Exact-length selector
Size Low-Pressure Schedule 40 Propane Pipe
IFGC 2024 Equation 4-1 · first unrounded capacity that meets the load
At the default 200,000 Btu/h and 50 ft equivalent length, the first qualifying listed size is NPS 3/4 (DN20). With JavaScript enabled, change the inputs to calculate an exact-length preliminary selection.
Safety and scope limit
This preliminary calculation applies only to undiluted propane vapor in the listed Schedule 40 metallic-pipe IDs, downstream of a single- or second-stage low-pressure regulator, on the stated 11.0 in. w.c. inlet and 0.5 in. w.c. drop basis. Verify the adopted code, permitted sizing method, simultaneous loads, available pressure, appliance requirements, equivalent length, regulator capacity, container vaporization, material approval, installation details, and authority having jurisdiction. Propane systems must be installed by qualified personnel.
Calculated reference matrix
Calculated Propane Capacity by Pipe Size and Equivalent Length
Maximum calculated energy capacity in MBH
Read across the equivalent-length row. The first pipe column whose unrounded capacity equals or exceeds the connected load qualifies under this page’s fixed basis. The live “Current input” row uses the exact entered length.
No Schedule 40 size from NPS 1/2 through 4 qualifies within this page’s verified scope. Use the adopted fuel-gas code and a qualified propane professional; do not extrapolate this chart.
Scroll horizontally to view additional pipe sizes and vertically to view additional lengths. Column headers and the equivalent-length column remain visible while scrolling.
| Maximum calculated propane capacity, MBH | |||||||||
|---|---|---|---|---|---|---|---|---|---|
| NPS 1/2 DN15 · ID 0.622 in |
NPS 3/4 DN20 · ID 0.824 in |
NPS 1 DN25 · ID 1.049 in |
NPS 1-1/4 DN32 · ID 1.380 in |
NPS 1-1/2 DN40 · ID 1.610 in |
NPS 2 DN50 · ID 2.067 in |
NPS 2-1/2 DN65 · ID 2.469 in |
NPS 3 DN80 · ID 3.068 in |
NPS 4 DN100 · ID 4.026 in |
|
| 10 ft (3.05 m) | 292 | 612 | 1,150 | 2,370 | 3,550 | 6,840 | 10,900 | 19,300 | 39,300 |
| 20 ft (6.10 m) | 201 | 420 | 792 | 1,630 | 2,440 | 4,700 | 7,490 | 13,300 | 27,000 |
| 30 ft (9.14 m) | 161 | 338 | 636 | 1,310 | 1,960 | 3,770 | 6,020 | 10,600 | 21,700 |
| 40 ft (12.19 m) | 138 | 289 | 545 | 1,120 | 1,680 | 3,230 | 5,150 | 9,110 | 18,600 |
| 50 ft (15.24 m) | 122 | 256 | 483 | 992 | 1,490 | 2,860 | 4,570 | 8,070 | 16,500 |
| 60 ft (18.29 m) | 111 | 232 | 438 | 899 | 1,350 | 2,590 | 4,140 | 7,320 | 14,900 |
| 75 ft (22.86 m) | 98.4 | 206 | 388 | 797 | 1,190 | 2,300 | 3,670 | 6,480 | 13,200 |
| 100 ft (30.48 m) | 84.2 | 176 | 332 | 682 | 1,020 | 1,970 | 3,140 | 5,550 | 11,300 |
| 125 ft (38.10 m) | 74.6 | 156 | 294 | 604 | 906 | 1,740 | 2,780 | 4,920 | 10,000 |
| 150 ft (45.72 m) | 67.6 | 141 | 267 | 548 | 821 | 1,580 | 2,520 | 4,460 | 9,100 |
| 200 ft (60.96 m) | 57.9 | 121 | 228 | 469 | 702 | 1,350 | 2,160 | 3,820 | 7,790 |
| 250 ft (76.20 m) | 51.3 | 107 | 202 | 415 | 623 | 1,200 | 1,910 | 3,380 | 6,900 |
| 300 ft (91.44 m) | 46.5 | 97.2 | 183 | 376 | 564 | 1,090 | 1,730 | 3,060 | 6,250 |
| 400 ft (121.92 m) | 39.8 | 83.2 | 157 | 322 | 483 | 930 | 1,480 | 2,620 | 5,350 |
| 500 ft (152.40 m) | 35.3 | 73.8 | 139 | 286 | 428 | 825 | 1,310 | 2,320 | 4,740 |
| Current input: 50 ft | 122 | 256 · selected | 483 | 992 | 1,490 | 2,860 | 4,570 | 8,070 | 16,500 |
Calculated values are not a reproduction of an ICC, NFPA, ASME, PERC, or manufacturer table. They do not establish regulator, container, appliance, material, installation, or jurisdictional compliance. Bulk CSV export is intentionally disabled.
