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Specifications


Aviation Kerosene (RT) specification (GOCT 10227-86)

1. Density @ 20 C kg/cm, min 775

2. Fractionation:
a) distillation point, C max 150
b) 10% of distillation, C max 165
c) 50% of distillation, C max 195
d) 90% of distillation, C max 230
e) 98% of distillation, C max 250

3. Kinematics viscosity, mm / c / c Ct @ 20 C min 1,25/ 1,25
@ 40 C min 8 / 8

4. Caloricity lowest point, kdg/kg min 42900

5. Free-smock flame, mm min 25

6. Acidity, mg/ 100 cm max 0,7

7. Iodine number, mg/ 100 gr 3,5

8. Flash temperature in a crucible, C min 28

9. Crystallization, C max -50

10. Thermal stability in static condition, 150C max
a) 4 hours sediment, mg/ 100 cm 10
b) 5 hours sediment, mg/ 100 cm 18

11. Aromatic hydrocarbons, % max 22

12. Non-deluded resin concentration, mg/ 100 cm max 5

13. Sulfur, % max 0,25

14. Hydrogen, % non

15. Cooper plate test 3 hours @ 100 C positive

16. Ash, % max 0,003

17. Water-dissoluble acids and alkalis non

18. Naphtane acids soups non

19. Mechanical contaminants non

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Specifications for Es Sider Light Crude oil (Libya)

   
Method
Density @ 15 C 0.8395 JP 365/D4052
Specific Gravity @ 60F 0.84 Calculation
API Gravity 37.0 Calculation
Total Sulphur % wt 0.39 IP 336/4294
Pour point C (F) +9 (+48) IP 15/D97
Ash Content %wt <0.01 IP 4/D482
Viscosity @ 70 F. cst 11.59 IP 71/D445
Viscosity @ 100 F. cst 4.867 IP 71/D445
Total Nitrogen % wt 0.17 IP 379 MOD/D4629MOD
Flash Point C (F) Below-20 (Below –4) IP 170
Characterisation factor 12.1 Calculation
Asphatenes % wt 0.53 IP 143
Hydrogen Sulphide ppm wt. <1 IP PM-BJ
Neutralisation Number, mg KOH/g 0.20 IP 177/D664
Bottom, Sediment and Water % vol <0.05 IP 359/D4007
Salt/as NaCI) mg/litre 20.0 (7.0) D3230

Fuel Specifications Sarir Crude Oil

Specifications for SARIR Crude Oil
 
Method
Density @ 15 C 0.8374 JP 365/D4052
Specific Gravity @ 60F 1.4 (4.0) Calculation
API Gravity 37.48 Calculation
Total Sulphur % wt 0.17 IP 336/4294
Pour point C (F) +21 (+70) IP 15/D97
Ash Content %wt <0.01 IP 4/D482
Viscosity @ 70 F. cst 67.54 IP 71/D445
Viscosity @ 100 F. cst 10.73 IP 71/D445
Total Nitrogen % wt 0.10 IP 379 MOD/D4629MOD
Flash Point C (F) Below-20 (Below –4) IP 170
Characterisation factor 12.5 Calculation
Asphatenes % wt 0.30 IP 143
Hydrogen Sulphide ppm wt. <1 IP PM-BJ
Neutralisation Number, mg KOH/g 0.085 IP 177/D664
Bottom, Sediment and Water % vol <0.05 IP 359/D4007
Salt/as NaCI) mg/litre 1.4 (4.0) D3230

Iranian Heavy Crude Oil

API 30.60 Max
Sulphur 1.8% WT PCT Max
Pour Point -11 C
Viscosity (CST) 10.38 @ 70 F 4.22 @ 130 F
Ash Content 5.00 PPM
Volume PCT 45c in 300 PCT
Kinematic Viscosity 25c 40c 60c
Carbon residue 5% WT PCT
Total acid number mg KOH 0.6 MG
Nickel 81 PPM
Iron 30 PPm
Vanadium 64 PPM
Resins 1.8% WT PCT max
Water content 0.10%
Water & Sediment 0.60%

Iranian Light Crude Oil Specifications

Gravity @15.6 C deg. g/cm, max 0.8551
API, max 33.8
Sulphur content, WT %, max 1.2-1.4%
Water and Sediment content, vol %, max 0.001
Water content, vol %, max 0.004
Salt content, Lb. 100.0 brl, max 4.3
Conradson carbon, WT %, max 49
R.V.P., Kg/SQ Cm 0.28
Pour point, Deg. 34
Ash content, WT %, max Nil
Neutralization Kg/sq Cm 0.24
ASTM Distillation: 3.70
Recovery at: 50 C deg. VM %, min 0.80
100 C deg 8.00
200 C deg. 28.00
250 C deg. 37.00
300 C deg 46.00
Total distillation 47.00
Total residue, max 52.50


M-100

STRAIGHT RUN FUEL OIL:
(GOST 10585-99)

Name of Characteristic
Guarantees
Density at 20 deg. Celsius, Kg/m3
957
Viscosity at 80 deg.C, BY
16.0
Vviscosity at 100 deg.C, BY
6.8
Pour Point deg. Celsius
25
Flash Point deg. Celsius
110
Sulfur Content, % wt
2.3
Ash Content, % wt
0.14
Colour
BLACK
Sediment, %WT
1.0
Water soluble acids & alkalisBromine content, g / 100g
NIL
Specific heat combustion,
Kj / kg
40530
Water Content % vol
1.0

Rebco

COMMODITY: RUSSIAN EXPORT BLEND CRUDE OIL (REBCO) IN ACCORDANCE WITH THE INTERNATIONAL SPECIFICATIONS AND STANDARDS FOR SUPPLY SET FORTH IN GOST 9965-75
ORIGIN: NIZHNEVARTOVSK REGION, TYUMEN, WESTERN SIBERIA, RUSSIAN FEDERATION
THE SELLER GUARANTEES THE DELIVERY OF REBCO IN COMPLYING WITH THE FOLLOWING SPECIFICATIONS:
1 Density at 20 degrees C Gr. /cm. Cub. Max. 0.870
2 Sulfur content % max. 1.8
3 Paraffin % max. 6.0
4 Water and Sediment Content % max 1.2
5

Distillation Vol. %

- Up to 200 degrees
- Up to 300 degrees
- Up to 350 degrees

 

Min. 21
Min. 41
Min. 50

6 Salts contents Mg/L max. 100
7 Index API at 20 degrees C 32.00

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Russian Origin Gas OIL 0.2/62

GOST 305-82

COMPONENT
UNIT
RESULTS
Density @ 20° C Kg/m°   .0870
Color     2.0
Flash point, PMCC °C 57 62
Kinematic Viscosity @ 20° C Cst 3.0 6.0
Pour point °C (*) -10.0
Cloud Point °C (*) -5.0
Mercaptan Sulphur     0.01
Acidity, mg/1000 cm     8
Iodine number G/100g   8
Ash % wt   0.01
Total Sulphur % wt   0.2
Copper corrosion (3 hrs @ 50°)     1A
CCR on 10% residues % wt   0.20
Cetane index   45  
Distillation range:      
50% Recovered Volume °C   280
90% Recovered Volume °C   360
Bacteria MBC Fibre/It   500
Bacteria CFU Fibre/It   1000

(*) Summer from March to October (PP –3.0 ° C)
    (CP 0 ° C)
Winter from November to February (FF –10.0 ° C)
    (CP – 5.0 ° CC)

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ULSD / EN590

TEST METHOD    
DENSITY AT 15 DEG C 0.8232 ASTM D 4052
SULPHUR PPM 6.548 ASTM D 5453
CLOUD POINT DEG C -10 MIN ASTM D 5773
CFPP DEG C -15 MIN IP 309
FLASH POINT DEG C 66.7 ASTM D 93
COLOUR BELOW 0.5 ASTM D 1500
APPEARANCE CLEAR AND BRIGHT ASTM D 4176

DISTILLATION DEG C
FBP
98.0 ASTM D 86

VOL.PCT RECOVERED/250 49.4  
VOL.PCT RECOVERED/345 95.5  
CALCULATED CETANE INDEX 53.4 ASTM D 4737
KINEMATIC VISCOSITY
CST AT 40 DEG C
2.332 ASTM D 445
COPPER STRIP CORROSION
3 HRS AT 122 F
1 ASTM D 130
OXIDATIVE STABILITY
MG/100 ML
BELOW 0.01 ASTM D 2274
TOTAL ACID NUMBER
MGKOH/G
0.001 ASTM D 974

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