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LPG
PROPANE
| RESULTS | METHODS | |
| DENSITY AT 15ºC | 0.5102 | ASTM D-1657 |
| VAPOUR PRESSURE AT 40ºC,kPa | 1281 | ANNEX A |
| TOTAL BUTANE % | 1.10 | EN 27941 |
| RESIDUE ml/100 ml | 0.00 | ASTM D-2158 |
| OIL STAIN OBSERVATION | NORMAL | ASTM D-2158 |
| CORROSION COPPER | 1 | EN ISO-6251 |
| SULFUR,mg/kg | 24.0 | ASTM D-6667 |
| WATER CONTENT | NIL | |
| ODOUR | CHARACTERISTIC | ANNEX B |
| HYDROGEN SULPHIDE | NIL | ISO-8819 |
| 1,3 BUTADIENE % | 0.00 | EN 27941 |
LPG MIXTURE
| RESULTS | METHODS | |
| DENSITY AT 15ºC | 0.5646 | ASTM D-1657 |
| VAPOUR PRESSURE AT 40ºC,kPa | 558 | ANNEX A |
| TOTAL PROPANE % | 25.3 | EN 27941 |
| TOTAL BUTANE % | 73.10 | EN 27941 |
| PENTANE AND HEAVIER % | 1.60 | EN 27941 |
| RESIDUE ml/100 ml | 0.00 | ASTM D-2158 |
| OIL STAIN OBSERVATION | NORMAL | ASTM D-2158 |
| CORROSION COPPER | 1 | EN ISO-6251 |
| SULFUR,mg/kg | 40.0 | ASTM D-6667 |
| WATER CONTENT | NIL | |
| ODOUR | CHARACTERISTIC | ANNEX B |
| HYDROGEN SULPHIDE | NIL | ISO-8819 |
| 1,3 BUTADIENE % | 0.00 | EN 27941 |
LPG AUTOMOTIVE
| RESULTS | METHODS | |
| DENSITY AT 15ºC | 0.5566 | ISO -8973 |
| OCTANE NUMBER(MON) | 91.2 | ANNEX B |
| TOTAL DIENES CONTENT %m/m | 0.0 | EN 27941 |
| 1,3 BUTADIENE % | 0.0 | DIN-51619 |
| PROPANE CONTENT,%m/m | 33 | EN 27941 |
| HYDROGEN SULPHIDE | NEGATIVE | EN ISO-8819 |
| TOTAL SULPHUR MG/KG | 29 | ASTM D-6667 |
| CORROSION COPPER(1HR AT40ºC) | 1 | EN ISO-6251 |
| EVAPORATION RESIDUE MG/KG | 0 | EN-15471 |
| VAPOUR PRESSURE ,GAUGE | EN ISO-8973 & ANNEX C | |
| AT 0ºC,KPA | 164 | |
| AT 40ºC,KPA | 703 | |
| WATER CONTENT | PASS | VISUAL INSPECTION |
| METHANOL CONTENT MG/KG | 0 | ISO-8174 |
| ODOUR | UNPLEASANT AND DINSTNCTIVE AT 20% LFL | ANNEX A |
GASOLINES
UNLEADED 100 RON (BIO)
| RESULTS | METHODS | |
| DENSITY AT 15ºC gr/ml | 0.7522 | EN ISO-12185 |
| EVAPORATED AT 70ºC, % v/v | 27.0 | EN ISO-3405 |
| EVAPORATED AT 100ºC, % v/v | 53.1 | EN ISO-3405 |
| EVAPORATED AT 150ºC, % v/v | 88.3 | EN ISO-3405 |
| FBP ºC | 193.7 | EN ISO-3405 |
| RESIDUE % v/v | 0.8 | EN ISO-3405 |
| REID VAPOR PRESSURE Kpa | 74.8 | EN 13016-1 |
| VLI | 936 | EN 13016-1 |
| SULPHUR mg/Kgr | 2.0 | EN ISO-20846 |
| RON | 100.1 | EN 25164 |
| MON | 88.1 | EN 25163 |
| LEAD g/L | 0.001 | EN 237 |
| COPPER CORROSION CLASSIFICATION | 1 | EN ISO-2160 |
| EXISTENT GUMS mg/100ml | 2.00 | EN ISO-26246 |
| OXIDATION STABILITY min | >360 | EN ISO 7536 |
| BENZENE % v/v | 0.81 | EN ISO-22854 |
| AROMATICS % v/v | 34.10 | EN ISO -22854 |
| OLEFINS % v/v | 11.1 | EN ISO -22854 |
| OXYGEN CONTENT % m/m | 2.24 | EN ISO -22854 |
| MANGANESE | 0.0 | EN 16135 |
| APPEARANCE | B/C | Visual evaluation |
| TOTAL ETHERS %v/v | 13.22 | EN ISO-22854 |
| ETHYL,TERTIARY BUTYL ETHER (BIO) % v/v | 0.75 | EN ISO-22854 |
| ETHYL,TERTIARY AMYL ETHER (BIO) % v/v | 4.71 | EN ISO-22854 |
| ETHYL,TERTIARY HEXYL ETHER (BIO) % v/v | 0.30 | EN ISO-22854 |
| ETHANOL (BIO)% v/v | 0.06 | EN ISO-22854 |
| QUINIZARIN mg/L | 0 | 298 |
| COLOR | NATURAL | Visual evaluation |
UNLEADED 95 RON (BIO)
| RESULTS | METHODS | |
| DENSITY AT 15ºC gr/ml | 0.7334 | EN ISO-12185 |
| EVAPORATED AT 70ºC, % v/v | 38.2 | EN ISO-3405 |
| EVAPORATED AT 100ºC, % v/v | 63.3 | EN ISO-3405 |
| EVAPORATED AT 150ºC, % v/v | 90.6 | EN ISO-3405 |
| FBP ºC | 190.7 | EN ISO-3405 |
| RESIDUE % v/v | 0.8 | EN ISO-3405 |
| REID VAPOR PRESSURE Kpa | 79.0 | EN 13016-1 |
| VLI | 1057 | EN 13016-1 |
| SULPHUR mg/Kgr | 4.1 | EN ISO-20846 |
| RON | 96.3 | EN 25164 |
| MON | 85.1 | EN 25163 |
| LEAD g/L | 0.001 | EN 237 |
| COPPER CORROSION CLASSIFICATION | 1 | EN ISO-2160 |
| EXISTENT GUMS mg/100ml | 2.0 | EN ISO-26246 |
| OXIDATION STABILITY min | >360 | EN ISO 7536 |
| BENZENE % v/v | 0.82 | EN ISO-22854 |
| AROMATICS % v/v | 25.9 | EN ISO -22854 |
| OLEFINS % v/v | 14.6 | EN ISO -22854 |
| OXYGEN CONTENT % m/m | 1.79 | EN ISO -22854 |
| MANGANESE | 0.0 | EN 16135 |
| APPEARANCE | B/C | Visual evaluation |
| TOTAL ETHERS %v/v | 10.54 | EN ISO-22854 |
| ETHYL,TERTIARY BUTYL ETHER (BIO) % v/v | 1.67 | EN ISO-22854 |
| ETHYL,TERTIARY AMYL ETHER (BIO) % v/v | 3.92 | EN ISO-22854 |
| ETHYL,TERTIARY HEXYL ETHER (BIO) % v/v | 0.26 | EN ISO-22854 |
