Aviation Jet Fuel (JETA1)
TEST | UNITS | SPECIFICATIONS | METHOD |
|
| D1655 |
|
|
| Degree C (F) |
|
Saybolt Color | Number | Report | D156 |
Total Acid, Max | mgKOH/g | 0.10 | D3242 |
Aromatic Content, Max. | vol % | 25 | D1319 |
Naphthalenes, Max | vol % | 3 | D1840 |
Mercaptan Sulfur, Max. | wt. % | 0.003 | D3227 |
Total Sulfur, Max | wt. % | 0.30 | D4294 |
Initial Boiling Point | Celsius | Report | D86 |
10% Recovery Point, Max | Celsius | 205 (401) | D86 |
20% Recovery Point | Celsius | Report | D86 |
50% Recovery Point | Celsius | Report | D86 |
90% Recovery Point | Celsius | Report | D86 |
Final Boiling Point, Max | Celsius | 300 (572) | D86 |
Residual, Max. | vol % | 1.5 | D86 |
Loss, Max. | vol % | 1.5 | D86 |
Flash Point, Min. | Celsius | 38.0 (100) | D56 |
Viscosity @-20C, Max. | cSt | 8.0 | D445 |
Gravity | API | 37 – 51 | D4052 |
Density @15 C, | kg/m3 | 775 – 840 | D4052 |
Freeze Point, Max. | Celsius | -45.5(-50) Jet A | D5972 |
Freeze Point, Max | Celsius | -47 (-53) Jet A – 1 | D5972 |
Heat Content, Min. | Btu/lb | 18,400 | D3338 |
Net Heat of Combustion, Min | MJ/kg | 42.8 | D3338 |
Smoke Point, Min. | mm | 18.00 | D1322 |
Copper Corrosion, Max | Code | 1 | D130 |
Stability, P, Max. @ 260C | mm HG | 25 | D3241 |
Preheat Code, Max | Code | <3 | D3241 |
Existent Gum, Max | mg/100ml | 7 | IP540 |
Water Separation | MSEP | 85 | D3948 |
Jet Fuel (JP45)
TEST | MEAN UNIT | METHOD | RESULT |
Density at 15℃ | g / ml | ASTM_D4052 | 0.8 / 0.83 |
DIST_D86 / I.B.P. | ℃ | ASTM_D86 | 159.8 |
DIST_D86 / 10% recovered | ℃ | ASTM_D86 | 187.4 |
DIST_D86 / 20% recovered | ℃ | ASIM_D86 | 194.8 |
DIST_D86 / 50% recovered | ℃ | ASTM_D86 | 208.8 |
DIST_D86 / 90% recovered | ℃ | ASTM_De6 | 232.7 |
DIST_D86 / F.B.P. | ℃ | ASTM_D86 | 244.1 |
DIST_D86 / Residue | % vol | ASTM_D86 | 1.2 |
DIST_D86 / Loss | % vol | ASTM_D86 | 1.4 |
Say bolt Color | — | ASTM_D156 | 28 |
Appearance | — | — | Clear & Bright |
Flash Point | ℃ | ASTM_D56 | 51.5 |
Copper Strip Corrosion 2h@100℃ | — | ASTM_D130 | Class 1 |
Acid number | mg KOH / g | ASTM_D3242 | 0.004 |
Virgin Fuel Oil (D6)
METHOD UNITS | TEST | RESULTS | UNIT | |||
ASTM D5002 | Density and Relative Density of Crude Oil and Average API Gravity | 29.7(29.7)Min | API | |||
ASTM D1298-99 | Density @ 15 Deg C | 0.87(0.775) | Kg/t | |||
ASTM D97 | Pour Point of Petroleum Pour Point Pour Point | <-33(-36)BELOW ZERO <-27.4(-32.8)BELOW ZERO |
®C ®F | |||
ASTM D93-IP34 | Pensky-Martens Closed cup Flash Point Corrected Flash Point |
117(137)Min |
®F | |||
ASTM D4294 | Sulfur content in petroleum Product by EDXRSulfur content |
0.38(0.358)Max |
W1% | |||
ASTM D445 | Kinematic/Dynamic viscosity Kinematic viscosity @ 122®F/50®C |
17.83(18.12)Max |
Mm2% | |||
ASTM D6304 | Water content by coulometric Karl Fisher Titration Water content |
0.20(0.7)Max |
W1% | |||
ASTM D482 | Ash from petroleum product Average Ash | 0.279(1.007)Max | W1% | |||
