latest published editions of ASTIVI D 2513 or applicable
international standards. YELL O STI IPE'o 8300 gas piping is available in 1/" through 2 " 6 mm
through 630 mm extruded polyethylene pipe and tubing, and molded butt, socket, and saddle fusion
fittings for domestic and international gas applications.
Research and Testing
Performance Pipe maintains ongoing testing and product improvement programs s to ensure the highest
quality polyethylene piping. A complete quality assurance program assures continuing product quality,
and new,products and product improvements are thoroughly tested before release. Both incoming
materials and-outgoing products are evaluated to ensure that all Performance Pipe products meet-our
oven exacting standards as well as current industry standards and governmental standards and
regulations.
Formerly-Pie o , a Division of Chevron Chemical Company
Formerly-Phillips Drise pip ,A Division of Phillips Petroleum Company
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Bulletin:PP 303 n April 2006 Supercedes all previous publications
Page I of 11 @ 2001-2006 Chevron Phillips chemical Company ny LP
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PERFORMAN"RPE
A Oms/OY or XV.Y PRIllys O TA I(Omajmf Ip
wwaperformarecepipe-.e rrs
'raining and Technical service
Performance Pipe offers recommendations and technical assistance for YELLOWSTRIPEO 8300 gas
piping. Jolninq procedures, training materials, and on-location training in socket, saddle and butt fusion
joiningare available, as well as technical assistance in. product capabilities, installation
recommendations, and testing and operating procedures. Contact your Performance Pipe Territory
Manager or Performance Pipe Distributor for information and assistance.
APWAIULCC Color Code
Performance Pipe YELLOWSTRIPEO 8300 gas pipe is produced with four, equally spaced longitudinal
}yellow stripes extruded into the pipe OD as permanent, highly visible identification of gas service and in
compliance with PWA/ LCC standards for color-coding of gas distribution lines..
Cautions
Polyethylene piping has been safely used in thousands of installations. However, there are general
precautions that should be observed when using any product. Below is a summary list of some of the
precautions that should be observed when using YELLOWSTRIPEO 8300. Further-precautions are
found within Performance Pipe literature.
Fusion
During the heat fusion process the equipment and products can reach temperatures in excess of 45 *F
(231'C). Caution should be taken to prevent burrs.
Do not bend pipes into ali nrr�ent against open butt fusion machine clamps. The pipe may spring out
and cause injury or damage.
sta tic Electricity
High static electric charges can develop on polyethylene Piping products,' especially when gas is flowing
at high velocities; such as, during squeeze-off, when repairing a leak, purging, making in a connection, etc.
Where a flammable gas atmosphere and static electric is charges may be present, observe all
Company (pipeline o era
tor utility, contractor, etc.) safety procedures for controlling and .
discharging static electricity and all requirements for personal,protection.
Weight, Unloading and Handing
Although polyethylene Pipe is not as heavy as some other piping products, significant weight may be
involved. Care should be exercised when handling and working around polyethylene pipet
Polyethylene is a tough, robust material, but t is not immune to damage. Improper handlingor
abuse can damage piping, compromise ise system performance result in injury or property damage. In
addition, personal injury may result. obtain and observe the handling instructions provided by the
delivery driver. Polyethylene piping should be roved with proper handling and lifting equipment.ent. Use
fabric slings. Lift truck forks should be padded and should extend completely across under the load. Do
not use chains or wire ropes. Do not roll or drop pipe off the truck, or drag piping over sharp rocs or
other abrasive objects. Store.piping so that the potential for mechanical damage is minimized., see the
Performance Pipe Engineering Manual for additional information on handling and storage.
While polyethylene piping has excellent impact resistance, striking the pipe with an instrument such as
a hammer may result in uncontrolled rebound.
Bulletin:PP 303 April 2006 Super cedes all previous publications
Page 2 of 11 @ 2001-2006Chevron Ph'11111ps Chemical Company LP
MEW-
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PERFORMANCEPPE
www.performanceplpexom
Coils
M
Gonad PE,pipe is restrained with straps to contain, spring-like e energy within the coil. Cutting r breaking
straps can result in uncontrolled release, Take all necessary safety precautions and use appropriate
equipment. Obtain and observe the handling instructions provided by the deliver driver
Testing
Fuel gas,distribution systems should be tested in, accordance with applicable codes and regulations and
distribution system olpera,tor procedures. Observe all safety measures,, retrain pipe against movement,
ire the evert catastrophic is failure, are observe limitations ns of terrmp rat rre test pressure, test duration,
and making repairs. See Perfdrmance Pipe Technical Note, PP-8,02 Leak Testing,PIE Piping Systems.
Protection Against shear and Bending Loads
Measures such as properly placed, compacted backfill, protective sleeves anid structural support are
necessary to, protect plastic pipe against shear and bending lads. Connections should e protected
ere an un er r and p ly t lene branch r ser is pipe is Joined t a rind ittirr� � �1 as a service
saddle, '' ranch'middle ortapping tee on a main pipe, and where pipes eater or exit casings or walls.
Properly place,, compacted hail till and a protective sleleve or a structural support are generally used
together. Whether or not a protective, sleeve or a structural support, is Installed, the area surrounding
the connection rarest he embedded In properly planed, compacted k a kfill to protect the polyethylene
pipe against shear and -ending loads.
