(53i) Lessons-Learned from Remote HAZOP/LOPA Applications
AIChE Spring Meeting and Global Congress on Process Safety
2022
2022 Spring Meeting and 18th Global Congress on Process Safety Proceedings
Global Congress on Process Safety
GCPS Alternate Presentations & Posters
Monday, April 11, 2022 - 5:00pm to 7:00pm
The consequences of many of the hazards evaluated by the PHA Team are relatively easy to characterize. However, rotating equipment consequences can be a bit more difficult to pin down. The failure mechanisms and release pathways associated with pumps can be complex, and determining the consequences (and severities) has been very reliant on âexpert judgementâ and operational experience. Determining the impact on a pump associated with:
- Loss of suction
- Blocked suction
- Blocked discharge
- Backspin
is not only dependent on the pump characteristics such as seal design, but also on process conditions:
- Temperature
- Pressure
- Process chemistry â Impacting not only the potential for and magnitude of pump damage, but also release quantity and phenomenology
When confronted with these challenges, a PHA Team will often overpredict severity, which can skew not only the PHA results, but also impact priorities for capital project investments in safety systems, mechanical integrity programs, and alarm rationalization.
This paper will review some common pump and seal designs, correlate failure mechanisms to important elements to be reviewed in the PHA and associated consequences, correlate these consequences to industry-observed failures and frequencies, and identify safety measures that should be considered by the PHA Team for specific configurations. The objective of the paper will be to provide a better foundation for the evaluation of pump failures in the PHA, as well as an improved basis for severity estimations (often overpredicted).