ship particulars
DESCRIPTION
Bente Kosan LNG carrierTRANSCRIPT
OCIMF SIGTTO
Ship Information Questionnairefor Gas Carriers1st Edition 2000
FORM - C
Oil Companies International Maritime ForumSocitety of International Gas Tanker & Terminal Operators Ltd
BENTE KOSAN
TABLE OF CONTENTS
SECTION A GENERAL INFORMATION Page
A1 Principal Ship Particulars 2 A2 Hull Dimensions 5 A3 Immersions 5 A4 Loaded Particilars 6 A5 Parallel Mid-body Dimensions 6 A6 Bunker Capacities 7 A7 Fuel Consumption Detailes 7 A8 Main Engine Particulars 8 A9 Auxiliary Plant 9 A10 Power/Speed Information 9 A11 Thrusters 10 A12 Fresh Water 10 A13 Ballast Capacities and Pumps 10 A14 Mooring Equipment 11 A15 Navigational Equipment 13 A16 Communications Equipment 15
SECTION B CARGO SYSTEMS
B1 Cargo - General Information 18 B2 Cargo Tanks 18 B3 Cargo Tank Capacities 19 B4 Loading Rates 19 B5 Discharging - General 20 B6 Discharge Performance 21 B7 Unpumpables 21 B8 Vaporising Unpumpables 21 B9 Reliquefaction Plant 22 B10 Cooling Capacity 22 B11 Cargo Temperature Lowering Capability (at sea) 23 B12 Inert Gas 24 B13 Cargo Tank Inerting/De-inerting 25 B14 Gas Freeing to Fresh Air 25 B15 Changing Cargo Grades 25
V
SECTION Page
B16 Deck Tank Capacities 26 B17 Pre-Loading Cooldown 26 B18 Vapouriser 26 B19 Blower 27 B20 Crago Re-Heater 27 B21 Hydrate Control 28 B22 Cargo Measurement 28 B23 Cargo Sampling 29 B24 Cargo Manifold 30 B25 Cargo Manifold Reducers 31 B26 Connections to shore for ESD and Communication System 31 B27 Manifold Derrick/Crane 32 B28 Store Handling 32
