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PERFORMANdftff
www.performancepipe.com
YELLOWSTRIPEO8300 Piping Products for
LPG and Propane Gas Distribution
Natural Gas Distribution
Performance Pipe
PERFORMANCE CE PiPE is the functional successor to the operations of Ple col and Dr'Isoopipel. On.July
1, 2000, Chevron Chemical Company and Phillips Chemical Company announced the combination of
their worldwide chemicals businesses into a joint venture, Chevron Phillips Chemical Company LP.
Performance Pipe, a division of Chevron Phillips Chemical Company LP, succeeds Plexeo and
Driseopipe as North aerie 's largest producer of polyethylene piping products for gas, industrial,
municipal, raining, 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 quality
products.
A Commitment to Quality and Performance -
Y L L O WS TRIPO 8300
Performance Pipe YELLOWSTRIPEO 8300 gas piping is a product of choice for premium high-density
polyethylene gas piping sy terns.' YELLOWSTRIPEO 8300 gas pipe is produced from exceptionally high
performance material which meets al the requirements for PPi listing as a P E3408/471 o PE1 oo product.
The pipe is manufactured in accordance with the latest published editions of ASTM D 2513 or applicable
international standards. YELLOWSTRIPEO 8300 gas piping is available in 1/2 through 24" mm
through 630 m 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 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
own enacting standards as well as current industry standards and governmental standards and
regulations.
Formerly-Plexco, a Division of Chevron Comical Company
2 Formerly-Phillips Dris op1pe,A Division of Phillips Petroleum Cor parry
[ 'I CE:: p. io ::for: r .ptipoo 1:... e. .: sintended ... :. :.. erer eid : ::.lt.. #ou
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Bulletin:PP 303 April 2006 supere des all previous publications
Page 1 of 11 @ 2001-2006 Chevron Phillips Chemical Company LP
5
l
PERFORMANCERPE
www.performancepipe.com
Training and Technical Service
Performance Pipe offers recommendations and technical assistance for YELLOWSTRIPEO 8300 gas
piping. Joining,procedures, training materials, and on-location training in socket, saddle and butt fusion
joining are 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 API A ULCC 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 YELLOWSTRIFIEO 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 450OF
(231°C . Caution should be taken to prevent burns.
Do not bend pipes into alignment against open butt fusion machine clamps. The pipe may spring out
and cause injury or damage.
Static 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 a connection, etc,
Where a flammable gas atmosphere and static electric charges may be present, observe all
Company pipe i e operator, utility contractor
etc.) safety procedures for controlling and
discharging static electricity and all requirements for personal protection.
Weight, Unloading and Handling
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 pipe.
Polyethylene piping is a tough, robust material, but it is net immune to damage. Improper handling or
abuse can damage piping, compromise 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 moved with proper handling and lifting equipment. 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 roil or drop pipe off the truck, or dreg piping over sharp rocks or
ether 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 upercedes all previous publications
Page 2 of 1 i @ 2001-2006 Chevron Phillips chemical Company LP
w ti
PERFORmAmd'RPE
Coils
Coiled P,E pipe is es i'nee with straps to contain spring-like energy within the coil. Cutting or 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 delivery driver.
Testing
Fu l as distribution systems should tested in accordance with applicable codes and regulations and
distribution system operator procedures,, Observe all safety measures, restrain pipe against movement
in the vent of catastrophic failure, and observe limitations of temperature, 'test pressure, test duration,
and making repairs. See Performance Pipe Technical Note " "- 2 beak Testing PE Piping ,systems.
Protection Against shear and Bending Loads
Measures such as properly placed, compacted backfill, protective sleeves and structural support are
necessary to protect plastic pipe against shear and bending loads. Connections should be protected
where are underground polyethylene branch or service pipe is joined to a branch fitting, such as a service
saddle, branch saddle or tapping tee on a main pips, and where pipes enter, r exit casings or walls.
Properly perly placed, compacted backfill and a protective sleeve or a structural support are generally used
t gather. Whether or not a protective sleeve, r a structural support is installed, the area surrounding
the connection uust be embedded in properly placed, compacted back fill to ,protect the, polyethylene
pipe against shear and bending loads.,
For additional information ant protecting against shear and beading load's at service or branch
connections and where PE, pipe penetrates a structure or eaters or exits a casing, see the Performance
Pipe Engineering Manual and ATM D 2774, Underground Installation of Thermoplastic Pressure,
In .