| ETHANOL (BIO)% v/v | 0.06 | EN ISO-22854 |
| QUINIZARIN mg/L | 3 | 298 |
| COLOR | NATURAL | Visual evaluation |
AVIATION FUELS
JET A1
| PROPERTY | RESULTS | LIMITS | TEST METHOD ASTM or IP |
| QUANTITY OF FUEL IN THE TANK m3 | 9180 | ||
| APPEARANCE | |||
| Visual Appearance,at ampient temperature | Clear bright and visually free from solid matter and undissolved water | C/B | Visual |
| Saybolt color | 20+ | Report | D 156 |
| Particularate Contamination,mg/l | 0.30 | 1.0 Max | D 5452 |
| Cumulative chanel particle coumts/ml | Report | IP 565 | |
| >_ 4μm individual channel counts | 230 | ||
| >_ 6μm individual channel counts | 73 | ||
| >_ 14μm individual channel counts | 8 | ||
| >_ 21μm individual channel counts | 3 | ||
| >_ 25μm individual channel counts | 2 | ||
| >_ 30μm individual channel counts | 1 | ||
| ISO CODE | 15/13/10/09/08/06 | ||
| COMPOSITION | |||
| Total Acidity,mg KOH/g | 0.0030 | 0.015 max | D 3242 |
| *Total Aromatics,% v/v | 16.0 | 26,5 max | D 6379 |
| Sulfur,Total,% m/m | 0.15 | 0.30 max | D 4294 |
| Sulfur,Mercaptan,% m/m | 0.0008 | 0.003 max | D 3227 |
| or Doctor test | Negative | D 4952 | |
| Refinery Hydroprocessed at point of manufacture: | Report | ||
| Non Hydroprocessed components % v/v | 100 | ||
| Mildly Hydroprocessed components % v/v | Nil | ||
| Severely Hydroprocessed components % v/v | Nil | ||
| Synthetic components % v/v | Nil | ||
| VOLALITILY | |||
| Distillation | D 86 | ||
| Initial boiling point, ºC | 153.0 | Report | |
| 10% v/v recovered, ºC | 175.6 | 205 max | |
| 50% v/v recovered, ºC | 197.9 | Report | |
| 90% v/v recovered, ºC | 233.3 | Report | |
| End point, ºC | 255.7 | 300 max | |
| Residue,% v/v | 1.0 | 1.5 max | |
| Loss,% v/v | 0.5 | 1.5 max | |
| *Flash point, ºC | 41.0 | 40 min | D 56 |
| Density at 15ºC, Kg/l | 0.7932 | 0.775-0.840 | D 4052 |
| FLUIDITY | |||
| *Freezing point, ºC | -50 | -47 max | D 5972 |
| Viscosity at -20ºC, cst(mm2/s) | 3.9 | 8 max | d 445 |
| COMBUSTION | |||
| Net Heat of Combustion,MJ/Kg | 43,343 | 42.8 min | D 3338 |
| (Specific energy,Net) | |||
| Smoke point,mm | 26.2 | 25 min | D 1322 |
| or Smoke point,mm | – | 18 min | D 1323 |
| and Napthalenes,% v/v | – | 3 max | D 1840 |
| CORROSION | |||
| Copper strip (2h,100ºC),Classification | 1 | 1 max | D 130 |
| THERMAL STABILITY | |||
| JFTOT | D 3241 | ||
| Control Temperature, ºC | 260 | Min 260 | |
| Filter Pressure Differential,mm Hg | 0.0 | 25 max | |
| Tube Deposit Rating Visual | 1 | <3 max | Annex B |
| <
> or <> deposits |
NO | NO | Annex B |
| CONTAMINANTS | |||
| Existent gum,mg/100ml | 2.0 | 7 max | D 381 |
| WATER SEPARATION CHARACTERISTICS | |||
| Microseparometer(MSEP) rating | D 3948 | ||
| Fuel with SDA | 75 | 70 min | |
| Fuel without SDA | 85 min | ||
| CONDUCTIVITY | |||
| Electrical Conductivity,pS/m, at 25ºC | |||
| (Fuel with SDA) | 480 | 50-600 | D 2624 |
| ADDITIVES | |||
| Static Dissipator (Statis 450),mg/l | 1.7 | 3 max | |
| Antioxidant(kerobit TP26RDE/A/609).mg/l | Nil | 17-24 | |
| on hydroprocessed | |||
| Lubricity improver Additive (RDE/A/662),mg/l | Nil | 9-23 | |
| Metal Deactivator,mg/l | Nil | 2 | |
| INCIDENTAL MATERIALS | |||
| FAME,mg/kg | <20 | 50 max | IP 583 |
DIESELS
ULSD 10 ppm (EN 590)
| Density at 20ºC | Summer season (April – October): 0.820-0.846 with reference point 0.845 |
| Density at 20ºC | Winter season (November to April): 0.800-0.840, with reference point 0.825 |
| Cetane Index | 46 min. |
| Color index | 1.5 max. |
| Cetane Number | 51 min. |
| Fractional composition | Distillation at 250°C max 64,5 |
| Fractional composition | at 350°C min 85% |
| Fractional composition | at 360°C min 95% |
| Kinematic viscosity at 40 C | 2.0-4.5 cSt (mm2/s) |
| Cold filtration plugging point | -2ºC max. summer season |
| Cold filtration plugging point | -22ºC max. winter season |
| Resin concentration (100 cm3 fuel) | 40 mg max. |
| Cloud point | -7ºC max. winter season |
| Cloud point | +5ºC max. summer season |
| Iodine number (lg/100g of fuel) | 6 mg max. |
| Flash point | 58ºC min. |
| Ash | 0.01% max. |
| Sulfur | 10 ppm. (0.001% max.) |
| Carbon | 0.2 % max. |
| Mercaptam sulfur | 0.01% max. |
