GAS FORM-C. based on the OCIMF / SIGTTO SHIP INFORMATION QUESTIONNAIRE for GAS CARRIERS 2nd Edition 1998

Transcription

1 GAS FORM-C based on the OCIMF / SIGTTO SHIP INFORMATION QUESTIONNAIRE for GAS CARRIERS 2nd Edition 1998 Specifications of the vessel and the gas installations are believed to be correct, but not guaranteed. Gas Form-C Page 0

2 INDEX 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 SYSTEMS B1 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

3 SECTION A GENERAL INFORMATION A1 PRINCIPAL SHIP PARTICULARS 1.1 Date questionnaire completed 29-Feb Name of vessel NIZWA LNG 1.3 LR/IMO number Last previous name None Date of name change None 1.5 Second last previous name None Date of name change None 1.6 Third last previous name None Date of name change None 1.7 Fourth last previous name None Date of name change None 1.8 Flag PANAMA 1.9 Port of Registry PANAMA 1.10 Official number 1.11 Call sign 3ECP INMARSAT A or B number N/A 1.13 Vessel's telephone number Vessel's mobile number N/A 1.14 Vessel's fax number Vessel s telex number Vessel's address nizwalng@amosconnect.com 1.17 INMARSAT C number Vessel's MMSI number Type of vessel LNG Carrier OWNERSHIP AND OPERATION 1.20 Registered Owner ORYX LNG CARRIER S.A. Full address HongKong Bank Building, 6th Floor, Samuel Lewis Ave.,Panama, Republic of Panama Office telephone number Office telex number N/A Office fax number Office address andrew.boyce@omanship.co.om Contact person Andrew Boyce Contact person after hours telephone number Name of technical operator (If different from above) Full Address Oman Ship Management Company S.A.O.C. Dohat Al Adab Street OOSC Bldg, PO Box 104 P.C. 118, Sultanate of Oman Office telephone number Office telex number N/A Office fax number Office address andrew.boyce@omanship.co.om Contact person (Designated Person Ashore) Andrew Boyce Contact person after hours telephone number Emergency callout number Emergency callout pager number N/A Contact details for person responsible for oil spill response Capt. Andrew Boyce Number of years controlled by technical operator 7 Years 1.22 Total number of ships operated by this Operator Number of years ship owned 11 Years Gas Form-C Page 2

4 Name of commercial operator (If different from above) Itochu Corporation Full Address 5-1, KITA-AOYAMA 2-CHOME, MINATO-KU, TOKYO , Japan Office telephone number Office telex number N/A Office fax number Office address Contact person Contact person after hours telephone number Kunihiro Yamaguchi Emergency callout number N/A Emergency callout pager number N/A Number of years controlled by commercial operator 7 Years BUILDER 1.24 Builder Kawasaki Shipbuilding Corporaqtion 1.25 Name of yard vessel built at Sakaide,Japan 1.26 Hull number Date keel laid Date launched Date delivered Date of completion of major hull changes, - if any. N/A 1.31 If changes were made, what changes were made and at which yard were they carried out CLASSIFICATION 1.32 Classification society NK 1.33 Class Notation NS* MNS*,NK (M0-B, BRS-1) 1.34 If Classification society changed, name of previous society None 1.35 If Classification society changed, date of change None 1.36 Was ship built in accordance with the following regulations: IMO US COAST GUARD RINA Other: 1.37 IMO certification Certificate of fitness - IGC Certificate - A328 Certificate - A329 Letter of Compliance NO Issued by 1.38 Unattended Machinery Space Certificate 1.39 Net Registered Tonnage 35, Gross Registered Tonnage 118, Suez Net Tonnage - Canal Tonnage 103,945 Suez Gross Tonnage 119, Panama Net Tonnage - Canal Tonnage None Panama Gross Tonnage None Gas Form-C Page 3

5 A2 HULL DIMENSIONS 2.1 Length overall (LOA) Metres 2.2 Length between perpendiculars (LBP) Metres 2.3 Distance bow to bridge Metres 2.4 Distance bridge front - mid point manifold Metres 2.5 Distance bow to mid-point manifold Metres 2.6 Extreme breadth Metres 2.7 Extreme depth Metres 2.8 Summer draught Metres 2.9 Corresponding Summer deadweight Light displacement Loaded displacement (Summer deadweight) 110, Cargo tanks cubic capacity - 100% Cubic metres Deck tank(s) cubic capacity - 100% None Cubic metres Cargo tanks cubic capacity - 98% Cubic metres Deck tank(s) cubic capacity - 98% None Cubic metres 2.13 Distance from keel to highest point Metres 2.14 Air draught (normal ballast condition) Metres A3 IMMERSION / metres draught 3.1 TPC - in normal ballast condition TPC - in loaded condition (summer deadweight) A4 LOADED PARTICULARS 4.1 Cargo grade Butane Propane 4.2 Density 4.3 Cargo loadable 4.4 Bunkers - FO 4.5 Bunkers - DO 4.6 Fresh water 4.7 Stores & spares 4.8 Lub oil 4.9 Ballast 4.10 Deadweight 4.11 Draught - forward Metres Draught - aft Metres Draught - mean Metres Cargo grade Butadiene Propylene Density Cargo loadable Bunkers - FO Bunkers - DO Fresh water Stores & spares Lub oil Ballast Deadweight Draught - forward Draught - aft Draught - mean Cargo grade Ethylene Ammonia Density Cargo loadable Bunkers - FO Bunkers - DO Fresh water Stores & spares Lub oil Ballast Deadweight Draught - forward Draught - aft Draught - mean Metres Metres Metres Metres Metres Metres Gas Form-C Page 4

