Tanker Cargo Calculations

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

###

###

###

###

###

5.4171713027

###

###

###

###

###

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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###

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###

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###

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###

###

###

###

###

ULLAGE after

###

###

###

###

###

### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ### ###

### ### ### ### ### ### ### ### ### ###

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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!