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LPG, 35.232 cbm LPG/NH3 , Loa 173, 70m, Carrier, 2010, Ref C3605
[LPG, 35.232 cbm LPG/NH3 , Loa 173, 70m, Carrier]
Usd 35,000
Charter price per day
Please contact us, Charter, Ref C3605
  

LPG, 35.232 cbm LPG/NH3 , Loa 173, 70m, Carrier, 2010, Ref C3605

GENERAL INFORMATION

Flag GERMANY
Port of Registry LEER

Class Lloyds Register
Builders Hyundai Mipo Dockyard Co. Ltd, Ulsan - South Korea
Delivery 18 October 2010


Length o.a. 173,70 m Draft SW on SFB 10,42 m
Length b.p. 165,00 m Draft FW 10,64 m
Breadth overall hull 28,04 m Max draft full cargo NH3 (dens. 0,68) 10,50 m
Depth moulded 17,80 m Max draft full cargo LPG (dens. 0,58) 9,85 m (100% cons.)
Distance Keel-Antenna 48,41 m Max draft ballast cond. (AP) 7,85 m (100% cons.)
Antenna folded n/a m Normal draft ballast cond. (AP) 6,85 m
TPC on summer draft 41,51 mts/cm
International Gross 22.977 Light ship 10.463 mts
Net 6.893 Max DWT (SFB) 26.645 mts
Suez Gross 24.433,18
Net 20.572,49
Panama Gross Draft calculation: 90pct bunkers / FW optimized / full stores /

PROPULSION AND MACHINERY
Main Engine HYUNDAI-MAN 6S50MC-C7 (MCR : 9,480 kW x 127 RPM)
Auxiliary engines HYUNDAI-MAN 7L23/30H (960kW, 2Sets), 6L23/30H (780kW, 1Set)
Shaft Generator N/A
Bow Thruster No KW
Propeller Type: Keyless, Four(4) blades, Dia. 5,800mm FPP

HFO 27 mts/day
AUX HFO 3,5 mts/day
at sea economical speed ME HFO TBA mts/day
AUX HFO 3,5 mts/day
at sea service speed - ME HFO 27 mts/day
while cooling cargo AUX HFO 8 mts/day
at sea economical speed ME HFO TBA mts/day
while cooling cargo AUX HFO 8 mts/day
in port loading AUX HFO 6 mts/day
Boiler 2,5 mts/day
in port loading - while cooling cargo AUX HFO 6 mts/day
Boiler 2,5 mts/day
in port discharging - 6 DWL pumps AUX HFO 8 mts/day
Boiler 2,5 mts/day
in port idle AUX HFO 3,5 mts/day
Boiler 2,5 mts/day
Boiler for evaporator water production, if required Evaporator - mts/day
Boiler for heating up cargo, if required Cargoheater - mts/day
Incenerator for burning sludge, if required Incenerator 0,2 mts/day
Fuel Grade: IFO 380cst MGO: Auxiliaries to run on MGO where compulsory
"GasChem Bremen" 35.232 cbm LPG/NH3 Carrier
S

Fuels to be used, to be in line with IMO requirements
1) THIS TABLE IS PREPARED FOR PREDICTION OF APPROXIMATE FUEL OIL COMSUMPTION AND THESE VALUES SHOULD BE USED
FOR REFERENCE DATA ONLY, DIFFERING FROM ACTUAL VALUES OF SHIP OPERATIONAL CONDITION UNDER VARIABLE CIRCUMSTANCE.
2) S.F.O.C. OF H.F.O. IS CONVERTED BY : S.F.O.C. (M.D.O.) X 10,200 / 9,700
3) S.F.O.C. FOR M/E, D/G & COMPOSITE BOILER IS BASED ON DESIGN VALUES FROM EACH MAKER.
4) S.F.O.C. OF H.F.O. IS CONVERTED BY : S.F.O.C. (M.D.O.) X 10,200 / 9,700
5) S.F.O.C. FOR M/E, D/G & COMPOSITE BOILER IS BASED ON DESIGN VALUES FROM EACH MAKER.


