Gas Turbine HRSG Duct Burner Supplemental Firing Simulator
Vitiated Combustion Kinetics • Flue Gas O₂ Depletion • Firing Temperature Rise • Steam Generation Boost
1. Gas Turbine Exhaust (TEG) Feed
2. Duct Burner Fuel & Firing Duty
3. HRSG Steam Circuit & Boiler Response
Duct Burner Cross-Section & Thermal Flame Envelope Visualizer
Comprehensive Thermochemical & Hydraulic Balance
Governing Thermodynamic & Combustion Equations
m_fuel = Q_fuel / (LHV × η_burn)
O2_out (vol%) = [(m_O2,in - m_fuel × Stoich_O2) / M_O2] / [m_flue,tot / M_flue] × 100
T₂ = T₁ + (Q_fuel × η_burn × 1000) / [(m_teg + m_fuel) × Cp(T_avg)]
Δm_steam (kg/s) = (Q_fuel × 1000 × η_hrsg) / Δh_steam → Δm_steam (t/h) = Δm_steam × 3.6
5 Fatal Traps & Engineering Pitfalls
1. Flame Impingement on First-Row HARP / Superheater Tubes
If duct burner firing rate is increased without adequate firing duct length, visible flame tips lick the leading high-pressure superheater tube bank. Localized heat flux spikes by 300%–500%, triggering internal steam film boiling (departure from nucleate boiling, DNB), rapid tube wall overheating (>700°C), and catastrophic tube rupture.
2. Oxygen Depletion Below Vitiated Flame Stability Limit (<10.5% O₂)
Unlike conventional package boilers using ambient air (20.9% O₂), duct burners operate on gas turbine exhaust already diluted to 12–15% O₂. When heavy supplemental firing reduces downstream O₂ below 10.5%–11.0% by volume wet, reaction rates stall, resulting in severe flame detachment, roaring acoustic vibrations, unburned fuel accumulation, and dangerous downstream deflagration.
3. Economizer Steaming & Header Water Hammer During High Firing
Elevating flue gas temperature at the duct burner cascades extra enthalpy all the way back to the cold-end economizer. If feedwater flow is not throttled or subcooling margin is insufficient, liquid water in the economizer tubes flashes into steam prior to reaching the steam drum, provoking violent water hammer, fractured tube support clips, and ruptured header welds.
4. Duct Internal Refractory Insulation Liner Buckling & Casing Burnout
At fired temperatures above 760°C (1400°F), internal stainless steel liner plates expand significantly. Inadequate expansion slip joints, sheared ceramic fiber anchor pins, or missing corner expansion pillows allow 850°C gas to short-circuit behind the insulation directly to the carbon steel outer casing, forming glowing red hot spots and structural casing collapse.
5. Turbine Exhaust Gas Flow Maldistribution Across Burner Runners
Turbine diffusers impart high residual swirl and velocity stratification into the inlet duct. If perforated flow distribution grids or turning vanes fail, local gas velocities past individual burner runners can range from 4 m/s to 30 m/s. High velocity quenches local flame stabilization wings (causing blow-off), while low velocity zones overheat burner fuel nozzles, causing nozzle coking and distortion.