For additional information about protecting against shear and bending loads at service or branch
connections. and where PE pipe penetrates a structure r eaters or exits a casing, see the Performance
,Pipe ngineer Manual and ASTM D 277 , Underground Installation of Thermoplastic Pressure
Piping.
Liquid Mtdrocarbon Permeation
When present, liquid hydrociarbons may ermea,t (solvate!) polyethylene, pipe. Liquid hydrocarbon
p
r ation a n rr when liquid hydrocarbons are present in the pipe when soil surroundingthe pipe
is ntamill" atad with liquid hydrocarbons, or When liqu�id hydrocarbon -condensates form in gas
pipelines. All types of liquid hydrocarbons (aromatic, paraffinic, to.) have a similar oect, and the affect
on different polyethylene pipe resins is essentially the same. Heat fusion joining to permeated pipes may
result in a low strength joint and is not recommended.
Li ri ' hydrocarbon contamination is indicated by discoloration, by a hydrocarbon fuel odor, or
rough, sandpaper-like, bubbly, or pockmarked surface when a fusion heating iron -is removed from tl
pips surface. ee thPerformancee Engi ea n , a s for additional in dr atior� on per e tion
and chemical resistance.
CAUTION-Once polyethylene pipe has been permeated with liquid hydrocarbons, heat,fusion or
elect'ro,f6sionjoining is not recommendedbecause liquid hydrocarbons can leach out during
heating and contaminate the Joint. Liquid hydrocarbon permeated polyethylene pips should be
joined using suitable mechanical connection methods.
Mechanical fittings must be installed in accordance with the fitting manufacturer's instructions., Obtain
these instructions from, e fitting manufacturer
Bu
ll i '�! April 2 Supersedes all previous �u ri ti rl
Doge 3 of I 1 2 -2 I Chevron Phillips rn,% company LP
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www.performancepipexorn
Locating
Polyethylene materials, are not detectable with standard magnetic locating li r ue. rt. To, aid. in the
detection underground l � i ing,' measures such as tracer wires, i r ti ' ti rr and dete'diontapes,
litre marl erg, electronic marker systems, acoustic pipetracing, and "call before you dig" lire location
ensures may be used. Whereposted' signs-are used., the signs should indicate that the i line i
polyethylene to alert'locating personnel that the: pipeline may not be detectable with .standard locating
equipment. Gas Futilities in the area should always be contacted before the start of anyunderground
installation work such as excavation, trenching, directional boring, atc.
Jln
.O.T Regulations require that:
Each Joint in a, gas pipling system must made in accordance with written procedures that
have been proved by test or experience to produce, strong gastight joints 9 CFR, hart 192,,
912.23 .
- Written prociedures for butt fusion, saddle fusion, and socket,fusion Joining of polyethylene gas
piping must be qualifiedbefore use by subjecting specimen joints to required test procedures
(CFR 4 , Part 192, §1921-283(a)).
All persons who make Joints in pol, ethylene gas piping must be qualifiedunder the operator's
written procedures ('CFR 49,, Part 192, §192.,285(a)).
The gas system operator must ensure thiat,all persons who, make e r inspect joints are quallified
C FR 4 9, Part 192, .28 5, & §1922817).
Performance Pipe recommends Fusing Performance Pipe Bulletin PP-7'50 Performance Pipe Fusion
Joining Procedures when making beat fusion joints with Y LLOWSTF IPEO 8300 piping. Contact your
Performance Pipe 'Territory Manager, www.perfo:rmancepipe.com, or Distributor for a copy. When used
to join Performance Pipe polyethylene gas piping, Performance hips fusion joining r ce u!res are,
qualified in, accor ance with U.S. Department of Transportation Regulations.
CAUTION - Performance Pipe polyethylene � �products cannot Joined with adhesives or
solvent cement. "fie-thread Joining and joining by hot air (gas) welding or extrusion ing
techniques are not recommended for pressure service. Molded butt-outlet fittings are intended
for butt fusion and may not be suitable, for joining with mechanical stab, fittings or mechanical
fittings that require ID stiffeners.
Squeeze
See above Cautions on Static iectric y. Squeeze- (pinch- is used to control flow in PE pipe
y flattening the pipe between parallial bars. Squeeze-off i's used for routine and emergency situations.
, not squeeze-off more than once at the same point on the i, I. or repeated flow' control,
throttling,, r partial flow restriction, install a valveor are appropria,te flow control device.
Complete flow stoppage will not occur in all cases., I r larger pipes, particularly at higher pressures
some seepage is likely, If seepage is not permissible, the piipe should be vented in-between two
squeeze-offs.
