CHAPTER 12 FUEL PIPING

CHAPTER 12 FUEL PIPING.0 Scope of Gas Piping..1 (A) Coverage of Piping System. Coverage of piping systems shall extend from the point of delivery to the appliance connections with each gas utilization device. For other than undiluted liquefied petroleum gas systems, the point of delivery shall be considered the outlet of the service meter assembly, or the outlet of the service regulator or service shutoff valve where no meter is provided. For undiluted liquefied petroleum gas systems, the point of delivery shall be considered the outlet of the final pressure regulator, exclusive of the line gas regulators, in the system where no meter is installed. Where a meter is installed the point of delivery shall be the outlet of the meter. [NFPA 54-12:1.1.1.1(A)].2 (B) Piping System Requirements. Piping systems requirements shall include design, materials, components, fabrications, assembly, installation, testing, inspection, operation, and maintenance. [NFPA 54:1.1.1.1(C)]. (C) Application. This code shall not apply to the following (reference standards for some of which appear in Chapter 14 [NFPA 54-12:1.1.1.2]: (1) Portable LP-Gas appliances of all types that are not connected to a fixed fuel piping system. (2) Installation of farm appliances and equipment such as brooders, dehydrators, dryers, and irrigation equipment used for agricultural purposes. () Raw material (feedstock) applications, except for piping to special atmosphere generators. (4) Oxygen-fuel gas cutting and welding systems. (5) Industrial gas applications using gases such as acetylene and acetylenic compounds, hydrogen, ammonia, carbon monoxide, oxygen, and nitrogen. (6) Petroleum refineries, pipeline compressor or pumping stations, loading terminals, compounding plants, refinery tank farms, and natural gas processing plants. (7) Large integrated chemical plants or portions of such plants where flammable or combustible liquids or gases are produced by chemical reactions or used in chemical reactions. (8) LP-Gas installations at utility gas plants. (9) Liquefied natural gas (LNG) installations. () Fuel gas piping in electric utility power plants. [NFPA 54-09:1.1.1.2()] () Proprietary items of equipment, apparatus, or instruments such as gas-generating sets, compressors, and calorimeters. (12) LP-Gas appliances for vaporization, gas mixing, and gas manufacturing. (1) LP-Gas piping for buildings under construction or renovations that are not to become part of the permanent building piping system that is, temporary fixed piping for building heat. (14) Installation of LP-Gas systems for railroad switch heating. () Installation of LP-Gas and compressed natural gas systems on vehicles. (16) Gas piping, meters, gas-pressure regulators, and other appurtenances used by the serving gas supplier in distribution of gas, other than undiluted LP-Gas. 12.0 General. The regulations of this chapter shall govern the installation of fuel gas piping in or in connection with any a building, structure or within the property lines of any premises up to five (5) psi (4.5 kpa), other than service pipe. Fuel oil piping systems shall be installed in accordance with NFPA 1. 1.0 Definitions. For the purposes of this code, these definitions shall apply to this chapter. Certain terms, phrases, words, and their derivatives shall be interpreted as set forth in this section, provided, however, that whenever the words gas meters appear, they shall be construed to also mean valves and those devices required for the regulation of pressure and the measurement of natural gas being dispensed for any building, structure, or premises. 1.1 Appliance Fuel Connector An assembly of listed semi-rigid or flexible tubing and fittings to carry fuel between a fuel-piping outlet and a fuel-burning appliance. 1.2 Bonding Jumper A reliable conductor to ensure the required electrical conductivity between metal parts required to be electrically connected. [NFPA :0.1] 1. Fuel Gas Natural, manufactured, liquefied petroleum, or a mixture of these. 1.4 Gas Piping Any installation of pipe, valves, or fittings that is used to convey fuel gas, installed on any premises or in any building, but shall not include: (1) Any portion of the service piping. (2) Any approved piping connection six (6) feet (1,829 mm) or less in length between an existing gas outlet and a gas appliance in the same room with the outlet. 1.5 Gas-Piping System Any arrangement of gas piping or regulators after the point of delivery and each arrangement of gas piping serving a building, structure, or premises, whether individually metered or not. 1.6 Grounding Electrode A device that establishes an electrical connection to the earth. UNIFORM PLUMBING CODE 171

1.7 Liquefied Petroleum Gas (LPG) Facilities Liquefied petroleum gas (LPG) facilities means tanks, containers, container valves, regulating equipment, meters, and/or appurtenances for the storage and supply of liquefied petroleum gas for any building, structure, or premises. 1.8 Provision for Location of Point of Delivery The location of the point of delivery shall be acceptable to the serving gas supplier. [NFPA 54:5.2] 1.9 Quick-Disconnect Device A hand-operated device that provides a means for connecting and disconnecting an appliance or an appliance connector to a gas supply and that is equipped with an automatic means to shut off the gas supply when the device is disconnected. 1. Service Piping The piping and equipment between the street gas main and the gas piping system inlet that is installed by, and is under the control and maintenance of, the serving gas supplier. 1. Transition Gas Riser Any listed or approved section or sections of pipe and fittings used to convey fuel gas and installed in a gas piping system for the purpose of providing a transition from below ground to above ground. 14.0 Inspection. 14.1 Inspection Notification. Upon completion of the installation, alteration, or repair of any gas piping, and prior to the use thereof, the Authority Having Jurisdiction shall be notified that such gas piping is ready for inspection. 14.2 Excavation. All eexcavations required for the installation of underground piping shall be kept open until such time as the piping has been inspected and approved. If any Where such piping is covered or concealed before such approval, it shall be exposed upon the direction of the Authority Having Jurisdiction. 14. Type of Inspections. The Authority Having Jurisdiction shall make the following inspections and either shall approve that portion of the work as completed or shall notify the permit holder wherein the same fails to comply be in accordance with this code. 14..1 Rough Piping Inspection. This inspection shall be made after all gas piping authorized by the permit has been installed and before any such piping has been covered or concealed or any fixture or appliance has been attached thereto. This inspection shall include a determination that the gas-piping size, material, and installation meet the requirements of this code. 14..2 Final Piping Inspection. This inspection shall be made after all piping authorized by the permit has been installed and after all portions thereof that are to be covered or concealed are so concealed and before any fixtures, appliance, or shutoff valve has been attached thereto. This inspection shall be in accordance with Section 1214.1. Test gauges used in conducting tests shall comply be in accordance with Section 19.0, Test Gauges. 14.4 Inspection Waived In cases where the work authorized by the permit consists of a minor installation of additional piping to piping already connected to a gas meter, the foregoing inspections shall be permitted to be waived at the discretion of the Authority Having Jurisdiction. In this event, the Authority Having Jurisdiction shall make such inspection as deemed advisable in order to be assured that the work has been performed in accordance with the intent of this code. 4.0 Certificate of Inspection. 4.1 Issuance. If, Where upon final piping inspection, the installation is found to comply be in accordance with the provisions of this code, a certificate of inspection shall be permitted to be issued by the Authority Having Jurisdiction. 4.2 Gas Supplier. A copy of the certificate of such final piping inspection shall be issued to the serving gas supplier supplying gas to the premises. 4. Unlawful. It shall be unlawful for any a serving gas supplier, or person furnishing gas, to turn on or cause to be turned on, any a fuel gas or any a gas meter or meters, until such certificate of final inspection, as herein provided, has been issued. 165.0 Authority to Render Gas Service. 165.1 Authorized Personnel. It shall be unlawful for any a person, firm, or corporation, excepting an authorized agent or employee of a person, firm, or corporation engaged in the business of furnishing or supplying gas and whose service pipes supply or connect with the particular premises, to turn on or reconnect gas service in or on any a premises where and when gas service is, at the time, not being rendered. 165.2 Outlets. It shall be unlawful to turn on or connect gas in or on any a premises unless all outlets are properly and securely connected to gas appliances or capped or plugged with screw joint fittings. 176.0 Authority to Disconnect. 176.1 Disconnection. The Authority Having Jurisdiction or the serving gas supplier is hereby authorized to disconnect any gas piping or appliance or both that shall be found not to conform to comply the requirements of this code or that are found defective and in such condition as to endanger life or property. 176.2 Notice. Where such disconnection has been made, a notice shall be attached to such gas piping or appliance or both that shall state the same has been disconnected, together with the reasons thereof. 176. Capped Outlets. It shall be unlawful to remove or disconnect any gas piping or gas appliance without capping or plugging with a screw joint fitting, the outlet from which said pipe or appliance was removed. Outlets to which gas appliances are not connected shall be left capped, gastight on any a piping system that has been installed, altered, or repaired. Exception: When Where an approved listed quick- disconnect device is used. 172 UNIFORM PLUMBING CODE

7.0 Temporary Use of Gas. 17.1 General. Where temporary use of gas is desired and the Authority Having Jurisdiction deems the use necessary, a permit shall be permitted to be issued for such use for a period of time not to exceed that designated by the Authority Having Jurisdiction, provided that such gas-piping system otherwise conforms to is in accordance with the requirements of this code regarding material, sizing, and safety. 198.0 Gas-Piping System Design, Materials, and Components. 198.1 Piping Plan. 198.1.1 Installation of Piping System. Where required by the Authority Having Jurisdiction, a piping sketch or plan shall be prepared before proceeding with the installation. This plan shall show the proposed location of piping, the size of different branches, the various load demands, and the location of the point of delivery. [NFPA 54:5.1.1] 198.1.2 Addition to Existing System. When Where an additional gas utilization appliance is being connected to a gas-piping system, the existing piping shall be checked to determine whether it has adequate capacity (see Section 19.4.). If Where inadequate, the existing system shall be enlarged as required, or separate gas piping of adequate capacity shall be provided. [NFPA 54:5.1.2] 198.2 Provision for Location of Point of Delivery. The location of the point of delivery shall be acceptable to the serving gas supplier. [NFPA 54:5.2] 198. Interconnections Between Gas-Piping Systems. [NFPA 54:5.] 198..1 Interconnections Supplying Separate Users. Where two (2) or more meters, or two (2) or more service regulators where meters are not provided, are located on the same premises and supply separate users, the gas-piping systems shall not be interconnected on the outlet side of the meters or service regulators. [NFPA 54:5..1] 198..2 Interconnections for Standby Fuels. Where a supplementary gas for standby use is connected downstream from a meter or a service regulator where a meter is not provided, a device to prevent backflow shall be installed. A three-way valve installed to admit the standby supply and, at the same time, shut off the regular supply, shall be permitted to be used for this purpose. [NFPA 54:5..2] 198.4 Sizing of Gas-Piping Systems. [NFPA 54:5.4] 198.4.1 General Considerations. Gas-piping systems shall be of such size and so installed as to provide a supply of gas sufficient to meet the maximum demand and supply gas to each appliance inlet at not less than the minimum supply pressure required by the appliance. [NFPA 54-09:5.4.1] 198.4.2 Maximum Gas Demand. The volume volumetric flow rate of gas to be provided (in cubic feet per hour) shall be determined directly from calculated using the manufacturer's input ratings of the gas utilization appliance served. Where the input rating is not indicated, the gas supplier, appliance manufacturer, or a qualified agency shall be contacted or the rating from Table 12-1.4.2 shall be used for estimating the volume volumetric flow rate of gas to be supplied. The total connected hourly load shall be used as the basis for piping sizing, assuming the appliance is operating at full capacity simultaneously. [NFPA 54-12:5.4.2] Exception: Sizing shall be permitted to be based upon established load diversity factors. [NFPA 54:5.4.2.2] TABLE 12-1.4.2 APPROXIMATE GAS INPUT FOR TYPICAL APPLIANCES [NFPA 54: TABLE 5.4.2.1] APPLIANCE Space Heating Units Warm air furnace Single family Multifamily, per unit Hydronic boiler Single family Multifamily, per unit Space-and Water-Heating Units Hydronic boiler Single family Multifamily, per unit Water-Heating Appliances Water heater, automatic storage to gal. tank Water heater, automatic storage gal. tank Water heater, automatic instantaneous Capacity at 2 gal./minute Capacity at 4 gal./minute Capacity at 6 gal./minute Water heater, domestic, circulating or side-arm Cooking Appliances Range, freestanding, domestic Built-in oven or broiler unit, domestic Built-in top unit, domestic Other Appliances Refrigerator Clothes dryer, Type 1 (domestic) Gas fireplace direct vent Gas log Barbecue Gaslight INPUT Btu/h. (Approx.) 0,000,000 0,000,000 1,000 75,000 5,000,000 142,0 285,000 428,0 5,000 65,000 25,000,000,000 5,000,000,000,000 2,0 For SI units: 1 Btu 00 British thermal units per hour = 0.29 kw UNIFORM PLUMBING CODE 17

198.4. Sizing Methods. Gas piping shall be sized in accordance with one of the following : (1) Pipe sizing tables or sizing equations in this chapter. (2) Other approved engineering methods acceptable to the Authority Having Jurisdiction. () Sizing tables included in a listed piping system manufacturer's installation instructions. [NFPA 54:5.4.] 198.4.4 Allowable Pressure Drop. The design pressure loss in any a piping system under maximum probable flow conditions, from the point of delivery to the inlet connection of the appliance, shall be such that the supply pressure at the appliance exceeds is greater than or is equal to the minimum pressure required by the appliance. [NFPA 54-09:5.4.4] 198.5 Acceptable Piping Materials and Joining Methods. 198.5.1 General. 198.5.1.1 Acceptable Materials. Materials used for piping systems shall comply with the requirements of this chapter or shall be acceptable to the Authority Having Jurisdiction. [NFPA 54:5.6.1.1] 198.5.1.2 Used Materials. Pipe, fittings, valves, or other materials shall not be used again unless they are free of foreign materials and have been ascertained to be adequate approved for the service intended. [NFPA 54:5.6.1.2] 198.5.1. Other Materials. Material not covered by the standards specifications listed herein shall be investigated and tested to determine that it is safe and suitable for the proposed service and, in addition, shall be recommended for that service by the manufacturer and shall be acceptable to the Authority Having Jurisdiction. [NFPA 54:5.6.1.] 198.5.2 Metallic Pipe. 198.5.2.1 Cast-Iron. Cast-iron pipe shall not be used. [NFPA 54:5.6.2.1] 198.5.2.2 Steel and Wrought-Iron. Steel and wrought-iron pipe shall be not less than standard weight (Schedule ) and shall comply with one of the following standards (1) ASME B6., Welded and Seamless Wrought- Steel Pipe. (2) ASTM A 5, Standard Specification for Pipe, Steel, Black and Hot-Dipped, Zinc-Coated Welded and Seamless. () ASTM A 6, Standard Specification for Seamless Carbon Steel Pipe for High-Temperature Service [NFPA 54:5.6.2.2]:. 198.5.2. Copper and Brass. Copper and brass pipe shall not be used if the gas contains more than an average of 0. grains of hydrogen sulfide per one-hundred (0) standard cubic feet (scf) of gas (0.7 mg/0 L). [NFPA 54:5.6.2.] Threaded copper, brass, or aluminum alloy pipe shall not be used with gases corrosive to such material. [NFPA 54:5.6.2.4] 198.5.2.4 Aluminum Alloy. Aluminum alloy pipe shall comply with ASTM B 241, Standard Specification for Aluminum-Alloy Seamless Pipe and Seamless Extruded Tube (except that the use of alloy 5456 is prohibited) and shall be marked at each end of each length indicating compliance. Aluminum alloy pipe shall be coated to protect against external corrosion where it is in contact with masonry, plaster, insulation or is subject to repeated wettings by such liquids as water, detergents, or sewage. [NFPA 54:5.6.2.5] Aluminum alloy pipe shall not be used in exterior locations or underground. [NFPA 54:5.6.2.6] 198.5. Metallic Tubing. Seamless copper, aluminum alloy, or steel tubing shall not be used with gases corrosive to such material. [NFPA 54:5.6.] 198.5..1 Steel. Steel tubing shall comply with ASTM A 254, Standard Specification for Copper Brazed Steel Tubing. [NFPA 54-09:5.6..1] 198.5..2 Copper and Brass. Copper and brass tubing shall not be used if where the gas contains more than an average of 0. grains of hydrogen sulfide per one-hundred (0) scf of gas (0.7 mg/0 L). Copper tubing shall comply with standard Type K or L of ASTM B 88, Standard Specification for Seamless Copper Water Tube, or ASTM B 2, Specification for Seamless Copper Tube for Air- Conditioning and Refrigeration Field Service. [NFPA 54:5.6..2] 198.5.. Aluminum Alloy. Aluminum alloy tubing shall comply with ASTM B 2, Standard Specification for Aluminum-Alloy Drawn Seamless Tubes, or ASTM B 241, Standard Specification for Aluminum Alloy Seamless Pipe and Seamless Extruded Tube. Aluminum alloy tubing shall be coated to protect against external corrosion where it is in contact with masonry, plaster, insulation or is subject to repeated wettings by liquids such as water, detergent, or sewage. Aluminum alloy tubing shall not be used in exterior locations or underground. [NFPA 54:5.6..] 198.5..4 Corrugated Stainless Steel. Corrugated stainless steel tubing shall be tested and listed in compliance accordance with the construction, installation, and performance requirements of CSA LC-1, Standard for Fuel Gas Piping Systems Using Corrugated Stainless Steel Tubing. [NFPA 54:5.6..4] 198.5.4 Plastic Pipe, Tubing, and Fittings. Plastic pipe, tubing, and fittings used to supply fuel gas shall conform be in accordance with ASTM D 251, Standard Specification for Thermoplastic Gas Pressure Pipe, Tubing, and Fittings. Pipe to be used shall be marked "gas" and "ASTM D 251. [NFPA 54:5.6.4.1] Anodeless risers shall comply with the following sections. [NFPA 54:5.6.4.]: 174 UNIFORM PLUMBING CODE

198.5.4.1 Regulator Vent Piping. Plastic pipe, tubing, and fittings used to connect regulator vents to remote vent terminations shall be PVC conforming to in accordance with ANSI/UL 651, Schedule and Rigid PVC Conduit and Fittings. PVC vent piping shall not be installed indoors. [NFPA 54-19:5.6.4.2] 198.5.4.2 Factory-Assembled Anodeless Risers. Factory-assembled anodeless risers shall be recommended by the manufacturer for the gas used and shall be leak-tested by the manufacturer in accordance with written procedures. [NFPA 54:5.6.4.(1)] 198.5.4. Service Head Adapters and Field-Assembled Anodeless Risers. Service head adapters and field-assembled anodeless risers incorporating service head adapters shall be recommended by the manufacturer for the gas used by the manufacturer and shall be design-certified to meet be in accordance with the requirements of Category I of ASTM D 251, Standard Specification for Thermostatic Gas Pressure Pipe, Tubing, and Fittings and the code of Federal Regulations, Title 49, Part 192.281(e). The manufacturer shall provide the user with qualified installation instructions. as prescribed by the code of Federal Regulations, Title 49, Part 192.28(b). [NFPA 54:5.6.4.(2)] 198.5.4.4 Undiluted Liquefied Petroleum Gas Piping. The use of plastic pipe, tubing, and fittings in undiluted liquefied petroleum gas-piping systems shall be in accordance comply with NFPA 58, Liquefied Petroleum Gas Code. [NFPA 54:5.6.4.()] 198.5.5 Workmanship and Defects. Gas pipe or tubing and fittings shall be clear and free from cutting burrs and defects in structure or threading, and shall be thoroughly brushed and chip and scale blown. Defects in pipe, tubing, and fittings shall not be repaired. Defective pipe, tubing, and fittings shall be replaced. [NFPA 54:5.6.5] 198.5.6 Protective Coating. Where in contact with material or atmosphere exerting a corrosive action, metallic piping and fittings coated with a corrosion-resistant material shall be used. External or internal coatings or linings used on piping or components shall not be considered as adding strength. [NFPA 54:5.6.6] 198.5.7 Metallic Pipe Threads..5.7.1 (A) Specifications for Pipe Threads. Metallic pipe and fitting threads shall be taper pipe threads and shall comply with ASME B1..1, Standard for Pipe Threads, General Purpose (Inch). [NFPA 54:5.6.7.1].5.7.2 (B) Damaged Threads. Pipe with threads that are stripped, chipped, corroded, or otherwise damaged shall not be used. Where a weld opens during the operation of cutting or threading, that portion of the pipe shall not be used. [NFPA 54:5.6.7.2] NOMIL IRON PIPE SIZE (inches) 1.5.7. (C) Number of Threads. Field threading of metallic pipe shall be in accordance comply with Table 12-2.5.7.. [NFPA 54:5.6.7.] TABLE 12-2.5.7. SPECIFICATIONS FOR THREADING METALLIC PIPE [NFPA 54: TABLE 5.6.7.] 4 APPROXIMATE LENGTH OF THREADED PORTION (inches) APPROXIMATE NO. OF THREADS TO BE CUT 4 4 1 7 1 1 4 1 1 1 1 2 1 2 1 1 1 12 1 1 12 4 1 5 1 For SI units, 1 inch = 25.4 mm.5.7.4 (D) Thread Joint Compounds. Thread (joint) compounds (pipe dope) shall be resistant to the action of liquefied petroleum gas or to any other chemical constituents of the gases to be conducted through the piping. [NFPA 54-12:5.6.7.4] 198.5.8 Metallic Piping Joints and Fittings. The type of piping joint used shall be suitable approved for the pressure-temperature conditions and shall be selected giving consideration to joint tightness and mechanical strength under the service conditions. The joint shall be able to sustain the maximum end force due to the internal pressure and any additional forces due to temperature expansion or contraction, vibration, fatigue, or to the weight of the pipe and its contents. [NFPA 54:5.6.8] 198.5.8.1 Pipe Joints. Pipe joints shall be threaded, flanged, brazed, or welded. Where nonferrous pipe is brazed, the brazing materials shall have a melting point in excess of 1,000 F (58 C). Brazing alloys shall not contain more than 0.05 percent phosphorus. [NFPA 54:5.6.8.1] 198.5.8.2 Tubing Joints. Tubing joints shall either be made with approved gas tubing fittings, be brazed with a material having a melting point in excess of 1,000 F (58 C), or made by press-connect fittings complying in accordance with CSA ANSI LC-4. Brazing alloys shall not contain more than 0.05 percent phosphorus. [NFPA 54:5.6.8.2] 198.5.8. Flared Joints. Flared joints shall be used only in systems constructed from nonferrous pipe and tubing where experience or tests have demonstrated that the joint is suitable approved for the conditions and where provisions are made in the design to prevent separation of the joints. [NFPA 54:5.6.8.] UNIFORM PLUMBING CODE

