Chapter VII

Install and Align Piping and Associated Systems

Red Seal Practice study guide with diagrams.

Installing and Aligning Piping and Related Systems

Module Introduction

This chapter covers the installation, alignment, and commissioning of piping systems associated with boilers and pressure vessels. As a journeyperson boilermaker, you will be called upon to install feedwater piping, steam lines, blowdown systems, gas lines, and hydraulic circuits. The Red Seal exam assesses your ability to interpret drawings, apply alignment tolerances, perform thermal expansion calculations, and comply with applicable Canadian standards. This chapter prepares you specifically for these requirements.


1. Boilermaker Roles and Responsibilities in Piping

The boilermaker does not install piping the same way a plumber or pipefitter does. Your work focuses on systems directly connected to the boiler and pressure vessels. Your responsibilities include:

Installing headers and tubing that connect the boiler to auxiliary systems.
Precisely aligning flanges and fittings at connection points.
Verifying thermal expansion and installing expansion compensators (expansion joints).
Installing supports, guides, and anchors according to specifications.
Performing pressure tests and verifying leak-tightness.

You must be able to read isometric drawings and piping drawings, identify standardized symbols, and understand material specifications.


2. Applicable Canadian Standards and Codes

2.1 Canadian Electrical Code, Chapter V

Although this code primarily concerns electricity, it applies to piping systems when they carry flammable fluids or gases. Rule 8-200 of the Canadian Electrical Code, Chapter V, addresses grounding and bonding requirements for piping carrying hazardous materials. You must ensure that piping sections are properly bonded together to prevent the accumulation of electrostatic charges.

2.2 CSA B51 – Boiler, Pressure Vessel, and Pressure Piping Code

CSA B51 is the primary reference for the installation of boilers and pressure piping in Canada. It covers:

Design and fabrication of pressure piping.
Inspection and testing requirements.
Permitted materials (carbon steel, stainless steel, alloys).
Maximum allowable temperatures and pressures.

This standard requires that all pressure piping be marked in accordance with CSA B51 requirements and be inspected before being placed into service.

2.3 CSA B149.1 – Natural Gas and Propane Installation Code

CSA B149.1 applies to the installation of natural gas and propane piping. Key points for the boilermaker:

Gas piping must be supported at maximum intervals of 2.5 m for pipes with a nominal diameter ≤ 25 mm (1 in).
Threaded fittings must use an approved joint compound.
Gas lines must be purged before being placed into service.
Manual shut-off valves must be installed in an accessible location.

2.4 ASME B31.1 – Power Piping

Although American in origin, ASME B31.1 is widely adopted in Canada for power plant and boiler piping. It specifies:

Allowable stresses for materials.
Minimum wall thicknesses.
Support requirements.
Flange alignment tolerances.

3. Piping Materials and Identification

3.1 Types of Materials

MaterialTypical UseMax. TemperatureTypical Max. Pressure
Carbon steel (ASTM A106 Gr. B)Steam, hot water, condensate425 °C15 MPa (depending on thickness)
Stainless steel (ASTM A312 TP304/316)Corrosive fluids, food-grade650 °CVariable
Ductile ironLow-pressure feedwater120 °C2.5 MPa
Copper (Type K, L, M)Small instrumentation lines200 °C8 MPa
Nickel alloys (Inconel, Monel)Extreme temperatures, corrosion1000 °CVariable

3.2 Pipe Marking

Each pipe must bear markings indicating:

The material grade (e.g., A106 Gr. B).
The schedule – wall thickness (e.g., Sch 40, Sch 80).
The manufacturing standard (e.g., ASTM, CSA).
The heat number for traceability.

Exam Trap: You will often be asked to select the correct material for a given application. Remember that carbon steel is the default choice for steam and hot water, unless corrosion or temperature rules it out.


4. Pipe Preparation and Cutting

4.1 Cutting Methods

Oxy-fuel cutting (torch cutting): For carbon steel, thicknesses > 6 mm. Use an appropriate tip and preheat uniformly.
Band saw cutting: For small-diameter pipes and non-ferrous materials.
Abrasive disc cutting: Fast but generates heat; risk of distortion for thin walls.
Water jet cutting: For heat-sensitive materials (stainless steel, alloys).

4.2 Edge Preparation for Welding

Edges must be prepared according to the specified bevel (generally 37.5° ± 2.5°). The root face must measure between 1.5 mm and 2.5 mm for Schedule 40 pipes and heavier. The root gap between the two pieces must be 2 to 3 mm to allow for complete penetration.

4.3 Cleaning

Before welding or assembly, clean the inside and outside of the pipe over at least 25 mm on each side of the joint. Remove:

Rust and mill scale.
Oils and greases.
Moisture.
Cutting burrs.