VI
SECTION A
GENERAL INFORMATION
1
A1 PRINCIPAL PARTICULARS
1.1. Date Questionnnaire Completed 23-Mar-07
1.2. Name of Vessel BENTE KOSAN1.3. LR/IMO Number 9196333
1.4. Last Previous Name
1.4.1. Date of Name Change
1.5. Second Last Name Change
1.5.1. Date of Name Change -
1.6. Third Last Name Change -
Date of Name Change -
1.7. Fourth Last Name Change -
1.7.1. Date of Change -
1.8. Flag Singapore
1.9. Port of Registry Singapore
1.10. Official Number 392854
1.11. Call Sign S6BE4
1.12. Inmarsat A or B Number
1.13. Vessel's Telephone Number 356 540 010
1.14. Vessel's Fax number 356 540 012
1.15. Vessel's Telex Number 356 540 014
1.16. Vessel's E mail Address [email protected]
1.17. Inmarsat C Number 456 540 010
1.18. Vessel's MMSI Number 565 400 000
1.19. Type of Vessel- Min Tank Temperature(1) Pressurised, 0 deg.C(2) Semi-Pressurised,(3) Refrigerated,
2
Max Tank Pressure1.77 Mpa
OWNERSHIP AND OPERATION
1.20. Registered Owner Lauritzen Kosan A/S
Full Address Sankt Annae Plads 28DK-1291 Copenhagen KDenmark
Office Telephone Number -
Office Fax number -
Office Telex number -
Office E mail Address -
Contact Person -
Contact Person and -Telephone Number After HoursNumber of Years Vessel Owned
1.21. Name of Operator (if Different from AboveUnigas Kosan Ltd.
Full Address 1006 Lippo Centre Tower 2
89 Queensway, AdmiraltyHong Kong
Office Telephone number 852-3102-5577
Office Fax number 852-3102-0577
Office Telex Number 79145 EXCO HX
Office E mail Address [email protected]
Contact Person Mr Jeremy Lee
Contact Person and 852-3102-5577Telephone Number After Hours
1.22. Number of Years As Vessel Operator
1.23. Total Number of Vessel Operatedby this Operator
3
BUILDER
1.24 Builder Murakami Hide Shipbuilding Co.,Ltd.
1.25 Name of Yard Vessel built at Japan
1.26 Hull Number S.No.502
1.27 Date Keel Laid 21st May.1998
1.28 Date Launched 27th Sept.1998
1.29 Date Delivered 08th Dec.1998
1.30. Date of Completion of Major Hull Changes(if any) N/A
1.31 If Changes were made, what changeswere made and at which Yardwere they carried out N/A
CLASSIFICATION
1.32 Classification Society Class NK
1.33 Class Notation NS* (18 kgf/cm3, 0 deg. C, Type II PG)and MNS*
1.34 If Classification Society Changed,Name of Previous Society -
1.35 If Classification Society Changed,Date of Changed -
1.36 Was Ship built in Accordance With the Following Regulations:- Approval Received
IMO
USCG
RINA
Other (………………..)
1.37 IMO CertificationCertificate of Fitness -IGC
A328
A329
Letter of Compliance
Issued By
1.38. Unattended Machinery Space Certificate N/A
4
YES NO YES NO
NO NO YES NO
NO YES
YES NO
YES NO
YES NO
YES NO
YES
YES YES YES
YES
YES
TONNAGES
1.39. Net Registered Tonnage 1,062
1.40. Gross Tonnage 3,540
1.41. Suez Canal Tonnage 3,155.86
1.42. Panama Canal Tonnage 3,032.00
A2 HULL DIMENSIONS
2.1. Length Overall 99.92 m
2.2. Length Between Perpendiculars 92.87 m
2.3. Distance Bow to Bridge 75.20 m
2.4. Diatance Bridge Front to Mid-Point Manifold 30.00 m
2.5. Distance Bow to Mid-point Manifold 45.20 m
2.6. Extreme Breadth 16.20 m
2.7. Extreme Depth 7.20 m
2.8. Summer Draught 4.814 m
2.9. Corresponding Deadweight 2,854.42 tonnes
2.10. Light Displacement 2,350.42 tonnes
2.11. Loaded Displacement 5,204.84 tonnes
2.12. Cargo Tank Cubic Capacity (100% full) 4,021.579 m3
2.13. Distance from Keel to Highest Point 33.45 m
2.14. Air Draught (with normal ballast) 29.20 m
A3 IMMERSION
3.1. TPC - at Normal Ballast Draught 11.8 tonnes @ 3.8 m.draught
- at Loaded Draught (Summer) 12.1 tonnes @ 4.814 m.draught
5
A4 LOADED PARTICULARS
Complete the folloing table:
Cargo: N-Butane Propane Butadiene VCM Ballast4.1. only
4.2. Density:- -
4.3. Cargo tonnes
4.4. Bunkers - FO tonnes
4.5. - 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
4.12. Aft
4.13. Mean
Remarks : The above figures shall be extracted from Stability Information Booklet. Actual loadable cargo quantity to be refered to Damage Stability Booklet.
