FORM C GAS - Petredec

FORM C GASLPG CARRIERNIJINSKYCONSTRUCTED ATHyundai Heavy Industries16 February 2011

2A. VESSELS’ MAIN CHARACTERISTICSA.1. PREAMBLEName:NIJINSKYType:Flag State:Port of Registry:Owners:Technical Managers:LPG/CSINGAPORESINGAPORENIJINSKY SHIPPING CO.LTDBERNHARD SCHULTE SHIPMANAGEMENTCommercial Managers: PETREDEC LTDBuilding Shipyard:Hyundai Heavy IndustriesDelivered: Mar 26, 2008Classification Society: BUREAU VERITASClassification:BUREAU VERITASIceclass:Call Sign:XXX9VAX2Inmarsat ID - Code: Inmarsat C - 456 581 710Inmarsat B Voice - 764 839 283 / 764 839 284 / 764 839 285Fax - 764 839 286Tlx - 456 581 710 INM-CGross Tonnage: 16804Net Tonnage: 6561Email: master@nijinsky.bsmfleet.comSuez Canal Tonnage:GT-18178.56 / NT-14521.23 MTPanama Canal Tonnage: GT-14063 MTRina Inscription:IMO Type:Approval received from / for IMO, USCG, MOT, MARPOL, SOLAS2DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

3A.2. DIMENSIONS AND MAIN DATALength overall: 154.17 MMoulded Breadth: 25.524 MMoulded Depth: 16.00 MDeadweight: 16,967Full cargo (Ethylene)abt._ _N/A_____ tdwFull cargo (Ammonia)abt __ 16967 __ tdwFull cargo (VCM) abt._ 16536 __ tdwBallast abt.__ 8580 _ tdwDistance Keel - Top Antenna: 43 MDraft SW Summer : 8.8 MDraft FW Summer : 9.00 MDeadweightl: 16967 Freeboard: 7.20 MDeadweightl: 16968 Freeboard: 6.99 MTPC on Summer Draft basis Sea Water: 32.54Lightship Weight: 7965 TonsParallel Mid-Body Length on Ballast Draft: 56.8 MParallel Mid-Body Length on Summer Draft: 67.4 MSpeed at max. Bft. 2 and carrying a full cargo of Ethylene: N/ASpeed at max. Bft. 2 and carrying a full cargo of VCM: 16.0 KnotsCanal passages: 12.7 Knots Kiel15.1 Knots Suez12.7 Knots PanamaA.3.DECK MACHINERY EQUIPMENTDerricks / Cranes: Hose handling craneMaker: Oriental precision & engineering co., ltd.Hoisting Capacity: 5 tons S.W.LPROVISION CRANEHosting Capacity: 2.0 tons S.W.L -WindlassesMaker: PusnesDriven by: Electro – Hydraulic High pressureMaximum Pull:4,500 kg HHP3DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

4Mooring winchesMaker: PusnesDriven by: Electric powerMaximum Pull: 42.4 tonsA.4.MACHINERY EQUIPMENTMain Engine: Hyundai-B&WNumber of cylinders: 6Type: 6S50MC-C .Power: 9,4780Minimum Fuel Grade: 3.34 CSTAuxiliary Engines: HHI - EESNumber: 3 SETSType: HFC6 508-14KPower: AC 450 Volts 60Hz 2550 kilowatts(per engine) 720 RPM 850 kilowattsElectrical Current:Propeller: Keyless F.P.PType/Maker: HHI - EMDA.5.TANK CAPACITIESA.5.1. CARGO TANKS Tank Vol.100% Vol. 98%1 6757.77 6622.614(Volumes including tankdomes) 2 8713.912 8539.6343 7127.183 6984.639___________________Ttl 22598.865 22146.887DECK TANKSNo.: 1Size: 241.2 cu.mtr.Max. Pressure Setting: 18.2 bargSuitable for: C4 / VCMMinimum Cargo Temperature: -48 dec.CA.5.2. BUNKERA.5.3. BALLASTA.5.4.HFO : 1128.6 m3MDO: 228.6 m3Flanges located at cargo manifold aft.Storage capacity : 8851.4 m3Pumps : 2Capacity per unit: 400 m3/hr.Location : engine roomFRESH WATER4DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