Bulletin:PP 3100 A rll 2006 Spu r all r iou a Ii fiorm
Fags 4 of 11 0 2001-2005 Chevron'Phillips Chemical company LP
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A DAVOY or -Roar FF11 WS WHICH(OMPANT 1P �
www.performancepipe.com
Use squeeze-off procedures meeting ABTA F 1041 and tools meeting AST11 F 1563 with Performance
Pipe polyethylene pipe. The combination of pipe, tool and squeeze-off procedure should be qualified in
accordance with ASTM F 1734. correct tool closure stops and closing and opening rates are key
elements to squeezing-off without damaging the pipe. Teel closure stops rust be correct for the pipe size
and wall thickness (SD .I It is necessary to close-slowly and release slowly, with slow release being
more important.t. See Performance Pipe Technical Note PP-801 Squeeze-Off
Performance Characteristics
Polyethylene Material Properties
Cell Cla sifi i n - YELLOWSTRIPE@ 8300 piping is manufactured from premium high performance
bimodal polyethylene compound lnd that is classified according to ASTM D 3350, Standard,Specif ation for
Polyethyleneplastics Pipe and Fittings Materials. The cell classification number for Performance
PipeYELLOWSTRIPEO 8300 material is 445576G.
Long-Terrn Sfre g�t`h H -- Perforrnan e Pipe YELL v STI IPB Soo polyethylene piping compound
is listed with the Plastics Pipe Institute as PE 7` 0 and as PE1 oo. It also has PPl recommended
Hydrostatic Design Basis HDB ratings of 1600 psi at 73°F 1.03 Wa at 2 °C and 1000 psi at 1 o°F
(6.89 Wa at 23*C . Elevated temperature properties can be used to determine product capabilities for
applications where products will be exposed to elevated temperatures.
In addition to ASTM D 2837 and PP HDB requirelments,YELLOWSTRIPE Soo piping meets I SO 9080
Thermoplastics Piping for the Transport of Fluids-Methods of Extrapolation of Hydrostatic Stress Rupture
Data to Determine the Long-Team !Hydrostatic Strength of Thermoplastics Pipe Materials requirements with
a IVIES of 10.0 MPa (1450 Psl at 20°c °F . Thus, it is a fully qualified PB 4710 and PE 100 product
and is listed as such in PPI TP .
SCG Resistance - Resistance to slow crack growth is a critical performance requirement because long-
term stress can cause cracks to grow slowly through the material. Polyethylene gas pipe is under long-
term stress from internal pressure and earthloading.- Thus gas distribution service requires materials that
have superior long-term resistance to stress cracking and slow crack growth (SCG).
For many years, environmental stress crack resistance (ESCR) tests, such as ASTIR D 1693, have been
used to characterize resistance to cracking from long-term stress. But exceptional materials such as
YELLOWSTRIPEe 8300 piping rarely fall ESCR tests. For these superior materials, ESCR tests are
incapable of quantifying long-term resistance to SCG.
In recent years, new SGG tests have been developed. Predominant among these new tests-is ASTIR F
1473, the "PENT" test (for PEnnsylvania Notch Tensile test). Developed at the University of
Pennsylvania, a razor,-notched specimen is tested to failure under constant tensile load and elevated
temperature. Research has shown that this stringent test is an excellent indicator of SCG performance,
and further, that there may be an empirical correlation between PENT performance and long-term
if
service.
Under ASTIR F 1473, Standard Test Method to Measure the Desistance to Slow crack Growth of
Pipes and Resins, typicalperformance of the resin used to produce YELL WSTRIPE
Polyethylene E'�p p p
ago pipe is greater than 5000 hours before failure. ASTIR D 2513 requires that PE materials average
at least 100 hours before failure when tested per ASTER F 1473. Thus, the performance of the material
in this test lasted,50 times longer than required by the standard. Actual system field performance will be
determined by a variety of factors such as its application, operating conditions, and other unknown factors
that may impact the pipe over its expected service life.
Bulletin:PP 303 Apdr 2006 supersedes all previous publications
Page 5 of 11 02001-2006 chevron Phillips chemical Company LP
i
NRFORMM"PPE
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www.performancepipe.com
RCP Resistance - In rcent years, rapid crack propagation, RCP, research has been conducted on
polyethylene materials and pipes used for gas distribution piping. ISO, the International Standards
Organization, has developed two standards for characterizing RCP resistance, ISO,13478 Thermoplastics
Pipes for the conveyance of Fluids - Determination of Desistance to Rapid i Crack Propagation - Full-Scale
Test(FST) and ISO 13477 Thermoplastics Pipes forthe Conveyance o Fluids--Determination of Resistance
to Rapid Crack Propagation -- Small--Scale Steady State Tort (S4 Test). At a specified temperature, these
tests are used to determine a critical pressure abov6 which RCP may occur. The fail-scale test is used with
large diameter(greater than 250 mr . in)) pipes and the S4 test with small diameter sample pipes having
wall thickness greater than 1 in):
Although ASTM D 2513 does not currently have an RCP requirement, ISO 4437 Buried lye hylene Pipes
for the Supply of Gaseous Fuels - Metric Series - Specifications, specifies that the critical pressure ure for gas
distribution pipes must exceed 1.5 times the maximum operating pressure at '0 32° when tested
according to ISO 13478FST or when tested according to ISO 13477 (S4 Test) and converted to the full
scale critical pressure. YELLOWSTRIPEO 8300 materials and pipes meet or exceed these requirements.
SM Test VaNes
The chart below shows material physical properties,ASTM test methods for the property, and nominal values
for YE LL WST RIP EO 83 00 P E 3408/4710 P E 100 po 1yethylene materials,
#- Pypica
rocedure T
PE 340
PP1 Usting Designations PPi Tr 4 PE 710
PE 100
....
