2 VLCC example
2.1 General Data
L
|
:
|
321.10 m
|
(length as defined in regulation 1.19)
|
ds
|
:
|
21.20 m
|
(moulded load line draught)
|
dB
|
:
|
8.865 m
|
(moulded draught corresponding to
30% of the depth Ds)
|
Bs
|
:
|
60.00 m
|
(the greatest moulded breadth at
the deepest load line ds)
|
BB
|
:
|
60.00 m
|
(the greatest moulded breadth at the
waterline dB)
|
Ds
|
:
|
29.55 m
|
(moulded depth)
|
DW
|
:
|
300,000 ton
|
(deadweight as defined in regulation 1.23)
|
C
|
:
|
333,200 m3
|
(total volume of cargo oil at 98%
tank filling)
|
Tank Arrangement
Side Damage (No. 1 COT (Fr.96-Fr.106))
Side Damage (Nos. 2,3,4 COT (Fr.66-Fr.96))
Side Damage (No.5 COT & SLOP (Fr.56-Fr.66))
Bottom Damage (No.1 COT (Fr.96-Fr.106))
Bottom Damage (Nos.2,3,4 COT (Fr.66-Fr.96))
Bottom Damage (Nos.5 & SLOP (Fr.56-Fr.66))
2.2 Side damage outflow calculation
2.2.1 Each tank capacity and compartment boundaries
Xa, Xf, Zl, Zu and y are
as follows:
Cargo
Tank
|
98%
Vol (m3)
|
Xa (m)
|
Xf (m)
|
Zl (m)
|
Zu (m)
|
y
(m)
|
No.1
C.O.T. (P)
|
14,372
|
252.000
|
302.000
|
3.000
|
29.550
|
25.600
|
No.1
C.O.T. (C)
|
28,890
|
252.000
|
302.000
|
3.000
|
29.550
|
7.600
|
No.1
C.O.T. (S)
|
14,372
|
252.000
|
302.000
|
3.000
|
29.550
|
2.750
|
No.2
C.O.T. (P)
|
19,081
|
202.000
|
252.000
|
3.000
|
29.550
|
41.700
|
No.2
C.O.T. (C)
|
31,821
|
202.000
|
252.000
|
3.000
|
29.550
|
18.300
|
No.2
C.O.T. (S)
|
19,081
|
202.000
|
252.000
|
3.000
|
29.550
|
3.500
|
No.3
C.O.T. (P)
|
19,081
|
152.000
|
202.000
|
3.000
|
29.550
|
41.700
|
No.3
C.O.T. (C)
|
31,821
|
152.000
|
202.000
|
3.000
|
29.550
|
18.300
|
No.3
C.O.T. (S)
|
19,081
|
152.000
|
202.000
|
3.000
|
29.550
|
3.500
|
No.4
C.O.T. (P)
|
19,081
|
102.000
|
152.000
|
3.000
|
29.550
|
41.700
|
No.4
C.O.T. (C)
|
31,821
|
102.000
|
152.000
|
3.000
|
29.550
|
18.300
|
No.4
C.O.T. (S)
|
19,081
|
102.000
|
152.000
|
3.000
|
29.550
|
3.500
|
No.5
C.O.T. (P)
|
12,681
|
67.000
|
102.000
|
3.000
|
29.550
|
38.100
|
No.5
C.O.T. (C)
|
31,821
|
52.000
|
102.000
|
3.000
|
29.550
|
7.200
|
No.5
C.O.T. (S)
|
12,681
|
67.000
|
102.000
|
3.000
|
29.550
|
3.500
|
Slop
tank (P)
|
4,219
|
52.000
|
67.000
|
3.000
|
29.550
|
30.600
|
Slop
tank (S)
|
4,219
|
52.000
|
67.000
|
3.000
|
29.550
|
3.200
|
2.2.2 The probability Ps of breaching
a compartment from side damage is calculated in accordance with paragraph
8.1 of regulation 23:
Ps = PSL PSV PST
Where:
PSL
|
= |
1 - PSf - PSa
|
PSV
|
= |
1 - PSf - PSa
|
PST
|
= |
1 - PSy
|
|
(2.2.2)
|
From the ratios Xa/L, Xf/L,
Z/Bs, Zl/Ds, Zu/Ds,
Yl/Ds, and y, the probabilities associated with
these subdivision locations are interpolated from the table of probabilities
for side damage provided in Paragraph 8.3 of regulation 23.
