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Bonny Light Oil
Bonny Light oil is a high grade of Nigerian crude
oil with high API gravity (low specific gravity),
produced in the Niger Delta basin and named after
the prolific region around the city of Bonny.
The very low sulphur content of Bonny Light crude
makes it a highly desired grade for its low
corrosiveness to refinery infrastructure and the
lower environmental impact of its byproducts in
refinery effluent.
Other grades of Nigerian crude oil are Qua Ibo crude
oil, Brass River crude oil, and Forcados crude oil.
The Cabinda crude oil is a common grade of crude oil
produced in Angola.
Heavy crude oil or Extra Heavy oil
Heavy crude oil or Extra Heavy oil is any type of
crude oil which does not flow easily. It is a
relative term, compared to light crude oil, but
relates to specific technical issues of its own on
production, transportation, and refining. Physical
properties that distinguish heavy crudes from
lighter ones include higher viscosity and specific
gravity, as well as heavier molecular composition.
Extra heavy oil from the area north of the Orinoco
river in Venezula, which has by far the largest
volume of the 30 or more countries with known
reserves[1], has a viscosity of over 10,000
centipoise and 10° API specific gravity.[2]
Generally a diluent is added at regular distances in
a pipeline carrying heavy crude to facilitate its
flow.
Some petroleum geologists categorize bitumen from
tar sands as extra heavy oil although bitumen does
not flow at ambient conditions.
Specification of Heavy Fuel Oil MAZUT M100 (GOST
10585/75)
COMPONENT...............................................................
RESULT
Ash content, not more %
....................................................
0.14
Mass fraction of sulphur, not more % - low sulphur
residual oil..
0.8
Temperature of the flash, oC in the open
crucible oC........... 110 Min
The temperature of pour point, not higher oC
........................... 25
Kinematics
viscosity......................................................
118 max
Water content,
%..................................................................
0.5
Mechanical impurities, Lower than
%...................................... 0.1
Acidity Lower than, mg KOH/
100ml.......................................... 5
Alkalinity...............................................................................
nil
Gross Calorific Value, Kcal/kg /
KJ/kg................... 9200/41300 Min
Density at 15.0 oC Kg/l
.........................................
0.8800-0.9000
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
Distillation
@................................................................
4 mm Hg
Extracted to
............................................................
760 mm Hg
Initial Boiling Point deg. C
....................................................
216
5% recovered deg. C
..........................................................
259
10% recovered deg. C
.........................................................
310
24% recovered deg. C
.........................................................
358
30% recovered deg. C
.........................................................
445
40% recovered deg. C
.........................................................
502
50% recovered deg. C
.........................................................
534
60% recovered deg. C
.........................................................
538
75% recovered deg. C
.........................................................
545
80% recovered deg. C
.............................................................
-
95% recovered deg. C
.........................................................
550
End Boiling Point deg.
C........................................................
560
Percent Recovered vol........................................................
78%
Total Nitrogen
m/m........................................................
0.192%
Sodium (Na) ppm.............................................................
15
Specifications: GOST 305/82
1. Density at 20oC,
Kg/m3..................................... Max 860
2. Fraction composition (Distillation):
a. 50% distilled at
Co................................ Max 280
b. 96% distilled at
Co................................ Max 360
3. Cetane Index,
min...............................................
Min 45
4. Kinematic Viscosity at 20 Co, mm2 (cst)...
Min/Max 3.6-6.0
5. Acidity, mg KON for 100 cm3 of
fuel..................... Max 10
6. Ash Contents
%............................................... Max
0.01
7. Sulfur Contents
%.............................................. Max
0.2
8. Mercaptan Sulfur Contents
%............................ Max 0.02
9. Hydrogen Sulfide
Contents...................................... None
10. Copper Plate
Test................................................
Passed
11. Water Soluble Acids &
Alkalis.................................. None
12. Contents of Mechanical
Impurities............................ None
13. Water
Contents......................................................
None
14. Flash Point Determined in a Closed Cap,
20 Co...... Min. 62
15. Pour point,
Co...................................................
Max –10
16. Turbidity Temperature,
Co................................... Max –5
17. Iodine Number, g/iodine per 100 g of
fuel............... Max 5
18. Actual Resins, mg per 100 cm3 of
fuel.................. Max 25
19. Coking Capability of 10% residue,
%................... Max 0.2
20. Color ASTM
......................................................
Max 2.0
SPECIFICATIONS
for Russian Origin Gas Oil 0.2/62 (GOST 305-82)
|
Component |
Unit |
Min. |
Max. |
|
Density@
20 deg C |
Kg/m3 |
|
0,870 |
|
Colour |
|
|
2,0 |
|
Flash
point, PMCC |
deg C (
ºC ) |
57 |
62 |
|
Kinematic viscosity @20 deg C |
C ST |
3,0 |
6,0 |
|
Pour
point |
deg C (
ºC ) |
(*) |
-10,0 |
|
Cloud
point |
deg C (
ºC ) |
(*) |
-5,0 |
|
Mercaptan sulphur |
|
|
0,01 |
|
Acidity,
mg / 1000 cm3 |
|
|
5 |
|
Iodine
number |
g/100g |
|
6 |
|
Ash |
|
%wt |
0,01 |
|
Total
Sulphur |
%wt |
0,02 |
0,05 |
|
Copper
corrosion |
3
hrs@50
deg C |
(typical) |
1 A |
|
CCR on
10% Residues |
%wt |
|
0.20 |
|
Cetane
index |
|
45 |
|
|
Distillation range : |
|
|
|
|
- 50%
Recovered Volume |
deg C (
ºC ) |
|
280 |
|
- 90%
Recovered Volume |
deg C (
ºC ) |
|
360 |
|
-
Bacteria MBC |
Fibre /
it |
|
500 |
|
-
Bacteria CFU |
Fibre /
it |
|
1000 |
Kuwaiti Crude Oil
From a chemical composition standpoint, every
accumulation of crude oil is unique; its composition
is not exactly matched by other accumulations even
if they are apparently from the same oil field.
Fields are often made up of several unconnected
pockets in individual strata or locations.
While the specific compositions of crude oils
vary from field to field. The table below
shows the general chemical characteristics of
Kuwaiti crude oil:
Chemical composition of Kuwaiti crude oil
|
Constituent |
Quantity |
|
Sulfur |
2.44% by weight |
|
Nitrogen |
0.14% by weight |
|
Nickel |
7.7 ppm |
|
Vanadium |
28 ppm |
|
Naptha fraction (boiling pt. from 20 to
205° C) |
22.7% by weight |
|
High boiling fraction (boiling pt. above
205° C) |
77.3% |
|
Aromatics |
23.3% by weight |
|
Parrafins |
20.9% by weight |
|
Insolubles |
3.5% by weight |
|