Liquid Hkdrociarb,on Permeation
When Present, liquid hydrocarbons may permeate (solvate) polyethylene yl'ene pipe., L,i uid hydrocarbon
permeation may occur when li�quid l y 'r ar + ns, are present in the pipe when soil surrounding the pipe
is contaminated with liquid hydrocarbons, or when liquid hydrocarbon condensates forms in gas
pipelines. All types of liquid hydrocarbons (aromatic, paraffinic, etc.) have a similar effect, and the affect
on different polyethylene pipe rains is essentially,the same, Heat fusion joining to permeated pipes may,
result in a low strength joint and is not recommended'.
Liquidhydrocarbon contamination is indicated by discoloration, by a hydrocarbon fuel odor, or by a
rough, sandpaper-like,,e, bubbly, or pockmarked surface when a fusion, heating iron is removed from the
pipe surface. See the Performance Pipe Engineering Manua for additional information on permeation
and chemical resistance.
CAUTION-Once polyethylene ' e has been permeated with liquid hydrocarbons, heat fusion or
es Joining is not recommended because liquid hydrocarbons can leach out during
heating and contaminate the Joint® Liquid hydrocarbon a xc el polyethylene � eshould
IN
joined using suitable mechanical connection methods.
Mechanical fittings must be installed in, accordance with the fitting manufacturer's instructions Obtain
these, instructions from the fitting manufacturer.,
Bulletin: PP 3103April 2006,Su!percedes all previous pub4cations
Page 3,of 11 0 20,01-2006 Chevron Phillips hemi al Company LP
w
A Diviva OF Own hawn wo)Comput V
www.performancepipexom,
Locating
Polyethylene materials are not detectablewith standard netic locating equipment. To aid. in the
detection of un ' rg round ,piping, measures such as, tracer wires, identification and dete'dion tapes,
lire markers electronic marl r systems, a stir pipe tracing, sand ��call before you dig" Brie, location
measures may be used. Where posted signs are used, the signs should indicate that the pipeline is
polyethylene to alert.locating personnel that the pipeline may not be detectable with standard locating
equipment. Gas utilities in the area should always, e contacted' before the start of any underground
installation ation work such as excavation, trenching, dire tion al boring, etc.
Jn
, .T Regulations require that:
Each lilt in as gas piping system must be r ire acc r sacs, with ritt n pr c tur s that
have been proved by test or experience to produce strong sti hit joints 9 CF , Part 192,
§1 92.273(b)),
Written procedures for butt fusion, saddle fusion,, and socket fusion joining ly thylene gas
piping, rust be qualified be�fore use by subjecting specimen joints, to required test procedures
(CFR 4,9, Part 192, §192.283(a)).
All persons, who ra ke "loi�t irr� � cth lene gas ,piping must e quallifled under theoperator's
written procedures (CAR 49, Part 92', & §192.285(a)).
The gas system operator must ensure that all persons who make c or inspect Joints are qualified
i(CF�R 49, Pad 192, § 9�2.25 & § 9 .27�I.
Performance i recommends ends asing Performance Pipe Bulletin I- 50 Performance Pipe Fusion
Joining Procedures when making heat fusion, joints with YE WS,T l " " 83010 piping. Contact your
Performance Pipe Territory Manager, w .,per crr ancepipe.cc ,, or Distributor for a. copy. When used
to join Performance Pipe polyethylene gas, piping, Performance Pipe fusion joining procedures are
qualified in accordanc ith U.S. Department f Transportation Regulations.
CAUTION Performance Peel polyethylene piping products cannot joined with aldhesives or
solvent cemeinti. Pipe-thread Joining and joining by hot air (gas) welding or extrusi n welding
techniques are not recommended for pressure service. Melded outlet fittings, are intended
for butt fusion andmay niot be suitable for joining with mechanical stab fittings or mechanical
fittings that require ID stiffeners.
S � e-Off
See above Cautions on S a c Electricity. S cei ie-off (pinch-off) is used' to control flow in PE pipe
by latt ring thepipe between parallel bars., Squeeze-off is used for routine, and emergency situations.
Do not squeeze-off more than once at the same point on the � . For r repeated', flow control,
throttling, r,partial flow restriction, install a valve or an appropriate! low control e i e.