| Filter coefficient | 3 max. |
| Lubricity | 460 max |
| Oxidant stability | 2.5 mg/100 ml max. |
| Hydrogen sulfur | none |
| Hydrocarbons | none |
| Sediments | none |
| Water soluble acids | none |
| Water | 150 mg/kg max. (actual nil) |
| Acid number (mg KOH/g) | 0.05 max. |
| Copper corrosion strip (CCS) | 1 (3 hours at 50ºC) |
| Viscosity at 40ºC | 2.0 – 4.5 mm/s |
| Appearance | clear and bright (no sediments or water) |
| Polyaromatic carbohydrates | 8 % (m/m) |
| Fatty acid/methylester | 7.0 % (V/V) |
| Resin concentration (100 cm3 fuel) | 40 mg max. |
| Iodine number (lg/100g of fuel) | 6 mg max. |
| Acid number (mg KOH/g) | 0.05 max. |
DIESEL AUTOMOTIVE
| RESULTS | METHODS | |
| DENSITY AT 15ºC kg/m3 | 842.0 | EN ISO-12185 |
| FLASH POINT (PM) deg ºc | 70.0 | EN ISO-2719 |
| VISCOSITY AT 40ºC,mm2/s | 3.434 | EN ISO-3104 |
| SULPHUR CONTENT,mg/kg | 8.4 | EN ISO-20846 |
| CARBON RES,ON 10% BOTTOM,%m/m | 0.02 | EN ISO-10370 |
| ASH CONTENT %wt | 0.002 | EN-6245 |
| C.F.P.P deg ºC | -5 | EN-116 |
| OXIDATION STABILITY gr/m3 | 3.8 | EN ISO-12205 |
| OXIDATION STABILITY hours | 24.0 | EN 15751 |
| COR.COP.STRIP,3 HRS AT 50ºC | 1A | EN ISO-2160 |
| CETANE INDEX | 55.2 | EN ISO-4264 |
| WATER CONTENT mgr/kgr | 170 | EN ISO-12937 |
| TOTAL CONTAMINATION mgr/kgr | 3.9 | prEN 12662 |
| DISTILLATION | EN ISO-3405 | |
| RECOVERED AT 250 DEG C,% v/v | 21 | |
| RECOVERED AT 350 DEG C,% v/v | 92 | |
| RECOVERED AT 95% VOL deg C | 360 | |
| CETANE NUMBER | 56.4 | EN ISO-5165 |
| POLYCYCLIC AROMATICS, % m/m | 0.7 | EN 12916 |
| FATTY ACID METHYL ESTER,%v/v | 7.00 | EN 14078 |
| LUBRICITY (WSD 1,4) AT 60ºC m | 300.0 | ISO 12156-1 |
DIESEL HEATING
| RESULTS | METHODS | |
| DENSITY AT 15ºC gr/ml | 0.8316 | EN ISO-3675 |
| RECOVERED 50% , ºC | 256.3 | EN ISO-3405 |
| RECOVERED 95% , ºC | 362.8 | EN ISO-3405 |
| RECOVERED AT 350 ºc,% v/v | 91.8 | EN ISO-3405 |
| SULPHUR %m/m | 0.0770 | ISO-8754 |
| COPPER CORROSION CLASSIFICATION | 1 | EN ISO-2160 |
| FLASH POINT ºc | 58.0 | EN 22719 |
| COLOR | 3.5 | ASTM D-1500 |
| KINEMATIC VISCOSITY AT 40ºC, cSt | 2.5 | ISO-3104 |
| WATER AND SEDIMENT % v/v | <0,05 | ASTM D-1796 |
| CETANE INDEX | 50.6 | ISO-4264 |
| POUR POINT ºc | <-18 | ISO-3016 |
| CFPP ºc | -13 | EN 116 |
| ASH % m/m | 0.005 | EN ISO-6245 |
| MICROCARBON 10% DIST.RESIDUE % m/m | 0.02 | EN ISO-10370 |
| COLOR | RED | |
| SOLVED YELLOW 124 mg/l | 6.0 |
MAZUT
MARINE GAS OIL
(0,05%<S<=0,1%)
| RESULTS | METHODS | |
| DENSITY AT 15ºC KG/LIT | 0.8663 | ISO-12185 |
| ASH %MASS | 0.003 | ISO-6245 |
| FLASH POINT ºc (PM) | 84.0 | ISO-2719 |
| SULPHUR %MASS | 0.100 | ISO-8754 |
| SEDIMENTS %MASS | 0.001 | ISO-3735 |
| WATER CONTENT,mg/kg | 190 | EN ISO-12937 |
| VISCOSITY AT 40ºC,cSt | 5.127 | ISO-3104 |
| POUR POINT ºC | -3 | ISO-3016 |
| CARBON RESIDUE (MICRO),(10%B) | 0.03 | ISO-10370 |
| CETANE INDEX | 49.3 | ASTM D-976 |
| DISTIL.RECOV. AT 360ºC,%VOL | 88 | ASTM D-86 |
| CFPP AT ºC | -2 | IP-309 |
| COLOR | BLACK | |
| TRACKER QUINIZARIN,PPM | 3 | IP 298 |
FUEL OIL No1
| RESULTS | METHODS | |
| DENSITY AT 15ºC KG/LIT | 0.9640 | ISO-3675 |
| FLASH POINT ºc (PM) | 86.0 | ISO-2719 |
| VISCOSITY AT 50ºC,cSt | 155.0 | ISO-3104 |
| SULPHUR %MASS | 0.90 | ISO-8754 |
| POUR POINT ºC | -9 | ISO-3016 |
| ASH %MASS | 0.048 | EN-ISO-6245 |
| TOTAL SEDIMENTS % WT | 0.073 | ASTM D-4870 |
| WATER % VOL | 0.1 | ISO-3733 |
| VANADIUM ppm | 25 | IP-288 |
| SODIUM ppm | 32 | IP-288 |
| CARBON RESIDUE % m/m | 12.3 | ISO-10370 |
| NET CALORIFIC VALUE Kcal/kg | 9783 | ASTM D-4868 |
| ALUMINIUM PLUS SILICON,mg/kg | 56.0 | ISO-10478 |
MARINE RESIDUAL FUELS 380
| RESULTS | METHODS | |
| DENSITY AT 15ºC gr/ml | 0.9900 | EN ISO-3675 |
| KINEMATIC VISCOSITY AT 50ºC, cSt | 179.0 | ISO-3104 |
| CCA1 | 859 | |
| SULPHUR % m/m | 3.280 | ISO-8754 |
| FLASH POINT ºc | 64.0 | EN 22719 |
| POUR POINT ºc | -18.0 | ISO-3016 |
| WATER % m/m | 0.30 | ISO-3733 |
| POTENTIAL SEDIMENT %m/m | 0.05 | ISO 10307-2 |
| ASH %m/m | 0.040 | EN ISO-6245 |
| ACID NUMBER | 0.17 | ASTM D-664 |
| MICROCARBON RESIDUE % m/m | 17.21 | EN ISO-10370 |
| VANADIUM mg/kg | 144.0 | IP 470 |
| SODIUM mg/kg | 16 | IP 288 |
| ALUMINUM AND SILICON 19,4 | 20.3 | ISO-10478 |
| NET CALORIFIC VALUE Kcal/kg | 9495 | ASTM D-4868 |
| ZINC mg/kg | 3 | IP 470 |
| CALCIUM mg/kg | 4 | IP 470 |
| PHOSPHORUS | 2.5 | IP 500 |
| HYDROGEN SULPHIDE ppm m//m | 0.3 | IP 570 |
MARINE RESIDUAL FUELS 180
| RESULTS | METHODS | |
| DENSITY AT 15ºC gr/ml | 0.9583 | EN ISO-3675 |
| KINEMATIC VISCOSITY AT 50ºC, cSt | 177.0 | ISO-3104 |
| CCA1 | 828 | |
| SULPHUR % m/m | 0.570 | ISO-8754 |
| FLASH POINT ºc | 73.0 | EN 22719 |
| POUR POINT ºc | -15.0 | ISO-3016 |
| WATER % m/m | 0.05 | ISO-3733 |
| POTENTIAL SEDIMENT %m/m | 0.05 | ISO 10307-2 |
| ASH %m/m | 0.035 | EN ISO-6245 |
| ACID NUMBER | 0.17 | ASTM D-664 |
| MICROCARBON RESIDUE % m/m | 10.00 | EN ISO-10370 |
| VANADIUM mg/kg | 39.0 | IP 470 |
| SODIUM mg/kg | 19 | IP 470 |
| ALUMINUM AND SILICON 19,4 | 11.7 | ISO-10478 |
| NET CALORIFIC VALUE Kcal/kg | 9831 | ASTM D-4868 |
| ZINC mg/kg | 2 | IP 470 |
| CALCIUM mg/kg | 5 | IP 470 |
| PHOSPHORUS | 2.5 | IP 470 |
| HYDROGEN SULPHIDE ppm m//m | 0.3 | IP 570 |
ASPHALT
35/40
| RESULTS | METHODS | |
| PENETRATION 25ºC ,1/10mm | 37.0 | EN 1426 |
| SOFTENING POINT ºc | 52.0 | EN 1427 |
| FLASH POINT ºc | >250 | EN ISO-2952 |
| FLASH POINT ºc | >250 | EN ISO-2719 |
| SOLUBILITY IN TOLUENE %m/m | 99.6 | EN 12592 |
| CHANGE OF MASS AFTER RTFOT %m/m | 0.4 | EN 12607-1 |
| PENETRATION AFTER RTFOT 1/10 m/m | 22 | EN 12607-1 |
| SOFTENING POINT AFTER RTFOT ºc | 54.2 | EN 12607-1 |
50/70
| RESULTS | METHODS | |
| PENETRATION 25ºC ,1/10mm | 62.0 | EN 1426 |
| SOFTENING POINT ºc | 47.4 | EN 1427 |
| FLASH POINT ºc | >250 | EN ISO-2952 |
| FLASH POINT ºc | >250 | EN ISO-2719 |
| SOLUBILITY IN TOLUENE %m/m | 99.6 | EN 12592 |
| CHANGE OF MASS AFTER RTFOT %m/m | 0.4 | EN 12607-1 |
| PENETRATION AFTER RTFOT 1/10 m/m | 37 | EN 12607-1 |
| SOFTENING POINT AFTER RTFOT ºc | 49.6 | EN 12607-1 |
LNG
LNG
Reference standards based on ISO 6976 for calorific values combustion 25° metering 0°.
| Property | LNG Specifications | Unit | |
| Gross calorific value | Min. | 39.5 | MJ/m3(n) |
| Max. | 47 | MJ/m3(n) | |
| Net calorific value | Min. | 35.6 | MJ/m3(n) |
| Max. | 42.9 | MJ/m3(n) | |
| Wobbe Index (GCV) | Min. | 53 | MJ/m3(n) |
| Max. | 58.3 | MJ/m3(n) | |
| LNG density at atmospheric equilibrium pressure, i.e. 1013.25 mbar absolute | Min. | 420 | kg/m3 |
| Max. | 465 | kg/m3 | |
| Methane | Min. | 80 | mol-% |
| Ethane | Max. | 9 | mol-% |
| Propane | Max. | 3 | mol-% |
| n-butane + i-butane | Max. | 1 | mol-% |
| n-pentane + i-pentane | Max. | 0.03 | mol-% |
| Hexane | Max. | 0.0015 | mol-% |
| Nitrogen | Max. | 0.75 | mol-% |
| Carbon dioxide | Max. | 0.01 | mol-% |
| Total Sulphur | Max. | 7.3 | mg/m3(n) |
CNG
CNG Automotive Fuel
| Constituents | Value | Tolerance |
| Wobbe number (Btu/ft3 ) | 1340 | Variation shall be limited to ± 30 units during normal operation |
| Free water, mg/m3 | 8 | Maximum |
| Total sulphur including H2S, mg/m3 | 20 | Maximum |
| N2 + CO2, vol % | 3.5 | Maximum* |
| Oil mist content, ppm | Insignificant | |
| Oxygen, vol. % | 0.5 | Maximum |
| Methane (C1) | 87% | Minimum** |
| Ethane (C2) | 6% | Maximum |
| C3 and higher HC | 3% | Maximum |
| C6 and higher HC | 1% | Maximum |
| Total unsaturated HC | 1% | Maximum |
| Hydrogen (mole %) Maximum | 0.1 | Maximum |
| Carbon monoxide (mole %) | 0.1 | Maximum |
Note:
*occasionally may go up to 7 per cent when shutdown of a processing/handling plants/facilities happen however such events are to be duly notified and should be limited to 10% of time in a year
** In case of process upset/plant s/d may reach a level of 84 however such events are to be duly notified and should be limited to 10% of time in a year. These specifications are free from liquids over the entire range of temperature and pressure encountered in the engine and fuel system and free from solid particulate matter.
The above CNG specifications unanimously finalised by the committee appointed by EPCA were arrived at taking into account the requirements of vehicle manufacturers and the constraints of the gas supply agencies who all were represented in the committee. They are an improvement over the specifications proposed in the Auto Fuel Policy document and are comparable with the EU standards.
