VESSEL PARTICULARS (FORM C) LPG/C GAS KAIZEN (last updated 19/09/2012) Specifications of the vessel and the gas installation which are representations by the Owners. (A) VESSEL S CHARACTERISTICS PREAMBLE Name : GAS KAIZEN Owner : GENEVE BUTANE INC., Flag : MARSHALL IS. Build : 1991 Date on Service : 1991 Class : BV IMO NR : 8818817 GRT International : 4691 T Suez : 5140.69 T Panama : 5302.10 T NRT International : 1407 T Suez : 3677.14 T Panama : Is vessel build according to USCG regulations? : YES RINA regulations? : YES Japanese regulation? : Has vessel received USCG approval? : RINA approval? : HULL LOA : 105.00 M LBP : 97.55 M Breadth : 15.10 M Depth : 9.95 M Summer Draft : 6.10 M corresponding to Summer DWT = 4380 T Multiple Draft N/A M corresponding to Multiple DWT = N/A Estimated draft with full cargo and full bunkers are as follows. Product Draft Fore (m) Draft Aft (m) Draft Mean (m) Corresponding Deadweight (t) Propane ( 98%) 5.54 6.07 5.81 3980 Butadiene (98%) 4.84 5.34 5.09 3000 VCM (98%) 5.50 6.50 6.00 4220 Butane (98%) 5.76 6.04 5.90 4090 Ammonia (98%) 5.10 6.23 5.67 3790 Propylene (98%) 5.46 5.72 5.59 3670 Propeller immersion : At draft Loaded At 6.10 m mean correspond. : 120 % At draft Ballast At 4.42 m mean correspond. : 85 % Form C TBA 1
COMMUNICATION EQUIPMENT Call letter : V7GZ6 Radio Station normally watched : GMDSS Radio MF/HF NBDP : YES Radio MF/HFTEL/DSC : YES VHF : YES Satellite Communication : YES ( SATCOM C, MINI-M ) MACHINERY Main Engine x 1. Type and make : WARTSILA ECHEVARRIA 8 R 32 D. Service power No of Cylinders Cyl Bore x Stroke : 4025 BHP 8 320MM x 350. Grade of fuel used : IFO 180 Auxiliaries Type and make 4R22 HF-C / WARTSILA DIESEL (Electrical) (Mechanical) MECHANICAL Grade of fuel used MGO No off 2 Emergency Gen Type LSB-225-M/4 No off 1 Bow Thruster Type : Power: DRV-315S-4/F35 250 BHP Boiler Type COMMODORE Evaporation 600 kg/h Max Design 11.5 kg/cm2 Pressure Feed Water Temp 60 C No off 1 Exhaust Economiser Type N/A Evaporation N/A No off N/A Air Compressors (Main) Type / HATLAFA W-55 No off 2 Air Compressors (Emergency) Type No off 1 Form C TBA 2 ABC-VA-30 (V-3) / DRIVEN BY ENGINE
Fuel Oil Purifier Type ALFA LAVAL-FCPX605TFD-24.60 No off 2 4700 L/H Lub Oil Purifier Type MMP x 304SGP-11-60 / ALFA LAVAL No off 2 2900 L/H Evaporator Type J-60-FACET 340 L/H Fresh Water Sterilizer Type F-75-2/1 TS125 VA 100 / FACET 35-45 L/min Fresh Water Mineraliser Type / F-75-2 / 5125 VA 100 Waste Oil Incinerator (IMO MEPC 76 (40)) Type IRL 30 / DELTA 50 L/H Oily Water Separator Type 1-OWS-1/4.4-15 FACET 1.0 M3/H Sewage Treatment plant Hot Water Set (Calorifier unit) Type RED FOX-RF 500 2450L No off 1 Steering Gear Type I-18 M 320 / 2 GM 620 / TENFJORD Duty 80 kp/cm2 Hydraulic pump unit 2 Speed In Moderate weather: (up to weather conditions Beaufort scale 4, Douglas sea state 3) About: 12.0 KNOTS CONSUMPTION/ DAY Main Engine HFO 12.5 MT/DAY (+/-5%) Auxiliary Engine MDO At Sea: Loading : Discharge : At anchor/idle : 2.4 MT/DAY (If 2 D/G running) (+/-5%) 1.2 MT/DAY (+/-5%) 2.4 MT/DAY (+/-5%) 1.2 MT/DAY (+/-5%) Permanent bunker capacity (100%) HFO : 386.23 M3 Diesel : 88.42 M3 Fresh Water : 108.0 MT Form C TBA 3