5. Piping Alignment

5.1 Alignment Tolerances

Alignment is critical to avoid excessive stress, leaks, and premature failure. Typical tolerances per ASME B31.1:

ParameterAllowable Tolerance
Axial misalignment (mismatch)≤ 1.5 mm for wall ≤ 10 mm; ≤ 3 mm for wall > 10 mm
Angular deviation between axes≤ 1° (0.5° for high-pressure systems)
Flange misalignment≤ 0.5 mm across the flange diameter
Parallel gap between flange faces≤ 0.25 mm per 100 mm of diameter

5.2 Measurement Methods

Straightedge and level: For rough alignment.
Dial indicator: For precise alignment of flanges and shafts.
Alignment laser: For long piping runs (> 10 m).
Plumb bob: For checking verticality.

5.3 Flange Alignment

Flanges must be aligned so that:

74.Faces are parallel (tolerance: 0.25 mm per 100 mm of diameter).
75.Bolt holes are aligned (tolerance: 1.5 mm maximum offset).
76.The gap between faces is uniform (check at four points 90° apart).

Procedure:

78.Mount the flanges on the pipes before final welding.
79.Insert bolts into the aligned holes.
80.Tighten bolts in a cross pattern (opposite) in successive passes.
81.Check the gap with a feeler gauge.

5.4 Assembly Stresses

Never force a pipe to bring it to a flange. Excessive assembly stress causes:

Leaks at joints.
Premature wear of supports.
Metal fatigue.
Misalignment of connected equipment.

If the gap exceeds tolerance, cut and readjust the pipe rather than forcing it.


6. Thermal Expansion and Compensators

6.1 Calculating Thermal Expansion

The linear expansion of a pipe is calculated using the formula:

ΔL = α × L × ΔT

Where:

ΔL = expansion (mm)
α = coefficient of thermal expansion (mm/m·°C)
L = pipe length (m)
ΔT = temperature difference (°C)

Typical expansion coefficients:

Materialα (mm/m·°C)
Carbon steel0.0117
Stainless steel (304)0.0173
Copper0.0165
Ductile iron0.0108

Example: A 30 m carbon steel pipe carries steam at 200 °C. The ambient temperature is 20 °C. The expansion is:

ΔL = 0.0117 × 30 × (200 − 20) = 0.0117 × 30 × 180 = 63.2 mm

This expansion of more than 6 cm must be absorbed by compensators or expansion loops.

6.2 Types of Compensators

TypeAdvantagesDisadvantages
Expansion loopSimple, reliable, maintenance-freeBulky, takes up space
Bellows compensatorCompact, absorbs axial movementsLimited lifespan, susceptible to fatigue
Slip joint compensatorAbsorbs large axial movementsLeak risk, regular maintenance required
Ball joint compensatorAbsorbs angular movementsHigh pressure drop

6.3 Compensator Installation Rules

107.The compensator must be installed without preload (unless otherwise specified).
108.Guides must be placed at a maximum distance of 4 × diameter on each side of the compensator.
109.A fixed anchor must be installed between two compensators to distribute movements.
110.Bellows compensators must be protected against mechanical damage.
111.Verify that the flow direction matches the arrow indicated on the compensator.

7. Pipe Supports and Anchors

7.1 Types of Supports

TypeFunctionMaximum Spacing (steel, water)
Rigid hangerSupports the weight of the pipe3 m for DN ≤ 50 mm; 4.5 m for DN > 50 mm
GuideLimits lateral movementPer calculation
Fixed anchorPrevents all movementAt every change of direction
Spring supportAllows vertical movementPer calculation
Roller supportAllows axial movementPer calculation

7.2 Support Rules per CSA B149.1

For gas piping:

DN 15 mm (1/2 in) pipe: support every 1.5 m.
DN 25 mm (1 in) pipe: support every 2.5 m.
DN 50 mm (2 in) pipe: support every 3 m.
DN 100 mm (4 in) pipe and larger: support every 4 m.

7.3 Anchor Points

Anchors must be placed:

At changes of direction.
Between compensators.
At the ends of long straight runs.
Near sensitive equipment (turbines, pumps).

A poorly positioned anchor can concentrate stresses and cause failure.


8. Fittings and Joints

8.1 Threaded Fittings

Used for small-diameter pipes (≤ DN 50) and low pressures. Rules:

Use a joint compound or PTFE tape (Teflon).
Do not leave more than 3 threads visible after tightening.
Tighten with a chain wrench or pipe wrench, without over-tightening.
Threads must be clean and free of burrs.

8.2 Welded Fittings

Welding is the preferred method for high pressures and temperatures. Types of joints:

Butt weld: For pipes of the same diameter.
Socket weld: For small diameters (≤ DN 50).
Lap joint: With a lap joint flange.