Complete flow stoppage will not occur in all cases. For larger pipes, particularly at higher pressures,
some seepage is,, likely. If seepage is not permissible, the pipe should be vented in-between two
squeeze-offs.
a
Bulletin:PP 300 April 2,0,06,Super Supercedes all previous publications
Page 4 of 11 0 2 -20,05 Chevron Phillips Chemical Company P
LL PERFORMANCEPIPE
www.performancepipe.com
Use squeeze-off procedures ,meeting ASTM F 1041 and tools meeting ASTIVI F 1563 with Performance
Pipe polyethylene pipe. The combination of pipe, tool andsqueeze-off procedure should be qualified in
accordance with ASTIVI F 1734. correct tool closure stops and closing and opening rates are key
elements to squeezing-off without damaging the pipe. Tool closure stops must be correct for the pipe size
and wall thickness SD . It is necessary to close slowly and release slowly, with slow release being
more important. See Performance Pipe Technical Note PP-801 Squeeze--Off y
Performance Characteristics
Polyethylene Material Properties
Cell Classification - YELLOWSTRIPE@ 8300 piping is manufactured from premium high performance
bimodal polyethylene compound that is classified according to ASTIVI D 3350, Standard Specification for
Polyethylene Plastics Pipe and Fittings Materials. The cell classification number for Performance
PipeYELLOWSTRIPEO 8300 material is 445576G.
Long-Term Strength - Performance Pipe YELLOWSTRIPEO 8300polyethylene piping compound
is listed with the Plastics Pipe Institute as PE 710 and as PE100. It also has PPI recommended
Hydrostatic Design Basis HDE ratings of 1600 psi at 730F 1 . 3 Wa at 23°C and 1000 psi at 1 0°F
(6.89MPa at 23°c . Elevated temperature properties can be used to determine product capaMbilities for
applications where products will be exposed to elevated temperatures.
In addition to ASTIVI D 2837 and PPI HD8 requirements,YELLOWSTRIPEO 8300piping meets ISO 9080
Thermoplastics Pipings for the Transport of Fluids-Methods of Extrapolation of Hydrostatic Stress Rupture
Data to Determine ermin the Long-Term Hydrostatic Strength of Thermoplastics Pipe Materials requirements with
a M S of 10.0 Wa (1450 PSI) at 2 ° / (680F). Thus, it is a fully qualified PE 4710 and PEI 00 product
and is listed as such in PPI TP ,
SCG Resistance - Resistance to slow crack growth is a critical performance requirement becauselong-
term stress can cause cracks to grow slowly through the material. Polyethylene gas pipe is under long-
term stress from internal pressure and earthloadin . Thus gas distribution service requires materials that
have superior long-terra resistance to stress cracking and slow crack growth (SCG).
For many years, environmental stress crack resistance (ESCR)tests, such as ASTM D 1693, have been
used to characterize resistance to cracking from long-term stress. But exceptional materials such a
YELLOWSTRIPEO 8300piping rarely fail ESCR tests. For these superior materials, ESCR tests are
incapable of quantifying long-terra resistance to SCG.
In recent years, new SCG tuts have been developed. Predominant among these new tests is ASTM F
1473, the "PENT" test (for PEnnsvIvanja 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 PEAT performance and long-term
service,,
Under ASTIR F 1473, Standard Test Method to Leasure the Resistance tar ce to Slow crack Growth of
Polyethylene Pipes and Resins, typical performance of the resin used to produce YELL STRIPE
0000 pipe is greater than 5000 hours before failure. ASTM D 2513 requires that PE materials average
at least 100 hours before failure when tested per ASTM 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 Apr[2006 Supercedes all previous publications
Page 5 of 11 2001-2006 Chevron Phillips Chemical company LP
I'I
PERFORMANaPYPE
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RCP Resistance - In recent 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 Resistance to Rapid Crack Propagation - Full-Scale
Test FST and ISo 13477 Thermoplastics Pipes for the conveyance of Fluids -De termination ion of Resistance
o Rapid Crack Propagation - Small-Scale Steady State Test (S4 hest). At a specified temperature, these
tests are used to determine a critical pressure above which IGP may occur. The full-scale test is used with
large diameter(greater than 250 r r . in pipes and the S4 test with small diameter sample pipes having
wall thickness greeter than 15 m o. in).
Although ASTIR D 2513 does not currently have an RCP requirement, ISO 4437 Burred Polyethylene Pipes
for the supply of Gaseous Peers - Metric series - Specifications, specifies that the critical pressure for gals
distribution pipes rust exceed 1.5 times the maximum operating pressure at 'C 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.
AS TM Test values
The chart below shows material physical properties,ASTIR test methods for the property, and nominal values
for YELL OWST R1 P EO 8 30 0 PE340 71 o PE100 pol yeth ylene materials.
rt
Test Procedure I
PE 34081
PPI Listing Designations PPI TR4 PE 471 1"
PE 10
Cell Classification I AST I D 3350-051 445576C
Density glfcc. .. ASTM D 1505 6. 61 (black)
Melt Flow, MI 2.16 Kgl19 ° 11 omin I ASTIR D 1238 0,11
Melt Frew, MI21.6 K /1 ° m/1 Omin ASTIR D 12 8.00
Thermal Expansion/Contraction inlin1°l= ATE D 696 WO-4
Flexural Modulus @ %strata psi ASTIR D 790 140,000
...........