Cargo
Tank
|
Xa/L
|
Psa
|
Xf/L
|
Psf
|
Zl/Ds
|
Psl
|
Zu/Ds
|
Psu
|
y/Bs
|
Psy
|
No.1
C.O.T. (P)
|
0.7848
|
0.7518
|
0.9405
|
0.0315
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.4267
|
1.0000
|
No.1
C.O.T. (C)
|
0.7848
|
0.7518
|
0.9405
|
0.0315
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.1267
|
0.9029
|
No.1
C.O.T. (S)
|
0.7848
|
0.7518
|
0.9405
|
0.0315
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.0458
|
0.7247
|
No.2
C.O.T. (P)
|
0.6291
|
0.5961
|
0.7848
|
0.1822
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.6950
|
1.0000
|
No.2
C.O.T. (C)
|
0.6291
|
0.5961
|
0.7848
|
0.1822
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.3050
|
1.0000
|
No.2
C.O.T. (S)
|
0.6291
|
0.5961
|
0.7848
|
0.1822
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.0583
|
0.7876
|
No.3
C.O.T. (P)
|
0.4734
|
0.4404
|
0.6291
|
0.3379
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.6950
|
1.0000
|
No.3
C.O.T. (C)
|
0.4734
|
0.4404
|
0.6291
|
0.3379
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.3050
|
1.0000
|
No.3
C.O.T. (S)
|
0.4734
|
0.4404
|
0.6291
|
0.3379
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.0583
|
0.7876
|
No.4
C.O.T. (P)
|
0.3177
|
0.2847
|
0.4734
|
0.4936
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.6950
|
1.0000
|
No.4
C.O.T. (C)
|
0.3177
|
0.2847
|
0.4734
|
0.4936
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.3050
|
1.0000
|
No.4
C.O.T. (S)
|
0.3177
|
0.2847
|
0.4734
|
0.4936
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.0583
|
0.7876
|
No.5
C.O.T. (P)
|
0.2087
|
0.1757
|
0.3177
|
0.6493
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.6350
|
1.0000
|
No.5
C.O.T. (C)
|
0.1619
|
0.1289
|
0.3177
|
0.6493
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.1200
|
0.8992
|
No.5
C.O.T. (S)
|
0.2087
|
0.1757
|
0.3177
|
0.6493
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.0583
|
0.7876
|
Slop
tank (P)
|
0.1619
|
0.1289
|
0.2087
|
0.7583
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.5100
|
1.0000
|
Slop
tank (S)
|
0.1619
|
0.1289
|
0.2087
|
0.7583
|
0.1015
|
0.0011
|
1.0000
|
0.0000
|
0.0533
|
0.7652
|
Cargo
Tank
|
PSL
|
PSV
|
PST
|
PS
|
No.1
C.O.T. (P)
|
0.2167
|
0.9989
|
0.0000
|
0.0000
|
No.1
C.O.T. (C)
|
0.2167
|
0.9989
|
0.0971
|
0.0210
|
No.1
C.O.T. (S)
|
0.2167
|
0.9989
|
0.2753
|
0.0596