AUTOMOTIVE DIESEL
| DENSITITY AT 15oC | EN ISO 12185 | 0.8401 | gr/ml |
| 50% RECOVERED | EN ISO 3405 | 279.7 | oC |
| 95% RECOVERED | EN ISO 3405 | 359.3 | oC |
| RECOVERED AT 250oC | EN ISO 3405 | 30.3 | % v/v |
| RECOVERED AT 350oC | EN ISO 3405 | 91.8 | % v/v |
| RECOVERED AT 360oC | EN ISO 3405 | 95.1 | % v/v |
| SULFUR | EN ISO 20846 | 6.8 | Mg/kgr |
| COPPER CORROSION CLASSIFICATION | EN ISO 2160 | 1 | |
| FLASH POINT | EN ISO 22719 | 69.0 | oC |
| KINEMATIC VISCOSITY AT 40oC | ISO 3104 | 2.8 | cSt |
| WATER | EN ISO 12937 | 125.00 | Mg/Kg |
| CETANE NUMBER | ISO 5165 | 52.6 | |
| CETANE INDEX | ISO 4264 | 53.1 | |
| ASH | EN ISO 6245 | 0.003 | % m/m |
| MICROCARBON RESIDUE ON 10%DST. RESIDUE | EN ISO 10370 | 0.02 | % m/m |
| CFPP | EN 116 | -10 | oC |
| TOTAL CONTAMINATION | EN 12662 | <24.0 | mg/I |
| TOTAL INSOLUBLES | EN ISO 12205 | <25 | mg/L |
| OXIDATION STABILITY 110oC | EN 15751 | >20.0 | h |
| SOLVENT YELLOW 124 | ΦΕΚ 1273/Β/03 | 0.0 | mg/L |
| COLOR | ΦΥΣΙΚΟ | ||
| POLYCYCLIC AROMATIC HYDROCARBONS | ΕΝ 12916 | 5.2 | % m/m |
| CORR. WEAR SCAR DIAMETER WS 1,4 | ISO 12156 | 175 | um |
| FATTY ACID METHYL ESTER | EN 14078 | 7 | % v/v |
| MANGANESE | PrEN 16576 | 0.0 | mg/I |
AUTOMOTIVE DIESEL
| DENSITITY AT 15oC | EN ISO 12185 | 0,8397 | gr/ml |
| 50% RECOVERED | EN ISO 3405 | 276,4 | oC |
| 95% RECOVERED | EN ISO 3405 | 356,6 | oC |
| RECOVERED AT 250oC | EN ISO 3405 | 32,2 | %v/v |
| RECOVERED AT 350oC | EN ISO 3405 | 93,4 | %v/v |
| RECOVERED AT 360oC | EN ISO 3405 | 95,7 | %v/v |
| SULFUR | EN ISO 20846 | 6,2 | mg/kgr |
| COPPER CORROSION CLASSIFICATION | EN ISO2160 | 1 | |
| FLASH POINT | EN ISO 22719 | 70,0 | oC |
| KINEMATIC VISCOSITY AT 40oC | ISO 3104 | 2,7 | cSt |
| WATER | EN ISO 12937 | 110,0 | mg/Kgr |
| CETANE NUMBER | ISO 5165 | 52,0 | |
| CETANE INDEX | ISO 4264 | 52,5 | |
| ASH | EN ISO 6245 | 0,003 | %m/m |
| MICROCARBON RESIDUE ON 10%DST. RESIDUE | EN ISO 10370 | 0,02 | %m/m |
| CFPP | EN 116 | -11 | oC |
| TOTAL CONTAMINATION | EN 12662 | <24 | mg/Kgr |
| TOTAL INSOLUBLES | EN ISO 12205 | <25 | mg/L |
| OXIDATION STABILITY 110oC | En15751 | >20 | h |
| SOLVENT YELLOW 124 | ΦEK 1273/B/03 | 0,0 | mg/L |
| COLOR | ΦΥΣΙΚΟ | ||
| POLYCYCLIC AROMATIC HYDROCARBONS | EN 12916 | 5 | %m/m |
| CORR. WEAR SCAR DIAMETER WS 1,4 | ISO 12156 | 175 | um |
| FATTY ACID METHYL ESTER | EN 14078 | 7,0 | %v/v |
HEATING DESIEL
| DENSITITY AT 15oC | EN ISO 3675 | 0,8549 | gr/ml |
| 50% RECOVERED | EN ISO 3405 | 286,1 | Oc |
| 95% RECOVERED | EN ISO 3405 | 373,9 | Oc |
| RECOVERED AT 350oC | EN ISO 3405 | 86,4 | %v/v |
| SULFUR | ISO 8754 | 0,0950 | %m/m |
| COPPER CORROSION CLASSIFICATION | EN ISO 2160 | 1 | |
| FLASH POINT | EN 22719 | 71 | Oc |
| COLOR ASTM No | ASTM D-1500 | 3,5 | |
| KINEMATIC VISCOSITY AT 40oC | ISO 3104 | 3,3 | cSt |
| WATER AND SEDIMENT | ASTM D-1796 | <0,05 | %v/v |
| CETANE INDEX | ISO 4264 | 48,1 | |
| POUR POINT | ISO 3016 | -15 | Oc |
| CFPP | EN 116 | -12 | Oc |
| ASH | EN ISO 6245 | 0,005 | %m/m |
| MICROCARBON RESIDUE ON 10%DST. RESIDUE | EN ISO 10370 | 0,02 | %m/m |
| SOLVENT YELLOW 124 | ΦEK 1273/B/03 | 6,0 | Mg/L |
| COLOR | ΟΠΤΙΚΗ ΕΚΤΙΜΗΣΗ | KOKKINO |
UNLEADED 100 RON - Με Βιοσυστατικό
| DENSITITY AT 15oC | EN ISO 12185 | 0,7505 | gr/ml |
| EVAPORATED AT 70oC | EN ISO 3405 | 31,5 | %v/v |
| EVAPORATED AT 100oC | EN ISO 3405 | 56,0 | %v/v |
| EVAPORATED AT 150oC | EN ISO 3405 | 89,7 | %v/v |
| FBP | EN ISO 3405 | 190,5 | oC |
| RESIDUE | EN ISO 3405 | 0,9 | %v/v |
| REID VAPOR PRESSURE | EN 13016-1 | 75,1 | KPa |
| VLI | EN 13016-1 | 971 | |
| SULFUR | EN ISO 20846 | 1,7 | mg/Kgr |
| RON | EN 25164 | 100,0 | |
| MON | EN 25163 | 88,3 | |
| LEAD | EN 237 | 0,001 | g/L |
| COPPER CORROSION CLASSIFICATION | EN ISO 2160 | 1 | |
| EXISTENT GUMS | EN ISO 26246 | 2,00 | mg/100ml |
| OXIDATION STABILITY | EN ISO 7536 | >360 | min |
| BENZENE | EN ISO 22854 | 0,71 | % v/v |
| AROMATICS | EN ISO 22854 | 33,50 | % v/v |
