AS/NZS 5601.1:2022 Compliant — Last Updated: 8 August 2026
LPG (liquefied petroleum gas / propane) and natural gas (methane) are physically different fuels with distinct thermodynamic properties. If you are converting a venue from reticulated gas to bottled gas or vice versa, you cannot rely on natural gas sizing tables. Instead, cross-reference with our Natural Gas Pipe Sizing Calculator for comparison.
- Specific Gravity (SG): Commercial LPG has a specific gravity of 1.52 — roughly 2.5 times denser than natural gas (0.60). Because propane is heavier than air, it causes higher friction loss per metre inside copper and PEX lines.
- Gross Calorific Energy Density: LPG delivers 93.3 MJ per cubic metre (MJ/m³) versus 38.7 MJ/m³ for natural gas. Therefore, a given MJ/h appliance requires less volumetric gas flow in LPG, but higher operating pressure.
- Energy-to-Mass Ratio: 1 kilogram of commercial LPG yields approximately 50.2 MJ of heat energy (1 kg LPG = 50.2 MJ). For continuous flow hot water systems like a 157 MJ/h unit (e.g. Rinnai 26), the peak fuel draw is 157 / 50.2 = 3.13 kg/h. Compare this against household water demand using our Hot Water System Sizing Calculator.
The LPG Two-Stage Regulator System in Australia
Residential and light commercial LPG systems use a two-stage pressure regulation setup between the high-pressure gas cylinder (800 to 1,200 kPa internal bottle pressure) and the indoor appliances:
- Stage 1 Regulation (Cylinder Regulator): Drops cylinder vapor pressure down to an intermediate pressure of 35.0 kPa for main underground or exterior transport runs.
- Stage 2 Regulation (House Regulator): Reduces line pressure down to standard low-pressure delivery of 2.75 kPa at the building wall entry.
- Allowable Pressure Drop Budget: Under AS/NZS 5601.1, the minimum required pressure at appliance inlet terminals is 2.25 kPa. This leaves a strict maximum friction drop budget of 0.50 kPa (5.0 mbar) from the Stage 2 regulator to the furthest appliance. If you are calculating general hydraulic friction or velocity, see our Water Flow Rate Calculator.
LPG Cylinder Types & Vapour Withdrawal Limits
Unlike reticulated utility mains, LPG gas bottles have physical thermodynamic limits on how fast liquid propane can boil off into gas. When gas is drawn too fast, the liquid temperature plummets, causing moisture to freeze on the outside of the cylinder and lowering delivery pressure.
| Cylinder Setup | Max Continuous Vapour Withdrawal | Peak Mass Flow (kg/h) | Recommended Application |
|---|---|---|---|
| Single 45kg Bottle | ~65 MJ/h | 1.3 kg/h | Cooktop only / Single bayonet heater |
| Dual 45kg Manifold (Changeover) | ~130 MJ/h | 2.6 kg/h | Standard residential (Cooktop + Small HWS) |
| 4× 45kg Manifold Bank (2+2) | ~260 MJ/h | 5.2 kg/h | High-demand home (Cooktop + Instant HWS + Heating) |
| Bulk Tank 190kg | ~200 MJ/h | 4.0 kg/h | Off-grid rural residence / Farmhouse |
| Bulk Tank 500kg+ | ~450 MJ/h | 9.0 kg/h | Commercial kitchen / Restaurant / Poultry farm |
AS/NZS 5601.1 Pipe Capacity Reference Table (Copper)
Below is the standard capacity lookup matrix for Type A Copper Tube carrying LPG at 2.75 kPa supply pressure with a 0.50 kPa allowable pressure drop budget:
| Pipe Nominal Size | 5m Run | 10m Run | 15m Run | 20m Run | 25m Run | 30m Run | 40m Run |
|---|---|---|---|---|---|---|---|
| DN15 (12.7mm ID) | 37 MJ/h | 26 MJ/h | 21 MJ/h | 18 MJ/h | 16 MJ/h | 15 MJ/h | 13 MJ/h |
| DN20 (18.9mm ID) | 86 MJ/h | 61 MJ/h | 50 MJ/h | 43 MJ/h | 38 MJ/h | 35 MJ/h | 30 MJ/h |
| DN25 (25.0mm ID) | 161 MJ/h | 114 MJ/h | 93 MJ/h | 81 MJ/h | 72 MJ/h | 66 MJ/h | 56 MJ/h |
| DN32 (31.7mm ID) | 298 MJ/h | 211 MJ/h | 172 MJ/h | 149 MJ/h | 133 MJ/h | 122 MJ/h | 104 MJ/h |
| DN40 (38.1mm ID) | 469 MJ/h | 332 MJ/h | 271 MJ/h | 235 MJ/h | 210 MJ/h | 191 MJ/h | 164 MJ/h |
| DN50 (50.8mm ID) | 960 MJ/h | 679 MJ/h | 554 MJ/h | 480 MJ/h | 429 MJ/h | 392 MJ/h | 336 MJ/h |
Real-World Worked Example: Off-Grid QLD Farmhouse
Let's walk through an actual step-by-step sizing calculation for a rural property in Toowoomba, QLD with a dual 45kg cylinder bank and a 14-metre run from the regulator to the kitchen using hard copper pipe:
- 1. Tally Appliance Loads: Gas Cooktop (36 MJ/h) + Instant LPG Hot Water System (157 MJ/h) = 193 MJ/h Total Concurrent Load.
- 2. Cylinder Withdrawal Verification: Total demand (193 MJ/h) exceeds standard dual 45kg bottle capacity (130 MJ/h). Action: Upgrade to a 4× 45kg manifold bank (2 active + 2 reserve) to prevent winter bottle freeze-up.
- 3. Equivalent Pipe Length: Actual distance 14m × 1.25 (moderate elbows and tees allowance) = 17.5m Equivalent Length (evaluated at the 20m column).
- 4. Pipe Capacity Check at 20m: DN20 carries 43 MJ/h ❌. DN25 carries 81 MJ/h ❌. DN32 carries 149 MJ/h ❌. DN40 Copper carries 235 MJ/h ✅.
- 5. Final Pipe Specification: Run a DN40 Copper main header from the Stage 2 wall regulator to the central manifold tee, stepping down to a DN20 branch for the cooktop and DN32 for the instantaneous water heater. For trade waste or sanitary plumbing on the same site, check our Drainage Pipe Sizing Calculator and Backflow Prevention Sizing Calculator.
Common LPG Pipe Sizing Mistakes on Australian Sites
- Ignoring Ambient Temperature De-rating: In southern winter climates (e.g. Southern Highlands, Ballarat, Canberra), cylinder vaporization capacity drops by up to 30% when ambient temperatures dip below 5°C.
- Confusing Natural Gas & LPG Tables: Natural gas capacity tables assume a specific gravity of 0.60 and 1.05 kPa supply. Applying NG tables to LPG results in severe undersizing.
- Neglecting PEX-AL-PEX Internal Diameter: Multilayer PEX gas pipe has a thicker wall dimension than copper. For example, DN20 PEX-AL-PEX has an ID of ~16mm versus ~18.9mm for DN20 copper. Always size PEX by internal diameter.
- Exceeding 15 m/s Maximum Gas Velocity: AS/NZS 5601.1 limits gas velocity to 15 metres per second to prevent excessive pipe noise and regulator erosion.