VESSEL
:
LOCATION
:
GRADE
:
DATE
:
VOYAGE No.
:
DOCUMENTS RECEIPT
The undersigned officer of the above mentioned vessel, hereby acknowledge receipt of documents as listed below :Furthermore, these documents were received in good condition.
Document Receipt
One
Time Log
One
Vessel Ullage Report
Two
Interim Ullage Report
One
R.O.B. Report
Two
Slop Certificate
One
Vessel Experience Report
One
Void / Ballast Space Report
One
Crude Oil Wash Report
Two
Rate / Pressure Request
One
Rate / Pressure Report
Two
Main Cargo Pumping Record
Two
Bunker Report
Two
Letter of Protest Statement of Facts
Signed :
Three One
Master / Chief Officer
Saybolt Inspector
INTERIM ULLAGE REPORT
VESSEL NAME
0
GRADE
Murban Crude Oil
LOCATION
0
DATE
May 21 & 22 ,2003
BEFORE API Tanks No. 1-C 2-C 5-C 6-C 4-P 4-S
:
39.35
Obsd. Corr. Ullage Corr. Ullage mm. mm. mm. 2350 2290 2290 2310 2410 2410
-
Tank
API
T.O.V. Barrels.
2350 2290 2290 2310 2410 2410
238,131 158,537 158,537 185,485 139,731 139,731
Plus Lines :
705
TOTALS
AFTER
Draft Condition ;
:
FWD :
Free Water Dips Volume mm. Bbls. Nil Nil Nil Nil Nil Nil
0 0 0 0 0 0
1,020,857
39.35
Obsd. Corr. Ullage Corr. Ullage
No.
mm.
mm.
mm.
1-C 2-C 5-C 6-C 4-P 4-S
2350 2290 2290 2310 2410 2410
-
2350 2290 2290 2310 2410 2410
238,131 158,537 158,537 185,485 139,731 139,731
Plus Lines :
705
TOTALS
Barrels.
M. ,
AFT :
19.92
G.O.V.
A.P.I.
Temp.
V.C.F.
G.S.V.
Barrels.
@ 60oF
F
T-6A
Barrels.
FWD :
39.35 39.35 39.35 39.35 39.35 39.35
93.4 94.5 94.5 94.8 90.7 90.5
0.9832 0.9827 0.9827 0.9824 0.9847 0.9847
234,130 155,794 155,794 182,220 137,593 137,593
705
39.35
93.1
0.9835
693
93.1
1,003,817
M. ,
AFT :
19.92
Free Water Dips Volume
G.O.V.
A.P.I.
Temp.
V.C.F.
G.S.V.
mm.
Bbls.
Barrels.
@ 60oF
F
T-6A
Barrels.
Nil Nil Nil Nil Nil Nil
0 0 0 0 0 0
0
Nil
238,131 158,537 158,537 185,485 139,731 139,731
o
M.,List :
Nil
238,131 158,537 158,537 185,485 139,731 139,731
39.35 39.35 39.35 39.35 39.35 39.35
93.4 94.5 94.5 94.8 90.7 90.5
0.9832 0.9827 0.9827 0.9824 0.9847 0.9847
234,130 155,794 155,794 182,220 137,593 137,593
705
39.35
93.1
0.9835
693
1,020,857 Av.Temp.
Sea Condition/Temp.
Slight / 30oC
Segregated Ballast tanks
Fpt,2-P/S,3-P/S,5-P/S,E/R-P/S (WBT) & Apt.
Non-Segregated Ballast tanks
None
Lines drained to
-
Chief Officer
M.,List :
19.92
1,020,857
Are Gauge Corrected for Trim , Before :
o
1,020,857 Av.Temp.
Draft Condition ; T.O.V.
19.92
93.1
1,003,817
### No
After :
Yes
Saybolt Inspector
Temp. deg. C TOP MID LOW Average
Temp. deg. F Average
1-C 2-C 5-C 6-C 4-P 4-S 0 0 0 0
34.1 34.7 34.7 34.9 32.6 32.5 36.5 37.3 33.6 32.8
34.1 34.7 34.7 34.9 32.6 32.5 36.0 36.9 33.6 32.8
34.1 34.7 34.7 34.9 32.6 32.5 35.5 36.2 33.6 32.8
34.1 34.7 34.7 34.9 32.6 32.5 36.0 36.8 33.6 32.8
93.4 94.5 94.5 94.8 90.7 90.5 96.8 98.2 92.5 91.0
1 2 3 4 5 6 7 8 9 10
1-C 2-C 5-C 6-C 4-P 4-S 0 0 0 0
34.1 34.7 34.7 34.9 32.6 32.5 32.4 32.5 32.6 32.6
34.1 34.7 34.7 34.9 32.6 32.5 31.9 31.9 33.8 33.8
34.1 34.7 34.7 34.9 32.6 32.5 29.9 29.7 31.2 31.2
34.1 34.7 34.7 34.9 32.6 32.5 31.4 31.4 32.5 32.5
93.4 94.5 94.5 94.8 90.7 90.5 88.5 88.5 90.6 90.6
1 2 3 4 5 6 7 8 9 10
93.3 93.4 92.5 95.4 93.4 89.3 89.4 89.7 89.8 90.0
t (1,2 of 3) API 60 (K)
1 #REF! 0.13296
F
2,240.00
A1
34
A2
34.7
D1
0.85189645
B1
0.13299903
X
0.00000000
t=1
E_1
0.13299863
t=2
E_2
0.13299850
E1 D1! D2
0.13299863 0.13300000 0.85138387
B2 X E_1 E_2 E2 D2! C A1 W A2
0.13291889 0.00000000 0.1329183884 0.13291820 0.13291839 0.13292000 0.13296000 34.65 0 0
B1
5.41717170
E1
5.4171713027
D1
5.41717100
B2 E2 D2 C_3
(0.00019093) (0.00019133) (0.00019100) 5.41717000
t=1 t=2
t=3
En weer terug van WCF naar API etc. INPUT WCF OUTPUT API/RD fun 83 wcf x d
tafel 11 0.16804 API 1.0761175744 RD 1.0760246193 WCF
This is the function to regain API or RD from WCF
WCF TABLE RESULT RD
API RD
0.16804 2 1=T11,2=T13,3=T29 #REF! 1.0760220612 Calc T11
0 Result T11 1.0590459655 Calc T13
Vul 1,2 of 3 in
1 #REF!
Vul 1,2 of 3 in
T13 Calc
BUNKER before
#REF!
Fuel Oil
2240
API (b)
###
###
###
###
34
b+131.5
###
###
###
###
34.7
Vul 1,2 of 3 in
###
###
###
###
0.8518964479
Vul 1,2 of 3 in
###
###
###
###
0.1329990268 0 0.1329986268
ULLAGE before
0.1329985
### #REF!
###
###
###
0.1329986268 0.133 0.8513838748
### ### ###
### ### ### ### ### ### ### ### ### ### ### ###
0.1329188884 0 0.1329183884 0.1329182 0.1329183884 0.13292 0.13296 34.65 0 0
### ### ### ### ### ### ### ### ### ###
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5.4171717027
###
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5.4171713027
###
###
###
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###
wijz july 97
5.417171
###
###
###
###
###
wijz july 97 wijz july 97
-0.0001909295 -0.0001913295 -0.000191 5.41717
### ### ### ### ### ### ### ### ###
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wijz july 97
tafel 13 #REF! API #REF! RD -0.00019 WCF
tafel 29 #REF! RD #REF! WCF #REF!
1.075 0.16788
BUNKER before Diesel
BUNKER after
Diesel
###
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###
###
###
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###
ULLAGE after
###
###
###
###
###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ###
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###
### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ###
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VESSEL LOCATION GRADE DATE
: : : :
0 0 0 August 11, 2016
FAST TO THE POINT.
TO : WHOM IT MAY CONCERN
STATEMENT OF FACTS Dear Sirs, This is to advise that we, as Independent Surveyors,on behalf of our client(s) do hereby lodge to statement of facts in respect of :
RE :
Detected of ROB in nominated cargo tanks after completion of discharge operation was determined as following details :-
Liquid Oil Non-Liquid Oil Free Water Totals "ROB"
( Barrels ) ( Barrels ) ( Barrels ) ( Barrels )
: : : :
OMAN C.O.
