Grand Elena LNGC Machinery System Operation Manual
Transcript of Grand Elena LNGC Machinery System Operation Manual
L
N
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GRAND ELENA AND GRAND ARIVA Machinery System Operation Manual
PROVISIONAL
ISSUESD FEB. 20, 2007
IntroductionGeneral Although the ship is supplied with shipbuilder's plans and manufacturers instruction books, there is no single handbook which gives guidance on operating complete systems as installed on board, as distinct from individual items of machinery. The purpose of this manual is to fill some of the gaps and to provide the ships officers with additional information not otherwise available on board. It is intended to be used in conjunction with the other plans and instruction books already on board and in no way replaces or supersedes them. Information pertinent to the operation of the vessel has been carefully collated in relation to the systems of the vessel and is presented in two on board volumes consisting of CARGO OPERATING MANUAL and MACHINERY OPERATING MANUAL. The Cargo Operating Manual and the Machinery Operating Manual are designed to complement MARPOL 73/78, ISGOTT and Company Regulations. The vessel is constructed to comply with MARPOL 73/78. These regulations can be found in the Consolidated Edition, 1991 and in the Amendments dated 1992, 1994 and 1995. Officers should familiarise themselves with the contents of the International Convention for the Prevention of Pollution from Ships. Particular attention is drawn to Appendix IV of MARPOL 73/78, the form of Ballast Record Book. It is essential that a record of relevant ballast operations are kept in the Ballast Record Book and duly signed by the officer in charge. In many cases the best operating practice can only be learned by experience. If any information in these manuals is believed to be inaccurate or incomplete, the officer must use his professional judgment and other information available on board to proceed. Any such errors or omissions or modifications to the ships installations, set points, equipment or approved deviation from published operating procedures, must be reported immediately to Technical Operations Office. Safe Operation The safety of the ship depends on the care and attention of all on board. Most safety precautions are a matter of common sense and good housekeeping and are detailed in the various manuals available on board. However, records show that even experienced operators sometimes neglect safety precautions through over-familiarity and the following basic rules must be remembered at all times. 1. Never continue to operate any machine or equipment which appears to be potentially unsafe or dangerous and always report such a condition immediately. 2. Make a point of testing all safety equipment and devices regularly. Always test safety trips before starting any equipment. 3. Never ignore any unusual or suspicious circumstances, no matter how trivial. Small symptoms often appear before a major failure occurs. 4. Never underestimate the fire hazard of petroleum products, especially fuel oil vapour. 5. Never start a machine remotely from the control room without checking visually if the machine is able to operate satisfactorily. Auto standby machinery should be checked by observation during duty rounds. In the design of equipment and machinery, devices are included to ensure that, as far as possible, in the event of a fault occurring, whether on the part of the equipment or the operator, the equipment concerned will cease to function without danger to personnel or damage to the machine. If these safety devices are neglected, the operation of any machine is potentially dangerous. Description The concept of this Machinery Operating Manual is to provide information to technically competent ships officers, unfamiliar to the vessel, in a form that is readily comprehensible and thereby aiding their understanding and knowledge of the specific vessel. Special attention is drawn to emergency procedures and fire fighting systems. The manual consists of a number of parts and sections which describe the systems and equipment fitted and their method of operation related to a schematic diagram where applicable. . Illustrations All illustrations are referred to in the text and are located either in the text when sufficiently small or below the text on a separate page, so that both the text and illustration are accessible when the manual is laid face up. Where texts are shown with a blue colour in the manual, they can be jumped to linked page or space by clicking them. Symbols given in the manual adhere to international standards and keys to the symbols used throughout the manual are given on the symbols pages.
Notices The following notices occur throughout this manual :WARNING
Warnings are given to draw readers attention to operations where DANGER TO LIFE OR LIMB MAY OCCUR.CAUTION
Cautions are given to draw readers attention to operations where DAMAGE TO EQUIPMENT MAY OCCUR. (Note : Notes are given to draw readers attention to points of interest or to supply supplementary information.)
.
Index - Machinery System Operation ManualPART 1 : GENERAL1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.5a 1.5b 1.5c 1.5d 1.5e 1.5 f 1.5g General Arrangement Tank Capacity Table Principal Particulars of Hull Principal Particulars of Machinery Machinery Arrangement Glossary of Symbols Ship Speed Power Curve Machinery Arrangement Machinery Arrangement Machinery Arrangement Machinery Arrangement Machinery Arrangement Machinery Arrangement Machinery Arrangement - Tank Top Plan - 4th Deck Plan - 3rd Deck Plan - 2nd Deck Plan - Engine Casing Deck Plan - Engine Casing Deck Plan - Elevation Plan
3.1
Steam Systems3.1.1 3.1.2 3.1.3 3.1.4 3.1.5 3.1.6 3.1.1a 3.1.2a 3.1.3a 3.1.4a 3.1.5a 3.1.6a Superheated Steam System 6.0 MPa Desuperheated Steam System Auxiliary Steam System N/A 1.0 MPa Desuperheated Steam System Exhaust and Dump Steam System Superheated Steam System 6.0 MPa Desuperheated Steam System Auxiliary Steam System N/A 1.0 MPa Desuperheated Steam System Exhaust and Dump Steam System
3.6
Fuel Oil and Fuel Gas Service Systems3.6.1 3.6.2 3.6.3 3.6.4 3.6.5 3.6.6 3.6.7 3.6.1a 3.6.1b 3.6.2a 3.6.3a 3.6.4a 3.6.4b 3.6.5a 3.6.6a 3.6.7a Fuel Oil Bunkering System Heavy Fuel Oil Transfer System Diesel Oil and Gas Oil Transfer System Boiler Fuel Oil Service System Boiler Fuel Gas Service System Boil-off Gas System in Cargo Machinery Room Diesel Oil and Gas Oil Service System Fuel Oil Viscosity - Temperature Graph Fuel Oil Bunkering System Heavy Fuel Oil Transfer System Diesel Oil and Gas Oil Transfer System No.1 Boiler Fuel Oil Service System No.2 Boiler Fuel Oil Service System Boiler Fuel Gas Service System Boil Off Gas System in Cargo Machinery Room Diesel Oil and Gas Oil Service System
Illustrations
Illustrations
Illustrations
3.2
Condensate and Feed Water Systems3.2.1 3.2.2 3.2.3 3.2.4 3.2.5 3.2.6 3.2.1a 3.2.1b 3.2.2a 3.2.3a 3.2.4a 3.2.5a 3.2.6a Condensate Water System Boiler Feed Water System Boiler Water Sampling and Treatment System N/A Clean Drains System Contaminated Drains System Condensate Water System Deaerator Boiler Feed Water System Boiler Water Sampling and Treatment System N/A Clean Drains System Contaminated Drains System
PART 2: MACHINERY COMMISSIONING OPERATIONAL OVERVIEW2.1 2.2 2.3 2.4 2.5 2.6 2.7 To Bring Vessel into Live Condition To Prepare Main Plant for Operation (Raising Steam) To Prepare Main Plant for Manoeuvring from In Port Condition To Change Main Plant from Manoeuvring to Normal Conditions To Change Main Plant from Normal to Manoeuvring Conditions To Secure Plant at Finished with Engines To Secure Plant for Dry Dock
3.7
Lubricating Oil Systems3.7.1 3.7.2 3.7.3 3.7.4 3.7.1a 3.7.2a 3.7.3a 3.7.4a Main Turbine Lubricating Oil System Lubricating Oil Purification System Lubricating Oil Filling and Transfer System Stern Tube Lubricating Oil System Main Turbine Lubricating Oil System Lubricating Oil Purification System Lubricating Oil Filling and Transfer System Stern Tube Lubricating Oil System
Illustrations
Illustrations
PART 3: SHIPS SYSTEMS3.0 Heat Balance for Steam Turbine Plant Illustrations3.0.1 3.0.2 3.0.3 3.0.4 3.0.5 3.0.6 3.0.7 3.0.8 3.0.9 3.0.10 3.0.11 3.0.12 3.0.13 3.0.14 100% MCR On Fuel Oil Burning (FOC Guarantee Condition) 100% MCR On Fuel Oil Burning 100% MCR On Dual Fuel Burning 100% MCR On Gas Fuel Burning Cargo Unloading Full Dump by Main Condenser Cargo Loading Full Dump by Auxiliary Condenser Hotel Load 100% MCR On Fuel Oil Burning 90% MCR On Fuel Oil Burning Half Ahead On Fuel Oil Burning Slow Ahead On Fuel Oil Burning Hotel Load
3.8 3.3 Compressed Air Systems3.3.1 3.3.2 3.3.1a 3.3.2a Compressed Air System Starting Air System Compressed Air System Starting Air System
Engine Room Bilge Systems3.8.1 3.8.2 3.8.1a Engine Room Bilge System Bilge Separator Engine Room Bilge System Domestic Fresh Water System Sewage Treatment System Domestic Fresh Water System Sewage Treatment System
Illustrations 3.9 Sanitary and Fresh Water Service Systems3.9.1 3.9.2 3.9.1a 3.9.2a
Illustrations
3.4- Winter Condition - Winter Condition - Winter Condition - Winter Condition - Winter Condition
Fresh Water Cooling Systems3.4.1 3.4.1a Central Fresh Water Cooling System Central Fresh Water Cooling System
Illustrations
Illustrations 3.5 Sea Water Systems3.5.1 3.5.2 3.5.1a 3.5.2a Sea Water Circulating System Cooling Sea Water Service System Sea Water Circulating System Cooling Sea Water Service System
Illustrations
Index - Machinery System Operation ManualPART 4: MAIN MACHINERY AND CONTROL4.1 Control Room4.1.1 4.1.1a Machinery Control Room Overview Machinery Control Room Console
PART 5: ELECTRIC POWER GENERATING SYSTEM5.1 5.2 5.3 5.45.4.1 5.4.2 5.4.3 5.4.4 5.4.5 5.4.6 5.4.7
PART 7: ENGINE ROOM BALLAST SYSTEM7.1 7.2 7.1a 7.2a Engine Room Ballast System Ballast and Fuel Oil Valves Control System Engine Room Ballast System Ballast and Fuel Oil Valves Control System
Illustrations
Turbo Generator Diesel Generator Emergency Diesel Generator Power Distribution SystemElectrical Equipment Main Switchboard and Generator Operation Shore Power Main Alternators Emergency Alternator Preferential Tripping and Sequential Restarting 24 Volt Battery and Uninterruptible Power Supply Turbo Generator Overview Turbo Generator Alternator Turbo Generator Steam and Exhaust Systems Turbo Generator Lubrication and Control Oil Systems Diesel Generator Alternator Diesel Generator Piping Systems Emergency Diesel Generator Overview Emergency Diesel Generator Alternator Emergency Diesel Generator Piping Systems
Illustrations
4.2
Main Turbine4.2.1 4.2.2 4.2.3 4.2.4 4.2.1a 4.2.1b 4.2.1c 4.2.2a 4.2.3a 4.2.3b Main Turbine Overview Main Turbine Operation Main Turbine Control System Main Turbine Warming-up System Main Turbine Overview Main Turbine Overview Main Turbine Gear Arrangement Main Turbine Operation Main Turbine Remote Control System Main Turbine Control System
PART 8: INTEGRATED CONTROL AND AUTOMATION SYSTEM8.1 8.2 8.3 8.1a 8.3a ICAS Overview ICAS Operator Station Operations Graphic Displays Integrated Control and Automation System Overview Machinery Part Graphic Displays
Illustrations
Illustrations5.1a 5.1b 5.1c 5.1d 5.2a 5.2b 5.3a 5.3b 5.3c 5.4a 5.4.7a
Illustrations
PART 9: EMERGENCY PROCEDURES9.1 9.2 9.3 9.4 9.5 9.6 9.3a Flooding in the Engine Room Steaming on One Boiler Solo Running of the Main Turbine Steaming with One Forced Draft Fan Emergency Steering Fire in the Engine Room Emergency Operation of Main Turbines
4.3
Main Boiler4.3.1 4.3.2 4.3.3 4.3.4 4.3.1a 4.3.2a 4.3.2b 4.3.2c 4.3.2d 4.3.3a 4.3.3b 4.3.4a 4.3.4b Main Boiler Overview Main Boiler Operation Burner Characteristics Boiler Control Systems Main Boiler Overview Main Boiler Mounting System Combination Burner System Boiler Pressure Rising Charts Combustion Air, Seal Air and Flue Gas System Burner Characteristics Burner Assembly Boiler Gauge Board Automatic Combustion Control (ACC)
Power Distribution System24 Volt Battery and Uninterruptible Power Supply
Illustrations
Illustrations
PART 6: AUXILIARY MACHINERY6.1 Main Feed Water Pump 6.2 Distilling Plant 6.3 Incinerator 6.4 Nitrogen Generator System 6.5 Inert Gas Generator System Illustrations6.1a 6.1b 6.1c 6.2a 6.3a 6.4a 6.5a Main Feed Water Pump Sectional View Main Feed Water Pump Turbine Sectional View Main Feed Water Pump Trip System Distilling Plant Systems Incinerator Nitrogen Generator System Inert Gas Generator System
Part 10: FIRE FIGHTING SYSTEMS10.1 Fire Fighting Systems 10.2 Fire Detection System 10.3 Engine Room Fire Fighting Systems 10.3.1 Engine Room Fire Main System 10.3.2 Engine Room CO2 Fire Extinguishing System 10.3.3 Engine Room Hot Foam Fire Extinguishing System 10.3.4 10.3.5 10.3.1a 10.3.2a 10.3.3a 10.3.4a 10.3.5a Engine Room Local Fire Extinguishing System Quick-Closing Valves and Fire Dampers System Engine Room Fire Main System Engine Room CO2 Fire Extinguishing System Engine Room Hot Foam Fire Extinguishing System Engine Room Local Fire Extinguishing System Quick-Closing Valves and Fire Dampers System
Illustrations
PART 1 : GENERAL
1.1 1.2 1.3 1.4 1.5 1.6 1.7
General Arrangement Tank Capacity Table Principal Particulars of Hull Principal Particulars of Machinery Machinery Arrangement Glossary of Symbols Ship Speed Power Curve
Illustrations1.5a 1.5b 1.5c 1.5d 1.5e 1.5f 1.5g Machinery Arrangement Machinery Arrangement Machinery Arrangement Machinery Arrangement Machinery Arrangement Machinery Arrangement Machinery Arrangement - Tank Top Plan - 4th Deck Plan - 3rd Deck Plan - 2nd Deck Plan - Engine Casing Deck Plan - Engine Casing Deck Plan - Elevation Plan
1.1
General Arrangement
GENERAL ARRANGEMENTABT.72,000 ABOVE B.L.COMP.BRI.DK
COMP.BRI.DECK (CENT.)