6 Cargo grade VCM Propylene Oxide Density Cargo loadable Bunkers - FO Bunkers - DO Fresh water Stores & spares Lub oil Ballast Deadweight Draught - forward Draught - aft Draught - mean Metres Metres Metres Gas Form-C Page 5

7 A5 PARALLEL MID-BODY DIMENSIONS Load Draft Ballast Draft Light Ship C/L 5.1 Light ship Metres 5.2 Forward to mid-point manifold - light ship Metres 5.3 Aft to mid-point manifold - light ship Metres 5.4 Normal ballast Metres 5.5 Forward to mid-point manifold - normal ballast Metres 5.6 Aft to mid-point manifold - normal ballast Metres 5.7 Loaded SDWT Metres 5.8 Forward to mid-point manifold - loaded SDWT Metres 5.9 Aft to mid-point manifold - loaded SDWT Metres A6 BUNKER CAPACITIES Grade 98% Main engine M.F.O.(380cSt) Auxiliary engine(s) M.D.O.(DMB) Other: I.G.G. Plant M.G.O.(DMA) A7 FUEL CONSUMPTION DETAILS Grade /day /day /day /day /day Gas Form-C Page 6

8 A7 SPEED/CONSUMPTION Copies of the vessel's Speed and Consumption Graph for both Laden and Ballast conditions are enclosed? NO A8 MAIN ENGINE PARTICULARS 8.1 Main engine make and type Kawasaki UA-400 type Double Reduction Geared,2 Cylinder Cross Compound Impulse Steam Turbine 8.2 Number of units Maximum continuous rating (MRC) per engine RPM 26,900 kw 80 rpm 8.4 Total available power 36,570 HP 8.5 Normal service power 32,920 HP A9 AUXILIARY PLANTS 9.1 Make and type of auxiliary generators / engines (Diesel) 8N330L-SV, Yanmar 3,100kw x 450V x 1 (Turbine) Multi-Stage Impulse Vacuum type with 9.2 Single Reduction Gear(RG92), Shinko, 3,100kw x 450V x 2 Number of units Maximum generator output per unit RPM Kilowatts (Diesel) Unit no ,100 (Turbine) Unit no (Turbine) Unit no Shaft generator N/A 9.5 Total available power 9,300 kw x 450V 9.6 Emergency generator M200AL-SN, Yanmar, 560 kw x 450V x Emergency fire pump - type Vertical, centrifugal, elect. Motor driven Delivery pressure 10.5 Bar Motive power 480 /h x 100 mth If electrical, - indicate power required 200 Kilowatts 9.8 Steering gear - type Electro-Hydro, Ram type, FE T050 Indicate power required to steer the vessel with one pump unit 125 Kilowatts A10 POWER/SPEED INFORMATION 10.1 Trial data BHP MRC Speed Draught BHP MRC Speed Draught 36,342 SHP Knots 9.5 Metres 32,922 SHP Knots 9.5 Metres A11 THRUSTERS 11.1 Make and type KT-219B3, C.P.P. type, KHI 11.2 Bow thruster (output) 2,000 Kilowatts 11.3 Stern thruster (output) N/A Kilowatts A12 FRESH WATER Capacity of distilled tanks Capacity of domestic tanks Distilled Daily consumption Domestic Daily evaporator capacity (Max.) 90 Gas Form-C Page 7

9 A13 BALLAST CAPACITIES AND PUMPS Tank Capacity () Number 13.1 Fore peak Wing and or side tanks Double bottom tanks 13.4 Aft peak Other: None None 13.6 Total Ballast pump make and type SHINKO IND.,LTD Elect.motor driven,rvd500-2mh 13.8 Number of pumps Total capacity 8400 M3/hour Location E/R Control location CCR Gas Form-C Page 8

