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SALALAH LNG

Specifications of the vessel and the gas installations are believedto be correct, but not guaranteed.

GAS FORM-Cbased on the

OCIMF / SIGTTOSHIP INFORMATION QUESTIONNAIRE

forGAS CARRIERS

2nd Edition 1998

Gas Form-C Page 0

SALALAH LNGINDEX

GENERAL INFORMATION PAGE

A1 Principal Ship Particulars 2

A2 Hull Dimensions 4

A3 Immersion 4

A4 Loaded Particulars 4

A5 Parallel Mid-Body Dimensions 6

A6 Bunker Specifications and Capacities 6

A7 Fuel Consumption Details 6

A7 Speed/Consumption (Appendix) 7

A8 Main Engine Particulars 7

A9 Auxiliary Plants 7

A10 Power/Speed Information 7

A11 Thrusters 7

A12 Fresh Water 7

A13 Ballast Capacities and Pumps 8

A14 Mooring Equipment 8

A15 Navigational Equipment 10

A16 Communication and Electronics 12

CARGO SYSTEMSB1 Cargo - General Information 13

B2 Cargo Tanks 13

B3 Cargo Tank Capacities 14

B16 Deck Tank Capacities 17

B4 Loading Rates 17

B5 Discharging - General 19

B6 Discharge Performance 19

B7 Unpumpables 19

B8 Vaporising Unpumpables 19

B9 Reliquefaction Plant 20

B10 Section not in use.B11 Cargo Temperature Lowering Capability 20

B12 Inert Gas and Nitrogen 20

B13 Cargo Tank Inerting / De-Inerting 21

B14 Gas Freeing to Fresh Air 21

B15 Changing Cargo Grades 21

B17 Pre-Loading Cooldown 22

B18 Vaporiser 22

B19 Blower 22

B20 Cargo Re-Heater 23

B21 Hydrate Control 23

B22 Cargo Measurement 23

B23 Cargo Sampling 24

B24 Cargo Manifold 25

B25 Cargo Manifold Reducers 27

B26 Connections to Shore for ESD and Communication Systems 27

B27 Manifold Derrick/Crane 27

B28 Stores Derrick/Crane 27

B29 Sister Vessel(s) 27

Gas Form-C Page 1

SALALAH LNG

SECTION AGENERAL INFORMATION

A1 PRINCIPAL SHIP PARTICULARS1.1 Date questionnaire completed 29-Feb-121.2 Name of vessel SALALAH LNG1.3 LR/IMO number 93008171.4 Last previous name None1.4.1 Date of name change None1.5 Second last previous name None1.5.1 Date of name change None1.6 Third last previous name None1.6.1 Date of name change None1.7 Fourth last previous name None1.7.1 Date of name change None1.8 Flag PANAMA1.9 Port of Registry PANAMA1.10 Official number 31551-061.11 Call sign 3EDE91.12 INMARSAT A or B number N/A1.13 Vessel's telephone number Inmarsat F : 764-550-4631.13.1 Vessel's mobile number N/A1.14 Vessel's fax number 764-550-4581.15 Vessel’s telex number 4371561101.16 Vessel's E-mail address [email protected] INMARSAT C number 4371561101.18 Vessel's MMSI number 371 561 0001.19 Type of vessel LNG Carrier

OWNERSHIP AND OPERATION1.20 Registered Owner SNC Alice

Full address Dohat Al Adab Street, OOSC Building,Al Khuwair, PO Box 104, PC 118

Sultanate of Omanc/o Oman Ship Management Company

Office telephone number +968-24400900Office telex number N/AOffice fax number +968-24400923Office Email addressContact person Andrew BoyceContact person after hours telephone number +968-98048122

1.21 Name of technical operator (If different from above) Oman Ship Management Company S.A.O.C.

Full Address PO Box 104, P.C. 118, Al-Harthy Complex,

Dohat Al Adab Street, Bldg. No. A75,

3rd Floor, OOSC Building, Al Khuwair,

Muscat, Sultanate Of Oman.

Office telephone number +968-24400900Office telex number N/AOffice fax number +968-24400923Office Email addressContact person (Designated Person Ashore)Contact person after hours telephone numberEmergency callout numberEmergency callout pager number N/AContact details for person responsible for oil spill response

Number of years controlled by technical operator 6 Years

1.22 Total number of ships operated by this Operator 151.23 Number of years ship owned 11 Years

[email protected]

[email protected]

+968-98048122+968-98008999

Andrew Boyce

Capt. Andrew Boyce

Gas Form-C Page 2

SALALAH LNG

1.23.1 Name of commercial operator (If different from above) Qalhat LNG S.A.O.C.Full Address PO Box 514, Al Khuwair, PC 133

Sultanate of Oman

Office telephone number +968-2457-4046Office telex numberOffice fax number +968-2457-4094Office Email address [email protected] person Ragdha MahdiContact person after hours telephone number +968-9282-5808Emergency callout numberEmergency callout pager numberNumber of years controlled by commercial operator 6 Years

