Let's Test Your Process Engineering Fundamentals
1 / 10
When protecting our system from overpressure, which one of these is not considered as equipment protection in HAZOP?
Control loops are more subject to failure and their failure may even be the cause of overpressure which we should already be addressing, that's why we should add another safeguards to protect from overpressure such as pressure safety valves and using safety interlocks to stop the overpressure source.
2 / 10
In a typical project, which document is developed first?
3 / 10
Which of the following is NOT a commonly used process simulation software?
4 / 10
When emptying a vessel containing hydrocarbons, where do we send the hydrocarbon liquid inside the vessel?
5 / 10
For a control valve to be considered as properly sized, its opening range in operation including maximum and minimum cases should range between
This is the acceptable range at which the valve should handle all scenarios including maximum and minimum CV cases, although the ideal range for normal scenarios can be narrower.
6 / 10
In a process flow diagram, we typically show
7 / 10
Through the pump system curve, what can we get at a specific flow rate?
Remember! This is the pump system curve not the performance curve
8 / 10
Anti-surge control is used in
9 / 10
Which type of 2 phase flow in a pipe should be avoided?
10 / 10
What is the purpose of the Hazard and Operability (HAZOP) study?
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