|
No.2
C.O.T. (P)
|
0.2217
|
0.9989
|
0.0000
|
0.0000
|
No.2
C.O.T. (C)
|
0.2217
|
0.9989
|
0.0000
|
0.0000
|
No.2
C.O.T. (S)
|
0.2217
|
0.9989
|
0.2124
|
0.0470
|
No.3
C.O.T. (P)
|
0.2217
|
0.9989
|
0.0000
|
0.0000
|
No.3
C.O.T. (C)
|
0.2217
|
0.9989
|
0.0000
|
0.0000
|
No.3
C.O.T. (S)
|
0.2217
|
0.9989
|
0.2124
|
0.0470
|
No.4
C.O.T. (P)
|
0.2217
|
0.9989
|
0.0000
|
0.0000
|
No.4
C.O.T. (C)
|
0.2217
|
0.9989
|
0.0000
|
0.0000
|
No.4
C.O.T. (S)
|
0.2217
|
0.9989
|
0.2124
|
0.0470
|
No.5
C.O.T. (P)
|
0.1750
|
0.9989
|
0.0000
|
0.0000
|
No.5
C.O.T. (C)
|
0.2217
|
0.9989
|
0.1008
|
0.0223
|
No.5
C.O.T. (S)
|
0.1750
|
0.9989
|
0.2124
|
0.0371
|
Slop
tank (P)
|
0.1127
|
0.9989
|
0.0000
|
0.0000
|
Slop
tank (S)
|
0.1127
|
0.9989
|
0.2348
|
0.0264
|
2.2.3 The mean outflow for side damage OMS is
calculated in accordance with paragraph 6 of regulation 23.
C3 = 0.77 for ships having
two longitudinal bulkheads inside the cargo tanks extending over the
length of the cargo block, and 1.0 for all other ships. In this case,
there are two longitudinal bulkheads within the cargo tanks, and C3 =
0.77.
Cargo
Tank
|
OS(i)
|
(PS)(OS(i))
|
No.1
C.O.T. (P)
|
14,371.7
|
0.0
|
No.1
C.O.T. (C)
|
28,890.4
|
606.9
|
No.1
C.O.T. (S)
|
14,371.7
|
856.3
|
No.2
C.O.T. (P)
|
19,080.6
|
0.0
|
No.2
C.O.T. (C)
|
31,820.6
|
0.0
|
No.2
C.O.T. (S)
|
19,080.6
|
897.7
|
No.3
C.O.T. (P)
|
19,080.6
|
0.0
|
No.3
C.O.T. (C)
|
31,820.6
|
0.0
|
No.3
C.O.T. (S)
|
19,080.6
|
897.7
|
No.4
C.O.T. (P)
|
19,080.6
|
0.0
|
No.4
C.O.T. (C)
|
31,820.6
|
0.0
|
No.4
C.O.T. (S)
|
19,080.6
|
897.7
|
No.5
C.O.T. (P)
|
12,681.2
|
0.0
|
No.5
C.O.T. (C)
|
31,820.6
|
710.4
|
No.5
C.O.T. (S)
|
12,681.2
|
470.9
|
Slop
tank (P)
|
4,218.9
|
0.0
|
Slop
tank (S)
|
4,218.9
|
111.5
|
2.3 Bottom damage outflow calculation
2.3.1 Compartment boundaries Xa, Xf,
Yp, Ys and z are taken as follows:
Cargo
Tank
|
Xa (m)
|
Xf (m)
|
Yp (m)
|
Ys
(m)
|
Z
(m)
|
No.1
C.O.T. (P)
|
252.000
|
302.000
|
56.500
|
39.000
|
3.000
|
No.1
C.O.T. (C)
|
252.000
|
302.000
|
41.700
|
18.300
|
3.000
|
No.1
C.O.T. (S)
|
252.000
|
302.000
|
21.000
|
3.500
|
3.000
|
No.2
C.O.T. (P)
|
202.000
|
252.000
|
56.500
|
41.700
|
3.000
|
No.2
C.O.T. (C)
|
202.000
|
252.000
|
41.700
|
18.300
|
3.000
|
No.2
C.O.T. (S)
|
202.000
|
252.000
|
18.300
|
3.500
|
3.000
|
No.3
C.O.T. (P)
|
152.000
|
202.000
|