3,650NAV. BRI. DECK AN.LT.
NAV. BRI. DECK
3,650G-DECK
G-DECK
F-DECK
M.H.LT.
3,650F-DECKST.LT
3,000E-DECK
E-DECK
3,000D-DECK
D-DECK
3,000C-DECK
C-DECK
B-DECK
3,000A-DECKS.L. S.L.
NO. 4 TANK
CARGO MACHINERY ROOM
NO. 3 TANKCOMPRESSOR MOTOR ROOM
NO. 2 TANKS.L.
NO. 1 TANK
3,000B-DECK
A-DECK
4,000AN.LT. UPPER DECK
UPPER DECK (CENT.)STRAIGHT CAMBER 45/1000
UPPER DECK (SIDE)
NO.1 DIST.W.TK.(P) F.W.TK.(S) 2ND DECK(22,850)NO .2 D DR IN IST. K.W W.T .TK K (P (S ) )
(P& S)
ER O.S ER D. O.S G/E D. .1 G/E NO .2 NO
FORWARD STOREUNDER DECK PASSAGE (P & S)(22,850)ACC. TRUNK
2,400
UNDER DECK PASSAGE (P & S)(22,850)AIN
FORWARD STORE FLAT (22.850m)
2ND DK
F.O. SETT . TK
I.G.G.GAS OIL TK(P)
SULPH UR F.O .SIDE . TK(S) TK (P)
ER G. P. FIRE RM .
FOBITT BITT
R'D
EM
(P &S )
STEER. ENG. FLAT (16,550) 3RD DECK(15,650)E P.R
F.O. SID E F.O. SID TK (P) E TK (S)
W .B .T K
LOW
F.O
A.P.VOIDER
AF T
ESCAPE TRUNK
W .B .S .T K
.T
.T
.T
L.W.L.
.S
.S
.S
W .B
W .B
W .B
4TH DECK(9,470)
NO .8
NO
L.F. W.T
OO
.T.C
TANK TOP(3,800)B. W.ST. T. L.O. DRAIN TK L.O. DRAIN TK (S)
ST
TANK TOP(2,500)L.O. SUMP TK B.W.(P)GE (S) . BIL SEP OIL TK) .(S S.CA
Y BA
B.W.(P) ECHO SOUND. & MAG. LOG COMP.
SE
ECHO SOUND. COMP.B.L. B.L.
5,000
F.O.DRAIN TK (S)
N
O
.3
N
O
.2
N
O
.1
00 ,6 R2
W.B
.S.T
K
B.L.
DOUBLE BOTTOM PIPE PASSAGE10,100 24,500 9,350 5,050
1,590
LO
LO
LO
W
.B
BILGE PRIMARY SECT. (S)
W
W
W
11,230
BIL
G
.S
OLD EH
ER
ER
ER
LO
R WE
K
.T
K
. TK
W
W
NO
NO
(S)
.6 NO
.7
.B
.5
.B
.3
.T
K
.4 NO
.T
K
NO
.2
W
W
.B
.T
K
.1 NO
FO R'D (P W.B &S ) .T
W . F.O RFLO OVE
.B
K.
TK
(S)
K .T .S .B W
K .T .S .B W
.S
.T
K
K .T .S .B W
FOR'D PUMP RM
L.W.L.
L.W.L.
L.W.L.
W.B
.TK
B.L.
0A.P.
5
10
15
20
25
30
35
40
45
50
55CLEAN DRAIN TK (S)
60
65
70
75
80
85
90
95
100
105
110
115
1,600FRP 5,000 .S.1,800
FRP 00 . S. 8 6,000 15,200
FRP 900 . S. 45,000
FRP 4,700 .S.
FRP 5,300 .S. 45,000
FRP 5,000 .S.
FRP 4,700 .S.
FRP 5,300 .S.
FRP 5,000 .S. 45,000
FRP 4,700 .S.
FRP 5,300 .S. 45,300
FRP 5,000 .S.
FRP 3,200 .S. 32,000F.P.
44,700
8,000
VIEW OF BRIDGE FRONT & TANK SECTION
MAX. WORKING RADIUS ABT. 21,000
OUTREACH 4.0m FROM SHIP'S PARALLEL LINE
MAX. WORKING RADIUS ABT. 9,000
MAX. WORKING RADIUS ABT. 9,000
OUTREACH 2.0m FROM SHIP'S PARALLEL LINE MIN. WORKING RADIUS ABT. 3,000 4-R.FL. 4-R.FL. LR. (25PX2) MIN. WORKING RADIUS ABT. 4,500E N RA D.C ) AN H 1M -2
MIN. WORKING RADIUS ABT. 3,000 E.C.FL. CAPS. B. PILOT LADD.REELUP
LIFE BOAT (50P) (OV.)
5T HOSE HANDRING CRANE (SWL 49kN-22M) E.C.FL. CAPS. B. DUTY MEN RM. UP UP (TO JIB REST)DN
E.C.FL.
S.L.
E.C.FL. CAPS.
C.FL.
4-R.FL.
4-R.FL.
UPPER DECK4-R .FL . 4-R .FL . 4-R .FL .
3T
ACCOMM. LADD. STOW. SP.
L.P.NO OBSTRUCTIONS
L.P. B.
PR (SW OVISI L 29
B.E AN CR ) N -9M ISIOkN OV 29 PR WL (S
V.& O PR 5T
TS kN AR 49 .P G L EN (SW
ON kN CRAN -9M E )CAPS.3T
UP DN
DN
HYD.M.W. A.O.
UP SECURITY GUARD HOUSE
DN
SECURITY WATCH SHELTER
UP JIB REST
B.
I.G.G. RM N2 GEN. RMPOSITION HAND.CRANE STORAGE 5T PROV.& ENG.PARTSSAFTY EQUIP. STORE
C.P. FIRE STATIONSUEZ CANAL WORKER'S RM
B. B.
C.F L.
DN
L.O. & GREASE STOREV. T.
5-R .FL . 5-R .FL .
AOH.RM
V.
T.
SUEZ CANAL WORKER'S LAV.
HYD. M.W. D.S.R. HYD. M.W.
HYD.PUMP UNIT RM DNM
DN DN UP UP
DECK WORK SHOP
HOTEL LAUND.
FEMALE CHANG. RM. NO.2 CARGO SWBD. RM.OFF'S CHANG. RM. CREW'S CHANG. RM.
NO. 4 TANK
NO. 3 TANK
NO. 2 TANK
NO. 1 TANKHYD. WIND. C.C.
H.P.
DN
LINEN LKRUP
B. L.R. EMB. (6P) LADD. HYD. M.W.
M
DOME LIFT 35 40 45 HATCH 50 55 AIR COND.UNIT RM & REF.PROV.MACHI.RM & UP UP UP V.T. 60M
V.P. L.P. 75 80
DOME
V.P.L.P.
DOME
V.P.L.P.
DOME V.P. 105 D.S.R. D.S.R. 110
DN D.S.R. DAVIT 115 F.P. H. H.
DN 5 A.P. 10 15 20 25
30
65
70
85
90
95
PIPE PASSAGEE.C.T. H.
WALK WAYA.T .
D.S.R.
ELECT. CABLE PASSAGE
M.H. HYD. WIND.
UP DN DN INCINE.RM GARBAGE STR E.C.T.COMM.LAV
C.C. H.P.
H.R
PIPE PASSAGE
PIPE PASSAGEH.
PIPE PASSAGED.S.R.
WALK WAYBATH NO.1 CARGO SWBD. RM.V. T. V. T.
WALK WAY
WALK WAYUP
HYD. M.W.
ELECT. CABLE PASSAGECHEMICAL LKR PAINT STORE UP
ELECT. CABLE PASSAGE CO2 BOTT.RMC.P. MIN. WORKING RADIUS ABT.4,600
ELECT. CABLE PASSAGE
HYD. M.W. B. B.L. C.F
.FL 5-R .FL .
.
EMERG.GENE.& EMERG.SWBD.RM.
HYD.M.W.
HOSP.
DISP.
5-R
A.O. DN UP5T PR (S W O L 49 V.& EN -2 G 1M ) .P AR TS H AN D.C
SECURITY GUARD HOUSE3T
CARGO MACHI.RMDN
JIB REST UP
UP SPARE ANCHOR STOW.SPACE (TO JIB REST) UP LNG LIQUID LINE LNG LIQUID LINE DN LNG VAPOUR LINE LNG LIQUID LINE LNG LIQUID LINE UP B. CAPS. DUTY MEN RM. E.C.FL. L.P. CAPS. S.L. E.C.FL. C.FL. 4-R.FL. 4-R.FL. B.. .FL 4-R
&UP
DN
B.. .FL 4-R . .FL 4-R
PRO (SW VISION L 29k CRAN N-9 E M)
MOTOR RM (OVER)UPNO OBSTRUCTIONS
MIN. WORKING RADIUS ABT. 4,500
kN
UP LR. (25PX2)RA N E( O
UP UP B.
ACCOMM. LADD. STOW. SP. CAPS. LIFE/RESCUE BOAT (50P) (OV.) B. E.C.FL.
CAPS.
3,500
UP PILOT LADD.REEL
5-R.FL.
M.P.
T.B.
5-R.FL.
R.PL. UP
. FL C.
DECK STORE
4-R.FL. V.)
4-R.FL.
E.C.FL. OUTREACH 2.0m FROM SHIP'S PARALLEL LINE
PRINCIPAL PARTICULARSABT.288.0 m LENGTH (O.A.) 274.00 m LENGTH (B.P.) 49.00 m BREADTH (MLD) 26.80 m DEPTH (MLD) 11.25 m DRAUGHT (MLD)(DESIGNED) 12.30 m DRAUGHT (MLD)(SCANTLING) ABT. 71,200 t DEADWEIGHT (d = 11.25m) ABT. 123000 GROSS TONNAGE MHI STEAM TURBINE X 1 MAIN ENGINECAPTAN CLASS
COMPLEMENT2 P. 4 P. 5 P. 3 P. 16 P.
