Al Shaheen Crude Oil 2018
Crude Assay Report
on
Crude sample marked
Date:
Company details :
For the Attention of :
Sample(s) received from : Qatar
Sample(s) submitted as : Al Shaheen Crude Oil 2018
Description(s) on Label(s) : Al Shaheen Crude Oil 2018
Seals on Sample(s) : Nil
Sample(s) received on :
Logistics Base within Gulf Warehousing Company
Al Ghuwairiya Street
Street No. 512
West Side Support Service Area
Outside RLIC Khalifa Gate (Gate no. 2)
Ras Laffan - Qatar
AUTHORIZED SIGNATURE
George Idicula Laboratory Manager,O&P Laboratory
Bureau Veritas
Technopark – Plot 010407
Jebel Ali, Dubai, U.A.E
Please refer attached sheets for analysis report.
LABORATORY REPORT NO. IDL 5579/2018
December 21, 2018
The above sample(s) was/were examined and the following results obtained:
NORTH OIL COMPANY
21 November, 2018
Sl.No. Page No.
1 Front Cover 1
2 Title 2
3 Index 3
4 Main Assay Properties 4
5 True Boiling Point Distillation Data 5
6 True Boiling Point Distillation data - Graph 6
7 Summary of Product / Residue cut points & Yield 7
8 Summary of True Boiling Point Distillation Cuts - Graph 8
9 Whole Crude Analysis 9
10 Naphtha Cuts - Light Naphtha [IBP/C5/15-70°C] 10
11 Naphtha Cuts - Light Reformer Naphtha [70-165°C] 11
12 Naphtha Cuts - Reformer & Heavy Naphtha [165-195°C] 12
13 Kerosene Cut - Kerosene [195-235°C] 13
14 Vacuum Gas Oil Cuts - Light Gas Oil [235-325°C] 14
15 Vacuum Gas Oil Cuts - Gas Oil [325-370°C] 15
16 Vacuum Gas Oil Cuts - Gas Oil 1[370 - 540°C] 16
17 Vacuum Gas Oil Cuts - Heavy Vacuum Gas Oil [370 - 548°C] 17
18 Residue Cuts - Atmospheric Residue [+370°C] 18
19 Residue Cuts - Vacuum Residue [+548°C] 19
INDEX
Description
LABORATORY REPORT NO. IDL 5579/2018
Al Shaheen Crude Oil 2018
Page No: 3
Al Shaheen Crude Oil 2018
LABORATORY REPORT NO. IDL 5579/2018
Kerosene Cut
Lig
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Na
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Lig
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He
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Ke
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Ga
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CUTS, YIELDS AND DISTILLATIONS 1 2 3 4 5 6 7 8 9 10
Initial BP °C IBP /C5/15 70 165 195 235 325 370 370 370 + 548 +
Final BP °C 70 165 195 235 325 370 540 548
Yield % Wt.ASTM D5236/
ASTM D28923.27 9.58 5.10 5.52 17.65 7.51 22.71 24.79 49.50 24.65
Yield % Vol.ASTM D5236/
ASTM D28924.43 11.35 5.63 5.92 18.14 7.41 21.57 23.55 44.77 21.23
Density @ 15°C kg/LASTM D5002 / D4052 /
D25980.6481 0.7415 0.7951 0.8190 0.8546 0.8909 0.9229 0.9251 0.9713 1.0199
Specific Gravity @ 60/60° F Conversion 0.8790 0.6482 0.7417 0.7954 0.8194 0.8551 0.8914 0.9234 0.9256 0.9718 1.0206
API Gravity @ 60° F ° API Calculated 29.5 86.8 59.3 46.4 41.2 34.0 27.2 21.7 21.4 14.1 7.2
Sulphur Content % Wt. IP 336 / ASTM D4294 2.31 0.0274 0.0897 0.1930 0.304 1.08 2.25 2.49 2.55 3.70 4.87
Mercaptan Sulphur ppm Wt. UOP 163 322 243 356 380 354 69 52
Hydrogen Sulphide ppm Wt. UOP 163 <1 <1 <1
Total Nitrogen ppm Wt. ASTM D4629 / D5762 900 0.3 0.4 0.6 0.9 36 220 639 680 1823 2800
Basic Nitrogen % Wt UOP 269 0.0225 0.0017 0.0063 0.0179 0.0186 0.0484 0.0728
Vapour Pressure psi ASTM D323 / D5191 6.20 14.67 1.81
PIONA Analysis