How to Use the Propane Pipe Sizing Chart
- Total the connected input. Use appliance nameplate input ratings, not delivered heat output. Determine which appliances can operate simultaneously on the segment being sized.
- Establish the permitted length method. Enter the applicable equivalent length from the adopted code or approved design procedure, including fittings when that method requires them.
- Confirm the fixed pressure basis. This page assumes an 11.0 in. w.c. inlet reference and 0.5 in. w.c. allowable drop. It does not infer available pressure at the project.
- Read the first qualifying size. The calculator compares unrounded capacities, so displayed rounding never decides the nominal pipe selection.
- Verify the rest of the propane system. Check regulators, container vaporization, appliance requirements, approved materials, installation rules, local amendments, and the authority having jurisdiction.
Low-Pressure Propane Scope and Safety Limits
| Covered by this page | Requires another verified method |
|---|---|
| Undiluted propane vapor downstream of a single- or second-stage low-pressure regulator | Tank-to-first-stage piping, liquid propane, or elevated-pressure distribution |
| Fixed 0.5 in. w.c. pressure-drop calculation with the stated 11.0 in. w.c. inlet reference | 2 psi, 5 psi, 10 psi, or another inlet/drop basis |
| Limited Schedule 40 metallic-pipe IDs from NPS 1/2 through NPS 4 | Copper tubing, CSST, PE, appliance connectors, or another schedule/material system |
| Preliminary capacity and first-qualifying nominal-size comparison | Regulator selection, container vaporization, combustion-air design, joining approval, or complete network approval |
Natural-gas results are not interchangeable with propane results. The gases have different equation factors, heating values, operating arrangements, and applicable sizing tables.
Equation, Variables, and Length Methods
The page calculates propane flow from connected input and heating value, solves IFGC Equation 4-1 for required inside diameter, and then checks the limited actual-ID set from smallest to largest:
Q = H ÷ Hv
D = Q0.381 ÷ [19.17 × (ΔH ÷ (CrL))0.206]
- QPropane flow in standard cubic feet per hour, referenced at 60°F and 30 in. Hg
- HConnected appliance input in Btu/h
- HvPropane heating value; default 2,488 Btu/ft³
- DRequired pipe inside diameter in inches
- LApplicable equivalent piping length in feet
- ΔHAllowable pressure drop, fixed here at 0.5 in. w.c.
- CrIFGC undiluted-propane equation factor, 1.2462
Longest-length, branch-length, and equivalent length
The longest-length method commonly sizes applicable segments using the developed length to the most remote outlet. A branch-length method can use segment-specific lengths when permitted. Equivalent-length procedures account for fittings by an approved method. This page asks for the resulting applicable length; it cannot decide which method the adopted code or authority permits for a project.
Worked Propane Pipe Sizing Examples
Example 1: 200,000 Btu/h at 50 ft
Assume undiluted propane, 2,488 Btu/ft³, 50 ft applicable equivalent length, and 0.5 in. w.c. allowable drop. The load is 80.39 SCFH. Equation 4-1 gives a required ID of about 0.750 in. NPS 1/2, with a 0.622 in ID, calculates to about 122 MBH and is short by about 77.5 MBH. NPS 3/4, with a 0.824 in ID, calculates to about 256 MBH and is the first listed size that qualifies.
Example 2: 400,000 Btu/h at 100 ft
Using the same fuel and pressure-drop basis, the load is about 160.77 SCFH and the required ID is about 1.126 in. NPS 1 calculates to about 332 MBH and does not qualify. NPS 1-1/4 calculates to about 682 MBH and is the first qualifying listed size. Both examples remain preliminary because regulator behavior, container vaporization, adopted sizing method, and appliance pressure requirements are separate checks.