MAX. WORKING RADIUS ABT. 21,000
OUTREACH 4.0m
FROM SHIP'S PARALLEL LINE
TUG
MIN. WORKING RADIUS ABT. 3,000
TUGMAX. WORKING RADIUS ABT. 9,000
TUG
3,000abt. 11,800
3,000
3,000
3,000
TUG
TUG
5T HOSE HANDRING CRANE (SWL 49kN-22M)
SENIOR OFFICER CLASS JUNIOR OFFICER CLASS PETTY OFFICER CLASS RATING CREW CLASS
MAX. WORKING RADIUS ABT.22,000
PILOT(JUNIOR OFFICER CLASS)(1P x 1RM) LOADING MASTER(JUNIOR OFFICER CLASS)(1P x 1RM) OFFICER SPARE(JUNIOR OFFICER CLASS)(1P x 6RMS) CREW SPARE(CREW CLASS)(1P X 1RM)
22,850
ENGINE ROOM
F. P. VO ID
K
K
K
5,580
EM
26,800
BITT
ACC.TRUNK
G.FIR
M.
CH
STEER.GEAR ROOM
D.O.STOR.TK.(S) D.O.STRO.TK.(P)
F.O
.TK
(C
)
B.W.
LK
R
ABT. 1,075
) (S TK R. TO O.S L.
L. O.R EN OV. TK (O UT) (S )
3,950
) .(S ) TK V. TK.(S V.
UNDER DECK PASSAGE
UNDER DECK PASSAGE
HAND.CRANE 5T PROV.& ENG.PARTS
STORAGE POSITION
1 P. 1 P. 6 P. 1 P. 39 P. 6 P.
MCR 23,600 kW x 80 rpm SPEED (SERVICE SPEED) ABT.
19.5 kn
AFT MOORING DECK
2ND DECK(P)N.) (UE.T K. (P )
BOTTOM PLAN
BOTTOM PLAN
FORWARD STORE
CLASS Lloyd's Register of Shipping +100A1 Liquefied gas carrier, Ship Type 2G, Methane in independent spherical tanks type B, Maximum vapour pressure 0.25 bar G at sea Minimum cargo temperature -163C Maximum cargo density 500kg/m3 ShipRight(SDA), Ice Class 1B FS(hull), *IWS, LI, +LMC, UMS, ICC, NAV1, IBS,EP with the descriptive notes"ShipRight(FDA,CM,SCM,TCM, BWMP) Russian Maritime Register Ice Class LU2(propeller and shaft)
GRAND TOTALSUEZ CANAL WORKERS (CREW CLASS) (6P x 1RM)
CARGO TANK CAPACITYCARGO TANKS (98.5%full, -163C, atmospheric pressure,excluding dome space) NO.1 CARGO TANK NO.2 CARGO TANK NO.3 CARGO TANK NO.4 CARGO TANK TOTAL CARGO TANK CAPACITY ABT. 36,250 m3 ABT. 36,250 m3 ABT. 36,250 m3 ABT. 36,250 m3 ABT. 145,000 m3
TT .TK.
K.
.B
TK. AF T W
F.O. SE
F.
O.S
.T
ID
DN.FL. 4-R .FL. 4-R
OIL
(P )
I. G. G. RM.
D.O .S TO R.T K.
COFF
GAS
C.F
L.
UP
.S .T
C.F
L.
5-R
.FL
K(P
.
)
5-R
.FL
.
I.G.G.
UP
.7 NO
) K(P .T .S W.B
. (U N.)
NO.6
W.B
.S.T
K(P)
.5 NO
) K(P .T .S W.B
NO.4
W.B
.S.T
K(P)
.3 NO
) K(P .T .S W.B
NO.2
W.B
.S
P) .TK(
(P) S.TK W.B. NO.1M.H.
.TK
DIS T.W .TK
.W
DIST
NO .2
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LABORATORY
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DECK HEIGHTUPPER DECK A-DECK B-DECK C-DECK D-DECK E-DECK F-DECK G-DECK NAV.BRI.DECK SHEER CAMBERM.H.
ELECTRICAL & INSTR.WORK SHOPUP UP
NO.2 F.O. HEATING RM
NO. 4 TANKNO.2 SWBD.RM.
NO. 3 TANK
NO. 2 TANK
NO. 1 TANKM.H.
HYD.M.W. B.UP UP
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STORAGE DRUM UP A.P. STORAGE BOX 5 10 15 20BOG PIPE HOOD
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A-DECK B-DECK C-DECK D-DECK E-DECK F-DECK G-DECK NAV.BRI.DECK COMP.BRI.DECKNIL
4.00 m 3.00 m 3.00 m 3.00 m 3.00 m 3.00 m 3.65 m 3.65 m 3.65 m45/1000 20/1000 15/1000
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1.2
Tank Capacity TableLow Sulpher Fuel Oil Tanks (S.G. = 0.870)Center of Gravity 98.8% Full (163) Excluding Dome (m3) 36,250.000 36,250.000 36,250.000 36,250.000 145,000.000 NAME 100% Full AP G(m) 219.5 174.5 129.5 84.5 KG (m) 23.39 23.39 23.39 23.39 LOW F.O.T. SULPHER TOTAL ITEM Side C Position FR. NO. 64 - 69 100% Full (m3) 485.6 485.6 Capacity 90% Full (m3) L.F.O.(t) 437.0 437.0 380 380 Center of Gravity 100% Full AP G (m) KG (m) 57.95 17.48 MT of I (Max. F.S.) (m4) 392 392 Capacity 100% Full 100% Full 100% Full (163) (160) (163) Excluding Including Dome Including Dome Dome (m3) (m3) (m3)
Cargo Tanks (preliminary) (S.G. = 0.470)ITEM NAME Side NO.1 CARGO TANK C NO.2 CARGO TANK C NO.3 CARGO TANK C NO.4 CARGO TANK C TOTAL FR. NO. 97.39 - 105.65 88.35 - 96.69 79.39 - 87.65 70.35 - 78.69 Position
Diesel Oil Tanks (S.G. = 0.920)ITEM NAME D.O.T. D.O.T. G/E D.O. SERV. T. Side P S S TOTAL Position FR. NO. 49 54 49 54 49 54 100% Full (m3) 156.0 101.5 54.6 312.1 Capacity 90% Full (m3) D.O.(t) 140.4 129 91.4 84 *1 48.9 45 280.7 258 Center of Gravity MT of I 100% Full (Max. F.S.) AP G (m) KG (m) (m4) 44.45 24.58 392 44.45 24.54 115 44.45 24.65 15 522
Water Ballast Tanks (S.G. = 1.025)ITEM NAME Side FOR'D W.B.T. P FOR'D W.B.T. S NO.1 W.B.S.T. P NO.1 W.B.S.T. S NO.2 W.B.S.T. P NO.2 W.B.S.T. S NO.3 W.B.S.T. P NO.3 W.B.S.T. S NO.4 W.B.S.T. P NO.4 W.B.S.T. S NO.5 W.B.S.T. P NO.5 W.B.S.T. S NO.6 W.B.S.T. P NO.6 W.B.S.T. S NO.7 W.B.S.T. P NO.7 W.B.S.T. S NO.8 W.B.S.T. P NO.8 W.B.S.T. S NO.1 LOWER W.B.T. C NO.2 LOWER W.B.T. C NO.3 LOWER W.B.T. C AFT W.B.T. P AFT W.B.T. S TOTAL Position FR. NO. 106 - 110 106 - 110 100 - 106 100 - 106 94 - 100 94 - 100 91 - 94 91 - 94 85 - 91 85 - 91 82 - 85 82 - 85 76 - 82 76 - 82 73 - 76 73 - 76 69 - 73 69 - 73 96 - 98 87 - 89 78 - 80 42 - 54 42 - 54 (m3) 2,616.9 2,633.5 2,687.4 2,687.4 3,251.0 3,251.0 1,802.4 1,802.4 3,668.7 3,668.7 1,835.3 1,835.3 3,624.3 3,624.3 1,648.2 1,648.2 3,633.6 3,633.6 1,675.2 1,674.3 1,675.2 1,493.9 1,493.9 57,564.7 Capacity 100% Full S.W.(t) AP G (m) 2,682 247.80 2,699 247.77 2,755 228.77 2,755 228.77 3,332 196.42 3,332 196.42 1,847 174.46 1,847 174.46 3,760 151.99 3,760 151.99 1,881 129.50 1,881 129.50 3,715 107.11 3,715 107.11 1,689 84.67 1,689 84.67 3,724 67.38 3,724 67.38 1,717 196.99 1,716 152.00 1,717 106.99 1,,531 41.47 1,531 41.47 58,999 KG (m) 12.58 12.56 12.57 12.57 9.05 9.05 8.06 8.06 7.95 7.95 7.94 7.94 8.03 8.03 8.65 8.65 10.56 10.56 6.47 6.47 6.47 16.63 16.63 MT of I (Max. F.S.) (m4) 3,215 3,251 2,136 2,136 1,914 1,914 1,287 1,287 2,576 2,576 1,288 1,288 2,574 2,574 1,163 1,163 4,699 4,699 5,362 5,362 5,362 1,416 1,416 60,658
*189.6 % FULL (OVERFLOW LEVEL)
This section will be rectified after completion of the test.ITEM Position NAME I.G.G. GAS OIL T. Side P TOTAL FR. NO. 45 - 49 100% Full (m3) 124.8 124.8
I.G.G. Gas Oil Tank (S.G. = 0.870)
Capacity 90% Full (m3) G.O.(t) 112.3 98 112.3 98
Center of Gravity MT of I 100% Full (Max. F.S.) AP G (m) KG (m) (m4) 40.40 24.58 314 314
Fresh Water Tanks (S.G. = 1.000)Tank Side S S P P SUM ATH TOTAL
Position
NO.1 FRESH W. T. NO.2 FRESH W. T. NO.1 DIST. W.T. NO.2 DIST. W.T. ST. T.C.F.W.T.