Total Paraffins 93.0 59.0 62.7
n-Paraffins 34.8 8.3 7.5
iso-Paraffins 58.2 50.7 55.2
Total Olefins <0.1 <0.1 0.5
Total Napthenes 6.9 36.4 15.7
Total Aromatics <0.1 4.6 21.1
Unidentified <0.1 <0.1 <0.1
Research Octane Number (Clear) * ASTM D2699 70.0(2*) 55.0
Pour Point ° C IP 15 / ASTM D97 <-18 <-36 <-36 <-36 +6 +30 +33 +24 +39
Cold Filter Plugging Point ° C IP 309 <-51 -44 -16 +8
Cloud Point ° C IP 219 / ASTM D2500 <-42 <-42 -14 +8
Freeze Point ° C IP 16 /ASTM D2386 -81.5 -53.5
Cetane Index calc. IP 380 /ASTM D976 48.0 45.6
UOP K Factor calc. UOP 375 11.6 11.7 11.6 11.4
Kinematic Viscosity @ 15° C 31.88
Kinematic Viscosity @ 25° C 21.00
Kinematic Viscosity @ 35° C 13.31
Kinematic Viscosity @ 40° C 10.88 0.9690 1.517 3.338 8.472 55.97 62.50 1212 266400*
Kinematic Viscosity @ 55° C 7.203
Kinematic Viscosity @ 100° C 2.957 0.5520 0.7310 1.289 2.300 7.068 7.573 46.62 1131
Kinematic Viscosity @ 135° C ASTM D2170 3.575 3.754 15.90 188.1
Smoke Point mm IP 57 / ASTM D1322 26.0 25.0
Copper corrosion test @ 40° C, 3 hours IP 154 /ASTM D 130 2C 2C 3A 1A
Aniline Point ° C IP 2 / ASTM D 611 53.6 59.0 68.2 71.4 83.6 81.0
Hydrocarbon types by FIA
FIA-Aromatic 20.3 23.8
FIA-Olefins 0.7 2.1
FIA-Saturates 79.0 74.1
Organic Chloride mg/kg ASTM D4929B 1.0 <1.0 <1.0 <1.0 <1.0 <1.0 <1.0
Conradson carbon residue % Wt. ASTM D189 4.84 <0.10 <0.10 0.25 0.40 9.30 19.5
Total Acid Number mgKOH/g IP 177 / ASTM D664 0.20 0.24 0.08 0.12 0.18 0.21 0.16 0.19 0.25
Refractive Index @ 70°C ASTM D1218 1.4557 1.4770 1.4945 1.4959
Naphthalene Content %Wt / %Vol ASTM D1840 0.18 1.95
Wax Content % Wt. UOP 46 <5(1.8) <5(1.9) <5(3.5) 19.2 20.1 5.4 2.2
Metals
Nickel 7 <1 <1 15 29
Vanadium 26 <1 <1 49 94
Sodium <1 <1 3 5
Softening Point ASTM D36 NA(1*) 35.2
Penetration @ 25°C ASTM D5 NA(1*) 248.0
Asphaltene % Wt. IP 143 1.7 3.9 7.6
Ash Content % Wt. IP 4 / ASTM D482 0.008 0.013 0.027
Salt Content mg/kg IP 265 / ASTM D3230 15
B.S. & Water % Vol. ASTM D4007 0.025
Water Content % Vol. IP 74 / ASTM D95 <0.05
Flash Point ° C IP170 / ASTM D93 <40.0 <40.0 <40.0 <40.0 80.0 124.0 178.0
Distillation - - - - - - -
IBP ° C 27.7 83.2 161.1 202.8 250.9 311.8
10% Evaporated/Recovered ° C 37.6 99.3 170.5 210.8 264.3 334.3
20% Evaporated/Recovered ° C 39.9 104.7 173.5 212.2 267.2 333.8
30% Evaporated/Recovered ° C 41.9 109.5 175.8 213.3 270.2 334.8
40% Evaporated/Recovered ° C 44.1 115.3 177.6 214.5 274.0 336.4
50% Evaporated/Recovered ° C 46.4 121.1 179.7 216.2 278.3 338.3
60% Evaporated/Recovered ° C 49.1 128.3 181.8 217.2 283.2 340.3
70% Evaporated/Recovered ° C 52.5 135.2 184.2 219.1 289.6 342.6
80% Evaporated/Recovered ° C 57.1 142.4 187.3 221.7 297.1 345.5
90% Evaporated/Recovered ° C 63.1 151.4 191.4 225.2 307.5 349.7
95% Evaporated/Recovered ° C 66.6 157.0 195.2 228.5 315.8 353.4
FBP ° C 73.0 166.1 201.0 232.7 327.9 357.7
Residue % Vol. 0.9 0.7 0.7 1.2 1.0 0.8
Loss % Vol. 0.8 0.5 0.6 1.0 0.8 0.5
Composition (C1-C5) -
Methane % Wt. <0.01
Ethane % Wt. 0.02
Propane % Wt. 0.26
I-butane % Wt. 0.27
n-butane % Wt. 0.85
IP 501
Residue Cuts
TEST
% VolGC (ASTM D6839/
ASTM D6730)
cStIP 71 / D 445
Vacuum Gas Oil Cuts
ASTM D86
IP344 / IP 601
Remark(s): 1. Unable to test due to sample nature. 2. Results is calculated and only as indicative –
precision parameters are not applicable.
