Heads up:
There are no amended sections in this chapter.
| Adopting Agency | BSC | BSC-CG | SFM | HCD | DSA | OSHPD | BSCC | DPH | AGR | DWR | CEC | CA | SL | SLC | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| 1 | 2 | 1-AC | AC | SS | SS/CC | 1 | 1R | 2 | 3 | 4 | 5 | ||||||||||||
| Adopt Entire Chapter | X | X | X | X | X | X | X | ||||||||||||||||
| Adopt Entire Chapter as amended (amended sections listed below) | X | X | X | ||||||||||||||||||||
| Adopt only those sections that are listed below | |||||||||||||||||||||||
| Chapter/Section | |||||||||||||||||||||||
| 1211.6 | X | X | X | ||||||||||||||||||||
| 1211.7 | X | X | |||||||||||||||||||||
The Office of the State Fire Marshal's adoption of this chapter or individual sections is applicable to structures regulated by other state agencies pursuant to Section 1.11.0.
The regulations of this chapter shall
govern the installation of fuel gas piping in or in connection with a building, structure or within the property lines of premises up to 5 pounds-force per square inch (psi) (34 kPa) for natural gas and 10 psi (69 kPa) for undiluted propane, other
than service pipe. Fuel oil piping systems shall be installed
in accordance with NFPA 31.
Coverage of piping systems shall extend from the point of delivery to the appliance connections. For
other than undiluted liquefied petroleum gas (LP-Gas) systems, the point of delivery shall be 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 LP-Gas systems, the point of delivery shall be considered to
be the outlet of the final pressure regulator, exclusive of line
gas regulators where no meter is installed. Where a meter is installed, the point of delivery shall be the outlet of the meter.
[NFPA 54:1.1.1.1(A)]
Requirements for
piping systems shall include design, materials, components, fabrication, assembly, installation, testing, inspection, operation, and maintenance. [NFPA 54:1.1.1.1(C)]
This code shall not apply to the following items (reference standards for some of which appear in Chapter 17):
- Portable LP-Gas appliances and equipment of all types that are not connected to a fixed fuel piping system.
- Installation of appliances such as brooders, dehydrators, dryers, and irrigation equipment used for agricultural purposes.
- Raw material (feedstock) applications except for piping to special atmosphere generators.
- Oxygen-fuel gas cutting and welding systems.
- Industrial gas applications using such gases as acetylene and acetylenic compounds, hydrogen, ammonia, carbon monoxide, oxygen, and nitrogen.
- Petroleum refineries, pipeline compressor or pumping stations, loading terminals, compounding plants, refinery tank farms, and natural gas processing plants.
- 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.
- LP-Gas installations at utility gas plants.
- Liquefied natural gas (LNG) installations.
- Fuel gas piping in electric utility power plants.
- Proprietary items of equipment, apparatus, or instruments such as gas-generating sets, compressors, and calorimeters.
- LP-Gas equipment for vaporization, gas mixing, and gas manufacturing.
- LP-Gas piping for buildings under construction or renovations that is not to become part of the permanent building piping system—that is, temporary fixed piping for building heat.
- Installation of LP-Gas systems for railroad switch heating.
- Installation of LP-Gas and compressed natural gas (CNG) systems on vehicles.
- Gas piping, meters, gas-pressure regulators, and other appurtenances used by the serving gas supplier in distribution of gas, other than undiluted LP-Gas.
- Building design and construction, except as specified herein.
- Fuel gas systems on recreational vehicles manufactured in accordance with NFPA 1192.
- Fuel gas systems using hydrogen as a fuel.
- Construction of appliances. [NFPA 54:1.1.1.2]
Upon completion of the
installation, alteration, or repair of gas piping, and prior to the use thereof, the Authority Having Jurisdiction shall be notified that such gas piping is ready for inspection.
Excavations required for the installation of underground piping shall be kept open until the piping
has been inspected and approved. Where such piping is covered or concealed before such approval, it shall be exposed upon the direction of the Authority Having Jurisdiction.
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 be in accordance
with this code.
This inspection
shall be made after gas piping authorized by the permit has been installed and before such piping has been covered or concealed or 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.
This inspection shall be made after piping authorized by the permit has
been installed, and after portions, thereof that are to be covered or concealed are so concealed, and before fixture, appliance, or shutoff valve has been attached thereto. This inspection shall comply with Section 1213.1. Test gauges used in conducting tests shall be in accordance with Section 318.0.
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 preceding 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 to be assured that the work has been performed in accordance with the intent of this code.
Whereupon final piping inspection, the
installation is found to be in accordance with the provisions
of this code, a certificate of inspection shall be permitted to be
issued by the Authority Having Jurisdiction.
A copy of the certificate of such final
piping inspection shall be issued to the serving gas supplier supplying gas to the premises.
It shall be unlawful for 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 a premises where and when gas service is, at the time, not being rendered.
It shall be unlawful to turn on or connect gas in or on the premises unless outlets are securely connected to gas appliances or capped or plugged with screw joint fittings.
The Authority Having Jurisdiction or the serving gas supplier is hereby authorized to disconnect gas piping or appliance or both that shall be found not to be in accordance with the requirements of this code or that are found defective and in such condition as to endanger life or
property.
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.
It shall be unlawful to remove or disconnect 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 and gastight on a piping system that has been installed, altered, or repaired.
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 not to exceed that designated by the Authority Having Jurisdiction, provided that such gas piping system otherwise is in
accordance with the requirements of this code regarding material, sizing, and safety.
Where required by the Authority Having Jurisdiction, a piping sketch or plan
shall be prepared before proceeding with the installation. The 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]
When additional appliances are being connected to a gas piping system, the existing piping shall be checked to determine whether it has adequate capacity. If inadequate, the existing system shall be enlarged as required, or separate gas piping of adequate capacity shall be provided. [NFPA 54:5.1.2.1 — 5.1.2.2]
The location of the point of delivery shall be acceptable to
the serving gas supplier. [NFPA 54:5.2]
Where two or more meters, or two 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 54:5.3.1]
Where a supplementary gas for standby use is connected downstream from a meter or a service regulator where a meter is not provided, equipment 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 54:5.3.2.1 — 5.3.2.2]
Gas piping systems shall be of such size and so installed as to provide a supply 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 54:5.4.1]
The volumetric flow rate of gas to be provided shall be the sum of the maximum inputs of the appliances served. The volumetric flow rate of gas to be provided shall be adjusted for altitude where the installation is above 2000 feet (610 m). [NFPA 54:5.4.2.1 — 5.4.2.2]. Where the input rating
is not indicated, the gas supplier, appliance manufacturer, or a qualified agency shall be contacted, or the rating from Table 1208.4.1 shall be used for estimating the volumetric flow rate of gas to be supplied.
The total connected hourly load shall be used as the basis for piping sizing, assuming all the appliances are operating at full capacity simultaneously.
For SI units: 1000 British thermal units per hour = 0.293 kW
The total connected hourly load shall be used as the basis for piping sizing, assuming all the appliances are operating at full capacity simultaneously.
Exception: Sizing shall be permitted to be based upon established load diversity factors. [NFPA 54:5.4.2.3]
| APPLIANCE | INPUT (Btu/h approx.) |
|---|---|
| Space Heating Units | |
| Warm air furnace |
|
| Single family |
100 000 |
| Multifamily, per unit |
60 000 |
| Hydronic boiler |
|
| Single family |
100 000 |
| Multifamily, per unit | 60 000 |
| Space and Water Heating Units | |
| Hydronic boiler | |
| Single-family |
120 000 |
| Multifamily, per unit | 75 000 |
| Water Heating Appliances | |
| Water heater, automatic storage |
|
| 30 to 40 gallon tank | 35 000 |
| Water heater, automatic storage | |
| 50 gallon tank |
50 000 |
| Water heater, automatic instantaneous | |
| Capacity at 2 gallons per minute | 142 800 |
| Capacity at 4 gallons per minute |
285 000 |
| Capacity at 6 gallons per minute | 428 400 |
| Water heater, domestic, circulating or side-arm | 35 000 |
| Cooking Appliances | |
| Range, freestanding, domestic | 65 000 |
| Built-in oven or broiler unit, domestic | 25 000 |
| Built-in top unit, domestic | 40 000 |
| Other Appliances | |
| Refrigerator | 3000 |
| Clothes dryer, Type I (domestic) | 35 000 |
| Gas fireplace direct vent | 40 000 |
| Gas log | 80 000 |
| Barbecue | 40 000 |
| Gaslight | 2500 |
Gas piping shall be sized in
accordance with one of the following:
- Pipe sizing tables or sizing equations in this chapter.
- Other approved engineering methods acceptable to the Authority Having Jurisdiction.
- Sizing tables included in a listed piping system manufacturer's installation instructions. [NFPA 54:5.4.3]
The design pressure loss in any 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 is greater than or equal to the minimum pressure required by the appliance. [NFPA 54:5.4.4]
The maximum design operating pressure for piping systems located inside buildings shall not exceed 5 psi (34 kPa) unless one or more of the following conditions are met:
- The piping system is welded.
- 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:
- Industrial processing or heating
- Research
- Warehousing
- Boiler or mechanical rooms
- The piping is a temporary installation for buildings under construction.
- The piping serves appliances or equipment used for agricultural purposes.
- The piping system is an LP-Gas piping system with a design operating pressure greater than 20 psi (138 kPa) and complies with NFPA 58. [NFPA 54:5.5.1]
LP-Gas systems designed to operate below -5°F (-21°C) 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 a liquid. [NFPA 54:5.5.2]
Materials used for piping systems shall either
comply with the requirements of this chapter or be acceptable to the Authority Having Jurisdiction. [NFPA 54:5.6.1.1]
Material not covered by the standards specifications listed herein shall meet the following criteria:
- Be investigated and tested to determine that it is safe and suitable for the proposed service.
- Be recommended for that service by the manufacturer.
- Be acceptable to the Authority Having Jurisdiction. [NFPA 54:5.6.1.3]
Cast-iron pipe shall not be used. [NFPA 54:5.6.2.1]
Copper and copper alloy pipe shall not be used if the gas contains more than an average of 0.3 grains of hydrogen sulfide per 100 standard cubic feet (scf) of gas (0.7 mg/100 L).
Threaded copper, copper alloy, or aluminum alloy pipe shall not be used with gases corrosive to such material. [NFPA 54:5.6.2.3 — 5.6.2.4]
Threaded copper, copper alloy, or aluminum alloy pipe shall not be used with gases corrosive to such material. [NFPA 54:5.6.2.3 — 5.6.2.4]
Aluminum alloy pipe shall comply with ASTM B241 (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]
Seamless copper, aluminum alloy, or steel tubing shall not be used with gases corrosive to such material. [NFPA 54:5.6.3]
Steel tubing shall comply with ASTM A254. [NFPA 54:5.6.3.1]
Copper and copper alloy tubing shall not be used where the gas contains more than an average of 0.3 grains of hydrogen sulfide per 100 scf of gas (0. 7 mg/100 L). Copper tubing shall comply with standard Type K or L of ASTM B88 or ASTM B280. [NFPA 54:5.6.3.2]
Aluminum alloy tubing shall comply with ASTM B210 or
ASTM B241. 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 such liquids as water, detergent, or sewage. Aluminum alloy tubing shall not be used in exterior locations or underground. [NFPA 54:5.6.3.3]
Corrugated stainless steel tubing shall be listed in accordance with CSA LC-1. [NFPA 54:5.6.3.4]
Polyethylene plastic pipe, tubing, and fittings used to supply fuel gas shall conform to ASTM D2513. Pipe to be used shall be marked "gas" and "ASTM D2513." Polyvinyl chloride (PVC) and chlorinated polyvinyl chloride (CPVC) plastic pipe, tubing, and fittings shall not be used to supply fuel gas. [NFPA 54.5.6.4.1.1 — 5.6.4.1.3]
Anodeless risers shall comply with the following:
- 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.
- Service head adapters and field-assembled anodeless risers incorporating service head adapters shall be recommended by the manufacturer for the gas used and shall be design-certified to be in accordance with the requirements of Category I of ASTM D2513. The manufacturer shall provide the user qualified installation instructions.
- The use of plastic pipe, tubing, and fittings in undiluted LP-Gas piping systems shall be in accordance with NFPA 58. [NFPA 54:5.6.4.3(3)]
Gas pipe, 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]
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]
Field threading of metallic pipe shall be in accordance with Table 1208.6.10.2. [NFPA 54:5.6.7.3]
For SI units: 1 inch = 25.4 mm
| IRON PIPE SIZE (inches) | APPROXIMATE LENGTH OF THREADED PORTION (inches) | APPROXIMATE NUMBER OF THREADS TO BE CUT |
|---|---|---|
| 1/2 | 3/4 | 10 |
| 3/4 | 3/4 | 10 |
| 1 | 7/8 | 10 |
| 11/4 | 1 | 11 |
| 11/2 | 1 | 11 |
| 2 | 1 | 11 |
| 21/2 | 11/2 | 12 |
| 3 | 11/2 | 12 |
| 4 | 15/8 | 13 |
Thread joint compounds shall be resistant to the action of LP-Gas or to any other chemical constituents of the gases to be conducted through the piping. [NFPA 54:5.6.7.4]
The type of piping joint used shall be suitable for the pressure and 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 the weight of the pipe and its contents. [NFPA 54:5.6.8)
Pipe joints shall be threaded, flanged, brazed, welded, or press-connect fittings that comply with CSA LC-4. Where nonferrous pipe is brazed, the brazing materials shall have a melting point in excess of 1000°F (538°C). Brazing alloys shall not contain more than 0.05 percent phosphorus. [NFPA 54:5.6.8.1]
Tubing joints shall be made with approved gas tubing fittings, be brazed with a material having a melting point in excess of
1000°F (538°C), or made by press-connect fittings that comply with CSA LC-4. Brazing alloys shall not contain more than 0.05 percent phosphorus.
[NFPA 54:5.6.8.2]
Flared joints shall be used only in systems constructed from nonferrous pipe and tubing where experience or tests have demonstrated that the joint is approved for the conditions and where provisions are made in the design to prevent separation of the joints. [NFPA
54:5.6.8.3]
Metallic pipe fittings shall comply with the following:
- Threaded fittings in sizes larger than 4 inches (100 mm) shall not be used unless approved by the Authority Having Jurisdiction.
- Fittings used with steel or wrought-iron pipe shall be steel, copper alloy, malleable iron, or cast-iron.
- Fittings used with copper or copper alloy pipe shall be copper or copper alloy.
- Fittings used with aluminum alloy pipe shall be of aluminum alloy.
- Cast-iron fittings shall comply with the following:
- Flanges shall be permitted.
- Bushings shall not be used.
- Fittings shall not be used in systems containing flammable gas-air mixtures.
- Fittings in sizes 4 inches (100 mm) and larger shall not be used indoors unless approved by the Authority Having Jurisdiction.
- Fittings in sizes 6 inches (150 mm) and larger shall not be used unless approved by the Authority Having Jurisdiction.
- Aluminum alloy fitting threads shall not form the joint seal.
- Zinc-aluminum alloy fittings shall not be used in systems containing flammable gas-air mixtures.
- Special fittings such as couplings; proprietary-type joints; saddle tees; gland-type compression fittings; and flared, flareless, or compression-type tubing fittings shall be as follows:
- Used within the fitting manufacturer's pressure-temperature recommendations.
- Used within the service conditions anticipated with respect to vibration, fatigue, thermal expansion, or contraction.
- Installed or braced to prevent separation of the joint by gas pressure or external physical damage.
- Approved by the Authority Having Jurisdiction. [NFPA 54:5.6.8.4 (1-8)]
Plastic pipe, tubing, and fittings shall be installed in accordance with the manufacturer's installation instructions. Section 1208.6.12.1 through Section 1208.6.12.4 shall be observed where making such joints. [NFPA 54:5.6.9]
The joint shall be designed and installed so that the longitudinal pullout resistance of the joint will be at least equal to the tensile strength of the plastic piping material. [NFPA 54:5.6.9(1)]
Heat-fusion joints shall be made in accordance with qualified procedures that have been established and proven by test to produce gastight joints as strong as the pipe or
tubing being joined. Joints shall be made with the joining method recommended by the pipe manufacturer. Heat-fusion fittings shall be marked "ASTM D2513." [NFPA 54:5.6.9(2)]
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 and shall extend not less than the outside end of the compression fitting 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(3)]
Plastic piping joints and fittings for use
in LP-Gas piping systems shall be in accordance with NFPA 58. [NFPA 54:5.6.9(4)]
Flanges shall comply with Section 1208.6.13.1 through Section 1208.6.13.7.
Cast iron flanges shall be in accordance with ASME B16.1. [NFPA 54:5.6.10.1.1]
Steel flanges shall be in accordance with the following:
- ASME B16.5 or
- ASME B16.47. [NFPA 54:5.6.10.1.2]
Non-ferrous flanges shall be in accordance with ASME B16.24.
[NFPA 54:5.6.10.1.3]
Ductile iron flanges shall be in accordance with ASME B16.42. [NFPA 54:5.6.10.1.4]
Raised-face flanges shall not be joined to flat-faced cast iron, ductile iron or nonferrous material flanges.
[NFPA 54:5.6.10.2]
Standard facings shall be permitted for use under this code. Where 150 psi (1034 kPa) steel flanges are bolted to Class 125 cast-iron flanges, the raised face on the steel
flange shall be removed. [NFPA. 54:5.6.10.3]
Lapped flanges
shall be used only above ground or in exposed locations accessible for inspection. [NFPA 54:5.6.10.4]
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 54:5.6.11]
Acceptable materials shall include the following:
- Metal (plain or corrugated)
- Composition
- Aluminum o-rings
- Spiral-wound metal gaskets
- Rubber-faced phenolic
- Elastomeric [NFPA 54:5.6.11.1]
Metallic flange gaskets shall be in accordance with ASME B16.20. [NFPA 54:5.6.11.2.1]
Non-metallic flange gaskets shall be in accordance with ASME B16.21. [NFPA 54:5.6.11.2.2]
Full-face flange gaskets shall be used with all non-steel flanges. [NFPA 54:5.6.11.3]
When a flanged joint is separated, the gasket shall be replaced. [NFPA 54:5.6.11.2.4]
Gas meters shall be located in ventilated spaces readily accessible for examination, reading, replacement, or necessary maintenance. [NFPA 54:5.7.2.1]
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 where they will be subject to excessive corrosion or vibration.
[NFPA 54:5.7.2.2]
Gas meters shall not be located where they will be subjected to extreme temperatures or sudden extreme changes in temperature or in areas where they are subjected to temperatures beyond those recommended by the manufacturer. [NFPA 54:5.7.2.3]
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 furn footing or by other means providing equivalent support. [NFPA 54:5.7.3]
Gas piping at multiple meter installations shall be marked by a metal tag or other permanent means designating the building or the part of the building being supplied and attached by the installing agency. [NFPA 54:5.7.5]
The gas pressure regulator shall be accessible for servicing. [NFPA 54:5.8.3]
Pressure regulators shall be protected against physical damage. [NFPA 54:5.8.4]
Line pressure regulators shall comply with all of the following:
- An independent vent to the 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 more than one regulator is at a location, each regulator shall have a separate vent to the outdoors or, if approved by the Authority Having Jurisdiction, the vent lines shall be permitted to be manifolded in accordance with accepted engineering practices to minimize backpressure in the event of diaphragm failure. Materials for vent piping shall be in accordance with Section 1208.6 through Section 1208.6.12.3.
- The vent shall be designed to prevent the entry of water, insects, or other foreign materials that could cause a blockage.
- The regulator vent shall terminate at least 3 feet (914 mm) from a source of ignition.
- At locations where regulators might be 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
- A regulator shall not be vented to the appliance flue or exhaust system. [NFPA 54:5.8.5.1]
The discharge of vents shall be in accordance with the following requirements:
- The discharge stacks, vents, or outlet parts of all pressure-relieving and pressure-limiting devices shall be located so that gas is safely discharged to the outdoors. Discharge stacks or vents shall be designed to prevent the entry of water, insects, or other foreign material that could cause a blockage.
- The discharge stack or vent line shall be at least the same size as the outlet of the pressure-relieving device. [NFPA 54:5.9.8.1 — 5.9.8.2]
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]
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)
Where the serving gas supplier delivers gas at a pressure greater than 2 psi for piping systems serving appliances designed to operate at a gas pressure of 14 inches water column (3.5 kPa) or less,
overpressure protection devices shall be installed. Piping systems serving equipment designed to operate at inlet pressures greater than 14 inches water column (3.5 kPa) shall be equipped with overpressure protection devices as required by the appliance manufacturer's installation instructions. [NFPA 54:5.9.1]
Where piping systems serving appliances designed to operate with a gas supply pressure of 14 inches water column (3.5 kPa) or less are required to be equipped with overpressure protection by Section 1208.9, each overpressure protection device shall be adjusted to limit the gas pressure to each connected appliance to 2 psi (14 kPa) or less upon a failure of the line pressure regulator. [NFPA 54:5.9.2.1]
Where piping systems serving appliances designed to
operate with a gas supply pressure greater than 14 inches
water column (3.5 kPa) are required to be equipped with
overpressure protection by Section 1208.9, each over-pressure protection device shall be adjusted to limit the gas pressure to each connected appliance as required by
the appliance manufacturer's installation instructions.
[NFPA 54:5.9.2.2]
Each gas piping system for which an overpressure protection device is required by this section shall be designed and installed so that a failure of the primary pressure control device(s) is detectable. [NFPA 54:5.9.2.4]
If a pressure relief valve is used to meet the requirements of this section, it shall
have a flow capacity such that the pressure in the protected system is maintained at or below the limits specified in Section 1208.10 under the following conditions:
- The line pressure regulator for which the relief valve is providing overpressure protection has failed wide open.
- The gas pressure at the inlet of the line pressure regulator for which the relief valve is providing overpressure protection is not less than the regulator's normal operating inlet pressure. [NFPA 54:5.9.2.5]
Protective devices shall be installed as close to the equipment as practical where the design of the equipment connected is such that air, oxygen, or standby gases are capable of being forced into the gas supply system.
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 5 psi (34 kPa) or more. [NFPA 54:5.10.1.1 — 5.10.1.2]
Protective devices shall include, but not be limited to the following:
- Check valves.
- 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.
- Normally closed air-actuated positive shutoff pressure regulators. [NFPA 54:5.10.2]
A protective device
shall be installed between the meter and the appliance or
equipment if the operation of the appliance or equipment is
such that it could produce 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
54:5.11]
Piping systems shall be designed to prevent failure from thermal expansion or contraction. [NFPA 54:5.14.1]
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 54:5.14.2]
Where automatic excess flow valves are installed, they shall be listed to CSA Z21.93 and shall be sized and installed in accordance with the manufacturer's instructions. [NFPA 54:5.13]
Underground gas piping shall be installed with sufficient clearance from any other underground structure 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 clearance or shall be insulated from sources of heat to prevent the heat from impairing the serviceability of the pipe. [NFPA 54:7.1.1]
Underground piping systems shall be installed with a minimum of 12 inches (305 mm) of cover. The minimum cover shall be increased to 18 inches (457 mm) if external damage to the pipe or tubing from external forces is likely to result. Where a minimum of 12 inches (305 mm) of cover cannot be provided, the pipe shall be installed in conduit or bridged (shielded). [NFPA 54:7.1.2.1 (A)(B)]
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]
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 54:7.1.2.3]
Steel pipe and steel tubing installed underground shall be installed in accordance with Section 1210.1.3.1 through Section 1210.1.3.9.[NFPA54:7.1.3]
Zinc coating (galvanizing) shall not be deemed adequate protection for underground gas piping. [NFPA 54:7.1.3.1]
Underground piping shall comply with one or more of the following unless approved technical justification is provided to demonstrate that protection is unnecessary:
- The piping shall be made of a corrosion-resistant material that is suitable for the environment in which it will be installed.
- Pipe shall have a factory-applied, electrically insulating coating. Fittings and joints between sections of coated pipe shall be coated in accordance with the coating manufacturer's instructions.
- The piping shall have a cathodic protection system installed, and the system shall be maintained in accordance with Section 1210.1.3.3 or Section 1210.1.3.6. [NFPA 54:7.1.3.2]
Cathodic protection systems shall be monitored by testing, and the results shall be documented. The test results shall demonstrate one of the following:
- A pipe-to-soil voltage of -0.85 volts or more negative is produced, with reference to a saturated copper-copper sulfate half cell.
- A pipe-to-soil voltage of -0.78 volts or more negative is produced, with reference to a saturated KCl calomel half cell.
- A pipe-to-soil voltage of -0.80 volts or more negative is produced, with reference to a silver-silver chloride half cell.
- Compliance with a method described in Appendix D of Title 49 of the code of Federal Regulations, Part 192. [NFPA 54:7.1.3.3]
Sacrificial anodes shall be tested in accordance with the following:
- Upon installation of the cathodic protection system, except where prohibited by climatic conditions, in which case the testing shall be performed not later than 180 days after the installation of the system.
- 12 to 18 months after the initial test.
- Upon successful verification testing in accordance with Section 1210.1.3.4(1) and Section 1210.1.3.4(2), periodic follow-up testing shall be performed at intervals not to exceed 36 months. [NFPA54:7.1.3.4]
Systems failing a test shall be repaired not more than 180 days after the date of the failed testing. The testing schedule shall be restarted as required in Section 1210.1.3.4(1) and Section 1210.1.3.4(2), and the results shall comply with Section 1210.1.3.3. [NFPA
54:7.1.3.5]
Impressed current cathodic protection systems shall be inspected and tested in accordance with the following schedule:
- The impressed current rectifier voltage output shall be checked at intervals not exceeding two months.
- The pipe-to-soil voltage shall be tested at least annually. [NFPA 54:7.1.3.6]
Documentation of the results of the two most recent tests shall be retained. [NFPA 54:7.1.3.7]
Where dissimilar metals are joined underground, an insulating coupling or fitting shall be used. [NFPA 54:7.1.3.8]
Where the formation of hydrates or ice is known to occur, the piping shall be protected against freezing. [NFPA 54:7.1.4]
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 sleeve and between the sleeve and the wall shall be sealed to prevent entry of gas and water. [NFPA 54:7.1.5]
Where gas piping is installed underground beneath buildings, the piping shall be either of the following:
- Encased in an approved conduit designed to withstand the imposed loads and installed in accordance with Section 1210.1.6.1 or Section 1210.1.6.2.
- A piping or encasement system listed for installation beneath buildings. [NFPA 54:7.1.6]
The conduit shall extend into an 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 a gas leakage. Where the end sealing is of a type that retains the full pressure of the pipe, the conduit shall be designed for the same pressure as the pipe. The conduit shall extend at least 4 inches ( 102 mm) outside the building, be vented outdoors above finished ground level, and be installed to prevent the entrance of water and insects. [NFPA 54:7.1.6.1]
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]
Plastic piping shall be installed outdoors, underground only.
Exceptions:
- Plastic piping shall be permitted to terminate aboveground where an anodeless riser is used.
- Plastic piping shall be permitted to terminate with a wall head adapter aboveground in buildings, including basements, where the plastic piping is inserted in a piping material permitted for use in buildings. [NFPA 54:7.1.7.1]
Connections made between metallic and plastic piping shall be made with fittings conforming to one of the following:
- ASTM D2513, Category I transition fittings
- ASTM F1973
- ASTM F2509 [NFPA 54:7.1.7.2]
An electrically continuous corrosion-resistant tracer shall be buried with the plastic pipe to facilitate locating. The tracer shall be one of the following:
- A product specifically designed for that purpose.
- Insulated copper conductor not less than 14 AWG.
Where tracer wire is used, access shall be provided from aboveground, or one end of the tracer wire or tape shall be brought aboveground at a building wall or riser. [NFPA 54:7.1.7.3 — 7.1.7.3.2]
Piping installed aboveground shall be securely supported and located where it will be protected from physical damage. Where passing through an exterior wall, the piping shall also be protected from 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. [NFPA 54:7.2.1]
The installation of gas piping shall not cause structural stresses within building components to exceed allowable design limits. Approval shall be obtained before any beams or joists are cut or notched. [NFPA 54:7.2.2.1 — 7.2.2.2]
Piping for other than dry gas conditions shall be sloped not less than 1/4 inch in 15 feet (6.4 mm in 4.6 m) to prevent traps. [NFPA 54:7.2.3]
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 or equipment shutoff valves
required by this code shall be permitted to be
installed in accessible spaces containing vented
appliances.
