The cost of unplanned downtime in chemical and process plants
Unplanned downtime in chemical and process plants is among the most expensive losses in the plant because a single failure, such as rotating equipment failures (pumps, compressors) that trip a unit, can stop the flow, not just one asset. The true cost pairs lost contribution margin with emergency labour and expedited parts, and is usually several multiples of the repair itself.
What drives downtime cost in chemical and process plants
- Rotating equipment failures (pumps, compressors) that trip a unit.
- Heat exchanger fouling and tube failures.
- Instrument and control failures that force a shutdown.
- Deferred integrity and inspection work raising risk.
The failure modes behind it
- Rotating equipment failures (pumps, compressors) that trip a unit.
- Heat exchanger fouling and tube failures.
- Instrument and control failures that force a shutdown.
- Deferred integrity and inspection work raising risk.
Size it for your plant
Use the free unplanned downtime cost calculator with your own lost margin per hour to estimate the annual cost, then see how to calculate it properly.
Ranges on this page are practitioner estimates drawn from operational experience across heavy industry, provided for orientation. Your actual figures will differ. The Diagnostic measures them against your own CMMS and downtime data.
Frequently asked questions
Why is unplanned downtime so costly in chemical and process plants?
How do I estimate downtime cost for my site?
See where your plant is leaking profit.
Score your operation across five leak zones in 3 minutes, or book a free 30-minute Fit Call to confirm whether a Diagnostic is the right next step.
15 questions. 3 minutes. Instant grade. No email required.