Gas Pipe Sizing - Introduction - Page 1 2 3 4


 

Gas Properties

 

The Table below lists some of the more useful properties in building services for natural gas and liquid petroleum gas (LPG).

 

 

Properties

Natural Gas

Liquid Petroleum Gas (LPG)

Propane

 

Composition & Chemical symbol

92.6% Methane CH4

3.6%   Ethane   C2H6

0.8%   Propane C3H8

0.2%   Butane   C4H10

100% C3H8

Gross Calorific Value (GCV)

(MJ/m3)(kJ/litre)

41.6

95

as gas

Gross Calorific Value (GCV)

(MJ/litre)

0.0416

25.5

as liquid

Gross Calorific Value (GCV) (MJ/kg)

53.3

50

Net Calorific Value (NCV)

(MJ/m3)

38.7

86

Density of gas at 15oC

(kg/m3)

0.78

1.85

Density of liquid under pressure

(kg/litre) or (kg/m3)

-

0.512 kg/litre     or

512 kg/m3

Ignition temperature (oC)

650

510

Operating pressure (millibars)

20

37

Volume of gas per volume of liquid (m3/m3) or (m3/litre)

-

274 m3gas /m3 liquid   or

0.274 m3 gas / litre liquid

Volume of gas per kg mass of liquid (m3/kg)

-

0.54             

 

LPG (Gas) Pipe Sizing Notes

 

Allowable pressure drops

 

Medium pressure lines -        450 Pa per m run  ( 2 P.S.I. per 100 foot )

Low pressure lines     -        4.1 Pa per m run   ( ½” w.g. /100 ft)

                                 -        Maximum 1300 Pa total pressure drop in any run.

Gas Pressures

 

First stage regulation at tank pressure is reduced from 6 bar to 0.7 bar.

Second stage regulation at building pressure is reduced  to 50 mbar (0.05 bar)

At equipment and appliances     -        37 millibar (0.037 bar)

 

Natural Gas Pipe Sizing

 

Allowable pressure drops

 

The allowable pressure drop between the outlet of the meter and appliances must not exceed 1 mbar or 0.001 bar or  100 Pa.

Pressure loss is generally limited to between 75 Pa and 125 Pa from the meter to the point of use.

 

Gas Pressures

 

At equipment and appliances     -        20 millibar (0.020 bar)

 

 


Gas Pipe Sizing - Introduction - Page 1 2 3 4