UNIT METHOD
Wh
ole
Cru
de Naphtha Cuts
% Vol. IP 156
mg/kg
Page No: 4
Sample Descriptions / Label : Al Shaheen Crude Oil 2018
Sl. No. % Mass % Volume
1 1.38 2.16
2 3.27 4.43
3 9.58 11.35
4 5.10 5.63
5 5.52 5.92
6 17.65 18.14
7 7.51 7.41
9 24.79 23.55
10 24.65 21.23
LPG 1.38
Heavy Vacuum Gas Oil
(370-548C)74.80 78.59
LABORATORY REPORT NO. IDL 5579/2018
Vapour Temperature °C
19.33 23.57
TRUE BOILING POINT DISTILLATION DATA
(ASTM D 2892/D5236)
Cumulative %
Mass
Light Reformer Naphtha
(70-165C)
Cumulative %
Volume
17.94
Reformer & Heavy Naphtha
(165 - 195C)
Vacuum Residue
(548+C)
Light Naphtha
(C5-70C)4.65 6.59
14.23
99.45 99.82
2.16
Kerosene
(195- 235C)
Light Gas Oil
(235 - 325C)
29.49
47.63
55.04Gas Oil
(325-370C)
24.85
42.50
50.01
Page No: 5
Page No: 6
15
70
165
195
235
325
370
548
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
380
400
420
440
460
480
500
520
540
560
0.0 10.0 20.0 30.0 40.0 50.0 60.0 70.0 80.0
Te
mp
era
ture
°C
Recovery %
% Mass
% Volume
TRUE BOILING POINT DISTILLATION CURVE(ASTM D 2892 & ASTM D 5236)
LABORATORY REPORT NO. IDL 5579/2018
AL Shaheen Crude Assay Report 2018
Sample Descriptions / Label:
% mass Volume %
1.38 2.16
3.27 4.43
9.58 11.35
5.10 5.63
5.52 5.92
17.65 18.14
7.51 7.41
49.50 44.70
22.71 21.57
24.79 23.55
24.65 21.23
LABORATORY REPORT NO. IDL 5579/2018
370+ Res
370-548
Al Shaheen Crude Oil 2018
Yield %
Al Shaheen Crude Oil 2018
165-195
Cut Points
(° C)
SUMMARY OF PRODUCT / RESIDUE CUT POINTS AND YIELDS
195-235
370-540
0-15
15-70
70-165
548+ Res
235-325
325-370
Page No: 7
Page N
o: 8
0.0
0
5.0
0
10
.00
15
.00
20
.00
25
.00
30
.00
35
.00
40
.00
45
.00
50
.00
55
.00
60
.00
65
.00
70
.00
75
.00
80
.00
85
.00
90
.00
95
.00
10
0.0
0
0-1
515
-70
70
-165
16
5-1
95
19
5-2
35
23
5-3
25
32
5-3
70
37
0+
37
0-5
40
37
0-5
48
54
8+
% Yield
Fra
cti
on
Ran
ge (
°C
)
SU
MM
AR
Y O
F T
RU
E B
OIL
ING
PO
INT
DIS
TIL
LA
TIO
N W
IDE
CU
TS
LA
BO
RA
TO
RY
RE
PO
RT
NO
. ID
L 5
57
9/2
01
8
Al
Sh
ah
ee
n C
rud
e A
ssa
y R
ep
ort
20
18
% V
olu
me
% M
ass
Sample Descriptions / Label :
Specific Gravity @ 60/60° F ASTM D5002 - 0.8790
API Gravity @ 60° F Calculated ° API 29.5
Sulphur Content ASTM D4294 % Wt. 2.31
Mercaptan Sulphur UOP 163 ppm Wt. 322
Hydrogen Sulphide UOP 163 ppm Wt. <1
Total Nitrogen ASTM D5762 ppm Wt. 900
Basic Nitrogen UOP 269 % Wt 0.0225
Vapour Pressure ASTM D323 psi 6.20
Pour Point ASTM D97 ° C <-18
Kinematic Viscosity @ 15° C 31.88
Kinematic Viscosity @ 25° C 21.00
Kinematic Viscosity @ 35° C 13.31
Kinematic Viscosity @ 40° C 10.88
Kinematic Viscosity @ 55° C 7.203
Kinematic Viscosity @ 100° C 2.957
Organic Chloride ASTM D4929B mg/kg 1.0
Conradson carbon residue ASTM D189 % Wt. 4.84
