Piping Stress Analysis and Flexibility Design: Supports, Nozzle Loads and Expansion Joints – London, 4–15 Oct 2027
DestinationLondon
Dates4 – 15 October 2027
Reference464_14338
This session
4–15 Oct 2027
This Piping Stress Analysis and Flexibility Design: Supports, Nozzle Loads and Expansion Joints session in London runs from Monday 4 October to Friday 15 October 2027 (week 40, Q4 2027). It is the 2nd of 2 dates in London in 2027, at a fee of 41,400 SAR, the same for each of them. Registration is open for this date. It is held in person at Central London four-star.
DatesMonday 4 Oct – Friday 15 Oct 2027
Week40 of 2027
Duration12 days
Fee41,400 SAR
StatusOpen for registration
FormatIn person
VenueCentral London four-star
Programme overview
Introduction:
Piping stress analysis decides whether hot lines crack at elbows, overload pump nozzles, lift off supports or leak at flanges once a plant heats up. Many projects still release stress-critical lines with incomplete input data, unchecked spring hangers and nozzle loads nobody compared with vendor limits. This Core Concept course trains piping and mechanical engineers to calculate flexibility, design restraint schemes, check equipment nozzles and expansion joints, and run a software stress model from load cases to a signed report. Participants produce a Pump Suction and Discharge Piping Stress Analysis Report.
Course Objectives:
Select stress-critical lines and the right analysis method, and assemble the input data a stress model needs
Evaluate sustained, displacement and occasional stresses against ASME B31.3 allowables using stress intensification factors
Design flexibility and restraint schemes with loops, guides, line stops, anchors and spring hangers
Check pump, compressor, turbine, vessel and tank nozzle loads against the applicable equipment standards and vendor limits
Specify occasional load cases and select bellows expansion joints for lines where layout flexibility is not enough
Build, run and troubleshoot a pipe stress software model and issue a stress report with support loads and hold points
Target Audience:
Engineers who perform flexibility and code stress calculations on process and utility piping
Piping layout designers who route lines and locate supports around equipment and pipe racks
Rotating equipment engineers who accept or reject piping loads on pumps, compressors and turbines
Static equipment engineers who review nozzle loads and local stresses on vessels, exchangers and tanks
Pipe support and civil interface engineers who size supports from reported restraint loads
Engineering checkers who review stress models and reports before line release
Course Outline:
Day 1: Stress Analysis Purpose, Scope and Stress-Critical Line Selection
Piping Stress Analysis Objectives: Code Stress, Equipment Loads and Support Loads
ASME B31.3 and ASME B31.1 Flexibility Analysis Requirements Compared
Stress-Critical Line List Criteria: Temperature, Pipe Size and Connected Equipment
Stress Input Data Register: Isometrics, Line List, Equipment Drawings and Design Conditions
Day 2: Code Stress Categories and Allowable Stress Basis
Sustained Longitudinal Stress From Pressure, Weight and Insulation
Displacement Stress Range and the Cyclic Reduction Factor
Occasional Stress Evaluation and the Allowable Stress Increase Principle
Stress Intensification and Flexibility Factors for Elbows, Tees and Branch Fittings
Hot and Cold Allowable Stress Values From the Code Material Tables
Day 3: Thermal Growth, Layout Flexibility and Restraint Design
Thermal Growth Calculation From Mean Expansion Coefficient Tables and Anchor Movements
Expansion Loops, Offsets and Directional Changes as Flexibility Devices
Restraint Functions: Resting Supports, Guides, Line Stops and Directional Anchors
Variable and Constant Spring Hanger Selection and Load Variation Checks
Friction, Gaps and Lift-Off Effects at Shoes, Trunnions and Dummy Legs
Day 4: Equipment Nozzle Load Limits for Rotating and Static Equipment
API-610 Allowable Nozzle Loads for Centrifugal Pump Suction and Discharge
API-617 Nozzle Force and Moment Checks for Compressors
