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ENGI 910B Project CourseEngineering Analysis (Design and Installation) of Oil & Gas Storage and Transportation Infrastructure in Arctic RegionAmit BhadrawaleDhawal PhadkeRami ChmouryVedang DuragkarVijay SonawaneSupervisor: Dr. Faisal KhanCoordinator: Dr. Syed ImtiazProject TA: Mr. Pushpinder RanaCONTENTSIntroductionSite GeologyProcess DesignMechanical DesignCost estimationEconomic FeasibilityHealth and SafetyMajor ChallengesConclusionReferencesSITE GEOLOGYPotential Reserves

Oil 1.4 Billion Barrel Gas 12.3 Trillion Cubic Feet

TRANS-ALASKA PIPELINEMACKENZIE VALLEY PIPELINEPROCESS DESIGNLIGHT OIL COMPOSITIONComponentsMole fractionC10.4624C20.0715C30.0478iC40.0083nC40.0202iC50.0074nC50.0103C60.0131C70.0212C80.0227C90.0141C100.0104C110.0093C120.0772C130.0087C140.0074C150.0065C160.0049C170.0056C180.0046C190.0044C200.0346C210C220C230C240C250C260C270C280C290C300CO20.0421H200.08425Temperature = 60 degrees.Pressure = 15 bars. Fluid considered = Light Oil Production Capacity = 40,000 Bbl/day or 6360 m3

PROCESS CONDITIONSPROCESS FLOW DIAGRAM

3D LAYOUT

SIZING OF SEPARATORSeparator 1 : Required Parameters

Density(gas)5.61843lb/ft^3UT0.332075021ft/secDensity(oil)41lb/ft^3Uv0.249056266ft/secDensity(water)62lb/ft^3Hold-up time5minWv29431410lb/hrSurge time3minWLL93254580lb/hrVH191515.1358ft^3WHL2782205.2lb/hrVS114909.0815ft^3QV1455.102523ft^3/secL/D (0