Module 9 — Welding, Fabrication & Metallurgy · LEO Technical Academy
Lesson 9.4 — Pipe Schedules, Pressure Ratings, and Sizing Standards
Level 2 (1–2 Years Experience) 🔥 Fabrication ⏱ 50 min Intermediate LEO-ACE-09-004 v1.0 · 2026-11-02
📌 Training Use Only
This lesson builds knowledge. Completing it does not authorize field work, equipment servicing, LOTO, energized testing, or customer-site activity. Site rules, your supervisor, and required LEO Safety Training govern all work. Stop-Work Authority is absolute.
§01 — Learning Objectives

Learning Objectives

By the end of this lesson, the technician will be able to:

§02 — Field Scenario

Field Scenario

The Nipple That Matched Everything Except the Spec: A small leak at a threaded connection on a 300 PSI compressed-air header (Lesson 8.9's world) needs a new 1" nipple. The stores bin labeled "1-inch nipples" offers plenty; a technician grabs one, threads it in with sealant, tests it — holds fine. Job closed.

Four months later that nipple lets go — not at the threads, but through the wall, splitting under a pressure spike the header sees every compressor cycle. The investigation measures the failed part: Schedule 40? No — it mics out as light-wall (Schedule 10-class) stainless, from a batch bought years ago for a low-pressure drain project and shelved into the generic bin. Same NPS, same threads cut into a wall never intended to carry threads at pressure (thread roots cut into the wall — light-wall threaded connections lose most of their already-thin section), on a header whose line specification calls for Schedule 80 carbon steel for threaded small-bore at that pressure class.

Three system failures stacked: a stores bin organized by size instead of by specification; a selection made by "fits and holds" instead of by the line's spec class (the 10.6 discipline — every line has a specification listing exactly which pipe, fittings, and ratings belong on it); and a pressure-boundary repair executed without the document that governs it. The corrected practice: pull the line class from the line number (1"-IA-2204-A1 — that suffix is the spec), match the nipple to the spec sheet (schedule, material, end type), and disposition the contaminated bin. On pressure systems, "it fits" is not a criterion. The specification is the criterion — and wall thickness is the part you can't see once it's threaded in.

§03 — Concept Overview

Concept Overview

NPS and Schedule — the System's Two Numbers

Pipe is named by NPS (Nominal Pipe Size) — and nominal means it: a "1-inch" pipe has an actual OD of 1.315"; NPS 2 = 2.375" OD; NPS 4 = 4.500" OD. (At NPS 14 and above, OD finally equals the name.) The system's genius and its trap live in the same rule:

For a given NPS, the OD never changes. Schedule changes the wall thickness — inward.

Where Pressure Capability Comes From

A pipe's pressure rating is an engineering output (Barlow's-formula territory: pressure capability rises with wall thickness and material strength, falls with diameter), governed by the piping codes (ASME B31.1 power / B31.3 process). The technician doesn't run the calculation — but must own its consequences:

Flange Classes — the Companion Rating System

Flanged joints carry class ratings — 150, 300, 600 (and up) per ASME B16.5 — pressure-temperature envelopes, not PSI values (a Class 150 carbon flange is good for ~285 PSI at ambient, sliding down as temperature rises — the tables govern). Field rules:

The Spec Class — the Document That Decides

Every engineered line carries a piping specification (line class) — the suffix in the line number (10.2/10.6's grammar) keying to a spec sheet that lists, for that service and rating: pipe material and schedule by size range, fitting types and classes, flange class and facing, gasket spec, bolting spec, valve trim, branch rules (when a weldolet vs. a tee), and examination requirements. Repair matching means matching the spec, not the neighboring metal — the adjacent pipe might itself be a prior unauthorized substitution (10.9's discovered-discrepancy world).