198.5.8.4 Metallic Fittings (Including Valves, Strainers, Filters). Metallic fittings shall comply with the following: (1) Threaded fittings in sizes exceeding four (4) inches (0 mm) shall not be used unless acceptable to the Authority Having Jurisdiction. (2) Fittings used with steel or wrought-iron pipe shall be steel, brass, bronze, malleable iron, or cast-iron. () Fittings used with copper or brass pipe shall be copper, brass, or bronze. (4) Fittings used with aluminum alloy pipe shall be of aluminum alloy. (5) Cast-Iron Fittings. (a) Flanges shall be permitted. (b) Bushings shall not be used. (c) Fittings shall not be used in systems containing flammable gas-air mixtures. (d) Fittings in sizes four (4) inches (0 mm) and larger shall not be used indoors unless approved by the Authority Having Jurisdiction. (e) Fittings in sizes six (6) inches (1 mm) and larger shall not be used unless approved by the Authority Having Jurisdiction. (6) Aluminum Alloy Fittings. Threads shall not form the joint seal. (7) Zinc-Aluminum Alloy Fittings. Fittings shall not be used in systems containing flammable gas-air mixtures. (8) Special Fittings. Fittings such as couplings; proprietary-type joints; saddle tees; gland-type compression fittings; and flared, flareless, or compression-type tubing fittings shall be: (1a)uUsed within the fitting manufacturers' pressure-temperature recommendations;. (2b) uused within the service conditions anticipated with respect to vibration, fatigue, thermal expansion, or contraction;. (c) iinstalled or braced to prevent separation of the joint by gas pressure or external physical damage;. and (4d) aacceptable to the Authority Having Jurisdiction. [NFPA 54:5.6.8.4] 198.5.9 Plastic Piping, Joints, and Fittings. Plastic pipe, tubing, and fittings shall be joined in accordance with the manufacturers' instructions. The following sections shall be observed when where making such joints. [NFPA 54:5.6.9]:.5.9.1 Joint Design (A) The joint shall be designed and installed so that the longitudinal pullout resistance of the joint shall be equal to the tensile strength of the plastic piping material. [NFPA 54:5.6.9(1)].5.9.2 Heat-Fusion Joint (B) Heat-fusion joints shall be made in accordance with AWS B2.4 Specification for Welding Procedure and Performance Qualification for Thermoplastics. Joints shall be made with the joining method recommended by the pipe manufacturer. Heat-fusion fittings shall be marked "ASTM D 251." [NFPA 54:5.6.9(2)].5.9. Compression Type Mechanical Joints. (C) Where compression-type mechanical joints are used, the gasket material in the fitting shall be compatible with the plastic piping and with the gas distributed by the system. An internal tubular rigid stiffener shall be used in conjunction with the fitting. The stiffener shall be flush with the end of the pipe or tubing, shall extend not less than the outside end of the pipe or tubing and shall extend not less than to the outside end of the compression fitting when where installed. The stiffener shall be free of rough or sharp edges and shall not be a forced fit in the plastic. Split tubular stiffeners shall not be used. [NFPA 54:5.6.9()].5.9.4 (D) Liquefied Petroleum Gas Piping Systems. Plastic piping joints and fittings for use in liquefied petroleum gas-piping systems shall be in accordance with NFPA 58, Liquefied Petroleum Gas Code. [NFPA 54:5.6.9(4)] 198.5. Flanges. Flanges shall comply with ASME B16.1, Standard for Cast-Iron Pipe Flanges and Flanged Fittings; ASME B16., Standard for Ring- Joint Gaskets and Grooves for Steel Pipe Flanges; or MSS SP-6, Standard Finishes for Contact Faces of Pipe Flanges and Connecting-End Flanges of Valves and Fittings. The pressure-temperature ratings shall equal or exceed that required by the application. [NFPA 54:5.6.].5..1 (A) Flange Facings. Standard facings shall be permitted for use under this code. Where one-hundred and fifty (1) psi (1,0 4 kpa) steel flanges are bolted to Class cast-iron flanges, the raised face on the steel flange shall be removed. [NFPA 54:5.6..1].5..2 (B) Lapped Flanges. Lapped flanges shall be used only above ground or in exposed locations accessible for inspection. [NFPA 54:5.6..2] 198.5. Flange Gaskets. The material for gaskets shall be capable of withstanding the design temperature and pressure of the piping system and the chemical constituents of the gas being conducted without change to its chemical and physical properties. The effects of fire exposure to the joint shall be considered in choosing the material. [NFPA 54:5.6.] Flange gaskets shall comply with the following requirements: (1) Acceptable materials include the following [NFPA 54-12:5.6..1]: (a) Metal or metal-jacketed asbestos (plain or corrugated). (b) Asbestos Composition. (c) Aluminum "O" rings and spiral-wound metal gaskets. 176 UNIFORM PLUMBING CODE

(2) When Where a flanged joint is opened, the gasket shall be replaced. [NFPA 54:5.6..2] () Full-face gaskets shall be used with all bronze and cast-iron flanges. [NFPA 54:5.6..] 198.6 Gas Meters. 198.6.1 Capacity. Gas meters shall be selected for the maximum expected pressure and permissible pressure drop. [NFPA 54:5.7.1] 198.6.2 Location..6.2.1 Ventilated Spaces. (A) Gas meters shall be located in ventilated spaces readily accessible for examination, reading, replacement, or necessary maintenance. [NFPA 54:5.7.2.1].6.2.2 Subject to Damage. (B) Gas meters shall not be placed where they will be subjected to damage, such as adjacent to a driveway; under a fire escape; in public passages, halls, or coal bins; or where they will be subject to excessive corrosion or vibration. [NFPA 54:5.7.2.2].6.2. Extreme Temperatures. (C) Gas meters shall not be located where they will be subjected to extreme temperatures or sudden extreme changes in temperature. Meters shall not be located in areas where they are subjected to temperatures beyond those recommended by the manufacturer. [NFPA 54:5.7.2.4] 198.6. Supports. Gas meters shall be supported or connected to rigid piping so as not to exert a strain on the meters. Where flexible connectors are used to connect a gas meter to downstream piping at mobile homes in mobile home parks, the meter shall be supported by a post or bracket placed in a firm footing or by other means providing equivalent support. [NFPA 54:5.7.] 198.6.4 Meter Protection. Meters shall be protected against overpressure, back-pressure, and vacuum where such conditions are anticipated. [NFPA 54-12:5.7.4] 198.6.5 Identification. Gas piping at multiple meter installations shall be marked by a metal tag or other permanent means attached by the installing agency, designating the building or the part of the building being supplied. [NFPA 54:5.7.5] 198.7 Gas Pressure Regulators. 198.7.1 Where Required. A line gas pressure regulator or gas appliance pressure regulator, as applicable, shall be installed where the gas supply pressure exceeds that at which the branch supply line or gas utilization appliance is designed to operate or varies beyond design pressure limits. [NFPA 54-12:5.8.1].7.1.1 Where the gas supply pressure in piping systems located indoors exceeds 2 psi (14 kpa) and line pressure regulators are installed to reduce the supply pressure to 14 inches water column (.5 kpa) or less, the following shall apply: (1) Regulators shall be provided with factory installed overpressure protection devices. (2) Overpressure protection devices shall limit the pressure downstream of the line pressure regulator to 2 psi (14 kpa) in the event of failure of the line pressure regulator. 198.7.2 Listing. The line gas pressure regulator shall be listed in accordance with CSA Z21.. [NFPA 54:5.8.2] 198.7. Location. The gas pressure regulator shall be accessible for servicing. [NFPA 54:5.8.] 198.7.4 Regulator Protection. Pressure regulators shall be protected against physical damage. [NFPA 54:5.8.4] 198.7.5 Venting..7.5.1 (A) Line Gas Pressure Regulators. Line gas pressure regulators shall be installed in accordance with the following requirements: (1) An independent vent to the outside exterior of the building, sized in accordance with the regulator manufacturer's instructions, shall be provided where the location of a regulator is such that a ruptured diaphragm will cause a hazard. Where there is more than one (1) regulator is at a location, each regulator shall have a separate vent to the outside outdoors, or, if where approved by the Authority Having Jurisdiction, the vent lines shall be permitted to be manifolded in accordance with accepted engineering practices to minimize back-pressure in the event of diaphragm failure. (See NFPA 54:5.9.7 for information on properly locating the vent.) Materials for vent piping shall be in accordance comply with Section 198.5. Exception: A regulator and vent limiting means combination listed as complying in accordance with CSA Z21., Standard for Line Pressure Regulators, shall be permitted to be used without a vent to the outdoors. (2) The vent shall be designed to prevent the entry of water, insects, or other foreign materials that could cause blockage. () The regulator vent shall terminate not less than feet (914 mm) from a source of ignition. (4) At locations where regulators might be will submerged during floods, a special antiflood-type breather vent fitting shall be installed, or the vent line shall be extended above the height of the expected flood waters. (45) A regulator shall not be vented to the gas appliance flue or exhaust system. [NFPA 54:5.8.5.1].7.5.2 (B) Venting of Gas Appliance Pressure Regulators. Venting of gas appliance pressure regulators shall comply with the following requirements: (1) Gas aappliance pressure regulators requiring access to the atmosphere for successful operation shall be equipped with vent piping leading UNIFORM PLUMBING CODE 177

outdoors, or, if where the regulator vent is an integral part of the appliance, into the combustion chamber adjacent to a continuous pilot, unless constructed or equipped with a vent-limiting means to limit the escape of gas from the vent opening in the event of diaphragm failure. (2) Vent-limiting means shall be employed on listed gas appliance pressure regulators only. () In the case of vents leading outdoors, means shall be employed to prevent water from entering this piping and also to prevent blockage of vents by insects and foreign matter. (4) Under no circumstances shall a regulator be vented to the gas utilization appliance flue or exhaust system. (5) In the case of vents entering the combustion chamber, the vent shall be located so the escaping gas will be readily ignited by the pilot and the heat liberated thereby will not adversely affect the normal operation of the safety shutoff system. The terminus of the vent shall be securely held in a fixed position relative to the pilot. For manufactured gas, the need for a flame arrester in the vent piping shall be determined. (6) Vent lines from a gas appliance pressure regulator and bleed lines from a diaphragm-type valve shall not be connected to a common manifold terminating in a combustion chamber. Vent lines shall not terminate in positive-pressuretype combustion chambers. [NFPA 54:9.1.19].7.5. (C) Discharge of Vents. Discharge of vents shall be in accordance with the following requirements: (1) The discharge stacks, vents, or outlet parts of all pressure-relieving and pressure-limiting devices shall be located so that gas is safely discharged into the outside atmosphere outdoors. (2) Discharge stacks or vents shall be designed to prevent the entry of water, insects, or any other foreign material that could cause blockage. The discharge stack or vent line shall be not less than the same size as the outlet of the pressure-relieving device. [NFPA 54:5.9.7] 198.7.6 Bypass Piping. Valved and regulated bypasses shall be permitted to be placed around gas line pressure regulators where continuity of service is imperative. [NFPA 54:5.8.6] 198.7.7 Identification. Line pressure regulators at multiple regulator installations shall be marked by a metal tag or other permanent means designating the building or the part of the building being supplied. [NFPA 54:5.8.7] 198.8 Back-Pressure Protection. 198.8.1 Where to Install. Protective devices shall be installed as close to the utilization appliance as practical, where the design of utilization appliances connected are such that air, oxygen, or standby gases could be are capable of being forced into the gas supply system. [NFPA 54:5..1.1] Gas and air combustion mixers incorporating double diaphragm "zero" or "atmosphere" governors or regulators shall require no further protection unless connected directly to compressed air or oxygen at pressures of five (5) psi (4 kpa) or more. [NFPA 54:5..1.2] 198.8.2 Protective Devices. Protective devices shall include but not be limited to the following: (1) Check valves. (2) Three-way valves (of the type that completely closes one side before starting to open the other side). () Reverse flow indicators controlling positive shutoff valves. (4) Normally closed air-actuated positive shutoff pressure regulators. [NFPA 54:5..2] 198.9 Low-Pressure Protection. A protective device shall be installed between the meter and the gas utilization appliance or equipment if where the operation of the appliance or equipment (i.e., gas compressors) is such that it could produce is capable of producing a vacuum or a dangerous reduction in gas pressure at the meter. Such protective devices include, but are not limited to, mechanical, diaphragm-operated, or electrically operated low-pressure shutoff valves. [NFPA 54-12:5.] 198. Shutoff Valves. Shutoff valves shall be approved and shall be selected giving consideration to pressure drop, service involved, emergency use, and reliability of operation. Shutoff valves of size one (1) inch (25 mm) National Pipe Thread and smaller shall be listed. [NFPA 54:5.12] 198. Expansion and Flexibility. 198..1 Design. Piping systems shall be designed to have sufficient flexibility to prevent failure from thermal expansion or contraction. from causing excessive stresses in the piping material, excessive bending or loads at joints, or undesirable forces or moments at points of connections to equipment and at anchorage or guide points. Formal calculations or model tests shall be required only where reasonable doubt exists as to the adequate flexibility of the system. [NFPA 54-12:5.14.1] Flexibility shall be provided by the use of bends, loops, offsets, or couplings of the slip type. Provision shall be made to absorb thermal changes by the use of expansion joints of the bellows type, or by the use of "ball" or "swivel" joints. Expansion joints of the slip type shall not be used inside buildings or for thermal expansion. Where expansion joints are used, anchors or ties of sufficient strength and rigidity shall be installed to provide for end forces due to fluid pressure and other causes. [NFPA 54:5.1.1.1] Pipe alignment guides shall be used with expansion joints according to the recommended practice of the joint manufacturer. [NFPA 54:5.1.1.2] 178 UNIFORM PLUMBING CODE

198..2 Special Local Conditions. Where local conditions include earthquake, tornado, unstable ground, or flood hazards, special consideration shall be given to increased strength and flexibility of piping supports and connections. [NFPA 54:5.1.2] 129.0 Excess Flow Valve. 19.1 General. Where automatic excess flow gas valves are installed, they shall be listed, sized, and installed in accordance with the manufacturer s instructions. [NFPA 54-09:5.1] 121.0 Gas Piping Installation. 121.1 Piping Underground. 121.1.1 Clearances. Underground gas piping shall be installed with sufficient approved clearance from any other underground structures to avoid contact therewith, to allow maintenance, and to protect against damage from proximity to other structures. In addition, underground plastic piping shall be installed with sufficient approved clearance or shall be insulated from any a sources of heat so as to prevent the heat from impairing the serviceability of the pipe. [NFPA 54:7.1.1] 121.1.2 Protection Against Damage. 12.1.2.1 (A) Cover Requirements. Underground piping systems shall be installed with a minimum cover not less than of eighteen () inches (4 457 mm) of cover. Where external damage to the pipe is not likely to result, the cover shall be a minimum not less than of twelve (12) inches (05 mm). Where a minimum of cover not less than twelve (12) inches (05 mm) of cover cannot be provided, the pipe shall be installed in conduit or bridged (shielded). [NFPA 54:7.1.2.1] 12.1.2.2 (B) Trenches. The trench shall be graded so that the pipe has a firm, substantially continuous bearing on the bottom of the trench. [NFPA 54:7.1.2.2] 12.1.2. (C) Backfilling. Where flooding of the trench is done to consolidate the backfill, care shall be exercised to see that the pipe is not floated from its firm bearing on the trench bottom. [NFPA 54:7.1.2.] 121.1. Protection Against Corrosion. Gas piping in contact with earth or other material that could corrode is capable of corroding the piping shall be protected against corrosion in an approved manner. When Where dissimilar metals are joined underground, an insulating coupling or fitting shall be used. Piping shall not be laid in contact with cinders. Uncoated threaded or socketwelded joints shall not be used in piping in contact with soil or where internal or external crevice corrosion is known to occur. [NFPA 54:7.1.] 121.1.4 Protection Against Freezing. Where the formation of hydrates or ice is known to occur, piping shall be protected against freezing. [NFPA 54:7.1.4] 121.1.5 Piping Through Foundation Wall. Underground piping, where installed through the outer foundation or basement wall of a building, shall be encased in a protective sleeve or protected by an approved device or method. The space between the gas piping and the building or sleeve and between the sleeve and the wall shall be sealed to prevent entry of gas and water. [NFPA 54-12:7.1.5] 121.1.6 Piping Underground Beneath Buildings. Where the installation of gas piping is installed underground beneath buildings is unavoidable, the piping shall be either: (1) eencased in an approved conduit designed to withstand the superimposed loads and installed in accordance with Section 12.1.6.1 or Section 12.1.6.2, or. [NFPA 54:7.1.6] (2) A piping or encasement system listed for installation beneath buildings. 121.1.6.1 Conduit with One End Terminating Outdoors. The conduit shall extend into a normally usable and accessible portion of the building and, at the point where the conduit terminates in the building, the space between the conduit and the gas piping shall be sealed to prevent the possible entrance of any a gas leakage. Where the end sealing is of a type that will retain the full pressure of the pipe, the conduit shall be designed for the same pressure as the pipe. The conduit shall extend not less than (4) inches (02 mm) outside the building, be vented outdoors above finished ground level grade to the outside, and be installed so as to prevent the entrance of water and insects. [NFPA 54:7.1.6.1] 121.1.6.2 Conduit with Both Ends Terminating Indoors. Where the conduit originates and terminates within the same building, the conduit shall originate and terminate in an accessible portion of the building and shall not be sealed. [NFPA 54:7.1.6.2] 121.1.7 Plastic Pipe. 12.1.7.1 (A) Connection of Plastic Piping. Plastic pipe shall be installed outside, underground only. [NFPA 54:7.1.7.1] Exceptions: (1) Exception No. 1: Plastic pipe shall be permitted to terminate above ground where an anodeless riser is used. (2) Exception No. 2: Plastic pipe shall be permitted to terminate with a wall head adapter above ground in buildings, including basements, where the plastic pipe is inserted in a piping material permitted for use in buildings. 12.1.7.2 (B) Connections Between Metallic and Plastic Piping. Connections made between metallic and plastic piping shall be made only with fittings conforming to that are in accordance with one of the following: UNIFORM PLUMBING CODE 179