Tensile Strength a@ field psi ASTIR D 638 >3500
Slow Crack Growth(PENT) hours ASTM F 1473 560
Color; UV Stabilizer % AST D- 350
Elastic Moduluspsi AST D- 200,000
...............Brittleness Temperature OF ASTM D 7 -16 -1 1
icat So tening Temperature °F ASTM D 162 55
.
HardnessShore D ASTi D-2 5
Hydrostatic Design basis @ 7 °F °C psi ASTM D 27 1606
Hydrostatic Design Basis @ 14 OP 6 ° psi STM 2837 160
Minimum Required Strength(I RS)@ 2 ° 66#F [IriF'a psi IS09080 >10 1 5 .......
Rapid Crack Propagation (RCP) bar(psi) lS 1 377 12 bar � 4 si
Critical Pressure Pe , ° p p
F)
Critical Temperature Te ,6 bar D !� 1 477 -17 2
1. YELL WSTRI PEO 8390 pipe material is listed in PPI TR-4 for use in€natural gas distribution.
2. Meets new requirements for PE4710 material.49 CFR Part 192 references older versions of the standard that do not yet recognize
the new requirements and carry the P 3408 designation. The pipe will be deal marked as long as required by 49 CFR Part 19 .
Previous versions of ASTM D 3350 would have assigned a cell classification of 345564C or 345566C,
4. Determination made on 8°DR 11 pipes. No failures occurred. Pc calculated In accordance with ISO 13477 Annex C cone€ation.
S. NOTICE-This chart provides typi al physical property information for polyethylene resins used to manufacture Performance Pipe
polyethylene piping products. It is intended for comparing polyethylene pipe resins. It is not 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 molded plaques and can vary from these typical values. Performance Pipe has made
every reasonable effort to ensure the accuracy of this chart,but this chart may not provido all necessary information,particularly Wth
respect ko special or unusual applications.
Bulletin:PP 303 April 2006 Supercedes all previous publications
Page 6 of 11 @ 2001-2006 ChevronPhillips Chemical Company LP
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Permeability and Permeation
Plastics are permeable to gases to varying degrees. Although the constituents of natural gas can
permeate through polyethylene, the volume of gas lost through permeation' is generally so lour 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 methane, the primary constituent of natural
gas, as 4.2 x - . lasing the AGA factor, one rile of SDR 11 HDPE pipe carrying 00% methane at 60
psi would lose less than 0.27 ft3 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 i
o low 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 hlghertemperature , liquid h ydr carbon per neation m ay cause some sweIIing.
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 foam in gas pipelines. At lour temperatures and higher pressures, heavier
hydrocarbon gases such as propane or butane may condense and liquefy in the pipe. Such condensates
are known n 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 1s used to compute the Design Pressures for YELLOWSTRIPEO 8300 polyethylene
piping systems for natural gas service at operating temperatures up to but not over 4 'OF 60°C . For
operating temperatures below 730F 23°C , use 3°F 23°C Design Pressures.
S
= '
(DR -1
where P Design Pressure in pounds per square inch garage (prig ;
Long Terra Hydrostatic Strength (Hydrostatic Design Basis) stress, psi, at
pipeline operating temperature;
yrefee Der '.or Hydrostatic
Temperature S, psi �1a)
14 °F *C 1 .
HDB per ASTM D 2837&PPI TIC-3. t Interpolated in accordance with PPI 18.
DID = Dimension ion Ratio
R
Pipe Nominal Outside Diameter
Pipe Minimum Wall Thickness
f Design (Service) Factor
Bulletin:PP 303 Apr[2006 Suparcedesall previous publications
Page 7 of 11 0 2001-2006Chevron Phi[lips Chemical Company LP
r
Imp-
A iri'va of 0acraY Ai ups Own Comaw!P
www.performancepipe.com
ancepipe,corn
ApplicationDesign(S 'rVIC Factor, f
Gas distribution and transmission per CFR 49 Part 192, 192.121 0.32
Gas dist6butlon and tr nsr lsslon In Canada per Cs 2-96
Gas dist b ti n or transmission piping that is permeated by solvating Chemicals such
as liquid hydrocarbons or liquefied gas condensate
Operating Pressures (psig)'
The following chart provides maximum allowable operating pressures i P and recommended
maximum design pressure rating (PR) for YELLOWSTRIPE@ 8300 pipes for gas distribution service at
the indicated operating temperatures. YELLOWSTRIPEO 8300 pipes with the same DR but different
outside diameters have the same Design (Working)ing Pressure Ratings. Pipe minimum wall thickness is
determined by dividing the pipe average outside diameter . . by the DR number.
