Skip to content

Safety Valves: Inspection and Calibration per API 576 Training Course

Covers inspecting, testing and calibrating safety and pressure relief valves to API 576, protecting vessels, exchangers and piping from overpressure.

MEC · Mechanical EngineeringAll Levels#2215ClassroomEnglish , Arabic
Duration
5 Days
Download BrochureView Upcoming Dates

Free substitution at any time · 30+ days' notice: full refund minus 10%. Cancellation policy

Course Overview

Safety valves and pressure relief valves (PSV / PRV) are the last line of defense protecting pressure vessels, heat exchangers, piping, and fired heaters from overpressure in oil refineries, petrochemical plants, oil and gas facilities, and power plants. The Safety Valves: Inspection and Calibration per API 576 Training Course equips static equipment, inspection, and maintenance engineers and technicians with the technical knowledge and practical skills needed to ensure that every valve opens at the correct set pressure, reseats tightly, and operates without chatter or blockage at the moment when its performance separates safe operation from a serious incident. The course content is built on the realities of static equipment maintenance in refinery units, where specific problems recur and are well known to anyone who has worked in a valve shop or during a turnaround: valves sent for repair without an as-received test, losing critical information about their actual performance; set pressure adjusted on the test bench without correction for operating temperature or back pressure; seat leakage after reinstallation; plugged inlets and outlets in coking, polymerizing, and fouling services; corrosion of springs and internals in sour services; isolation valves inadvertently left closed after maintenance; and intense time pressure to complete hundreds of valves within a short shutdown window. The course is anchored in the requirements of API 576 for the inspection of pressure-relieving devices and links them in practical terms to the complementary standards engineers work with every day: API 520 for sizing, selection, and installation; API 521 for pressure-relieving and depressuring systems and flare systems; API 526 for flanged steel pressure relief valves; API 527 for seat tightness testing; API 510 for pressure vessel and protective device inspection programs; API 580 and API 581 for risk-based inspection; and ASME Section XIII for overpressure protection rules, together with material requirements for sour service in refineries. The course covers conventional and balanced bellows spring-loaded valves, pilot-operated valves, rupture disks, and pressure/vacuum vents for storage tanks, with a focus on the inspection and testing methodology for each device type rather than theory alone. The course is delivered in a classroom setting using an interactive, application-focused approach that compensates for field work through intensive practical tools. These include worked examples of cold differential test pressure calculations, analysis of real as-received test results, simulation of inspection, testing, and setting steps through presentations, videos, and photographs of damaged components, review of actual installation drawings, datasheets, and inspection records, and case studies of failures and incidents involving safety valves. Participants leave with a field inspection checklist, a shop repair and testing work procedure, an inspection and test report template, a justified methodology for setting inspection intervals, and an improvement plan for the pressure-relieving device program in their facilities.

Learning Objectives

  • Analyze the role of pressure-relieving devices in process safety and the scope of API 576 requirements and their relationship to related API standards and ASME Section XIII on Day 1.
  • Apply key technical terminology, including maximum allowable working pressure, set pressure, cold differential test pressure, overpressure, accumulation, blowdown, and superimposed and built-up back pressure, to interpret valve performance and read datasheets.
  • Evaluate the types of pressure-relieving devices, their components, operating principles, and appropriate applications in refinery units.
  • Assess installation requirements in accordance with API 520, including inlet pressure loss, outlet piping design, supports, drainage, isolation valve controls, and changeover valves for spare relief valves.
  • Analyze the causes of improper valve performance, including corrosion, fouling, damaged seats, galling, spring and bellows failures, chatter, plugging, and misapplication.
  • Assess material requirements and difficult refinery services, including sour service, hydrogen, coking, and polymerization, and their impact on valve performance and inspection intervals.
  • Develop an inspection program that defines inspection and test intervals based on service conditions, performance history, as-received test results, and risk-based inspection methodology.
  • Define the steps for on-stream visual inspection and as-received testing prior to disassembly, and interpret the results to support decision making.
  • Evaluate disassembly, component inspection, lapping, and reassembly procedures using photographs and real cases of damaged components.
  • Calculate cold differential test pressure and define the steps for set pressure testing, seat tightness testing per API 527, and blowdown adjustment.
  • Define inspection and testing requirements for pilot-operated valves, rupture disks, and pressure/vacuum vents, and assess the applications and limitations of in-situ testing.
  • Design a documentation, records, and performance indicator system for pressure-relieving devices and an improvement plan for the program in the participant's facility by the end of Day 5.

