VGLC Gas Tanker 54,490Dwt, Double hull, 2006, Charter, Ref C3601

March 31, 2006/ MITSUBISHI Heavy Industry, Nagasaki, Japan

Classification Society: Lloyd's Register (IACS)

54490, dwt on 11.628 m summer draft

GRT: 48772/ LOA: 230 M/ BREADTH: 36 M

M/E: Kawasaki MAN B&W 7S60MC

Aux engines: 3 x 970Kw, STX MAN B&W L23/30H –720rpm

GRT/ NRT

International 48,772 / 14,631
Suez 51,213.48 / 45,143.12

HULL
Metres
LOA 230 mtrs
LBP 219.0 mtrs
Breadth 36.6 mtrs
Depth 21.66 mtrs
Keel to highest point 51.08 mtrs / 47.10 mtrs ( in collapsed mast condition)
Max summer draft 11.628m Corresponding deadweight 54,490 mt
TPC fully loaded 71.3mt
Mean draft with 95% full bunkers and full cargo
Specific Gravity Mean draft Corresponding DW
0.580 11.15 51,239 mt
0.610 11.49 53,687 mt

Main Engine
Kawasaki MAN B&W 7S60MC
Max Cont. 13700kW – 18372BHP
Grade fuel used HFO 380 centistroke
Auxiliaries
Diesel 3 x 970kW
Make STX MAN B&W L23/30H – 720rpm
kW/RPM 970kW at 720rpm
Grade fuel used HFO 380 centistroke
Speed/Consumption*
Guaranteed average loaded/ballast speed over 12 months
Average consumption on Main Engine guaranteed speed
Average consumption on auxiliaries
*) Above based on 50/50 propane/butane and max force 5 Beaufort
Slow speed/consumption figures as guidance only
Average loaded/ballast Consumption

Average consumption in port
Inert gas plant when operating
Boiler consumption
Permanent bunkers capacity (95% full)
(Excl. daily service and settling tanks)
HFO 2,935 m3 2,850 mt
LSMGO 256 m3 217 mt

CARGO INSTALLATION
Transportable products and respective quantities
Tank
No. 100 %
m
3
98 %
m
3
Butane
0.610
-5
oC
mt
Propane
0.580
-46
oC
mt
NH3
0.680
-32oC
MT
Butadiene
0.651
-5
oC
MT
Naphtha
0.703
30oC
MT
Naphtha
0.676
30oC
MT
1 19,049.34 18,668.35 11,388 10,828 N/A N/A N/A N/A
2 21629.90 21,197.30 12,930 12,294 N/A N/A N/A N/A
3 21,632.87 21,200.21 12,932 12,296 N/A N/A N/A N/A
4 20,957.89 20,538.73 12,528 11,912 N/A N/A N/A N/A
Total 83,269.99 81,604.59 49,778 47,330 N/A N/A N/A N/A
Deck tank capacity 361.6 m3 / 18 barg / -50°C / 590 kg/m3
Transportable products and respective quantities
Other transportable products:
Pure Propane, Commercial Propane, Commercial Butane,
Mixture of Propane and Butane in any proportion
Scantlings of the cargo tanks are based on a maximum density of cargo of 610kg/m3
. Cargo with density
up to 1,000 kg/m3 may be carried in the cargo tanks on the following conditions:
For density of 1,000 kg/m3 N/A
For densities between 610 and 1,000
kg/m3
98.5% by volume for cargo density of 610 kg/m3


Tank working pressure
Maximum pressure 28 kpa
Minimum pressure -2 kpa
Minimum temperature acceptable in tanks -50 oC
Loading rate - tons/hour 4,400 m3/hr ( approximately 2500 mt/hr)
2.5 CARGO PUMPS
Number and type 8 x 550 m3/hr Ebara submerged type
Location 2 on each cargo tank
Max permissible specific gravity 610 kg/m3
Time for discharging full cargo using all pumps
against no backpressure 20 hrs
Cargo remaining onboard in cargo tanks after
completion pumping About 40 m3 unpumpable liquid (in each cargo tanks)
Total head when working in series with booster
pump 247 mLC
Booster pumps 2 x 300 m3/h Hamworthy NMB 150c, 147.7 mLC,580 KG

Number and type 5 x Opposed, single row, 2 cylinder, 2 satge
Propane Ammonia
Refrigeration Capacity 5 x 189,000 kcal/h (3.1 % Ethane) N/A
Suction pressure 20KPaG at -18°C N/A
2.7 INERT GAS SYSTEM
Does the vessel use inert gas? Yes
Utilization Inerting of Void spaces and Cargo tanks
Does the vessel produce inert gas? Yes
Type Gin 3000 – 0.3 BUFD
Daily production 3000 Nm3/hr
Composition of inert gas
Carbon dioxide 13.0 %
Oxygen max. 1.0 %
Carbon monoxide max. 1000 ppm by volume
Hydrogen max. Nil
Nitrogen Balance
Soot 0 ( on Bacharach scale)
Sulphur oxides max. 10 ppm by volume
Dew point -25oC after expansion to atmos.press