QATAR C.O.
19 62 Nil 81
287 113 Nil 400
Remarks : As above ROB volume"Liquid Cargo" of a pumpable nature and "Non-Liquid Cargo" of unpumpable nature.
Furthermore, on behalf of our clients, we reserve the right to refer to this matter at a later date. Signature of this document is acknowledgement of receipt only, and not an admission of responsibility for the incident.
Master/Chief Officer
Shore Representative
Saybolt Inspector
: : : :
VESSEL LOCATION GRADE DATE
0 0 Oman Export Blend Crude Oil #REF!
RATE / PRESSURE REPORT Shoreline size and length Shore,number / size of cargo hoses connected Ship,number / size of cargo manifolds Shore,max.permitted pumping rate and pressure Ship ,max. permitted pumping rate and pressure
DATE
TIME
04-May-2003 " " " " " " " 05-May-2003 " " " " " " " " " " " " "
1700 1800 1900 2000 2100 2200 2300 2400 0100 0200 0300 0400 0500 0600 0700 0800 0900 1000 1100 1200 1300 1400
: : : : :
SHIP PRESSURE
SHIP PRESSURE
(Kg/Cm2) Manifold No. 2 9.0 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.1 10.1 10.1 8.2 7.5 5.5
(Kg/Cm2) Manifold No. 3 9.0 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.2 10.1 10.1 10.1 8.2 7.5 5.5
Ship pressure reading taken at Dock pressure reading taken at Average huorly rate Average dock pressure Average ship pressure Average temperature
48 Inches and 19,500 Metres. 2 / 16 Inches. 4 / 20 Inches. 9,500 M3/Hr. and 10.5 Kg/Cm2. 3x5,000 M3/Hr. and 12.0 Kg/Cm2.
TEMP.
HOURLY RATE
(oC)
Cu.Mtrs.
-
3,757 7,734 7,536 7,519 7,667 7,425 7,118 5,657 7,673 7,927 7,325 7,596 7,711 7,494 7,931 7,073 7,733 6,940 4,128 6,621 4,839 8,343
REMARKS #REF! Hrs., On 04-May-2003 : Commenced Discharging 1040-1110 Hrs.,On 05-May-2003 : Suspended discharging at shore switching tanks from PUS to PUN.
1400 Hrs., On 05-May-2003 : Completed Discharging
Ship Portside Manifold No. 2 & 3 N/A Cu.Mtrs. N/A 9.7 N/A
Master / Chief Officer
Kg/Cm2
Saybolt Inspector
a
b
9.7 203.3
9.7 203.3
MAIN CARGO PUMPING RECORD VESSEL LOCATION GRADE DATE
: : : :
0 0 Oman Export Blend Crude Oil #REF! #REF!
Commenced Discharging Completed
Discharging
DATE
TIME
04-May-03 " " " " " " " 05-May-03 " " " " " " " " " " " " "
1700 1800 1900 2000 2100 2200 2300 2400 0100 0200 0300 0400 0500 0600 0700 0800 0900 1000 1100 1200 1300 1400
Rate Pressure Units
Hrs., On May 04 ,2003
(Kg/Cm2) CARGO PUMP No. 1 CARGO PUMP No. 2 CARGO PUMP No. 3 CARGO PUMP No. 4 1400
RPM 850 1010 1010 1010 1010 1010 1010 560 1040 1040 1040 1050 1055 1060 1050 1050 1060 1060 1080 970 910
Hrs., On May 05 ,2003
PRESSURE DEL.
SUC.
11.7 12.7 12.6 12.5 12.7 12.5 12.6 6.0 12.7 12.7 12.7 12.7 12.7 12.7 12.4 12.2 12.3 12.3 STOP 12.5 9.7 8.7
0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.0 0.0 0.0 0.0 0.0
RPM 850 1000 1000 1000 1010 1020 1010 550 1030 1030 1030 1050 1050 1050 1050 1050 1060 1060 1080 960 915
PRESSURE DEL.
SUC.
11.7 12.7 12.7 12.7 12.8 12.8 12.7 6.5 12.7 12.7 12.7 12.7 13.0 12.7 12.7 12.7 12.7 12.7 STOP 12.6 10.0 9.0
0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.0 0.0 0.0 0.0 0.0
RPM 850 1000 1000 1000 1010 1020 1010 560 1040 1040 1040 1050 1050 1050 1050 1050 1060 1060 1070 950 920
PRESSURE DEL.
SUC.
11.7 12.7 12.7 12.7 12.7 12.7 12.7 6.3 12.8 12.8 12.8 12.7 12.7 12.7 12.6 12.4 12.7 12.6 STOP 12.8 9.7 8.7
0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.0 0.0 0.0 0.0 0.0 0.0
RPM
REMARKS :
Master / Chief Officer
Saybolt Inspector
PRESSURE DEL.
SUC.
: : : :
VESSEL LOCATION GRADE DATE
0 0 Qatar Marine Crude Oil #REF!
RATE / PRESSURE REPORT Shoreline size and length Shore,number / size of cargo hoses connected Ship,number / size of cargo manifolds Shore,max.permitted pumping rate and pressure Ship ,max. permitted pumping rate and pressure
DATE
TIME
05-May-2003 " " " " " " " " " 06-May-2003 " " " " " " " " " " " "
1500 1600 1700 1800 1900 2000 2100 2200 2300 2400 0100 0200 0300 0400 0500 0600 0700 0800 0900 1000 1100 1200 1300
: : : : :
SHIP PRESSURE
SHIP PRESSURE
(Kg/Cm2) Manifold No. 2 9.8 9.8 10.1 10.1 10.1 10.1 10.1 10.1 4.3 10.1 10.0 10.0 10.0 3.9 10.0 9.8 7.6 5.3 4.5 4.0 2.2 0.4 0.2
(Kg/Cm2) Manifold No. 3 9.8 9.8 10.1 10.1 10.1 10.1 10.1 10.1 4.3 10.1 10.0 10.0 10.0 3.9 10.0 9.8 7.6 5.3 4.5 4.0 2.2 0.4 0.2
Ship pressure reading taken at Dock pressure reading taken at Average huorly rate Average dock pressure Average ship pressure Average temperature
48 Inches and 19,500 Metres. 2 / 16 Inches. 4 / 20 Inches. 9,500 M3/Hr. and 10.5 Kg/Cm2. 3x5,000 M3/Hr. and 12.0 Kg/Cm2.
TEMP.
HOURLY RATE
(oC)
Cu.Mtrs.
-
8,285 8,391 8,436 8,673 8,625 8,705 8,766 8,314 6,027 8,903 9,123 4,171 7,445 6,838 8,192 8,502 7,390 5,618 4,400 7,361 4,516 2,321 1,400
REMARKS #REF! Hrs., On 05-May-2003 : Commenced Discharging 0120-0150 Hrs.,On 06-May-2003 : Suspended discharging at shore switching tanks from PUN to PUS. 1330-1430 Hrs.,On 06-May-2003 : Stopped discharging for vessel stripping tanks internally.
#REF! Hrs., On 06-May-2003 : Completed Discharging
Ship Portside Manifold No. 2 & 3 N/A Cu.Mtrs. N/A 7.5 N/A
Master / Chief Officer
Kg/Cm2
Saybolt Inspector
a
b
7.5 172.5
7.5 172.5
MAIN CARGO PUMPING RECORD VESSEL LOCATION GRADE DATE
: : : :
0 0 Qatar Marine Crude Oil #REF! #REF!
Commenced Discharging Completed
Discharging
DATE
TIME
05-May-03 " " " " " " " " " 06-May-03 " " " " " " " " " " " "
1500 1600 1700 1800 1900 2000 2100 2200 2300 2400 0100 0200 0300 0400 0500 0600 0700 0800 0900 1000 1100 1200 1300
Rate Pressure Units
Hrs., On May 05 ,2003
(Kg/Cm2) CARGO PUMP No. 1 CARGO PUMP No. 2 CARGO PUMP No. 3 CARGO PUMP No. 4 #REF!
