STIR

Standardized Specification for Petroleum Products

Standard NT No. 04.52 Date (1990)


Butane Commercial

Technical characteristics Limits Methods
Odour Feature  
Relative vapor pressure Less than or equal to 7 bars at 50 ° centigrade NT 04.81:
ASTM D.1267
Sulfur compounds Absence of reaction to the sodium plombist test called "Doctor test" NT 04.82 (Referrer)
NF M 41.006
NT 04.83
ASTM D 2420
Water content Absence of separable water by decantation Visual
Corrosion to the copper plate (3 hours at 50 ° C) Rating of 1b maximum NT 04.84:
ASTM D.1838
Evaporation The end point of boiling by the so-called "95% point method" must be less than or equal to 2 ° C NT 04.85
ASTM D.1837
Residue The residue must be at most equal to 0.05% by volume NT 04.86
ASTM D.2158
Aromatic Content Equal to or less than 18% (V / V) NT 04.19
ASTM D.1657

 

Commercial Propane

Technical characteristics Limits Methods
Odour Feature  
Relative vapor pressure At least 8,3 bar at 37,8 ° C ensuring a minimum of 11,5 bar at 50 ° C and not more than 14,4 bar at 37,8 ° C guaranteeing a maximum of 19,3 bar at 50 ° C. Bars at 37.8 ° C NT 04.81:
ASTM D.1267
Sulfur compounds Absence of reaction to the sodium plombist test called "Doctor test" NT 04.82 (Referrer)
NF M 41.006
NT 04.83
ASTM D 2420
Water content Not detectable by cobalt bromide test NT 04.90
NF M 41.004
Sulfur content Less than or equal to 0.005% (w / w) NT 04.89
ASTM D .2784
Corrosion to the copper plate (3 hours at 50 ° C) Rating of 1b maximum NT 04.84 :
ASTM D .1838
Evaporation The end point of boiling by the so-called "95% point method" must be less than or equal to 15 ° C NT 04.85
ASTM D.1837
Density Greater than or equal to 0.502 Kg / l at 15 ° C (or 0.443 Kg / L at 50 ° C) NT 04.86
ASTM D.2158
Aromatic Content Equal to or less than 18% (V / V) NT 04.19
ASTM D.1657



Special fuel mixture (Butapro I and Butapro II)

A special mixture of commercial butane and commercial propane may be sold under the name "Butapro I" or "Butapro II" depending on the proportion of the liquefied gases composing the mixture.
The general characteristics of this mixture are those of commercial butane and commercial propane except for the relative vapor pressure which must not exceed:

  • 11.5 kg / cm2 at 50 ° C for Butapro I

  • and 8.5 kg / cm2 at 50 ° C for Butapro II.