GAS FORM-C. LOA LBP Breadth Depth Air draft (fm Summer LL) Draft (m)

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1 1. PREAMBLE Ship s name LPG/C MISR GAS Owners STERLING SHIP HOLDING S.A. Flag Registry ST. VINCENT & THE GRINADINES - KINGSTOWN Builder JOHN L. MEYER, PAPENBURG, GERMANY Delivery Class RUSSIAN REGISTER OF SHIPPING IMO No GT (International) 9367 NT (International) 2810 GRT (Suez) NRT (Suez) GRT (Panama) LWT (MT) Is vessel approved? USCG IMO NO 2. HULL Metres Feet LOA LBP Breadth Depth Air draft (fm Summer LL) Draft (m) Corresponding DWT Tropical Summer Winter TPC fully loaded (MT) 22.7 Estimated Mean draft with full bunkers and 98% cargo& full bunkers Cargo Mean draft (m) DWT displacement Ethene

2 Butane Propane Ammonia Butadiene VCM Propene Butene Prop.Oxide COMMUNICATION EQUIPMENT International call sign J8B2574 Radio station GR14 Inmarsat F77 - Telephone Telephone Telefax / Telex Inmarsat C / MMSI Cell phone master.misrgas@amosconnect.net 4. MACHINERY Main Engine Maker/model B & W 6K62EF MCR - Grade fuel used HFO 380 CST Auxiliaries Engines Type/Model HOLEBY, 8T23LH Maker B & W Output(KW/RPM) 3000 Generator (KW) 165 Grade fuel used GAS OIL 2

3 Speed Guarantee average loaded/ ballast speed (kt) 10.5 / 11.0 Draft at Guarantee average loaded/ ballast speed (m) 7.3/4.7 Consumption Consumption at sea Consumption at port Ballast condition Loaded Condition At port with c/ops. / without c/ops / 1.5 MDO Consumption alongside in port 3.2 Inert Gas plant when operating Boiler consumption(mt/day) 1.2 Permanent bunkers capacity(excl. daily service 98% HFO(MT ) 940 MDO(MT ) CARGO INSTALLATION Re-liquefaction plant Type 2-STAGE COMPRESSOR KA 140-2B Minimum temperature can maintain -48 DEG.C Tank No. Capacities 100% M 3 98%M 3 n-c4 -5 o C C30.582@ o C NH o C Butadien e -5 o C Total Carried Products BUTADIENE BUTANE BUTANE / PROPANE MIXTURE BUTYLENES PROPANE PROPILENE 3

4 Cooling before loading (for fully-refrigerated vessels what quantity of cargo is needed and which is the corresponding time to pre-cool the tanks and have them ready to load?) MT Hrs Propane - - Butane - - NH3 - - VCM CARGO TANKS Type C MARVS 4.8 BARS Maximum vacuum Minimum pressure Minimum temperature acceptable in tanks deg cent. Maximum Specipic Gravity Maximum Loading rate-m3/hr BUTANE=550MT/HR, PROPANE= 500MT/HR Number of deck tanks No. 1 P & S (100%) 3945 No. 2 P & S (100%) 4031 No. 3 P & S (100%) CARGO PUMPS Number/Type 6 / DEEPWELL 14M Maker Location Max permissible specific gravity Cargo remaining onboard in cargo tanks after total completion pumping Cargo remaining onboard in cargo tanks (heel) after completion pumping Total head when working in series with booster pump Booster pumps (number/type) Maker WORTHINGTON 2 PUMPS PER TANK 0.97 KG/M3 12 MT MLC 2 / 4XHA-123 WORTHINGTON 4

5 Stripping Stripping system Time required for all traces of liquid cargo Loading Rates Loading rate (storage tank at atmospheric pressure + vapor return) -BUTANE Loading rate (storage tank at atmospheric pressure) PROPANE* Loading rate (storage tank at atmospheric pressure) AMMONIA * Loading rate (storage tank at atmospheric pressure) BUTADIENE* Loading rate (pressurized storage tank without vapour return line) PROPANE Loading rate (pressurized storage tank without vapour return line) AMMONIA 700 MT/HR 500 MT/HR 500 MT/HR 385 MT/HR (*)Note: for pressure or semi-refrigerated vessels using the cargo heater with sea temperature +15 o C Time for discharging full cargo using all pumps against no backpressure With vapour return line (hours) Without vapour return line (hours) Discharging rate (atm) 1200 M3/HR 1200 M3/HR Discharging rate (1 bar) - - Discharging rate (5 bars) - - Discharging rate (10 bars) CARGO COMPRESSORS Number/Type : 3 / K-105-2F, oil free Maker/Model : Sulzer / 2 stages Total Swept volume : 2100 m3 Can re-liquefy VCM : Yes Ethylene Ammonia Refrigeration Capacity - - Suction pressure - - 5

