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LPG Tanker 37,000, 15,0 knots, 2003, Charter Ref C3608
A. Ships characteristics
A .1. General information
Name MT
Flag Italian (International register OWNERS )
Keel laid 2002-03
Date build 2003-11
In service since 2003-12
Main class Rina 100-A-1.1-Nav IL; Cst (gas)
Class notation Liquefied gas carrier-p.max 0,3 bar- t.min. – 48°C
R.i.na
Gross tonnage : 25300 Suez Canal: 26575 Panama Canal:
Net tonnage : 9780 Suez Canal: 21784 Panama Canal: 21050
Vessel build according to: IMO gas code
USCG
RINA
A.2. Main dimensions
LOA 180,42 m
LBP 169,00m
Breadth 29,00 m
Draft, s/w/t 12,60 /12,60/12,89 m
Corresponding deadweight, summer 38427 mt
Displacement 50705 mt
Depth 17,90 m
Keel to antenna top 46,80 m
Air draft, ballast 40,30 m
Air draft, loaded 34,20 m
Parallell body length, loaded/ballast : 88,8 / 67,60 m
Immersion, loaded 45,0 mt/cm
ballast 40,5 mt/cm
A.3. Estimated draft with full cargo and full bunkers
Product Draft Deadweight Cargo capacity
Propane 9,85 m 25.938 mt 21.282 mt
Ammonia 10,49 m 28.815 mt 24.865 mt
VCM 12,54 m 38.184 mt 35.542 mt
Butane 9,97 m 26.524 mt 21.976 mt
A.4. Communication
Call sign IBFL
Radio station normally watched GMDSS
Main transmitter SAILOR HC 4500
Radiotelephony SAILOR HC 4500
VHF SAILOR RT4722 / RT4822
Satellite communication Inmarsat-B
Inmarsat-C
A.5. Machinery
Main engine Type and maker : 5 RTA 62 U SULZER
Normal service output : 9.450 kW at 110,0 rpm
Max cont rating : 11.100 kW at 130,0 rpm
Spec fuel cons : 0,175 kg/kWh at ISO(Cimac) cond
Aux engines Type and maker : 3 x SULZER 8S20 , 4-stroke, 1160 kW/ea
Spec fuel cons : 0,210 kg/kWh at ISO(Cimac) cond
Generators: 3 x Marelli M8R : 1250 kVA /each
Service speed, loaded : 15,0 knots
Service speed, ballast : 15,0 knots
:
A.7. Consumption based on normal service speed average in loaded
and ballast condition
Main Engine:
HFO, ISO 8217- RMG 35, spec energy 42.70 MJ/kg Laden = 36,0 mt/day
Ballast = 36,0 mt/day
Aux. Engines during cargo cooling:
HFO, ISO 8217, RMG 35, spec energy 42,70 MJ/kg 6,0mt/day
Aux. Engine without cargo cooling:
HFO, ISO 8217, RMG 35, spec energy 42,70 MJ/kg 3,0mt/day
Aux boiler: (only when ME stopped)
HFO, ISO 8217, RMG 35 2,5 mt/day
Inert gas generator, only during gasfreeing operation
MGO, ISO 8217, DMA 9,3 mt/day
A.8. Bunker capacity
HFO : 1619,2 cbm (100%)
MDO : 1060,4 cbm (100%)
A.9. Safe cruising range
Normal service speed, loaded condition 19.300 n.m.
A.10. Fresh water capacity
Total FW capacity, boiler feed water included 468 cbm
Fresh water production capacity 20,0 cbm/24 h
Cargo installation
B.1. Transportable products and quantities
Vol.100% Vol.98% Butane Propane Butadiene Propilene Ammonia VCM
Tk no 1 8039 7878 4735 4585 5129 4829 5373 7658
Tk no 2 9798 9602 5771 5588 6251 5886 6549 9333
Tk no 3 9856 9659 5805 5621 6288 5921 6587 9388
Tk no 4 9526 9335 5611 5433 6077 5723 6367 9074
37219 36475 21921 21228 23745 22359 24876 35453
B - 2 OTHER TRANSPORTABLE PRODUCTS ACCORDING TO IMO GAS
CERTIFICATE: Butylene, Propane/Butane mixtures
B - 3 TANKS
3.1 Working pressure : 0.300 bar
3.2 Relief valve setting, at sea/in port : 0,300/0,300 bar
3.3 Max vacuum : -0,07 bar
3.4 Max density. : 972,0 kg/cbm
2.5 Min permitted temp . : - 48 C
B.3.1 DECK TANKS ( 2 )
3.1.1 Capacity: 220 cbm LPG / 110 cbm NH3
3.1.2 Max working pressure: 18,0 bar
3.1.3 Can deck tanks be loaded direct from shore : yes
3.1.4 Can deck tanks be filled from reliquefying plant : yes
3.1.5 Can deck tanks be gasfreed using inert gas : yes
B.4. LOADING RATE TONS/HOUR
4.1 Loading rate each tank 900 cbm/h
Loading rate each manifold 2200 cbm/h
B.5. CARGO PUMPS
5.1 Type : Deepwell, 3-stage
Maker : SVANEHOJ
Number/tank : 2
Max density : 972 kg/cbm
5.2 Capacity : 350 cbm/h at 120 m
Speed : Single
5.3 Location : Inside each tank
Removable : with tank gasfree, yes
5.4 Booster pumps : Horizontal.
Maker : SVANEHOJ
Total number : 2
5.5 Capacity : 350 cbm/h at 120 m
.
5.6 Location : Main deck
5.7 Time to discharge full cargo, using all pumps against backpressure of 1 bar: abt 14 hrs
5.8 Max back pressure
Without booster pumps : 12 bar
With booster pumps : 24 bar
5.9 Remaining cargo in tanks after completion of pumping:
5.9.1 Tank no 1: 4,5 cbm
Tank no 2: 4,5 cbm
Tank no 3: 4,5 cbm
Tank no 4: 4,5 cbm
5.10 Emergency pumping system: Bulkhead valve
B.6. STRIPPING
6.1 Stripping system: No, with cargo pumps only
6.2 Time required to remove all traces of liquid cargo as stated in 5.9
LPG : abt 10 hrs
Ammonia : abt 16 hrs
B.7. CARGO COMRESSOR
7.1 Type : Piston labyrinth
Maker : Sulzer Burckhardt
Total number : 3
7.2 Are compressor pistons oil free: yes
7.3 Can they reliquefy VCM: yes
7.4 Time needed at sea to cool full cargo down to atmospheric pressure from 200 mbar:
With 3 units With 2 units
Propane 68 hrs 102 hrs
Butane 40 hrs 61 hrs
Ammonia 77 hrs 115 hrs
Ambient temp 45 deg C, sw temp +32 deg C
B.8. INERTGAS SYSTEM
8.1 Does the ship use inert gas : yes
Fuel used : Marine Diesel
8.2 Can the ship produce inert gas : yes
Composition by volume: O2 = 0.2%, CO2 = 14.0%, CO max = 1000 ppm,
SOx = 10 ppm, Balance N2, Soot index = 0
Dewpoint – 40 °C
8.3 Inert gas production capacity 96.000 cbm/24 h
8.4 Storage facility of nitrogen: No. Only nitrogen generator 100 cbm/h for filling up
of void spaces.
8.5 State if shore supply of nitrogen might be required: yes if purging with nitrogen
of cargo tanks is required prior to loading
B.9. GAS FREEING
9.1 State method used giving all details
NH3: Venting with fresh air after liquidfreeing
LPG: Purging with inert gas, when within safe limits, inert gas vented
with fresh air.
9.2 State time required for gasfreeing, including stripping.
From LPG: abt 72 hrs
From NH3: abt 120 hrs
CHANGING CARGOES
10.1 Method used and time required for changing from NH3 to LPG or from LPG to NH3, ready
to load, tanks cooled down. Time stated does not include any tank
cleaning and it is assumed that sufficient amount of coolant is stored in deck tank
for purging/cooldown purpose.
It is also assumed that 20 ppm of last cargo remains in cargo tank atmosphere
and piping system after gasfreeing from ammonia.
