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TEST METHOD
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appearance |
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visual appearance |
clear, bright and visually free from solid matter and un-dissolved water at ambient fuel temperature |
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colour |
report |
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d 156 or d 6045 |
see note 1 |
particulate contamination mg/l |
max 1.0 |
423 |
d 5452 |
see note 2 |
particulate, cumulative channel particle counts, iso code & individual channel counts |
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564 or 565 or 577 |
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see note 3 |
≥ 4 μm(c) |
report |
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≥ 6 μm(c) |
report |
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≥ 14 μm(c) |
report |
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≥ 21 μm(c) |
report |
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≥ 25 μm(c) |
report |
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≥ 30 μm(c) |
report |
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composition |
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total acidity, mg koh/g |
max 0.015 |
354 |
d 3242 |
see note 4 |
aromatics, % v/v. |
max 25.0 |
156 |
d 1319 |
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or total aromatics, % v/v |
max 26.5 |
436 |
d 6379 |
see note 5 |
sulphur, total, % m/m |
max 0.30 |
336 |
d 1266 or d 2622 or d 4294 or d 5453 |
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sulphur, mercaptan, % m/m |
max 0.0030 |
342 |
d 3227 |
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or doctor test |
negative |
30 |
d 4952 |
see note 6 |
refinery components at point of manufacture: |
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see note 7 |
non hydroprocessed components, %v/v |
report (incl. ‘nil’ or ‘100%’) |
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mildly hydroprocessed components, % v/v |
report (incl. ‘nil’ or ‘100%’) |
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severely hydroprocessed components, % v/v |
report (incl. ‘nil’ or ‘100%’) |
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synthetic components, %v/v |
report (incl. ‘nil’ or ‘50%’) |
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see note 4 for limits for synthetic components |
incidental materials |
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fatty acid methyl ester (fame), mg/kg |
max 50 |
585 or 583 or 590 or 599 |
astm d7797 |
see notes 8, 9 and 10 |
volatility |
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distillation |
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123 |
d86 |
or d7345., see note 11 |
initial boiling point, ºc |
report |
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fuel recovered |
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see note 11 |
10% v/v at ºc |
max 205.0 |
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or ip 406 or d 2887 |
50% v/v at ºc |
report |
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see note 12 |
90% v/v at ºc |
report |
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end point, ºc |
max 300.0 |
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residue, % v/v |
max 1.5 |
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loss, % v/v |
max 1.5 |
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flash point, ºc |
min 38.0 |
170 or 523 |
d 56 or d 3828 |
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density at 15ºc, kg/m³ |
775.0 min to 840.0 max |
160 or 365 |
d 1298 or d 4052 |
see note 13 |
fluidity |
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freezing point, ºc |
max -47.0 |
16 or 435 or 528 or 529 |
d 5972 or d 7153 or d 7154 |
see note 14 |
viscosity at -20ºc, mm2/s(cst) |
max 8.000 |
71 |
d 445 |
or d7042, see note 15 |
combustion |
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specific energy, net, mj/kg |
min 42.80 |
12 or 355 |
d 3338 or d 4809 |
see note 16 |
smoke point, mm |
min 25.0 |
598 |
d 1322 |
see note 17 |
or |
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smoke point, mm |
min 18.0 |
598 |
d 1322 |
see note 17 |
and naphthalenes, % vol |
max 3.00 |
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d 1840 |
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corrosion |
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corrosion, copper strip, classification (2 hours +/- 5 min. at 100 ºc +/- 1ºc) |
max 1 |
154 |
d 130 |
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stability |
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thermal stability (jftot) |
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323 |
d 3241 |
see note 18 |
control temperature, ºc |
min 260 |
323 |
d 3241 |
see note 18 |
filter pressure differential, mm hg |
max 25 |
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one of the following requirements shall be met: |
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(1) annex b vtr |
less than 3, no ‘peacock’ or ‘abnormal’ colour deposits |
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(2) annex c itr or annex d etr, average over area of 2.5mm² |
max 85 |
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contaminants |
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existent gum, mg/100ml |
max 7 |
540 |
d 381 |
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microseparometer (msep), rating |
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fuel with static dissipator additive |
min 70 |
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d 3948 |
see note 19 |
or |
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fuel without static dissipator additive |
min 85 |
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conductivity |
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electrical conductivity, ps/m |
50 min to 600 max |
274 |
d 2624 |
see note 20 |
lubricity |
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bocle wear scar diameter, mm |
max 0.85 |
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d 5001 |
see note 21 |
additives (names and approval code from def stan 91-091/9 should be quoted on quality certificates). |
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antioxidant, mg/l (in final batch |
max 24.0 |
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see note 22 |
in hydroprocessed & synth. fuels (mandatory) |
min 17.0 |
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see note 23 |
in non-hydroprocessed fuels (optional) |
ma 24.0 |
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see note 24 |
metal deactivator, mg/l (optional) * |
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first doping |
max 2.0 |
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cumulative concentration after field re-doping |
max 5.7 |
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static dissipator, mg/l* |
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first doping |
max 3.0 |
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cumulative concentration after field re-doping |
max 5.0 |
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