State if any shore supply of liquid nitrogen may be required No
What quantity? N/A
2.8 GAS FREEING
Can this operation be carried out at sea? Yes
State method incl. all details
For LPG Boil Off 48/54 hrs C3/C4
Inerting 48 hrs
Ventilating for Entry 48 hrs
For NH3 N/A
Advise time required and consumption of inert gas if any
From LPG approximately 30 hrs / 144,000 m3
From NH3 approximately N/A
Is the vessel equipped with inert gas blower? Yes
Capacity 4043 m3/hr at 620mbar
Ventilation fan No

Can this operation be carried out at sea? NH3 - N/A
State method used and time required for changing from NH3 to LPG and vice versa, to reach 50 ppm of
previous cargo in tanks atmosphere, the tanks being dry and free of moisture (dewpoint plus 10 degrees
C)
From NH3 to LPG N/A
Time required N/A
From LPG to NH3 N/A
Time required N/A
Can vessel reduce in tank atmosphere and gas
installation concentration of previous cargo below
50 ppm?
N/A
Method used, time required and extra shore supply
if any N/A
How can it be checked that no liquid gas remain
onboard N/A
2.10 CARGO HEATER
State discharging rate for propane with 2.5 mol % ethane to be brought from -42
oC to
0
oC at sea temperature of 15 oC 600 m3/hr
2.11 CARGO VAPORIZER
In case of need of vapour gas during discharge, can vessel produce its own if no shore
gas available? Yes

REFRIGERATING APPARATUS
Is it independent of cargo? N/A
2.13 MEASURING APPARATUS
What gauges onboard Radar gauges
Location and type 2 for each cargo tank
AutroCARGO 2000 LPG
Number of temperature sensors/gauges pr tank 8 ( 2 top, 2 middle, 2 lower, 2 sump )
Number of pressure sensors/gauges pr tank 1 in each tank

CARGO LINES
(See also last page of this gas form C)
Is vessel fitted with midship manifolds Yes
Distance from cargo manifold to bow 114.425 mtrs
Distance from manifold to stern 115.525 mtrs
Height cargo manifold above main deck 1.620 mtrs
Height cargo manifold above waterline when in ballast 15.970 mtrs
Height cargo manifold above waterline when loaded 11.692 mtrs
Distance from shipside to manifold flange 4.000 mtrs
Distance between loading and vapour return connections 2.500 mtrs
Windage area in normal ballast condition 3,960.0 m2
Is vessel fitted with SPM chainstopper suitable for 76 mm chain. Yes
Is vessel fitted with cruziform bollards/fairleads/eye-pads in manifold area Yes
Dimension of lines
Diameter Flange size
Liquid 400 mm / 16 inch ASA 150
Gas Line 250 mm / 10 inch ASA 150
Booster Line 250 mm / 10 inch ASA 300
What reducers onboard
Number Diameter Length Pressure rating
4 Pcs 16”– 16” 50 cm 150 ASA –150 ASA
2 Pcs 16” – 12” 50 cm 150 ASA –150 ASA
2 Pcs 16” – 12” 50 cm 150 ASA – 300 ASA
2 Pcs 16– 10” 50 cm 150 ASA –150 ASA
2 Pcs 16”– 8” 50 cm 150 ASA –150 ASA
2 Pcs 12”– 10” 50 cm 150 ASA –150 ASA
1 Pc 12”– 8” 50 cm 150 ASA –150 ASA
2 Pcs 12”– 12” 50 cm 300 ASA –150 ASA
1 Pc 12”– 10” 50 cm 300 ASA –300 ASA
4 Pcs 10”– 10” 50 cm 150 ASA –150 ASA
3 Pcs 10”– 8” 50 cm 150 ASA –150 ASA
2 Pcs 10”– 6” 50 cm 150 ASA –150 ASA
2 Pcs 10”– 10” 50 cm 300 ASA –150 ASA
2 Pcs 10– 10” 50 cm 300 ASA –300 ASA
1 Pc 10”– 8” 50 cm 300 ASA –300 ASA
2 Pcs 10– 6” 50 cm 300 ASA –300 ASA
1 Pc 8”– 6” 50 cm 150 ASA –150 ASA
2 Pcs 8– 8” 50 cm 300 ASA –150 ASA
2 Pcs 16”– 10” 50 cm 150 ASA –300 ASA

LIFTING DEVICE
Where situated Aft Amidship
Number and type 2 1
Lifting capacity 1 x 5 tons and 1 x 2 tons 5 tons
Max. distance from ship's side
of lifting hook
Port 3.1 mtrs
Stb. 3.5 mtrs
3.0 mtrs
2.17 SPECIAL FACILITIES
How many grades can vessel segregate? 2
Indicate systems Separate lines
Is vessel able to load/discharge two or
more grades simultaneously? Two
Can vessel sail with slack tanks? Yes
Is vessel fitted with purge tank? No

Inspection can be arranged
LOCATION Singapore
Ref C3601

Regards Keith
UK office 0044(0)1342 459089
Mobile 0044(0)7885775317
www.Yachts-Global.com
commercial@yachts-global.com
Skype yachtsglobal

Year: 2006
Vessel Location: Asia
Telephone: 0044(0)1342 459089
Mobile: 0044(0)7885775317
E-mail Seller: Click here