NEMA-SM23 Steam Turbine Nozzle Load Evaluation at Overview
Vessel and Tank Nozzle Local Stresses With WRC 107/297 Concepts and API-650
Air Cooler and Exchanger Nozzle Allowables Under API-661 and HEI at Overview
Day 5: Week-One Case Study: Hot Line Flexibility Hand Check
Case Brief: Hot Hydrocarbon Line From Heater Outlet to Column Inlet
Guided Cantilever Hand Calculation for a Candidate Expansion Loop
Support Scheme Mark-Up on the Isometric: Guides, Stops and Spring Locations
Nozzle Load Screening Against Vendor Allowable Tables
Week-One Findings Review and Stress Input Data Gaps Log
Day 6: Occasional Loads and Dynamic Effects on Piping
Wind Load Application on Elevated and Pipe Rack Lines
Seismic Static Coefficient and Response Spectrum Methods at Overview
Relief Valve Discharge Thrust in Open and Closed Systems
Slug Flow and Water Hammer Force Estimation for Restraint Sizing
Modal and Harmonic Analysis for Vibrating Lines at Overview
Day 7: Expansion Joints, Flange Leakage and Design Risk Controls
Untied, Tied, Hinged and Gimbal Bellows Configurations and Pressure Thrust
Bellows Selection Under EJMA Standards: Cycle Life, Spring Rate and Squirm
Flange Leakage Checks at Overview: Equivalent Pressure and EN 1591 Methods
Stress Model Design Review Checklist and Independent Checking
Change Control for Rerouted Lines, Added Supports and Revised Design Conditions
Day 8: Software Modelling Workflow and Interdisciplinary Interfaces
CAESAR II-Type Model Build: Nodes, Elements, Material and Section Properties
Restraint, Hanger and Nozzle Flexibility Modelling in Pipe Stress Software
Load Case Set-Up: Operating, Sustained, Expansion and Occasional Combinations
Restraint Load Transfer to Civil and Structural Teams at Pipe Racks
Nozzle Load Resolution Meetings With Rotating Equipment Vendors
Day 9: Results Review, Iteration and Stress Deliverable Metrics
Code Compliance Output: Stress Ratios and Highest Stressed Nodes
Displacement, Restraint Load and Spring Hanger Table Review
Overstress Troubleshooting: Rerouting, Added Flexibility or Restraint Changes
Stress Report Structure: Basis, Assumptions, Load Cases, Results and Hold Points
Stress Deliverable Tracking: Line Coverage, Rework Rate and Checker Findings
Day 10: Capstone: Pump Suction and Discharge Stress Analysis
Capstone Data Pack: Pump Datasheet, Isometrics and Operating Scenarios
Model Build of Parallel Pump Lines With Running and Standby Cases
Pump Nozzle Compliance and Support Scheme Optimisation
Pump Suction and Discharge Piping Stress Analysis Report Drafting
Capstone Presentation and Peer Challenge of Model Assumptions
Skills You Will Gain:
Pipe Flexibility Calculation
Code Stress Evaluation
Restraint Scheme Design
Spring Hanger Sizing
Equipment Nozzle Load Assessment
Bellows Expansion Joint Selection
Pipe Stress Software Modelling
Stress Report Preparation
Why Attend This Course:
Return with a Pump Suction and Discharge Piping Stress Analysis Report built from a working software model
Resolve nozzle overloads and support conflicts before they turn into site rework or equipment misalignment
Defend a stress-critical line list and load case set to checkers, vendors and project managers
Compare stress practice with engineers from refining, petrochemicals, gas processing, power and utilities
Conclusion:
Piping stress analysis protects equipment and supports only when inputs, load cases and restraint assumptions match how the line will operate. The first week moves from stress-critical line selection and code stress categories through thermal growth, restraint design and equipment nozzle limits to a hand-check case study. The second week adds occasional and dynamic loads, bellows expansion joints, flange leakage, software modelling, results review and reporting, and ends with a Pump Suction and Discharge Piping Stress Analysis Report ready for checking and line release.
Piping Stress Analysis and Flexibility Design: Supports, Nozzle Loads and Expansion Joints runs in London over 12 days, with 2 upcoming dates in London. The course fee is 41,400 SAR.
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