| OLEFINS | EN ISO 22854 | 12,00 | % v/v |
| OXYGEN CONTENT | EN ISO 22854 | 2,51 | %m/m |
| MANGANESE | EN 16135 | 0 | |
| APPEARENCE | ΟΠΤΙΚΗ ΕΚΤΙΜΗΣΗ | B/C | |
| TOTAL ETHRERS | EN ISO 22854 | 14,67 | % v/v |
| EETHYL TERTIARY BUTYL ETHER (BIO) | EN ISO 22854 | 0,98 | % v/v |
| ETHANOL(BIO) | EN ISO 22854 | 0,00 | % v/v |
| QUINIZARIN | IP 298 | 0 | mg/L |
| COLOR | ΟΠΤΙΚΗ ΕΚΤΙΜΗΣΗ | ΦΥΣΙΚΟ |
UNLEADED GASOLINE - Με Βιοσυστατικό
| DENSITITY AT 15oC | EN ISO 12185 | 0,7382 | gr/ml |
| EVAPORATED AT 70oC | EN ISO 3405 | 38,1 | %v/v |
| EVAPORATED AT 100oC | EN ISO 3405 | 60,8 | %v/v |
| EVAPORATED AT 150oC | EN ISO 3405 | 90,7 | %v/v |
| FBP | EN ISO 3405 | 180,0 | oC |
| RESIDUE | EN ISO 3405 | 0,9 | %v/v |
| REID VAPOR PRESSURE | EN 13016-1 | 78,2 | KPa |
| VLI | EN 13016-1 | 1049 | |
| SULFUR | EN ISO 20846 | 4,8 | mg/kgr |
| RON | EN 25164 | 96,1 | |
| MON | EN 25163 | 85,4 | |
| LEAD | EN 234 | 0,001 | g/L |
| COPPER CORROSION CLASSIFICATION | EN ISO 2160 | 1 | |
| EXISTENT GUMS | EN ISO 26246 | 2,0 | mg/10ml |
| OXIDATION STABILITY | EN ISO 7536 | >360 | min |
| BENZENE | EN ISO 22854 | 0,76 | %v/v |
| AROMATICS | EN ISO 22854 | 29,5 | %v/v |
| OLEFINS | EN ISO 22854 | 12,3 | %v/v |
| OXYGEN CONTENT | EN ISO 22854 | 1,44 | %m/m |
| MANGANESE | EN 16135 | 0,0 | mg/it |
| APPEARENCE | ΟΠΤΙΚΗ ΕΚΤΙΜΗΣΗ | Β/C | |
| TOTAL ETHRERS | EN ISO 22854 | 8,5 | %v/v |
| EETHYL TERTIARY BUTYL ETHER (BIO) | EN ISO 22854 | 1,44 | %v/v |
| ETHANOL(BIO) | EN ISO 22854 | 0 | %v/v |
| QUINIZARIN | IP 298 | 3 | mg/L |
| COLOR | ΟΠΤΙΚΗ ΕΚΤΙΜΗΣΗ | ΦΥΣΙΚΟ |
FUEL OIL NO 1
| DENSITITY AT 15oC | EN ISO 3675 | 0,9730 | gr/ml |
| KINEMATIC VISCOSITY AT 50oC | ISO 3104 | 176,0 | cSt |
| SULFUR | ISO 8754 | 0,870 | %m/m |
| FLASH POINT | EN 22719 | 79,0 | oC |
| POUR POINT | ISO 3016 | -15,0 | oC |
| WATER | ISO 3733 | 0,20 | %m/m |
| TOTAL SEDIMENT | ASTM D-4870 | 0,05 | %m/m |
| ASH | EN ISO 6245 | 0,04 | %m/m |
| MICROCARBON REDIDE | EN ISO 10370 | 10,41 | %m/m |
| VANADIUM | IP 288 | 36,9 | mg/Kg |
| SODIUM | IP 288 | 22,2 | mg/Kg |
| NET CALORIFIC VALUE | ASTM D-4368 | 9744 | Kcal/kg |
| HYDROGEN SULFIDE | IP 570 | Ppm m/m |
FUEL OIL NO 1
| DENSITITY AT 15oC | EN ISO 3675 | 0,9478 | gr/ml |
| KINEMATIC VISCOSITY AT 50oC | ISO 3104 | 201,0 | cSt |
| SULFUR | ISO 8754 | 0,460 | %m/m |
| FLASH POINT | EN 22719 | >100 | oC |
| POUR POINT | ISO 3016 | 0,0 | oC |
| WATER | ISO 3733 | 0,05 | %m/m |
| TOTAL SEDIMENT | ASTM D-4870 | 0,05 | %m/m |
| ASH | EN ISO 6245 | 0,04 | %m/m |
| MICROCARBON REDIDE | EN ISO 10370 | 7 | %m/m |
| VANADIUM | IP 288 | 19,3 | mg/Kg |
| SODIUM | IP 288 | 6,1 | mg/Kg |
| NET CALORIFIC VALUE | ASTM D-4368 | 9872 | Kcal/kg |
| HYDROGEN SULFIDE | IP 570 | Ppm m/m |
ASPHALT 35/40
| PENETRATION 25oC | EN 1426 | 38,0 | 1/10 mm |
| SOFTENING POINT | EN 1427 | 52,6 | oC |
| FLASH POINT | EN ISO 2952 | >250 | oC |
| FLASH POINT | EN ISO 2719 | >250 | oC |
| SOLUBILITY IN TOLUENE | EN 12592 | 99,6 | % m/m |
| CHANGE OF MASS AFTER RTFOT | EN 12607-1 | 0,4 | % m/m |
| PENETRATION AFTER RTFOT | EN 12607-1 | 23 | 1/1 mm |
| SOFTENING POINT AFTER RTFOT | EN 12607-1 | 54,9 | oC |
ASPHALT 50/70
| PENETRATION 25oC | EN 1426 | 63.0 | 1/10 mm |
| SOFTENING POINT | EN 1427 | 48.7 | oC |
| FLASH POINT | EN ISO 2952 | >250 | oC |
| FLASH POINT | EN ISO 2719 | >250 | oC |
| SOLUBILITY IN TOLUENE | EN 12592 | 99.60 | % m/m |
| CHANGE OF MASS AFTER RTFOT | EN 12607-1 | 0.40 | % m/m |
| PENETRATION AFTER RTFOT | EN 12607-1 | 38 | 1/1 mm |
| SOFTENING POINT AFTER RTFOT | EN 12607-1 | 51.0 | oC |
JET A-1
| PROPERTY | RUSULT | LIMITS | TEST METHOD
ASTM OR IP |
| QUALITY OF FUEL IN THE TANK, m3 | 9164 | ||
| APPEARANCE
VISUAL APPEARANCE, AT AMPIENT TEMPPERATURE SAYBOLT COLOR PARTICULATE CONTAMINATION,MG/L CUMULATIVE CHANNEL PARTICALE COUNTS/ml >4μm individual channel counts >6μm “ >14μm ‘’ >21μm ‘’ >25μm “ >30μm ‘’ ISO CODE |
CLEAR, BRIGHT AND VISUALLY FREE FROM SOLID MATTER AND UNDISSOLVED WATER