ASTM D2161 | Conversion of kinematic viscosity To SUS/SFS I Saybolt furol Viscosity 122®F |
10.9SFS |
Max | |||
ASTM D5184 | Aluminum and Silicon in Fuel Oils By KP-AES or AAS Aluminum content Silicon content |
102(max) 93(max) |
Mg/kg Mg/kg | |||
ASTM D95 | Water by Distillation Vol% | 0.70(Max) | Vol% | |||
ASTM D4530.06 | Carbon Residue | 1.11(max) | W1% | |||
Method Test Result Unit | ||||||
IP 143 Asphalteness Heptane Insoluble | ||||||
| Asphaltene content | 0.08 | W1% | |||
IP 501 Determination of AL, Si, V, Ni, Fe, Na, Ca, Zn, P in Fuel Oil | ||||||
| Aluminum Silicon Sodium | 372 187 117 | Mg/kg Mg/kg Mg/kg | |||
| Vanadium Calcium Zinc Phosphorus Iron | 1 779 298 4176 545 | Mg/kg Mg/kg Mg/kg Mg/kg Mg/kg |
Diesel Gasoil D2 L-0.2-62 GOST 305-82
COMPONENT | UNIT | MIN | MAX |
Density@ 20 deg C | Kg / m³ | 0.82 | 0.870 |
Colour |
| 0.5 | 1.0 |
Flash point, PMCC | Deg C (°C) | 57 | 62 |
Kinematic viscosity @20 deg C | CST | 3.0 | 6.0 |
Pour point | Deg C (°C) | (*) | -10.0 |
Cloud point | Deg C (°C) | (*) | -5.0 |
Mercaptan sulphur |
|
| 0.004 |
Acidity, mg / 1000 cm³ |
|
| 5 |
Iodine number | g/100g |
| 6 |
Ash | %wt |
| 0.01 |
Total Sulphur | %wt |
| 0.02 |
Copper corrosion | 3hrs@50 deg C | (typical) | 1 A |
CCR on 10% Residues | %wt |
| 0.20 |
Cetane index |
| 45 |
|
Distillation range : |
|
|
|
– 50% Recovered Volume | deg C (°C) |
| 280 |
– 90% Recovered Volume | deg C (°C |
| 360 |
– Bacteria MBC | Fibre / it |
| 500 |
– Bacteria CFU | Fibre / it |
| 1000 |
Diesel EN590 (10PPM) USLD
N | CHARACTERISTICS | Unit | TEST RESULT | TEST METHOD | ||
Min | Max | EN STANDRADS | ASTM STAND | |||
1 | Cetane number | no | 51,0 |
| EN ISO 5165 EN 151 | D 613 |
2 | Cetane Index | Index | 46,0 |
| EN ISO 4264 | D 4737 |
3 | Density at 15°C | kg/m’ | 820 | 840 | EN ISO 3675 EN ISO 12185 | D 4052 D 1298 |
4 | Polycyclic aromatic hydrocarbons | % m/m |
| 11,0 | EN 12916 |
|
5 | Sulphur content | mg/kg |
| 10 | EN ISO 20846 EN ISO 20884 |
|
6 | Distillation |
|
|
|
|
|
| – Recovered @150 65 °C | % Vol |
| 2,0 |
|
|
| – Recovered @25085 °C | % Vol |
| 65,0 | EN ISO 3405;2000 | D86 |
| – Recovered @350 95 °C – Recovered @95 | % Vol °C | 85,0 | 360 |
|
|
7 | Kinematic viscosity at 40°C | mm2/s | 2,00 | 4,50 | EN ISO 3104 | D 445 |
8 | Flash point | °C | 55 |
| EN ISO 2719 | D93 |
9 | Cold filter plugging point (CFPP): (CFPP) Summer | °C |
| -2 | EN116:1997 |
|
| (CFPP) Winter | °C | 50,0 | -12 |
| |
1 | Cloud point: |
|
|
| EN23015:1994 | D 2500 D 5772 |
Summer (1 April to 30 September) | cc | Report | ||||
Winter (1 October to 31 March) | cc |
| +0 | |||
1 | Carbon residue (on 10% distillation residue) | % m/m |
| 0,15 | EN ISO 10370 | D 4530 |
1 | Lubricity, corrected wear scar diameter (corrected WSD 1,4) at 60’C | µm |
| 460 | EN ISO 12156-1 |
|
1 | Water content | mg/kg |
| 200 | EN ISO 12937 |
|
1 | Total, contamination (Solid particles) | mg/kg |
| 15 | EN 12662 |
|
1 | Ash content | % m/m |
| 0,01 | EN ISO 6245 | D 482 |
1 | Corrosion to copper (3h at 50°C) | Indice | 1stClass | EN ISO 2160 | D 130 | |
1 | Oxidation stability | g/m3 |
| 25 | EN ISO 12205 | D 2274 |
1 | Oxidation stability (9) | hours | 20 |
| EN 15751 |
|
1 | FAME Content (10) | % VN |
| 0 | EN 14078 |
|
2 | Colour | ASTM scale |
| 2,0 |
| D 1500 D 6045 |
2 | Aspect |
| Cl | ar | Visual Inspection | D 4176 |
2 | Biodiesel content | % Vol | 4,5 | 7,0 |
|
|
2 | Electrical Conductivity | % m/m |
|
| ISO6297 IP274 | D 2624 |
2 | Total, Acidity | MgKOH/g |
|
|
| D 974-06 |
Mazut M100 10585-99
N R. |
SPECIFICATIONS |
RESULTS |
METHOD | |
TYPICAL |
MAX. | |||
1 |
Relative Viscosity at 80 °C, mm²/s (cSt) |
13.5 |
16.0 |
ASTM D 445 |
Kinematic Viscosity at 80 °C, mm²/s (cSt) |
101.0 |
118.0 |
ASTM D 445 | |
2 |
Relative Viscosity at 100 °C, mm²/s (cSt) |
6.2 |
6.8 |
ASTM D 445 |
Kinematic Viscosity at 100 °C, mm²/s (cSt) |
45.3 |
50.0 |
ASTM D 445 | |
3 |
Ash Content, wt. % |
0.06 |
0.14 |
ASTM D 482 |
4 |
Sediments by Extraction Method, wt. % |
0.02 |
1.0 |
ASTM D 473 |
5 |
Water Content, wt.% |
0.1 |
1.0 |
ASTM D 85 |
6 |
Water Soluble Acid & Alkali Content |
NIL |
— |
GOST 8307 |
7 |
Sulphur, wt.% |
1.2 |
1.8 |
ASTM D 4294 |
8 |
Flash Point (COC), °C, min. |
110 |
180 |
ASTM D 92 |
9 |
Pour Point, °C, |
+18 |
+42 |
GOST 20267 |
10 |
Net Heat of Combustion, KJ/kg (kcal/kg) |
39900 (9530) | 40717 (9726) |
ASTM D 4868 |
11 |
Density, at 20 °C, kg/m3 |
939.1 |
968 |
GOST 3900 |
12 | Conradson Carbon Residue, wt.% |
|
|
|
13 | Water by Distillation % wt | 0.36 | 0.8 | ASTM-D 95 |
Mazut M100 10585-75
COMPONENT RESULT |
| |
Ash content, not more % |
| 0.14 |
Mass fraction of sulphur, not more % |
| |
– Low – sulphur – residual – oil |
| 0.5 Max |
Temperature of the flash, not less ºC in the closed crucible |
| 65 |
In the open crucible ºC |
| 110 min |
The temperature of solidification, not higher ºC |
| 25 |
Kinematics viscosity content |
| 118 Max |
Water |
| 0.5% |
Mechanical impurities |
| Lower Than 0.1% |
Acidity |
| Lower Than 5 mg KOH/100 ml |
Alkalinity |
| Nil |
Gross Calorific Value Kcal/kg / KJ/kg |
| Min 9700/41300 |
Density at 15.0 deg. C Kg/l |
| 0.8900-0.9200 |
Hydrogen Sulfide Content (H2S) pom |
| 0.5 Max |
Carbon Residua |
| Lower Than 7% |
Vanadium (V) ppm |
| 23 |
Aluminum (Al) ppm |
| 5 |
Silicon (Si) ppm |
| 12 |
Nickel (Ni) ppm |
| 29 |
Aspartames m/m |
| 3.6% |
Liquefied Natural Gas GOST 57431-2017
COMPONENT | SUBSTANCE PERMISSIBLE LIMITS |
Gross Heating Value (GCV) range | 9,340 – 10,420 Kcal/SCM (1,050 – 1,170 BTU/SCF) |
Methane | not less than 85.0 Mol % |
Ethane | not more than 9.2 Mol % |
Propane | not more than 3.00 Mol % |
Butanes and heavier | not more than 2.00 Mol % |
Pentanes and heavier | not more than 0.25 Mol % |
Nitrogen | 1.0 molecular % |
Total Sulphur | 10.0 ppm (w) |
Sulphur in form of Hydrogen Sulphide | 10.0 ppm (w) |
Maximum variation in Wobbe Index (WI) [ WI = LHV (Volumetric Basis / (Specific Gravity w.r.t.Air)0.5] | +/- 5.0 % |
Contaminants |
|
(a) Trace Metals |
|
I. Pb + Zn | 0.50 ppm (w) |
ii. Na + K | 0.30 ppm (w) |
iii. Vanadium | 0.50 ppm (w) |
iv. Calcium | 2.0 ppm (w) |
v. Magnesium | 2.0 ppm (w) |
vi. Sum of heavy metals (Hg+V+Pb+Zn+Ni+Others) | 1.0 ppm (w) |
(b) Solids / Particulates |
|
i. Total for particle size up to 10 microns | 20.0 ppm (w) |
ii. For 2 micron < d < 10 microns | 1.50 ppm (w) |
iii. For particle size greater than 10 microns | 0.30 ppm (w) |
(c) Liquid contents | Nil |
(d) Moisture | 112 kg/million SCM |
Hydrogen content | 1.00 % (by volume) |
Acetylene (C2H2) | 0.10 % (by volume) |
Higher Hydrocarbons for n>=3 | 10.0 % (by volume) |
Liquefied Natural Gas
ORIGIN LIQUEFIED PETROLEUM GAS LPG – 50% Propane and 50% Butane Separate | ||||
SPECIFICATION (Butane) | ||||
| PROPERTY | UNITS | TEST METHOD | VALUE |
1 | Ethane | mol % | G.C | 0.08 max |
2 | Propane | mol % | G.C | 2 max |
3 | Total – C4 | mol % | G.C | 97.5 min |
4 | Total – C5 | mol % | G.C | 0.82 max |
5 | Sp. Gr. @ (60°F / 60°F) | – | ASTM D-2598 | To be reported |
6 | Copper Corrosion | – | ASTM D-1838 | No. 1a max |
7 | Total Sulfide | wt.ppm | (ASTM D-3246) | 30 max |
8 | Hydrogen Sulfide | vol.ppm | ASTM D-2420 | Nil |
9 | Vapor Press @ (100°F) | Psig | ASTM D-2598 | 70 max |
10 | Water Content | vol.ppm | Shaw Dew Point | 10 max |
11 | Residue on Evaporation | vol % | ASTM D-2158 | 0.0 max |
| ||||
SPECIFICATION (Propane) | ||||
| PROPERTY | UNITS | TEST METHOD | VALUE |
1 | Ethane | mol % | G.C | 0.4 max |
2 | Propane | mol % | G.C | 98 max |
3 | Butane | mol % | G.C | 1.4 max |
4 | Pentanes & Heavier | mol % | G.C | 0.01 max |
5 | Copper Corrosion | – | ASTM D-1838 | No 1a max |
6 | Hydrogen Sulfide | vol.ppm | ASTM D-2420 / DRAGER | 5 max |
7 | Sp. Gr. @ (60°F / 60°F) | – | ASTM D-2598 | To be reported |
8 | Sulphur (Volatile) | wt.ppm | (Based on ASTM D-3246) | 30 max |
9 | Vapor Pressure @ (100°F) | Psig | ASTM D-2598 | 200 max |
10 | Water Content | – | ASTM D-2713 | pass |
Light Cycle Oil
Properties | Unit | Result | Test Method |
Sulphur content | % | <0.15 | ASTM D4294-10 |
ASH CONTENT | %(MASS) | 0.0005 | ASTM D482 |
CARBON RESIDUE | %(M/M) | 0.0 | ASTM D4530 |
Density (15OC) | Kg/l | 0.8811 | ASTM D1298-12b |
Water Content | % | 0.0 | ASTM D4006 |
Flash point | OC | 63.0 | ASTM D93-15 |
Pour point | OC | -15 | ASTM D97-12 |
Viscosity (40OC) | MM2/S | 2.719 | ASTM D445-15 |
Chroma | ASTM Color | 1.0 | ASTM D1500-12 |
Benzene | % (volume fraction) | <0.10 | ASTM D5580-13 |
Toulene | % (volume fraction) | <1.00 |
|
Xylene | % (volume fraction) | <1.00 |
|
Naphthalene | % (mass fraction) | 1.1 | ASTM D2425-04(2009) |
Total aromatics | % (mass fraction) | 54.4 |
|
Primary distillate | OC | 167.5 | ASTM D86-12 |
5% distillate | OC | 189.9 |
|
10% distillate | OC | 202.1 |
|
50% distillate | OC | 279.9 |
|
90% distillate | OC | 350.8 |
|
95% distillate | OC | 368.1 |
|
Final distillation | OC | 380.9 |
|
Olefin content | % (volume fraction) | 4 | ASTM D1319-14 |
Aromatics content | % (volume fraction) | 56.4 |
|
Saturated hydrocarbon content | % (volume fraction) | 39.6 |
|
Sixteen alkanes index | / | 39.1 | ASTM D976-06 |
Espo Crude Oil
Density at 15oC | kg/L | ASTM D 5002 | 0.8508 |
Specific Gravity at 60/60°F | kg/L | ASTM D 5002 | 0.8512 |
API gravity |
| ASTM D 1250 | 34 |
Kinematic viscosity at 20°C | CST | ASTM D 445 | 6.949 |
Total acid Number | mg KOH/g | ASTM D 664 | <0.050 |
Pour Point | °C | ASTM D 5853 | <=-36 |
Water by distillation | mass% | ASTM D 4006 | 0.35 |
Sediment by extraction | mass % | ASTM D 473 | 0.01 |
Chloride salt content | mg/dm3 | GOST 21534-75(A) | 17 |
Organic chlorine content | mg/kg | ASTM D 4929(B) | *1 |
Sulphur content | mass% | ASTM D 4294 | 0.535 |
Hydrogen Sulphide | ppm | UOP 163 | less 1 |
Mercaptan Sulphur | ppm | UOP 163 | 111 |
Ash content | mass % | ASTM D 482 | 0.011 |
Nickel | ppm | IP 470 | 4 |
Sodium | ppm | IP 470 | 1 |
Iron | ppm | IP 470 | 19 |
Copper | ppm | AAS | less 1 |
Vanadium | ppm | IP 470 | 4 |
Calcium | ppm | IP 470 | 2 |
Paraffin Wax content | mass % | UOP 46 | 3.3 |
RVPE | kPa | ASTM D 5191 | 40.4 |
Asphaltenes (heptane | mass % | IP 143 | 0.2 |
insolubles) content |
|
|
|
Export Blend Crude Oil Rebco (Specification GOST 9965 -76)
Density At 20 Deg C Kg/M | % | Max | 0.870 |
Sulphur Content | % | Max | 1.8 |
Parafin Content | % | Max | 1.8 |
Water And Sedment | % | Max | 1.2 |
Ash Content | % | Max | 0,05 |
Chloride Content | % | Max | 100 |
DISTILATION: | |||
Up To 200 Degrees C. | % | Max | 21 |
Up To 300 Degrees C. | % | Max | 41 |
Up To 350 Degrees C. | % | Max | 50 |
INDEX APT At 20C Degrees | % | Max | 32,00 |
Salts Content, Mg/L | % | Max | 100 |
Export Blend Ccrude Oil Rebco (Sspecification GOST 9965 -76)
EXPORT BLEND CRUDE OIL REBCO (SPECIFICATION GOST 51858-2002) | |||
CHARACTERISTICS | UNITS | RESULT | TEST METHOD |
Density (Specific Gravity) @ 20 °C | g /sm3 | 0.870 | ASTM D5002 |
Sulphur Content max | wt.% | 1.8 | ASTM D4294 |
Paraffin Content max | % | 1.8 | ASTM D5443 |
Water & Sediment Content max | vol. % | 1.2 | ASTM D4007 |
Distillated recovered max | % |
| ASTM 86 |
@ 200°C |
| 21.0 |
|
@ 300°C |
| 41.0 |
|
@ 350°C |
| 50.0 |
|
Chlorine Salt Content max | mg/dm3 | 100 | ASTM D3230 |
Density API | °API | 32.0 | ASTM D5002 |
Salts Content as NaCl | mg /l | 17.3 | ASTM D3230 |
Ash Content max | wt.% | 0.05 | ASTM D482 |
Mercaptans | mg/kg | <1 | ASTM D3227 |
Pour Point | °C | 15 | ASTM D5863 |
Kinematic Viscosity CST @ 20°C | mm2 /s | 4.92 | ASTM D455 |
Hydrogen Sulfide | mg/kg | <1 | ASTM D3227 |
Asphaltenes | % | 0.9 | ASTM D6560 |
Nitrogen | mg /l | 342 | ASTM D4629 |
KOH Number | mg/g | 0.39 | ASTM D8045 -17 |