Gas piping inside any building shall not be installed in or through a clothes chute, chimney or gas vent, dumbwaiter, elevator shaft, or air duct, other than combustion air ducts. [NFPA
54:7.2.4]
Exception: Ducts used to provide ventilation air in
accordance with Section 506.0 or to above-ceiling spaces
in accordance with Section 1210.2.2.1.
Piping shall be supported with metal pipe hooks, metal pipe
straps, metal bands, metal brackets, metal hangers, or
building structural components, approved for the size of
piping; of adequate strength and quality; and located at
intervals 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 the requirements of MSS SP-58. [NFPA
54:7.2.5.1]
Spacing of supports in gas piping installations shall not exceed the distance shown in Table 1210.2.4.1. Spacing of supports for
CSST shall be in accordance with the CSST manufacturer's instructions. [NFPA 54:7.2.5.2]
For SI units: 1 inch = 25 mm, 1 foot = 304.8 mm
| STEEL PIPE, NOMINAL SIZE OF PIPE (inches) | SPACING OF SUPPORTS (feet) | NOMINAL SIZE OF TUBING SMOOTH-WALL (inches) | SPACING OF SUPPORTS (feet) |
|---|---|---|---|
| 1/2 | 6 | 1/2 | 4 |
| 3/4 or 1 | 8 | 5/8 or 3/4 | 6 |
| 11/4 or larger (horizontal) | 10 | 7/8 or 1 (horizontal) | 8 |
| 11/4 or larger (vertical) | Every floor level | 1 or larger (vertical) | Every floor level |
Gas piping installed on the roof surfaces shall be elevated above the roof surface and shall be supported in accordance with Table 1210.2.4.1. [NFPA 54:7.2.5.4]
Gas piping in concealed locations shall be installed in accordance with this section. [NFPA 54:7.3.1]
Where gas piping is to be concealed, connections shall be of the following type:
- Pipe fittings such as elbows, tees, couplings, and right/left nipple/couplings.
- Joining tubing by brazing (see Section 1208.6.11.2).
- Fittings listed for use in concealed spaces or that have been demonstrated to sustain, without leakage, forces due to temperature expansion or contraction, vibration, or fatigue based on their geographic location, application, or operation.
- Where necessary to insert fittings in the gas pipe that has been installed in a concealed location, the pipe shall be reconnected by welding, flanges, or the use of a right/left nipple/coupling.
Concealed gas piping shall not be located in solid partitions. [NFPA 54:7.3.3]
This provision shall not apply to tubing that pierces walls, floors, or partitions. Tubing installed vertically and horizontally inside
hollow walls or partitions without protection along its entire concealed length shall meet the following requirements:
- A steel striker barrier not less than 0.0508 of an inch ( 1.3 mm) thick, or equivalent, is installed between the tubing and the finished wall and extends at least 4 inches ( 102 mm) beyond concealed penetrations of plates, firestops, wall studs, and similar construction features.
- The tubing is installed in single runs and is rigidly secured. [NFPA 54:7.3.4]
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 is exposed to excessive moisture or corrosive substances, the piping shall be protected in an approved manner.
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 of 11/2 inches (38 mm) of concrete and shall not be in physical contact with other metallic structures such as reinforcing rods or electrically neutral conductors. All piping, fittings, and risers shall be protected against corrosion in accordance with Section 1208.6.9. Piping shall not be embedded in concrete slabs containing quick-set additives or cinder aggregate. [NFPA 54:7.3.5.1 — 7.3.5.2]
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 of 11/2 inches (38 mm) of concrete and shall not be in physical contact with other metallic structures such as reinforcing rods or electrically neutral conductors. All piping, fittings, and risers shall be protected against corrosion in accordance with Section 1208.6.9. Piping shall not be embedded in concrete slabs containing quick-set additives or cinder aggregate. [NFPA 54:7.3.5.1 — 7.3.5.2]
Where gas piping exceeding 5 psi (34 kPa) is located within vertical chases in accordance with Section 1208.5(2), the requirements of Section 1210.4.1 through Section 1210.4.3 shall apply. [NFPA 54:7.4]
Where pressure reduction is required in branch connections for compliance with Section 1208.5, 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 1208.8.4 and Section 1208.9 through Section 1208.10.4. The regulator shall be accessible for service and repair, and vented in accordance with one of the following:
- 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 permitted to be vented either directly to the outdoors or to a point within the top 1 foot (305 mm) of the chase.
- Where the fuel gas is heavier than air, the regulator vent shall be vented only directly to the outdoors. [NFPA 54:7.4.1]
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]
A chase shall be ventilated to the outdoors and only at the top. The opening(s) shall have a minimum free area [in square inches (square meters)] equal to the product of one-half of the maximum pressure in the piping [in pounds per square inch (kilopascals)] times the largest nominal diameter of that piping [in inches (millimeters)], or the cross-sectional area of the chase, whichever is smaller. Where more than one
fuel gas piping system is present, the free area for each
system shall be calculated, and the largest area used.
[NFPA 54:7.4.3]
Changes in direction of gas pipe shall be made by the use of fittings, factory bends, or field bends. [NFPA 54:7.5]
Metallic pipe bends shall comply with the following:
- Bends shall be made with bending equipment and procedures intended for that purpose.
- 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.
- The pipe shall not be bent through an arc of more than 90 degrees (1.57 rad).
- The inside radius of a bend shall be not less than six times the outside diameter of the pipe. [NFPA 54:7.5.1]
Plastic pipe bends shall comply with the following:
- The pipe shall not be damaged, and the internal diameter of the pipe shall not be effectively reduced.
- Joints shall not be located in pipe bends.
- The radius of the inner curve of such bends shall not be less than 25 times the inside diameter of the pipe.
- Where the piping manufacturer specifies the use of special bending tools or procedures, such tools or procedures shall be used. [NFPA 54:7.5.2]
Factory-made welding elbows or transverse segments cut therefrom shall have an arc length measured along the crotch at least 1 inch (25.4 mm) for pipe sizes 2 inches (50 mm) and larger. [NFPA 54:7.5.3]
For other than dry gas conditions, a drip shall be provided at a point in the line of pipe where condensate 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 shuts off the flow of gas before it runs back into the meter. [NFPA 54:7.6.1]
All drips shall be installed only in such locations that they are 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]
The installation of sediment traps shall be in accordance with Section 1212.9. [NFPA 54:7.6.3]
Outlets shall be located and installed in accordance with the following requirements:
- The outlet fittings or piping shall be securely fastened in place.
- Outlets shall not be located behind doors.
- 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.
- The unthreaded portion of gas piping outlets shall extend not less than 1 inch (25.4 mm) through finished ceilings or indoor or outdoor walls.
- The unthreaded portion of gas piping outlets shall extend not less than 2 inches (51 mm) above the surface of floors or outdoor patios or slabs.
- The provisions of Section 1210.7(4) and Section 1210.7(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 54:7.7.1.1 — 7.7.1.6]
Each outlet, including a valve, shall be closed gastight with a threaded plug or cap immediately after installation and shall be left closed until the appliance or equipment is connected thereto. Where an appliance or equipment is disconnected from an outlet, and the outlet is not to be used again immediately, it shall be capped or plugged gastight.
Exceptions:
- Laboratory appliances installed in accordance with Section 1212.3.1 shall be permitted.
- The use of a listed quick-disconnect device with integral shutoff or listed gas convenience outlet shall be permitted. [NFPA 54:7.7.2.1]
Appliance shutoff valves installed in fireplaces shall be removed, and the piping capped gastight where the fireplace is used for solid-fuel burning. [NFPA 54:7.7.2.2]
Main gas shutoff valves controlling several gas piping
systems shall be readily accessible for operation and
installed 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 are readily identified. [NFPA 54:7.9.2.1]
In multiple-tenant buildings supplied through a master
meter, through one service regulator where a meter is not
provided, or where meters or service regulators are not
readily accessible from the appliance or 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]
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 54:7.9.2.3]
Each laboratory space containing two 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 all such gas outlets are supplied. The shutoff valve shall be accessible, located within the laboratory or adjacent to the laboratory's egress door, and identified. [NFPA 54:7.9.2.4]
No device shall be placed inside the gas piping or fittings that reduces the cross-sectional area or otherwise obstructs the free flow of gas, except where an allowance in the piping system design has been made for such a device and where approved by the Authority Having Jurisdiction. [NFPA 54:7.1O]
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 54:7.11]
Systems containing flammable gas-air mixtures shall be in accordance with Section 1210.12.1 through Section 1210.12.6.
A central premix system with a flammable mixture in the blower or compressor shall consist of the following components:
- Gas-mixing machine in the form of an automatic gas-air proportioning device combined with a downstream blower or compressor.
- Flammable mixture piping, minimum Schedule 40.
- Automatic firecheck(s).
- Safety blowout(s) or backfire preventers for systems utilizing flammable mixture lines above 2 1/2 inches (65 mm) nominal pipe size (NPS) or the equivalent. [NFPA 54:7.12.1]
The following components shall also be permitted to be utilized in any type of central premix system:
- Flowmeter(s)
- Flame arrester(s) [NFPA 54:7.12.2]
Gas-mixing machines shall have nonsparking blowers and shall be constructed so that a flashback does not rupture machine
casings. [NFPA 54:7.12.3]
A mixing blower system shall be limited to applications with minimum practical lengths of mixture piping, limited to a maximum mixture pressure of 10 inches water column (2.5 kPa) and limited to gases containing no more than 10 percent hydrogen. The blower shall be equipped with a gas-control valve at its air entrance arranged so that gas is admitted to the airstream, entering the blower in proper proportions for correct combustion by the type of burners employed, the said gas-control valve being of either the zero governor or mechanical ratio valve type that controls the gas and air
adjustment simultaneously. No valves or other obstructions shall be installed between the blower discharge and the burner or burners. [NFPA 54:7.12.4]
Installation of gas-mixing machines shall comply with the following:
- The gas-mixing machine shall be located in a well-ventilated area or in a detached building or cutoff room provided with room construction and explosion vents in accordance with sound engineering principles. Such rooms or below-grade installations shall have adequate positive ventilation.
- Where gas-mixing machines are installed in well-ventilated areas, the type of electrical equipment shall be in accordance with NFPA 70, for general service conditions unless other hazards in the area prevail. Where gas-mixing machines are installed in small detached buildings or cutoff rooms, the electrical equipment and wiring shall be installed in accordance with NFPA 70 for hazardous locations.
- Air intakes for gas-mixing machines using compressors or blowers shall be taken from outdoors whenever practical.
- Controls for gas-mixing machines shall include interlocks and a safety shutoff valve of the manual reset type in the gas supply connection to each machine arranged to automatically shut off the gas supply in the event of high or low gas pressure. Except for open-burner installations only, the controls shall be interlocked so that the blower or compressor stops operating following a gas supply failure. Where a system employs pressurized air, means shall be provided to shut off the gas supply in the event of air failure.
- Centrifugal gas-mixing machines in parallel shall be reviewed by the user and equipment manufacturer before installation, and means or plans for minimizing the effects of downstream pulsation and equipment overload shall be prepared and utilized as needed. [NFPA 54:7.12.5.1 — 7.12.5.5]
Automatic firechecks and safety blowouts or backfire preventers shall be provided in piping systems distributing flammable air-gas mixtures from gas-mixing machines to protect the piping and the machines in the event of flashback, in accordance with the following:
- Approved automatic firechecks shall be installed upstream as close as practical to the burner inlets following the firecheck manufacturer's instructions.
- A separate manually operated gas valve shall be provided at each automatic firecheck for shutting off the flow of the gas-air mixture through the firecheck after a flashback has occurred. The valve shall be located upstream as close as practical to the inlet of
the automatic firecheck.
Caution: These valves shall not be reopened after a flashback has occurred until the firecheck has cooled sufficiently to prevent re-ignition of the flammable mixture and has been reset properly. - A safety blowout or backfiring preventer shall be provided in the mixture line near the outlet of each gas-mixing machine where the size of the piping is larger than 21/2 inches (65 mm) NPS, or equivalent, to protect the mixing equipment in the event of an explosion passing through an automatic firecheck. The manufacturer's instructions shall be followed when installing these devices, particularly after a disc has burst. The discharge from the safety blowout or backfire preventer shall be located or shielded so that particles from the ruptured disc cannot be directed towards personnel. Wherever there are interconnected installations of gas-mixing machines with safety blowouts or backfire preventers; provision shall be made to keep the mixture from other machines from reaching any ruptured disc opening. Check valves shall not be used for this purpose.
- Large-capacity premix systems provided with explosion heads (rupture discs) to relieve excessive pressure in pipelines shall be located at and vented to a safe outdoor location. Provisions shall be provided for automatically shutting off the supply of the gas-air mixture in the event of a rupture. [NFPA 54:7.12.6]
Each aboveground 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 where it is connected to appliances that are connected to the appliance grounding conductor of the circuit supplying that appliance. [NFPA 54:7.13.1]
CSST gas piping systems, and gas piping systems containing one or more segments of CSST, shall be bonded to the electrical service grounding electrode system or, where provided, lightning protection grounding electrode system. [NFPA 54:7.13.2]
The bonding jumper shall not be smaller than 6 AWG copper wire or equivalent. [NFPA 54:7.13.2.2]
The length of the jumper between the connection to the gas piping system
and the grounding electrode system shall not exceed 75 feet (22 875 mm). Any additional electrodes shall be bonded to the electrical service grounding electrode system or, where provided, lightning protection grounding electrode system. [NFPA 54:7.13.2.3]
Bonding connections shall be in accordance with NFPA 70. [NFPA 54:7.13.2.4]
Devices used for the bonding connection shall be listed for the application in accordance with UL 467. [NFPA 54:7.13.2.5]
Gas piping shall not be used as a grounding conductor or electrode. [NFPA 54:7.13.3]
Where a lightning protection system is installed, the bonding of the gas piping shall be in accordance with NFPA 780. [NFPA 54:7.13.4]
Electrical circuits shall not utilize gas piping or components as conductors.
Exception: Low-voltage (50V 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. [NFPA 54:7.14]
All electrical connections
between the wiring and electrically operated control devices in a piping system shall conform to the requirements of California Electrical Code. [NFPA 54:7.15.1]
Any 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 54:7.15.2]
Earthquake-actuated gas shutoff valves designed to automatically
shut off the gas at the location of the valve in the event of a seismic disturbance and certified by the State Architect as conforming to California Code of Regulations, Title 24, Part 12, Chapter 12-16-1, shall be provided for buildings when such installation is required by local ordinance. Earthquake-actuated gas shutoff valves which have not been certified by the State Architect shall be prohibited in buildings open to the public under mandatory installation by local ordinance. Installation
of the valves shall be in accordance with local ordinance, and in the absence of such per the manufacturers installation instructions.
Appliances and equipment shall be connected to the building
piping in compliance with Section 1212.5 through Section
1212.8 by one of the following:
- Rigid metallic pipe and fittings.
- Semirigid metallic tubing and metallic fittings. Aluminum alloy tubing shall not be used in exterior locations.
- A listed connector in compliance with CSA Z21.24. The connector shall be used in accordance with the manufacturer's installation instructions and shall be in the same room as the appliance. Only one connector shall be used per appliance.
- A listed connector in compliance with CSA Z21.75. Only one connector shall be used per appliance.
- CSST where installed in accordance with the manufacturer's installation instructions.
- Listed nonmetallic gas hose connectors in accordance with Section 1212.3.
- Unlisted gas hose connectors for use in laboratories and educational facilities in accordance with Section 1212.4. [NFPA 54:9.6.1]
Connectors used with commercial cooking appliances that
are moved for cleaning and sanitation purposes shall be
installed in accordance with the connector manufacturer's installation instructions. Such connectors shall be listed in accordance with CSA Z21.69. [NFPA 54:9.6.1.3]
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 54:9.6.1.4]
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 Z21.24 as follows:
Listed gas hose connectors shall be installed in accordance
with the manufacturer's installation instructions and in accordance with Section 1212.3.1 and Section 1212.3.2. [NFPA 54:9.6.2]
Indoor gas hose connectors shall be used only to connect laboratory, shop, and ironing appliances requiring mobility during operation and installed in accordance with the following:
- An 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 6 feet (1829 mm).
- The connector shall not be concealed and shall not extend from one room to another or pass through wall partitions, ceilings, or floors. [NFPA 54:9.6.2(1)]
Where outdoor gas hose connectors are used to connect portable outdoor appliances, the connector shall be listed in accordance with CSA Z21.54 and installed in accordance with the following:
- 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. [NFPA 54:9.6.2(2)]
The connector length shall not exceed 15 feet
(4572 mm).
Injection (Bunsen) burners used in laboratories and educational facilities shall be permitted to be connected to the gas supply by an unlisted hose. [NFPA 54:9.6.3]
Where portable industrial 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 and safe for the conditions under which it can be used. [NFPA 54:9.6.4.1]
Where industrial 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 for the service required, and only the minimum number required shall be installed. [NFPA 54:9.6.4.2]
Where industrial appliances subject to vibration are connected to the building piping system by the use of all metal flexible connectors, the connectors shall be suitable for the service required. [NFPA 54:9.6.4.3]
Where flexible connections are used, they shall be of the minimum practical length and shall not extend from one room to another or pass through any walls, partitions, ceilings, or floors.
Flexible connections shall not be used in any 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 54:9.6.4.4]
Each appliance connected to a piping system shall have an accessible, approved manual shutoff valve with a nondisplaceable valve member or a listed gas convenience outlet. Appliance shutoff valves and convenience outlets shall serve a single appliance only. The shutoff valve shall be located within 6 feet (1829 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 the valve to permit removal of appliance controls. Shutoff valves serving decorative appliances shall
be permitted to be installed in fireplaces if listed for such use.[NFPA 54:9.6.5, 9.6.5.1(A)(B)]
Exceptions:
- Shutoff valves shall be permitted to be accessibly located inside or under an appliance where such appliance is removed without removal of the shutoff valve.
- Shutoff valves shall be permitted to be accessibly located inside wall heaters and wall furnaces listed for recessed installation where necessary maintenance is performed without removal of the shutoff valve.
Quick-disconnect
devices used to connect appliances to the building piping shall be listed to CSA Z21.41. Where installed indoors, an approved manual shutoff valve with a non-displaceable valve member shall be installed upstream of the quick-disconnect device. [NFPA 54:9.6.6.1 — 9.6.6.2]
Appliances shall be permitted to be connected to the building piping by means of a listed gas convenience outlet, in conjunction with a listed appliance connector, installed in accordance with the manufacturer's installation instructions.
Gas convenience outlets shall be listed in accordance with CSA Z21.90 and installed in accordance with the manufacturer's installation instructions. [NFPA 54:9.6.7)
Where a sediment trap is not incorporated as a part of the appliance, a sediment trap shall be installed downstream of the appliance shutoff valve as close to
the inlet of the appliance as practical, before the flex connector, where used 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 1212.9, or other device recognized as an effective sediment trap. Illuminating appliances, ranges, clothes dryers, decorative appliances for installation in vented fireplaces, gas fireplaces, and outdoor grills shall not be required to be so equipped. [NFPA 54:9.6.8)
For SI units: 1 inch= 25.4 mmFIGURE 1212.9
METHOD OF INSTALLING A TEE FITTING SEDIMENT TRAP
[NFPA 54: FIGURE 9.6.8]
For SI units: 1 inch= 25.4 mm
METHOD OF INSTALLING A TEE FITTING SEDIMENT TRAP
[NFPA 54: FIGURE 9.6.8]
Piping shall be installed in a manner not to interfere with inspection, maintenance, or servicing of the appliance. [NFPA 54:9.6.9]
Liquefied petroleum gas facilities shall be in accordance with NFPA 58.
Prior to acceptance and initial operation, all piping installations shall be visually inspected and pressure tested to determine that the materials, design, fabrication, and installation practices comply with the requirements of this code. [NFPA 54:8.1.1.1]
Inspection shall consist of visual examination during or after manufacture, fabrication, assembly, or pressure tests. [NFPA 54:8.1.1.2]
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 54:8.1.1.3]
Where new branches are installed to new appliances the newly installed branch(es) shall be required to be pressure tested. Connections between the new piping and the existing piping shall be tested with a noncorrosive leak-detecting fluid or
approved leak-detecting methods. [NFPA 54:8.1.1.4]
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 section of the piping system and test medium in an adjacent section, unless a double block and bleed valve system is installed. A valve shall not be subjected to the test pressure unless it can be determined that
the valve, including the valve closing mechanism, is designed to safely withstand the pressure. [NFPA 54:8.1.1.5]
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]
The test medium shall be air, nitrogen, carbon dioxide, or an inert gas. OXYGEN SHALL NEVER BE USED. [NFPA 54:8.1.2]
Test preparation shall comply with Section 1213.2.1 through Section 1213.2.6.
Expansion joints shall be provided with temporary restraints, where required, for the additional thrust load under test. [NFPA 54:8.1.3.2]
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 54:8.1.3.3]
Where the piping system is connected to appliances or equipment designed for operating pressures of less than the test pressure, such appliances or equipment shall be isolated from the piping system by disconnecting them and capping the outlet(s). [NFPA 54:8.1.3.4]
Where the piping system is connected to appliances or equipment designed for operating pressures equal to or greater than the test pressure, such appliances or equipment shall be isolated
from the piping system by closing the individual appliance or equipment shutoff valve(s). [NFPA 54:8.1.3.5]
All testing of piping systems shall be performed in a manner that protects the safety of employees and the public during the test. [NFPA 54:8.1.3.6]
This inspection shall include an air, CO2, or nitrogen pressure test, at which time the gas piping
shall stand a pressure of not less than 10 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 15 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 (3.5 kPa), the test pressure shall be not less than 60 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 30 minutes. For CSST carrying gas at pressures in excess of 14 inches water column (3.5 kPa) pressure, the test pressure shall be not less than 30 psi (207 kPa) for 30 minutes. These tests shall be made using air, CO2
, 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 318.0.
The piping system shall withstand the test pressure specified without showing any evidence of leakage or other defects. Any reduction of test pressures as indicated by pressure gauges shall be deemed to indicate the presence of a leak unless such reduction can be readily attributed to some other cause. [NFPA
54:8.1.5.1]
Where leakage or other defects are located, the affected portion of the piping system shall be repaired or replaced and retested. [NFPA 54:8.1.5.3]
Leak checks using fuel gas shall be permitted in piping systems that have been pressure-tested in accordance with Section 1213.0. [NFPA 54:8.2.1]
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 54:8.2.2]
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 54:8.2.3]
Appliances and equipment shall not be
placed in operation until after the piping system has been checked in accordance with Section 1213.5.2; connections to the appliance are checked for leakage and purged in accordance with Section 1213.6. [NFPA 54:8.2.4]
The purging of piping shall be in accordance with Section 1213.6.1 through Section 1213.6.3. [NFPA 54:8.3]
The purging of piping systems shall be in
accordance with the provisions of Section 1213.6.1.1
through Section 1213.6.1.5 where the piping system meets either of the following:
For SI units: 1 inch = 25 mm, 1 foot = 304.8 mm
* CSST EHD size of 62 is equivalent to nominal 2 inches (50 mm) pipe or tubing size.
- The design operating gas pressure is greater than 2 psig (14 kPa).
- The piping being purged contains one or more sections of pipe or tubing meeting the size and length criteria of Table 1213.6.1. [NFPA 54:8.3.1]
| NOMINAL PIPING SIZE (inches) | LENGTH OF PIPING (feet) |
|---|---|
| ≥ 21/2 3 | > 50 |
| ≥ 3 < 4 | > 30 |
| ≥ 4 < 6 | > 15 |
| ≥ 6 < 8 | > 10 |
| ≥ 8 | Any length |
* CSST EHD size of 62 is equivalent to nominal 2 inches (50 mm) pipe or tubing size.
Where existing gas piping is opened, the section that is opened
shall be isolated from the gas supply and the line
pressure vented in accordance with Section
1213.6.1.4. Where gas piping meeting the criteria of
Table 1213.6.1 is removed from service, the residual
fuel gas in the piping shall be displaced with an inert
gas. [NFPA54:8.3.1.1]
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 cutting, or welding is done.
Where gas piping containing air and meeting the criteria of Table 1213.6.1 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 1213.6.1.4. [NFPA 54:8.3.1.2]
The open end of a piping system being pressure vented or purged shall discharge directly to an outdoor location. Purging operations shall comply with the following requirements:
- The point of discharge shall be controlled with a shutoff valve.
- The point of discharge shall be located at least 10 feet (3048 mm) from sources of ignition, at least 10 feet (3048 mm) from building openings, and at least 25 feet (7620 mm) from mechanical air intake openings.
- During discharge, the open point of discharge shall be continuously attended and monitored with a combustible gas indicator that is in accordance with Section 1213.6.1.5.
- Purging operations introducing fuel gas shall be stopped where 90 percent fuel gas by volume is detected within the pipe.
- Persons not involved in the purging operations shall be evacuated from areas within 10 feet (3048 mm) of the point of discharge. [NFPA 54:8.3.1.3]
Combustible gas indicators shall be listed and calibrated
in accordance with the manufacturer's instructions. Combustible gas indicators shall numerically display a volume scale from 0 percent to 100 percent in 1 percent or smaller increments. [NFPA 54:8.3.1.4]
The purging of piping systems shall be in accordance with the provisions of Section 1213.6.2.1 where the piping system meets both of the following:
- The design operating pressure is 2 psig (14 kPa) or less.
- The piping being purged is constructed entirely from pipe or tubing not meeting the size and length criteria of Table 1213.6.1. [NFPA 54:8.3.2]
The piping system shall be purged in accordance with one or more of the following:
- The piping shall be purged with fuel gas and shall discharge to the outdoors.
- The piping shall be purged with fuel gas and shall discharge to the indoors or outdoors through an appliance burner not located in a combustion chamber. Such burner shall be provided with a continuous source of ignition.
- The piping shall be purged with fuel gas and shall discharge to the indoors or outdoors through a burner that has a continuous source of ignition, and that is designed for such purpose.
- The piping shall be purged with fuel gas that is discharged to the indoors or outdoors, and the point of discharge shall be monitored with a listed combustible gas detector in accordance with Section 1213.6.2.2. Purging shall be stopped where fuel gas is detected.
- The piping shall be purged by the gas supplier in accordance with written procedures. [NFPA 54:8.3.2.1]
After the piping system has been placed in operation, appliances and equipment shall be purged before being placed into operation. [NFPA 54:8.3.3]
The following regulations shall comply with this section and Section 1215.0, shall be the standard for the installation of gas piping. Natural gas regulations and tables are based on the use of a gas having a specific gravity of 0.60 and for undiluted liquefied petroleum gas, having a specific gravity of 1.50. Where gas of a different specific gravity is to be delivered, the specific gravity conversion factors provided by the serving gas supplier shall be used in sizing piping systems from the pipe sizing tables in this chapter.
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.
Where the gas appliances to be installed have not been specified, Table 1208.4.1 shall be permitted to be used as a reference to estimate requirements of typical appliances.
To obtain the cubic feet per hour (m3/h) of gas required, divide the input of the appliances by the average Btu (kW•h) heating value per cubic foot (m3) of the gas. The average Btu (kW•h) per cubic foot (m3) of the gas in the area of the installation shall be permitted to be obtained from the serving gas supplier.
To obtain the cubic feet per hour (m3/h) of gas required, divide the input of the appliances by the average Btu (kW•h) heating value per cubic foot (m3) of the gas. The average Btu (kW•h) per cubic foot (m3) of the gas in the area of the installation shall be permitted to be obtained from the serving gas supplier.
Where the pipe size is to be determined using any of the methods in Section 1215.1.1 through Section 1215.1.3, the diameter of each pipe segment shall be obtained from the pipe sizing tables in Section 1215.2
or the sizing equations in Section 1215.3. [NFPA 54:6.1]
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 (see calculation example in Figure 1215.1.1]. [NFPA 54:6.1.1]
FIGURE 1215.1.1
EXAMPLE ILLUSTRATING USE OF TABLE 1208.4.1 AND TABLE 1215.2(1)
Problem: Determine the required pipe size of each section and outlet of the piping system shown in Figure 1215.1.1. Gas to be
used has a specific gravity of 0.60 and 1100 British thermal units (Btu) per cubic foot (0.0114 kW•h/L), delivered at 8 inch water
column (1.9 kPa) pressure.
For SI units: 1 foot = 304.8 mm, 1 gallon = 3.785 L, 1000 British thermal units per hour = 0.293 kW, 1 cubic foot per hour = 0.0283 mm3/h
Solution:
EXAMPLE ILLUSTRATING USE OF TABLE 1208.4.1 AND TABLE 1215.2(1)
Solution:
- Maximum gas demand of Outlet A —
32 cubic feet per hour (0.91 m3/h) (from Table 1208.4.1).
