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Chimney Diameter Calculator Guide

Complete guide to sizing chimney and flue pipes for heating appliances following EN 13384 standards and combustion safety principles

Enginist HVAC Team
Certified HVAC engineers specializing in heating system design, load calculations, and energy efficiency.
Reviewed by ASHRAE-Certified Engineers
Published: October 15, 2025
Updated: November 9, 2025

Chimney Diameter Calculator Guide

Quick AnswerHow do you calculate chimney diameter?
Size chimneys using D=(4VD = \sqrt{}(4V̇ / (π×v\pi \times v)), where V̇ is flue gas flow (m³/s) and v is velocity (3-6 m/s typical). Verify draft pressure ≥ 12 Pa per EN 13384.
Example

50kW gas boiler produces ~0.05 m³/s flue gas at 5 m/s velocity, giving D=4×0.05/(π×5)=0.11mD = \sqrt{4 \times 0.05 / (\pi \times 5)} = 0.11m = 110mm minimum. Select 120mm standard size.

Introduction

Chimney diameter sizing is critical for safe and efficient removal of combustion gases from heating appliances including boilers, furnaces, and stoves. Proper chimney sizing prevents backdrafting, incomplete combustion, and carbon monoxide hazards while maintaining adequate draft pressure for reliable appliance operation. Undersized chimneys cause poor draft, spillage of combustion gases into living spaces, and incomplete combustion leading to carbon monoxide production.

Why This Calculation Matters

Accurate chimney sizing is crucial for:

  • Safety: Ensuring complete removal of combustion products including carbon monoxide to prevent health hazards.
  • Appliance Performance: Maintaining adequate draft pressure for efficient combustion and proper appliance operation.
  • Condensation Prevention: Achieving sufficient flue gas velocity to prevent condensation and corrosion.
  • Code Compliance: Meeting EN 13384 and local building code requirements for combustion venting systems.

The Fundamental Challenge

The primary challenge in chimney sizing lies in balancing diameter, height, and velocity requirements. Undersized chimneys create excessive pressure drop and poor draft, leading to combustion gas spillage into living spaces. Oversized chimneys have insufficient velocity, causing poor draft during low-fire operation and increased condensation as flue gases cool below dew point. Additionally, natural draft depends on temperature difference between flue gases and ambient air—cold weather increases draft while mild weather may cause insufficient draft. Chimney height, construction material, and appliance type all interact to determine proper sizing.

What You'll Learn

In this comprehensive guide, you will learn:

  • The core formula for chimney diameter based on flue gas flow rate and velocity.
  • How to calculate natural draft pressure from chimney height and temperature difference.
  • Velocity requirements for different appliance types (boilers, furnaces, stoves).
  • Installation requirements and chimney height guidelines.
  • Step-by-step examples applying EN 13384 chimney sizing methods.

Quick Answer: How to Size a Chimney?

Chimney diameter sizing ensures safe and efficient removal of combustion gases from heating appliances. Proper sizing prevents backdrafting, incomplete combustion, and carbon monoxide hazards while maintaining adequate draft pressure.

Core Sizing Formula

Velocity-Based Method:

D=4VπvD = \sqrt{\frac{4V}{\pi v}}

Where:

  • DD = Chimney diameter (m)
  • VV = Flue gas flow rate (m³/s)
  • vv = Flue gas velocity (m/s, typically 2-4 m/s)
  • π = 3.14159

Additional Formulas

Flue Gas Flow Rate:

V=Pη×Hf×ρfgV = \frac{P}{\eta \times H_f \times \rho_{\text{fg}}}

Where:

  • PP = Heating capacity (kW)
  • η\eta = Combustion efficiency (decimal)
  • HfH_f = Fuel warming value (MJ/kg or MJ/m³)
  • ρfg\rho_{\text{fg}} = Flue gas density (kg/m³)

Natural Draft Pressure:

ΔP=H×g×(ρairρfg)\Delta P = H \times g \times (\rho_{\text{air}} - \rho_{\text{fg}})