FR. NO. 14 - 19 9 - 14 14 - 19 9 - 14 19
(m3)
10.38
204.9 164.2 204.9 164.2 738.2 57.6 795.8
Capacity 100% Full F.W. (t) AP G (m) 205 13.26 164 9.28 205 13.26 164 9.28 738 58 13.09 796
MT of I (Max. F.S.) KG (m) (m4) 19.92 229 19.99 134 19.92 229 19.99 134 726 4.67 10 736
Lubricating Oil Tanks (S.G. = 0.880)Tank L.O. STOR. T. L.O. RENOV. T. L.O. GRAVITY T. S/T L.O. SUMP T. L.O. DRAIN T. L.O. SUMP T. Side S S S C C C TOTAL Position FR. NO. 45 - 48 42 - 45 55 - 59 27 - 29 39 - 41 36 - 43 Capacity (m3) 56.1 56.1 40.4 4.8 3.9 57.4 218.7 Center of Gravity 100% Full AP G (m) KG (m) 39.95 37.25 49.40 23.30 34.10 33.80 MT of I (Max. F.S.) (m4) 24.62 24.62 17.65 3.00 3.15 2.69 47 47 7 1 1 49 152
Fuel Oil Tanks (S.G. = 0.950)ITEM NAME FORD F.O.T. F.O. SIDE T. F.O. SIDE T. NO.1 F.O. SETT. T. NO.2 F.O. SETT. T. SUM F.O. OVERFLOW T. S F.O. DRAIN T. S TOTAL Side C P S S S Position FR. NO. 106 - 110 54 - 69 54 - 69 59 - 64 54 - 59 64 - 69 64 - 66 100% Full (m3) 1,262.5 2,152.4 865.2 350.1 333.9 4,964.1 117.0 3.0 5,084.1 Capacity 90% Full (m3) F.O.(t) 1,136.3 1,079 1,937.2 1,840 778.7 740 315.1 299 300.5 285 4,467.8 4,243 105.3 100 2.7 3 4,575.8 4,346 Center of Gravity 100% Full AP G (m) KG (m) 248.63 19.25 53.60 17.75 52.40 17.73 53.45 19.28 49.04 19.03 57.97 10.80 56.60 2.00 MT of I (Max. F.S.) (m4) 3,171 1,176 651 79 79 5,156 392 1 5,549
Other TanksTank BILGE HOLD T. BILGE PRIMARY S SECTION DECK WASH T. P SEP. BILGE OIL T. S CLEAN DRAIN T. P TOTAL Side S Position FR. NO. 54 - 64 54 54 55 58 59 69 59 63 Capacity (m3) 240.9 19.2 446.2 15.1 44.6 766.0 Center of Gravity 100% Full AP G (m) KG (m) 51.86 7.48 48.95 54.27 49.40 52.78 8.62 7.44 1.25 1.07 MT of I (Max. F.S.) (m4) 528 6 1,226 1 50 1,811
1.3
Principal Particulars of Hull5. CAPACITY S.NO.2229GRAND ELENA S.NO.2230GRAND ARIVA Cargo Capacity Cargo tank including dome space (at cryogenic temperature = -163) Cargo tank excluding dome space (at cryogenic temperature = -163) Tank Capacity Water Ballast Fresh Water (excluding ST.T.C.F.W.T.) Fuel Oil (Including Low Sulphur F.O. tank, excluding F.O. Overflow tank and F.O. Drain ank) Diesel Oil I.G.G. Gas Oil 6. SPEED Trial max. Service Delivery S.NO.2229 January 15th, 2006 (preliminary) S.NO.2230 March 15th, 2006 (preliminary) p.p. : 274.00 m * : preliminary abt. 19.5 knots on the designed draught at 100% MCR of main engine with 21% sea margin 100 % 100 % 98.5 % 100 % 100 % 100 % 100 % 100 % * 147,208.122 m3 * 147,208.122 m3 * 145,000.000 m3 54,600 m3 795.8 m3 4,800 m3 370 m3 200 m3 S.NO.2229NYK-SCF LNG SHIPPING No.1 LTD S.NO.2230NYK-SCF LNG SHIPPING No.2 LTD Lloyds Register of Shipping +1A1 Liquefied Gas Carrier, Ship Type 2G, Methane in independent spherical tanks type B, Maximum vapour pressure 0.25 barG at sea Minimum cargo temperature -163 Maximum cargo density 500 kg/m3 ShipRight (SDA), Ice Class 1B FS (hull), *IWS, LI, +LMC, UMS, SCM with the descriptive notes ShipRight (FDA, CM,SERS, SCM,TCM, BWMP(S)) pt higher tensile steel, ETA Russian Maritime Register Ice Class LU2 (propeller and shaft) Port OSLO Official Number S.NO.2229 S.NO.2230 Launching S.NO.2229 February 4th, 2005 S.NO.2230 May 20th, 2005 Call Letter S.NO.2229 S.NO.2230
1. GENERAL Ships Name Owner Classification
Registration
Date
Keel Laying
S.NO.2229 August 17th, 2004 S.NO.2230 November 29th, 2004 2. PRINCIPAL DIMENSION Length Breadth Depth Design Draught Summer Draught Scantling Draught Normal Ballast Draught Heavy Ballast Draught Gross Tonnage Net Tonnage 4. DEADWEIGHT At Summer Draft o.a. mld. mld. mld. mld. mld. mld. mld. : : : : : : :
: abt.288.00 m 49.00 m 26.80 m 11.25 m 12.30 m 9.20 m 9.80 m
12.30 m
This section will be rectified after completion of the test.
3. TONNAGE (International, 1969) *abt.123,000
*abt.71,200 metric tons
1.4
Principal Particulars of Machinery1. Main TurbinePARTICULARS Type & Number DESCRIPTION Impulse, reaction, two cylinders, cross-compounded marine steam turbine with articulated type double reduction type gear Mitsubishi MS36-2 1 set MCR (=NR) : 23,600kW (32,090PS)80.0 rpm Astern Turbine: Output (Reference) abt. 8,100kw Operating conditions : For a period of 2 hours continuous running at 70 % of the max. ahead revolution (56.0 rpm) Design torque : 80 % of the max. ahead torque at 50 % of the max. ahead revolution ( 40.0 rpm) 5.88MPaG (60kg/cm2g)510 at Ahead stop valve inlet Planetary gear type : 11kW 1,800rpm 5.1kPaA (722mmHgV) at MCR (Sea water temperature=27) Main condenser : Scoop / pump cooling
Abbreviation List MCR NR S.W. F.W. L.O. F.O. D.O. G.S. K. D.P. TH M/T T/G D/G E/G IGG M.D. H. V. G. S. C. P. F.A. B.P. S. & T. D.D. T. CCS ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... ........................... Maximum Continuous Rating Normal Rating Sea Water Fresh Water Lubrication Oil Fuel Oil Diesel Oil General Service kg/cm2G Delivery Pressure Total Head Main Turbine Turbo Generator Diesel Generator Emergency Generator Inert Gas Generator Motor Driven Horizontal Vertical Gear Screw Centrifugal Piston Free Air Back Pressure Shell and Tube Type Diesel Driven Turbo Central Cooling System
Shaft Horsepower & Revolution Astern Turbine
Steam Conditions Turning Motor Vacuum Remarks
2. Main BoilerPARTICULARS Type & Number DESCRIPTION Two-drum, water tube marine boiler with dual fuel burners Mitsubishi MB-3E 2 sets 6.0MPaG (61.5kg/cm2g)515 at MCR condition : : : Maximum flow Temperature up Maximum MCR 55,000 kg/h 47,200 kg/h (at gas burning) 46,600 kg/h (at oil burning) : 38,000 kg/h limit at max. steam flow : 350
Steam Conditions at Superheater Outlet Evaporation (per each set) Internal Desuperheater Air Heater Economizer Ambient Room Temp Feed Water Temp. Fuel Oil
Steam heating type Extended surface type 50 at Forced draught fan suction 145 at Economizer inlet RMH55 as specified in ISO 8217:1996
1.4
Principal Particulars of Machinery3. ShaftingPARTICULARS Thrust Shaft Intermediate Shaft No.1 Intermediate shaft No.2 Intermediate shaft Propeller Shaft Stern Tube Stern Tube Sealing DESCRIPTION Located on aft of the main reduction gear 1 set PARTICULARS Main Turbo Turbine Generator SetNO.
5. Electric Generating Set2 TYPE 6-stage impulse, condensing turbine with single reduction CAPACITY NOTES Steam condition:: 5.88MPaG510, Exhaust condition: 6.7kPaA (710mmHgV) abt. 2,250kw at atmospheric back pressure
Mitsubishi AT42CT-Babt.600 mm abt. 5,600 mm in length abt.600 mm abt.11,800 mm in length abt.880 mm abt.11,960 mm in length Fabricated steel welded construction with oil lubricating bearing of white metal facing (WJ-2) Air seal type Generator 2 Main Diesel Generator Set Diesel 2 Generator 2 AC 6.6kV 3 phase, 60Hz, totally enclosed, brushless marine type 4,000 kVA (3,200 kW) 1,800rpm 1,690 kw 720 rpm 2,000 kVA (1,600 kW) 720 rpm 768 kW 1,800rpm 787.5 kVA (630 kW) 1,800rpm
Taiyo HPW 65B-4Four cycle single acting turbo-charged trunk piston type Yanmar 6EY26L AC 6.6kV 3 phase, 60Hz, totally enclosed, brushless marine type
Taiyo HPW 558C-10
4. PropellerPARTICULARS Type, Material & Number Diameter Pitch Area (Expanded DESCRIPTION Six (6) blades, solid wet-fit keyless type, of Nickel aluminium bronze 1 set 8,800mm 7,770mm 41.0 m2
Emergency Generator Set
Diesel
1
Four cycle radiator cooled type
STX KTA38DMGEGenerator 1 AC 450V 3 phase, 60Hz, totally enclosed, brushless marine type
Taiyo HPW 558C-10
1.4
Principal Particulars of Machinery6. Pump for Fresh Water HandlingPARTICULARS Main condensate pump Drain pump Main feed water pump Cold start feed water pump Main condenser vacuum pump Central cooling fresh water pump Cargo mach. Cooling F.W. boost pump Fresh water pump Drink water pump Fire fighting fresh water pump Hot water circulating pump W/H & CCR unit cooler F.W. boost pump D/G cooling fresh water pump Dist. plant circ. water pump Dist water tank recirc. pump Fresh water tank recirc. pump Drink. water tank recirc. pump NO. 2 3 2 1 2 2 2 2 2 1 2 1 2 2 1 1 1 TYPE M.D.V.C. M.D.V.C. T.D.H.C. M.D.H.C. M.D.H.C. M.D.V.C. M.D.H.C. M.D.V.C. M.D.V.C. M.D.H.C. M.D.H.C. M.D.H.C. M.D.H.C. M.D.V.C. Diaphragm Diaphragm Diaphragm CAPACITY m /h mTH 90 85 45 70 1407.84 Mpa D.P. 52.45MPa.D.P. 5.1 kPaA (722 mmHgV) 600 22 55 20 10 65 5 65 5 110 5 15 55 20 90 20 130 10 3 70 (max) 3 70 (max) 3 70 (max) Pneumatic Pneumatic Pneumatic 22 3,600 22 1,800 55 1,800 5.5 1,800 11 1,800 5.5 3,600 7.5 3,600 1.5 3,600 5.5 1,800 7.5 1,800 7.5 1,2003
7. Pump for Sea Water HandlingMOTOR kW rpm 45 1,800 22 1,800 PARTICULARS Main circulating pump Auxiliary circulating pump Main cooling S.W. pump Diesel generator cooling S.W. pump Water ballast Pump Water spray pump Main circulating pump Bilge & G.S. pump Fire & bilge pump Fire pump Eductor driving. & IGG cooling S.W. pump Engine room bilge pump Sewage discharge pump Distilling plant cooling S.W. pump Fire line pressurizing pump Bilge sep. service pump NO. 1 1 2 2 3 1 1 1 1 1 1 1 1 2 1 1 TYPE M.D.V.C. M.D.V.C. M.D.V.C M.D.V.C M.D.V.C. M.D.V.C. M.D.V.C. M.D.V.C. M.D.V.C. M.D.V.C. M.D.V.C. M.D.H.P M.D.V.C M.D.V.C. M.D.H.C M.D.H Snake CAPACITY m /h mTH 5,000/2,600 X 3/6 5,000/2,600 X 3/6 65020 20025 2,80035 1,050100 5,000/2,6003/6 25535 (8850) 170/255 100/35 (88 50) 170100 1,00040 5 40 4 20 10550 13100 50.343 MPa D.P With self-priming With self-priming3
NOTES
NOTES
MOTOR kW rpm 80360 80360 551,800 221,800 3751200 420 1,800 80360 451,800 100/301,800/1,200 1001,800 1851,800 1.51,200 1.53,600 301,800 113,600 1.51,200
1.4
Principal Particulars of Machinery8. Pump for Lub. Oil & Fuel Oil HandlingPARTICULARS Main L.O. pump Auxiliary L.O. pump. Control oil pump Stern tube L.O. pump L.O. transfer pump L.O. purifier feed pump T/G main L.O. pump T/G L.O. priming pump D/G main L.O. pump D/G L.O. priming pump F.O. burning pump Heavy F.O. transfer pump Diesel oil transfer pump Waste oil transfer pump NO. 1 2 2 2 1 1 2 2 2 2 4 1 1 1 TYPE M/T D.V.G. M.D.V.C. M.D.H. Vane M.D.H.G. M.D.H.G M.D.H.G. G/T D.V.G. M.D.H.G. G/E D.V.G. M.D.V.G. M.D.H.S. M.D.V.G. M.D.H.G. M.D.H. Snake CAPACITY m /h Mpa D.P. 1500.294 1500.294 2.41.47 10.196 10.294 3.10.294 240.6 90.2 400.9 7.50.15 5.02.74 500.294 100.294 100.392 2.21,800 151,800 18.51,200 3.71,200 5.51,200 Engine room supply fan Engine room exhaust fan F.O. pump room exhaust fan F.O. heating room exhaust fan Gland exhaust fan Vent duct exhaust fan Boiler flame eye seal air fan Waste oil settling tank exhaust fan W/S welding space exhaust fan 4 2 2 2 1 2 2 1 1 M.D.V. Axial M.D.V. Axial M.D.V. Axial M.D.V. Axial M.D.H.C M.D.H.C M.D.H.C M.D.H.C M.D.V. Axial PARTICULARS Forced draught fan NO. 2 TYPE M.D.H.C. 3.71,8003
9. Air Compressor and Air ReservoirMOTOR kW rpm PARTICULARS Air compressor NO. 3 2 1 2 1 1 2 1 1 4 TYPE M.D. screwM.D.H.P 2 stage
NOTES
CAPACITY m /h Mpa D.P. 5500.9 20 2.45 5 2.45 400 Nm3/h 5 0.9 5 0.9 0.5 2.45 0.2 2.45 10 0.9 0.1 0.93
NOTES F.W. cooled Oil injection Air cooled Air cooledDew point -40 at atmos.