Total Acid Number ASTM D664 mgKOH/g 0.20
Wax Content UOP 46 % Wt. <5(1.8)
Nickel IP 501 mg/kg 7
Vanadium IP 501 mg/kg 26
Asphaltene IP 143 % Wt. 1.7
Ash Content ASTM D482 % Wt. 0.008
Salt Content ASTM D3230 mg/kg 15
B.S. & Water ASTM D4007 % Vol. 0.025
Water Content ASTM D95 % Vol. <0.05
Flash Point ASTM D93 ° C <40.0
Composition (C1-C5) -
Methane <0.01
Ethane 0.02
Propane 0.26
I-butane 0.27
n-butane 0.85
Al Shaheen Crude Oil 2018
LABORATORY REPORT NO. IDL 5579/2018
WHOLE CRUDE PROPERTIES
TESTTEST METHOD UNIT RESULT
ASTM D445 cSt
IP 601 % Wt.
Page No: 9
Sample Descriptions / Label :
Yield ASTM D2892 / D5236 % Wt. 3.27
Yield ASTM D2892 / D5236 % Vol. 4.43
Density @ 15°C ASTM D4052 kg/L 0.6481
Specific Gravity @ 60/60° F Conversion - 0.6482
API Gravity @ 60° F Calculated ° API 86.8
Sulphur Content ASTM D 5453 % Wt. 0.0274
Mercaptan Sulphur UOP 163 ppm Wt. 243
Total Nitrogen ASTM D4629 ppm Wt. 0.3
Vapour Pressure ASTM D5191 psi 14.7
PIONA Analysis % Vol -
Total Paraffins % Vol 93.0
n-Paraffins % Vol 34.8
iso-Paraffins % Vol 58.2
Total Olefins % Vol <0.1
Total Napthenes % Vol 6.9
Total Aromatics % Vol <0.1
Unidentified % Vol <0.1
Research Octane Number (Clear) * ASTM D2699/ GC Cal 70.0(*)
Organic Chloride ASTM D4929 mg/kg <1.0
Flash Point ASTM D93 ° C <40.0
Distillation - -
IBP ° C 27.7
10% Evaporated/Recovered ° C 37.6
20% Evaporated/Recovered ° C 39.9
30% Evaporated/Recovered ° C 41.9
40% Evaporated/Recovered ° C 44.1
50% Evaporated/Recovered ° C 46.4
60% Evaporated/Recovered ° C 49.1
70% Evaporated/Recovered ° C 52.5
80% Evaporated/Recovered ° C 57.1
90% Evaporated/Recovered ° C 63.1
95% Evaporated/Recovered ° C 66.6
FBP ° C 73.0
Residue % Vol. 0.9
Loss % Vol. 0.8
ASTM D6839
ASTM D86
LABORATORY REPORT NO. IDL 5579/2018
Light Naphtha [IBP/C5 - 70° C]
Al Shaheen Crude Oil 2018
TEST METHOD UNIT RESULT
Page No: 10
Sample Descriptions / Label :
Yield ASTM D2892 / D5236 % Wt. 9.58
Yield ASTM D2892 / D5236 % Vol. 11.35
Density @ 15°C ASTM D4052 kg/L 0.7415
Specific Gravity @ 60/60° F Conversion - 0.7417
API Gravity @ 60° F Calculated ° API 59.3
Sulphur Content ASTM D5453 % Wt. 0.0897
Mercaptan Sulphur UOP 163 ppm Wt. 356
Total Nitrogen ASTM D4629 ppm Wt. 0.4
Vapour Pressure ASTM D5191 psi 1.81
PIONA Analysis % Vol -
Total Paraffins % Vol 59
n-Paraffins % Vol 8.3
iso-Paraffins % Vol 50.7
Total Olefins % Vol <0.1
Total Napthenes % Vol 36.4
Total Aromatics % Vol 4.6
Unidentified % Vol <0.1
Research Octane Number (Clear) ASTM D2699/ GC Cal - 55
Copper corrosion test @ 40° C, 3 hours ASTM D130 - 2C
Organic Chloride ASTM D4929 mg/kg <1.0
Flash Point ASTM D93 ° C <40.0
Distillation ° C -
IBP ° C 83.2
10% Evaporated/Recovered ° C 99.3