Where:

  • ΔP\Delta P = Draft force (Pa)
  • HH = Chimney height (m)
  • gg = Gravity (9.81 m/s²)
  • ρair\rho_{\text{air}} = Ambient air density (kg/m³)
  • ρfg\rho_{\text{fg}} = Hot flue gas density (kg/m³)

Worked Example

35 kW Natural Gas Boiler: 8m Chimney Height, 180°C Flue Gas

Given:

  • Heat system capacity: P=35P = 35 kW
  • Fuel: Natural gas
  • Chimney height: H=8H = 8 m
  • Flue gas temperature: 180°C
  • Appliance: Conventional boiler
  • Combustion efficiency: 85%

Step 1: Calculate Flue Gas Flow Rate

Natural gas combustion produces approximately 1.1 m³ flue gas per kW at 180°C:

V=35×1.1=38.5 m3/hr=0.0107 m3/sV = 35 \times 1.1 = 38.5 \text{ m}^3\text{/hr} = 0.0107 \text{ m}^3\text{/s}

Step 2: Select Target Velocity

For natural draft conventional boiler: v=2.5v = 2.5 m/s (typical range 2-3 m/s)

Step 3: Calculate Required Diameter

D=4×0.0107π×2.5=0.04287.85=0.00545=0.074 m=74 mmD = \sqrt{\frac{4 \times 0.0107}{\pi \times 2.5}} = \sqrt{\frac{0.0428}{7.85}} = \sqrt{0.00545} = 0.074 \text{ m} = 74 \text{ mm}

Step 4: Select Standard Size

Standard chimney pipe sizes: 80, 100, 120, 130, 150, 180, 200 mm

Selected: 80 mm chimney diameter (next standard size up)

Step 5: Verify Velocity at Standard Size

vactual=4VπD2=4×0.0107π×0.082=2.13 m/sv_{\text{actual}} = \frac{4V}{\pi D^2} = \frac{4 \times 0.0107}{\pi \times 0.08^2} = 2.13 \text{ m/s}

Step 6: Determine Natural Draft

At 180°C: ρfg=0.76\rho_{\text{fg}} = 0.76 kg/m³ At 20°C ambient: ρventilation air=1.20\rho_{\text{ventilation air}} = 1.20 kg/m³

ΔP=8×9.81×(1.200.76)=34.5 Pa\Delta P = 8 \times 9.81 \times (1.20 - 0.76) = 34.5 \text{ Pa}

Result:

  • Required chimney diameter: 80 mm
  • Flue gas velocity: 2.13 m/s ✔ (within range)
  • Natural draft: 34.5 Pa ✔ (adequate)
  • Installation: Single-wall steel or stainless steel

Reference Table

ParameterTypical RangeStandard
Flue Gas Velocity (Natural Draft Gas)2.0-3.0 m/sEN 13384
Flue Gas Velocity (Natural Draft Oil)2.5-3.5 m/sEN 13384
Flue Gas Velocity (Natural Draft Solid)3.0-4.5 m/sEN 13384
Flue Gas Velocity (Condensing)5.0-8.0 m/sEN 13384
Minimum Chimney Height (Natural Draft)3-4 mEN 13384
Minimum Chimney Height (Solid Fuel)4-5 mEN 13384
Draft Pressure (Natural Draft)10-30 PaTypical
Draft Pressure (Atmospheric)15-40 PaTypical
Flue Gas per kW (Natural Gas)1.0-1.1 m³/hrTypical
Flue Gas per kW (Fuel Oil)1.2-1.3 m³/hrTypical

Key Standards

Combustion Fundamentals

Flue Gas Production

Complete combustion produces flue gases consisting primarily of:

  • Carbon dioxide (CO₂): 8-15%
  • Water vapor (H₂O): 10-20%
  • Nitrogen (N₂): 70-80%
  • Oxygen (O₂): 2-8% (excess fresh air)

Flue Gas Volume per Fuel Type (at 180°C):