Maximum gas demand of Outlet B —
3 cubic feet per hour (0.08 m3/h) (from Table 1208.4.1).
Maximum gas demand of Outlet C —
59 cubic feet per hour (l .67 m3/h) (from Table 1208.4.1).
Maximum gas demand of Outlet D —
136 cubic feet per hour (3.85 m3/h) [150 000 Btu/hour (44 kW) divided by 1100 Btu per cubic foot (0.0114 kW•h/L)]. - The length of pipe from the gas meter to the most remote outlet (Outlet A) is 60 feet ( 18 288 mm).
- Using the length in feet column row marked 60 feet (18 288 mm) in Table 1215.2(1):
- Outlet A, supplying 32 cubic feet per hour (0.91 m3/h), requires 1/2 of an inch (15 mm) pipe.
- Section 1, supplying Outlets A and B, or 35 cubic feet per hour (0.99 m3/h) requires 1/2 of an inch ( 15 mm) pipe.
- Section 2, supplying Outlets A, B, and C, or 94 cubic feet per hour (2.66 m3/h) requires 3/4 of an inch (20 mm) pipe.
- Section 3, supplying Outlets A, B, C, and D, or 230 cubic feet per hour (6.51 m3/h), requires 1 inch (25 mm) pipe.
- Using the column marked 60 feet (18 288 mm) in Table 1215.2(1) [no column for actual length of 55 feet (16 764 mm)]:
- Using the column marked 60 feet (18 288 mm) in Table 1215.2(1):
- Outlet D, supplying 136 cubic feet per hour (3.85 m3/h), requires 3/4 of an inch (20 mm) pipe.
Pipe shall be sized as follows:
- The 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.
- 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. [NFPA 54:6.1.2]
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 54:6.1.3]
Table 1215.2(1) through Table 1215.2(36) shall be used to size gas
piping in conjunction with one of the methods described in Section 1215.1.1 through Section 1215.1.3. [NFPA 54:6.2]
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm , 1 cubic foot per hour = 0.0283 m3 /h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column= 0.249 kPa
Notes:
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour = 0.0283 m3/h,
1 pound-force per square inch = 6.8947 kPa, 1 inch water column = 0.249 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283 m3
/h, 1 pound-force per square inch= 6.8947 kPa, 1 mm water column= 0.249 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour = 0.0283 m3
/h, 1 pound-force per square inch= 6.8947 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283 m3/h, 1 pound-force per square inch= 6.8947 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour = 0.0283 m3/h, 1 pound-force per square inch= 6.8947 kPa
* Table entries are rounded to 3 significant digits.
For SI units:1 inch= 25 mm, 1 foot = 304.8 mm, 1 cubic foot per hour= 0.0283 m3/h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column= 0.249 kPa
Notes:
For SI units:1 inch= 25 mm, 1 foot = 304.8 mm, 1 cubic foot per hour= 0.0283 m3/h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column= 0.249 kPa
Notes:
For SI units:1 inch= 25 mm, 1 foot = 304.8 mm, 1 cubic foot per hour= 0.0283 m3/h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column= 0.249 kPa
Notes:
For SI units:1 inch= 25 mm, 1 foot = 304.8 mm, 1 cubic foot per hour= 0.0283 m3/h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column= 0.249 kPa
Notes:
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283 m3
/h, 1 pound-force per square inch= 6.8947 kPa
Notes:
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283 m3
/h, 1 pound-force per square inch= 6.8947 kPa
Notes:
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283 m3
/h, 1 pound-force per square inch= 6.8947 kPa
Notes:
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283, m3
/h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column = 0.249 kPa
Notes:
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283 m3
/h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column = 0.249 kPa
Notes:
For SI units: 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283 m3
/h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column = 0.249 kPa
Notes:
For SI units: 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283 m3/h, 1 pound-force per square inch= 6.8947 kPa
Notes:
For SI units: 1 foot= 304.8 mm, 1 cubic foot per hour= 0.0283 m3/h, 1 pound-force per square inch= 6.8947 kPa
Notes:
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour = 0.0283 m3
/h, 1 pound-force per square inch = 6.8947 kPa, 1 inch water column= 0.249 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour = 0.0283 m3
/h, 1 pound-force per square inch = 6.8947 kPa, 1 inch water column= 0.249 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 cubic foot per hour = 0.0283 m3
/h, 1 pound-force per square inch = 6.8947 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch = 25 mm, 1 foot = 304.8 mm, 1 cubic foot per hour =
0.0283m3/h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column
=0.249 kPa
Notes:
For SI units: 1 inch = 25 mm, 1 foot = 304.8 mm, 1 cubic foot per hour =
0.0283m3/h, 1 pound-force per square inch= 6.8947 kPa, 1 inch water column
=0.249 kPa
Notes:
For SI units: 1 inch = 25 mm, 1 foot = 304.8 mm, 1000 British thermal units per hour = 0.293 kW, 1 pound-force per square inch= 6.8947 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1000 British thermal units per hour= 0.293 kW, 1 pound-force per square inch= 6.8947 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1000 British thermal units per hour= 0.293 kW, 1 pound-force per square inch= 6.8947 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch = 25 mm, 1 foot = 304.8 mm, 1000 British thermal units per hour = 0.293 kW, 1 inch water column= 0.249 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot = 304.8 mm, 1000 British thermal units per hour= 0.293 kW, 1 pound-force per square inch = 6.8947 kPa
For SI units: 1 inch = 25 mm, 1 foot= 304.8 mm, 1000 British thermal units per hour= 0.293 kW, I inch water column= 0.249 kPa
For SI units: 1 inch = 25 mm, 1 foot= 304.8 mm, 1000 British thermal units per hour= 0.293 kW, 1 pound-force per square inch= 6.8947 kPa
For SI units: 1 foot = 304.8 mm, 1000 British thermal units per hour = 0.293 kW, 1 inch water column= 0.249 kPa
For SI units: 1 foot= 304.8 mm, 1000 British thermal units per hour= 0.293 kW, 1 pound-force per square inch= 6.8947 kPa
For SI units: 1 foot= 304.8 mm, 1000 British thermal units per hour= 0.293 kW, 1 pound-force per square inch= 6.8947 kPa
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1 000 British thermal units per hour= 0.293 kW, 1 inch water column= 0.249 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, 1 foot= 304.8 mm, 1000 British thermal units per hour= 0.293 kW, 1 pound -force per square inch= 6.8947 kPa
* Table entries are rounded to 3 significant digits.
For SI units: 1 inch= 25 mm, I foot= 304.8 mm, 1 000 British thermal units per
hour= 0.293 kW, 1 inch water column - 0.249 kPa
| GAS: | NATURAL | |||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |||||||||||||
| PRESSURE DROP: | 0.5 in. w.c. |
|||||||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||||||
| PIPE SIZE (inch) | ||||||||||||||
| NOMINAL: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 | 5 | 6 | 8 | 10 | 12 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 | 5.047 | 6.065 | 7.981 | 10.020 | 11.938 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||||||
| 10 | 172 | 360 | 678 | 1390 | 2090 | 4020 | 6400 | 11 300 | 23 100 | 41 800 | 67 600 | 139 000 | 252 000 | 399 000 |
| 20 | 118 | 247 | 466 | 957 | 1430 | 2760 | 4400 | 7780 | 15 900 | 28 700 | 46 500 | 95 500 | 173 000 | 275 000 |
| 30 | 95 | 199 | 374 | 768 | 1150 | 2220 | 3530 | 6250 | 12 700 | 23 000 | 37 300 | 76 700 | 139 000 | 220 000 |
| 40 | 81 | 170 | 320 | 657 | 985 | 1900 | 3020 | 5350 | 10 900 | 19 700 | 31 900 | 65 600 | 119 000 | 189 000 |
| 50 | 72 | 151 | 284 | 583 | 873 | 1680 | 2680 | 4740 | 9660 | 17 500 | 28 300 | 58 200 | 106 000 | 167 000 |
| 60 | 65 | 137 | 257 | 528 | 791 | 1520 | 2430 | 4290 | 8760 | 15 800 | 25 600 | 52 700 | 95 700 | 152 000 |
| 70 | 60 | 126 | 237 | 486 | 728 | 1400 | 2230 | 3950 | 8050 | 14 600 | 23 600 | 48 500 | 88 100 | 139 000 |
| 80 | 56 | 117 | 220 | 452 | 677 | 1300 | 2080 | 3670 | 7490 | 13 600 | 22 000 | 45 100 | 81 900 | 130 000 |
| 90 | 52 | 110 | 207 | 424 | 635 | 1220 | 1950 | 3450 | 7030 | 12 700 | 20 600 | 42 300 | 76 900 | 122 000 |
| 100 | 50 | 104 | 195 | 400 | 600 | 1160 | 1840 | 3260 | 6640 | 12 000 | 19 500 | 40 000 | 72 600 | 115 000 |
| 125 | 44 | 92 | 173 | 355 | 532 | 1020 | 1630 | 2890 | 5890 | 10 600 | 17 200 | 35 400 | 64 300 | 102 000 |
| 150 | 40 | 83 | 157 | 322 | 482 | 928 | 1480 | 2610 | 5330 | 9650 | 15 600 | 32 100 | 58 300 | 92 300 |
| 175 | 37 | 77 | 144 | 296 | 443 | 854 | 1360 | 2410 | 4910 | 8880 | 14 400 | 29 500 | 53 600 | 84 900 |
| 200 |
34 | 71 | 134 | 275 | 412 | 794 | 1270 | 2240 | 4560 | 8260 | 13 400 | 27 500 | 49 900 | 79 000 |
| 250 | 30 | 63 | 119 | 244 | 366 | 704 | 1120 | 1980 | 4050 | 7320 | 11 900 | 24 300 | 44200 | 70 000 |
| 300 | 27 | 57 | 108 | 221 | 331 | 638 | 1020 | 1800 | 3670 | 6630 | 10 700 | 22 100 | 40 100 | 63 400 |
| 350 | 25 | 53 | 99 | 203 | 305 | 587 | 935 | 1650 | 3370 | 6100 | 9880 | 20 300 | 36 900 | 58 400 |
| 400 | 23 | 49 | 92 | 189 | 283 | 546 | 870 | 1540 | 3140 | 5680 | 9190 | 18 900 | 34 300 | 54 300 |
| 450 | 22 | 46 | 86 | 177 | 266 | 512 | 816 | 1440 | 2940 | 5330 | 8620 | 17 700 | 32 200 | 50 900 |
| 500 | 21 | 43 | 82 | 168 | 251 | 484 | 771 | 1360 | 2780 | 5030 | 8150 | 16 700 | 30 400 | 48 100 |
| 550 | 20 | 41 | 78 | 159 | 239 | 459 | 732 | 1290 | 2640 | 4780 | 7740 | 15 900 | 28 900 | 45 700 |
| 600 | 19 | 39 | 74 | 152 | 228 | 438 | 699 | 1240 | 2520 | 4560 | 7380 | 15 200 | 27 500 | 43 600 |
| 650 | 18 | 38 | 71 | 145 | 218 | 420 | 669 | 1180 | 2410 | 4360 | 7070 | 14 500 | 26 400 | 41 800 |
| 700 | 17 | 36 | 68 | 140 | 209 | 403 | 643 | 1140 | 2320 | 4190 | 6790 | 14 000 | 25 300 | 40 100 |
| 750 | 17 | 35 | 66 | 135 | 202 | 389 | 619 | 1090 | 2230 | 4040 | 6540 | 13 400 | 24400 | 38 600 |
| 800 | 16 | 34 | 63 | 130 | 195 | 375 | 598 | 1060 | 2160 | 3900 | 6320 | 13 000 | 23 600 | 37 300 |
| 850 | 16 | 33 | 61 | 126 | 189 | 363 | 579 | 1020 | 2090 | 3780 | 6110 | 12 600 | 22 800 | 36 100 |
| 900 | 15 | 32 | 59 | 122 | 183 | 352 | 561 | 992 | 2020 | 3660 | 5930 | 12 200 | 22 100 | 35 000 |
| 950 | 15 | 31 | 58 | 118 | 178 | 342 | 545 | 963 | 1960 | 3550 | 5760 | 11 800 | 21 500 | 34 000 |
| 1000 | 14 | 30 | 56 | 115 | 173 | 333 | 530 | 937 | 1910 | 3460 | 5600 | 11 500 | 20 900 | 33 100 |
| 1100 | 14 | 28 | 53 | 109 | 164 | 316 | 503 | 890 | 1810 | 3280 | 5320 | 10 900 | 19 800 | 31 400 |
| 1200 | 13 | 27 | 51 | 104 | 156 | 301 | 480 | 849 | 1730 | 3130 | 5070 | 10 400 | 18 900 | 30 000 |
| 1300 | 12 | 26 | 49 | 100 | 150 | 289 | 460 | 813 | 1660 | 3000 | 4860 | 9980 | 18 100 | 28 700 |
| 1400 |
12 | 25 | 47 | 96 | 144 | 277 | 442 | 781 | 1590 | 2880 | 4670 | 9590 | 17 400 | 27 600 |
| 1500 |
11 | 24 | 45 | 93 | 139 | 267 | 426 | 752 | 1530 | 2780 | 4500 | 9240 | 16 800 | 26 600 |
| 1600 |
11 | 23 | 44 | 89 | 134 | 258 | 411 | 727 | 1480 | 2680 | 4340 | 8920 | 16 200 | 25 600 |
| 1700 |
11 | 22 | 42 | 86 | 130 | 250 | 398 | 703 | 1430 | 2590 | 4200 | 8630 | 15 700 | 24 800 |
| 1800 |
10 | 22 | 41 | 84 | 126 | 242 | 386 | 682 | 1390 | 2520 | 4070 | 8370 | 15 200 | 24 100 |
| 1900 |
10 | 21 | 40 | 81 | 122 | 235 | 375 | 662 | 1350 | 2440 | 3960 | 8130 | 14 800 | 23 400 |
| 2000 | NA | 20 | 39 | 79 | 119 | 229 | 364 | 644 | 1310 | 2380 | 3850 | 7910 | 14 400 | 22 700 |
Notes:
- 1 Table entries are rounded to 3 significant digits.
- 2 NA means a flow of less than 10 ft3/h (0.283 m3/h).
| GAS: | NATURAL | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | ||||||||
| PRESSURE DROP: | 3.0 in. w.c. | ||||||||
| SPECIFIC GRAVITY: | 0.60 | ||||||||
| INTENDED USE: INITIAL SUPPLY PRESSURE OF 8.0 IN. W.C. OR GREATER | |||||||||
| PIPE SIZE (inch) | |||||||||
| NOMINAL: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | ||||||||
| 10 | 454 | 949 | 1790 | 3670 | 5500 | 10 600 | 16 900 | 29 800 | 60 800 |
| 20 | 312 | 652 | 1230 | 2520 | 3780 | 7280 | 11 600 | 20 500 | 41 800 |
| 30 | 250 | 524 | 986 | 2030 | 3030 | 5840 | 9310 | 16 500 | 33 600 |
| 40 | 214 | 448 | 844 | 1730 | 2600 | 5000 | 7970 | 14 100 | 28 700 |
| 50 | 190 | 397 | 748 | 1540 | 2300 | 4430 | 7060 | 12 500 | 25 500 |
| 60 | 172 | 360 | 678 | 1390 | 2090 | 4020 | 6400 | 11 300 | 23 100 |
| 70 | 158 | 331 | 624 | 1280 | 1920 | 3690 | 5890 | 10 400 | 21 200 |
| 80 | 147 | 308 | 580 | 1190 | 1790 | 3440 | 5480 | 9690 | 19 800 |
| 90 | 138 | 289 | 544 | 1120 | 1670 | 3230 | 5140 | 9090 | 18 500 |
| 100 | 131 | 273 | 514 | 1060 | 1580 | 3050 | 4860 | 8580 | 17 500 |
| 125 | 116 | 242 | 456 | 936 | 1400 | 2700 | 4300 | 7610 | 15 500 |
| 150 | 105 | 219 | 413 | 848 | 1270 | 2450 | 3900 | 6890 | 14 100 |
| 175 | 96 | 202 | 380 | 780 | 1170 | 2250 | 3590 | 6340 | 12 900 |
| 200 | 90 | 188 | 353 | 726 | 1090 | 2090 | 3340 | 5900 | 12 000 |
| 250 | 80 | 166 | 313 | 643 | 964 | 1860 | 2960 | 5230 | 10 700 |
| 300 | 72 | 151 | 284 | 583 | 873 | 1680 | 2680 | 4740 | 9660 |
| 350 | 66 | 139 | 261 | 536 | 803 | 1550 | 2470 | 4360 | 8890 |
| 400 | 62 | 129 | 243 | 499 | 747 | 1440 | 2290 | 4050 | 8270 |
| 450 | 58 | 121 | 228 | 468 | 701 | 1350 | 2150 | 3800 | 7760 |
| 500 | 55 | 114 | 215 | 442 | 662 | 1280 | 2030 | 3590 | 7330 |
| 550 | 52 | 109 | 204 | 420 | 629 | 1210 | 1930 | 3410 | 6960 |
| 600 | 50 | 104 | 195 | 400 | 600 | 1160 | 1840 | 3260 | 6640 |
| 650 | 47 | 99 | 187 | 384 | 575 | 1110 | 1760 | 3120 | 6360 |
| 700 | 46 | 95 | 179 | 368 | 552 | 1060 | 1690 | 3000 | 6110 |
| 750 | 44 | 92 | 173 | 355 | 532 | 1020 | 1630 | 2890 | 5890 |
| 800 | 42 | 89 | 167 | 343 | 514 | 989 | 1580 | 2790 | 5680 |
| 850 | 41 | 86 | 162 | 332 | 497 | 957 | 1530 | 2700 | 5500 |
| 900 | 40 | 83 | 157 | 322 | 482 | 928 | 1480 | 2610 | 5330 |
| 950 | 39 | 81 | 152 | 312 | 468 | 901 | 1440 | 2540 | 5180 |
| 1000 | 38 | 79 | 148 | 304 | 455 | 877 | 1400 | 2470 | 5040 |
| 1100 | 36 | 75 | 141 | 289 | 432 | 833 | 1330 | 2350 | 4780 |
| 1200 | 34 | 71 | 134 | 275 | 412 | 794 | 1270 | 2240 | 4560 |
| 1300 | 33 | 68 | 128 | 264 | 395 | 761 | 1210 | 2140 | 4370 |
| 1400 | 31 | 65 | 123 | 253 | 379 | 731 | 1160 | 2060 | 4200 |
| 1500 | 30 | 63 | 119 | 244 | 366 | 704 | 1120 | 1980 | 4050 |
| 1600 | 29 | 61 | 115 | 236 | 353 | 680 | 1080 | 1920 | 3910 |
| 1700 | 28 | 59 | 111 | 228 | 342 | 658 | 1050 | 1850 | 3780 |
| 1800 | 27 | 57 | 108 | 221 | 331 | 638 | 1020 | 1800 | 3670 |
| 1900 | 27 | 56 | 105 | 215 | 322 | 619 | 987 | 1750 | 3560 |
| 2000 | 26 | 54 | 102 | 209 | 313 | 602 | 960 | 1700 | 3460 |
* Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | ||||||||
| PRESSURE DROP: | 6.0 in. w.c. | ||||||||
| SPECIFIC GRAVITY: | 0.60 | ||||||||
| INTENDED USE: INITIAL SUPPLY PRESSURE OF 11.0 IN. W.C. OR GREATER | |||||||||
| PIPE SIZE (inch) | |||||||||
| NOMINAL: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | ||||||||
| 10 | 660 | 1380 | 2600 | 5340 | 8000 | 15 400 | 24 600 | 43 400 | 88 500 |
| 20 | 454 | 949 | 1790 | 3670 | 5500 | 10 600 | 16 900 | 29 800 | 60 800 |
| 30 | 364 | 762 | 1440 | 2950 | 4410 | 8500 | 13 600 | 24 000 | 48 900 |
| 40 | 312 | 652 | 1230 | 2520 | 3780 | 7280 | 11 600 | 20 500 | 41 800 |
| 50 | 276 | 578 | 1090 | 2240 | 3350 | 6450 | 10 300 | 18 200 | 37 100 |
| 60 | 250 | 524 | 986 | 2030 | 3030 | 5840 | 9310 | 16 500 | 33 600 |
| 70 | 230 | 482 | 907 | 1860 | 2790 | 5380 | 8570 | 15 100 | 30 900 |
| 80 | 214 | 448 | 844 | 1730 | 2600 | 5000 | 7970 | 14 100 | 28 700 |
| 90 | 201 | 420 | 792 | 1630 | 2440 | 4690 | 7480 | 13 200 | 27 000 |
| 100 | 190 | 397 | 748 | 1540 | 2300 | 4430 | 7060 | 12 500 | 25 500 |
| 125 | 168 | 352 | 663 | 1360 | 2040 | 3930 | 6260 | 11 100 | 22 600 |
| 150 | 153 | 319 | 601 | 1230 | 1850 | 3560 | 5670 | 10 000 | 20 500 |
| 175 | 140 | 293 | 553 | 1140 | 1700 | 3270 | 5220 | 9230 | 18 800 |
| 200 | 131 | 273 | 514 | 1056 | 1580 | 3050 | 4860 | 8580 | 17 500 |
| 250 | 116 | 242 | 456 | 936 | 1400 | 2700 | 4300 | 7610 | 15 500 |
| 300 | 105 | 219 | 413 | 848 | 1270 | 2450 | 3900 | 6890 | 14 100 |
| 350 | 96 | 202 | 380 | 780 | 1170 | 2250 | 3590 | 6340 | 12 900 |
| 400 | 90 | 188 | 353 | 726 | 1090 | 2090 | 3340 | 5900 | 12 000 |
| 450 | 84 | 176 | 332 | 681 | 1020 | 1960 | 3130 | 5540 | 11 300 |
| 500 | 80 | 166 | 313 | 643 | 964 | 1860 | 2960 | 5230 | 10 700 |
| 550 | 76 | 158 | 297 | 611 | 915 | 1760 | 2810 | 4970 | 10 100 |
| 600 | 72 | 151 | 284 | 583 | 873 | 1680 | 2680 | 4740 | 9660 |
| 650 | 69 | 144 | 272 | 558 | 836 | 1610 | 2570 | 4540 | 9250 |
| 700 | 66 | 139 | 261 | 536 | 803 | 1550 | 2470 | 4360 | 8890 |
| 750 | 64 | 134 | 252 | 516 | 774 | 1490 | 2380 | 4200 | 8560 |
| 800 | 62 | 129 | 243 | 499 | 747 | 1440 | 2290 | 4050 | 8270 |
| 850 | 60 | 125 | 235 | 483 | 723 | 1390 | 2220 | 3920 | 8000 |
| 900 | 58 | 121 | 228 | 468 | 701 | 1350 | 2150 | 3800 | 7760 |
| 950 | 56 | 118 | 221 | 454 | 681 | 1310 | 2090 | 3690 | 7540 |
| 1000 | 55 | 114 | 215 | 442 | 662 | 1280 | 2030 | 3590 | 7330 |
| 1100 | 52 | 109 | 204 | 420 | 629 | 1210 | 1930 | 3410 | 6960 |
| 1200 | 50 | 104 | 195 | 400 | 600 | 1160 | 1840 | 3260 | 6640 |
| 1300 | 47 | 99 | 187 | 384 | 575 | 1110 | 1760 | 3120 | 6360 |
| 1400 | 46 | 95 | 179 | 368 | 552 | 1060 | 1690 | 3000 | 6110 |
| 1500 | 44 | 92 | 173 | 355 | 532 | 1020 | 1630 | 2890 | 5890 |
| 1600 | 42 | 89 | 167 | 343 | 514 | 989 | 1580 | 2790 | 5680 |
| 1700 | 41 | 86 | 162 | 332 | 497 | 957 | 1530 | 2700 | 5500 |
| 1800 | 40 | 83 | 157 | 322 | 482 | 928 | 1480 | 2610 | 5330 |
| 1900 | 39 | 81 | 152 | 312 | 468 | 901 | 1440 | 2540 | 5180 |
| 2000 | 38 | 79 | 148 | 304 | 455 | 877 | 1400 | 2470 | 5040 |
* Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 2.0 psi | ||||||||
| PRESSURE DROP: | 1.0 psi | ||||||||
| SPECIFIC GRAVITY: | 0.60 | ||||||||
| PIPE SIZE (inch) | |||||||||
| NOMINAL: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | ||||||||