TANKS & CAPACITIES
Bunker HFO 1.591 cbm
MDO 131 cbm
Location of Bunker Flange Manifold area (IFO - FWD and AFT / MGO - AFT from Cargo Manifold)
Ballast water 11.392 cbm
Pumping capacity 2 x 500 cbm/hr
Filling time 11,5 hours
Discharge time 11,5 hours
Fresh water 298 cbm
Fresh water generator 20 mts/day


PRODUCTS
Propane (Pure)
Anhydrous Ammonia Propylene
1,3 - Butadiene Commercial Propane (maximum 2.5 mole% Ethane in Liquid Phase)
Butane (i, n) Vinyl Chioride Monomer (reduced filling limits)
Butylenes Propane and Butane mixtures


CARGO HANDLING EQUIPMENT
Cargo tanks Type IMO Independent Type A (prismatic)
No. 100% 98% Material Fine grain, fully killed low temp. carbon manganese steel
1 9.770,97 9.575,55 Max. tank pressure:
2 14.767,38 14.472,04 IMO 0,25 bar (g)
3 10.694,11 10.480,23 USCG 0,25 bar (g)
DTK (P) 100,05 98,05 fully ref 0,45 bar (g) (Harbour Setting)
DTK (S) 241,16 236,34 vaccum 0,95 bar (a) (5% vacuum)
35.573,68 34.862,21 min. temp. -50 degC
max. density 700 kg/m³ (98% Full)
max. density 970 kg/m³ (reduced filling limit 70% Full)

Segregation Transport grade 2
Discharge grade 2
Reliquefaction grade 2
Sequences
System 1 1 1+2 1+3 1+2+3 -
System 2 2+3 3 2 - 1+2+3

Deck tank Type IMO type C Cylindrical
Material low temp. carbon, manganese steel
Capacity 1 100 cbm D.TK. (P)
Capacity 2 240 cbm C.TK. 3 (P) C.TK. 2 (P) C.TK. 1 (P) Foreship
Max. press. 18,2 bar (g) for (C3+NH3) C.TK. 3 (S) C.TK. 2 (S) C.TK. 1 (S)
Max. press. 6,7 bar (g) for (C4+VCM)
min. temp. -50 °C D.TK. (S)
max. density 700 kg/m³ (98% Full) 18,20 bar(g)
max. density 970 kg/m³ 6,70 bar(g)
Cargo pumps
Type Deepwell Booster
Maker Hamworthy Hamworthy
Number 6 2
Capacity 400 400 cbm/hr
Disch. head 120 120 m.l.c.
Max. density 700 700 kg/m³ (98% Full)
Max. density 970 970 kg/m³
Loading From fully refrigerated storage From semi.-ref. storage cargo
t= +20°C / IMO & USCG setting
without with without with
TE/hr TE/hr TE/hr TE/hr
Ammonia 1.550 2.864 - -
Butane 1.651 2.529 87 87
Propylene 737 2.559 12 12
Propane 777 2.430 13 13
BTD 1.736 2.732 74 74
VCM 2.289 4.084 71 71
Volume
Arrangement of Cargo / Deck Tanks

Discharging
capacity 2.400 cbm/hr Using all depwell pumps and both manifolds
Cargo Compressor
Cargo Commercial Propane (2.5 mole% Ethane) Motor Rating. 270 kW
Number 3 power abs. 220 kW
Booster 0
Cargo Heating Direct Cargo
Number 1
System
Type shell and tube
Heating seawater
Sea water 15°C
Capacity Ammonia 330 cbm/hr
Propane 400 cbm/hr
Propylene -
Min. working temperature -42.8°C
The cargo heaters may also serve as cargo vaporizer with a capacity of approx. 3500 Nm³/h
Cargo vapourizer Number 1 (combined use with heater as above)
Type
Heating medium 50 / 50 Freshwater / Glycol
Capacity 3.500 Nm³/h vapour production