BUILDER1.24 Builder1.25 Name of yard vessel built at Geoje Shipyard1.26 Hull number 15361.27 Date keel laid 08 Nov 20041.28 Date launched 05 Mar 20051.29 Date delivered 30 Dec 20051.30 Date of completion of major hull changes, - if any. N/A1.31 If changes were made, what changes were made and at which

yard were they carried out

CLASSIFICATION1.32 Classification society NK1.33 Class Notation

1.34 If Classification society changed, name of previous society None1.35 If Classification society changed, date of change None1.36 Was ship built in accordance with the following regulations:

IMO YES/NOUS COAST GUARD YES/NORINA YES/NOOther:______________________________________

YES/NO

1.37 IMO certificationCertificate of fitness - IGC YES/NO

Certificate - A328 YES/NOCertificate - A329 YES/NO

Letter of Compliance NOIssued by

1.38 Unattended Machinery Space Certificate YES/NO

1.39 Net Registered Tonnage 290011.40 Gross Registered Tonnage 966711.41 Suez Net Tonnage - Canal Tonnage 99956.26

Suez Gross Tonnage1.42 Panama Net Tonnage - Canal Tonnage None

Panama Gross Tonnage None

+A1(E), SH, SH-DLA, SFA(40) SHCM, +AMS, +ACCU, UWILD, NIBS, PMS & CMS, DNV-FAMC

Samusung Heavy Indstry Co., Ltd

Gas Form-C Page 3

SALALAH LNGA2 HULL DIMENSIONS2.1 Length overall (LOA) 285.103Metres

2.2 Length between perpendiculars (LBP) 272.040Metres

2.3 Distance bow to bridge 224.154Metres

2.4 Distance bridge front - mid point manifold 95.20Metres

2.5 Distance bow to mid-point manifold 142.5Metres

2.6 Extreme breadth 43.40Metres

2.7 Extreme depth 26.00Metres

2.8 Summer draught 12.122 (Extreme) 12.10 (Mld) Metres

2.9 Corresponding Summer deadweight 81034.6Tonnes

2.10 Light displacement 29809.4Tonnes

2.11 Loaded displacement (Summer deadweight) 110844Tonnes

2.12 Cargo tanks cubic capacity - 100% 148173.717Cubic metres

2.12.1 Deck tank(s) cubic capacity - 100% NoneCubic metres

2.12.2 Cargo tanks cubic capacity - 98% 145210.244Cubic metres

2.12.3 Deck tank(s) cubic capacity - 98% NoneCubic metres

2.13 Distance from keel to highest point 54.995Metres

2.14 Air draught (normal ballast condition) 45.395Metres

A3 IMMERSION Tonnes / cm @metres draught

3.1 TPC - in normal ballast condition 97.4TPC - in loaded condition (summer deadweight) 102.6

A4 LOADED PARTICULARS4.1 Cargo grade Butane Propane

4.2 Density4.3 Cargo loadable Tonnes

4.4 Bunkers - FO Tonnes

4.5 Bunkers - DO Tonnes

4.6 Fresh water Tonnes

4.7 Stores & spares Tonnes

4.8 Lub oil Tonnes

4.9 Ballast Tonnes

4.10 Deadweight Tonnes

4.11 Draught - forward Metres

Draught - aft Metres

Draught - mean Metres

Cargo grade Butadiene Propylene

DensityCargo loadable Tonnes

Bunkers - FO Tonnes

Bunkers - DO Tonnes

Fresh water Tonnes

Stores & spares Tonnes

Lub oil Tonnes

Ballast Tonnes

Deadweight Tonnes

Draught - forward Metres



Gas Form-C Page 4

SALALAH LNG

Cargo grade Ethylene Ammonia


Bunkers - FO Tonnes

Bunkers - DO Tonnes

Fresh water Tonnes


Lub oil Tonnes

Ballast Tonnes

Deadweight Tonnes




Cargo grade VCM Propylene Oxide


Bunkers - FO Tonnes

Bunkers - DO Tonnes

Fresh water Tonnes


Lub oil Tonnes

Ballast Tonnes

Deadweight Tonnes




Gas Form-C Page 5

SALALAH LNG

A5 PARALLEL MID-BODY DIMENSIONS

5.1 Light ship 107.70Metres

5.2 Forward to mid-point manifold - light ship 39.00Metres

5.3 Aft to mid-point manifold - light ship 68.30Metres

5.4 Normal ballast 140.7Metres

5.5 Forward to mid-point manifold - normal ballast 56.0 Metres

5.6 Aft to mid-point manifold - normal ballast 84.7 Metres

5.7 Loaded SDWT 153.2Metres

5.8 Forward to mid-point manifold - loaded designed 60.7 Metres

5.9 Aft to mid-point manifold - loaded designed 92.5 Metres

A6 BUNKER CAPACITIESGrade Capacity @ 98%

Main engine M.F.O.(380cSt) 7070MTAuxiliary engine(s) M.D.O.(DMB) 344MTOther: I.G.G. Plant M.G.O 146MT

A7 FUEL CONSUMPTION DETAILSGrade

Tonnes/day

Tonnes/day

Tonnes/day

Tonnes/day

Tonnes/day

LoadDraft

BallastDraftLightShip

C/L

Gas Form-C Page 6

SALALAH LNG

A7 SPEED/CONSUMPTIONCopies of the vessel's Speed and Consumption Graph for both Laden and Ballast conditions are enclosed?