10 A14 MOORING EQUIPMENT 14.1 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. Refer to the attached documents MOORING ROPES (ON DRUMS) Mooring Ropes (On Drums) Forecastle - Number 10 Diameter 44 mm. Material Galvanised Steel Length 275 Metres Breaking Strength Mooring Ropes (On Drums) Forward Main Deck - Number None Diameter mm. Material Length Metres Breaking Strength Mooring Ropes (On Drums) Aft Main Deck - Number 2 Diameter 44 mm. Material Galvanised Steel Length 275 Metres Breaking Strength Mooring Ropes (On Drums) Poop - Number 8 Diameter 44 mm. Material Galvanised Steel Length 275 Metres Breaking Strength OTHER MOORING LINES Mooring Ropes not on Drums - Number None Diameter mm. Material Length Metres Breaking Strength Emergency Towing Wires / Fire Wires - Number 2 Diameter 38 mm. Material Galvanised Steel Length 90 Metres Breaking Strength 200 Gas Form-C Page 9

11 14.2 MOORING WINCHES Forecastle - Number 5 Single Drum or Double Drums Double Split Drums Y/N Yes Motive Power Hydraulic Heaving Power 29.4 Brake Capacity 82.8 Hauling Speed 15 Metres/Min. Forward Main Deck - Number None Single Drum or Double Drums Split Drums Y/N Motive Power Heaving Power Brake Capacity Hauling Speed Metres/Min. Aft Main Deck - Number 2 Single Drum or Double Drums Double Split Drums Y/N Yes Motive Power Hydraulic Heaving Power 29.4 Brake Capacity 82.8 Hauling Speed 15 Metres/Min. Poop - Number 3 Single Drum or Double Drums Double Split Drums Y/N Yes Motive Power Hydraulic Heaving Power 29.4 Brake Capacity 82.8 Hauling Speed 15 Metres/Min ANCHORS AND WINDLASS Windlass motive power(e.g. steam, hydraulic) Hydraulic Hauling power 66.3 / Brake holding power Anchor type High Holding Power Stockless Anchor Weight Is spare anchor carried NO Cable diameter 117 mm. Number of shackles port cable 14 Number of shackles starboard cable TOWING ARRANGEMENTS Is the vessel fitted with a Towing Bracket Aft? YES If Yes, state SWL 200 Is Towing chain provided YES Dimensions of Towing wire Diameter 79 mm. Length 95 Metres 14.5 WINDAGE Windage on ballast draught End-on 1900 Squaremetres Lateral 8750 Squaremetres Gas Form-C Page 10

12 A15 NAVIGATIONAL EQUIPMENT 15.1 Magnetic compass YES 15.2 Off Course Alarm - Magnetic compass YES 15.3 Gyro compass YES Number of Units Off Course Alarm - Gyro compass YES 15.5 Gyro (Bridge) Repeaters YES Number of Units Radar 3cm YES 15.7 Radar 10cm YES 15.8 Are radars gyro stabilised? YES 15.9 Radar plotting equipment YES ARPA YES ECDIS YES Depth sounder with recorder YES Depth sounder without recorder YES Speed/distance indicator YES Doppler log YES Docking approach Doppler YES Rudder angle indicator YES Rudder angle indicator on Each Bridge Wing YES RPM indicator YES RPM indicator on Each Bridge Wing YES Controllable pitch propeller indicator NONE Thruster(s) indicator YES Rate of turn indicator YES Radio direction finder NO Navtex receiver YES GPS YES DGPS YES Transit SATNAV NO Decca navigator NO Omega NO Loran C NO Weather fax YES Sextant(s) YES Signal lamp ALDIS YES Anemometer YES Engine order recorder YES VDR (Voyage Data Recorder) YES Course recorder YES Are steering motor controls and engine controls fitted on bridge wings? NO Is bridge equipped with a 'Dead-Man' alarm? YES What chart outfit coverage is provided World-wide NO Limited YES If limited, - please indicate area(s) covered JP, Far E, NW Aus, W Eur, N Am Formal chart correction system in use YES Electronic Chart system in use NO Gas Form-C Page 11

13 A16 COMMUNICATIONS AND ELECTRONICS 16.2 What GMDSS areas is the vessel classed for? A1 A2 A3 A4 A1,A2 & A Transponder (SART) YES 16.4 EPIRB YES 16.5 How many VHF radios are fitted on the bridge? 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? Is vessel fitted with an INMARSAT satellite communications system? YES Does vessel carry at least three survival craft two-way radio telephones? YES Inmarsat satellite system YES Specify system type A, B or C B and C kHz bridge auto alarm YES Radio telephone distress frequency watch receiver YES Emergency lifeboat transceiver YES Can vessel transmit the helicopter homing signal on 410 khz? YES Full set of Radio List publications YES Gas Form-C Page 12

