Section
Piping
The piping body of work, end to end: materials and specification, layout and supports, fabrication and welding, testing and erection, and in-service inspection.
- Topics
- 53
- Standards covered
- 93
Materials & specification
What a line is made of and how the specification says so. Pipe and plate materials, sizes and schedules, fittings, valves, flanges, gaskets and bolting — ending at the line class that pulls them together.
11 topics
Beginner
No prior knowledge assumed
Pipe materials — what the grade on the spec actually means
A106, A312, P11 — how to read a piping material grade, why carbon steel is the default, and what forces an upgrade to alloy or stainless.
Plate materials — what vessels and tanks are actually made from
A516, A240, Monel, Hastelloy and titanium — why a plate specification is not a pipe specification, what each alloy is bought to survive, and why you almost never buy a solid exotic vessel.
Pipe sizes and schedules — why NPS 2 is not 2 inches
NPS, DN and schedule numbers explained. Why the outside diameter is fixed, what changes when the schedule goes up, and how to read a pipe size chart.
Line sizing — why pipe diameter is an economic decision
The two criteria that size every line, why a bigger pipe costs once and a smaller one costs forever, and the lines where neither rule applies.
Fittings and branch connections — how a pipe changes direction
Elbows, tees, reducers and caps, and the branch fittings that take a small line off a big one. What each is for, why the dimensions are fixed, and why a branch needs reinforcement.
Valve types — picking one for the duty, not the drawing
Gate, globe, ball, butterfly and check valves explained by what each is built to do. Why throttling with a gate valve destroys it, what double block and bleed means, and how check valves slam.
Intermediate
Builds on the basics
Valve actuation and fail position — deciding what happens when everything stops
Pneumatic, electric and hydraulic actuators, why a spring is what makes fail-safe possible, how fail open and fail closed are chosen per service, and what a positioner actually does.
Flanges and pressure classes — why Class 150 is not 150 psi
What a flange class means, how pressure–temperature ratings work, the common facing types, and why a gasket and bolt set are part of the rating.
Gaskets and bolting — why most flange leaks are assembly, not hardware
How a bolted joint actually seals, reading a spiral wound gasket by its colours, choosing stud and nut materials, and the bolt-up sequence that decides whether any of it works.
Reading a line class — the document that has already decided
How a piping material specification works, how to decode a line number, what a spec break is, and why almost every piping decision on a project was made before you arrived.
Advanced
Design and compliance detail
Layout & supports
Where the line runs and what holds it up. Supports and restraint, expansion loops and joints, spring hangers, nozzle loads, pump piping, plot plan and the access a line needs to be maintained.
11 topics
Intermediate
Builds on the basics
Pipe supports and thermal expansion — why you cannot just bolt it down
Hot pipe grows, and it grows with enormous force. How expansion is calculated, why loops exist, what anchors, guides and spring hangers actually do, and how supports protect equipment nozzles.
Expansion loops and offsets — sizing the detour that absorbs the growth
How a loop actually absorbs movement, the guided cantilever hand calculation that gives you a first size, why the answer never fits the rack, and the honest ranking of what to do when it does not.
Pipe support standards and details — reading SP-58, SP-69 and a project detail sheet
What the support standards actually fix, why a project standard detail is a specification rather than a catalogue, the welded attachment problem on alloy and sour service, shoes and trunnions and shields, and what goes wrong when a support is left to the field.
Pump piping layout — the suction side is where the decisions are made
NPSH available as a consequence of layout rather than a number handed to you. Eccentric reducers and the pocket they prevent, straight run before the impeller, the elbow that must not be in the shaft plane, parallel pump symmetry, strainers, minimum flow, and the discharge order.
Plot plan and equipment spacing — the drawing everything else inherits
What actually sets the distance between equipment, the four drivers that pull against each other, the pipe rack as the spine and how its tiers are allocated, prevailing wind and fired equipment, roads and containment, and why a plot plan mistake cannot be recovered downstream.
Access, operability and maintenance space — what the plant is judged on afterwards
Valve reach and stem orientation, why a chain operator is a confession, platforms and the dead-end with one ladder, headroom, bundle pull and rotor withdrawal, drop-out areas and davits, and the model review that is the last chance to find any of it.
Advanced
Design and compliance detail
Expansion joints and bellows — pressure thrust and why they are the last resort
What a bellows can and cannot absorb, the pressure thrust that dwarfs the thermal force it was fitted to relieve, tied and hinged and gimbal arrangements, guide spacing, cycle life, and the installation errors that kill them early.
Anchors, guides and restraint schemes — deciding where the pipe may move
A restraint scheme is one decision for a whole run, not a scatter of supports. Where an anchor belongs, what it actually carries once friction is counted, line stops against full anchors, the gap that is the design, and the accidental anchors that site creates.
Spring hanger selection — variable, constant, and the pin nobody pulled
Choosing a spring for a line that moves vertically. Hot and cold load, the load variation limit and when it forces a constant effort unit, travel and rod swing, why the pointer is the most useful thing on a walkdown, and the installation errors that make a spring worse than no spring.