Cell Classific.......
ation A TiI D 38 0-05 44557 C
Density gmicc ASTM D 1505 0.90 b...ac......k
.... .... ..........................
........
rei ]ow}� 1 100° Orliln AST D 0,........................................elt Flow,M 1(21.6 11 0° m/10minj ASTM D 1238 8.00
Thermal Expansion/Contraction inftn1 F ASTIR D 000 Ixl 0
#... ............
:Flexural ModuIus @ 2%strain psi AST 1 D 79.0 140,000
................... .
Tensile Strength a@ Yield psi ASTII D 038 3500
.. ........
Slow Crack Growth(PENT) hours ASTM F 1473 >5000
vier Stabilizer % STi D-8 50 2
Elastic Modulus psi ASTIR D-038 200,000
Brittleness Ter peratur AST D 74 -180(<-1 1.8)
Vicet Softening TemperatureFFASTM D 1525 255
Hardness Store D AST D-220 0
Hydrostatic Design Saris .730F.(?30C) psi ASTM D 237 1 000
------------------—
Hydrostatic Design Basis a@ 1 0T 00° psi ASTIR D 28371000.
Minimum e uire Stre.ngt S).@ 0° 03°F r a(psi) IS09080 >10(145). -
Rapid Crack Propagation P bars iS 'i 477 > 12 far 4 sr
Critical Pressure Po),0' OC F ES 13477 17 2 F
Critical Temperature (To),5 bar
1. YELL w T R1 P E@ 83 60 pipe rnatefial is listed in PP Tl-4 for use in natural gas distribution. -
. Meets new requl rem ent for PE4710 material.49 C F R Pert 192 references older versions of the standard that do not yet re cog nine
the new requirements and carry the PE3403 designation. The pipe vill be dual marked as long as required by 49 CFR Part 192.
. Previous versions of A TM D 3350 would have assigned a cell cla sibcatlon of 345564C or 345566C.
4. Detemination made on 3"DR I I pipes. No failures occurred, Pe calculated in accordance vAth[50 1 477 Annex C correlation.
. NOTICE-This chart provides typical physical property information for polyethylene resins used to manufacture Performance Pipe
polyethylene piping products. it is intended for comparing polyethylene pipe resins. It is net a product specification,and it does not
establish minimum or maximum values for manufacturing tolerances for resins or for piping products. Some of the values were
obtained from tests of specimens taken from melded plaques and can vary from these typical values. Performance Pipe has made
every reasonable effaft to ensure the accuracy of this chart,but this chart may not provide all necessary infoffnation,particulady Wth
respect to special or unusual applications.
Bulletin,PP 303 April 2006 Supercedes all previous publications
Page 6 of 11 @ 2001-2000 Chevron Phillips Chemical Company LP
PERFORMAMWPIPE
A DlY7NY OF CHRICY PSIU Wr(JI COMP Y IP
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Permeability n Permeation
Plastics are permeable to gases to varying degrees. Although- the constituents of natural gas can
permeate through polyethylene, the volume of gars lost through permeation tion is generally so low as to have
an insignificant effect on the handling of natural gas in a Piping system. The A.G.A. Plastic Pipe Manual
for Gas Service lists the permeability of polyethylene pipe to meth one, the primary constituent of natural
gas, as .2 x 1 - , using the AGAfactor# one mile of SDR I I H DIDE pipe carrying 00 methane at 60
psi wound lose less than 0.27 U per day.
Other constituents of natural gas are typically heavier than methane, thus, less permeable through
polyethylene. Hydrogen is the exception, however, the concentration of hydrogen in most natural gas is
o love that the actual amount of hydrogen permeation would be insignificant.
Liquid hydrocarbons will permeate (solvate) polyethylene pipe after several months' exposure. Liquid
hydrocarbon permeated polyethylene may have slightly reduced long-terra strength; therefore pressure
rating may be reduced. At higher temperatures, liquid hydrocarbon permeation may cause some swelling.
Liquid hydrocarbon permeation should be considered when the fluid in the pipe has a liquid hydrocarbon
concentration, or where soil surrounding the pipe is contaminated with liquid hydrocarbons, or where liquid
hydrocarbon condensates can form in gas pipelines'. At low temperatbres and higher pressures, heavier
hydrocarbon-gases such propane or butane may condense and liquefy in the pipe. Such condensates
are known to permeate polyethylene pipe. All types of hydrocarbons aromatic, paraffinic, etc. have a
similar effect, and the relative effect on different polyethylene pipe resins is essentially the same. Liquid
hydrocarbon permeation will affect joining. See above Cautions on Liquid Hydrocarbon Permeation.
Design Pressure
The following formula is used to compute the Design Pressures for YELLOWSTRIPEO 8300 polyethylene
piping systems for natural gas service at operating temperatures up to but not over 11 o°F o'C . For
operating temperatures below 3°F 23°C , use 3°F 2 °C Design Pressures.