| 10 | 1510 | 3040 | 5560 | 11 400 | 17 100 | 32 900 | 52 500 | 92 800 | 189 000 |
| 20 | 1070 | 2150 | 3930 | 8070 | 12 100 | 23 300 | 37 100 | 65 600 | 134 000 |
| 30 | 869 | 1760 | 3210 | 6590 | 9880 | 19 000 | 30 300 | 53 600 | 109 000 |
| 40 | 753 | 1520 | 2780 | 5710 | 8550 | 16 500 | 26 300 | 46 400 | 94 700 |
| 50 | 673 | 1360 | 2490 | 5110 | 7650 | 14 700 | 23 500 | 41 500 | 84 700 |
| 60 | 615 | 1240 | 2270 | 4660 | 6980 | 13 500 | 21400 | 37 900 | 77 300 |
| 70 | 569 | 1150 | 2100 | 4320 | 6470 | 12 500 | 19 900 | 35 100 | 71 600 |
| 80 | 532 | 1080 | 1970 | 4040 | 6050 | 11 700 | 18 600 | 32 800 | 67 000 |
| 90 | 502 | 1010 | 1850 | 3810 | 5700 | 11 000 | 17 500 | 30 900 | 63 100 |
| 100 | 462 | 934 | 1710 | 3510 | 5260 | 10 100 | 16 100 | 28 500 | 58 200 |
| 125 | 414 | 836 | 1530 | 3140 | 4700 | 9060 | 14 400 | 25 500 | 52 100 |
| 150 | 372 | 751 | 1370 | 2820 | 4220 | 8130 | 13 000 | 22 900 | 46 700 |
| 175 | 344 | 695 | 1270 | 2601 | 3910 | 7530 | 12 000 | 21 200 | 43 300 |
| 200 | 318 | 642 | 1170 | 2410 | 3610 | 6960 | 11 100 | 19 600 | 40 000 |
| 250 | 279 | 583 | 1040 | 2140 | 3210 | 6180 | 9850 | 17 400 | 35 500 |
| 300 | 253 | 528 | 945 | 1940 | 2910 | 5600 | 8920 | 15 800 | 32 200 |
| 350 | 232 | 486 | 869 | 1790 | 2670 | 5150 | 8210 | 14 500 | 29 600 |
| 400 | 216 | 452 | 809 | 1660 | 2490 | 4790 | 7640 | 13 500 | 27 500 |
| 450 | 203 | 424 | 759 | 1560 | 2330 | 4500 | 7170 | 12 700 | 25 800 |
| 500 | 192 | 401 | 717 | 1470 | 2210 | 4250 | 6770 | 12 000 | 24 400 |
| 550 | 182 | 381 | 681 | 1400 | 2090 | 4030 | 6430 | 11 400 | 23 200 |
| 600 | 174 | 363 | 650 | 1330 | 2000 | 3850 | 6130 | 10 800 | 22 100 |
| 650 | 166 | 348 | 622 | 1280 | 1910 | 3680 | 5870 | 10 400 | 21 200 |
| 700 | 160 | 334 | 598 | 1230 | 1840 | 3540 | 5640 | 9970 | 20 300 |
| 750 | 154 | 322 | 576 | 1180 | 1770 | 3410 | 5440 | 9610 | 19 600 |
| 800 | 149 | 311 | 556 | 1140 | 1710 | 3290 | 5250 | 9280 | 18 900 |
| 850 | 144 | 301 | 538 | 1100 | 1650 | 3190 | 5080 | 8980 | 18 300 |
| 900 | 139 | 292 | 522 | 1070 | 1600 | 3090 | 4930 | 8710 | 17 800 |
| 950 | 135 | 283 | 507 | 1040 | 1560 | 3000 | 4780 | 8460 | 17 200 |
| 1000 | 132 | 275 | 493 | 1010 | 1520 | 2920 | 4650 | 8220 | 16 800 |
| 1100 | 125 | 262 | 468 | 960 | 1440 | 2770 | 4420 | 7810 | 15 900 |
| 1200 | 119 | 250 | 446 | 917 | 1370 | 2640 | 4220 | 7450 | 15 200 |
| 1300 | 114 | 239 | 427 | 878 | 1320 | 2530 | 4040 | 7140 | 14 600 |
| 1400 | 110 | 230 | 411 | 843 | 1260 | 2430 | 3880 | 6860 | 14 000 |
| 1500 | 106 | 221 | 396 | 812 | 1220 | 2340 | 3740 | 6600 | 13 500 |
| 1600 | 102 | 214 | 382 | 784 | 1180 | 2260 | 3610 | 6380 | 13 000 |
| 1700 | 99 | 207 | 370 | 759 | 1140 | 2190 | 3490 | 6170 | 12 600 |
| 1800 | 96 | 200 | 358 | 736 | 1100 | 2120 | 3390 | 5980 | 12 200 |
| 1900 | 93 | 195 | 348 | 715 | 1070 | 2060 | 3290 | 5810 | 11 900 |
| 2000 | 91 | 189 | 339 | 695 | 1040 | 2010 | 3200 | 5650 | 11 500 |
* Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 3.0 psi | ||||||||
| PRESSURE DROP: | 2.0 psi | ||||||||
| SPECIFIC GRAVITY: | 0.60 | ||||||||
| PIPE SIZE (inch) | |||||||||
| NOMINAL: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | ||||||||
| 10 | 2350 | 4920 | 9270 | 19 000 | 28 500 | 54 900 | 87 500 | 155 000 | 316 000 |
| 20 | 1620 | 3380 | 6370 | 13 100 | 19 600 | 37 700 | 60 100 | 106 000 | 217 000 |
| 30 | 1300 | 2720 | 5110 | 10 500 | 15 700 | 30 300 | 48 300 | 85 400 | 174 000 |
| 40 | 1110 | 2320 | 4380 | 8990 | 13 500 | 25 900 | 41 300 | 73 100 | 149 000 |
| 50 | 985 | 2060 | 3880 | 7970 | 11 900 | 23 000 | 36 600 | 64 800 | 132 000 |
| 60 | 892 | 1870 | 3520 | 7220 | 10 800 | 20 800 | 33 200 | 58 700 | 120 000 |
| 70 | 821 | 1720 | 3230 | 6640 | 9950 | 19 200 | 30 500 | 54 000 | 110 000 |
| 80 | 764 | 1600 | 3010 | 6180 | 9260 | 17 800 | 28 400 | 50 200 | 102 000 |
| 90 | 717 | 1500 | 2820 | 5800 | 8680 | 16 700 | 26 700 | 47 100 | 96 100 |
| 100 | 677 | 1420 | 2670 | 5470 | 8200 | 15 800 | 25 200 | 44 500 | 90 800 |
| 125 | 600 | 1250 | 2360 | 4850 | 7270 | 14 000 | 22 300 | 39 500 | 80 500 |
| 150 | 544 | 1140 | 2140 | 4400 | 6590 | 12 700 | 20 200 | 35 700 | 72 900 |
| 175 | 500 | 1050 | 1970 | 4040 | 6060 | 11 700 | 18 600 | 32 900 | 67 100 |
| 200 | 465 | 973 | 1830 | 3760 | 5640 | 10 900 | 17 300 | 30 600 | 62 400 |
| 250 | 412 | 862 | 1620 | 3330 | 5000 | 9620 | 15 300 | 27 100 | 55 300 |
| 300 | 374 | 781 | 1470 | 3020 | 4530 | 8720 | 13 900 | 24 600 | 50 100 |
| 350 | 344 | 719 | 1350 | 2780 | 4170 | 8020 | 12 800 | 22 600 | 46 100 |
| 400 | 320 | 669 | 1260 | 2590 | 3870 | 7460 | 11 900 | 21 000 | 42 900 |
| 450 | 300 | 627 | 1180 | 2430 | 3640 | 7000 | 11 200 | 19 700 | 40 200 |
| 500 | 283 | 593 | 1120 | 2290 | 3430 | 6610 | 10 500 | 18 600 | 38 000 |
| 550 | 269 | 563 | 1060 | 2180 | 3260 | 6280 | 10 000 | 17 700 | 36 100 |
| 600 | 257 | 537 | 1010 | 2080 | 3110 | 5990 | 9550 | 16 900 | 34 400 |
| 650 | 246 | 514 | 969 | 1990 | 2980 | 5740 | 9150 | 16 200 | 33 000 |
| 700 | 236 | 494 | 931 | 1910 | 2860 | 5510 | 8790 | 15 500 | 31 700 |
| 750 | 228 | 476 | 897 | 1840 | 2760 | 5310 | 8470 | 15 000 | 30 500 |
| 800 | 220 | 460 | 866 | 1780 | 2660 | 5130 | 8180 | 14 500 | 29 500 |
| 850 | 213 | 445 | 838 | 1720 | 2580 | 4960 | 7910 | 14 000 | 28 500 |
| 900 | 206 | 431 | 812 | 1670 | 2500 | 4810 | 7670 | 13 600 | 27 700 |
| 950 | 200 | 419 | 789 | 1620 | 2430 | 4670 | 7450 | 13 200 | 26 900 |
| 1000 | 195 | 407 | 767 | 1580 | 2360 | 4550 | 7240 | 12 800 | 26 100 |
| 1100 | 185 | 387 | 729 | 1500 | 2240 | 4320 | 6890 | 12 200 | 24 800 |
| 1200 | 177 | 369 | 695 | 1430 | 2140 | 4120 | 6570 | 11 600 | 23 700 |
| 1300 | 169 | 353 | 666 | 1370 | 2050 | 3940 | 6290 | 11 100 | 22 700 |
| 1400 | 162 | 340 | 640 | 1310 | 1970 | 3790 | 6040 | 10 700 | 21 800 |
| 1500 | 156 | 327 | 616 | 1270 | 1900 | 3650 | 5820 | 10 300 | 21 000 |
| 1600 | 151 | 316 | 595 | 1220 | 1830 | 3530 | 5620 | 10 000 | 20 300 |
| 1700 | 146 | 306 | 576 | 1180 | 1770 | 3410 | 5440 | 9610 | 19 600 |
| 1800 | 142 | 296 | 558 | 1150 | 1720 | 3310 | 5270 | 9320 | 19 000 |
| 1900 | 138 | 288 | 542 | 1110 | 1670 | 3210 | 5120 | 9050 | 18 400 |
| 2000 | 134 | 280 | 527 | 1080 | 1620 | 3120 | 4980 | 8800 | 18 000 |
* Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 5.0 psi | ||||||||
| PRESSURE DROP: | 3.5 psi | ||||||||
| SPECIFIC GRAVITY: | 0.60 | ||||||||
| PIPE SIZE (inch) | |||||||||
| NOMINAL: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | ||||||||
| 10 | 3190 | 6430 | 11 800 | 24 200 | 36 200 | 69 700 | 111 000 | 196 000 | 401 000 |
| 20 | 2250 | 4550 | 8320 | 17 100 | 25 600 | 49 300 | 78 600 | 139 000 | 283 000 |
| 30 | 1840 | 3720 | 6790 | 14 000 | 20 900 | 40 300 | 64 200 | 113 000 | 231 000 |
| 40 | 1590 | 3220 | 5880 | 12 100 | 18 100 | 34 900 | 55 600 | 98 200 | 200 000 |
| 50 | 1430 | 2880 | 5260 | 10 800 | 16 200 | 31 200 | 49 700 | 87 900 | 179 000 |
| 60 | 1300 | 2630 | 4800 | 9860 | 14 800 | 28 500 | 45 400 | 80 200 | 164 000 |
| 70 | 1200 | 2430 | 4450 | 9130 | 13 700 | 26 400 | 42 000 | 74 300 | 151 000 |
| 80 | 1150 | 2330 | 4260 | 8540 | 12 800 | 24 700 | 39 300 | 69 500 | 142 000 |
| 90 | 1060 | 2150 | 3920 | 8050 | 12 100 | 23 200 | 37 000 | 65 500 | 134 000 |
| 100 | 979 | 1980 | 3620 | 7430 | 11 100 | 21 400 | 34 200 | 60 400 | 123 000 |
| 125 | 876 | 1770 | 3240 | 6640 | 9950 | 19 200 | 30 600 | 54 000 | 110 000 |
| 150 | 786 | 1590 | 2910 | 5960 | 8940 | 17 200 | 27 400 | 48 500 | 98 900 |
| 175 | 728 | 1470 | 2690 | 5520 | 8270 | 15 900 | 25 400 | 44 900 | 91 600 |
| 200 | 673 | 1360 | 2490 | 5100 | 7650 | 14 700 | 23 500 | 41 500 | 84 700 |
| 250 |
558 | 1170 | 2200 | 4510 | 6760 | 13 000 | 20 800 | 36 700 | 74 900 |
| 300 | 506 | 1060 | 1990 | 4090 | 6130 | 11 800 | 18 800 | 33 300 | 67 800 |
| 350 | 465 | 973 | 1830 | 3760 | 5640 | 10 900 | 17 300 | 30 600 | 62 400 |
| 400 | 433 | 905 | 1710 | 3500 | 5250 | 10 100 | 16 100 | 28 500 | 58 100 |
| 450 | 406 | 849 | 1600 | 3290 | 4920 | 9480 | 15 100 | 26 700 | 54 500 |
| 500 | 384 | 802 | 1510 | 3100 | 4650 | 8950 | 14 300 | 25 200 | 51 500 |
| 550 | 364 | 762 | 1440 | 2950 | 4420 | 8500 | 13 600 | 24 000 | 48 900 |
| 600 | 348 | 727 | 1370 | 2810 | 4210 | 8110 | 12 900 | 22 900 | 46 600 |
| 650 | 333 | 696 | 1310 | 2690 | 4030 | 7770 | 12 400 | 21 900 | 44 600 |
| 700 | 320 | 669 | 1260 | 2590 | 3880 | 7460 | 11 900 | 21 000 | 42 900 |
| 750 | 308 | 644 | 1210 | 2490 | 3730 | 7190 | 11 500 | 20 300 | 41 300 |
| 800 | 298 | 622 | 1170 | 2410 | 3610 | 6940 | 11 100 | 19 600 | 39 900 |
| 850 | 288 | 602 | 1130 | 2330 | 3490 | 6720 | 10 700 | 18 900 | 38 600 |
| 900 | 279 | 584 | 1100 | 2260 | 3380 | 6520 | 10 400 | 18 400 | 37 400 |
| 950 | 271 | 567 | 1070 | 2190 | 3290 | 6330 | 10 100 | 17 800 | 36 400 |
| 1000 | 264 |
551 | 1040 | 2130 | 3200 | 6150 | 9810 | 17 300 | 35 400 |
| 1100 | 250 | 524 | 987 | 2030 | 3030 | 5840 | 9320 | 16 500 | 33 600 |
| 1200 | 239 | 500 | 941 | 1930 | 2900 | 5580 | 8890 | 15 700 | 32 000 |
| 1300 | 229 | 478 | 901 | 1850 | 2770 | 5340 | 8510 | 15 000 | 30 700 |
| 1400 | 220 | 460 | 866 | 1780 | 2660 | 5130 | 8180 | 14 500 | 29 500 |
| 1500 | 212 | 443 | 834 | 1710 | 2570 | 4940 | 7880 | 13 900 | 28 400 |
| 1600 | 205 | 428 | 806 | 1650 | 2480 | 4770 | 7610 | 13400 | 27 400 |
| 1700 | 198 | 414 | 780 | 1600 | 2400 | 4620 | 7360 | 13 000 | 26 500 |
| 1800 | 192 | 401 | 756 | 1550 | 2330 | 4480 | 7140 | 12 600 | 25 700 |
| 1900 | 186 | 390 | 734 | 1510 | 2260 | 4350 | 6930 | 12 300 | 25 000 |
| 2000 | 181 | 379 | 714 | 1470 | 2200 | 4230 | 6740 | 11 900 | 24 300 |
* Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |||||||||
| PRESSURE DROP: | 0.3 in.w.c. | |||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:3 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||
| 10 | 20 | 42 | 85 | 148 | 210 | 448 | 806 | 1270 | 2650 | |
| 20 | 14 | 29 | 58 | 102 | 144 | 308 | 554 | 873 | 1820 | |
| 30 | 11 | 23 | 47 | 82 | 116 | 247 | 445 | 701 | 1460 | |
| 40 | 10 | 20 | 40 | 70 | 99 | 211 | 381 | 600 | 1250 | |
| 50 | NA | 17 | 35 | 62 | 88 | 187 | 337 | 532 | 1110 | |
| 60 | NA | 16 | 32 | 56 | 79 | 170 | 306 | 482 | 1000 | |
| 70 | NA | 14 | 29 | 52 | 73 | 156 | 281 | 443 | 924 | |
| 80 | NA | 13 | 27 | 48 | 68 | 145 | 262 | 413 | 859 | |
| 90 | NA | 13 | 26 | 45 | 64 | 136 | 245 | 387 | 806 | |
| 100 | NA | 12 | 24 | 43 | 60 | 129 | 232 | 366 | 761 | |
| 125 | NA | 11 | 22 | 38 | 53 | 114 | 206 | 324 | 675 | |
| 150 | NA | 10 | 20 | 34 | 48 | 103 | 186 | 294 | 612 | |
| 175 | NA | NA | 18 | 31 | 45 | 95 | 171 | 270 | 563 | |
| 200 | NA | NA | 17 | 29 | 41 | 89 | 159 | 251 | 523 | |
| 250 | NA | NA | 15 | 26 | 37 | 78 | 141 | 223 | 464 | |
| 300 | NA | NA | 13 | 23 | 33 | 71 | 128 | 202 | 420 | |
| 350 | NA | NA | 12 | 22 | 31 | 65 | 118 | 186 | 387 | |
| 400 | NA | NA | 11 | 20 | 28 | 61 | 110 | 173 | 360 | |
| 450 | NA | NA | 11 | 19 | 27 | 57 | 103 | 162 | 338 | |
| 500 | NA | NA | 10 | 18 | 25 | 54 | 97 | 153 | 319 | |
| 550 | NA | NA | NA | 17 | 24 | 51 | 92 | 145 | 303 | |
| 600 | NA | NA | NA | 16 | 23 | 49 | 88 | 139 | 289 | |
| 650 | NA | NA | NA | 15 | 22 | 47 | 84 | 133 | 277 | |
| 700 | NA | NA | NA | 15 | 21 | 45 | 81 | 128 | 266 | |
| 750 | NA | NA | NA | 14 | 20 | 43 | 78 | 123 | 256 | |
| 800 | NA | NA | NA | 14 | 20 | 42 | 75 | 119 | 247 | |
| 850 | NA | NA | NA | 13 | 19 | 40 | 73 | 115 | 239 | |
| 900 | NA | NA | NA | 13 | 18 | 39 | 71 | 111 | 232 | |
| 950 | NA | NA | NA | 13 | 18 | 38 | 69 | 108 | 225 | |
| 1000 | NA | NA | NA | 12 | 17 | 37 | 67 | 105 | 219 | |
| 1100 | NA | NA | NA | 12 | 16 | 35 | 63 | 100 | 208 | |
| 1200 | NA | NA | NA | 11 | 16 | 34 | 60 | 95 | 199 | |
| 1300 | NA | NA | NA | 11 | 15 | 32 | 58 | 91 | 190 | |
| 1400 | NA | NA | NA | 10 | 14 | 31 | 56 | 88 | 183 | |
| 1500 | NA | NA | NA | NA | 14 | 30 | 54 | 84 | 176 | |
| 1600 | NA | NA | NA | NA | 13 | 29 | 52 | 82 | 170 | |
| 1700 | NA | NA | NA | NA | 13 | 28 | 50 | 79 | 164 | |
| 1800 | NA | NA | NA | NA | 13 | 27 | 49 | 77 | 159 | |
| 1900 | NA | NA | NA | NA | 12 | 26 | 47 | 74 | 155 | |
| 2000 | NA | NA | NA | NA | 12 | 25 | 46 | 72 | 151 | |
Notes:
- 1 Table entries are rounded to 3 significant digits.
- 2 NA means a flow of less than 10 ft3/h (0.283 m3/h).
- 3 Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products.
| GAS: | NATURAL | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |||||||||
| PRESSURE DROP: | 0.5 in.w.c. | |||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:3 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||
| 10 | 27 | 55 | 111 | 195 | 276 | 590 | 1060 | 1680 | 3490 | |
| 20 | 18 | 38 | 77 | 134 | 190 | 406 | 730 | 1150 | 2400 | |
| 30 | 15 | 30 | 61 | 107 | 152 | 326 | 586 | 925 | 1930 | |
| 40 | 13 | 26 | 53 | 92 | 131 | 279 | 502 | 791 | 1650 | |
| 50 | 11 | 23 | 47 | 82 | 116 | 247 | 445 | 701 | 1460 | |
| 60 | 10 | 21 | 42 | 74 | 105 | 224 | 403 | 635 | 1320 | |
| 70 | NA | 19 | 39 | 68 | 96 | 206 | 371 | 585 | 1220 | |
| 80 | NA | 18 | 36 | 63 | 90 | 192 | 345 | 544 | 1130 | |
| 90 | NA | 17 | 34 | 59 | 84 | 180 | 324 | 510 | 1060 | |
| 100 | NA | 16 | 32 | 56 | 79 | 170 | 306 | 482 | 1000 | |
| 125 | NA | 14 | 28 | 50 | 70 | 151 | 271 | 427 | 890 | |
| 150 | NA | 13 | 26 | 45 | 64 | 136 | 245 | 387 | 806 | |
| 175 | NA | 12 | 24 | 41 | 59 | 125 | 226 | 356 | 742 | |
| 200 | NA | 11 | 22 | 39 | 55 | 117 | 210 | 331 | 690 | |
| 250 |
NA | NA | 20 | 34 | 48 | 103 | 186 | 294 | 612 | |
| 300 | NA | NA | 18 | 31 | 44 | 94 | 169 | 266 | 554 | |
| 350 | NA | NA | 16 | 28 | 40 | 86 | 155 | 245 | 510 | |
| 400 | NA | NA | 15 | 26 | 38 | 80 | 144 | 228 | 474 | |
| 450 | NA | NA | 14 | 25 | 35 | 75 | 135 | 214 | 445 | |
| 500 | NA | NA | 13 | 23 | 33 | 71 | 128 | 202 | 420 | |
| 550 | NA | NA | 13 | 22 | 32 | 68 | 122 | 192 | 399 | |
| 600 | NA | NA | 12 | 21 | 30 | 64 | 116 | 183 | 381 | |
| 650 | NA | NA | 12 | 20 | 29 | 62 | 111 | 175 | 365 | |
| 700 | NA | NA | 11 | 20 | 28 | 59 | 107 | 168 | 350 | |
| 750 | NA | NA | 11 | 19 | 27 | 57 | 103 | 162 | 338 | |
| 800 | NA | NA | 10 | 18 | 26 | 55 | 99 | 156 | 326 | |
| 850 | NA | NA | 10 | 18 | 25 | 53 | 96 | 151 | 315 | |
| 900 | NA | NA | NA | 17 | 24 | 52 | 93 | 147 | 306 | |
| 950 | NA | NA | NA | 17 | 24 | 50 | 90 | 143 | 297 | |
| 1000 | NA | NA | NA | 16 | 23 | 49 | 88 | 139 | 289 | |
| 1100 | NA | NA | NA | 15 | 22 | 46 | 84 | 132 | 274 | |
| 1200 | NA | NA | NA | 15 | 21 | 44 | 80 | 126 | 262 | |
| 1300 | NA | NA | NA | 14 | 20 | 42 | 76 | 120 | 251 | |
| 1400 | NA | NA | NA | 13 | 19 | 41 | 73 | 116 | 241 | |
| 1500 | NA | NA | NA | 13 | 18 | 39 | 71 | 111 | 232 | |
| 1600 |
NA | NA | NA | 13 | 18 | 38 | 68 | 108 | 224 | |
| 1700 |
NA | NA | NA | 12 | 17 | 37 | 66 | 104 | 217 | |
| 1800 |
NA | NA | NA | 12 | 17 | 36 | 64 | 101 | 210 | |
| 1900 |
NA | NA | NA | 11 | 16 | 35 | 62 | 98 | 204 | |
| 2000 | NA | NA | NA | 11 | 16 | 34 | 60 | 95 | 199 | |
Notes:
- 1 Table entries are rounded to 3 significant digits.
- 2 NA means a flow of less than 10 ft3/h (0.283 m3/h).
- 3 Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products.
| GAS: | NATURAL | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |||||||||
| PRESSURE DROP: | 1.0 in.w.c. | |||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||
| INTENDED USE:TUBE SIZING BETWEEN HOUSE LINE REGULATOR AND THE APPLIANCE | ||||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:3 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||
| 10 | 39 | 80 |
162 |
283 | 402 | 859 | 1550 | 2440 |
5080 | |
| 20 | 27 | 55 | 111 | 195 | 276 | 590 | 1060 | 1680 | 3490 | |
| 30 | 21 | 44 | 89 | 156 | 222 | 474 | 853 | 1350 | 2800 | |
| 40 | 18 | 38 | 77 | 134 | 190 | 406 | 730 | 1150 | 2400 | |
| 50 | 16 | 33 | 68 | 119 | 168 | 359 | 647 | 1020 | 2130 | |
| 60 | 15 | 30 | 61 | 107 | 152 | 326 | 586 | 925 | 1930 | |
| 70 | 13 | 28 | 57 | 99 | 140 | 300 | 539 | 851 | 1770 | |
| 80 | 13 | 26 | 53 | 92 | 131 | 279 | 502 | 791 | 1650 | |
| 90 | 12 | 24 | 49 | 86 | 122 | 262 | 471 | 742 | 1550 | |
| 100 | 11 | 23 | 47 | 82 | 116 | 247 | 445 | 701 | 1460 | |
| 125 | NA | 20 | 41 | 72 | 103 | 219 | 394 | 622 | 1290 | |
| 150 | NA | 18 | 37 | 65 | 93 | 198 | 357 | 563 | 1170 | |
| 175 | NA | 17 | 34 | 60 | 85 | 183 | 329 | 518 | 1080 | |
| 200 | NA | 16 | 32 | 56 | 79 | 170 | 306 | 482 | 1000 | |
| 250 |
NA | 14 | 28 | 50 | 70 | 151 | 271 | 427 | 890 | |
| 300 | NA | 13 | 26 | 45 | 64 | 136 | 245 | 387 | 806 | |
| 350 | NA | 12 | 24 | 41 | 59 | 125 | 226 | 356 | 742 | |
| 400 | NA | 11 | 22 | 39 | 55 | 117 | 210 | 331 | 690 | |
| 450 | NA | 10 | 21 | 36 | 51 | 110 | 197 | 311 | 647 | |
| 500 | NA | NA | 20 | 34 | 48 | 103 | 186 | 294 | 612 | |
| 550 | NA | NA | 19 | 32 | 46 | 98 | 177 | 279 | 581 | |
| 600 | NA | NA | 18 | 31 | 44 | 94 | 169 | 266 | 554 | |
| 650 | NA | NA | 17 | 30 | 42 | 90 | 162 | 255 | 531 | |
| 700 | NA | NA | 16 | 28 | 40 | 86 | 155 | 245 | 510 | |
| 750 | NA | NA | 16 | 27 | 39 | 83 | 150 | 236 | 491 | |
| 800 | NA | NA | 15 | 26 | 38 | 80 | 144 | 228 | 474 | |
| 850 | NA | NA | 15 | 26 | 36 | 78 | 140 | 220 | 459 | |
| 900 | NA | NA | 14 | 25 | 35 | 75 | 135 | 214 | 445 | |
| 950 | NA | NA | 14 | 24 | 34 | 73 | 132 | 207 | 432 | |
| 1000 | NA | NA | 13 | 23 | 33 | 71 | 128 | 202 | 420 | |
| 1100 | NA | NA | 13 | 22 | 32 | 68 | 122 | 192 | 399 | |
| 1200 | NA | NA | 12 | '21 | 30 | 64 | 116 | 183 | 381 | |
| 1300 | NA | NA | 12 | 20 | 29 | 62 | 111 | 175 | 365 | |
| 1400 | NA | NA | 11 | 20 | 28 | 59 | 107 | 168 | 350 | |
| 1500 | NA | NA | 11 | 19 | 27 | 57 | 103 | 162 | 338 | |
| 1600 |
NA | NA | 10 | 18 | 26 | 55 | 99 | 156 | 326 | |
| 1700 |
NA | NA | 10 | 18 | 25 | 53 | 96 | 151 | 315 | |
| 1800 |
NA | NA | NA | 17 | 24 | 52 | 93 | 147 | 306 | |
| 1900 |
NA | NA | NA | 17 | 24 | 50 | 90 | 143 | 297 | |
| 2000 | NA | NA | NA | 16 | 23 | 49 | 88 | 139 | 289 | |
Notes:
- 1 Table entries are rounded to 3 significant digits.
- 2 NA means a flow of less than 10 ft3/h (0.283 m3/h).