Nozzle loads and allowables — the constraint that really governs hot piping
Why machine nozzle allowables are so small, where they come from for pumps, compressors, turbines and vessels, what exceeding them actually does, why the symptom surfaces in somebody else's report, and the design and field rules that prevent it.
Relief valve and flare piping — the 3 per cent rule, backpressure and reaction force
The piping engineer's half of overpressure protection. Why a relief valve inlet must be short and generous, what chatter actually is, built-up and superimposed backpressure and the 10 per cent limit, reaction force on an open discharge, flare header slope, and the car-sealed valve that must never be closed.
Fabrication, welding & NDE
How a joint is made and how it is proved. Welding processes, WPS and PQR, Section IX variables, welder qualification, fit-up and heat treatment, non-destructive examination and the test plans that govern them.
11 topics
Intermediate
Builds on the basics
Welding processes, WPS and NDT — what happens before an arc is struck
SMAW, GTAW, GMAW and the rest, explained by what they are good at. Then the paperwork that makes a weld legal — WPS, PQR and welder qualification — and how welds are inspected.
Reading a WPS and a PQR — what is on the sheet and what the tests proved
The practical document skill — what each field on a welding procedure specification is for, what a qualification record actually recorded, and what tensile, bend, impact, macro and hardness results each demonstrate about the joint.
Welder qualification and continuity — the ranges a ticket covers, and the register nobody updates
What a welder performance qualification actually establishes, the ranges it carries in thickness, diameter, position and process, how continuity lapses at six months, and why the expired ticket is always found after the weld is made.
Joint preparation and fit-up — the hold point you only get once
Bevels and root gaps, internal misalignment and the limits on it, why trimming or counterboring is allowed where grinding the bore is not, tack welds as part of the final weld, and what an inspector checks in the minutes before the root goes in.
Non-destructive examination — choosing the method and reading the result
Why every NDE method is blind to something, what magnetic particle cannot do on stainless, why ultrasonics can miss a crack lying the wrong way, the difference between an indication and a defect, and why the examiner's qualification is part of the result.
Inspection and test plans — hold, witness, review, and who signs
What an ITP actually is, how it is built line by line from the code and the specification, what each of the four intervention levels obliges, why a document full of hold points is worse than a short one, and the notification failure that turns a witness point into nothing.
Non-conformance and corrective action — the four dispositions, and why NCRs repeat
Writing an NCR somebody can act on, the difference between rework, repair, use-as-is and reject, who may grant a concession, and why closing non-conformances one at a time without ever raising a corrective action guarantees the same defect next week.
Inspector competence and certification — who may interpret, and who only operates
SNT-TC-1A as an employer's written practice rather than a certificate, ISO 9712 as the independent route, what Levels I, II and III may each do, and why the inspector's own qualification is the first thing a client audits.
Advanced
Design and compliance detail
Section IX essential variables — what invalidates a procedure qualification
Why a WPS can be revised freely in some respects and requalified from scratch in others. Essential, non-essential and supplementary essential variables, the ranges a PQR actually qualifies, and the low-temperature trap that turns a harmless change into a requalification.
Preheat and post-weld heat treatment — hydrogen, hardness, and reading the chart
What preheat is actually for, why interpass temperature has a ceiling as well as a floor, when PWHT is required and when it may be exempted, how to read a chart recorder trace against the specified cycle, and the hardness survey that decides it in sour service.
Examination extent and progressive sampling — what five per cent actually obliges
How fluid service sets the amount of examination, why the sample has to represent each welder on each procedure, and the progressive sampling rule that turns one rejected weld into a widening scope — the part of Chapter VI taught almost nowhere.
Testing, erection & supervision
Getting the line installed and signed off. Isometrics to installed spools, rigging and scaffold, pressure test packs, tie-ins and shutdown windows, progress measurement and the site records that support a claim.
12 topics
Beginner
No prior knowledge assumed
Intermediate
Builds on the basics
From isometric to installed line — fabrication, erection and testing
How to read a piping isometric, why spool breaks decide what happens in the shop and what happens at height, and the test and reinstatement sequence that gets a line handed over.
Erection sequence and constructability — why the isometric order is not the build order
Why the number on an isometric says nothing about what has to be built first, how access is lost and regained, the dependencies that decide a piping sequence, and the habit of working backwards from the date that cannot move rather than forwards from today.
Spool handling and temporary support — the hours between landed and supported
The period in which a spool has been released by the crane but does not yet have the supports it was designed to have, why that state has no design behind it, what has to be established before the hook comes off, and why Friday afternoon is when pipe ends up on the floor.
Lift plans and rigging basics — sling angle, centre of gravity, and the reasons to stop
What a lift plan has to state before anybody touches a spool, why the tension in a sling leg is not the load divided by the number of legs, how an offset centre of gravity behaves, and the short list of conditions under which a supervisor stops a lift regardless of who is waiting.
Pressure test packs and reinstatement — the gate, and what gets put back afterwards
What a test pack contains and why it is built as the work proceeds, the procedure and the calibrated gauge, the falling pressure that is temperature rather than a leak, and the reinstatement register that is what actually keeps a tested system honest.