20% Evaporated/Recovered ° C 104.7
30% Evaporated/Recovered ° C 109.5
40% Evaporated/Recovered ° C 115.3
50% Evaporated/Recovered ° C 121.1
60% Evaporated/Recovered ° C 128.3
70% Evaporated/Recovered ° C 135.2
80% Evaporated/Recovered ° C 142.4
90% Evaporated/Recovered ° C 151.4
95% Evaporated/Recovered ° C 157.0
FBP ° C 166.1
Residue % Vol. 0.7
Loss % Vol. 0.5
LABORATORY REPORT NO. IDL 5579/2018
ASTM D6839
ASTM D86
RESULT
Al Shaheen Crude Oil 2018
TEST METHOD UNIT
Light Reformer Naphtha [70 - 165° C]
Page No: 11
Sample Descriptions / Label :
Yield ASTM D2892 / D5236 % Wt. 5.10
Yield ASTM D2892 / D5236 % Vol. 5.63
Density @ 15°C ASTM D4052 kg/L 0.7951
Specific Gravity @ 60/60° F Conversion - 0.7954
API Gravity @ 60° F Calculated ° API 46.4
Sulphur Content ASTM D5453 % Wt. 0.193
Mercaptan Sulphur UOP 163 ppm Wt. 380
Total Nitrogen ASTM D4629 ppm Wt. 0.6
PIONA Analysis % Vol -
Total Paraffins % Vol 62.7
n-Paraffins % Vol 7.5
iso-Paraffins % Vol 55.2
Total Olefins % Vol 0.5
Total Napthenes % Vol 15.7
Total Aromatics % Vol 21.1
Unidentified % Vol <0.1
Pour Point ASTM D97 ° C <-36
Cold Filter Plugging Point IP 309 ° C <-51
Cloud Point ASTM D2500 ° C <-42
Freeze Point ASTM D2386 ° C -81.5
Kinematic Viscosity @ 40° C ASTM D445 cSt 0.969
Kinematic Viscosity @ 100° C ASTM D445 cSt 0.552
Smoke Point ASTM D1322 mm 26.0
Copper corrosion test @ 40° C, 3 hours ASTM D130 - 2C
Aniline Point ASTM D611 ° C 53.6
Hydrocarbon types by FIA - -
FIA-Aromatic % Vol. 20.3
FIA-Olefins % Vol. 0.7
FIA-Saturates % Vol. 79
Organic Chloride ASTM D4929 mg/kg <1.0
Flash Point ASTM D93 ° C <40.0
Distillation ° C -
IBP ° C 161.1
10% Evaporated/Recovered ° C 170.5
20% Evaporated/Recovered ° C 173.5
30% Evaporated/Recovered ° C 175.8
40% Evaporated/Recovered ° C 177.6
50% Evaporated/Recovered ° C 179.7
60% Evaporated/Recovered ° C 181.8
70% Evaporated/Recovered ° C 184.2
80% Evaporated/Recovered ° C 187.3
90% Evaporated/Recovered ° C 191.4
95% Evaporated/Recovered ° C 195.2
FBP ° C 201
Residue % Vol. 0.7
Loss % Vol. 0.6
LABORATORY REPORT NO. IDL 5579/2018
Reformer & Heavy Naphtha [165 - 195° C]
ASTM D6839
ASTM D86
IP 156
RESULT
Al Shaheen Crude Oil 2018
TEST METHOD UNIT
Page No: 12
Sample Descriptions / Label :
Yield ASTM D 2892 / D5236 % Wt. 5.52
Yield ASTM D 2892 / D5236 % Vol. 5.92
Density @ 15°C ASTM D4052 kg/L 0.8190
Specific Gravity @ 60/60° F Conversion 0.8194
API Gravity @ 60° F Calculated ° API 41.2
Sulphur Content ASTM D 4294 % Wt. 0.304
Mercaptan Sulphur UOP 163 ppm Wt. 354
Total Nitrogen ASTM D4629 ppm Wt. 0.9
Pour Point ASTM D97 ° C <-36
Cold Filter Plugging Point IP 309 ° C -44
Cloud Point ASTM D2500 ° C <-42