14 SECTION B CARGO SYSTEMS B1 CARGO - GENERAL INFORMATION 1.1 List products which the ship is Certified to carry LIQUEFIED NATURAL GAS Transport and Carriage Conditions 1.2 Minimum allowable tank temperature -163 elsius 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 NA contamination? 1.5 List the Number of grades that can be carried simultaneously and completely segregated without risk of NA contamination? 1.6 What is the Number of Products that can be conditioned by reliquefaction simultaneously? State the number of natural segregation's (NB: Separation must be by the removal of spools or the insertion of blanks) 4 B2 CARGO TANKS 2.1 Type and materials of cargo tanks Independent Spherical Aluminium 2.2 Maximum allowable relief valve setting 25kpaG Bar gauge IMO Setting 25kpaG Bar gauge 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 Gas Form-C Page 13

15 B3 CARGO TANK CAPACITIES Tank number / location 1 / FRAME No Capacity (100%) Capacity 98% Butane capacity Butane temperature Propane capacity Propane temperature Butadiene capacity Butadiene temperature Propylene capacity Propylene temperature Vinyl Chloride Monomer capacity Vinyl Chloride Monomer temperature Ethylene capacity Ethylene temperature Propylene Oxide capacity Propylene Oxide temperature Ammonia capacity Ammonia temperature Tank number / location 2 / FRAME No Capacity (100%) Capacity 98% Butane capacity Butane temperature Propane capacity Propane temperature Butadiene capacity Butadiene temperature Propylene capacity Propylene temperature Vinyl Chloride Monomer capacity Vinyl Chloride Monomer temperature Ethylene capacity Ethylene temperature Propylene Oxide capacity Propylene Oxide temperature Ammonia capacity Ammonia temperature Tank number / location 3 / FRAME No Capacity (100%) Capacity 98% Butane capacity Butane temperature Propane capacity Propane temperature Butadiene capacity Butadiene temperature Propylene capacity Propylene temperature Vinyl Chloride Monomer capacity Vinyl Chloride Monomer temperature Ethylene capacity Ethylene temperature Propylene Oxide capacity Propylene Oxide temperature Ammonia capacity Ammonia temperature Gas Form-C Page 14

16 Tank number / location 4 / FRAME No Capacity (100%) Capacity 98% Butane capacity Butane temperature Propane capacity Propane temperature Butadiene capacity Butadiene temperature Propylene capacity Propylene temperature Vinyl Chloride Monomer capacity Vinyl Chloride Monomer temperature Ethylene capacity Ethylene temperature Propylene Oxide capacity Propylene Oxide temperature Ammonia capacity Ammonia temperature Tank number / location Capacity (100%) Capacity 98% Butane capacity Butane temperature Propane capacity Propane temperature Butadiene capacity Butadiene temperature Propylene capacity Propylene temperature Vinyl Chloride Monomer capacity Vinyl Chloride Monomer temperature Ethylene capacity Ethylene temperature Propylene Oxide capacity Propylene Oxide temperature Ammonia capacity Ammonia temperature Tank number / location Capacity (100%) Capacity 98% Butane capacity Butane temperature Propane capacity Propane temperature Butadiene capacity Butadiene temperature Propylene capacity Propylene temperature Vinyl Chloride Monomer capacity Vinyl Chloride Monomer temperature Ethylene capacity Ethylene temperature Propylene Oxide capacity Propylene Oxide temperature Ammonia capacity Ammonia temperature Gas Form-C Page 15

17 Tank number / location Capacity (100%) Capacity 98% Butane capacity Butane temperature Propane capacity Propane temperature Butadiene capacity Butadiene temperature Propylene capacity Propylene temperature Vinyl Chloride Monomer capacity Vinyl Chloride Monomer temperature Ethylene capacity Ethylene temperature Propylene Oxide capacity Propylene Oxide temperature Ammonia capacity Ammonia temperature Tank number / location Capacity (100%) Capacity 98% Butane capacity Butane temperature Propane capacity Propane temperature Butadiene capacity Butadiene temperature Propylene capacity Propylene temperature Vinyl Chloride Monomer capacity Vinyl Chloride Monomer temperature Ethylene capacity Ethylene temperature Propylene Oxide capacity Propylene Oxide temperature Ammonia capacity Ammonia temperature Total Capacity of all cargo tanks (100%) 147, Total Capacity of all cargo tanks (98%) 144, Total Capacity of Butane Total Capacity of Propane Total Capacity of Butadiene Total Capacity of Propylene Total Capacity of Vinyl Chloride Monomer Total Capacity of Ethylene Total Capacity of Propylene Oxide Total Capacity of Ammonia Gas Form-C Page 16