Diameter-inch and progress measurement — the unit piping is paid in
What a diameter-inch is and how it is counted, why it under-represents small bore, the difference between claimed and earned progress, the measurement rule that has to be agreed before work starts, and why the last ten per cent of a piping package takes months.
Construction productivity factors — why the same weld takes three times as long
Why a norm measured in the shop does not survive contact with a live unit, the conditions that multiply the hours without changing the work, crew composition and what a waiting welder costs, and the difference between a crew that is busy and a crew that is producing.
Supervising under a permit — the shift you signed for
Not what a permit is, which is covered elsewhere and free, but what changes when you are the person who signed it — what to verify at the work rather than on the form, the conditions routinely accepted and not met, why a gas test expires, and what handing back actually requires.
Site records and the daily diary — writing for somebody who will not believe you
Why the site diary is the most valuable document a supervisor produces, what distinguishes an entry that is evidence from one that is worthless, what to record every day regardless, and why contemporaneous matters more than detailed.
Variations, backcharges and notice — the difference between noticing and notifying
How to recognise an instruction that is really a variation, why the entitlement usually depends on the notice rather than the change, what a backcharge is and how it runs in both directions, and the one-sentence note that protects a position without starting an argument.
Advanced
Design and compliance detail
Inspection & integrity
The forty years after handover, and the core of the API 570 syllabus. Damage mechanisms, corrosion loops and circuits, integrity operating windows, and risk-based inspection from assessment to recommendation.
8 topics
Intermediate
Builds on the basics
Vessels, exchangers and relief devices — the static equipment
What MAWP means and why it matters more than design pressure, how heat exchanger types differ, and why the relief device is the one protection that cannot be bypassed.
Insulation, tracing and coatings — the layers outside the pipe
Four different reasons to insulate and why confusing them causes corrosion, how steam and electric tracing differ, why tracing fails silently, and why surface preparation is most of a paint system.
Material degradation — sensitisation, hardness limits and galvanic attack
Why welding can ruin the corrosion resistance of stainless steel without touching the weld, what the three conditions for galvanic corrosion are and which one to break, why sour service controls hardness rather than strength, what carbon equivalent predicts, and why zinc and stainless are kept apart.
Risk-based inspection — deciding what to inspect, and how often
Why nobody inspects everything equally, how likelihood and consequence combine into an inspection plan, why naming the damage mechanism is the whole job, and the ways an RBI programme quietly goes wrong.
Advanced
Design and compliance detail
Corrosion loops and piping circuits — the two groupings an RBI study is built on
Why a corrosion loop and a piping circuit are different things, how each one is drawn and bounded, what goes wrong when a circuit is too big or a loop mixes two streams, and why every number downstream depends on getting these right.
Corrosion control documents — writing down why the plant corrodes
What a CCD is for, what API 970 expects it to contain, what happens in a corrosion workshop and why the operators in the room change the answer, and why a document written once and never reopened has already failed.
Integrity operating windows — limits that protect the metal, not the product
What an IOW is and how it differs from a process alarm or a safety trip, the three tiers in API 584, why an exceedance invalidates the inspection plan rather than causing immediate failure, and why windows nobody implemented are the usual outcome.
Running an RBI assessment — from data to an inspection plan that happens
How probability and consequence of failure are actually estimated, why inventory group and detection time decide consequence more than vessel size does, what inspection effectiveness really changes, and why most RBI programmes fail after the study rather than during it.
Standards referenced in this section
- API 14E
- API 510
- API 520
- API 521
- API 553
- API 570
- API 571
- API 574
- API 577
- API 579
- API 580
- API 581
- API 583
- API 584
- API 594
- API 5L
- API 600
- API 607
- API 608
- API 609
- API 610
- API 617
- API 653
- API 660
- API 686
- API 6D
- API 752
- API 753
- API 941
- API 970
- ASME B16.11
- ASME B16.20
- ASME B16.21
- ASME B16.25
- ASME B16.28
- ASME B16.34
- ASME B16.47
- ASME B16.5
- ASME B16.9
- ASME B30.26
- ASME B30.5
- ASME B30.9
- ASME B31.1
- ASME B31.3
- ASME B36.10M
- ASME B36.19M
- ASME BPVC VIII
- ASME PCC-1
- ASME Section II Part C
- ASME Section IX
- ASME Section V
- ASME Section VIII
- ASNT SNT-TC-1A
- ASTM A106
- ASTM A193
- ASTM A194
- ASTM A240
- ASTM A312
- ASTM A320
- ASTM A333
- ASTM A335
- ASTM A36
- ASTM A516
- ASTM B127
- ASTM B265
- ASTM B575
- AWS A3.0
- AWS D1.1
- EJMA
- EN 10164
- EN 10204
- EN 12811-1
- IEC 60534
- IEC 61511
- IEEE 515
- ISO 12480-1
- ISO 12944
- ISO 15156
- ISO 17637
- ISO 21508
- ISO 45001
- ISO 9001
- ISO 9712
- MSS SP-58
- MSS SP-69
- MSS SP-97
- NACE MR0175
- NAMUR NE 43
- NEMA SM-23
- NFPA 59A
- OISD-STD-118
- TEMA
- WRC 537