- 3 Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products.
| GAS: | NATURAL | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |||||||||
| PRESSURE DROP: | 17.0 in.w.c. | |||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:1 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||
| 10 | 190 | 391 |
796 | 1390 |
1970 |
4220 |
7590 | 12 000 |
24 900 |
|
| 20 | 130 | 269 | 547 | 956 | 1360 | 2900 | 5220 | 8230 | 17 100 | |
| 30 | 105 |
216 | 439 | 768 | 1090 | 2330 | 4190 | 6610 | 13 800 | |
| 40 | 90 | 185 | 376 | 657 | 932 | 1990 | 3590 | 5650 | 11 800 | |
| 50 | 79 | 164 | 333 | 582 | 826 | 1770 | 3180 | 5010 | 10 400 | |
| 60 | 72 | 148 ' | 302 | 528 | 749 | 1600 ' | 2880 | 4540 | 9460 | |
| 70 | 66 | 137 | 278 | 486 | 689 | 1470 | 2650 | 4180 | 8700 | |
| 80 | 62 | 127 | 258 | 452 | 641 | 1370 | 2460 | 3890 | 8090 | |
| 90 | 58 | 119 | 243 | 424 | 601 | 1280 | 2310 | 3650 | 7590 | |
| 100 | 55 | 113 | 229 | 400 | 568 | 1210 | 2180 | 3440 | 7170 | |
| 125 | 48 | 100 | 203 | 355 | 503 | 1080 | 1940 | 3050 | 6360 | |
| 150 | 44 | 90 | 184 | 321 | 456 | 974 | 1750 | 2770 | 5760 | |
| 175 | 40 | 83 | 169 | 296 | 420 | 896 | 1610 | 2540 | 5300 | |
| 200 | 38 | 77 | 157 | 275 | 390 | 834 | 1500 | 2370 | 4930 | |
| 250 |
33 | 69 | 140 | 244 | 346 | 739 | 1330 | 2100 | 4370 | |
| 300 | 30 | 62 | 126 | 221 | 313 | 670 | 1210 | 1900 | 3960 | |
| 350 | 28 | 57 | 116 | 203 | 288 | 616 | 1110 | 1750 | 3640 | |
| 400 | 26 | 53 | 108 | 189 | 268 | 573 | 1030 | 1630 | 3390 | |
| 450 | 24 | 50 |
102 |
177 |
252 |
538 | 968 |
1530 |
3180 |
|
| 500 | 23 | 47 | 96 | 168 | 238 | 508 | 914 | 1440 | 3000 | |
| 550 | 22 | 45 | 91 | 159 | 226 | 482 | 868 | 1370 | 2850 | |
| 600 | 21 | 43 | 87 | 152 | 215 | 460 | 829 | 1310 | 2720 | |
| 650 | 20 | 41 | 83 | 145 | 206 | 441 | 793 | 1250 | 2610 | |
| 700 | 19 | 39 | 80 | 140 | 198 | 423 | 762 | 1200 | 2500 | |
| 750 | 18 | 38 | 77 | 135 | 191 | 408 | 734 | 1160 | 2410 | |
| 800 | 18 | 37 | 74 | 130 | 184 | 394 | 709 | 1120 | 2330 | |
| 850 | 17 | 35 | 72 | 126 | 178 | 381 | 686 | 1080 | 2250 | |
| 900 | 17 | 34 | 70 | 122 | 173 | 370 | 665 | 1050 | 2180 | |
| 950 | 16 | 33 | 68 | 118 | 168 | 359 | 646 | 1020 | 2120 | |
| 1000 | 16 | 32 | 66 | 115 | 163 | 349 | 628 | 991 | 2060 | |
| 1100 | 15 | 31 | 63 | 109 | 155 | 332 | 597 | 941 | 1960 | |
| 1200 | 14 | 29 | 60 | 104 | 148 | 316 | 569 | 898 | 1870 | |
| 1300 | 14 | 28 | 57 | 100 | 142 | 303 | 545 | 860 | 1790 | |
| 1400 | 13 | 27 | 55 | 96 | 136 | 291 | 524 | 826 | 1720 | |
| 1500 | 13 | 26 | 53 | 93 | 131 | 280 | 505 | 796 | 1660 | |
| 1600 |
12 | 25 | 51 | 89 | 127 | 271 | 487 | 768 | 1600 | |
| 1700 |
12 | 24 | 49 | 86 | 123 | 262 | 472 | 744 | 1550 | |
| 1800 |
11 | 24 | 48 | 84 | 119 | 254 | 457 | 721 | 1500 | |
| 1900 |
11 | 23 | 47 | 81 | 115 | 247 | 444 | 700 | 1460 | |
| 2000 | 11 | 22 | 45 | 79 | 112 | 240 | 432 | 681 | 1420 | |
Notes:
- 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 Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 2.0 psi | |||||||||
| PRESSURE DROP: | 1.0 psi | |||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:1 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||
| 10 | 245 | 506 | 1030 | 1800 | 2550 | 5450 | 9820 | 15 500 | 32 200 | |
| 20 | 169 | 348 | 708 | 1240 | 1760 | 3750 | 6750 | 10 600 | 22 200 | |
| 30 | 135 | 279 | 568 | 993 | 1410 | 3010 | 5420 | 8550 | 17 800 | |
| 40 | 116 | 239 | 486 | 850 | 1210 | 2580 | 4640 | 7310 | 15 200 | |
| 50 | 103 | 212 | 431 | 754 | 1070 | 2280 | 4110 | 6480 | 13 500 | |
| 60 | 93 | 192 | 391 | 683 | 969 | 2070 | 3730 | 5870 | 12 200 | |
| 70 | 86 | 177 | 359 | 628 | 891 | 1900 | 3430 | 5400 | 11 300 | |
| 80 | 80 | 164 | 334 | 584 | 829 | 1770 | 3190 | 5030 | 10 500 | |
| 90 | 75 | 154 | 314 | 548 | 778 | 1660 | 2990 | 4720 | 9820 | |
| 100 | 71 | 146 | 296 | 518 | 735 | 1570 | 2830 | 4450 | 9280 | |
| 125 | 63 | 129 | 263 | 459 | 651 | 1390 | 2500 | 3950 | 8220 | |
| 150 | 57 | 117 | 238 | 416 | 590 | 1260 | 2270 | 3580 | 7450 | |
| 175 | 52 | 108 | 219 | 383 | 543 | 1160 | 2090 | 3290 | 6850 | |
| 200 | 49 | 100 | 204 | 356 | 505 | 1080 | 1940 | 3060 | 6380 | |
| 250 |
43 | 89 | 181 | 315 | 448 | 956 | 1720 | 2710 | 5650 | |
| 300 | 39 | 80 | 164 | 286 | 406 | 866 | 1560 | 2460 | 5120 | |
| 350 | 36 | 74 | 150 | 263 | 373 | 797 | 1430 | 2260 | 4710 | |
| 400 | 33 | 69 | 140 | 245 | 347 | 741 | 1330 | 2100 | 4380 | |
| 450 | 31 | 65 | 131 | 230 | 326 | 696 | 1250 | 1970 | 4110 | |
| 500 | 30 |
61 | 124 | 217 | 308 | 657 | 1180 | 1870 | 3880 | |
| 550 | 28 | 58 | 118 | 206 | 292 | 624 | 1120 | 1770 | 3520 | |
| 600 | 27 | 55 | 112 | 196 | 279 | 595 | 1070 | 1690 | 3520 | |
| 650 | 26 | 53 | 108 | 188 | 267 | 570 | 1030 | 1620 | 3370 | |
| 700 | 25 | 51 | 103 | 181 | 256 | 548 | 986 | 1550 | 3240 | |
| 750 | 24 | 49 | 100 | 174 | 247 | 528 | 950 | 1500 | 3120 | |
| 800 | 23 | 47 | 96 | 168 | 239 | 510 | 917 | 1450 | 3010 | |
| 850 | 22 | 46 | 93 | 163 | 231 | 493 | 888 | 1400 | 2920 | |
| 900 | 22 | 44 | 90 | 158 | 224 | 478 | 861 | 1360 | 2830 | |
| 950 | 21 | 43 | 88 | 153 | 217 | 464 | 836 | 1320 | 2740 | |
| 1000 | 20 | 42 | 85 | 149 | 211 | 452 | 813 | 1280 | 2670 | |
| 1100 | 19 | 40 | 81 | 142 | 201 | 429 | 772 | 1220 | 2540 | |
| 1200 | 18 | 38 | 77 | 135 | 192 | 409 | 737 | 1160 | 2420 | |
| 1300 | 18 | 36 | 74 | 129 | 183 | 392 | 705 | 1110 | 2320 | |
| 1400 | 17 | 35 | 71 | 124 | 176 | 376 | 678 | 1070 | 2230 | |
| 1500 | 16 | 34 | 68 | 120 | 170 | 363 | 653 | 1030 | 2140 | |
| 1600 |
16 | 33 | 66 | 116 | 164 | 350 | 630 | 994 | 2070 | |
| 1700 |
15 | 31 | 64 | 112 | 159 | 339 | 610 | 962 | 2000 | |
| 1800 |
15 | 30 | 62 | 108 | 154 | 329 | 592 | 933 | 1940 | |
| 1900 | 14 | 30 | 60 | 105 | 149 | 319 | 575 | 906 | 1890 | |
| 2000 | 14 | 29 | 59 | 102 | 145 | 310 | 559 | 881 | 1830 | |
Notes:
- 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 Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 2.0 psi | |||||||||
| PRESSURE DROP: | 1.5 psi | |||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||
| INTENDED USE: PIPE SIZING BETWEEN POINT OF DELIVERY AND THE HOUSE LINE REGULATOR. TOTAL LOAD SUPPLIED BY A SINGLE HOUSE LINE REGULATOR NOT EXCEEDING 150 CUBIC FEET PER HOUR.2 | ||||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:1 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||
| 10 | 303 | 625 | 1270 | 2220 | 3150 | 6740 | 121 00 | 19 100 | 39 800 | |
| 20 | 208 | 430 | 874 | 1530 | 2170 | 4630 | 8330 | 13 100 | 27 400 | |
| 30 | 167 | 345 | 702 | 1230 | 1740 | 3720 | 6690 | 10 600 | 22 000 | |
| 40 | 143 | 295 | 601 | 1050 | 1490 | 3180 | 5730 | 9030 | 18 800 | |
| 50 | 127 | 262 | 532 | 931 | 1320 | 2820 | 5080 | 8000 | 16 700 | |
| 60 | 115 | 237 | 482 | 843 | 1200 | 2560 | 4600 | 7250 | 15 100 | |
| 70 | 106 | 218 | 444 | 776 | 1100 | 2350 | 4230 | 6670 | 13 900 | |
| 80 | 98 | 203 | 413 | 722 | 1020 | 2190 | 3940 | 6210 | 12 900 | |
| 90 | 92 | 190 | 387 | 677 | 961 | 2050 | 3690 | 5820 | 12 100 | |
| 100 | 87 | 180 | 366 | 640 | 907 | 1940 | 3490 | 5500 | 11 500 | |
| 125 | 77 | 159 | 324 | 567 | 804 | 1720 | 3090 | 4880 | 10 200 | |
| 150 | 70 | 144 | 294 | 514 | 729 | 1560 | 2800 | 4420 | 9200 | |
| 175 | 64 | 133 | 270 | 472 | 670 | 1430 | 2580 | 4060 | 8460 | |
| 200 | 60 | 124 | 252 | 440 | 624 | 1330 | 2400 | 3780 | 7870 | |
| 250 | 53 | 110 | 223 | 390 | 553 | 1180 | 2130 | 3350 | 6980 | |
| 300 | 48 | 99 | 202 | 353 | 501 | 1070 | 1930 | 3040 | 6320 | |
| 350 | 44 | 91 | 186 | 325 | 461 | 984 | 1770 | 2790 | 5820 | |
| 400 | 41 | 85 | 173 | 302 | 429 | 916 | 1650 | 2600 | 5410 | |
| 450 | 39 | 80 | 162 | 283 | 402 | 859 | 1550 | 2440 | 5080 | |
| 500 | 36 | 75 | 153 | 268 | 380 | 811 | 1460 | 2300 | 4800 | |
| 550 | 35 | 72 | 146 | 254 | 361 | 771 | 1390 | 2190 | 4560 | |
| 600 | 33 | 68 | 139 | 243 | 344 | 735 | 1320 | 2090 | 4350 | |
| 650 | 32 | 65 | 133 | 232 | 330 | 704 | 1270 | 2000 | 4160 | |
| 700 | 30 | 63 | 128 | 223 | 317 | 676 | 1220 | 1920 | 4000 | |
| 750 | 29 | 60 | 123 | 215 | 305 | 652 | 1170 | 1850 | 3850 | |
| 800 | 28 | 58 | 119 | 208 | 295 | 629 | 1130 | 1790 | 3720 | |
| 850 | 27 | 57 | 115 | 201 | 285 | 609 | 1100 | 1730 | 3600 | |
| 900 | 27 | 55 | 111 | 195 | 276 | 590 | 1060 | 1680 | 3490 | |
| 950 | 26 | 53 | 108 | 189 | 268 | 573 | 1030 | 1630 | 3390 | |
| 1000 | 25 | 52 | 105 | 184 | 261 | 558 | 1000 | 1580 | 3300 | |
| 1100 | 24 | 49 | 100 | 175 | 248 | 530 | 954 | 1500 | 3130 | |
| 1200 | 23 | 47 | 95 | 167 | 237 | 505 | 910 | 1430 | 2990 | |
| 1300 | 22 | 45 | 91 | 160 | 227 | 484 | 871 | 1370 | 2860 | |
| 1400 | 21 | 43 | 88 | 153 | 218 | 465 | 837 | 1320 | 2750 | |
| 1500 | 20 | 42 | 85 | 148 | 210 | 448 | 806 | 1270 | 2650 | |
| 1600 | 19 | 40 | 82 | 143 | 202 | 432 | 779 | 1230 | 2560 | |
| 1700 | 19 | 39 | 79 | 138 | 196 | 419 | 753 | 1190 | 2470 | |
| 1800 | 18 | 38 | 77 | 134 | 190 | 406 | 731 | 1150 | 2400 | |
| 1900 | 18 | 37 | 74 | 130 | 184 | 394 | 709 | 1120 | 2330 | |
| 2000 | 17 | 36 | 72 | 126 | 179 | 383 | 690 | 1090 | 2270 | |
Notes:
- 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 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 inch water column (0.249 kPa).
- 3 Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 5.0 psi | |||||||||
| PRESSURE DROP: | 3.5 psi | |||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:1 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||
| 10 | 511 | 1050 | 2140 | 3750 | 5320 | 11 400 | 20 400 | 32 200 | 67 100 | |
| 20 | 351 | 724 | 1470 | 2580 | 3650 | 7800 | 14 000 | 22 200 | 46 100 | |
| 30 | 282 | 582 | 1180 | 2070 | 2930 | 6270 | 11 300 | 17 800 | 37 000 | |
| 40 | 241 | 498 | 1010 | 1770 | 2510 | 5360 | 9660 | 15 200 | 31 700 | |
| 50 | 214 | 441 | 898 | 1570 | 2230 | 4750 | 8560 | 13 500 | 28 100 | |
| 60 | 194 | 400 | 813 | 1420 | 2020 | 4310 | 7750 | 12 200 | 25 500 | |
| 70 | 178 | 368 | 748 | 1310 | 1860 | 3960 | 7130 | 11 200 | 23 400 | |
| 80 | 166 | 342 | 696 | 1220 | 1730 | 3690 | 6640 | 10 500 | 21 800 | |
| 90 | 156 | 321 | 653 | 1140 | 1620 | 3460 | 6230 | 9820 | 20 400 | |
| 100 | 147 | 303 | 617 | 1080 | 1530 | 3270 | 5880 | 9270 | 19 300 | |
| 125 | 130 | 269 | 547 | 955 | 1360 | 2900 | 5210 | 8220 | 17 100 | |
| 150 | 118 | 243 | 495 | 866 | 1230 | 2620 | 4720 | 7450 | 15 500 | |
| 175 | 109 | 224 | 456 | 796 | 1130 | 2410 | 4350 | 6850 | 14 300 | |
| 200 | 101 | 208 | 424 | 741 | 1050 | 2250 | 4040 | 6370 | 13 300 | |
| 250 | 90 | 185 | 376 | 657 | 932 | 1990 | 3580 | 5650 | 11 800 | |
| 300 | 81 | 167 | 340 | 595 | 844 | 1800 | 3250 | 5120 | 10 700 | |
| 350 | 75 | 154 | 313 | 547 | 777 | 1660 | 2990 | 4710 | 9810 | |
| 400 | 69 | 143 | 291 | 509 | 722 | 1540 | 2780 | 4380 | 9120 | |
| 450 | 65 | 134 | 273 | 478 | 678 | 1450 | 2610 | 4110 | 8560 | |
| 500 | 62 | 127 | 258 | 451 | 640 | 1370 | 2460 | 3880 | 8090 | |
| 550 | 58 | 121 | 245 | 429 | 608 | 1300 | 2340 | 3690 | 7680 | |
| 600 | 56 | 115 | 234 | 409 | 580 | 1240 | 2230 | 3520 | 7330 | |
| 650 | 53 | 110 | 224 | 392 | 556 | 1190 | 2140 | 3370 | 7020 | |
| 700 | 51 | 106 | 215 | 376 | 534 | 1140 | 2050 | 3240 | 6740 | |
| 750 | 49 | 102 | 207 | 362 | 514 | 1100 | 1980 | 3120 | 6490 | |
| 800 | 48 | 98 | 200 | 350 | 497 | 1060 | 1910 | 3010 | 6270 | |
| 850 | 46 | 95 | 194 | 339 | 481 | 1030 | 1850 | 2910 | 6070 | |
| 900 | 45 | 92 | 188 | 328 | 466 | 1000 | 1790 | 2820 | 5880 | |
| 950 | 43 | 90 | 182 | 319 | 452 | 967 | 1740 | 2740 | 5710 | |
| 1000 | 42 | 87 | 177 | 310 | 440 | 940 | 1690 | 2670 | 5560 | |
| 1100 | 40 | 83 | 169 | 295 | 418 | 893 | 1610 | 2530 | 5280 | |
| 1200 | 38 | 79 | 161 | 281 | 399 | 852 | 1530 | 2420 | 5040 | |
| 1300 | 37 | 76 | 154 | 269 | 382 | 816 | 1470 | 2320 | 4820 | |
| 1400 | 35 | 73 | 148 | 259 | 367 | 784 | 1410 | 2220 | 4630 | |
| 1500 | 34 | 70 | 143 | 249 | 353 | 755 | 1360 | 2140 | 4460 | |
| 1600 | 33 | 68 | 138 | 241 | 341 | 729 | 1310 | 2070 | 4310 | |
| 1700 | 32 | 65 | 133 | 233 | 330 | 705 | 1270 | 2000 | 4170 | |
| 1800 | 31 | 63 | 129 | 226 | 320 | 684 | 1230 | 1940 | 4040 | |
| 1900 | 30 | 62 | 125 | 219 | 311 | 664 | 1200 | 1890 | 3930 | |
| 2000 | 29 | 60 | 122 | 213 | 302 | 646 | 1160 | 1830 | 3820 | |
Notes:
- 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 Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | |||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |||||||||||||
| PRESSURE DROP: | 0.5 in. w.c. | |||||||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||||||
| TUBE SIZE (EHD)3 | ||||||||||||||
| FLOW DESIGNATION : | 13 | 15 | 18 | 19 | 23 | 25 | 30 | 31 | 37 | 39 | 46 | 48 | 60 | 62 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||||||
| 5 | 46 | 63 | 115 | 134 | 225 | 270 | 471 | 546 | 895 | 1037 | 1790 | 2070 | 3660 | 4140 |
| 10 | 32 | 44 | 82 | 95 | 161 | 192 | 330 | 383 | 639 | 746 | 1260 | 1470 | 2600 | 2930 |
| 15 | 25 | 35 | 66 | 77 | 132 | 157 | 267 | 310 | 524 | 615 | 1030 | 1200 | 2140 | 2400 |
| 20 | 22 | 31 | 58 | 67 | 116 | 137 | 231 | 269 | 456 | 536 | 888 | 1050 | 1850 | 2080 |
| 25 | 19 | 27 | 52 | 60 | 104 | 122 | 206 | 240 | 409 | 482 | 793 | 936 | 1660 | 1860 |
| 30 | 18 | 25 | 47 | 55 | 96 | 112 | 188 | 218 | 374 | 442 | 723 | 856 | 1520 | 1700 |
| 40 | 15 | 21 | 41 | 47 | 83 | 97 | 162 | 188 | 325 | 386 | 625 | 742 | 1320 | 1470 |
| 50 | 13 | 19 | 37 | 42 | 75 | 87 | 144 | 168 | 292 | 347 | 559 | 665 | 1180 | 1320 |
| 60 | 12 | 17 | 34 | 38 | 68 | 80 | 131 | 153 | 267 | 318 | 509 | 608 | 1080 | 1200 |
| 70 | 11 | 16 | 31 | 36 | 63 | 74 | 121 | 141 | 248 | 295 | 471 | 563 | 1000 | 1110 |
| 80 | 10 | 15 | 29 | 33 | 60 | 69 | 113 | 132 | 232 | 277 | 440 | 527 | 940 | 1040 |
| 90 | 10 | 14 | 28 | 32 | 57 | 65 | 107 | 125 | 219 | 262 | 415 | 498 | 887 | 983 |
| 100 | 9 | 13 | 26 | 30 | 54 | 62 | 101 | 118 | 208 | 249 | 393 | 472 | 843 | 933 |
| 150 | 7 | 10 | 20 | 23 | 42 | 48 | 78 | 91 | 171 | 205 | 320 | 387 | 691 | 762 |
| 200 | 6 | 9 | 18 | 21 | 38 | 44 | 71 | 82 | 148 | 179 | 277 | 336 | 600 | 661 |
| 250 | 5 | 8 | 16 | 19 | 34 | 39 | 63 | 74 | 133 | 161 | 247 | 301 | 538 | 591 |
| 300 | 5 | 7 | 15 | 17 | 32 | 36 | 57 | 67 | 95 | 148 | 226 | 275 | 492 | 540 |
Notes:
- 1 Table entries are rounded to 3 significant digits.
- 2 Table includes losses for four 90 degree ( 1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.3 n, where L is additional length (ft) of tubing and n is the number of additional fittings, bends, or both.
- 3 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.
| GAS: | NATURAL | ||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | ||||||||||||
| PRESSURE DROP: | 3.0 in. w.c. | ||||||||||||
| SPECIFIC GRAVITY: | 0.60 | ||||||||||||
| INTENDED USE: INITIAL SUPPLY PRESSURE OF 8.0 INCH WATER COLUMN OR GREATER | |||||||||||||
| TUBE SIZE (EHD)3 | |||||||||||||
| FLOW DESIGNATION : | 13 | 15 | 18 | 19 | 23 | 25 | 30 | 31 | 37 | 46 | 48 | 60 | 62 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | ||||||||||||
| 5 | 120 | 160 | 277 | 327 | 529 | 649 | 1180 | 1370 | 2140 | 4430 | 5010 | 8800 | 10 100 |
| 10 | 83 | 112 | 197 | 231 | 380 | 462 | 828 | 958 | 1530 | 3200 | 3560 | 6270 | 7160 |
| 15 | 67 | 90 | 161 | 189 | 313 | 379 | 673 | 778 | 1250 | 2540 | 2910 | 5140 | 5850 |
| 20 | 57 | 78 | 140 | 164 | 273 | 329 | 580 | 672 | 1090 | 2200 | 2530 | 4460 | 5070 |
| 25 | 51 | 69 | 125 | 147 | 245 | 295 | 518 | 599 | 978 | 1960 | 2270 | 4000 | 4540 |
| 30 | 46 | 63 | 115 | 134 | 225 | 270 | 471 | 546 | 895 | 1790 | 2070 | 3660 | 4140 |
| 40 | 39 | 54 | 100 | 116 | 196 | 234 | 407 | 471 | 778 | 1550 | 1800 | 3180 | 3590 |
| 50 | 35 | 48 | 89 | 104 | 176 | 210 | 363 | 421 | 698 | 1380 | 1610 | 2850 | 3210 |
| 60 | 32 | 44 | 82 | 95 | 161 | 192 | 330 | 383 | 639 | 1260 | 1470 | 2600 | 2930 |
| 70 | 29 | 41 | 76 | 88 | 150 | 178 | 306 | 355 | 593 | 1170 | 1360 | 2420 | 2720 |
| 80 | 27 | 38 | 71 | 82 | 141 | 167 | 285 | 331 | 555 | 1090 | 1280 | 2260 | 2540 |
| 90 | 26 | 36 | 67 | 77 | 133 | 157 | 268 | 311 | 524 | 1030 | 1200 | 2140 | 2400 |
| 100 | 24 | 34 | 63 | 73 | 126 | 149 | 254 | 295 | 498 | 974 | 1140 | 2030 | 2280 |
| 150 | 19 | 27 | 52 | 60 | 104 | 122 | 206 | 240 | 409 | 793 | 936 | 1660 | 1860 |
| 200 | 17 | 23 | 45 | 52 | 91 | 106 | 178 | 207 | 355 | 686 | 812 | 1440 | 1610 |
| 250 | 15 | 21 | 40 | 46 | 82 | 95 | 159 | 184 | 319 | 613 | 728 | 1290 | 1440 |
| 300 | 13 | 19 | 37 | 42 | 75 | 87 | 144 | 168 | 234 | 559 | 665 | 1180 | 1320 |
Notes:
- 1 Table entries are rounded to 3 significant digits.
- 2 Table includes losses for four 90 degree ( 1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.3 n, where L is additional length (ft) of tubing and n is the number of additional fittings, bends, or both.
- 3 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.
| GAS: | NATURAL | ||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | ||||||||||||
| PRESSURE DROP: | 6.0 in. w.c. | ||||||||||||
| SPECIFIC GRAVITY: | 0.60 | ||||||||||||
| INTENDED USE: INITIAL SUPPLY PRESSURE OF 11.0 INCH WATER COLUMN OR GREATER | |||||||||||||
| TUBE SIZE (EHD)3 | |||||||||||||
| FLOW DESIGNATION : | 13 | 15 | 18 | 19 | 23 | 25 | 30 | 31 | 37 | 46 | 48 | 60 | 62 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | ||||||||||||
| 5 | 173 | 229 | 389 | 461 | 737 | 911 | 1690 | 1950 | 3000 | 6280 | 7050 | 12 400 | 14 260 |
| 10 | 120 | 160 | 277 | 327 | 529 | 649 | 1180 | 1370 | 2140 | 4430 | 5010 | 8800 | 10 100 |
| 15 | 96 | 130 | 227 | 267 | 436 | 532 | 960 | 1110 | 1760 | 3610 | 4100 | 7210 | 8260 |
| 20 | 83 | 112 | 197 | 231 | 380 | 462 | 828 | 958 | 1530 | 3120 | 3560 | 6270 | 7160 |
| 25 | 74 | 99 | 176 | 207 | 342 | 414 | 739 | 855 | 1370 | 2790 | 3190 | 5620 | 6400 |
| 30 | 67 | 90 | 161 | 189 | 313 | 379 | 673 | 778 | 1250 | 2540 | 2910 | 5140 | 5850 |
| 40 | 57 | 78 | 140 | 164 | 273 | 329 | 580 | 672 | 1090 | 2200 | 2530 | 4460 | 5070 |
| 50 | 51 | 69 | 125 | 147 | 245 | 295 | 518 | 599 | 978 | 1960 | 2270 | 4000 | 4540 |
| 60 | 46 | 63 | 115 | 134 | 225 | 270 | 471 | 546 | 895 | 1790 | 2070 | 3660 | 4140 |
| 70 | 42 | 58 | 106 | 124 | 209 | 250 | 435 | 505 | 830 | 1660 | 1920 | 3390 | 3840 |
| 80 | 39 | 54 | 100 | 116 | 196 | 234 | 407 | 471 | 778 | 1550 | 1800 | 3180 | 3590 |
| 90 | 37 | 51 | 94 | 109 | 185 | 221 | 383 | 444 | 735 | 1460 | 1700 | 3000 | 3390 |
| 100 | 35 | 48 | 89 | 104 | 176 | 210 | 363 | 421 | 698 | 1380 | 1610 | 2850 | 3210 |
| 150 | 28 | 39 | 73 | 85 | 145 | 172 | 294 | 342 | 573 | 1130 | 1320 | 2340 | 2630 |
| 200 | 24 | 34 | 63 | 73 | 126 | 149 | 254 | 295 | 498 | 974 | 1140 | 2030 | 2280 |
| 250 | 21 | 30 | 57 | 66 | 114 | 134 | 226 | 263 | 447 | 870 | 1020 | 1820 | 2040 |
| 300 | 19 | 27 | 52 | 60 | 104 | 122 | 206 | 240 | 409 | 793 | 936 | 1660 | 1860 |
Notes:
- 1 Table entries are rounded to 3 significant digits.
- 2 Table includes losses for four 90 degree ( 1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.3 n, where L is additional length (ft) of tubing and n is the number of additional fittings, bends, or both.
- 3 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.
| GAS: | NATURAL | |||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 2.0 psi | |||||||||||||
| PRESSURE DROP: | 1.0 psi | |||||||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||||||
| TUBE SIZE (EHD)5 | ||||||||||||||
| FLOW DESIGNATION : | 13 | 15 | 18 | 19 | 23 | 25 | 30 | 31 | 37 | 39 | 46 | 48 | 60 | 62 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||||||
| 10 | 270 | 353 | 587 | 700 | 1100 | 1370 | 2590 | 2990 | 4510 | 5037 | 9600 | 10 700 | 18 600 | 21 600 |
| 25 | 166 | 220 | 374 | 444 | 709 | 876 | 1620 | 1870 | 2890 | 3258 | 6040 | 6780 | 11 900 | 13 700 |
| 30 | 151 | 200 | 342 | 405 | 650 | 801 | 1480 | 1700 | 2640 | 2987 | 5510 | 6200 | 10 900 | 12 500 |
| 40 | 129 | 172 | 297 | 351 | 567 | 696 | 1270 | 1470 | 2300 | 2605 | 4760 | 5380 | 9440 | 10 900 |
| 50 | 115 | 154 | 266 | 314 | 510 | 624 | 1140 | 1310 | 2060 | 2343 | 4260 | 4820 | 8470 | 9720 |
| 75 | 93 | 124 | 218 | 257 | 420 | 512 | 922 | 1070 | 1690 | 1932 | 3470 | 3950 | 6940 | 7940 |
| 80 | 89 | 120 | 211 | 249 | 407 | 496 | 892 | 1030 | 1640 | 1874 | 3360 | 3820 | 6730 | 7690 |
| 100 | 79 | 107 | 189 | 222 | 366 | 445 | 795 | 920 | 1470 | 1685 | 3000 | 3420 | 6030 | 6880 |
| 150 | 64 | 87 | 155 | 182 | 302 | 364 | 646 | 748 | 1210 | 1389 | 2440 | 2800 | 4940 | 5620 |
| 200 | 55 | 75 | 135 | 157 | 263 | 317 | 557 | 645 | 1050 | 1212 | 2110 | 2430 | 4290 | 4870 |
| 250 | 49 | 67 | 121 | 141 | 236 | 284 | 497 | 576 | 941 | 1090 | 1890 | 2180 | 3850 | 4360 |
| 300 | 44 | 61 | 110 | 129 | 217 | 260 | 453 | 525 | 862 | 999 | 1720 | 1990 | 3520 | 3980 |
| 400 | 38 | 52 | 96 | 111 | 189 | 225 | 390 | 453 | 749 | 871 | 1490 | 1730 | 3060 | 3450 |
| 500 | 34 | 46 | 86 | 100 | 170 | 202 | 348 | 404 | 552 | 783 | 1330 | 1550 | 2740 | 3090 |
Notes:
- 1 Table does not include effect of pressure drop across the line regulator. Where regulator loss exceeds 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 are capable of varying with flow rate.
- 2 CAUTION: Capacities shown in table are capable of exceeding maximum capacity for a selected regulator. Consult with regulator or tubing manufacturer for guidance.