(B) CARGO INSTALLATIONS 1. Transportable products and respective quantities, calculated in accordance with IMO maximum filling formula. (Tonnes) 100% (CBM) 98% (CBM) NO.1 CARGO TANK 1516.580 1486.248 NO.2 CARGO TANK 584.730 573.035 NO.3 CARGO TANK 2008.510 1968.339 T O T A L 4109.820 4027.622 SPSV (bar g) Ref. Temp. (deg. C.) Density at (Ref. Temp.) Corresponding Quantity (MT) Commercial Propane 7.0-42 0.5816 2330.7 Butane (ISO-N-) 7.0-4 0.6000 2415.6 Anhydrous Ammonia 7.0-33 0.6800 2734.4 Propylene 7.0-48 0.6136 2413.0 Butadiene 4.8-5 0.6530 2611.1 Vinyl Chloride Monomer 7.0-15 0.9700 3900.9 Propane/Butane Mixtures 7.0 +45 0.5532 2342.0 Pentanes (All Isomers) 1.5 Pentene (All Isomers) 1.5 Butylene 4.8 Note(1): In case of USCG, propylene, propane and B/P mixtures are not to be carried except the vapour pressure of B/P mixtures is not more than 4.50 bar g, 4.75 kg/cm 2 @ 45 C Note(2): On and after, the pressure value in parentheses is shown as a conversion value Mixing ratio of above mentioned B/P mixtures is as follows: Butane 35 wt% and propane 65 wt% 2. Other transportable products ( NLS ) Ethylene Oxide/Propylene-Oxide Mixtures w/ Ethylene Oxide Content of not more than 30% by weight Vinyl Ethyl Ether Ethylamine/Mono-Ethylamine Isopropylamine Propylene Oxide Isoprene Diethyl Ether SPSV Ref. Temp. ( C.) Density at Ref. Temp. Corresponding Quantity (MT) 3. TANKS 3.1 Design pressure (Vapour) BV-IGC : 7.0 bar g - USCG : 4.8 bar g 3.2 Valve setting : 0.5 bar g / 1.5 bar g / 4.85 bar g / 7.0 bar g 3.3 3.4 Maximum vacuum obtainable Maximum Specific Gravity : : 50% 0.9700 3.5 Maximum temperature acceptable : +45 C 3.6 Minimum temperature acceptable : - 48 C 3.7 Hydrostatic Test Pressure : bar g 4. LOADING RATE (TONS/HOUR) For Full Cargo Parcels Ex-atmospheric storage with gas : 550 m3/hr Form C TBA 4
return Remarks: Ex-atmospheric storage without gas return Butane 0-30 : 500 m3/hr Propane 0 : 400 m3/hr Propane 20 : 360 m3/hr Propane 30 : 150 m3/hr 5. CARGO PUMPS 5.1 Type : DEEPWELL Make : KVAERNER EUREKA CLG 80 N4 How many : 5 Maximum specific gravity : 0.990 5.2 (CMB/Hour) : 110 M3/HR AT 120 m LC Two speed or variable speed : 65 kw / 1780 RPM Rated kw (each) Working pressure maximum : 20 BAR 5.3 Location : CARGO TANK DOME Removable : NO 5.4 Booster pumps : YES Type : CENTRIFUGAL Maker : KVAERNER EUREKA CP 80L 5.5 (CMB/Hour) : 220 M3/HR AT 120 m LC Working pressure : 20 BAR 5.6 Location : MAINDECK P/S NEAR MANIFOLD AREA 5.7 Time to discharge a full liquid cargo using all pumps against back pressure at pump 1 bar : about 10 hours for LPG 5 bars : about 15 hours for LPG 10 bars : About 20 hours for LPG 5.8 Nominal back pressure when working : about 1 bar In series corresponding head : N/A Maximum back pressure : about 5 bar Nominal pressure at rail (propane) : about 13 bar at 20 degree C of cargo temperature 5.9 What amount of cargo remains in tanks after completion pumping before stripping: - liquid : About 0.12m3 per tank (total 0.36m3) - vapour : Approx. 4000 m3 6. STRIPPING 6.1 Stripping system, if any : YES 6.2 Time required to remove all traces of liquid cargo as stated in 5.9 for: - LPG : About 6 hours 7. CARGO COMPRESSORS Form C TBA 5
7.1 Type : SULZER 2K-105-2F Make : SULZER GERMANY How many : 3 Piston displacement Rated Kw 150 kw Stroke Max discharge pressure 20 bar Pressure differential Normal 3.2 to 4.0 bar No of Revolutions 710 rpm 7.2 Are compressors oil free : YES 7.3 Can they reliquefy VCM without risk : YES 7.4 State time to bring full cargo of butane to atmospheric pressure from : FROM +20 C TO -0.5 C = 75 HRS FROM +10 C TO -0.5 C = 50 HRS 8. INERT GAS SYSTEM 8.1 Does the vessel use inert gas? : YES If so, state utilization and quantities : GAS FREEING / MIN. 6000M3 8.2 Can the vessel produce inert gas? : YES If so, state type and composition of gas produce: INERT GAS NITROGEN O2 max CO max CO2 max H2 SO2 max NOx max N2 Soot Dewpoint Discharge Discharge Pressure 0.5-0.2% vol 0.5 0.2% vol 200 1000 ppm 200 1000 ppm 14.0% vol 100 ppm 200-1000 ppm 200-1000 ppm 10 ppm 10 ppm 100 ppm 100 ppm Balance balance 0 0-40 C -40 C (at 760mm HG) (at 760mm HG) 400 m3/hr 240 m3/hr 5 bar gauge 5 bar gauge 8.3 Maximum production obtainable NOTE:- Above quantities obtained at engine room temperature 45 C 8.4 State if there are storage facilities for inert gas onboard: N/A - Size : N/A - Pressure : N/A 8.5 State if any shore supply of nitrogen may be required: : YES - for what purpose : GAS FREEING - what quantities : 8000 M3 Form C TBA 6