RPM 1010 1010 1030 1030 1050 1050 1050 650 1060 1060 1080 1070 1070 650 1090 1090 1020 910 860 820 600 600 -
Hrs., On May 06 ,2003
PRESSURE DEL.
SUC.
12.7 12.7 12.7 12.7 12.4 12.7 12.6 6.5 12.8 12.7 12.7 12.7 12.7 6.5 12.7 13.3 10.6 8.2 7.1 7.0 5.0 3.3 STOP
0.2 0.2 0.2 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 -
RPM 1010 1010 1030 1030 1050 1050 1050 650 1070 1060 1070 1070 1070 650 1090 1090 1020 900 860 820 600 600 600
PRESSURE DEL.
SUC.
12.7 12.7 12.7 12.7 13.2 13.0 12.9 6.5 13.2 13.1 13.3 13.3 13.3 6.5 13.3 13.3 10.2 9.0 8.2 7.5 5.0 3.1 3.5
0.2 0.2 0.2 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.0 0.0 0.0 0.0 0.0 0.0
RPM 1010 1010 1030 1030 1050 1050 1050 650 1070 1060 1080 1070 1070 650 1090 1090 1020 910 860 820 600 600 600
PRESSURE DEL.
SUC.
12.7 12.7 12.7 12.7 12.8 12.8 12.7 6.5 12.9 12.8 12.7 12.7 12.7 6.5 12.7 12.7 10.7 8.7 7.9 7.0 5.0 3.4 3.5
0.2 0.2 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
RPM
REMARKS :
Master / Chief Officer
Saybolt Inspector
PRESSURE DEL.
SUC.
WEDGE CALCULATION REPORT VESSEL NAME
#REF!
GRADE
OMECO & QMCO
LOCATION
#REF!
DATE
August 11, 2016
Tk.Height Ull.Dist. (D) (U) Nos. Metres Metres
Tank
(-) DF
Length Length ( + ) of Tank Factor S (L) ( LF ) Metres
A
(x) Volume W Metres Cu.Mtrs.
A
2
Trim Factor (F)
Volume Barrels
2-C
30.920
7.850
0.2945
49.050
0.46715
0.010
0.0820
0.006724
23.800
8.401
0.009524
53
3-C
30.920
6.550
0.2945
32.700
0.31143
0.030
0.0896
0.008028
23.800
10.031
0.009524
63
5-C
30.920
6.550
0.2945
32.700
0.31143
0.020
0.0796
0.006336
23.800
7.917
0.009524
50
6-C
30.920
7.000
0.2945
47.750
0.45477
0.030
0.0939
0.008817
23.800
11.017
0.009524
69
2-S
20.900
6.350
0.1991
49.050
0.46715
0.010
0.0686
0.004706
13.700
3.385
0.009524
21
4-P
20.900
6.350
0.1991
49.050
0.46715
0.010
0.0686
0.004706
13.700
3.385
0.009524
21
4-S
20.900
6.350
0.1991
49.050
0.46715
0.010
0.0686
0.004706
13.700
3.385
0.009524
21
6-P
20.900
11.900
0.1991
38.150
0.36334
0.010
0.1214
0.014738
3.600
2.785
0.009524
18
6-S
20.900
11.900
0.1991
38.150
0.36334
0.040
0.1514
0.022922
3.600
4.332
0.009524
27
Totals Volume " Liquid Oil " Code A D S
ALL MEASUREMENTS MUST BE UNIT IN METRES Adjusted innage at aft. bulkhead of tank Mean total guage height
W
Sounding (innage) Distance from sounding point to aft. bulkhead of tank Width of tank
DF
Mean total guage height x trim factor
U F L
LF
Trim factor
Length of tank
Length of tank x trim factor Note
54.638
343
FIELD INFORMATION Draft condition Draft
(Metres)
(Aft-Fwd)
7.00
AFT
10.00
LBP
315.00
TRIM
Length between perpendicular Trim Factor (Trim/LBP)
WEDGE FORMULA
((( U-DF ) x F ) + S )2 x W
Sea Condition
FWD
2F
F
= Cu.Metres.
#REF!
: If " A " is greaten than " LF " use ship calibration tables. If " A " is less than " LF " use wedge formula.
Chief Officer
Saybolt Inspector
3.00 ###
VESSEL LOCATION GRADE DATE
: : : :
0 0 0 August 11, 2016
TO : WHOM IT MAY CONCERN
LETTER OF PROTEST Dear Sirs, This is to advise that we, as Independent Surveyors, on behalf of our client(s) do hereby lodge to letter of protest in respect of : Re : Discrepancy of cargo quantity difference. GRADE :
Masila Export Blend Crude Oil
Bbls@60oF
Metric Tons
Long Tons
Bill of Lading (Gross)
:
950,347
130,710.726
128,648.47
Vessel Before Discharge Quantity
:
948,923
130,514.869
128,415.77
Difference Quantity
:
-1,424
-195.857
-232.70
Difference Percentage
:
-0.15
-0.15
-0.18
Vessel After Loading Quantity
:
948,605
130,471.131
128,412.66
Vessel Before Discharge Quantity
:
948,923
130,514.869
128,415.77
Difference Quantity
:
+318
+43.738
+3.11
Difference Percentage
:
+0.03
+0.03
+0.00
Bbls@60oF
Metric Tons
Long Tons
GEADE :
Oman Export Blend Crude Oil
Bill of Lading (Gross)
:
509,949
69,594.850
68,495.50
Vessel Before Discharge Quantity
:
508,881
69,396.102
68,300.06
Difference Quantity Difference Percentage
: :
-1,068 -0.21
-198.748 -0.29
-195.44 -0.29
Vessel After Loading Quantity Vessel Before Discharge Quantity Difference Quantity Difference Percentage
: : : :
510,215 508,881 -1,334 -0.26
69,578.020 69,396.102 -181.918 -0.26
68,479.10 68,300.06 -179.04 -0.26
Remarks : As above quantities compared are inclusive of OBQ/ROB
Furthermore, on behalf of our clients, we reserve the right to refer to this matter at a later date. Signature of this document is acknowledgement of receipt only, and not an admission of responsibility for the incident.
Master/Chief Officer
Shore Representative
Saybolt Inspector
VESSEL ULLAGE REPORT BEFORE DISCHARGE
VESSEL NAME
0
GRADE
Oman Export Blend Crude Oil
LOCATION
0
DATE
June 21 ,2003
No.
Obsd. Corr. Ullage Corr. Ullage mm. mm. mm.
3-C 5-C 1-P 1-S
13430 1820 8310 8320
Tanks
Plus
T.O.V. Barrels.
13430 1820 8310 8320 Line
118,936 234,850 81,038 80,998 632
TOTALS
Free Water Dips Volume mm. Bbls. Nil Nil Nil Nil
516,454
A.P.I.
Barrels.
@ 60oF
0 0 0 0
0
TOTAL QUANTITIES DISCHARGED
G.O.V. 118,936 234,850 81,038 80,998 632
Temp.
V.C.F.
G.S.V.
F
T-6A
Barrels.
90.0 94.8 88.2 88.0 91.5
0.9861 0.9838 0.9870 0.9870 0.9854
o
33.10 33.10 33.10 33.10 33.10
516,454 Av.Temp.
DRAFT CONDITION :-
90.5
117,283 231,045 79,985 79,945 623
508,881
W.C.F.(T-13)
0.13637
T.O.V. ( Barrels.)
516,454
Fwd
16.25
M.
Metric Tons.
69,396.102
G.O.V.( Barrels.)
516,454
Aft
16.25
M.
Long Tons.
68,300.06
T.C.V. ( Barrels.)
508,881
Trim
Nil
Table 1
0.984206
G.S.V. ( Barrels.)
508,881
List
Nil
A.P.I. @ 60 F o
Less ROB (Barrels)
#REF!
Sea Condition/Temp.
Slight / 30oC
G.S.V. ( Barrels.)
#REF!
Segregated Ballast tanks
Fpt,2-P/S,4-P/S,6-P/S(WBT) & Apt.