(1) ASTM D251, Standard Specification for Thermoplastic Gas Pressure Pipe, Tubing, and Fittings, Category I transition fittings. (2) ASTM F197, Standard Specification for Factory Assembled Anodeless Risers and Transition Fittings in Polyethylene (PE) and Polyamide (PA) Fuel Gas Distribution Systems. () ASTM F29, Standard Specification for Field- Assembled Anodeless Riser Kits for Use on Outside Diameter Controlled Polyethylene Gas Distribution Pipe and Tubing. [NFPA 54-09:7.1.7.2] 12.1.7. (C) Tracer Wire. An electrically continuous corrosion-resistant tracer wire (minimum not less than AWG 14) or tape shall be buried with the plastic pipe to facilitate locating. One (1) end shall be brought above ground at a building wall or riser. [NFPA 54:7.1.7.] 121.2 Installation of Piping. 121.2.1 Protection. Piping installed above ground shall be securely supported and located where it will be protected from physical damage (also see 12.1.4). Where passing through an outside wall, the piping shall also be protected against corrosion by coating or wrapping with an inert material approved for such applications. The piping shall be sealed around its circumference at the point of the exterior penetration to prevent the entry of water, insects, and rodents. Where piping is encased in a protective pipe sleeve, the annular spaces between the gas piping and the sleeve and between the sleeve and the wall opening shall be sealed at the exterior wall to prevent the entry of water, insects, or rodents. [NFPA 54-12:7.2.1] 121.2.2 Building Structure. 12.2.2.1 Installation. (1) The installation of gas piping shall not cause structural stresses within building components to exceed allowable design limits. [NFPA 54:7.2.2.1] 12.2.2.2 Approval. (2) Approval shall be obtained before any beams or joists are cut or notched. [NFPA 54:7.2.2.2] Permission shall be obtained from the Authority Having Jurisdiction. 12.2. Other than Dry Gas. Drips, sloping, protection from freezing, and branch pipe connections, as provided for in Section 12.1.4, 12.8.1, and Section 12., shall be provided when other than dry gas is distributed and climactic conditions make such provisions necessary. [NFPA 54:7.2.] 121.2.4 Gas Piping to be Sloped. Piping for other than dry gas conditions shall be sloped not less than one-fourth ( 1 4) inch in fifteen () feet (8 mm in 4,572 mm) (1.4 mm/m) to prevent traps. [NFPA 54:7.2.4] 121.2.4.1 Ceiling Locations. Gas piping shall be permitted to be installed in accessible spaces between a fixed ceiling and a dropped ceiling, whether or not such spaces are used as a plenum. Valves shall not be located in such spaces. Exception: Appliance shutoff valves required by this code shall be permitted to be installed in accessible spaces containing vented gas utilization appliances. 121.2.54 Prohibited Locations. Gas piping inside any a building shall not be installed in or through a circulating air duct, clothes chute, chimney or gas vent, ventilating duct, dumbwaiter, or elevator shaft, or air duct, other than combustion air ducts. [NFPA 54:7.2.5] Exception: This provision shall not apply to dducts used to provide combustion and ventilation air in accordance with Section 76.0 or to above-ceiling spaces as covered in Section 12.2.4.1. 121.2.65 Hangers, Supports, and Anchors. 12.2.5.1 General Requirements. (A) Piping shall be supported with metal pipe hooks, metal pipe straps, metal bands, metal brackets, metal hangers, or building structural components, suitable approved for the size of piping, of adequate strength and quality; and located at intervals so as to prevent or damp out excessive vibration. Piping shall be anchored to prevent undue strains on connected appliances and equipment and shall not be supported by other piping. Pipe hangers and supports shall conform to comply with the requirements of MSS SP-58, Pipe Hangers and Supports Materials, Design and Manufacture. [NFPA 54:7.2.6.1] 12.2.5.2 Spacing. (B) Spacings of supports in gas-piping installations shall not exceed as the distance shown in Table 12-12.2.5.2. Spacing of supports for CSST shall be in accordance with the CSST manufacturer's instruction. [NFPA 54:7.2.6.2] 12.2.5. Expansion and Contraction. (C) Supports, hangers, and anchors shall be installed so as not to interfere with the free expansion and contraction of the piping between anchors. All pparts of the supporting equipment system shall be designed and installed so they will are not be disengaged by movement of the supported piping. [NFPA 54:7.2.6.] STEEL PIPE, NOMIL SIZE OF PIPE (inches.) TABLE 12-12.2.5.2 SUPPORT OF PIPING [NFPA 54: Table 7.2.6.2] SPACING OF SUPPORTS (feet.) NOMIL SIZE OF TUBING SMOOTH- WALL (Iinches. O.D.) SPACING OF SUPPORTS (feet.) 1 6 1 4 4 or 1 8 5 or 4 6 1 1 4 or larger 7 or 1 8 (horizontal) (horizontal) 1 1 4 or larger (vertical) every floor level 1 or larger (vertical) every floor level For SI units: 1 inch = 25 mm, 1 foot. = 0.5 m 4.8 mm. 1 UNIFORM PLUMBING CODE

121.2.76 Removal of Pipe Piping. Where piping containing gas is to be removed, the line shall be first disconnected from sources of gas and then thoroughly purged with air, water, or inert gas before any cutting or welding is done. (See Section 1214.6.) [NFPA 54:7.2.7] 121. Concealed Piping in Buildings. 121..1 General. Gas piping in concealed locations shall be installed in accordance with this section. [NFPA 54:7..1] 121..2 Connections. Where gas piping is to be concealed, unions, tubing fittings, right and left couplings, bushings, swing joints, and compression couplings made by combinations of fittings shall not be used. Cconnections shall be of the following type: (1) Pipe fittings such as elbows, tees, and couplings, and right/left nipple/couplings. (2) Joining tubing by brazing (See Section 198.5.8.2). () Fittings listed for use in concealed spaces or that have been demonstrated to sustain, without leakage, any forces due to temperature expansion or contraction, vibration, or fatigue based on their geographic location, application, or operation. (4) Where necessary to insert fittings in gas pipe that has been installed in a concealed location, the pipe shall be reconnected by welding, flanges, or the use of a ground joint union with the nut center-punched to prevent loosening by vibration right/left nipple/coupling. [NFPA 54:7..2] 121.. Piping in Partitions. Concealed gas piping shall not be located in solid partitions. [NFPA 54:7..] 121..4 Tubing in Partitions. This provision shall not apply to tubing that pierces walls, floors, or partitions or to tubing installed vertically and horizontally inside hollow walls or partitions without protection along its entire concealed length where both of the following requirements are met: (1) A steel striker barrier not less than 0.08 inches (1. mm) thick, or equivalent, is installed between the tubing, the finished wall and extends at least not less than 4 inches (02 mm) beyond concealed penetrations of plates, fire stops, wall studs, and so on. (2) The tubing is installed in single runs and is not rigidly secured. [NFPA 54:7..4] 121..5 Piping in Floors. In industrial occupancies, gas piping in solid floors such as concrete shall be laid in channels in the floor and covered to permit access to the piping with minimum damage to the building. Where piping in floor channels could be is capable of being exposed to excessive moisture or corrosive substances, the piping shall be protected in an approved manner. [NFPA 54:7..5.1] Exception: In other than industrial occupancies and where approved by the Authority Having Jurisdiction, gas piping embedded in concrete floor slabs constructed with portland cement shall be surrounded with a minimum not less than of one and one half (1 1 ) inches (8 mm) of concrete and shall not be in physical contact with other metallic structures such as reinforcing rods or electrically neutral conductors. Piping, fittings, and risers shall be protected against corrosion in accordance with Section 198.5.6. Piping shall not be embedded in concrete slabs containing quick-set additives or cinder aggregate. [NFPA 54:7..5.2] 121.4 Piping in Vertical Chases. (See Section 12.0.) Where gas piping exceeding five (5) psi (4 kpa) is located within vertical chases in accordance with Section 121.5, the requirements of Sections 121.5.1 through Section 121.5. shall apply. [NFPA 54:7.4] 121.5 Maximum Design Operating Pressure. The maximum design operating pressure for piping systems located inside buildings shall not exceed five (5) psi (4 kpa) unless one (1) or more of the following conditions are met: (1) The piping system is welded. (2) The piping is located in a ventilated chase or otherwise enclosed for protection against accidental gas accumulation. () The piping is located inside buildings or separate areas of buildings used exclusively for one of the following: (a) Industrial processing or heating. (b) Research. (c) Warehousing. (d) Boiler or mechanical equipment rooms. (4) The piping is a temporary installation for buildings under construction. (5) The piping serves appliances or equipment used for agricultural purposes. (6) The piping system is an LP-Gas piping system with a design operating pressure greater than exceeding psi ( kpa) and complies in accordance with NFPA 58 54:5.5.2. Liquefied Petroleum Gas Systems LP-Gas systems designed to operate below -5ºF (-21ºC) or with butane or a propane-butane mix shall be designed to either accommodate liquid LP-Gas or to prevent LP-Gas vapor from condensing back into liquid. [NFPA 54-09:5.5.1 and 5.5.2] 121.5.1 Pressure Reduction. (See Section 12.0.) Where pressure reduction is required in branch connections for compliance in accordance with Section 121.5, such reduction shall take place either inside the chase or immediately adjacent to the outside wall of the chase. Regulator venting and downstream overpressure protection shall comply with Section 198.7.5 and NFPA Section 5.9. The regulator shall be accessible for service and repair, and vented in accordance with one (1) of the following: (1) Where the fuel gas is lighter than air, regulators equipped with a vent-limiting means shall be permitted to be vented into the chase. Regulators not equipped with a vent-limiting means shall be per- UNIFORM PLUMBING CODE 1

mitted to be vented either directly to the outdoors or to a point within the top one (1) foot (0.5 mm) of the chase. (2) Where the fuel gas is heavier than air, the regulator vent shall be vented only directly to the outdoors. [NFPA 54:7.4.1] 121.5.2 Liquefied Petroleum Gas Systems. The maximum operating pressure of LP-Gas piping systems shall be: (1) In accordance with Section 121.5.1; (2) In accordance with NFPA 58, where the pressure exceeds twenty () psi ( kpa) and; () Designed to either accommodate liquid LP-Gas or prevent LP-Gas vapor from condensing back into a liquid in buildings having systems designed to operate below -5ºF (-21ºC) or with butane or a propane butane mix. 121.5. Construction. Chase construction shall comply with local building codes with respect to fire resistance and protection of horizontal and vertical openings. [NFPA 54:7.4.2] 121.5.4 Ventilation. A chase shall be ventilated to the outdoors and only at the top. The openings shall have a minimum free area (in square inches) equal to the product of one-half (1) of the maximum pressure in the piping (in psi) times the largest nominal diameter of that piping (in inches), or the cross-sectional area of the chase, whichever is smaller. Where more than one (1) fuel gas piping system is present, the free area for each system shall be calculated and the largest area used. [NFPA 54:7.4.] 121.6 Appliance Over Pressure Protection. The maximum operating pressure for piping systems serving appliances designed to operate at fourteen (14) inches w.c. water column (.5 kpa) inlet pressure or less shall be two (2) psig 14 kpa) unless an over-pressure protection device designed to limit pressure at the appliance to two (2) psig (14 kpa) upon failure of the line gas pressure regulator is installed. 121.7 Gas Pipe Turns. Changes in direction of gas pipe shall be made by the use of fittings, or factory bends, or field bends. [NFPA 54:7.5] 121.7.1 Metallic Pipe. Metallic pipe bends shall comply with the following: (1) Bends shall be made only with bending equipment and procedures intended for that purpose. (2) Bends shall be smooth and free from buckling, cracks, or other evidence of mechanical damage. () The longitudinal weld of the pipe shall be near the neutral axis of the bend. (4) The pipe shall not be bent through an arc of more than degrees (1.57 rad). (5) The inside radius of a bend shall be not less than six (6) times the outside diameter of the pipe. [NFPA 54:7.5.1] 121.7.2 Plastic Pipe. Plastic pipe bends shall comply with the following: (1) The pipe shall not be damaged and the internal diameter of the pipe shall not be effectively reduced. (2) Joints shall not be located in pipe bends. () The radius of the inner curve of such bends shall be not less than twenty-five (25) times the inside diameter of the pipe. (4) Where the piping manufacturer specifies the use of special bending equipment or procedures, such equipment or procedures shall be used. [NFPA 54:7.5.2] 121.7. Elbows. Factory-made welding elbows or transverse segments cut therefrom shall have an arc length measured along the crotch of at least not less than one (1) inch (25.4 mm) for pipe sizes two (2) inches ( mm) and larger. [NFPA 54:7.5.] 121.8 Drips and Sediment Traps. 121.8.1 Provide Drips Where Necessary. For other than dry gas conditions, a drip shall be provided at any a point in the line of pipe where condensate is capable of collecting could collect. Where required by the Authority Having Jurisdiction or the serving gas supplier, a drip shall also be provided at the outlet of the meter. This drip shall be so installed as to constitute a trap wherein an accumulation of condensate will shut off the flow of gas before it will run back into the meter. [NFPA 54:7.6.1] 121.8.2 Location of Drips. Drips shall be installed only in such locations that they will be readily accessible to permit cleaning or emptying. A drip shall not be located where the condensate is likely to freeze. [NFPA 54:7.6.2] 121.8. Sediment Traps. (See Section 1212.7.) The installation of sediment traps shall comply with Section 12.7. 121.9 Outlets. 121.9.1 Location and Installation. Outlets shall be located and installed in accordance with the following requirements: (1) The outlet fittings or piping shall be securely fastened in place. [NFPA 54:7.7.1.1] (2) Outlets shall not be located behind doors. [NFPA 54:7.7.1.2] () Outlets shall be located far enough from floors, walls, patios, slabs, and ceilings to permit the use of wrenches without straining, bending, or damaging the piping. [NFPA 54:7.7.1.] (4) The unthreaded portion of gas piping outlets shall extend not less than one (1) inch (25.4 mm) through finished ceilings or indoor or outdoor walls. [NFPA 54:7.7.1.4] (5) The unthreaded portion of gas piping outlets shall extend not less than two (2) inches (1 mm) above the surface of floors or outdoor patios or slabs. [NFPA 54:7.7.1.5] 2 UNIFORM PLUMBING CODE

(6) The provisions of Sections 121.79.1(4) and Section 12.9.1(5) shall not apply to listed quick-disconnect devices of the flush-mounted type or listed gas convenience outlets. Such devices shall be installed in accordance with the manufacturer s installation instructions. [NFPA 54:7.7.1.6] 121.9.2 Cap Outlets. 12.9.2.1 Gas-Tight. (A) Each outlet, including a valve, shall be closed gas-tight with a threaded plug or cap immediately after installation and shall be left closed until the gas utilization appliance is connected thereto. When Where an appliance is disconnected from an outlet and the outlet is not to be used again immediately, it shall be closed gas-tight. [NFPA 54:7.7.2.1] Exceptions: (1) Exception No. 1: Laboratory equipment installed in accordance with Section 12121.2(A1) shall be permitted. (2) Exception No. 2: The use of a listed quick-disconnect device with integral shutoff or listed gas convenience outlet shall be permitted. 12.9.2.2 Appliance Shutoff Valves (B) Appliance shutoff valves installed in fireplaces shall be removed and the piping capped gas-tight where the fireplace is used for solid-fuel burning. [NFPA 54:7.7.2.2] 121. Branch Pipe Connection. When Where a branch outlet is placed on a main supply line before it is known what size pipe will be connected to it, the outlet shall be of the same size as the line that supplies it. [NFPA 54:7.8] 121. Manual Gas Shutoff Valves. (Also see Section 1212.5) 121..1 Valves at Regulators. An accessible gas shutoff valve shall be provided upstream of each gas pressure regulator. Where two (2) gas pressure regulators are installed in series in a single gas line, a manual valve shall not be required at the second regulator. [NFPA 54:7.9.1] 121..2 Valves Controlling Multiple Systems. 12..2.1 (A) Accessibility of Gas Valves. Main gas shutoff valves controlling several gas piping systems shall be readily accessible for operation and installed so as to be protected from physical damage. They shall be marked with a metal tag or other permanent means attached by the installing agency so that the gas piping systems supplied through them can be are readily identified. [NFPA 54:7.9.2.1] 12..2.2 (B) Shutoff Valves for Multiple House Lines. In multiple-tenant buildings supplied through a master meter, or through one (1) service regulator where a meter is not provided, or where meters or service regulators are not readily accessible from the equipment location, an individual shutoff valve for each apartment or tenant line shall be provided at a convenient point of general accessibility. In a common system serving a number of individual buildings, shutoff valves shall be installed at each building. [NFPA 54:7.9.2.2] 121.. Emergency Shutoff Valves. An exterior shutoff valve to permit turning off the gas supply to each building in an emergency shall be provided. The emergency shutoff valves shall be plainly marked as such and their locations posted as required by the Authority Having Jurisdiction. [NFPA 54:7.9.2.] 121..4 Shutoff Valve For Laboratories. Each laboratory space containing two (2) or more gas outlets installed on tables, benches, or in hoods in educational, research, commercial and industrial occupancies shall have a single shutoff valve through which such gas outlets are supplied. The shutoff valve shall be accessible and shall be located within the laboratory or located adjacent to the laboratory s egress door and shall be identified. [NFPA 54-09:7.9.2.4] 121.12 Prohibited Devices. No device shall be placed inside the gas piping or fittings that will reduce the cross-sectional area or otherwise obstruct the free flow of gas, except where proper an allowance in the piping system design has been made for such a device and where approved by the Authority Having Jurisdiction. [NFPA 54:7.] 121.1 Systems Containing Gas-Air Mixtures Outside the Flammable Range. Where gas-air mixing machines are employed to produce mixtures above or below the flammable range, they shall be provided with stops to prevent adjustment of the mixture to within or approaching the flammable range. [NFPA 54:7.] 121.14 Systems Containing Flammable Gas-Air Mixtures. Systems containing flammable gas-air mixtures shall be in accordance with NFPA 54. 121. Electrical Bonding and Grounding. 121..1 Pipe and Tubing other than CSST. Each above ground portion of a gas piping system other than CSST that is likely to become energized shall be electrically continuous and bonded to an effective ground-fault current path. Gas piping, other than CSST shall be considered to be bonded when where it is connected to appliances that are connected to the appliance grounding conductor of the circuit supplying that appliance. [NFPA 54-09:7.1.1] 121..2 Bonding of CSST Gas Piping. CSST gas piping systems shall be bonded to the electrical service grounding electrode system at the point where the gas service enters the building. The bonding jumper shall connect to a metallic pipe or fitting between the point of delivery and the first downstream CSST fitting. The bonding jumper shall be not smaller than six (6) AWG copper wire or equivalent. Gas piping systems that contain one or more segments of CSST shall be bonded in accordance with this section. [NFPA 54-0912:7.1.2] UNIFORM PLUMBING CODE

121.. Grounding Conductor or Electrode. Gas piping shall not be used as a grounding conductor or electrode. This does not preclude the bonding of metallic piping to a grounding system. [NFPA 54-0912:7.1.] 121..4 Lighting Protection System. Where a lightning protection system is installed, the bonding of the gas piping system shall be in accordance with NFPA 7, Standard for Installation of Lightning Protection Systems. [NFPA 54-09:7.1.4] 121.16 Electrical Circuits. Electrical circuits shall not utilize gas piping or components as conductors. [NFPA 54:7.14] Exception: Low-voltage (V or less) control circuits, ignition circuits, and electronic flame detection device circuits shall be permitted to make use of piping or components as a part of an electric circuit. 121.17 Electrical Connections. 12.17.1 Connections. (A) Electrical connections between wiring and electrically operated control devices in a piping system shall conform to comply with the requirements of NFPA, National Electrical Code. (See Section 12.14) [NFPA 54:7..1] 12.17.2 Safety Control. (B) Any An essential safety control depending on electric current as the operating medium shall be of a type that will shut off (fail safe) the flow of gas in the event of current failure. [NFPA 54:7..2] 12121.0 Appliance Connections to Building Piping. 12121.1 Connecting Gas Appliances. Gas utilization aappliances shall be connected to the building piping in compliance accordance with Sections 12121.5 and Section 12121.6 by one of the following [NFPA 54:9.6.1]: (1) Rigid metallic pipe and fittings. [NFPA 54:9.6.1(1)] (2) Semirigid metallic tubing and metallic fittings. Aluminum alloy tubing shall not be used in exterior locations. [NFPA 54:9.6.1(2)] () A Llisted flexible gas connectors installed in compliance accordance with CSA ANSI Z21.24/CSA 6., Standard for Connectors for Gas Appliances. The connector shall be used in accordance with the terms of their listing that are completely manufacturer s installation instructions and shall be in the same room as the appliance. One connector shall be used per appliance. [NFPA 54:9.6.1()] (4) CSST where installed in accordance with the manufacturer's installation instructions. [NFPA 54:9.6.1(5)] (5) Listed nonmetallic gas hose connectors installed in accordance with Section 12121.. [NFPA 54:9.6.1(6)] (6) Gas-fired food service (ccommercial cooking) appliances listed for use with casters or otherwise subject to movement that are moved for cleaning and sanitation purposes, and other large and heavy gas utilization appliances that can be moved, shall be connected in accordance with the connector manufacturer's installation instructions using a listed appliance connector complying that is in accordance with CSA ANSI Z21.69/CSA 6.22, Standard for Connectors for Movable Gas Appliances. The commercial cooking appliance connector installation shall be configured in accordance with the manufacturer s installation instructions. (NFPA 54:9.6.1.1) (7) Movement of appliances with casters shall be limited by a restraining device installed in accordance with the connector and appliance manufacturer's installation instructions. [NFPA 54-09:9.6.1.2] (8) In Sections 12121.1(2), 12.1(), and 12.1(5), the connector or tubing shall be installed so as to be protected against physical and thermal damage. Aluminum alloy tubing and connectors shall be coated to protect against external corrosion where they are in contact with masonry, plaster, insulation, or are subject to repeated wettings by such liquids as water (except rainwater), detergents, or sewage.[nfpa 54:9.6.1(7)] 12121.2 Suspended Low-Intensity Infrared Tube Heaters. Suspended low-intensity infrared tube heaters shall be connected to the building piping system with a connector listed for the application in accordance with CSA ANSI Z21.24/CGA 6., Connectors for Gas Appliances and the following requirements. [NFPA 54-09:9.6.1.] (A1) The connector shall be installed in accordance with the tube heater installation instructions, and shall be in the same room as the appliance. (B2) Only oone connector shall be used per appliance. 12121. Use of Nonmetallic Gas Hose Connectors. Listed nonmetallic gas hose connectors shall be used in accordance with the terms of their listing manufacturer s installation instructions and as follows indicated in the following sections. [NFPA 54:9.6.2]: 12..1 (A) Indoor. Indoor gas hose connectors shall be used only to connect laboratory, shop, and ironing equipment requiring mobility during operation. An equipment appliance shutoff valve shall be installed where the connector is attached to the building piping. The connector shall be of minimum length and shall not exceed six (6) feet (1,829 mm). The connector shall not be concealed and shall not extend from one (1) room to another or pass through wall partitions, ceilings, or floors. 12..2 (B) Outdoor. Where Ooutdoor gas hose connectors are permitted used to connect portable outdoor gas-fired appliances, the connector shall be listed in accordance with CSA Z21.54b. An appliance shutoff valve, a listed quick-disconnect device, or a listed gas convenience outlet shall be installed where the connector is attached to the supply piping and in such a manner to prevent the accumulation of water or foreign matter. This connection shall be made only in the outdoor area where the appliance is to be used. The connector length shall not exceed fifteen () feet (4,572 mm). 4 UNIFORM PLUMBING CODE

