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AIChE CCPS Process Safety Professional Certification Sample Questions:

1. All three flammable gas detection alarms have indicated in the control room the presence of a flammable vapor in the containment area below a horizontal butane storage tank. The correct operator response to this emergency would include (select all that apply):

A) Notify management of the situation
B) Remotely isolate the inlet and outlet lines of the butane tank, if this capability exists
C) Remotely activate the tank area deluge system, if one exists
D) Deploy an operator with a combustible gas meter to determine the extent of the flammable cloud
E) Notify workers to leave the butane tank area

2. 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) The rupture disc may have failed or leaked, compromising the relief system and creating overpressure risk
D) No hazard exists because the relief valve will always protect the system

3. For a vapor explosion in an unconfined and uncongested area, the amount of thermodynamic energy that ends up in the overpressure is approximately:

A) 50-75%
B) 2-5%
C) 100%
D) 0%
E) 10-15%

4. Which is the main objective for investigating process safety incidents?

A) Determine root causes and avoid recurrence
B) Optimize inspection and maintenance
C) Reduce the number of incidents and improve plant performance
D) Improve the Control of Work system

5. Which of the following is generally a disadvantage of a rupture disc vs a relief valve?

A) Protect against rapid pressure rise caused by heat exchanger tube ruptures or internal deflagrations
B) Less expensive way to achieve corrosion resistance
C) Is relatively more susceptible to damage during installation
D) Reduced fugitive emissions - no simmering or leakage prior to bursting

Solutions: