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1
M.T “AQUAMARINE GAS”
GAS FORM C
SECTION A
GENERAL INFORMATION
NHAT VIET TRANSPORTATION CORPORATION
06-04-R2 the EverRich Bld, 968 3 thang 2 str, ward 15, Dict 11 - HCM City -VN
Tel: + 84. 8 .22251001 Fax: + 84.8 .22251004 Email: [email protected]
2
A1 PRINCIPAL SHIP PARTICULARS
1.1 Name of Ship : AQUAMARINE GAS
1.2 Registered Owner : Nhat Viet Transportation Corporation
1.3 Address : Office 06-04-R2,The EVERRICH Building, No.986 - 3 thang 2
street, W.15, D.11, HCM city, Vietnam
Telephone : (84) 08.22251001
Fax : (84) 08.22251004
1.4 Operator : Nhat Viet Transportation Corporation
1.5 Address : Office 06-04-R2 The EVERRICH Building, # 986 - 3 thang 2
street, W.15, D.11, HCM city, Vietnam
1.6 Telephone : (84) 08.22251001
Fax : (84) 08.22251004
1.7 Flag : VIETNAM
1.8 Port of Registry : SAIGON
1.9 Official No. : VNSG-1965-TG
1.10 Call Sign : 3WKN
1.11 Inmarsat C No. : [email protected]
1.12 IMO No. : 8514277
1.13 Previous Name(s) : JAPAN / KOSHIN MARU NO.10
1.14 Builder : JAPAN/ SHINHAMA SHIPBUILDING CO.,LTD
1.15 Date of Delivery : 1985 – RENOVATION 2004 -LEVEL 2SS (1995)
1.16 Classification Society : VIRES (Class No. VR 852215)
1.17 Gross Registered Tonnage : 1358
1.18 Net Registered Tonnage : 506
1.19 Was Ship built in accordance with the
following regulations –
Approval Received
IMO
USCG
RINA
YES YES
YES
YES
YES
YES
3
Other ( NKK )
1.19 IMO certification
Certificate of Fitness - IGC
- A328
- A329
Letter of Compliance
Issued by : VIRES
1.20 Date Questionaire Complied …………………………………………………………
A2 HULL DIMENSIONS
2.1 Length Overall : 71.50 m
2.2 Length Between Perpendiculars : 66.25 m
2.3 Extreme Breadth : 12.00 m
2.4 Extreme Depth : 5.40 m
2.5 Summer Draught : 4.699 m
2.6 Corresponding Deadweight : 1670 T
2.7 Light Displacement : 959.21 T
2.8 Loaded Displacement (Summer) : 1670 T
2.9 Cargo Tank Cubic Capacity (100% full): 1904 m3
2.10 Distance from Keel to Highest Point : 24.00 m
2.11 Air Draught (with normal ballast) : 19.31 m
A3 BALLAST PARTICULARS
Normal Maximum
3.1 Ballast Quantity (Salt Water) : 252 tonnes 405.19 tonnes
3.2 Bunkers, Stores, etc : 92.9 tonnes 125.18 tonnes
3.3 Draught – Forward : 2.43 m 4.91 m
– Aft : 3.74 m 4.12 m
– Mean : 1.31 m 0.79 m
NO YES
YES
YES
YES
NO
4
A4 IMMERSION
4.1 TPC – at Normal Ballast Draught : 5.23 tonnes @ 1.31 m.draught
– at Loaded Draught : 6.05 tonnes @ 4.52 m.draught
A5 LOADED PARTICULARS
Complete the following table:
5.1 Cargo:- Butane Propane Ammonia VCM
5.2 Density:- 0.596 0.583 N/A N/A
5.3
5.4
5.5
5.6
5.7
5.8
5.9
Cargo tones
Bunkers- FO tones
- DO tones
Fresh Water tones
Stores/ Spares tones
Lub Oil tones
Ballast tones
1112.00
98.14
27.04
106.00
14.78
4.42
300.0
1087.80
98.14
27.04
106.00
14.78
4.42
300.0
…………
…………
…………
…………
…………
…………
…………
…………
…………
…………
…………
…………
…………
………….
5.10 Deadweight tones 1662 1638 …… …………
5.11
Draught - Forward
- Aft
- Mean
4,12m
4,91m
4,52 m
4,12m
4,91m
4,52m
…… m
…… m
…… m
………. m
……… m
……… m
A6 PARALLEL MID- BODY DIMENSIONS
m m
m m
MANIFOLD
LOAD DRAFT
BALLAST DRAFT
m m
L.O.A 66.25 m
5
A7 BUNKER CAPACITIES *
7.1 M.E Fuel Oil – Grade : S/G : 0.96
– Capacity @ 98% : 103.00 m3
7.2 Diesel Oil – Grade : GASOIL SG. 0-8383
– Capacity @ 98% : 32.00 m3
A8 FUEL CONSUMPTION DETAILS *
8.1 At Sea (Normal Service Speed) FO : at 270 RPM 5.1 tonnes/day
DO : 0.6 tonnes/day
8.2 In Port, Loading DO : 0.9 tonnes/day
8.3 In Port, Discharging DO : 1.2 tonnes/day
8.4 In Port, Idle DO : 0.6 tonnes/day
(See also consumption Graph on the following page : N/A)
A9 MAIN ENGINE PARTICULARS *
9.1 Main Engine Make and Type HANSHIN DIESEL - GEL32
9.2 No. of Units 6
9.3 Maximum Continuous Rating (MCR) per
Engine 2100 SPH@ 285 RPM
9.4 Total Available Power 2100 HP
9.5 Normal Service Power (85%) 1785 x 270 RPM
A10 AUXILIARY PLANT
10.1 Make and Type of Auxiliary Generators No 01 & No 02 YANMAR S165L – T
P/G: YANMAR 4 K DL
10.2 No. of Units 02
10.3 Maximum Generation Output unit 300 PS
10.4 Total Available Power 695 PS
A11 POWER/SPEED INFORMATION
11.1 Trial Data BHP 2100 PS
MCR 2100 SHP
6
Speed 12.5 knots
Draught 4.699 m
11.2 Normal Service Speed BHP 1785 PS
Speed 11.0 knots
Draught 4.50 m
A12 THRUSTERS (N/A)
12.1 Make and Type …N/A………..
12.2 No. Installed ……………
12.3 Location and Rated Bolled Pull ……………
A13 FRESH WATER
13.1 Capacity of Distilled Tanks N/A m3
13.2 Capacity of Domestic Tank N/A m3
13.3 Daily Consumption – Distilled …………… tonnes
13.4 – Dometic 1.70 tonnes
13.5 Daily Evaporator Output …………… tonnes
A14 BALLAST CAPACITIES AND PUMPS
Complete the following table:
Tank Capacity (m3)
14.1
14.2
14.3
14.4
14.5
Fore Peak
Wing or Side Tanks
Double Bottoms
Aft Peak
Other (…………………………….)
25.16
77.30
249.52
43.33
14.6 Total 395.31
14.7 Ballast Pump Make and Type VMQ – M/50
DAITO PUMP KOGYO Co., Ltd
7
14.8 No. of Pump 1
14.9 Total Capacity 120/50 m3/hr
14.10 Location ENGINE ROOM
14.11 Control Location ENGINE ROOM
A15 MOORING EQUIPMENT
15.1 ROPES and WIRES
On the diagram below indicate the position of Winch Mounted Wires (W) and Ropes (R) together
with Open (O) and Closed (C ) Fairleads
Mooring Wires (On Drums) Morring 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
Forecastle 2 50mm 147
For’d Main Deck
Aft Main Deck 2 50mm 147
Poop 1
8
Other Mooring Lines
No. Type Dia Length MBL
Mooring Wires not on Drums
Mooring Ropes not on Drums 4 50mm 147
Emergency Towing Wires (Fire Wires) 1 6x24 185
MOORING WINCHES
Poop 2 D No Hydraulic 30 KW
15.2 ANCHORS AND WINDLASSES
Windlass Motive Power (e.g. Steam, Hydraulic) Hydraulic
Hauling Power ……9.0 … tonnes
Brake Holding Power ……………… tonnes
Anchor Type ……………..
Weight ……………… tonnes
Is Spare Carried
Cable Diameter ……………. mm
No. of Shackles Port 6
No. of Shackles Starboard 7
15.3 TOWING EQUIPMENT
Is Ship fitted with a Towing Bracket Aft
If Yes, state SWL ……………… tonnes
Is Towing Chain provided
Dimensions of Towing Wire – Diameter ……………… mm
– Length ……………… m
No
Serving
Single or
Double
Drums
Split
Drums
(Yes/No)
Motive
Power (eg
Steam,
Hydraulic)
Heaving
Power
(tonnes)
Brake
capacity
(tonnes)
Hauling Speed
(m/min)
Forecastle 2 D No Hydraulic 37 KW 5t x 05m/min
For’d Main Deck
Aft Main Deck 4t x 20m/min
YES
YES
YES
9
15.4 WINDAGE
Windage on Ballast Draught – End-on ……………… m2
– Lateral ……………… m2
A16 NAVIGATIONAL EQUIPMENT
Is the following equipment fitted:
16.1 Magnetic Compass
16.2 Gyro Compass and Repeaters
16.3 Radars
16.4 Radar Plotting Equipment
16.5 ARPA
16.6 Echo Sounder
16.7 Speed/Distance Indicator
16.8 Doppler Log
16.9 Speed of Approach Doppler
16.10 Rudder Angle, RPM, Controllable
and Indicators
16.11 Rate of Turn Indicators
16.12 Radio D.F
16.13 Navtex Receiver
16.14 Satellite Navigator
16.15 Decca Navigator
16.16 Omega
NO
YES
YES
NO
NO
NO
NO
NO
NO
NO
NO NO
YES
NO
YES
NO
NO YES
10
16.17 Loran C
16.18 Sextant(s)
16.19 Signal Lamp (Aldis)
16.20 Course Recorder
16.21 Engine Order Printer
16.22 What Chart Outfit Coverage is Provided Worldwide
Or
Limited
If Limited, Indicate areas covered ASIA
……………
16.23 Formal Chart Correction System in use
A17 COMMUNICATIONS EQUIPMENT
Is the following equipment fitted
17.1 Radio Telegraph Main Transmitter including facility
to transmit on Radio Telephone Distress Frequency
17.2 Radio Telephone Main Receiver including facility to
receive on Radio Telephone Distress Freqency
17.3 Radio Telephone Distress Frequency Watch Receiver
17.4 Main Radio Antenna
17.5 Radio Telegraph Reserve Transmitter
17.6 Radio Telegraph Reserve Receiver
17.7 Reserve Radio Antenna
17.8 Are the Main and Reserve Installations electrically
separate and electrically independent of each other
17.9 Radio Telegraph Auto Alarm
17.10 2182 kHz Bridge Watch Receiver
17.11 Alarm Signal Generating Device
17.12 VHF Radio
17.13 Inmarsat Satellite Communications System
If yes, state Identification Number 457427210 / 457427211
NO NO
NO
NO
YES
YES
NO
NO
NO
NO
YES
NO
NO
NO
NO
YES
NO
NO
YES
NO
YES
11
17.14 Telex
If yes, state Identification Number 457427210 / 457427211
17.15 Telefax
If yes, state Identification Number ………………………………………………….
17.16 Weatherfax
17.17 EPIRBS
17.18 At least three Survival Craft two- way radio telephone
apparatus.
17.19 Emergency lifeboat Transmitter
17.20 Full set of Publications
NO
YES
YES
NO
NO
YES
12
SECTION B
CARGO SYSTEMS
13
B1 CARGO- GENERAL INFORMATION
1.1 List Products which the ship is certified LPG
to carry
Transport and Carriage Conditions
1.2 Minimum allowable tank temperature 0.00 oC
1.3 Maximum permissible tank pressure 15.6 Barg
1.4 List grades which can be transported 1 GRADE ONLY
simultaneously
1.5 List grades which can be loaded or 1 GRADE ONLY
discharged simultaneously
1.6 State natural tank segregations NONE
(NB. Separation must be by the removal
of spools or the insertion of blanks)
1.7 Number of products that can be conditioned N/A
by reliquefaction simultaneously
B2 CARGO TANKS
2.1 Type of Cargo Tanks STEEL-PLATEWELDING, HORIZONTAL
CYLINKAL TYPE WITH HEMISPHERICAL
AND PLATE
2.2 Maximum Allowable Relief Valve Setting 18.0 kg/cm2
2.3 Safety valve set pressure – if variable give 15.6 kg/cm2
rang for pilot valves
2.4 Maximum vacuum 0.00
2.5 Maximum cargo density 0.97 kg/m3
2.6 State any limitations regarding partially None
filled tanks
2.8 State allowable combinations of filled NO LIMITATIONS
and empty tanks
B3 CARGO TANK CAPACITIES
Complete the following table:
Tank Capacity
m3 (100%)
Butane Propane Ammonia VCM ………………… …………………
Tonnes oC Tonnes
oC Tonnes
oC Tonnes
oC Tonnes
oC Tonnes
oC
1 760 360 15 358 15
2 1.140 360 15 358 15
3
14
4
5
6
7
8
Total 1900 720 716
B4 LOADING RATES
4.1 From Refrigerated Storage: Product Rate (m3/hr)
With Vapour
Return
Without Vapour
Return
Butane 635 m3/hr Depending on
Shore Condition Propane 635 m3/hr
4.2 From Pressure Storage: Product Rate (m3/hr)
With Vapour
Return
Without Vapour
Return
Butane 0-30oC
600 m3/hr
Depending on
Shore Condition
Propane 0 o
C
10 oC
20 oC
30 oC
4.3 Special Remarks:
B5 DISCHARGING – GENERAL
Cargo Pumps
5.1 Types of pumps ELECTRIC MOTOR DRIVEN,VERTICAL CENTRIFUGAL
DEEP- WELL TYPE
5.2 Number per tank 1
5.3 Rate (per pump) 400 m3/hr
5.4 Delivery head mlc
5.5 Maximum density 12 (120m) kg/m3
Booster Pump
5.6 Type of pump DH – M15
5.7 Number per tank No 2 P,S TANK ( FO)
5.8 Rate (per pump) 0.7 m3/hr
5.9 Delivery head ……………………… mlc
15
5.10 Maximum density 0,57………………… kg/m3
Pumps Curves
Insert in the space below copies of pumping Curves for cargo Pumps and Booster Pumps:
B6 DISCHARGE PERFORMANCE
Fulll Cargo Discharge Times (using all main pumps):
6.1 Fully Refrigerated:
Manifold Back
Pressure
Hours
With Vapour Return Without Vapour
Return
6.2 1 Bar
6.3 5 Bar
6.4 10 Bar
6.5 Pressurized:
Manifold Back
Pressure
Hours
With Vapour Return With Vapour Return
6.6 1 Bar N/A 5
6.7 5 Bar OK 5
6.8 10 Bar OK 10
B7 UNPUMPABLES
Tank No 1 2 3 4 5 6 7 8 Total tonnes
7.1 Vapour 16 25 41
7.2 Liquid 396 583 979
7.3 Total liquid vapour 1020
B8 VAPORISING UNPUMPABLES
8.1 Process used time to vaporise liquid ……………………………
unpumpables remaining after cargo discharge
8.2 - Propane …………………………… hrs
8.3 - Butane …………………………… hrs
8.4 - Ammonia …………………………… hrs