5Capacity of domestic water tanks: 301 mtsGenerator: Sasakura Engineering , Average daily production abt 20 mts/dA.6.CONSUMPTIONA.6.1. SHIP AT SEA MAINTAINING CARGO TEMPERATURECargo: NH3Mean Draft: 8.8 MSpeed:16.0 KnotsOil consumption - HFO /M/E:Consumption M/E at 14 kts: 22 tonsConsumption M/E at 15kts: 26 tonsNo. aux. eng. needed : 2Oil consumption - MDO/A/E :NO MDO/MGO NEEDEDA.6.2. SHIP AT SEA COOLING DOWN CARGOCargo: NH3Draft: 8.8 MSpeed: 16.0 KnotsOil consumption - HFO /M/E: 33.6 tonsConsumption M/E at 14 kts: 23 tonsConsumption M/E at 15kts: 28 tonsNo. aux. eng. needed : 2Oil consumption - HFO/A/E : 5.0 tonsNo. ofGenerators Consumption- Generators Consumption- Loading ethylene at atmospheric pressure: N/A- Loading ethylene with cooling down: N/A- Loading LPG/VCM at atmospheric Pressure 3 7.5 tons/day- Nitrogen generator:A.6.2. SHIP IN PORTBoiler: - in port M.D.O / 0.0 MT/DAY- at sea M.D.O / 1.3 MT/DAYB. CARGO INSTALLATION MAIN CHARACTERISTICSB.1.TRANSPORTABLE PRODUCTS AND TRANSPORT CONDITIONS5DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

6THE GAS HANDLING AND RELIQUEFACTION PLANT IS PROVIDED FOR THETRANSPORTATION OF FOLLOWING LIQUEFIED GASES, THEIR SATURATED PRESSURE(ABSOLUTE) RANGING BETWEEN 1 AND 6 BAR AND THEIRSATURATED TEMPERATURE BETWEEN + 45° AND - 48° C.B.1.1. EXTRACT FROM THE LIST OF CARGOES FOR TYPE IIG CARRIER+ ANHYDROUS AMMONIA+ 1,3 BUTADIENE+ COMMERCIAL BUTANE (NORMAL AND ISO)+ BUTYLENE+ PROPANE+ COMMERCIAL PROPANE (MAX. 2.5 MOLE% ETHANE IN THE LIQUID PHASE)+ PROPYLENE+ VINYL CHLORIDE MONOMER ( AT REDUCED FILLING LIMITS)B.1.2. TRANSPORT CONDITIONSB.2.Fully refrigerated: Sea going 0.28 (g) IMO / Harbour 0.40 BAR(g) IMOSemi-refrigerated : BAR(g) IMO: BAR(g) USCGSIMULTANEOUS TRANSPORT OF DIFFERENT GRADESB.2.1. GRADES WHICH CAN BE TRANSPORTED SIMULTANEOUSLYTWO PRODUCTS AS PER B.1., ALL TWO RELIQUEFIED INSOFAR AS IMO REGULATIONSWILL BE OBSERVED.BOTH PRODUCTS CAN BE COOLED.MANIFOLD I OR MANIFOLD II CAN BE CONNECTED TO TK1/TK2: YESB.2.2GRADES WHICH CAN BE LOADED / DISCHARGED SIMULTANEOUSLYTWO GRADES CAN BE LOADED AND DISCHARGED SIMULTANEOUSLY: YES6DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

7B.3.TRANSPORTABLE PRODUCTS, RESPECTIVE QUANTITIES (MTS) AND CORRESPONDINGDRAFTPRODUCT d t TOTAL max draftAMMONIA 0.68 -33 15035 8.8 MButadiene 0.65 -5 14380 8.75 MPROPYLENE 0.61 -47 13480 8.65 MPROPANE 0.58 -42 12820 8.55 MVCM 0.97 -14 15325 8.80 MB.3.1. LOADING CAPACITY OF A FULL CARGO PROPYLENE AT DIFFERENT TEMPERATURESTemperature Density t/cbm Quantity mts (21.649 cbm (98%))-40 °C 0.61 13480-30 °C 0.61 13485-20 °C 0.61 13490-10 °C 0.61 13495d =t =density (mts/cbm)cargo temperature (degrees centigrade)quantities in mts excluding gas phase 98 % filling1 bar absolute pressure volume calculated including tank domeB.4.CARGO TANKS CHARACTERISTICSNumber of tanks: 6 (tk 1 p&s)(tk2 p&s)(tk3 p&s)Type: Independent type AMax. Tank Pressure IMO: Seagoing 0.28 barg Harbour 0.40 bargMax Tank Pressure USCG:Max. Permissible Vacuum: -0.10Min. Cargo Temperature: -48 deg.CMax. Cargo Density: 0.9700B.5.CARGO DECK TANKSNo.: 1Tank Size: 241.2 cbmMax. Pressure: 18.2 bargMin Cargo Temperature: -48 °C / Max. +45°CMax. Cargo Density: 0.972 kg/DM3B.6.LOADINGB.6.1. LOADING IN CBM/HR FROM A FULLY REFRIGERATED STORAGE WITHOUT COOLING DOWNButane 1264Propane 1216cbm/hrcbm/hr7DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