Metric Tons.(in air)
#REF!
Non-Segregated Ballast tanks
None
Long Tons.
#REF!
Lines drained to
-
Chief Officer
33.10
###
Saybolt Inspector
Temp. deg. C TOP MID LOW Average 3-C 5-C 1-P 1-S 0 0 0 0 0 0 0 0 0 0 0 0
36.1 35.1 33.4 33.2 34.1 34.0 36.5 37.3 33.6 32.8 32.8 33.5 33.4 36.8 35.9 36.3 32.1 32.2 32.2 32.4 32.4 32.5 32.6
36.1 35.0 32.7 32.5 33.1 33.3 36.0 36.9 33.6 32.8 32.8 33.5 33.4 36.8 35.9 36.3 31.5 31.7 31.9 32.2 31.9 31.9 33.8
36.0 34.8 32.5 32.3 32.8 32.8 35.5 36.2 33.6 32.8 32.8 33.5 33.4 36.8 35.9 36.3 30.1 30.5 29.9 30.2 29.9 29.7 31.2
Total average
Temp. deg. F Average
36.1 35.0 32.9 32.7 33.3 33.4 36.0 36.8 33.6 32.8 32.8 33.5 33.4 36.8 35.9 36.3 31.2 31.5 31.3 31.6 31.4 31.4 32.5
96.9 94.9 91.2 90.8 92.0 92.1 96.8 98.2 92.5 91.0 91.0 92.3 92.1 98.2 96.6 97.3 88.2 88.6 88.4 88.9 88.5 88.5 90.6
33.6
92.5
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23
93.3 93.4 92.5 95.4 93.4 89.3 89.4 89.7 89.8 90.0 90.4 91.0 91.6
t (1,2 of 3) API 60 (K)
1 33.10 0.13296
F
t=1 t=2
t=1 t=2
t=3
2,240.00
A1
34
W A2
0.05 34.7
D1
0.85189645
B1
0.13299903
X
0.00000000
E_1 E_2
0.13299863 0.13299850
E1 D1! D2
0.13299863 0.13300000 0.85138387
B2 X E_1 E_2 E2 D2! C A1 W A2 B1 E1 D1 B2 E2 D2 C_3
0.13291889 0.00000000 0.1329183884 0.13291820 0.13291839 0.13292000 0.13296000 34.65 0 0 5.41717170 5.4171713027 5.41717100 (0.00019093) (0.00019133) (0.00019100) 5.41717000
En weer terug van WCF naar API etc. INPUT WCF OUTPUT API/RD fun 83 wcf x d x1 API
tafel 11 0.16804 API 1.0761175744 RD 1.0760246193 WCF 131.5025673746 0.0025673746 WCF RD API
This is the function to regain API or RD from WCF
WCF TABLE RESULT RD API RD API RD
0.16804 2 1=T11,2=T13,3=T29 2.11 1.0760220612 Calc T11 0 Result T11 1.0590459655 Calc T13 2.11 Result T13 1.076 Calc+ResultT29
Vul 1,2 of 3 in
1 33.10
Vul 1,2 of 3 in
T13 Calc
BUNKER before
0.13296
Fuel Oil
2240
API (b)
33.10
###
###
###
34
b+131.5
164.6
###
###
###
535.1911/b+131.5 Vul 1,2 of 3 in
### ###
### ###
### ###
### ###
Vul 1,2 of 3 in
###
###
###
###
ULLAGE before ### #REF! ### ###
###
0.05 34.7 0.8518964479 0.1329990268 0 0.1329986268 0.1329985
wijz july 97
wijz july 97
wijz july 97 wijz july 97
0.1329986268 0.133 0.8513838748
### ### ###
### ### ### ### ### ### ### ### ### ### ### ###
0.1329188884 0 0.1329183884 0.1329182 0.1329183884 0.13292 0.13296 34.65 0 0 5.4171717027 5.4171713027 5.417171 -0.0001909295 -0.0001913295 -0.000191 5.41717
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
tafel 13 33.10 API 0.8596597813 RD -0.00019 WCF
-0.00019 WCF
tafel 29 33.10 RD
1.075
0.85966 WCF 0.13637
0.16788
WCF
0.16788
0.13637 RD
5.94486650905105E-006 RD
0.859681
23801916.84 API
33.1
1.075
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
BUNKER before Diesel
BUNKER after
Diesel
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
###
###
###
###
###
###
###
###
###
###
###
ULLAGE after ### ### ###
###
###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
VESSEL ULLAGE REPORT BEFORE DISCHARGE
VESSEL NAME
0
GRADE
Masila Export Blend Crude Oil
LOCATION
0
DATE
June 21 ,2003
Tanks No. 1-C 2-C 4-C 3-P 3-S 5-P 5-S
Obsd. MMC Corr. Ullage Corr. Ullage mm. mm. mm. 4110 3920 4250 4270 4250 5000 4940
Less
T.O.V. Barrels.
4110 3920 4250 4270 4250 5000 4940 Line
Free Water Dips Volume mm. Bbls.
153,471 Nil 145,671 Traec 143,718 Traec 142,518 Nil 142,631 Nil 117,165 Nil 117,467 Nil -120
TOTALS
962,521
A.P.I.
Barrels.
@ 60oF
0 0 0 0 0 0 0
0
TOTAL QUANTITIES DISCHARGED
G.O.V. 153,471 145,671 143,718 142,518 142,631 117,165 117,467 -120
Temp.
V.C.F.
G.S.V.
F
T-6A
Barrels.
90.9 92.8 93.2 89.1 88.9 91.4 91.0 91.0
0.9859 0.9850 0.9850 0.9868 0.9868 0.9857 0.9859 0.9859
o
31.70 31.70 31.70 31.70 31.70 31.70 31.70 31.70
962,521 Av.Temp.
DRAFT CONDITION :-
91.0 W.C.F. ( T-13 )
151,307 143,486 141,562 140,637 140,748 115,490 115,811 -118
948,923 0.13754
T.O.V. ( Barrels.)
962,521
Fwd
19.92
M.
Metric Tons.
130,514.869
G.O.V.( Barrels.)
962,521
Aft
19.92
M.
Long Tons.
128,415.77
T.C.V. ( Barrels.)
948,923
Trim
Nil
Table 11
G.S.V. ( Barrels.)
948,923
List
Nil
A.P.I. @ 60oF
Less ROB (Barrels) G.S.V. ( Barrels.) Metric Tons.(in air) Long Tons.
0 948,923 130,514.869 17,667.80
Chief Officer
Sea Condition/Temp.
Slight / 30oC
Segregated Ballast tanks
Fpt,2-P/S,4-P/S,6-P/S(WBT) & Apt.