- 3 Table includes losses for four 90 degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, fittings, or both shall be increased by an equivalent length of tubing according to the following equation: L = 1.3 n, where L is additional length (ft) of tubing and n is the number of additional fittings, bends, or both.
- 4 Table entries are rounded to 3 significant digits.
- 5 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.
| GAS: | NATURAL | |||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 5.0 psi | |||||||||||||
| PRESSURE DROP: | 3.5 psi | |||||||||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||||||||
| TUBE SIZE (EHD)5 | ||||||||||||||
| FLOW DESIGNATION : | 13 | 15 | 18 | 19 | 23 | 25 | 30 | 31 | 37 | 39 | 46 | 48 | 60 | 62 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||||||||
| 10 | 523 | 674 | 1080 | 1300 | 2000 | 2530 | 4920 | 5660 | 8300 | 9140 | 18 100 | 19 800 | 34 400 | 40 400 |
| 25 | 322 | 420 | 691 | 827 | 1290 | 1620 | 3080 | 3540 | 5310 | 5911 | 11 400 | 12 600 | 22 000 | 25 600 |
| 30 | 292 | 382 | 632 | 755 | 1180 | 1480 | 2800 | 3230 | 4860 | 5420 | 10 400 | 11 500 | 20 100 | 23 400 |
| 40 | 251 | 329 | 549 | 654 | 1030 | 1280 | 2420 | 2790 | 4230 | 4727 | 8970 | 10 000 | 17 400 | 20 200 |
| 50 | 223 | 293 | 492 | 586 | 926 | 1150 | 2160 | 2490 | 3790 | 4251 | 8020 | 8930 | 15 600 | 18 100 |
| 75 | 180 | 238 | 403 | 479 | 763 | 944 | 1750 | 2020 | 3110 | 3506 | 6530 | 7320 | 12 800 | 14 800 |
| 80 | 174 | 230 | 391 | 463 | 740 | 915 | 1690 | 1960 | 3020 | 3400 | 6320 | 7090 | 12 400 | 14 300 |
| 100 | 154 | 205 | 350 | 415 | 665 | 820 | 1510 | 1740 | 2710 | 3057 | 5650 | 6350 | 11 100 | 12 800 |
| 150 | 124 | 166 | 287 | 339 | 548 | 672 | 1230 | 1420 | 2220 | 2521 | 4600 | 5200 | 9130 | 10 500 |
| 200 | 107 | 143 | 249 | 294 | 478 | 584 | 1060 | 1220 | 1930 | 2199 | 3980 | 4510 | 7930 | 9090 |
| 250 | 95 | 128 | 223 | 263 | 430 | 524 | 945 | 1090 | 1730 | 1977 | 3550 | 4040 | 7110 | 8140 |
| 300 | 86 | 116 | 204 | 240 | 394 | 479 | 860 | 995 | 1590 | 1813 | 3240 | 3690 | 6500 | 7430 |
| 400 | 74 | 100 | 177 | 208 | 343 | 416 | 742 | 858 | 1380 | 1581 | 2800 | 3210 | 5650 | 6440 |
| 500 | 66 | 89 | 159 | 186 | 309 | 373 | 662 | 766 | 1040 | 1422 | 2500 | 2870 | 5060 | 5760 |
Notes:
- 1 Table does not include effect of pressure drop across the line regulator. Where regulator loss exceeds 1 psi (7 kPa), DO NOT USE THIS TABLE. Consult with regulator manufacturer for pressure drops and capacity factors. Pressure drops across a regulator are capable of varying with flow rate.
- 2 CAUTION: Capacities shown in table are capable of exceeding maximum capacity for a selected regulator. Consult with regulator or tubing manufacturer for guidance.
- 3 Table includes losses for four 90 degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, fittings, or both shall be increased by an equivalent length of tubing according to the following equation: L = 1.3 n, where L is additional length (ft) of tubing and n is the number of additional fittings, bends, or both.
- 4 Table entries are rounded to 3 significant digits.
- 5 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.
| GAS: | NATURAL | |||||||
|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |||||||
| PRESSURE DROP: | 0.3 in.w.c. | |||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||
| PIPE SIZE (inch) | ||||||||
| NOMINAL OD: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 3 | 4 |
| DESIGNATION: | SDR 9.3 | SDR 11 | SDR 11 | SDR 10 | SDR 11 | SDR 11 | SDR 11 | SDR 11 |
| ACTUAL ID: | 0.660 | 0.860 | 1.077 | 1.328 | 1.554 | 1.943 | 2.864 | 3.682 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||
| 10 | 153 | 305 | 551 | 955 | 1440 | 2590 | 7170 | 13 900 |
| 20 | 105 | 210 | 379 | 656 | 991 | 1780 | 4920 | 9520 |
| 30 | 84 | 169 | 304 | 527 | 796 | 1430 | 3950 | 7640 |
| 40 | 72 | 144 | 260 | 451 | 681 | 1220 | 3380 | 6540 |
| 50 | 64 | 128 | 231 | 400 | 604 | 1080 | 3000 | 5800 |
| 60 | 58 | 116 | 209 | 362 | 547 | 983 | 2720 | 5250 |
| 70 | 53 | 107 | 192 | 333 | 503 | 904 | 2500 | 4830 |
| 80 | 50 | 99 | 179 | 310 | 468 | 841 | 2330 | 4500 |
| 90 | 46 | 93 | 168 | 291 | 439 | 789 | 2180 | 4220 |
| 100 | 44 | 88 | 159 | 275 | 415 | 745 | 2060 | 3990 |
| 125 | 39 | 78 | 141 | 243 | 368 | 661 | 1830 | 3530 |
| 150 | 35 | 71 | 127 | 221 | 333 | 598 | 1660 | 3200 |
| 175 | 32 | 65 | 117 | 203 | 306 | 551 | 1520 | 2940 |
| 200 | 30 | 60 | 109 | 189 | 285 | 512 | 1420 | 2740 |
| 250 | 27 | 54 | 97 | 167 | 253 | 454 | 1260 | 2430 |
| 300 | 24 | 48 | 88 | 152 | 229 | 411 | 1140 | 2200 |
| 350 | 22 | 45 | 81 | 139 | 211 | 378 | 1050 | 2020 |
| 400 | 21 | 42 | 75 | 130 | 196 | 352 | 974 | 1880 |
| 450 | 19 | 39 | 70 | 122 | 184 | 330 | 914 | 1770 |
| 500 | 18 | 37 | 66 | 115 | 174 | 312 | 863 | 1670 |
* Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | |||||||
|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |||||||
| PRESSURE DROP: | 0.5 in.w.c. | |||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||
| PIPE SIZE (inch) | ||||||||
| NOMINAL OD: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 3 | 4 |
| DESIGNATION: | SDR 9.3 | SDR 11 | SDR 11 | SDR 10 | SDR 11 | SDR 11 | SDR 11 | SDR 11 |
| ACTUAL ID: | 0.660 | 0.860 | 1.077 | 1.328 | 1.554 | 1.943 | 2.864 | 3.682 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||
| 10 | 201 | 403 | 726 | 1260 | 1900 | 3410 | 9450 | 18 260 |
| 20 | 138 | 277 | 499 | 865 | 1310 | 2350 | 6490 | 12 550 |
| 30 | 111 | 222 | 401 | 695 | 1050 | 1880 | 5210 | 10 080 |
| 40 | 95 | 190 | 343 | 594 | 898 | 1610 | 4460 | 8630 |
| 50 | 84 | 169 | 304 | 527 | 796 | 1430 | 3950 | 7640 |
| 60 | 76 | 153 | 276 | 477 | 721 | 1300 | 3580 | 6930 |
| 70 | 70 | 140 | 254 | 439 | 663 | 1190 | 3300 | 6370 |
| 80 | 65 | 131 | 236 | 409 | 617 | 1110 | 3070 | 5930 |
| 90 | 61 | 123 | 221 | 383 | 579 | 1040 | 2880 | 5560 |
| 100 | 58 | 116 | 209 | 362 | 547 | 983 | 2720 | 5250 |
| 125 | 51 | 103 | 185 | 321 | 485 | 871 | 2410 | 4660 |
| 150 | 46 | 93 | 168 | 291 | 439 | 789 | 2180 | 4220 |
| 175 | 43 | 86 | 154 | 268 | 404 | 726 | 2010 | 3880 |
| 200 | 40 | 80 | 144 | 249 | 376 | 675 | 1870 | 3610 |
| 250 | 35 | 71 | 127 | 221 | 333 | 598 | 1660 | 3200 |
| 300 | 32 | 64 | 115 | 200 | 302 | 542 | 1500 | 2900 |
| 350 | 29 | 59 | 106 | 184 | 278 | 499 | 1380 | 2670 |
| 400 | 27 | 55 | 99 | 171 | 258 | 464 | 1280 | 2480 |
| 450 | 26 | 51 | 93 | 160 | 242 | 435 | 1200 | 2330 |
| 500 | 24 | 48 | 88 | 152 | 229 | 411 | 1140 | 2200 |
* Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | |||||||
|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 2.0 psi | |||||||
| PRESSURE DROP: | 1.0 psi | |||||||
| SPECIFIC GRAVITY: | 0.60 | |||||||
| PIPE SIZE (inch) | ||||||||
| NOMINAL OD: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 3 | 4 |
| DESIGNATION: | SDR 9.3 | SDR 11 | SDR 11 | SDR 10 | SDR 11 | SDR 11 | SDR 11 | SDR 11 |
| ACTUAL ID: | 0.660 | 0.860 | 1.077 | 1.328 | 1.554 | 1.943 | 2.864 | 3.682 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||
| 10 | 1860 | 3720 | 6710 | 11 600 | 17 600 | 31 600 | 87 300 | 169 000 |
| 20 | 1280 | 2560 | 4610 | 7990 | 12 100 | 21 700 | 60 000 | 116 000 |
| 30 | 1030 | 2050 | 3710 | 6420 | 9690 | 17 400 | 48 200 | 93 200 |
| 40 | 878 | 1760 | 3170 | 5490 | 8300 | 14 900 | 41 200 | 79 700 |
| 50 | 778 | 1560 | 2810 | 4870 | 7350 | 13 200 | 36 600 | 70 700 |
| 60 | 705 | 1410 | 2550 | 4410 | 6660 | 12 000 | 33 100 | 64 000 |
| 70 | 649 | 1300 | 2340 | 4060 | 6130 | 11 000 | 30 500 | 58 900 |
| 80 | 603 | 1210 | 2180 | 3780 | 5700 | 10 200 | 28 300 | 54 800 |
| 90 | 566 | 1130 | 2050 | 3540 | 5350 | 9610 | 26 600 | 51 400 |
| 100 | 535 | 1070 | 1930 | 3350 | 5050 | 9080 | 25 100 | 48 600 |
| 125 | 474 | 949 | 1710 | 2970 | 4480 | 8050 | 22 300 | 43 000 |
| 150 | 429 | 860 | 1550 | 2690 | 4060 | 7290 | 20 200 | 39 000 |
| 175 | 395 | 791 | 1430 | 2470 | 3730 | 6710 | 18 600 | 35 900 |
| 200 | 368 | 736 | 1330 | 2300 | 3470 | 6240 | 17 300 | 33 400 |
| 250 | 326 | 652 | 1180 | 2040 | 3080 | 5530 | 15 300 | 29 600 |
| 300 | 295 | 591 | 1070 | 1850 | 2790 | 5010 | 13 900 | 26 800 |
| 350 | 272 | 544 | 981 | 1700 | 2570 | 4610 | 12 800 | 24 700 |
| 400 | 253 | 506 | 913 | 1580 | 2390 | 4290 | 11 900 | 22 900 |
| 450 | 237 | 475 | 856 | 1480 | 2240 | 4020 | 11 100 | 21 500 |
| 500 | 224 | 448 | 809 | 1400 | 2120 | 3800 | 10 500 | 20 300 |
| 550 | 213 | 426 | 768 | 1330 | 2010 | 3610 | 9990 | 19 300 |
| 600 | 203 | 406 | 733 | 1270 | 1920 | 3440 | 9530 | 18 400 |
| 650 | 194 | 389 | 702 | 1220 | 1840 | 3300 | 9130 | 17 600 |
| 700 | 187 | 374 | 674 | 1170 | 1760 | 3170 | 8770 | 16 900 |
| 750 | 180 | 360 | 649 | 1130 | 1700 | 3050 | 8450 | 16 300 |
| 800 | 174 | 348 | 627 | 1090 | 1640 | 2950 | 8160 | 15 800 |
| 850 | 168 | 336 | 607 | 1050 | 1590 | 2850 | 7890 | 15 300 |
| 900 | 163 | 326 | 588 | 1020 | 1540 | 2770 | 7650 | 14 800 |
| 950 | 158 | 317 | 572 | 990 | 1500 | 2690 | 7430 | 14 400 |
| 1000 | 154 | 308 | 556 | 963 | 1450 | 2610 | 7230 | 14 000 |
| 1100 | 146 | 293 | 528 | 915 | 1380 | 2480 | 6870 | 13 300 |
| 1200 | 139 | 279 | 504 | 873 | 1320 | 2370 | 6550 | 12 700 |
| 1300 | 134 | 267 | 482 | 836 | 1260 | 2270 | 6270 | 12 100 |
| 1400 | 128 | 257 | 463 | 803 | 1210 | 2180 | 6030 | 11 600 |
| 1500 | 124 | 247 | 446 | 773 | 1170 | 2100 | 5810 | 11 200 |
| 1600 | 119 | 239 | 431 | 747 | 1130 | 2030 | 5610 | 10 800 |
| 1700 | 115 | 231 | 417 | 723 | 1090 | 1960 | 5430 | 10 500 |
| 1800 | 112 | 224 | 404 | 701 | 1060 | 1900 | 5260 | 10 200 |
| 1900 | 109 | 218 | 393 | 680 | 1030 | 1850 | 5110 | 9900 |
| 2000 | 106 | 212 | 382 | 662 | 1000 | 1800 | 4970 | 9600 |
* Table entries are rounded to 3 significant digits.
| GAS: | NATURAL | |
|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |
| PRESSURE DROP: | 0.3 in.w.c. | |
| SPECIFIC GRAVITY: | 0.60 | |
| PLASTIC TUBING SIZE (CTS)1 (inch) | ||
| NOMINAL OD: | 1/2 | 1 |
| DESIGNATION: | SDR 7 | SDR 11 |
| ACTUAL ID: | 0.445 | 0.927 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |
| 10 | 54 | 372 |
| 20 | 37 | 256 |
| 30 | 30 | 205 |
| 40 | 26 | 176 |
| 50 | 23 | 156 |
| 60 | 21 | 141 |
| 70 | 19 | 130 |
| 80 | 18 | 121 |
| 90 | 17 | 113 |
| 100 | 16 | 107 |
| 125 | 14 | 95 |
| 150 | 13 | 86 |
| 175 | 12 | 79 |
| 200 | 11 | 74 |
| 225 | 10 | 69 |
| 250 | NA | 65 |
| 275 | NA | 62 |
| 300 | NA | 59 |
| 350 | NA | 54 |
| 400 | NA | 51 |
| 450 | NA | 47 |
| 500 | NA | 45 |
Notes:
- 1 CTS = Copper tube size.
- 2 Table entries are rounded to 3 significant digits.
- 3 NA means a flow of less than 10 ft3/h (0.283 m3/h).
| GAS: | NATURAL | |
|---|---|---|
| INLET PRESSURE: | LESS THAN 2 psi | |
| PRESSURE DROP: | 0.5 in.w.c. | |
| SPECIFIC GRAVITY: | 0.60 | |
| PLASTIC TUBING SIZE (CTS)1 (inch) | ||
| NOMINAL OD: | 1/2 | 1 |
| DESIGNATION: | SDR 7 | SDR 11 |
| ACTUAL ID: | 0.445 | 0.927 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |
| 10 | 72 | 490 |
| 20 | 49 | 337 |
| 30 | 39 | 271 |
| 40 | 34 | 232 |
| 50 | 30 | 205 |
| 60 | 27 | 186 |
| 70 | 25 | 171 |
| 80 | 23 | 159 |
| 90 | 22 | 149 |
| 100 | 21 | 141 |
| 125 | 18 | 125 |
| 150 | 17 | 113 |
| 175 | 15 | 104 |
| 200 | 14 | 97 |
| 225 | 13 | 91 |
| 250 | 12 | 86 |
| 275 | 11 | 82 |
| 300 | 11 | 78 |
| 350 | 10 | 72 |
| 400 | NA | 67 |
| 450 | NA | 63 |
| 500 | NA | 59 |
Notes:
- 1 CTS = Copper tube size.
- 2 Table entries are rounded to 3 significant digits.
- 3 NA means a flow of less than 10 ft3/h (0.283 m3/h).
| GAS: | UNDILUTED PROPANE | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 10.0 psi | ||||||||
| PRESSURE DROP: | 1.0 psi | ||||||||
| SPECIFIC GRAVITY: | 1.50 | ||||||||
| INTENDED USE: PIPE SIZING BETWEEN FIRST STAGE (HIGH PRESSURE) REGULATOR AND SECOND STAGE (LOW PRESSURE) REGULATOR | |||||||||
| PIPE SIZE (inch) | |||||||||
| NOMINAL INSIDE: |
1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | ||||||||
| 10 | 3320 | 6950 | 13 100 | 26 900 | 40 300 | 77 600 | 124 000 | 219 000 | 446 000 |
| 20 | 2280 | 4780 | 9000 | 18 500 | 27 700 | 53 300 | 85 000 | 150 000 | 306 000 |
| 30 | 1830 | 3840 | 7220 | 14 800 | 22 200 | 42 800 | 68 200 | 121 000 | 246 000 |
| 40 | 1570 | 3280 | 6180 | 12 700 | 19 000 | 36 600 | 58 400 | 103 000 | 211 000 |
| 50 | 1390 | 2910 | 5480 | 11 300 | 16 900 | 32 500 | 51 700 | 91 500 | 187 000 |
| 60 | 1260 | 2640 | 4970 | 10 200 | 15 300 | 29 400 | 46 900 | 82 900 | 169 000 |
| 70 | 1160 | 2430 | 4570 | 9380 | 14 100 | 27 100 | 43 100 | 76 300 | 156 000 |
| 80 | 1080 | 2260 | 4250 | 8730 | 13 100 | 25 200 | 40 100 | 70 900 | 145 000 |
| 90 | 1010 | 2120 | 3990 | 8190 | 12 300 | 23 600 | 37 700 | 66 600 | 136 000 |
| 100 | 956 | 2000 | 3770 | 7730 | 11 600 | 22 300 | 35 600 | 62 900 | 128 000 |
| 125 | 848 | 1770 | 3340 | 6850 | 10 300 | 19 800 | 31 500 | 55 700 | 114 000 |
| 150 | 768 | 1610 | 3020 | 6210 | 9300 | 17 900 | 28 600 | 50 500 | 103 000 |
| 175 | 706 | 1480 | 2780 | 5710 | 8560 | 16 500 | 26 300 | 46 500 | 94 700 |
| 200 | 657 | 1370 | 2590 | 5320 | 7960 | 15 300 | 24 400 | 43 200 | 88 100 |
| 250 | 582 | 1220 | 2290 | 4710 | 7060 | 13 600 | 21 700 | 38 300 | 78 100 |
| 300 | 528 | 1100 | 2080 | 4270 | 6400 | 12 300 | 19 600 | 34 700 | 70 800 |
| 350 | 486 | 1020 | 1910 | 3930 | 5880 | 11 300 | 18 100 | 31 900 | 65 100 |
| 400 | 452 | 945 | 1780 | 3650 | 5470 | 10 500 | 16 800 | 29 700 | 60 600 |
| 450 | 424 | 886 | 1670 | 3430 | 5140 | 9890 | 15 800 | 27 900 | 56 800 |
| 500 | 400 | 837 | 1580 | 3240 | 4850 | 9340 | 14 900 | 26 300 | 53 700 |
| 550 | 380 | 795 | 1500 | 3070 | 4610 | 8870 | 14 100 | 25 000 | 51 000 |
| 600 | 363 | 759 | 1430 | 2930 | 4400 | 8460 | 13 500 | 23 900 | 48 600 |
| 650 | 347 | 726 | 1370 | 2810 | 4210 | 8110 | 12 900 | 22 800 | 46 600 |
| 700 | 334 | 698 | 1310 | 2700 | 4040 | 7790 | 12 400 | 21 900 | 44 800 |
| 750 | 321 | 672 | 1270 | 2600 | 3900 | 7500 | 12 000 | 21 100 | 43 100 |
| 800 | 310 | 649 | 1220 | 2510 | 3760 | 7240 | 11 500 | 20 400 | 41 600 |
| 850 | 300 | 628 | 1180 | 2430 | 3640 | 7010 | 11 200 | 19 800 | 40 300 |
| 900 | 291 | 609 | 1150 | 2360 | 3530 | 6800 | 10 800 | 19 200 | 39 100 |
| 950 | 283 | 592 | 1110 | 2290 | 3430 | 6600 | 10 500 | 18 600 | 37 900 |
| 1000 | 275 | 575 | 1080 | 2230 | 3330 | 6420 | 10 200 | 18 100 | 36 900 |
| 1100 | 261 | 546 | 1030 | 2110 | 3170 | 6100 | 9720 | 17 200 | 35 000 |
| 1200 | 249 | 521 | 982 | 2020 | 3020 | 5820 | 9270 | 16 400 | 33 400 |
| 1300 | 239 | 499 | 940 | 1930 | 2890 | 5570 | 8880 | 15 700 | 32 000 |
| 1400 | 229 | 480 | 903 | 1850 | 2780 | 5350 | 8530 | 15 100 | 30 800 |
| 1500 | 221 | 462 | 870 | 1790 | 2680 | 5160 | 8220 | 14 500 | 29 600 |
| 1600 | 213 | 446 | 840 | 1730 | 2590 | 4980 | 7940 | 14 000 | 28 600 |
| 1700 | 206 | 432 | 813 | 1670 | 2500 | 4820 | 7680 | 13 600 | 27 700 |
| 1800 | 200 | 419 | 789 | 1620 | 2430 | 4670 | 7450 | 13 200 | 26 900 |
| 1900 | 194 | 407 | 766 | 1570 | 2360 | 4540 | 7230 | 12 800 | 26 100 |
| 2000 | 189 | 395 | 745 | 1530 | 2290 | 4410 | 7030 | 12 400 | 25 400 |
* Table entries are rounded to 3 significant digits.
| GAS: | UNDILUTED PROPANE | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 10.0 psi | ||||||||
| PRESSURE DROP: | 3.0 psi | ||||||||
| SPECIFIC GRAVITY: | 1.50 | ||||||||
| INTENDED USE: PIPE SIZING BETWEEN FIRST STAGE (HIGH PRESSURE) REGULATOR AND SECOND STAGE (LOW PRESSURE) REGULATOR | |||||||||
| PIPE SIZE (inch) | |||||||||
| NOMINAL INSIDE: |
1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | ||||||||
| 10 | 5890 | 12 300 | 23 200 | 47 600 | 71 300 | 137 000 | 219 000 | 387 000 | 789 000 |
| 20 | 4050 | 8460 | 15 900 | 32 700 | 49 000 | 94 400 | 150 000 | 266 000 | 543 000 |
| 30 | 3250 | 6790 | 12 800 | 26 300 | 39 400 | 75 800 | 121 000 | 214 000 | 436 000 |
| 40 | 2780 | 5810 | 11 000 | 22 500 | 33 700 | 64 900 | 103 000 | 183 000 | 373 000 |
| 50 | 2460 | 5150 | 9710 | 19 900 | 29 900 | 57 500 | 91 600 | 162 000 | 330 000 |
| 60 | 2230 | 4670 | 8790 | 18 100 | 27 100 | 52 100 | 83 000 | 147 000 | 299 000 |
| 70 | 2050 | 4300 | 8090 | 16 600 | 24 900 | 47 900 | 76 400 | 135 000 | 275 000 |
| 80 | 1910 | 4000 | 7530 | 15 500 | 23 200 | 44 600 | 71 100 | 126 000 | 256 000 |
| 90 | 1790 | 3750 | 7060 | 14 500 | 21 700 | 41 800 | 66 700 | 118 000 | 240 000 |
| 100 | 1690 | 3540 | 6670 | 13 700 | 20 500 | 39 500 | 63 000 | 111 000 | 227 000 |
| 125 | 1500 | 3140 | 5910 | 12 100 | 18 200 | 35 000 | 55 800 | 98 700 | 201 000 |
| 150 | 1360 | 2840 | 5360 | 11 000 | 16 500 | 31 700 | 50 600 | 89 400 | 182 000 |
| 175 | 1250 | 2620 | 4930 | 10 100 | 15 200 | 29 200 | 46 500 | 82 300 | 167 800 |
| 200 | 1160 | 2430 | 4580 | 9410 | 14 100 | 27 200 | 43 300 | 76 500 | 156 100 |
| 250 | 1030 | 2160 | 4060 | 8340 | 12 500 | 24 100 | 38 400 | 67 800 | 138 400 |
| 300 | 935 | 1950 | 3680 | 7560 | 11 300 | 21 800 | 34 800 | 61 500 | 125 400 |
| 350 | 860 | 1800 | 3390 | 6950 | 10 400 | 20 100 | 32 000 | 56 500 | 115 300 |
| 400 | 800 | 1670 | 3150 | 6470 | 9690 | 18 700 | 29 800 | 52 600 | 107 300 |
| 450 | 751 | 1570 | 2960 | 6070 | 9090 | 17 500 | 27 900 | 49 400 | 100 700 |
| 500 | 709 | 1480 | 2790 | 5730 | 8590 | 16 500 | 26 400 | 46 600 | 95 100 |
| 550 | 673 | 1410 | 2650 | 5450 | 8160 | 15 700 | 25 000 | 44 300 | 90 300 |
| 600 | 642 | 1340 | 2530 | 5200 | 7780 | 15 000 | 23 900 | 42 200 | 86 200 |
| 650 | 615 | 1290 | 2420 | 4980 | 7450 | 14 400 | 22 900 | 40 500 | 82 500 |
| 700 | 591 | 1240 | 2330 | 4780 | 7160 | 13 800 | 22 000 | 38 900 | 79 300 |
| 750 | 569 | 1190 | 2240 | 4600 | 6900 | 13 300 | 21 200 | 37 400 | 76 400 |
| 800 | 550 | 1150 | 2170 | 4450 | 6660 | 12 800 | 20 500 | 36 200 | 73 700 |
| 850 | 532 | 1110 | 2100 | 4300 | 6450 | 12 400 | 19 800 | 35 000 | 71 400 |
| 900 | 516 | 1080 | 2030 | 4170 | 6250 | 12 000 | 19 200 | 33 900 | 69 200 |
| 950 | 501 | 1050 | 1970 | 4050 | 6070 | 11 700 | 18 600 | 32 900 | 67 200 |
| 1000 | 487 | 1020 | 1920 | 3940 | 5900 | 11 400 | 18 100 | 32 000 | 65 400 |
| 1100 | 463 | 968 | 1820 | 3740 | 5610 | 10 800 | 17 200 | 30 400 | 62 100 |
| 1200 | 442 | 923 | 1740 | 3570 | 5350 | 10 300 | 16 400 | 29 000 | 59 200 |
| 1300 | 423 | 884 | 1670 | 3420 | 5120 | 9870 | 15 700 | 27 800 | 56 700 |
| 1400 | 406 | 849 | 1600 | 3280 | 4920 | 9480 | 15 100 | 26 700 | 54 500 |
| 1500 | 391 | 818 | 1540 | 3160 | 4740 | 9130 | 14 600 | 25 700 | 52 500 |
| 1600 | 378 | 790 | 1490 | 3060 | 4580 | 8820 | 14 100 | 24 800 | 50 700 |
| 1700 | 366 | 765 | 1440 | 2960 | 4430 | 8530 | 13 600 | 24 000 | 49 000 |
| 1800 | 355 | 741 | 1400 | 2870 | 4300 | 8270 | 13 200 | 23 300 | 47 600 |
| 1900 | 344 | 720 | 1360 | 2780 | 4170 | 8040 | 12 800 | 22 600 | 46 200 |
| 2000 | 335 | 700 | 1320 | 2710 | 4060 | 7820 | 12 500 | 22 000 | 44 900 |
* Table entries are rounded to 3 significant digits.