12121.4 Connection of Portable and Mobile Industrial Gas Appliance. 12.4.1 Flexible Hose (A) Where portable industrial gas utilization appliances, or appliances requiring mobility or subject to vibration, are connected to the building gas piping system by the use of a flexible hose, the hose shall be suitable approved and safe for the conditions under which it can be is used. [NFPA 54:9.6..1] 12.4.2 Swivel Joints or Couplings. (B) Where industrial gas utilization appliances requiring mobility are connected to the rigid piping by the use of swivel joints or couplings, the swivel joints or couplings shall be suitable approved for the service required, and only the minimum number required shall be installed. [NFPA 54:9.6..2] 12.4. All-Metal Flexible Connectors. (C) Where industrial gas utilization appliances subject to vibration are connected to the building piping system by the use of all-metal flexible connectors, the connectors shall be suitable approved for the service required. [NFPA 54:9.6..] 12.4.4 Flexible Connectors. (D) Where flexible connections are used, they shall be of the minimum practical length and shall not extend from one (1) room to another or pass through any walls, partitions, ceilings, or floors. Flexible connections shall not be used in any a concealed location. They shall be protected against physical or thermal damage and shall be provided with gas shutoff valves in readily accessible locations in rigid piping upstream from the flexible connections. [NFPA 54:9.6..4] 12121.5 Appliance Shutoff Valves and Connections. Gas utilization aappliance connected to a piping system shall have an accessible, approved manual shutoff valve with a nondisplaceable valve member, or a listed gas convenience outlet installed within six (6) feet (1.8 29 mm) of the appliance it serves. Where a connector is used, the valve shall be installed upstream of the connector. A union or flanged connection shall be provided downstream from this valve to permit removal of controls. Shutoff valves serving decorative gas appliances shall be permitted to be installed in fireplaces if where listed for such use. [NFPA 54:9.6.4] 12121.6 Quick-Disconnect Devices. Quick-disconnect devices used to connect appliances to the building piping shall be listed. Where they are installed indoors, an approved manual shutoff valve with a nondisplaceable valve member shall be installed upstream of the quick-disconnect device. [NFPA 54:9.6.5] 12121.7 Sediment Trap. Where a sediment trap is not incorporated as a part of the gas utilization appliance, a sediment trap shall be installed downstream of the appliance shutoff valve as close to the inlet of the appliance as practical at the time of appliance installation. The sediment trap shall be either a tee fitting with a capped nipple in the bottom outlet, as illustrated in Figure 12-1 12.7, or other device recognized as an effective sediment trap. Illuminating appliances, ranges, clothes dryers, decorative vented appliances for installation in vented fireplaces, gas fireplaces, and outdoor grills shall not be required to be so equipped. [NFPA 54-09:9.6.7] For SI units: 1 inch = 25.4 mm FIGURE 12-1 12.7 METHOD OF INSTALLING A TEE FITTING SEDIMENT TRAP. 12121.8 Installation of Piping. Piping shall be installed in a manner not to interfere with inspection, maintenance, or servicing of the gas utilization equipment appliance. [NFPA 54:9.6.8] 1212.0 Liquefied Petroleum Gas Facilities and Piping. 1212.1 General. Liquefied petroleum gas facilities shall comply with NFPA 58, Liquefied Petroleum Gas Code. 1214.0 Pressure Testing and Inspection. 1214.1 General. 1214.1.1 Inspection and Testing. Prior to acceptance and initial operation, piping installations shall be visually inspected and pressure-tested to determine that the materials, design, fabrication, and installation practices comply are in accordance with the requirements of this code. [NFPA 54-12:8.1.1.1] 1214.1.2 Inspection Requirements. Inspection shall consist of visual examination during or after manufacture, fabrication, assembly, or pressure tests., as appropriate. Supplementary types of non-destructive inspection techniques, such as magnetic-particle, radiographic, and ultrasonic, shall not be required unless specifically listed herein or in the engineering design. [NFPA 54-12:8.1.1.2] 1214.1. Repairs and Additions. Where repairs or additions are made following the pressure test, the affected piping shall be tested. Minor repairs and additions are not required to be pressure-tested provided that the work is inspected and connections are tested with a noncorrosive leak-detecting fluid or other leak-detecting methods approved by the Authority Having Jurisdiction. [NFPA 54:8.1.1.] 1214.1.4 New Branches. Where new branches are installed from the point of delivery to new appliances, only the newly installed branches shall be required to be pressure-tested. Connections between the new piping and UNIFORM PLUMBING CODE 5

the existing piping shall be tested with a noncorrosive leak-detecting fluid or approved leak-detecting methods. [NFPA 54:8.1.1.4] 1214.1.5 Testing. A piping system shall be tested as a complete unit or in sections. Under no circumstances shall a valve in a line be used as a bulkhead between gas in one (1) section of the piping system and test medium in an adjacent section, unless two (2) valves are installed in series with a valved "telltale" located between these valves. A valve shall not be subjected to the test pressure unless it can be is determined that the valve, including the valve-closing mechanism, is designed to safely withstand the pressure. [NFPA 54:8.1.1.5] 1214.1.6 Regulators and Valves. Regulator and valve assemblies fabricated independently of the piping system in which they are to be installed shall be permitted to be tested with inert gas or air at the time of fabrication. [NFPA 54:8.1.1.6] 1214.1.7 Test Medium. The test medium shall be air, nitrogen, carbon dioxide, or an inert gas. OXYGEN SHALL NEVER BE USED. [NFPA 54:8.1.2] 1214.2 Test Preparation. 1214.2.1 Pipe Joints. Pipe joints, including welds, shall be left exposed for examination during the test. [NFPA 54:8.1..1] Exception: Covered or concealed pipe end joints that have been previously tested in accordance with this code. 1214.2.2 Expansion Joints. Expansion joints shall be provided with temporary restraints, if where required for the additional thrust load under test. [NFPA 54:8.1..2] 1214.2. Appliances and Equipment. Appliances and equipment that are not to be included in the test shall be either disconnected from the piping or isolated by blanks, blind flanges, or caps. Flanged joints at which blinds are inserted to blank off other equipment during the test shall not be required to be tested. [NFPA 54:8.1..] 1214.2.4 Designed for (less than) Operating Pressures. Where the piping system is connected to appliances, equipment, or equipment components designed for operating pressures of less than the test pressure, such appliances, equipment, or equipment components shall be isolated from the piping system by disconnecting them and capping the outlets. [NFPA 54:8.1..4] 1214.2.5 Designed for (equal to or more than) Operating Pressures. Where the piping system is connected to appliances, equipment, or equipment components designed for operating pressures equal to or greater than exceeding the test pressure, such appliances and equipment shall be isolated from the piping system by closing the individual appliance or equipment shutoff valve(s). [NFPA 54:8.1..5] 1214.2.6 Safety. Testing of piping systems shall be done with due regard for the safety of employees and the public during the test. Bulkheads, anchorage, and bracing suitably designed to resist test pressures shall be installed if where necessary. Prior to testing, the interior of the pipe shall be cleared of foreign material. [NFPA 54:8.1..6] 1214. Test Pressure. 1214..1 General. Test pressure shall be measured with a manometer or with a pressure-measuring device designed and calibrated to read, record, or indicate a pressure loss due to leakage during the pressure test period. The source of pressure shall be isolated before the pressure tests are made. Mechanical gauges used to measure test pressures shall have a range such that the highest end of the scale does not exceed five (5) times the test pressure. [NFPA 54:8.1.4.1] 1214..2 The test pressure to be used shall be not less than one and one half (1-1 ) times the proposed maximum working pressure, but not less than three () psi ( kpa), irrespective of design pressure. [NFPA 54:8.1.4.2] 1214.. Test duration shall be not less than one-half ( 1 ) hour for each five-hundred (0) cubic feet (14 m ) of pipe volume or fraction thereof. When testing a system having a volume less than ten () cubic feet (0.28 m ) or a system in a single-family dwelling, the test duration shall be not less than ten () minutes. The duration of the test shall not be required to exceed twenty-four (24) hours. [NFPA 54:8.1.4.] This inspection shall include an air, CO 2, or nitrogen pressure test, at which time the gas piping shall stand a pressure of not less than psi (69 kpa) gauge pressure. Test pressures shall be held for a length of time satisfactory to the Authority Having Jurisdiction, but in no case less than minutes with no perceptible drop in pressure. For welded piping, and for piping carrying gas at pressures in excess of 14 inches water column pressure (.5 kpa), the test pressure shall be not less than psi (414 kpa) and shall be continued for a length of time satisfactory to the Authority Having Jurisdiction, but in no case for less than minutes. These tests shall be made using air, CO 2, or nitrogen pressure and shall be made in the presence of the Authority Having Jurisdiction. Necessary apparatus for conducting tests shall be furnished by the permit holder. Test gauges used in conducting tests shall be in accordance with Section 17.0. 1214.4 Detection of Leaks and Defects. 1214.4.1 Indication of Leaks. The piping system shall withstand the test pressure specified without showing any evidence of leakage or other defects. Any rreduction of test pressures as indicated by pressure gauges shall be deemed to indicate the presence of a leak unless such reduction can be is readily attributed to some other cause. [NFPA 54:8.1.5.1] 1214.4.2 Detecting Leaks. The leakage shall be located by means of an approved gas detector, a noncorrosive leak detection fluid, or other approved leak detection methods. Matches, candles, open flames, or other methods that provide a source of ignition shall not be used. [NFPA 54:8.1.5.2] 6 UNIFORM PLUMBING CODE

1214.4. Repair or Replace. Where leakage or other defects are located, the affected portion of the piping system shall be repaired or replaced and retested. [(See Section 1214.1.).] [NFPA 54:8.1.5.] 1214.5 Piping Systems Leak Check. 1214.5.1 Test Gases. Leak checks using fuel gas shall be permitted in piping systems that have been pressure-tested in accordance with Section 1214.0. [NFPA 54:8.2.1] 1214.5.2 Turning Gas On. During the process of turning gas on into a system of new gas piping, the entire system shall be inspected to determine that there are no open fittings or ends and that valves at unused outlets are closed and plugged or capped. [NFPA 54-09:8.2.2] 1214.5. Leak Check. Immediately after the gas is turned on into a new system or into a system that has been initially restored after an interruption of service, the piping system shall be checked for leakage. Where leakage is indicated, the gas supply shall be shut off until the necessary repairs have been made. [NFPA 54:8.2.] 1214.5.4 Placing Appliances and Equipment in Operation. Gas utilization aappliances and equipment shall not be placed in operation until after the piping system has been tested checked in accordance with Section 1214.5., connections to the appliance are checked for leakage, and purged in accordance with Section 1214.6.2. [NFPA 54-12:8.2.4] 1214.6 Purging. 1214.6.1 Removal From Service. When gas piping is to be opened for servicing, addition, or modification, the section to be worked on shall be turned off from the gas supply at the nearest convenient point and the line pressure vented to the outdoors or to ventilated areas of sufficient size to prevent accumulation of flammable mixtures. The remaining gas in this section of pipe shall be displaced with an inert gas as required by Table 12-5. [NFPA 54:8..1] 1214.6.2 Placing in Operation. When piping full of air is placed in operation, the air in the piping shall be displaced with fuel gas, except where such piping is required by Table 12-6 to be purged with an inert gas prior to introduction of fuel gas. The air can be safely displaced with fuel gas provided that a moderately rapid and continuous flow of fuel gas is introduced at one (1) end of the line and air is vented out at the other end. The fuel gas flow shall be continued without interruption until the vented gas is free of air. The point of discharge shall not be left unattended during purging. After purging, the vent shall then be closed. Where required by Table 12-6, the air in the piping shall first be displaced with an inert gas, and the inert gas shall then be displaced with fuel gas. [NFPA 54:8..2] 1214.6. Discharge of Purged Gases. The open end of piping systems being purged shall not discharge into confined spaces or areas where there are sources of ignition unless precautions are taken to perform this operation in a safe manner by ventilation of the space, control of purging rate, and elimination of hazardous conditions. [NFPA 54:8..] 1214.6.4 Placing Appliances in Operation. After the piping has been placed in operation, appliances shall be purged and then placed in operation, as necessary. [NFPA 54:8..4] 121.6 Purging. Purging shall comply with Section 121.6.1 and Section 121.6.4. 121.6.1 Where Required. 121.6.1.1 Conditions. The purging of piping systems shall be in accordance with Section 121.6.2 through Section 121.6.4 where the piping system meets either of the following: (1) The designed operating gas pressure is greater than 2 psig (14 kpa). (2) The piping being purged contains pipe sizes greater than 2 inches ( mm). 121.6.1.2 Monitored. Where piping systems not covered under Section 121.6.1.1 are purged with fuel gas the discharge point, whether indoor or outdoor, shall be attended and monitored with a combustible gas indicator and purging stopped where fuel gas is indicated at the discharge point. 121.6.2 Removal From Service. Where existing gas piping meeting Section 121.6.1 is to be opened for an addition, or modification, or service, the section to be worked on shall be isolated from the gas supply and the line pressure vented in accordance with Section 121.6.4. Where gas piping meeting the criteria of Table 121.6.2 is removed from service the residual fuel gas in the piping shall be displaced with an inert gas. TABLE 12-5 121.6.2 LENGTH OF PIPING REQUIRING PURGING WITH INERT GAS FOR SERVICING OR MODIFICATION [NFPA 54: TABLE 8..1] NOMIL PIPE SIZE LENGTH OF PIPING REQUIRING PURGING (inch.) (feet.) 2 1 > > 4 > 6 > 8 or larger Any length For SI units: 1 inch = 25 mm, 1 foot. = 0.5 4.8 mm. 121.6. Placing in Operation. Where gas piping meeting the criteria of Table 121.6.2, containing air, is placed in operation the air in the piping shall first be displaced with an inert gas. The inert gas shall then be displaced with fuel gas in accordance with Section 121.6.4. 121.6.4 Outdoor Discharge of Purged Gases. The open end of piping systems being pressure vented or purged shall discharge directly to an outdoor location in accordance with the following requirements: UNIFORM PLUMBING CODE 7

(1) The point of discharge shall be controlled with a shutoff valve. (2) The discharge point shall be not less than feet (48 mm) from sources of ignition, located not less than feet (48 mm) from building openings, and not less than 25 feet (76 mm) from mechanical air intake openings. () During discharge, the open discharge point shall be continuously attended and monitored with a combustible gas indicator. TABLE 12-6 Length of Piping Requiring Purging with Inert Gas Before Placing in Operation [NFPA 54: Table 8..2] NOMIL PIPE SIZE (in.) LENGTH OF PIPING REQUIRING PURGING (ft.) > 4 > 6 > 8 or larger Any length For SI units: 1 ft. = 0.5 m. 124.0 Interconnections Between Gas Piping Systems. [NFPA 54:5.] 124.1 Interconnections Supplying Separate Users. Where two (2) or more meters, or two (2) or more service regulators where meters are not provided, are located on the same premises and supply separate users, the gas-piping systems shall not be interconnected on the outlet side of the meters or service regulators. [NFPA 54:5..1] 124.2 Interconnections for Standby Fuels. Where supplementary gas for standby use is connected downstream from a meter or a service regulator where a meter is not provided, a device to prevent backflow shall be installed. [NFPA 54:5..2.1] A three-way valve installed to admit the standby supply and at the same time shut off the regular supply shall be permitted to be used for this purpose. [NFPA 54:5..2.2] 12165.0 Required Gas Supply. 12165.1 General. The following regulations, as set forth in this section and in Section 12176.0, Required Gas Piping Size, shall be the standard for the installation of gas piping. Natural gas regulations and tables are based on the use of gas having a specific gravity of sixty-hundredths (0.), supplied at six (6) to eight (8) inches (2 to mm) water column (1.5 kpa to 1.9 kpa) pressure at the outlet of the meter or regulator. For undiluted liquefied petroleum gas, gas piping shall be permitted to be sized at eleven () inches (279 mm) water column (2.7 kpa) pressure at the outlet of the meter or regulator and specific gravity of one and fifty-hundredths (1.). Note: Where gas of a different specific gravity is to be delivered, the serving gas supplier should be contacted for specific gravity conversion factors to use provided by the serving gas supplier shall be used in sizing piping systems from the pipe sizing tables in this chapter. 12165.2 Volume. The hourly volume of gas required at each piping outlet shall be taken as not less than the maximum hourly rating as specified by the manufacturer of the appliance or appliances to be connected to each such outlet. 12165. Gas Appliances. Where the gas appliances to be installed have not been definitely specified, Table 12-1.4.2 shall be permitted to be used as a reference to estimate requirements of typical appliances. To obtain the cubic feet per hour (L/sec.) of gas required, divide input of appliances by the average Btu (Watt-hour kw) heating value per cubic foot (L) of the gas. The average Btu (Watt-hour kw) per cubic foot (L) of the gas in the area of the installation shall be permitted to be obtained from the serving gas supplier. 12165.4 Size of Piping Outlets. The size of the supply piping outlet for any a gas appliance shall not be less than one-half ( 1 ) of an inch ( mm). The minimum size of any a piping outlet for a mobile home shall be not less than three-quarters ( 4) of an inch ( mm). 12176.0 Required Gas Piping Size. 12176.1 Pipe Sizing Methods. Where the pipe size is to be determined using any a of the methods in Sections 12176.1.1 through Section 12176.1., the diameter of each pipe segment shall be obtained from the pipe-sizing tables in Section 12176.2 or from the sizing equations in Section 12176.. [NFPA 54:6.1] 12176.1.1 Longest Length Method. The pipe size of each section of gas piping shall be determined using the longest length of piping from the point of delivery to the most remote outlet and the load of the section (ssee calculation example in Figure 12-2 1216.1.1). [NFPA 54:6.1.1] 12176.1.2 Branch Length Method. Pipe shall be sized as follows [NFPA 54:6.1.2]: (1) (A) Pipe size of each section of the longest pipe run from the point of delivery to the most remote outlet shall be determined using the longest run of piping and the load of the section. (2) (B) The pipe size of each section of branch piping not previously sized shall be determined using the length of piping from the point of delivery to the most remote outlet in each branch and the load of the section. 12176.1. Hybrid Pressure. The pipe size for each section of higher-pressure gas piping shall be determined using the longest length of piping from the point of delivery to the most remote line pressure regulator. The pipe size from the line pressure regulator to each outlet shall be determined using the length of piping from the regulator to the most remote outlet served by the regulator. [NFPA 54:6.1.] 12176.2 Tables for Sizing Gas-Piping Systems. Tables 12-8 1216.2(1) through Table 12-41 1216.2(6) shall be used to size gas piping in conjunction with one (1) of the methods described in Sections 12176.1.1 through Section 12176.1.. [NFPA 54:6.2] 12176. Sizing Equations. The inside diameter of smooth-wall pipe or tubing shall be determined by the sizing eequations 12-1 1216.(1) or Equation 12-2 1216.(2), using the equivalent pipe length determined by Sections 12176.1.1 through Section 12176.1.. [NFPA 54:6.4] 8 UNIFORM PLUMBING CODE