Pressure ratings are calculated in accordance with applicable U.S Federal codes. A check should be
made to determine if these pressures apply under the state and/or local codes governing the specific
application. Use 73°F 23°C pressure ratings for operating temperatures below 7 * 23°C , It should
be noted that while YELLOWSTRIPE Soo pipe is produced from PE 7 0 0 PE100 pressure rated
materials, the PE 710 and PE1 oo 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.
MA OP #aximum Design Pressure Rating(PR)t for Dry Natural Gas Service—YELLOWS TRIP 3 0 Pipes .
.'Service �3 0
Tamp .F 2 .. . 6 C
!Pipe DR
A P(Max Design M P(Max Design .. MA P(MaxDesign . - DP(Max Design
}'PR% ps f f
.. . 125t 16 12 t 1 11 8t 0 1 .1 02t
:9. 1 2t 1 opt o
9.3 12t12 103f1 9 9 ) ,...77(7
:
Class 1,2,3,and 4 locations per U.S.federal regulations using 0.32 Design(service)Factor. For pressure ratings at 0.40
.design factor(Canada only), multiply by 1.2 ; for pressure ratings at 0.25 design factor,multiply 0.78. t where the pipe
can be,rated at 125 prig or higher, U.S. Federal regulations limit gas pressures in plastic pipe to 123 psi max€r um unless a
waiver for higher pressure has been granted.
Bulletin-PP 303 April 20 Supercedes all previous publications
Page 8 of 11 2001-2006 Chevron Phillips Chemical Company LP
PERAMM4NCEPIPE
www.performancepipe.com
Cold Sending Radius
The allowable cold beading radius for YELL WSTI IP '*@ 8300 pipe is dependent upon the pipe OD,
DR and the presence of fittings in the bend.
R Allowable Cold Bending Radios
r less20 tunes pipe OD
.to.13... :25.fim.es.pipe.0 0 .
Fitting or fl ange present in bend 10 tires pipe OD
Fluid Flow
Formulas for high pressure and low pressure gas flow in polyethylene pipe are presented in the
Performance Pipe Engineering Manual, and in Performance Pipets free PlexCalcO program for personal
computers.
Outdoor storage
The recommended maximum for unprotected outdoor storage of YELLOWSTRIPEO 8300 is twenty
years.
Propane (LPG) Gas Service
The Office of Pipeline Safety Advisory Bulletin No. 3- , 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 safety standards do permit the use of plastic in a properly engineered underground system of
.PG distribution conforming to the limitations of these regulations.' YELLOWSTRIPE@ 8300 piping
products meet the requirements of ANSI NFPA 58 Standard for the Storage and Handling of Liquefied
Petroleum Gases.
The Plastics Pipe Institute has made the following "Use Recommendation" for polyethylene piping
systems for commercial propane systems:
PPl 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
based on propane gas should be adequate and reasonable. However, until more information is
available, these use recommendations cover only commercial propane vapor in detail.
1. The polyethylene plastic pipe, tubing and fittings should be only those specific types designated
as PE 2406 or PE 3408and meeting the appropriate requirements of ASTM D 2513.
2. A Hydrostatic Design Basis of 1000 psi should be used in the design of polyethylene pipe
systems for propane gas distribution at pipe temperatures of 730F or lower. The long-tern
hydrostatic strength measurements should be made in accordance with ASTM 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 Supercedesall previous publications
'age 9 of 11 Q 2001-2006bewon Phillips Chemical Company LP
PERFORAWdPIPE
It S also cmee thatpressures ,
In cases where condensation does occur in a propane system or propane enriched system and the
presence condensation is of relatively abort,duration, th r is no indication of loss,of physical integrity
r observable change in polyethylenepipe, Under actual riating, conditions, in a properly designed
system, the pressures, andtemperatures, are such that revaporization 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'p,ropane condensate on polyethylene.
For additional information, see PPI Technical Report TR . 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 Perfbrmance PikeEngineeringManual for a "i i ; i
Information.
Performance 'i e YEL,LOWSTRIPEO 83003 8/4710 PE100 polyethylene gas,pipig may be use
In propane gas service when used in accordance with the above recommendations.
Bulletin:PP 303 April 2006 Supercedes,all previous,publications
Page 10of 11 @2001-2006 Chevron Phillip Ch: r lcal Company IMP
1
I I M
A viSto ti 0 f 0ii vR o ii Pin hips(Hfhri c,4 i PA it I P PERFORMANCE PIPE PLAITS
CONTACT INFORMATION: PERAORM"CEAPE
PERFORMANCE PIPE
divisionf
Chevron -
:+n:;.:°
PO Box 269006
BlavrNid
x
............. .....:.......