+21 0.30 446 152 17 5 2 1 16/14/11/09/08/07 |
C/B
REPORT 1.0 MAX REPORT |
VISUAL
D 156 D 5452 IP 565 |
| COMPOSITION
TOTAL ACICIDTY, mg KOH/g *TOTAL AROMATICS, % v/v SULFUR, MERCAPTAN,% m/m OR DOCTOR TEST REFINERY COMPONENTS AT POINTS OF MANUFACTURE: NON HYDROPROCESSED COMPONENTS % v/v MILDLY HYDROPROCESSED COMPONENTS % v/v SEVERELY HYDROPROCESSED COMPONENTS % v/v SYNTHETIC COMPONENTS % v/v |
0.0050
17.3 0.23 0.0021 94.1 4.9 1.0 Nil |
0.015 MAX
26.5 MAX 0.30 MAX 0.003 MAX NEGATIVE REPORT |
D 3242
D 6379 D4294D3227 D 4952 |
| VOLATILITY
DISTILLATIOM INITIAL BOILING POINTS, °C 10 % v/v RECOVERD, °C 50% v/v RECOVERD, °C 90% v/v RECOVERD, °C END POINT, °C RESIDUE, % v/v LOSS, % v/v *FLASH POINTS, °C DENSITY AT 15°C, kg/L |
153.3
171.1 194.9 231.4 251.9 1.0 0.9 42.0 0.7941 |
REPORT
205 MAX REPORT REPORT 300 MAX 1.5 MAX 1.5 MAX 40 MIN 0,775-0.840 |
D 86
D56 D 4052 |
| FLUIIDITY
*FREEZING POINT, °C VISCOSITY AT -20°C,cst (mm2/s) |
-54.3
3.7 |
-47 MAX
8 MAX |
D 5972
D 445 |
| PROPERTY | RUSULT | LIMITS | TEST METHOD
ASTM OR IP |
| COMBUSTION
NET HEAT OF COMBUSTION, MJ/Kg (SPESICIFIC ENERGY, NET) SMOKE POINT, mm OR SMOKE POINT, mm AND NAPHITHALENES,% v/v |
43.270 25.0 – – |
42.8 MIN 25 MIN 18 MIN 3 MAX |
D 3338 D 1322 D1322 D1840 |
| CORROSION
CCOPPERR STRIP(2H,100 °C), CLASSFICATION |
1 |
1 MAX |
D 130 |
| THERMAL STABILITY
JFTOT CONTROL TEMPERATURE,°C FILTER PRESSURE DIFFERENTIAL, mm Hg TUBE DEPOSIT RATING VISUAL “P” OR “A” DEPOSITS |
280 0.1 1 NO |
MIN 260 25 MAX <3 MAX NO |
D 3241 Annex B Annex B |
| CONTAMINANTS
EXISTEMENT GUM, mg/100 ml |
2.0 |
7 MAX |
D 381 |
| WATER SEPARATION CHARECTERISTICS
MICROSEPAROMETER (MSEP), RATING FUEL WITH SDA FUEL WITOUT SDA |
80 |
70 MIN 85 MIN |
D 3948 |
| CONDUCTIVITY
ELECTRICAL CONDUCTIVITY, pS/m, AT 25°C (FUEL WITH SDA) |
470 |
50-600 |
D 2624 |
| ADDITIVITY
ANTIOXIDANT(KEROBIT TP26RDE/Q/609), mg/I ON HYDROPROCESSED STATIC DISSIPATOR (STATIS 450) mg/I LUBRICITY IMPRONER ADDITIVE (RDE/A/662), mg/1 |
18 1.7 11 |
17-24 3 MAX 9-23 |
|
| INCIDENTAL MATERIALS
FAME,mg/kg |
<2.0 |
50 max |
IP 583 |
| LUBRICITY
BOCLE WEAR SCAR DIAMETER, mm |
N.A. |
0.85 MAX |
D 5001 |
MARINE DISTILLATE FUEL
| DENSITITY AT 15oC | EN ISO 12185 | 0,8554 | gr/ml |
| 10% RECOVERD | EN ISO 3405 | 217,4 | oC |
| 50% RECOVERD | EN ISO 3405 | 286,2 | oC |
| 90% RECOVERD | EN ISO 3405 | 359,2 | oC |
| 95% RECOVERD | EN ISO 3405 | 375,9 | oC |
| SULFUR | ISO 8754 | 0,092 | %m/m |
| POUR POINT | ISO 3016 | <-18 | oC |
| CETANE INDEX | ISO 4264 | 48,2 | |
| ASH | EN ISO 6245 | 0,005 | %m/m |
| FLASH POINT | EN 22719 | 72,0 | oC |
| KINEMATIC VISCOSITY AT 40oc | ISO 3104 | 3,4 | cSt |
| MICROCARBON RECIDUE ON 10% DIST. RESIDUE | EN ISO 10370 | 0,02 | %m/m |
| ACID NUMBER | ASTM D 664 | 0,08 | mgKOH/g |
| TOTAL INSOLUBIES | EN ISO 12205 | <20 | mg/L |
| WATER | EN ISO 12937 | 200 | mg/kg |
| COLOR | ASTM D-1500 | ΜΑΥΡΟ | |
| QUINIZARIN | IP 298 | 3 | mg/L |
| HYDROGEN SULFIDE | IP 570 | 0,3 | ppm m/m |
MARINE DISTILLATE FUEL
| DENSITITY AT 15oC | EN ISO 12185 | 0.8702 | gr/ml |
| 10% RECOVERD | EN ISO 3405 | 229.4 | oC |
| 50% RECOVERD | EN ISO 3405 | 314.8 | oC |
| 90% RECOVERD | EN ISO 3405 | 375.9 | oC |
| 95% RECOVERD | EN ISO 3405 | 389.4 | oC |
| SULFUR | ISO 8754 | 0.0950 | %m/m |
| POUR POINT | ISO 3016 | -15.0 | oC |
| ACID NUMBER | ASTM D-664 | 0.080 | mgKOH/g |
| CETANE INDEX | ISO 4264 | 46.6 | |
| ASH | EN ISO 6245 | 0.005 | %m/m |
| FLASH POINT | EN 22719 | 83.0 | oC |
| KINEMATIC VISCOSITY AT 40oc | ISO 3104 | 4.8 | cSt |
| MICROCARBON RECIDUE ON 10% DIST. RESIDUE | EN ISO 10370 | 0.02 | %m/m |
| COLOR | ΜΑΥΡΟ | ||
| QUINIZARIN | IP 298 | 3.0 | mg/L |
| TOTAL INSOLUBIES | EN ISO 12205 | <20 | mg/L |
| WATER | EN ISO 12937 | 200.0 | mg/Kg |
| HYDROGEN SULFIDE | IP 570 | 0.30 | ppm m/m |
MARINE DISTILLATE FUEL
| DENSITITY AT 15oC | EN ISO 12185 | 0.8550 | gr/ml |
| 10% RECOVERD | EN ISO 3405 | 216.5 | oC |