18 B16 DECK TANK CAPACITIES Are Deck pressure tank(s) fitted? Material of tank(s) Maximum allowable relief valve setting Deck tank number 1 - capacity (100%) Capacity 98% Propane Capacity Butane Capacity Propylene capacity Ethylene capacity Ammonia Capacity Deck tank number 2 - capacity (100%) Capacity 98% Propane Capacity Butane Capacity Propylene capacity Ethylene capacity Ammonia Capacity Bar gauge B4 LOADING RATES From Refrigerated Storage (Fully Refrigerated at Vessel's 4.1 Manifold) Butane - with vapour return Butane - without vapour return Propane - with vapour return Propane - without vapour return Butadiene - with vapour return Butadiene - without vapour return Propylene - with vapour return Propylene - without vapour return Ethylene - with vapour return Ethylene - without vapour return Ammonia - with vapour return Ammonia - without vapour return Vinyl Chloride Monomer - with vapour return Vinyl Chloride Monomer - without vapour return Propylene Oxide - with vapour return Propylene Oxide - without vapour return /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. 4.8 From Pressure Storage Butane 0 deg C - with vapour return /Hr. 0 deg C - without vapour return /Hr. 10 deg C - with vapour return /Hr. 10 deg C - without vapour return /Hr. 20 deg C - with vapour return /Hr. 20 deg C - without vapour return /Hr. Propane minus 30 deg C - with vapour return /Hr. Minus 30 deg C - without vapour return /Hr. Minus 20 deg C - with vapour return /Hr. Minus 20 deg C - without vapour return /Hr. Minus 10 deg C - with vapour return /Hr. Minus 10 deg C - without vapour return /Hr. 0 deg C - with vapour return /Hr. 0 deg C - without vapour return /Hr. 10 deg C - with vapour return /Hr. 10 deg C - without vapour return /Hr. 20 deg C - with vapour return /Hr. 20 deg C - without vapour return /Hr. Butadiene 0 deg C - with vapour return /Hr. 0 deg C - without vapour return /Hr. 10 deg C - with vapour return /Hr. 10 deg C - without vapour return /Hr. 20 deg C - with vapour return /Hr. 20 deg C - without vapour return /Hr. Gas Form-C Page 17

19 Propylene minus 30 deg C - with vapour return /Hr. Minus 30 deg C - without vapour return /Hr. Minus 20 deg C - with vapour return /Hr. Minus 20 deg C - without vapour return /Hr. Minus 10 deg C - with vapour return /Hr. Minus 10 deg C - without vapour return /Hr. 0 deg C - with vapour return /Hr. 0 deg C - without vapour return /Hr. 10 deg C - with vapour return /Hr. 10 deg C - without vapour return /Hr. 20 deg C - with vapour return /Hr. 20 deg C - without vapour return /Hr. Ethylene minus 100 deg C - with vapour return Minus 100 deg C - without vapour return Minus 95 deg C - with vapour return Minus 95 deg C - without vapour return Minus 90 deg C - with vapour return Minus 90 deg C - without vapour return Minus 85 deg C - with vapour return Minus 85 deg C - without vapour return /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. /Hr. Ammonia minus 20 deg C - with vapour return /Hr. Minus 20 deg C - without vapour return /Hr. Minus 10 deg C - with vapour return /Hr. Minus 10 deg C - without vapour return /Hr. 0 deg C - with vapour return /Hr. 0 deg C - without vapour return /Hr. VCM minus 10 deg C - with vapour return /Hr. Minus 10 deg C - without vapour return /Hr. 0 deg C - with vapour return /Hr. 0 deg C - without vapour return /Hr. 10 deg C - with vapour return /Hr. 10 deg C - without vapour return /Hr. 20 deg C - with vapour return /Hr. 20 deg C - without vapour return /Hr Special remarks: Gas Form-C Page 18

20 B5 DISCHARGING - GENERAL Cargo Pumps 5.1 Type of Pumps Electric motor driven centrifugal submerged 5.2 Number of pumps per tank Rate per Pump 1500 /hr 5.4 At Delivery Head mlc 175mTH mlc 5.5 Maximum density 0.5 Kg/ Booster Pump N/A 5.6 Type of Booster Pumps N/A 5.7 Number of pumps per tank 5.8 Rate per Pump /hr 5.9 At Delivery Head mlc mlc 5.10 Maximum density Kg/ Copies of pumping curves for cargo and booster pumps are enclosed? B6 DISCHARGE PERFORMANCE Full Cargo Discharge Times (using all cargo pumps) 14 Hrs Fully Refrigerated Manifold Back Press 1 kp/cm2, with vapour return Manifold Back Press 1 kp/cm2, without vapour return Manifold Back Press 5 kp/cm2, with vapour return Manifold Back Press 5 kp/cm2, without vapour return Manifold Back Press 10 kp/cm2, with vapour return Manifold Back Press 10 kp/cm2, without vapour return Pressurised Manifold Back Press 1 kp/cm2, with vapour return Manifold Back Press 1 kp/cm2, without vapour return Manifold Back Press 5 kp/cm2, with vapour return Manifold Back Press 5 kp/cm2, without vapour return Manifold Back Press 10 kp/cm2, with vapour return Manifold Back Press 10 kp/cm2, without vapour return B7 UNPUMPABLES 7.1 Tank number / location 1 11 Tank number / location 2 11 Tank number / location 3 11 Tank number / location 4 11 Tank number / location Tank number / location Tank number / location Tank number / location Total 44 B8 VAPORISING UNPUMPABLES 8.1 Process used Time to vaporise liquid unpumpables remaining after full cargo discharge of: 8.2 Butane 8.3 Propane 8.4 Butadiene 8.5 Propylene 8.6 Ethylene 8.7 Ammonia 8.8 Vinyl Chloride Monomer 8.9 Propylene Oxide Gas Form-C Page 19