6 9. INERT GAS SYSTEM Does the vessel use inert gas? Method - Maker BABCOCK Fuel used - Does the vessel produce inert gas? Type - Daily production - Composition of inert gas (Nitrogen) Garbon dioxide - Oxygen max. - Garbon monoxide max. - Hydrogen max. - Nitrogen - Soot - Suphur oxides max. - Dewpoint - State if any shore supply of liquid nitrogen may be required May be required for pumping tanks prior to loading butadiene and ammonia What quantity? M3 10. GAS FREEING Can this operation be carried out at sea? For LPG For NH 3 State method incl. all details INERT GAS / FM TOP TO BOTTOM AIR / FM BOTTOM TO TOP Advise time required and consumption of inert gas if any From LPG about 48 HRS From NH 3 about 6

7 Is the vessel equipped with inert gas blower? Capacity Ventilation fan 1200 M3/HR 1000 M3/HR 11. CHANGING GRADE Can this operation be carried out at sea? State method used and time required for charging from NH 3 to LPG and vice versa, to reach 50 ppm to previous cargo in tanks atmosphere, the tanks being dry and free of moisture (dewpoint plus 10 o C) From NH 3 to LPG Time required From LPG to NH3 Time required Can vessel reduce in tank atmosphere and gas installation concentration of previous cargo below 50 ppm? Method used, time required and extra shore supply if any How can it be checked that no liquid gas remain onboard NO CARGO HEATER Cargo Heater 2 Maker Type SHELL & TUBE Discharging rate for C3 & NH3 to be brought 200 MT/HR fm atmospheric pressure to -5 o S.W 15 o C State discharging rate for propane with 2.5 mol % ethane to be brought from -44oC to -5oC at sea temperature of 15oC 200 MT/HR 13. CARGO VAPORIZER In case of need of vapor gas during discharge, can vessel produce its own if no shore gas available? 7

8 14. REFRIGERATING APPARATUS It is independent of cargo? SW COOLING 15. MEASURING APPARATUS What gauges onboard Location and type Number of temperature sensors/gauges per tank Number of pressure sensors/gauges on tank LEVEL FLOAT IN EACH CARGO TANK SAMPLES Where samples can be taken? Are sample bottles available onboard? MANIFOLD/CARGO PUMPS 17. CARGO LINES Is vessel fitted with midship manifolds Number of lines on each side 2 Lines Configuration L-V-V-L Distance from cargo manifold to bow 69.1 Distance from manifold to stern 70.6 Height upper cargo manifold above main deck 1.17 Height above Summer Draft mark 9.39 Height upper cargo manifold waterline when LWT 12.1 Height upper cargo manifold above waterline when in ballast 11.1 Distance manifold from ship s rail 2.4 Distance between liquid lines 3.1 Distance between vapour lines 1.5 Distance between loading and vapour return connections 0.8 Is vessel fitted with stern discharge NO 8

9 Is vessel fitted with fore discharge NO Note: Above distances from center line of liquid and vapour crossovers Dimension of lines Diameter Flange size Liquid (P/S) 304.8mm/203.2mm 12 x300/8 x300 Vapour mm 6 x 150 Vapour mm 6 x 150 What reducers onboard Number Diameter Length Pressure rating X X X X X X X X X X X X LIFTING APPLIANCES Where situated Main deck Port/s Main deck Stbd/s Number and lifting capacity 3t 3t Max. distance from ship s side of lifting hook 2m 2m 9

10 Number and lifting capacity 1 Aft store crane 2t 19. HOSES For what products are hoses suitable Inert Gas / Air Venting Number Length Diameter Working pressure Flange 20. SPECIALFACILITIES How many grades can vessel segregate? 2 Grades Indicate systems Is vessel able to load/discharge two or more grades simultaneously? Can vessel sail with slack tanks? Is vessel fitted with purge tank? I & II NO All the above given in good faith and to the best of our knowledge. All times indicated in various operations are Owner s best estimates, and cannot be guaranted, as they will vary under different Operating conditions. UPDATED 01ST OF JANUARY

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