A5 PARALLEL MID-BODY DIMENSION
To aft PP 54.72 m 45.20 m
33.46 m 29.20m
LOADED DRAFT (4.814 m)BALLAST DRAFT (4.32 m)
32.00 m 23.4 m16.50 m 18.33 m
LOA 99.92 m MANIFOLD
6
A6 BUNKER CAPACITIES
6.1 M.E.. Fuel Oil - Grade HFO180-R.W.No.1 1500sec
- Capacity@ 98% 473 m3
6.2 Diesel Oil - Grade MDO
Capacity@ 98% 162 m3
A7 FUEL CONSUMPTION DETAILS
7.1 At Sea (Normal Service Speed) - HFO-180 tonnes/day
- MDO tonnes/day7.2 At Sea (Normal Service Speed)
while conditioning cargo - HFO-180 tonnes/day
(for N2 Gen') - MDO tonnes/day
7.3 In Port,Loading - HFO-180 tonnes/day
- MDO tonnes/day
7.4 In Port, Discharging - HFO-180 tonnes/day
- MDO tonnes/day
7.5 In Port, Idle - HFO-180 tonnes/day
- MDO tonnes/day
(See also Consumption Graph on the following Page)
7
SPEED CONSUMPTION GRAPH
60
50
Consumption(tonnes/day) 40
30
20
11 12 13 14 15 16 17 18 19SPEED (Knots)
In the graph above, enter curves for both Loaded and Ballast conditions.(if necessary, amended consumption and speed scales to suit)
A8 MAIN ENGINE PARTICULARS
8.1 Main Engine Make and Type Akasaka Diesel LimitedA41
8.2 No.of Units 1 set
8.3 Maximum Continuous Rating (MCR) per Engine 3300PS @ 230 RPM
8.4 Total Available Power 2063 kw
8.5 Normal Service Power 2063 kw
8
A9 AUXILIARY PLANT9.1 Make and Type of Auxiliary Generators Yanmar S165-DT
9.2 No. of Units 2 sets
9.3 Maximum Generator Output per unit 1,200 RPM 309 kilowatts
RPM kilowatts
RPM kilowatts
9.4 Shaft Generator kilowatts
9.5 Total Available Powe 445 Volts 60 Hz 618 kilowatts
9.6 Emergency Generat 2,400 RPM 100 Volts 60 Hz 9.9 kilowatts
9.7 Emergency Fire PumpType Engine driven contrifugalDelivery Pressure 30 m3/h x 50mMotive Power Engine drivenif Electrical, Indicate Power Required in Kw
9.8 Steering GearType Electro-Hydraulic
Indicate Power Required in Kw
to Steer the Vessel with One Pump Unit 5.5 kw
A10 POWER/SPEED INFORMATION
10.1 Trial Data BHP
10.2 MCR RPM
Speed knots
Draught m
10.2 Normal Service Speed BHP KW
MCR RPM
Speed knots
Draught m
9
A11 THRUSTERS
11.1 Make and Type
11.2 No. Installed
11.3 Location and Rated Bollard Pull or Kw output / /
A12 FRESH WATER
12.1 Capacity of Distilled Tanks tonnes
12.2 Capacity of Domestic Tanks 149 tonnes
12.3 Daily Consum - Distilled tonnes
- Domestic about 6 tonnes
12.4 Daily Evaporator Output 10 tonnes
A13 BALLAST CAPACITIES AND PUMPS
Complete the following table:
Tank Capacity (m3 Number13.1 Fore Peak13.2 Wing or Side Tanks 13.3 Double Bottoms 13.4 Aft Peak13.5 Other (Deep Tank.)
13.6 TotalRemarks : Hopper Ballast Tanks to be entry in Wing Tanks column.
13.7 Ballast Pump Make and Type Centrifugal
13.8 No.of Pumps
13.9 Total Capacity m3/hr
13.10. Location Engine room
13.11. Control Location Engine room / Engine control room
10
each 210
0
1431.06
2
104.54790.20536.32
A14 MOORING EQUIPMENT
14.1 ROPES AND WIRESOn the diagram below indicate the position of Which Mounted Wires (W) and Ropes (R)together with Open (O) and Closed (C) Fairleads. Indicate also the position of mooring Bitts (B).