S
(DR -1
There P - Design Pressure in pounds per square inch gauge psi ;
S Long Tern Hydrostatic Strength (Hydrostatic Design Basis) stress, psi, at
pipeline operating temperature;
Hydrostatic Design n Basis or Long Term Hydrostatic Strength,S
Temperature S, psi MPe
730F 23° 1600 11 M
HDB per ASTM D 2837&PPI `i`I -- . t Interpolated in accordance with PPI TN-18. i
DR Dimension Ratio
.-
Pipe Norml Outside Diameter
Pipe Minimum Fail Thickness
f Design (Service) Factor
Bull the PP 303 April 2006 Supercedesall previous publications :.
Page 7 of 11 0 2001-2006 Chevron Phillips Chemical Company LP
ti
PERFORMANCOPPE
VM0N of OnZoX ANIIin MIC-4x 104VY
www. arformanca 1p . earn
pplicatlon Design (Service) Factor,
Gas d1stfl but[on and transmission per C FR 49 Part 192,§192.121 0.3
Gas distribution and tr'ansmi [on in Canada per of o
Gas distdbution or transmission piping that is perme' ted by solvating chemicals such .
25
as liquid hydrocarbons or ligoelw d- a condensate
Operating Pressures ig The following chart provides maximum allowable operating pressures i1 AOP and recommended
maximum design pressure rating P for YELLOWSTRIPEO 8300 pipes for gas distribution service at
the indicated operating temperature . YELLOWSTRIPEO 8300pipes with the sane DR but different
outside diameters have the I Design,(Working)i Pressure Ratings. Piper minimum wall thickness is
determined by dividing the pipe average outside diameter .D. by the DR number.
Pressure ratings are calculated in accordance with applicable U.S Federal cedes. A check should be
made to determine if these pressures apply under the state and/or local cedes governing the specific
application. Use 73"F 23°C pressure ratings for operating temperatures below 7 'F 2 °C , It should -
be noted that while YELL WSTl I PEI@ 8300pipe is produced from PE4710/3408PE 100 pressure rated
materials, the PE47 o and PE100 rating methods are currently not recognized in the applicable DOT
Federal Code. Neither is the rating method included in the current edition of ASTM D2513. Therefore,
the PE3408 design basis is binding.
l P&Maximum Design Pressure Rating PR for Dry Natural ural Gas Service—YELLOWSTRIPe 8300 Pipes
Service 73*FI230C 100OF1380C 20'OF 43 OC 14 "F
Temp
e l P(Max Design i MA OP(Max Design P(Max Design M P(Max Design
PipPR),ps PR), { PR),psfg PR),psig
7.0 125t171 t14 4t124 10f 17
.0 125t 1 107t 107 3 80 8
.3 1 3 f 2 1 3t 10 0 77
11.0 1 0f 1 o 8 74'74 4 )
1 . 75(75)
13.15 ) 1.
t Class 1,2,3,and 4 locations per U.S.federal regulations using 0.32 Design(service)Fact r. For pressure ratings at 0.4
,design factor(Canada only), multiply by 1.2 ; for pressure ratings at 0.25 design factor,multiply by 0.78. f Where the pipe
can rated at 125 prig or higher, U.S. Federal regulations limit gas pressures in plastic pipe to 12 psi maximum unless a
waiver for highdr pressure has been granted.
Bulletin;PP 303 April 2006 Supercedes all previous publications
Page 8 of 11 001-200 Chevron Phillips Chemical Company LP
i
F
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Cold ending Radius
The allowable cold bending' r d i us for YE LLOWSTR IP �) 8300-pipe is dependent upon the pipe oD,
Dry and the presence of fittings in the bend. ,.
P Allowable Cord Beading Radius
r less 20 times pipe OD
to 13. 25 times pipe OD
rifting or flange present in bend. 100 times pipe OD
Fluid Flow
Foemulas for high pressure and love pressure gas flow in polyethylene -pipe are presented in the
Performance Pipe Engineering Manual, and in Performance Pipe's free PlexCafc@ program for per onarl
computers.
Outdoor Storage
The recommended maximum for unprotected outdoor storage of YELLOWSTRIPE@ 6300 is twenty
years.
Propane (LPG) Gas Service
The office of Pipeline Safety Advisory Bulletin No. - � dated April 1973, states, "it is the operator's
responsibility to assure the integrity of the plastic pipe selected for use in the Piping system, and this
should be based on a favorable recommendation from the manufacturer. Therefore, the Federal
minimum m safety standards do permit the use of plastic in a properly engineered underground system of
LPG distribution conforming to the limitations of these regulations." YELLOWSTRIPEO 8300 piping
products meet the requirements of ANSI/NFPA 56 Standard for the Storage and Handlingof Liquefied
Petroleum Gases.
The Plastics Pipe Institute has made the following "UseRecommendation" for polyethylene piping
systems for commercial propane systems:
PPI Use Recommendation (Technical Report TR-22)
The information collected indicates that polyethylene plastic piping is satisfactory for transporting LPG
and its major component, propane gas. This information also indicates that pressure design parameters
l based on propane gas should be adequate and reasonable. However, until more information is
available, these use recommendations cover only commercial propane gaper in detail.
`i. The polyethylene plastic pipe, tubing and fittings should be only those specific types designated
as PE 2406 or PE 3408 and meeting the appropriate requirements of ASTM D 2513.