8.3 Flanged Fittings

Flanges are classified by their pressure class:

ClassMax. Pressure (MPa) at 38 °CUse
1501.96Water, low-pressure steam
3005.11Medium-pressure steam
60010.21High pressure
90015.32Very high pressure
150025.53Critical applications
250042.55Ultra-high pressure

Flange bolt tightening procedure:

146.Hand-tighten all bolts.
147.Tighten in a cross pattern to 30% of final torque.
148.Tighten in a cross pattern to 60%.
149.Tighten in a cross pattern to 100%.
150.Re-check after 24 hours (gasket relaxation).

9. Pressure Testing and Commissioning

9.1 Hydrostatic Test

The hydrostatic test is mandatory before any pressure piping is placed into service. Requirements per CSA B51:

Test pressure: 1.5 × the design pressure (minimum 150 kPa).
Duration: Maintain the pressure for at least 10 minutes after stabilization.
Fluid temperature: Must not exceed 50 °C to avoid vaporization risks.
Verification: Inspect all joints, flanges, and welds for leaks.

9.2 Pneumatic Test

Used when a hydrostatic test is impossible (weight of water, sensitive materials). More dangerous:

Test pressure: 1.1 × the design pressure.
Safety zone: Keep personnel clear during the test.
Use nitrogen or dry air.

9.3 Test Procedure

165.Filling: Fill the system slowly, purging air through the vents.
166.Pressure ramp-up: Increase in stages of 10% of the test pressure.
167.Stabilization: Wait for temperature and pressure to stabilize.
168.Hold: Maintain the pressure for the required duration.
169.Inspection: Check each joint with a leak detector or visually.
170.Depressurization: Release the pressure slowly and drain.

9.4 Purging and Flushing

Before commissioning:

Flushing: Circulate clean water to remove debris.
Purging: Evacuate air and gases from high points.
Drying: For gas systems, dry with nitrogen.

10. Boiler-Specific Systems

10.1 Feedwater Line

Must be equipped with a check valve and an isolation valve.
Line pressure must be higher than boiler pressure.
An economizer may be installed to improve efficiency.

10.2 Main Steam Line

Must be fitted with a steam separator.
Steam traps must be installed at low points.
The minimum slope is 10 mm per metre in the direction of flow.

10.3 Blowdown Line

The quick-opening blowdown valve must be installed close to the boiler.
Blowdown must be directed to a blowdown tank.
Never close the quick-opening valve before the slow-opening valve.

10.4 Condensate System

Condensate returns to the boiler by gravity or pump.
Condensate pipes must be insulated to prevent heat loss.
A condensate filter protects the boiler from impurities.

11. Safety During Installation

11.1 Specific Hazards

Burns: Hot piping, steam, welding.
Cuts: Sharp edges, cutting burrs.
Falls: Working at height on scaffolding.
Poisoning: Residual gases, welding fumes.
Explosion: Pneumatic tests, gas leaks.

11.2 Personal Protective Equipment (PPE)

Safety helmet with chin strap.
Safety glasses and face shield.
Leather gloves for handling.
Flame-resistant clothing for welding.
Safety harness above 1.8 m.

11.3 Work Permits

Hot work permit: Required for welding, grinding, oxy-fuel cutting.
Confined space permit: For work inside tanks or pits.
Work at height permit: For work on scaffolding or platforms.

12. Reading Drawings and Symbols

12.1 Piping Symbols

SymbolMeaning
————Piping (solid line)
— — —Existing piping
════Insulated piping
Flange
Valve
Check valve
Steam trap
Expansion compensator

12.2 Common Abbreviations

AbbreviationMeaning
DNNominal diameter
PNNominal pressure
SchSchedule (wall thickness)
NPSNominal Pipe Size (inches)
BOPBottom of Pipe
CLCenterline
TOSTop of Steel

12.3 Reading Isometric Drawings

Isometric drawings represent piping in three dimensions on a flat surface. Rules:

The three axes are drawn at 30°, 90°, and 150°.
Dimensions are given in millimetres or inches.
Elevations are given relative to a reference point (usually finished floor level).
Valves and fittings are represented by standardized symbols.

13. Practical Calculations for the Exam

13.1 Wall Thickness Calculation

Per ASME B31.1, the minimum wall thickness is calculated:

t = (P × D) / (2 × (S × E + P × Y))

Where:

t = minimum thickness (mm)
P = internal design pressure (MPa)
D = outside diameter (mm)
S = allowable stress of the material (MPa)
E = joint quality factor (0.85 to 1.0)
Y = temperature coefficient (0.4 for carbon steel ≤ 480 °C)

Example: Pressure of 10 MPa, outside diameter of 168 mm, allowable stress of 120 MPa, E = 1.0, Y = 0.4.

t = (10 × 168) / (2 × (120 × 1.0 + 10 × 0.4)) = 1680 / (2 × 124) = 1680 / 248 = 6.77 mm

Choose the schedule whose thickness is ≥ 6.77 mm (Sch 40 for DN 150 has a thickness of 7.11 mm).