(O) (C) (C) (C) (O) (C)
(O) (O)
(O) (R) (R) (O)
(C) (R) (R) (C)
(O) (R) (R) (O)
(O) (R) (R) (O)
(O) (C) (C) (C) (O) (C)
Mooring Wire (On Drums) Mooring Wire Tails
No. Dia Length MBL No. Type Dia Length MBL
Forecastle
For'd Main Deck
Aft Main Deck
Poop
Mooring Ropes (On Drums)
No. Type Dia Length MBL
Forcastle 4 55
For'd Main Deck
Aft Main Deck
Poop 4 55
Other Mooring Lines
No. Type Dia Length MBL
Mooring Wires not on Drums
Mooring Ropes not on Drums PE 359
Emergency Towing Wires (Fire Wires)
11
359
359
48
24
PE
PE
200
200
2
2
200
50
14.2 MOORING WINCHES
No. Serving Split Motive Heaving Brake HaulingSingle or Drums Power Power Capacity Speed Double (Yes/No)(eg Steam (tonnes) (tonnes) (m/min) Drums Hydraulic)
Forecastle 2 Double No 5 15 15
For'd Main Deck
Aft Main Deck
Poop 2 Double No 5 15 15
14.3 ANCHORS AND WINDLASSES
Windlass Motive Power (eg. Steam, Hydraulic) HydraulicHauling Power tonnes
Breke Holding Power tonnes
Anchor Type
Weight tonnes
Is Spare Carried
Cable Diameter 46 mm
No. of Shackles Port 9
No. of Shackles Starboard 8
14.4 TOWING EQUIPMENT
Is Ship fitted with a Towing Bracket Aft
If Yes, state SWL tonnes
Is Towing Chain provided
Dimensions of Towing Wire - Diameter 34 mm
- Length 190 m
14.5 WINDAGE
Windage on Ballast Draught - End-on m2
- Lateral m2
12
760.00
820.00
Hydraulic
Hydraulic
9
53.7
Hall's patent anchor
YE NO
YES NO
YES NO
A15 NAVIGATIONAL EQUIPMENTIs the following equipment fitted:-
15.1. Magnetic Commpass
15.2. Off Course Alarm - Magnetic
15.3. Gyro Compass
Specify Number 1
15.4. Off Course Alarm - Gyro
15.5. Bridge Repeaters
Specify Number 4
15.6. Radar 3cm
15.7. Radar 10cm
15.8. Are Radars Gyro Satbilished
15.9. Radar Plotting Equipment
15.10. ARPA
15.11. ECDIS (Electric Display and Information System)
15.12. Depth Echo Sounder with Recorder
15.13. Depth Echo Sounder without Recorder
15.14. Speed/Distance Indicator
15.15. Doppler Log
15.16. Speed of Approach Doppler
15.17. Rudder Angle Indicator
15.18. Rudder Angle Indicator on Each Bridge Wing
15.19. R.P.M. Indicator
15.20. R.P.M. Indicator on Each Bridge Wing
15.21. Controllable Propeller Pitch Indicator
15.22. Thruster(s) Indicator
15.23. Rate of Turn Indicator
13
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
NO
y YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
15.24. Radio Direction Finder
15.25. NAVITEX Receiver
15.26. G.P.S
15.27. Transit SATNAV
15.28. DECCA Navigator
15.29. Omega
15.30. Loran C
15.31. Weather Fax
15.32. Sextant(s)
15.33. Signal Lamp ALDIS
15.34. Anemometer
15.35. Engine Order Recorder
15.36. Course Recorder
15.37. Are steering motor controls and engine controls fitted on bridge wings
15.38. Is Bridge Equipped with a "Dead Man" Alarm Equipment
15.39. What chart outfit coverage is provided
Worldwide
Limited
If limited Please Indicate Area Covered South East Asia
15.40. Formal Chart Correction System in use
15.41. Electronic Chart System in use.
15.21. Controllable Propeller Pitch Indicator
15.22. Thruster(s) Indicator
15.23. Rate of Turn Indicator
14
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YS NO
YES NO
YES NO
YES NO