8Ammonia 1432cbm/hrVCM 570 cbm/hrPropene (Propylene) 1216cbm/hrB.6.2. LOADING IN CBM/HR FROM A SEMI-REFRIGERATED STORAGE AT A CARGO TEMPERATUREOF + 18°C ACCORDING IMO SAFETY VALVE SETTINGwithout vapour returnButane 700cbm/hrPropane 1000cbm/hrAmmonia 1000cbm/hrVCM 570 cbm/hrButadiene 570cbm/hrRELIQUEFACTION CAPACITIES ( IN KCAL/HR )Refrigerating CapacityPropylene at -42 °CAmmonia at -34 °CAmmonia at +10 °C_516___kcal/hr (direct cycle)_825_ _ kcal/hr (direct cycle)_______ kcal/hr (direct cycle)B.6.3. COOLING DOWN ETHYLENE AT SEA WATER TEMPERATURE OF + 20°CN/AB.6.4. COOLING DOWN PMG PROPYLENE AT SEA WATER TEMPEARTURE OF + 20 °CCOOLING DOWN A FULL CARGO OF POLYMER GRADE PROPYLENE STARTING AT -45°CWILL TAKE APPROXIMATELY 24 HOURS PER 3°C WITH ALL CARGO COMPRESSORS INOPERATION. YESB.6.5. HEAT LOSS DUE TO TANK INSULATION(INFORMATION NOT AVAILABLE)Average K-Value:K = kcal/m 2 h°CPropane at -42 °CAmmonia at -34 °CTank 1 Tank 2,B. 6.6. DISCHARGING(DISCHARGING IN GENERAL)against 120 m. L.C. against 240 m L.C.Propane 350 cbm/hr cbm / hr8DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

9Propene 350 cbm/hr cbm / hrButane 350 cbm/hr cbm / hrAmmonia 350 cbm/hr cbm / hrVCM 350 cbm/hr cbm / hrNo. of pumps able to work simultaneously: in series: 6in parallel: 6No. of Cargo Grades that can be discharged simultaneously: 2Time to discharge a full cargo using all pumps: 15 HRSADDITIONAL INFORMATIONNormal unpumpables at the end of unloading (at atmospheric conditions):Vapour mass/TankPropylene 18 mtsPropane 18 mtsButane 18 mtsAmmonia 18 mtsVCM 18 mtsB.7.CARGO WARMING UPNumber of heaters: 1Type: SShell and TubeHeating medium: Sea waterFrom saturated temperature at 1 bar abs to -2 °C (Sea water temperature abt. +18°C):Capacities: Propane 125 TE/hrPropene (Propylene) 135 TE/hrPropane / Butane mix. TE/hr (no cargo heater capacity curves available)B.8.LOADING / DISCHARGING LINES AND MANIFOLD ARRANGEMENTSB.8.1. CROSSOVERSequence of manifold from bow to stern: Liquid-Vapour-Vapour-LiquidLiquid connections (N'size): L1 : 14” x 300L2 : 10” x 3009DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

10Vapour connections (N'size): V1: 6” x 150V2 : 6” x 150Distance of centre of L1 from bow: 70.85 MDistance of centre of L1 from stern: 83.32 MDistance between center of L to center of V: 1.70 MDistance between center of V to center of L: 1.70 MDistance of manifold above deck: 1.428 MDistance of manifold from ship's side: 3.70 MDistance of manifold above waterline summer: 7.20 MDistance of manifold above waterline ballast: 10.04 MB.8.2.REDUCERSANSI Class 3001 off 16”NB 300# × 14”NB 300#1 off 14”NB 300# × 12”NB 300#1 off 14”NB 300# × 10”NB 300#1 off 14”NB 300# × 8”NB 300#1 off 12”NB 300# × 10”NB 300#1 off 10”NB 300# × 10”NB 300#1 off 10”NB 300# × 8”NB 300#1 off 10”NB 300# × 6”NB 300#ANSI Class 300 to Class 1501 off 16”NB 300# x 14”NB 150#1 off 14”NB 300# × 12”NB 150#1 off 14”NB 300# × 10”NB 150#1 off 14”NB 300# × 8”NB 150#1 off 12”NB 300# × 10”NB 150#1 off 10”NB 300# × 10”NB 150#1 off 10”NB 300# × 8”NB 150#1 off 10”NB 300# × 6”NB 150#ANSI Class 1501 off 12”NB 150# × 10”NB 150#1 off 10”NB 150# × 10”NB 150#1 off 10”NB 150# × 8”NB 150#1 off 10”NB 150# × 6”NB 150#1 off 8”NB 150# × 6”NB 150#1 off 6”NB 150# × 6”NB 150#1 off 6”NB 150# × 4”NB 150#1 off 6”NB 150# × 3”NB 150#10DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