Non-Segregated Ballast tanks
None
Lines drained to
-
Saybolt Inspector
0.13537 31.70
Temp. deg. C TOP MID LOW Average 1-C 2-C 4-C 3-P 3-S 5-P 5-S 0 0 0 0 0 0 0 0 0
33.5 33.4 32.7 32.7 32.7 32.9 32.8 32.6 33.0 32.8 32.8 33.5 33.4 36.8 35.9 36.3 32.1 32.2 32.2 32.4 32.4 32.5 32.6
33.5 33.4 32.7 32.7 32.7 32.9 32.8 32.6 33.0 32.8 32.8 33.5 33.4 36.8 35.9 36.3 31.5 31.7 31.9 32.2 31.9 31.9 33.8
33.5 33.4 32.7 32.7 32.7 32.9 32.8 32.6 33.0 32.8 32.8 33.5 33.4 36.8 35.9 36.3 30.1 30.5 29.9 30.2 29.9 29.7 31.2
Total average
Temp. deg. F Average
33.5 33.4 32.7 32.7 32.7 32.9 32.8 32.6 33.0 32.8 32.8 33.5 33.4 36.8 35.9 36.3 31.2 31.5 31.3 31.6 31.4 31.4 32.5
92.3 92.1 90.9 90.9 90.9 91.2 91.0 90.7 91.4 91.0 91.0 92.3 92.1 98.2 96.6 97.3 88.2 88.6 88.4 88.9 88.5 88.5 90.6
33.0
91.4
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23
93.3 93.4 92.5 95.4 93.4 89.3 89.4 89.7 89.8 90.0 90.4 91.0 91.6
t (1,2 of 3) API 60 (K)
1 31.70 0.13296
F
t=1 t=2
t=1 t=2
t=3
2,240.00
A1
34
W A2
0.05 34.7
D1
0.85189645
B1
0.13299903
X
0.00000000
E_1 E_2
0.13299863 0.13299850
E1 D1! D2
0.13299863 0.13300000 0.85138387
B2 X E_1 E_2 E2 D2! C A1 W A2 B1 E1 D1 B2 E2 D2 C_3
0.13291889 0.00000000 0.1329183884 0.13291820 0.13291839 0.13292000 0.13296000 34.65 0 0 5.41717170 5.4171713027 5.41717100 (0.00019093) (0.00019133) (0.00019100) 5.41717000
En weer terug van WCF naar API etc. INPUT WCF OUTPUT API/RD fun 83 wcf x d x1 API
tafel 11 0.16804 API 1.0761175744 RD 1.0760246193 WCF 131.5025673746 0.0025673746 WCF RD API
This is the function to regain API or RD from WCF
WCF TABLE RESULT RD API RD API RD
0.16804 2 1=T11,2=T13,3=T29 2.11 1.0760220612 Calc T11 0 Result T11 1.0590459655 Calc T13 2.11 Result T13 1.076 Calc+ResultT29
Vul 1,2 of 3 in
1 31.70
Vul 1,2 of 3 in
T13 Calc
BUNKER before
0.13296
Fuel Oil
2240
API (b)
31.70
###
###
###
34
b+131.5
163.2
###
###
###
535.1911/b+131.5 Vul 1,2 of 3 in
### ###
### ###
### ###
### ###
Vul 1,2 of 3 in
###
###
###
###
ULLAGE before ### #REF! ### ###
###
0.05 34.7 0.8518964479 0.1329990268 0 0.1329986268 0.1329985
wijz july 97
wijz july 97
wijz july 97 wijz july 97
0.1329986268 0.133 0.8513838748
### ### ###
### ### ### ### ### ### ### ### ### ### ### ###
0.1329188884 0 0.1329183884 0.1329182 0.1329183884 0.13292 0.13296 34.65 0 0 5.4171717027 5.4171713027 5.417171 -0.0001909295 -0.0001913295 -0.000191 5.41717
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
tafel 13 31.70 API 0.8670343137 RD -0.00019 WCF
-0.00019 WCF
tafel 29 31.70 RD
1.075
0.867034 WCF 0.13754
0.16788
WCF
0.16788
0.13754 RD
5.94486650905105E-006 RD
0.867046
23801916.84 API
31.7
1.075
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
BUNKER before Diesel
BUNKER after
Diesel
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
###
###
###
###
###
###
###
###
###
###
###
ULLAGE after ### ### ###
###
###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
ROB REPORT VESSEL NAME
0
GRADE
Masila Export Blend Crude Oil
LOCATION
0
DATE
August 11, 2016
Tanks No. 1-C 2-C 4-C 3-P 3-S 5-P 5-S
Totals Obsd.Oil+Water Dips Cms. Nil Nil Nil Nil Nil Nil Nil
Volume Barrels -
Totals
Liquid Oil Dips Cms. Nil Nil Nil Nil Nil Nil Nil
Non-Liquid Oil
Volume Barrels -
0
Dips Cms. Nil Nil Nil Nil Nil Nil Nil
0
R.O.B. Volume ( Barrels )
Volume Barrels -
Free Water Dips Cms. Nil Nil Nil Nil Nil Nil Nil
Volume Barrels -
0
0
Vessel Draft Condition
Obs. Oil+Water
0
Fwd
#REF! M. Measurements location point(s)
Aft of Centre
Liquid Oil
0
Aft
#REF! M. Trim/Heel corrections applied
No
Non-Liquid Oil
0
Trim
#REF! M. Wedge formula applied
Yes
Free Water
0
List
Totals R.O.B.
0
Sea Condition / Temp.
Sea Chest Valves Notes.
Sealed Nos.
Nil
Tanks washing performed
No
Slight / 30oC
Hydraullically Operated from CCR.
1. Above volume presumed to be at standard temperature unless otherwise noted. 2.Above volume exclude any clingage. 3. Measurements are taken at one point only unless otherwise stated. 4. Vessel's tanks inerted.
REMARKS :1). The above ROB volume "Liquid Cargo" of a pumpable nature and "Non-Liquid Cargo" of unpumpable nature. 2). The above ROB of Liquid volume are calculated as applied by vessel wedge table on board.
Chief Officer
Saybolt Inspector
WEDGE CALCULATION REPORT VESSEL NAME
#REF!
GRADE
#REF!
LOCATION
#REF!
DATE
#REF!
Tk.Height Ull.Dist. (D) (U) Nos. Metres Metres
Tank
(-) DF
Length Length ( + ) of Tank Factor S (L) ( LF ) Metres
A
(x) Volume W Metres Cu.Mtrs.
A
2
Trim Factor (F)
Volume Barrels
2-C
30.920
7.850
0.2945
49.050
0.46715
0.010
0.0820
0.006724
23.800
8.401
0.009524
53
3-C
30.920
6.550
0.2945
32.700
0.31143
0.030
0.0896
0.008028
23.800
10.031
0.009524
63
5-C
30.920
6.550
0.2945
32.700
0.31143
0.020
0.0796
0.006336
23.800
7.917
0.009524
50
6-C
30.920
7.000
0.2945
47.750
0.45477
0.030
0.0939
0.008817
23.800
11.017
0.009524
69
2-S
20.900
6.350
0.1991
49.050
0.46715
0.010
0.0686
0.004706
13.700
3.385
0.009524
21
4-P
20.900
6.350
0.1991
49.050
0.46715
0.010
0.0686
0.004706
13.700
3.385
0.009524
21
4-S
20.900
6.350
0.1991
49.050
0.46715
0.010
0.0686
0.004706
13.700
3.385
0.009524
21
6-P
20.900
11.900
0.1991
38.150
0.36334
0.010
0.1214
0.014738
3.600
2.785
0.009524
18
6-S
20.900
11.900
0.1991
38.150
0.36334
0.040
0.1514
0.022922
3.600
4.332
0.009524
27
Totals Volume " Liquid Oil " Code A D S
ALL MEASUREMENTS MUST BE UNIT IN METRES Adjusted innage at aft. bulkhead of tank Mean total guage height
W
Sounding (innage) Distance from sounding point to aft. bulkhead of tank Width of tank
DF
Mean total guage height x trim factor
U F L
LF
Trim factor
Length of tank
Length of tank x trim factor Note
54.638
343
FIELD INFORMATION Draft condition Draft
(Metres)
(Aft-Fwd)
FWD
7.00
AFT
10.00
LBP
315.00
TRIM
Length between perpendicular Trim Factor (Trim/LBP)
WEDGE FORMULA
F
((( U-DF ) x F ) + S )2 x W = Cu.Metres. Sea Condition
2F
#REF!
: If " A " is greaten than " LF " use ship calibration tables. If " A " is less than " LF " use wedge formula.
Chief Officer
Saybolt Inspector
3.00 ###
VESSEL
:0
LOCATION
:0
GRADE
:0
DATE
:0
BUNKER REPORT Diesel Oil
Main engine type
: IHI-SULZER 7RTA84
Daily consumption :At sea, speed
:
Nil
Inport (Loading)
:
2.50
Inport (Discharging)
:
At anchor
:
ARRIVAL BUNKER ,
Last Port of Call
: Mina Al Fahal ,Oman
M/Tons.
Sailing date
: 07-06-2003
3.20
M/Tons.
Sailing F.O.
:
2,820.348 M/Tons.
2.50
M/Tons.
Sailing D.O.
:
121.611 M/Tons.
Date :
21-06-03 Time : 0330 hrs. Draft, FWD
16.25
M. Draft, AFT
16.25
M.
Tank
Corr.Ullage
Obsd. Volume
Temp.