MOTOR kW rpm 751,800 5.51,800 abt.2 PS
Submerged
373,600 2.21,800 0.751,200 0.751,200 1.51,200
D/G starting air compressor E/G starting air compressor Control air dryer Control air receiver General service air receiver D/G. starting air receiver E/G starting air receiver Nitrogen buffer tank Air press. lighting system air receiver
D.D.H. Duplex adsorption Cylindrical. Cylindrical. Cylindrical. Cylindrical. Cylindrical. Cylindrical.
10. FanCAPACITY m /min mmAq 950/1,110/1,900 500/650/500 1,65050 1,80015 10040 5040 10040 7300 50150 4900 10150 2020 No.1 No.23
NOTES
MOTOR kW rpm 130/300/300 900/1,200/1,200 30900 18.5900 1.51,800 1.51,800 1.53,600 3.73,600 3.73,600 1.53,600 0.21,800
No1 is reversible
1.4
Principal Particulars of Machinery11. Miscellaneous MachineryPARTICULARS Distilling plant NO. 2 TYPE Plate type 1.5 ppm M.D.C. Total discharge Automatic discharge typeSludge & solid waste disposal Ultraviolet Silver ion
12. Engine Workshop MachineryNOTES MOTOR kW rpm PARTICULARSLathe
CAPACITY 45 T/D
NO. 1 1
TYPE M.D. M.D.
CAPACITY C.D. : 2,000mm C.H. : 300mm Boring: Max. dia.: 32mm Milling: Table size : 800mm x 220mm Max. dia : 50mm Wheel dia.: 300mm 3-O2, 2-C2H2 200A
NOTES
MOTOR kW rpm 5.5900 5.51,800
1-S.W. cooled (S.W. Temp:30) 1-condens.cooled 5.51,800
L.O. purifier
1
3.1m3/h 5 m3/h (15ppm) 1,465 MJ/h (350 Mcal / h) 5 m3/h 90 T/D 2-Mineral
Combination Boling / milling Machine
Bilge separator
1
-
Pedestal drilling machine Pedestal grinder Gas welder
1 1 1 1 1 1 1
M.D. M.D. 2 wheels Acetylene D.C. arc
0.751,800 1.51,800
Incinerator Sterilizer Sterilizer Mineral injection unit Boiler water management system Chlorinator Sewage unit Unit cooler for switchboard room Unit cooler for mach. control room Unit cooler for instrument.& electric. workshop Unit cooler for engine workshop Unit cooler for laboratory Engine room heater N2 generator
1 1 1 1 1 1 1 2 2 1
0.751,800 111,800
Electric welder Plasma arc welder Electric hoist
Naltrack 3000HP
M.D. hoist Electrolyze
0.95ton Injection rate 0.2 ppm
For work shop
1.51,800
Electrolyze
Injection rate 0.2 ppm 40 persons 100% capacity for each room 100% capacity 100% capacity
Chlorinator
Packaged Packaged Packaged
1 2 2
Packaged Packaged Steam heating Membrane
100% capacity 100% capacity 890kW 60 Nm3/h
1.4
Principal Particulars of Machinery13. Heat Exchanger 14. Tank for L.O. HandlingPARTICULARS Main condenser Auxiliary condenser 1st stage feed water heater Deaerator feed water heater 3rd stage feed water heater Gland condenser CCS F.W. cooler Drain cooler L.O. cooler Stern tube L.O. cooler Hot water heater Boiler fuel oil heater Purifier L.O. heater D/G cooling fresh water cooler Stern tube L.O. fresh water heater Hydrant heater NO. 1 1 1 1 1 1 2 1 2 1 1 4 1 2 1 1 TYPE Vacuum type H.S. & T. Atmos. type H.S. & T. H.S. & T. Direct contact H.S. & T. H.S. & T. Plate H.S. & T. H.S. & T. H.S. & T. Electric & steam heating Steam heating Steam heating Plate Steam heating Steam heating 5 m3/h (20 to 80) 5.0 m3/h (60 to 150) 3.1 m3/h (40 to 85) F.W. 37 2.0 m3/h (0 to 10) 200 m3/h (0 to 10) 161.2Storage 360 liter
14. Tank for L.O. HandlingREMARKS S.W. 27 S.W. 32 C.W. 75 PARTICULARS L.O. sump tank L.O. gravity tank L.O. storage tank L.O. renovating tank Control oil tank NO. 1 1 1 1 1 1 1 1 1 1 1 1 1 CAPACITY Storage: abt. 40 m3 Normal : 15 m3 abt.20 m3 abt.60 m3 abt.60 m3 0.5 m3 1.5 m3 0.015 m3 0.18 m3 5.0 m3 5.0 m3 5.0 m3 5.0 m3 0.4 m3 H.R. 0.2m2/m3 H.R. 0.2m2/m3 In double bottom H.R. 0.2m2/m3 H.R. 0.2m2/m3 HEATING COIL Fitted(Around suction pipe)
CAPACITY 5.1 kPaA
TUBE O.D.t. 190.7 190.7 191.2
REMARKS In double bottom Hull construction Hull construction Hull constructionAttached on M/T
Storage capacity: 22.5 m3
F.W. 37 161.2 Each 100% cap. S.W. 32 F.W. 37 Each 100% cap. S.W. 27 F.W. 37 With 220 kW electric heater Each 100% capacity of a boiler
Stern tube L.O. drain tank Stern tube FWD seal oil tank Stern tube AFT seal oil tank Aux. turbine L.O storage tank Aux. turbine L.O. renovating tank Gen. engine L.O. storage tank Gen. engine L.O. renovating tank L.O. sludge tank
In double bottom
Each 100% cap S.W. 30
1.4
Principal Particulars of Machinery15. Tank for F.O. HandlingPARTICULARS Forward F.O. tank F.O. side tank F.O. settling tank Low sulphur F.O. tank D.O. storage tank Gen. engine D.O. service tank E/G engine D.O. service tank Incinerator D.O. service tank F.O. overflow tank IGG gas oil tank Waste oil settling tank F.O. drain tank F.O. additive tank NO. 1 2 2 1 2 2 1 1 1 1 2 1 1 CAPACITY abt. 1,200 m3 Total abt. 3,000 m3 Total abt. 1,000 m3 Total abt. 600 m3 abt. 370 m3 Total abt. 50 m3 3 m3 1 m3 abt. 75 m3 abt. 100 m3 1 m3 2 m3 4 m3 HEATING COIL H.R. 0.06m2/m3 H.R. 0.06m2/m3 H.R. 0.1m2/m3 H.R. 0.06m2/m3 H.R. 0.1m2/m3 H.R. 0.1m2/m3 H.R. 0.1m2/m3 H.R. 0.1m2/m3 H.R. 0.12m2/m3 H.R. 0.1m2/m3 H.R. 0.6m2/m3 H.R. 0.1m2/m3 In double bottom Hull construction Hull construction REMARKS Hull construction Hull construction Hull construction Hull construction Hull construction Hull construction Hull construction PARTICULARS Fresh water tank Drink. Water tank Distilled water tank Drain inspection tank Atmospheric drain tank CCS F.W. expansion tank Fresh water pressure tank Fire fight F.W. pressure tank Boiler compound tankOxygen scavenging chemical tank
16. Tank for Fresh Water & Bilge HandlingNO. 1 1 2 1 1 1 1 1 1 1 1 1 1 1 1 1 CAPACITY abt. 100 m3 abt. 100 m3 Total abt. 200 m3 1.5 m3 6 m3 1.0 m3 2.0 m31.5 m3
HEATING COIL
REMARKS Hull construction Hull construction Hull construction
H.R. 0.06m2/m3 H.R. 0.1m2/m3 H.R. 0.1m2/m3
Hull construction Hull construction Hull construction
0.15 m3 0.15 m3 Abt.100 m3 Abt.20 m3 Abt.10 m3 5.0 m3 2.0 m3 1.0 m3 H.R. 0.12m2/m3 Hull construction In double bottom
Bilge hold tank Clean drain tank Separated bilge oil tank Vacuum Unit tank for vacuum toilet system Dist. Plant Circ. Water Tank Drinking water Pressure tank
1.5a
Machinery Arrangement -Tank Top Plan
69
64
54WATER SPRAY PUMP
49
BALLAST STRIP. EDUCTOR EDUCTOR DRIVING & IGG C.S.W. PUMP DN
FIRE LINE PRESS. PUMP
45DN
FIRE PUMP
DIST. PLANT COOL. S.W. PUMP DN SOLENOID V. BOARD FOR BALLAST LINE
42 39 36S/T AIR CONT. UNIT UP BILGE & G.S. PUMP NO.3 WATER BALLAST PUMPW.
HIG
59
HS
.C.
FIRE & BILGE PUMPUP
ATMOS DRAIN TK MAIN CONDR DN. W B. UP
33
B.
28 19B. W
S/T AFT SEAL OIL TK
.
UP
HO
DN
T
WE
24UP UP AUX. L.O. PUMP
MAIN COND. PUMP
DRAIN PUMP
LL
AUX. CONDR
SEA BA
Y
REDUCT. GEAR
S/T FWD SEAL OIL TKN AI DR TK
19
S/T L.O. PUMP
24 28
S/T L.O. CLR
DN L.O. TRANSF. PUMP
UP
DRAIN COLLECT. UNIT
ESC
ALARM CHAMBER
AP
ET
S/T
RU
NK
O. L.
UP
AUX. L.O. PUMP) OW . (L S.C
L.O. PURIF. FEED PUMP
TK IN RA .D L.O
MAIN L.O. PUMP
NO.1WATER BALLAST PUMP
UPPA CE
ECHO SO
.S L.O
PT UM
K
UP
CL
DN
SP
33 36 39 42UP
LIF
AUX. CIRC. PUMP AUTO BACK-WASH FILTER L.O. COOLER
LIF
AC
TS
E
MAIN CIRC. PUMP
T.
SLUDGE COLLECTOR UP
F.OL.O. STRAINER
.D
RA
IN
TK
DN
BILGE SEP.UNIT
MAIN COOL. S.W. PUMP BILGE SEP.SERV. PUMP E/R BILGE PUMP D/G C.S.W. PUMP UP
49
54BIL GE PR IM .S
EC
.
59.T K
LG BI
EH
OL
D
TK
DN
45
TK OIL GE . BIL SEP
WASTE OIL TRANS. PUMP DN
B.
W
.
UND. & MA G. LO G
EA
N
DN
DR
COM P.
NO.2 WATER BALLAST PUMP
AI
N
TK
B.
W.
NO
.8
W
.B
.T
K
C L
64VOID
NO
.8
W.B
69
TANK TOP PLAN
1.5b
Machinery Arrangement -4th Deck Plan69 64 59 54F. COF
49ND ER )
45 42AF T .T LL
(P)
.S
TT.
F.O
39
. V.T
F.O
. SE
F.O
. SI
W.
IDE
TK
BA
TK
(P)
DE
TK
K
(P)
(P
)
F.O
.S
ID
K ET
(P
)(U
36
MAIN DUMP V. UP
UP
33
1ST STAGE FEED W. HTR
MAIN CONDR VACUUM PUMP
F.O. BURN. PUMP
CHLORINATOR
DN GREASE EXTRACT.
28V.T .
DN
DN
UP
UP
DIST. PLANT CIRC.W. TK DN
24UP
19DN DN N
REDUCT.GEAR
L.P.TURB.
DIST. PLANT CIRC.W. PUMP
F.O .PU MP RO OM (P )DIST.PLANT (C.C.) DIST.PLANT (S.W.C.)
ESCAPE TRU NKV.L.
GAUGE BOARD
LI
FT
CENTRAL COOL.F.W.PUMP
C L
19 24
H.P.TURB.
GLAND CONDR & EXH.FAN
V.T
.
DN DN DNSP LIFT AC . E
TEL.BOOTH UP DN
LI
FT
SP
AC
E
CCS F.W. CLR
28
UP DN
SPARE MOTOR FOR AUX. CIRC. P'P
PIPE PASS.
UP
UP
PURIF. L.O. HTR L.O.SLUDGE TK CLEAN. TABLE
33DRAIN INSPECT. TK CUNO FILTER
F.O. BURN. PUMP D.O.TRANS.PUMP H.F.O. TRANS. PUMP
D/G COOL. F.W. PUMP
D/G COOL. F.W. CLR UP
36DRAIN CLR
) M(S ROO UMP F.O.P
L.O. PURIF. UP
. V.T
.TK
(S)
LP
.S
F.O
45
F.O
.S
ID
E
T
U K(
ND
49
54 59
LO
ER
W
)
COFF.