NO

A8 MAIN ENGINE PARTICULARS8.1 Main engine make and type

8.2 Number of units 18.3 Maximum continuous rating (MRC) per engine kW @ RPM

36800 kw 88.58.4 Total available power 36800kW

8.5 Normal service power 33120kW

A9 AUXILIARY PLANTS9.1 Make and type of auxiliary generators / engines (Diesel)

(Turbine)9.2

Number of units 39.3 Maximum generator output per unit RPM Kilowatts

(Diesel) Unit no. 1 720 3960(Turbine) Unit no. 2 1800 3750(Turbine) Unit no. 3 1800 3750

9.4 Shaft generator N/A9.5 Total available power 11460 kw x 6600V9.6 Emergency generator KTA50DMGE 1100 x 440V x 19.7 Emergency fire pump - type RVP250MS

Delivery pressure Bar

Motive power 460 m3/h x 120 mTHIf electrical, - indicate power required 250 Kilowatts

9.8 Steering gear - type R4ST 700HIndicate power required to steer the vessel with one pump unit

55Kilowatts

A10 POWER/SPEED INFORMATION10.1 Trial data BHP

MRC SHP

Speed 19.5 Knots

Draught 11.4 Metres

BHPMRC SHP

Speed Knots

Draught Metres

A11 THRUSTERS11.1 Make and type Kawasaki, Pitch control type11.2 Bow thruster (output) 2000Kilowatts

11.3 Stern thruster (output) N/A Kilowatts

A12 FRESH WATER12.1 Capacity of distilled tanks 408.4Tonnes

12.2 Capacity of domestic tanks Distilled 19 Tonnes

12.3 Daily consumption Domestic 20 Tonnes

12.4 Daily evaporator capacity (Max.) 120 Tonnes

MAN B&W

Mitsubishi Multi stage Single Cylinder,condensing turbine

10

double reaction geared marine turbineKHI UA-4--Cross compound impulse

Gas Form-C Page 7

SALALAH LNG

A13 BALLAST CAPACITIES AND PUMPSTank Capacity (m3) Number

13.1 Fore peak 1,463.60 113.2 Wing and or side tanks 54,919.96 1413.3 Double bottom tanks13.4 Aft peak 26-Sep-02 113.5 Other: None None13.6 Total 57,383.90 16

13.7 Ballast pump make and type SHINKO IND.,LTD

Elect.motor driven,GVD500-3M

13.8 Number of pumps 313.9 Total capacity 9,000 M3/hour

13.10 Location Engine Room13.11 Control location Cargo Control Room

Gas Form-C Page 8

SALALAH LNGA14 MOORING EQUIPMENT14.1 ROPES

Indicate on the diagram below the position of:Winch Mounted Ropes (R)Open Fairleads (O)Closed Fairleads (C)

Alternatively enclosed copy of vessel's Mooring arrangements in A4 format.

YES/NO

MOORING ROPES (ON DRUMS)Mooring Ropes (On Drums) Forecastle - Number 9Diameter 44 mm.

Material Galvanised SteelLength 275 Metres

Breaking Strength 128 Tonnes

Mooring Ropes (On Drums) Forward Main Deck - Number

None

Diameter mm.

MaterialLength Metres

Breaking Strength Tonnes

Mooring Ropes (On Drums) Aft Main Deck - Number 4Diameter 44 mm.



Mooring Ropes (On Drums) Poop - Number 7Diameter 44 mm.



OTHER MOORING LINESMooring Ropes not on Drums - Number NoneDiameter mm.

MaterialLength Metres

Breaking Strength Tonnes

Emergency Towing Wires / Fire Wires - Number 2Diameter 38 mm.



Refer to the attached documents

Gas Form-C Page 9

SALALAH LNG14.2 MOORING WINCHES

Forecastle - Number 4Single Drum or Double Drums DoubleSplit Drums Y/N YesMotive Power HydraulicHeaving Power 30 Tonnes

Brake Capacity 102.4 Tonnes

Hauling Speed 15 Metres/Min.

Forward Main Deck - Number NoneSingle Drum or Double DrumsSplit Drums Y/NMotive PowerHeaving Power Tonnes

Brake Capacity Tonnes

Hauling Speed Metres/Min.

Aft Main Deck - Number 2Single Drum or Double Drums DoubleSplit Drums Y/N YesMotive Power HydraulicHeaving Power 30 Tonnes



Poop - Number 3Single Drum or Double Drums DoubleSplit Drums Y/N YesMotive Power HydraulicHeaving Power 30 Tonnes



14.3 ANCHORS AND WINDLASSWindlass motive power(e.g. steam, hydraulic) Hydraulic

Hauling power 50.4 / 30.0 Tonnes

Brake holding power 335.8 Tonnes

Anchor typeWeight 13.4 Tonnes

Is spare anchor carried NOCable diameter 102 mm.

Number of shackles port cable 14Number of shackles starboard cable 13

14.4 TOWING ARRANGEMENTSIs the vessel fitted with a Towing Bracket Aft? YES

If Yes, state SWL 200 Tonnes

Is Towing chain provided YESDimensions of Towing wire Diameter mm.

