Standards index
Every code cited on this site, and where it is explained. 147 standards across29 publishing bodies.
These pages explain what a standard means and how it is used. They are not a substitute for it — buy and work to the current edition.
ACI
AISC
API
API 553
API 556
- PipingSpecial piping components — the places that do not corrode like the pipe
- PipingCorrosion loops and piping circuits — the two groupings an RBI study is built on
- PipingRisk-based inspection — deciding what to inspect, and how often
- PipingRunning an RBI assessment — from data to an inspection plan that happens
- PipingReading a WPS and a PQR — what is on the sheet and what the tests proved
- PipingSection IX essential variables — what invalidates a procedure qualification
- PipingWelder qualification and continuity — the ranges a ticket covers, and the register nobody updates
- PipingJoint preparation and fit-up — the hold point you only get once
- PipingPreheat and post-weld heat treatment — hydrogen, hardness, and reading the chart
- PipingNon-destructive examination — choosing the method and reading the result
- PipingExamination extent and progressive sampling — what five per cent actually obliges
- PipingSpecial piping components — the places that do not corrode like the pipe
- PipingCorrosion loops and piping circuits — the two groupings an RBI study is built on
- PipingCorrosion control documents — writing down why the plant corrodes
- PipingIntegrity operating windows — limits that protect the metal, not the product
- PipingRisk-based inspection — deciding what to inspect, and how often
- PipingRunning an RBI assessment — from data to an inspection plan that happens
- Civil & StructuralInspecting and repairing structures — the other forty years
API 585
- PipingPipe supports and thermal expansion — why you cannot just bolt it down
- PipingAnchors, guides and restraint schemes — deciding where the pipe may move
- PipingSpring hanger selection — variable, constant, and the pin nobody pulled
- PipingNozzle loads and allowables — the constraint that really governs hot piping
- PipingPump piping layout — the suction side is where the decisions are made
- Rotating EquipmentPumps — head, NPSH and why cavitation is a suction problem
API 674
ASCE
ASME
ASME B16.28
- PipingPipe supports and thermal expansion — why you cannot just bolt it down
- PipingExpansion loops and offsets — sizing the detour that absorbs the growth
- PipingExpansion joints and bellows — pressure thrust and why they are the last resort
- PipingAnchors, guides and restraint schemes — deciding where the pipe may move
- PipingPipe support standards and details — reading SP-58, SP-69 and a project detail sheet
- PipingSpring hanger selection — variable, constant, and the pin nobody pulled
- ProcessWhat the plant actually does — the shape of a process
- ProcessReading a PFD and the material balance — where every number starts
- PipingPipe materials — what the grade on the spec actually means
- PipingPipe sizes and schedules — why NPS 2 is not 2 inches
- PipingLine sizing — why pipe diameter is an economic decision
- PipingFittings and branch connections — how a pipe changes direction
- PipingFlanges and pressure classes — why Class 150 is not 150 psi
- PipingReading a line class — the document that has already decided
- PipingPipe supports and thermal expansion — why you cannot just bolt it down
- PipingExpansion loops and offsets — sizing the detour that absorbs the growth
- PipingExpansion joints and bellows — pressure thrust and why they are the last resort
- PipingAnchors, guides and restraint schemes — deciding where the pipe may move
- PipingPipe support standards and details — reading SP-58, SP-69 and a project detail sheet
- PipingSpring hanger selection — variable, constant, and the pin nobody pulled
- PipingNozzle loads and allowables — the constraint that really governs hot piping
- PipingPump piping layout — the suction side is where the decisions are made
- PipingPlot plan and equipment spacing — the drawing everything else inherits
- PipingAccess, operability and maintenance space — what the plant is judged on afterwards
- PipingRelief valve and flare piping — the 3 per cent rule, backpressure and reaction force
- PipingWelding processes, WPS and NDT — what happens before an arc is struck
- PipingReading a WPS and a PQR — what is on the sheet and what the tests proved
- PipingSection IX essential variables — what invalidates a procedure qualification
- PipingWelder qualification and continuity — the ranges a ticket covers, and the register nobody updates
- PipingJoint preparation and fit-up — the hold point you only get once
- PipingPreheat and post-weld heat treatment — hydrogen, hardness, and reading the chart
- PipingNon-destructive examination — choosing the method and reading the result
- PipingExamination extent and progressive sampling — what five per cent actually obliges
- PipingInspection and test plans — hold, witness, review, and who signs
- PipingNon-conformance and corrective action — the four dispositions, and why NCRs repeat
- PipingFrom isometric to installed line — fabrication, erection and testing
- PipingPressure test packs and reinstatement — the gate, and what gets put back afterwards