2. A Hydrostatic tati Design Basis of 1000 psi should be used in the design of polyethylene pipe
systems for propane gas distribution at pipe temperatures of 3'F or lower. The long-terra
hydrostatic strength measurements should be made in aiocordance with ABTA D 2837.
3.. Polyethylene should be used only in underground propane gas distribution systems designed to
operate at internal pressures and temperatures such that condensation will not occur.
Bulletin:PP 303 April 2006 Supersedes all previous publications
Page 9 of 11 - 2001-2006 Chevron Phillips Chemical Company LP
PERFORMAN-l"PIPE
www.performancepipe.com
It is also recommended that operating 12ressures be limited to 30 i2sigless.
In cases where condensation does occur in a propane system or propane enriched system and the
presence of condensation is of relatively short duration, there is no indication df loss Of physical integrity
or observable change in polyethylene pipe. Under actual operating conditions, in a properly designed
system, the pressures and temperatures are such that revapor�i ation of any propane condensates will
usually occur. Also, experience with propane liquids on polyethylene shows that there is no cumulative
effect of intermittent short duration exposure of propane condensate on polyethylene.
For additional information, see PPl Technical Report T -22. Exposure to liquified propane condensates
for extended periods may affect joining. See Liquid Hydrocarbon Permeation and Permeability and
Permeation earlier in this publication, and the Performance Pipe Engineering Manual for additional
information.
Performan ce Pipe YE LL WST R I EO 8 30 PE 34 08/4710 P E 10 g polyethylene gas piping may be used
in propane gas service when used in accordance with the above recommendations.
Bulletin:PP 303 April 2006 Su pereed es all previous publications
Page 10 of 11 2001-2006 Chevron Phillips Chemical Company LP
.P,9RF0RmANCkP1PE
i IS/01 OF Of wo it PINIIP 111141 A I COMFA 9 r PERFORMANCE PIPE PLANTS
-----------------
CONTACT INFORMATION:
A Aff is & ram'+
..ry
� r
.+ryN
PERFORMANCE PI division
■�
Chevron Phillips
LP
:...:
�::i -
r
.............. .........
T
............ ......
.. k.......: ..... '::i -
:S {
Plano, TX 756-9006
02 4V fI R' P
................. ............ ..
.ti
T
4
To secureproduct
information
.sa SC
s
assistance. - - --
0'
- a
Phone: 800-527-0662
iesa- # a
Fax: 72- -73
WWW.performancepipe.com
SIE11fri-7itegically Located Plants
A S T C-S , E•INS TITUT
T Better Beare Your N C.I I
PERFORMANCE PIPE
Product Literature
Technical Notes & Bulletins*:
PP 156 DRISCOPLEXI&6500 Series Piping Systems Size &Dimension Sheet
PP 157 DRISCOPLEXO 6800Series Piping Systems Size & Dimension Sheet
PP 158 DRI SCOPI PE@ 8100 Series Piping Systems Size & Dimension Sheet
PP 159 YELLOWSTRIPE@8300Series Piping Systems Size &Dimension Sheet
PP 300 PE 2406 II DPE Pipe &Tubing - DRISCOPLEXO 6500 Series Piping Systems
PP 301 PE 3408 HDPE Pipe &Tubing - DRISCOPLEXO 6800Series Piping Systems
PP 302 DRISCOPIPEO 8100 Series Polyethylene Piping
PP 304 Model Specifications-- DRISCOPLEXO 6500 Series Piping Systems
PP 305 Model Specifications- DRISCOPLEXO 6800 Series Piping Systems
PP 306 Model Specifications - DRISCOPIPEO 810OSeries Piping Systems
PP 387 Model Specifications-Yellowstrip& 8300 Series Piping Systems
PP 752 Socket Fusion Tip Card
PP 73 Butt Fusion Tip Card
PP 754 Saddle Fusion Tip Card
PP 801-TN Squeeze-Off
PP 8 --TN Leak Testing
PP 8 7--TN Large Diameter Called Wipe
PP 8 A--T ! Tapping Tee &Purg6 Point Cap Tightening- Flat Ping Gasket
PP 808E-TN Tapping Tee &Purge Point Cap Tightening - -Ring
PP-8 -TN Protective Sleeves and Tapping the Main
Bulletin:PP 303 April 2006 Supercedes all previous publications
Page 11 of 11 (D 2001-2006 Chevron Phillips Chemical Company LP :.
`Additional product literature will be available upon compieuon. Visit Performance Plpa can the web for the latest completed literature.
i
PERFORMAAWEPIPE YELLOWSTRIPE 8300 Series
jv{s}ott or 0ii viam Pint iips Ckmwi Comm N Y I P Size Dimension Sheet
CTS = COPPER TuI3E SIZE
Nominal I P si Number umber
Nominal Minimum Weight Coil I Nominal PacWcln Pallet
Outside Dimension per F# Part � Coils I,faints Pallet 1 48 ft.