Length Metres

14.5 WINDAGEWindage on ballast draught End-on 1283 Squaremetres

Lateral 6763 Squaremetres

High Holding Power Stockless Anchor

Gas Form-C Page 10

SALALAH LNG

A15 NAVIGATIONAL EQUIPMENT15.1 Magnetic compass YES15.2 Off Course Alarm - Magnetic compass YES15.3 Gyro compass YES

Number of Units 215.4 Off Course Alarm - Gyro compass YES15.5 Gyro (Bridge) Repeaters YES

Number of Units 415.6 Radar 3cm YES15.7 Radar 10cm YES15.8 Are radars gyro stabilised? YES15.9 Radar plotting equipment YES15.10 ARPA YES15.11 ECDIS YES15.12 Depth sounder with recorder YES15.13 Depth sounder without recorder YES15.14 Speed/distance indicator YES15.15 Doppler log YES15.16 Docking approach Doppler YES15.17 Rudder angle indicator YES15.18 Rudder angle indicator on Each Bridge Wing YES15.19 RPM indicator YES15.20 RPM indicator on Each Bridge Wing YES15.21 Controllable pitch propeller indicator NONE15.22 Thruster(s) indicator YES15.23 Rate of turn indicator YES15.24 Radio direction finder NO15.25 Navtex receiver YES15.26 GPS YES15.26.1 DGPS YES15.27 Transit SATNAV NO15.28 Decca navigator NO15.29 Omega NO15.30 Loran C NO15.31 Weather fax YES15.32 Sextant(s) YES15.33 Signal lamp ALDIS YES15.34 Anemometer YES15.35 Engine order recorder YES15.35.1 VDR (Voyage Data Recorder) YES15.36 Course recorder YES15.37 Are steering motor controls and engine controls fitted on

bridge wings?NO

15.38 Is bridge equipped with a 'Dead-Man' alarm? YES15.39 What chart outfit coverage is provided World-wide NO

Limited YESIf limited, - please indicate area(s) covered

15.40 Formal chart correction system in use YES15.41 Electronic Chart system in use NO

JP, Far E, NW Aus, W Eur, N Am

Gas Form-C Page 11

SALALAH LNG

A16 COMMUNICATIONS AND ELECTRONICS16.2 What GMDSS areas is the vessel classed for? A1 A2 A3 A4 A1,A2 & A316.3 Transponder (SART) YES16.4 EPIRB YES16.5 How many VHF radios are fitted on the bridge? 216.6 Is vessel fitted with VHF in the cargo control room (CCR)?

YES

16.7 Is the CCR connected to the vessel's internal communication system?

YES

16.8 How many intrinsically safe walkie talkies are provided for cargo handling?

12

16.9 Is vessel fitted with an INMARSAT satellite communications system?

YES

16.10 Does vessel carry at least three survival craft two-way radio telephones?

YES

16.11 Inmarsat satellite system YESSpecify system type A, B or C F & C

16.12 2182kHz bridge auto alarm YES16.13 Radio telephone distress frequency watch receiver YES16.14 Emergency lifeboat transceiver YES16.15 Can vessel transmit the helicopter homing signal on 410 kHz?

YES

16.16 Full set of Radio List publications YES

Gas Form-C Page 12

SALALAH LNG

SECTION BCARGO SYSTEMS

B1 CARGO - GENERAL INFORMATION1.1 List products which the ship is Certified to carry

LIQUEFIED NATURAL GAS

Transport and Carriage Conditions1.2 Minimum allowable tank temperature -163 Deg. Celsius

1.3 Maximum Permissible tank pressure 25kpaG Kp/cm2

1.4 List Number of grades that can be loaded/discharged simultaneously and completely segregated without risk of contamination?

NA

1.5 List the Number of grades that can be carried simultaneously and completely segregated without risk of contamination? NA

1.6 What is the Number of Products that can be conditioned by reliquefaction simultaneously?

1

1.7 State the number of natural segregation's (NB: Separation must be by the removal of spools or the insertion of blanks) 4

B2 CARGO TANKS2.1 Type and materials of cargo tanks2.2 Maximum allowable relief valve setting 25kpaG Bar gauge

2.2.1 IMO Setting Bar gauge

2.2.2 USCG Setting Bar gauge

2.3 Safety valve set pressure, - if variable stipulate range of pilot valves Bar gauge

2.4 Maximum allowable vacuum Bar gauge

2.5 Maximum cargo density at 15 deg Celsius 0.5 Kp/cm2

2.6 Maximum rate of cool-down -20 Deg Cel / Hour

2.7 State any limitations regarding partially filled tanks

2.8 State allowable combinations of filled and empty tanks

Membrane type, GTT Mark III

Gas Form-C Page 13

SALALAH LNG

B3 CARGO TANK CAPACITIESTank number / location 1 / FRAME No. 117-127Capacity m3 (100%) 22,643.51 m3

Capacity 98% 22,190.64 m3

Butane capacity Tonnes

Butane temperature Deg. C

Propane capacity Tonnes

Propane temperature Deg. C

Butadiene capacity Tonnes

Butadiene temperature Deg. C

Propylene capacity Tonnes

Propylene temperature Deg. C

Vinyl Chloride Monomer capacity Tonnes

Vinyl Chloride Monomer temperature Deg. C

Ethylene capacity Tonnes

Ethylene temperature Deg. C

Propylene Oxide capacity Tonnes

Propylene Oxide temperature Deg. C

Ammonia capacity Tonnes

Ammonia temperature Deg. C

Tank number / location 2 / FRAME No. 102-116Capacity m3 (100%) 42,933.67 m3

Capacity 98% 42,075.00 m3

















Tank number / location 3 / FRAME No.87-101Capacity m3 (100%) 42,931.32 m3

Capacity 98% 42,072.69 m3

















Gas Form-C Page 14

SALALAH LNGTank number / location 4 / FRAME No. 73-86Capacity m3 (100%) 39,665.22 m3