Density
V.C.F.
Std.Volume
W.C.F.
Metric Tons
Nos.
Metres
Cu.Mtrs.
oC
@ 15oC
T-54 B
Cu.Mtrs.
T-56
in air
Storage Serv-Tk
5.720 Gauge
35.00 40.00
0.9835 0.9793
0.9862 0.9826
130.00 7.70
DEPARTURE BUNKER, Date :
11-08-16 Time :
Tank
Corr.Ullage
Obsd. Volume
Nos.
Metres
Cu.Mtrs.
Storage Serv-Tk
4.580 Gauge
Totals Bunkers Arrival Departure Difference
246.80 7.60
Density
oC 35.00 38.00
Metric Tons
Cu.Mtrs. 135.772 250.872 -115.100
in air 133.351 246.425 -113.074 No
Laboratory analysis carried out
No
REMARKS
Temp.
Std. Volume
Gauges corrected for trim ,before : :
1630 hrs. Draft, FWD
after :
128.206 7.566
7.50
M. Draft, AFT
V.C.F.
Std.Volume
@ 15oC
T-54 B
Cu.Mtrs.
0.9835 0.9793
0.9862 0.9840
243.394 7.478
Bunkers loaded this port
0.9824 0.9782
10.50
M.
W.C.F.
Metric Tons
T-56
in air
0.9824 0.9782
:
239.110 7.315
No
Obs.Volume(M3)
-
Std.Volume(M3)
-
Metric Tons
-
Density @15oC
-
Yes
:
Chief Engineer
125.950 7.401
Saybolt Inspector
VESSEL
:0
LOCATION
:0
GRADE
:0
DATE
:0
BUKER REPORT Fuel Oil
Main engine type
: IHI-SULZER 7RTA84
Daily consumption :At sea, speed
:
60.00 M/Tons.
Last Port of Call
: Mina Al Fahal ,Oman
Inport (Loading)
:
12.00 M/Tons.
Sailing date
: 07-06-2003
Inport (Discharging)
:
60.00 M/Tons.
Sailing F.O.
:
2,820.348 M/Tons.
At anchor
:
10.00 M/Tons.
Sailing D.O.
:
121.611 M/Tons.
ARRIVAL BUNKER ,
Date :
21-06-03 Time : 0330 hrs. Draft, FWD
16.25
M. Draft, AFT
16.25
M.
Tank
Corr.Ullage
Obsd. Volume
Temp.
Density
V.C.F.
Std.Volume
W.C.F.
Metric Tons
Nos.
Metres
Cu.Mtrs.
oC
@ 15oC
T-54 B
Cu.Mtrs.
T-56
in air
Port-Tk Stbd-Tk Serv-Tk Sett-Tk Ov-Flow
12.710 12.890 Gauge Gauge Empty
53.00 51.00 88.00 85.00
0.9731 0.9745 0.9480 0.9502
0.9733 0.9748 0.9466 0.9490
1,080.30 1,055.30 32.50 30.00
DEPARTURE BUNKER, Date : Tank
11-08-16 Time :
Corr.Ullage
Obsd. Volume
Nos.
Metres
Cu.Mtrs.
Port-Tk Stbd-Tk Serv-Tk Sett-Tk Ov-Flow
12.710 12.890 Gauge Gauge Empty
Totals
1,080.30 1,055.30 32.50 30.00
Std. Volume
Bunkers Arrival Departure Difference
Cu.Mtrs. 2,139.397 2,139.397 0.000
Density
oC 53.00 51.00 88.00 85.00
Laboratory analysis carried out
No
after :
7.50
Std.Volume
@ 15oC
T-54 B
Cu.Mtrs.
0.9731 0.9745 0.9480 0.9502
0.9733 0.9748 0.9466 0.9490
1,051.456 1,028.706 30.765 28.470
Bunkers loaded this port
0.9720 0.9734 0.9469 0.9491
M. Draft, AFT
V.C.F.
in air 2,079.509 2,079.509 0.000 No
REMARKS
Temp.
Metric Tons
Gauges corrected for trim ,before : :
1630 hrs. Draft, FWD
1,051.456 1,028.706 30.765 28.470
W.C.F. T-56 0.9720 0.9734 0.9469 0.9491
:
10.50 in air
1,022.015 1,001.342 29.131 27.021
No -
Std.Volume(M3)
-
Metric Tons
-
Density @15oC
-
Yes
Saybolt Inspector
M.
Metric Tons
Obs.Volume(M3)
:
Chief Engineer
1,022.015 1,001.342 29.131 27.021
VESSEL
:0
LOCATION
:0
GRADE
:0 :0
DATE
SLOP CERTIFICATE
Tank Nos.
Slop-Port
Slop-Port
Previous Cargo Loaded Density @ 15oC / API @ 60oF Uncorrected Ullage (mm.) Trim Correction (mm.) MMC Correction (mm.) Corrected Ullage (mm.) Total Observed Volume (Barrels) Free Water Ullage (mm.)
NO SLOP ON BOARD
Corrected Ullage (mm.) Free Water Volume (Barrels) Gross Observed Volume (Barrels) Observed Temperature (oC) Density @ 15oC / API @ 60oF V.C.F.( T-
)
Gross Standard Volume (Barrels) W.C.F.( T-
)
Metric Tons.(in air) Calibrated Height (mm.) Reference Height (mm.) Before Will cargo be load on top of slop :
No
REMARKS
Chief Officer
Saybolt Inspector
After
VESSEL LOCATION GRADE DATE
: : : :
0 0 0 Dec-99
VOID/BALLAST SPACE REPORT
BEFORE COMPARTMENT/TANKS TYPE/VOLUME OF CONTENTS Fore Peak Tank S.Ballast : 1,975 1-Port ( WBT ) Empty 1-Stbd ( WBT ) Empty 2-Port ( WBT ) Empty 2-Stbd ( WBT ) Empty 3-Port ( WBT ) Empty 3-Stbd ( WBT ) Empty 4-Port ( WBT ) Empty 4-Stbd ( WBT ) Empty 5-Port ( WBT ) Empty 5-Stbd ( WBT ) Empty Aft Peak Tank Empty
TOTALS
Ballasted :
1,975
AFTER TYPE/VOLUME OF CONTENTES M/Tons. S.Ballast : 1,230 S.Ballast : 7,370 S.Ballast : 7,370 S.Ballast : 9,500 S.Ballast : 9,500 S.Ballast : 10,500 S.Ballast : 10,500 S.Ballast : 9,250 S.Ballast : 9,250 S.Ballast : 6,100 S.Ballast : 6,100 S.Ballast :
M/Tons. M/Tons. M/Tons. M/Tons. M/Tons. M/Tons. M/Tons. M/Tons. M/Tons. M/Tons. M/Tons. M/Tons.
M/Tons. Ballasted :
M/Tons.
1. Volume of oil received from ballast pumped ashore
: Nil
2. Tanks used by ship for previous ballast voyage
: Same as above tanks
- Commenced ballasting operation - Completed ballasting operation
86,670
: 2000 Hrs.,On May 04 ,2003 : 1500 Hrs.,On May 06 ,2003
REMARKS
Chief Officer
Saybolt Inspector
VESSEL
: 0
LOCATION
: 0
GRADE
: 0
DATE
: 0
VESSEL EXPERIENCE REPORT
Date
Grade
Loadport
Ships Quantity Less OBQ
Bill of Lading
Bbls.
Bbls.
V.L.R. Ship Shore
QL Voy. Y/N
09-03-2003
AMCO./ALCO./AXLCO.
Ras Tanura
1,982,789
1,981,323
1.00074
N
29-01-2003
QLCO./MBCO./OMECO.
Mesaieed/J.Dhanna/M.A.F.
1,926,027
1,930,645
0.99761
Y
12-12-2002
Soroosh CO./Kuwait Ex.CO.
Soroosh/M.Al Ahmadi
1,913,810
1,912,145
1.00087
N
28-10-2002
Khafji CO./ Arab Ext. Lt.CO.
Khafji / Ras Tanura
1,951,251
1,956,495
0.99732
Y
16-09-2002
Arabian Light CO.