TABLE 12-4 1216. Cr AND Y FOR TURAL GAS AND UNDILUTED PROPANE AT STANDARD CONDITIONS [NFPA 54: TABLE 6.4.2] FORMULA FACTORS GAS Cr Y Natural Gas 0.94 0.9992 Undiluted Propane 1.2462 0.99 For SI units: 1 ft. cubic foot = 0.028 m, 1 foot = 0.54.8mm, 1 inch water column = 0.249 kpa, 1 psi pound-force per square inch = 6.894 kpa, 1,000 Btu/h British thermal units per hour = 0.29 kw. Equation 12-1 1216.(1) Low-Pressure Gas Formula (Less than 1.5 psi [. kpa]): [NFPA 54:6.4.1] D = 19.17 Q 0.81 0.6 H ( Cr x L) where: D = inside diameter of pipe, inches Q = input rate appliance(s), cubic feet per hour at F (16ºC) and inch (759 mm) mercury column P 1 = upstream pressure, psia (P 1 + 14.7) P 2 = downstream pressure, psia (P 2 + 14.7) L = equivalent length of pipe, feet H =pressure drop, inches water column (27.7 in. H 2 O=1 psi) Cr and Y in accordance with with Table 1216. For SI units: 1 inch = 25 mm, 1 pound-force per square inch = 6.894 kpa, t/ C = (t/ F-2)/1.8, 1 inch mercury column =.9 kpa, 1 inch water column = 0.249 kpa. Equation 12-2 1216.(2) High-Pressure Gas Formula (1.5 psi [. kpa] and above): [NFPA 54:6.4.2] D = Q 0.81 0.6.9 [ (P 12 P 22 ) Y Cr x L ] where: D = inside diameter of pipe, inches Q = input rate appliance(s), cubic feet per hour at ºF (16ºC) and inch (759 mm) mercury column P 1 = upstream pressure, psia (P 1 + 14.7) P 2 = downstream pressure, psia (P 2 + 14.7) L = equivalent length of pipe, feet. H = pressure drop, inches water column (27.7 in. H 2 O=1 psi) Cr and Y in accordance with with Table 1216. For SI units: 1 inch = 25 mm, 1 pound-force per square inch = 6.894 kpa, t/ C = (t/ F-2)/1.8, 1 inch mercury column =.9 kpa, 1 inch water column = 0.249 kpa. 12176.4 Sizing of Piping Sections. To determine the size of each section of pipe in any a system within the range of the Table 1216.2(1) through Table 1216.2(6), proceed as follows: (1) (A) Measure the length of the pipe from the gas meter location to the most remote outlet on the system. (2) (B) Select the length in feet column and row showing the distance, or the next longer distance if where the table does not give the exact length. () (C) Starting at the most remote outlet, find in the row just selected the gas demand for that outlet. If Where the exact figure of demand is not shown, choose the next larger figure in the row. (4) (D) At the top of this column will be found the correct size of pipe. (5) (E) Using this same row, proceed in a similar manner for each section of pipe serving this outlet. For each section of pipe, determine the total gas demand supplied by that section. Where gas piping sections serve both heating and cooling appliances and the installation prevents both units from operating simultaneously, only the larger of the two (2) demand loads needs be used in sizing these sections. (6) (F) Size each section of branch piping not previously sized by measuring the distance from the gas meter location to the most remote outlet in that branch and follow the procedures of steps B, C, D, and E 2,, 4, and 5 above. Note: Size branch piping in the order of their distance from the meter location, beginning with the most distant outlet not previously sized. 12176.5 Engineering Methods. For conditions other than those covered by Section 12176.1, such as longer runs or greater gas demands, the size of each gas piping system shall be determined by standard engineering methods acceptable to the Authority Having Jurisdiction, and each such system shall be so designed that the total pressure drop between the meter or other point of supply and any an outlet when where full demand is being supplied to all outlets, shall comply be in accordance with the requirements of Section 198.4. 12176.6 Variable Gas Pressure. Where the gas pressure exceeds fourteen (14) inches (56 mm.5 kpa) or less than six (6) inches (2 mm 1.5 kpa) of water column, or when where diversity demand factors are used, the design, pipe, sizing, materials, location, and use of such systems first shall be approved by the Authority Having Jurisdiction. Piping systems designed for pressures exceeding the serving gas supplier's standard delivery pressure shall have prior verification from the gas supplier of the availability of the design pressure. UNIFORM PLUMBING CODE 9

FIGURE 12-2 1216.1.1 EXAMPLE ILLUSTRATING USE OF TABLES 12-1.4.2 AND 12-8 1216.2(1) Problem: Determine the required pipe size of each section and outlet of the piping system shown in Figure 12-2 1216.1.1. Gas to be used has a specific gravity of sixty-hundredths (0.) and eleven-hundred (1,0) British thermal units (Btu) per cubic foot (.4 0.04 Watt-hour/L kw/l), delivered at eight (8) inch ( mm 1.9 kpa) water column pressure. For SI units: 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 cubic foot per hour = 0.00787 L/s Solution: (1) Maximum gas demand of outlet A 2 cubic feet per hour (0.2 L/sec.) (from Table 12-1.4.2). Maximum gas demand of outlet B cubic feet per hour (0.02 L/sec.) (from Table 12-1.4.2). Maximum gas demand of outlet C 59 cubic feet per hour (0.46 L/sec.) (from Table 12-1.4.2). Maximum gas demand of outlet D 16 cubic feet per hour (1.1 L/sec.) (1,000 Btu/hour [4,9 kw]) divided by 1,0 Btu per cubic foot (.4 Watt-hour/L 0.04 kw/l) (2) The length of pipe from the gas meter to the most remote outlet (outlet A) is feet (,288 mm). () Using the length in feet column row marked feet (,288 mm) in Table 12-8 1216.2(1): Outlet A, supplying 2 cubic feet per hour (0.2 L/sec.), requires one-half ( 1 ) of an inch ( mm) pipe. Section 1, supplying outlets A and B, or 5 cubic feet per hour (ft /h)(0.27 L/s) (0.24 L/sec.) requires one-half ( 1 ) of an inch ( mm) pipe. Section 2, supplying outlets A, B, and C, or 94 cubic feet per hour (0.74 L/sec.) requires three-quarters ( 4) of an inch ( mm) pipe. Section, supplying outlets A, B, C, and D, or 2 cubic feet per hour (1.9 L/sec.), requires one (1) inch (25 mm) pipe. (4) Using the column marked feet (,288 mm) in Table 12-8 1216.2(1) (no column for actual length of 55 feet [16,764 mm]: Outlet B supplying cubic feet per hour (0.02 L/sec.), requires one-half ( 1 ) of an inch ( mm) pipe. Outlet C, supplying 59 cubic feet per hour (0.46 L/sec.), requires one-half ( 1 ) of an inch ( mm) pipe. (5) Using the column marked feet (,288 mm) in Table 12-8 1216.2(1): Outlet D, supplying 16 cubic feet per hour (1.7 L/sec.), requires ( 4) of an inch ( mm) pipe. 1 UNIFORM PLUMBING CODE

TABLE 12-8 1216.2(1) SCHEDULE METALLIC PIPE [NFPA 54: TABLE 6.2(b)] GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 0.5 in w.c. SPECIFIC GRAVITY: 0. NOMIL: 1 PIPE SIZE (inch) 4 1 1 1 4 1 1 2 2 1 4 5 6 8 12 ACTUAL ID: 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 5.047 6.065 7.981.0.98 LENGTH (feet) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 172 1 95 81 72 65 56 52 44 7 4 27 25 2 22 21 19 17 17 16 16 14 14 1 12 12 247 199 1 1 17 1 7 1 4 92 8 77 71 6 57 5 49 46 4 41 9 8 6 5 4 2 1 28 27 25 24 2 22 22 21 678 466 74 284 257 27 2 7 195 17 7 144 14 9 8 99 92 86 82 78 74 71 68 66 6 61 59 58 56 5 51 49 47 45 44 42 41 9 1 957 768 657 58 528 486 452 424 0 55 22 296 275 244 221 9 177 168 9 2 145 1 1 1 122 1 5 9 4 0 96 9 89 86 84 81 79 14 985 87 791 728 677 65 0 52 482 44 412 66 1 5 28 6 251 29 228 2 9 2 195 9 178 17 164 6 1 144 19 14 1 1 122 9 CAPACITY IN CUBIC FEET OF GAS PER HOUR 27 22 10 16 10 12 928 854 794 4 68 587 546 512 484 459 48 4 89 75 6 52 42 16 1 289 277 7 258 2 242 25 229 40 5 24 22 19 16 14 1 12 95 8 816 771 72 699 669 64 619 598 579 561 545 5 4 4 442 4 4 98 86 75 64 0 77 62 5 47 42 9 6 4 2 28 24 22 19 10 16 14 1 12 12 992 96 97 8 849 81 781 752 727 682 662 644 2 0 0 12 0 0 96 87 74 66 58 5 49 45 6 1 29 27 25 24 2 22 21 19 19 17 16 14 14 1 1 1 41 0 28 0 2 000 19 0 17 0 0 14 0 1 0 12 0 12 000 0 96 88 82 7 66 56 5 47 45 4 41 0 7 6 5 4 2 1 00 28 27 25 25 24 2 67 0 46 0 7 0 1 0 28 0 25 0 2 0 22 000 0 19 0 17 0 0 14 0 1 0 0 0 98 91 86 81 77 7 67 65 6 61 59 57 5 48 46 40 4 9 8 19 000 95 0 76 0 65 0 58 0 52 0 48 0 45 0 42 0 000 5 0 2 0 29 0 27 0 24 0 22 0 0 0 17 0 16 0 0 0 14 0 14 000 1 0 1 000 12 0 12 0 0 0 0 0 99 95 92 89 86 8 81 79 252 000 17 000 19 000 9 000 6 000 95 0 88 0 81 0 76 0 72 0 64 0 58 0 5 0 49 0 44 0 0 6 0 4 0 2 0 0 28 0 27 0 0 25 0 24 0 2 0 22 0 22 0 21 0 0 19 0 0 0 17 0 16 0 16 0 0 0 14 0 14 0 99 000 275 000 2 000 9 000 167 000 2 000 19 000 1 000 122 000 5 000 2 000 92 0 84 0 79 000 000 6 0 58 0 54 0 0 48 0 45 0 4 0 41 0 0 8 0 7 0 6 0 5 000 4 000 0 1 0 000 28 0 27 0 0 25 0 24 0 24 0 2 0 22 0 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa Notes: (1) All ttable entries are rounded to significant digits. (2) means a flow of less than cfh ft /h (0.08 L/s). UNIFORM PLUMBING CODE 191

TABLE 1216.2(2) SCHEDULE METALLIC PIPE [NFPA 54-12: TABLE 6.2(c)] NOMIL 1 GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP:.0 in. w.c. SPECIFIC GRAVITY: 0. INTENDED USE: INITIAL SUPPLY PRESSURE OF 8.0 IN. W.C. OR GREATER PIPE SIZE (inch) 4 1 1 1 4 1 1 2 2 1 4 ACTUAL ID 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 LENGTH (feet) CAPACITY IN CUBIC FEET OF GAS PER HOUR 454 949 1787 669 5497 588 16 875 29 82 4 678 12 652 1228 2522 778 7277 598 0 2 524 986 25 4 5844 914 16 465 24 7 214 448 844 17 2597 01 7971 14 092 62 1 97 748 6 22 44 65 12 489 286 172 678 192 85 16 61 16 16 569 8 1 624 12 1919 695 5889 4 24 147 8 5 91 1785 47 5479 9685 14 1 289 544 1675 225 51 87 1 5 0 27 514 56 82 46 4856 8584 12 568 6 242 456 96 12 20 4 78 19 1 5 219 41 848 12 2446 899 689 09 96 2 7 69 2251 587 642 9285 0 8 5 7 87 94 7 50 868 2 166 1 64 964 56 2958 5229 7656 0 72 1 284 58 87 1681 478 697 66 19 1 56 47 2465 459 682 0 62 129 24 499 747 149 2294 55 597 4 58 121 228 468 1 1 22 4 55 0 55 4 2 442 662 1275 594 52 5 52 9 4 4 629 12 191 41 4997 0 4 195 0 0 56 42 256 4767 6 47 99 7 84 575 17 1764 1 4565 0 46 95 179 68 552 6 1695 2996 486 7 44 92 17 55 52 24 162 2886 4225 0 42 89 167 4 514 989 76 2787 8 41 86 162 2 497 957 97 949 0 8 7 22 482 928 1479 828 9 9 81 2 12 468 1 146 259 7 00 8 79 148 4 455 877 197 24 616 10 6 75 141 289 42 8 127 246 45 4 71 14 275 412 794 16 228 277 68 128 4 95 761 1212 214 10 1 65 12 25 79 71 65 59 14 10 6 9 244 66 4 22 198 24 10 29 61 5 5 6 8 19 24 10 28 59 1 228 42 658 48 54 2714 10 27 57 8 221 1 68 17 1797 1 10 27 56 5 2 22 619 987 1745 2555 00 54 2 9 1 2 9 1698 2485 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa Note: Table entries are rounded to significant digits. 192 UNIFORM PLUMBING CODE

TABLE 1216.2() SCHEDULE METALLIC PIPE [NFPA 54: TABLE 6.2(d)] NOMIL 1 GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 6.0 in. w.c. SPECIFIC GRAVITY: 0. INTENDED USE: INITIAL SUPPLY PRESSURE OF 8.0 IN. W.C. OR GREATER PIPE SIZE (inch) 4 1 1 1 4 1 1 2 2 1 4 ACTUAL ID 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 LENGTH (feet) CAPACITY IN CUBIC FEET OF GAS PER HOUR 6 1 20 58 7999 5 24 55 4 5 6 551 454 949 1787 669 5497 588 16 875 29 82 4 678 64 762 145 2946 44 82 1 551 2 956 5 075 12 652 1228 2522 778 7277 598 0 276 578 89 225 49 6449 279 172 6 2 524 986 25 4 5844 914 16 465 24 7 2 482 7 6 2791 576 8568 147 22 178 214 448 844 17 2597 01 7971 14 092 62 1 4 792 16 247 469 7479 1 222 19 59 0 1 97 748 6 22 44 65 12 489 286 168 52 66 161 928 61 069 16 7 1 19 1 124 48 559 567 029 14 684 1 29 55 5 10 275 5219 9227 1 9 0 27 514 56 82 46 4856 8584 12 568 2 6 242 456 96 12 20 4 78 19 0 5 219 41 848 12 2446 899 689 09 96 2 7 69 2251 587 642 9285 0 8 5 7 87 94 7 50 868 4 84 176 2 681 1965 555 85 0 166 1 64 964 56 2958 5229 7656 5 76 8 297 6 9 1762 29 4966 7271 0 72 1 284 58 87 1681 478 697 6 69 144 272 558 86 16 2566 457 664 0 66 19 1 56 47 2465 459 682 7 64 14 252 516 774 14 275 4199 6148 0 62 129 24 499 747 149 2294 55 597 8 25 48 72 19 22 924 5745 0 58 121 228 468 1 1 22 4 55 9 56 1 221 454 681 1 695 54 00 55 4 2 442 662 1275 594 52 10 52 9 4 4 629 12 191 41 4997 4 195 0 0 56 42 256 4767 47 99 7 84 575 17 1764 1 4565 10 46 95 179 68 552 6 1695 2996 486 10 44 92 17 55 52 24 162 2886 4225 10 42 89 167 4 514 989 76 2787 10 41 86 162 2 497 957 97 949 10 8 7 22 482 928 1479 828 10 9 81 2 12 468 1 146 259 7 00 8 79 148 4 455 877 1 97 2 4 616 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa Note: Table entries are rounded to significant digits. UNIFORM PLUMBING CODE 19

TABLE 12-9 1216.2(4) SCHEDULE METALLIC PIPE [NFPA 54-12: TABLE 6.2(ce)] NOMIL: 1 PIPE SIZE (inch) GAS: TURAL INLET PRESSURE: 2.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 2 1 4 ACTUAL ID: 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 869 75 67 6 569 52 2 462 414 72 44 279 25 22 216 192 2 174 166 1 4 149 144 19 12 9 4 1 6 2 99 96 9 91 21 17 1 12 94 86 751 695 642 58 528 486 452 424 1 81 6 48 4 22 1 292 28 275 2 2 29 2 221 214 7 0 195 9 55 9 2 27 24 22 20 19 17 1 12 945 869 9 759 717 681 6 622 598 576 556 58 522 7 49 468 446 427 4 96 82 58 48 9 CAPACITY IN CUBIC FEET OF GAS PER HOUR 0 65 57 51 46 4 8 5 1 28 21 24 21 19 17 16 14 10 1 12 12 10 9 917 878 84 812 784 759 76 7 695 17 0 12 0 98 85 76 69 64 50 52 40 42 9 6 2 29 24 2 22 00 19 17 17 16 10 14 1 1 12 12 10 2 0 2 0 19 000 16 0 14 0 1 0 12 0 0 000 0 81 75 69 61 51 47 40 42 8 6 5 4 2 1 00 29 27 25 24 2 22 21 21 52 0 7 0 0 0 2 0 21 0 19 0 0 17 0 16 0 14 0 1 000 12 000 0 98 89 82 76 71 67 64 61 58 56 54 52 49 47 46 44 42 8 7 6 4 2 0 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa Note: All ttable entries are rounded to significant digits. 92 0 65 0 5 0 46 0 41 0 7 0 5 0 2 0 0 28 0 25 0 22 0 21 0 19 0 17 0 0 14 0 1 0 12 0 12 000 0 0 0 99 96 92 89 87 84 82 78 74 71 68 60 6 61 59 58 56 9 000 14 000 9 000 94 0 84 0 77 0 71 0 67 000 6 0 58,0 52 0 46 0 4 0 000 5 0 2 0 29 0 27 0 25 0 24 0 2 0 22 0 21 0 0 19 0 0 0 17 0 17 0 16 0 0 0 14 0 14 000 1 0 1 000 12 0 12 0 0 0 194 UNIFORM PLUMBING CODE

TABLE 12-1216.2(5) SCHEDULE METALLIC PIPE [NFPA 54-12: TABLE 6.2(df)] NOMIL: 1 PIPE SIZE (inch) GAS: TURAL INLET PRESSURE:.0 psi PRESSURE DROP: 2.0 psi SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 2 1 4 ACTUAL ID: 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 2 16 985 892 821 764 717 677 0 544 0 465 412 74 44 0 28 9 257 246 228 2 21 6 0 195 5 177 169 162 6 1 146 142 14 49 27 2 17 10 10 14 12 97 862 781 719 669 627 59 56 57 514 494 476 4 445 41 419 7 87 69 5 27 16 6 296 288 2 92 6 51 4 8 5 2 28 2 21 19 16 14 1 12 969 91 897 866 88 812 789 767 729 695 666 6 616 595 576 558 542 527 CAPACITY IN CUBIC FEET OF GAS PER HOUR 19 000 1 0 0 89 79 72 66 61 50 54 48 40 7 27 25 24 22 21 19 19 17 17 16 16 10 14 1 1 12 12 28 0 19 0 0 1 0 0 0 99 92 86 72 65 56 00 45 41 8 6 4 2 1 29 28 27 25 20 24 2 22 21 19 10 17 17 16 16 54 0 7 0 0 25 0 2 000 0 19 0 17 0 16 0 0 14 000 12 0 0 0 96 87 74 00 66 62 59 57 55 5 51 49 48 46 45 4 41 9 7 6 5 4 2 1 87 0 0 48 0 41 0 6 0 0 0 28 0 0 25 0 22 0 0 0 17 0 0 1 0 12 0 0 0 0 000 95 91 87 84 81 79 76 74 72 68 65 62 58 56 54 52 51 49 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa Note: All ttable entries are rounded to significant digits. 5 000 6 000 85 0 7 0 64 0 58 0 54 000 0 47 0 44 0 9 0 5 0 2 0 0 27 0 24 0 22 0 21 000 19 0 0 17 0 16 0 16 0 0 000 14 0 14 000 1 0 1 0 12 0 12 0 0 0 0 0 000 96 9 80 16 000 217 000 174 000 149 000 12 000 1 000 1 000 00 96 0 0 0 72 0 67 0 62 0 55 0 0 46 0 42 0 0 8 000 6 0 4 0 000 1 0 0 29 0 28 0 27 0 0 0 24 0 2 0 22 0 21 0 21 000 0 19 0 19 000 0 000 UNIFORM PLUMBING CODE 195

TABLE 12-1216.2(6) SCHEDULE METALLIC PIPE [NFPA 54-12: TABLE 6.2(eg)] NOMIL: 1 PIPE SIZE (inch) GAS: TURAL INLET PRESSURE: 5.0 psi PRESSURE DROP:.5 psi SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 2 1 4 ACTUAL ID: 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 1 22 14 979 876 786 728 67 558 6 465 4 6 84 64 48 8 298 288 279 271 4 2 29 229 2 212 5 198 192 6 1 64 45 7 2 28 24 2 21 19 17 14 1 97 5 849 2 762 727 696 669 644 622 2 584 567 551 524 0 478 4 44 428 414 1 79 0 8 67 58 52 40 44 42 9 6 2 29 24 20 19 17 10 14 1 1 12 12 10 987 941 1 866 84 6 7 756 74 714 CAPACITY IN CUBIC FEET OF GAS PER HOUR 24 0 17 0 14 000 12 0 0 98 91 85 74 66 59 55 45 7 0 2 0 29 28 25 24 24 2 22 21 21 19 17 17 16 10 14 6 0 25 0 0 0 16 0 14 0 1 0 12 0 12 0 0 99 89 82 76 67 61 56 52 49 46 44 42 8 7 6 4 2 0 20 27 25 24 20 2 22 20 69 0 49 0 0 4 0 1 0 28 0 0 24 0 2 0 21 0 19 0 17 0 0 14 0 1 000 0 0 0 94 89 81 77 74 71 69 67 65 6 61 58 55 5 51 49 47 46 44 4 42 1 000 78 0 64 0 55 0 49 0 45 0 42 000 9 0 7 000 4 0 0 27 0 25 0 2 0 0 0 17 0 16 0 0 14 0 1 0 12 0 12 0 0 0 0 0 0 0 98 9 88 85 81 78 76 7 71 69 67 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa Note: All ttable entries are rounded to significant digits. 196 000 19 000 000 98 0 87 0 0 74 0 69 0 65 0 0 54 000 48 0 44 0 41 0 6 0 0 0 28 0 0 25 0 24 000 22 0 21 0 21 000 0 19 0 0 0 17 0 17 0 16 0 0 000 14 0 1 0 1 0 1 000 12 0 12 0 0 1 000 28 000 21 000 0 000 179 000 164 000 1 000 142 000 14 000 12 000 1 000 98 0 91 0 84 0 74 0 67 0 62 0 58 0 54 0 51 0 48 0 46 0 44 0 42 0 41 0 9 0 8 0 7 0 6 0 5 0 0 2 000 0 29 0 28 0 27 0 0 25 0 25 000 24 0 196 UNIFORM PLUMBING CODE