21 B9 RELIQUEFACTION PLANT N/A 9.1 Plant Design Conditions - air temperature 9.3 Plant Design Conditions - sea temperature Plant Type 9.4 Is the plant single stage/direct? 9.5 Is the plant two stage/direct? 9.6 Is the plant simple cascade? 9.7 Coolant type Compressors 9.8 Compressor type Compressor makers name 9.9 Number of compressors 9.10 Capacity per unit /hr 9.11 Are they Oil Free? B11 CARGO TEMPERATURE LOWERING CAPABILITY (AT SEA WITH SEA TEMPERATURE +15C) Time taken to lower the temperature of: 11.1 Propane from -5 deg C to - 42 deg C 11.2 Propane from -20 deg C to - 42 deg C 11.3 Propane from -38 deg C to - 42deg C 11.4 Propane from +20 deg C to 0 deg C 11.5 Propane from 0 deg C to -20 deg C 11.6 Butane from +20 deg C to 0 deg C 11.7 Butane from +10 deg C to 0 deg C 11.8 Butane from +10 deg C to -5 deg C 11.9 Butadiene From +20 deg C to -5 deg C Propylene From -20 deg C to -47 deg C Ethylene From -100 deg C to -104 deg C Ammonia From -15 deg C to -33 deg C Vinyl Chloride Monomer From -5 deg C to -14 deg C B12 INERT GAS AND NITROGEN Main IG Plant 12.1 Type of system Oil burning type with cooling and drying unit 12.2 Capacity /hr 12.3 Type of fuel used Gas oil 12.4 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 Used for Cargo Tank, Hold Space, Liquid & Vapor Line Auxiliary IG or Nitrogen plant N2 Generator 12.7 Type of System Membrane permeation type 12.8 Capacity 60 /hr 12.9 Composition of IG - oxygen - % Composition of IG - CO2 - % Composition of IG - Nox - % Composition of IG - N2 97 % Lowest dewpoint achievable Used for Annuller Space, Liquid & Vapor Line Nitrogen N/A Liquid storage capacity Daily boil-off loss Maximum supply pressure - Kp/Cu. Cm Supply capacity - /hr Used for - Gas Form-C Page 20

22 B13 CARGO TANK INERTING/DE-INERTING Time taken to inert from fresh air to under 5% O2 at minus degree C? 13.2 Time taken to inert from cargo vapour to fully inert at minus 25 degrees dewpoint when IG density is less than product? Time taken to inert from cargo vapour to fully inert at minus 25 degrees dewpoint when IG density is greater than product? B14 GAS FREEING TO FRESH AIR 14.1 Plant used 14.2 Time taken from fully inert condition to fully breathable fresh air? IGG (Dry air mode) 30 B15 CHANGING CARGO GRADES Indicate number of hours needed to change grades from the removal of pumpables to tanks fit to load and the estimated quantity of Inert Gas and or Nitrogen consumed during the operation: Inert Gas Nitrogen From Propane to Butane From Propane to Butadiene From Propane to Ethylene From Propane to Ammonia From Propane to Vinyl Chloride Monomer From Propane to Propylene Oxide From Butane to Propane From Butane to Butadiene From Butane to Ethylene From Butane to Ammonia From Butane to Vinyl Chloride Monomer From Butane to Propylene Oxide From Butadiene to Propane From Butadiene to Butane From Butadiene to Ethylene From Butadiene to Ammonia From Butadiene to Vinyl Chloride Monomer From Butadiene to Propylene Oxide From Ethylene to Propane From Ethylene to Butane From Ethylene to Butadiene From Ethylene to Ammonia From Ethylene to Vinyl Chloride Monomer From Ethylene to Propylene Oxide From Ammonia to Propane From Ammonia to Butane From Ammonia to Butadiene From Ammonia to Ethylene From Ammonia to Vinyl Chloride Monomer From Ammonia to Propylene Oxide From Vinyl Chloride Monomer to Propane From Vinyl Chloride Monomer to Butane From Vinyl Chloride Monomer to Butadiene From Vinyl Chloride Monomer to Ammonia From Vinyl Chloride Monomer to Ethylene From Vinyl Chloride Monomer to Propylene Oxide From Propylene Oxide to Propane From Propylene Oxide to Butane From Propylene Oxide to Butadiene From Propylene Oxide to Ethylene From Propylene Oxide to Vinyl Chloride Monomer From Propylene Oxide to Ammonia Cargo Grade Change Operations that cannot be carried out at sea: Gas Form-C Page 21