Freeze Point ASTM D2386 ° C -53.5
Kinematic Viscosity @ 40° C ASTM D445 cSt 1.517
Kinematic Viscosity @ 100° C ASTM D445 cSt 0.7310
Smoke Point IP 57 / ASTM D1322 mm 25.0
Copper corrosion test @ 40° C, 3 hours ASTM D130 3A
Aniline Point ASTM D611 (Proc. A) ° C 59.0
Hydrocarbon types by FIA - -
FIA-Aromatic % Vol. 23.8
FIA-Olefins % Vol. 2.1
FIA-Saturates % Vol. 74.1
Organic Chloride ASTM D4929B mg/kg <1.0
Total Acid Number ASTM D664 mgKOH/g 0.08
Naphthalene Content ASTM D1840 %Wt / %Vol 1.95
Flash Point ASTM D93 ° C >70.0
Distillation - -
IBP ° C 202.8
10% Evaporated/Recovered ° C 210.8
20% Evaporated/Recovered ° C 212.2
30% Evaporated/Recovered ° C 213.3
40% Evaporated/Recovered ° C 214.5
50% Evaporated/Recovered ° C 216.2
60% Evaporated/Recovered ° C 217.2
70% Evaporated/Recovered ° C 219.1
80% Evaporated/Recovered ° C 221.7
90% Evaporated/Recovered ° C 225.2
95% Evaporated/Recovered ° C 228.5
FBP ° C 232.7
Residue % Vol. 1.2
Loss % Vol. 1.0
LABORATORY REPORT NO. IDL 5579/2018
Kerosene [195 - 235° C]
IP 156
ASTM D86
RESULT
Al Shaheen Crude Oil 2018
TEST METHOD UNIT
Page No: 13
Sample Descriptions / Label :
Yield ASTM D2892 / D5236 % Wt. 17.65
Yield ASTM D2892 / D5236 % Vol. 18.14
Density @ 15°C ASTM D4052 kg/L 0.8546
Specific Gravity @ 60/60° F Conversion 0.8551
API Gravity @ 60° F Calculated ° API 34.0
Sulphur Content ASTM D4294 % Wt. 1.080
Total Nitrogen ASTM D4629 ppm Wt. 36
Basic Nitrogen UOP 269 % Wt 0.0017
Pour Point ASTM D97 ° C <-36
Cold Filter Plugging Point IP 309 ° C -16
Cloud Point ASTM D2500 ° C -14
Cetane Index ASTM D976 calc. 48.0
Kinematic Viscosity @ 40° C ASTM D445 cSt 3.338
Kinematic Viscosity @ 100° C ASTM D445 cSt 1.289
Copper corrosion test @ 40° C, 3 hours ASTM D130 - 1A
Aniline Point ASTM D611 (Proc. A) ° C 68.2
Organic Chloride ASTM D4929 mg/kg <1.0
Conradson carbon residue ASTM D189 % Wt. <0.10
Total Acid Number ASTM D664 mgKOH/g 0.12
Refractive Index @ 70°C ASTM D1218 1.4557
Wax Content UOP 46 % Wt. <5(1.9)
Flash Point ASTM D93 ° C 124.0
Distillation - -
IBP ° C 250.9
10% Evaporated/Recovered ° C 264.3
20% Evaporated/Recovered ° C 267.2
30% Evaporated/Recovered ° C 270.2
40% Evaporated/Recovered ° C 274.0
50% Evaporated/Recovered ° C 278.3
60% Evaporated/Recovered ° C 283.2
70% Evaporated/Recovered ° C 289.6
80% Evaporated/Recovered ° C 297.1
90% Evaporated/Recovered ° C 307.5
95% Evaporated/Recovered ° C 315.8
FBP ° C 327.9
Residue % Vol. 1.0
Loss % Vol. 0.8
LABORATORY REPORT NO. IDL 5579/2018
Light Gas Oil [235 - 325° C]
ASTM D86
RESULT
Al Shaheen Crude Oil 2018
TEST METHOD UNIT
Page No: 14
Sample Descriptions / Label :
Yield ASTM D2892 % Wt. 7.51
Yield ASTM D2892 % Vol. 7.41
