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AIChE CCPSC Exam Syllabus Topics:
| Section | Objectives |
|---|---|
| Topic 1: Risk-Based Process Safety (RBPS) Framework | - Hazard Identification and Risk Analysis - Emergency Management - Safe Work Practices - Metrics and Performance Measurement - Training and Performance Assurance - Process Safety Culture - Process Knowledge Management - Operating Procedures - Auditing - Asset Integrity and Reliability - Conduct of Operations - Operational Readiness - Compliance with Standards - Management of Change - Contractor Management - Management Review and Continuous Improvement - Incident Investigation |
AIChE CCPS Process Safety Professional Certification Sample Questions:
1. 
During a field inspection of the process piping in a production unit, a section of piping is identified as containing a dead leg in which stagnant liquid is trapped. It is determined that this dead leg branch line is used very infrequently. Assume that the plant is in a location where winter temperatures drop below 20°F (-7°C) and summer temperatures can exceed 90°F (32°C). Which of the following are valid process safety reasons to remove the line? (Select all that apply)
A) The cost of removing the line will be greater if done at a later time
B) Water could accumulate in the line and freeze during colder weather, potentially rupturing the piping
C) The current position of the line may be a tripping hazard
D) Stagnant liquids in piping could result in accelerated corrosion
2. Which of the following statements apply to the purpose of an incident investigation? (Select all that apply)
A) To help continually improve the process safety management efforts
B) To document all injuries as process safety incidents
C) To determine who should be disciplined for causing the event
D) To prevent reoccurrence of the same or similar process safety incidents
3. Which of the following is generally a disadvantage of a rupture disc vs a relief valve?
A) Is relatively more susceptible to damage during installation
B) Less expensive way to achieve corrosion resistance
C) Reduced fugitive emissions - no simmering or leakage prior to bursting
D) Protect against rapid pressure rise caused by heat exchanger tube ruptures or internal deflagrations
4. What minimum size is normally used for laboratory test apparatus to determine dust explosion severity?
A) 20 liters
B) 5 liters
C) 1 cubic meter
D) 50 liters
5. 
A chemical processor has a chlorine unloading facility shown in the sketch. The area has an ambient chlorine detector with audible alarm and a chemical operator is continually in attendance during the unloading operation. In the event of a leak, the action plan is to spray water on the leak and the contained spill to effect some dilution. Identify and discuss any negative consequences that might result from implementing this plan.
A) Water spray always neutralizes chlorine safely with no risks
B) There are no significant consequences if an operator is present
C) Water spray may increase hazard by forming toxic/corrosive byproducts, spreading contamination, and increasing exposure risk
D) The plan eliminates the need for detection systems
Solutions:
| Question # 1 Answer: B,D | Question # 2 Answer: A,D | Question # 3 Answer: A | Question # 4 Answer: A | Question # 5 Answer: C |



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