Hose Handling Number 1
SWL 5 mts
Outreach 22 mts ( approx. 8 m outboards )
Measuring Level Henri system Float type level gauge 807
Temperature inside ABB Automation Products
Temperature tank wall
Pressure ABB Automation Products
Samples
Liq. Samples Cargo Tanks - Top, Middle, Bottom
Deck Tanks - Top, Bottom
Deepwell Pumps - Discharge lines


CHANGE GRADE EQUIPMENT
Type Fuel Oil Combustion
Inert Gas capacity 3.000 Nm³/h at 0.5 % Oxygen (Dewpoint -40° inert Gas)
Inert Gas capacity 3.000 ~Nm³/h at 1.0 % Oxygen
Inert Gas capacity - m³/h at 2.0 % Oxygen
Discharge pressure 0,4 bar(g)
Dry air capacity 3.000 m³/h (Dewpoint -20°)
Blower Capacity 10.000 Nm³/h at 120 mbar
Dewpoint - °C
Padding N/A
Decktank Capacity (P) (100%) 100,051 m³
Capacity (S) (100%) 241,161 m³
max. press. 18,2 bar (g)
max. density 0,97 kg/dm³
suitable for same as cargo tank

MANIFOLD POSITION
Number of liquid lines 2
Number of vapour lines 2
Flanges liquid lines L1 - 30bar (300#) 12" Raised Face
L2 - 30bar (300#) 12" Raised Face
Flanges vapour lines V1 - 18.6bar (150#) 8" Raised Face
V2 - 18.6bar (150#) 8" Raised Face

Reducers on board (ASA):
Reducer Number of sets
12" #300 X 16" #300 2
12" #300 X 12" #300 2
12" #300 X 10" #300 2
12" #300 X 8" #300 2
12" #300 X 6" #300 2
12" #300 X 16" #150 2
12" #300 X 12" #150 2
12" #300 X 10" #150 2
12" #300 X 8" #150 2
12" #300 X 6" #150 2
8" #150 X 10" #150 2
8" #150 X 6" #150 2
8" #150 X 4" #150 2

CARGO CAPACITIES
Tank capacities
Tank Cap. Cap.
No. 100% 98%
1 (P&S) 9.770,97 9.575,55
2 (P&S) 14.767,38 14.472,04
3 (P&S) 10.694,11 10.480,23
all intakes calculated on 98% tankfilling
(cbm) 35.232,47 34.527,82 shrinkage not corrected / drafts at full bunkers
all details "abt:" any may differ between ships of same class.
Ammonia Propane Butane
Tank No. -33,5 Tank No. -42,1 Tank No. -0,5
s.g. 0,6800 s.g. 0,5820 s.g. 0,6007
1 6.511 1 5.573 1 5.752
2 9.841 2 8.423 2 8.693
3 7.127 3 6.099 3 6.295
(mts) 23.479 (mts) 20.095 (mts) 20.741
DFTs F/A in Mtrs: 10.00/10.50 DFTs F/A in Mtrs: 9.30/9.80 DFTs F/A in Mtrs: 9.45/9.95
Propylene Butadiene Crude C4
Tank No. -47,3 Tank No. -4,5 Tank No. -5
s.g. 0,6100 s.g. 0,6500 s.g. 0,6323
1 5.841 1 6.224 1 6.055
2 8.828 2 9.407 2 9.151
3 6.393 3 6.812 3 6.627
(mts) 21.062 (mts) 22.443 (mts) 21.832
DFTs F/A in Mtrs: 9.50/10.00 DFTs F/A in Mtrs: 9.80/10.30 DFTs F/A in Mtrs: 9.70/10.20
VCM
Tank No. -13,9
s.g. 0,9700
1 6.634
2 10.027
3 7.261
(mts) 23.923
DFTs F/A in Mtrs: 10.10/10.60

Inspection can be arranged
Ref C3605
Charter Rate 35k Usd Perday

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

Year: 2010
Telephone: 0044(0)1342 459089
Mobile: 0044(0)7885775317
E-mail Seller: Click here

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