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

UP

C.F

L.

B.

NO

.1

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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 Planetary gear type : 11kW ~ at Ahead stop valve inlet 1,800rpm

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

5.1kPaA (722mmHgV) at MCR (Sea water temperature=27 ) Main condenser : Scoop / pump cooling

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 : : : Maximum flow Temperature up Maximum MCR at MCR condition

Steam Conditions at Superheater Outlet Evaporation (per each set) Internal Desuperheater Air Heater Economizer Ambient Room Temp Feed Water Temp. Fuel Oil

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 heating type Extended surface type 50 145 at Forced draught fan suction 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:: 5.88MPaG~ 510 , Exhaust condition: 6.7kPaA (710mmHgV) abt. 2,250kw at atmospheric back pressure

Mitsubishi AT42CT-Babt. 600 mm ~ abt. 600 mm ~ abt. 880 mm ~ abt. 5,600 mm in length abt.11,800 mm in length abt.11,960 mm in length 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-4Fabricated steel welded construction with oil lubricating bearing of white metal facing (WJ-2) Air seal type Generator 2 Four 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 (Expandedj 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 ~ 90 ~ 45 ~3

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 22 ~ 22 ~ 55 ~ 5.5 ~ 11 ~ 5.5 ~ 7.5 ~ 1.5 ~ 5.5 ~ 7.5 ~ 7.5 ~ 3,600 1,800 1,800 1,800 1,800 3,600 3,600 3,600 1,800 1,800 1,200 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 3/6 650~ 20 200~ 25 2,800~ 35 1,050~ 100 5,000/2,600~ 3/6 255~ 35 (88~ 50) 170/255 ~ 100/35 (88 ~ 50) 170~ 100 1,000~ 40 5~ 4~ 40 20 With self-priming With self-priming3

mTH 85 70

NOTES

NOTES

MOTOR kW ~ rpm 80~ 360 80~ 360 55~ 1,800 22~ 1,800 375~ 1200 420 ~ 1,800 80~ 360 45~ 1,800 100/30~ 1,800/1,200 100~ 1,800 185~ 1,800 1.5~ 1,200 1.5~ 3,600 30~ 1,800 11~ 3,600 1.5~ 1,200

140~ 7.84 Mpa D.P. 5~ 2.45MPa.D.P. 5.1 kPaA (722 mmHgV) 600 ~ 55 ~ 10 ~ 5 ~ 5 ~ 5 ~ 55 ~ 90 ~ 130 ~ 3 ~ 3 ~ 3 ~ 22 20 65 65 110 15 20 20 10 Pneumatic Pneumatic Pneumatic

105~ 50 13~ 100 5~ 0.343 MPa D.P

70 (max) 70 (max) 70 (max)

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. 150~ 0.294 150~ 0.294 2.4~ 1.47 1~ 0.196 1~ 0.294 3.1~ 0.294 24~ 0.6 9~ 0.2 40~ 0.9 7.5~ 0.15 5.0~ 2.74 50~ 0.294 10~ 0.294 10~ 0.392 2.2~ 1,800 15~ 1,800 18.5~ 1,200 3.7~ 1,200 5.5~ 1,200 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. 3.7~ 1,8003

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. 550~ 0.9 20~ 5~ 2.45 2.453

NOTES F.W. cooled Oil injection Air cooled Air cooledDew point -40 at atmos.

MOTOR kW ~ rpm 75~ 1,800 5.5~ 1,800 abt.2 PS

Submerged

37~ 3,600 2.2~ 1,800 0.75~ 1,200 0.75~ 1,200 1.5~ 1,200

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.

400 Nm3/h 5 ~ 5 ~ 0.5~ 0.2 ~ 10 ~ 0.1 ~ 0.9 0.9 2.45 2.45 0.9 0.9

10. FanCAPACITY m /min ~ mmAq 950/1,110/1,900 ~ 500/650/500 1,650~ 50 1,800~ 15 100~ 40 50~ 40 100~ 40 7~ 300 50~ 150 4~ 900 10~ 150 20~ 20 No.1 No.23

NOTES

MOTOR kW ~ rpm 130/300/300 ~ 900/1,200/1,200 30~ 900 18.5~ 900 1.5~ 1,800 1.5~ 1,800 1.5~ 3,600 3.7~ 3,600 3.7~ 3,600 1.5~ 3,600 0.2~ 1,800

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 5.5~ 900 5.5~ 1,800

1-S.W. cooled (S.W. Temp:30 ) 1-condens.cooled 5.5~ 1,800

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

0.75~ 1,800 1.5~ 1,800

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

0.75~ 1,800 11~ 1,800

Electric welder Plasma arc welder Electric hoist

Naltrack 3000HP

M.D. hoist Electrolyze

0.95ton Injection rate 0.2 ppm

For work shop

1.5~ 1,800

Electrolyze

Injection rate 0.2 ppm 40 persons 100% capacity for each room 100% capacity 100% capacity

Chlorinator

Packaged Packaged Packaged

P 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 ) 16~ 1.2Storage 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. 19~ 0.7 19~ 0.7 19~ 1.2

REMARKS In double bottom Hull construction Hull construction Hull constructionAttached on M/T

Storage capacity: 22.5 m3

F.W. 37 16~ 1.2 Each 100% cap. S.W. 32 F.W. 37 Each 100% cap. S.W. 27 F.W. 37 With 2~ 20 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