Broyjnv*cd,TX
Far€idd
t
Piano, TX 75026-9006
:..:..:...:.n... :..............::............:.::: .......:.....
P-YEW,09
T rRtnG,IN
product information
cart sc
'technical jai assistance-
or
kiL1S 'R9 {
Phoned
Falk: 972-599-7348
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Strategically Located Plants
PLASTICST1 * NST1T T � To Better Serve Your lee sl
PERFORMANCE PIPE
Product Literature
Technical Notes & Bulletins*:
PP 156 DRISCOPLEXO 6500 Series Piping Systems Size &Dimension Sheet
PP 157 DRISCOPLEXO 6800 Series Piping Systems Size &Dimension Sheet
PP 158 DRISCOPIPE@ 8100Series Piping Systems Size & Dimension Sheet
PP 159 YELLOWSTRIPEI@8300 Series Piping Systems Size & Dimension Sheet
PP 300 PE 2406 IDPE Pipe &Tubing - DRISCOPLEX&6500 Series Piping Systems
PP 301 PE 3408 HDPE Pipe &Tubing - DRISCOPLEXO 6800 Series Piping Systems
PP 302 DRISCOPIPE@ 8100 Series Polyethylene Piping
PP 304 Model Specifications- DRISCOPLEXO 6500 Series Piping Systems
PP 305 Model Specifications T DRISCOPLEXO 6800 Series Piping Systems
PP 306 M ode I Specifications- D R I S CO PIP 8100 Seri s Piping Systems
PP 307 Model Specifications -Yellowstripel@ 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 02-T l Leak Testing
PP 07-T Large Diameter Coiled Pipe
PP -Tip Tapping Tee & Purge Point Cep Tightening - Flat Ping Gasket
PP g -TN Tapping Tee &Purge Point Cap Tightening - --Ding
PP 09-TI Protective Sleeves and Tapping the Main
Bulletin:PP 303 April 2006 Supersedes all previous publications
Page 11 of 11 @2001-2006Chevron Phillips Chemical Company LP
*Additional product literature will be available upon completion. Visit Performance Pipe on the web for the latest completed literature.
PEMFORMANCEPYPE YELLOWSTRIPEO 8,300 Series
so
ize and Dimension Sheet
CT'S COFFER Tu�BE SIZE
Nominal' MAOP NumberNominal NIJI a MUWallM ' " INominalJoint er,ht Coil PackiDimensionsng � Pallet
Size �
Number
Dimension per CF PartCulls/douu�1Bundle Pallet 8 .
1 Ia r ter lu 1 Per Pallet t r BundlesTruck
Inch Ira h (Inches) or less, 110 1 (feet) ID/' /Width Bundle Footage Per Truck
I
.1 1 DR 11.4 100 14
� j
�.1 R 11 1a
1.125, .121 DR 9.3 123 1 00' 301" 4 " 11 8 4, 26 1 4",0 "
0.161 DR 7.0 125
3 72
1 114'" 1.3090 0.12,11 DR 11.4 99 21 ' '' " 45" 141121M , ! ' 24 72,000"
ips"N"ARON PIPE S12
Number Number
r
Nominal � 1�11r�lr��a�um, 'Weight Coil Nominal min Pallet 1
ua +�rrsiru Outside per Fly Part ells�Joints Pallet 1 48 ft.
"i� �' l'JI per Jwlu�t Clruu�slu"�s Bundle
Ratio Diameter 1 �1 Per Pallet r Bundles Truck
Ilradhes (Inches) (Inches) r le 1 ft (feet) l 1 /Width Bundle Footage
Per Truck
DR 7 .1 , 125 1
DR 9.3 1. 1 .141 1 3 ,fir 30"144 7 12" "
D' 11 0.'1 1 �"+fi b' " ,
DR 7
, 4 ,
0.339 12
11 0.,2116 10 64
1 5, 27' 4 ' soft bun l s 29 1,1 14 1 " 40'.,50
bundles,DR,
1,0001
4O soft 13, 5,20 6M DR 116.625
14 , '
1 1 W� um41 � 4160 4 �'1 0 /5 '" Uprightprr ;ht 4,0010"
DR 9 . 1 '5 111
" D DR 11 8.625 0.784 1 49 4 ' soft bundles 9 3,60' 10, 3" '
DR 13.5
DR 11 1..1 59 100 1 55
1 " DR 15.5 12.750 '1 1357 407 bulk packs 8 jis/layer 3 ' 6 1 920'
DR 21 0.607 51 1 ,1
1 DR 11 16.000,.000 1.455 100 2921 "
DR 1 . 4�1 64 11
4 uilk peace ats11 a er 4 " 1" '
1 w, DR 13.5 18.000 1, 3 82 3071 Available upon,rat
LDR 17.0 L1.0591 64 2482
Other sizes and packaging configurations may be available. Pipe weightsare calculated in acc,lor ncewith T - .