A16 COMMUNICATIONS EQUIPMENTIs the following equipment fitted:-
16.1. Main Transmitted Including Radio TelephoneDistress Frequency
16.2. Main Receiver Including Radio Telephone DistressFrequency
16.3. Radio Telephone Distress Frequency Watch Receiver
16.4. Main Radio Antenna
16.5. Reserve Radio Antenna
16.6. Are the Main and Recerve Installations ElectricallySeparate and Electrically Independent of each other
16.7. 2182kHZ Bridge Auto Alarm
16.8. Alarm Signal Generating Device
16.9. VHF Radio(s)
Specify Number 2-sets
16.10. Portable VHF/UHF Radios
Specify Type and Number 4-sets
Are Sets Intrindically Safe
16.11. Inmarsat Satellite System B & C
Specify System Type A,B or C
16.12. Is the Ship Equipped as per GMDSS requirements
If yes, which area of operation is vessel certified to operate in A1 + A2 + A3
16.13. EPIRB
16.14. SARTS
16.15. Emergency Lifeboat Tansmitter
16.16. At least Three Survival Craft Two-Way Radio Telephone Apparatus
16.17. Full Set of Publications.
15
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
16
SECTION B
CARGO SYSTEM
17
B1 CARGO - GENERAL INFORMATION
1.1. List Products Which the Ship is Certified to Propylene, Propane, Butane,Carry Butadiene, VCM, B/P Mix,
Butylenes, Isoprene
Transport and Carriage Conditions
1.2. Minimum Allowable Tank Temperature ℃
1.3. Maximum Permissible Tank Pressure
1.4. List Grades which can be Loaded orDischarged Simultaneously
1.5. List Grades which can be TransportedSimultaneously
1.6. Number of Products that can be Conditioned N/Aby Reliquefaction Simultaneously
1.7. State Natural Tank Segregations N/A(NB. Separation must be by the removalof spools or the insertion of blanks)
B2 CARGO TANKS Independent Type - "C"
2.1. Type and materials of Cargo Tanks Carbon Manganese Steel
2.2. Maximum Allowable Relief Valve Setting
2.3. Safety Valve Set Pressure - if Variable GiveFilled Tanks
2.4. Maximum Vacuum
2.5. Maximum Cargo Density kg/m3
2.6. Maximum Rate of Cool - Down N/A ℃
2.7. State any Limitations Regarding Partially No cargo tanks should be loaded more than 98%Filled Tanks liquid full at reference temperature.
2.8. State Allowable Combinations of Filled and Empty Tanks
18
1.77 Mpa
0.69 Mpa
0.948
0
18
One (1) Grade
One (1) Grade
B3 CARGO TANK CAPACITY
Complete the Following Table (for example)
Capacity m3 N- Butane Propane VCM Propylene Butadiene Butylene Tank ( 100% ) Tonnes ℃ Tonnes ℃ Tonnes ℃ Tonnes ℃ Tonnes ℃ Tonnes ℃
1 1017.0 868.0 1695.0 917.0 45 1103.0 1058.0
2 1017.0 868.0 1695.0 917.0 45 1103.0 1058.0
Totals 4021.579 2034.0 1736.0 3390.0 1834.0 2206.0 2116.0 S.G 0.519 0.443 0.865 0.468 0.563 0.540
Remarks : Actual loadable quantity to be refered to Damage Stability Booklet. The specific gravity of cargo at the highest temperature which the cargo
may reach upon the termination of loading, during the transport, or at thedischarging under the ambient design temperature condition, should bedepending on the ship's service route.
B4 LOADING RATES4.1. From Refrigereted Storege:
Rate (tonnes/hr) With Vapour Without Vapour Return Return
4.2. Butane
4.3. Propane
4.4. Ammonia
4.5.
4.6.
4.7. (To be entry in case of Re-Heater installed.)