23 B17 PRE-LOADING COOLDOWN The following questions ask the Time and Quantity of coolant required to cooldown cargo tanks from ambient temperature to fully gassed up state sufficient to allow loading to commence Propane - Quantity of Coolant Required Propane - Time required to cooldown cargo tanks from ambient temperature with vapour return line Propane - Time required to cooldown cargo tanks from ambient temperature without vapour return line 17.2 Butane - Quantity of Coolant Required Butane - Time required to cooldown cargo tanks from ambient temperature with vapour return line Butane - Time required to cooldown cargo tanks from ambient temperature without vapour return line Hrs Butadiene - Quantity of Coolant Required Butadiene - Time required to cooldown cargo tanks from ambient temperature with vapour return line Butadiene - Time required to cooldown cargo tanks from ambient temperature without vapour return line 17.4 Propylene - Quantity of Coolant Required Propylene - Time required to cooldown cargo tanks from ambient temperature without vapour return line Propylene - Time required to cooldown cargo tanks from ambient temperature with vapour return line 17.5 Ethylene - Quantity of Coolant Required Ethylene - Time required to cooldown cargo tanks from ambient temperature with vapour return line Ethylene - Time required to cooldown cargo tanks from ambient temperature without vapour return line Hrs Ammonia - Quantity of Coolant Required Ammonia - Time required to cooldown cargo tanks from ambient temperature with vapour return line Ammonia - Time required to cooldown cargo tanks from ambient temperature without vapour return line 17.7 VCM - Quantity of Coolant Required VCM - Time required to cooldown cargo tanks from ambient temperature without vapour return line VCM - Time required to cooldown cargo tanks from ambient temperature with vapour return line B18 VAPORISER 18.1 Type of Vaporiser Horizontral shell & tube, direct steam heated 18.2 Number of Vaporisers fitted Capacity per unit - Propane /hr Vap 18.4 Liquid Supply Rate /hr Liq 18.5 Delivery Temperature 18.6 Capacity per unit - Ammonia /hr Vap 18.7 Liquid Supply Rate /hr Liq 18.8 Delivery Temperature 18.9 Capacity per unit - Nitrogen /hr Vap Liquid Supply Rate /hr Liq Delivery Temperature B19 BLOWER 19.1 Type of Blower Electric motor driven 19.2 Rated Capacity 32,000 /hr 19.3 Delivery Pressure 203 kpaa Gas Form-C Page 22

24 B20 CARGO RE-HEATER 20.1 Type of Re-Heater Horizontral shell & tube, direct steam heated 20.2 Number Fitted Heating Medium Discharge rates with sea water at 15 degrees C to raise 20.4 product temperature of Propane from -42 degrees C to -5 /hr degrees C 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 /hr B21 HYDRATE CONTROL 21.1 Type of Depressant? Freezing point temperature? 21.2 Quantity of Depressant Carried? Ltr Means of injection? Name any other system used B22 CARGO MEASUREMENT Level Gauges 22.1 Are level gauges local or remote? Remote 22.2 Name of manufacture SAAB MARINE ELECTRONICS AB 22.3 Type Radar type level gauge 22.4 Rated Accuracy ± 5 mm Certifying Authority NK Temperature Gauges 22.6 Name of manufacture SAAB MARINE ELECTRONICS AB 22.7 Type Electric resistance type 22.8 Rated Accuracy ± 0.2 ( -165 ~ -140 ) ± 1.5 ( -140 ~ + 40 ) 22.9 Certifying Authority NK Pressure Gauges Name of manufacture SAAB MARINE ELECTRONICS AB Type Absolute pressure type Rated Accuracy 0.25 % F.S. (0.15kPaA) Certifying Authority NK Oxygen Analyser Name of manufacture Type What is the lowest level measurable? % Fixed Gas Analyser Name of manufacture Type Are Cargo tank calibration tables available? Name of Measuring Company Name of Certifying Authority Calibration calculated to cm? Calibration calculated to 1/2 cm? Tables established to cm? Tables established to mm? Tables established to "other" (state what other) Are trim and list corrections available? Are temperature corrections available? Are float gauge tape corrections available? Gas Form-C Page 23