| GAS: | UNDILUTED PROPANE | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 2.0 psi | ||||||||
| PRESSURE DROP: | 1.0 psi | ||||||||
| SPECIFIC GRAVITY: | 1.50 | ||||||||
| INTENDED USE: PIPE SIZING BETWEEN 2 PSI SERVICE AND LINE PRESSURE REGULATOR | |||||||||
| PIPE SIZE (inch) | |||||||||
| NOMINAL INSIDE: |
1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | ||||||||
| 10 | 2680 | 5590 | 10 500 | 21 600 | 32 400 | 62 400 | 99 500 | 176 000 | 359 000 |
| 20 | 1840 | 3850 | 7240 | 14 900 | 22 300 | 42 900 | 68 400 | 121 000 | 247 000 |
| 30 | 1480 | 3090 | 5820 | 11 900 | 17 900 | 34 500 | 54 900 | 97 100 | 198 000 |
| 40 | 1260 | 2640 | 4980 | 10 200 | 15 300 | 29 500 | 47 000 | 83 100 | 170 000 |
| 50 | 1120 | 2340 | 4410 | 9060 | 13 600 | 26 100 | 41 700 | 73 700 | 150 000 |
| 60 | 1010 | 2120 | 4000 | 8210 | 12 300 | 23 700 | 37 700 | 66 700 | 136 000 |
| 70 | 934 | 1950 | 3680 | 7550 | 11 300 | 21 800 | 34 700 | 61 400 | 125 000 |
| 80 | 869 | 1820 | 3420 | 7020 | 10 500 | 20 300 | 32 300 | 57 100 | 116 000 |
| 90 | 815 | 1700 | 3210 | 6590 | 9880 | 19 000 | 30 300 | 53 600 | 109 000 |
| 100 | 770 | 1610 | 3030 | 6230 | 9330 | 18 000 | 28 600 | 50 600 | 103 000 |
| 125 | 682 | 1430 | 2690 | 5520 | 8270 | 15 900 | 25 400 | 44 900 | 91 500 |
| 150 | 618 | 1290 | 2440 | 5000 | 7490 | 14 400 | 23 000 | 40 700 | 82 900 |
| 175 | 569 | 1190 | 2240 | 4600 | 6890 | 13 300 | 21 200 | 37 400 | 76 300 |
| 200 | 529 | 1110 | 2080 | 4280 | 6410 | 12 300 | 19 700 | 34 800 | 71 000 |
| 250 | 469 | 981 | 1850 | 3790 | 5680 | 10 900 | 17 400 | 30 800 | 62 900 |
| 300 | 425 | 889 | 1670 | 3440 | 5150 | 9920 | 15 800 | 27 900 | 57 000 |
| 350 | 391 | 817 | 1540 | 3160 | 4740 | 9120 | 14 500 | 25 700 | 52 400 |
| 400 | 364 | 760 | 1430 | 2940 | 4410 | 8490 | 13 500 | 23 900 | 48 800 |
| 450 | 341 | 714 | 1340 | 2760 | 4130 | 7960 | 12 700 | 22 400 | 45 800 |
| 500 | 322 | 674 | 1270 | 2610 | 3910 | 7520 | 12 000 | 21 200 | 43 200 |
| 550 | 306 | 640 | 1210 | 2480 | 3710 | 7140 | 11 400 | 20 100 | 41 100 |
| 600 | 292 | 611 | 1150 | 2360 | 3540 | 6820 | 10 900 | 19 200 | 39 200 |
| 650 | 280 | 585 | 1100 | 2260 | 3390 | 6530 | 10 400 | 18 400 | 37 500 |
| 700 | 269 | 562 | 1060 | 2170 | 3260 | 6270 | 9990 | 17 700 | 36 000 |
| 750 | 259 | 541 | 1020 | 2090 | 3140 | 6040 | 9630 | 17 000 | 34 700 |
| 800 | 250 | 523 | 985 | 2020 | 3030 | 5830 | 9300 | 16 400 | 33 500 |
| 850 | 242 | 506 | 953 | 1960 | 2930 | 5640 | 9000 | 15 900 | 32 400 |
| 900 | 235 | 490 | 924 | 1900 | 2840 | 5470 | 8720 | 15 400 | 31 500 |
| 950 | 228 | 476 | 897 | 1840 | 2760 | 5310 | 8470 | 15 000 | 30 500 |
| 1000 | 222 | 463 | 873 | 1790 | 2680 | 5170 | 8240 | 14 600 | 29 700 |
| 1100 | 210 | 440 | 829 | 1700 | 2550 | 4910 | 7830 | 13 800 | 28 200 |
| 1200 | 201 | 420 | 791 | 1620 | 2430 | 4680 | 7470 | 13 200 | 26 900 |
| 1300 | 192 | 402 | 757 | 1550 | 2330 | 4490 | 7150 | 12 600 | 25 800 |
| 1400 | 185 | 386 | 727 | 1490 | 2240 | 4310 | 6870 | 12 100 | 24 800 |
| 1500 | 178 | 372 | 701 | 1440 | 2160 | 4150 | 6620 | 11 700 | 23 900 |
| 1600 | 172 | 359 | 677 | 1390 | 2080 | 4010 | 6390 | 11 300 | 23 000 |
| 1700 | 166 | 348 | 655 | 1340 | 2010 | 3880 | 6180 | 10 900 | 22 300 |
| 1800 | 161 | 337 | 635 | 1300 | 1950 | 3760 | 6000 | 10 600 | 21 600 |
| 1900 | 157 | 327 | 617 | 1270 | 1900 | 3650 | 5820 | 10 300 | 21 000 |
| 2000 | 152 | 318 | 600 | 1230 | 1840 | 3550 | 5660 | 10 000 | 20 400 |
* Table entries are rounded to 3 significant digits.
| GAS: | UNDILUTED PROPANE | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 11.0 in. w.c. | ||||||||
| PRESSURE DROP: | 0.5 in. w.c. | ||||||||
| SPECIFIC GRAVITY: | 1.50 | ||||||||
| INTENDED USE: PIPE SIZING BETWEEN SINGLE OR SECOND STAGE (LOW PRESSURE) REGULATOR ANO APPLIANCE | |||||||||
| PIPE SIZE (inch) | |||||||||
| NOMINAL INSIDE: |
1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 21/2 | 3 | 4 |
| ACTUAL ID: | 0.622 | 0.824 | 1.049 | 1.380 | 1.610 | 2.067 | 2.469 | 3.068 | 4.026 |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | ||||||||
| 10 | 291 | 608 | 1150 | 2350 | 3520 | 6790 | 10 800 | 19 100 | 39 000 |
| 20 | 200 | 418 | 787 | 1620 | 2420 | 4660 | 7430 | 13 100 | 26 800 |
| 30 | 160 | 336 | 632 | 1300 | 1940 | 3750 | 5970 | 10 600 | 21 500 |
| 40 | 137 | 287 | 541 | 1110 | 1660 | 3210 | 5110 | 9030 | 18 400 |
| 50 | 122 | 255 | 480 | 985 | 1480 | 2840 | 4530 | 8000 | 16 300 |
| 60 | 110 | 231 | 434 | 892 | 1340 | 2570 | 4100 | 7250 | 14 800 |
| 80 | 101 | 212 | 400 | 821 | 1230 | 2370 | 3770 | 6670 | 13 600 |
| 100 | 94 | 197 | 372 | 763 | 1140 | 2200 | 3510 | 6210 | 12 700 |
| 125 | 89 | 185 | 349 | 716 | 1070 | 2070 | 3290 | 5820 | 11 900 |
| 150 | 84 | 175 | 330 | 677 | 1010 | 1950 | 3110 | 5500 | 11 200 |
| 175 | 74 | 155 | 292 | 600 | 899 | 1730 | 2760 | 4880 | 9950 |
| 200 | 67 | 140 | 265 | 543 | 814 | 1570 | 2500 | 4420 | 9010 |
| 250 | 62 | 129 | 243 | 500 | 749 | 1440 | 2300 | 4060 | 8290 |
| 300 | 58 | 120 | 227 | 465 | 697 | 1340 | 2140 | 3780 | 7710 |
| 350 | 51 | 107 | 201 | 412 | 618 | 1190 | 1900 | 3350 | 6840 |
| 400 | 46 | 97 | 182 | 373 | 560 | 1080 | 1720 | 3040 | 6190 |
| 450 | 42 | 89 | 167 | 344 | 515 | 991 | 1580 | 2790 | 5700 |
| 500 | 40 | 83 | 156 | 320 | 479 | 922 | 1470 | 2600 | 5300 |
| 550 | 37 | 78 | 146 | 300 | 449 | 865 | 1380 | 2440 | 4970 |
| 600 | 35 | 73 | 138 | 283 | 424 | 817 | 1300 | 2300 | 4700 |
| 650 | 33 | 70 | 131 | 269 | 403 | 776 | 1240 | 2190 | 4460 |
| 700 | 32 | 66 | 125 | 257 | 385 | 741 | 1180 | 2090 | 4260 |
| 750 | 30 | 64 | 120 | 246 | 368 | 709 | 1130 | 2000 | 4080 |
| 800 | 29 | 61 | 115 | 236 | 354 | 681 | 1090 | 1920 | 3920 |
| 850 | 28 | 59 | 111 | 227 | 341 | 656 | 1050 | 1850 | 3770 |
| 900 | 27 | 57 | 107 | 220 | 329 | 634 | 1010 | 1790 | 3640 |
| 950 | 26 | 55 | 104 | 213 | 319 | 613 | 978 | 1730 | 3530 |
| 1000 | 25 | 53 | 100 | 206 | 309 | 595 | 948 | 1680 | 3420 |
| 1100 | 25 | 52 | 97 | 200 | 300 | 578 | 921 | 1630 | 3320 |
| 1200 | 24 | 50 | 95 | 195 | 292 | 562 | 895 | 1580 | 3230 |
| 1300 | 23 | 48 | 90 | 185 | 277 | 534 | 850 | 1500 | 3070 |
| 1400 | 22 | 46 | 86 | 176 | 264 | 509 | 811 | 1430 | 2930 |
| 1500 | 21 | 44 | 82 | 169 | 253 | 487 | 777 | 1370 | 2800 |
| 1600 | 20 | 42 | 79 | 162 | 243 | 468 | 746 | 1320 | 2690 |
| 1700 | 19 | 40 | 76 | 156 | 234 | 451 | 719 | 1270 | 2590 |
| 1800 | 19 | 39 | 74 | 151 | 226 | 436 | 694 | 1230 | 2500 |
| 1900 | 18 | 38 | 71 | 146 | 219 | 422 | 672 | 1190 | 2420 |
| 2000 | 18 | 37 | 69 | 142 | 212 | 409 | 652 | 1150 | 2350 |
* Table entries are rounded to 3 significant digits.
| GAS: | UNDILUTED PROPANE | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 10.0 psi | |||||||||
| PRESSURE DROP: | 1.0 psi | |||||||||
| SPECIFIC GRAVITY: | 1.50 | |||||||||
| INTENDED USE:TUBE SIZING BETWEEN FIRST STAGE (HIGH PRESSURE) REGULATOR AND SECOND STAGE (LOW PRESSURE) REGULATOR | ||||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:1 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | |||||||||
| 10 | 513 | 1060 | 2150 | 3760 | 5330 | 11 400 | 20 500 | 32 300 | 67 400 | |
| 20 | 352 | 727 | 1480 | 2580 | 3670 | 7830 | 14 100 | 22 200 | 46 300 | |
| 30 | 283 | 584 | 1190 | 2080 | 2940 | 6290 | 11 300 | 17 900 | 37 200 | |
| 40 | 242 | 500 | 1020 | 1780 | 2520 | 5380 | 9690 | 15 300 | 31 800 | |
| 50 | 215 | 443 | 901 | 1570 | 2230 | 4770 | 8590 | 13 500 | 28 200 | |
| 60 | 194 | 401 | 816 | 1430 | 2020 | 4320 | 7780 | 12 300 | 25 600 | |
| 70 | 179 | 369 | 751 | 1310 | 1860 | 3980 | 7160 | 11 300 | 23 500 | |
| 80 | 166 | 343 | 699 | 1220 | 1730 | 3700 | 6660 | 10 500 | 21 900 | |
| 90 | 156 | 322 | 655 | 1150 | 1630 | 3470 | 6250 | 9850 | 20 500 | |
| 100 | 147 | 304 | 619 | 1080 | 1540 | 3280 | 5900 | 9310 | 19 400 | |
| 125 | 131 | 270 | 549 | 959 | 1360 | 2910 | 5230 | 8250 | 17 200 | |
| 150 | 118 | 244 | 497 | 869 | 1230 | 2630 | 4740 | 7470 | 15 600 | |
| 175 | 109 | 225 | 457 | 799 | 1130 | 2420 | 4360 | 6880 | 14 300 | |
| 200 | 101 | 209 | 426 | 744 | 1060 | 2250 | 4060 | 6400 | 13 300 | |
| 250 | 90 | 185 | 377 | 659 | 935 | 2000 | 3600 | 5670 | 11 800 | |
| 300 | 81 | 168 | 342 | 597 | 847 | 1810 | 3260 | 5140 | 10 700 | |
| 350 | 75 | 155 | 314 | 549 | 779 | 1660 | 3000 | 4730 | 9840 | |
| 400 | 70 | 144 | 292 | 511 | 725 | 1550 | 2790 | 4400 | 9160 | |
| 450 | 65 | 135 | 274 | 480 | 680 | 1450 | 2620 | 4130 | 8590 | |
| 500 | 62 | 127 | 259 | 453 | 643 | 1370 | 2470 | 3900 | 8120 | |
| 550 | 59 | 121 | 246 | 430 | 610 | 1300 | 2350 | 3700 | 7710 | |
| 600 | 56 | 115 | 235 | 410 | 582 | 1240 | 2240 | 3530 | 7350 | |
| 650 | 54 | 111 | 225 | 393 | 558 | 1190 | 2140 | 3380 | 7040 | |
| 700 | 51 | 106 | 216 | 378 | 536 | 1140 | 2060 | 3250 | 6770 | |
| 750 | 50 | 102 | 208 | 364 | 516 | 1100 | 1980 | 3130 | 6520 | |
| 800 | 48 | 99 | 201 | 351 | 498 | 1060 | 1920 | 3020 | 6290 | |
| 850 | 46 | 96 | 195 | 340 | 482 | 1030 | 1850 | 2920 | 6090 | |
| 900 | 45 | 93 | 189 | 330 | 468 | 1000 | 1800 | 2840 | 5910 | |
| 950 | 44 | 90 | 183 | 320 | 454 | 970 | 1750 | 2750 | 5730 | |
| 1000 | 42 | 88 | 178 | 311 | 442 | 944 | 1700 | 2680 | 5580 | |
| 1100 | 40 | 83 | 169 | 296 | 420 | 896 | 1610 | 2540 | 5300 | |
| 1200 | 38 | 79 | 161 | 282 | 400 | 855 | 1540 | 2430 | 5050 | |
| 1300 | 37 | 76 | 155 | 270 | 383 | 819 | 1470 | 2320 | 4840 | |
| 1400 | 35 | 73 | 148 | 260 | 368 | 787 | 1420 | 2230 | 4650 | |
| 1500 | 34 | 70 | 143 | 250 | 355 | 758 | 1360 | 2150 | 4480 | |
| 1600 | 33 | 68 | 138 | 241 | 343 | 732 | 1320 | 2080 | 4330 | |
| 1700 | 32 | 66 | 134 | 234 | 331 | 708 | 1270 | 2010 | 4190 | |
| 1800 | 31 | 64 | 130 | 227 | 321 | 687 | 1240 | 1950 | 4060 | |
| 1900 | 30 | 62 | 126 | 220 | 312 | 667 | 1200 | 1890 | 3940 | |
| 2000 | 29 | 60 | 122 | 214 | 304 | 648 | 1170 | 1840 | 3830 | |
- 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 Table entries are rounded to 3 significant digits.
| GAS: | UNDILUTED PROPANE | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 11.0 in. w.c. | |||||||||
| PRESSURE DROP: | 0.5 in. w.c. | |||||||||
| SPECIFIC GRAVITY: | 1.50 | |||||||||
| INTENDED USE: TUBE SIZING BETWEEN SINGLE OR SECOND STAGE (LOW PRESSURE) REGULATOR AND APPLIANCE | ||||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:1 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | |||||||||
| 10 | 45 | 93 | 188 | 329 | 467 | 997 | 1800 | 2830 | 5890 | |
| 20 | 31 | 64 | 129 | 226 | 321 | 685 | 1230 | 1950 | 4050 | |
| 30 | 25 | 51 | 104 | 182 | 258 | 550 | 991 | 1560 | 3250 | |
| 40 | 21 | 44 | 89 | 155 | 220 | 471 | 848 | 1340 | 2780 | |
| 50 | 19 | 39 | 79 | 138 | 195 | 417 | 752 | 1180 | 2470 | |
| 60 | 17 | 35 | 71 | 125 | 177 | 378 | 681 | 1070 | 2240 | |
| 70 | 16 | 32 | 66 | 115 | 163 | 348 | 626 | 988 | 2060 | |
| 80 | 15 | 30 | 61 | 107 | 152 | 324 | 583 | 919 | 1910 | |
| 90 | 14 | 28 | 57 | 100 | 142 | 304 | 547 | 862 | 1800 | |
| 100 | 13 | 27 | 54 | 95 | 134 | 287 | 517 | 814 | 1700 | |
| 125 | 11 | 24 | 48 | 84 | 119 | 254 | 458 | 722 | 1500 | |
| 150 | 10 | 21 | 44 | 76 | 108 | 230 | 415 | 654 | 1360 | |
| 175 | NA | 20 | 40 | 70 | 99 | 212 | 382 | 602 | 1250 | |
| 200 | NA | 18 | 37 | 65 | 92 | 197 | 355 | 560 | 1170 | |
| 250 | NA | 16 | 33 | 58 | 82 | 175 | 315 | 496 | 1030 | |
| 300 | NA | 15 | 30 | 52 | 74 | 158 | 285 | 449 | 936 | |
| 350 | NA | 14 | 28 | 48 | 68 | 146 | 262 | 414 | 861 | |
| 400 | NA | 13 | 26 | 45 | 63 | 136 | 244 | 385 | 801 | |
| 450 | NA | 12 | 24 | 42 | 60 | 127 | 229 | 361 | 752 | |
| 500 | NA | 11 | 23 | 40 | 56 | 120 | 216 | 341 | 710 | |
| 550 | NA | 11 | 22 | 38 | 53 | 114 | 205 | 324 | 674 | |
| 600 | NA | 10 | 21 | 36 | 51 | 109 | 196 | 309 | 643 | |
| 650 | NA | NA | 20 | 34 | 49 | 104 | 188 | 296 | 616 | |
| 700 | NA | NA | 19 | 33 | 47 | 100 | 180 | 284 | 592 | |
| 750 | NA | NA | 18 | 32 | 45 | 96 | 174 | 274 | 570 | |
| 800 | NA | NA | 18 | 31 | 44 | 93 | 168 | 264 | 551 | |
| 850 | NA | NA | 17 | 30 | 42 | 90 | 162 | 256 | 533 | |
| 900 | NA | NA | 17 | 29 | 41 | 87 | 157 | 248 | 517 | |
| 950 | NA | NA | 16 | 28 | 40 | 85 | 153 | 241 | 502 | |
| 1000 | NA | NA | 16 | 27 | 39 | 83 | 149 | 234 | 488 | |
| 1100 | NA | NA | 15 | 26 | 37 | 78 | 141 | 223 | 464 | |
| 1200 | NA | NA | 14 | 25 | 35 | 75 | 135 | 212 | 442 | |
| 1300 | NA | NA | 14 | 24 | 34 | 72 | 129 | 203 | 423 | |
| 1400 | NA | NA | 13 | 23 | 32 | 69 | 124 | 195 | 407 | |
| 1500 | NA | NA | 13 | 22 | 31 | 66 | 119 | 188 | 392 | |
| 1600 | NA | NA | 12 | 21 | 30 | 64 | 115 | 182 | 378 | |
| 1700 | NA | NA | 12 | 20 | 29 | 62 | 112 | 176 | 366 | |
| 1800 | NA | NA | 11 | 20 | 28 | 60 | 108 | 170 | 355 | |
| 1900 | NA | NA | 11 | 19 | 27 | 58 | 105 | 166 | 345 | |
| 2000 | NA | NA | 11 | 19 | 27 | 57 | 102 | 161 | 335 | |
- 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 Table entries are rounded to 3 significant digits.
- 3 NA means a flow of less than 10 000 Btu/h (2.93 kW).
| GAS: | UNDILUTED PROPANE | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 2.0 psi | |||||||||
| PRESSURE DROP: | 1.0 psi | |||||||||
| SPECIFIC GRAVITY: | 1.50 | |||||||||
| INTENDED USE: TUBE SIZING BETWEEN 2 PSIG SERVICE AND LINE PRESSURE REGULATOR | ||||||||||
| TUBE SIZE (inch) | ||||||||||
| NOMINAL | K& L: | 1/4 | 3/8 | 1/2 | 5/8 | 3/4 | 1 | 11/4 | 11/2 | 2 |
| ACR: | 3/8 | 1/2 | 5/8 | 3/4 | 7/8 | 11/8 | 13/8 | - | - | |
| OUTSIDE: | 0.375 | 0.500 | 0.625 | 0.750 | 0.875 | 1.125 | 1.375 | 1.625 | 2.125 | |
| INSIDE:1 | 0.305 | 0.402 | 0.527 | 0.652 | 0.745 | 0.995 | 1.245 | 1.481 | 1.959 | |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | |||||||||
| 10 | 413 | 852 | 1730 | 3030 | 4300 | 9170 | 16 500 | 26 000 | 54 200 | |
| 20 | 284 | 585 | 1190 | 2080 | 2950 | 6310 | 11 400 | 17 900 | 37 300 | |
| 30 | 228 | 470 | 956 | 1670 | 2370 | 5060 | 9120 | 14 400 | 29 900 | |
| 40 | 195 | 402 | 818 | 1430 | 2030 | 4330 | 7800 | 12 300 | 25 600 | |
| 50 | 173 | 356 | 725 | 1270 | 1800 | 3840 | 6920 | 10 900 | 22 700 | |
| 60 | 157 | 323 | 657 | 1150 | 1630 | 3480 | 6270 | 9880 | 20 600 | |
| 70 | 144 | 297 | 605 | 1060 | 1500 | 3200 | 5760 | 9090 | 18 900 | |
| 80 | 134 | 276 | 562 | 983 | 1390 | 2980 | 5360 | 8450 | 17 600 | |
| 90 | 126 | 259 | 528 | 922 | 1310 | 2790 | 5030 | 7930 | 16 500 | |
| 100 | 119 | 245 | 498 | 871 | 1240 | 2640 | 4750 | 7490 | 15 600 | |
| 125 | 105 | 217 | 442 | 772 | 1100 | 2340 | 4210 | 6640 | 13 800 | |
| 150 | 95 | 197 | 400 | 700 | 992 | 2120 | 3820 | 6020 | 12 500 | |
| 175 | 88 | 181 | 368 | 644 | 913 | 1950 | 3510 | 5540 | 11 500 | |
| 200 | 82 | 168 | 343 | 599 | 849 | 1810 | 3270 | 5150 | 10 700 | |
| 250 | 72 | 149 | 304 | 531 | 753 | 1610 | 2900 | 4560 | 9510 | |
| 300 | 66 | 135 | 275 | 481 | 682 | 1460 | 2620 | 4140 | 8610 | |
| 350 | 60 | 124 | 253 | 442 | 628 | 1340 | 2410 | 3800 | 7920 | |
| 400 | 56 | 116 | 235 | 411 | 584 | 1250 | 2250 | 3540 | 7370 | |
| 450 | 53 | 109 | 221 | 386 | 548 | 1170 | 2110 | 3320 | 6920 | |
| 500 | 50 | 103 | 209 | 365 | 517 | 1110 | 1990 | 3140 | 6530 | |
| 550 | 47 | 97 | 198 | 346 | 491 | 1050 | 1890 | 2980 | 6210 | |
| 600 | 45 | 93 | 189 | 330 | 469 | 1000 | 1800 | 2840 | 5920 | |
| 650 | 43 | 89 | 181 | 316 | 449 | 959 | 1730 | 2720 | 5670 | |
| 700 | 41 | 86 | 174 | 304 | 431 | 921 | 1660 | 2620 | 5450 | |
| 750 | 40 | 82 | 168 | 293 | 415 | 888 | 1600 | 2520 | 5250 | |
| 800 | 39 | 80 | 162 | 283 | 401 | 857 | 1540 | 2430 | 5070 | |
| 850 | 37 | 77 | 157 | 274 | 388 | 829 | 1490 | 2350 | 4900 | |
| 900 | 36 | 75 | 152 | 265 | 376 | 804 | 1450 | 2280 | 4750 | |
| 950 | 35 | 72 | 147 | 258 | 366 | 781 | 1410 | 2220 | 4620 | |
| 1000 | 34 | 71 | 143 | 251 | 356 | 760 | 1370 | 2160 | 4490 | |
| 1100 | 32 | 67 | 136 | 238 | 338 | 721 | 1300 | 2050 | 4270 | |
| 1200 | 31 | 64 | 130 | 227 | 322 | 688 | 1240 | 1950 | 4070 | |
| 1300 | 30 | 61 | 124 | 217 | 309 | 659 | 1190 | 1870 | 3900 | |
| 1400 | 28 | 59 | 120 | 209 | 296 | 633 | 1140 | 1800 | 3740 | |
| 1500 | 27 | 57 | 115 | 201 | 286 | 610 | 1100 | 1730 | 3610 | |
| 1600 | 26 | 55 | 111 | 194 | 276 | 589 | 1060 | 1670 | 3480 | |
| 1700 | 26 | 53 | 108 | 188 | 267 | 570 | 1030 | 1620 | 3370 | |
| 1800 | 25 | 51 | 104 | 182 | 259 | 553 | 1000 | 1570 | 3270 | |
| 1900 | 24 | 50 | 101 | 177 | 251 | 537 | 966 | 1520 | 3170 | |
| 2000 | 23 | 48 | 99 | 172 | 244 | 522 | 940 | 1480 | 3090 | |
- 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 Table entries are rounded to 3 significant digits.
| GAS: | UNDILUTED PROPANE | |||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 11.0 in. w.c. | |||||||||||||
| PRESSURE DROP: | 0.5 in. w.c. | |||||||||||||
| SPECIFIC GRAVITY: | 1.50 | |||||||||||||
| INTENDED USE: CSST SIZING BETWEEN SINGLE OR SECOND STAGE (LOW PRESSURE) REGULATOR AND APPLIANCE SHUTOFF VALVE | ||||||||||||||
| TUBE SIZE (EHD)3 | ||||||||||||||
| FLOW DESIGNATION : | 13 | 15 | 18 | 19 | 23 | 25 | 30 | 31 | 37 | 39 | 46 | 48 | 60 | 62 |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | |||||||||||||
| 5 | 72 | 99 | 181 | 211 | 355 | 426 | 744 | 863 | 1420 | 1638 | 2830 | 3270 | 5780 | 6550 |
| 10 | 50 | 69 | 129 | 150 | 254 | 303 | 521 | 605 | 971 | 1179 | 1990 | 2320 | 4110 | 4640 |
| 15 | 39 | 55 | 104 | 121 | 208 | 248 | 422 | 490 | 775 | 972 | 1620 | 1900 | 3370 | 3790 |
| 20 | 34 | 49 | 91 | 106 | 183 | 216 | 365 | 425 | 661 | 847 | 1400 | 1650 | 2930 | 3290 |
| 25 | 30 | 42 | 82 | 94 | 164 | 192 | 325 | 379 | 583 | 762 | 1250 | 1480 | 2630 | 2940 |
| 30 | 28 | 39 | 74 | 87 | 151 | 177 | 297 | 344 | 528 | 698 | 1140 | 1350 | 2400 | 2680 |
| 40 | 23 | 33 | 64 | 74 | 131 | 153 | 256 | 297 | 449 | 610 | 988 | 1170 | 2090 | 2330 |
| 50 | 20 | 30 | 58 | 66 | 118 | 137 | 227 | 265 | 397 | 548 | 884 | 1050 | 1870 | 2080 |
| 60 | 19 | 26 | 53 | 60 | 107 | 126 | 207 | 241 | 359 | 502 | 805 | 961 | 1710 | 1900 |
| 70 | 17 | 25 | 49 | 57 | 99 | 117 | 191 | 222 | 330 | 466 | 745 | 890 | 1590 | 1760 |
| 80 | 15 | 23 | 45 | 52 | 94 | 109 | 178 | 208 | 307 | 438 | 696 | 833 | 1490 | 1650 |
| 90 | 15 | 22 | 44 | 50 | 90 | 102 | 169 | 197 | 286 | 414 | 656 | 787 | 1400 | 1550 |
| 100 | 14 | 20 | 41 | 47 | 85 | 98 | 159 | 186 | 270 | 393 | 621 | 746 | 1330 | 1480 |
| 150 | 11 | 15 | 31 | 36 | 66 | 75 | 123 | 143 | 217 | 324 | 506 | 611 | 1090 | 1210 |
| 200 | 9 | 14 | 28 | 33 | 60 | 69 | 112 | 129 | 183 | 283 | 438 | 531 | 948 | 1050 |
| 250 | 8 | 12 | 25 | 30 | 53 | 61 | 99 | 117 | 163 | 254 | 390 | 476 | 850 | 934 |
| 300 | 8 | 11 | 23 | 26 | 50 | 57 | 90 | 107 | 147 | 234 | 357 | 434 | 777 | 854 |
- 1 Table includes losses for four 90 degree (1.57 rad) bends and two end fitting s. Tubing runs with larger numbers of bends, fittings, or both shall be increased by an equivalent length of tubing to the followin g equation : L = 1.3 n, where Lis additional length (ft) of tubing and n is the number of additional fittings, bends, or both.
