๐Ÿ“‹ Case Study

Industrial Plant Power Design: Aluminum Smelter Load Flow Optimization

Severe voltage sag during anode changing cycles causing PLC trip cascades

๐Ÿ—๏ธ Project Overview

Greenfield 320 MW aluminum smelter in Iceland with 100% renewable hydro supply

๐ŸŽฏ Challenge

Severe voltage sag during anode changing cycles causing PLC trip cascades

๐Ÿ”ง Design Approach

Integrated STATCOM + dynamic tap changer coordination with load flow-driven reactive reserve allocation

๐Ÿ“ Design Diagram

Rectifier BusSC Ratio = 2.8STATCOM+Q ReserveTap ChangerDynamicPLC TripVoltage Sag: 6.2%Anode Changing Cycle (200 ms)โ†’ Reactive Reserve Allocation Engine โ†

AI-generated project design illustration

๐Ÿ“ Key Calculations

Short Circuit Ratio at Rectifier Bus

SC_MVA / Converter_MVA
Result: 2.8
Determines STATCOM sizing for voltage support

Voltage Sag Depth During 200ms Load Step

Z_line ร— I_step / V_base
Result: 6.2%
Triggered protective undervoltage lockout

๐Ÿ“Š Results

Zero trips over 18-month operation; 12% reduction in reactive energy penalties

๐Ÿ’ก Lessons Learned

  • โ€ขStatic VAR compensation must be sized for worst-case dI/dt, not steady-state
  • โ€ขTap changers require coordinated delay logic to avoid counteracting STATCOM action

โœ… Key Takeaways

  • 1Static VAR compensation must be sized for worst-case dI/dt, not steady-state
  • 2Tap changers require coordinated delay logic to avoid counteracting STATCOM action