56.500
|
41.700
|
3.000
|
No.3
C.O.T. (C)
|
152.000
|
202.000
|
41.700
|
18.300
|
3.000
|
No.3
C.O.T. (S)
|
152.000
|
202.000
|
18.300
|
3.500
|
3.000
|
No.4
C.O.T. (P)
|
102.000
|
152.000
|
56.500
|
41.700
|
3.000
|
No.4
C.O.T. (C)
|
102.000
|
152.000
|
41.700
|
18.300
|
3.000
|
No.4
C.O.T. (S)
|
102.000
|
152.000
|
18.300
|
3.500
|
3.000
|
No.5
C.O.T. (P)
|
67.000
|
102.000
|
56.500
|
41.700
|
3.000
|
No.5
C.O.T. (C)
|
52.000
|
102.000
|
41.700
|
18.300
|
3.000
|
No.5
C.O.T. (S)
|
67.000
|
102.000
|
18.300
|
3.500
|
3.000
|
Slop
tank (P)
|
52.000
|
67.000
|
51.780
|
41.700
|
3.000
|
Slop
tank (S)
|
52.000
|
67.000
|
18.300
|
8.220
|
3.000
|
2.3.2 The probability PB of breaching
a compartment from bottom damage is calculated in accordance with
paragraph 9.1 of regulation 23.
PB = PBL PBT PBV
Where:
PBL
|
= |
1 - PBf - PBa
|
PBT
|
= |
1 - PBp - PBS
|
PBV
|
= |
1 - PBZ
|
|
(2.3.2)
|
2.3.3 From the ratios Xa/L, Xf/L,
Yp/BB, Ys/ BB, and z,
the probabilities associated with these subdivision locations are
interpolated from the table of probabilities for bottom damage provided
in paragraph 9.3 of regulation 23.
Cargo
Tank
|
Xa/L
|
PBa
|
Xf/L
|
PBf
|
Yp/BB
|
PBp
|
Ys/BB
|
PBs
|
z/Ds
|
PBZ
|
No.1
C.O.T. (P)
|
0.7848
|
0.3892
|
0.9405
|
0.0379
|
0.9417
|
0.0128
|
0.6500
|
0.4940
|
0.1015
|
0.7817
|
No.1
C.O.T. (C)
|
0.7848
|
0.3892
|
0.9405
|
0.0379
|
0.6950
|
0.1750
|
0.3050
|
0.1750
|
0.1015
|
0.7817
|
No.1
C.O.T. (S)
|
0.7848
|
0.3892
|
0.9405
|
0.0379
|
0.3500
|
0.4940
|
0.0583
|
0.0128
|
0.1015
|
0.7817
|
No.2
C.O.T. (P)
|
0.6291
|
0.2257
|
0.7848
|
0.2766
|
0.9417
|
0.0128
|
0.6950
|
0.5390
|
0.1015
|
0.7817
|
No.2
C.O.T. (C)
|
0.6291
|
0.2257
|
0.7848
|
0.2766
|
0.6950
|
0.1750
|
0.3050
|
0.1750
|
0.1015
|
0.7817
|
No.2
C.O.T. (S)
|
0.6291
|
0.2257
|
0.7848
|
0.2766
|
0.3050
|
0.5390
|
0.0583
|
0.0128
|
0.1015
|
0.7817
|
No.3
C.O.T. (P)
|
0.4734
|
0.1302
|
0.6291
|
0.5200
|
0.9417
|
0.0128
|
0.6950
|
0.5390
|
0.1015
|
0.7817
|
No.3
C.O.T. (C)
|
0.4734
|
0.1302
|
0.6291
|
0.5200
|
0.6950
|
0.1750
|
0.3050
|
0.1750
|
0.1015
|
0.7817
|
No.3
C.O.T. (S)
|
0.4734
|
0.1302
|
0.6291
|
0.5200
|
0.3050
|
0.5390
|
0.0583
|
0.0128
|
0.1015
|
0.7817
|
No.4
C.O.T. (P)
|
0.3177
|
0.0644
|
0.4734
|
0.7120
|
0.9417
|
0.0128
|
0.6950
|
0.5390
|
0.1015
|
0.7817
|
No.4
C.O.T. (C)
|
0.3177
|
0.0644
|
0.4734
|