Density @ 15°C ASTM D4052 kg/L 0.8909
Specific Gravity @ 60/60° F Conversion 0.8914
API Gravity @ 60° F Calculated ° API 27.2
Sulphur Content ASTM D4294 % Wt. 2.25
Total Nitrogen ASTM D4629 ppm Wt. 220
Basic Nitrogen UOP 269 % Wt 0.0063
Pour Point ASTM D97 ° C +6
Cold Filter Plugging Point IP 309 ° C +8
Cloud Point ASTM D2500 ° C +8
Cetane Index ASTM D976 calc. 45.6
UOP K Factor UOP 375 calc. 11.6
Kinematic Viscosity @ 40° C ASTM D445 cSt 8.472
Kinematic Viscosity @ 100° C ASTM D445 cSt 2.300
Aniline Point ASTM D611 (Proc. A) ° C 71.40
Organic Chloride ASTM D4929 mg/kg <1.0
Conradson carbon residue ASTM D189 % Wt. <0.10
Total Acid Number ASTM D664 mgKOH/g 0.18
Refractive Index @ 70°C ASTM D1218 1.4770
Wax Content UOP 46 % Wt. <5(3.5)
Flash Point ASTM D93 ° C 178.0
Distillation - -
IBP ° C 311.8
10% Evaporated/Recovered ° C 334.3
20% Evaporated/Recovered ° C 333.8
30% Evaporated/Recovered ° C 334.8
40% Evaporated/Recovered ° C 336.4
50% Evaporated/Recovered ° C 338.3
60% Evaporated/Recovered ° C 340.3
70% Evaporated/Recovered ° C 342.6
80% Evaporated/Recovered ° C 345.5
90% Evaporated/Recovered ° C 349.7
95% Evaporated/Recovered ° C 353.4
FBP ° C 357.7
Residue % Vol. 0.8
Loss % Vol. 0.5
LABORATORY REPORT NO. IDL 5579/2018
Gas Oil [325 - 370° C]
RESULT
ASTM D86
Al Shaheen Crude Oil 2018
TEST METHOD UNIT
Page No: 15
Sample Descriptions / Label :
Yield ASTM D2892/ D5236 % Wt. 22.71
Yield ASTM D2892/ D5236 % Vol. 21.57
Density @ 15°C ASTM D4052 kg/L 0.9229
Specific Gravity @ 60/60° F Conversion 0.9234
API Gravity @ 60° F Calculated ° API 21.7
Sulphur Content ASTM D 4294 % Wt. 2.49
Total Nitrogen ASTM D 4629 ppm Wt. 639
Basic Nitrogen UOP 269 % Wt 0.0179
Pour Point ASTM D97 ° C +30
UOP K Factor UOP 375 calc. 11.7
Kinematic Viscosity @ 40° C ASTM D445 cSt 55.97
Kinematic Viscosity @ 100° C ASTM D445 cSt 7.068
Kinematic Viscosity @ 135° C ASTM D2170 cSt 3.575
Aniline Point ASTM D611 (Proc. A) ° C 83.6
Conradson carbon residue ASTM D189 % Wt. 0.25
Total Acid Number ASTM D664 mgKOH/g 0.21
Refractive Index @ 70°C ASTM D1218 1.4945
Wax Content UOP 46 % Wt. 19.2
Metals - -
Nickel mg/kg <1
Vanadium mg/kg <1
Sodium mg/kg <1
LABORATORY REPORT NO. IDL 5579/2018
Vacuum Gas Oil 1 [370 - 540°C]
RESULT
IP 501
Al Shaheen Crude Oil 2018
TEST METHOD UNIT
Page No: 16
Sample Descriptions / Label :
Yield ASTM D2892 / D5236 % Wt. 24.79
Yield ASTM D2892 / D5236 % Vol. 23.55
Density @ 15°C ASTM D4052 kg/L 0.9251
Specific Gravity @ 60/60° F Conversion 0.9256
API Gravity @ 60° F Calculated ° API 21.4
Sulphur Content ASTM D4294 % Wt. 2.55
Total Nitrogen ASTM D4629 ppm Wt. 680
Basic Nitrogen UOP 269 % Wt 0.0186
Pour Point ASTM D97 ° C +33