Capacity 98% 38,871.92 m3

















Tank number / locationCapacity m3 (100%) m3

Capacity 98% m3


















Capacity 98% m3

















Gas Form-C Page 15

SALALAH LNGTank number / locationCapacity m3 (100%) m3

Capacity 98% m3


















Capacity 98% m3

















Total Capacity of all cargo tanks (100%) 148,173.717 m3

Total Capacity of all cargo tanks (98%) 145,210.244 m3

Total Capacity of Butane Tonnes

Total Capacity of Propane Tonnes

Total Capacity of Butadiene Tonnes

Total Capacity of Propylene Tonnes

Total Capacity of Vinyl Chloride Monomer Tonnes

Total Capacity of Ethylene Tonnes

Total Capacity of Propylene Oxide Tonnes

Total Capacity of Ammonia Tonnes

Gas Form-C Page 16

SALALAH LNGB16 DECK TANK CAPACITIES

Are Deck pressure tank(s) fitted? YES/NOMaterial of tank(s)Maximum allowable relief valve setting Bar gauge

Deck tank number 1 - capacity (100%) m3

Capacity 98% m3

Propane Capacity Tonnes

Butane Capacity Tonnes



Ammonia Capacity Tonnes

Deck tank number 2 - capacity (100%) m3

Capacity 98% m3

Propane Capacity Tonnes

Butane Capacity Tonnes



Ammonia Capacity Tonnes

B4 LOADING RATES4.1 From Refrigerated Storage (Fully Refrigerated at Vessel's

Manifold)Butane - with vapour return Tonnes/Hr.

Butane - without vapour return Tonnes/Hr.

Propane - with vapour return Tonnes/Hr.

Propane - without vapour return Tonnes/Hr.

Butadiene - with vapour return Tonnes/Hr.

Butadiene - without vapour return Tonnes/Hr.

Propylene - with vapour return Tonnes/Hr.

Propylene - without vapour return Tonnes/Hr.

Ethylene - with vapour return Tonnes/Hr.

Ethylene - without vapour return Tonnes/Hr.

Ammonia - with vapour return Tonnes/Hr.

Ammonia - without vapour return Tonnes/Hr.

Vinyl Chloride Monomer - with vapour return Tonnes/Hr.

Vinyl Chloride Monomer - without vapour return Tonnes/Hr.

Propylene Oxide - with vapour return Tonnes/Hr.

Propylene Oxide - without vapour return Tonnes/Hr.

4.8 From Pressure StorageButane 0 deg C - with vapour return Tonnes/Hr.

0 deg C - without vapour return Tonnes/Hr.

10 deg C - with vapour return Tonnes/Hr.




Propane minus 30 deg C - with vapour return Tonnes/Hr.

Minus 30 deg C - without vapour return Tonnes/Hr.

Minus 20 deg C - with vapour return Tonnes/Hr.










Butadiene 0 deg C - with vapour return Tonnes/Hr.






Gas Form-C Page 17

SALALAH LNGPropylene minus 30 deg C - with vapour return Tonnes/Hr.












Ethylene minus 100 deg C - with vapour return Tonnes/Hr.








Ammonia minus 20 deg C - with vapour return Tonnes/Hr.






VCM minus 10 deg C - with vapour return Tonnes/Hr.








4.14 Special remarks:

Gas Form-C Page 18

SALALAH LNGB5 DISCHARGING - GENERAL

Cargo Pumps5.1 Type of Pumps

5.2 Number of pumps per tank 25.3 Rate per Pump 1750 m3/hr

5.4 At Delivery Head mlc 170mTH mlc

5.5 Maximum density 0.5 Kg/m3

Booster Pump N/A5.6 Type of Booster Pumps N.A5.7 Number of pumps per tank5.8 Rate per Pump m3/hr

5.9 At Delivery Head mlc mlc

5.10 Maximum density Kg/m3

Copies of pumping curves for cargo and booster pumps are enclosed?

YES/NO

B6 DISCHARGE PERFORMANCEFull Cargo Discharge Times (using all cargo pumps) 14 HrsFully RefrigeratedManifold Back Press 1 kP/cm2, with vapour return Hours

Manifold Back Press 1 kP/cm2, without vapour return Hours

Manifold Back Press 5 kP/cm2, with vapour return Hours




PressurisedManifold Back Press 1 kP/cm2, with vapour return Hours






B7 UNPUMPABLES7.1 Tank number / location 1 50 m3

Tank number / location 2 50 m3



Tank number / location m3




Total 200 m3

B8 VAPORISING UNPUMPABLES8.1 Process used

Time to vaporise liquid unpumpables remaining after full cargo discharge of:

8.2 Butane Hours

8.3 Propane Hours

8.4 Butadiene Hours

8.5 Propylene Hours

8.6 Ethylene Hours

8.7 Ammonia Hours

8.8 Vinyl Chloride Monomer Hours

8.9 Propylene Oxide Hours

Electric motor driven centrifugal submerged

Gas Form-C Page 19

SALALAH LNG

B9 RELIQUEFACTION PLANT N/A9.1 Plant Design Conditions - air temperature Deg. C

9.3 Plant Design Conditions - sea temperature Deg. C

Plant Type9.4 Is the plant single stage/direct? YES/NO9.5 Is the plant two stage/direct? YES/NO9.6 Is the plant simple cascade? YES/NO9.7 Coolant type

Compressors9.8 Compressor type9.8.1 Compressor makers name9.9 Number of compressors9.10 Capacity per unit m3/hr

9.11 Are they Oil Free? YES/NO

B11 CARGO TEMPERATURE LOWERING CAPABILITY (AT SE A WITH SEA TEMPERATURE +15C)Time taken to lower the temperature of:

11.1 Propane from -5 deg C to - 42 deg C Hours

11.2 Propane from -20 deg C to - 42 deg C Hours

11.3 Propane from -38 deg C to - 42deg C Hours

11.4 Propane from +20 deg C to 0 deg C Hours

11.5 Propane from 0 deg C to -20 deg C Hours

11.6 Butane from +20 deg C to 0 deg C Hours

11.7 Butane from +10 deg C to 0 deg C Hours

11.8 Butane from +10 deg C to -5 deg C Hours

11.9 ButadieneFrom +20 deg C to -5 deg C Hours

11.10 PropyleneFrom -20 deg C to -47 deg C Hours

11.11 EthyleneFrom -100 deg C to -104 deg C Hours

11.12 AmmoniaFrom -15 deg C to -33 deg C Hours

11.13 Vinyl Chloride MonomerFrom -5 deg C to -14 deg C Hours

B12 INERT GAS AND NITROGENMain IG Plant

12.1 Type of system12.2 Capacity 14000 m3/hr

12.3 Type of fuel used Gas oil12.4 Composition of IG - oxygen 0.5 vol %

Composition of IG - CO2 Max. 14 %

Composition of IG - Nox Max 100ppm %

Composition of IG - N2 Balance %

12.5 Lowest dewpoint achievable -45 Deg. C

12.6 Used for

Auxiliary IG or Nitrogen plant N2 Generator12.7 Type of System

12.8 Capacity 90 m3/hr

12.9 Composition of IG - oxygen - %

Composition of IG - CO2 - %

Composition of IG - Nox - %

Composition of IG - N2 97 %

12.10 Lowest dewpoint achievable -70 Deg. C

12.11 Used for

Nitrogen N/A12.12 Liquid storage capacity - m3

12.13 Daily boil-off loss - m3

12.14 Maximum supply pressure - Kp/Cu. Cm

12.15 Supply capacity - m3/hr

12.16 Used for -

IBS & IS

Cargo Tank, Cofferdam Space, Liquid & Vapor Line

Gln 14000-0.25 BUFD

Membrane permeation type

Gas Form-C Page 20

SALALAH LNG

B13 CARGO TANK INERTING/DE-INERTING13.1 Time taken to inert from fresh air to under 5% O2 at minus 25

degree C?20

Hours

13.2 Time taken to inert from cargo vapour to fully inert at minus 25 degrees dewpoint when IG density is less than product? -

Hours

Time taken to inert from cargo vapour to fully inert at minus 25 degrees dewpoint when IG density is greater than product?

20Hours

B14 GAS FREEING TO FRESH AIR14.1 Plant used14.2 Time taken from fully inert condition to fully breathable fresh

air?20

Hours

B15 CHANGING CARGO GRADESIndicate number of hours needed to change grades from the removal of pumpables to tanks fit to load andthe estimated quantity of Inert Gas and or Nitrogen consumed during the operation:

Hours Inert Gas NitrogenFrom Propane to ButaneFrom Propane to ButadieneFrom Propane to EthyleneFrom Propane to AmmoniaFrom Propane to Vinyl Chloride MonomerFrom Propane to Propylene OxideFrom Butane to PropaneFrom Butane to ButadieneFrom Butane to EthyleneFrom Butane to AmmoniaFrom Butane to Vinyl Chloride MonomerFrom Butane to Propylene OxideFrom Butadiene to PropaneFrom Butadiene to ButaneFrom Butadiene to EthyleneFrom Butadiene to AmmoniaFrom Butadiene to Vinyl Chloride MonomerFrom Butadiene to Propylene OxideFrom Ethylene to PropaneFrom Ethylene to ButaneFrom Ethylene to ButadieneFrom Ethylene to AmmoniaFrom Ethylene to Vinyl Chloride MonomerFrom Ethylene to Propylene OxideFrom Ammonia to PropaneFrom Ammonia to ButaneFrom Ammonia to ButadieneFrom Ammonia to EthyleneFrom Ammonia to Vinyl Chloride MonomerFrom Ammonia to Propylene OxideFrom Vinyl Chloride Monomer to PropaneFrom Vinyl Chloride Monomer to ButaneFrom Vinyl Chloride Monomer to ButadieneFrom Vinyl Chloride Monomer to AmmoniaFrom Vinyl Chloride Monomer to EthyleneFrom Vinyl Chloride Monomer to Propylene OxideFrom Propylene Oxide to PropaneFrom Propylene Oxide to ButaneFrom Propylene Oxide to ButadieneFrom Propylene Oxide to EthyleneFrom Propylene Oxide to Vinyl Chloride MonomerFrom Propylene Oxide to Ammonia

Cargo Grade Change Operations that cannot be carried out at sea:

IGG (Dry air mode)

Gas Form-C Page 21

SALALAH LNG

B17 PRE-LOADING COOLDOWN

17.1 Propane - Quantity of Coolant Required m3

Propane - Time required to cooldown cargo tanks from ambient temperature with vapour return line Hours

Propane - Time required to cooldown cargo tanks from ambient temperature without vapour return line Hours

17.2 Butane - Quantity of Coolant Required m3

Butane - Time required to cooldown cargo tanks from ambient temperature with vapour return line Hours

Butane - Time required to cooldown cargo tanks from ambient temperature without vapour return line Hrs.

17.3 Butadiene - Quantity of Coolant Required m3

Butadiene - Time required to cooldown cargo tanks from ambient temperature with vapour return line Hours

Butadiene - Time required to cooldown cargo tanks from ambient temperature without vapour return line Hours

17.4 Propylene - Quantity of Coolant Required m3

Propylene - Time required to cooldown cargo tanks from ambient temperature without vapour return line Hours

Propylene - Time required to cooldown cargo tanks from ambient temperature with vapour return line Hours

17.5 Ethylene - Quantity of Coolant Required m3

Ethylene - Time required to cooldown cargo tanks from ambient temperature with vapour return line Hours

Ethylene - Time required to cooldown cargo tanks from ambient temperature without vapour return line Hrs.

17.6 Ammonia - Quantity of Coolant Required m3

Ammonia - Time required to cooldown cargo tanks from ambient temperature with vapour return line Hours

Ammonia - Time required to cooldown cargo tanks from ambient temperature without vapour return line Hours

17.7 VCM - Quantity of Coolant Required m3

VCM - Time required to cooldown cargo tanks from ambient temperature without vapour return line Hours

VCM - Time required to cooldown cargo tanks from ambient temperature with vapour return line Hours

B18 VAPORISER18.1 Type of Vaporiser

18.2 Number of Vaporisers fitted 2-Jan-0018.3 Capacity per unit - Propane m3/hr Vap

18.4 Liquid Supply Rate m3/hr Liq

18.5 Delivery Temperature Deg. C

18.6 Capacity per unit - Ammonia m3/hr Vap



18.9 Capacity per unit - Nitrogen m3/hr Vap



B19 BLOWER19.1 Type of Blower19.2 Rated Capacity 32000 m3/hr

19.3 Delivery Pressure 203 kPaA

The following questions ask the Time and Quantity of coolantrequired to cooldown cargo tanks fromambient temperature to fully gassed up state sufficient to allow loading to commence.

Electric motor driven

Horizontral shell & tube, direct steam heated

Gas Form-C Page 22

SALALAH LNG

B20 CARGO RE-HEATER20.1 Type of Re-Heater20.2 Number Fitted 220.3 Heating Medium20.4 Discharge rates with sea water at 15 degrees C to raise

product temperature of Propane from -42 degrees C to -5 degrees C m3/hr

20.5 Discharge rates with sea water at 15 degrees C to raise product temperature of Ammonia from -42 degrees C to -5 degrees C m3/hr

B21 HYDRATE CONTROL21.1 Type of Depressant?21.1.1 Freezing point temperature? Deg. C

21.2 Quantity of Depressant Carried? Ltr.

21.3 Means of injection?Name any other system used

B22 CARGO MEASUREMENTLevel Gauges

22.1 Are level gauges local or remote? Remote22.2 Name of manufacture22.3 Type 22.4 Rated Accuracy ± 5 mm.

22.5 Certifying Authority ABS

Temperature Gauges22.6 Name of manufacture22.7 Type 22.8 Rated Accuracy


Pressure Gauges22.10 Name of manufacture22.11 Type

22.12 Rated Accuracy


Oxygen Analyser22.14 Name of manufacture22.15 Type 22.15.1 What is the lowest level measurable? %

Fixed Gas Analyser22.16 Name of manufacture22.17 Type

22.18 Are Cargo tank calibration tables available? YES22.19 Name of Measuring Company SGS22.20 Name of Certifying Authority ABS22.21 Calibration calculated to cm? NO22.21.1 Calibration calculated to 1/2 cm? NO22.22 Tables established to cm? NO22.22.1 Tables established to mm? YES22.22.2 Tables established to "other" (state what other)22.23 Are trim and list corrections available? YES22.24 Are temperature corrections available? YES22.25 Are float gauge tape corrections available? YES

Kongsberg Maritime SA

± 1.5 ℃ ( -140℃ ～　+ 40℃)

Horizontral shell & tube, direct steam heated

Electric resistance type


Reiken Keki Korea Co ltd

NDIR / CATALYTIC TYPE


Absolute pressure type

± 0.2 ℃ ( -165℃ ～　-140℃)

Radar type level gauge

± 1% of full span (+0.6 Kpa)

Gas Form-C Page 23

SALALAH LNG

B23 CARGO SAMPLING23.1 May cargo samples be obtained from the levels; top, middle

and bottom in all cargo tanks?YES/NO

If no, - the arrangement for sampling is limited to:At shore sampling facility

23.2 Can samples be drawn from tank vapour outlet? YESCan samples be drawn from manifold liquid line? YESCan samples be drawn from manifold vapour line? YESCan samples be drawn from pump discharge line? YES/NO

23.3 State sample connection type Size of sample connection mm.

Gas Form-C Page 24

SALALAH LNG

B24 CARGO MANIFOLD

Manifold arrangement diagram

Center of manifold to bow 124.4M.