0.7120
|
0.6950
|
0.1750
|
0.3050
|
0.1750
|
0.1015
|
0.7817
|
No.4
C.O.T. (S)
|
0.3177
|
0.0644
|
0.4734
|
0.7120
|
0.3050
|
0.5390
|
0.0583
|
0.0128
|
0.1015
|
0.7817
|
No.5
C.O.T. (P)
|
0.2087
|
0.0313
|
0.3177
|
0.8307
|
0.9417
|
0.0128
|
0.6950
|
0.5390
|
0.1015
|
0.7817
|
No.5
C.O.T. (C)
|
0.1619
|
0.0199
|
0.3177
|
0.8307
|
0.6950
|
0.1750
|
0.3050
|
0.1750
|
0.1015
|
0.7817
|
No.5
C.O.T. (S)
|
0.2087
|
0.0313
|
0.3177
|
0.8307
|
0.3050
|
0.5390
|
0.0583
|
0.0128
|
0.1015
|
0.7817
|
Slop
tank (P)
|
0.1619
|
0.0199
|
0.2087
|
0.8898
|
0.8630
|
0.0549
|
0.6950
|
0.5390
|
0.1015
|
0.7817
|
Slop
tank (S)
|
0.1619
|
0.0199
|
0.2087
|
0.8898
|
0.3050
|
0.5390
|
0.1370
|
0.0549
|
0.1015
|
0.7817
|
Cargo
Tank
|
PBL
|
PBV
|
PBT
|
PB
|
No.1
C.O.T. (P)
|
0.5728
|
0.4932
|
0.2183
|
0.0617
|
No.1
C.O.T. (C)
|
0.5728
|
0.6500
|
0.2183
|
0.0813
|
No.1
C.O.T. (S)
|
0.5728
|
0.4932
|
0.2183
|
0.0617
|
No.2
C.O.T. (P)
|
0.4977
|
0.4482
|
0.2183
|
0.0617
|
No.2
C.O.T. (C)
|
0.4977
|
0.6500
|
0.2183
|
0.0706
|
No.2
C.O.T. (S)
|
0.4977
|
0.4482
|
0.2183
|
0.0487
|
No.3
C.O.T. (P)
|
0.3498
|
0.4482
|
0.2183
|
0.0342
|
No.3
C.O.T. (C)
|
0.3498
|
0.6500
|
0.2183
|
0.0496
|
No.3
C.O.T. (S)
|
0.3498
|
0.4482
|
0.2183
|
0.0342
|
No.4
C.O.T. (P)
|
0.2236
|
0.4482
|
0.2183
|
0.0219
|
No.4
C.O.T. (C)
|
0.2236
|
0.6500
|
0.2183
|
0.0317
|
No.4
C.O.T. (S)
|
0.2236
|
0.4482
|
0.2183
|
0.0219
|
No.5
C.O.T. (P)
|
0.1381
|
0.4482
|
0.2183
|
0.0135
|
No.5
C.O.T. (C)
|
0.1494
|
0.6500
|
0.2183
|
0.0212
|
No.5
C.O.T. (S)
|
0.1381
|
0.4482
|
0.2183
|
0.0135
|
Slop
tank (P)
|
0.0903
|
0.4061
|
0.2183
|
0.0080
|
Slop
tank (S)
|
0.0903
|
0.4061
|
0.2183
|
0.0080
|
2.3.4 Per paragraph 7.3.2 of regulation 23, the cargo level
after damage, measured in metres above Zl, is calculated
as follows:
hc = {(ds + tc - Zl) (
ρs) - (1000 p) / g }/ ρn
Where:
ds
|
= |
the load line draught = 21.20 m |
tc
|
= |
the tidal change = 0 m and -2.5 m |
Zl
|
= |
the height of the lowest point in the cargo tank
above baseline = 3.0 m |
ρs
|
= |
density of seawater, to be taken as 1,025
kg/m3
|
p |
= |
inert gas overpressure = 5 kPa |
g |
= |
acceleration of gravity = 9.81 m/s2
|
ρn
|
= |
nominal density of cargo oil = 900
kg/m3
|
|
(2.3.4)
|
2.3.5 For the condition with the tidal change
tc equal to 0 m, the cargo level after damage hc is 20.153 m. The