Ras Tanura
1,964,280
1,974,105
0.99502
Y
02-08-2002
Arabian Light CO.
Ras Tanura
1,963,846
1,974,180
0.99477
Y
21-06-2002
Kuwait Ex.CO./Iran Lt.CO.
M.Al Ahmadi/Kharg Is.
1,941,337
1,942,854
0.99922
Y
07-05-2002
OMECO./AL./AM./IRHCO.
M.A.F./R.Tanura/Kharg Is.
1,855,326
1,860,044
0.99746
Y
20-03-2002
Um.Shaif CO./ QMCO.
Das Island/Halul
1,895,034
1,897,040
0.99894
Y
06-02-2002
QLCO./AEL./L.Zakum CO.
Mesaieed/Juaymah/Das Is.
1,940,137
1,947,399
0.99627
Y
27-12-2001
AXLCO.Khafi CO./UZCO.
R.Tanura/Khafji/Zirku Is.
1,990,084
1,997,665
0.99621
Y
04-11-2001
Sirri /Ratawi /OMECO.
Sirri Is./M.Saud/M.A.F.
1,859,166
1,866,430
0.99611
Y
10-09-2001
Sirri/Ratawi/AHCO./AELCO.
Sirri Is./M.Saud/R.Tanura
1,971,387
1,973,494
0.99893
Y
26-07-2001
U.Zakum CO./Iran Lt.CO.
Zirku Is./Kharg Is.
1,972,529
1,978,037
0.99722
Y
12-06-2001
QLCO./AHCO./AXLCO.
Mesaieed/R.Tanura
1,915,312
1,919,437
0.99785
Y
07-05-2001
Kuwait Export Blend CO.
Mina Al Ahmadi
1,885,100
1,887,270
0.99885
Y
Totals.
30,927,415
30,998,563
0.99770
Qualifying Totals.
27,030,816
27,105,095
0.99726
1st Average (Total Ship/Total B/L)
0.99770
1st average of (0.3%) = +/-
(+)
2nd average(Qualitying Total Ship/Qualfying Total B/L) Range of accuracy (0.3 %) = +/-
1.00069
(-)
0.99471
(-)
0.99427
0.99726
(+)
Ship Figures this voyage (Excluding OBQ) Bill Of Lading this voyage Vessel loaded ratio this voyage
1.00025
0.9973
Vessel Experience Factor based on 2nd average
The Above mentioned quantities are for the last ### voyages as obtained from ships record and cannot be guaranteed as accurate by Saybolt. No liability can be assumed for errors resulting from improper information supplied by the vessel. Voyages Excludes :When Bill of Lading is established from vessels measurements. Prior to major cargo tank modifications. Lighterings. First voyage after dry dock. Signed : Chief Officer
Saybolt Inspector
0 1,926,027 0 1,951,251 1,964,280 1,963,846 1,941,337 1,855,326 1,895,034 1,940,137 1,990,084 1,859,166 1,971,387 1,972,529 1,915,312 1,885,100
0 1,930,645 0 1,956,495 1,974,105 1,974,180 1,942,854 1,860,044 1,897,040 1,947,399 1,997,665 1,866,430 1,973,494 1,978,037 1,919,437 1,887,270
27,030,816
27,105,095
1st 2nd
0.30%
-0.30%
0.00299
-0.00299
0.00299
-0.00299
VESSEL LOCATION GRADE DATE
: : : :
0 0 0 0
CRUDE OIL WASH REPORT Page 1 of 2
Type of Vessel
Oil Tankers
Is the Inert Gas sytem confirmed to be fully operational by the Vessel
Yes
Pressure of Inert Gas in tanks to be wash
450 mmAq
Tanks nominated to be COW Have ship and shore personnel reashed agreement on the proposed COW operation Cargo Pump Capacities - Main cargo pump - General purpose pump - Stripping pump - Eductors
All nominated cargo tanks bottom wash Yes (TCP)
4 x 4,000 1 x 2,750 1 x 300 2 x 1,100
Specify pumps to be used for COW
Cu.Mtres. per Hour. Cu.Mtres. per Hour. Cu.Mtres. per Hour. Cu.Mtres. per Hour. TCP
Type / Number of COW machines fitted and location
Fixed COW Machines -
Date when was integrity of COW system last checked
27-Mar-2003
Date when in-line oxygen analysing equipment last checked
27-Mar-2003
Maximum oxygen content to be maintained in cargo tanks according to local port regulations
8.0%
Actual oxygen content of tanks at start of COW
3.1%
Are operational alarm systems fitted to in-line oxygen analysing equipment situated in ship cargo control room Cargo control room oxygen alarm set at
Yes 8.0%
REMARKS : 1).Full COW was allowed to conducts by the vessel at a maximum with 25% of all nominated cargo tanks as according to local port regulations. 2).An additional COW operation as instructed by Terminal,with bottom wash only.(for all nominated cargo tanks).
Cont / 2
Chief Officer
Saybolt Inspector
VESSEL LOCATION GRADE DATE
: : : :
0 0 0 0
CRUDE OIL WASH REPORT Page 2 of 2
TANK
COW STARTED Time
REMARKS
Date
COW FINISHED Time
Date
DRIVE TANK Pressure Oxygen Kg/Cm2 %
TANK SECTION WASHED
:
Chief Officer
Saybolt Inspector
VESSEL ULLAGE REPORT BEFORE DISCHARGE
VESSEL NAME
#REF!
GRADE
#REF!
LOCATION
#REF!
DATE
March 30 ,2003
Tanks No. 1-C 2-C 3-C 4-C 5-C 1-P 1-S 3-P 3-S 5-P 5-S SL-P SL-S
Obsd. MMC Corr. Ullage Corr. Ullage mm. mm. mm. 1310 1280 1300 1280 1220 1310 1310 1450 1370 1580 1580 1350 1410
-
TOTALS
T.O.V. Barrels.
1310 1280 1300 1280 1220 1310 1310 1450 1370 1580 1580 1350 1410
185,057 207,933 207,796 207,933 230,798 99,584 99,584 135,705 136,072 102,576 102,576 22,794 22,727
Free Water Dips Volume mm. Bbls. Trace Nil Nil Trace Nil Nil Trace Trace Nil Nil Nil Trace Nil
1,761,135
A.P.I.
Barrels.
@ 60oF
0 0 0 0 0 0 0 0 0 0 0 0 0
0
TOTAL QUANTITIES DISCHARGED
G.O.V. 185,057 207,933 207,796 207,933 230,798 99,584 99,584 135,705 136,072 102,576 102,576 22,794 22,727
Temp.
V.C.F.
G.S.V.
F
T-6A
Barrels.
95.2 98.1 96.8 98.2 98.2 89.6 89.6 91.0 91.4 91.0 91.0 92.3 92.1
0.9841 0.9827 0.9831 0.9827 0.9827 0.9866 0.9866 0.9859 0.9857 0.9859 0.9859 0.9852 0.9854
o
31.70 31.70 31.70 31.70 31.70 31.70 31.70 31.70 31.70 31.70 31.70 31.70 31.70
1,761,135 Av.Temp.
DRAFT CONDITION :-
94.2 W.C.F. ( T-13 )
182,115 204,336 204,284 204,336 226,805 98,250 98,250 133,792 134,126 101,130 101,130 22,457 22,395
1,733,406 0.13754
T.O.V. ( Barrels.)
1,761,135
Fwd
19.90
M.
Metric Tons.
238,412.661
G.O.V.( Barrels.)
1,761,135
Aft
19.90
M.
Long Tons.
234,651.17
T.C.V. ( Barrels.)
1,733,406
Trim
Nil
Table 11
G.S.V. ( Barrels.)
1,733,406
List
Nil
A.P.I. @ 60oF
Less ROB (Barrels)
#REF!
Sea Condition/Temp.
Slight / 30oC
G.S.V. ( Barrels.)
#REF!
Segregated Ballast tanks
Fpt,2-P/S,4-P/S,6-P/S(WBT) & Apt.
Metric Tons.(in air)
#REF!
Non-Segregated Ballast tanks
None
Long Tons.