See Diameter wall Ratio 192 @a7 .4 F por Joint Di ensia s Per Pallet or Bundle Bundles Truck
(Inches) Inches (Inches) or loss 100 ft (feet) ID 1 D I width Bundle Footage Per Truck
0.062 DR 19.1 4.8 D° 30" 3W!B" ,OQ ' 156,000,
1 I2 .0625 100 {y�{� � }�
{. 1000, 39'�44"1 " 1ry,000' 3'12,000'
314" 0.875 0.090 DR 9.7 100' 9.7 500 30"1 " 11"$ 5 3,0001' 26 78,000'
0.090 DES 12.5 89 13
,191 DR 11.4 100 14
'f 1. 25 0.'l 2 500" 30"14 "111" 8 4, 0' 26 104,000'
.121 DR 9.3 '23 17
0.125 DR 9.9 125 17
0.161 DR 7.9 125 2
1 114'" 1.37 0.0 D1 15.3 72 16500" 32"145" 14 112" 6 3,900' 24 72,000'
0.121 DR 11.4 99 21
IPS IRON PIPE,SIZE
Nominal Nominal al Minimum l I P{ t Weight Coil f Nominal Packing Number Pallet 1 Number
Size Dimension Outside wall per CFI Pad per Joint Dimensions Gods I Joints Bundle Pallet J 4 ft.
Inches fade Diameterlc 1 he 19 @ 1 F 10] feet 1D f !widkl Per Ballet or Bundles Truck
(inches) or less Bundle Per Truck
112#' OR 9.3 0.840 0.999 123 9 500, 30"144"- " 14 7,000� 20 182,000'
DR 7 0.150 19
125314" DR 9 1.050 0.117 15 500' 30°!44"1 10" 7 3,500' 26 91,000'
DR 11 9.995 180 13
l� DR 9.3 't.3'l 0.141 '�23 23
500, 0"144" 12" 6 3,090' 23 78,000-
DR 11 0.120 100 20
1 '114� D1 7 1.800 37 12 4
00' 43"17 17-112" 12 6,300, 7 42,000'
DR 11 .0.151 100 31
DR 7 0.339 125 95
2" DR 9 2.375 0.255 125 75 509" 2"178"113" 7 3,500' 7 24,599'
DR 11 0.216 100 64
3" D 11 3, 9 .318 100 14 4D� Soak f ndfe �# 5 2,000' 14 8,OOC!
00 70 /9 123 314 4 12,000
D :........::: 0.50 12 27' 40' soft bundles 29 1,-1 O' 14 16,240'
0.499 100 230 500' 70t'193"14V 3 1,000' 8 8,000'
DID 9 ` 0.736 12 40" soft bundles 13 520F 14 7128 "
BR DR 11 6.625 0.602 100 501 500' 84"1 120" 501$ Upright Upright 8 4, C'
DR 13.5 0.491 32 41
DR 9 04958 125 1013
" DR 11 8.625 .7 4 190 849 40' soft bundles 9 360, io 3r600
DR 13.5 0.639 82 70
DR 11 1.1=9 100 1855
12" DR 15.6 12.750 9.823 71 1357 40' bulk packs 8 jIsMa r 329' 6 1,920'
DR 1 0.607 1 1921
............------
DR 11 1.455 199 921
16" ❑ ' 0
�7 1 .09� .94�i 84 198'i �49' bulk packs atshayer 249' 11 200'
DR 11 1.636 100 3697
181, DR 13.5 18.000 1 M3 82 3071 Available upon request
DR 17.0 1.059 64 2482
Other sizes and packaging configurations may be available. Pipe weights are calWated in accordance with PPI T -'7.
Performance Pipe,a division of www.performancepipe.com Phone:.800- 27-9562
Chevron Phillips Chemical Company LP Fax:972- 9 -734
Bulletin:PIP 159 August 2013 Supersedes all previous publications
Page 1 of 1 02012 Chevron Phillips Chemical Cornpany LIP
TRANSITION FITTINGS WELD END
FOR REF tEWE ONLY
Central PlaWcs C ompimy Phorse,80045U-M
RIP 1901 W.fndepende a St 405-273-6302
S ha,6 M CK USA M01 Fax 8M733-5993 T
yr*rr.centta'p+astl[ corn 40273-5993
DOSED POL=TYLENF, OAL, TEEL
me
E"OSED STHEL(SC .4
W
I.D.(MIN. .� O.D.(MAX.)