TABLE 12-12 1216.2(7) SEMI-RIGID COPPER TUBING [NFPA 54-12: TABLE 6.2(fh)] NOMIL: K & L: 1 4 ACR: 1 1 5 5 4 TUBE SIZE (inch) GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 0. in. w.c. SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 14 42 29 2 17 16 14 1 1 12 85 58 47 5 2 29 27 24 22 17 1 12 CAPACITY IN CUBIC FEET OF GAS PER HOUR 148 2 82 62 56 52 48 45 4 8 4 1 29 2 22 19 17 16 14 14 1 1 1 12 12 00 12 25 46 72 1 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa *Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. Notes: (1) All ttable entries are rounded to significant digits. (2) means a flow of less than cfh ft /h (0.08 L/s). 2 144 6 99 88 79 7 68 64 5 48 45 41 7 1 28 27 25 24 2 22 21 19 17 16 16 14 14 1 1 1 12 448 8 247 2 7 1 6 145 16 129 4 95 89 78 71 65 61 57 54 51 49 47 45 4 42 9 8 7 5 4 2 1 29 28 27 6 554 445 81 7 6 281 2 245 22 6 6 171 9 141 128 1 1 97 92 88 84 81 78 75 7 71 69 67 6 58 56 54 52 49 47 12 87 1 0 52 482 44 41 87 66 24 294 2 251 22 2 6 17 162 145 19 1 128 12 9 5 1 8 5 0 95 91 88 84 82 79 77 74 14 12 00 924 859 6 761 675 612 56 52 464 4 87 8 19 289 277 6 256 247 29 22 225 219 8 199 1 176 1 164 9 5 UNIFORM PLUMBING CODE 197

TABLE 12-1 1216.2(8) SEMI-RIGID COPPER TUBING [NFPA 54-12: TABLE 6.2(gi)] GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 0.5 in. w.c. SPECIFIC GRAVITY: 0. TUBE SIZE (inch) NOMIL: K & L: 1 4 1 5 4 1 1 1 4 1 1 2 ACR: 1 5 4 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) CAPACITY IN CUBIC FEET OF GAS PER HOUR 27 1 55 8 2 1 77 61 5 47 195 14 7 92 82 276 1 2 6 5 6 279 247 7 586 2 445 16 925 791 1 4 20 19 16 14 0 21 19 17 16 42 9 6 4 2 74 68 6 59 56 5 96 84 79 224 6 192 1 1 71 45 24 6 65 585 544 5 482 1 12 00 1 0 2 14 1 12 28 24 22 45 41 9 4 64 59 55 48 1 16 7 271 245 2 2 6 427 87 56 1 294 8 6 742 6 612 0 0 4 0 16 14 1 1 28 25 2 44 8 5 94 86 75 71 169 5 144 128 6 245 228 214 2 554 5 474 445 4 5 0 6 0 7 1 12 12 22 21 19 2 29 28 27 68 64 62 59 57 122 6 1 7 192 168 162 99 81 65 8 0 8 0 9 00 17 17 16 25 24 24 2 55 5 52 49 99 96 9 88 6 1 147 14 19 6 297 289 10 10 10 14 1 1 22 21 19 46 44 42 41 9 84 76 7 71 12 1 1 6 1 274 2 251 241 22 10 10 10 10 00 1 12 12 17 17 16 16 8 7 6 5 4 68 66 64 62 8 4 1 98 95 224 217 2 4 199 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa *Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. Notes: (1) All ttable entries are rounded to significant digits. (2) means a flow of less than cfh ft /h (0.08 L/s). 198 UNIFORM PLUMBING CODE

TABLE 12-14 1216.2(9) SEMI-RIGID COPPER TUBING [NFPA 54: TABLE 6.2(hj)] NOMIL: K & L: 1 4 ACR: INTENDED USE: TUBE SIZING BETWEEN HOUSE LINE REGULATOR AND THE APPLIANCE. 1 1 5 TUBE SIZE (inch) 5 4 GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 1.0 in. w.c. SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 9 27 21 16 1 1 12 55 44 8 28 24 2 17 16 14 1 12 162 1 89 77 68 61 57 5 49 47 41 7 4 2 28 24 22 21 19 17 16 16 14 14 1 1 12 12 CAPACITY IN CUBIC FEET OF GAS PER HOUR 28 195 6 14 9 7 99 92 86 82 72 65 56 45 41 9 6 4 2 1 28 27 25 24 2 22 21 19 17 17 00 16 2 49 88 19 289 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa *Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. Notes: (1) All ttable entries are rounded to significant digits. (2) means a flow of less than cfh ft /h (0.08 L/s). 2 276 222 1 168 2 1 122 6 9 85 79 64 59 55 51 48 46 44 42 9 8 6 5 4 2 29 28 27 25 24 24 859 5 474 6 59 0 279 2 247 219 198 1 1 16 7 1 98 94 86 8 78 75 7 71 68 64 62 59 57 55 5 52 85 7 647 586 59 2 471 445 94 57 29 6 271 245 2 2 197 6 177 169 162 5 1 144 1 12 128 122 6 1 7 99 96 9 24 16 1 925 851 791 742 1 622 56 5 482 427 87 56 1 294 279 6 255 245 228 2 214 7 2 192 168 162 6 1 147 14 4 20 20 21 19 17 16 14 12 00 8 6 742 6 647 612 581 554 51 5 491 474 459 445 42 4 99 81 65 8 6 297 UNIFORM PLUMBING CODE 199

TABLE 12-1216.2() SEMI-RIGID COPPER TUBING [NFPA 54-12: TABLE 6.2(ik)] NOMIL: K & L: 1 4 ACR: 1 1 5 5 4 TUBE SIZE (inch) GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 17.0 in. w.c. SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 1 1 5 79 72 66 62 58 55 48 44 8 28 24 2 22 21 19 17 17 16 16 14 14 1 1 12 12 91 9 216 5 164 148 17 127 9 0 8 77 69 62 57 5 47 45 4 41 9 8 7 5 4 2 1 29 28 27 25 24 24 2 22 796 547 49 76 2 278 258 24 229 4 169 7 1 1 6 8 2 96 91 87 8 77 74 72 68 66 6 57 55 5 51 49 48 47 45 CAPACITY IN CUBIC FEET OF GAS PER HOUR 1 956 768 657 582 528 486 452 424 0 55 21 296 275 244 221 9 177 168 9 2 145 1 1 1 122 1 5 9 4 0 96 9 89 86 84 81 79 19 1 92 8 749 689 641 1 568 456 4 46 1 288 8 252 28 2 2 6 198 191 4 178 17 168 16 5 148 142 16 127 12 9 5 2 42 20 2 19 17 10 14 1 12 12 974 896 84 79 6 616 57 58 8 482 4 441 42 8 94 81 59 49 2 16 291 2 271 2 254 247 2 75 52 41 5 1 28 24 2 21 19 17 16 10 1 12 968 914 868 829 79 762 74 9 686 665 646 628 597 569 545 524 5 487 472 457 444 42 12 000 82 66 56 45 41 8 6 4 27 25 2 20 10 17 16 14 1 1 12 991 941 898 8 8 796 768 744 721 0 681 24 0 17 0 1 0 0 0 94 80 75 71 6 57 49 4 9 6 1 00 28 27 20 24 2 22 21 21 19 17 17 16 10 10 14 14 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa *Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. Note: All ttable entries are rounded to significant digits. 0 UNIFORM PLUMBING CODE

TABLE 12-16 1216.2() SEMI-RIGID COPPER TUBING [NFPA 54-12: TABLE 6.2(jl)] NOMIL: K & L: 1 4 ACR: 1 1 5 TUBE SIZE (inch) GAS: TURAL INLET PRESSURE: 2.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 0. For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa *Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. Note: All ttable entries are rounded to significant digits. 5 4 4 1 1 1 4 1 1 2 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 245 169 6 9 86 75 71 6 57 52 49 4 9 6 1 28 27 25 24 2 22 22 21 19 17 16 16 14 14 6 48 279 29 212 192 177 164 4 146 129 7 8 0 89 74 69 65 61 58 55 5 51 49 47 46 44 4 42 8 6 5 4 1 29 8 568 486 41 91 59 4 14 296 28 219 4 1 164 1 1 124 1 2 8 0 96 9 88 85 81 77 74 71 68 66 64 62 59 CAPACITY IN CUBIC FEET OF GAS PER HOUR 10 12 99 8 754 68 628 584 548 5 459 416 8 56 286 245 2 217 6 196 8 1 174 168 16 8 149 142 129 124 1 6 2 8 5 2 25 17 14 12 969 891 829 778 75 651 5 54 5 448 6 7 47 8 292 279 7 256 247 29 21 224 217 2 1 192 176 1 164 9 4 149 145 54 7 25 22 10 17 16 1 12 956 866 797 741 696 657 624 595 5 548 528 5 49 478 464 452 429 9 92 76 6 9 29 19 98 67 54 46 41 7 4 1 29 28 20 22 19 17 14 1 12 986 9 917 888 861 86 81 772 77 5 678 65 6 6 592 575 559 0 0 85 7 64 58 47 44 9 5 2 27 24 22 20 19 17 16 16 10 14 10 1 1 12 12 994 962 9 6 881 2 0 22 0 17 0 0 1 0 12 0 0 0 98 92 82 74 68 6 56 51 47 4 41 8 6 5 2 1 29 28 27 25 24 2 22 21 00 19 UNIFORM PLUMBING CODE 1

TABLE 12-17 1216.2(12) SEMI-RIGID COPPER TUBING [NFPA 54: TABLE 6.2(km)] GAS: TURAL INLET PRESSURE: 2.0 psi PRESSURE DROP: 1.5 psi SPECIFIC GRAVITY: 0. NOMIL: INTENDED USE: PIPE SIZING BETWEEN POINT OF DELIVERY AND THE HOUSE LINE REGULATOR. TOTAL LOAD SUPPLIED BY A SINGLE HOUSE LINE REGULATOR NOT EXCEEDING 1 CUBIC FEET PER HOUR. 2 K & L: 1 4 ACR: 1 1 5 TUBE SIZE (inch) 5 4 4 1 1 1 4 1 1 2 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 1 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 8 167 14 127 5 6 98 92 87 77 64 5 48 44 41 9 6 5 2 29 28 27 27 25 24 2 22 21 19 19 625 4 45 295 2 27 2 1 1 9 144 1 124 1 99 91 85 75 72 68 65 6 58 57 55 5 52 49 47 45 4 42 9 8 7 CAPACITY IN CUBIC FEET OF GAS PER HOUR 12 874 2 1 52 482 444 41 87 66 24 294 2 252 22 2 6 17 162 146 19 1 128 12 9 5 1 8 5 0 95 91 88 85 82 79 77 74 22 12 91 84 776 722 677 6 567 514 472 4 5 25 2 28 8 254 24 22 22 2 8 1 195 9 4 167 1 148 14 14 1 1 21 17 14 1 10 961 7 4 729 6 624 55 1 461 429 2 61 44 17 5 295 285 276 8 1 248 27 227 2 2 67 46 7 1 28 25 2 21 19 17 14 1 984 916 859 8 771 75 4 676 652 629 9 5 57 558 5 5 484 465 448 12 0 8 66 57 40 42 9 6 4 20 25 20 21 19 17 16 14 1 1 12 12 10 00 954 9 871 87 6 19 0 1 0 0 00 72 66 62 58 50 48 44 7 27 20 24 21 00 19 17 17 16 16 10 14 1 1 12 9 0 27 0 22 000 0 16 0 0 1 0 12 0 12 0 0 0 84 78 69 6 58 54 40 45 4 41 00 8 7 0 4 0 1 29 28 27 00 17 6 72 1 179 8 6 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa * 1 Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. 2 When Where this table is used to size the tubing upstream of a line pressure regulator, the pipe or tubing downstream of the line pressure regulator shall be sized using a pressure drop no greater than 1 in. w.c. inch water column (0.249 kpa) Note: All ttable entries are rounded to significant digits. 2 196 1 4 42 419 6 94 779 75 71 9 12 25 24 20 2 22 2 UNIFORM PLUMBING CODE

TABLE 12-1216.2(1) SEMI-RIGID COPPER TUBING [NFPA 54-12: TABLE 6.2(ln)] NOMIL: K & L: 1 4 ACR: 1 1 5 5 4 TUBE SIZE (inch) GAS: TURAL INLET PRESSURE: 5.0 psi PRESSURE DROP:.5 psi SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 5 51 282 241 214 194 178 166 6 147 1 1 9 1 81 75 69 65 62 58 56 5 51 49 48 46 45 4 42 8 7 5 4 2 1 29 724 582 498 441 0 68 42 21 9 24 224 8 5 167 4 14 14 127 121 5 1 6 2 98 95 92 87 8 79 76 7 68 65 6 62 21 14 898 81 748 696 65 617 547 495 456 424 76 1 291 27 258 245 24 224 2 7 0 194 8 2 177 169 161 4 148 14 1 129 122 CAPACITY IN CUBIC FEET OF GAS PER HOUR 7 25 17 14 1 12 955 866 796 741 657 595 547 9 478 451 429 9 92 76 62 9 28 19 295 281 9 259 249 241 2 2 219 21 5 6 29 25 22 17 16 1 12 92 844 777 722 678 6 8 5 556 54 514 497 481 466 452 4 4 99 82 67 5 41 2 0 62 5 47 4 9 6 4 2 20 24 22 19 10 16 14 1 12 10 00 967 9 89 852 816 784 755 729 5 684 664 646 0 14 000 0 96 85 77 71 66 62 58 52 47 4 5 2 29 27 24 2 22 21 19 19 17 17 16 16 14 14 1 1 12 12 2 0 22 0 17 0 0 1 0 12 0 0 0 98 92 82 74 68 6 56 51 47 4 41 8 6 5 2 1 29 28 27 25 24 2 22 21 00 19 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa *Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. Note: All ttable entries are rounded to significant digits. 67 0 46 0 7 000 1 0 28 0 25 0 2 0 21 0 0 19 0 17 0 0 14 0 1 0 0 0 98 91 85 76 7 67 64 62 58 57 55 52 48 46 44 4 41 9 8 UNIFORM PLUMBING CODE

TABLE 12-19 1216.2(14) CORRUGATED STAINLESS STEEL TUBING (CSST) [NFPA 54-12: TABLE 6.2(mo)] GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 0.5 in. w.c. SPECIFIC GRAVITY: 0. TUBE SIZE (EHD)* FLOW DESIGTION: 1 19 2 25 1 7 9 46 48 62 LENGTH (feet) CAPACITY IN CUBIC FEET OF GAS PER HOUR 5 25 0 1 0 2 46 2 25 22 19 1 12 9 7 6 5 6 44 5 1 27 25 21 19 17 16 14 1 9 8 5 82 66 58 52 47 41 7 4 1 29 28 16 14 95 77 67 55 47 42 8 6 2 2 21 19 225 161 12 6 4 96 8 75 68 6 57 54 42 8 4 2 192 7 17 122 2 97 87 74 69 65 62 48 44 9 471 7 21 6 8 162 144 121 7 1 78 71 6 0 5 7 17 2 6 57 67 95 148 2 275 492 For SI units: 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa *EHD = Equivalent Hydraulic Diameter, which is a measure of the relative hydraulic efficiency between different tubing sizes. The greater the value of EHD, the greater the gas capacity of the tubing. Notes: (1) Table includes losses for four degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, and/or fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.n, where L is additional length (ft) of tubing and n is the number of additional fittings, and/or bends, or both. (2) All ttable entries are rounded to significant digits. 546 8 9 2 2 8 168 141 12 1 91 82 74 895 69 524 456 9 74 25 292 7 248 22 219 8 171 148 1 7 746 6 56 482 442 86 47 295 277 2 249 5 179 161 17 12 888 79 72 625 559 9 471 4 4 9 277 247 14 96 856 742 665 8 56 527 498 472 87 6 1 6 20 21 16 1 00 9 887 84 691 0 58 41 29 20 10 14 1 98 9 762 661 591 5 4 UNIFORM PLUMBING CODE

TABLE 12-1216.2() CORRUGATED STAINLESS STEEL TUBING (CSST) [NFPA 54-12: TABLE 6.2(np)] INTENDED USE: INITIAL SUPPLY PRESSURE OF 8.0 INCH WATER COLUMN OR GREATER. TUBE SIZE (EHD)* GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP:.0 in. w.c. SPECIFIC GRAVITY: 0. FLOW DESIGTION: 1 19 2 25 1 7 46 48 62 LENGTH (feet) CAPACITY IN CUBIC FEET OF GAS PER HOUR 5 25 0 1 0 2 0 1 8 67 57 51 46 9 5 2 29 27 24 19 17 1 1 2 78 69 6 54 48 44 41 8 6 4 27 2 21 19 277 197 161 1 5 0 89 82 76 71 67 6 52 45 7 27 21 9 164 147 14 6 4 95 88 82 77 7 52 46 42 529 1 27 245 225 196 176 161 1 141 1 1 4 91 82 75 649 462 79 29 295 2 24 2 192 178 167 7 149 122 6 95 87 For SI units: 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa *EHD = Equivalent Hydraulic Diameter, which is a measure of the relative hydraulic efficiency between different tubing sizes. The greater the value of EHD, the greater the gas capacity of the tubing. Notes: (1) Table includes losses for four degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, and/or fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.n, where L is additional length (ft) of tubing and n is the number of additional fittings, and/or bends, or both. (2) All ttable entries are rounded to significant digits. 828 67 5 5 471 7 6 6 285 8 254 6 178 9 144 1 958 778 672 599 546 471 421 8 55 1 295 2 7 4 168 21 12 978 895 778 698 69 59 555 524 498 9 55 19 24 44 0 25 20 19 17 1 12 974 79 686 61 559 5 29 25 22 10 16 14 1 12 96 812 728 665 80 62 51 44 00 6 1 28 20 24 22 21 16 14 12 0 71 58 45 41 5 2 29 27 25 20 22 16 14 1 UNIFORM PLUMBING CODE 5

TABLE 12-21 1216.2(16) CORRUGATED STAINLESS STEEL TUBING (CSST) [NFPA 54-12: TABLE 6.2(oq)] GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 6.0 in. w.c. SPECIFIC GRAVITY: 0. INTENDED USE: INITIAL SUPPLY PRESSURE OF.0 INCH WATER COLUMN OR GREATER. TUBE SIZE (EHD)* FLOW DESIGTION: 1 19 2 25 1 7 46 48 62 LENGTH (feet) 5 25 0 1 0 2 17 1 96 8 74 67 57 51 46 42 9 7 5 28 24 21 229 1 1 2 99 78 69 6 58 54 51 48 9 4 89 277 227 197 176 161 1 5 6 0 94 89 7 6 57 461 27 7 21 7 9 164 147 14 124 6 9 4 85 7 66 77 529 46 42 1 27 245 225 9 196 5 176 145 1 4 CAPACITY IN CUBIC FEET OF GAS PER HOUR 9 649 52 462 414 79 29 295 2 2 24 221 2 172 149 14 16 9 828 79 67 5 5 471 45 7 8 6 19 1 958 855 778 672 599 546 5 471 444 421 00 21 17 1 12 978 895 8 778 75 698 62 44 6 1 27 25 20 19 17 16 14 1 5 1 29 25 22 19 10 10 16 12 0 80 72 62 56 51 44 00 6 1 00 28 14 2 0 82 71 58 45 41 8 5 2 0 19 27 52 4 122 6 2 9 79 96 16 For SI units: 1 foot = 4.8 mm 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa *EHD = Equivalent Hydraulic Diameter, which is a measure of the relative hydraulic efficiency between different tubing sizes. The greater the value of EHD, the greater the gas capacity of the tubing. Notes: (1) Table includes losses for four degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, and/or fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.n, where L is additional length (ft) of tubing and n is the number of additional fittings, and/or bends, or both. (2) All ttable entries are rounded to significant digits. 294 254 2 42 295 57 498 447 974 8 1 2 22 6 UNIFORM PLUMBING CODE