| 50% RECOVERD | EN ISO 3405 | 287.2 | oC |
| 90% RECOVERD | EN ISO 3405 | 360.9 | oC |
| 95% RECOVERD | EN ISO 3405 | 379.0 | oC |
| SULFUR | ISO 8754 | 0.0910 | %m/m |
| POUR POINT | ISO 3016 | <-18.0 | oC |
| ACID NUMBER | ASTM D-664 | 0.080 | mgKOH/g |
| CETANE INDEX | ISO 4264 | 48.4 | |
| ASH | EN ISO 6245 | 0.005 | %m/m |
| FLASH POINT | EN 22719 | 71.0 | oC |
| KINEMATIC VISCOSITY AT 40oc | ISO 3104 | 3.3 | cSt |
| MICROCARBON RECIDUE ON 10% DIST. RESIDUE | EN ISO 10370 | 0.02 | %m/m |
| COLOR | ΜΑΥΡΟ | ||
| QUINIZARIN | IP 298 | 3.0 | mg/L |
| TOTAL INSOLUBIES | EN ISO 12205 | <20 | mg/L |
| WATER | EN ISO 12937 | 160.00 | mg/Kg |
| HYDROGEN SULFIDE | IP 570 | 0.30 | ppm m/m |
MARINE RESIDUAL FUELS
| DENSITITY AT 15oC | EN ISO 3675 | 0,9834 | gr/ml |
| KINEMATIC VISCOSITY AT 50oC | ISO 3104 | 173,0 | cSt |
| CCAI | 853,0 | ||
| SULFUR | ISO 8754 | 3,210 | %m/m |
| FLASH POINT | EN 22719 | 77,0 | oC |
| POUR POINT | ISO 3016 | -12,0 | oC |
| WATER | ISO 3733 | 0,2 | %m/m |
| POTENTIAL SEDIMENT | ISO 10307-2 | 0,04 | %m/m |
| ASH | EN ISO 6245 | 0,04 | %m/m |
| ACID NUMBER | ASTM D-664 | 0,17 | mgKOH/g |
| MICROCARBON RECIDUE | EN ISO 10370 | 13,4 | %m/m |
| VANADIUM | IP 470 | 142 | mg/Kg |
| SODIUM | IP 470 | 35 | mg/Kg |
| ALUMINUM AND SILICON | ISO 10478 | 22 | 19,4 |
| NET CALORIFIC VALUE | ASTM D-4868 | 9533 | Kcal/kg |
| ZINC | IP 470 | 3 | mg/Kg |
| CALCIUM | IP 470 | 7 | mg/Kg |
| PHOSPHORUS | IP 470 | 3,5 | mg/Kg |
| HYDROGEN SULFIDE | IP 570 | 0,3 | ppm m/m |
MARINE RESIDUAL FUELS
| DENSITITY AT 15oC | EN ISO 3675 | 0,9730 | gr/ml |
| KINEMATIC VISCOSITY AT 50oC | ISO 3104 | 176,0 | cSt |
| CCAI | 842 | ||
| SULFUR | ISO 8754 | 0,870 | %m/m |
| FLASH POINT | EN 22719 | 79,0 | oC |
| POUR POINT | ISO 3016 | -15 | oC |
| WATER | ISO 3733 | 0,2 | %m/m |
| POTENTIAL SEDIMENT | ISO 10307-2 | 0,06 | %m/m |
| ASH | EN ISO 6245 | 0,04 | %m/m |
| ACID NUMBER | ASTM D-664 | 0,17 | mgKOH/g |
| MICROCARBON RECIDUE | EN ISO 10370 | 10,41 | %m/m |
| VANADIUM | IP 470 | 37,0 | mg/Kg |
| SODIUM | IP 470 | 22 | mg/Kg |
| ALUMINUM AND SILICON | ISO 10478 | 34,7 | 19,4 |
| NET CALORIFIC VALUE | ASTM D-4868 | 9744 | Kcal/kg |
| ZINC | IP 470 | 7 | mg/Kg |
| CALCIUM | IP 470 | 10 | mg/Kg |
| PHOSPHORUS | IP 470 | 5 | mg/Kg |
| HYDROGEN SULFIDE | IP 570 | 0,3 | ppm m/m |
MARINE RESIDUAL FUELS
| DENSITITY AT 15oC | EN ISO 3675 | 0,9478 | gr/ml |
| KINEMATIC VISCOSITY AT 50oC | ISO 3104 | 201,0 | cSt |
| CCAI | 816 | ||
| SULFUR | ISO 8754 | 0,460 | %m/m |
| FLASH POINT | EN 22719 | >100 | oC |
| POUR POINT | ISO 3016 | 0,0 | oC |
| WATER | ISO 3733 | 0,05 | %m/m |
| POTENTIAL SEDIMENT | ISO 10307-2 | 0,06 | %m/m |
| ASH | EN ISO 6245 | 0,04 | %m/m |
| ACID NUMBER | ASTM D-664 | 0,17 | mgKOH/g |
| MICROCARBON RECIDUE | EN ISO 10370 | 7,00 | %m/m |
| VANADIUM | IP 470 | 19,0 | mg/Kg |
| SODIUM | IP 470 | 6 | mg/Kg |
| ALUMINUM AND SILICON | ISO 10478 | 14,3 | 19,4 |
| NET CALORIFIC VALUE | ASTM D-4868 | 9872 | Kcal/kg |
| ZINC | IP 470 | 2 | mg/Kg |
| CALCIUM | IP 470 | 6 | mg/Kg |
| PHOSPHORUS | IP 470 | 2,5 | mg/Kg |
| HYDROGEN SULFIDE | IP 570 | 0,3 | ppm m/m |
MARINE RESIDUAL FUELS
| DENSITITY AT 15oC | EN ISO 3675 | 0,9900 | gr/ml |
| KINEMATIC VISCOSITY AT 50oC | ISO 3104 | 217.0 | cSt |
| CCAI | 857 | ||
| SULFUR | ISO 8754 | 3.4200 | %m/m |
| FLASH POINT | EN 22719 | 71.0 | oC |
| POUR POINT | ISO 3016 | -6.0 | oC |
| WATER | ISO 3733 | 0.30 | %m/m |
| POTENTIAL SEDIMENT | ISO 10307-2 | 0.06 | %m/m |
| ASH | EN ISO 6245 | 0.040 | %m/m |
| ACID NUMBER | ASTM D-664 | 0.170 | mgKOH/g |
| MICROCARBON RECIDUE | EN ISO 10370 | 17.00 | %m/m |
| ALUMINUM AND SILICON | ISO 10478 | 12.8 | mg/Kg |
| NET CALORIFIC VALUE | ASTM D-4868 | 9485 | Kcal/kg |
| VANADIUM | IP 470 | 142 | mg/Kg |
| SODIUM | IP 470 | 23 | mg/Kg |
| CALCIUM | IP 470 | 3 | mg/Kg |
| ZINK | IP 470 | 2 | mg/Kg |
| PHOSPHORUS | IP 470 | 3.0 | mg/Kg |
| HYDROGEN SULFIDE | IP 570 | 0.30 | ppm m/m |