PLAMC CAPSO- G
RINS
T P.EACH END ADAPTER
TAM
NOMINAL DIMENSION DIMENSION DIMENSION DIAMETER DIAMETER DIMENSION
SIZE A B c D E F
STEEL x PLASTIC DOSED PLASTIC O L STEEL EXPOSED STEEL RETAMER EPDXY COATED BLOCK BACK
14"x 1I2" T 4LL.090 12.14 12.67 11.56 0.324 1.390
26.67rnm x 15.88mm 308.36mm 321,8 mm 293.62rr m 8,23mm 35.31mrn SOMMM
314"x1/ "IPA(SDR 9,3 11.81 12.88 11.56 0.516 1,390
26.07mm x 21.34nnm 299.97r'r3m 327.i5rarn 293.62mm 13.1ImM 35.31€ m 60.80rnm
3/4"x 314"1P DR 11 11.81 12,88 11.38 0.630 1.45 2
26.67m x 26.67r• m 299.97mm 327.15mm 289,05mm 1 .00mm 36.91mm 80.8iomm
1"x VIP DE 11 11.00 13_16 11.38 0.817 1.703
33.40fnm x 33.40mm 302. 6mm 334.26rnrn 289.05mm 20.75mm 43. 6mm 50.80mm
1 114p'x 1114"1PS(SDR 10 or 11) 11.94 13.44 11.44 1.056 2.070 2
4 _16rnrn x 42.16mm 303.28mm 341.38mm 290.58mrn 2 .82mm 8 .58mm 5.0.80mm
1 112"x 1 112*IPA SD 11 12.03 13.66 11.44 1,322 2.317
48.26rmrn x 48.26mm 305.66mm 40.96mm 290.58mm 33. 8mm 58.85rt m 50.80MM
2'x "IPE DR 11 12.16 13.78 11.44 1.625 2.700
60.33mm x 60.33mm 308.86mm 308.8 mm 290.58rnm 41.28mm 68.58mm 50.80mm
3'"x 31P DR 11 or 11.6 11.97 14.84 11.69 2.360 4.08
88.90mm x 88.90rnm 304.04mm 376.94mm 296.93mrn 89.94mm 103.632mm 50.80rf3m
11.62.08'
114.30mm x 114.30mm 306.32mm 377.05mm 296.93mm 75,06mm 1.2 .73mm 50.80mm
6" 6"IPS MR 11 or'11.5 17.40 17.90 11.69 4.985 7.330 2
1 .28 rn x 168.28m .441.96rr m 454.66mm 296.93rmm 126.62mm 186.18mm 50.80mm
8"x 8"IPA(SDR 11 or 11.5 4.44 22.88 15.31 6.482 9.59 2
...............
168.28mm x 114.30mm 620.78mm 581.15mrn 388.87mm 164, 4r71r'r'1 243.59mm 50.80mrrt
1V*x 1U 1P8(SDR 11 or 11.5) 22.50 27.09 17.56 7.972 11.595 4
27 .05r'm x 27 .05mrn 571.60mm 888,09mm 44 .02mm 20 .49mm 94.51m 101.80mm
12"x 12"IPS(SDR I or 11, ) 20.44 27,88 16.31 9.716 14.100 4
168.28mm'x I14.30mm 519.18mm 708.15mm 14.27mrn- 24 .79rnm 358.14mm 101.80 m
Items shown are standard sizes and wall thicknesses.pitting sizes offer than those shown can be furnished upon request,
TR4Pd%ELD-xh -
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No Component Material
Body
Polyethylene
2 End Polyethylene (PE)
3. Ball Polypropylene p
4 Ball Seat N (Rubber)
Supporting Ring Polypropylene (pp)
6 Stern Ael
High Impact Wrench Adapter P (Polypropylene) Plus FRP
8 Stem -- inn N € bber
9 Adapter Ground Water Seal N R U er
General Inform tion for Gas and Water
Item Operating Spocifications
For Gas For Water
Resin T - 1 8Y PE 26 (PE80)
TR-480B PE 3408 (PEI 00)ITR-480B P E.8 10)
Temperature Range --2 "
Pipe.Connection Butt Fusion or Efectro Fusion
Bare Full Bore and Standard
Stem Type. Short Stem or Extended Lon Stem
Standard Dimension RbO SD SDR; 11, Or as Specified
Open/Closeturn
OL
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BROEN Makes the c islon Easy Aga
"The Natural Choice RO N BALLOMAXO PE Valves
i * Over 50 'dears of Engineering,Excelle
i
Largest Port offering In the its
" Extra High Impact Operating Nut
' Full Size Range 2"--161)
Fully Tested and Qualified To:
Meet or Exceed ANSI B.i 6.4o
' Meet or Exceed ASTM D25 3, US DOT Part 192
• (SO 92 Approved
Ali ire Medium or High Density Polyethylene
Easy Ordering Code
Manufacturer Size Poi Resin
Dens
itr �€
B 2 F 2406Y
" Furl[= ' Medlum=240 As Specified
By
MAX High= B
or C S
Service Pressures
in prig and bar for service temperatures up to 3* 2T C
PE 4
SDR psig bar psig bar
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'' 80 6115 100 6.9
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10.4.bar-(1 50psi)-
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.3 bar (4psi)-S. � e Air Test Under Watert
:.:.. 10.4 bar p 1 F'ea
t.. Valve Operated. -times at Full Differential 0.3 bar ; :.
Operational `r -
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Pressu` --29 -C and 3 #C -2 ' ' 0 #:a
+ er i Ter --.2 °C and '00
Tor. .Te � IROT and I 00T) i
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r: LI 4� �F �..LI 4 i Seat, 23"C and *C 2. "cs 18.6 ham ! (2650s'
PreSSLIee Test (74T and I 00T) OC-: 14.8 bar (2-15psi)
H 9-h PresSUre Test Su�talned
High re . e Shell Test - bar.5 st
-
.: 25% Neck Down e &
Pull e Hydraulic Elongation Pull
External 'i
{5
},..:RQ. Box 100849 Birmlhgham,Alabama 362 6-7326 'Tel A5.956-9444 Fax:,2 5-9 -2 3 f
Ate.
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BAI9 �• wa
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112
W/2" Nut Operator
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pose:S ta Ad atd is.SO R I I or Sp& i Red,o n P f��has .Order