TABLE 12-22 1216.2(17) CORRUGATED STAINLESS STEEL TUBING (CSST) [NFPA 54-12: TABLE 6.2(pr)] GAS: TURAL INLET PRESSURE: 2.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 0. TUBE SIZE (EHD)* FLOW DESIGTION: 1 19 2 25 1 7 9 46 48 62 LENGTH (feet) CAPACITY IN CUBIC FEET OF GAS PER HOUR 25 75 0 1 0 2 0 0 0 2 166 1 129 5 9 89 79 64 55 49 44 8 4 5 2 0 172 4 124 1 7 87 75 67 61 52 46 587 74 42 297 6 2 2 9 5 121 1 96 86 0 444 5 51 14 257 249 222 2 7 141 129 1 0 10 9 6 567 5 4 7 66 2 217 9 1 1 876 1 696 624 512 496 445 64 17 284 2 225 2 25 16 14 12 922 892 795 646 557 497 45 48 29 10 14 1 9 748 645 576 525 45 4 45 28 16 16 14 12 941 862 749 552 7 258 2987 25 24 192 74 1685 9 1212 999 871 78 55 47 42 4 00 24 21 17 14 1 0 67 5 48 9 8 4 20 24 21 19 17 0 0 0 94 84 69 67 49 42 8 5 27 21 0 1 0 12 0 0 97 79 76 68 56 48 4 9 4 For SI units: 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa *EHD = Equivalent Hydraulic Diameter, which is a measure of the relative hydraulic efficiency between different tubing sizes. The greater the value of EHD, the greater the gas capacity of the tubing. Notes: (1) Table does not include effect of pressure drop across the line regulator. Where regulator loss exceeds 4 0.75 psi (5.17 kpa), do not use this table. Consult with regulator manufacturer for pressure drops and capacity factors. Pressure drops across a regulator may vary are capable of varying with flow rate. (2) CAUTION: Capacities shown in table may exceed are capable of exceeding the maximum capacity for a selected regulator. Consult with regulator or tubing manufacturer for guidance. () Table includes losses for four degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, and/or fittings, or both shall be increased by an equivalent length of tubing according to the following equation: L = 1.n, where L is additional length (ft) of tubing and n is the number of additional fittings, and/or bends, or both. (4) All ttable entries are rounded to significant digits. UNIFORM PLUMBING CODE 7

TABLE 12-2 1216.2() CORRUGATED STAINLESS STEEL TUBING (CSST) [NFPA 54-12: TABLE 6.2(qs)] TUBE SIZE (EHD)* GAS: TURAL INLET PRESSURE: 5.0 psi PRESSURE DROP:.5 psi SPECIFIC GRAVITY: 0. FLOW DESIGTION: 1 19 2 25 1 7 9 46 48 62 LENGTH (feet) 25 75 0 1 0 2 0 0 0 52 22 292 251 22 1 174 4 124 7 95 86 74 66 674 4 82 29 29 28 2 5 166 14 128 6 0 89 691 62 549 492 91 287 249 22 4 177 9 827 755 654 586 479 46 4 9 294 2 8 6 00 12 9 76 7 665 548 478 4 94 4 9 CAPACITY IN CUBIC FEET OF GAS PER HOUR 25 49 56 91 0 16 5 5 59 0 14 20 2 48 54 0 12 24 27 42 4727 89 21 24 7 4251 944 9 8 672 584 524 479 416 7 17 16 12 945 8 742 662 19 17 14 12 995 858 766 1 27 22 19 17 1 6 0 57 2521 2199 1977 1 81 1422 65 6 56 40 9 5 2 20 20 19 0 12 0 0 000 89 7 6 45 6 2 28 4 0 22 000 0 17 0 0 12 0 12 0 0 91 79 71 60 56 0 25 0 2 0 0 0 14 0 14 0 12 0 0 81 74 64 57 For SI units: 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa *EHD = Equivalent Hydraulic Diameter, which is a measure of the relative hydraulic efficiency between different tubing sizes. The greater the value of EHD, the greater the gas capacity of the tubing. Notes: (1) Table does not include effect of pressure drop across the line regulator. Where regulator loss exceeds 1 psi (6.89 kpa), do not use this table. Consult with regulator manufacturer for pressure drops and capacity factors. Pressure drops across regulator may vary are capable of varying with the flow rate. (2) CAUTION: Capacities shown in table may exceed are capable of exceeding the maximum capacity of selected regulator. Consult tubing manufacturer for guidance. () Table includes losses for four degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, and/or fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.n, where L is additional length (ft) of tubing and n is the number of additional fittings, and/or bends, or both. (4) All ttable entries are rounded to significant digits. 8 UNIFORM PLUMBING CODE

TABLE 12-24 1216.2(19) POLYETHYLENE PLASTIC PIPE [NFPA 54-12: TABLE 6.2(rt)] NOMIL OD: 1 PIPE SIZE (inch) GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 0. in. w.c. SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 4 DESIGTION: SDR 9. SDR.00 SDR.00 SDR.00 SDR.00 SDR.00 SDR SDR ACTUAL ID: 0.6 0.8 1.077 1.28 1.554 1.94 2.864.682 LENGTH (feet) 0 1 0 2 0 0 4 0 5 84 72 64 58 5 46 44 9 5 2 27 24 22 21 19 5 2 169 144 128 6 7 99 9 88 78 71 65 54 48 45 42 9 7 551 79 4 2 21 9 192 179 168 9 141 127 7 9 97 88 81 75 66 CAPACITY IN CUBIC FEET OF GAS PER HOUR 955 656 527 451 0 62 291 275 24 221 9 167 2 19 1 122 5 14 991 796 681 4 547 468 49 4 68 6 285 25 229 2 196 4 174 25 17 14 12 98 4 841 789 745 661 598 551 512 454 4 78 52 12 71 49 9 00 27 20 2 21 16 14 12 974 914 86 1 0 95 76 65 50 52 48 40 42 9 5 0 29 27 24 20 17 16 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa Note: All ttable entries are rounded to significant digits. UNIFORM PLUMBING CODE 9

TABLE 12-25 1216.2() POLYETHYLENE PLASTIC PIPE [NFPA 54-12: TABLE 6.2(su)] NOMIL OD: 1 PIPE SIZE (inch) GAS: TURAL INLET PRESSURE: LESS THAN 2 psi PRESSURE DROP: 0.5 in. w.c. SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 4 DESIGTION: SDR 9. SDR.00 SDR.00 SDR.00 SDR.00 SDR.00 SDR SDR ACTUAL ID: 0.6 0.8 1.077 1.28 1.554 1.94 2.864.682 LENGTH (feet) 0 1 0 2 0 0 4 0 1 1 95 84 76 65 61 58 51 46 4 5 2 29 27 24 277 222 1 169 1 12 6 9 86 71 64 59 55 51 48 7 499 1 4 4 276 254 221 9 5 168 4 144 127 5 6 99 9 88 CAPACITY IN CUBIC FEET OF GAS PER HOUR 12 865 695 594 527 477 49 9 8 62 21 291 8 249 221 0 4 171 1 2 10 1 898 796 721 66 617 579 547 485 49 4 76 2 278 258 242 229 4 2 16 14 98 871 789 7 675 598 542 499 464 45 4 94 64 52 44 9 5 0 28 27 24 21 16 10 1 12 2 12 5 0 86 76 69 6 59 55 52 46 42 8 6 0 20 24 2 20 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa Note: All ttable entries are rounded to significant digits. 2 UNIFORM PLUMBING CODE

TABLE 12-1216.2(21) POLYETHYLENE PLASTIC PIPE [NFPA 54-12: TABLE 6.2(tv)] NOMIL OD: 1 PIPE SIZE (inch) GAS: TURAL INLET PRESSURE: 2.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 0. 4 1 1 1 4 1 1 2 4 DESIGTION: SDR 9. SDR.00 SDR.00 SDR.00 SDR.00 SDR.00 SDR SDR ACTUAL ID: 0.6 0.8 1.077 1.28 1.554 1.94 2.864.682 LENGTH (feet) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 12 878 778 5 649 566 55 474 429 95 68 295 272 25 27 224 21 194 7 1 174 168 16 8 4 146 19 14 128 124 9 5 2 9 6 7 25 17 4 12 949 8 791 76 652 591 544 6 475 448 4 6 89 74 48 6 17 8 29 279 7 257 247 29 21 224 2 212 67 46 7 1 28 25 2 21 19 17 14 1 981 91 856 9 768 7 2 674 649 627 7 588 572 556 528 4 482 46 446 41 417 4 9 82 CAPACITY IN CUBIC FEET OF GAS PER HOUR 0 79 64 54 48 44 7 5 29 24 10 14 10 1 12 12 9 96 9 87 86 77 747 72 1 6 662 17 0 12 0 96 7 66 61 50 5 44 7 4 27 25 2 22 21 19 17 10 16 10 14 1 1 12 12 00 1 0 21 0 17 0 14 0 1 0 12 000 000 0 96 72 67 62 55 46 42 0 6 4 0 1 29 28 27 24 2 22 21 20 19 10 10 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa Note: All ttable entries are rounded to significant digits. 87 0 000 48 0 41 0 6 0 0 0 28 0 0 25 0 22 0 0 0 17 0 0 1 0 12 0 0 0 0 99 95 91 87 84 81 78 76 74 72 68 65 62 58 56 54 52 51 49 169 000 6 000 9 0 79 0 0 64 000 58 0 54 0 51 0 48 0 4 000 9 000 5 0 0 29 0 0 24 0 22 0 21 0 0 19 0 0 17 0 16 0 16 0 0 0 14 0 14 0 14 000 1 0 12 0 12 0 0 0 0 0 0 90 UNIFORM PLUMBING CODE 2

TABLE 12-27 1216.2(22) POLYETHYLENE PLASTIC TUBING [NFPA 54-12: TABLE 6.2(uw)] GAS: TURAL NOMIL OD: 1 INLET PRESSURE: LESS THAN 2.0 psi PRESSURE DROP: 0. in. w.c. SPECIFIC GRAVITY: 0. PLASTIC TUBING SIZE (CTS)* (inch) DESIGTION: SDR 7.00 SDR.00 ACTUAL ID: 0.445 0.927 LENGTH (feet) 0 1 0 225 2 275 0 0 4 0 CAPACITY IN CUBIC FEET OF GAS PER HOUR 54 7 2 21 19 17 16 14 1 12 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa * CTS = Copper tube size. Notes: (1) All ttable entries are rounded to significant digits. (2) means a flow of less than cfh ft /h (0.08 L/s). 4 72 256 5 176 6 141 1 121 7 95 86 79 74 69 65 62 59 54 51 47 45 TABLE 12-28 1216.2(2) POLYETHYLENE PLASTIC TUBING [NFPA 54-12: TABLE 6.2(vx)] NOMIL OD: 1 GAS: TURAL INLET PRESSURE: LESS THAN 2.0 psi PRESSURE DROP: 0.5 in. w.c. SPECIFIC GRAVITY: 0. PLASTIC TUBING SIZE (CTS)* (inch) DESIGTION: SDR 7.00 SDR.00 ACTUAL ID: 0.445 0.927 LENGTH (feet) 0 1 0 225 2 275 0 0 4 0 CAPACITY IN CUBIC FEET OF GAS PER HOUR 72 49 9 4 27 25 2 22 21 17 14 1 12 4 4 7 271 22 5 6 171 9 149 141 4 97 91 86 82 78 72 67 6 59 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 1 cubic foot per hour = 0.00787 L/s, 1 pound-force per square inch = 6.894 kpa, 1 inch water column = 0.249 kpa * CTS = Copper tube size. Notes: (1) All ttable entries are rounded to significant digits. (2) means a flow of less than cfh ft /h (0.08 L/s). 212 UNIFORM PLUMBING CODE

TABLE 12-29 1216.2(24) SCHEDULE METALLIC PIPE [NFPA 54: TABLE 6.(a)] GAS: UNDILUTED PROPANE INLET PRESSURE:.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 1. INTENDED USE: PIPE SIZING BETWEEN FIRST STAGE (HIGH PRESSURE REGULATOR) AND SECOND STAGE (LOW PRESSURE REGULATOR). NOMIL INSIDE: 1 PIPE SIZE (inch) 4 1 1 1 4 1 1 2 2 1 4 ACTUAL: 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 22 1 12 956 848 768 6 657 582 528 486 452 424 0 6 47 4 21 0 291 28 275 1 249 29 229 221 21 6 0 194 69 47 8 2 29 24 22 21 00 17 16 14 1 12 10 945 886 87 795 759 7 698 672 649 628 9 592 575 546 521 499 4 462 446 42 419 7 1 0 00 72 61 54 49 45 42 9 7 27 25 22 19 17 16 10 14 1 1 12 12 982 9 8 8 81 789 766 CAPACITY IN THOUSANDS OF BTU PER HOUR 0 0 14 0 12 0 0 0 9 87 81 77 68 62 57 5 47 42 9 6 4 2 29 28 20 20 25 24 2 22 22 21 19 17 17 16 16 0 27 0 22 0 19 000 16 0 0 14 0 1 0 12 0 0 0 85 79 58 54 51 48 46 40 42 0 7 6 5 4 1 28 27 77 0 5 0 42 0 6 0 2 0 29 0 27 0 25 0 2 0 22 0 19 0 17 0 16 0 0 1 0 12 0 0 0 98 9 88 84 81 77 72 60 60 64 58 55 5 51 124 000 85 000 68 0 58 0 51 0 46 0 4 0 0 7 0 5 0 1 0 28 0 0 24 0 21 0 19 0 0 16 0 0 14 0 14 0 1 0 12 0 12 0 12 000 0 0 0 0 0 97 92 88 85 82 219 000 1 000 121 000 000 91 0 82 0 76 0 0 66 0 62 0 55 0 0 46 0 4 0 8 0 4 0 1 0 29 0 27 0 0 25 000 2 0 22 0 21 0 21 0 0 19 0 19 0 0 0 17 0 16 0 0 0 14 0 00 9 95 745 22 44 12 0 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 pound-force per square inch = 6.894 kpa Note: All ttable entries are rounded to significant digits. 25 20 24 2 49 48 46 45 79 76 74 72 14 000 1 0 1 0 12 0 446 000 6 000 246 000 2 000 7 000 169 000 6 000 145 000 16 000 128 000 4 000 000 94 0 88 0 78 0 0 65 0 0 56 0 5 0 51 000 48 0 46 0 44 0 4 0 41 0 0 9 0 7 0 6 0 5 000 0 2 000 0 29 0 28 0 27 0 0 0 25 0 UNIFORM PLUMBING CODE 21

TABLE 12-1216.2(25) SCHEDULE METALLIC PIPE [NFPA 54: TABLE 6.(b)] GAS: UNDILUTED PROPANE INLET PRESSURE:.0 psi PRESSURE DROP:.0 psi SPECIFIC GRAVITY: 1. INTENDED USE: PIPE SIZING BETWEEN FIRST STAGE (HIGH PRESSURE REGULATOR) AND SECOND STAGE (LOW PRESSURE REGULATOR). NOMIL INSIDE: 1 PIPE SIZE (inch) 4 1 1 1 4 1 1 2 2 1 4 ACTUAL: 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 58 2 27 24 22 19 17 16 10 1 12 95 8 0 751 9 67 642 6 591 569 5 52 516 1 487 46 442 42 6 91 78 66 55 44 5 12 0 84 67 58 51 46 00 7 5 1 28 24 21 19 10 16 14 14 1 12 12 968 92 884 849 8 7 765 741 7 0 2 0 0 12 0 000 97 87 75 66 59 5 49 45 6 1 29 27 25 24 2 22 21 20 19 19 17 16 10 14 14 10 1 1 CAPACITY IN THOUSANDS OF BTU PER HOUR 47 0 2 0 0 22 0 19 0 0 16 0 0 14 0 1 0 12 0 000 0 94 8 75 69 64 57 54 49 47 40 44 41 9 7 5 4 2 1 29 28 27 27 71 0 49 000 9 0 0 29 0 27 0 24 0 2 0 21 0 0 0 16 0 0 14 0 12 0 0 0 96 85 81 77 74 71 60 66 64 62 50 56 5 51 49 47 45 44 41 17 000 94 0 75 0 64 0 57 0 52 0 47 0 44 0 41 0 9 0 5 000 1 0 29 0 27 0 24 0 21 0 0 0 17 0 16 0 0 000 14 0 1 0 1 0 12 0 12 0 12 000 0 0 0 0 98 94 91 88 85 82 78 219 000 1 000 121 000 000 91 0 8 000 76 0 71 0 66 0 6 000 55 0 0 46 0 4 0 8 0 4 0 2 000 29 0 27 0 0 25 000 2 0 22 0 22 000 21 0 0 19 0 19 0 0 0 17 0 16 0 0 0 14 0 14 0 1 0 1 0 12 0 12 0 87 000 6 000 214 000 000 162 000 147 000 000 1 000 1 000 1 000 98 0 89 0 82 0 76 0 67 0 61 0 56 0 52 0 49 0 46 0 44 0 42 0 0 8 0 7 0 6 0 5 000 0 2 0 2 000 0 29 000 27 0 0 25 0 24 0 24 000 2 0 22 0 22 000 For SI units:1 inch = 25 mm 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 pound-force per square inch = 6.894 kpa Note: All ttable entries are rounded to significant digits. 789 000 54 000 46 000 7 000 000 299 000 275 000 256 000 2 000 227 000 1 000 2 000 167 0 6 0 0 0 5 0 7 0 0 0 95 0 0 86 0 82 0 79 0 76 0 7 0 71 0 69 0 67 0 65 0 62 0 59 0 56 0 54 0 52 0 0 49 000 47 0 46 0 44 0 214 UNIFORM PLUMBING CODE

TABLE 12-1 1216.2() SCHEDULE METALLIC PIPE [NFPA 54: TABLE 6.(c)] INLET PRESSURE: 2.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 1. INTENDED USE: PIPE SIZING BETWEEN 2 PSI SERVICE AND LINE PRESSURE REGULATOR PIPE SIZE (inch) GAS: UNDILUTED PROPANE NOMIL 1 4 1 1 1 4 1 1 2 2 1 4 ACTUAL ID: 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 14 12 94 869 8 7 682 6 569 529 469 425 91 64 41 22 6 292 2 9 259 2 242 25 228 222 2 1 192 5 178 172 166 161 7 55 8 2 21 19 10 16 14 12 981 889 817 7 714 674 6 6 585 562 541 52 6 4 476 46 4 4 2 86 72 59 48 7 27 0 72 58 49 44 00 6 4 2 24 22 16 14 1 12 12 10 985 95 924 897 87 829 791 757 727 1 677 655 65 617 CAPACITY IN THOUSANDS OF BTU PER HOUR 21 0 14 0 0 0 82 75 65 62 55 00 40 42 7 4 1 29 27 24 2 22 21 19 10 17 10 16 14 14 1 1 12 2 0 22 0 17 0 0 1 0 12 0 0 0 98 9 82 74 68 64 56 51 47 44 41 9 7 5 2 1 29 28 27 25 24 2 22 21 62 0 42 0 4 0 29 0 0 2 0 21 0 0 19 000 000 0 14 0 1 0 12 0 0 99 91 84 79 75 71 68 65 62 58 56 54 5 51 49 46 44 4 41 99 0 68 0 54 0 47 000 41 0 7 0 4 0 2 0 0 28 0 25 0 2 000 21 0 19 0 17 0 0 14 0 1 0 12 0 12 000 0 0 0 99 96 00 87 84 82 78 74 71 68 66 176 000 121 000 97 0 8 0 7 0 66 0 61 0 57 0 5 0 0 44 0 0 7 0 4 0 0 27 0 25 0 2 0 22 0 21 0 0 19 0 0 17 0 17 000 16 0 0 0 000 14 0 1 0 1 0 12 0 12 0 0 00 2 0 12 5 56 000 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 pound-force per square inch = 6.894 kpa Note: All ttable entries are rounded to significant digits. 19 10 8 7 6 6 61 00 58 0 0 0 0 59 000 247 000 198 000 1 000 1 000 16 000 000 6 000 9 000 000 91 0 82 0 76 0 71 000 62 0 57 000 52 0 48 0 45 0 4 0 41 0 9 0 7 0 6 000 4 0 0 2 0 1 0 0 29 0 28 0 0 25 0 24 0 2 0 2 000 22 0 21 0 21 000 0 UNIFORM PLUMBING CODE 2

TABLE 12-2 1216.2(27) SCHEDULE METALLIC PIPE [NFPA 54: TABLE 6.(d)] 00 7 69 142 212 9 652 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 inch water column = 0.249 kpa Note: All ttable entries are rounded to significant digits. GAS: UNDILUTED PROPANE INLET PRESSURE:.0 in. w.c. PRESSURE DROP: 0.5 in. w.c. SPECIFIC GRAVITY: 1. INTENDED USE: PIPE SIZING BETWEEN SINGLE OR SECOND STAGE (LOW PRESSURE REGULATOR) AND APPLIANCE PIPE SIZE (inch) NOMIL INSIDE: 1 4 1 1 1 4 1 1 2 2 1 4 ACTUAL ID: 0.622 0.824 1.049 1. 1.6 2.067 2.469.068 4.0 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 291 0 1 17 122 1 1 94 89 84 74 67 62 58 51 46 42 7 5 2 29 28 27 25 25 24 2 22 21 19 19 8 4 6 287 255 21 212 197 5 5 1 129 1 7 97 89 8 78 7 66 64 61 59 57 55 5 52 48 46 44 42 9 8 787 62 541 4 44 0 72 49 292 5 24 227 1 2 167 6 146 1 5 1 7 4 0 97 95 86 82 79 76 74 71 CAPACITY IN THOUSANDS OF BTU PER HOUR 2 16 985 892 821 76 716 677 0 54 0 465 412 7 44 0 28 9 257 246 227 2 21 6 0 195 5 176 169 162 6 1 146 5 24 19 16 14 1 12 899 814 749 697 6 5 5 479 449 424 85 68 54 41 29 19 9 0 292 277 4 25 24 24 2 219 67 46 7 2 28 25 2 20 19 17 14 1 991 922 865 817 776 741 9 681 656 64 61 595 578 562 54 9 487 468 451 46 422 0 74 59 51 45 7 5 2 1 27 20 21 10 17 14 1 12 978 948 921 895 8 8 777 746 719 694 672 19 0 10 0 00 72 66 62 58 50 48 44 7 27 20 24 21 00 19 17 17 16 16 10 14 1 1 12 12 9 000 0 21 0 0 16 0 14 0 1 0 12 0 0 0 99 82 77 68 61 50 49 40 44 42 9 7 6 5 4 2 29 20 25 20 24 2 216 UNIFORM PLUMBING CODE

