
|
Commercial |
Commercial |
|
|
Relative density of liquid at 15 ƒC |
0,57 to 0,58 |
0,50 to 0,51 |
|
Imperial gallons/ton at 15 ƒC |
385 to 393 |
439 to 448 |
|
Litre/tonne at 15 ƒC |
1 723 to 1 760 |
1 965 to 2 019 |
|
Relative density of gas compared with air at 15 ƒC and 1 013,25 mbar |
1,90 to 2,10 |
1,40 to 1,55 |
|
Volume of gas (litres) per kg of liquid at 15 ƒC and 1 013,25 mbar |
406 to 431 |
537 to 543 |
|
Volume of gas (ft3) per lb of liquid at 60ƒ F and 30 in Hg |
6,5 to 6,9 |
8,5 to 8,7 |
|
Boiling point at atmospheric pressure ƒC approx. |
-2 |
-45 |
|
Vapour pressure for products at their maximum specified vapour pressure (gauge): Vapour pressure for products at their maximum specified vapour pre Temp. ƒC -40 -18 0 15 38 45 |
Bar - * 0,9 1,93 4,83 5,86 |
Bar 0,5 2,3 4,5 6,9 14,5 17,6 |
|
Latent heat of vaporisation (kJ/kg) at 15 ƒC |
372,2 |
358,2 |
|
Latent heat of vaporisation (Btu/lb) at 60ƒ F |
160 |
154 |
|
Specific heat of liquid at 15 ƒC (kJ/kg ƒC) |
2,386 |
2,512 |
|
Sulphur content per cent weight |
Negligible to 0,02 |
Negligible to 0,02 |
|
Limits of flammability (percentage by volume of gas in a gas-air mixture to form a combustible mixture) |
Upper 9,0 Lower 1,8 |
Upper 10,0 Lower 2,2 |
|
Calorific Values: Gross: (MJ/m3) dry (Btu/ft3) dry (MJ/kg) (Btu/lb) Nett: (MJ/m3) dry (Btu/ft3) dry (MJ/kg) (Btu/lb) |
121,8 3 270 49,3 21 200
112,9 3 030 45,8 19 700 |
93,1 2 500 50,0 21 500
86,1 2 310 46,3 19 900 |
|
Air required for combustion (m3 to burn 1 m3 of gas) |
30 |
24 |
* Minimum Commercial Butane vapour pressure at ñ18ƒ is minus 5224 mbar g.