16
B9 RELIQUEFACTION PLANT (N/A)
9.1 Plant design conditions – Air temperature …………………………… oC
9.2 – Sea temperature …………………………… oC
Plant Type
9.3 Single stage/direct
9.4 Two stage/direct
9.5 Simple cascade
9.6 Coolant type ……………………………
Compressors
9.7 Type LPGOS – 97A, VERTICAL ONE STAGE WATER COOLED
9.8 Number 2
9.9 Capacity (per unit) 460 m3/hr
9.10 Are they oil- free
B10 COOLING CAPACITY ( N/A)
State Cooling Capacity (in kcal/hr) for-
10.1 Propane @ -42 oC ……………………… kcal/hr
10.2 @ -20 oC ……………………… kcal/hr
10.3 @ -5 oC ……………………… kcal/hr
10.4 Butane @ -5 oC ……………………… kcal/hr
10.5 …………… @ …… oC ……………………… kcal/hr
10.6 …………… @ …… oC ……………………… kcal/hr
B11 CARGO TEMPERATURE LOWERING CAPABILITY (AT SEA)
Time taken to lower the temp. of:
11.1 Propane from …… oC to -42
oC ……………………… hrs
11.2 -5 oC to -42
oC ……………………… hrs
11.3 -38 oC to -42
oC ……………………… hrs
11.4 +20oC to -0.5
oC ……………………… hrs
11.5 +10oC to -0.5
oC ……………………… hrs
11.6 Butane from +20oC to -0.5
oC ……………………… hrs
11.7 +10oC to -0.5
oC ……………………… hrs
11.8 +10oC to -5
oC ……………………… hrs
11.9 …………from…………to……………… ……………………… hrs
11.10 …………from…………to……………… ……………………… hrs
11.11 …………from…………to……………… ……………………… hrs
11.12 …………from…………to……………… ……………………… hrs
NO YES
NO YES
NO YES
NO
17
B12 INERT GAS
Main I.G Plant
12.1 Type of System ………………………
12.2 Capacity ……………………… m3/hr
12.3 Composition of I.G ………………………
………………………
12.4 Lowest dewpoint achievable ……………………… oC
12.5 Used for ………………………
Auxiliary I.G. Plant
12.6 Type of System ………………………
12.7 Capacity ……………………… m3/hr
12.8 Composition of I.G ………………………
………………………
12.9 Lowest dewpoint achievable ……………………… oC
12.10 Used for ………………………
Nitrogen
12.11 Liquid storage capacity ……………………… m3
12.12 Daily boil- off loss ……………………… m3
12.13 Maximum supply pressure ……………………… kg/cm2
12.14 Supply capacity ……………………… m3/hr
12.15 Used for ………………………
………………………
B13 CARGO TANK INERTING/DE- INERTING
WITH N2 FROM SHORE
13.1 Time taken from fresh air under 5% O2, at –25oC hrs
dewpoint
Time taken from cargo vapour to fully inert at
-25oC dewpoint when:
13.2 - I.G density less than product hrs
- I.G density greater than product ……………………… hrs
B14 GAS FREEING TO FRESH AIR
14.1 Plant used ………………………
14.2 Time taken from fully inerted condition
to fully breathable fresh air ……………………… hrs
18
B15 CHANGING CARGO GRADES
In the table below, show the number of hours needed to changed 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 VCM
From
Time
(hours)
I.G. used
(m3)
Time
(hours)
I.G. used
(m3)
Time
(hours)
I.G. used
(m3)
Time
(hours)
I.G. used
(m3)
Propane
Butane
Ammonia
VCM
Note any operation thet cannot be carried out at sea: ………………………………………
………………………………………
………………………………………
B16 DECK TANK CAPACITIES
16.1 Propane capacity 39 m3
16.2 Butane capacity 34 m3
16.3 Ammonia capacity 13 m3
B17 PRE-LOADING COOLDOWN
In 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
Product
Quantity of
Coolant
Required (m3
)
Time (hours)