From NH3 to LPG
Heating, liquid freeing 45 h
Venting with fresh air 60 h
Tank inspection 10 h
Inerting 30 h
Purging /cool down with LPG 60 h
Total time required 205 h
From LPG to NH3
Liquid freeing, heating 33 h
Inerting 30 h
Venting with fresh air 10 h
Tank inspection 10 h
Purging/cool down with NH3 50 h
Total time required 133 h
10.2 Can ship reduce atmosphere in tanks and cargo installation below 100 ppm of
previous cargo: yes
10.3 Can the changing of cargo grade be done at sea: yes
10.4 How can it be checked that no liquid cargo is remaining in tanks:
Temp sensors installed in pump sumps
B.11. COOLING BEFORE LOADING:
Condensate return introduced to spraylines in cargo tanks
B.12. CARGO HEATER
12.1 Total Two
2.2 Type Horizontal, shell/tube, cargo inside of shell
12.3 Design pressure Cargo side 25.0 bar, sw side 6.0 bar
12.4 Design temp Cargo side –48 degC, sw side 0 degC
12.5 Capacity Propane 350 cbm/h from –42 degC to 0 deg C, sw = 15 °C to 9,3 °C
12.6 Total sw flow 850 cbm/h
B.13. CARGO VAPORIZER
13.1 State heating source Steam
13.2 Capacity Liquid propane from –43 C to vapour +10 C at 2 bar,
100 cbm/h
B.14. REFRIGERATING APPARATUS
14.1 Is it independent of cargo: no
14.2 Time needed at sea to lower the cargo temp of full cargo by 1 degr C from given pressure in
cargo tanks:
3 units 2 units
Butane 17 h : 25 h
Propane 28 h 42 h
Ammonia 31 h 47 h
B.15. MEASURING APPARATUS
What type of gauges :
Tank level Temp Pressure
TYPE : Float Resistance Transmitter
Local reading Yes Yes Yes
Remote in CCR Yes Yes Yes
B.16. SAMPLING
16.1 State how tank atmosphere samples can be taken and where:
Gas sampling cocks on tank domes, from 0%-50%-75%-100% levels,
On each side of tank halves.
16.2 State how liquid samples can be taken:
From sample cock on each cargo pump discharge.
16.3 Sample connection: ½” BSP
16.4 Are sample bottles available onboard: Yes
B.17. CARGO LINES
17.1 Is the ship fitted with a port and stbd cargo manifold: yes, according to recommendation by
OCIMF
17.2 Position of manifolds
Distance from bow to centre of manifolds: 92,41 m
Distance from stern to centre of manifolds 88,05 m
Height above deck 1,93 m
Distance between each manifold 2,00 m
Height above waterline, light ship 13,33 m
Height above waterline, loaded 7,23 m
Distance from ship’s rail 3,60
17.3 LIQUID LINE
Total number 2
Nominal diameter 12 inch (300 mm)
Flange size 12’’ ANSI 300
VAPOUR LINE
Total number 2
Nominal diameter 10 inch (250 mm)
Flange size 10’’ ANSI 300
17.4 Certified reducers onboard
10”(300)/12”(300) - 10”(300)/8”(300) - 10”(300)/6”(300) - 10”(300)/12”(150)-
10”(300)/10”(150) - 10”(300)/8”(150) - 10”(300)/6”(150) - 12”(300)/16”(300)-
12”(300)/8”(300) - 12”(300)/6”(300) - 12”(300)/16”(150) - 12”(300)/12”(150)-
12”(300)/10”(150) - 12”(300)/8”(150) - 12”(300)/6”(150)
Is ship fitted with stern discharge: No
Are certified hoses onboard for cargo transfer: No
19. HOSE HANDLING CRANE
19.1 Where situated: Midship, centre, frame 91
19.2 Capacity: 5 ton-speed 10 m/min
19.3 Outreach from ships side: 12,00 m
20.0 SPECIAL FACILITIES
20.1 How many grades can be segregated 2
20.2 How many grades can be cooled 2
20.3 Can vessel sail with slack tanks: yes
Inspection can be arranged
Price Please contact us
Ref C3608
Regards Keith
UK office 0044(0)1342 459089
Mobile 0044(0) 7885775317
www.Yachts-Global.com
broker@yachts-global.com
commercial@yachts-global.com
Skype yachtsglobal
Year: 2003
Vessel Location: East of India
Hull Type: Double hull
Telephone: 0044(0)1342 459089
Mobile: 0044(0)7885775317
E-mail Seller: Click here
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