AIChE CCPSC dumps - in .pdf

CCPSC pdf
  • Exam Code: CCPSC
  • Exam Name: CCPS Process Safety Professional Certification
  • Updated: Jul 04, 2026
  • Q & A: 114 Questions and Answers
  • PDF Price: $59.99
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  • Exam Code: CCPSC
  • Exam Name: CCPS Process Safety Professional Certification
  • Updated: Jul 04, 2026
  • Q & A: 114 Questions and Answers
  • PDF Version + PC Test Engine + Online Test Engine
  • Value Pack Total: $119.98  $79.99
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AIChE CCPSC dumps - Testing Engine

CCPSC Testing Engine
  • Exam Code: CCPSC
  • Exam Name: CCPS Process Safety Professional Certification
  • Updated: Jul 04, 2026
  • Q & A: 114 Questions and Answers
  • Software Price: $59.99
  • Testing Engine

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CCPSC exam dumps

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AIChE CCPS Process Safety Professional Certification Sample Questions:

1. Management of Change review should be done: (select all that apply)

A) For process related changes
B) For replacement in kind
C) To evaluate compliance with safe work practices
D) Throughout the process lifecycle
E) To confirm operational readiness


2. Asset Integrity inspection/test methods for tubes in shell and tube heat exchangers include (select all that apply):

A) Hydrostatic test
B) Radiography
C) Borescope
D) Dye injection


3. Which of the following are evidence that good workforce involvement exists at a facility? (Select all that apply)

A) Operators are consulted on the content of training programs
B) Operators are always included on PHA teams
C) Operators are expected to report minor process safety incidents
D) Operators participate on incident investigation teams
E) Operators are disciplined for not following procedures


4. Which one of the following Hazard Identification and Risk Analysis (HIRA) methods is generally considered to be most quantitative in nature?

A) Hazard and Operability (HAZOP)
B) Bow-Tie Analysis
C) What-If/Checklist Analysis
D) Failure Modes and Effects Analysis
E) What-If Analysis


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) No hazard exists because the relief valve will always protect the system
C) The pressure gauge is faulty and can be ignored
D) The rupture disc may have failed or leaked, compromising the relief system and creating overpressure risk


Solutions:

Question # 1
Answer: A,D
Question # 2
Answer: A,C
Question # 3
Answer: A,B,C,D
Question # 4
Answer: D
Question # 5
Answer: D

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