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AIChE CCPSC Exam Syllabus Topics:
| Section | Weight | Objectives |
|---|---|---|
| Topic 1: Incident Investigation and Learning | 10-15% | - Investigation Report Development - Lessons Learned and Knowledge Management - Incident Classification and Severity - Root Cause Analysis Methods - Trending and Performance Metrics |
| Topic 2: Emergency Planning and Response | 5-10% | - Inherently Safer Design Principles - Containment and Mitigation Barriers - Emergency Response Planning - Safety Instrumented Systems (SIS) |
| Topic 3: Process Safety Management Systems | 15-20% | - Management Leadership and Commitment - Continuous Improvement Frameworks - Elements of PSM Systems - Policy and Strategic Planning |
| Topic 4: Management of Change (MOC) | 8-12% | - Personnel and Organizational Changes - MOC Process Requirements - Temporary vs. Permanent Changes - Technical Review and Risk Assessment |
| Topic 5: Process Safety Engineering Fundamentals | 15-20% | - Equipment Design and Integrity - Chemical Process Safety Fundamentals - Fire and Explosion Dynamics - Toxicology and Exposure Assessment - Thermodynamics and Reaction Hazards |
| Topic 6: Risk Assessment and Analysis | 20-25% | - Event Tree Analysis (ETA) - Quantitative Risk Assessment (QRA) - Bow-Tie Analysis - Layer of Protection Analysis (LOPA) - Fault Tree Analysis (FTA) - Hazard and Operability Analysis (HAZOP) - Hazard Identification (HAZID) |
| Topic 7: Operating Procedures and Practices | 10-15% | - Startup and Shutdown Procedures - Permit-to-Work Systems - Standard Operating Procedures (SOPs) - Safe Work Practices - Operations Training and Competency |
| Topic 8: Regulatory Compliance and Auditing | 5-10% | - EPA RMP Regulations - Process Safety Auditing Techniques - OSHA PSM Requirements - Compliance Verification Methods - International Process Safety Standards |
AIChE CCPS Process Safety Professional Certification Sample Questions:
1. Which of the following changes require a Management of Organizational Change (MOOC) Review? (Select all that apply.)
A) Relocating from offices to cubicles
B) Moving an operator from one shift team to another in the same operating unit
C) Replacing site maintenance department with contractors
D) Reducing the number of operators per shift team
E) Modification of shift schedules from 8-hour shifts to 12-hour shifts
2. The Risk Based Process Safety element which is designed to verify that a process is verified safe to start after a short term shutdown is Operational Readiness. True or False?
A) False
B) True
3. Which of the following Risk-Based Process Safety elements are expected to be most directly and frequently involved with the Emergency Management Element? (select all that apply)
A) Training and Performance Assurance
B) Management of Change
C) Stakeholder Outreach
D) Hazard Identification and Risk Analysis
4. A process calls for the addition of a reactant over a certain period of time. The flow controller on the reactant' s feed line was out of calibration and reduced the flow rate of the reactant. The operator noticed the addition rate was too low and, contrary to the operating procedures, he opened a bypass valve around the flow control valve to increase the flow rate. As a result, the operator added the remaining reactant too quickly, and a runaway reaction occurred. Weaknesses in which of the following Risk Based Process Safety elements could have contributed to the cause of this incident? (Select all that apply)
A) Asset Integrity and Reliability
B) Training and Performance Assurance
C) Workforce Involvement
D) Incident Investigation
E) Conduct of Operations
5. A vessel has a rupture disc and pressure relief valve in series to protect against high pressure in the vessel.
There is a pressure gauge on the pipe between the rupture disc and the relief valve. The gauge normally reads zero. As part of regular maintenance inspections, these pressure gauges are supposed to be routinely checked.
Today, a pressure of nearly 50 psig (~3.5 barg) was observed by an operator. There is a significant hazard now. Identify the hazard and discuss which elements of Risk-Based Process Safety could have been involved in the development of this situation.
A) The system is operating normally under transient conditions
B) The pressure gauge is faulty and can be ignored
C) No hazard exists because the relief valve will always protect the system
D) The rupture disc may have failed or leaked, compromising the relief system and creating overpressure risk
Solutions:
| Question # 1 Answer: C,D,E | Question # 2 Answer: A | Question # 3 Answer: A,C,D | Question # 4 Answer: A,B,E | Question # 5 Answer: D |
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