1、Polyethylene Piping Distribution Systems for Components of Liquid Petroleum Gases TR-22 2013 105 Decker Court, Suite 825, Irving, TX 75063 P: 469-499-1044 F: 469-499-1063 www.plasticpipe.orgForeword POLYETHYLENE PIPING DISTRIBUTION SYSTEMS FOR COMPONENTS OF LIQUID PETROLEUM GASES This report was dev
2、eloped and published with the technical help and financial support of the members of the PPI (Plastics Pipe Institute, Inc.). The members have shown their interest in quality products by assisting independent standards-making and user organizations in the development of standards, and also by develo
3、ping reports on an industry-wide basis to help engineers, code officials, specifying groups, and users. The purpose of this technical report is to provide important information available to PPI on a particular aspect of polyethylene piping systems for distribution of liquid petroleum gases. This rep
4、ort has been prepared by PPI as a service of the industry. The information in this report is offered in good faith and believed to be accurate at the time of its preparation, but is offered “as is” without any express or implied warranty, including WARRANTIES OF MERCHANTABILITY AND FITNESS FOR A PAR
5、TICULAR PURPOSE. Any reference to or testing of a particular proprietary product should not be construed as an endorsement by PPI, which does not endorse the proprietary products or processes of any manufacturer. The information in this report is offered for consideration by industry members in fulf
6、illing their own compliance responsibilities. PPI assumes no responsibility for compliance with applicable laws and regulations. PPI intends to revise this report from time to time, in response to comments and suggestions from users of the report. Please send suggestions of improvements to PPI. Info
7、rmation on other publications can be obtained by contacting PPI directly or visiting the web site. The Plastics Pipe Institute, Inc. www.plasticpipe.org This Technical Report, TR-22, was issued in August 1998 and was revised in June 2006, and May 2013.POLYETHYLENE PIPING DISTRIBUTION SYSTEMS FOR COM
8、PONENTS OF LIQUID PETROLEUM GASES 1.0 INTRODUCTION Polyethylene (PE) gas piping is the most widely used plastic piping material for the distribution of natural gas. PE has a well-documented inertness to both the external soil environment and to natural gas. Extensive testing and over 45 years of suc
9、cessful field experience confirm that the long-term strength of polyethylene is unaffected by natural gas and its common constituents. Polyethylene (PE) piping systems complying with ASTM D 2513 have been successfully used in all types of fuel gas piping applications since the mid 1960s. These PE pi
10、ping materials have been continually improved throughout the ensuing three decades assuring the safe, cost effective, transport of fuel gases in residential, commercial and industrial applications. PE piping is the only approved plastic piping under NFPA 58, Liquefied Petroleum Gas Code, and is comm
11、only used in the piping of liquefied petroleum gases (vapor LP-Gas). To be Code-complaint, PE lines must transport gas only in a vapor state, and therefore, must operate at 30 psig or less to avoid LP gas liquefaction. Vapor LP-Gas is one of those fuel gases, which can be safely piped in PE gas pipi
12、ng systems. The use of D 2513 PE piping for the transport of vapor LP-Gas is permitted and codified under US DOT CFR Title 49 Part 192. By reference, Part 192 identifies ANSI/NFPA 58 as the installation standard for PE vapor LP-Gas piping systems. NFPA 54 / ANSI Z223.1 National Fuel Gas Code paragra
13、ph 2.6.4 also refers the user to ANSI/NFPA 58 by stating “The use of plastic pipe, tubing and fittings in undiluted liquefied petroleum gas piping systems shall be in accordance with Standard for the Storage and Handling of Liquefied Petroleum Gases Liquefied Petroleum Gas Code, NFPA 58.” NFPA 58 pl
14、aces certain restrictions on the use of PE piping for vapor LP-Gas distribution. NFPA limits the size of PE piping to 2” NPS piping with a nominal OD of 2.375”. Furthermore, NFPA 58 limits the maximum operating pressure of PE vapor LP-Gas piping systems to 30 psig. The reader should refer to NFPA 58
15、 for the details of these and other installation requirements. 2.0 BACKGROUND The components of liquid LP-Gas are known to have short-term, reversible effects on PE gas piping. At low temperatures and high pressures, vapor LP-Gas will condense into a liquid state. The effect of liquid LP-gas is to l
16、ower the long-term strength capabilities (hydrostatic design basis) of PE gas piping, as summarized in Table I. These data were obtained on a PE 2306 piping material. It is therefore prudent to limit the operating pressure (stress) when using PE gas piping to transport vapor LP-Gas. In addition, vap
17、or LP-Gas systems operating within particular temperature and pressure guidelines are less likely to produce condensation. Many PE gas-piping materials have been evaluated to determine their long-term strength using vapor LP-Gas as the pressurizing medium. A design factor of 0.25 (chemical design fa
18、ctor of 0.5 times service design factor of 0.5) has thus been established for PE piping in vapor LP-Gas service. As stated above, NFPA 58 prescribes the established pressure and design limitations. 3.0 USE RECOMMENDATIONS a) Any plastic material to qualify for use as a vapor LP-Gas piping system sho