- PipingTie-ins and shutdown windows — preparing for the hours that cannot be extended
- PipingSupervising under a permit — the shift you signed for
- Instrumentation & ControlReading a P&ID — the drawing every discipline works from
- Instrumentation & ControlInstrument installation and loop checking — where most readings go wrong
ASME B73.1
ASME BPVC VIII
- PipingWelding processes, WPS and NDT — what happens before an arc is struck
- PipingReading a WPS and a PQR — what is on the sheet and what the tests proved
- PipingSection IX essential variables — what invalidates a procedure qualification
- PipingWelder qualification and continuity — the ranges a ticket covers, and the register nobody updates
- PipingJoint preparation and fit-up — the hold point you only get once
- PipingPreheat and post-weld heat treatment — hydrogen, hardness, and reading the chart
- PipingNon-conformance and corrective action — the four dispositions, and why NCRs repeat
- PipingFrom isometric to installed line — fabrication, erection and testing
- PipingWelding processes, WPS and NDT — what happens before an arc is struck
- PipingNon-destructive examination — choosing the method and reading the result
- PipingExamination extent and progressive sampling — what five per cent actually obliges
- PipingInspector competence and certification — who may interpret, and who only operates
ASNT
ASTM
ASTM A193
ASTM A194
ASTM A240
ASTM A312
ASTM A320
ASTM A333
ASTM A335
ASTM A36
ASTM A516
ASTM B127
ASTM B265
ASTM B575
ATEX
AWS
BS
EEMUA
EJMA
EN
EN 10164
- PipingPlate materials — what vessels and tanks are actually made from
- PipingInspection and test plans — hold, witness, review, and who signs
- PipingNon-conformance and corrective action — the four dispositions, and why NCRs repeat
- PipingPressure test packs and reinstatement — the gate, and what gets put back afterwards
EN 1993
EN 206
IEC
IEC 60076
- ElectricalHazardous areas — zones, gas groups and Ex protection explained
- ElectricalCables — construction, selection and why sizing is never just about current
- ElectricalEarthing and bonding — several different jobs sharing one word
- ElectricalEx installation and inspection — where compliance is actually won or lost
- ElectricalElectrical commissioning and turnover — from dead to live
IEC 60364-5-52
IEC 60364-6
IEC 60502
IEC 61439
- PipingValve actuation and fail position — deciding what happens when everything stops
- Instrumentation & ControlReading a P&ID — the drawing every discipline works from
- Instrumentation & ControlSafety instrumented systems and SIL — the layer that acts on its own
- Instrumentation & ControlInstrument installation and loop checking — where most readings go wrong
- Instrumentation & ControlAlarm management — why an operator with 400 alarms has none
IEC 61892
IEC 62305
IEC 62424
IEEE
IEEE 142
IEEE 515
IEEE 81
IP
IP Refining Safety Code
IS
IS 1786
IS 1904
IS 3764
IS 800
ISA
- ProcessReading a PFD and the material balance — where every number starts
- Instrumentation & ControlWhat a transmitter is, and why it sends 4–20 mA
- Instrumentation & ControlReading a P&ID — the drawing every discipline works from
- Instrumentation & ControlInstrument installation and loop checking — where most readings go wrong
ISO
- PipingErection sequence and constructability — why the isometric order is not the build order
- PipingDiameter-inch and progress measurement — the unit piping is paid in
- PipingConstruction productivity factors — why the same weld takes three times as long
- PipingSite records and the daily diary — writing for somebody who will not believe you
- PipingVariations, backcharges and notice — the difference between noticing and notifying
MSS
- PipingPipe supports and thermal expansion — why you cannot just bolt it down
- PipingExpansion joints and bellows — pressure thrust and why they are the last resort
- PipingAnchors, guides and restraint schemes — deciding where the pipe may move
- PipingPipe support standards and details — reading SP-58, SP-69 and a project detail sheet
- PipingSpring hanger selection — variable, constant, and the pin nobody pulled
- PipingRelief valve and flare piping — the 3 per cent rule, backpressure and reaction force
- PipingPipe supports and thermal expansion — why you cannot just bolt it down
- PipingExpansion loops and offsets — sizing the detour that absorbs the growth
- PipingAnchors, guides and restraint schemes — deciding where the pipe may move
- PipingPipe support standards and details — reading SP-58, SP-69 and a project detail sheet
- PipingSpring hanger selection — variable, constant, and the pin nobody pulled
MSS SP-97
NACE
- PipingPipe materials — what the grade on the spec actually means
- PipingGaskets and bolting — why most flange leaks are assembly, not hardware
- PipingReading a line class — the document that has already decided
- PipingPipe support standards and details — reading SP-58, SP-69 and a project detail sheet
- PipingPreheat and post-weld heat treatment — hydrogen, hardness, and reading the chart
- PipingMaterial degradation — sensitisation, hardness limits and galvanic attack
NAMUR
NEMA
NFPA
OSHA
TEMA
UL
WRC
Other
HSG250
HSG253
HSG47