25 B23 CARGO SAMPLING May cargo samples be obtained from the levels; top, middle 23.1 and bottom in all cargo tanks? If no, - the arrangement for sampling is limited to: At shore sampling facility 23.2 Can samples be drawn from tank vapour outlet? YES Can samples be drawn from manifold liquid line? YES Can samples be drawn from manifold vapour line? YES Can samples be drawn from pump discharge line? 23.3 State sample connection type Size of sample connection mm. Gas Form-C Page 24

26 B24 CARGO MANIFOLD Manifold arrangement diagram Center of manifold to bow M. Center of manifold to stern M. Dimension A 8,750 mm. Dimension B 8,000 mm. Dimension C (Please refer to our Ship/Shore Interface Plan) 6,000 mm. Dimension D 3,000 mm. Dimension E 3,000 mm. Dimension F 6,000 mm. Dimension G 8,000 mm. Dimension H 8,750 mm. Pipe Flange A - duty Fuel Oil Pipe Flange A - rating 10 bar Pipe Flange A - size 200 mm. Pipe Flange A raised or flat face Flat face Pipe Flange B - duty Gas Oil Pipe Flange B - rating 10 bar Pipe Flange B - size 100 mm. Pipe Flange B raised or flat face Flat face Pipe Flange C - duty Cargo Pipe Flange C - rating 10 bar Pipe Flange C - size 400 mm. Pipe Flange C raised or flat face Flat face Gas Form-C Page 25

27 Pipe Flange D - duty Cargo Pipe Flange D - rating 10 bar Pipe Flange D - size 400 mm. Pipe Flange D raised or flat face Flat face Pipe Flange V - duty Vapor Pipe Flange V - rating 10 bar Pipe Flange V - size 400 mm. Pipe Flange V raised or flat face Flat face Pipe Flange E - duty Cargo Pipe Flange E - rating 10 bar Pipe Flange E - size 400 mm. Pipe Flange E raised or flat face Flat face Pipe Flange F - duty Cargo Pipe Flange F - rating 10 bar Pipe Flange F - size 400 mm. Pipe Flange F raised or flat face Flat face Pipe Flange G - duty Gas Oil Pipe Flange G - rating 10 bar Pipe Flange G - size 100 mm. Pipe Flange G raised or flat face Flat face Pipe Flange H - duty Fuel Oil Pipe Flange H - rating 10 bar Pipe Flange H - size 200 mm. Pipe Flange H raised or flat face Flat face Height above uppermost continuous deck 4,000 mm. Distance from ship side 3,500 mm. Height above load waterline 19,149 mm. Height above light waterline 26,640 mm. Manifold Arrangement Located on Top of Compressor Distance from rail of compressor room/platform to presentation flanges Distance from deck of compressor room/platform/try to centre of manifold mm. mm. Gas Form-C Page 26

28 B25 CARGO MANIFOLD REDUCERS 25.1 Number of ANSI Class 300 reducers carried onboard NIL Flange rating of ANSI Class 300 reducer Size of ANSI Class 300 reducer Length of ANSI Class 300 reducer 25.2 Number of ANSI Class 300 to Class 150 reducers carried onboard Flange rating of ANSI Class 300 to Class 150 reducer Size of ANSI Class 300 to Class 150 reducer Length of ANSI Class 300 to Class 150 reducer 25.3 Number of ANSI Class 150 reducers carried onboard Flange rating of Class 150 reducer Size of ANSI Class 150 reducer Length of ANSI Class 150 reducer bar mm. mm. bar mm. mm. bar mm. mm. B26 CONNECTIONS TO SHORE FOR ESD AND COMMUNICATIONS SYSTEMS 26.1 Is ESD connection to shore available? If yes, is the system pneumatic? /NA If yes, is the system electrical? /NA If yes, is the system fiber optic? /NA 26.2 What is the type of connection used? Pneumatic / Electrical / Fiber Optic 26.3 Are ESD hoses or cables available on board? 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 Is there a connection available for a telephone line? 26.5 Are ESD connections available on both sides of vessel? Are ESD Fusible plugs fitted at tank domes? Are ESD Fusible plugs fitted at manifolds? Is the link compatible with the SIGTTO guidelines? Type of manifold valve Butterfly Closing time in seconds 24 secs Is closing time adjustable? Is Independent high level shut down system fitted(overflow control)? If yes, does the independent high level shutdown system also switch off running cargo pumps? /NA Shut down level % 99.7 % B27 MANIFOLD DERRICK/CRANE 27.1 Is manifold derrick provided NO 27.2 Is manifold crane provided YES 27.3 Is lifting equipment same for port and starboard? YES If no, then stipulate details 27.4 State SWL at maximum outreach Maximum outreach of lifting equipment 5 Metres B28 STORES DERRICK/CRANE 28.1 State location Accomodation SWL 7 B29 SISTER VESSEL(S) 29.1 Name of vessel IBRI LNG FUJI LNG Gas Form-C Page 27