Petformiance Pipe,a dI^ sl n of .performancepi pe.com Phone: -57-
ri Phillips Chemical Cmpany LP Fax: 7 - , -7 4
Bulletin:PP 159 August 2013 Supersedes all previous publications
Page 1 of 1 @2012 Chevron Phillips Chemical al Company L,P
wtl
TRANSITION FITTINGS WELD END
gyp, FOR RE FER EN'!E ONLY
Sh&Ane e,,OK USA 74501 Fax 60,0-733-5S931
z
I. Y� M13............................ ,
EXPOSED POLYETHYLFINE OALSTEEL
,.............
DOSED ST,EEL xM,40
S '.
W,
" Po..y v,^x rm ��rY' �,�,A.�r;F�.�%.�wm�b,�vu hMx.7 7,�,,.M../. ,����,hw,dw.'w!V✓vun. J�..`
I.D. 1 . _ O.D.(MAX.,)
PLASUC CAPS
TYP.EACH END ADAPTER
RETAINER
NOMINAL DIMENSION DIMENSION DIMENSION DIAMETER DIAMETER DIMENSION
SIZE A 8 c D E I
STEAL x PLASTIC EXPOSES PLASTIC L STEEL EXPOSED STEED: RETAINER, EPDXY COATED BLOCK BACK
3/411 1/2"C S L L. 0.. 12.14 12.67 111,56 0.324 24 1.390
26.67mm x 15.88mrmm 308.36mm 321.82mm 293.62,mm 8.23rnm 35.31mm 5 , m mrm
/4""X 1/ "IP SD' r .11.81 12'.88 11.56 0.516 1.390
i
. 7mr'mm x,21.34mm 29,9.97mm -32,7.15mm 293.62nim 1 .'11mmtn 3531mm 5,0.80mm
i
/4"'x 314"IPSSCAR 11 11,81 12.88 11.38 0.630 1,453
f
i
.. 7rnm x 2 . 7mrmm 299.97nim, 327.1,5mm 289.05,rnm 1 .010M m, 36.91mm. 50.80mm
.40m rn x 5 .4 mm 302.26mm 334.26mm mrm 20,7'5mm 43,26mm 50.80 mmrm
/' 'l 1141"P 1 1 11 11.94 1 .44 111,.44 1.056 2.070
42.16mm x 4 .1 m rm 303,28rnm 3411.38mm mm 26.82mirn 52,58mm 50.80mm
1 1/ "x 1 1/2 1 �S SDI 11' 12,03 11616 11.44 1.322 2,317 2
48.26mm,x 4 .2 m mrm 3051.56inim 346.,96mm 290.58mm 33.58mm 58,.85mm 50.80mm
2"x 21PS all 11 12'.16 13.78 11.44 1.625 2.7010
0.3 mm x 6,0.33mm ® mm 308.86,mm 290.58mm 41, " mm 68.58mrn 50,80mm,
W 11PS(SDR 111 or 11.5 11.9714.84 11.6'9 2.360 4.080,
88.90mm x 88.,90mm 304.04MM 76. 4 mmrm 296.93mm 59.,94mm 10 . 3 mmrm 50. 0mrmmm
i
495 "4. 5 ' 2
114.30mm x 114.30m arm 3106.32mm 377,95non296.93,mim 75.06mm 125.73mm 50.80mm
"x 6"IPS(SDR 11 or 11. 17.40 17.90 11.69 4.985
1,68.28mm x'168.28mm 441.96rnm 464.66mm 296.93mm 126.62mm 1 ' .18 mm 50,,80m,m
"" ""IPS SCR 11 or 11. 4.44 22'.88 151,311 6.482 9.590,
168.,28mm x 1,14.30mm 620.78mm 5 1.15mrmrm 38,8.87mm 1 44, 4mmxm 2413.59mm 50.80mm
7I M I mmmrm 7 .I0 mrn 571.50MM 688.09mm 446.02mm 202.49mm 294.511mm 1 1, rrmrrm,
1 "x 1 "W (80 11 or 11.. ) 201.44 27.88 16.311 .71 ' 14.100 4
t
1 .28 m,m x 114.3 m rn 619,18MM 708.1,5mm 414. ' rnm 246.79ITIM 358.14mM j 101.1 0 mm
Items h n are standard sizesn wall thicknesses.Fitting sizes anther than those sh n,oan be furnished ul mm request.