remaining volume for each cargo tank after damage, in m3,
the oil outflow OB(i) are as follows:
Cargo
Tank
|
hc (m)
|
Remain
Vol. (m3)
|
OB(i) (m3)
|
No.1
C.O.T. (P)
|
20.153
|
10,558
|
3813.7
|
No.1
C.O.T. (C)
|
20.153
|
21,267
|
7623.4
|
No.1
C.O.T. (S)
|
20.153
|
10,558
|
3813.7
|
No.2
C.O.T. (P)
|
20.153
|
14,163
|
4917.6
|
No.2
C.O.T. (C)
|
20.153
|
23,427
|
8393.6
|
No.2
C.O.T. (S)
|
20.153
|
14,163
|
4917.6
|
No.3
C.O.T. (P)
|
20.153
|
14,163
|
4917.6
|
No.3
C.O.T. (C)
|
20.153
|
23,427
|
8393.6
|
No.3
C.O.T. (S)
|
20.153
|
14,163
|
4917.6
|
No.4
C.O.T. (P)
|
20.153
|
14,163
|
4917.6
|
No.4
C.O.T. (C)
|
20.153
|
23,427
|
8393.6
|
No.4
C.O.T. (S)
|
20.153
|
14,163
|
4917.6
|
No.5
C.O.T. (P)
|
20.153
|
9,342
|
3339.2
|
No.5
C.O.T. (C)
|
20.153
|
23,427
|
8393.6
|
No.5
C.O.T. (S)
|
20.153
|
9,342
|
3339.2
|
Slop
tank (P)
|
20.153
|
2,960
|
1258.9
|
Slop
tank (S)
|
20.153
|
2,960
|
1258.9
|
For the condition with tidal change tc equal
to -2.5m, the remaining volume for each cargo tank after damage, in
m3, and the oil outflow OB(i) is as follows:
Cargo
Tank
|
hc (m)
|
Remain
Vol. (m3)
|
OB(i) (m3)
|
No.1
C.O.T. (P)
|
17.307
|
8,974
|
5397.7
|
No.1
C.O.T. (C)
|
17.307
|
18,263
|
10627.4
|
No.1
C.O.T. (S)
|
17.307
|
8,974
|
5397.7
|
No.2
C.O.T. (P)
|
17.307
|
12,070
|
7010.6
|
No.2
C.O.T. (C)
|
17.307
|
20,119
|
11701.6
|
No.2
C.O.T. (S)
|
17.307
|
12,070
|
7010.6
|
No.3
C.O.T. (P)
|
17.307
|
12,070
|
7010.6
|
No.3
C.O.T. (C)
|
17.307
|
20,119
|
11701.6
|
No.3
C.O.T. (S)
|
17.307
|
12,070
|
7010.6
|
No.4
C.O.T. (P)
|
17.307
|
12,070
|
7010.6
|
No.4
C.O.T. (C)
|
17.307
|
20,119
|
11701.6
|
No.4
C.O.T. (S)
|
17.307
|
12,070
|
7010.6
|
No.5
C.O.T. (P)
|
17.307
|
7,926
|
4755.2
|
No.5
C.O.T. (C)
|
17.307
|
20,119
|
11701.6
|
No.5
C.O.T. (S)
|
17.307
|
7,926
|
4755.2
|
Slop
tank (P)
|
17.307
|
2,436
|
1782.9
|
Slop
tank (S)
|
17.307
|
2,436
|
1782.9
|
2.3.6 In accordance with paragraphs 7.1 and 7.2
of regulation 23, the mean
outflow from bottom damage is calculated as follows:
2.3.7 It is recognized that a portion of the oil
escaping from a cargo tank may be entrapped by a double bottom tank
below, thereby preventing the oil from reaching the sea. In accordance
with paragraph 7.4 of regulation
23, CDB(i) is to be taken as 0.6 when a cargo tank
is bounded from below by a non-oil compartment.
