π Case Study
Hydrocarbon Separation in Offshore Gas Processing Skid
Insufficient liquid carryover removal causing downstream compressor fouling
ποΈ Project Overview
Integrated gas processing module for North Sea platform
π― Challenge
Insufficient liquid carryover removal causing downstream compressor fouling
π§ Design Approach
Redesigned vertical separator with optimized inlet vane geometry and residence time extension
π Design Diagram
AI-generated project design illustration
π Key Calculations
Terminal Droplet Velocity
v_t = β(4g(Ο_lβΟ_g)d_p / (3C_dΟ_g))
Result: 0.18 m/s
Determines minimum vessel height for droplet settling
Gas Capacity Constraint
Q_g = A Γ v_g
Result: 12,500 SmΒ³/h
Sets maximum allowable gas throughput
π Results
99.7% liquid removal efficiency; 0 compressor trips over 18-month operationπ‘ Lessons Learned
- β’Inlet momentum dissipation is as critical as vessel sizing
- β’Real-time level monitoring prevents surge-induced carryover
β Key Takeaways
- 1Inlet momentum dissipation is as critical as vessel sizing
- 2Real-time level monitoring prevents surge-induced carryover