#REF!
Lines drained to
-
Chief Officer
Saybolt Inspector
0.13537 31.70
Temp. deg. C TOP MID LOW Average 1-C 2-C 3-C 4-C 5-C 1-P 1-S 3-P 3-S 5-P 5-S SL-P SL-S 0 0 0
35.1 36.7 36.0 36.8 36.8 32.0 32.0 32.8 33.0 32.8 32.8 33.5 33.4 36.8 35.9 36.3 32.1 32.2 32.2 32.4 32.4 32.5 32.6
35.1 36.7 36.0 36.8 36.8 32.0 32.0 32.8 33.0 32.8 32.8 33.5 33.4 36.8 35.9 36.3 31.5 31.7 31.9 32.2 31.9 31.9 33.8
35.1 36.7 36.0 36.8 36.8 32.0 32.0 32.8 33.0 32.8 32.8 33.5 33.4 36.8 35.9 36.3 30.1 30.5 29.9 30.2 29.9 29.7 31.2
Total average
Temp. deg. F Average
35.1 36.7 36.0 36.8 36.8 32.0 32.0 32.8 33.0 32.8 32.8 33.5 33.4 36.8 35.9 36.3 31.2 31.5 31.3 31.6 31.4 31.4 32.5
95.2 98.1 96.8 98.2 98.2 89.6 89.6 91.0 91.4 91.0 91.0 92.3 92.1 98.2 96.6 97.3 88.2 88.6 88.4 88.9 88.5 88.5 90.6
33.7
92.6
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23
93.3 93.4 92.5 95.4 93.4 89.3 89.4 89.7 89.8 90.0 90.4 91.0 91.6
t (1,2 of 3) API 60 (K)
1 31.70 0.13296
F
t=1 t=2
t=1 t=2
t=3
2,240.00
A1
34
W A2
0.05 34.7
D1
0.85189645
B1
0.13299903
X
0.00000000
E_1 E_2
0.13299863 0.13299850
E1 D1! D2
0.13299863 0.13300000 0.85138387
B2 X E_1 E_2 E2 D2! C A1 W A2 B1 E1 D1 B2 E2 D2 C_3
0.13291889 0.00000000 0.1329183884 0.13291820 0.13291839 0.13292000 0.13296000 34.65 0 0 5.41717170 5.4171713027 5.41717100 (0.00019093) (0.00019133) (0.00019100) 5.41717000
En weer terug van WCF naar API etc. INPUT WCF OUTPUT API/RD fun 83 wcf x d x1 API
tafel 11 0.16804 API 1.0761175744 RD 1.0760246193 WCF 131.5025673746 0.0025673746 WCF RD API
This is the function to regain API or RD from WCF
WCF TABLE RESULT RD API RD API RD
0.16804 2 1=T11,2=T13,3=T29 2.11 1.0760220612 Calc T11 0 Result T11 1.0590459655 Calc T13 2.11 Result T13 1.076 Calc+ResultT29
Vul 1,2 of 3 in
1 31.70
Vul 1,2 of 3 in
T13 Calc
BUNKER before
0.13296
Fuel Oil
2240
API (b)
31.70
###
###
###
34
b+131.5
163.2
###
###
###
535.1911/b+131.5 Vul 1,2 of 3 in
### ###
### ###
### ###
### ###
Vul 1,2 of 3 in
###
###
###
###
ULLAGE before ### #REF! ### ###
###
0.05 34.7 0.8518964479 0.1329990268 0 0.1329986268 0.1329985
wijz july 97
wijz july 97
wijz july 97 wijz july 97
0.1329986268 0.133 0.8513838748
### ### ###
### ### ### ### ### ### ### ### ### ### ### ###
0.1329188884 0 0.1329183884 0.1329182 0.1329183884 0.13292 0.13296 34.65 0 0 5.4171717027 5.4171713027 5.417171 -0.0001909295 -0.0001913295 -0.000191 5.41717
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
tafel 13 31.70 API 0.8670343137 RD -0.00019 WCF
-0.00019 WCF
tafel 29 31.70 RD
1.075
0.867034 WCF 0.13754
0.16788
WCF
0.16788
0.13754 RD
5.94486650905105E-006 RD
0.867046
23801916.84 API
31.7
1.075
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
BUNKER before Diesel
BUNKER after
Diesel
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
### ###
###
###
###
###
###
###
###
###
###
###
###
ULLAGE after ### ### ###
###
###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###
SAYBOLT (THAILAND) LIMITED
VESSEL LOCATION GRADE DATE
: : : :
#REF! #REF! #REF! #REF!
CRUDE OIL WASH REPORT Page 1 of 2
Type Of Vessel
Oil Tankers
Is the Inert Gas sytem confirmed to be fully operational by the Vessel Pressure of Inert Gas in tanks to be wash Tanks nominated to be COW Have ship and shore personnel reashed agreement on the proposed COW operation Cargo Pump Capacities - Main cargo pump - General purpose pump - Stripping pump - Eductors Specify pumps to be used for COW
Yes 600 mmWG 4-C,4-P/S & Slop-S ( Minimum marpol ) Yes 3 x 2,500 N/A 1 x 200 1 x 450
Cu.Mtres. per Hour. Cu.Mtres. per Hour. Cu.Mtres. per Hour.
COP No. 3
Type / Number of COW machines fitted and location
Fixed COW Machines -
Date when was integrity of COW system last checked
11-Oct-2002
Date when in-line oxygen analysing equipment last checked
11-Oct-2002
Maximum oxygen content to be maintained in cargo tanks according to local port regulations
8.0%
Actual oxygen content of tanks at start of COW
2.5%
Are operational alarm systems fitted to in-line oxygen analysing equipment situated in ship cargo control room Cargo control room oxygen alarm set at
Yes 8.0%
REMARKS : 1).Full COW allowed 25% of all nominated cargo tanks as according with local port regulations the vessel was performed. 2).An additional COW operation as instructed by Terminal,with bottom wash only.(for all nominated cargo tanks). 3).The vessel COW was conducted of 25% with minimun marpol only by performed as per charter parties.
Cont / 2
Chief Officer
Saybolt Inspector
Cont / 2
A
B
t (1,2 of 3) API 60 (K)
1 2 3 4 5 6 7 8 9 10
t=1 12 t=2 11 13 14 15 16 17
t=1 19 t=2 18 20 21 22 23 24 25 26 27
t=3
F A1 W A2 D1 B1 X E_1 E_2 E1 D1! D2 B2 X E_1 E_2 E2 D2! C A1 W A2 B1 E1
C
D
1 Table11 31.70 0.13537 Ltons/Bbl-60 2,240.00 31.7 0 0 0.86703431 0.13536576 0.00000000 0.13536536 0.13536530 0.13536536 0.13537000 1.07604563 0.16804368 0.00000000 0.1680431845 0.16804300 0.16804318 0.16804000 0.13537000 31.7 0 0 wijz july 97 4.95595324 4.9559528391
E
1 31.70 0.13537 2240 31.7 0 0 0.8670343137 0.1353657601 0 0.1353653601 0.1353653 0.1353653601 0.13537 1.0760456274 0.1680436845 0 0.1680431845 0.168043 0.1680431845 0.16804 0.13537 31.7 0 0 4.9559532391 4.9559528391
A 28 29 30 31 32
B
D1 B2 E2 D2 C_3
C
4.95595300 (0.00019093) (0.00019133) (0.00019100) 4.95595000
33 34
En weer terug van WCF naar API etc. WCF 36 INPUT 37 OUTPUT API/RD 35
D
wijz july 97
wijz july 97 wijz july 97
E
4.955953 -0.0001909295 -0.0001913295 -0.000191 4.95595
F
G
H
I
J
1
T13 Calc
2 3 4 5 6 7 8
API (b) b+131.5 535.1911/b+131.5 Ltons/Bbl-60 Ltons/Bbl-60
31.70 163.2 3.2793572304 3.2747 0.13754
9 10
ULLAGE
11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27
#REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF!
#REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF!
F 28 29 30 31 32 33 34 35 36 37
G
H
I
J
#REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF!
#REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF!
