Lead Process Engineer ( Oil & Gas)

PFD DEVELOPMENT PID DEVELOPMENT Data sheets and specifications (equipment and instruments, piping special parts) Schedules (equipment list, line list, elec. load list) Inter-Discipline Checks IDC (plot plan, equipment layout, piping model / layout, isometrics, Data sheets of equipment, packages and instruments) Vendor data review for process equipment. Utility Flow Diagrams (UFD s), Process Safety Diagrams, Material Selection Flow Diagrams (MSD s), Pressure and Temperature Diagrams (PTD s) Utility demand calculation.

 

Mass balance and Heat Balance for process using hysys Checking/preparation of control valves calculation. Trip logic diagram/control Philosophy Preparation of CAUSE AND EFFECT DIAGRAM (BS-132/BS-131) for safe plant shut down. Material Request for Process Equipment.

 

Heat Exchanger design Sizing Preparing project reports, flow diagrams, layout, equipment specifications etc Surge analysis calculation. Hydraulic analysis for long distance pipeline Critical line sizing hydraulic and sizing validations. PUMP DESIGN/SIZING/SECLECTION HYDRAULIC : (CENTRIFUGAL/RECIPROCATING) Pumps hydraulic calculations (NPSHA,NPSHR,SHUT OFF, Power requirement)) calculation npsh Pumps hydraulic checks.

FLARE SYSTEM DESIGN: Complete network design like Basis for design Header network, Relief valve or safety valve sizing, Drum sizing and stack Sizing. (WITH EXAMPLE). Flare PSV load summary Blow down Depressurization calculations using Hysys Control philosophy ESD philosophy Flare load/header size reduction by taking appropriate credits as per API- Recommendations. Software:1) HTRI2) ASPEN HYSYS3) Aspen Flare Net4) Pipenet (standard and transient model) Guide to PIPENET4) Cost Estimation (via. Software OR HYSYS)