UOP K Factor UOP 375 calc. 11.6
Kinematic Viscosity @ 40° C ASTM D445 cSt 62.50
Kinematic Viscosity @ 100° C ASTM D445 cSt 7.573
Kinematic Viscosity @ 135° C ASTM D2170 cSt 3.754
Aniline Point ASTM D611 (Proc. A) ° C 81.0
Conradson carbon residue ASTM D189 % Wt. 0.40
Total Acid Number ASTM D664 mgKOH/g 0.16
Refractive Index @ 70°C ASTM D1218 1.4959
Wax Content UOP 46 % Wt. 20.1
Metals - -
Nickel mg/kg <1
Vanadium mg/kg <1
Sodium mg/kg <1
LABORATORY REPORT NO. IDL 5579/2018
Heavy Vacuum Gas Oil [370 - 548°C]
RESULT
IP 501
Al Shaheen Crude Oil 2018
TEST METHOD UNIT
Page No: 17
Sample Descriptions / Label :
Yield ASTM D2892 / D5236 % Wt. 49.50
Yield ASTM D2892 / D5236 % Vol. 44.77
Density @ 15°C IP 365 kg/L 0.9713
Specific Gravity @ 60/60° F Conversion 0.9718
API Gravity @ 60° F Calculated ° API 14.1
Sulphur Content ASTM D 4294 % Wt. 3.70
Mercaptan Sulphur UOP 163 ppm Wt. 69
Hydrogen Sulphide UOP 163 ppm Wt. <1
Total Nitrogen ASTM D4629 ppm Wt. 1823
Basic Nitrogen UOP 269 % Wt 0.0484
Pour Point ASTM D97 ° C +24
Kinematic Viscosity @ 40° C ASTM D445 cSt 1212
Kinematic Viscosity @ 100° C ASTM D445 cSt 46.62
Kinematic Viscosity @ 135° C ASTM D2170 cSt 15.90
Conradson carbon residue ASTM D189 % Wt. 9.30
Total Acid Number ASTM D664 mgKOH/g 0.19
Asphaltene IP 143 % Wt. 3.9
Wax Content UOP 46 % Wt. 5.4
Metals - -
Nickel mg/kg 15
Vanadium mg/kg 49
Sodium mg/kg 3
Atmospheric Residue [370°C+]
LABORATORY REPORT NO. IDL 5579/2018
IP 501
RESULT
Al Shaheen Crude Oil 2018
TEST METHOD UNIT
Page No: 18
Sample Descriptions / Label :
Yield ASTM D2892 / D5236 % Wt. 24.65
Yield ASTM D2892 / D5236 % Vol. 21.23
Density @ 15°C ASTM D70 kg/L 1.0199
Specific Gravity @ 60/60° F Conversion - 1.0206
API Gravity @ 60° F Calculated ° API 7.2
Sulphur Content ASTM D4294 % Wt. 4.87
Mercaptan Sulphur UOP 163 ppm Wt. 52
Hydrogen Sulphide UOP 163 ppm Wt. <1
Total Nitrogen ASTM D4629 ppm Wt. 2800
Basic Nitrogen UOP 269 % Wt 0.0728
Pour Point ASTM D97 ° C +39
UOP K Factor UOP 375 calc. 11.4
Kinematic Viscosity @ 40° C ASTM D445 cSt 266400*
Kinematic Viscosity @ 100° C ASTM D445 cSt 1131
Kinematic Viscosity @ 135° C ASTM D2170 cSt 188.1
Conradson carbon residue ASTM D189 % Wt. 19.5
Total Acid Number ASTM D664 mgKOH/g 0.25
Wax Content UOP 46 % Wt. 2.2
Softening Point D 36 ° C 35.2
Penetration @ 25°C ASTM D5 mm 248.0
Asphaltene IP 143 % Wt. 7.6
Ash Content IP 4 / ASTM D482 % Wt. 0.027
Metals - -
Nickel mg/kg 29
Vanadium mg/kg 94
Sodium mg/kg 5
Al Shaheen Crude Oil 2018
TEST METHOD
LABORATORY REPORT NO. IDL 5579/2018
Vacuum Residue [548°C+]
Remark(s): Results is calculated and only as indicative – precision parameters are not applicable.
UNIT RESULT
IP 501
Page No: 19