Cargo
Tank
|
CDB(i)
|
PB(i)
|
PB(i)OB(i)CDB(i)
(m3) [tc=0 m]
|
PB(i)OB(i)CDB(i)
(m3) [tc=-2.5m]
|
No.1
C.O.T. (P)
|
0.6
|
0.0617
|
141.1
|
199.7
|
No.1
C.O.T. (C)
|
0.6
|
0.0813
|
371.8
|
518.3
|
No.1
C.O.T. (S)
|
0.6
|
0.0617
|
141.1
|
199.7
|
No.2
C.O.T. (P)
|
0.6
|
0.0487
|
143.7
|
204.8
|
No.2
C.O.T. (C)
|
0.6
|
0.0706
|
355.7
|
495.9
|
No.2
C.O.T. (S)
|
0.6
|
0.0487
|
143.7
|
204.8
|
No.3
C.O.T. (P)
|
0.6
|
0.0342
|
101.0
|
144.0
|
No.3
C.O.T. (C)
|
0.6
|
0.0496
|
250.0
|
348.6
|
No.3
C.O.T. (S)
|
0.6
|
0.0342
|
101.0
|
144.0
|
No.4
C.O.T. (P)
|
0.6
|
0.0219
|
64.6
|
92.0
|
No.4
C.O.T. (C)
|
0.6
|
0.0317
|
159.8
|
222.8
|
No.4
C.O.T. (S)
|
0.6
|
0.0219
|
64.6
|
92.0
|
No.5
C.O.T. (P)
|
0.6
|
0.0135
|
27.1
|
38.5
|
No.5
C.O.T. (C)
|
0.6
|
0.0212
|
106.8
|
148.9
|
No.5
C.O.T. (S)
|
0.6
|
0.0135
|
27.1
|
38.5
|
Slop
tank (P)
|
0.6
|
0.0080
|
6.0
|
8.6
|
Slop
tank (S)
|
0.6
|
0.0080
|
6.0
|
8.6
|
ΣPB(i) OB(i)
CDB(i)
|
2,211
m3
|
3,110
m3
|
2.3.8 In accordance with paragraph 5.2 of regulation 23, mean outflow values
from the 0.0 m and -2.5 m tide conditions are combined in a 70%:30%
ratio to obtain the bottom damage mean outflow:
2.4 Mean oil outflow parameter OM
2.4.1 The non-dimensional mean oil outflow parameter
OM is calculated as follows in accordance with paragraph
5.1 of regulation 23.
2.4.2 For oil tanker of 5,000 metric tons deadweight
and above, the required mean oil outflow parameter is calculated in
accordance with paragraph 3.1 of regulation
23.
OM≤0.015
|
(for C ≤ 200,000
m3)
|
OM≤ 0.012 +
(0.003/200,000)(400,000 - C)
|
(for 200,000
m3 < C < 400,000 m3)
|
OM≤0.012
|
(for C ≥ 400,000
m3)
|
Since C is equal to 333,200 m3,
the required mean oil outflow parameter OM is as follows.
-
Required OM ≤ 0.012 + (0.003/200,000)(400,000
- 333,200) = 0.0130
Required OM, 0.0130 > actual OM, 0.0095
The vessel is therefore in compliance with the "Accidental oil
outflow performance" regulation
23.
|