64 69
F.O
SU
F.O. SIDE TK(S)
.OV
42
RF
HU
ET
ER
T.
FLO
.O
TK
WT
K(U N
AFT W
DE
R)
39
. BAL
L. TK
(S)
4TH DECK PLAN
1.5c
Machinery Arrangement -3rd Deck Plan42 45 49 54 59COFF.
64
69
39 36 33
TK
(P
)
F.O . SE TT. TK(P )
F.O . SID ET K(P )
AS
BA
UP
UP
24 19 14E OR ST
COMBUSTION AIR BLOWER
I.G. GENERATOR
AL IC EM CH
M .R .G I. G
AF
28
AT
I.G.G.F.O. PUMP UNIT
T
F.O
W
. SID
ER
ET
LL
K(P
T
)
V.T.
CONT. PANELV
NO.T.
.8
W.
B.
TK
SHO WER SPA CE
.W
.T
9.T W T. KNO .1 DI
COLD START FD W. PUMP 3RD STG FD.W.HTR
K
CONT.PANEL F.O. PUMP RM EXH. FAN MAIN FD W. PUMP NO.9 BALLAST SOL.V. BOARD
NO
.2
DI
S
ST
NO.3 AIR COMP.
GENE. SERV. AIR RECEIVER
CONT. AIR RECEIVERUP
UP
CONT. AIR DRYER NO.2 AIR COMP. NO.2 NO.1 DN UPUP
NO.2 MAIN TURBO GENERATOR
NO.2UP
MAIN BLR
NO.1 AIR COMP. STEERING ENGINE ROOM
DOSING & DILUTION STATION
UP
UP
NO.1 MAIN TURBO GENERATOR
UP
UP UP
CE PA TS LIF
NO.2 H/V TRANS. SPACE
REMOV. GRAT.
AY IR W STAESCAPE TRUNK FIRE FIGHT. F.W. PRESS. TKLIF T
LIF
TM
OT
R OR
M
C L
UP
NO.1 H/V TRANS. SPACESTERILISER (SILVER ION) FIRE FIGHT. F.W. PUMPLIF TS
PA
CE
P
E AC
UP
D.W. PRESS. TK & PUMP UNIT
LOCAL FIRE CONT. PANEL MICRO FOG PUMP PANEL LOCAL FIRE FIGHT SYS. F.W. TK LOCAL FIRE PUMP UNIT UP UP
LIF TS
NO.1
MAIN BLR
UP
UP
UP
F.W. PRESS. TK & PUMP UNIT
CARGO MACH. RM COOL. F.W. BOOST PUMP
F.O. PUMP RM EXH. FAN
UP
SEWAGE UNIT. TK
DRIN
K. W
W F.
.T
K
MINERAL INJECT. UNIT VACCUM TOILET SYS. L.O. DAIRY TK
UP
UP
LO
GR
AV
IT
Y
TK
NO.2 AUX.DIESEL GENE. UP UP
NO.1 AUX. DIESEL GENE.
9 14
V.T.
V.T.
ENG
. ST
ORE
SPARE MOTORS
24LIF T.
28 33 36 39 42NO .8 W. B. TKCOFF.
45
49
54
LOW
SP
E AC
SUL
PHU
T AF
RF
ER AT W
.O.
59
F.O
. SE
TK
TT.
19
T AS LL BA
64
F.O . SID E TK (S)
TK(S
TK
) (S
)
UP
STERILIZER(UV TYPE)
NO.2 D/G START. AIR COMP.
NO.2 AIR RECEIV.
NO.1 AIR RECEIV.
NO.1 D/G START. AIR COMP.
69
3RD DECK PLAN
1.5d
Machinery Arrangement -2nd Deck Plan45 49 54COFF.
59
64
69
36 33 28 24DN
39
42CONDENSING UNIT
I.G.G . GA SO IL T K
W AT ER
BA LL .T K( P)
COFF.
AF T
TK(P
)
NDE
TT.
F.(U
. SE
19LS TO RE ICA
COF
F.O
I. G. COOLER & DRYER
EM
CH
D.
PACKAGE AIR COND.
O.
ST
OR
GAS BLOWER
.TK
(P
)
F.O
. SID
ET
K(P
R)
)
LAB OR ATO RY
NO
W.
.1 D
TK
IST
M .R .G I. G
. TK
. NOUP UP
8W
.B
.T
K
.W
DIS
BLR SAMPLE COND. & ANALY. UNIT
T.
SINK
NO
.2
V.T
V.T.
ELECTRICAL & INSTR.WORK SHOPFEED W. SAMPLE COND. & ANALY. UNIT NO.2 F.O. HTG RM EXH. FAN VISCO. CONT. UP PACKAGE AIR COND.
PACKAGE AIR COND.
NO HEA .2 F.O TIN . GR M
UP UP UP HOT W.CIRC.PUMP W/H & CCR UNIT COOL. F.W. BOOST PUMP UP
UP
HOT W.HTR
(U) NO.1/(D) NO.2
BLR F.O. HTR (2 SETS)
D AR BO CH IT W SUP DN
) (P RM
BOG PIPE HOO D
BNR CLEAN. TABLE
DN
TS
PA
CE
DN
AFT MOOR. DK
BLR GAUGE BOARD
LIF
PACKAGE AIR COND.
ROO
DNCE
DN
UP
BLR F.O. HTR (2 SETS) (U) NO.1/(D) NO.2
LIF
TS
DN
PA
NO HEA .1 F.O TIN . GR M
DN
DRINK. W. FOUNTAIN UP BLR SOLENOID VALVE BOARD UP AUX. TURB. L.O. RENOV. TK AUX. TURB. L.O. STOR. TK UP OIL MIST DETECT. SYS.
MAC
HI. C
ONT
ROL
FT LI
C L
DN
M
PACKAGE AIR COND.
NO.1 F.O. HTG RM EXH. FAN
VISCO. CONT. BLR FLAME EYE SEAL AIR FAN
TK
F.W
E AC
.T
O .B
DR
TT
K.
.R
MCLEAN. OIL TKV.T V.T
W.
RE
NO
G/E V.T
L.O K
.
ST
G/E OR
L.O
K
.TK
.
IN
AIR PURGE LIGHT. SYS.
TT
SINK
R F.O
TK(S
PHU
. SE TT.
AT
28 33 36 39 42AF
ER
BA
LL
.T
K(
S)
24
L.O
E
. NG
HATCH
.R
EN
19
WELD. SPACE EXH. FAN
WO
RK
OV
SH
OP
D. O. ST OR .T K( S)
.T
K
LOW
F.O
/E TK .1 G NO SERV. . D.O
SUL
F.O
. SID
ET
K(S
PACKAGE AIR COND.
COFF.
. TK
O L.
OX
.S
Y.
TO
BO
R.
TK
M
G/E . TK NO.2 SERV . D.O
.R
SW IT CH BO AR D
RM (S ))
)
TK B. W. .8 NOCOFF.
T
W
45
49
54
59
64
69
2ND DK PLAN
1.5e
Machinery Arrangement -Engine Casing Deck Plan
28
33SHORE POWER CONN. BOX
36N2 BUFF. TANK
42N2 GE NE .R MCOMPRESSOR
I.G
.G
.RMDN
N2 GENE. UNIT
C
B O2
OTT
F . &
OA
MT
AN
KR
M
EXH. DAMPERV.T
WET GAS BLOWER
L.O. & HYD. OIL STOREV.T
49
28V.T
33
36V.T
42
49
28V.T
33
36V.T
42
F.O. ADD. TK
HYD.PUMP UNIT RM
DECK WORK SHOPNO.2 EXH.GAS ECO.
DN DN
DN
DN UP UP
DECK STOREUP
F.D. FAN SPARE MOTORDN DN UP
DEAERAT. FD W. HTRTS PA
BOLTED PLATE
VENTURI
CE
F.D. FAN
33
36
C L
CABLE DRUM FOR SHIP TO SHIP
33
36CCS F.W. EXP. TK
C LSMALL HATCH
DEAERAT.FD.W.HTR
33
36
C L
VENTURIDN
INCINE. RMUP UP UP UP
DN
INCINERATORDN
UP
VENT DUCT EXH. FAN
A/C UNIT RM & REF.PROV.MACH.RM
DN
NO.1 EXH.GAS ECO.
SILENCER FOR D/G EHX. PIPE
CONTROL PANEL
GARBAGE STRNO.1 EXH.GAS ECONOMIZER
INCINE. D.O. SERV. TK ECO. SPARE TUBE SPACEV.T
WASTE OIL SETT.TK
D/G C.F.W. EXP. TKV.T V.T V.T V.T V.T
DAMPER
COFF.
WALL VENT. EMERG.GENE.START AIR RESERV.
COFF.. SE RV. TK
CHEMICAL LKR
PAINT STORE
RM HTR EXH.DAMPER
EMERG.GENE.AIR COMP.
.DU
RM HTR
E/G CONT.PANEL
BATTERY
SUC.D
UCT
28 28 33 36 39 42
33
36
39
DN
R G. DE ER UN EM FF.( CO
EXH
N GE
E.
SW
RM BD ) DK P. UP
M NE.R .GE ERG EM
E/G
D.O
28
33
36
DN
UP
F.D. FAN
LIF
39
42
UP
CT
EMERG. GENE. ENG.
LOUVER BATTERY CHARGER
42
UPPER DECK PLAN
A DECK PLAN
B DECK PLAN
1.5f
Machinery Arrangement -Engine Casing Deck Plan
28NO.4 E/R SUPPLY VENT FANV. T
33
36
39V.T
42
28
33LOUVER
36LOUVER
39V.T
42
28
33
36
39
42
MIST SEPARATOR
MIST SEPARATOR
BOLTED PLATE
SU PP LY VE NT FA NR M
RM
SU
NO.2 E/R SUPPLY VENT FAN
E/R
NO .2 E/R
.4
NO
.2
E/R
SU
PP
NO
LY
.4 E
/R S
VE
UPP
PP
NT
L
LY
EN YV
FA
VE
TF
AN
NT
RM
NR M
FA
BOLTED PLATE
N
NO.2 E/R EXH. VENT FAN LOUVER
RM
DN
LOUVER
UP
DEAERAT. FD. W. HTRUP DN
33
36
C LRM
NO
.2
E/R
EX
H.
VE NT FA N
DN
NO
BOLTED PLATE
33
36
C L
33
36
C L
FUNNEL
UP
EX
H.
VE
NT
FA
N
DN
NO
.1
E/R
BOLTED PLATE
FA
M
NR
M
NO.1 E/R SUPPLY VENT FAN (REV.)
NO.1 E/R EXH. VENT FAN
DN
BOLTED PLATE
NR
FA
V.
NT
VE
RM
PP
SU
SU
MIST SEPARATOR WASTE OIL SETT. TK EXH. FAN
NOV.T
E/R
.3
E/R
SU
PP
L PP
LY
NO
YV
VE
.1
EN
NT
TF
E/R
MIST SEPARATOR
28
NO
LOUVER
LOUVER
.3
NO
AN
FA
.1
RM
N
E/R
NO.3 E/R SUPPLY VENT FAN
LY
SU
PP
LY
VE
T
NT
BOLTED PLATE
V.T
33
36
39
42
28
33
36
39
42
28
33
36
39
42
C DECK PLAN
D DECK PLAN
CASING TOP PLAN
1.5g
Machinery Arrangement -Elevation Plan
COMP. BRI. DK
NAV. BRI. DK
G DECK
F DECK
E DECK
EX
H.
VE
F NT
AN
M NR FA NT VE LY PP SU
SU P FA PLY N R VE NT M
RM
D DECK E/R SUPPLY VENT FAN E/R SUPPLY VENT FAN
C DECK
B DECK DEAERATOR FD.W.HTR
V.T.
A DECKV.T.
F.D. FAN
EXH. GAS ECONOMIZER
LIFT TRUNK
49
54
59
64
UPP.DK 27875S)
STAIR WAY
OO
BLR GAUGE BOARD STEAM AIR HEATERCON T. RM
BO
SW
G
IT
B CH
PIP
OA
RD
EH
RM
(P&
D
AFT MOOR. DK
23267
MA
CH.
2ND DK 22,850 MAIN BOILER
K(S .T
)TK (P)
F.W DIS . TK( S) T. W. TK (P)
INK
.W
T.
W.