§04 — How the Principle Works

How the Principle Works: Identifying and Matching Pipe in the Field

  1. Read before measuring: line number stencils (the class suffix), material stencils on the pipe, stamps on fittings/flanges (class, material, schedule on butt-weld fittings), the iso's BOM (10.6). The documentation chain is identification done right.
  2. Measure when reading fails: OD with a tape/caliper → NPS from the OD table (1.315 = NPS 1; 2.375 = NPS 2...). Wall: at an open end with a caliper, or ultrasonic thickness gauge on closed systems — measured wall vs. the schedule tables gives the schedule (and, trended, the corrosion story; significant wall loss vs. nominal is an engineering finding, not a note).
  3. Never identify by what threads onto it or what it "matches": the Field Scenario's bin proved fit is no test. Schedules share threads; materials share dimensions.
  4. Match repairs to the spec class — pipe, fitting class, flange/gasket/bolting — with the spec sheet physically in hand (or its controlled digital twin), and the materials' pedigree verified (stencils/certs per site requirements).
  5. The boundary stack for any pressure-boundary work: opening the line = 1.7's line-breaking controls; welded repairs on pressure boundaries = certified welders under qualified procedures with required examination (9.5/9.7/9.8) — squarely 9.10 sign-off territory; threaded/flanged component replacement = within technician scope per the spec, under isolation, with the joint reassembled to specification. When the spec sheet is missing, ambiguous, or contradicted by the field — engineering, before parts.
§05 — Reference Matrix

Pipe System Reference Matrix

NPS Actual OD Sch 40 Wall / ID Sch 80 Wall / ID
1/2 0.840" 0.109" / 0.622" 0.147" / 0.546"
1 1.315" 0.133" / 1.049" 0.179" / 0.957"
2 2.375" 0.154" / 2.067" 0.218" / 1.939"
4 4.500" 0.237" / 4.026" 0.337" / 3.826"
6 6.625" 0.280" / 6.065" 0.432" / 5.761"

(Representative values — the published tables govern; STD=Sch 40, XS=Sch 80 through these sizes.)

Element Rule Failure If Ignored
OD fixed per NPS Identification by OD table Mis-sized fittings, wrong NPS calls
Schedule = wall, inward Wall is invisible installed The Field Scenario
Threading cuts the wall Threaded small-bore jumps schedules per spec Split nipples at pressure
Temperature derates Ratings are P-T envelopes "Rated 285 PSI" failing hot
Flange class (150/300/600) Stamped on the flange; match line class Built-in weak point
Gasket/bolting per joint spec 10.6 BOM + 1.7 reassembly + 3.5 torque Leaks, blown gaskets, injury
Spec class governs all components The line-number suffix is the law Bin-label engineering
Pipe ≠ tube Different sizing, different fittings Cross-bred connections leak/fail
§06 — Field Application Checklist

Field Application Checklist: Pressure-Boundary Component Replacement (Threaded/Flanged, Within Spec)

  1. Boundaries first: isolation, depressurization, drain/vent, and zero-energy verification per Lessons 1.2/1.3/1.7 (with accumulator/receiver awareness per 8.7/8.9). No-hands leak rule (8.1) on anything suspect before isolation.
  2. Pull the governing documents: line class spec sheet (via the line number), the iso/P&ID (10.6/10.2, current rev per 10.1), and the joint's gasket/bolting spec.
  3. Identify what's actually there (Section 4's read-then-measure), and reconcile against the spec — existing nonconformances found during the job (the prior bad nipple, the wrong-class flange) are discovery findings (10.9 + immediate escalation where safety-relevant), not patterns to copy.
  4. Procure by specification: material grade, schedule/class, end type — verified by markings on receipt, charged to the asset (10.8). No bin-label trust on pressure parts; mis-binned stock gets reported and quarantined.
  5. Make the joint per the rules: threaded — correct sealant per spec/service, proper engagement, no doping over bad threads; flanged — specified gasket (new, never reused), specified studs/nuts, faces inspected, bolting pattern and torque per spec (3.5).
  6. Examine and test per the spec class: the line's specification states the required examination/leak-test for the work performed (service test, pressure test requirements where invoked are engineering-administered) — the spec, not habit, decides what "done" requires.
  7. Restore and verify in service: controlled re-pressurization per procedure, leak check (cardboard/soap per service — never hands), supports restored (10.6).
  8. Document: components installed with pedigree (spec, markings/heat numbers where required), torque values, test performed, and any discoveries routed — the 10.8 record that makes the pressure boundary auditable.
§07 — Knowledge Check

Knowledge Check

During a steam-line repair (line 2"-LS-1808-B2; the B2 spec sheet specifies: NPS 2, Sch 80 A106-B pipe, Class 300 flanges raised-face, spiral-wound gaskets spec G-7, B7 studs with 2H nuts, torque table T-3), a technician finds the failed section's mating flange is stamped "150" — apparently installed in a previous undocumented repair. Stores can supply everything to the B2 spec today except the spiral-wound gaskets; the storeroom offers red-rubber sheet gasket "that we use everywhere" as a substitute so the line can return tonight. The supervisor suggests: reuse the existing Class 150 flange since it "held for years," cut the new gasket from red rubber, and get steam back up. What is the correct disposition?
§08 — Source List

Source List

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