4.8. From Pressure Storage:Rate (tonnes/hr)
With Vapour Without Vapour Return Return
4.9. Butane 0-30℃ 360 250
4.10. Propane 0℃ 320 220
4.11. 10℃ 300 210
4.12. 20℃ 300 210
4.13. 30℃ 280 200
4.14. Special Remarks: 19
60
60
49
49
63
63
MARVS (1.77 MPa)
2012.247
2009.332
68
68
Product
Product
54
54
00 0 0
B5 DISCHARGING - GENERAL
Cargo Pumps
5.1. Type of Pumps Fixed deepwell pumps
5.2. Number Per Tank 1 set
5.3. Rate (per Pump) 300/250 m3/hr
5.4. Delivery Head 110 / 120 mlc
5.5. Maximum Density kg/m3
Booster Pump
5.6. Type of Pump
5.7. Number Per Tank
5.8. Rate (per pump) m3/hr
5.9. Delivery Head mlc
5.10. Maximum Density kg/m3
Pumping Curves
Insert in the space below copies of Pumping Curves for Cargo Pumps and Booster pumps:
CARGO COMPRESSOR
5.11 Type Water cooled Stage Double Acting Oilless Compressor
5.12 Number 2 set
5.13 Capacity (per unit) 460 m3/hr
5.14 Are they oil free? Yes
20
0.948
B6 DISCHARGE PERFORMANCE
Full Cargo Discharge Times (using all main pumps):
6.1 Fully Refrigerated:
Manifold Hours* Back Pressure With Vapour Without Vapour
Return Return
6.2 1 kP/cm2
6.3 5 kP/cm2
6.4 10 kP/cm2
* Indicate difference when manifold strainers are installed
6.5 Pressurized:
Mainfold Hours Back Pressure With Vaopur Without Vapour
Return Return
6.6 1 kP/cm2
6.7 5 kP/cm2 Depending on
6.8 10 kP/cm2 Shore Condition
B7 UNPUMPABLES
Tank No. 1 2 3 4 5 6 7 8 Totals m3
7.1 Liquid 0 0 0 0 0 0 0 0 0
B8 VAPOURISING UNPUMPABLES
8.1 Process usedTime to Vapourise Liquid Unpumpables Remaining After Full Cargo Discharge:
8.2 - Propane hrs
- Butane hrs
- Ammonia hrs
- …………… hrs
- ……………. hrs
- ……………. hrs
21
B9 RELIQUEFACTION PLANT
9.1. Plant Design Condition - Air Temperature ℃
- Sea Temperature ℃
Plant Type
9.3. Single Stage/Direct
9.4. Two Stage/Direct
9.5. Simple Cascade
9.7. Coolant Type
Compressors
9.8. Type and Makers Name
9.9. Number
9.10. Capacity (per unit) m3/hr
9.11. Are they Oil-Free
B10 COOLING CAPACITY
State Cooling Capacity (in kj/hr) for -
10.1. Propane @ -42 ℃ Kcal/hr
10.2. @ -20 ℃ Kcal/hr
10.3. Butane @ -5 ℃ Kcal/hr
10.4. @ -5 ℃ Kcal/hr
10.5. @ ℃ Kcal/hr
10.6. @ ℃ Kcal/hr
22
YES NO
YES NO
YES NO
YES NO
B11 CARGO TEMPERATURE LOWERING CAPABILITY (AT SEA WITH SEA TEMPERATU + 15 ℃ )
Time taken to lower the temp. of:
11.1. Propane from . . . ℃ - 42 ℃ hrs
11.2. - 5 ℃ to - 42 ℃ hrs
11.3. - 38 ℃ to - 42 ℃ hrs
11.4. + 20 ℃ to - 1 ℃ hrs
11.5. + 10 ℃ to - 1 ℃ hrs
11.6. Butane from + 20 ℃ to - ℃ hrs
11.7. + 10 ℃ to - ℃ hrs
11.8. + 10 ℃ to - ℃ hrs
11.9. from to hrs
11.10. from to hrs
11.11. from to hrs
11.12. from to hrs
23
B12 INERT GAS
Main I.G. Plant
12.1. Type of System Nitrogen Generator
12.2. Capacity 118 m3/hr @ 99.5% purity
12.3. Type of Fuel Used -
12.4. Composition of I.G.(O2 - Co2 - Co - Nox - N2)
12.5. Lowest Dewpoint Achievable Minus 65 DEG.C ℃
12.6. Used For Cargo Grade Changes
Auxiliary I.G. or Nitrogen Plant
12.7. Type of System
12.8. Capacity m3/hr
12.9. Composition of I.G.(O2 - Co2 - Co - Nox - N2)
12.10. Lowest Dewpoint Achievable ℃
12.11. Used For
Nitrogen Nitrogen for Tank padding to be mentioned in this section.