13.2 Pressure Drop Calculation

The pressure drop in piping is calculated using the Darcy-Weisbach formula:

ΔP = f × (L/D) × (ρ × v² / 2)

Where:

ΔP = pressure drop (Pa)
f = friction factor (dimensionless)
L = pipe length (m)
D = inside diameter (m)
ρ = fluid density (kg/m³)
v = fluid velocity (m/s)

13.3 Unit Conversions

UnitEquivalent
1 in25.4 mm
1 ft0.3048 m
1 psi6.895 kPa
1 bar100 kPa
1 MPa145 psi
1 kg/cm²98.1 kPa
1 BTU1.055 kJ
1 hp0.746 kW

14. Pitfalls to Avoid

253.Confusing design pressure and test pressure: The hydrostatic test pressure is 1.5 × the design pressure, never the reverse.
254.Forgetting thermal expansion: A 30 m pipe at 200 °C expands more than 6 cm. Never neglect this calculation.
255.Forcing flange alignment: Never use a jack or chain to force alignment. This creates dangerous residual stresses.
256.Ignoring supports: A missing or poorly positioned support can cause catastrophic failure.
257.Using the wrong material: Always verify material compatibility with the fluid being carried and the service temperature.
258.Incorrect bolt tightening: Always tighten in a cross pattern and in successive passes. Uneven tightening causes leaks.
259.Neglecting air purging: Residual air in piping can cause destructive water hammer.
260.Confusing the standards: CSA B51 applies to boilers and pressure vessels; CSA B149.1 applies to gases; ASME B31.1 applies to power piping. Choose the correct standard based on context.
261.Forgetting tolerances: Alignment tolerances are precise. A 2 mm deviation may be acceptable for a large pipe but fatal for a small one.
262.Working without permits: Hot work and confined space permits are mandatory. Their absence can lead to penalties and accidents.

15. Exam Tips

Memorize the expansion coefficients: carbon steel 0.0117; stainless steel 0.0173; copper 0.0165.
Know the test pressures: 1.5 × design pressure for hydrostatic; 1.1 × for pneumatic.
Remember support spacing: 2.5 m for DN 25; 3 m for DN 50; 4 m for DN 100 (gas).
Identify symbols: You will have questions on isometric drawings and valve symbols.
Practice the calculations: Wall thickness, expansion, pressure drop. These calculations appear regularly.
Re-read the questions: Examiners often trap with mixed units (inches vs. millimetres, psi vs. MPa).

Summary

Boilermaker piping installation concerns systems directly connected to boilers and pressure vessels: feedwater, steam, blowdown, condensate, and gas.
Key standards are CSA B51 (boilers and pressure piping), CSA B149.1 (gas), and ASME B31.1 (power piping).
Flange alignment requires precise tolerances: parallelism of 0.25 mm/100 mm, bolt hole alignment to 1.5 mm.
Thermal expansion is calculated with ΔL = α × L × ΔT. For carbon steel, α = 0.0117 mm/m·°C.
Compensators absorb expansion; they require correctly positioned guides and anchors.
Supports must respect maximum spacing based on diameter and fluid.
The hydrostatic test is performed at 1.5 × the design pressure; the pneumatic test at 1.1 ×.
Wall thickness calculations use the ASME B31.1 formula: t = (P × D) / (2 × (S × E + P × Y)).
Safety requires work permits, appropriate PPE, and compliance with purging and flushing procedures.
Common pitfalls include confusing pressures, forgetting expansion, forcing alignments, and choosing the wrong materials.

Pitfalls to Avoid

PitfallConsequenceSolution
Confusing design pressure and test pressurePipe ruptureRemember: test = 1.5 × design
Neglecting thermal expansionDeformation, leaks, ruptureAlways calculate ΔL = α × L × ΔT
Forcing flange alignmentResidual stresses, leaksCut and readjust the pipe
Uneven bolt tighteningFlange leaksTighten in a cross pattern in successive passes
Wrong material selectionCorrosion, ruptureVerify fluid/temperature compatibility
Forgetting supportsExcessive sag, ruptureRespect maximum spacing
Ignoring air purgingWater hammerPurge from high points before commissioning
Confusing CSA B51 and CSA B149.1Applying the wrong standardIdentify the fluid and context
Neglecting alignment tolerancesPremature wear, leaksMeasure with dial indicator or laser
Working without permitsAccidents, penaltiesObtain permits before any work

This chapter has prepared you to master the installation and alignment of piping according to Red Seal requirements. Review the formulas, tolerances, and standards. Good luck with your preparation!

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