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AIChE CCPSC Exam Syllabus Topics:

AIChE CCPS Process Safety Professional Certification Sample Questions:

1.
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) There are no significant consequences if an operator is present
B) The plan eliminates the need for detection systems
C) Water spray always neutralizes chlorine safely with no risks
D) Water spray may increase hazard by forming toxic/corrosive byproducts, spreading contamination, and increasing exposure risk

2. What are the main objectives for conducting a Process Safety Management audit? (Select all that apply)

A) Certify that all Operating Procedures are correct and up-to-date
B) Identify program improvement opportunities
C) Verify effectiveness of Risk-Based Process Safety management systems
D) Prepare an emergency response plan
E) Reduce process safety risks

3. A facility's process safety staff does consequence modeling for releases of various toxic substances that the facility handles. Which elements of Risk Based Process Safety would be most likely to use the results of this modeling? (Select all that apply)

A) Stakeholder Outreach
B) Operational Readiness
C) Measurement and Metrics
D) Hazard Identification and Risk Analysis
E) Emergency Management

4. Which of the following is not a leading metric for emergency management?

A) Number of actual process safety incidents in past year
B) Number of realistic emergency response drills in past year
C) Number of trained emergency response team members on each shift
D) Number of revisions to emergency response plans in past year

5. A 3000 gallon, stainless steel, insulated vessel rated for 30 psig is equipped with a rupture disc set for 30 psig for emergency relief. Assuming each of the following scenarios has been deemed possible, which would require the smallest sized relief?

A) An internal ignition of the vessel's vapor space, the vessel containing a solvent
B) A runaway reaction of the vessel's contents, in solvent service, where testing has determined a temperature rise rate of 500°C/min at disc relief setting
C) A pool fire from the leak of a common solvent beneath the vessel

Solutions: