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Products

Origin of Product: Russia

TEST	MEAN UNIT	METHOD	RESULT
Density at 15	g /ml	ASTM _D4052	0.8 /0.83
DIST_D86/1.B.P	----	ASTM_D86	159.8
DIS_D86/10% recovered	----	ASTM_D86	187.4
DIST_D86/20% recovered	----	ASTM_D86	194.8
DIST_D86/50% recovered	----	ASTM_D86	208.8
DIST_D86/90% recovered	----	ASTM_Deb	232.7
DIST_D86/F.B.P	----	ASTM_D86	244.1
DIST_D86/ Residue	----	ASTM_D86	1.2
DIST_D86/ Loss	----	ASTM_D86	1.4
Say bolt Color	% vol	ASTM_D156	28
Appearance	% vol	ASTM_D56	Clear&Bright
Flash Point	----	ASTM_D56	51.5
Copper Strip Corrosion 2h@100	----	ASTM_D130	Class1
Acid number	mg KOH /g	ASTM_D3242	0.004
Total Sulphur	% w / w	IS08754	0.12
Mercaptan Sulphur	% w / w	ASTM_D3227	0.0005
Existent Gum	mg/100 MI	ASTM_D381	1
FIA / Aromatics	% vol	D1319_95	16.5
Water Reaction:Interface Rating	----	----	1
Net Heat of Specifice Energy	MI /kg	ASTM_D3338	43.222
Freezing Point	----	ASTM_D2386	-43.5
Kinematics Viscosity @-20	CST	IS03104	6.86

Origin of Product: Russia
LOWEST SULPHUR CONTENT (0.02%)

TEST ITEM	TEST METHOD	LIMITS
Appearance	Visual	C & B
Calculated Cetane	ASTM D 976-91	Min 47
API Gravity @ 60° F Upper	ASTM D 4052-96	Report
API Gravity @ 60° F Lower	ASTM D 4052-96	Report
Specific Gravity @ 15.6/15.6°C Upper	ASTM D 4052-96	0.82-0.84
Specific Gravity @ 15.6/15.6°C Lower	ASTM D 4052-96	0.82-0.84
Kinematics Viscosity @ 40°C	ASTM D 445-01	1.8-4.1
Pour Point° C	ASTM D 97-96	min -10
Sulphur Content % WL	ASTM D 5453-00	max 0.02%
Water and Sediment % vol.	ASTM D 2709-96	max 0.05
Flash Point (P.M.) ° C	ASTM D 93-00	min 52
Distillation :Initial Boiling Point° C	ASTM D 86-01	Report
Distillation :10% Boiling Point° C	ASTM D 86-01	Report
Distillation :50% Boiling Point° C	ASTM D 86-01	Report
Distillation: 90% Boiling Point° C	ASTM D 86-01	max-357
Colour ASTM	ASTM D 1500-98	max 2.0

Origin of Product: Russia, CIS (Kazakhstan, Azerbaijan, Turkmenistan)
LOWEST SULPHUR CONTENT (0.02%)

COMPONENT RESULT

Ash content, not more % 0,14

Mass fraction of sulphur, not more % - low sulphur residual oil 0,5

Temperature of the flash, not less ºC in the closed crucible In the open crucible ºC 110 min

The temperature of solidification, not higher ºC 25

Kinematics viscosity 118 max

Water content 0.5%

Mechanical impurities Lower than 0.1%

Acidity Lower than 5 mg KOH/ 100ml

Alkalinity nil

Gross Calorific Value Kcal/kg / KJ/kg Min9200/41300

Density at 15.0 deg. C Kg/l 0.8900-0.9200

Hydrogen Sulfide Content (H2S) pom 0.5 max

Carbon Residual Lower than 7%

Vanadium (V) ppm 123

Aluminium (Al) ppm 5

Silikon (Si) ppm 12

Nickel (Ni) ppm 49

Asphaltenes m/m 3.6%

Destilation @4 mm Hg

Extracted to 760 mm Hg

Initial Boiling Point deg. C 216

5% recovered deg. C 259

10% recovered deg. C 310

20% recovered deg. C 358

30% recovered deg. C 445

40% recovered deg. C 502

Crude Petroleum
Origin of the Product:
Russia
CIS (Kazakhstan, Azerbaijan)
Kuwait
UAE
Saudia