DR
DIS
.2
OT
OR
RM
NO
TM
NO
.1
LIF
14
STEER ENG. 16,550 FLAT RAIL FOR M/T RAIL FOR PROP. SHAFT
NO
.2
H/
V
TA R
AN
S.
SP
AC
E
MAIN TURBO GENE.
3RD DK 15,650
A.P.
ESCAPE TRUNKVOID
AUX. CONDR.F .W .T K
4TH DK 9,470
CO
OL
S/T
WATER BALLAST PUMP
AUX. L.O. PUMP
ATMOS. DRAIN TK(S)
B. W.S/TSEA CHEST (S) FOR EMERG. FIRE PUMP
L.O
. DR
AIN
TKL.O .D
IN RA
TK
K TAN MP . SU L.O
SE
P.
BI
LG
E
O
SEA CHEST (S)
IL
CL
EA
N.
DR
AIN
TK
(S)
13
16
19
24
28
33
36
39
42
45
49
54
59
64
45,000 (FR SP.900 X 50)
E & CHO MA S G. OU LO ND G . CO MP
B.W
.(P)TK
(S
)SE
A
BA
Y
) .(P B.W
TANK TOP.
69
1.6 Glossary of Symbols
ABBREVIATION A A/C ACC ACCOM. AHD AST ATMOS. AUX. BD BLR BMS BNR BOG B.W. C CAP. CCR CCS CLR CMR COFF. COMPR COND. COND.W. CONDR CONDS D.D. D/G DIST. DK D.O. D.P. Absolute
GLOSSARY
ABBREVIATION DP DSH ECR E.F.P. ENG. E/R EXH. EXT. F.G. F.O. F.W. FD.W. FWR G G.O. G.S. G/E GEN. H H.P. H/D HDR HFO HTD HTG HTR HYD. ICAS IGG IR L LCL
GLOSSARY Differential Pressure Desuperheater Engine Control Room Emergency Fire Pump Engine Engine Room Exhaust External Fuel Gas Fuel Oil Fresh Water Feed Water Feed Water Regulator Gauge or Gear Gas Oil General Service Generator Engine Generator High or Horizontal High Pressure High Duty Header Heavy Fuel Oil Heated Heating Heater Hydraulic or Hydrant Integrated Control and Automation System Inert Gas Generator Infrared Low or Level Local
ABBREVIATION L/D L.O. L.P. LPSG M M/B MCR M.D. MSB M/T NOR NR OVBD P P.C.V. P.R.V. R/G RM S S.C. S/T STBD STBY STC STD STG STM STR S.W. SW T TBN Low Duty Lubricating Oil Low Pressure
GLOSSARY
ABBREVIATION T.C.V. T.H. T/C T/G TK UV V V.T. W. WB W.B. WC W/H W.O.
GLOSSARY Temperature Control Valve Total Head Turbo Charger Turbo Generator Tank Ultraviolet Vacuum or Vertical or Valve Vent Trunk Water or Working Wash Basin Water Ballast Water Closet Wheel-House Waste Oil
Air Conditioner Automatic Combustion Control Accommodation Ahead Astern Atmosphere Auxiliary Board Boiler Burner Management System Burner Boil Off Gas Bilge Well Compound or Centrifugal Capacity Cargo Control Room Central Cooling System Cooler Cargo Machinery Room Cofferdam Compressor Condition or Conditioner Condensate Water Condenser Condensate Diesel Driven Diesel Generator Distilling or Distilled Deck Diesel Oil Discharge Pressure
Low Pressure Steam Generator Motor Main Boiler Maximum Continuous Rating or Machinery Control Room Motor Driven Main Switch Board Main Turbine Normal Normal Rating Overboard Pressure or Piston or Pump or Pipe Pressure Control Valve Pressure Reducing Valve Reduction Gear Room Solenoid or Screw Sea Chest Stern Tube Starboard Standby Steam Temperature Control Standard Stage Steam Store Sea Water Switch Temperature or Turbine Turbine
1.6 Glossary of Symbols
SYMBOLS FOR PIPE DIAGRAM IN MACHINERY PART (1/6) Crossing Pipes, Not Connected Hopper
SYMBOLS FOR PIPE DIAGRAM IN MACHINERY PART (2/6) Stop Valve Geared Valve
Crossing Pipes, Not Connected
Hopper with Cover
Stop Valve
Screw Down Stop Check Valve Electric Moter Operated Screw Down Stop Check Valve Lift Check Valve
Crossing Pipes, Connected
Air Vent Pipe
Stop Valve Welded End
M
Joint , Flanged
Air Pipe Head without Wire Net
Three Way Valve
Joint , Welded
Air Pipe Head with Wire Net
M
Electric Moter Operated Valve
Swing Check Valve
Reducer Penetration, Water Tight Bulkhead Crossing Blank Flange Spectacle Flange "O" . . . Normal Open "C" . . . Normal Close Orifice
Sounding Head with Wire Cap Sounding Head with Self Closing Cock Deck Filling Piece
Hose Valve
Butterfly Check Valve
Pressure Reducing Valve
Float Check Valve
Safety or Relief Valve
Diaphragm Valve
Deck Scupper
Self Closing Valve
Ball Valve
Deck Scupper with Plug
Emergency Shut Off ValveS
Needle Valve
Flexible Pipe or Hose
Boss
Regulating Valve
Solenoid Valve
Expansion Joint
Boss with Plug
Butterfly Valve Electric Moter Operated Butterfly Valve Hydraulically Operated Butterfly Valve Gate Valve Electric Moter Operated Gate Valve
Piston Valve
Open Bilge
Driving Oil Line
M
Diaphragm Operated Valve Diaphragm Operated Valve with Positioner Three Way Rotary Valve Self Contained Pressure Control Valve
Hose Coupling
Control Air Line
Bellmouth
Capillary Tube
Sprinkler
Electric Cable
M
1.6 Glossary of Symbols
SYMBOLS FOR PIPE DIAGRAM IN MACHINERY PART (3/6) Self Contained Temperature Control Valve (With Handle) Wax Type Temperature Control Valve Air Vent Valve Y-Type Strainer or Filter
SYMBOLS FOR PIPE DIAGRAM IN MACHINERY PART (4/6) Tray or Coaming Float Type Flow Gauge
Mud Box
Salinity Cell
E
Seal Pot with Ethylene Glycol
Rose Box
Gauge Glass with Valve
PS
Pressure Switch
Separator
Flat Glass Level Gauge
DPS
Differential Pressure Switch
Degassing Valve
Pump
Float Level Gauge
TS
Thermal Switch
Drain Trap with Filter Regulating and Stop Valve with Filter Cock
Hand Pump
LI
Diaphragm Level Gauge
FS
Float Switch
Ejector or Eductor
Local Indication
LS
Limit Switch Electric Current/Pneumatic Converter Transmitter
Silencer
Remote Indication
I/P
Three Way Cock (L-Port)
Steam Horn or Air Horn
T
Thermometer
Three Way Cock (T-Port)
Flame Arrester
P
Pressure Gauge
For Trial Use
Four Way Cock
Sea Chest
C
Compound Gauge
Cock with Lock
Overboard Distance Piece
V
Vacuum Gauge
Self Closing Cock
Rose Plate
DP
Differential Pressure Gauge
Fauset
Bilge Hat
L
Level Indicator
Simlex Strainer or Filter
Sight Glass in Line
SI
Salinometer
Duplex Strainer or Filter
Sight Glass on Tank
FS
Flow Meter
1.6 Glossary of Symbols
SYMBOLS FOR PIPE DIAGRAM IN MACHINERY PART (5/6) AC Automatic Changeover FM Flow Monitoring PM
SYMBOLS FOR PIPE DIAGRAM IN MACHINERY PART (6/6) Pressure Monitoring TA Temperature Alarm
AOS
Automatic Open and Shut
FR
Flow Recording
PR
Pressure Recording
TI
Temperature Indication
AS
Automatic Stop
H
High
QA
Quality Alarm
TIC
Temperature Control
ASLD
Automatic Slow Down
L
Low
QI
Quality Indication
TM
Temperature Monitoring
ASS
Automatic Start and Stop
LA
Level Alarm
QM
Quality Monitoring
TR
Temperature Recording
AST
Automatic Stop
LI
Level Indication
QR
Quality Recording
VA
Viscosity Alarm
DPA
Differential Pressure Alarm
LIC
Level Control
RI
Running Indication
VI
Viscosity Indication
DPI
Differential Pressure Indication
LM
Level Monitoring
RM
Running Monitoring
VIC
Viscosity Control
DPM
Differential Pressure Monitoring
LR
Level Recording
RO
Remote Operation
VM
Viscosity Monitoring
DPR
Differential Pressure Recording
MFA
Malfunction Alarm
SA
Stop Alarm
VR
Viscosity Recording
ES
Emergency Stop Operation
OI
Opening Indication
SAH
Salinity Alarm
XA
Miscellaneous Alarm
ESA
Emergency Stop Alarm
OIO
Open Position Indication
SI
Salinity Indication
XI
Miscellaneous Indication
ESD
Emergency Shut Down
OIS
Shut Position Indication
SM
Salinity Monitoring
XM
Miscellaneous Monitoring
FA
Flow Alarm
PA
Pressure Alarm
SR
Salinity Recording
XR
Miscellaneous Recording
FI
Flow Indication
PI
Pressure Indication
FIC
Flow Control
PIC
Pressure Control
1.7 Ship Speed Power Curve
30,000
28,000
26,000
24,000
22,000
Output SHP(kw)
20,000
18,000
16,000
This section will be rectified after completion of the test.
14,000
12,000
10,000
8,000
6,000 14 15 16 17 18 19 20 21 22 23
Ship's Speed Vs(kn)
PART 2 : MACHINERY COMMISSIONING OPERATIONAL OVERVIEW
2.1 2.2 2.3 2.4 2.5 2.6 2.7
To Bring Vessel into Live Condition To Prepare Main Plant for Operation (Raising Steam) To Prepare Main Plant for Manoeuvring from In Port Condition To Change Main Plant from Manoeuvring to Normal Conditions To Change Main Plant from Normal to Manoeuvring Conditions To Secure Plant at Finished with Engines To Secure Plant for Dry Dock
2.1 To Bring Vessel Into Live ConditionNote: This procedure assumes that the main turbine and the main condenser are not readily available.
Dead Ship Condition
Shore Supply AvailableEstablish shore supply.
No Shore Supply Available 5.4.3Prepare the emergency generator for operation. If necessary fill the emergency diesel generator fuel tank from drums.
5.3
Fill a boiler to 100mm below the normal water level by using the cold start feed water pump, with suction from the distilled water tank.
3.2.2 4.3.2
Start the emergency generator and supply the emergency and main switchboards through the respective breakers
5.3 5.4.5
Supply main and emergency lighting throughout the vessel, together with necessary ventilation.
3.2.1
With a burner in a boiler, supply diesel oil to the burner using atomizing air. Supply main and emergency lighting throughout the vessel, together with necessary ventilation.
4.3.2
5.4.2
Put the generator air start system into operation. Start up the main diesel generator and place in parallel with emergency generator. The emergency generator will automatically disconnect from the switchboard
3.3.2 5.4.4
Start the boiler forced draught fan. With all required vents and drains open, begin to flash up the boiler. Ensure that the furnace is adequately purged prior to ignition. If the boiler has been shut down for a long period, use a low fuel pressure to ensure heat and boiler pressure rise slowly. Start the E R vent fans.
4.3.2
Put the following into operation: Cooling sea water system, cooling fresh water system, hydraulic power pack for the ship side valves.
3.5.2 3.4.1 7.2Open the boiler stop valves to: The superheated steam system. The 6.0Mpa desuperheated steam system. The auxiliary steam system. The 1.0Mpa desuperheated steam system. The superheater vent valve Ensure all steam line drains are open. Open the valves to the heating coils of one F O settling tank, placing the coil drains to the contaminated drains system.
3.1.1 3.1.2 3.1.3 3.1.5 3.2.5 3.2.6
Check all main turbine LO system lines are satisfactory, with the LO cooler drain valves closed. Ensure that the level in the main sump is correct. Start one main LO pump and allow the system to circulate. Check all sight glasses on bearings and gearing for oil flow. Ensure the LO gravity tank is overflowing.
3.7.1
Put the control air systems into operation.
3.3.1Shut the drum vent when steam issues from it, at approximately 0.1MPa. Open the steam inlet and drains to one fuel oil heater and allow the fuel temperature to rise slowly
4.3.2 3.1.5
Put the fire detection system into operation.