With Vapour
Return Line
Without Vapour
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 ……………………………
19
18.3 Capacity (per unit) ………………………….. m3/hr Vapour
18.4 Liquid supply rate ………………………….. m3/hr Liquid
18.5 Delivery temperature …………………………… oC
B 19 BLOWER
19.1 Type of Blower …………………………………….
19.2 Rated capacity …………………… ……………… m3/hr
19.3 Delivery pressure …………………… ……………… kg/m2
B20 CARGO RE-HEATER
20.1 Tyre of Re-heater ………………………………………………
20.2 Number fitted ………………………………………………
20.3 Heating medium ………………………………………………
Discharge rates with sea water at 15oC to raise
Product temperture:
20.4 - for Propane from –42oC to –5
oC ……………………………………… m
3/hr
20.5 - for Ammonia from –33oC to 0
oC ……………………………………… m
3/hr
20.6 Cargo Heater Curve:
Seawater Density: 1.015t/m3
Back Pressure: 3-5 bars
20
20
18
16
14
12
Sea Water 10
Temperature
oC 8
6
4
2
20 40 60 80 100 120 140 160 180
Discharge Rate tonnes/hr
Ammonia/Propane Discharge @ -10oC
B21 HYDRATE CONTROL
21.1 Freezing point temperature of Depressant ………………………………………… oC
21.2 Quantity of Depressant carried …………metanol……………………………… litres
21.3 Means of injection …………………………………………
B 22 CARGO MESUREMENT
Level Gauges
22.1 Are level gauges local or remote
22.2 Manufactuer ENRAF NONRUS
22.3 Type m
22.4 Rated accuracy +/- 10 mm
22.5 Certifying authority SGS RED WOOD
Temperature Gauges
22.6 Manufacturer JAPAN
22.7 Type meter
22.8 Rated accuracy +/- 0.30o
C
22.9 Certifying authority Division for standardization metrology and quality
LOCAL REMOTE
21
Control of Hai phong city - Vietnam
Pressure Gauges
22.10 Manufacturer JAPAN
22.11 Type meter
22.12 Rated accuracy 1.5
22.13 Certifying authority Division for standardization metrology and quality
Control of Hai phong city - Vietnam
Oxygen Analyser
22.14 Manufacturer JAPAN
22.15 Type meter
Gas Analyser
22.16 Manufacturer JAPAN
22.17 Type meter
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
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 ………………………………………………..
YES
NO
NO
YES
22
B 24 CARGO MEASUREMENT
Complete the following table:
BOW …33….. m STERN 33 m
A B C D E F G H
16.6 m 7.10 m
16.70 m
16.75 m 7.25 m
16.8 m 7.30 m
Notes 1. Indicate liquid, vapour and Nitrogen lines
2. Indicate pipe groupings for separate systems
3. Indicate fuel oil connections
4. Indicate flange rating
5. Show any cross manifolding arrangements
6. Indicate distances from centreline of manifold
Pipe
Flange
Duty Rating Size Raised (R) or
Flat (F) Face
A Liquid 60-1800 mm Center
B Liquid 1730 – 3500 mm P’side S’side
C Vapour 3 4 F
D liquid 8 8 F
E vapour 4 4 F
F liquid 3430 – 5200 mm Center
G Liquid 5130 – 6900mm Center
H Liquid 6830 – 8600 mm Center
14.00
b
-------------
a 1050 a Height above uppermost
------------------ continuous deck 1.05 m
b Distance from ship’s side 1.4 m
c d c Height above load W/L 1.2 m
d Height above light W/L m
Load W/L ………
Light W/L ……………………
23
B25 CARGO MANIFOLD REDUCERS
State number of reducers carried on board and their
flange rating and size:
25.1 WHAT REDUCER ON BOARD ? ASA 8B x ASA 8B = 1 ANSI 300
ASA 6B x ASA 6B = 1 ANSI 300
ASA 6B x ASA 6B = 1 ANSI 300
ASA 5B x ASA 5B = 1 ANSI 300
ASA 6B x ASA 2B = 1 ANSI 300
B 26 MANIFOLD DERRICK/CRANE
26.1 Is manifold derrick provided
26.2 Is manifold crane provided
26.3 Is lifting equipment same port and starboard
If No, give detail ………………………………………………………………
26.4 State SWL at maximum outreach ……………………………………………………………… tonnes
B27 STONES HANDLING
27.1 Stones crane/derrick location and SWL ……………………………NIL………………..
………………………………………………………………
………………………………………………………………
YES
YES
YES