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Flue Gas Sulfuric Acid Dew Point & Cold-End Corrosion Calculator (Verhoff-Banchero)

Combustion of sulfur-bearing fossil fuels (heavy fuel oil, coal, petcoke) oxidizes sulfur to SO2, of which 1% to 5% further converts to sulfur trioxide (SO3).

Volumetric concentration of SO3 in combustion flue gas (typically 5 - 35 ppmv for coal/oil boilers).

Water vapor volumetric percentage from fuel hydrogen and combustion air moisture.

Flue duct operating absolute pressure (typically near atmospheric ~1.013 bar).

Calculated Result
139.5 °C

Acid Dew Point (T_adp)

Safe Operating Flue Temp

154.5 °C

Pure Water Dew Point

42 °C

Acid Elevation Margin

+97.4 °C

SO3 Concentration

15 ppmv

Calculation Breakdown

  1. Flue Gas Constituent Partial PressuresP_H2O = 60.8 mmHg (8% vol); P_SO3 = 0.0114 mmHg (15 ppmv)
  2. Verhoff-Banchero Sulfuric Acid Dew Point (T_adp)Acid Dew Point T_adp = 139.5 °C (Elevated +97.4 °C above water dew point of 42 °C)
  3. Economizer / Air Preheater Safe Metal LimitMinimum Cold-End Temperature = 154.5 °C (includes +15 °C corrosion safety margin)

Flue Gas Dew Points & Operating Safety

Interactive visualization based on your current inputs

Value
0.03875113151Water Dew PointAcid Dew PointSafe Operating MinParameterTemperature (°C)

What Is the Flue Gas Sulfuric Acid Dew Point & Cold-End Corrosion Calculator (Verhoff-Banchero)?

Combustion of sulfur-bearing fossil fuels (heavy fuel oil, coal, petcoke) oxidizes sulfur to SO2, of which 1% to 5% further converts to sulfur trioxide (SO3).

SO3 reacts instantly with water vapor to form sulfuric acid vapor (H2SO4), raising the condensation dew point from ~50°C (pure water) to 120-160°C.

Operating air preheater or economizer tube metal below the acid dew point causes rapid cold-end metal wastage and fouling. This calculator uses the Verhoff-Banchero correlation to predict T_adp and determine safe flue gas temperatures.

How Does the Flue Gas Sulfuric Acid Dew Point & Cold-End Corrosion Calculator (Verhoff-Banchero) Work?

The calculation evaluates user-provided measurements using recognized domain equations, converts between measurement units, and adjusts for real-world efficiency factors.

Flue Gas Sulfuric Acid Dew Point & Cold-End Corrosion Calculator (Verhoff-Banchero) Formula & Variables

The core mathematical equation utilized by this calculator is expressed as:

\frac{1}{T_{adp}} = 2.276 \times 10^{-3} - 2.943 \times 10^{-5} \ln P_{H_2O} - 8.58 \times 10^{-5} \ln P_{SO_3} + 6.2 \times 10^{-6} \ln P_{H_2O} \ln P_{SO_3}

Verhoff-Banchero thermodynamic vapor-liquid equilibrium correlation for H2SO4-H2O systems.

How to Use the Flue Gas Sulfuric Acid Dew Point & Cold-End Corrosion Calculator (Verhoff-Banchero)

  1. Enter your primary measurements in the input fields above.
  2. Select your preferred units (e.g. metric or imperial) if applicable.
  3. Review or adjust operational assumptions such as field efficiency.
  4. Click Calculate to instantly generate the full results breakdown and visual chart.
  5. Use the Reset button at any time to clear the form and test a new scenario.

Step-by-Step Example Calculation

Coal-Fired Boiler Flue Gas (15 ppm SO3, 8% H2O, 1.013 bar)

Input Values:

sulfurTrioxidePpm:15.0
waterVaporVolumePercent:8.0
flueGasPressureBarA:1.013
Worked Steps: Generates sulfuric acid dew point T_adp = 135.5°C (compared to 41.5°C water dew point), requiring minimum flue temperature of 150.5°C.

Understanding Your Result

Your calculated result represents the realistic operational capacity or baseline output under the specified conditions. Comparing theoretical and effective outputs reveals the direct impact of turns, overlap, and practical downtime.

Factors That Affect the Result

Field terrain, operator experience, equipment maintenance, overlap margin, and weather conditions can significantly influence real-world output.

When Should You Use This Calculator?

Use this calculator whenever you need quick, verified estimates for job planning, budgeting, equipment sizing, or project timelines.

Assumptions & Limitations

  • Verhoff-Banchero Equation: 1 / T_adp(K) = 0.002276 - 0.00002943 · ln(P_H2O) - 0.0000858 · ln(P_SO3) + 0.0000062 · [ln(P_H2O) · ln(P_SO3)].
  • Partial pressures P_H2O and P_SO3 are evaluated in mmHg atmospheres.
  • Cold-End Metal Margin: Recommended minimum tube metal temperature = T_adp + 15°C.

Frequently Asked Questions

Calculation Accuracy & Reference Note

This calculator implements verified, deterministic mathematical equations based on published standards. Results should be treated as professional engineering estimates; always verify critical operations with local equipment manuals and site inspections.

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