Facility and Pipeline Safety
Hazards and safe work at batteries, compressor stations, sour gas plants and pipelines for field operators, plant operators, maintenance workers and pipeline crews: separators, treaters, tanks, compressors, amine, Claus, glycol and liquids units, OSHA general industry standards, PSM and the general duty clause, EPA's RMP rule, state oil and gas agencies, PHMSA's 49 CFR 192 and 195 and TSA security directives, pressure equipment under state boiler laws and the ASME code, overpressure, relief valves, gas blowby and shutdown systems, corrosion, sour service cracking, hydrates and integrity, amine, molten sulfur, benzene, methanol, mercury, NORM and pyrophoric iron sulfide, tanks, static, flares and radiation, process safety management, management of change and bypass control, isolation, first breaks and nitrogen purging, pipeline design, class locations, cathodic protection, in-line inspection and leak detection, 811 and tolerance zones, crossings and strikes, pigging and pig trap closures, hot taps and blowdowns, and emergency response, case studies and a facility hazard review.
HSE-332 12 lessons · 5 h 26 min
Offered by HSM University · Safety Training
This is the American version of this course. See the Canadian version.
What you'll learn
- Describe the equipment and purpose of batteries, compressor stations, sour gas plants and the main types of pipeline, and identify where each holds flammable, toxic and pressurized inventory.
- Map the rules that apply to facilities and pipelines in the US, including OSHA's general industry standards and PSM, EPA's RMP rule, state oil and gas agencies, PHMSA's 49 CFR 192 and 195, TSA security directives, state boiler laws and the ASME code, and explain who holds which duty.
- Distinguish operating pressure, design pressure, MAWP, relief set pressure, accumulation and test pressure, recognize common causes of overpressure such as gas blowby and trapped liquid, and protect relief and shutdown systems.
- Explain how corrosion, sour service cracking, erosion, hydrates, deposits and mechanical damage threaten integrity, calculate corrosion rates and remaining life, and handle hydrate plugs and freeze-ups safely.
- Identify the hazards of amine, sulfur recovery, glycol dehydration, methanol and treatment chemicals, mercury, NORM and pyrophoric iron sulfide, and add service-specific questions to task hazard assessments.
- Describe the fittings that protect field tanks, control vapor, static and lightning hazards during gauging and loading, and explain how flare systems work, why flame-outs matter and how radiation limits work near flares.
- Explain the elements of process safety management and the field worker's part in them, including safe operating limits, management of change, bypass and alarm control and process safety event indicators.
- Describe levels of process isolation, explain why valves pass and pressure is trapped, apply safe practices at the first break and recognize the hazards of nitrogen, steam and air purging and of blinds and reinstatement.
- Apply Barlow's formula and class location design factors, describe coatings, cathodic protection, in-line inspection, integrity management, SCADA and leak detection, and explain the lessons of control room failures.
- Manage work near pipeline rights-of-way, including 811 one-call requirements, tolerance zones, crossings, the effect of depth of cover on loads, induced voltage and the response to a strike.
- Explain why pipelines are pigged, the parts and hazards of launchers and receivers, how to confirm zero pressure before opening a closure, how to plan for liquid slugs and debris, and the hazards of digs, repairs, hot taps and blowdowns.
- Respond to facility and pipeline emergencies, draw lessons from major failures, and carry out and rank a hazard review with actions, owners and interim measures.
Course content
12 lessons · 5 h 26 min total · final exam
- 1 Facility types and how they work 28 min · quiz
- 2 Law, regulators and standards for facilities and pipelines 28 min · quiz
- 3 Hazards of pressurized equipment 28 min · quiz
- 4 Corrosion, hydrates and integrity threats 27 min · quiz
- 5 Process chemicals and special hazards 26 min · quiz
- 6 Tanks, flares and vapor hazards 27 min · quiz
- 7 Process safety management for facility workers 26 min · quiz
- 8 Isolation, blinding and line breaking: the hazards 27 min · quiz
- 9 Pipelines: design, operation and integrity 26 min · quiz
- 10 Pipeline right-of-way and ground disturbance 27 min · quiz
- 11 Pigging and pipeline maintenance 27 min · quiz
- 12 Capstone: emergency response, case studies and a facility hazard review 29 min · quiz
- E Final exam 20 questions
Requirements
Recommended background. You can start any course at any time.
Description
Hazards and safe work at batteries, compressor stations, sour gas plants and pipelines for field operators, plant operators, maintenance workers and pipeline crews: separators, treaters, tanks, compressors, amine, Claus, glycol and liquids units, OSHA general industry standards, PSM and the general duty clause, EPA's RMP rule, state oil and gas agencies, PHMSA's 49 CFR 192 and 195 and TSA security directives, pressure equipment under state boiler laws and the ASME code, overpressure, relief valves, gas blowby and shutdown systems, corrosion, sour service cracking, hydrates and integrity, amine, molten sulfur, benzene, methanol, mercury, NORM and pyrophoric iron sulfide, tanks, static, flares and radiation, process safety management, management of change and bypass control, isolation, first breaks and nitrogen purging, pipeline design, class locations, cathodic protection, in-line inspection and leak detection, 811 and tolerance zones, crossings and strikes, pigging and pig trap closures, hot taps and blowdowns, and emergency response, case studies and a facility hazard review.