19、uld be recommended by the manufacturer for such use, should be qualified using vapor LP-Gas as the medium, and have a hydrostatic design basis (HDB) category of at least 1250 psi (8.6 MPa) at 73F (23C) as determined by test method ASTM D2837. All PE piping systems complying with ASTM D 2513 meet the
20、se criteria. b) The vapor LP-Gas PE piping system shall be made from PE materials specified in and manufactured in accordance with ASTM D 2513. c) To determine the maximum use pressure in vapor LP-Gas distribution, a design factor of 0.25 is recommended (see also PPI TR-9 on recommended design facto
21、rs) to derate the PE materials hydrostatic design basis (HDB) as listed in PPI TR4 and determined in accordance with ASTM D 2837. This design factor is more conservative than the 0.32 design factor used for PE piping used in natural gas (methane) distribution systems. ASTM D2513 states the following
22、, “X1.7.2.1 However, it has also been shown by the above referenced studies that propane, propylene and butane, when in the liquid phase, can cause a greater reduction in long-term strength, up to 40 %. Accordingly, the use of PE piping to convey LPG gaseous fuels should recognize this effect and th
23、e design and operation of such piping should consider the possibility for the occurrence of condensates. Extensive experience has shown that the NFPA maximum recommended operating pressure of 30 psig for LPG systems (see X1.3.4) both minimizes the possible occurrence of condensates and gives adequat
24、e consideration of the effect of LPG fuels on the long-term strength of PE piping.” d) With the exception of PE piping in anodeless risers, PE gas piping and fittings should only be used in underground distribution systems designed to operate at internal pressures and temperatures such that condensa
25、tion will not occur. Condensation is unlikely at the temperature and pressure combinations shown in Table 2. e) It has been reported (1, 2 and 3) that during the heat fusion joining of PE piping that has been in service conveying fuel gases that consist of, or that include heavier liquid hydrocarbon
26、s, the PE surfaces being heated in preparation for fusion sometimes exhibit a “bubbly” appearance. This bubbling is the result of the rapid expansion (by heat) and passage of absorbed heavier liquid hydrocarbons through the molten material. Heat fusion (butt, socket, saddle, or electrofusion) joint
27、strength may be reduced by the presence of the heavier liquid hydrocarbons. Pimputkar et al (8) conclude that for a system operating at 50 psi and conveying a mixture of as high as 16 volume percent in methane the liquid propane concentration in PE will be under 0.2 percent, sufficient to sometimes
28、show some bubbling, but not high enough to effect any significant degradation in fusion strength. However, if the concentration of propane in PE exceeds 0.2 percent, there is the risk of a rapid and large drop in fusion strength. Field tests to verify the level of contamination and subsequent degrad
29、ation of joint strength are not currently available. Therefore, in the case of PE pipe that has previously been installed in these types of services, one should use mechanical fittings to join or repair the pipe. (1) Sudheer M. Pimputkar, Barbara Belew, Michael L. Mamoun, Joseph A. Stets, “Strength
30、of Fusion Joints Made From Polyethylene Pipe Exposed to Heavy Hydrocarbons”, Fifteenth International Plastics Pipe Symposium, Lake Buena Vista, Florida, October 1997. (2) S.M. Pimputkar, J.A. Stets, and M.L. Mamoun, “Examination of Field Failures”, Sixteenth International Plastics Pipe Symposium, Ne
31、w Orleans, Louisiana, November 1999. (3) Gas Research Institute Topical Report GRI-96/0194, “Service Effects of Hydrocarbons on Fusion and Mechanical Performance of Polyethylene Gas Distribution Piping”, May 1997. Table 1 Summary of Stress Rupture Data for PE 2306 Pipe (This testing was conducted on
32、 early vintage Aldyl “A” pipe that was designated PE 2306) Test Medium NPS, Pipe Sizing Wall Thickness LTHS, psi HDB, psi Methane Vapor 2 0.070”, (DR 34) 1390 1250 (LTHS 1200 to 1530) Propane Vapor 2 0.070”, (DR 34) 1140 1000 (LTHS 960 to 1200) Propane Liquid 1 0.119”, (SDR 11) 800 800 (LTHS 760 to
33、960) Propylene Vapor 2 0.070”, (DR 34) 1210 1250 (LTHS 1200 to 1520) Butane Liquid 1 0.119”, (SDR 11) 850 800 (LTHS 760 to 960) Liquid Condensate 1 0.119”, (SDR 11) 650 630 (LTHS 600 to 760) Table 2 Temperature and pressure Combinations Where Condensation Will Not Occur Temperature F (C) Maximum Pre
34、ssure, psig (kPa) Maximum Pressure, psig (kPa) Propane Butane 10 (-12.2) 30 (207) 20 (-6.7) 40 (276) 30 (-1.1) 50 (345) 40 (4.4) 60 (414) 2.5 (17) 50 (10.0) 75 (517) 5 (35) 60 (15.6) 90 (621) 10 (67) 65 (18.3) 100 (690) 14 (97) Note: Varieties of LPG bought and sold include mixes that are primarily
35、propane (C3H8), primarily butane (C4H10) and, most commonly, mixes including both propane and butane, depending on the season in winter more propane, in summer more butane. APPLICABLE CODES AND STANDARDS ASTM D 2513, Standard Specification for Thermoplastic Gas Pressure Pipe, Tubing and Fittings. ASTM D2837, Standard Test Method for Obtaining Hydrostatic Design Basis for Thermoplastic Pipe Materials or Pressure Design Basis for Thermoplastic Pipe Products NFPA 58, Liquefied Petroleum Gas Code