Fuel TypeFlue Gas per kWTypical Temp
Natural Gas1.0-1.1 m³/hr150-200°C
LPG1.1-1.2 m³/hr150-200°C
Fuel Oil1.2-1.3 m³/hr180-250°C
Coal1.3-1.5 m³/hr200-300°C
Wood1.4-1.6 m³/hr200-400°C

Temperature Effects:

  • Higher flue gas heat = lower density = better draft
  • Lower thermal value = risk of condensation and reduced draft
  • Condensing boilers: 40-80°C (require special venting)

Stack Effect and Draft

Stack effect creates natural draft due to density difference between hot flue gases and cold ambient air supply:

ΔP=H×g×(ρairflowρfg)\Delta P = H \times g \times (\rho_{\text{airflow}} - \rho_{\text{fg}})

Draft load requirements:

  • Natural draft appliances: 10-30 Pa
  • Atmospheric burners: 15-40 Pa
  • Induced draft appliances: Variable (fan-assisted)

Factors affecting draft:

  1. Chimney height: Greater height = stronger draft
  2. Degree difference: Higher difference = stronger draft
  3. Chimney diameter: Proper sizing critical
  4. Surface roughness: Smooth surfaces reduce friction
  5. Bends and offsets: Each bend reduces draft by 10-20%

Sizing Methodology

Velocity-Based Sizing

Proper flue gas velocity ensures:

  • Adequate draft to remove combustion products
  • Prevention of condensation (minimum velocity)
  • Reduced noise and erosion (maximum velocity)
  • Efficient heat transfer (balanced velocity)

Recommended Velocities:

Appliance TypeVelocity Range
Natural draft (gas)2.0-3.0 m/s
Natural draft (oil)2.5-3.5 m/s
Natural draft (solid fuel)3.0-4.5 m/s
Fan-assisted3.0-5.0 m/s
Condensing boilers5.0-8.0 m/s (plastic vent)

Diameter Determination:

D=4Vπv×1000 (convert to mm)D = \sqrt{\frac{4V}{\pi v}} \times 1000 \text{ (convert to mm)}

Stream Rate Calculation

Method 1: Simplified (Fuel-Based)

Vm3/hr=PkW×CfuelV_{\text{m}^3\text{/hr}} = P_{\text{kW}} \times C_{\text{fuel}}

Where CfuelC_{\text{fuel}} is flue gas production coefficient (see table above).

Method 2: Detailed (Combustion Evaluation)

V=P×(1+λ×L0)η×Hf×ρfgV = \frac{P \times (1 + \lambda \times L_0)}{\eta \times H_f \times \rho_{\text{fg}}}

Where:

  • λ\lambda = Excess atmosphere ratio (1.2-1.4 for gas, 1.3-1.5 for oil)
  • L0L_0 = Theoretical ventilation air requirement (m³/kg or m³/m³)

Typical Values:

  • Natural gas: L0=9.5L_0 = 9.5 m³ fresh air/m³ gas
  • LPG: L0=24L_0 = 24 m³ air supply/m³ gas
  • Fuel oil: L0=11L_0 = 11 m³ airflow/kg oil

Fuel-Specific Considerations

Natural Gas

Characteristics:

  • Clean burning, low particulates
  • Moderate flue gas heat level (150-200°C)
  • Low condensation risk (above 55°C)

Sizing Guidelines:

  • Velocity: 2.0-3.0 m/s for natural draft
  • Minimum height: 3 m
  • Material: Stainless steel 316L or aluminum

Example: 50 kW gas boiler

V=50×1.05=52.5 m3/hr=0.0146 m3/sV = 50 \times 1.05 = 52.5 \text{ m}^3\text{/hr} = 0.0146 \text{ m}^3\text{/s}

D=4×0.0146π×2.5=86 mm100 mm standardD = \sqrt{\frac{4 \times 0.0146}{\pi \times 2.5}} = 86 \text{ mm} \rightarrow \textbf{100 mm standard}

LPG

Characteristics:

  • Similar to natural gas, slightly higher flue gas volume
  • Moderate temp (150-200°C)

Sizing Guidelines:

  • Velocity: 2.0-3.0 m/s
  • Typically 10% larger diameter than natural gas
  • Stainless steel preferred

Fuel Oil

Characteristics:

  • Higher flue gas thermal reading (180-250°C)
  • Contains sulfur → acidic condensate
  • Soot formation possible

Sizing Guidelines:

  • Velocity: 2.5-3.5 m/s (higher velocity helps prevent soot deposit)
  • Minimum height: 4 m
  • Material: Stainless steel, soot-resistant

Coal and Wood

Characteristics:

  • Highest flue gas heat (200-400°C)
  • High particulate content
  • Variable fuel quality

Sizing Guidelines:

  • Velocity: 3.0-4.5 m/s (high velocity for creosote/tar removal)
  • Minimum height: 4-5 m
  • Larger diameter due to particulates
  • Masonry, refractory-lined, or heavy-duty steel

Appliance Types

Condensing Boilers

Special Requirements:

  • Flue gas thermal value: 40-80°C
  • Acid-resistant materials required (PP, PVC, stainless steel)
  • Positive pressure value (fan-assisted) or balanced flue
  • Condensate drainage essential

Sizing:

  • Higher velocities acceptable: 5-8 m/s
  • Smaller diameters typical: 60-80 mm for residential
  • Follow manufacturer specifications strictly

Example: 30 kW condensing boiler

  • Manufacturer specifies: 60 mm concentric vent
  • Maximum length: 10 m equivalent
  • Condensate trap required

Conventional Boilers

Characteristics:

  • Flue gas degree: 150-250°C
  • Natural draft or induced draft
  • Standard chimney materials

Sizing:

  • Velocity: 2.0-3.5 m/s
  • Standard diameter assessment applies
  • Minimum height for adequate draft

Stoves and Furnaces

Characteristics:

  • Solid fuel (wood, coal)
  • High heat level: 300-600°C at appliance
  • Intermittent operation

Sizing Considerations:

  • Oversizing acceptable (thermal mass)
  • Velocity at rated output: 3.5-5.0 m/s
  • Minimum 5 m height recommended
  • Masonry or insulated metal chimney

Draft Calculation

Available Draft System pressure:

ΔPavailable=H×g×(ρatmosphereρfg)\Delta P_{\text{available}} = H \times g \times (\rho_{\text{atmosphere}} - \rho_{\text{fg}})

Required Draft Power:

ΔPrequired=ΔPappliance+ΔPfriction+ΔPfittings\Delta P_{\text{required}} = \Delta P_{\text{appliance}} + \Delta P_{\text{friction}} + \Delta P_{\text{fittings}}

Friction Loss (Simplified):

ΔPfriction=f×HD×ρv22\Delta P_{\text{friction}} = f \times \frac{H}{D} \times \frac{\rho v^2}{2}

Where ff is friction factor (0.02-0.03 for smooth chimneys).

Example Solution:

Given:

  • Chimney height: 8 m
  • Diameter: 150 mm
  • Flue gas velocity: 3.0 m/s
  • Temp: 200°C (ρ\rho = 0.75 kg/m³)
  • Ambient: 20°C (ρ\rho = 1.20 kg/m³)

Available Draft:

ΔPavail=8×9.81×(1.200.75)=35.3 Pa\Delta P_{\text{avail}} = 8 \times 9.81 \times (1.20 - 0.75) = 35.3 \text{ Pa}

Friction Loss:

ΔPfriction=0.025×80.15×0.75×3.022=4.5 Pa\Delta P_{\text{friction}} = 0.025 \times \frac{8}{0.15} \times \frac{0.75 \times 3.0^2}{2} = 4.5 \text{ Pa}

Net Draft:

ΔPnet=35.34.5=30.8 Pa\Delta P_{\text{net}} = 35.3 - 4.5 = 30.8 \text{ Pa}

Adequate for natural draft appliance (requires 15-25 Pa).