Center of manifold to stern 142.7M.

Dimension A 8000 mm.

Dimension B 6000 mm.

3000 mm.

Dimension D 0 mm.

Dimension E 3000 mm.

Dimension F 6000 mm.

Dimension G 8000 mm.

Dimension H 8750 mm.

Pipe Flange A - duty Fuel OilPipe Flange A - rating 10 bar

Pipe Flange A - size 300 mm.

Pipe Flange A raised or flat face Flat facePipe Flange B - duty LNGPipe Flange B - rating 10 bar

Pipe Flange B - size 400 mm.

Pipe Flange B raised or flat face Flat facePipe Flange C - duty LNG

Dimension C (Please refer to our Ship/Shore Interface Plan)

Gas Form-C Page 25

SALALAH LNGPipe Flange C - rating 10 bar

Pipe Flange C - size 400 mm.

Pipe Flange C raised or flat face Flat facePipe Flange D - duty VaporPipe Flange D - rating 10 bar

Pipe Flange D - size 400 mm.

Pipe Flange D raised or flat face Flat facePipe Flange E - duty LNGPipe Flange E - rating 10 bar

Pipe Flange E - size 400 mm.

Pipe Flange E raised or flat face Flat facePipe Flange F - duty LNGPipe Flange F - rating 10 bar

Pipe Flange F - size 400 mm.

Pipe Flange F raised or flat face Flat facePipe Flange G - duty Fuel OilPipe Flange G - rating 10 bar

Pipe Flange G - size 300 mm.

Pipe Flange G raised or flat face Flat facePipe Flange H - duty Diesle OilPipe Flange H - rating 10 bar

Pipe Flange H - size 100 mm.

Pipe Flange H raised or flat face Flat faceHeight above uppermost continuous deck 4800 mm.

Distance from ship side 3500 mm.

Height above load waterline 18715 mm.

Height above light waterline 21815 mm.

Manifold Arrangement Located on Top of CompressorDistance from rail of compressor room/platform to presentation flanges mm.

Distance from deck of compressor room/platform/try to centre of manifold mm.

Gas Form-C Page 26

SALALAH LNG

B25 CARGO MANIFOLD REDUCERS25.1 Number of ANSI Class 300 reducers carried onboard NIL

Flange rating of ANSI Class 300 reducer bar

Size of ANSI Class 300 reducer mm.

Length of ANSI Class 300 reducer mm.

25.2 Number of ANSI Class 300 to Class 150 reducers carried onboardFlange rating of ANSI Class 300 to Class 150 reducer bar

Size of ANSI Class 300 to Class 150 reducer mm.

Length of ANSI Class 300 to Class 150 reducer mm.

25.3 Number of ANSI Class 150 reducers carried onboardFlange rating of Class 150 reducer bar

Size of ANSI Class 150 reducer mm.

Length of ANSI Class 150 reducer mm.

B26 CONNECTIONS TO SHORE FOR ESD AND COMMUNICATIO NS SYSTEMS26.1 Is ESD connection to shore available? YES/NO

If yes, is the system pneumatic? YES/NO/NAIf yes, is the system electrical? YES/NO/NAIf yes, is the system fiber optic? YES/NO/NA

26.2 What is the type of connection used?26.3 Are ESD hoses or cables available on board? YES/NO

If yes, length of pneumatic 15 mm X 30 M mm.

If yes, length of electrical N/A mm.

If yes, length of fiber optic N/A mm.

26.4 Is there a connection available for a telephone line? YES/NO26.5 Are ESD connections available on both sides of vessel?

YES/NO

Are ESD Fusible plugs fitted at tank domes? YES/NOAre ESD Fusible plugs fitted at manifolds? YES/NOIs the link compatible with the SIGTTO guidelines? YES/NOType of manifold valve ButterflyClosing time in seconds 24 secs

Is closing time adjustable? YES/NOIs Independent high level shut down system fitted(overflow control)?

YES/NO

If yes, does the independent high level shutdown system also switch off running cargo pumps?

YES/NO/NA

Shut down level % 99.3 %

B27 MANIFOLD DERRICK/CRANE27.1 Is manifold derrick provided NO27.2 Is manifold crane provided YES27.3 Is lifting equipment same for port and starboard? YES

If no, then stipulate details27.4 State SWL at maximum outreach 5 Tonnes

27.4.1 Maximum outreach of lifting equipment 25 Metres

B28 STORES DERRICK/CRANE28.1 State location

SWL 5 Tonnes

B29 SISTER VESSEL(S)29.1 Name of vessel IBRA LNG

Accomodation

Pneumatic / Electrical / Fiber Optic

Gas Form-C Page 27

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