10.2
Next Page
2.1 To Bring Vessel Into Live Condition
Previous Page Recirculate DO around the fuel rail until its temperature reaches approximately 70. Change the burner over to HFO and shut down the diesel oil supply. 4.3.2 With the boiler superheater being circulated, and steam being supplied to the feed pump and turbine generator, all the boiler drains and vents can now be closed in. Continue to raise steam pressure, with fuel and air under the control of the ICAS. Check each system is now operational and gradually change over all control systems to automatic and/or remote. Ensure systems and components that have been used are put back on standby condition or isolated e.g. cold start feed water pump, emergency diesel generator etc. 4.3.2
As the steam pressure rises, use the cold start feed water pump to maintain the boiler water level. With the boiler now being fired on HFO, the fuel oil pressure will require adjusting to maintain a steady and safe pressure rate. Raise HFO temperature steadily.
4.3.2
Start the auxiliary sea water circulating pump to supply the auxiliary condenser. At 1.5MPa put one main feed pump into operation to maintain the boiler level. The turbine exhaust will go the either the deaerator or the auxiliary condenser.
3.5.1 4.3.2 3.1.6
Ensure that the ICAS has taken the control of the boiler out of the flashing ramp to the normal control mode. The boiler should now be providing normal steam pressure to the turbine generator, main feed pump and fuel oil heating etc. Unload and shut down the diesel generator.
4.3.4
5.4.2
Put the auxiliary condenser condensate and drain system into operation pump.
3.2.1
Start up all the remaining auxiliaries, such as refrigeration units, air conditioning units, fans not in use, galley and accommodation supplies etc.
At approximately 2.0MPa, warm through and start up a turbine generator. The exhaust will dump to the auxiliary condenser. Unload the diesel generator and parallel the turbine generator with the diesel generator.
5.1 3.1.6 5.4.4
(Note: If the vessel is in dry dock or alongside a shore installation, electrical power may be supplied through the shore breaker. However, this is normally used for dry dock purposes when separate arrangements are made for cooling sea water supplies to cooling fresh water cooler.
3.5.2
Having warmed through and drained the atomising steam system, when boiler pressure reaches 1.5Mpa, change the burner atomising to steam. Close the atomising air supply valve 025VPB or 035VPB.
3.1.3
Vessel in Live Condition
2.2 To Prepare Main Plant for Operation (Raising Steam)
One Boiler in Operation And Auxiliary Plant Operation
Open the vents on the superheater inlet pipe, and the drains on the desuperheater and superheater, on the non-operational boiler.
4.3.2
Allow the fuel temperature to rise to approx. 90C. Purge the boiler furnace. When the purge sequence is completed, flash the boiler and adjust the air and fuel to the minimum for good combustion. (Note: The length of time the boiler has been out of operation governs the amount of time to allow for raising steam. The longer the unit has been off line, the greater the number of flashes and soaks should be allowed, before continuous firing.)
4.3.2
At approximately 5MPa, open up the desuperheated system main valve bypass valve. Allow the pressure to increase to that of the in-use boiler and float the boiler on-line by opening the main valve and closing the drains and the bypass valve.
4.3.2
Fill the boiler to approximately 80mm above the normal operating level, using the main feed pump on the auxiliary feed system, with suction and recirculation from the deaerator. Ensure careful use of the filling valve and closely monitor the deaerator and boiler water levels.
4.3.2
Before opening the superheater valves, ensure the line drains to the in-use main feed pump and turbine generator are open. When the superheated temperature approaches the in-use boiler, slowly open the superheater system stop valves.
4.3.2
Slowly raise the steam pressure. At approx. 0.1MPa and with steam emitting from the superheater inlet pipe vent, close the vent valve.
4.3.2
Fit clean burner atomizers. Commence circulating fuel oil through the main fuel rail to raise the temperature.
4.3.2 Continue to raise the steam pressure, closing in the various drains as required to maintain good drainage without excessive water loss. 4.3.2
Close all drains and vents. Ensure that the IAS has normal control of combustion and level control, and the firing ramp has reset. The plant is now operating with two boilers, one turbine generator and one main feed pump, with exhausts and dumps to the auxiliary condenser.
4.3.2
Start a forced draft fan. Open atomising steam to the burners. Supply steam to the air heater. Reset all boiler trips. Place the boiler controls on manual and local in the ICAS.
4.3.2 4.3.4
Ensure that all drains from the main condenser sea water pipes are closed. Start a main sea water circulating pump to the main condenser, ensuring all valves on the system are open. 3.5.2 Start the stern tube and shaft seal LO system.
3.5.1
Isolate the auxiliary feed line to normal condition and line up the main feed line from the main feed pump. Maintain water level control on manual.
3.7.4
Next Page
2.2 To Prepare Main Plant for Operation (Raising Steam)
Previous Page Start the main turbine turning gear. 4.2.2 The plant is now operating with both boilers, all exhaust dumps to the main condenser and both main condensate and atmospheric drain systems in use. The main turbine has its vacuum raised with gland steam in use. The main turbine and stern tube LO systems are in use. The main turbine is being turned with the turning gear. 4.3.2
Crack open the main turbine gland steam make-up bypass valve and allow the turbine to warm through slowly.
3.1.3 4.2.2
Open the cooling sea water circulating system to a main turbine LO cooler.
3.5.1 4.2.2 3.1.6
Open the gland steam inlet valve 057VPB. Adjust the controller set steam pressure.
3.1.3 4.2.2
Ensure all the exhaust and drain systems are transferred from the auxiliary to the main condenser. Isolate and shut down the auxiliary condenser.
3.1.6
Start the gland condenser exhaust fan.
3.1.6
Place all pumps in use to remote start and their second pumps to standby conditions, with all required valves open.
Open the suction, discharge and casing vent to one of the main condensate pumps. Fill the main condenser to a working level from a distilled water tank. Start the main condensate pump.
3.2.1
When the auxiliary condenser has cooled down, shut down the SW cooling system and stop the auxiliary circulating water pump.
3.5.1
Start the one of main condenser vacuum pumps. When the vacuum approaches 700mmHg, transfer the turbine generator and other exhausts to the main condenser.
3.1.6
Main Plant Ready For Operation
2.3 To Prepare Main Plant for Manoeuvring from In Port Condition
Two Boilers in Operation Main Condenser Vacuum Established. Main Turbine Gear in Operation Bypass valve on main boiler superheated steam stop valves to the main turbine adjusted to maintain a pressure of 1.4Mpa on the main steam line.
Prepare and run up the second turbine generator. Place the second generator on the main switchboard in parallel with the generator in use.
5.1 5.4.2
Slowly open the main boiler stop valves and close the by-pass valves to the main turbine once the main steam line pressure is at normal.
3.1.1
After the Turbine has been warmed through, turning in the manual mode, place the controls in automatic mode, and allow the engine to continue to warm through by spinning manually (ahead and astern abt. 10rpm).
4.2.2
Ensure that the diesel generators are on standby and ready to run, should it be required.
5.2
Advise the bridge that the main turbine will be operated and confirm that the propeller area is clear. As required by international rules, ensure all the information concerning the above being carried out is recorded along with the times at which each section is completed. 4.3.2
Once loading arms are confirmed as disconnected, commence raising the main steam line pressure to the main turbine by slowly opening the main boiler's stop superheated steam valves to the main turbine.
3.1.1 Close the warming through steam line valves for main turbine. Open the astern guardian valve. 3.1.1 4.2.4
When the deck officer is available on the bridge, proceed with following test: With the main turbine controls on manual stop, move the telegraph lever to all its points, and prove the turbine remote control unit follows and answers the bridge unit.
4.2.3
Reset the main turbine trip, ensuring that the control oil pressure is correct for the manoeuvring system. Disengage the turning gear.
4.2.3
Ensure that if any burners are off, they are in place and ready to be used.
Check and inspect the steering gear systems, ensuring the LO levels and hydraulic oil levels are correct. As each unit is tested, check all movements of the rams and rudder are satisfactory and as required. Maintain contact with the bridge as these tests are undertaken. (Note: When steering gear tests are completed, to prevent the pumps delivering in the same mode for long periods and risk overheating the unit, ensure the deck officer alters the rudder angle regularly to overcome this.)
With the manoeuvring controls in manual mode, from the MCR with some attendance at the turbine side, operate the control to allow main steam into the turbine and rotate ahead and astern at 5 revolutions per minute. DEC. for astern and INC. for ahead. While the above is being undertaken, the main turbine is checked to ensure it turns satisfactorily in both directions.
Inform the bridge that the main engines are ready for use.
At standby, put the main turbine controls to bridge control mode and monitor their response as manoeuvring proceeds.
4.2.2
Using the controls in manual mode, repeat the ahead and astern movements to warm through the turbine to a superheated temperature approaching that of the boiler.
4.2.2
The Main Turbine is Now Ready to Put to Sea
2.4 To Change Main Plant from Manoeuvring to Normal Conditions
Vessel Is Manoeuvring On Bridge Control Put the boiler firing controls to the required firing mode in the ICAS, whereby boil-off gas may be used in conjunction with fuel oil if this is available. 4.3.4 Stop and isolate the off load turbine generator. Check that the electric LO pump starts as the LO pressure drops. Engage the turning gear when the turbine stops. 5.1
Bridge informs the MCR that the vessel is full away on passage, and indicates as such by moving the telegraph to full sea revolutions.
Record the following: Time Main engine revolution counter reading Fuel oil counter reading Fuel oil service tank levels Diesel oil service tank level Fuel and gas oil bunker tank levels Gas flow meter reading
Confirm the automatic stop of the main turbine standby auxiliary LO pump and that all LO pressures remain normal.
3.7.1
Ensure that the live steam make-up valves close and the main turbine bleed steam valves open as the main turbine revolutions increase. The main circulating system changes over from pump to scoop.
4.3.2 3.1.3 3.5.1
Pump the contents of the bilge tank overboard through the oily water separator unit. Note that MARPOL regulations apply.
3.8.1 3.8.2 Check that the changeover of the auxiliary heating steam system, from live to HP bleed, has occurred. 6.2 Confirm with the bridge that the boilers may be sootblown and proceed as appropriate. 3.1.5
Confirm that the astern guard valve is closed, the main turbine drains are automatically closed and the main feed water pump automatic recirculating valve is closed.
4.2.3 6.1
Evaporators may be used to fill the fresh and the distilled water tanks as long as the ship is in permitted waters. Run up and use these units as required.
Change to BOG burning only if required or remain on dual fuel burning. Allow the main engine revolutions to increase as per the timed program, which will open the manoeuvring valve a set amount over a period of time until it is fully open. This will take approximately 40 minutes from full ahead manoeuvring revolutions to full sea revolutions. 4.2.3
4.3.2 When full sea speed has been achieved, make final adjustments to the plant to give optimum performance at the required speed. Refer to the heat balance diagrams. 3.0
Remove one turbine generator from the main switchboard, allow it to run light for a few minutes to cool down. (Note: It is possible to test the turbine generator trips while the unit is in this condition.)
5.1 The vessel is now at Normal conditions, on bridge control.
The Main Turbine is Nav. Full On Bridge Control
2.5 To Change Main Plant from Normal to Manoeuvring Conditions
Vessel Is At Full Revolutions On Bridge Control
Approximately 2 hours before manoeuvring operations are to commence, run up and parallel the standby turbine generator. (Note: Trips may be tested at this time. When the unit is up to speed, parallel with the unit already on the main switchboard.)
5.1 5.4.4
As the main turbine revolutions reduce, the operating mode select switch will automatically change over to manoeuvring mode.
4.2.3
Approximately 1 hour before manoeuvring operations is to commence, request the bridge to bring the telegraph position to standby full ahead rpm gradually on the telegraph vernier over 40 minutes. The revolutions will be at the full ahead.
4.2.2
At manoeuvring rpm, the astern guardian valve opens, the turbine drains open and the feed pump recirculating valve opens.
4.2.3 6.1
When the bridge notifies the engine room of end of passage, record the following: Time Main engine revolution counter Fuel oil counter Fuel oil settling tank levels Diesel oil service tank level Fuel and diesel oil bunker tank levels Distilled and FW tanks levels Gas meter reading
As the turbine rpm continues to fall, the main condensate recirculation valve will open. As the main turbine rpm reduces, ensure that the following occurs: As the bleed steam pressures reduce, ensure the automatic valves close and the make-up valves open as required. 3.1.3 This allows condensate to re