Chapter VIII

Industrial Sheet Metal and Process Ductwork

Red Seal Practice study guide with diagrams.

Industrial Sheet Metal and Process Ductwork

Introduction to the Industrial Field

Industrial sheet metal represents a distinct sector from building sheet metal. While residential and commercial work primarily concerns thermal comfort and ventilation, industrial sheet metal deals with manufacturing processes, pneumatic material handling, chemical corrosion, and high temperatures. For the Red Seal exam, you must understand that design criteria, tolerances, and assembly methods differ radically from those in the commercial sector.

The term process duct refers to any duct transporting an industrial effluent: abrasive dusts, corrosive vapors, hot fumes, wood chips, or suspended chemicals. Unlike standard HVAC ducts, these systems are not governed by ASHRAE standards or the National Building Code for comfort, but rather by specific process requirements and the applicable safety codes for the materials being transported.

Classification of Industrial Systems

Categories by Content

CategoryExamplesMain Characteristics
Class A — Combustible MaterialsWood chips, grain dust, flourExplosion risk, minimum transport velocity required
Class B — Corrosive MaterialsAcid vapors, alkaline mistsRequires stainless steel, reinforced plastic, or coatings
Class C — Abrasive MaterialsSand, cement, slagRapid wear, wear plates at elbows, increased thicknesses
Class D — High-Temperature MaterialsFurnace fumes, combustion gasesThermal expansion, special supports, flexible joints
Class E — Hygroscopic or Sticky MaterialsSludges, gums, resinsSteep slopes, cleaning access, smooth surfaces

Material Selection Criteria

The choice of base metal depends on three factors: the chemical nature of the product being transported, the service temperature, and the abrasiveness. For corrosive applications, stainless steel type 304 or 316 is common. Type 316 contains molybdenum, which improves resistance to chlorides and acids. For temperatures exceeding 400 °C, alloy steels or refractory stainless steel are used. Aluminum is generally prohibited for metallic dusts due to the risk of exothermic reaction.

Rule of thumb: the minimum thickness of an industrial carbon steel duct is 16 gauge (1.5 mm) for diameters up to 300 mm, and 14 gauge (1.9 mm) for larger diameters. For abrasive materials, add 2 additional gauges of thickness or install reinforcement plates at impact points.

Design and Calculations of Industrial Ducts

Transport Velocity and Flow Rate

The air velocity in a process duct must keep particles suspended. If the velocity is too low, particles settle and obstruct the duct. If it is too high, wear and noise increase unnecessarily.

Flow rate formula: Q = V × A, where Q is the flow rate in m³/s, V is the velocity in m/s, and A is the cross-sectional area in m². For a circular duct, A = π × D² / 4, where D is the inside diameter in meters.

Recommended minimum velocities (according to common industrial practice and dust collector manufacturer data):

Material TransportedMinimum Velocity (m/s)
Light vapors and fumes8 to 10
Fine dusts (flour, cement)15 to 18
Medium dusts (sawdust, fine chips)18 to 20
Heavy and wet materials (wet chips, grains)20 to 23
Highly abrasive materials (sand, shot)25 to 30

Pressure Loss and Balancing

The total pressure loss of a system is the sum of friction losses in straight sections and fitting losses (elbows, connections, entries). For the exam, you must know that the pressure loss in a 90° short-radius elbow (R = 1.5 × D) is expressed as an equivalent length of straight duct. A long-radius elbow (R = 2.5 × D) reduces the pressure loss by approximately 30% compared to a short-radius elbow.

Balancing: in a system with multiple branches, balancing is done with dampers or by calculating diameters. The golden rule: the pressure loss of each branch must equal the pressure loss of the most unfavorable path. If a branch has less pressure loss than the main path, it will receive too much flow. You then install a balancing damper or reduce the branch diameter.

Thermal Expansion

For ducts transporting hot gases, expansion is a critical factor. The linear expansion coefficient of carbon steel is approximately 12 × 10⁻⁶ m/(m·°C). For a 10-meter length with a temperature rise of 200 °C, the total expansion is:

ΔL = 12 × 10⁻⁶ × 10 × 200 = 0.024 m (24 mm)

This expansion must be absorbed by expansion joints or compensators. Supports must allow axial movement: use sliding supports or roller hangers. Never rigidly fix a hot duct at both ends — this would cause buckling or weld failure.