Propane Pipe Sizing Mistakes That Cause Bad Results
- Using appliance output instead of input: fuel piping is based on the maximum input rating.
- Omitting simultaneous loads: each segment must carry the applicable connected demand downstream.
- Entering straight-line distance: use the developed or equivalent length required by the permitted sizing method.
- Using a natural-gas chart: its fuel factor and heat-content basis do not transfer to propane.
- Treating NPS as actual ID: the equation uses actual inside diameter, not the nominal designation.
- Assuming 0.5 in. w.c. is always available: confirm supply pressure, regulator performance, appliance minimum pressure, and permissible drop.
- Ignoring the container and regulator: adequate pipe capacity does not prove adequate vaporization or regulator capacity.
Schedule 40, Copper, CSST, PE, and Elevated-Pressure Systems
Material systems use different dimensions, installation rules, and sometimes manufacturer-specific sizing methods. Do not convert this result by matching nominal labels.
- Schedule 40 metallic pipe: use this page only when the stated fuel, pressure, size, and length scope all apply.
- Copper tubing: verify that copper is permitted and use the applicable tubing dimensions, code provisions, and joining requirements.
- CSST: use the exact manufacturer’s current sizing tables and equivalent hydraulic diameter system.
- Underground PE: use approved PE dimensions, pressure basis, joining rules, tracer requirements, and adopted code provisions.
- First-stage or elevated pressure: use the applicable pressure-specific method and complete the required downstream pressure-reduction checks.
Sources, Edition, Calculation Scope, and Data Rights
Original equation-generated capacities for low-pressure undiluted propane; no complete standards or manufacturer table is reproduced.
The calculator and matrix use a limited set of source-controlled constants and pipe IDs to create original calculated values. The adopted local code and authority having jurisdiction control actual design and installation.
- International Code Council — 2024 IFGC, Chapter 4Section 402.4, Equation 4-1, propane factor 1.2462, reference conditions, and low-pressure equation scope.
- Propane Education & Research Council — Propane Technical Pocket GuideApproximate propane properties, 2,488 Btu/ft³ default heat content, total-load method, and professional-safety context.
- ICC CodeNotes — Fuel Gas Pipe SizingLongest-length and branch-length method context; published September 15, 2023.
- ASME B36.10-2022 — Welded and Seamless Wrought Steel PipeLimited Schedule 40 NPS/DN and nominal inside-diameter inputs from NPS 1/2 through 4.
Dataset and Source-Check Details
- Dataset
- LP-SCH40-IFGC2024-EQ4-1-v1.0
- Publisher
- Turn2Engineering
- Source checked
- August 9, 2026
- Calculated range
- 10–500 ft; NPS 1/2–4; 0.5 in. w.c. drop
- Reference conditions
- SCFH at 60°F and 30 in. Hg; undiluted propane
- Rights decision
- Limited factual inputs and original calculations; full CSV disabled
- Excluded systems
- Elevated pressure, copper, CSST, PE, regulators, and container vaporization
- Display precision
- Capacity about 3 significant figures; selection uses unrounded values
Related Engineering Resources
Propane Pipe Sizing FAQs
Length and pressure basis control the answer. Under this page’s defaults—50 ft equivalent length, 0.5 in. w.c. allowable drop, and 2,488 Btu/ft³—NPS 3/4 is the first qualifying listed Schedule 40 size.
No. Fuel properties, heat content, equation factors, regulator arrangements, operating pressures, and applicable tables differ. Do not transfer a natural-gas result to propane.
Use the developed-length or equivalent-length procedure required by the adopted code or approved sizing method. There is no universal fitting percentage that this page can apply safely.
No. Those systems require their own verified dimensions, code provisions, joining requirements, pressure bases, or manufacturer sizing data.
No. Regulator capacity and pressure behavior, container vaporization, ambient temperature, fill level, and appliance requirements are separate system checks.
Propane Pipe Sizing Summary
- Use maximum appliance input and the applicable simultaneous load.
- Determine length using the sizing method permitted by the adopted code.
- Confirm that the low-pressure propane and 0.5 in. w.c. drop basis apply.
- Use the first listed actual ID whose unrounded calculated capacity meets the load.
- Separately verify regulator capacity, container vaporization, materials, joining, and appliance pressure.
- Have qualified personnel confirm the final design and installation with the authority having jurisdiction.