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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

🔵 Gas Turbine Exhaust Inflow 🔥 Vitiated Flame Runners 🟡 Mixed Firing Zone (T₂) 🛡️ HARP / Superheater Tube Bank
Downstream Flue Temp (T₂)
-- °C
✓ Safe Metallurgical Limit
Downstream Flue Gas O₂
-- %
✓ Stable Combustion Margin
Incremental Steam Boost
-- t/h
+--% over baseline
Flame Length & Clearance
-- m
✓ No Flame Impingement

Comprehensive Thermochemical & Hydraulic Balance

Fuel Gas Consumption Rate: -- kg/s (-- Nm³/h)
Total Mixed Flue Gas Flow: -- kg/s
Oxygen Consumption Rate: -- kg/s
Effective Flue Gas Specific Heat (Cp): -- kJ/kg·K
Total Fired Steam Generation: -- t/h
Burner Grid Gas Pressure Drop: -- mbar (-- in.wg)
Specific Fuel per Incremental Steam: -- kg fuel/t steam
Calculated Flame Safety Margin: -- m

Governing Thermodynamic & Combustion Equations

1. Fuel Consumption & Oxygen Depletion:

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

2. Downstream Mixed Flue Gas Temperature:

T₂ = T₁ + (Q_fuel × η_burn × 1000) / [(m_teg + m_fuel) × Cp(T_avg)]

3. Steam Production Boost:

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.

Frequently Asked Questions

What is supplemental duct firing in a Heat Recovery Steam Generator (HRSG)? +
Why is downstream oxygen depletion critical for duct burner flame stability? +
How does duct firing elevate HRSG steam generation? +
What is the maximum allowable firing temperature for duct burners? +
How is flame length calculated and why does it dictate duct geometry? +
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