Who Should Attend

This course is designed for static equipment engineers, inspection engineers, mechanical maintenance engineers, pressure vessel and piping inspectors, valve shop and test bench technicians, and maintenance supervisors responsible for the inspection, repair, testing, and calibration of safety valves. It is also suitable for reliability and process safety engineers, process engineers working with pressure relief and flare systems, and turnaround planners responsible for scheduling valve work and ensuring availability of spares. The course is particularly valuable for professionals in oil refineries, petrochemical, fertilizer, and gas processing plants, onshore and offshore production facilities, power generation and boiler plants, and technical service companies and valve repair shops. Quality assurance and quality control engineers, HSE professionals, project and design engineers responsible for valve selection and installation, and maintenance and inspection managers who oversee asset integrity programs and approve inspection intervals and turnaround plans will also benefit from the course.

Learning Outcomes

  • By the end of the course, participants will be able to:
  • Explain the core requirements of API 576 and relate them to API 520, API 527, API 510, and ASME Section XIII in daily work.
  • Identify the type of pressure-relieving device, its components, and operating principle from the nameplate, datasheet, and technical drawings.
  • Review valve installation drawings and identify issues related to inlet pressure loss, back pressure, supports, and isolation valves.
  • Diagnose common failures such as leakage, chatter, early or late opening, and plugging, and link them to service and installation conditions.
  • Plan an as-received test, interpret its results, classify valve performance, and use the findings to adjust inspection intervals.
  • Assess the condition of valve components from photographs and inspection reports and determine lapping, repair, or replacement requirements against clear criteria.
  • Calculate cold differential test pressure with temperature and back pressure corrections and define the steps for setting the opening pressure on the test bench.
  • Interpret seat tightness test results per API 527 and evaluate them against applicable acceptance criteria.
  • Define inspection and replacement requirements for rupture disks and their holders, and inspection and testing requirements for pilot-operated valves.
  • Select the appropriate test medium for the valve service and define safety requirements in the test shop and during removal and reinstallation.
  • Prepare complete inspection and test reports and traceable historical records for each valve.
  • Propose technically justified inspection intervals and a practical plan to improve the pressure-relieving device management program.

Course Outline

Course Outline:

Day 1

Overpressure Protection Fundamentals and Reference Framework

  • The role of safety valves and pressure relief valves in process safety and static equipment protection
  • Scope of API 576 and its relationship to API 510, API 520, API 521, API 526, API 527, and ASME Section XIII
  • Technical terminology: maximum allowable working pressure, set pressure, cold differential test pressure, overpressure, accumulation, blowdown, superimposed and built-up back pressure
  • Overpressure scenarios in refinery units and their relationship to valve sizing and flare systems
  • Practical application: participants analyze nameplates and datasheets of actual valves and extract critical data for inspection and testing
Day 2

Device Types, Materials, and Installation

  • Conventional and balanced bellows spring-loaded valves: components, operation, and effect of back pressure
  • Pilot-operated valves, rupture disks, and pressure/vacuum vents for storage tanks
  • Material requirements for sour service, hydrogen service, and high-temperature service
  • Installation requirements: inlet pressure loss, outlet piping, supports, drainage, isolation valves and car-seal controls, spare valves and changeover valves
  • Practical application: participants review actual installation drawings and identify deficiencies and their impact on valve performance and operational safety
Day 3

Failure Mechanisms and the Inspection Program

  • Causes of improper performance: corrosion, fouling, damaged seats, galling, spring and bellows failures, misapplication
  • Chatter, rapid cycling, and leakage: operational and design causes and corrective actions
  • Difficult refinery services: coking, polymerization, fouling, and sour service
  • Determining inspection and test intervals per API 510 and risk-based inspection methodology per API 580 and API 581
  • Practical application: participants analyze historical records and as-received test results and propose technically justified inspection intervals
Day 4