511512003
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x
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Polyethylene Ball Valves
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41
.r+ ..6..�.: t'i�':••fix �' �.,;� } -F":.�� F}�� � F- i� Y>
.71
uROEN
thru 16"
# `
Size Range with Larg''--'e' st Port Offerings)
for Worldwide9Appli '{U lations
BR(OEN
www.broeninc.com
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Material Table
ComponentMaterial
BodyPolyethylene (PE)
2 End
Polyethylene (PE)
Ball
Polypropylene P
Ball SeatNBR Rubber)
Supporting RiniPolypropylene
8 Stern Aetl
High Impact Wrench Adapter PP (Polypropylene) Plus FRP
Stem -Ring NBA Rubber
9 Adaptor Ground Water Seal NBA Rubber
General Information for Gas and Water
Item
............
Operating eifiis
For Gas For Water
Resin TR-418Y PE 2406 (PE80)
TR- 80 3408 1 ` R- 80 3408 oo
Temperature Range -20T to 140T
Pipe ConnectionButt Fusionr otre Fusion
BoreFull Bore and Standard
Stem ' fie Short stem or Extended (Long)
Standard Dimension Ratio (SDR) :
r as Specified
Open/Close turn
a
BROEN Makes the cision Easy Agai
"The Natural Choice"m BROEN BALLOMAX0 PE Valves
Over 50 Fears of Engineering Excellence
41 Largest Port Offering In the industry
Extra High Impact Operating Nut
* Full Size Range 2"-
* Fully Tested and Qualified
Meet or Exceed ANSI B.16.40
" Meet or Exceed ASTM D2513S DOT Part 192
" ISO 9002 Approved
Available in Medium or High Density Polyethylene
Easy Ordering
Manufacturer Size Por ResintSOR
Density
2
BROEN �� F1 As Specified
r �-
BALLOMAXII, "to 16" 1pS r M di 0 719,93t 1 1
h=3408B
or C � Re ed- .6
Service
n Psig and bar for service temperatures up to 7310F
PE 2
SDR psig bar PsIg bar F
9.3 96 6.6
0
�. 100 6+
Gear O it l
I OIJ
WNil Gear Op. iv
D
rr -._,..t ....+.,.+t��k����T..........*�•
M1 ..
7.
:-.:.. ..
00......
M1
4
..........
... ......'
..........
.00 12-06 30.07 18.67 39.37 219.3 `.
Method
Seat Test y
y... .".:'..:......
........ it
Air Seat Test
.3 bar (4psi) k.
:ry.. 10.4 bar 5si `
.3 bar (4psi)Shell Test Air Test Under rater °.k
O.4 bay 1 -_-
Valve Operated times t Full Differential .3 bar s�
:.::. Operational Test 'S
.=. Pressure t -29 C and 38 C (-200'Fand I OOOF) bar 5 si
r q t
for �� �` � t�r� Tor � 8 �
bar (11-2 and 1 'DFi
1000 Hour SLIst i Seat 230C and 88°C f
Test
(74"F
and
.8 C `i 8.6 r (265psl)PreSSUre �.�
1000F)
38"
14.8 bar (215ps!)
High PresSUreTest �
8 Sustained Hi Pr i .
x;
:: Full Test Hydraulic �� 1~ *
E.. Elongation i Full + :.
xr y
:. 1 ' ;. :.
.': -2537 8 0 8-73 Tel: 2 5-958- 44 Fax:2 -95842 37
;::r
F777 .......... .......... ........:.
...........
1/2 -.77.
..... ..
t
.. ,
:y. W! Nut Operator �"
IRW - t.- -
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2
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mPerial .. ................:.....
:We!6'ht,-
.............
S.
...................
. ..............
... ..
..............
2 0.63 1.7
3/4 1.02 1.05 4.06
1.6
ice+8
�r
NW
01.31 1.13 6.42
#
8
1 1/4
[ }3 } 2 �.
21
2 1.81 2.38 9.09 6.09 5.13 -91
.1
3 2,76 3.50 9.07 10,64 6.98 27.76 13.2
................
4 3.54 4.50 '10-20 12,61 8.07 29-10 26.4
6 5.24 6,60 8.50 '16-80 10.00 29.45 61.3
8 6.89
8.63 9.60 22.36 13.94 31-85 94.9
A: ulhM Q-Mlet r of End 8:Les-91h of End(Spigot end
C,Top Of Pipe TO TOP of Operating Nut , ,,, to Operator Top
L.Total Len lh f Valve :Port Diameter
.Note-Standard� D I I r Spec i on Purchase �r j r
1.vr,:o;7 Y
F