12.12. Liquid Storage Capacity m3
12.13. Daily Boil-Off Loss m3
12.14. Maximum Supply Pressure kP/cm2
12.15. Supply Capacity m3/hr
12.16. Used For
12.17. HP Nitrogen Nm3
24
B13 CARGO TANK INERTING/DE-INERTING(Experienced Data)
13.1. Time taken From Fresh Air to Under 5% O2 at -25 ℃ hrsDewpoint
Time Taken From Cargo Vapour to Fully Inert at - 25 ℃ Dewpoint when:
13.2. - I.G. Density less than Product hrs
- I.G. Density greater than Product hrs
B14 GAS FREEING TO FRESH AIR(Experienced Data)
14.1. Plant Used By Cargo Compressor
14.2. Time Taken from Fully inert Condition to FullyBreathable Fresh Air hrs
B15 CHANGING CARGO GRADES (Experienced Data)
In the table below, show the number of hours needed to change grades from the removal of unpumpables to tanks fit to load. Also indicate quantity of inert gas consumed during the operation:
To Propane Butane Ammonia VCMFrom Time I.G.Used Time I.G.Used Time I.G.Used Time I.G.Used
(hours) (m3) (hours) (m3) (hours) (m3) (hours) (m3)
Propane
Butane
Ammonia
VCM
Note any operation that cannot be carried out at sea
* Restrictions may apply.
( To be mentioned in case of Not installed Inert Gas /Nitrogen Generator)
25
62
170
30
B16 DECK TANK CAPACITIES
16.1 Propane Capacity m3
16.2 Butane Capacity m3
16.3 Ammonia Capacity m3
16.4 Maximum Allowable Relief Valve Setting kP/cm2
16.5 Lowest Permissible Temperature ℃
16.6 Materials
B17 PRE-LOADING COOLDOWNIn the table below,show time and quantity of coolant required to cooldown cargo tanks from ambient temperature and fully gassed up state sufficient to allow loading to commence.
Quantity of Time (hours)Product Coolant With Vapour Without Vapour
Required (m3) Return Line Return Line
17.1 Propane
17.2 Butane
17.3 Ammonia
17.4 VCM
B18 VAPORISER
18.1 Type of Vaporiser
18.2 Number Fitted
18.3 Capacity (per unit) - Propane m3/hr Vapour
18.4 Liquid Supply Rate m3/hr Liquid
18.5 Delivery Temperature ℃
18.6 Capacity (per unit) - Ammonia m3/hr Vapour
18.7 Liquid Supply Rate m3/hr Liquid
18.8 Delivery Temperature ℃
18.9 Capacity (per unit) - Nitrogen m3/hr Vapour
18.10. Liquid Supply Rate m3/hr Liquid
18.11. Delivery Temperature ℃
26
B19 BLOWER
19.1 Type of Blower
19.2 Rated Capacity m3/hr
19.3 Delivery Pressure kP/cm2
B20 CARGO RE-HEATER
20.1 Type of Re-Heater None
20.2 Number Fitted
20.3 Heating Medium
Discharge retes with sea water at 15℃ to raiseproduct temperature:
20.4 - for V.C.M from 14 ℃ to 0 ℃ m3/hr
20.5 - for PROPYLENE from 48 ℃ to 0 ℃ m3/hr
20.6 Cargo Heater Curve:
Seawater Density: Back Pressure :
28
26
24
22
20Sea WaterTemperaure 18
℃ 16
14
12
10
Loading Rate tonnes/hrAmmonia/Propane Dischar @ - 10 ℃
( In case of Pressurized Vessel to be changed to "LOADING")27
450250 300 350 40050 100 150 200
B21 HYDRATE CONTROL21.1. Type of Depressant with Freezing Point Temperature ℃
21.2. Quantity of Depressant Carried Litters
21.3. Means of Injection
Any other system used
B22 CARGO MEASUREMENTLevel Gauges
22.1. Are level gauges Loacal or Remote
22.2. Manufacturer Musashino Co., Ltd.
22.3. Type M-LMZ
22.4. Rated Accuracy 1 cm
22.5. Certifiying Authority Class/Owner/Service Comp
Temperature Gauges22.6. Manufacturer Hyoda Gauge Mfg. Co., Ltd.