How Should You Install?

Height Requirements

Minimum Heights:

  • Natural draft appliances: 3-4 m minimum
  • Solid fuel: 4-5 m minimum
  • Condensing boilers: Follow manufacturer specs (often 1-2 m)

Height Above Roof:

  • Minimum 0.6 m above roof penetration
  • 0.6 m above any part within 3 m horizontal distance
  • Higher in high-wind areas or near tall buildings

Material Selection

MaterialThermal reading RatingFuel CompatibilityNotes
Single-wall steelUp to 200°CGas, oilRequires clearances
Double-wall insulatedUp to 600°CAll fuelsReduced clearances
Stainless steel 316Up to 650°COil, solid fuelCorrosion resistant
AluminumUp to 230°CGas onlyLightweight, economical
Polypropylene (PP)Up to 120°CCondensing onlyAcid resistant
MasonryUp to 1000°CSolid fuelHeavy, permanent

Clearances

Combustible Material Clearances:

  • Single-wall pipe: 450 mm minimum
  • Insulated pipe: 50-150 mm (check listing)
  • Through walls: Fire-rated thimble required
  • Through floors: Properly sealed penetration

Condensate Management

For all chimneys with potential condensation:

  • Install condensate drain at base
  • Stainless steel or acid-resistant materials
  • Neutralization unit if required by code
  • Trap to prevent ventilation air infiltration

Our heating calculations are based on proven methodologies used in professional practice.

Our heating calculations are based on proven methodologies used in professional practice.

Conclusion

Proper chimney sizing is essential for safe and efficient furnace system arrangement operation. Undersized chimneys create dangerous backdrafting and carbon monoxide risks, while oversized chimneys suffer from condensation and poor draft. Following EN 13384 computation methods ensures code-compliant, safe, and efficient chimney design.

Export as PDF — Generate professional reports for documentation, client presentations, or permit submissions.

Key takeaways:

  • Compute flue gas current rate based on appliance capacity and fuel type
  • Size diameter for velocity range: 2.0-4.0 m/s depending on appliance
  • Verify natural draft pressure value is adequate: 10-50 Pa depending on appliance type
  • Provide minimum chimney height: 3-5 m depending on fuel
  • Select appropriate materials for fuel type and degree
  • Install properly with correct clearances and condensate drainage

Always consult local building codes and appliance manufacturer specifications for final chimney sizing and installation requirements.

Key Takeaways

Further Learning

References & Standards

Primary Standards

EN 13384-1 Chimneys - Thermal and fluid dynamic calculation methods - Part 1: Chimneys serving one heating appliance. Provides standardized methods for calculating chimney diameter, flue gas flow rates, natural draft pressure, and velocity requirements.

EN 13384-2 Chimneys - Part 2: Chimneys serving more than one heating appliance. Specifies calculation methods for multiple appliance installations and shared chimney systems.

Supporting Standards & Guidelines

NFPA 211 Standard for Chimneys, Fireplaces, Vents, and Solid Fuel-Burning Appliances. Provides comprehensive safety requirements for chimney installation and operation.

UL 103 Standard for Factory-Built Chimneys for Residential Type and Building Heating Appliances. Defines material specifications and testing requirements for factory-built chimneys.

Further Reading

  • ASHRAE Technical Resources - American Society of Heating, Refrigerating and Air-Conditioning Engineers resources
  • [Local Building Codes] - Always consult authority having jurisdiction (AHJ) for jurisdiction-specific requirements
  • [Manufacturer Specifications] - Appliance-specific venting requirements vary by manufacturer

Note: Standards and codes are regularly updated. Always verify you're using the current adopted edition applicable to your project's location. Consult with local authorities having jurisdiction (AHJ) for specific requirements.


Disclaimer: This guide provides general technical information based on international heating standards. Always verify calculations with applicable local codes and consult licensed professionals for actual installations. Heating system design should only be performed by qualified professionals. Component ratings and specifications may vary by manufacturer.

Frequently Asked Questions

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