Fabrication and Assembly

Joining Methods

MethodApplicationAdvantagesLimitations
Continuous weldingAirtight ducts, high temperaturePerfect seal, mechanical strengthHigh cost, possible thermal distortion
Spot welding + lap jointDust ductsFast, economicalLimited sealing
Bolted flangesEquipment connections, frequent disassemblyRemovable, airtight with gasketFlange cost, bulkiness
Sleeve joint with clampRound low-pressure ductsQuick installationLow pressure resistance
Pittsburgh lock seamStandard rectangular ductsAirtight, rigidNot suitable for high temperatures

For industrial ducts, continuous welding is required when the duct transports hazardous or flammable materials. CSA B149.1 (Natural Gas and Propane Code) requires welded vent ducts for certain gas appliances. Welds must be visually inspected and, for critical applications, tested by dye penetrant or radiography.

Fabrication Tolerances

Tolerances for industrial sheet metal are tighter than for commercial work. For a circular duct, the maximum deviation on diameter is ±1% of the nominal diameter. Ovalization must not exceed 2% of the diameter. For rectangular ducts, the tolerance on dimensions is ±3 mm for sides up to 600 mm, and ±5 mm beyond that.

Frequent exam trap: industrial ducts must be fabricated with joints oriented in the direction of flow to prevent particles from catching on surface irregularities. A transverse joint facing against the flow creates material accumulation and progressive obstruction.

Reinforcements and Stiffeners

Large rectangular ducts require reinforcements to withstand internal pressure (positive or negative). Negative pressure (vacuum) is particularly dangerous: a 600 mm × 600 mm duct with an internal pressure of −5 kPa experiences a force of 1,800 N on each face. Reinforcements can be angle iron, U-channels, or perimeter frames. The maximum spacing of reinforcements depends on sheet thickness, pressure, and panel dimension.

Industrial Ventilation Systems

Dilution Ventilation vs. Capture Ventilation

Dilution ventilation involves introducing clean air to dilute contaminants to an acceptable level. It is used when contaminants are mildly toxic and uniformly distributed. Capture ventilation (or local exhaust ventilation) involves capturing the contaminant at the source before it disperses. This is the preferred method for toxic contaminants or combustible dusts.

Capture Hoods

The design of a capture hood depends on the distance between the source and the hood, and the required capture velocity. Capture velocity is the air velocity at the point of release needed to draw the contaminant toward the hood.

Typical capture velocities:

Release ConditionExampleCapture Velocity (m/s)
Release with no initial velocitySolvent evaporation from a tank0.25 to 0.5
Release with low velocityLight spraying, welding0.5 to 1.0
Active releaseGrinding, sanding, blasting1.0 to 2.5
High-velocity releaseCrushing, material unloading2.5 to 10

The flow rate calculation formula for a slotted hood is: Q = V × (10 × X² + A), where X is the distance from the source to the hood in meters, A is the hood face area in m², and V is the required capture velocity in m/s. This formula is a practical approximation — it accounts for the fact that velocity decreases with the square of the distance.

Dust Collectors and Separators

Before the fan, the particle-laden air stream must pass through a separation device. Common types include:

Cyclone: separation by centrifugal force. Effective for particles larger than 10 μm. Typical pressure loss: 750 to 1,500 Pa.
Baghouse filter: high efficiency (99%+), used for fine particles. Sensitive to humidity and temperature (generally 260 °C limit for fiberglass bags).
Cartridge dust collector: compact, high efficiency, used for fine and dry dusts.
Wet scrubber: uses a liquid to capture particles and soluble gases. Suitable for flammable dusts or corrosive gases.

Fan position: the fan can be installed upstream (pushing) or downstream (pulling) of the dust collector. For abrasive dusts, place the fan downstream of the dust collector to protect the fan wheel from erosion. For hot gases, verify the fan's maximum allowable temperature.