22.7. Type S5.5-GT-M
22.8. Rated Accuracy ± 0.1℃
22.9. Certifiying Authority Class/Owner/Service Comp
Pressure Gauges22.10. Manufacturer Nagano Keiki
22.11. Type Bourdon's tube
22.12. Rated Accuracy
22.13. Certifiying Authority Class/Owner/Service Comp
Oxygen Analyser (portable)22.14. Manufacturer Riken Keiki
22.15. Type OX-62B
Lowest Level Measurable 0
Fixed Gas Analyser22.16. Manufacturer Tokai seiki Co., Ltd.
22.17. Type TS-303-PS
22.18. AreCargo Tank Calibration Table Available
22.19. Measuring Compaany
22.20. Certifiying Authority
22.21. Calibration Calculated to cm cm 1 mm
22.22. Tables Established to cm 1 cm mm
22.23. Trim and List Corrections Available
22.24. Temperature Correction Available
22.25. Float Gauge Tape Corrections Available
28
LOCAL REMOTE
YES NO
YES NO
YES NO
YES NO
YES NO
B23 CARGO SAMPLING
23.1. In the table below, indicate whether samples may be obtained from the levels specified:
Cargo Tank: - 1 2 3 4 5 6 7 8 Sample Level
Top
Middle
Bottom 0 0
23.2. Can samples be drawn from - Tank Vapour Outlet
- Manifold Liquid Line
- Manifold Vapour Line
- Pump Discharge Line
23.3. State Connection Type and Size 3/8" coupling
29
YES NO
YES NO
YES NO
YES NO
B24 CARGO MANIFOLD
Complete the following table:
BOW m STERN 54.72 m
A B C D E F G
2 m 1.5 m
m m
m m
Notes 1. Indicate liquid, vapour and Nitrogene lines2. Indicate pipe groupingd for separate system3. Indicate fuel oil connections4. Indicate flange rating5. Show any cross manifolding arrangements6. Indicate distances from centerline of manifold7. Indicate if manifold strainers can be installed if yes specify type and mesh
Pipe Duty Rating Size Raised (R) or Frange Flat (F) Face
ABC Vapor ANSI #300 5" RD Liquid ANSI #300 8" RE Vapor ANSI #300 5" RFGH
b
a
a Height above uppermost continuous deck 0.93 m
c b Distance from ship's side 2.60 m
d c Height above load W/L 2.42 m
LOAD W/L draft4.814 m d Height above light W/L 4.83 m
LIGHT W/L dra 2.41m c = To be entry Summer L/L Condition.d = To be entry Light Condition.
30
45.20
B25 CARGO MANIFOLD REDUCERS
State number of reducers carried on board and theirflange rating and size:
25.1. ANSI Class 300 8 x 6,5,4,8
5 x 6,4 3,2
25.2. ANSI Class 300 to Class 150 8 x 8,6,5,4,3
5 x 6,4,3,2
25.3. ANSI Class 300 to JIS 20kg/cm2
JIS20kg/cm2 to ANSI 300Lbs
BLIND FLANGE ANSI 300Lbs
B26 CONNECTIONS TO SHORE FOR ESD AND COMMUNICATIONS SYSTEM
26.1. Is ESD connection to Shore available
If yes which of the following systems are fitted: -
Pneumatic
Electrical
Fibre Optic
26.2. Type of Plug Used: -
Pneumatic
Electrical Intrincically Safe Type.
Fibre Optic
26.3. Is Hose or Cables Available on Board
Specify Length
Pneumatic
Electrical 30m
Fibre Optic
26.4. Is Connection Available for Telephone Line
26.5. Are Connections Available on Both Side of Vessel
31
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
YES NO
B27 MANIFOLD DERRICK/CRANE
27.1. I s Manifold Derrick Provided
27.2. I s Manifold Crane Provided
27.3. I s Lifting Equipment Same Port and Starboard
If No, give detailes Porable cargo hose rollers available
27.4. State SWL at maximum Outreach STBD : 4ton/6M
PORT : 0.9ton
B28 STORES HANDLING
28.1. Stores Crane/Derrick Location and SWL Navigation Deck
tonnes
32
0.9
YES
YES
NO
NO
YES NO