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Updated: Aug 23, 2026
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| Certification Vendor: | AIChE (American Institute of Chemical Engineers) / CCPS (Center for Chemical Process Safety) |
| Exam Name: | CCPS Process Safety Professional Certification |
| Exam Number: | CCPSC |
| Exam Price: | USD $1,200 - $1,500 (member/non-member pricing varies) |
| Exam Format: | Multiple Choice, Scenario-Based Questions, Case Study Analysis |
| Real Exam Qty: | 150-175 |
| Available Languages: | English |
| Related Certifications: | Certified Safety Professional (CSP) Process Safety Management (PSM) Certifications NEBOSH Diploma in Process Safety |
| Passing Score: | 70% (approximately) |
| Certificate Validity Period: | 5 years (with recertification requirements) |
| Exam Duration: | 240-300 (4-5 hours) |
| Sample Questions: | AIChE CCPSC Sample Questions |
| Exam Way: | Computer-based testing at Pearson VUE testing centers; remote proctoring may be available |
| Pre Condition: | Bachelor's degree in engineering or science plus 5+ years of process safety experience; OR 10+ years of process safety experience without degree. Recommended completion of CCPS Academy courses or equivalent process safety training. |
| Official Syllabus URL: | https://www.aiche.org/ccps/certification |
| Section | Weight | Objectives |
|---|---|---|
| Regulatory Compliance and Auditing | 5-10% | - International Process Safety Standards - OSHA PSM Requirements - Compliance Verification Methods - Process Safety Auditing Techniques - EPA RMP Regulations |
| Management of Change (MOC) | 8-12% | - MOC Process Requirements - Personnel and Organizational Changes - Temporary vs. Permanent Changes - Technical Review and Risk Assessment |
| Emergency Planning and Response | 5-10% | - Inherently Safer Design Principles - Safety Instrumented Systems (SIS) - Containment and Mitigation Barriers - Emergency Response Planning |
| Operating Procedures and Practices | 10-15% | - Operations Training and Competency - Safe Work Practices - Permit-to-Work Systems - Standard Operating Procedures (SOPs) - Startup and Shutdown Procedures |
| Incident Investigation and Learning | 10-15% | - Incident Classification and Severity - Trending and Performance Metrics - Root Cause Analysis Methods - Lessons Learned and Knowledge Management - Investigation Report Development |
| Risk Assessment and Analysis | 20-25% | - Hazard Identification (HAZID) - Hazard and Operability Analysis (HAZOP) - Fault Tree Analysis (FTA) - Layer of Protection Analysis (LOPA) - Bow-Tie Analysis - Quantitative Risk Assessment (QRA) - Event Tree Analysis (ETA) |
| Process Safety Engineering Fundamentals | 15-20% | - Equipment Design and Integrity - Toxicology and Exposure Assessment - Thermodynamics and Reaction Hazards - Fire and Explosion Dynamics - Chemical Process Safety Fundamentals |
| Process Safety Management Systems | 15-20% | - Policy and Strategic Planning - Continuous Improvement Frameworks - Elements of PSM Systems - Management Leadership and Commitment |
1. The Management of Change element: (select all that apply)
A) Helps maintain safe process operations
B) Requires communicating approved changes to affected contractors
C) Makes the evaluation of the safety impact of a small change optional
D) Helps avoid inaccuracies in process safety information
2. What are the main objectives for conducting a Process Safety Management audit? (Select all that apply)
A) Reduce process safety risks
B) Certify that all Operating Procedures are correct and up-to-date
C) Identify program improvement opportunities
D) Verify effectiveness of Risk-Based Process Safety management systems
E) Prepare an emergency response plan
3. A Management of Change system should address all types of changes to the process that can be reasonably foreseen.
A) True
B) False
4. The photo below represents part of the overhead piping for a reactor with a 90 psig maximum allowable working pressure (MAWP). Which of the following statements are correct? (select all that apply)
A) A drain valve between the rupture disc and relief valve can compromise overpressure protection
B) The pressure gauge shown can be used to verify that the relief device is set correctly
C) A rupture disc installed upstream of a relief valve can protect the valve from corrosion and fouling
D) The combination of rupture disc and relief valve is an acceptable overpressure protection configuration
5. A line is provided for adding a chemical to a reactor to quench the reaction. The line has an automatic valve which is designed to open when reactor temperature exceeds the High-High limit. Which of the items are key parts of the ITPM (Inspection, Testing, and Preventive Maintenance) requirements for the valve? (Select all that apply)
A) Valve and its control system must be inspected and tested with sufficient frequency to confirm that it will reliably open when required
B) Valve must be functionally tested to ensure that it opens quickly enough to quench the reaction
C) Valve must be designed to fail open
D) Valve must be designed to open quickly enough to quench the reaction
Solutions:
| Question # 1 Answer: A,B,D | Question # 2 Answer: A,C,D | Question # 3 Answer: A | Question # 4 Answer: B,D | Question # 5 Answer: A,B |
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