Dust Explosion Prevention

Conditions for a Dust Explosion

Five conditions must be present simultaneously: fuel (dust), oxidizer (oxygen), ignition source, particle dispersion, and confinement. Eliminating any one of these conditions prevents an explosion. In a duct, suspended dust forms a cloud; a spark or hot surface can ignite it.

Protection Equipment

Ducts transporting combustible dusts must be equipped with:

Explosion vents: panels or membranes that release at a predetermined pressure (typically 10 to 20 kPa) to vent pressure and flames to the outside.
Rotary valves: installed at inlet and outlet points to prevent flame propagation between equipment.
Spark detection systems with extinguishing capability: installed upstream of dust collectors to detect and extinguish sparks before they reach the filter.

Grounding requirement: all metal ducts transporting dusts must be grounded to prevent static electricity accumulation. Grounding resistance must be less than 1 MΩ according to common industrial practices. Non-conductive connections (rubber sleeves, flexible joints) must be bridged with copper braids.

Applicable Standards

The National Fire Code of Canada and adopted provincial codes reference NFPA (National Fire Protection Association) standards for dust explosion prevention. Although NFPA is an American standard, it is widely adopted in Canada by reference. Relevant sections include NFPA 68 (explosion venting) and NFPA 69 (explosion prevention systems).

Vent and Flue Ducts

CSA B149.1 Requirements

CSA B149.1 (Natural Gas and Propane Code) governs the installation of vent ducts for gas appliances. Key rules for the sheet metal worker:

Rule 8-200: vent ducts must be made of materials resistant to corrosion and to the expected temperatures. Galvanized steel is prohibited for gas vents — use black carbon steel, stainless steel, or enameled sheet metal.
Rule 8-202: ducts must be gas-tight against combustion products and installed with a minimum slope of 6 mm per meter toward the appliance (to allow condensate drainage).
Rule 8-204: ducts must be supported at intervals not exceeding 1.2 meters for horizontal ducts and 2.4 meters for vertical ducts.
Rule 8-206: ducts must be spaced at least 25 mm from any combustible material, unless insulated or protected.

Double-Wall Ducts

For high-temperature gas vents, double-wall ducts with insulation are used. The inner wall is stainless steel (often 316L), the outer wall is galvanized or stainless steel, and the insulation is typically mineral wool. The spacing between walls varies from 25 to 75 mm depending on service temperature. These ducts are classified according to their maximum service temperature (for example, Class A for 540 °C, Class B for 400 °C).

Corrosion Control

Corrosion Mechanisms

Corrosion in industrial ducts results from the chemical action between the metal and the transported fluid. The main mechanisms are:

Uniform corrosion: regular attack on the surface. Predictable; you size the thickness accordingly.
Pitting corrosion: localized attack creating perforations. Common with chlorides on stainless steel.
Stress corrosion cracking: metal cracking under the combined effect of mechanical stress and a corrosive environment.
Galvanic corrosion: caused by contact between two dissimilar metals in the presence of an electrolyte. The more anodic (less noble) metal corrodes preferentially.

Corrosion Protection

Protection strategies include:

Choosing a resistant material (stainless steel, nickel alloys, fiber-reinforced plastics).
Interior coatings: enamel, rubber, epoxy, or ceramic coatings.
Cathodic protection for buried or submerged structures.
Avoiding galvanic couples by using materials from the same family or insulators at junctions.

Exam trap: galvanized steel must never be used for ducts transporting acid vapors. Zinc dissolves rapidly in the presence of acids, even weak ones, and the duct will perforate in a short time. Similarly, aluminum is not suitable for alkaline vapors or for environments containing copper or brass (galvanic corrosion).

Supports and Anchors

Support Calculations

Industrial duct supports must withstand the weight of the duct, the weight of the contents (accumulated particles), and the dynamic forces of the fluid. The total load is the sum of these three components. For a 600 mm diameter duct in 3 mm steel, the linear weight is approximately 45 kg/m. With accumulated dust content (assuming 50% of the section filled), add approximately 15 kg/m. The support must therefore carry approximately 60 kg/m.

