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LPG is the acronym of
Liquefied Petroleum Gases.
LPG are the light hydrocarbons fraction of the
paraffin series, derived from refinery
processes, crude oil stabilisation plants and
natural gas processing plants comprising
propane, butane and butylenes or a combination
of them.
LPG may be also called liquefied refinery gases.
LPG have no natural odor
As light hydrocarbons of the paraffin series,
LPG are derived solely from the distillation of
crude oil.
LPG can be liquefied under low pressure (5-10
atmospheres).
In the liquid state and at a temperature of 38
¢XC, LPG have a relative vapor pressure less than
or equal to 24.5 bars.
LPG specific gravity ranges from 0.50 to 0.58.
Unlike the liquefied natural gas (LNG), LPG do
not require cooling to be liquefied.
Large quantities of LPG are now available as a
by-products from the gas and petroleum
industries.
LPG are obtained as light ends from the
fractionation of the crude oil.
LPG have good caloric value, to be used for
transportation fuel as well as cooking fuel.
Since LPG have no natural odor, a distinctive
odorant is added so that it will be noticeable
should a leak occur.
Because of the low boiling point (−44 to 0¢XC)
and high vapor pressure of these gases, their
handling as liquids in pressure cylinders is
necessary.
Then LPG transportation is easy with steel
pressurized bottles to be used in remote areas
as domestic fuel.
LPG are often employed as fuel for tractors,
trucks, buses.
LPG have a high octane rating, making it useful
in engines having compression ratios above 10:1.
Another factor of importance in internal
combustion engines is that LPG leave little or
no engine deposit in the cylinders when they
bum.
The exhausted gas from engine combustion are
also pretty clean compared with gasoline and
diesel so that LPG can be used in industrial
applications for handling and forklift trucks.
Owing to demand from industry for butane
derivations, LPG sold as fuel are made up
largely of propane.
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Liquefied Petroleum Gas (LPG)-BULTANE
50% SPECIFICATION
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PROPERTY |
UNITS |
TEST METHOD |
VALUE |
1 |
Ethane |
mol% |
G.C |
0.08max |
2 |
Propane |
mol% |
G.C |
2max |
3 |
Total-c4 |
mol% |
G.C |
97.5min |
4 |
Total-c4 |
mol% |
G.C |
0.82max |
5 |
Sp.Gr. @ (60F / 60F) |
- |
ASTM D-2598 |
To be reported |
6 |
Copper Corrosion |
- |
ASTM-D1838 |
No. la max |
7 |
Total Sulfide |
wt.ppm |
Based on ASTM D-3246 |
30max |
8 |
Hyfrogen Sulfide |
vol.ppm |
ASTM D2420 / DRAGER |
Nil |
9 |
Vapor press @ (100F) |
Psig |
ASTM D-2598 |
70max |
10 |
Water Content |
vol.ppm |
shaw dew point |
10max |
11 |
Residue on evaporation |
vol% |
ASTM D-2158 |
0.0max |
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Liquefied Petroleum Gas (LPG)-PROPANE
50% SPECIFICATION
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PROPERTY |
UNITS |
TEST METHOD |
VALUE |
1 |
Ethane |
mol% |
G.C |
0.4max |
2 |
Propane |
mol% |
G.C |
98max |
3 |
Butane |
mol% |
G.C |
1.4max |
4 |
Pentanes & Heavier |
mol% |
G.C |
0.01max |
5 |
Copper Corrosion |
- |
ASTM D-1838 |
No la max |
6 |
Hyfrogen Sulfide |
vol.ppm |
ASTM D2420 / DRAGER |
5max |
7 |
Sp.Gr. @ (60F / 60F) |
- |
ASTM D-2598 |
To be reported |
8 |
Sulphur (Volatile) |
wt.ppm |
Based on ASTM D-3248 |
30max |
9 |
Vapor press @ (100F) |
Psig |
ASTM D-2598 |
200max |
10 |
Water Content |
- |
ASTM D-2713 |
pass |
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