11B.9.CARGO PUMPSPumps DEEP WELL BOOSTERNumber: 6Maker: Hamworthy Svanehoj A/SMax. density kg/cdm: 970 kg/m cu.mtr.Capa. cbm/h nominal:Location: Tank DomeSpeed RPM: 1785Driven by: E-MotorPower consumption: 180 kwB.10. CARGO COMPRESSORSCargo PropaneNumber: 3Maker: BURCHARDT COMPRESSIONType: 3 K 140 AOil Free: Oil free reciprocating compressorB.11. GAS FREEING AND INERTINGPRODUCING NITROGEN AND DRY AIR FOR GAS FREEING OF CARGO TANKS RESP. GASPLANT AND FEEDING THE HOLD SPACES.B.11.1.NITROGEN PLANTThe nitrogen production plant is based on an application of the pressure swing adsorption(PSA-process) and consists of four adsorbers which are filled with carbon molecular sieves.On board Inert gas generatorNitrogen PurityCapacity: 2000 m3 / hr.Dew point: -25 deg.CGas Composition: O2 : 0.5 vol%, CO2 : 14 vol%, CO : 100ppm,Sox : 1ppm, Nitrogen & Air balanceNitrogen: BalanceOxygen: BalanceDew point atmm HG: Below - 45 0 CDischarge pressure: 0.4 BargElectric Power Requirement: 440V, 3ph,60 HzCooling Water Requirement: Filtered sea water (mesh size 5 mm)11DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

12Dry Air Production Capacity:Nm 3 /HrB.11.2.NITROGEN BOTTLESNumber:Purpose:Capacity:Pressure:Nitrogen Manifold:kg eachbar (g)12DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

13B.12. MEASURING APPARATUSB.12.1.CARGO LEVELMAINNumber: 1 PER TANKReading: TANK DOME / CARGO CONTROL ROOMAccuracy: +/- 2MMSUBNumber:Reading:Accuracy: +/-B.12.2.CARGO TEMPERATURENumber: 1 PER TANK (TOP, MID ,BOT)DIGITAL TERMOMETER DISPLAYReading: TANK / CARGO CONTROL ROOM/BRIDGE : YESAccuracy: +/- 0.10 deg.CLocation: TOP ( 12356 mm), MID( 6969 mm), BOTTOM( 109 mm)B.12.3.CARGO TANK WALLNumber :Reading:Accuracy:Location:B.12.4.CARGO PRESSURENumber: 1PER TANK(LOW AND HIGH)Reading: TANK / CARGO CONTROL ROOM/BRIDGE: YESAccuracy: +/- 0.01 BARGB.13. SAMPLESB.13.1.GAS SAMPLESNumber: 1 PER TANKLocation:TANK DOMEB.13.2.LIQUID CARGO SAMPLESNumber: 1PER TANKLocation: BOTTOM (?? mm), MIDDLE (?? m ),TOP (?? m)(No details of measurement on the plan/drawing only the location)13DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE

14C. CREWC.1.CREW MANAGERBERNHARD SCHULTE SHIPMANAGEMENTC.2.CREW COMPLEMENTRankNo.Master 1Chief Officer 12nd Officer 13rd Officer 1Chief Engineer 12nd Engineer 13rd Engineer 1Gas Engineer 1Electrician 1Bosun 1FitterAble Seaman 3D/C 1Oiler 3E/C 1Cook 1Mess man 1Total Complement 21Additional parallel body informationDistances are based from manifold centre.Distances quoted are approximate.Ballast (approx 6.0m)Parallel body Fwd of manifold: 24.4 MParallel body Aft of manifold: 32.4 MSummer Draft (8.78m)Parallel body Fwd of manifold: 29.0 MParallel body aft of manifold: 38.4 M14DETAILS BASED ON FACTS AVAILABLE AT THE TIME & ARE GIVEN IN GOOD FAITH, BUT WITHOUT ANY GUARANTEE