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LPG
PROPANE
LPG MIXTURE
LPG AUTOMOTIVE
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)
UNLEADED 95 RON (BIO)
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
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)
DIESEL AUTOMOTIVE
DIESEL HEATING
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
FUEL OIL No1
MARINE RESIDUAL FUELS 380
MARINE RESIDUAL FUELS 180
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
50/70
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 |
AUTOMOTIVE DIESEL
AUTOMOTIVE DIESEL
HEATING DESIEL
UNLEADED 100 RON - Με Βιοσυστατικό
UNLEADED GASOLINE - Με Βιοσυστατικό
FUEL OIL NO 1
FUEL OIL NO 1
ASPHALT 35/40
ASPHALT 50/70
JET A-1
MARINE DISTILLATE FUEL
MARINE DISTILLATE FUEL
MARINE DISTILLATE FUEL
MARINE RESIDUAL FUELS
MARINE RESIDUAL FUELS
MARINE RESIDUAL FUELS
MARINE RESIDUAL FUELS
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 |