9. GAS FREEING 9.1 State method used giving all details : IGG Plant / Fans 9.2 State time required including stripping : About 72 hours 10. CHANGING GRADE 10.1 From completion discharge of cargo Propane, time required in hours and inert gas in CBM required to reach a tank and gas installation atmosphere of less than 100 ppm of Propane in Vapour phase. Time required: about 72 hours 10.2 Can this operation be carried out at sea? : YES 10.3 Can the ship measure the number of ppm in vapour phase? : YES 10.4 Has vessel deck tank for changing grade/cooling operations? : NO 10.5 Deck tanks : NIL : NIL Purpose : NIL 11. COOLING CAPACITY LPG : CONDENSER 11.1 Maker / Type VILLA SCAMBIATORI / Horizontal Shell & Tube 11.2 Flow 220 m3/hr 11.3 Surface area 60.3 cm 11.4 Thermal SHELL 0/+150 C / TUBES 0/+45 C 11.5 Location COMPRESSOR ROOM 12. CARGO HEATER 12.1 Type : HORIZONTAL SHELL AND TUBE TYPE 12.2 Inside Diameter 69.44 cm 12.3 Overall length 78.76 cm 12.4 Cargo flow rate 220 m3/hr 12.5 Min Inlet Temp +1 C 12.6 Min Outlet Temp +5 C 12.7 Required Sea water 640 m3/hr 12.8 Design Pressure 27 bar 12.9 Hydrostatic Test Pressure 40.5 bar 12.10 Tightness Test Pressure 12.0 State discharging rate for propane to be brought from atmospheric pressure Loading rate for Propane 42 C /0 C: about 220 m3/hr For NH3 33 C /0 C: about 140 m3/hr 13. CARGO VAPORIZER In case vapour gas is needed to feed compressors, can vessel produce its own if no shore available: No 14. REFRIGERATING APPARATUS NA 14.1 Is it independent of cargo? : NA Is so, state cooling agents : NA 14.2 What minimum temperature can be maintained : NA 14.3 What time required at sea to lower by 1 o C the full cargo of : NA Form C TBA 7
15. MEASURING APPARATUS What gauges on board? Type : Float type level gauge Location : At each cargo tank dome 16. SAMPLES 16.1 State how tank atmosphere samples can be taken and where from? (98%, 50%, 0% ) TOP, MIDDLE, BOTTOM Standard of fitting? : GAS TIGHT COUPLING ½ NPT M 16.2 Same question for cargo : YES, OUT OF CARGO PUMP 16.3 Are sample bottles available on board? : NO 17. CARGO LINES 17.1 Is ship fitted with a port and starboard cargo manifold? : Yes 17.2 Position of cargo manifold - distance from stern (AP) (S / P) : 55 M - distance form stem (FP) (S / P) : 50 M - height above deck : 1.57 m for Liquid manifold - distance from ship s rail : 3.30 M - underside keel to manifold : 11.52 M 17.3 Liquid line Gas line - flange-size : 6 in. - type : ASA 300 RF - flange-size : 4 in. - type : ASA 300 RF 17.4 What reducers on board? : For Liquid line (low temperature) 6 ASA 150 3 ASA 300 6 ASA 300 4 ASA 150 6 ASA 300 6 ASA 150 6 ASA 150 6 ASA 300 6 ASA 300 8 ASA 300 6 ASA 300 8 ASA 300 8 ASA 150 6 ASA 300 8 ASA 300 6 ASA 150 10 ASA 300 6 ASA 150 For Vapor line (normal temp.) 2 ASA 150 4 ASA 300 4 ASA 300 2 ASA 150 4 ASA 300 4 ASA 150 4 DIN 300 4 DIN 150 17.5 Is ship fitted with stern discharge? NO Form C TBA 8
- Liquid line - diameter : N/A - flange size : N/A - type : N/A 18. HOSES Are serviceable hoses available on board? : None 18.1 : N/A Length : N/A Diameter : N/A Flange-size : N/A Type : N/A Bending radius : N/A 18.2 Minimum temperature acceptable : N/A Maximum pressure acceptable : N/A 18.3 For what products are hoses suitable?: N/A 19. DERRICKS - Hose cranes : YES - Where situated : PORT & STBD SIDE MANIFOLD - Lifting capacity : 3 T - Working radius : 4 M 20. SPECIAL FACILITIES 20.1 How many grades can be segregated? : 2 20.2 How many cooled? : 2 20.3 Can vessel sail with slack cargo tanks? : YES Form C TBA 9