TABLE 12-1216.2(28) SEMI-RIGID COPPER TUBING [NFPA 54-09: TABLE 6.(e)] GAS: UNDILUTED PROPANE INLET PRESSURE:.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 1. INTENDED USE: TUBE SIZING BETWEEN FIRST STAGE (HIGH PRESSURE) REGULATOR AND SECOND STAGE (LOW PRESSURE) REGULATOR. NOMIL: K & L: 1 4 ACR: 1 1 5 TUBE SIZE (inch) For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 pound-force per square inch = 6.894 kpa *Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. Note: All ttable entries are rounded to significant digits. 5 4 4 1 1 1 4 1 1 2 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 51 52 28 242 2 194 179 166 6 147 1 9 1 81 75 65 62 59 56 54 51 48 46 45 44 42 8 7 5 4 2 1 29 727 584 0 44 1 69 4 22 4 2 244 225 9 5 168 5 144 127 121 5 1 6 2 99 96 9 88 8 79 76 7 68 66 64 62 21 14 1 816 751 699 655 619 549 497 457 4 77 42 14 292 274 259 246 25 225 216 8 1 195 9 178 169 161 5 148 14 14 1 1 122 CAPACITY IN THOUSANDS OF BTU PER HOUR 7 25 17 14 1 12 959 869 799 744 659 597 549 5 4 45 4 4 9 78 64 51 296 282 2 2 2 241 24 227 2 214 5 6 29 25 22 17 16 1 12 95 847 779 725 6 64 6 582 558 56 516 498 482 468 454 442 4 0 8 68 55 4 1 21 12 4 0 78 62 5 47 4 9 0 4 2 29 24 22 00 16 14 1 12 10 00 9 944 896 855 819 787 758 72 8 687 667 648 0 14 0 0 96 85 77 71 66 62 50 52 47 4 0 2 00 27 24 2 22 21 19 19 10 17 10 16 14 14 1 1 12 12 2 0 22 0 17 0 0 1 0 12 0 0 0 98 9 82 74 68 56 51 47 40 41 0 0 5 2 1 29 28 27 25 24 2 22 21 19 67 0 46 0 7 0 1 0 28 0 25 0 2 0 21 0 0 19 0 17 0 0 14 0 1 0 0 0 98 91 85 81 77 7 67 65 62 59 57 55 48 46 44 4 41 9 8 UNIFORM PLUMBING CODE 217

TABLE 12-4 1216.2(29) SEMI-RIGID COPPER TUBING [NFPA 54-09: TABLE 6.(f)] NOMIL: GAS: UNDILUTED PROPANE INLET PRESSURE:.0 in. w.c. PRESSURE DROP: 0.5 in. w.c. SPECIFIC GRAVITY: 1. INTENDED USE: TUBE SIZING BETWEEN SINGLE OR SECOND STAGE (LOW PRESSURE REGULATOR) AND APPLIANCE. K & L: 1 4 ACR: 1 1 5 TUBE SIZE (inch) 00 19 27 57 2 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 inch water column = 0.249 kpa *Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. Note: (1) All ttable entries are rounded to significant digits. (2) means a flow of less than,000 Btu/hr. (2. kw) 5 4 4 1 1 1 4 1 1 2 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 45 1 25 21 19 17 16 14 1 9 64 51 44 9 5 2 28 27 24 21 16 14 1 12 8 129 4 89 79 71 66 61 57 54 48 44 7 28 24 2 22 21 19 17 17 16 16 14 14 1 1 12 12 CAPACITY IN THOUSANDS OF BTU PER HOUR 29 2 2 5 5 7 0 95 84 76 65 58 52 48 45 42 8 6 4 2 1 29 28 27 25 24 2 22 21 19 467 21 258 2 195 177 16 2 142 14 9 8 99 92 82 74 68 6 56 5 51 49 47 45 44 42 41 9 7 5 4 2 1 29 28 27 997 685 5 471 417 78 48 24 4 287 254 2 212 197 8 146 16 127 1 4 9 4 0 96 9 87 85 8 78 75 72 69 66 64 62 58 10 12 991 848 752 681 6 58 547 517 458 4 82 55 285 2 244 229 216 5 196 8 1 174 168 162 7 149 141 129 124 9 5 2 8 5 28 19 1 988 919 862 814 722 654 2 5 496 449 414 85 61 41 24 9 296 284 274 4 256 248 241 24 22 212 195 8 2 176 1 166 161 58 2 27 24 22 19 10 10 10 1 12 96 861 1 752 7 674 64 616 592 5 551 5 517 2 488 464 442 42 7 92 78 66 55 45 5 2 UNIFORM PLUMBING CODE

TABLE 12-5 1216.2() SEMI-RIGID COPPER TUBING [NFPA 54-09: TABLE 6.(g)] NOMIL: K & L: 1 4 ACR: INLET PRESSURE: 2.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 1. INTENDED USE: TUBE SIZING BETWEEN 2 PSIG SERVICE AND LINE PRESSURE REGULATOR 1 1 5 TUBE SIZE (inch) GAS: UNDILUTED PROPANE 00 2 48 99 172 244 522 9 14 For SI units:1 inch = 25 mm, 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 pound-force per square inch = 6.894 kpa *Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. Note: All ttable entries are rounded to significant digits. 5 4 4 1 1 1 4 1 1 2 7 1 1 1 OUTSIDE: 0.75 0.0 0.625 0.7 0.875 1. 1.75 1.625 2. INSIDE:* 0.5 0.2 0.527 0.652 0.745 0.995 1.245 1.481 1.959 LENGTH (feet.) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 41 284 228 195 17 7 144 14 1 9 5 95 88 82 72 66 56 5 47 45 4 41 9 7 6 5 4 2 1 28 27 25 24 852 585 4 2 56 2 297 276 259 245 217 197 1 168 149 124 6 9 97 9 89 86 82 77 75 72 71 67 64 61 59 57 55 5 51 17 956 8 725 657 5 562 528 498 442 0 68 4 4 275 25 25 221 9 198 9 1 174 168 162 7 2 147 14 16 1 124 1 5 1 8 4 1 CAPACITY IN THOUSANDS OF BTU PER HOUR 16 14 12 98 922 871 772 0 644 599 51 481 442 4 86 65 46 16 4 29 28 274 5 258 251 28 227 217 9 1 194 8 2 177 29 2 10 16 10 1 1 12 10 992 91 849 75 682 628 584 548 517 491 469 449 41 4 1 88 76 66 56 8 22 9 296 286 276 7 259 251 91 6 4 8 4 0 29 27 2 21 19 16 14 1 12 00 959 921 888 857 829 4 781 7 721 688 659 6 6 589 5 55 57 16 0 0 91 69 62 57 5 47 42 8 5 2 20 24 22 21 19 10 17 16 10 14 14 14 1 12 10 00 966 000 17 0 14 0 12 0 0 98 84 79 74 66 55 51 45 41 0 5 1 29 28 27 25 24 2 22 22 21 19 10 17 16 16 54 0 7 0 29 0 25 0 22 0 0 0 17 0 16 0 0 1 0 12 0 0 0 95 86 79 7 69 65 62 59 56 54 52 40 47 46 44 42 0 7 6 4 2 1 UNIFORM PLUMBING CODE 219

TABLE 12-6 1216.2(1) CORRUGATED STAINLESS STEEL TUBING (CSST) [NFPA 54-09: TABLE 6.(h)] GAS: UNDILUTED PROPANE INLET PRESSURE:.0 in. w.c. PRESSURE DROP: 0.5 in. w.c. SPECIFIC GRAVITY: 1. INTENDED USE: CSST SIZING BETWEEN SINGLE OR SECOND STAGE (LOW PRESSURE) REGULATOR AND APPLIANCE SHUTOFF VALVE TUBE SIZE (EHD)* FLOW DESIGTION: 1 19 2 25 1 7 9 46 48 62 LENGTH (feet) 5 25 0 1 0 2 0 72 9 4 28 2 19 17 14 9 8 8 99 69 55 49 42 9 25 2 22 14 12 1 129 4 91 82 74 64 58 5 49 45 44 41 1 28 25 2 2 1 121 6 94 87 74 66 57 52 47 6 55 254 8 164 1 1 7 99 94 85 66 5 CAPACITY IN THOUSANDS OF BTU PER HOUR 4 248 216 192 177 17 1 7 9 2 98 75 69 61 57 744 521 422 65 25 297 256 227 7 191 178 169 9 12 2 99 For SI units: 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 inch water column = 0.249 kpa *EHD = Equivalent Hydraulic Diameter, which is a measure of the relative hydraulic efficiency between different tubing sizes. The greater the value of EHD, the greater the gas capacity of the tubing. Notes: (1) Table includes losses for four degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, and/or fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.n, where L is additional length (ft) of tubing and n is the number of additional fittings, and/or bends, or both. (2) All ttable entries are rounded to significant digits. 86 5 4 425 79 44 297 5 241 222 8 197 6 14 129 7 7 14 971 775 661 58 528 449 97 59 7 286 2 217 16 147 168 79 972 847 762 698 6 548 2 466 48 414 9 24 28 254 24 28 19 16 10 12 988 884 5 745 696 656 621 6 48 57 2 2 10 16 14 1 961 8 8 787 746 6 51 476 44 57 41 29 20 17 14 10 1 948 8 777 65 46 7 2 29 2 10 17 16 14 12 94 854 2 UNIFORM PLUMBING CODE

TABLE 12-7 1216.2(2) CORRUGATED STAINLESS STEEL TUBING (CSST) [NFPA 54-09: TABLE 6.(i)] INLET PRESSURE: 2.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 1. INTENDED USE: CSST SIZING BETWEEN 2 PSI SERVICE AND LINE PRESSURE REGULATOR TUBE SIZE (EHD)* GAS: UNDILUTED PROPANE FLOW DESIGTION: 1 19 2 25 1 7 9 46 48 62 LENGTH (feet) 25 75 0 1 0 2 0 0 0 4 2 28 1 147 1 124 1 86 77 69 5 558 47 16 271 24 196 9 169 17 1 5 96 82 72 927 591 5 469 4 44 298 245 21 191 17 1 1 6 554 496 6 9 287 248 222 8 17 896 6 66 64 578 477 4 7 4 298 8 CAPACITY IN THOUSANDS OF BTU PER HOUR 21 1 12 10 986 9 768 575 1 448 4 55 19 25 2 17 14 14 12 8 785 716 616 5 47 29 2 16 16 14 9 829 716 68 71 45 41 6 2 25 2 19 16 14 1 7958 5147 4719 46 2 5 2961 62 2195 19 1722 78 176 127 0 95 87 75 67 54 47 8 29 27 2 20 16 0 0 97 76 62 54 44 8 4 1 27 24 29 0 0 17 0 14 0 1 0 000 0 95 78 67 55 48 4 4 0 21 0 19 0 17 0 0 12 0 12 0 0 88 77 60 54 48 For SI units: 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 pound-force per square inch = 6.894 kpa *EHD = Equivalent Hydraulic Diameter, which is a measure of the relative hydraulic efficiency between different tubing sizes. The greater the value of EHD, the greater the gas capacity of the tubing. Notes: (1) Table does not include effect of pressure drop across the line regulator. Where regulator loss exceeds 1 psi (6.89 kpa), do not use this table. Consult with regulator manufacturer for pressure drops and capacity factors. Pressure drops across a regulator may vary are capable of varying with flow rate. (2) CAUTION: Capacities shown in table may exceed are capable of exceeding the maximum capacity for a selected regulator. Consult with regulator or tubing manufacturer for guidance. () Table includes losses for four degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, and/or fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.n, where L is additional length (ft) of tubing and n is the number of additional fittings, and/or bends, or both. (4) All ttable entries are rounded to significant digits. UNIFORM PLUMBING CODE 221

TABLE 12-8 1216.2() CORRUGATED STAINLESS STEEL TUBING (CSST) [NFPA 54-09: TABLE 6.(j)] TUBE SIZE (EHD)* INLET PRESSURE: 5.0 psi PRESSURE DROP:.5 psi SPECIFIC GRAVITY: 1. GAS: UNDILUTED PROPANE FLOW DESIGTION: 1 19 2 25 1 7 9 46 48 62 LENGTH (feet) 25 75 0 1 0 2 0 0 0 8 9 461 96 52 284 275 24 196 169 1 16 7 4 664 5 46 76 6 24 2 2 2 8 1 17 999 867 777 67 6 55 45 9 52 22 279 251 1 9 757 71 656 55 464 4 79 28 294 1 16 14 12 866 755 679 622 542 488 CAPACITY IN THOUSANDS OF BTU PER HOUR 00 25 2 14 14 92 828 757 657 589 78 48 44 8 4 27 2 19 16 14 1 89 40 9 1 27 22 19 17 1 12 10 76 66 59 49 47 42 5 27 25 21 19 14 444 99 8564 7469 6717 559 572 48 98 474 124 2865 2498 2247 28 0 000 16 0 14 0 12 0 0 99 89 72 62 56 51 44 9 1 0 19 0 0 0 14 0 0 0 000 82 71 6 58 45 54 0 4 0 1 0 27 0 24 0 0 19 0 17 0 14 0 12 0 0 0 89 00 60 0 6 0 2 000 28 0 20 22 0 0 16 0 14 0 12 0 0 0 91 For SI units: 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 pound-force per square inch = 6.894 kpa *EHD = Equivalent Hydraulic Diameter, which is a measure of the relative hydraulic efficiency between different tubing sizes. The greater the value of EHD, the greater the gas capacity of the tubing. Notes: (1) Table does not include effect of pressure drop across the line regulator. Where regulator loss exceeds 1 psi (6.89 kpa), do not use this table. Consult with regulator manufacturer for pressure drops and capacity factors. Pressure drops across a regulator may vary are capable of varying with flow rate. (2) CAUTION: Capacities shown in table may exceed are capable of exceeding the maximum capacity for a selected regulator. Consult with regulator or tubing manufacturer for guidance. () Table includes losses for four degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, and/or fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.n, where L is additional length (ft) of tubing and n is the number of additional fittings, and/or bends, or both. (4) All ttable entries are rounded to significant digits. 222 UNIFORM PLUMBING CODE

TABLE 12-9 1216.2(4) POLYETHYLENE PLASTIC PIPE [NFPA 54-12: TABLE 6.(k)] GAS: UNDILUTED PROPANE INLET PRESSURE:.0 in. w.c. PRESSURE DROP: 0.5 in. w.c. SPECIFIC GRAVITY: 1. INTENDED USE: PE SIZING BETWEEN INTEGRAL 2-STAGE REGULATOR AT TANK OR 2ND STAGE (LOW PRESSURE REGULATOR) AND BUILDING NOMIL OD: 1 PIPE SIZE (inch) 4 1 1 1 4 1 1 2 4 DESIGTION: SDR 9. SDR.00 SDR.00 SDR.00 SDR.00 SDR.00 SDR SDR ACTUAL ID: 0.6 0.8 1.077 1.28 1.554 1.94 2.864.682 LENGTH (feet) 0 1 0 2 0 0 4 0 2 7 1 142 129 9 1 98 87 78 72 67 54 46 4 41 6 468 75 21 285 258 27 221 7 196 17 7 145 9 8 99 92 87 82 12 844 677 5 514 466 428 98 74 5 1 284 1 24 2 195 179 167 7 148 CAPACITY IN THOUSANDS OF BTU PER HOUR 21 14 00 8 7 742 6 648 612 542 491 452 4 7 8 289 271 256 2 22 17 1 12 978 924 819 742 68 65 56 5 469 46 9 87 57 9 1 27 24 21 17 16 14 1 12 916 84 784 76 695 For SI units: 1 inch = 25 mm, 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 inch water column = 0.249 kpa Note: All ttable entries are rounded to significant digits. 16 000 000 88 75 66 55 51 48 45 6 1 20 25 2 21 19 0 21 0 17 000 14 0 12 0 0 0 000 71 65 54 40 45 41 9 7 UNIFORM PLUMBING CODE 22

TABLE 12-1216.2(5) POLYETHYLENE PLASTIC PIPE [NFPA 54-12: TABLE 6.(l)] NOMIL OD: 1 INLET PRESSURE: 2.0 psi PRESSURE DROP: 1.0 psi SPECIFIC GRAVITY: 1. GAS: UNDILUTED PROPANE INTENDED USE: PE PIPE SIZING BETWEEN 2 PSI SERVICE REGULATOR AND LINE PRESSURE REGULATOR PIPE SIZE (inch) 4 1 1 1 4 1 1 2 4 DESIGTION: SDR 9. SDR.00 SDR.00 SDR.00 SDR.00 SDR.00 SDR SDR ACTUAL ID: 0.6 0.8 1.077 1.28 1.554 1.94 2.864.682 LENGTH (feet) 0 1 0 2 0 0 4 0 5 0 6 0 7 0 8 0 9 00 10 10 10 10 10 10 10 00 1 21 17 14 1 952 899 797 722 664 6 548 496 457 425 99 77 58 41 27 14 2 292 28 274 6 259 246 24 225 216 8 1 194 8 178 62 4 29 2 21 19 10 10 14 1 12 10 994 914 851 798 754 716 68 654 628 5 585 566 549 5 5 492 4 4 42 416 2 89 77 66 56 0 77 62 5 47 42 9 6 4 2 28 20 22 19 17 16 14 1 12 12 9 961 95 888 847 8 779 751 725 2 6 661 64 CAPACITY IN THOUSANDS OF BTU PER HOUR 19 0 1 0 0 92 81 74 68 6 59 56 49 45 41 8 4 1 28 20 2 22 21 19 17 17 16 16 14 14 1 12 12 29 0 0 16 0 14 000 12 0 0 0 95 00 75 68 62 58 51 46 4 7 5 2 29 28 27 25 25 24 2 22 21 19 10 17 17 16 6 0 29 0 25 0 22 0 0 0 17 0 16 0 0 1 0 12 0 0 0 84 77 72 67 6 57 55 5 51 49 40 46 45 40 41 9 8 6 5 4 0 0 1 147 000 1 000 81 0 69 0 61 0 55 0 51 0 47 0 44 0 42 0 7 0 0 1 0 29 000 25 0 2 0 21 0 12 000 0 17 0 16 0 16 000 0 14 0 14 0 1 0 1 0 12 0 12 0 12 0 0 000 0 0 97 94 91 88 85 8 For SI units: 1 inch = 25 mm, 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29 kw, 1 pound-force per square inch = 6.894 kpa Note: All ttable entries are rounded to significant digits. 284 000 195 000 7 000 14 0 9 000 8 000 99 0 92 0 86 0 81 0 72 0 65 0 0 56 0 49 0 4 410 6 0 4 0 2 0 1 000 29 0 28 0 27 0 0 25 0 24 0 24 0 2 0 22 0 21 0 0 19 0 0 0 17 0 17 0 16 0 16 0 224 UNIFORM PLUMBING CODE

TABLE 12-41 1216.2(6) POLYETHYLENE PLASTIC TUBING [NFPA 54-12: TABLE 6.(m)] GAS: UNDILUTED PROPANE INLET PRESSURE:.0 in. w.c. PRESSURE DROP: 0.5 in. w.c. SPECIFIC GRAVITY: 1. INTENDED USE: PE TUBE SIZING BETWEEN INTEGRAL 2-STAGE REGULATOR AT TANK OR SECOND STAGE (LOW PRESSURE REGULATOR) AND BUILDING. NOMIL OD: 1 PLASTIC TUBING SIZE (CTS) (inch) DESIGTION: SDR 7.00 SDR.00 ACTUAL ID: 0.445 0.927 LENGTH (feet) 0 1 0 225 2 275 0 0 4 0 CAPACITY IN THOUSANDS OF BTU PER HOUR 121 8 67 57 51 46 42 9 7 5 1 28 24 22 21 19 16 4 828 569 457 91 47 14 289 9 252 28 2 191 176 164 4 145 12 121 6 0 For SI units: 1 inch = 25 mm, 1 foot = 4.8 mm, 00 British thermal units per hour = 0.29kW, 1 inch water column = 0.249 kpa Note: All ttable entries are rounded to significant digits. UNIFORM PLUMBING CODE 225

2 UNIFORM PLUMBING CODE