Maximum support spacing by diameter:

Duct Diameter (mm)Maximum Spacing (m)
≤ 3003.0
301 to 6003.5
601 to 9004.0
901 to 1,2004.5
> 1,2005.0

These values are practical guidelines; precise calculations must account for allowable deflection (generally L/600 for industrial ducts).

Special Supports

For hot ducts, roller or sliding supports are used to allow axial expansion. Spring supports are used when the duct undergoes significant vertical movement (vertical expansion). Fixed anchors are placed at points where you want to control the direction of expansion — for example, near expansion joints.

Testing and Commissioning

Leakage Testing

Before commissioning, industrial ducts must undergo a leakage test. For low-pressure ducts (less than 500 Pa), a visual inspection and joint verification often suffice. For ducts with higher positive or negative pressure, a smoke test or pressure test is performed.

Pressure test: close all openings, introduce air at a test pressure (generally 1.5 times the service pressure, with a minimum of 1 kPa), and check the pressure drop over a given period. The allowable drop is typically 10% of the test pressure in 10 minutes for new ducts.

Flow and Velocity Verification

After installation, measure the actual flow at each outlet or branch using an anemometer or Pitot tube. Measured flow rates must be within ±10% of design flow rates. If a discrepancy is found, adjust the balancing dampers.

Pitot tube method: measure the dynamic pressure (Pd) at several points across the duct section. Velocity is calculated by V = √(2 × Pd / ρ), where ρ is the air density (approximately 1.2 kg/m³ at 20 °C and 101.3 kPa). For a circular duct, take measurements along two perpendicular diameters at predetermined logarithmic positions.

Summary

Industrial sheet metal is distinguished by material, thickness, and assembly method requirements adapted to the transported product.
Transport velocity must keep particles suspended without causing excessive wear: refer to the minimum velocity tables.
Thermal expansion is a major design factor for hot ducts: calculate ΔL = α × L × ΔT and provide expansion joints.
Combustible dust ducts require explosion vents, proper grounding, and rotary valves at interfaces.
CSA B149.1 (Rules 8-200 to 8-206) governs gas appliance vent ducts: resistant materials, minimum slope, supports, and clearances.
Balancing multi-branch systems is done by equalizing pressure losses; use dampers or adjust diameters.
Leakage and flow testing are integral parts of commissioning: ±10% tolerances on flow rates, maximum 10% pressure drop in testing.
Galvanic corrosion is avoided by not mixing metals of different potentials without isolation.

Traps to Avoid

107.Confusing transport velocities with comfort velocities: an HVAC duct operates at 5–8 m/s, but a chip transport duct requires 20 m/s minimum. Never transpose the values.
108.Forgetting thermal expansion: a duct rigidly fixed at both ends with a 200 °C temperature rise will experience enormous stresses. Always provide expansion joints and sliding supports.
109.Using galvanized steel for a gas vent duct: this is a frequent error. CSA B149.1 explicitly prohibits it. Use black steel or stainless steel.
110.Neglecting the slope of vent ducts: the minimum slope of 6 mm/m toward the appliance is mandatory to allow condensate drainage. A reversed slope causes water accumulation and accelerated corrosion.
111.Placing the fan upstream of a dust collector for abrasive dusts: the fan wheel will erode rapidly. Place the fan downstream.
112.Ignoring grounding of dust ducts: static electricity can ignite a dust cloud. All metal elements must be grounded, including flexible sections (by bridging).
113.Confusing commercial and industrial tolerances: industrial tolerances are tighter (diameter ±1%, ovalization ≤2%). Commercial tolerances do not apply.
114.Forgetting wear plates in elbows for abrasive materials: 90° elbows are the points of greatest erosion. Provide long-radius elbows (R ≥ 2.5 × D) and removable reinforcement plates.
115.Calculating the pressure loss of an elbow as simple straight length: use fitting loss coefficients (K) or equivalent lengths provided by manufacturers. A short-radius 90° elbow can have a loss equivalent to 10 to 15 diameters of straight duct.
116.Not checking the maximum allowable temperature of the fan and filters: for hot gases, the fan temperature limit is often 80 to 120 °C for standard models. Beyond that, special fans or pre-cooling are required.

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