- 2 Table entries are rounded to 3 significant digits.
- 3 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.
| GAS: | UNDILUTED PROPANE | |||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 2.0 psi | |||||||||||||
| PRESSURE DROP: | 1.0 psi | |||||||||||||
| SPECIFIC GRAVITY: | 1.50 | |||||||||||||
| INTENDED USE: CSST SIZING BETWEEN 2 PSI SERVICE AND LINE PRESSURE REGULATOR | ||||||||||||||
| TUBE SIZE (EHD)5 | ||||||||||||||
| FLOW DESIGNATION : | 13 | 15 | 18 | 19 | 23 | 25 | 30 | 31 | 37 | 39 | 46 | 48 | 60 | 62 |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | |||||||||||||
| 10 | 426 | 558 | 927 | 1110 | 1740 | 2170 | 4100 | 4720 | 7130 | 7958 | 15 200 | 16 800 | 29 400 | 34 200 |
| 25 | 262 | 347 | 591 | 701 | 1120 | 1380 | 2560 | 2950 | 4560 | 5147 | 9550 | 10 700 | 18 800 | 21 700 |
| 30 | 238 | 316 | 540 | 640 | 1030 | 1270 | 2330 | 2690 | 4180 | 4719 | 8710 | 9790 | 17 200 | 19 800 |
| 40 | 203 | 271 | 469 | 554 | 896 | 1100 | 2010 | 2320 | 3630 | 4116 | 7530 | 8500 | 14 900 | 17 200 |
| 50 | 181 | 243 | 420 | 496 | 806 | 986 | 1790 | 2070 | 3260 | 3702 | 6730 | 7610 | 13 400 | 15 400 |
| 75 | 147 | 196 | 344 | 406 | 663 | 809 | 1460 | 1690 | 2680 | 3053 | 5480 | 6230 | 11 000 | 12 600 |
| 80 | 140 | 189 | 333 | 393 | 643 | 768 | 1410 | 1630 | 2590 | 2961 | 5300 | 6040 | 10 600 | 12 200 |
| 100 | 124 | 169 | 298 | 350 | 578 | 703 | 1260 | 1450 | 2330 | 2662 | 4740 | 5410 | 9530 | 10 900 |
| 150 | 101 | 137 | 245 | 287 | 477 | 575 | 1020 | 1180 | 1910 | 2195 | 3860 | 4430 | 7810 | 8890 |
| 200 | 86 | 118 | 213 | 248 | 415 | 501 | 880 | 1020 | 1660 | 1915 | 3340 | 3840 | 6780 | 7710 |
| 250 | 77 | 105 | 191 | 222 | 373 | 448 | 785 | 910 | 1490 | 1722 | 2980 | 3440 | 6080 | 6900 |
| 300 | 69 | 96 | 173 | 203 | 343 | 411 | 716 | 829 | 1360 | 1578 | 2720 | 3150 | 5560 | 6300 |
| 400 | 60 | 82 | 151 | 175 | 298 | 355 | 616 | 716 | 1160 | 1376 | 2350 | 2730 | 4830 | 5460 |
| 500 | 53 | 72 | 135 | 158 | 268 | 319 | 550 | 638 | 1030 | 1237 | 2100 | 2450 | 4330 | 4880 |
- 1 Table does not include effect of pressure drop across the line regulator. Where regulator loss exceeds 0.5 psi (3.4 kPa) [based on 13 inch water column (3.2 kPa) outlet pressure], DO NOT USE THIS TABLE. Consult with regulator manufacturer for pressure drops and capacity factors. Pressure drops across a regulator are capable of varying with flow rate.
- 2 CAUTION: Capacities shown in table are capable of exceeding the maximum capacity for a selected regulator. Consult with regulator or tubing manufacturer for guidance.
- 3 Table includes losses for four 90 degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.3 n, where Lis additional length (ft) of tubing and n is the number of additional fittings, bends, or both
- 4 Table entries are rounded to 3 significant digits.
- 5 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.
| GAS: | UNDILUTED PROPANE | |||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 5.0 psi | |||||||||||||
| PRESSURE DROP: | 3.5 psi | |||||||||||||
| SPECIFIC GRAVITY: | 1.50 | |||||||||||||
| TUBE SIZE (EHD)5 | ||||||||||||||
| FLOW DESIGNATION : | 13 | 15 | 18 | 19 | 23 | 25 | 30 | 31 | 37 | 39 | 46 | 48 | 60 | 62 |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | |||||||||||||
| 10 | 826 | 1070 | 1710 | 2060 | 3150 | 4000 | 7830 | 8950 | 13 100 | 14 441 | 28 600 | 31 200 | 54 400 | 63 800 |
| 25 | 509 | 664 | 1090 | 1310 | 2040 | 2550 | 4860 | 5600 | 8400 | 9339 | 18 000 | 19 900 | 34 700 | 40 400 |
| 30 | 461 | 603 | 999 | 1190 | 1870 | 2340 | 4430 | 5100 | 7680 | 8564 | 16 400 | 18 200 | 31 700 | 36 900 |
| 40 | 396 | 520 | 867 | 1030 | 1630 | 2030 | 3820 | 4400 | 6680 | 7469 | 14 200 | 15 800 | 27 600 | 32 000 |
| 50 | 352 | 463 | 777 | 926 | 1460 | 1820 | 3410 | 3930 | 5990 | 6717 | 12 700 | 14 100 | 24 700 | 28 600 |
| 75 | 284 | 376 | 637 | 757 | 1210 | 1490 | 2770 | 3190 | 4920 | 5539 | 10 300 | 11 600 | 20 300 | 23 400 |
| 80 | 275 | 363 | 618 | 731 | 1170 | 1450 | 2680 | 3090 | 4770 | 5372 | 9990 | 11 200 | 19 600 | 22 700 |
| 100 | 243 | 324 | 553 | 656 | 1050 | 1300 | 2390 | 2760 | 4280 | 4830 | 8930 | 1 0000 | 17 600 | 20 300 |
| 150 | 196 | 262 | 453 | 535 | 866 | 1060 | 1940 | 2240 | 3510 | 3983 | 7270 | 8210 | 14 400 | 16 600 |
| 200 | 169 | 226 | 393 | 464 | 755 | 923 | 1680 | 1930 | 3050 | 3474 | 6290 | 7130 | 12 500 | 14 400 |
| 250 | 150 | 202 | 352 | 415 | 679 | 828 | 1490 | 1730 | 2740 | 3124 | 5620 | 6390 | 11 200 | 12 900 |
| 300 | 136 | 183 | 322 | 379 | 622 | 757 | 1360 | 1570 | 2510 | 2865 | 5120 | 5840 | 10 300 | 11 700 |
| 400 | 117 | 158 | 279 | 328 | 542 | 657 | 1170 | 1360 | 2180 | 2498 | 4430 | 5070 | 8920 | 10 200 |
| 500 | 104 | 140 | 251 | 294 | 488 | 589 | 1050 | 1210 | 1950 | 2247 | 3960 | 4540 | 8000 | 9110 |
- 1 Table does not include effect of pressure drop across the line regulator. Where regulator loss exceeds 0.5 psi (3.4 kPa) [based on 13 inch water column (3.2 kPa) outlet pressure], DO NOT USE THIS TABLE. Consult with regulator manufacturer for pressure drops and capacity factors. Pressure drops across a regulator are capable of varying with flow rate.
- 2 CAUTION: Capacities shown in table are capable of exceeding the maximum capacity for a selected regulator. Consult with regulator or tubing manufacturer for guidance.
- 3 Table includes losses for four 90 degree (1.57 rad) bends and two end fittings. Tubing runs with larger numbers of bends, fittings, or both shall be increased by an equivalent length of tubing to the following equation: L = 1.3 n, where Lis additional length (ft) of tubing and n is the number of additional fittings, bends, or both
- 4 Table entries are rounded to 3 significant digits.
- 5 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.
| GAS: | UNDILUTED PROPANE | |||||||
|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 11.0 in. w.c. | |||||||
| PRESSURE DROP: | 0.5 in. w.c. | |||||||
| SPECIFIC GRAVITY: | 1.50 | |||||||
| INTENDED USE: PE SIZING BETWEEN INTEGRAL SECOND-STAGE REGULATOR AT TANK OR SECOND-STAGE (LOW PRESSURE) REGULATOR AND BUILDING | ||||||||
| PIPE SIZE (inch) | ||||||||
| NOMINAL OD: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 3 | 4 |
| DESIGNATION: | SDR 9.3 | SDR 11 | SDR 11 | SDR 10 | SDR 11 | SDR 11 | SDR 11 | SDR 11 |
| ACTUAL ID: | 0.660 | 0.860 | 1.077 | 1.328 | 1.554 | 1.943 | 2.864 | 3.682 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||
| 10 | 340 | 680 | 1230 | 2130 | 3210 | 5770 | 16 000 | 30 900 |
| 20 | 233 | 468 | 844 | 1460 | 2210 | 3970 | 11 000 | 21 200 |
| 30 | 187 | 375 | 677 | 1170 | 1770 | 3180 | 8810 | 17 000 |
| 40 | 160 | 321 | 580 | 1000 | 1520 | 2730 | 7540 | 14 600 |
| 50 | 142 | 285 | 514 | 890 | 1340 | 2420 | 6680 | 12 900 |
| 60 | 129 | 258 | 466 | 807 | 1220 | 2190 | 6050 | 11 700 |
| 70 | 119 | 237 | 428 | 742 | 1120 | 2010 | 5570 | 10 800 |
| 80 | 110 | 221 | 398 | 690 | 1040 | 1870 | 5180 | 10 000 |
| 90 | 103 | 207 | 374 | 648 | 978 | 1760 | 4860 | 9400 |
| 100 | 98 | 196 | 353 | 612 | 924 | 1660 | 4590 | 8900 |
| 125 | 87 | 173 | 313 | 542 | 819 | 1470 | 4070 | 7900 |
| 150 | 78 | 157 | 284 | 491 | 742 | 1330 | 3690 | 7130 |
| 175 | 72 | 145 | 261 | 452 | 683 | 1230 | 3390 | 6560 |
| 200 | 67 | 135 | 243 | 420 | 635 | 1140 | 3160 | 6100 |
| 250 | 60 | 119 | 215 | 373 | 563 | 1010 | 2800 | 5410 |
| 300 | 54 | 108 | 195 | 338 | 510 | 916 | 2530 | 4900 |
| 350 | 50 | 99 | 179 | 311 | 469 | 843 | 2330 | 4510 |
| 400 | 46 | 92 | 167 | 289 | 436 | 784 | 2170 | 4190 |
| 450 | 43 | 87 | 157 | 271 | 409 | 736 | 2040 | 3930 |
| 500 | 41 | 82 | 148 | 256 | 387 | 695 | 1920 | 3720 |
* Table entries are rounded to 3 significant digits.
| GAS: | UNDILUTED PROPANE | |||||||
|---|---|---|---|---|---|---|---|---|
| INLET PRESSURE: | 2.0 psi | |||||||
| PRESSURE DROP: | 1.0 psi | |||||||
| SPECIFIC GRAVITY: | 1.50 | |||||||
| INTENDED USE: PE PIPE SIZING BETWEEN 2 PSI SERVICE REGULATOR AND LINE PRESSURE REGULATOR | ||||||||
| PIPE SIZE (inch) | ||||||||
| NOMINAL OD: | 1/2 | 3/4 | 1 | 11/4 | 11/2 | 2 | 3 | 4 |
| DESIGNATION: | SDR 9.3 | SDR 11 | SDR 11 | SDR 10 | SDR 11 | SDR 11 | SDR 11 | SDR 11 |
| ACTUAL ID: | 0.660 | 0.860 | 1.077 | 1.328 | 1.554 | 1.943 | 2.864 | 3.682 |
| LENGTH (feet) | CAPACITY IN CUBIC FEET OF GAS PER HOUR | |||||||
| 10 | 3130 | 6260 | 11 300 | 19 600 | 29 500 | 53 100 | 147 000 | 284 000 |
| 20 | 2150 | 4300 | 7760 | 13 400 | 20 300 | 36 500 | 101 000 | 195 000 |
| 30 | 1730 | 3450 | 6230 | 10 800 | 16 300 | 29 300 | 81 100 | 157 000 |
| 40 | 1480 | 2960 | 5330 | 9240 | 14 000 | 25 100 | 69 400 | 134 100 |
| 50 | 1310 | 2620 | 4730 | 8190 | 12 400 | 22 200 | 61 500 | 119 000 |
| 60 | 1190 | 2370 | 4280 | 7420 | 11 200 | 20 100 | 55 700 | 108 000 |
| 70 | 1090 | 2180 | 3940 | 6830 | 10 300 | 18 500 | 51 300 | 99 100 |
| 80 | 1010 | 2030 | 3670 | 6350 | 9590 | 17 200 | 47 700 | 92 200 |
| 90 | 952 | 1910 | 3440 | 5960 | 9000 | 16 200 | 44 700 | 86 500 |
| 100 | 899 | 1800 | 3250 | 5630 | 8500 | 15 300 | 42 300 | 81 700 |
| 125 | 797 | 1600 | 2880 | 4990 | 7530 | 13 500 | 37 500 | 72 400 |
| 150 | 722 | 1450 | 2610 | 4520 | 6830 | 12 300 | 33 900 | 65 600 |
| 175 | 664 | 1330 | 2400 | 4160 | 6280 | 11 300 | 31 200 | 60 300 |
| 200 | 618 | 1240 | 2230 | 3870 | 5840 | 10 500 | 29 000 | 56 100 |
| 250 | 548 | 1100 | 1980 | 3430 | 5180 | 9300 | 25 700 | 49 800 |
| 300 | 496 | 994 | 1790 | 3110 | 4690 | 8430 | 23 300 | 45 100 |
| 350 | 457 | 914 | 1650 | 2860 | 4320 | 7760 | 21 500 | 41 500 |
| 400 | 425 | 851 | 1530 | 2660 | 4020 | 7220 | 12 000 | 38 600 |
| 450 | 399 | 798 | 1440 | 2500 | 3770 | 6770 | 18 700 | 36 200 |
| 500 | 377 | 754 | 1360 | 2360 | 3560 | 6390 | 17 700 | 34 200 |
| 550 | 358 | 716 | 1290 | 2240 | 3380 | 6070 | 16 800 | 32 500 |
| 600 | 341 | 683 | 1230 | 2140 | 3220 | 5790 | 16 000 | 31 000 |
| 650 | 327 | 654 | 1180 | 2040 | 3090 | 5550 | 15 400 | 29 700 |
| 700 | 314 | 628 | 1130 | 1960 | 2970 | 5330 | 14 700 | 28 500 |
| 750 | 302 | 605 | 1090 | 1890 | 2860 | 5140 | 14 200 | 27 500 |
| 800 | 292 | 585 | 1050 | 1830 | 2760 | 4960 | 13 700 | 26 500 |
| 850 | 283 | 566 | 1020 | 1770 | 2670 | 4800 | 13 300 | 25 700 |
| 900 | 274 | 549 | 990 | 1710 | 2590 | 4650 | 12 900 | 24 900 |
| 950 | 266 | 533 | 961 | 1670 | 2520 | 4520 | 12 500 | 24 200 |
| 1000 | 259 | 518 | 935 | 1620 | 2450 | 4400 | 12 200 | 23 500 |
| 1100 | 246 | 492 | 888 | 1540 | 2320 | 4170 | 11 500 | 22 300 |
| 1200 | 234 | 470 | 847 | 1470 | 2220 | 3980 | 11 000 | 21 300 |
| 1300 | 225 | 450 | 811 | 1410 | 2120 | 3810 | 10 600 | 20 400 |
| 1400 | 216 | 432 | 779 | 1350 | 2040 | 3660 | 10 100 | 19 600 |
| 1500 | 208 | 416 | 751 | 1300 | 1960 | 3530 | 9760 | 18 900 |
| 1600 | 201 | 402 | 725 | 1260 | 1900 | 3410 | 9430 | 18 200 |
| 1700 | 194 | 389 | 702 | 1220 | 1840 | 3300 | 9130 | 17 600 |
| 1800 | 188 | 377 | 680 | 1180 | 1780 | 3200 | 8850 | 17 100 |
| 1900 | 183 | 366 | 661 | 1140 | 1730 | 3110 | 8590 | 16 600 |
| 2000 | 178 | 356 | 643 | 1110 | 1680 | 3020 | 8360 | 16 200 |
* Table entries are rounded to 3 significant digits.
| GAS: | UNDILUTED PROPANE | |
|---|---|---|
| INLET PRESSURE: | 11.0 in. w.c. | |
| PRESSURE DROP: | 0.5 in.w.c. | |
| SPECIFIC GRAVITY: | 1.50 | |
| INTENDED USE: PE TUBE SIZING BETWEEN INTEGRAL SECOND-STAGE REGULATOR AT TANK OR SECOND-STAGE (LOW PRESSURE) REGULATOR AND BUILDING |
||
| PLASTIC TUBING SIZE (CTS)1 (inch) | ||
| NOMINAL OD: | 1/2 | 1 |
| DESIGNATION: | SDR 7 | SDR 11 |
| ACTUAL ID: | 0.445 | 0.927 |
| LENGTH (feet) | CAPACITY IN THOUSANDS OF BTU PER HOUR | |
| 10 | 121 | 828 |
| 20 | 83 | 569 |
| 30 | 67 | 457 |
| 40 | 57 | 391 |
| 50 | 51 | 347 |
| 60 | 46 | 314 |
| 70 | 42 | 289 |
| 80 | 39 | 269 |
| 90 | 37 | 252 |
| 100 | 35 | 238 |
| 125 | 31 | 211 |
| 150 | 28 | 191 |
| 175 | 26 | 176 |
| 200 | 24 | 164 |
| 225 | 22 | 154 |
| 250 | 21 | 145 |
| 275 | 20 | 138 |
| 300 | 19 | 132 |
| 350 | 18 | 121 |
| 400 | 16 | 113 |
| 450 | 15 | 106 |
| 500 | 15 | 100 |
- 1 CTS = Copper tube size
- 2 Table entries are rounded to 3 significant digits.
The inside diameter of smooth-wall pipe or tubing shall be determined by Equation 1215.3(1), Equation 1215.3(2), Table 1215.3 and using the
equivalent pipe length determined by the methods in Section 1215.1.1 through Section 1215.1.3. [NFPA 54:6.4]
EQUATION 1215.3(1)
LOW-PRESSURE GAS FORMULA (LESS THAN 1.5 psi)
[NFPA 54:6.4.1]
EQUATION 1215.3(2)
HIGH-PRESSURE GAS FORMULA (1.5 psi AND ABOVE)
[NFPA 54:6.4.2]
LOW-PRESSURE GAS FORMULA (LESS THAN 1.5 psi)
[NFPA 54:6.4.1]
Where:
- D = inside diameter of pipe, inches
- Q = input rate appliance(s), cubic feet per hour at 60°F and 30 inch mercury column
- L = equivalent length of pipe, feet
- ΔH = pressure drop, inches water column
- Cr = in accordance with Table 1215.3
HIGH-PRESSURE GAS FORMULA (1.5 psi AND ABOVE)
[NFPA 54:6.4.2]
Where:
- D = inside diameter of pipe, inches
- Q = input rate appliance(s), cubic feet per hour at 60°F and 30 inch mercury column
- P1 = upstream pressure, psia (P1 + 14.7)
- P2 = downstream pressure, psia (P2 + 14.7)
- L = equivalent length of pipe, feet
- Cr = in accordance with Table 1215.3
- Y = in accordance with Table 1215.3
| GAS | FORMULA FACTORS | |
|---|---|---|
| Cr | Y | |
| Natural Gas | 0.6094 | 0.9992 |
| Undiluted Propane | 1.2462 | 0.9910 |
To determine the size of each section of pipe in a system within the range of Table 1215.2(1) through Table 1215.2(36), proceed as follows:
- Measure the length of the pipe from the gas meter location to the most remote outlet on the system.
- Select the length in feet column and row showing the distance, or the next longer distance where the table does not give the exact length.
- Starting at the most remote outlet, find in the row just selected the gas demand for that outlet. Where the exact figure of demand is not shown ,choose the next larger figure in the row.
- At the top of this column will be found the correct size of pipe.
- Using this same row, proceed in a similar manner to 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, the larger of the two demand loads needs to be used in sizing these sections.
- 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 2, 3, 4, and 5 above. Size branch piping in the order of their distance from the meter location, beginning with the most distant outlet not previously sized.
For conditions other than those covered by Section 1215.1, 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 another point of supply and an outlet where full demand is being supplied to all outlets, shall be in accordance with the requirements of Section 1208.4.
Where the supply gas pressure exceeds 5 psi (34.6 kPa) for natural gas and 10 psi (69 kPa) for undiluted propane or is less than 6 inches (1.5 kPa) of water column, or 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.
For purposes of this section, certain terms shall be defined as follows:
Downstream of the Gas Utility Meter shall refer to all customer owned gas piping, downstream of the bypass valve, as specified by the public gas utility company.
Excess Flow Shutoff Valve shall mean a shutoff system activated by significant gas leaks or overpressure surges downstream of the valves.
Residential Building shall mean any single-family dwelling, duplex, apartment building, condominium, townhouse, lodging house, congregate residence, hotel or motel.
Seismic Gas Shutoff Valve shall mean a system consisting of a seismic sensing means and actuating means designed to automatically actuate a companion gas shutoff means installed in a gas piping system in order to shutoff the gas downstream of the location of the gas shutoff means in the event of a severe seismic disturbance. The system may consist of separable components or may incorporate all functions in a single body. The terms "Seismically Activated Gas Shutoff Valves" and "Earthquake Sensitive Gas Shutoff Valves" are synonymous.
Upstream of the Gas Utility Meter shall refer to all gas piping installed by the utility up to and including the meter and the utility's bypass tee at the connection to the customer owned piping.
Downstream of the Gas Utility Meter shall refer to all customer owned gas piping, downstream of the bypass valve, as specified by the public gas utility company.
Excess Flow Shutoff Valve shall mean a shutoff system activated by significant gas leaks or overpressure surges downstream of the valves.
Residential Building shall mean any single-family dwelling, duplex, apartment building, condominium, townhouse, lodging house, congregate residence, hotel or motel.
Seismic Gas Shutoff Valve shall mean a system consisting of a seismic sensing means and actuating means designed to automatically actuate a companion gas shutoff means installed in a gas piping system in order to shutoff the gas downstream of the location of the gas shutoff means in the event of a severe seismic disturbance. The system may consist of separable components or may incorporate all functions in a single body. The terms "Seismically Activated Gas Shutoff Valves" and "Earthquake Sensitive Gas Shutoff Valves" are synonymous.
Upstream of the Gas Utility Meter shall refer to all gas piping installed by the utility up to and including the meter and the utility's bypass tee at the connection to the customer owned piping.
An approved seismic gas shutoff valve or excess flow shutoff valve shall be installed downstream of the gas utility meter on each fuel gas line where the gas line serves the following buildings or structures:
A building or structure containing fuel gas piping for which a building permit was first issued on or after September 1, 1995.
An existing building or structure which is altered or added to; and
That building or structure has fuel gas piping supplying the existing building or structure or the addition to the building or structure; and
The alteration or addition is valued at more than $10,000 and a building permit for the work in commercial buildings was first issued on or after September 1, 1995. Alterations or additions to individual units or tenant spaces shall require a seismic gas shutoff valve or excess flow shutoff valve to be installed for all gas piping serving that individual unit or tenant space; or
The alteration or addition is valued at more than $10,000 and a building permit for the work in residential buildings, including condominium units, is first issued on or after January 10, 1998. Alterations or additions to an individual condominium unit shall require a seismic gas shutoff valve or excess flow shutoff valve to be installed for all gas piping serving that individual condominium unit; or
The alteration or addition is to the fuel gas piping system and involves the alteration or replacement of the gas meter.
Prior to entering into an agreement of sale, or prior to the close of escrow when an escrow agreement has been executed in connection with the sale,
- Buildings or structures which contain fuel gas piping shall have a seismic gas shutoff valve or excess flow shutoff valve installed.
- The sale of an individual condominium unit in a building shall require the installation of a seismic gas shutoff valve or excess flow shutoff valve for all gas piping serving that individual unit.
EXCEPTIONS:
- Seismic gas shutoff valves or excess flow shutoff valve may be installed upstream of a gas utility meter provided they meet the requirements of this section.
- Seismic gas shutoff valves or excess flow shutoff valve installed on a building or structure prior to September 1, 1995, are exempt from the requirements of this section provided they remain installed on the building or structure and are maintained for the life of the building or structure.
- Notwithstanding LAMC Subdivisions 94.1217.2.1, 94.1217.2.2 and 94.1217.2.3 above, these provisions shall not apply to a building or structure if the Department determines that a building or structure satisfies all three of the following criteria:
- That the building or structure is owned, operated, and maintained by a governmental entity or public utility; or that the building or structure is owned by a private concern and provides a public benefit, such as a co-generation facility which shares its excess power with a public utility or with a large industrial facility which has governmental contracts;
- That the building or structure has available 24-hour, year round maintenance staffing; and
- That the gas piping system contained in the building or structure is designed to withstand seismic effects of earthquakes.
- A single seismic gas shutoff valve or excess flow shutoff valve may be installed upstream of the gas utility meter at the discretion of the gas utility.
Seismic gas shutoff valves or excess flow shutoff valves installed either in compliance with LAMC Subsection 94.1217.2, et seq., or voluntarily with a permit issued on or after September 1, 1995, shall comply with the following requirements:
Seismic gas shutoff valves or excess flow shutoff valve shall be installed by a contractor licensed in the appropriate classification by the State of California.
EXCEPTIONS:
- A person who has been determined by the Department to meet the qualifications of a Qualified Installer pursuant to the definition of a Qualified Installer set forth in Article 4, Chapter IX of the LAMC may install a seismic gas shutoff valve or excess flow shutoff valve to a single-family dwelling which is or is intended to be occupied by the Qualified Installer.
- Seismic gas shutoff valves or excess flow shutoff valve may be installed, without a permit, by a gas utility or a contractor authorized by the gas utility when the valves are installed upstream of the gas utility meter and the valves are installed and approved in accordance with this section.
Seismic gas shutoff valves or excess flow shutoff valve shall be mounted rigidly to the exterior, or other approved location, of the building or structure containing the fuel gas piping.
EXCEPTION:
If the Department determines that the seismic gas shutoff valve or excess flow shutoff valve has been tested and listed for an alternate method of installation, then a seismic gas shutoff valve or excess flow shutoff valve need not be mounted rigidly to the exterior of the building or structure containing the fuel gas piping.
Be certified by the Office of the State Architect.
Be approved by the Department of Building and Safety, Mechanical Testing Laboratory.
Have a thirty (30) year warranty which warrants that the valve is free from defects and will continue to properly operate for thirty (30) years from the date of installation.
Where seismic gas shutoff valves or excess flow shutoff valve are installed as required by this section, they shall be maintained for the life of the building or structure or be replaced with a valve complying with the requirements of this section.
Seismic gas shutoff valves must be in compliance with all requirements of California Referenced Standard 12-16-1, at Part 12, Title 24, of the California Code of Regulations (CCR).
Excess flow shutoff valves must be in compliance with all requirements of California Referenced Standard 12-16-2. (Part 12, Title 24, of the CCR).