Shop Repair, Testing, and Calibration

  • On-stream visual inspection, safe removal in coordination with operations, and as-received testing before disassembly
  • Disassembly, component inspection, lapping, reassembly, and acceptance and replacement criteria
  • Cold differential test pressure calculation, test medium selection, set pressure testing, and calibration of test bench instruments
  • Seat tightness testing per API 527, blowdown adjustment, pilot-operated valve testing, and rupture disk inspection
  • Practical application: worked examples of cold differential test pressure calculations, simulation of testing and setting steps using videos and photographs of damaged components, and evaluation of actual test results
Day 5

In-Situ Testing, Documentation, and Program Management

  • In-situ testing and lift-assist devices: applications, limitations, and precautions
  • Documentation, inspection tags, sealing and marking, and management of the pressure-relieving device register
  • Planning valve work during turnarounds, spare valve availability, and safety requirements in the shop and on site
  • Performance indicators for the pressure-relieving device program and qualification of repair shops and technicians
  • Final workshop: participants develop an inspection and testing work procedure, an inspection report template, and an improvement plan for the pressure-relieving device management program in their facilities

Upcoming Dates

Selected date

Paris · 5 – 9 Apr 2027 · Classroom

Need more details?Chat with us on WhatsApp

CityDatesPrice per ParticipantEarly Bird
AmsterdamScheduled
2 – 6 Nov 2026€6,000—
BakuScheduled
9 – 13 Nov 2026€5,300—
BangkokScheduled
16 – 20 Nov 2026€6,700—
BarcelonaScheduled
23 – 27 Nov 2026€6,000€5,400until 2 Nov
BerlinScheduled
30 Nov – 4 Dec 2026€6,300€5,670until 9 Nov
CasablancaScheduled
7 – 11 Dec 2026€4,700€4,230until 16 Nov
CairoScheduled
7 – 11 Dec 2026€3,800€3,420until 16 Nov
DammamScheduled
14 – 18 Dec 2026€4,800€4,320until 23 Nov
DohaScheduled
21 – 25 Dec 2026€4,700€4,230until 30 Nov
DubaiScheduled
27 – 31 Dec 2026€4,700€4,230until 7 Dec
FrankfurtScheduled
4 – 8 Jan 2027€6,200€5,580until 14 Dec
GenevaScheduled
11 – 15 Jan 2027€7,300€6,570until 21 Dec
IstanbulScheduled
18 – 22 Jan 2027€5,300€4,770until 28 Dec
Kuala LumpurScheduled
25 – 29 Jan 2027€4,700€4,230until 4 Jan
LisbonScheduled
25 – 29 Jan 2027€6,000€5,400until 4 Jan
LondonScheduled
1 – 5 Feb 2027€5,800€5,220until 11 Jan
MadinahScheduled
8 – 12 Feb 2027€4,800€4,320until 18 Jan
MadridScheduled
15 – 19 Feb 2027€6,000€5,400until 25 Jan
MakkahScheduled
22 – 26 Feb 2027€4,800€4,320until 1 Feb
ManamaScheduled
1 – 5 Mar 2027€5,300€4,770until 8 Feb
MarrakeshScheduled
8 – 12 Mar 2027€4,700€4,230until 15 Feb
MilanScheduled
8 – 12 Mar 2027€7,000€6,300until 15 Feb
MunichScheduled
15 – 19 Mar 2027€6,000€5,400until 22 Feb
MuscatScheduled
22 – 26 Mar 2027€6,300€5,670until 1 Mar
OnlineScheduled
28 Mar – 1 Apr 2027€2,700€2,430until 8 Mar
ParisScheduled
5 – 9 Apr 2027€6,700€6,030until 15 Mar
RiyadhScheduled
12 – 16 Apr 2027€4,800€4,320until 22 Mar
RomeScheduled
19 – 23 Apr 2027€7,000€6,300until 29 Mar
ViennaScheduled
26 – 30 Apr 2027€6,400€5,760until 5 Apr
AmmanScheduled
2 – 6 May 2027€4,000€3,600until 12 Apr

Available in: Istanbul · Dubai · London · Riyadh · Doha · Amsterdam

Related Courses

Ready to Elevate Your Team's Capabilities?

Speak with our advisors about upcoming programmes or a bespoke corporate training plan.